Home

TriSep Catalog 11-10-08.indd - liquidfiltration

1. 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 45 20 Length A 40 0 1 016 Diameter B 8 5 215 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TriSep ACM5 Composite am RO Membrane Elements TRIS S CORPORATION The ACM5 membrane offers the highest flux in the ACM family allowing operation at ultra low pressures The ACMS will typically operate at feed pressure of 75 125 psi 5 9 bar Even at these high flux rates the ACMS still averages 98 5 salt rejection Due to the high specific flux these membranes are best suited to applicaitons with relatively low TDS 3 000 ppm to achieve balanced flux rates within the system 2540 ACM5 TSF 2 5 diamete
2. 1 NTU Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION S 9 ACM RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 ACM2 TSAN 9 700 36 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane COMTI GUN AU ON M Spiral Wound Fiberglass Outer Wrap Active Membrane Area 365 ft 33 5 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temp
3. Configuration Active Membrane Area Recommended Applied Pressure Maximum Applied Pressure Recommended Operating Temperature Feedwater pH Range Chlorine Tolerance Maximum Feed Flow Minimum Brine Flow Permeate Flow Ratio Maximum SDI 15 minutes Maximum Turbidity haec M een AUM Advanced Ultrafiltration Membrane Spiral Wound Turboclean Shell 78 ft 7 2 m 5 200 psi 0 3 14 bar 600 psi 41 bar 35 113 F 2 45 C 2 11 continuous 10 0 ppm 20 GPM 4 5 m3 hr 5 1 5 0 1 NTU Dialysis Make Up Water Element Weight Length A 12 5 4 40 00 1 016 Diameter B 4 00 101 Permeate Tube C 0 62 15 9 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Feed Spacer 0 031 thick diamond spacer Desal DuPont Style Core Tube Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Go
4. 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 15 7 Length A 40 00 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION S 9 ACM RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 ACM1 TSA 8 000 30 0 99 50 99 00 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane COMM QUIN GIOI L ste uqu La cet T Spiral Wound Fiberglass Outer Wrap Active Membrane Area
5. XN45 Polyamide Advanced Nanofiltration Membrane CGopnfguraton a k Spiral Wound High Temperature Turboclean Shell Active Membrane Area 53 ft 4 9 m Recommended Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 5 ppm nominal 1 0 ppm max Maximum Feed Flow 25 GPM 5 6 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Apple AMOI u u usu uo iA Animal Feed W M PA III I MI Ma o d d p la Element Weight 15 T Length A 38 00 965 Diameter B 3 8 96 Permeate Tube C 0 83 21 2 Units in pounds and inches units in paranthesis in kilograms and millimetes Dim A does not include ATD Mechanical Configuration Sanitary Style Core Tube ATD not included with element Feed Spacer 0 047 thick parallel spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 1596 Engineered Membrane SOLUTIONS
6. 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU APPIANO M Dialysis Make up Water Element Weight 15 7 Length A 40 1016 Diameter B 4 0 101 Permeate Tube C 0 78 19 8 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Osmo Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Es 8 ACM RO Turboclean Element Series TRI CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 M2P3T6 9 400 35 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic P
7. SB Cellulose Acetate Blend Spiral Wound Fiberglass Outer Wrap 80 ft 7 4 m 200 500 psi 14 34 bar 600 psi 41 bar 50 90 F 10 32 C 5 5 nominal 4 7 0 5 ppm nominal 1 0 ppm max 20 GPM 4 5m3 hr 5 1 5 0 1 NTU Element Weight Length A 15 7 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TRIS gt CORPORATION Permeate flow Model GPD m3 day 4040 SB50 TSA 2 000 7 0 PRODUCT SPECIFICATION 4 CA RO Element Series Minimum Salt Rejection Average Salt Rejection 95 00 92 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 420 0 psi 25 C 15 recovery pH 5 5 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type Configuration Active Membrane
8. 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane EE SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Zum 8 TS80 Nanofiltration Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 TS80 TSAN 9 000 34 0 99 00 97 00 Performance is based on the following test conditions 2 000 0 ppm MgSOA 110 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ANM Aromatic Polyamide Advanced Nanofiltration Membrane COMIC UA OND ME Spiral Wound Fiberglass Outer Wrap Active Membrane Area
9. ACM Fully Aromatic Polyamide Advanced Composite Membrane ONTO ON I uu aan wa Spiral Wound Fiberglass Outer Wrap Active Membrane Area 85 ft 7 9 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 15 7 Length A 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com
10. 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Application Beer Dealcoholization ab li MILL ll ul A AAA Mo ALI lli MN li anes SW AEN A AW AM m ll ii iili M d 4 a mm UD kk ak J Element Weight 12 5 4 Length A 38 965 Diameter B 3 8 96 Permeate Tube C 0 83 21 2 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Sanitary Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane rmcwi SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Aa N 4 ACM RO Turboclean Element TRIS gt CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 M2E6U5 2 400 9 0 99 50 98 50
11. AUM Advanced Ultrafiltration Membrane Configuration Spiral Wound Fiberglass Outer Wrap Active Membrane Area 85 ft 7 9 m2 Recommended Applied Pressure 20 200 psi 1 4 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 10 0 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 15 7 Length A 40 00 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TRIS CORPORATION Permeate flow Model GPD m3 day 8040 UE50 QSA 20 000 75 0 PRODUCT SPECIFICATION 8 AUM Ultrafiltration Eleme
12. 355 ft 32 6 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU ADDIIG300I1 uuuu uuu A degen General Pharmaceutical Element Weight 45 20 Length A 40 00 1 016 Diameter B 7 90 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION lt 8 ACM LP Low Pressure RO Turboclean Element TRIS CORPORATION Permeate flo
13. 1 NTU Element Weight 50 23 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 028 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Za 8 TS80 Nanofiltration Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 TS83 TSAN 10 000 37 0 98 50 97 00 Performance is based on the following test conditions 2 000 0 ppm MgSOA 110 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ANM Aromatic Polyamide Advanced Nanofiltration Membrane Configuration Spiral Wound Fiberglass Outer Wrap Active Membrane Area 365 ft 33 5 m Recommended Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressure
14. 70 GPM 15 8 m3 hr y M Minimum Brine Flow Permeate Flow Ratio 5 1 V S y N Maximum SDI 15 minutes 5 0 APPROV d Maximum T urbuditv 1 NTU APPIC AUO ete een ene ee Whey Fractionation Element Weight 28 12 7 Length A 38 965 Diameter B 6 3 160 Permeate Tube C 1 14 28 9 Units in pounds and inches units in paranthesis in kilograms and millimetes Dim A does not include ATD Mechanical Configuration Sanitary Style Core Tube ATD not included with element Feed Spacer 0 065 thick diamond spacer Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TRIS gt CORPORATION Model 6338 N6D9V8 OPERATIONAL AND DESIGN DATA Membrane Type Configuration Active Membrane Area Recommended Applied Pressure Maximum Applied Pressure Recommended Operating Temperature Feedwater pH Range Chlorine Tolerance Maximum Feed Flow Minimum Brine Flow Permeate Flow Ratio Maximum SDI 15 minutes Maximum Turbidi
15. 5 0 Maximum Turbidity 2NTU Application Enzyme Concentration Element Weight 40 18 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 047 thick parallel spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane en SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION A lt 8 X 20 RO High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 N1J4S4 7 100 26 0 99 00 98 00 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane Cong AMON uuu aa E oa akana URS Spiral Wound Turboclean Shell with FoulGuard Technology Active Membrane Area
16. Maximum Turbidity PDD NGAUGM A Element Weight 50 23 Length A 40 0 1 016 Diameter B 8 3 210 AUM Advanced Ultrafiltration Membrane Spiral Wound Turboclean Shell 372 ft 34 6 m 5 200 psi 0 3 14 bar 600 psi 41 bar 35 113 F 2 45 C 2 11 continuous 10 0 ppm 80 GPM 18 m3 hr 5 1 Permeate Tube C 1 14 29 0 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Osmo Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TurboClean Sanitary Elements for Industrial Applications um TRIS S CORPORATION TurboClean elements have been used extensively in the industrial market for process and wastewater applications The polypropylene outershell contruction is resistant to chemical attack while maintaining a sanitary element environment The sanitary nature of the TurboClean element provides a continous by pass flow around the outside of the element This eliminates the stagnant area normally present on sta
17. 355 ft 32 6 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 2NTU ADDICION uuu 2 iss usia zase General Pharmaceutical Element Weight 45 20 Length A 40 00 1 016 Diameter B 7 90 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Za 8 X 20 Low Fouling RO Turboclean Element TRIS CORPORATION Permeate flow Average Salt Min
18. 1 NTU olei m Beverage Water Make up Element Weight 45 20 Length A 40 1016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION X 8 X 20 Low Fouling RO Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 N1EGT6 9400 35 0 99 50 98 50 Performance is based on the following test conditions 2000 ppm NaCl 225 psi 25 C 15 recovery pH 8 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane Configuration Spiral Wound Turboclean Shell with FoulGuard Technology Active Membrane Area 355 ft 32 6 m Recommended Applied Pressure 100 300 psi 7
19. 153 ft 14 2 m Recommended Applied Pressure Not applicable Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 10 0 ppm Maximum Feed Flow 70 GPM 15 8 m3 hr y M Minimum Brine Flow Permeate Flow Ratio 5 1 S y N Maximum SDI 15 minutes 5 0 APPROV d Maximum T urbuditv 1 NTU APPIC AUO ete een ene ee Milk Fractionation Element Weight 30 14 Length A 38 00 965 Diameter B 6 4 162 Permeate Tube C 1 14 29 0 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Sanitary Style Core Tube Feed Spacer 0 045 thick diamond spacer Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION LA NI 6 4 PE High Temperature UF Turboclean Element TRIS gt CORPORATION Model M W C O 6438 N9D4Z9 10 000 OPERATIONAL AND DESIGN DATA Membrane Type PerSep Advanced Ultrafiltration Membrane CGopnfguraton a k Spiral Wound High Temperature Turboclean Shell Active Membran
20. 5 0 Maximum Turbidity 2 NTU ADDIIG300I Rm Nitrate Removal A Th _ am ea c DU e i B A Ww A 3 E Element Weight 40 18 Length A 40 00 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 047 thick parallel spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 1596 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION TRIS CORPORATION 4 AUM Ultrafiltration Turboclean Element Series Permeate flow Model GPD m3 day M W C O 4040 N6E2U8 3 100 11 0 Performance is based on the following test conditions 500 00 ppm PEG 30 00 psi 25 C 15 recovery pH 8 00 30 minutes operation 10 000 OPERATIONAL AND DESIGN DATA Membrane Type Configuration Em Active Membrane Area Recommended Applied Pressure Maximum Applied Pressure Recommended Operating Temperature
21. 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane y SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION LA C 8 ACM RO Element Series TRIS gt CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 ACM3 UWAN 12 000 45 0 99 20 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C
22. Maximum Operating Temperature Feedwater pH Range Max Chlorine Concentartion AUM Advanced Ultrafiltration Membrane opiral Wound Turboclean Shell 41 ft 3 8 m 100 140 psi 7 10 bar 150 psi 10 3 bar 122 F 50 C 2 11 continuous 180 0 ppm pH 9 11 Maximum SDI 15 minutes 5 0 Va d Maximum Turtudifv 1 NTU PADDING AMON sinisiin nne ia EN iDa Whey Fractionation Dee hh i MN NN A WW AAR 1 UU M Wu Wl I ii I uu M TS eT WAN WAN A Bee x usa i NA tp Y d Element Weight 12 5 4 Length A 38 965 Diameter B 3 8 96 Permeate Tube C 0 83 21 2 Units in pounds and inches units in paranthesis in kilograms and millimetes Dim A does not include ATD Mechanical Configuration Sanitary Style Core Tube ATD not included with element Feed Spacer 0 065 thick diamond spacer Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION 3 8 TS50 High Temperature Turboclean Element TRI gt e rr M Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 94 3838 08D1U8 1 600 6 0 99 00 98 00 Performance is based on the following test conditions 2 000 00 ppm
23. 1 NTU olei m Milk Concentration LN IK d R cy Element Weight 12 5 4 Length A 39 984 Diameter B 3 8 96 Permeate Tube C 0 83 21 2 Units in pounds and inches units in paranthesis in kilograms and millimetes Dim A does not include ATD Mechanical Configuration Sanitary Style Core Tube ATD not included with element Feed Spacer 0 045 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Zz 3 8 ACM High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 3840 M2D2X3 1000 3 0 99 50 98 50 Performance is based on the following test conditions 2000 ppm NaCl 225 psi 25 C 15 recovery pH 8 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Configuration Spiral Wound Turboclean Shell Active Membrane Area 40 ft 3 7 m R
24. 1 NTU Application Beverage Water Make Up Element Weight 15 7 Length A 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 62 15 9 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Desal DuPont Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane ss SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Lum 8 ACM RO High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 M1F1W1 5 00 21 0 99 00 98 00 Performance is based on the following test conditions 2 000 00 ppm NaCl 225 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Configuration Spiral Wound High Temperature Turboclean Shell Active Membrane Area 2 0 ft 24 8 m Reco
25. 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Application Coffee Extract Concentration UHT Val ul MU 1 WA l 1 i l HT FIPIPPIT TIT l ull ll UA Element Weight 15 7 Length A 38 8 984 Diameter B 3 8 96 Permeate Tube C 0 83 21 2 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Sanitary Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane en SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION A N 6 3 AUM High Temperature UF Turboclean Element TRIS gt CORPORATION Model M W C O 6338 N6P5V9 10 000 OPERATIONAL AND DESIGN DATA Membrane Type AUM Advanced Ultrafiltration Membrane CGopnfguraton a k Spiral Wound High Temperature Turboclean Shell Active Membrane Area 157 ft 14 7 m
26. 80 ft 7 3 m Recommended Applied Pressure 20 200 psi 1 4 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 10 0 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 15 7 Length A 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Zi 4 AUM Ultrafiltration Element Series TRIS CORPORATION Model M W C O 4040 UE10 QSF 10 000 OPERATIONAL AND DESIGN DATA Membrane Type
27. 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 45 20 Length A 40 0 1 016 Diameter B 8 5 215 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TriSep ACM3 Composite LZ RO Membrane Elements TRISS CORPORATION The ACM3 membrane offers the highest rejection 99 5 but operates at lower pressure than the ACM1 or ACM2 typically at 125 175 psi 9 12 bar The lower specific flux of this membrane compared to the ACM4 and ACMS allows for a more balanced hydraulic flow through the system and more balanced permeate flux rates due to the high osmotic pressure of these feedwaters 4040 ACM3 TSA 4 diameter by
28. Spiral Wound Fiberglass Outer Wrap with FoulGuard Technology Active Membrane Area 88 ft 8 2 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 2NTU Element Weight 15 7 Length A 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 62 15 9 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Desal DuPont Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane En SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION LO 4 X 20 Low Fouling RO Element Series TR
29. 4 0 Maximum Turbidity 1 NTU Element Weight 50 23 Length A 40 00 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 028 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TriSep TS80 TS83 and XN45 L MN Low Fouling TRI CIS Nanofiltration Elements CORPORATION TriSep offers two different nanofiltration NF membrane chemistries the TS80 and the XN45 Both are based on proprietary and patented technology developed by DuPont The unique chemistries of these membranes allow them to have lower organic fouling than standard 344 type NF membranes The TS80 is typically used in municipal membrane softening applications It has a higher relative sodium chloride rejection 90 than the XN45 30 The TS80 or its higher flow cousin are excellent choices to remove THM precursors color iron and hardness from surface and well waters The XN45 is typically used in process application where there is a de
30. X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane Configuration Spiral Wound Fiberglass Outer Wrap with FoulGuard Technology Active Membrane Area 400 ft 37 2 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 2NTU K 20 3 Veehnelegy L 1 A i i KK Je id B Es itn i xt D y E Del Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 028 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane Sane s hi SOLUTIONS TriSep Corporation 93 South La Patera
31. 1 NTU Element Weight 50 23 Length A 40 0 1 016 Diameter B 8 5 215 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com emm TriSep Corporation Chemical Manual TRIS gt CORPORATION TriSep Corporation Membrane Support Chemicals Following is a copy of TriSep s chemical catalog with information about our full line of membrane support chemicals Two of the greatest concerns facing membrane system designers and operators are control of foulants and developing efficient system cleaning protocols that do not adversely affect membrane performance As a leading manufacturer of membrane elements TriSep made these two criteria the cornerstones for developing our chemical product line In 1995 TriSep assigned a team of engineers and chemists the task of developing membrane support products that would provide maximum efficiency with 100 membrane compatibility After extensive laboratory research and highly s
32. 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU jojo e Tel ae ee eee eee ee Whey Concentration d WWW III d LL TRATAR LE Li A AM l d WAI M N d Z a F Element Weight 12 5 4 Length A 38 965 Diameter B 3 8 96 Permeate Tube C 0 83 21 2 Units in pounds and inches units in paranthesis in kilograms and millimetes Dim A does not include ATD Mechanical Configuration Sanitary Style Core Tube ATD not included with element Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane EE SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION oO NN 3 8 XN45 High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 3838 N2D1U8 1700 6 0 95 00 92 00 Performance is based on the following test conditions 2000 ppm MgSO4 110 psi 25 C 15 recovery pH 8 30 minutes operation OPERATIONAL AND DESIGN DATA
33. 20 200 psi 1 4 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 10 0 ppm Maximum Feed Flow 95 GPM 22 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU eelere In E Fruit Juice Must Refining m J C p W w v Element Weight 40 18 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 047 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Lum 9 ACM LP Low Pressure RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 M5E6T6 11 000 41 6 98 50 97 50
34. 270 ft 24 8 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 95 GPM 22 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 2NTU ele Lee Peptide Concentration Element Weight 40 18 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 047 thick parallel spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION lt 8 X 20 RO High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day
35. 1 NTU Application Pharmaceutical Separations LU KIA NN l eeh 2 o d E maus Element Weight 12 5 4 Length A 38 75 984 Diameter B 3 80 96 Permeate Tube C 0 83 21 2 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Sanitary Style Core Tube Feed Spacer 0 045 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane ee ee SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION ow NN 3 8 XN45 High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 3840 N2J4U9 1 300 4 0 95 00 92 00 Performance is based on the following test conditions 2 000 0 ppm MgSOA 110 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type XN45 Polyamide Advanced Nanofiltration Membrane COMMUN ANON EEN Spiral Wound Turboclean Shell Active Membrane Area 53 ft 4 9 m Recommended Applied Pressure
36. 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 15 7 Length A 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION v 4 ACM RO Element Series TRIS gt CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 ACM2 TSOA 2 450 9 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanc
37. 5 0 Maximum Turbidity 1 NTU Application Beverage Water Make Up n o c m D am et k Element Weight 45 20 Length A 40 1016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 028 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane ku nF I Y i SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Oo NN 8 AUM UF High Temperature Turboclean Element TRIS CORPORATION Permeate flow Model GPD m3 day M W C O 8040 M8F2W6 10 000 37 0 3 500 Performance is based on the following test conditions 500 0 ppm Dextran 110 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Tvpe AUM Advanced Ultrafiltration Membrane Configuration Spiral Wound High Temperature Turboclean Shell Active Membrane Area 252 ft 23 4 m Recommended Applied Pressure
38. Steam Recovery Element Weight 40 18 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 047 thick parallel spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION p SN 8 X 20 RO High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 N1C8S4 7 100 26 0 99 00 98 00 Performance is based on the following test conditions 2 000 00 ppm NaCl 225 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane Configuration Spiral Wound High Temperature Turboclean Shell Active Membrane Area 270 ft 24 8 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pr
39. 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1NTU Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION oN 8 ACM LP Low Pressure RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 ACM5 TSFA 11 900 45 0 98 50 97 50 Performance is based on the following test conditions 2 000 00 ppm NaCl 150 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM LP Fully Aromatic Polyamide Low Pressure Advanced Composite CGopnfguraton a k Spiral Wound Fibergl
40. Recommended Applied Pressure Maximum Applied Pressure Recommended Operating Temperature Feedwater pH Range Chlorine Tolerance Maximum Feed Flow Minimum Brine Flow Permeate Flow Ratio Maximum SDI 15 minutes Maximum Turbidity Element Weight Length A 45 20 40 0 1 016 Diameter B 7 9 200 PRODUCT SPECIFICATION 8 CA RO Element Series Minimum Salt Rejection Average Salt Rejection 8040 SB50 TSA 95 00 92 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 420 0 psi 25 C 15 recovery pH 5 5 30 minutes operation SB Cellulose Acetate Blend Spiral Wound Fiberglass Outer Wrap 350 ft 32 5 m 200 500 psi 14 34 bar 600 psi 41 bar 50 90 F 10 32 C 5 5 nominal 4 7 0 5 ppm nominal 1 0 ppm max 80 GPM 18 m3 hr 5 1 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engin
41. 1 NTU APPIANO c Pa Lactose Concentration Element Weight 40 18 Length A 38 965 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Dim A does not include ATD Mechanical Configuration Filmtec Style Core Tube ATD not included with element Feed Spacer 0 046 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION oN 8 ACM RO High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8038 M2C9X3 5800 21 0 99 00 98 00 Performance is based on the following test conditions 2000 ppm NaCl 225 psi 25 C 15 recovery pH 8 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Configuration Spiral Wound High Temperature Turboclean Shell Active Membrane Area 225 ft 20 9 m Recommended Applied Pressure
42. 40 200 psi 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 5 ppm nominal 1 0 ppm max Maximum Feed Flow 25 GPM 5 6 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Application Peptide Demineralization UHT Val ul MU 1 WA l 1 i l HT FIPIPPIT TIT l ull ll UA Element Weight 15 7 Length A 38 8 984 Diameter B 3 8 96 Permeate Tube C 0 83 21 2 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Sanitary Style Core Tube Feed Spacer 0 047 thick parallel spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane en SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Za 4 ACM RO Turboclean Element
43. COMM OQUPAUON S Active Membrane Area Recommended Applied Pressure Maximum Applied Pressure Recommended Operating Temperature Feedwater pH Range Chlorine Tolerance Maximum Feed Flow Minimum Brine Flow Permeate Flow Ratio Maximum SDI 15 minutes Maximum Turbidity PRODUCT SPECIFICATION 8 5 CA RO Element Series Minimum Salt Rejection Average Salt Rejection 8540 SB50 TSA 95 00 92 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 420 0 psi 25 C 15 recovery pH 5 5 30 minutes operation SB Cellulose Acetate Blend Spiral Wound Fiberglass Outer Wrap 440 ft 40 4 m 200 500 psi 14 34 bar 600 psi 41 bar 50 90 F 10 32 C 5 5 nominal 4 7 0 5 ppm nominal 1 0 ppm max 80 GPM 18 m3 hr 5 1 Element Weight Length A 50 23 40 0 1 016 Diameter B 8 5 215 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater co
44. 365 ft 33 5 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION 8 ACM RO Element Series TRI gt CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 ACM1 UWA 8 800 33 0 99
45. Not applicable Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 100 GPM 22 7 m3 hr 4 y M Minimum Brine Flow Permeate Flow Ratio 5 1 V S y N Maximum SDI 15 minutes 5 0 APPROV d Maximum Turbudtv 1 NTU Allee le PL Lactose Concentration Element Weight 30 14 Length A 38 965 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Dim A does not include ATD Mechanical Configuration Filmtec Style Core Tube ATD not included with element Feed Spacer 0 065 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane INCLUSE SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION TRIS CORPORATION 8 ACM RO High Temperature Turboclean Element Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection 94 Rejection 94
46. 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU TS80 A ocn Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane MER nni SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION LA 8 TS80 Nanofiltration Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 TS83 UWAN 11 000 41 0 98 50 97 00 Performance is based on the following test conditions 2 000 0 ppm MgSOA 110 0 psi 25 C 15 recovery
47. ACM Fully Aromatic Polyamide Advanced Composite Membrane ele Lett GIOI uu uuu u carte eb T m Spiral Wound Fiberglass Outer Wrap Active Membrane Area 85 ft 7 9 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 15 7 Length A 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION 4 ACM RO Element Ser
48. 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 15 7 Length A 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 028 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION v 4 ACM LP RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 ACM4 TWF 3 500 13 0 99 00 98 00 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM LP Fully Aromatic Polyamide Low Pressure Advanced Composite Cong AMON uuu aa E oa akana URS Spiral Wound Fiberglass Outer Wrap Active Membrane Area 88 ft
49. Maximum Turbidity AMM Advanced Microfiltration Membrane Spiral Wound Fiberglass Outer Wrap 80 ft 7 4 m 5 200 psi 0 3 14 bar 600 psi 41 bar 35 113 F 2 45 C 2 11 continuous 10 0 ppm 20 GPM 4 5m3 hr 5 1 5 0 1 NTU Element Weight Length A 15 7 40 00 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Feed Spacer TriSep Style Core Tube 0 031 thick diamond spacer Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION lt 4 AMM Microfiltration Element Series TRIS CORPORATION Permeate flow Model GPD m3 day Pore Size 4040 TM10 QXA 2 600 9 0 0 2 microns Permeate flow is based on the clean water flux at the following test conditions 10 0 psi 25 C pH 8 0 15 recovery 15 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type AMM Advanced Microfiltration Membrane Cong AMON sa ciuem tears aa E oa akana URS Spiral Wound Fiberglass Outer Wrap Active Membrane Area 65 ft 6 0 m Recommended Applied Pressure 5 200 psi 0 3 14 bar
50. Minimum Brine Flow Permeate Flow Ratio Maximum SDI 15 minutes Maximum Turbidity Element Weight Length A 50 23 40 0 1 016 Diameter B 8 5 215 SB Cellulose Acetate Blend Spiral Wound Fiberglass Outer Wrap 440 ft 40 4 m 200 500 psi 14 34 bar 600 psi 41 bar 50 90 F 10 32 C 5 5 nominal 4 7 0 5 ppm nominal 1 0 ppm max 80 GPM 18 m3 hr 5 1 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane Y SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TRIS CORPORATION Permeate flow Model GPD m3 day 8540 SB50 TSA 10 000 37 0 PRODUCT SPECIFICATION 8 5 CA RO Element Series Minimum Salt Rejection Average Salt Rejection 95 00 92 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 420 0 psi 25 C 15 recovery pH 5 5 30 minutes operation OPERATIONAL AND DESIGN DATA
51. 5 0 Maximum Turbidity 1 NTU Element Weight 15 7 Length A 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION 2 4 ACM LP Low Pressure RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 ACM4 TSF 3 350 12 0 99 00 98 00 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM LP Fully Aromatic Polyamide Low Pressure Advanced Composite Configuration Spiral Wound Fiberglass Outer Wrap Active Membrane Area 85 ft 7 9 m Recommended Applied Pressure 40 300 psi 3 21 bar
52. ACM LP Fully Aromatic Polyamide Low Pressure Advanced Composite Configuration Spiral Wound Turboclean Shell Active Membrane Area 355 ft 32 6 m Recommended Applied Pressure 40 300 psi 3 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU olei m Dialysis Make up Water Element Weight 45 20 Length A 40 00 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 1596 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com
53. H ONi SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION S 8 3 ACM RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8340 ACM2 TSOA 11 000 41 0 99 00 98 00 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane COMM QUIN GIOI L ste uqu La cet T Spiral Wound Fiberglass Outer Wrap Active Membrane Area 415 ft 38 1 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 50 23 Length A 40 0
54. Not applicable Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU lee len u uuu eee eee eee eee Lactose Concentration AK MM Element Weight 12 5 4 Length A 39 984 Diameter B 3 8 96 Permeate Tube C 0 83 21 2 Units in pounds and inches units in paranthesis in kilograms and millimetes Dim A does not include ATD Mechanical Configuration Sanitary Style Core Tube ATD not included with element Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 1596 Engineered Membrane iw SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Zam 3 8 XN45 High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD
55. 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 2 NTU Element Weight 15 7 Length A 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Jai 4 X 20 Low Fouling RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 X201 TSDA 2 450 9 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane Configuration
56. 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 6 GPM 1 4 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 7 3 2 Length A 40 0 1 016 Diameter B 2 5 63 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Lum 4 ACM LP Low Pressure RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 ACM4 TSA 3 450 13 0 99 00 98 00 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane
57. Lun 8 ACM RO High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 M2P3W7 9 200 34 0 99 50 98 50 Performance is based on the following test conditions 2 000 00 ppm NaCl 225 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane CGopnfguraton a k Spiral Wound High Temperature Turboclean Shell Active Membrane Area 385 ft 35 4 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 1000 psi 69 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 4 0 Maximum Turbidity 1 NTU 7 16 0 0121 0 u u nee ee Dialysis Make up Water gn UN d n s I e e c K CC i A B w w gr as w GE we CN gt Element Weight 50 23 Length A 40 00 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28
58. 1 NTU Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane y SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION A lt 8 ACM LP Low Pressure RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 ACM4 TSFA 14 600 55 0 99 00 98 00 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM LP Fully Aromatic Polyamide Low Pressure Advanced Composite Cong AMON uuu aa E oa akana URS Spiral Wound Fiberglass Outer Wrap Active Membrane Area 365 ft 33 5 m Recommended Applied Pressure 50 300 psi 3 21 bar Maximum Applied Pressure 600 psi
59. 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 95 GPM 22 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Applicators Beer Kettle Condensate Recovery Element Weight 40 18 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 047 thick parallel spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Lum 8 ACM LP Low Pressure RO Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 M4E6T6 14000 52 0 99 00 98 00
60. PRODUCT SPECIFICATION 9 ACM RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 ACM2 TSFA 9 700 36 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Configuration Spiral Wound Fiberglass Outer Wrap Active Membrane Area 365 ft 33 5 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube
61. SB Cellulose Acetate Blend Spiral Wound Fiberglass Outer Wrap 415 ft 38 1 m 200 500 psi 14 34 bar 600 psi 41 bar 50 90 F 10 32 C 5 5 nominal 4 7 0 5 ppm nominal 1 0 ppm max 80 GPM 18 m3 hr 5 1 Element Weight Length A 50 23 40 0 1 016 Diameter B 8 3 210 Permeate Tube C 1 14 29 0 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Osmo Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com Competitive Element Replacement Guide k Hydranautics Style Elements TRIS IS P CORPORATION Hydranautics Replacement Elements TriSep Model Number Hydranautics Model Comments 8540 ACM2 TSFA 8540 LS Y CPA2 same diameter different permeate tube 8540 ACM4 TSFA 8540 UHY ESPA Same diameter different permeate tube 8540 SB20 TSA 8540 MS Y CAB2 Same diameter different permeate tube 8540 SB50 TSA 8540 MS Y CABI same diameter different permeate tube 8540 TS80 TSFA same diameter different permeate tube TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA
62. SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION a 3 8 XN45 High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 3838 N2D3U8 1700 6 0 95 00 92 00 Performance is based on the following test conditions 2000 ppm MgSO4 110 psi 25 C 15 recovery pH 8 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type XN45 Polyamide Advanced Nanofiltration Membrane Configuration Spiral Wound Turboclean Shell Active Membrane Area 68 ft 6 2 m Recommended Applied Pressure Not applicable Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 5 ppm nominal 1 0 ppm max Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU APPIANO c Pa Milk Demineralization i MUI LU AM A LI
63. TriPol 8010 TriPol 8010 is a good performance low cost scale inhibitor formulated to protect and enhance the performance of RO and NF membranes by inhibiting the formation of carbonate scales associated with calcium barium and strontium as well as sulfate scales TriPol 8010 is a pure acrylic acid product with no added phosphates or phosphanates TriPol 7510 TriPol 7510 was designed to provide control for waters with moderate to high scaling tendencies that require a low level of assimible organic carbon AOC This scale inhibitor contains no organic polymers and is 100 phosphate based It works well on wastewaters with high levels of calcium phospahte scaling potential or with high levels or iron or metal hydroxides TriPol 8510 TriPol 8510 was scientifically designed to provide control for waters with moderate to high scaling tendencies with moderate levels of silica This high tech scale inhibitor contains a blend of an acrylic acid co polymer and an organic phosphonate that gives a high degree of protection especially with high levels of saturation of sulfate scales TriPol 8510 is approved by NSF for use in drinking water at feed concentration of up to 4 ppm TriPol 9010 TriPol 9010 was chemically engineered to meet the pretreatment demands of state of the art high recovery RO and NF system with high fouling tendencies TriPol 9010 offers increased protection against calcium carbonate scaling while still providing a hig
64. TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION lt N 8 X 20 Low Fouling RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 X201 TSFA 9 700 36 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane Configuration Spiral Wound Fiberglass Outer Wrap with FoulGuard Technology Active Membrane Area 365 ft 33 5 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 2 NTU
65. 4 00 101 Permeate Tube C 0 62 15 9 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Feed Spacer 0 031 thick diamond spacer Desal DuPont Style Core Tube Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION LAN 4 ACM RO Turboclean Element TRIS gt CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 O6G1Y2 1350 5 0 99 00 98 00 Performance is based on the following test conditions 2000 ppm NaCl 225 psi 25 C 15 recovery pH 8 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Configuration Spiral Wound Turboclean Shell Active Membrane Area 88 ft 8 1 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range
66. Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com Competitive Element Replacement Guide x N GE Osmonics Style Elements TRIS IS P CORPORATION GE Osmonics Replacement Elements TriSep Model Number GE Osmonics Model Comments 4040 ACM2 TSOA 411 HR PA 411 HF PA Same diameter and permeate tube 8340 ACM2 TSOA 811 HR PA 811 HF PA Same diameter and permeate tube 8340 SB20 TSOA 811 HR same diameter and permeate tube TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 298 PRODUCT SPECIFICATION ES 4 ACM RO Element Series TRIS gt CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 ACM2 TSOA 2 450 9 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery
67. SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Za 4 ACM RO Element Series TRIS gt CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 ACM1 TSF 1 900 7 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Configuratio EE Spiral Wound Fiberglass Outer Wrap Active Membrane Area 85 ft 7 9 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 15 7 Length A 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Units in
68. 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 4 0 Maximum Turbidity 1 NTU Element Weight 50 23 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 028 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Za 8 TS80 Nanofiltration Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 TS83 UWAN 11 000 41 0 98 50 97 00 Performance is based on the following test conditions 2 000 0 ppm MgSOA 110 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ANM Aromatic Polyamide Advanced Nanofiltration Membrane eidele e EE Spiral Wound Fiberglass Outer Wrap Active Membrane Area 400 ft 37 2 m Recommended
69. 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Application RO Permeate Polisher Element Weight 45 20 Length A 38 965 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Dim A does not include ATD Mechanical Configuration Filmtec Style Core Tube ATD not included with element Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane End nF I Y i SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION 8 XN45 NF High Temperature Turboclean Element TRIS SP c HS Ch A T di Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8038 N2D1U8 9 000 34 0 95 00 92 00 Performance is based on the following test conditions 2 000 00 ppm MgSO4 110 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type XN45 Po
70. 805 964 8003 805 964 1235 fax www trisep com 0105 302 PRODUCT SPECIFICATION 8 5 ACM RO Element Series TRIS gt CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8540 ACM2 TSFA 11 500 43 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane E ele Le UT AU ON ee Spiral Wound Fiberglass Outer Wrap Active Membrane Area 440 ft 40 4 m Recommended Applied Pressure 50 300 psi 3 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 45 20 Length A 40 0 1 016 Diameter B 8 5 215 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kil
71. Based on the results of this test the Trisep T9880 membrane is a superior mem brane for membrane softening applications requiring high inorganic and THMFP rejections at low operating pressures The TS80 operated on this feedwater with a minimum of pretreatment and chemical cleanings Table 1 Daytona Beach Raw Water Analysis Solute Raw Water Concentration TOXFP 1120 Color cpu 31 NPDOC ppm 9 TDS ppm 368 Na ppm 30 Total Hardness ppm as Caco3 289 Calcium Hardness ppm as caco3 264 Cl ppm 29 Alkalinity ppm as caco3 295 Fe ppb 372 pH 6 3 TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 367 Table 2 Daytona Beach lonic Rejections Solute Rejection versus Operating Time 470 hrs 4754 hrs 8152 hrs TOXFP1 99 97 98 THMFP 98 99 98 Color 99 97 98 NPDOC 97 99 99 TDS 97 97 96 Na 87 84 83 Total Hardness 97 99 98 Calcium Hardness 99 99 98 Cl 94 93 94 Alkalinity 96 93 Fe 99 96 97 1TOXFP Total organic halide formation potential THMFP Trihalomethane formation potential 3NPDOC Non purgable dissolved organic carbon TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax e www trisep com 0703 368 s TRIS S P CORPORATION BULLETIN NO TYPE APPLICATION CLIENT LOCATION PRODUCT PROCESS CONCLUSIONS APPLICATION BULLETIN
72. TriSep Corporation TRIS Digital Product Catalog CORPORATION Rev 102808 Thank you for your interest in Trisep Corporation products Following is the latest version of our product catalog In an effort to give our customers the most current information on our products in a timely and low cost format we have spent considerable time and effort to make the catalog user friendly with detailed technical administrative and sales related information This catalog is in Adobe Acrobat format and you can browse the catalog one page at a time or you can jump to specific pages Following this page is the table of contents which lists the page numbers There are hyperlinks to the different sections and if you click on the section you want in the contents it will jump you to that page To return to the first page click on the double left arrow at the top of the page To proceed one page at a time click on the right arrow This new version of the catalog includes the new SpiraSep Backflushable Ultrafiltration Membrane element This product is designed to remove suspended solids from surface and waste waters as well as removal of oocysts such as giardia and crytosporidium for drinking water applications New data on bypass information for our Turboclean sanitary elements shows how you can save up to 25 35 of your by pass energy costs by using this product as compared to standard cage or net wrapped elements This manual also contains the newest man
73. adversely effect the system economics PACKAGING TriPol 8510 is shipped as a liquid in gallon SOLUTION sample sizes 5 gallon 40 Ib plastic pails and 55 500 Ib gallon plastic drums Pricing is F O B our factory in Goleta CA Salem VA or Duisberg Germany Delivery for most orders 1s 1 2 days after receipt of order TriPol 8510 protects and enhances the operation of RO and NF systems by controlling mineral scale formation due to carbonate sulfate and fluoride compounds In most water types proper use of TriPol 8510 can significantly increase allowable system recoveries and thus expand the suitability MSDS SHEETS m For the most up to date information on MSDS sheets for use in a wider range of applications please contact our web site at www trisep com TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 313 wm TriSep Corporation Chemical Manual LAS nnd TRIS S CORPORATION TRIPOL 9010 APPLICATION SCALE INHIBITOR TriPol 9010 is metered into the feed water at a DI SPERS ANT point where turbulent flow will ensure adequate chemical mixing prior to entering the RO or NF system This is usually done prior to the cartridge filters and high pressure pump Dosing rates vary 2 Extends useful membrane life depending on feedwater quality and recovery but e Superior control of carbonate normally run between 2 and 5 ppm For exact sca
74. 0 10 20 30 40 50 60 Bypass TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 37 TurboClean Sanitary Elements wm for Beverage Applications TRIS gt CORPORATION TurboClean elements have been used extensively in the beverage markets From production of bottled water to purification of water used in beer wine or soft drinks many bottlers see the advantage of using sanitary elements in their beverage applications Although not required by law and not classified as a food by the USDA contamination of these products can incur huge costs 1f product recalls of contaminated products are required The sanitary nature of the TurboClean element provides a continous by pass flow around the outside of the element This eliminates the stagnant area normally present on standard brine seal elements which can result in bio growth that can contaminate the beverage product This stagnant area Is difficult to clean or sanitize in place as there 1s no flow of cleaning or sanitizing chemicals into this area If cleaning or sanitizing chemicals do get into this area it is difficult to predict the rinse out time for these chemicals Standard net wrap sanitary elements have traditionally been used in food and dairy applica tions Due to the high by pass flow inherent with these designs food and dairy systems incorporate large recirculation pumps to insure a certain
75. 365 ft 33 5 m Recommended Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane EE SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION S NN 8 TS80 Nanofiltration Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 TS80 TSFA 9 000
76. Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Lum 3 8 ACM High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 3840 M2D7X3 1 000 3 0 99 50 98 50 Performance is based on the following test conditions 2 000 00 ppm NaCl 225 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Con figuratloni L uuu uuu uui Spiral Wound High Temperature Turboclean Shell Active Membrane Area 40 ft 3 7 m Recommended Applied Pressure Not applicable Maximum Applied Pressure 1000 psi 69 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 25 GPM 5 6 m3 hr sD J A Minimum Brine Flow Permeate Flow Ratio 5 1 u s y N Maximum SDI 15 minutes 5 0 appro 4 Maximum Turbidity 1 NTU e eje lor Le E Whey Concentration M JA WIR MEHR eed VALVE RELA A T 4 WUAYYWWWWWWWWWWW ETETEN a nM AUN WAY A ML MA 1 ALETA 1
77. Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane ipa s SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION lt 8 X 20 Low Fouling RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 X201 UWA 10 400 39 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane eidele e EE Spiral Wound Fiberglass Outer Wrap with FoulGuard Technology Active Membrane Area 400 ft 37 2 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F
78. Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 10 0 ppm Maximum Feed Flow 25 GPM 5 6 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 15 7 Length A 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 047 thick parallel spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION lt 4 AMM Microfiltration Element Series TRIS CORPORATION Permeate flow Model GPD m3 day Pore Size 4040 TM10 QXF 2 500 9 0 0 2 microns Permeate flow is based on the clean water flux at the following test conditions 10 0 psi 25 C pH 8 0 15 recovery
79. Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 15 7 Length A 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION L O38 4 ACM LP Low Pressure RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 ACM5 TWF 2 900 9 0 98 50 97 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 150 0 psi 25 C 15 recovery pH
80. Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 2NTU Application Waste Water High Pressure Element Weight 40 18 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 046 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION ow NN 8 X 20 Low Fouling RO Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 N1G3T4 7100 26 0 99 00 98 00 Performance is based on the following test conditions 2000 ppm NaCl 225 psi 25 C 15 recovery pH 8 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane Configuration
81. NJ Lei A ae E W w d Y m Permeate Tube C 1 14 29 0 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Osmo Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 1596 Engineered Membrane am SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com Zs TRIS gt CORPORATION Permeate flow Model GPD m3 day 8340 N6J8W8 15 000 56 0 PRODUCT SPECIFICATION 8 3 AUM Ultrafiltration Turboclean Element Series M W C O 10 000 Performance is based on the following test conditions 500 0 ppm 10K PEG 60 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type Oe TN e E Active Membrane Area Recommended Applied Pressure Maximum Applied Pressure Recommended Operating Temperature Feedwater pH Range Chlorine Tolerance sinesine Maximum Feed FlowW Minimum Brine Flow Permeate Flow Ratio Maximum SDI 15 minutes
82. ONRFOd8nIJ3OO 049 901 Ir Omd3sni3NOO S8v ecl S NOHdMOSJG IVRHIVW ON Lad PALO S ON Will 14 O3AO3ddv ava NOIlIdli2s3d KE SNOISIA33l TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 w SPIRASEP Jes ms TRI SP Ultrafiltration Membrane Technology CORPORATION EP T 11443 WEIGHT SHEET TOF ATRI SpiraSep Pilot Manifold Assembly IZE DWG NO o LLI E eQ 5 N E Bei E uc N 2 lt N z S SE DE lt c Di OQ 3 mg lt H Jo IE 2 Lu C z S gt lt 2 Qo lt dio o lt 22 a T Zz U a c O ol oi 2 G S s x 2 oia 9 06 Feb fo i i eo ol a m wj Z Gaja e e ed lt z HSS2 x ul TERU D x Ugga r lt Saag oo o wj u ol zm uuoloz OY xwOO lt CO lt 2532 3555 82 lt ta 2 lt JAA x len SIE z s Geo E gt 89 68z z9 2 g Tau n zago at Ze Do wi en Z E lt O O lt z w S bs z o a z lt gt ec lt C a 2 a EM THE INFORMATION CON DRAWING IS THE SOLE P TRISEP ANY REPRODUCTION IN PART OR AS A WHOLE WITHO PERMISSION OF TRISEP P o 7 ENS o o T e No kel lt lt L lt u N LLI lt N QO c oo co O O ca lt TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964
83. Performance is based on the following test conditions 2 000 0 ppm NaCl 150 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM LP Fully Aromatic Polyamide Low Pressure Advanced Composite Configuration Spiral Wound Turboclean Shell Active Membrane Area 355 ft 32 6m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU EE Beverage Water Make Up d a r n C ae GA Se A car 3 L ue Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applica
84. Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Configuration Spiral Wound Turboclean Shell Active Membrane Area 85 ft 7 9 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Application Beverage Water Make Up Element Weight 15 7 Length A 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 62 15 9 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Desal DuPont Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all f
85. Solute Raw Water Concentration TOXFP ppb as cl 7164 Color cpu 210 NPDOC ppm 27 TDS ppm 41 3 Na ppm 54 Total Hardness ppm as caco3 147 Calcium Hardness ppm as cacoa 100 Cl ppm 99 Alkalinity ppm as caco3 81 Fe ppb 263 pH 8 0 TOXFP Total organic halide formation potential NPDOC non purgable dissolved organic carbon TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 369 TRIS gt CORPORATION Table 2 Melbourne lonic Rejections Rejection versus Operating Time Solute 300 hrs 3734 hrs TOXFP 97 98 THMFP 99 96 Color BDL BDL NPDOC 95 BDL TDS 94 89 Na 80 13 Total Hardness 98 96 Calcium Hardness 98 97 Cl 85 83 Alkalinity 93 Fe 98 1TOXFP Total organic halide formation potential THMFP Trihalomethane formation poetntial 3NPDOC Non purgable dissolved organic carbon NOTES The above listed rejections are actuals based on average feed brine concentrations and have not been normalized BDL means permeate concentrations were below detectabllevels The raw data for this test is available on request TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 370 Manual ing TriSep Engineer TRIS 5 CORPORATION Filtration Spectrum COCHE 00Z uoneJodjo desu Www dog desu Aq p vieuu p
86. TRICLEAN 218 pressure recirculation pump and cartridge or bag filter This cleaner works best when applied at a HIGH PH LIQUID flow rate of 8 10 gpm per 4 pressure tube or CLE ANER 30 40 gpm per 8 pressure tube at a pressure of between 20 50 psi at a pH of 11 5 Caution pH s above 12 may damage membrane Add 0 5 gallons Used to beet owes biological of TriClean 218 per 100 gallons of RO permeate organic and colloidal fouling or DI water Recirculate solution for 1 hour check on Polyamide Composite mem ing pH regularly Use sulfuric acid to lower pH brane and add additional TriClean 218 to increase pH in Shutdown pump and allow to soak for 1 hour After e Specifically formulated for use soak recirculate for an additional 20 minutes and in dairy and food processing then rinse mu PACKAGING TriClean 218 1s shipped as a liquid in 5 gallon PROBLEM plastic pails or 55 gallon plastic drums Pricing In most dairy and food processing plants world is F O B our factory in Goleta CA Salem VA wide RO NF and UF membranes can become or Duisberg Germany Delivery for most orders is fouled with biological organic and colloidal fou 1 2 days after receipt of order lants These plants must be cleaned on a daily basis to maintain a sanitary environment This rig MSDS SHEETS orous cleaning regime requires a high performance For the most up to date information on cleaner that will not adversely affect the long term MSDS sheets
87. dad Element Weight 50 23 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 028 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane N SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www triseb com PRODUCT SPECIFICATION Za 8 TS80 Nanofiltration Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 TS80 UWAN 10 000 37 0 99 00 97 00 Performance is based on the following test conditions 2 000 0 ppm MgSOA 110 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ANM Aromatic Polyamide Advanced Nanofiltration Membrane Configuration Spiral Wound Fiberglass Outer Wrap Active Membrane Area 400 ft 37 2 m Recommended Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressure 600 psi 41 ba
88. 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane w Gs p SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TRIS gt CORPORATION Permeate flow Model GPD m3 day 4040 SB20 TSA 1 600 6 0 PRODUCT SPECIFICATION 4 CA RO Element Series Minimum Salt Rejection Average Salt Rejection 98 00 97 00 Performance is based on the following test conditions 2 000 0 ppm NaCl 420 0 psi 25 C 15 recovery pH 5 5 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type Oe e EE Active Membrane Area Recommended Applied Pressure Maximum Applied Pressure Recommended Operating Temperature Feedwater pH Range Chlorine Tolerance Maximum Feed Flow Minimum Brine Flow Permeate Flow Ratio Maximum SDI 15 minutes Maximum Turbidity
89. 200 psi 1 4 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 10 0 ppm Maximum Feed Flow 95 GPM 22 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU ADDIIG300I1 uuuu uuu A degen Enzyme Fractionation Element Weight 40 18 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 047 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Lum 8 AUM UF High Temperature Turboclean Element TRIS CORPORATION Permeate flow Model GPD m3 day M W C O 8040 N6J7W6 10 400 39 0 10 000 Performance is based on the fo
90. 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 10 0 ppm Maximum Feed Flow 95 GPM 22 m3 hr sD A Minimum Brine Flow Permeate Flow Ratio 5 1 v s p A Maximum SDI 15 minutes 9 0 APPROV d Maximum Turbudtv 1 NTU ele e Tel EE Milk Fractionation Element Weight 40 18 Length A 38 965 Diameter B 7 9 200 Permeate Tube C 1 14 29 0 Units in pounds and inches units in paranthesis in kilograms and millimetes Dim A does not include ATD Mechanical Configuration Filmtec Style Core Tube ATD not included with element Feed Spacer 0 046 thick diamond spacer Engineered Membrane EE SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Z 8 AUM Ultrafiltration Turboclean Element Series TRIS CORPORATION Model M W C O 8038 N6D9V8 10 000 OPERATIONAL AND DESIGN DATA Membrane Type AUM Advanced Ultrafiltration Membrane Configuration Spiral Wound High Temperature Turboclean Shell Active Membrane Area 355 ft 33 0 m Recommended Applied Pressure Not a
91. 8038 M2D V6 7500 28 0 99 00 98 00 Performance is based on the following test conditions 2000 ppm NaCl 225 psi 25 C 15 recovery pH 8 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Configuration Spiral Wound High Temperature Turboclean Shell Active Membrane Area 288 ft 26 8 m Recommended Applied Pressure Not applicable Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 95 GPM 22 m3 hr a Y M Minimum Brine Flow Permeate Flow Ratio 5 1 K y W Maximum SDI 15 minutes 5 0 appro d Maximum T urbuditv 1 NTU Application Whey Concentration Element Weight 40 18 Length A 38 965 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Dim A does not include ATD Mechanical Configuration Filmtec Style Core Tube ATD not included with element Feed Spacer 0
92. 805 964 8003 PRODUCT SPECIFICATION Za 2 5 X 20 Low Fouling Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 2540 X201 TSF 650 2 0 99 00 98 00 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane Configuration Spiral Wound Fiberglass Outer Wrap Active Membrane Area 26 ft 2 4 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 6 GPM 1 4 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 7 3 2 Length A 40 0 1 016 Diameter B 2 5 63 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthes
93. 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION A 4 ACM High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 M4P3U8 3 200 12 0 99 00 98 00 Performance is based on the following test conditions 2 000 00 ppm NaCl 225 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM LP Fully Aromatic Polyamide Low Pressure Advanced Composite CGopnfguraton a k Spiral Wound High Temperature Turboclean Shell Active Membrane Area 80 ft 7 4 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU PRONG AMOI u u idtastsistentt iA Dialysis Make up Water Element Weight 15 7 Length A 40 00 1 016 Di
94. Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Appligal IOni eee qasa 6 Dialysis Make up Water Element Weight 15 7 Length A 40 00 1 016 Diameter B 4 0 101 Permeate Tube C 0 62 15 9 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Desal DuPont Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane EE SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TRIS CORPORATION Permeate flow Model GPD m3 day 4040 N6P3X4 3 100 11 0 PRODUCT SPECIFICATION 4 AUM Ultrafiltration Turboclean Element Series M W C O 10 000 Performance is based on the following test conditions 500 00 ppm PEG 30 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type
95. Maximum Turbidity 1 NTU Application Beverage Water Make Up Element Weight 45 20 Length A 40 00 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 028 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane Pest SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION A lt 8 ACM RO High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 M2L7S4 7 200 27 0 99 00 98 00 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Conn B gs le opiral Wound Turboclean Shell Active Membrane Area 270 ft 24 8 m Recommended Applied Pressure
96. Membrane Type XN45 Polyamide Advanced Nanofiltration Membrane Configuration E Spiral Wound Turboclean Shell Active Membrane Area 68 ft 6 2 m Recommended Applied Pressure Not applicable Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 5 ppm nominal 1 0 ppm max Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU leiere Rm Lactose Demineralization ll i WU H WWW BAI WW u WM AAAAN m e Ed Element Weight 15 T Length A 38 965 Diameter B 3 8 96 Permeate Tube C 0 83 21 2 Units in pounds and inches units in paranthesis in kilograms and millimetes Dim A does not include ATD Mechanical Configuration Sanitary Style Core Tube ATD not included with element Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane
97. PRODUCT SPECIFICATION A lt 8 X 20 Low Fouling RO Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 N1P3T6 9 200 34 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane Cong AMON uuu aa E oa akana URS Spiral Wound Turboclean Shell with FoulGuard Technology Active Membrane Area 355 ft 32 6 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 2NTU Applicators Dialysis Make up Water Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in para
98. Performance is based on the following test conditions 2000 ppm NaCl 225 psi 25 C 15 recovery pH 8 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM LP Fully Aromatic Polyamide Low Pressure Advanced Composite Configuration Spiral Wound Turboclean Shell Active Membrane Area 355 ft 32 6 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU ADDIICOUOFI cesses een ee chess cuan Beverage Water Make Up Element Weight 45 20 Length A 40 1016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable
99. Rejection Rejection 8040 N1J4T9 9 400 35 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane ONTO ON I uu aan wa Spiral Wound Turboclean Shell with FoulGuard Technology Active Membrane Area 355 ft 32 6 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 2NTU Application Peptide Concentration Element Weight 40 18 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond
100. element has advantages over standard net wrapped elements by reducing by pass flow and having a more robust construction ts W 4 3 E B A ua e E m j gem mL UE E b BU 1 F TurboClean elements are available for all TriSep membranes including reverse osmosis nanofiltration ultrafiltration and microfiltration TurboClean HWS elements should not be subjected to changes in water temperature that exceed 3 5 F 2 C per minute Feed pressures should be kept below 60 psi 4 bar during the sanitization process During high temperature sanitization feed brine differential pressure drops should be kept below 5 psi 0 3 bar per element or 30 psi 2 bar per pressure tube 10 06 TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 36 TurboClean By Pass Graphs versus Standard Sanitary Elements TRIS gt CORPORATION Percent Bypass Flow vs Delta P 60 00 Net Wrapped 55 00 s Caged 50 00 Tailed 7 Hard Shell 45 00 z Ke 40 00 cb LL 35 00 30 00 Q ty 25 00 7 9 20 00 2 m SZ 15 00 UU U U U 10 00 5 00 0 00 T T T T T T T l 0 2 4 6 8 10 12 14 16 Delta P psid Annual Cost of Power Consumed by Bypass Flow for Various HP 0 10 kwh 25 20 Yearly Bypass Power Cost x 1000
101. levels reported TriSep s ACM elements have maintained permeate water quality permeate water flow rates consistent low operating pressures contributing towards meeting boiler feedwater specifications The Trisep ACM elements have not been cleaned and continue to perform without indications of fouling The ACM elements operate efficiently at low pressures 150 250 psi 10 2 17 bar yielding significantly lower passage of silica salt and naturally occurring low molecular weight organic compounds than does cellulosic and other thin film type reverse osmosis membranes This presents cost savings and operational maintenance advantages by reducing ion exchange resin fouling regeneration frequencies and silica leakage with fewer associated chemicals being used in the above application TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 364 APPLICATION BULLETIN um TRIS S CORPORATION BULLETIN NO ACM 03 TYPE Reverse Osmosis CLIENT Nevada Cogeneration Associates Bonneville Pacific Services Blank Mountain Plant 2 APPLICATION Low Pressure Boiler Feedwater Treatment Silica and dissolved solids TDS reduction LOCATION Las Vegas Nevada USA PRODUCT 8040 ACM1 TSA Spiral Wound Element ACM Membrane In 1993 TriSep Corporation reloaded two 2 reverse osmosis RO systems at a cogen eration power plant located in Las Vegas Nevada wi
102. which allows a portion of the concentrate to be fed back to the feed of the system This 1s sometimes desirable to increase the feed flow rate to a system without changing the system recovery You can also specify a blend flow rate which blends some feedwater with the permeate water This increases the TDS of the permeate water and allows you to increase the capacity of a TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 399 TriSep Troi Design Program A Manual ver 2 0 0 TRIS CORPORATION system without adding membrane area at the expense of permeate quality The temperature units can be selected as either C or F from the radio button next to the feedwater temperature The permeate flow recirculation flow and blend flow can be selected as either gallons per minute gpm gallons per day gpd or cubic meters per hour m3 hr The last three fields that can be entered on the top section of the screen allow you to adjust the system performance with age This allows some empirical method to account for possible degradation in membrane permeate flow which could be caused by fouling and degradation of element rejection which could be caused by wear and tear of the membrane elements The age is input in years and the flux decline coefficient Flux Decl is a decimal value which corresponds to an inverse exponential decline with most of the decline o
103. 1 016 Diameter B 8 3 210 Permeate Tube C 1 14 29 0 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Osmo Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Zum 8 5 ACM RO Element Series TRIS gt CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8540 ACM2 TSFA 11 500 43 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane COMM QUIN GIOI L ste uqu La cet T Spiral Wound Fiberglass Outer Wrap Active Membrane Area 440 ft 40 4 m Recommended Applied Pressure 50 300 psi 3 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range
104. 15 minutes 4 0 Maximum Turbidity 1 NTU Element Weight 50 23 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 028 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION S 9 ACM RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 ACM3 TSAN 11 000 41 0 99 20 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane COMTI GUN AU ON M Spiral Wound Fiberglass Outer Wrap Active Membrane Area 365 ft 33 5 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure
105. 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 2NTU Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 028 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION oO NN 8 X 20 Low Fouling RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 X201 UWAN 10 400 39 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type
106. 34 0 99 00 97 00 Performance is based on the following test conditions 2 000 0 ppm MgSOA 110 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ANM Aromatic Polyamide Advanced Nanofiltration Membrane Configuration Spiral Wound Fiberglass Outer Wrap Active Membrane Area 365 ft 33 5 m Recommended Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1NTU TS80 Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate f
107. 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane Sane s hi SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Z 8 ACM RO Element Series TRIS gt CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 ACM3 TSAN 11 000 41 0 99 20 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane eidele e EE Spiral Wound Fiberglass Outer Wrap Active Membrane Area 365 ft 33 5 m Recommended Applie
108. Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane Sane s hi SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION 8 ACM RO Element Series TRIS gt CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 ACM2 UWA 10 700 40 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane COMTI GUN AU ON M Spiral Wound Fiberglass Outer Wrap Active Membrane Area 400 ft 37 2m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine F
109. Fixed Film Bioreactor 7 500 1000 15 January 2006 Canada Fixed Film Bioreactor z 500 1000 15 January 2006 Canada For additional information regarding SpiraSep UF membranes please contact Mike Snodgrass at 1 805 964 8003 ext 113 or send e mail to snodgrass trisep com The Ultimate A Sp EP ch minl lo m L ltratiliraLisn Membrana Te be lt co SPIRAL WOUND BACK FLUSHABLE CORPORATION PRODUCT SPECIFICATIONS i Chipa Gen V SPIRASEP TRI f Ultrafiltration Membrane Technology CORPORATION Model Permeate Turbidity Typical Pore Size SpiraSep 900 lt 0 1 NTU 0 05 micron Operation and Design Data Membrane Type Polyethersulfone Ultrafiltration Membrane Configuration SpiralWound Backflushable Immersed Negative Pressure Recommended Applied Pressure 1 to 10 psi 0 07 to 0 7 bar Maximum Applied Back Pressure 10 psi 0 7 bar Recommended Back Pressure 5 10 psi 0 34 0 69 bar Active Membrane Area 178 ft 16 6 m Recommended Operating Temp 35 113 F 2 45 C Feed water pH Range 2 11 continuous Air Scour Requirements 4 5 6 5 scfm if applicable Maximum Chlorine Exposure 2000 ppm Feed Spacer 125 mil Element Weight 45 20 Length A 42 8 1087 Permeate Tube C 1 87 0 D 47 5 Units in pounds and inches units in parenthesis in kilograms and millimeters TriSep Corporation 93 S La Patera Lane Goleta CA 93117 805 964 8003 phone 80
110. Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 45 20 Length A 40 0 1 016 Diameter B 8 5 215 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TRIS gt CORPORATION Permeate flow Model GPD m3 day 8 400 31 0 OPERATIONAL AND DESIGN DATA Membrane Type COMM OQUPAUON S Active Membrane Area Recommended Applied Pressure Maximum Applied Pressure Recommended Operating Temperature Feedwater pH Range Chlorine Tolerance Maximum Feed Flow Minimum Brine Flow Permea
111. Maximum SDI 15 minutes 5 0 Maximum Turbidity 2NTU PD DNCAU OM EE General Pharmaceutical Element Weight 40 18 Length A 40 00 1 016 Diameter B 7 90 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 046 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane ipa s SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION 8 X 20 Low Fouling RO Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 N1P4T6 9 400 35 0 99 50 98 50 Performance is based on the following test conditions 2 000 00 ppm NaCl 225 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane Configuration Spiral Wound Turboclean Shell with FoulGuard Technology Active Membrane Area
112. Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Application General Pharmaceutical Element Weight 45 20 Length A 40 00 1 016 Diameter B 7 90 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane en SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Es 8 ACM RO Turboclean Element Series TRI CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 M3P4T6 10 500 39 0 99 50 98 50 Performance is based on the following test conditions 2 000 00 ppm NaCl 225 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Oe TN e E Spiral Wound Turboclean Shell Active Membrane Area
113. Modified polysulfone Non woven polyester ANM polyamide composite Modified polysulfone Non woven polyester Cellulose acetate triacetate blend N A Non woven polyester AUM PES Modified polysulfone Non woven polyester AMM PVDF Modified polyvinylidenefluoride Non woven polyester 345 TriSep Flat Sheet Membrane TRIS gt CORPORATION MEMBRANE FLUSHING HANDLING amp STORAGE Handling and Storage of Flat Sheet Membrane Stock Use butyl or nitrile gloves when handling membrane to prevent contact with residual organic amines and sodium metabisulfite IMPORTANT TriSep roll stock flat sheet membrane includes twenty 20 linear feet of leader at no additional charge The first twenty 20 linear feet of leader is to be discarded We have found the first twenty 20 linear feet may be damaged in shipment and should be discarded Rolling of elements with the first twenty 20 feet of membrane may result in sub spec sub quality final product Storage of Flat Sheet Membrane Stock IMPORTANT TriSep flat sheet membrane stock are supplied wet in a rolled format for ex works shipment For optimal storage and performance membranes must be kept away from direct sunlight and are best kept refrigerated at 40 F to 45 F 4 C to 7 C This prevents biological growth and oxidation of the residual organic amines in the membrane Not refrigerating the flat sheet membrane stock may result in accelerated darkening of the membr
114. Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION ow NN 3 8 X 20 High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 3838 N1J4U9 1 300 4 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane COMMUN ANON EEN Spiral Wound Turboclean Shell with FoulGuard Technology Active Membrane Area 53 ft 4 9 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 25 GPM 5 6 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Application Peptide Concentration Ba wh TY I I L
115. PoploM YUM osn jue oqn g 9107 esoq aqn L 2100 juodn q eseqq 06 8C eqn 2107 juodnq Teseq L cc eqn 2107 juodnqq Teseq or cI1 aqn L 2100 juodn j eseq 6 cI qn L OD SWI tZIS qn L 9107 IUTA CH Ce aqn L 3109 IUA GE cI aqn L 2107 IAWU 61 c eqni owes ut SL 9S SOI pue SMH Joy VI ds c OI YM VA qn L 9107 UA OE PES qn 9107 SWI pt ES qn L 9107 SWI pt SES qn 1oO IUA 61 SE qn L 9107 SOW OE VES qn 9107 oojyu pt SES qn 9107 SWI pt SES Id sju ourtuo Jo3depy UO OS LL OI ce Cl 00 TI 09 CS 09 00 c 00 OV 09 SI Gei ST Iv9l Iv 9I SIS SIS Iv9l Iv 9I 1809 A Gei AAAA on BA FA Jo3depy ouogj nsA oq JAd S wepoeipAH OAd dS 8H HOS VOS euognnsA oq dS 8H 08 VOS euojgpsA od dS 8 H08 VOS ouoj nsAToq ouogj nsA od UIe oeJp H euog nsA oq dS 8H H08 VOS JAd JAd ure oeJpAH JAd S ure oepAH OAd dS 8H 09 VOS JAd JAd S ure oepAH OAd dS 8H A08 VOS IENIJEN PPOW Joydepy 9qn 94nssoaq s19jedpy p reoqug SUNIA pue ISTI Seg SOIUOUIS soruoutso o AS PIO sonneuteJpAH o A1S plo eut opo AIS PIO TRUS PINONNS TS V SUlspo eut opo 41S PIO oddeuy sonneueJpA H Tejusq emjonas Ts V SUt 9p0 oddeuy sonneueJp H SoIUOUIS sonneueJpAH TRUS PINONNS TS V SUT 9p0 oddeuy SOIUOWUSC sonneueJp H Teua PINONYS TS V our epo J9 11n329 enu A oqn oynsso
116. Recommended Applied Pressure Not applicable Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 176 F 2 80 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 10 0 ppm Maximum Feed Flow 70 GPM 15 8 m3 hr y M Minimum Brine Flow Permeate Flow Ratio 5 1 S y N Maximum SDI 15 minutes 5 0 APPROV d Maximum T urbuditv 1 NTU APPIC AUO ete een ene ee Meat Processing Element Weight 30 14 Length A 38 00 965 Diameter B 6 3 160 Permeate Tube C 1 14 29 0 Units in pounds and inches units in paranthesis in kilograms and millimetes Dim A does not include ATD Mechanical Configuration Sanitary Style Core Tube ATD not included with element Feed Spacer 0 045 thick diamond spacer Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION ow NN 8 ACM RO Turboclean Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 M1F6T6 7500 28 0 99 50 98 50 Performance is based on the following test conditions 2000 ppm NaCl 225 psi 25 C 15 recovery pH 8 30 minutes operation
117. Spiral Wound Fiberglass Outer Wrap Active Membrane Area 365 ft 33 5 m Recommended Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 19 30 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com s Competitive Element Replacement Guide TRIS gt CORPORATION Dow Filmtec Replacement Elements TriSep Model Nu
118. Standard Test Conditions and the specified product water flow and salt passage for X20 ACM CA TS80 and XN45 element are set forth in product specification sheets provided by TriSep 4 3 2 Periodic Cleanings Periodic cleanings of the membranes will be required to maintain this performance TriSep will not be responsible for any costs associated with these element and or system cleanings Membrane cleaning protocols are to be approved by TriSep Required frequency of cleaning will be determined during operation of the system and may vary with time of year feedwater temperature feedwater contaminants and microbial challenge level Other variables not mentioned above may also effect the required cleaning frequency TriSep Corporation 93 S La Patera Lane Goleta CA 93117 805 954 8003 phone 805 964 1235 fax www trisep com TRIS gt CPAP GAR AT Pe B If TriSep determines that replacement is required under this warranty TriSep will credit the Customer 1 36 of the original purchase price of the element s per Terms and Conditions of Sale for each unexpired month of the warranty period This credit will be toward the purchase of TriSep replacement element s at the then current selling price set by TriSep 5 0 CONDITIONS OF WARRANTIES 5 1 Limitation of Warranties 5 1 1 Occurrence of any of the following as determined by TriSep shall void all warranties hereunder a Operation of the elements that deviates from t
119. TRIS gt CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 M2Q3U5 2 400 9 0 99 50 98 50 Performance is based on the following test conditions 2 000 00 ppm NaCl 225 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Conn B gs le opiral Wound Turboclean Shell Active Membrane Area 85 ft 7 9 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1NTU eelere u uuu uasskanasadawaasakhasia Pharm Make Up Water Element Weight 15 7 Length A 40 00 1 016 Diameter B 4 00 101 Permeate Tube C 0 62 15 9 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Desal DuPont Sty
120. TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TRIS gt CORPORATION Model 3838 N6F V8 2 00 10 0 OPERATIONAL AND DESIGN DATA Membrane Type Configuration Active Membrane Area Recommended Applied Pressure Maximum Applied Pressure Recommended Operating Temperature Feedwater pH Range Chlorine Tolerance Maximum Feed Flow Minimum Brine Flow Permeate Flow Ratio Maximum SDI 15 minutes Maximum Turbidity jojo e Tel ae ee eee eee ee AUER LENKA PL LOR LUD KKKWAAKKNKMAAKAUKMU NAA y i AU AWAYYANA AAA NN NW Nt M d ll li II Element Weight Length A 12 5 4 38 965 Units in pounds and inches units in paranthesis in kilograms and millimetes Diameter B Mechanical Configuration Sanitary Style Core Tube Feed Spacer 3 8 96 0 031 thick diamond spacer PRODUCT SPECIFICATION 3 8 AUM High Temperature UF Turboclean Element M W C O 10 000 AUM Advanced Ultrafiltration Membrane Spiral Wound Turboc
121. gt CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 SB50 TSF 1 900 7 0 95 00 92 50 Performance is based on the following test conditions 2 000 00 ppm NaCl 420 00 psi 25 C 15 recovery pH 5 50 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type SB Cellulose Acetate Blend Configuration Spiral Wound Fiberglass Outer Wrap Active Membrane Area 80 ft 7 4 m Recommended Applied Pressure 200 500 psi 14 34 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 50 90 F 10 32 C Feedwater pH Range 5 5 nominal 4 7 Chlorine Tolerance 0 5 ppm nominal 1 0 ppm max Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbiditly 1 NTU Element Weight 15 7 Length A 40 00 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick
122. hardness sulfate and other multivalent ions and soluble low molecular weight gt 200 Daltons neutral and charged organic compounds The ACM product line is available in 5 versions The ACMI and ACM2 offer the highest rejection 99 5 and typically operate at 150 200 psi 10 14 bar The ACM2 is one of our most popular membrane elements It is a defacto standard for typical water purification requirements The ACMI and ACM2 are preferred in applications with high feedwater TDS 73 000 ppm and or high recovery The lower specific flux of these membranes compared to the ACM4 and ACMS allows for a more balanced hydraulic flow through the system and more balanced permeate flux rates due to the high osmotic pressure of these feedwaters For applications where a lower operating pressure 1s required but you still need very high salt rejections the ACMG may fit the bill This membrane typically operates at 125 175 psi 9 12 bar but still maintains a very high salt rejection 99 5 For ultra low pressure operation the ACM LP line of ACM4 and the new ACMS may be the best choise These membranes have extremely high specific flux comparable to NF membranes while still offering excellent salt reyection 98 5 99 2 These membranes typically operate at feed pressures of 75 150 psi 5 10 bar Due to the high specific flux these membranes are best suited to applicaitons with relatively low TDS lt 3 000 ppm to achieve balanced flux rates wi
123. m3 day Rejection Rejection 3840 N2D3U8 1750 6 0 95 00 92 00 Performance is based on the following test conditions 2000 ppm MgSOA 110 psi 25 C 15 recovery pH 8 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type XN45 Polyamide Advanced Nanofiltration Membrane Configuration Spiral Wound Turboclean Shell Active Membrane Area 70 ft 6 4 m Recommended Applied Pressure Not applicable Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 5 ppm nominal 1 0 ppm max Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Application Milk Demineralization wi a OU 4 ATA ALI lll d AAR ARR WW m W Wi UNA A IA a Z n AE Element Weight 15 7 Length A 39 984 Diameter B 3 8 96 Permeate Tube C 0 83 21 2 Units in pounds and inches units in paranthesis in kilograms and millimet
124. pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ANM Aromatic Polyamide Advanced Nanofiltration Membrane COMTI GUN AU ON M Spiral Wound Fiberglass Outer Wrap Active Membrane Area 400 ft 37 2 m Recommended Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 4 0 Maximum Turbidity 1 NTU Element Weight 50 23 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 028 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane Y SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta C
125. performance associated with a decrease in perme ate flow and increase in differential pressure and PACKAGING a loss of element rejection If left unchecked this TriClean 214CA is shipped as a liquid in 5 gallon fouling can permanently damage the membrane plastic pails and 55 gallon plastic drums Pricing elements leading to costly and premature mem is F O B our factory in Goleta CA Salem VA brane replacement or Duisberg Germany Delivery for most orders 1s 1 2 days after receipt of order SOLUTION TriClean 214CA is a liquid version of TriClean MSDS SHEETS 212CA for applications where handling of pow For the most up to date information on dered cleaners is not desirable IriClean 214CA is MSDS sheets please contact our web site at buffered to a pH of 7 8 to prevent hydrolysis of CA www trisep com membranes while removing biological organic and colloidal foulants TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax e www trisep com e 0105 324 TriSep Corporation Chemical Manual TRIS CORPORATION TRICLEAN 214TF HIGH PH LIQUID CLEANER e Used to remove biological organic and colloidal fouling on Polyamide Composite mem brane e Effective for emulsified oil and silica PROBLEM In many installations worldwide polyamide com posite RO and NF membranes can become fouled with biological organic and colloidal foulants These foulants can q
126. please contact our web site at membrane performance while not introducing any www trisep com chemicals that may be harmful to the process SOLUTION TriClean 218 is a specifically designed to handle the daily cleaning rigors of the dairy or food pro cessing membrane plant TriClean 218 will remove biological organic and colloidal foulants without damaging RO NF or UF membrane elements TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 327 TriSep Corporation Chemical Manual TRIS CORPORATION TRICLEAN 310 LOW PH LIQUID ACID MEMBRANE CLEANER e Removes iron and metal hydroxide fouling e Removes calcium carbonate scale e Removes sulfate scales PROBLEM In many installations worldwide RO membranes can become fouled with calcium carbonate scale and or iron and other metal hydroxide colloids These foulants can quickly lead to a loss of system performance associated with a decrease In perme ate flow and increase in differential pressure and a loss of element rejection If left unchecked this fouling can permanently damage the membrane elements leading to costly and premature mem brane replacement SOLUTION TriClean 310 a 40 concentration liquid version of the TriClean 210 can be used where powder cleaners are undesirable TriClean 310 removes calcium carbonate scale and iron and metal hydroxide colloids without damaging s
127. 0 95 00 92 00 Performance is based on the following test conditions 2 000 0 ppm MgSOA 110 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type XN45 Polyamide Advanced Nanofiltration Membrane COMTI GUN AU ON M Spiral Wound Fiberglass Outer Wrap Active Membrane Area 365 ft 33 5 m Recommended Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 5 ppm nominal 1 0 ppm max Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 2NTU EC Technology Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element
128. 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane eidele e EE Spiral Wound Fiberglass Outer Wrap with FoulGuard Technology Active Membrane Area 88 ft 8 2 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 2NTU Element Weight 15 7 Length A 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 62 15 9 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Desal DuPont Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep
129. 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type Configuration Active Membrane Area Recommended Applied Pressure Maximum Applied Pressure Recommended Operating Temperature Feedwater pH Range Chlorine Tolerance Maximum Feed Flow Minimum Brine Flow Permeate Flow Ratio Maximum SDI 15 minutes Maximum Turbidity PRO COM e EN amp Element Weight 50 23 Length A 40 00 1 016 Diameter B 7 9 200 AUM Advanced Ultrafiltration Membrane opiral Wound Turboclean Shell 355 ft 33 0 m 5 200 psi 0 3 14 bar 600 psi 41 bar 35 113 F 2 45 C 2 11 continuous 10 0 ppm 80 GPM 18 m3 hr 5 1 5 0 1 NTU Beverage Water Make Up UF a gt SL Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Feed Spacer Filmtec Style Core Tube 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s perm
130. 1 0 point where turbulent flow will ensure adequate chemical mixing prior to entering the RO or NF SCALE INHIBITOR system This is usually done prior to the cartridge filters and high pressure pump Dosing rates vary DI SPERSANT depending on feedwater quality and recovery but normally run between 2 and 5 ppm For exact dosing use the latest version of TroiWin TriPol e Superior control of carbonate 8510 contains a dispersant and can be used if there and sulfate scales are Iron or other metal hydroxides in the feedwater T Since this product is anionic in nature care should e Iron and silica d Ispersant capa be taken when using cationic polyelectrolytes in bility the pretreatment system PROBLEM PEROS M NEE I Max Langlier Saturation Index 2 0 n many installations worldwide higher permeate U Max CaSO4 Saturation 400 recoveries from reverse osmosis RO systems are W Max SrSO4 Saturation 1 200 often limited by the potential for sulfate scales Se e rere Max BaSO4 Saturation 12 000 This 1s especially problematic for waters with high a Max CaF Saturation 8 000 amounts of silica or metal hydroxides which can Silica 100 form insoluble polymeric gels with conventional acrylic acid scale inhibitors In many applications the tendency for sulfate scale formation has the effect of lowering the system recovery that could In the concentrate Levels may be exceeded on occasion Contact TriSep for advice
131. 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Configuratio EE Spiral Wound Fiberglass Outer Wrap Active Membrane Area 400 ft 37 2 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 4 0 Maximum Turbidity 1 NTU Element Weight 50 23 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 028 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 80
132. 19S u eiquu lN OW 9 e195V eso n o9 s AGINS LNalN3oV 1d3s AAILILAdNOD VOS1L 02d8S 07S8 VS1 028S 0708 VS1 028S 0707 R CORPO 352 TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com e 0105 s us uoneoiioeds jonpoud pue s u uu uinb i uo 5 uuoo 104 BDIAJOS JOWOISNYD UOl eJOdIOD desu 19631002 sei quiesse eje d pue Buisnou oj Buroeuuoo io s10 depe pue jonpoud pieoqui eJinbeJ Aew sjapow jueujeoej daJ uoneJ40d402 deSu 9 ON 00vY 064N 00v S cC68 EE 00v MOTOS 1H VNS3 AHf1T 0v08 OOv OZAN VMNn 08S1 0708 6268 00vT 00c JN SLZ68 4ovogya 00r 0 Z43JN 00r ZHS Z28 Vd 0O0 J3N S18 J40roe1a J0c9 ns VMN SVNX 0708 6268 Ov 09 SrJN S1LZ68 4ovogyad Ov08 4HOVAN CHS 248 VWd OOEAN SL8 4ovosi1d 0r08 0F3JN 40v071H 44 0v071H 0Z9 NS VS L SPNX 0r08 OvOV O6AN OvOV OZAN VNSAVHN OVOV OLc ns AS1 08S1 0707 VNSA LHN OVOV OFOrF ShFdN OFOF 4H0FdN OFOrF OFdN SCH vd 00 4N v Lt 44 4Ovorya OvOv AN OL9 NS CHS 024v Vd 00 JN L Lt 44 J0vOT 1G OvOv OLZAN eseq T38OMN d3Sl41 suiejs S DILL HOOM SOIUOWSO 39 39 sonneueJp H 29 Luul g Moq L1N3JHWN3OV Id3H SOLIBS eueJquia y uoneaj ljoueN Jidin 9 LNAWSAQV 1d3s AAILILAdINOD 4S L SPNX 0r0r KeJo CORPORATION 353 TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep
133. 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 2NTU Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 028 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com Competitive Element Replacement Guide um TRIS S CORPORATION Replacing elements from one competitor to the next can be a difficult and frustrating task Inboard adpaters the piece that adapts the first and last element within a pressure tube to the pressure tube end cap must be designed and manufactured for both the proper element and pressure tube This makes for a large matrix of possible combination
134. 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1NTU Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION LA N 8 ACM LP Low Pressure RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 ACM4 UWA 16 000 60 0 99 00 98 00 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OP
135. 5 0 1 NTU Mt Milk Fractionation A I l M Permeate Tube C 0 83 21 2 ATD not included with element Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TRIS gt CORPORATION Model 3840 N6D9V7 OPERATIONAL AND DESIGN DATA Membrane Type CONT QUPATION E Active Membrane Area Recommended Applied Pressure Maximum Applied Pressure Recommended Operating Temperature Feedwater pH Range Chlorine Tolerance Maximum Feed Flow Minimum Brine Flow Permeate Flow Ratio Maximum SDI 15 minutes Maximum Turbidity ADDIIG300I Rm A dd ANN MA WA lll ll Il n Wl Element Weight Length A 12 5 4 39 984 Units in pounds and inches units in paranthesis in kilograms and millimetes Dim A does not include ATD Mechanical Configuration Diameter B Sanitary Style Core Tube Feed Spacer 3 8 96 0 065 thick diamond spacer PRODUCT SPECIFICATION 3 8 AUM High Temperature UF Turboclean Element M W C O 10 000 AUM Adva
136. 76 76 76 76 ppm 8010 1 0 150 200 200 200 100 0 5 0 1 7510 2 0 300 800 10 000 8 000 100 1 0 0 5 8510 2 0 400 1 200 12 000 8 000 100 1 0 0 5 9010 2 6 300 800 10 000 10 000 100 1 0 0 3 9110 2 6 300 1 200 10 000 10 000 100 2 0 0 3 9510 2 6 400 1 200 12 000 10 000 200 1 0 4 0 Saturation levels for CaSO4 SrSO4 BaSO4 CaF2 and Silica are percent of saturation index where 100 is assumed saturated These values should be calculated using Troi version 2 0 0 or later Maximum recommended concentration of any antiscalant should not exceed 50 ppm in the concentrate TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 310 TriSep Corporation Chemical Manual TRIS CORPORATION TRIPOL 8010 SCALE INHIBITOR e Extends useful membrane life e Superior control of calcium car bonate PROBLEM In many installations worldwide higher permeate recoveries from reverse osmosis RO systems are often limited by the potential for calcium carbon ate scale This is especially problematic for the new generation polyamide composite membranes since feedwater acidification 1s no longer required to insure long service lifes In many application the tendency for calcium carbonate scale formation has the effect of lowering the system recovery that could adversely effect the system economics SOLUTION TriPol 8010 protects and enhances the operation of RO and
137. 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM LP Fully Aromatic Polyamide Low Pressure Advanced Composite Configuration Spiral Wound Fiberglass Outer Wrap Active Membrane Area 88 ft 8 2 m Recommended Applied Pressure 40 300 psi 3 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 15 7 Length A 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane lt s SOLUTIONS TriSep Corporation
138. 8 2 m Recommended Applied Pressure 40 300 psi 3 21 bar Maximum Applied Pressure 350 psi 24 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 15 7 Length A 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 028 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Zane 8 ACM LP Low Pressure RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 ACM4 TSA 14 600 55 0 99 0
139. 8003 805 964 1235 fax www trisep com 0703 15 C y SI 33H AWVN ANVdWOO I33SNI JO NOISSIWYAd NALUYM FHL LNOHLIM CVV sl HSINId nog PTI 31OHA V SV JO LaWd NI NOLLOnGO3d33 e 7 EE JO Als3dO3d 31OS 3H1 SI ONIMYJA Add ON OMQ 3ZIS W SIHL NI GANIVLNOD NOILVW3IOJNI 3H1 SINAIWWOO I dad ONIONVAFTOL 1VIIN3dHNOO ANY A3V13l34O3d x 9 sao L 000000 VWIO3d 3Ovld OML _ SR e Lo 1 1VNOILOV2H SAONVAFIOL IN3WQT3M Q 1O3INVW SS191 3dld OL HS Pl SivIlill C 3103234 AMVIINVS DIAM S I WIEL erc e O NNMdNOO ONYNLOIA ddid t SS9i l je OSIA JANLANA 3OOZ S diHdvsoO sercll i fe EES AVINVS Sl o waa ll S ONBW O SI 1 1 WGddj Serclll 9 JATVA 3S V3 133 3I V JAIVATIVEOAd C A sid JiddN3Jdd Z L 9O d j B8 O INGWgHd3sVvalds Or XOlly OfddgnidNODd3Svalds 1 1 gv EEL NOL INAS NOUVN3V 6 d3SValds 1 Sev rer ONO OfdddSvalds WGdd O0rtll 8 Cl dWVIO ANVIINVS SEP SIE mell fel NOldBOS3d IVRHIVW OH LV PALO OH WLI SPIRASEP Ultrafiltration Membrane Technology E Y 4 PSNI l y S TRL CORPORATION 16 TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 S 9 L 8 LJO LI33HS HOI3M S l SKS E GALIGIHOdd d
140. 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Lum 4 TS80 Nanofiltration Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 TS83 TSF 2 300 8 0 98 00 96 00 Performance is based on the following test conditions 2 000 0 ppm MgSOA 110 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ANM Aromatic Polyamide Advanced Nanofiltration Membrane Configuration Spiral Wound Fiberglass Outer Wrap Active Membrane Area 85 ft 7 9 m Recommended Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 15 7 Length A 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and mi
141. 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane COMMUN AU OM EEN Spiral Wound Turboclean Shell Active Membrane Area 355 ft 32 6 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Application Beverage Make up Water Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all fee
142. A screen with checkboxes next to the different units pops up Check the boxes whose units you want to set as default Next time when you add a project the default units will be displayed in the respective drop down boxes The program will remember the last setting you used so check this before you start a new project As an example if you set the Pressure units bar flow units m3 hr flux units to Imh and temperature C the next time you start the program and add a new project the units will be populated with what you had set through the Units option Help Currently the help menu only displays the version of the program TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 408 TriSep Tron Normalization Program L CM Manual ver 1 1 0 TRIS S CORPORATION Main Toolbar The main toolbar selections are Add Project Edit Project Delete Project View Projects Export to Excel Print Whole Project Print Input Details Print Calculated Fields Units Recalculate Graph Exit and Help All except Recalculate and Graph correspond to the menus above Recalculate is used if you change any input variables on the Project the records in the grid below will be recalculated to reflect the new calculations Graph is used to provide a graphical view of the data entered on the Grid File Add Project Select this option to input a Proje
143. ANM TS80 01 Nanofiltration Color removal THM reduction Daytona Beach Pilot Plant Daytona Beach Florida U S A 4040 TS80 TSA Spiral Wound Element ANM Nanofiltation Membrane TriSep TS80 elements operated in a pilot plant at Daytona Beach lorida for 8000 hours on a test conducted by an independent testing organization All critical process variables were logged on a daily basis along with periodic monitoring of norganic as well as various organic halide formation potentials Raw water pre treatment consisted of acid dosing and cartridge filtration Table 1 contains a typical feedwater analysis while Table 2 next page gives typical ionic rejections observed during the course of this test As can be seen from Table 2 the TS80 elements gave very good inorganic ion rejections and trihalomethane formation potential THMFP rejections During the course of this test the average THMFP in the system permeate was less than 25 ppb The TS80 membrane also exhibited very high water flux rates At a pressure of 100 psi this equates to 22 GFD or 2000 GPD for a 4040 TS80 TSA element and 8000 GPD for a 8040 TS80 TSA element The TS80 also proved to be resistant to fouling There was no noticeable flux decline after 500 hours of operation and only a 1096 flux decline after 4750 hours of operation If we assume that the elements would be cleaned after a 10 1596 loss in element flux we can calculate an interval between cleanings of 7 3 months
144. ANM TS80 02 Nanofiltration Color removal THM reduction Melbourne Pilot Plant Florida U S A 4040 TS80 TSA Spiral Wound Element ANM Nanofiltration Membrane TriSep TS80 elements operated in a pilot plant at Melbourne Florida for 3800 hours on a test conducted by an independent testing organization All critical process variables were logged on a daily basis with periodic measurement of inorganic as well as various organic halide formation potentials Pretreatment consisted of an activated carbon filter acid and scale inhibitor dosing Table 1 contains a typical feedwater analysis while Table 2 next page gives typical ionic rejections observed during the course of this test As can be seen from Table 2 the TS80 elements gave very good inorganic ion rejections and trihalomethane formation potential THMFP rejections During the course of this test the average THMFP in the system permeate was less than 25 ppb The TS80 membrane also exhibited very high water flux rates Normalized to a pressure of 100 psi this equates to 18 GFD or 1600 GPD for a 4040 TS80 TSA element and 6200 GPD for a 8040 TS80 TSA element Based on the results of this test the TriSep T9880 membrane is a superior membrane for membrane softening applications requiring high inorganic and THMFP rejections at low operating pressures The TS80 operated on this feedwater with a minimum of pretreatment and chemical cleanings Table 1 Melbourne Raw Water Analysis
145. Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 2 NTU Element Weight 15 T Length A 40 00 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 028 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 1596 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Zam 8 X 20 Low Fouling RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 X201 TSA 9 700 36 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane elle e EE Spiral Wound Fiberglass Outer Wrap with FoulGuard Technology Active Membrane Area 365 ft 33 5 m Recommended App
146. Calculations Design Calculation Single Stage System Here is where you get to design your own membrane separation plant First it will ask you to select a project that you have previously input or a water analysis that you have to input Once you have made this selection click OK and the main design window pops up The first field Projection By allows you to input your name for future reference The next field allows you to specify the system design recovery This field is required The recovery is defined as the ratio of permeate flow to feed flow expressed as a percentage Feed temperature and feed pH defaults to what was input in the water analysis but can be modified at this point If the pH 1s lowered acid will be dosed to the feed water analysis to adjust the pH to the desired level The feed pH can also be increased in version 2 0 0 using 30 caustic soda Both of these will effect the CO2 HCO3 and CO3 concentrations in the feedwater analysis You can select either hydrochloric acid HCl or sulfuric acid H2SO4 as the acid or caustic soda as a base to use for adjusting the pH If you use H2SO4 the sulfate ion concentration will also be adjusted in the feedwater If you select HCl the chloride ion will be adjusted in the feedwater If you use caustic soda the sodium level will be adjusted The next field allows you to input the required permeate flow rate In addition you can specify a recirculation flow rate Recirc Flow
147. Conventional sanitary elements have significant clearances between the soft wrap and the inside of the pressure vessel resulting in by pass of feed flow around the element of 40 60 This adds to the required recirculation flow Comparative tests at a major California Cheese producer were performed to compare the by pass flow of the TurboClean element to a standard net wrap element by isolating one pressure vessel in a continuous recirculation stage The vessel was equipped with flow control valves on the feed and concentrate side pressure gauges on feed and concentrate and flow meters to measure the concentrate and permeate flow The tests showed a reduction in feed flow rate of 44 when comparing the TurboClean elements versus conventional soft wrapped elements What effect will this new element design have on the food and dairy industry The hard shell TurboClean energy savings can be as high as 4496 of the required recirculation flow and in certain application a corresponding decrease in required cooling energy Improved hydraulic flow control may also lead to increased membrane life and improved membrane cleaning efficiencies Although initial tests tend to support this hypothesis conclusive data is still pending Effects of improved hydraulic flow control may result in improved separation efficiencies since the effect of high by pass flow 1s to reduce membrane cross flow and increase concentration polarization a h
148. Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane y SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION v 4 ACM LP RO Element Series TRL CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 ACM4 TWA 3 600 13 0 99 00 98 00 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM LP Fully Aromatic Polyamide Low Pressure Advanced Composite Cong AMON uuu aa E oa akana URS Spiral Wound Fiberglass Outer Wrap Active Membrane Area 90 ft 8 4 m Recommended Applied Pressure 40 300 psi 3 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow
149. Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION 9 ACM RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 ACM1 TSDA 8 000 30 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Configuration Spiral Wound Fiberglass Outer Wrap Active Membrane Area 365 ft 33 5 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1NTU Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1
150. Feed Spacer 0 045 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Lum 3 8 X 20 High Temperature Turboclean Element TRI CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 3838 N1D U8 1700 6 0 99 50 98 50 Performance is based on the following test conditions 2000 ppm NaCl 225 psi 25 C 15 recovery pH 8 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane Configuration Spiral Wound Turboclean Shell with FoulGuard Technology Active Membrane Area 68 ft 6 2 m Recommended Applied Pressure Not applicable Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow
151. Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Zama 8 X 20 Low Fouling RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 X201 UNA 11 000 41 0 99 50 98 50 Performance is based on the following test conditions 2 000 00 ppm NaCl 225 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane Configuration uU uu uuu etes breiten Spiral Wound Fiberglass Outer Wrap with FoulGuard Technology Active Membrane Area 430 ft 40 0 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine 0 1 ppm Maximum Feed 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum 2 NTU X 20 Element Weight 45 20 Length A 40 00 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep
152. MAU WW M dl I it MA MU NW WM I Element Weight 15 7 Length A 38 965 Diameter B 3 8 96 Permeate Tube C 0 83 21 2 Units in pounds and inches units in paranthesis in kilograms and millimetes Dim A does not include ATD Mechanical Configuration Sanitary Style Core Tube ATD not included with element Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TRIS gt CORPORATION Model 3838 N6D4V9 OPERATIONAL AND DESIGN DATA Membrane Type Configuration Active Membrane Area Recommended Applied Pressure Maximum Applied Pressure Recommended Operating Temperature Feedwater pH Range Chlorine Tolerance Maximum Feed Flow Minimum Brine Flow Permeate Flow Ratio Maximum SDI 15 minutes Maximum Turbidity jojo e Te
153. Membrane Type Configuration Active Membrane Area Recommended Applied Pressure Maximum Applied Pressure Recommended Operating Temperature Feedwater pH Range Chlorine Tolerance Maximum Feed Flow Minimum Brine Flow Permeate Flow Ratio Maximum SDI 15 minutes Maximum Turbidity Element Weight Length A 50 23 40 0 1 016 Diameter B 8 5 215 SB Cellulose Acetate Blend Spiral Wound Fiberglass Outer Wrap 440 ft 40 4 m 200 500 psi 14 34 bar 600 psi 41 bar 50 90 F 10 32 C 5 5 nominal 4 7 0 5 ppm nominal 1 0 ppm max 80 GPM 18 m3 hr 5 1 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane Y SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta Californi
154. Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane eidele e EE Spiral Wound Fiberglass Outer Wrap Active Membrane Area 365 ft 33 5 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 19 30 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Desal DuPont Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com
155. Membrane Type XN45 Polyamide Advanced Nanofiltration Membrane E elle Ur LE Spiral Wound Turboclean Shell Active Membrane Area 70 ft 6 4 m Recommended Applied Pressure Not applicable Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 5 ppm nominal 1 0 ppm max Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Apple AMOI u u usu uo iA Whey Fractionation W M PA III I MI Ma o d d p la Element Weight 15 T Length A 39 984 Diameter B 3 8 96 Permeate Tube C 0 83 21 2 Units in pounds and inches units in paranthesis in kilograms and millimetes Dim A does not include ATD Mechanical Configuration Sanitary Style Core Tube ATD not included with element Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 1596 Engineered Membrane SOLUTIONS TriSep Corpora
156. MgSOA 110 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type TS50 Polyamide Advanced Nanofiltration Membrane Configuration Spiral Wound High Temperature Turboclean Shell Active Membrane Area 70 ft 6 4 m Recommended Applied Pressure Not applicable Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr UD A Minimum Brine Flow Permeate Flow Ratio 5 1 LY 2 TAL Maximum SDI 15 minutes a 5 0 AppRO Maximum Turbidity 1 NTU PAD ONC AMON TE Lactose Demineralization Element Weight 15 7 Length A 38 00 965 Diameter B 3 8 96 Permeate Tube C 0 83 21 2 Units in pounds and inches units in paranthesis in kilograms and millimetes Dim A does not include ATD Mechanical Configuration Sanitary Style Core Tube ATD not included with element Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable fo
157. My Computer and look for the drive with the CD symbol Double click on your CD to open the disk and then search for the file named Setup click on it then click Open then click OK The setup installation program should then start The first screen will ask you if you want to continue or exit The next screen will allow you to continue the installation with the default settings copying the files into the folder c Program Files TROI If you wish to copy the files into a different directory you may change the default by clicking on Change Directory If you wish to exit the Setup program click on Exit or hit F3 The installation process should take about a minute and give you a message that the installation is complete and was successful TROIWIN is now installed on your hard disk under folder c Program Files TROI NETWORK INSTALLATION OF DATABASE TROI needs to be individually installed on each work station but the database can now be shared on the network Copy the Romain mdb Romain ini Elements dat and Elements mdb onto a shared network folder Then on each work station create a database ini file with notepad pointing to the database folder path For example you have a shared folder DataTroi on the network and its mapped to drive M Then you would just type in the M DataTroi in the database ini file A UNC path is preferred and the syntax of that would be servername foldername For example if the name of the server is MyServer and the
158. Ny 1o3depe z 6Z qn1 9100 s esoq JUOgNG I8 SI u o ooqun oqnj 3109 3S SOW 9 dwt L US ueo ooqun qn1 9109 o As DOW LY u o ooqun qn 9109 o 41s SOIT 6t 0 dual 99 ce US ueo ooqun L qnj 9109 KS IUA ouq pue Daat NA 1a3depe z eqn 3100 TI c9 0 nous TO S 0 C9 8C eqn 9107 TI S 8 0 nous GO SLL 0 69 utiq pue pooj II 1o1depe c 6c ccs eqn 23107 TT c9 0 mous GO SLL 0 80 qI c9 0 98 6c AT uS 8 0 0c oc qI c9 0 c c aqn 1oo 3s SOW FI OC jo uuoo JAP STF I popoeu jou aqny 3109 o 1s IUJ OTSTES oqnj 109 3s OWI pT 0 jo uuoo ANP STF YIM p p u jou qn1 9109 3S oojui rq 9S 67 IOYES 1691 equ SS mous QO SY80 10 VEs mous TO uSLL 0 SUSCS SISCH 00 ISXXr JequimN SPO OC NC SO OI L 9IS SUH Nor Daat s1o3depe z Sun xo euids od apis rsd 0001 01 Spr deo puo Sun ooord co crg joeuuoo 0 8I o9JIp YIM YIOM LO deo puo Sun deus IHd U3UIUIO LO CI c APN Joydepy LS EC GK 06 I OTI 00 I Oc SI g c lt Oc cl SL ST LS ET OI vl t Gl Sr cl 00 91 8 Cl c Ol OL 01 8 CI L OT 09 CI OS VI IC L OS vI 00 cI 00 cI SL lt l OIL che 8 tC 18 s US J 0 Jo3depy if oo Gei A Gei on on A Gei A 0 o A Gei on oO Gei Gei Gei Gei G i Un un gn gn A Gei JAd VOV JAd dr 395 V I d I
159. OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Configuration Spiral Wound Turboclean Shell Active Membrane Area 355 ft 32 6 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Application Sugar Concentration n o c D D am et k Element Weight 45 20 Length A 40 1016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 En
160. S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION NN 8 3 ACM RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8340 ACM2 TSOA 11 000 41 0 99 00 98 00 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Configuration Spiral Wound Fiberglass Outer Wrap Active Membrane Area 415 ft 38 1 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance lt 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1NTU Element Weight 50 23 Length A 40 0 1 016 Diameter B 8 3 210 Permeate Tube C 1 14 29 0 Units in pounds
161. S LNHWIADTTH WALAWN VIG HONI P Sold OOP SSUIY C XI pue s eos vung LO ZI Z AOU SUIDIAg pue ISI sJ1Ed 426 TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax e www trisep com 0703 WY OG OT 8007 67 01 SBULI CO 8 seos uuq Z 6E ZI SBULI CO 8 seas IUUQ Z 6E ZI VI pue OI eqn 940 SS CI t I 79 0 SuLI O T WW qoos 0 VSL Li T CLV 8 doseuds I aqn 1oo 8 dogexidg 7 0 Ld We dg 86A S qeppof vS L I 0 sull C Surgsng LA VSL IC qn s eourjq 930 o VSL 17 0 eqni SA 0 VSL IC OS SULI O VSL 0 oreureg 70 oqn 2102 9 AS LIO L 80 T aqn L 9107 9 A1S soruouisQ 60 0 omge1oduuo ug1H ITOS ueo ooqun duio 1 ugrg AKS PIO Le ueo oogmn o AS PIO 170 LO LA ueo ooqm M N 0 LO Ld ueo ooqun p dur 1 u81H MON I7 O qn 2107 YWA T7 0 oqn 2107 juodn q Tesoq 17 0 qn 2102 d Sul Ic 0 qn L 10D S LIO L 98 6 omjeoduro uSIH 98 S eqni 9109 JWJ 98 6 qn L 2107 juodn qT Teso q og Cd qn 3100 d Sul 98 S IVd sju oururo Ia LO cI c APA 8CS 8CS Ic 0 OS 0 OS 0 LO 0 LO 0 LO 0 LO 0 LO 0 LO 0 LEO GI LO 0 LO 0 LO 0 LO 0 LO 0 LO 0 LO 0 LO 0 0S c US C 0S lt 0S lt 0S lt Dis eos gn A A Gei A Gei Gei FHA FHA A Gei FA FAA FHA FAA Gei Gei AHA FH dda adda dd dda Uda Uda Uda dda dd dda dda dda dda dda dda dda dda dda dda dda dda dd Uda dd Uda dd E119
162. Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 M2F8S4 7 200 27 0 99 00 98 00 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane COMMUN AU OM EEN Spiral Wound Turboclean Shell Active Membrane Area 270 ft 24 8 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 95 GPM 22 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Application Boiler Condensate Recovery Element Weight 40 18 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 047 thick paralle
163. Spiral Wound High Temperature Turboclean Shell Active Membrane Area 288 ft 26 8 m Recommended Applied Pressure Not applicable Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 10 0 ppm Maximum Feed Flow 95 GPM 22 m3 hr sD A Minimum Brine Flow Permeate Flow Ratio 5 1 u s 0 Maximum SDI 15 minutes 5 0 APPROV N Maximum Turbidity 1 NTU Application Whey Fractionation Element Weight 40 18 Length A 38 965 Diameter B 7 9 200 Permeate Tube C 1 14 29 0 Units in pounds and inches units in paranthesis in kilograms and millimetes Dim A does not include ATD Mechanical Configuration Filmtec Style Core Tube ATD not included with element Feed Spacer 0 046 thick diamond spacer Engineered Membrane Beet SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION 8 ACM RO High Temperature Turboclean Element Permeate flow Average Salt Minimum Salt Model GP
164. Spiral Wound High Temperature Turboclean Shell Active Membrane Area 53 ft 4 9 m Recommended Applied Pressure 20 200 psi 1 4 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 10 0 ppm Maximum Feed Flow 25 GPM 5 6 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Application Pharmaceutical Separations E p a l u E f AWA WALLET T tt a AAA Ai MM MMAM MUI A I W SN H i NN M M NN UU D V Element Weight 12 5 4 Length A 38 0 965 Diameter B 3 8 96 Permeate Tube C 0 83 21 2 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Sanitary Style Core Tube Feed Spacer 0 045 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A
165. Spiral Wound Turboclean Shell with FoulGuard Technology Active Membrane Area 270 ft 24 8 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 95 GPM 22 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 2 NTU Application Whey Electro Dialyses Recovery e i c uu E B k RE r H Element Weight 40 18 Length A 40 1016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 047 thick parallel spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane ku nF I Y i SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 80
166. TSC 7 TSR 1 TSR 2 X Very Heavy Biological with without TSC 1 TSR 1 TSC 2 TSR 1 scales metals and or silt organic colloid TSC 6 TSR 1 TSR 2 Performance Loss is possible with TSC 6 TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 338 emm TriSep Corporation Chemical Manual TRIS gt CORPORATION TriSep Corporation Cleaning TSC and Rinsing TSR Methods Cleaning TSC Methods TSC 1 Low pH Cleaning Powder A B C Clean and fill solution tank with proper volume of RO Permeate Water Start water recirculating through pump and back into the tank during chemical mixing Add 1 5 pounds of TriClean 210 per every 10 gallons of water in the tank Allow to recirculate until thoroughly mixed Optional Add 1 gallon of TriClean 211 per every 100 gallons of water in the tank Allow to recirculate until thoroughly mixed Check pH of solution proper range is between 2 5 and 3 5 unless otherwise specified by membrane manufacturer pH may be raised by adding sodium hydroxide or lowered by adding additional TriClean 210 Isolate first pass to be cleaned With Concentrate and Product Lines diverted to proper drain slowly run cleaning solution through pressure vessels until all remaining water is out of vessels and cleaning solution is coming out of concentrate line Shutdown pump and divert Concentrate and Product lines to cleaning so
167. This will bring up a window with all your drives Look for the one with a CD Symbol or the one called CD drive Click on the sign on the left of it then click on the normalization folder in the right hand pane and scroll through the files and find setup exe Click on that to start installation of the program It will take a couple of minutes to install the program Once installed it will give a message that the installation is complete and successful TRON is now installed on your hard disk under folder c Normalization NETWORK INSTALLATION OF DATABASE TRON can be installed from a workstation directly on the network For other workstations to access the software a shortcut pointing to the program on the network will have to be created and placed on each users desktop as well as certain files need to be copied under the users system directory The list of files are TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 407 TriSep Tron Normalization Program L CM Manual ver 1 1 0 TRIS S CORPORATION 3 USER S GUIDE TRON follows the standard Windows methodology in operating programs The selections to perform tasks can be accomplished by selecting the drop down menus at the top of the screen or by clicking on the toolbar icons Menu Selection Menu selections may be made by left clicking the mouse button when the mouse pointer is over the particul
168. Type ACM LP Fully Aromatic Polyamide Low Pressure Advanced Composite COMTI GUN AU ON M Spiral Wound Fiberglass Outer Wrap Active Membrane Area 88 ft 8 2 m Recommended Applied Pressure 40 300 psi 3 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 15 7 Length A 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODU
169. and millimetes Dim A does not include ATD Mechanical Configuration Sanitary Style Core Tube ATD not included with element Feed Spacer 0 046 thick diamond spacer Engineered Membrane EE SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Zl 6 3 AUM High Temperature UF Turboclean Element TRIS CORPORATION Model M W C O 6338 N6DAV7 10 000 OPERATIONAL AND DESIGN DATA Membrane Type AUM Advanced Ultrafiltration Membrane Configuration Spiral Wound Turboclean Shell Active Membrane Area 138 ft 12 8 m Recommended Applied Pressure Not applicable Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 10 0 ppm Maximum Feed Flow 70 GPM 15 8 m3 hr p A Minimum Brine Flow Permeate Flow Ratio 5 1 S y 0 Maximum SDI 15 minutes 5 0 APPROV N Maximum Turbidity 1 NTU tel 9 077 6 1 RR ET Milk Fractionation Element Weight 28 12 7 Length A 3
170. com 0105 s us uololji5 ds jonpoud pue s u uu uinb i uonooeuuoo 104 BDIAIOS JOWO SNYD uoneJodJo2 desu 1961002 saljquasse e d pue Buisnou o Burpeuuoo 104 SJOJdepe pue onpoid pieoqui ssinbes Aew sjapow jueujeoe doJ UOI eJOdIOD degu 91oN OLINL Ti Et 40v0exr sene s Sd Ld SL9 JOVOSM JN 4001 8 olan Jn EZES re dN MOL 8 osvn sso Jn MS 8 OLINL 40v0rxr dN 1120 v Sdrld L Lf osan Sd ld L iY JOPOTM3 00Ld A3 L 0rOT dN M00L E Olan 4n LZer ere dN MOL v 09vn sarapas AN MS v TAGOW delt Jesoq L sui s S pinid HOOM SIIUOWSO 39 AS sonneueipAH 9 Luul dq MOG NAMWAIV Ida SOLIS DUBIQWIOIAN uoned joJ9lNA uoned 1e43l f KeJo Jidin 9 LNAWAQV 1d3s AAILILAdINOD CORPORATION 354 TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com e 0105 TriSep Applications Bulletins TRIS gt CORPORATION Following is a partial list of TriSep application bulletins Data obtained during tests or operation of actual system depend on feedwater quality operation of the system and other variables which may not be an accurate reflection of expected performance on other feedwater For more detailed help on predicting membrane or chemical performance please contact your TriSep representative TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 12
171. continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Application Dialysis Make Up Water Element Weight 45 20 Length A 40 00 1 016 Diameter B 7 90 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane ss SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Oe N 8 ACM LP Low Pressure RO Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 M5P3T6 11 500 43 0 98 50 97 50 Performance is based on the following test conditions 2 000 00 ppm NaCl 150 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type
172. dia by 40 long 0 75 O D male perm tube protruding permeate tube 90 ft 8040 ACM4 TSA 8 diameter by 40 long 1 50 LD female permeate tube flush cut 8040 ACM4 TSAN Same as 8040 ACM4 TSA but NSF approved 8040 ACM4 TSFA 8 diameter by 40 long 1 12 I D female permeate tube flush cut Filmtec style 8040 ACM4 UWA 8 diameter by 40 long 1 50 I D female permeate tube flush cut 400 ft 8040 ACM4 UWAN Same as 8040 ACM4 UWA but NSF approved 8540 ACM4 TSFA 8 5 diameter by 40 long 1 12 I D female permeate tube flush cut TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 197 PRODUCT SPECIFICATION A 2 5 ACM LP RO Element Series TRIS gt CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 2540 ACM4 TSF 1 000 3 0 99 00 98 00 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane eidele e EE Spiral Wound Fiberglass Outer Wrap Active Membrane Area 26 ft 2 4 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature
173. dia by 40 long 1 12 I D female permeate tube flush cut Filmtec replacement 8 diameter by 40 long 1 50 I D female permeate tube flush cut 400 ft Same as 8040 ACM2 UWA but NSF approved 8 dia by 40 long 1 50 I D female perm tube flush cut 430 ft 8 3 diameter by 40 long Osmo style 1 14 I D permeate tube and diameter 19 Comparison of X 20 Silica Rejection LX versus Time TRL CORPORATION AN 2 E lt L E gt 1 e x e o E c fa a 3 a an Se SE Q A ee gt E ef ba Ke 7 x un E L p un i 2g 3 G s 2 o BU Oo tr D m 9 o0 Cc en tT oO I st Q e ue O e O O O 2 oc ca d c 0 Mm c mM c mn c wv cC gt q d 2 Oo oO Gi S o a A uonssloy TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 20 A TRIS S Comparison of X 20 Delta P over Time versus Standard 344 Membrane CORPORATION sKep our YLI SEA Cl Srel HI 6L c9 LY It 91 0 ISVIOAV UO Lo uow K19A5 Surueo YLI SSI Cl 9cI HI 6L ON LV It 91 0 COl O0 VI CLI pouvoy IO oAvEH 0 Ic G CVC SUIUUNY Sujuo jA 9 is S It OSE d 9q W9 SAg q JUv g T A0d isd o1nssolg isd o1nssoJq 21 e 805 964 1235 fax e www trisep com e 0105 TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA
174. element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TRIS CORPORATION TriSep ACM2 Composite RO Membrane Elements The ACM2 membrane offers the highest rejection 99 5 and typically operate at 150 200 psi 10 14 bar The ACM2 is one of our most popular membrane elements It is a defacto standard for typical water purification requirements The ACM2 is preferred in applications with high feedwater TDS 73 000 ppm and or high recovery The lower specific flux of this membrane compared to the ACMA and ACMS allows for a more balanced hydraulic flow through the system and more balanced permeate flux rates due to the high osmotic pressure of these feedwaters 2540 ACM2 TSF 4040 ACM2 TSA 4040 ACM2 TSDA 4040 ACM2 TSF 4040 ACM2 TSOA 4040 ACM2 TWF 8040 ACM2 TSA 8040 ACM2 TSAN 8040 ACM2 TSDA 8040 ACM2 TSFA 8040 ACM2 UWA 8040 ACM2 UWAN 8040 ACM2 UWFA 8340 ACM2 TSOA 8540 ACM2 TSFA 2 5 diameter by 40 long 0 75 O D male permeate tube protruding permeate tube 4 diameter by 40 long 0 75 I D female permeate tube flush cut 4 dia by 40 long 0 62 I D female permeate tube flush cut Desal replacement 4 diameter by 40 long 0 75 O D male permeate tube protruding permeate tube 4 dia by 40 long 0 78 I D female permeate tube flush cut
175. folder name is DataTroi Then the path would be WMyServer DataTroi To start the TroiWin software once it is installed Click on Start Programs Troi For Windows Version 2 0 0 You can also place a copy on your desktop by right clicking your mouse in the desktop area and then click on New and then click on Shortcut and a pop up window will appear You can type in the above listed folder location or click on Browse and find the above listed folder then select the file TROLexe Click on the Next button and then you can input a name for the shortcut Click on Finish and you should have a shortcut on your desktop TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 396 TriSep Troi Design Program A Manual ver 2 0 0 TRIS CORPORATION 4 USER S GUIDE Before you run TroiWin software there are a few things you need to know The program is written in Visual Basic and we have tried to stay with the standard Windows methodology in operating programs The selections to perform tasks can be accomplished by selecting the drop down menus at the top of the screen or by clicking on the toolbar icons Menu selections may be made by left clicking the mouse button when the mouse pointer is over the particular menu selection or by depressing the Alt key while typing in the underlined letter of the selection you want to make 1 e Alt F would drop down the file menu
176. food and dairy and wastewater applications TriSep personnel have a long history of solving water treatment problems with some having been involved in developing and manufacturing membrane elements since the early 1970 s TriSep has and will continue to devote countless hours to engineering our membrane products to specifically meet your projects unique requirements By providing technical support with the objectives of maximizing reliability and minimizing maintenance TriSep is now established as a leading quali fied supplier of spiral wound membrane elements worldwide TriSep s elements are among the best in the industry offering a combination of high product water flux and high salt rejection rates In 1991 TriSep purchased DuPont s entire spiral wound membrane element business This acquisition included the Advanced Composite Membrane ACM technology which enabled us produce a full line of thin film composite membrane products to suit most reverse osmosis system requirements The DuPont acquisition also provided TriSep with the patented X 20 Polyamide Urea Composite low fouling membrane Originally developed by DuPont as the next generation of thin film compos ite membrane the X 20 has been further developed and commercialized by TriSep Superior fouling resistance and silica rejection compared to all other thin film composite membranes makes X 20 the membrane of choice for well in to the 21 century TriSep is the first membran
177. for more than 2 3 weeks a storage solution of 2 sodium metabisulfite and 18 glycerine in RO permeate water at a pH of 6 8 should be used for a storage solution This solution should be recirculated through the system for 30 minutes at 60 psi pressure Feed concentrate and permeate valves should be closed after the pump is shut down to keep the storage solution in the pressure tubes FLUSHING PRIOR TO USE TriSep 8 and 4 diameter elements as shipped contain the standard aqueous solution of approximately 396 of Sodium metabisulfite and 1896 glycerine These solutions must be flushed from the elements both concentrate and permeate before the elements are placed in service initially or returned to service from storage Adequate flushing can be achieved with water at a TDS up to 5000 mg l at 225 psi 15 3 bar at the permeate and concentrate rates listed below Be sure that the solubility guidelines for sparingly soluble salts maximum feed flow maximum flux rates and maximum pressure drop are not exceeded Element Minimum Concentration Rate Minimum Quantity of Permeate Diameter Inches Pressure Vessel US GPM LPM Element US Gallons liters 19 145 510 5 56 8 540 2040 The quality of the flush water is important Flush water must meet the RO feedwater guidelines detailed in the TriSep document Guidelines for Operation The flushing procedures given will reduce the total organic carbon TOC to less than 1 mg l in the perme
178. for the first stage on the print out The ionic analysis for the raw feed brine and permeate can be seen individually by clicking on the View button The second stage analysis can be seen by clicking on the View Second Stage button Clicking on the Print button will print both the first TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 401 TriSep Troi Design Program A Manual ver 2 0 0 TRIS CORPORATION and the second stage analysis To preview the print out click on File then Print Preview from the drop down menu for either the projection preview or the individual element preview This will take a few seconds to open the report writer and will create two reports To view the first stage report minimize or close the second stage report or click on the first analysis on your windows tool bar at the bottom of your screen These previews can be printed and saved as described above in the single stage section When you print an analysis from the preview screen it will only print the analysis that is currently being displayed You must print both the first and the second stage analysis individually from this screen Ionic Rejections One last feature allows you to modify the individual ionic rejections of certain classes of membranes Click on the Supplement menu selection and then select Modify Ion Salt Parameter Limits This
179. have been removed However if you experience a problem with your particular copy or hardware please let us know so that we can remedy it for future revisions by sending an e mail to info trisep com Any comments that you may want to make to improve the software will be considered for future modifications Thank you for considering TriSep in your membrane selection process TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 406 TriSep Tron Normalization Program L CM Manual ver 1 1 0 TRIS S CORPORATION 1 INTRODUCTION Welcome to TriSep s Reverse Osmosis Normalization TRON software This program is designed to help membrane operators monitor their reverse osmosis RO and nanofiltration NF systems by normalizing permeate flow rejection and delta P coefficients to account for changes in feed water and system operation The complexity of RO and NF systems coupled with the many changing process and operating variables makes it difficult for operators to detect problems Problems can develop quickly or slowly over time The ability for an operator to diagnose and remedy problems at an early stage is a key to minimizing costly membrane element replacement Our experience shows that systems that are monitored through the use of graphical normalized data experience fewer problems and enjoy longer membrane life Normalizing RO and NF data requires the use
180. hour operation Chlorine tolerance 1 000 ppm Flux rates based on clean water flux TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax e www trisep com e 0105 344 TRIS gt CORPORATION TriSep Flat Sheet Membrane SHEET MEMBRANE MATERIALS OF CONSTRUCTION Materials of construction for TriSep Corporation flat sheet stock RO and NF membranes consist of the following by membrane type Membrane Type ACMI ACM2 ACM3 ACM4 FULLY AROMATIC POLYAMIDE Membrane composition Membrane support Substrate Membrane Type X20 POLYAMIDE UREA Membrane composition Membrane support Substrate Membrane Type XN45 AROMATIC POLYAMIDE Membrane composition Membrane support Substrate Membrane Type TS80 AROMATIC POLYAMIDE Membrane composition Membrane support Substrate Membrane Type SB50 CELLULOSE ACETATE BLEND Membrane composition Membrane support Substrate Membrane Type UEIO AND UE50 POLYETHERSULFONE Membrane composition Membrane chemistry Substrate Membrane Type TM10 POLYVINYLIDENEFLUORIDE Membrane composition Membrane chemistry Substrate TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 ACM polyamide composite Modified polysulfone Non woven polyester X 20 polyamide urea composite Modified polysulfone Non woven polyester ANM polyamide composite
181. in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Sanitary Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION 3 9 TS50 High Temperature Turboclean Element TRIS gt G F PFP C E A T iN Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 3940 O8D1U8 1 600 6 0 99 00 98 00 Performance is based on the following test conditions 2 000 00 ppm MgSO4 110 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Tvpoe eene TS50 Polyamide Advanced Nanofiltration Membrane Configuration Spiral Wound High Temperature Turboclean Shell Active Membrane Area 70 ft 6 4 m Recommended Applied Pressure Not applicable Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tole
182. in this section is a copy of our competitive element replacement guide to help you in selecting the proper TriSep element for your element replacement needs Most of these elements are non standard and are made to order The only exceptions are the 4040 XXXX TSF which are normally stocked by TriSep TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 275 TRIS gt CORPORATION Desal DuPont Replacement Elements Competitive Element Replacement Guide 4040 ACM3 TSF 4040 ACM4 TSF 4040 ACMS TSF 4040 ACMS5 TWF 4040 TS80 TSF 4040 TS83 TSF 4040 X201 TSF 8040 ACM2 TSFA 8040 ACM2 UWFA 8040 ACM4 TSFA 8040 ACM5 UWFA 8040 TS80 UWFA 8040 X201 TSFA GE Osmonics Replacement Elements TriSep Model Number 4040 ACM2 TSOA 8340 ACM2 TSOA 8340 SB20 TSOA Hydranautics Replacement Elements TriSep Model Number 8540 ACM2 TSFA 8540 ACMA TSFA 8540 SB20 TSA 8540 SB50 TSA 8540 TS80 TSFA BW30HP 4040 BW30 LE4040 XLE 4040 XLE 4040 NF90 4040 NF70 4040 BW30 8040 BW30 365 BW30 400 BW30 440 BW30 LE 400 XLE 400 LE 400 LE 440 NF90 400 NF70 400 BW30 365FR GE Osmonics Model 411 HR PA 411 HF PA 811 HR PA 811 HF PA 811 HR Hydranautics Model 8540 LS Y CPA2 8540 UHY ESPA 8540 MS Y CAB2 8540 MSY CABI TriSep Model Number Desal Model Number DuPont Model Number Comments 4040 ACM2 TSDA AG4040F SG4040F 2440 Same diameter and permeate tube 4040 TS
183. inspected for length and I D Since it determines the final length of the element and the critical O ring sealing dimensions Membrane manufacture includes the use of three major sheet materials These are the brine channel spacer product channel materials and membrane substrate TriSep in conjunction with each of the manufacturers of these materials has developed specifications which are a combination of the manufacturer s product specifications and our own The combination of these specifications assures that the products are uniform and will consistently perform in their applications Depending on the material and specification in question tests are performed on a daily or weekly lot basis More routine functions i e thickness wale count are performed in house Other testing requiring laboratory analysis is performed on a more random basis at an independent test facility TriSep specifies chemical grade and purity and requires certified test reports from the manufacturer for all solvent used to produce the membrane casting solution Outerwrap resins and leaf adhesives are controlled by a combination of ratio checks and hardness cure tests on a daily and element basis TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 379 TriSep Engineering Manual TRIS gt QUALITY CONTROL PROCEDURE FOR THE CORPORATION MANUFACTURE OF TRISEP ELEMENTS 2 I
184. loaded with multiple elements in a single pressure tube This allows systems to operate at high conversions or recoveries typically 75 90 for a RO or NF system A typical pressure tube can hold 1 7 elements with 6 and 7 element long tubes being the most common for large systems To allow the permeate to exit the pressure tube the permeate tubes of each element in a pressure tube must be connected together in such a way as to not allow feed water to enter the permeate stream This is typically accomplished using a plastic interconneter that has O rings on each end At the end of the pressure tube an inboard adapter is used to adapt the element permeate tube to the pressure tube endcap The ability to use different materials for the membrane feed spacer and permeate carrier fabric depending on the application makes the spiral design a very flexible design If you wish to make an element that can operate at high pressure you can use a special permeate carrier fabric To use a NF instead of an RO membrane switch the membrane material For a high solids application use a thicker feed spacer For high temperature applications a special adhesive and the use of i temperature plastic parts End Cap Membrane Segmented Ring Element Adaptor m Ten wi M me em e G e e i e mm mm m wes Wu esch Bossa Conc Tu Iz i ee ED SS Pressuevesl Z A segmented Ring cen Ges Sem lef a A
185. manufacturing or faulty material as specified in 4 1 above 4 2 Initial Performance TriSep warrants for a period up to the Warranty Start Date per Paragraph 3 that the individual element s will have 85 of the initial minimum product flow specified and the initial minimum salt rejection as specified by TriSep in its published product specifications when such elements are tested under specified Standard Test Conditions The test period for determining minimum product flow shall be limited to no more than 24 consecutive hours 4 2 1 TriSep Liability TriSep reserves the right to repair or replace such element s as TriSep determines to be necessary to correct any deficiencies as specified in 4 2 above 4 3 Three year Element Performance The three year performance warranties set forth in 4 3 1 start on the Warranty Start Date apply to individual element s only and incorporate by reference all Conditions of Warranties described in paragraphs 5 1 to 5 5 4 3 1 X 20 ACM CA TS80 XN45 Element Performance For a period of three 3 years the minimum product water flow for X 20 ACM CA TS80 and XN45 elements under Standard Test Conditions will be at least 70 percent of the TriSep specified initial minimum flow The maximum overall salt passage X 20 ACM CA TS80 and XN45 element s under Standard Test Conditions and pressure required to give the initial specified flow will not be more than 2 times the TriSep initial maximum level
186. membrane Ultrafiltration Membrane Elements Polysulfone UF membrane 10 000 MWCO Polysulfone UF membrane 100 000 MWCO Microfiltration Membrane Elements Polyvinylideneflouride MF membrane 0 2 micron Listing for NSF Standard 61 certified elements Page 18 35 38 54 66 116 130 158 166 167 173 189 197 209 217 219 234 239 250 254 259 260 2 A TRIS S CORPORATION Replacements Replacement Guide Desal DuPont DOW Filmtec GE Osmonics Hydranautics Chemicals TriPol TriClean TF Powder TriClean TF Liquid Support Chemicals When to Clean Cleaning Procedures CONTENTS Retrofitting with TriSep Membrane Separation Products Competitive replacement guide Desal Dupont style permeate tubes Filmtec style permeate tube elements Osmonics style permeate tubes and diameters Hydranautics 8 5 diameter elements TriSep s Complete Line of Membrane Support Chemicals TriPol Antiscalants 8010 8510 9010 and 9510 Max Sat TriClean PA Powder Membrane Cleaners TriClean PA Liquid Membrane Cleaners Biocides and support chemicals When to clean your membranes Cleaning procedures and protocols Flat Sheet Membrane Flat sheet membrane manual and specs Product Applications Applications Bulletins Engineering Manual Using TriSep membrane Separation Products Filtration Spectrum Cross flow membranes Principles of RO Definitions Membranes Temperature Spirals Q C lonic Reje
187. minimum flow through the elements These net wrap elements cannot be used in standard 2 1 arrays normally used in water applications The Turboclean element minimized by pass flow to 15 20 of the feed flow This allows the TurboClean element to be used in standard water type applications like beverage water make up Following are some TriSep TurboClean elements specifically engineered for the beverage market TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 38 PRODUCT SPECIFICATION 3 8 TS 80 High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 3838 M E5U8 1700 6 0 99 00 97 00 Performance is based on the following test conditions 500 ppm MgSOA 110 psi 25 C 15 recovery pH 8 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ANM Aromatic Polyamide Advanced Nanofiltration Membrane Configuration Spiral Wound High Temperature Turboclean Shell Active Membrane Area 68 ft 6 2 m Recommended Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range
188. pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Configuration Spiral Wound Fiberglass Outer Wrap Active Membrane Area 88 ft 8 1 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 15 7 Length A 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 78 19 8 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Osmo Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U
189. pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ANM Aromatic Polyamide Advanced Nanofiltration Membrane Configuratio EE Spiral Wound Fiberglass Outer Wrap Active Membrane Area 365 ft 33 5 m Recommended Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU EH Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fa
190. passage through a semipermeable membrane is defined by Equation 1 Q K AP An A t 1 where Q Flow rate of water through the membrane K membrane permeability coefficient for water hydraulic pressure differential across membrane At osmotic pressure differential across membrane A membrane surface area t membrane thickness similarly the rate of salt passage 1s defined by Equation 2 Q K AC A 2 where Qs flow rate of salt through the membrane Ks membrane permeability coefficient for salt AC salt concentration differential across membrane The rate of water flow through the membrane is proportional therefore to the pressure differential across the membrane while the rate of salt flow is proportional to the concentraion differential and independant of the applied pressure Thus an increase in operating pressure will increase the water flow without changing the salt flow Conversion or recovery as it is sometimes called is defined by Equation 3 Y Q Q x 100 3 where Y conversion or recovery Q product water flow rate Q feed water flow rate Operation at 75 recovery means that from 100 gpm of feed water 75 gpm of product water will be produced together with 25 gpm of concentrate or brine containing most of the dissolved solids The term salt passage is defined by Equation 4 SP C C x 100 4 where SP salt passage C salt concentration in product stream C salt concentrati
191. pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION 4 ACM RO Element Series TRIS gt CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 ACM1 TWF 2 000 7 0 99 50 98 50 Performance is based on the following test conditions 2 000 00 ppm NaCl 225 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane CGopnfguraton a k Spiral Wound Fiberglass Outer Wrap Active Membrane Area 90 ft 8 4 m Recommended Applied Pressure 40 300 psi 3 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow
192. ppm max 80 GPM 18 m3 hr 5 1 Permeate Tube C 1 14 29 0 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Osmo Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TRIS CORPORATION Permeate flow Model GPD m3 day 8540 SB20 TSA 8 400 31 0 PRODUCT SPECIFICATION 8 5 CA RO Element Series Minimum Salt Rejection Average Salt Rejection 98 00 97 00 Performance is based on the following test conditions 2 000 0 ppm NaCl 420 0 psi 25 C 15 recovery pH 5 5 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type Configuration Active Membrane Area Recommended Applied Pressure Maximum Applied Pressure Recommended Operating Temperature Feedwater pH Range Chlorine Tolerance Maximum Feed Flow
193. s permeate flow may vary 15 Engineered Membrane Ira y SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION TRIS gt CORPORATION 8 XN45 Nanofiltration Element Series Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 XN45 UWA 10 500 39 0 95 00 92 00 Performance is based on the following test conditions 2 000 00 ppm MgSOA 110 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type XN45 Polyamide Advanced Nanofiltration Membrane Configuration Spiral Wound Fiberglass Outer Wrap Active Membrane Area 400 ft 37 2 m Recommended Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 5 ppm nominal 1 0 ppm max Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum T
194. the following quality wore city water quality varies considerably Conductivity 1000 2400 u mho cm Total Hardness 50 300 mg L as CaCO Silica SiO 3 0 6 0 mg L Temperature 50 88 F Pre treatment consists of a clarifier multimedia filter 1 0 micron bag filters 1 0 micron cartridge filter nominal sodium bisulfite feeder and UV 232 NM wavelength System design consists of 2 parallel trains each train with a 6 3 array using 6M vessels ach train is designed to produce 150 gpm of product water Since the introduction of the X 20 elements cleaning frequency has been reduced to once every 14 days The elements have been in operation for over 1 year with no loss in flux or rejection The X 20 membrane is showing a significant increase in silica rejection versus the previously installed standard composite membranes Performance after 16 800 hours of operation and over 700 cleaning hours is as follows Start Up After 16 800 hours Inlet Pressure 165 psi 170 psi Product Flow 150 gpm 150 gpm System Recovery 75 75 System TDS Rejection gt 99 gt 99 System Silica Rejection gt 99 gt 99 1 Stage Delta P 23 psi 24 psi 2 Stage Delta P 15 psi 16 psi The X 20 spiral wound elements have provided increased silica rejection The superior low fouling performance of the X 20 membrane has decreased cleaning intervals from 2 days to 14 days The membrane has been subjected to over 700 cleaning hours without a loss in p
195. tic pails Pricing is F O B our factory in Goleta CA Delivery for most orders 1s 1 2 days after receipt of order MSDS SHEETS For the most up to date information on MSDS sheets please contact our web site at www trisep com 334 emm TriSep Corporation Chemical Manual TRIS gt CORPORATION TRISTORE 110 MEMBRANE STORAGE SOLUTION e Preserves elements for long term storage PROBLEM In many installations worldwide RO NF and UF membrane elements need to be stored for extended periods of time If not stored properly elements may foul from biological growth dry out or freeze This can result in irreverisble loss of permeate flow and rejection SOLUTION TriStore 110 is a specially formulated storage solution that will not harm polyamide cellulose acetate polysulfone or other types of RO NF and UF membrane elements APPLICATION TriStore 110 should be mixed in a cleaning tank equipped with a mechanical mixer low pressure recircu lation pump and cartridge or bag filter This solution should be applied at a flow rate of 8 10 gpm per 4 pressure tube or 30 40 gpm per 8 pressure tube at a pressure of between 60 120 psi Adjust pH to 4 6 with sodium hydroxide Add 1 gallon of TriStore 110 per 5 gallons of RO permeate or DI water Recirculate solu tion for 15 to 30 minutes or until some permeate 1s pro duced This indicates the storage solution has permeated the membrane The above solution will
196. tl I e Ajs soruotusO I Iv801I L VOXX XXXX 0p08 OLOCCII JojooeuuooJoQu C0 9y OH 6I euoj nsAqoqd AIl e A1S soruouisQ I I 80I L VOXX XXXX 0p08 c9ITVCII 1ojoouuooJo9ju LS STS 06 0T OA d duct I IS soruotusO CI 80I L VOXX XXXX 0p08 tc9 kCI I Sn d puq S6 Lv vv Oc euoj nsA oq AISIT dat ua C6c600I L HXX XXXX 0p08 LICVCII 10jo euuooJoju 96 Ic euog nsA oq AIII duio L ua CYESOLL HXX XXXX 0p08 CSIVcll sn d pud S6 Lv vv Oc euog nsA oq AISTII domat OS oq S PIO COCOOLL DXX XXXX 0p08 LICVCII JoJsouUOdJOUT 96 IC uoj ns od AISIT duio T y31H oq 914S pO CYESOLL DXX XXXX 0p08 SIvCII 0708 maat Aumunq ZO SOT LL bh SHV d l4 duct I ueop ogquin p SAXX XXXX 0p08 SOITCII Sn d pud 8 8c Ol CI AION duct l uUeo oqan CO0S80I L SAXx Xxxx 0p08 OSCTCII Jojoouuo9Jo1u 0 00 c AION duct l uUeo oqan CO0SLOI L SAXx Xxxx 0p08 SIb snid puq 0 89 00 6c euoj nsA oqd QGI cUI o A1s QUA 1I 0 6801 L DJXX XXXX 0p08 8crcll 1ojoouuooJoju C0 9p c9 6T euoj nsA oqd Q I cUI o A1s 20101 1 08L0I L DAXX XXXX 0p08 6ZIvCII 0708 mwg Aurumq 0 UO Or SHV d l4 QGI cUI e Ajs SOPOT V JIXX XXXX 0p08 90vcII Sn d pud 8 8c OL CI AION duct I S UA COS80I L VAXX Xxxx Q708 OSCTCII 10 99UU09194U PO 8 00 c AION duct l AIS SOPOT CO8LOI L VAXX Xxxx Q708 OSITCII Snid puq ST 9 Iv SI OA d AISIT e A4js esoq juognd I 6c601 L VOXxX xxxx 0708 SSOvCII JojuuooJu OC FCI S
197. window allows modification of the individual ion rejections relative to sodium and chloride which are normally set to 1 Do not use this feature unless you fully understand the impacts of these changes To reset the values to their defaults click on Reset Ion Salt Parameter Limits When a change is in effect a message Ionic Rejections is displayed in the upper right hand corner of the calculation window 5 Engineering Considerations for Spiral Wound Membrane Systems When designing a SWMS system two factors are very important to insuring a reliable design membrane flux and the element Beta Factor Both of these values are listed on the screen displays and on the print outs Flux The membrane flux is the amount of product water made per unit area of membrane in a given period of time It is normally expressed in units of gallons per square foot per day GFD or liters per square meter per hour LMH For a given element which has a given area the higher the flux the higher the permeate water productivity The overall system flux can then be controlled by varying the pressure or the number of modules used to build the system The overall system flux is displayed on the calculation window Higher water fluxes can result in higher fouling rates Table 2 gives some guidelines for fluxes that should be used under varying feedwater conditions In general feed waters with high fouling potentials should use low membrane fluxes to minimize
198. 0 1 016 Diameter B X 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 028 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TriSep ACM4 Composite V RO Membrane Elements TRIS IS P CORPORATION The ACM4 membrane offers higher flux than the ACMI or ACM2 allowing operation at ultra low pressures The ACM4 will typically operate at feed pressure of 100 150 psi 7 10 bar Even at these high flux rates the ACMA still averages 99 2 salt rejection Due to the high specific flux these membranes are best suited to applicaitons with relatively low TDS 3 000 ppm to achieve balanced flux rates within the system 2540 ACMA TSF 2 5 diameter by 40 long 0 75 O D male permeate tube protruding permeate tube 4040 ACM4 TSA 4 diameter by 40 long 0 75 I D female permeate tube flush cut 4040 ACM4 TSF 4 diameter by 40 long 0 75 O D male permeate tube protruding permeate tube 4040 ACM4 TWA 4 diameter by 40 long 0 75 I D female permeate tube flush cut 90 ft 4040 ACM4 TWE 4
199. 0 98 00 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM LP Fully Aromatic Polyamide Low Pressure Advanced Composite Configuration Spiral Wound Fiberglass Outer Wrap Active Membrane Area 365 ft 33 5 m Recommended Applied Pressure 50 300 psi 3 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 45 20 Length A 40 0 1 016 Diameter B X 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Indi
200. 0 NTU The SpiraSep process removes suspended solids and other particulate matter consistently providing permeate water with an SDI lt 2 0 and turbidity lt 0 1 NTU UF permeate is then fed directly to the RO system which reduces the salinity to drinking water levels allowing for safe discharged back into the ground water tables via a percolating pond Figure 1 Landfill leachate pond complete with alligator HI mg Triseo Corocration A Crystal Clear Solution Submerged Ultrafiltration System Improves Swimming Pool Water Safety at Rehabilitation Center Case Study Denmark The Challenge A rehabilitation center was concerned about the safety of their pool water due to disinfection by products and chlorine resistant microorganisms such as cryptosporidium and giardia warranted the need for improved treatment methods It has been found that certain chlorinated organic compounds commonly found in swimming pools can cause bladder cancer owimming pool water is traditionally treated using a combination of coagulation sand filtration and chlorination The goal was to provide a treatment process that can safely remove all pathogens while eliminating the need for chlorine addition and subsequent harmful disinfection byproducts he Solution A process was developed using a combination of ultrafiltration UF and ultraviolet UV light to treat and disinfect the swimming pool water The swimming pool water is
201. 03 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION LA Zi 8 ACM LP Low Pressure RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 ACM4 TSAN 14 600 55 0 99 00 98 00 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM LP Fully Aromatic Polyamide Low Pressure Advanced Composite COMTI GUN AU ON M Spiral Wound Fiberglass Outer Wrap Active Membrane Area 365 ft 33 5 m Recommended Applied Pressure 50 300 psi 3 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms
202. 03 409 TriSep Tron Normalization Program L CM Manual ver 1 1 0 TRIS S CORPORATION View Projects When this option is selected you will be prompted to select a project from a drop down list of entered projects Click on the project you wish to edit and then click on OK Alternatively you can double click on the project that you want to edit This will open the project and allow you to edit any of the data Double clicking will not work to select the first project on the list Simply highlight this project and close the window to select Once you have finished inputting all of the data on this screen click on the ReCalculate button Delete Analysis Once a Project is deleted the detail data records of the project are deleted and permanently removed from your list of files on record in your table Click on the project that you want to delete then click OK To delete a detail point position or click on the record you want to delete and then click on the delete button below the grid This will delete only that particular data point and not the entire project Print This will allow you to print out a project that has previously been calculated and saved It is not necessary to recalculate the design before printing it To print a particular project select it from View projects and then click on of the print options Exit Select this option when you are finished using Trisep s Reverse Osmosis Normalization Soft
203. 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Zum 8 ACM RO High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 M2D7T9 9 400 35 0 99 00 98 00 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Configuration Spiral Wound Turboclean Shell Active Membrane Area 355 ft 32 6 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Fl
204. 046 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane End nF I Y i SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION TRIS CORPORATION 8 ACM RO High Temperature Turboclean Element Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8038 M2G4U8 9400 35 0 99 50 98 50 Performance is based on the following test conditions 2000 ppm NaCl 225 psi 25 C 15 recovery pH 8 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Configuration Spiral Wound High Temperature Turboclean Shell Active Membrane Area 355 ft 32 6 m Recommended Applied Pressure Not applicable Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow
205. 1 is shipped as a liquid in 7 gallon 10 x gallon 5 gallon and 55 gallon plastic containers Pricing 1s F O B our factory in Goleta CA Salem VA or Duisberg Germany Delivery for most orders 1s 1 2 days after receipt of order MSDS SHEETS For the most up to date information on MSDS sheets please contact our web site at www trisep com 319 TriSep Corporation Chemical Manual TRIS gt CORPORATION TRICLEAN 212CA HIGH PH POWDER CLEANER e Used to remove biological organic and colloidal fouling on CA membrane e Buffered pH to prevent hydroly sis of CA membrane PROBLEM In many installations worldwide celluslose acetate CA RO membranes can become fouled with bio logical organic and colloidal foulants These fou lants can quickly lead to a loss of system perfor mance associated with a decrease in permeate flow and increase in differential pressure and a loss of element rejection If left unchecked this fouling can permanently damage the membrane elements leading to costly and premature membrane replace ment SOLUTION TriClean 212CA removes biological organic and colloidal foulants without damaging sensitive CA membrane elements TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 APPLICATION TriClean 212CA should be mixed in a cleaning tank equipped with a mechanical mixer heater low pressure recirculati
206. 11 TERMS AND CONDITIONS OF SALE GENERAL SELLER provides all data in good faith and believes the information and data contained herein to be accurate and useful It is the user s responsibility to determine the appropriateness of SELLER s products for the user s specific end uses 1 PRICES AND PAYMENT Terms of payment on open accounts only are net 30 days from the date of invoice This agreement is subject to credit approval Retention is NOT allowed Interest will be charged on past due accounts Interest charges will be calculated on the unpaid balance at 1 25 per month 15 per annum or the maximum rate allowed by law whichever is more Unless specifically included as a separate item or required by contract prices quoted do not include any city county state or federal taxes or transportation of SELLER s material or service 2 WARRANTIES SELLER warrants that the material will conform to the description contained in the applicable published specifications and Standard Guarantee for Spiral Wound Products SELLER makes no warranty express or implied of merchantability or of fitness for a particular end use SELLER s liability for breach of warranty is limited solely to the supply or repair or replacement of element materials and SELLER shall not be held liable for consequential or incidental damages resulting to CUSTOMER or others from the furnishing or use of materials said to be defective SELLER s maximum total
207. 15 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type AMM Advanced Microfiltration Membrane Cong AMON uuu aa E oa akana URS Spiral Wound Fiberglass Outer Wrap Active Membrane Area 62 ft 5 7 m Recommended Applied Pressure 5 200 psi 0 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 10 0 ppm Maximum Feed Flow 25 GPM 5 6 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 12 5 4 Length A 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 047 thick parallel spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 80
208. 19 30 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Desal DuPont Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION 9 ACM RO Element Series TRIS gt CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 ACM2 TSDA 9 700 36 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane ONTO ON I uu aan wa Spiral Wound Fiberglass Outer Wrap Active Membrane Area 365 ft 33 5 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Toleranc
209. 20 Low Fouling RO Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 N1F3T7 9 400 35 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane ei le le e NEE Spiral Wound Turboclean Shell with FoulGuard Technology Active Membrane Area 355 ft 32 6 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 2NTU Application Waste Water High Pressure Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mech
210. 2008 USA Dye House Wastewater 495 20 50 22 March 2008 Honduras Dye House Wastewater 495 20 50 29 January 2008 Dominican Republic Dye House Wastewater 385 20 50 22 July 2008 Honduras Surface Water 20 100 300 20 March 2008 Peru Surface Water 20 100 300 20 March 2008 Peru Chip Sawing Wastewater 40 50 100 18 April 2008 Singapore Swimming Pool 15 5 10 30 April 2008 Germany Surface Water 15 100 200 25 August 2007 Peru Industrial Wastewater 200 50 100 15 July 2007 India Coal Bed Methane 500 10 20 30 August 2007 USA Municipal Wastewater 550 10 20 30 April 2005 Spain Surface Water 550 5 1000 20 June 2006 Canada Surface Water 100 50 100 Do June 2006 Spain Swimming Pool 285 10 30 35 July 2006 Denmark Industrial Landfill Leachate 67 100 300 15 February 2006 Canada Municipal Landfill Leachate 30 10 50 15 October 2005 USA Chip Sawing Wastewater 80 50 100 18 May 2006 Philippines Fixed Film Bioreactor 15 500 1000 15 November 2007 Canada Fixed Film Bioreactor 15 500 1000 15 November 2007 Canada Fixed Film Bioreactor 9 500 1000 15 February 2007 Canada Fixed Film Bioreactor 9 500 1000 15 February 2007 Canada Fixed Film Bioreactor 9 500 1000 15 January 2007 Canada Fixed Film Bioreactor 9 500 1000 15 January 2007 Canada Fixed Film Bioreactor 9 500 1000 15 January 2007 Canada Fixed Film Bioreactor 9 500 1000 15 November 2006 Canada Fixed Film Bioreactor 9 500 1000 15 November 2006 Canada Fixed Film Bioreactor 7 500 1000 15 February 2006 Canada
211. 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 2 NTU JADI rez U DE Beverage Water Make up Element Weight 45 20 Length A 40 1016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane n SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION 8 AUM Ultrafiltration Turboclean Element Series RI E2 QA A FERANT Permeate flow Model GPD m3 day M W C O 8040 N6E6Q2 14 000 52 0 10 000 Performance is based on the following test conditions 500 00 ppm 10K PEG 30
212. 25 gallons of water in the tank Allow to recirculate until thoroughly mixed D Add 1 gallon of TriClean 211 per every 100 gallons of water in the tank Allow to recirculate until thoroughly mixed E Check pH of solution proper range is between 2 0 and 3 5 unless otherwise specified by membrane manufacturer TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax e www trisep com e 0105 341 emm TriSep Corporation Chemical Manual TRIS gt CORPORATION F Isolate first pass to be cleaned With Concentrate and Product Lines diverted to proper drain slowly run cleaning solution through pressure vessels until all remaining water is out of vessels and cleaning solution is coming out of concentrate line Shutdown pump and divert Concentrate and Product lines to cleaning solution tank G If tank volume is now too low mix additional cleaning solution H Start recirculating the cleaning solution through the vessels at specified flow rate or if different at manufacturer s specified flow rate per vessel Pump pressure should be between 20 and 50 psi Recirculate for 1 hour checking pH periodically If pH goes above 5 0 a new solution will have to be mixed l Shutdown pump and allow to static soak overnight After soaking recirculate each pass for 20 minutes J Rinse using rinsing method TSR 1 Rinsing TSR Procedures TSR 1 Post Cleaning Rinse A With pump in the off posit
213. 3 JAI 89S SSUIY C O I pue s eos vung SUNIA pue ISTI SUE WT PSS IW TPIS Surq O OT Surq O OT LV oqn 9107 Surq O V I 96CvcII SUTs O 9A99IS O CVCII Surq O VI S60vcII Surq O V I SIOPCII Surq O V I ICOVCII Surq O OT Surq O O I Surq O OT Surd O OT Surq O OT Surq O OT Surq O OT Surq O OT Surq O OT Surq O OT TEIS vulg TEIS vulg TEIS vulg TEIS vulg TEIS SUuH od BIS SPPON mun V4IXX XXXX 0vp08 ttlIvcII VXX XXXX 0v08 OCIVCII COTVCII VXX XXXX 0p08 SSOETII d SerdsS p 0 c1I desexds 8 0 c11 L6CVc1I C 7PTII 860vCII LEOETII 600 ZII V LXX XXXX 0p08 610 C I VOXX XXXX 0p08 6 0 c 11 Hxx Xxxx 0p08 6L0 c11 r XX XXXX 0v08 6LOETIT SXx XXXX 0t08 6LOETII SAXX XXXX 0 P08 PIDETII SAXX XXXX 0H08 PIDETIT VAXX XXXX 0 P08 PIDETII VAXX XXxx 0708 6LOETII VXX XXXX 0p08 LOOPZII V LXX XXXX 0p08 ZOOETIT HXX XXXX Q 08 ZOOETIT WAXX XXXX 0 P08 ZOOETII VAXX XXXXx 0708 ZOOETII VXX XXXX 0p08 ZOOETII JoquinN Med p Jo Sed S INWINA TH WALA VIG HONI 8 SSMS 0708 427 TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax e www trisep com 0703 WY OG OT 8002 62 01 oqn T O 1edng Jayleg os ces IVd sJu oururo eos SSULI C 8 s eos uttq Z c6 vI eqn 2102 d Sul Ic 0 qn 2102 d Sul 08 9 IVd ju2ululo 69S IZ O omge1oduuo 1 ug1H 70 oqn L 9102 9 A1S soruouis 600 ueo ooqmn g dat ut ais P
214. 3117 USA 805 964 8003 805 964 1235 fax e www trisep com 0703 The average gallons per square foot of membrane area per day GFD per element must not exceed 20 if the turbidity is less than 0 1 or 18 if the turbidity is equal to 0 1 but less than 0 3 or 15 if the turbidity is equal to 0 3 but less than or equal to 0 5 or 12 if the turbidity is equal to 0 5 but less than or equal to 1 0 or 10 if the turbidity is equal to 1 0 but less than or equal to 2 0 Operation at turbidities gt 0 3 may result in increased cleaning frequencies When the feedwater is RO permeate elements may operate at flux rates up to 30 gfd Turbidities may not be a good indicator of organic fouling potential FOR STANDARD WARRANTY SPIRAL WOUND ELEMENTS 3 YEAR STANDARD WARRANTY FLUSHING Flush water must be of good quality meeting Guidelines and of low TDS 2000 ppm The product side must be open to atmosphere when flushing or adding water to the element When scale inhibitor 1s used the element must be flushed at shutdown within 15 minutes to remove the Antiscalant and the supersaturated salt solution SHIPPING HANDLING AND STORAGE When not in operation the membrane must be kept saturated with good quality feedwater meeting Guidelines and having a low TDS 2000 mg l at all times The as shipped elements must be kept sealed in its original double plastic bag in a cool dry place out of direct sunlight until required for instal
215. 35 fax www trisep com 0105 300 A TRI CORPORATION Triseo Corocration A Crystal Clear Solution Alkalinity Reduction Process Using Ultrafiltration Provides Cost Effective Solution for the Bottling Industry Case Study Pilot Test The Challenge Bottling facilities typically rely on treatment methods such as lime softening clarification chlorination and filtration for their water treatment needs These traditional treatment technologies require large footprints and generate large volumes of waste i e sludge Chlorination also increases the risk of disinfection by products that are highly undesirable he Solution A pilot study was conducted to determine the feasibility of using a new treatment method for the beverage industry alkalinity reduction using ultrafiltration UF membranes where a lime softening process is combined with submerged membrane filtration This system schematic provides a superior quality effluent while reducing total footprint The precipitation of alkalinity through the addition of lime allows the UF membrane to effectively reduce alkalinity concentrations to desired levels Since UF membranes are a complete barrier layer suspended solids and viruses are removed generating a pure water supply For additional information regarding SpiraSep UF membranes please contact Mike Snodgrass at 1 805 964 8003 ext 113 or send e mail to snodgrass trisep com he Results A Spira
216. 35 fax www trisep com 0703 390 TriSep Engineering Manual ion TROUBLESHOOTING IRIS CU TRISEP ELEMENTS INTRODUCTION The performance of a element system is determined by the quality and quantity of product water Salt rejection and product flow are therefore important parameters for system evaluation In certain situations changes in the element s differential pressure AP can be used as another parameter for system evaluation A problem exists when these factors are outside the range of protected values Although performance may still satisfy the end user any unexpected change in these parameters should be investigated and corrective action taken immediately to prevent further deterioration of the system Many factors affect salt rejection product flow and element AP Some of these items involve changes in operating conditions These changes can be taken into account by normalizing to a fixed set of conditions Performance variations unexplained by operating conditions involve troubleshooting the subject of this section ONLINE INVESTIGATION Online investigation is done while the system is in operation It involves analyzing performance trends in normalized salt rejection and product flow and correlating these trends with symptoms of known problems The information for the online investigation is obtained from the plant operating data log and basic plant design package The frequency accuracy and completeness of the operating lo
217. 355 ft 32 6 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Aple Le E General Pharmaceutical Element Weight 45 20 Length A 40 00 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Zl 8 X 20 Low Fouling RO Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Reje
218. 384 TriSep Engineering Manual TRIS JS TRISEP ELEMENT JES tabii LOADING PROCEDURES HANDLING ELEMENTS Do not manually lift elements and or pressure vessels which weigh more than can be safely handled by one person See the document Shipping Information for the approximate dimensions and weights for packaged TriSep elements For shipping the elements in sealed double plastic bags and placed in cardboard containers PROTECTION AGAINST OVER PRESSURE Install adequate pressure controls and or relief devices TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 385 TriSep Engineering Manual TRIS gt CORPORATION INSTALLING REMOVING ELEMENTS Only qualified personnel should install remove elements Do not use gas or hydraulic pressure to remove a pressure vessel end plate or element from a pressure vessel 1 8 9 10 11 12 13 14 15 New elements are shipped in vacuum sealed three ply bags that are packaged in individual cardboard boxes or styrofoam cartridges Please inspect all elements for signs of physical damage that may have occurred during shipping Remove the elements from their plastic bags and stand vertically with the brine seals at the bottom Check that each element brine seal has a light coating of Parker Super O Lube or glycerine Open and remove the pressure vessel end caps and check that the perme
219. 3Sl31 dO NOISSIW l3d SPLA Se eet ee as SIN SUM zm SINJWWOO Badii TVILN3GI3NOO ON ANVI dOd CSEVC L L 8 6rrL HL IA Lserzlt resp wi OSerZLL O 6rrlLlLL Whe ddd ONIONVAAIOL AddV DJW OLO IWWIDSG 3OV Id 3338HL 0 IVWIO3Q 3OVld OML v ie ML D erercil S 6rblll Wel d CD esa seem srevelt rom WOL _ dasta Y SYS noon L31vOS Lrerell tt we IN3WQ 3M Q1OJINVW SS191 Jdid OL HS PI SIVIL 0 1 V vaq Qrercll Zepp WO ITE CEM ANVINVSSI SEIT EVEL L aere Lem Wy SSES EES ON 1ivd ON ONIMVEG AZIS WLSAS EXSvO AVIN SI DOE CEP E ONO SIL NS SPE L S EECHER L SPIRASEP Itration Membrane Technology EN A Y Ultrafi Y Ul O EES IS NOILdINOSIA Aaa SNOISIA33 l C y S 9 Z 8 FRISE CORPORATION 17 TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 X 20 Low Fouling RO Membrane N The Unique Chemistry that just works TRIS gt CORPORATION Almost all commercially available reverse osmosis membranes available today are based on the chemistry patented by John Cadotte patent number 4 277 344 344 Most recent improvements in the RO industry have come from optimizing either the flux or the rejection of the 344 chemistry This chemistry is classified as a fully aromatic polyamide but has res
220. 4 8003 805 964 1235 fax www trisep com 0703 389 TriSep Engineering Manual TRIOS ELEMENT STORAGE RECOMMENDATIONS CORPORATION FOR SB20 and SB50 MEMBRANE TYPES This document covers all SB20 and SB50 spiral wound cellulose acetate CA blend RO membrane elements SHORT TERM ELEMENT STORAGE For elements that will be shut down for short periods of time less than 2 3 weeks pretreated feedwater should be flushed through the system daily at low pressure 20 30 psi This will minimize the growth of microbiological organisms and reduce the chance of scaling LONG TERM ELEMENT STORAGE TRISEP 8 20 3 cm and 4 10 2 cm diameter CA elements stored in the factory shipping solution will retain the flow salt passage performance for a period of at least twelve 12 months from date of shipment ex works or twelve 12 months following the addition of the sanitizing solution if the elements remain sealed away from direct sunlight and storage temperature guidelines are followed between 32 F 0 C 104 F 40 C For extended storage times exceeding three 3 months optimum storage temperature must be less than 60 F 15 C If elements are to be stored for periods greater than twelve 12 months consult TriSep Corporation for procedures to minimize long term effects For elements that have been placed in service and will be out of service for more than 2 3 weeks a storage solution of 2 sodium metabisulfite and 18 glyceri
221. 40 long 0 75 I D female permeate tube flush cut 4040 ACM3 TSF 4 diameter by 40 long 0 75 O D male permeate tube protruding permeate tube 4040 ACM3 TWF 4 dia by 40 long 0 75 O D male perm tube protruding perm tube high area 8040 ACM3 TSA 8 diameter by 40 long 1 50 I D female permeate tube flush cut 8040 ACM3 TSAN Same as 8040 ACM3 TSA but NSF approved 8040 ACM3 UWA 8 diameter by 40 long 1 50 LD female permeate tube flush cut 400 ft 8040 ACM3 UWAN Same as 8040 ACM3 UWA but NSF approved TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 189 PRODUCT SPECIFICATION Za 4 ACM RO Element Series TRIS gt CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 ACM3 TSA 2 800 10 0 99 20 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane COMM QUIN GIOI L ste uqu La cet T Spiral Wound Fiberglass Outer Wrap Active Membrane Area 88 ft 8 2 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Tempe
222. 5 964 1235 fax www trisep com Permeate specific flux is clean water flux at standard conditions above Not applicable for all feed water conditions Triseo Corporation A Crystal Clear Solution Ge Integrated Submerged Membrane Module Featuring SpiraSeo Ultrafiltration Technology Process Description iSGO is a patented submerged membrane technology U S Patent No 6 755 970 where the element and process tank have been integrated into one module reducing membrane fouling and life cycle costs The need for a large process tank is eliminated simplifying design construction and maintenance over the life of the system ico Membrane cassette By integrating the membrane element and process tank into one module the overall liquid feed volume is reduced by as much as 50 This allows the 5S0 design to effectively manage the solids loading inside the membrane element with frequent tank draining Chemical consumption is also reduced as the system cleaning solution volume is much lower as well For additional information regarding SpiraSe UF membranes please contact Mike Snodgrass at 1 805 964 8003 ext 113 or send e mail to snodgrass trisep com Lower Membrane Fouling With ei design the TSS concentration never reaches a steady state value as the feed solution is completely removed and replenished with fresh feed after every backwash As a result the solids profile inside the element has a saw too
223. 5 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION A lt 8 ACM LP Low Pressure RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 ACM5 TSA 11 900 45 0 98 50 97 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 150 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM LP Fully Aromatic Polyamide Low Pressure Advanced Composite Configuration Spiral Wound Fiberglass Outer Wrap Active Membrane Area 365 ft 33 5 m Recommended Applied Pressure 50 300 psi 3 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in k
224. 5 964 8003 Fax 805 964 1235 www trisep com TRIS CORPORATION Permeate flow Model GPD m3 day 8040 TM10 QXA 10 800 40 0 PRODUCT SPECIFICATION 8 AMM Microfiltration Element Series Pore Size 0 2 microns Permeate flow is based on the clean water flux at the following test conditions 10 0 psi 25 C pH 8 0 15 recovery 15 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type Configuration Active Membrane Area Recommended Applied Pressure Maximum Applied Pressure Recommended Operating Temperature Feedwater pH Range Chlorine Tolerance Maximum Feed Flow Minimum Brine Flow Permeate Flow Ratio Maximum SDI 15 minutes Maximum Turbidity AMM Advanced Microfiltration Membrane Spiral Wound Fiberglass Outer Wrap 2 0 ft 24 8 m 5 200 psi 0 3 14 bar 600 psi 41 bar 35 113 F 2 45 C 2 11 continuous 10 0 ppm 95 GPM 22 m3 hr 5 1 Element Weight Length A 45 20 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in ki
225. 5 964 8003 Fax 805 964 1235 www trisep com TurboClean Sanitary Elements for Food Applications TRIS CORPORATION The TurboClean element can reduce by pass flow by 35 44 when compared to commercially avail able sanitary membrane elements This improves overall hydraulic control in the pressure vessels resulting in energy savings improved membrane life and significant improvements in processing and cleaning efficiency The TurboClean element was developed by TriSep Corporation as a sanitary membrane that uses a hard outer shell A basic design requirement of a sanitary element is that it has no dead zones or non flow areas Conventional spiral wound elements use a brine or peripheral seal to prevent feed water from bypassing through the annular area formed between the pressure vessel inner diameter and the element outer diameter This results in a dead zone or stagnant area between the outside of the element and the inside of the pressure vessel For food and dairy applications it 1s a requirement that some of the process fluid must by pass or flow around the outside of the element to insure that this annular area is continuously flushed and that there are no areas In which product can become stagnant or which are not fully exposed to cleaning agents Different manufacturers employ different means of enclosure In an attempt to provide mechanical stability for the element while assuring this by pas
226. 50 98 50 Performance is based on the following test conditions 2 000 00 ppm NaCl 225 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Configuration Spiral Wound Fiberglass Outer Wrap Active Membrane Area 400 ft 37 2m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 4 0 Maximum Turbidity 1 NTU Element Weight 50 23 Length A 40 00 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 028 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual
227. 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 028 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION A N 8 ACM RO Turboclean Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 M3P3T6 11 000 41 0 99 50 98 50 Performance is based on the following test conditions 2 000 00 ppm NaCl 225 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Configuration Spiral Wound Turboclean Shell Active Membrane Area 355 ft 32 6 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11
228. 7 cm wide nominal polyester substrate Above performance based on 2000 ppm NaCl DI water 225 psig 15 3 bar 770F 250C negligible recovery pH 8 1 hour operation Chlorine tolerance lt 0 1 ppm 2 XN45 membrane type is provided rolled In approximately 300 ft 91 44 m lengths on a 42 in 106 7 cm wide nominal polyester substrate Above performance based on 500 ppm NaCl DI water 100 psig 6 8 bar 770F 250C negligible recovery pH 8 1 hour operation Chlorine tolerance lt 0 1 ppm 3 SB50 cellulose triacetate blend membrane is provided rolled in approximately 250 ft 76 2 m lengths on a 39 8 in 101 1 cm wide nominal polyester substrate Above performance based on 2000 ppm NaCl DI water 420 psig 28 6 bar 770F 250C negligible recovery pH 5 5 30 minutes operation Chlorine tolerance 0 5 ppm nominal 1 0 ppm maximum 4 UES0 and UE10 membrane type is provided rolled in approximately 300 ft 91 44 m lengths on a 42 in 106 7 cm wide nominal polyester substrate Above performance based on 500 ppm Dextran DI water 30 psig 2 bar 770F 250C negligible recovery pH 8 1 hour operation Chlorine tolerance 1 000 ppm Flux rates based on clean water flux 5 TM10 membrane type is provided rolled In approximately 300 ft 91 44 m lengths on a 42 in 106 7 cm wide nominal polyester substrate Above performance based on clean water 10 psig 0 7 bar 770F 250C negligible recovery pH 8 1
229. 78 ft 7 2 m 5 200 psi 0 3 14 bar 600 psi 41 bar 35 113 F 2 45 C 2 11 continuous 10 0 ppm 20 GPM 4 5 m3 hr 5 1 5 0 1 NTU General Pharmaceutical Element Weight Length A 12 5 4 40 00 1 016 Diameter B 4 00 101 Permeate Tube C 0 62 15 9 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Feed Spacer 0 031 thick diamond spacer Desal DuPont Style Core Tube Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane EE SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION pA N 4 ACM High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 O6Q3U8 1 400 5 0 99 50 98 50 Performance is based on the following test conditions 2 000 00 ppm NaCl 225 00 psi 25 C 15 recovery pH 8 00 30 minutes operation Permeate flow rate is after thermal set OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Configuration Spiral
230. 7P4U8 1 800 6 0 99 00 97 00 Performance is based on the following test conditions 2 000 00 ppm MgSOA 110 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ANM Aromatic Polyamide Advanced Nanofiltration Membrane CONTI EE Spiral Wound Turboclean Shell Active Membrane Area 70 ft 6 4 m Recommended Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 25 GPM 5 6 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU PAO DNCAUO MW ERR RR Pharmaceutical Separations V AN VW TM Element Weight 12 5 4 Length A 38 75 984 Diameter B 3 80 96 Permeate Tube C 0 83 21 2 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Sanitary Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedw
231. 8 965 Diameter B 6 3 160 Permeate Tube C 1 14 28 9 Units in pounds and inches units in paranthesis in kilograms and millimetes Dim A does not include ATD Mechanical Configuration Sanitary Style Core Tube ATD not included with element Feed Spacer 0 065 thick diamond spacer Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Zam 6 3 AUM High Temperature UF Turboclean Element TRIS CORPORATION Model M W C O 6338 N6D4V8 10 000 OPERATIONAL AND DESIGN DATA Membrane Type AUM Advanced Ultrafiltration Membrane Configuration E Spiral Wound Turboclean Shell Active Membrane Area 225 ft 20 9 m Recommended Applied Pressure Not applicable Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 10 0 ppm Maximum Feed Flow 70 GPM 15 8 m3 hr a p Minimum Brine Flow Permeate Flow Ratio 5 1 S Y N Maximum SDI 15 minutes 5 0 APPROV d Maximum T urbuditv 1 NTU leiere Rm Mi
232. 8 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 028 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION A N 8 5 ACM LP Low Pressure RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8540 ACM4 TSFA 17 500 66 0 99 00 98 00 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM LP Fully Aromatic Polyamide Low Pressure Advanced Composite eidele e EE Spiral Wound Fiberglass Outer Wrap Active Membrane Area 440 ft 40 4 m Recommended Applied Pressure 50 300 psi 3 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance
233. 80 TSDA HL4040F Same diameter and permeate tube 4040 X201 TSDA 8040 ACMI TSDA SG8040F 2840 Same diameter and permeate tube 8040 ACM2 TSDA AG8040F 2840 Same diameter and permeate tube 8040 TS80 TSDA HL8040F Same diameter and permeate tube Dow Filmtec Replacement Elements TriSep Model Number Dow Filmtec Comments 4040 ACM1 TSF Same diameter and permeate tube 4040 ACM2 TSF BW30 4040 Same diameter and permeate tube Same diameter and permeate tube Same diameter and permeate tube Same diameter and permeate tube Same diameter and permeate tube Same diameter and permeate tube Same diameter and permeate tube Same diameter and permeate tube Same diameter and permeate tube Same diameter and permeate tube Same diameter and permeate tube Same diameter and permeate tube Comments Same diameter and permeate tube Same diameter and permeate tube Same diameter and permeate tube Comments Same diameter different permeate tube Same diameter different permeate tube Same diameter different permeate tube Same diameter different permeate tube Same diameter different permeate tube TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 2 6 TRIS gt CORPORATION TriSep Model Number 4040 ACM2 TSDA 4040 TS80 TSDA 4040 X201 TSDA 8040 ACM1 TSDA 8040 ACM2 TSDA 8040 TS80 TSDA Competitive Element Replacement Guide Desal DuPont Style Elements Desal Mod
234. 80 XNA5 SB20 Sodium Na 23 9 99 98 85 20 95 Calium Cat 40 99 999 9 98 60 97 Magnesium Mgr 24 99 99 99 97 00 97 Potasium K 39 98 98 98 85 20 95 Ammonium NH4 18 os 98 98 70 10 92 Chloide Cl 35 99 999 98 90 20 95 Bicarbonate HCO3 61 98 98 98 90 J 30 95 Sulfate S04 os 99 99 39 98 55 9 Silicate Sio2 60 99 999 9 86 50 90 L Nimte NO 62 98 7 L 39 99 9 99 99 99 84 10 75 Fluoride F l Nominal Rejection by Membrane Type Constituent Name Specific Ions MW X 20TM ACM ACM LP TS80 XN45 SB20 Sucrose 342 99 9 99 9 99 9 99 96 99 9 Lactose 36 999 999 999 99 95 95 Giwos i180 399 999 995 99 95 Bob T To L T x c TL T s x m L s TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 80 99 805 964 1235 fax e www trisep com 0105 382 TriSep Engineering Manual di TRIS System Design Parameters For TriSep Spiral Wound Elements Maximum Recommended Average Flux Rates GFD Feedwater Source Avergae Flux GFD RO UF Permeate 25 to 30 18 to 22 Shallow Well 15 to 18 surface 12 to 15 Surface river Lake 8 to 14 Was
235. 900 Submerged Ultrafiltration UF Membrane Process Overview SpiraSep is a patented U S Patent No 6 755 970 submerged negative pressure ultrafiltration UF membrane process complete with backwashing and aeration capabilities The process utilizes spiral wound membranes that remove suspended solids turbidity cryptosporidium and oocysts with the 0 03 um ultrafiltration membrane Major Components of a SpiraSep UF system are Membrane elements Membrane tank Permeate pump Backwash pump Blower Membrane aeration system Reject pump Metering pumps Valves Piping Instrumentation eu aae e I O OD O O O D gt o Process Schematic In a SpiraSep UF system an array of membrane manifold assemblies is submerged in a common process tank Each membrane manifold assembly is connected to a main header which is connected to the permeate pump Feed is delivered to the membrane tank submerging the membrane elements A For additional information regarding SpiraSep UF membranes please contact Mike Snodgrass at 1 805 964 8008 ext 113 or send e mail to snodgrass trisep com vacuum is generated by the suction of a self priming centrifugal pump creating the necessary net drive pressure to pull water through the SpiraSep membrane Air is bubbled up through each membrane element via bubble diffusers creating tremendous shear forces on the membrane surface that remove any suspended so
236. 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION um 4 TS80 Nanofiltration Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 TS80 TSF 2 000 7 0 99 00 97 00 Performance is based on the following test conditions 2 000 0 ppm MgSO4 110 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ANM Aromatic Polyamide Advanced Nanofiltration Membrane ele el ie le NP Spiral Wound Fiberglass Outer Wrap Active Membrane Area 85 ft 7 9 m Recommended Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 15 7 Length A 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Unit
237. 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane eidele e EE Spiral Wound Fiberglass Outer Wrap Active Membrane Area 88 ft 8 1 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 15 7 Length A 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Memb
238. Ad JAd JAd JAd ouoj nsAToq AION EL19 E AI OI ouoj nsATod ouoj nsATod E1193 8 AI OI O SL 0 Q qI49c90 TI c 0 Q I49t 80 TI Sc9 0 WO SL 0 dO SL 0 O SL 0 O SL 0 TI SCc9 0 TI Sc9 0 TI S O dT SL0 d1 S20 dT SZ0 oqn 910 Suorsu uutGq Ower QqI4et 80 oqn 910 suoisuouin q TANS UJA ueo ooqun o A3g soruouis dat ysty duio ur oq ueo ooqun 4S UJI domat YstH oqiny ae UA S JUA S S 1tu 14 a Ajs esoq juognqg a Ajs esoq juognqg ejas d SuLy ejas d SuL ejas d SuLy S d SuI uondrnbsoq V 9080I1 L CLLLOI L COLOI L 9IVOI L I LL ZOT LL 1790801 L 9080T L V 9080I1 L C LL000I dds I 110001I d4GS 0ccOT L IccOT L c 9001 L S900I L SUIMBI T Jo 38ed Lxx xxxx Qp0t Fetz Sxx xxxx Qpop I9ZFZ1I VOXX XXXX 0f0t OSCPCII HXx Xxxx Qpop FIPZII 2 xx Xxxx Qp0p Z9ZFZ1I SAXX XXXX 0P0F F60FZ11 2 4pxx xxxx op0t 69ZFZ11 qXx Xxxx opot LSTPZTI qXx xxxx opot 611FZ1I Vqxx xxxx Qpop 9S0tc11 Vqxx xxxx Qopop TSOPTZIT VXX XXXX 0p0t ICOPCEI VXX XXXX 0f0t S00PCLI VXX XXXX 0f0t 6SIFZII VXX XXXX 0p0t 610PCLI S opo A juw quiny 3 18 SLNHIAR TH 0EA ELAIA VIG HONI P SIMS opor K1ejIUegS eso q K1ejIUeS pesoq uondrnbsoq C tvY80I L C O9LOI L SUIMBI T 2 XX XXXX 0p8 69OETII 2 XX XXXX 0p8 66IFZII S 9poJA pwy quinyw 3 18 SLNOHIAUT TM WALA VIG HONI SIIS 0p8t suwy amp urumn sSn
239. Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance sinesine 0 5 ppm nominal 1 0 ppm max Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU ADDIIGG00OI uuuu uuu uu A degen Peptide Demineralization 4 P3 MILL LUI NW MI d d Element Weight 15 7 Length A 38 0 965 Diameter B 3 8 96 Permeate Tube C 0 83 21 2 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Sanitary Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Zn 3 8 TS 80 High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 3840 M
240. Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 4 0 Maximum Turbidity 1 NTU Element Weight 50 23 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 028 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Za 8 5 TS80 Nanofiltration Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8540 TS80 TSFA 10 800 40 0 99 00 97 00 Performan
241. Area Recommended Applied Pressure Maximum Applied Pressure Recommended Operating Temperature Feedwater pH Range Chlorine Tolerance Maximum Feed Flow Minimum Brine Flow Permeate Flow Ratio Maximum SDI 15 minutes Maximum Turbidity SB Cellulose Acetate Blend Spiral Wound Fiberglass Outer Wrap 80 ft 7 4 m 200 500 psi 14 34 bar 600 psi 41 bar 50 90 F 10 32 C 5 5 nominal 4 7 0 5 ppm nominal 1 0 ppm max 20 GPM 4 5 m3 hr 5 1 5 0 1 NTU Element Weight Length A 15 7 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane EEN SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Dmm 4 CA RO Element Series TRIS
242. Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 15 7 Length A 40 0 1 016 Diameter B 2 5 63 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Zs 4 XN45 Nanofiltration Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 XN45 TSF 2 000 7 0 95 00 92 00 Performance is based on the following test conditions 2 000 0 ppm MgSO4 110 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type XN45 Polyamide Advanced Nanofiltration Membrane Configuration Spiral Wound Fiberglass Outer Wrap Active Membrane Area 85 ft 7 9 m
243. CLS SSrOt AISIT ois Tesoq juognd CVE8OI L VQXX XXXX 0p08 C8crcll 10 99UU09194U 089 CC Iv vl JAd AISTI e A4js esoq juognd VesOl L VWOXxX xxxx 0708 c OvclI 1ojoouuooJoju Z 88 OI AION TI cl I IojeAeog BAIS oou 08L0I L VJXS XXXX 0p08 C80 CIT Joj euuooJoQu I Ur CL OAd QI 0ST ToyeMedg o 41S desum 8t80I L VXS XXXX 0p08 SLCVCII 0708 mwg Aurum q 0 UO Or SdV ddd AISTI s desur VXX XXXX 0r08 SOITCII Sn d puq S TC 8I 6 JAd AISI s desur C OSTOI L VXX XXXX 0p08 600vCIT Sn d PHOS JoJoUUOdIOU GF OES 00 I JAd AISI s desur T OSTOI L VXX XXXX 0p08 9CCrCII Joao 0C PIT SL 9 SSTOt OT eps dagit L t StCOI L VXX XXXX 0p08 v8CVCIT Joj euuooJoQu C UI Ur CL JAd AISI S doen 8t80I L VXX XXXX 0 08 CCOVCIT Jojoouuo9Jo1Uu 6L S LV C AION d1 0 T es d SH L I 8 COI L VXX XXXX 0p08 OCOVCII ddI ISO IELIAIEIW qn L 2107 sju urtu0o YI YI I suoisuour q uondrosoq SUIMBIG S 9po A 3uouro q quinyw JAB SLNHIAWTH DX LHIA VIG HONI 8 S9H9S 0708 suwy amp urumnq sSn q S 10 99UU09 19 UT LO TI Z AOU Suid pue SIT SEd TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax e www trisep com 0703 WV v 01I 8007 67 01 LO CI C AoA 3n d puq S6 LI Sn d ptloS 1032ouuoodoju Z 1O o ouuooJ1olu C I JOJIOUUOSIO 6 III suwu OI 1oj2ouuooJ9 u Z 3n d puq ST Oc 1ojoouuo
244. CT SPECIFICATION Lum 4 ACM LP Low Pressure RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 ACM4 TSF 3 350 12 0 99 00 98 00 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM LP Fully Aromatic Polyamide Low Pressure Advanced Composite COMTI GUN AU ON M Spiral Wound Fiberglass Outer Wrap Active Membrane Area 85 ft 7 9 m Recommended Applied Pressure 40 300 psi 3 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 15 7 Length A 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style
245. D m3 day Rejection Rejection 8040 M2C9Q1 9 400 35 0 99 00 98 00 Performance is based on the following test conditions 2 000 00 ppm NaCl 225 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Con tigurationi uu a a aaasasan Spiral Wound High Temperature Turboclean Shell Active Membrane Area 355 ft 32 6 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU PRODI CAMO u DP Lactose Concentration PA gt Element Weight 45 20 Length A 40 00 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0
246. Diameter B 4 0 101 Permeate Tube C 0 62 15 9 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Desal DuPont Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Za 4 ACM RO Element Series TRIS gt CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 ACM2 TSF 2 400 9 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane COMM QUIN GIOI L ste uqu La cet T Spiral Wound Fiberglass Outer Wrap Active Membrane Area 85 ft 7 9 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range
247. ERATIONAL AND DESIGN DATA Membrane Type ACM LP Fully Aromatic Polyamide Low Pressure Advanced Composite COMTI GUN AU ON M Spiral Wound Fiberglass Outer Wrap Active Membrane Area 400 ft 37 2 m Recommended Applied Pressure 50 300 psi 3 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 4 0 Maximum Turbidity 1 NTU Element Weight 50 23 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 028 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane y SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Pho
248. Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU jojo e Tel ae ee eee eee ee Sugar Concentration d WWW III d LL TRATAR LE Li A AM l d WAI M N d Z a F Element Weight 15 7 Length A 38 965 Diameter B 3 8 96 Permeate Tube C 0 83 21 2 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Sanitary Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane EE SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Ns 3 8 XN45 High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 3838 N2P1U9 1 300 4 0 95 00 92 00 Performance is based on the following test conditions 2 000 00 ppm MgSOA 110 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type
249. Feedwater pH Range Chlorine Tolerance Maximum Feed Flow Minimum Brine Flow Permeate Flow Ratio Maximum SDI 15 minutes Maximum Turbidity Application AUM Advanced Ultrafiltration Membrane Spiral Wound Turboclean Shell 78 ft 7 2 m 5 200 psi 0 3 14 bar 600 psi 41 bar 35 113 F 2 45 C 2 11 continuous 10 0 ppm 20 GPM 4 5 m3 hr 5 1 5 0 1 NTU RO Pretreatment Element Weight Length A 12 5 4 40 00 1 016 Diameter B 4 00 101 Permeate Tube C 0 62 15 9 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Feed Spacer 0 031 thick diamond spacer Desal DuPont Style Core Tube Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane H ONi SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Za 8 ACM RO High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average
250. Flow Ratio 5 1 Maximum SDI 15 minutes 4 0 Maximum Turbidity 1 NTU Element Weight 50 23 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 028 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Za 8 ACM LP Low Pressure RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 ACM4 TSFA 14 600 55 0 99 00 98 00 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM LP Fully Aromatic Polyamide Low Pressure Advanced Composite ele Lett GIOI uu uuu u carte eb T m Spiral Wound Fiberglass Outer Wrap Active Membrane Area 365 ft 33 5 m Recommended Applied Pressur
251. Flow Ratio 5 1 Maximum SDI 15 minutes Maximum Turbidity Applicators A Element Weight 50 23 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 028 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Zam 8 ACM RO High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 M5P4T9 11 500 43 0 98 50 97 50 Performance is based on the following test conditions 2 000 00 ppm NaCl 150 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM LP Fully Aromatic Polyamide Low Pressure Advanced Composite Configuration Spiral Wound High Temperature Turboclean Shell Active Membrane Area
252. Germany Delivery for most orders 1s 1 2 days after receipt of order MSDS SHEETS For the most up to date information on MSDS sheets please contact our web site at www trisep com 311 TRIS CORPORATION TRIPOL 7510 SCALE INHIBITOR DISPERSANT e Superior control of phosphate and carbonate scales e Iron and silica dispersant capa bility PROBLEM In many installations worldwide higher permeate recoveries from reverse osmosis RO systems are often limited by the potential for carbonate and phosphate scales This is especially problematic for wastewaters with high amounts of iron or metal hydroxides which can form insoluble polymeric gels with conventional acrylic acid scale inhibitors In many applications the tendency for carbonate or phosphate scale formation has the effect of low ering the system recovery that could adversely effect the system economics SOLUTION TriPol 7510 protects and enhances the operation of RO and NF systems by controlling mineral scale formation due to carbonate sulfate and phosphate compounds In most water types proper use of TriPol 7510 can significantly increase allowable system recoveries and thus expand the suitability for use In a wider range of applications TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 TriSep Corporation Chemical Manual APPLICATION TriPol 7510 is metered into the
253. Hovering the mouse pointer over any of the toolbar icons will display a brief description of what that button does i e New for creating a new analysis file The upper right hand corner of each screen has the standard windows icons for minimizing maximizing and exiting each particular program screen If you have any comments or suggestions or bugs that you have identified please send your comments by e mail to info trisep com To move from one data field to the next use the tab key and not the enter key Menu Selection Menu selections may be made by left clicking the mouse button when the mouse pointer is over the particular menu selection or by depressing the Alt key while typing in the underlined letter of the selection you want to make Le Alt F would drop down the file menu Hovering the mouse pointer over any of the toolbar icons will display a brief description of what that button does i e New for creating a new analysis file Main Menu Notice the blue bar along the top of the screen This is the title bar and gives the name of the screen that you are in In the main screen this bar says TriSep Reverse Osmosis Implementation TROI v 2 0 0 The v 2 0 0 indicates the revision level of the program you are using You can check our web site to make sure that you have the most current version of the software at trisep com download htm The main menu has four selections available File Calculations Units and He
254. I A Tee LULL 1 nl li l LIN L LALLLL 1 TY M Wu W l III d u A k d NAAAAN M d d Element Weight 12 5 4 Length A 38 0 965 Diameter B 3 8 96 Permeate Tube C 0 83 21 2 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Sanitary Style Core Tube Feed Spacer 0 047 thick parallel spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane H ONi SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Z 3 8 XN45 High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 3838 N2J4U8 1 700 6 0 95 00 92 00 Performance is based on the following test conditions 2 000 0 ppm MgSOA 110 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type XN45 Polyamide Advanced Nanofiltration Membrane Oe TN e E Spiral Wound Turboclean Shell Active Membrane Area 68 ft 6 2 m Recommended Applied Pressure 40 200 psi 3 14 bar Maximum
255. IO IZ 0 ueo ooqung o AS PIO LC 0 LO LA ueo ooqun pj MON 17 0 LO L4 ueo ooqun p dur 1 u81H MON Z 0 eqn 2102 d Sul Ic 0 omjeoduro uSIH 98 S oqn 210 d Su 98 69 IVd sJu ourturo Ia 8c Ul Dis eos Hr 9 LO O 06 Dis eos LO O LO O 00 LO O LO O LO O LO O LO 0 0S c US C Dis eos Fi n A A A FAA FAA HA FH IV E1193 A eos dda dda dda I ELI9J EJAI BIS dda dda dda dda d dda Uda dda dda Uda E1193 AI eos p JO p Sed eqn T 2urg O IV 9T0S CI uondrnbsoq SPpoy USWA Joquinw LE s IquimmN IPPON ITV WA IESS VJIXX XXXX 0vp68 PEIVCII Suq O DTI VXX XXXX OPC8 LOOVCII eos sung VXX XXXX 0v68 COOECIT od BIS SPpow juw 1oquinyw Jed SILNQHIALT TH WALAW VIG HONI S 8 SIMOS ts Sumq O DTI XXX XXXX 78 890 c1I SUY O OI HXX Xxxx 07 8 6LO CII SUIY O OTI VOXX XXXX 0p 8 6 0 c1I Sutj O OT OXX XXXX 0pt8 6L0 cII suly O OT SXX XXXX 0v 8 6LOETII SUIJ O OTI Suaxx xxxx 0r 8 PIDETIT SUIY O OIT 534Xx XXxx 0pc8 v90 c1I SO OIT VXX XXXX 0pt8 LOOPTIT Peg SUI HXX XXXX 0vt 8 ZOOETII eos SUG WXX XXXX QPE8 ZOOETIT od BIS S opoJy juw AOqUINNY Jed SILNQHIALT TAH WALAW VIG HONI 8 SIMOS tr SSUIY C O I pue s eos vung LO cI c APA SUNIA pue ISTI SUE 428 TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax e www trisep com 0703
256. ION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 ACM2 TWF 2 900 9 0 99 50 98 50 Performance is based on the following test conditions 2 000 00 ppm NaCl 225 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane CONTIG UL ANON E Spiral Wound Fiberglass Outer Wrap Active Membrane Area 90 ft 8 4 m Recommended Applied Pressure 40 300 psi 3 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 15 7 Length A 40 00 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applica
257. IS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 X201 TSF 2 400 9 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane Configuration Spiral Wound Fiberglass Outer Wrap with FoulGuard Technology Active Membrane Area 85 ft 7 9 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 2NTU Element Weight 15 7 Length A 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core T
258. Ib plastic containers Pricing is F O B our factory in Goleta CA Salem VA or Duisberg Germany Delivery for most orders 1s 1 2 days after receipt of order MSDS SHEETS For the most up to date information on MSDS sheets please contact our web site at www trisep com 321 emm TriSep Corporation Chemical Manual TRIS gt CORPORATION TRICLEAN 212TFNE APPLICATION HIGH PH POWDER TriClean 212TFNE should be mixed in a cleaning tank equipped with a mechanical mixer heater low CLEANER pressure recirculation pump and cartridge or bag filter This cleaner works best when applied at a e Used to remove biological flow rate of 8 10 gpm per 4 pressure tube or b 30 40 gpm per 8 pressure tube at a pressure of organic and colloidal fouling between 20 50 psi at a pH of 11 5 For silica on Polyamide Composite mem useata pH of 12 Use caution as pH s above 12 brane may damage membrane Add 2 Ibs of TriClean I 212TFNE per 15 gallons of RO permeate or DI e Does not contain EDTA water Recirculate solution for 1 hour checking pH regularly Use sulfuric acid to lower pH and add PROBLEM additional TriClean 212TFNE or sodium hydrox In many installations worldwide polyamide com ide to increase pH Shutdown pump and allow posite RO and NF membranes can become fouled to soak for 1 hour After soak recirculate for an with biological organic and colloidal foulants additional 20 minutes and then rinse This solution These foul
259. Id pue ISTI sj eq Tea Jo uuoo JOOIIP L st 206 eurpopo y JO p oSeq sonneueJpAH SCCOI L VXX XXXX 0p68 C8tVCII sonneueJpAH 8IIOI L VXX XXXX 0p68 vIOVCIT J91nj3egnue A oqn INSS d SumeIq SPPON pow 1oqumN med SLNAWATA WALAN VIG HONI Sg SIMS reg won I vStII L DXxXx Xxxx oee8 ELEPTII soruouisQ 9141S PIO CCLOI L Sxx xxxx 0F 9 ZLIPZII SOTUOUIS ISCOI L VXX XXXX 0vt 8 9vOvCII J9 11n39 egnut Al oqn inss id 4 SUIMBIG SI9DO A Juour 4 1oqumnN ye SINN IA WaLANVIG HONI 8 S H9S OVES 421 TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax e www trisep com 0703 WV vS 0TI 8007 67 01 JOJIOUUOIIOT 8Q 6 IOJIOUUODIOIUT 9Z Jojo ouuooJz olu Z ETS Jojo ouuoo1z olu 6 09 Jojo ouuooJz olu 6 9 Joj2ouuooJo9jU 9 0 Jojo ouuoozolu CS LIS juouro q Am 86 p Joj12ouuooJojUu q 6 Sn d puq LL 8I IOJIOUUODIOUT CC CIS Sn d ptloS Jolo ouuoor lu 77 STF snid puq t6 vI IOJIOUUOIIOIUT Op EZS JOJIOUUOIIOU 90 IDI sju oururop OI J0j59UUO C T PHOS GLV 99 61 1oljo ouuooJolu T LV OO elt Id sju oururo 3 OI LO cI c APN OCT 00 cI GER SL ST SL ST ILC LVL SESCH OCT 00 8 Ics SL Ol Lt9 00 0I c0 c 18509 OI St 8 8t 8 18509 xs A A A FAA FAFA FAFA oo on on on on on JAd AION JAd ouoj nsAToq ouoj nsAToq AION ouoJj ns od JAd AION J
260. Individual element s permeate flow may vary 15 Engineered Membrane End nF I Y i SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION NN 8 X 20 RO High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 N1A2W1 7 100 26 0 99 00 98 00 Performance is based on the following test conditions 2 000 00 ppm NaCl 225 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane Configuration Spiral Wound High Temperature Turboclean Shell Active Membrane Area 270 ft 24 8 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 1000 psi 69 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 95 GPM 22 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes
261. LEM In most water treatment plants worldwide RO NF and UF membranes can become fouled with biological and organic foulants These plants must be cleaned to maintain membrane performance SOLUTION TriClean 510 is a liquid cleaner used to remove organic foulants without damaging sensitive poly amide composite membrane elements APPLICATION TriClean 510 should be mixed mn a cleaning tank equipped with a mechanical mixer low pressure recirculation pump and cartridge or bag filter This cleaner works best when applied at a flow rate of 8 10 gpm per 4 pressure tube or 30 40 gpm per 8 pressure tube at a pressure of between 20 50 psi at a pH of 6 8 Caution pH s above 12 may damage membrane Add 1 0 gallons of TriClean 510 per 50 gallons of RO permeate or DI water Recirculate solution for 1 hour Shutdown pump and allow to soak for 1 hour After soak recirculate for an additional 20 minutes and then rinse PACKAGING TriClean 510 is shipped as a liquid in 5 gallon plastic pails or 55 gallon plastic drums Pricing is F O B our factory in Goleta CA Salem VA or Duisberg Germany Delivery for most orders is 1 2 days after receipt of order MSDS SHEETS For the most up to date information on MSDS sheets please contact our web site at www trisep com TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 329 emm TriSep Corporation Chemica
262. LLETIN ACM 01 Reverse Osmosis Petrochemical Complex Argentina 8040 ACM1 TSA Spiral Wound Element ACM Membrane TriPol 9000 Advanced Scale Inhibitor Solution Brackish well water with the following average constituancy Total Hardness 38 mg L as caco Sodium na 250 mg L Carbonate co 8 6 mg L as caco Bicarbonate uco 170 mg L as caco Sulfate so 79 7 mg L Chloride CI 228 mg L Nitrate No 22 3 mg L Silica sio 36 mg L Conductivity 1600 uS cm Temperature 60 C wei 35 C membrane feed pH 8 4 Pretreatment consists of cooling towers followed by media filtration 5 0 micron cartridge filters nominal and chemical dosage of TriPol 9000 Scale Inhibitor The reverse osmosis plant is designed as a 2 stage product staging system operating at 80 overall recovery with 2nd stage brine recycle to 1st stage feed producing 12 m h 76 032 gpd of permeate for high purity requirements Array design consists of a 1st stage of 3 tubes in a 2 1 configuration The 2nd stage consists of 2 tubes in a 1 1 configuration Each tube housing seven TriSep 8040 ACM1 TSA spiral wound RO elements Product Flow tst stage 2nd stage 3 960 GPH 5 mi 3 168 GPH 12 mn Concentrate Recycle 2nd stage 792 GPH 3 mim Overall Recovery 80 Feed Pressure st stage 2nd stage 156 psi 188 psi Delta P Pressure ist stage 2nd stage 46 psi 55 psi Product Conductivity 1st stage 2nd stage 20 uS cm 0 7 uS cm System Silica
263. Length A 38 00 965 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Dim A does not include ATD Mechanical Configuration Filmtec Style Core Tube ATD not included with element Feed Spacer 0 047 thick parallel spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION LA NI 8 AUM Ultrafiltration Turboclean Element Series TRIS gt CORPORATION Model M W C O 8038 N6DAV7 10 000 OPERATIONAL AND DESIGN DATA Membrane Type AUM Advanced Ultrafiltration Membrane CGopnfguraton a k Spiral Wound High Temperature Turboclean Shell Active Membrane Area 225 ft 20 9 m Recommended Applied Pressure Not applicable Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 10 0 ppm Maximum Feed Flow 100 GPM 22 7 m3 hr 3 y M M
264. M RO Element Series TRIS gt CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 ACM2 TSAN 9 700 36 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Configuration Spiral Wound Fiberglass Outer Wrap Active Membrane Area 365 ft 33 5 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamo
265. MAIN edit screen From this screen you have six buttons on the toolbar The first is to exit the program the second is to cancel an input the third is to save changes the fourth is to add a new custom element the fifth is to delete a custom element and the sixth is to copy a standard element to a custom element On the left hand side of the screen are two list of elements sorted by element diameter If there is a to the left of the diam eter this indicates that the list can be expanded and that there are additional elements to view As a default there are no custom elements but only the TriSep standard elements To view the properties of an element lets look at the 8040 X201 TSA element Left click on the next to the 7 9 on the TriSep elements This will expand the list and show you all the TriSep standard elements Click on the 8040 X201 TSA model and the fields to the right will be populated Now you should see four pages of data for each element TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 404 TriSep Troi Design Program A Manual ver 2 0 0 TRIS CORPORATION Explanation of the Fields The data on page one on the right hand side outlined in a box are used in the element calculations In addition the spec rejection and spec flow at the bottom of the page are used in the calculations The rest of the data is used in th
266. NF systems by controlling mineral scale formation due to carbonate sulfate and fluoride compounds In most water types proper use of TriPol 8010 can significantly increase allowable system recoveries and thus expand the suitability for use In a wider range of applications TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax e www trisep com 9 00 APPLICATION TriPol 8010 is metered into the feed water at a point where turbulent flow will ensure adequate chemical mixing prior to entering the RO or NF system This is usually done prior to the cartridge filters and high pressure pump Dosing rates vary depending on feedwater quality and recovery but normally run between 2 and 5 ppm For exact dosing use the latest version of TroiWin TriPol 8010 should not be used if there is more than 0 1 ppm of iron or other metal hydroxides in the feedwater Since this product is anionic In nature care should be taken when using cationic polyelec trolytes in the pretreatment system PERFORMANCE Max Langlier Saturation Index 1 0 Max CaSO4 Saturation 150 Max SrSO4 Saturation 200 Max BaSO4 Saturation 200 Max CaF Saturation 2 000 Silica 100 in the concentrate PACKAGING TriPol 8010 is shipped as a liquid in 2 gallon sample sizes 5 gallon 40 Ib plastic pails and 55 500 Ib gallon plastic drums Pricing is F O B our factory in Goleta CA Salem VA or Duisberg
267. NSPECTION OF SUB ASSEMBLIES Each roll of membrane is sampled and tested under the same test conditions used for the finished membrane element In addition a visual inspection of the membrane is done by the casting machine operators during the preparation of the membrane leaf assembly Membrane testing is done in a test loop designed to duplicate element operation Feed water concentration is controlled as are feed flow operating pressure and temperature Salt passage and product flows are measured to determine membrane performance Inspection of the membrane leaf sub assembly includes a random check of material length including brine channel Spacer proper spacing and fold position Inspection of the product channel pack sub assembly includes a random check of material lengths per TriSep specifications and inspection of the product channel pack for leaf count weld integrity and spacing 3 FINAL WET TESTING AND INSPECTION The element integrity test is performed on every element prior to final acceptance The data collected at this point is correlated with original membrane data and calculations are made to verify uniformity and efficiency Final element inspection includes a tolerance check to determine that the attached brine seal carriers are within the specified range This test is followed by a cleaning and a visual check The elements are then packaged for inventory Inventory control includes periodic random sampling of the elemen
268. Not applicable Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 10 0 ppm Maximum Feed Flow 70 GPM 15 8 m3 hr sD y M Minimum Brine Flow Permeate Flow Ratio 5 1 v s V 0 Maximum SDI 15 minutes 5 0 APPROV d Maximum T urbuditv 1 NTU Application Milk Fractionation Element Weight 30 14 Length A 38 00 965 Diameter B 6 4 162 Permeate Tube C 1 14 29 0 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Sanitary Style Core Tube Feed Spacer 0 031 thick diamond spacer Engineered Membrane uw Fr SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION LA NI 6 4 PE High Temperature UF Turboclean Element TRIS gt CORPORATION Model M W C O 6438 N9D4V9 10 000 OPERATIONAL AND DESIGN DATA Membrane Type PerSep Advanced Ultrafiltration Membrane CGopnfguraton a k Spiral Wound High Temperature Turboclean Shell Active Membrane Area
269. OEMd 29 Luul d moq VS L NOV 0r08 CETA ORK TAGOW d3SIler L INANAIV 1d321 SOLIDS oueJquie J J9 eM YUSIYOeIG AGINS LNAWSAQV 1d3s AAILILAdNOD 349 TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com e 0105 s ys uomneoiioeds JONpOJd pue si u uui uinb i uo uuoo 10J 921AJ9S JAWOISND UOIeJIOGIOD d s joe UOyD seiquiesse 9 e d pue Hulsnoy o HuljosuUOd 104 sJo1depe pue jonpoud pieoqui uinb i Aew sjapow zu w asejd uoljpiodioo degu 91oN OvOV A IX LML SINDV 0707 d If1 OvOv OvOV d 1 OVOV dHOEML LSL VINDV 0707 L d1N0csvr ALOVOVUV VdSa3 LHN OvOV OvrOT 3 IOEML Vd dH SL Y 310v0vOS LS 1 ZWOV 0v0F d 19c8r Vd JH SLt JIOVOTPOV CVdO LH T 0vYOY OVOV 0O ML T3GOM d3Sld Aeio SWI91SA in S3IUOUIS s23nneueJp 99 WII MO SOLIDS ueiquu lN deJM ede AGINS LNAWSAOV 1d3s AAILILAdINNOD CORPORATION 350 TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 s us uorneoiieds jonpoud pue sl u uu uinb i uo 5 uuoo 104 BDIAIOS JOWO SNYD UOl eJOdIOD desu 19610025 seiquiuesse eje d pue Buisnou oj Bunoc uuoo 104 SJOJdepe pue onpoid pieoqui asinbses Aew sjapow ju ui oe d i uoneJodJo2 degu 91oN 028 ns vJOze ns lec Am LOMS ASH 0v09 ge 00t 0zgl L VOMS 007 31 YHOEMS OLE OZ8WL AH cc8c 40v089S OMS OZE MHOEMS 0 H0OZ8WL SS ZZ8Z 40v0sav ZOM
270. OPERATIONAL AND DESIGN DATA Membrane Type ACM LP Fully Aromatic Polyamide Low Pressure Advanced Composite Cong AMON uuu aa E oa akana URS Spiral Wound Fiberglass Outer Wrap Active Membrane Area 88 ft 8 2 m Recommended Applied Pressure 40 300 psi 3 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 15 7 Length A 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 80
271. Osmo replacement 4 dia by 40 long 0 75 O D male perm tube protruding permeate tube high area 8 diameter by 40 long 1 50 I D female permeate tube flush cut Same as 8040 ACM2 TSA but NSF approved 8 dia by 40 long 1 19 I D female permeate tube flush cut Desal replacement 8 dia by 40 long 1 12 I D female permeate tube flush cut Filmtec replacement 8 diameter by 40 long 1 50 I D female permeate tube flush cut 400 ft Same as 8040 ACM2 UWA but NSF approved 8 dia by 40 long 1 12 I D female perm tube flush cut 400 ft Filmtec replacement 8 3 diameter by 40 long Osmo style 1 14 I D permeate tube and diameter 8 5 diameter by 40 long 1 12 female permeate tube flush cut TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 173 PRODUCT SPECIFICATION c 2 5 ACM RO Element Series TRI gt CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 2540 ACM2 TSF 650 2 0 99 00 98 00 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Configuration Spiral Wound Fiberglass Outer Wrap Active M
272. PERATIONAL AND DESIGN DATA Membrane Type ANM Aromatic Polyamide Advanced Nanofiltration Membrane COMTI GUN AU ON M Spiral Wound Fiberglass Outer Wrap Active Membrane Area 85 ft 7 9 m Recommended Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 15 7 Length A 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane y SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805
273. PROBLEM In many installations worldwide higher permeate recoveries from reverse osmosis RO systems are often limited by the potential for silica scales This is especially problematic for well waters in certain geographic locations that have high levels of silica In many applications the tendency for silica scale formation has the effect of lowering the system recovery that could adversely effect the system economics SOLUTION TriPol 9510 protects and enhances the operation of RO and NF systems by controlling mineral scale formation due to silica carbonate sulfate and flu oride compounds In most water types proper use of TriPol 9510 can significantly increase allowable system recoveries and thus expand the suitability for use in a wider range of applications TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 APPLICATION TriPol 9510 is metered into the feed water at a point where turbulent flow will ensure adequate chemical mixing prior to entering the RO or NF system This is usually done prior to the cartridge filters and high pressure pump Dosing rates vary depending on feedwater quality and recovery but normally run between 2 and 5 ppm For exact dosing use the latest version of TroiWin Since this product is anionic in nature care should be taken when using cationic polyelectrolytes in the pretreatment system PERFORMANCE Max Langlie
274. PRODUCT SPECIFICATION Dmm 4 ACM RO Element Series TRIS gt CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 ACM3 TWF 2 800 10 0 99 20 98 50 Performance is based on the following test conditions 2 000 00 ppm NaCl 225 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Configuration Spiral Wound Fiberglass Outer Wrap Active Membrane Area 90 ft 8 4 m Recommended Applied Pressure 40 300 psi 3 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbiditly 1 NTU Element Weight 15 7 Length A 40 00 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mecha
275. Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane deele D ON MI m denne Spiral Wound Fiberglass Outer Wrap with FoulGuard Technology Active Membrane Area 365 ft 33 5 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 2NTU Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow
276. Permeate End Cap Brine Seals Brine Seals Plug Thrust Collar End Cap Membrane Element Adaptor TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 378 TriSep Engineering Manual TRIS gt CORPORATION QUALITY CONTROL PROCEDURE FOR THE MANUFACTURE OF TRISEP ELEMENTS In order to assure consistent product quality TriSep maintains a stringent Quality Control Program which insures the highest quality finished product This Quality Control Program encompasses all aspects of manufacturing starting with inspection of raw materials through monitoring process parameters culminating in complete testing of 100 of the finished product While there are many points of inspection four general areas are described below 1 Raw materials inspection 2 Inspection of sub assemblies 3 Final wet testing and inspection 4 Operation parameters 1 RAW MATERIALS INSPECTION TriSep maintains a Quality Control Department which inspects molded and machined parts per drawings and material receiving specifications These parts include the permeate tubes the molded plastic brine seal carriers interconnectors and the brine seals and O rings Our Quality Control Department is responsible for maintaining the standards on all incoming raw material All of our procedures and standards are designed to produce 100 compliance with our specifications Every core tube is
277. Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Zum 8 XN45 NF High Temperature Turboclean Element Ehl ele LIESER BE G F PFP G E A T N Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8038 N2D1U9 7 100 26 0 95 00 92 00 Performance is based on the following test conditions 2 000 00 ppm MgSO4 110 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type XN45 Polyamide Advanced Nanofiltration Membrane el ele Spiral Wound High Temperature Turboclean Shell Active Membrane Area 270 ft 24 8 m Recommended Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 5 ppm nominal 1 0 ppm max Maximum Feed Flow 95 GPM 22 m3 hr i M Minimum Brine Flow Permeate Flow Ratio Bi y 5 9 x Maximum SDI 15 minutes 5 0 App Maximum Turbidity 2 NTU Application Lactose Demineralization i Element Weight 40 18
278. Recommended Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 5 ppm nominal 1 0 ppm max Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 15 7 Length A 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Za 8 XN45 Nanofiltration Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 XN45 TSA 9 500 35
279. S 08 HHO MS 0Lg ns OL 8IA L JH OC LOMSNVSH 0rOTr 43 40v0vOS OVOV COMS JSS SIWOV 0t0t OLSIA L SS 028I 33 JOvOvaV OvOT LOMS OvOv HHOEMS 73QOWN d3SldL suiejs S pin 43 HOM SIIUOWSOC 49 sonneueJp H 28 Uul I4 MOG AN3IHNS3OV Id34H Salag oueJquio yJ 19jeMeeg 00t XZzc99 VSS S8IN2V 0r08 H0Zz ns S9S HXZZ98 J0r083S DA 0P08 0 MS JJOvOP3S 4ISS GINDV 0r0r YOLZ NS GK 40r0ras OPOt PVdO 0P0t 0 MS 1T3GON dell suiajs gs pinid H2OM SOIUOWSO 39 sonneueJp H 2e Luul 3 Mog LN3AA32 V 1d3 S9IJ9S oueJquioe N J93eM Uusry4oeJg uornoefey uBiH AGINS LNalNa3oV 1d3s 3AILIL3dINOD CORPORATION 351 TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com e 0105 s us uol olJi5 ds jonpoud pue s u uu uinb i uo 5 uuoo 104 BDIAIOS JOWO SNYD uoneJodJo2 desu 1961002 saljquasse e d pue Buisnou oj Buroeuuoo 104 sio depe pue onpoid pieoqui ssinbes Aew sjapow jueujoeoe doJ UOI eEJOdIOD degu 91oN 068S SE JN VO 8 00 3S 00c9 OS 00cv OS 00c OS LOZY 9S HL cn XL0c9 OS YH ccc8 YH SL8 4A0v08d9 CEVO ASW OV08 068S 40099 JN V V 001Z 0S SO9LY WS LLE L elt OO pum LOlZ OS asLzev 400390 Or0r LaVvo VS1 0S8S 0t0P OOLI OS 00Lv OS LOLV OS YHOIL P Cavo VSIN 0vOY L0L97 2S HdHLiccv YH LLV JOrorao OvrOv cavo leseg T3GON d3Sl4L KeJo suiejs S DI HOO soOiuouuso 35 39 sonneueJp H 2e ui I4 MOG ININFDV day S
280. S OF PACKAGED TRISEP ELEMENTS CONTAINER DIMENSIONS INCHES MM Gross Type of Element Size Quantity Width Weight lb kg Packaging Height Length 2 5 x 40 1 4 5 114 45 1143 4 5 114 7 3 Box 4 9 5 240 46 1168 9 5 240 28 12 Box 4 x 40 1 4 5 114 45 1143 4 5 114 14 6 Box 4 9 5 240 46 1168 9 5 240 56 25 Box 24 19 483 48 1220 40 1016 375 170 Pallet 64 40 1016 48 1220 40 1016 935 424 Pallet 8 x 40 1 9 229 5 1143 9 229 45 20 Box 4 15 381 8 1220 40 1016 220 100 Pallet 24 610 48 1220 40 1016 400 181 Pallet 12 33 838 8 1220 40 1016 580 263 Pallet 16 40 1016 8 1220 40 1016 750 340 Pallet Beware of hand pinch points between elements and other objects when moving elements Beware of sharp edges and rough surfaces when moving elements Do not stack unpackaged elements directly upon each other TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax e www trisep com 0703 393 TriSep Software RER CORPORATION The following pages contain manuals for TriSep s two software programs Troi version 2 0 and Tron version 1 1 Troi is used to design RO and NF systems It requires that you input a water analysis permeate flow rate and system design infomration It will then give you a prediction of the required pressures flow rates and permeate concentrations of the plant Tron is a normal
281. Sep 900 pilot unit consisting of a lime reactor and submerged UF system was operated on a municipal water supply to determine the feasibility of the process With an influent alkalinity concentration and pH of 76 mg l and 7 3 respectively the pilot unit was operated at various pH levels to optimize the performance The UF system maintained a flux rate of 30 gfd 52 Imh and an effluent turbidity 0 050 NTU A total organic carbon TOC reduction rate of 13 was also observed through the duration of the pilot The alkalinity reduction results are Influent Effluent pH 1 9 9 18 Alkalinity mg l 76 0 26 8 Triseo Corporation RS TRI gt A Crystal Clear Solufion VEM JL CORPORATION Boiler Feed Make up System Utilizes Submerged Ultrafiltration System as Pre treatment Case Study Canada The Challenge The Results A natural gas plant in Western Canada is Feedwater is delivered to two SpiraSep UF needed to install a reverse osmosis RO trains as the gas plant required 10096 system to provide boiler feed make up redundancy with the UF membranes to water Since the raw water source is a ensure there would never be any water nearby river an advanced pre treatment shortages Effluent from the SpiraSep technology was needed to provide high membranes which consistently has an SDI quality water for the RO system less than 2 0 and turbidity less than 0 1 Conventional RO pre treatment NTU is delivered directly to the RO sy
282. Sep to be invalid the Customer shall pay to TriSep a minimum fee of 450 per day plus all direct expenses incurred by TriSep employee s conducting such inspection testing The RGA Procedure is part of TriSep s RGA Return Goods Authorization procedure NO OTHER WARRANTIES EXPRESS OR IMPLIED ARE MADE IN CONNECTION WITH THE SALE OF THESE PRODUCTS INCLUDING NO WARRANTIES OF FITNESS FOR ANY PARTICULAR USE OR MERCHANTABILITY OF THESE PRODUCTS THE REMEDY HEREBY PROVIDED SHALL BE THE EXCLUSIVE AND SOLE REMEDY OF CUSTOMER AND IN NO EVENT SHALL TRISEP BE LIABLE FOR SPECIAL INDIRECT OR CONSEQUENTIAL DAMAGES WHETHER OR NOT CAUSED BY OR RESULTING FROM TRISEP S NEGLIGENCE TriSep Corporation 93 S La Patera Lane Goleta CA 93117 805 954 8003 phone 805 964 1235 fax www trisep com TRIS 2 CPAP RA TER GUIDELINES FOR OPERATION TriSep provides all data in good faith and believes the information and data contained herein to be accurate and useful It is the user s responsibility to determine the approp riateness of TriSep s products for the user s specific end uses x 20 ACM TS80 CA XNA5 UE10 UESO IM AND TM10 RO NF UF MF Membrane Guidelines SUSPENDED SOLIDS e Turbidity of element RO feed must be 1 0 for all elements measured upstream of the micron filters preferably 0 1 Operation at turbidities higher than 1 0 may require more frequent membrane cleanings and may reduce membrane l
283. Style Core Tube Feed Spacer 0 028 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane EE SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION oO N 8 X 20 Low Fouling RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8340 X201 TSOA 11 000 41 0 99 00 98 00 Performance is based on the following test conditions 2 000 00 ppm NaCl 225 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane Configuration Spiral Wound Fiberglass Outer Wrap Active Membrane Area 415 ft 38 1 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed F
284. TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Loe 8 ACM RO Element Series TRIS gt CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 ACM3 UWAN 12 000 45 0 99 20 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Configuration Spiral Wound Fiberglass Outer Wrap Active Membrane Area 400 ft 37 2 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 4 0 Maximum Turbidity 1 NTU Element Weight 50 23 Length A 40
285. Troi in the database ini file TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 405 TriSep Troi Design Program Lo Manual ver 2 0 0 TRIS CORPORATION A UNC path is preferred and the syntax of that would be servername foldername For example if the name of the server is MyServer and the folder name is DataTroi Then the path would be MyServer DataTro1 To start the TroiWin software once it 1s installed Click on Start Programs Troi For Windows Version 2 0 0 You can also place a copy on your desktop by right clicking your mouse in the desktop area and then click on New and then click on Shortcut and a pop up window will appear You can type in the above listed folder location or click on Browse and find the above listed folder then select the file TROLexe Click on the Next button and then you can input a name for the shortcut Click on Finish and you should have a shortcut on your desktop 8 DISCLAIMER We at TriSep have put a lot of time and energy into making TROIWIN a user friendly program for our customers that is as accurate as possible The output from this program should not be used for warranty purposes and is accurate to 10 TriSep Corporation assumes no liability for any errors or costs that may result from the use of this program TROIWIN has been extensively tested by our in house engineers and we feel that most of the bugs
286. Turboclean Shell Active Membrane Area 355 ft 32 6 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU ApplicatO m me ee RO Permeate Polishing E Ww GE 1 M e Uh 1 x T Element Weight 45 20 Length A 40 00 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane ni SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Zl 8 X
287. Wound High Temperature Turboclean Shell Active Membrane Area 80 ft 7 4 m Recommended Applied Pressure 100 200 psi 7 14 bar Maximum Applied Pressure 200 psi 14 bar at 70 C Recommended Operating Temperature 35 160 F 2 70 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Application Pharmaceutical Makeup Water Element Weight 15 7 Length A 40 00 1 016 Diameter B 4 0 101 Permeate Tube C 0 62 15 9 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Desal DuPont Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane EE SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Zum 8 ACM RO Turboclean E
288. a 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com UE Ultrafiltration Membranes 7 NN 100 000 MWCO TRIS SP CORPORATION TriSep offers two conventional ultrafiltration UF membrane elements the UE10 and the UESO Both of these membranes are made from a polysulfone chemistry that offers high specific flux uniform pore sizes and excellent chemical resistance The UE10 have a molecular weight cut off MWCO of 10 000 while the UE50 has a MWCO of 100 000 UF membranes do not reject any dissolved salts such as hardness alkalinity sodium chloride or sulphate They do reject large organic molecules and are typically characterized by the molecular weight of a group of organic molecules where a minimum of 90 rejection 1s achieved Rejection of organic molecules varies depending on the geometry of the molecule and the size and distribution of the membranes pore size TriSep characterizes the UE10 using a combination of proteins Cytochrome C and dextran molecules of varying molecular weight The UESO is tested on varying molecular weight dextran molecules The UE10 has a clean water specific flux of aroung 1 3 gfd psi 32 Imh bar while the UE50 has a specific flux of around 1 7 gfd psi 42 Imh bar The UE10 is typically used for applications where rejection of proteins is required such as for whey protein concentration in the dairy industry The UE50 is used where removal of suspended solids are require
289. acer 0 065 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane ee ee SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION A 8 XN45 NF High Temperature Turboclean Element TRI CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 N2P4W1 7 100 26 0 95 00 92 00 Performance is based on the following test conditions 2 000 00 ppm MgSOA 110 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type XN45 Polyamide Advanced Nanofiltration Membrane eidele e EE Spiral Wound High Temperature Turboclean Shell Active Membrane Area 270 ft 24 8 m Recommended Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance sinesine 0 5 ppm nominal 1 0 ppm max Maximum Feed Flow 95 GPM 22 m3 hr Minimum Brine Flow Perme
290. ad to TOC breakthrough of the DI columns For the most up to date information on MSDS sheets please contact our web site at www trisep com TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 391 emm TriSep Corporation Chemical Manual TRIS gt CORPORATION Deactivating TriStat 110 When used in concentrations greater than 50 ppm TriStat 110 should be deacti vated prior to disposal using the following procedure Check with Federal State and local regulations in your area concerning disposal 1 Calculate total gallon volume of Tristat 110 solution in the cleaning tank and in the piping hoses and pressure vessels 2 For every gallon of solution add 75 Ib of sodium metabisulfite and mix thor oughly Adjust pH to 4 0 using sulfuric acid Recirculate for 20 minutes and then shutdown pump Allow to static soak for 1 hour Rinse to appropriate drain 3 4 5 6 A a TriStat 110 Toxicological Report Species Ceriodaphnia dubia Pimephales promelas Daphnia Waterflea Fathead Minnow 48 Hour LC50 Estimated LC50 156 10 mg L 105 30 mg L 95 Upper C L 172 60 mg L 113 80 mg L 95 Lower C L 141 60 mg L 97 44 mg L Chronic Biomonitoring 1100 hrs Survival LOEC 200 00 mg L 100 00 mg L NOEC 150 00 mg L 50 00 mg L Reproduction LOEC 150 00 mg L NOEC 100 00 mg L Growth LOEC N A NOEC 50 00 mg L LOEC Lowest Obs
291. alifornia 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION oO NN 8 X 20 Low Fouling RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 X201 TSAN 9 700 36 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane Configuration Spiral Wound Fiberglass Outer Wrap with FoulGuard Technology Active Membrane Area 365 ft 33 5 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 2NTU K 20 3 Veehnelegy L 1 A i i KK Je id B Es itn i xt D y E Del Element Wei
292. ameter B 4 0 101 Permeate Tube C 0 62 15 9 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Desal DuPont Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION LA 4 ACM LP Low Pressure RO Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 M5P3U5 2 400 9 0 98 50 97 50 Performance is based on the following test conditions 2 000 00 ppm NaCl 150 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM LP Fully Aromatic Polyamide Low Pressure Advanced Composite Configuration Spiral Wound Turboclean Shell Active Membrane Area 85 ft 7 9 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C
293. and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Osmo Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com r TRIS gt CORPORATION Permeate flow Model GPD m3 day 8340 SB20 TSOA 8 000 30 0 PRODUCT SPECIFICATION 8 3 CA RO Element Series Minimum Salt Rejection Average Salt Rejection 98 00 97 00 Performance is based on the following test conditions 2 000 0 ppm NaCl 420 0 psi 25 C 15 recovery pH 5 5 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type COMI OUT ANON T Active Membrane Area Recommended Applied Pressure Maximum Applied Pressure Recommended Operating Temperature Feedwater pH Range Chlorine Tolerance Maximum Feed Flow Minimum Brine Flow Permeate Flow Ratio Maximum SDI 15 minutes Maximum Turbidity
294. and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane y SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Za 8 ACM LP Low Pressure RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 ACM4 UWAN 16 000 60 0 99 00 98 00 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM LP Fully Aromatic Polyamide Low Pressure Advanced Composite Configuration Spiral Wound Fiberglass Outer Wrap Active Membrane Area 400 ft 37 2 m Recommended Applied Pressure 50 300 psi 3 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine To
295. ane TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 346 Competitive Replacement Guide um TRIS SE CORPORATION Replacing elements from one competitor to the next can be a difficult and frustrating task Following is a cross reference list that gives the TriSep equivalent to many competitive membrane elements currently on the market Manufacturers frequently change models and specifications so there is no guarantee that our listing is accurate up to date or that the TriSep element listed has exactly the performance of the product you are currently using It should help guide you in determining what element has similar or equivalent performance to a competitive product Besides differences in flow and rejection there are also mechanical differences from one element to another Most variations in elements center around different permeate tube diameters and or configurations male versus female There are also special element diameters 8 3 and 8 5 that some manufacturers have produced to try and minimize competition To address different permeate tube diameters you must also instruct us to ship an inboard adapter This is the piece that adapts from the first and last element in a pressure tube to the pressure tube end cap To supply the correct adapter we will need to know the manufacturer and possibly the model of your pressure tube Attached in th
296. anical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION LA 8 X 20 RO Turboclean Element TRIS gt CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 N1F3X5 7 100 26 0 99 00 98 00 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane ei le le e NEE Spiral Wound Turboclean Shell with FoulGuard Technology Active Membrane Area 270 ft 24 8 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 800 psi 55 bar Recommended Operating Temperature 35 104 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 95 GPM 22 m3 hr
297. anitize in place as there 1s no flow of cleaning or sanitizing chemicals into this area If cleaning or sanitizing chemicals do get into this area it is difficult to predict the rinse out time for these chemicals Standard net wrap sanitary elements have traditionally been used in food and dairy applications Due to the high by pass flow inherent with these designs food and dairy systems incorporate large recirculation pumps to insure a certain minimum flow through the elements These net wrap elements cannot be used in standard 2 1 arrays normally used In water applications The Turboclean element minimized by pass flow to 15 20 of the feed flow This allows the TurboClean element to be used in standard water type applications like dialysis water make up Following are some TriSep TurboClean elements specifically engineered for the pharmaceudical water market TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 130 PRODUCT SPECIFICATION Z 3 8 AUM UF High Temperature Turboclean Element TRIS CORPORATION Permeate flow Model GPD m3 day M W C O 3838 M8P4V6 1 700 6 0 3 500 Performance is based on the following test conditions 500 0 ppm Dextran 110 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type AUM Advanced Ultrafiltration Membrane ei le le e NEE
298. ants can quickly lead to a loss of system should be used after a low pH cleaning with Tri performance associated with a decrease in perme Clean 210 except for emulsified oil fouling in ate flow and increase in differential pressure and which case the order should be reversed a loss of element rejection If left unchecked this fouling can permanently damage the membrane PACKAGING elements leading to costly and premature mem TriClean 212TFNE is shipped as a powder in 45 brane replacement Some municipal wastewater kg plastic containers Pricing is F O B our factory treatment plants do not allow discharge of EDTA in Germany Delivery for most orders is 1 2 days into the plant TriClean 212TFNE was created to after receipt of order meet these requirements MSDS SHEETS SOLUTION For the most up to date information on TriClean 212TFNE removes biological organic MSDS sheets please contact our web site at and colloidal foulants without damaging sensitive www trisep com polyamide composite membrane elements TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax e www trisep com e 0105 322 emm TriSep Corporation Chemical Manual TRIS gt CORPORATION TRICLEAN 213 APPLICATION OXIDIZING TriClean 213 should be mixed in a cleaning tank equipped with a mechanical mixer heater low POWDER CLEANER pressure recirculation pump and cartridge or bag filter This cleaner works best w
299. anual APPLICATION TriPol 9110 is metered into the feed water at a point where turbulent flow will ensure adequate chemical mixing prior to entering the RO or NF system This 1s usually done prior to the cartridge filters and high pressure pump Dosing rates vary depending on feedwater quality and recovery but normally run between 2 and 5 ppm For exact dosing use the latest version of TroiWin TriPol 9110 contains a dispersant and can be used if there is iron or other metal hydroxides in the feedwater PERFORMANCE Max Langlier Saturation Index 42 6 Max CaSO4 Saturation 300 Max SrSO4 Saturation S00 Max BaSO4 Saturation 10 000 Max CaF Saturation 10 000 Max CaPO4 Saturation SE Silica 100 1n the concentrate Levels may be exceeded on occasion Contact TriSep for advice PACKAGING TriPol 9110 is shipped as a liquid in 2 gallon sample sizes 5 gallon 40 Ib plastic pails and 55 500 Ib gallon plastic drums Pricing 1s F O B our factory in Goleta CA Salem VA or Duisberg Germany Delivery for most orders is 1 2 days after receipt of order MSDS SHEETS For the most up to date information on MSDS sheets please contact our web site at www trisep com 315 TriSep Corporation Chemical Manual TRIS CORPORATION TRIPOL 9510 SCALE SILICA INHIBITOR AND DISPERSANT e Silica dispersant capability e Superior control of sulfate scales e ron and silica dispersant capa bility
300. aq TESSA 120uuoo Domp V st Op ourpopo C 1880T L CCLOT L CLCOT L I ZI 0I L c LISO IL tO eg CSR be Oc80I L 6r780I L 2981151 1880I L Oc80I L C 6v80T L P2921 IL I 1880I L Oc80I L C680 I L 4 SUIMBIG S 9po A puw y Jo a8eg DOJIXX XXXX 0p08 86cvclI SXX XXXX 0p08 CLIVCII SXX XXXX 0p08 ot TT SXX XXXX OVOS 9S0 cTI HXx xxxx 0op08 8ICVCIT XX XXXX 0p08 SICVCIT DHXXXXXX OPO8 STEVI OJIXX XXXX 0p08 ItOvcII DO IXX XXXX 0p08 6 h lt ll V IXX XXXX 0y08 vItVCIUI V IXX XXXX 0p08 SOtVPCIUI V IXX XXXX 0y08 O6CVCII V AXX XXXX 0p08 OVOVCI I V IXX XXXX 0p08 SLCVCII S IXX XXXX 0v08 vItvcII S IXX XXXX 0708 06CvclI S JXX XXXX 07 08 OrOVCII S IXX XXXX 0708 SZCVCII JoquimN ed SLNHIAWTH 0DA LHIAVIG HONI 8 7 SIMS 0708 420 TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax e www trisep com 0703 WV S 01 8007 67 01 LO CI C APN aqny 1eoeds Ott 00 9 OAd ure oeJpAH 9Jnso o JOYS WELTI EUJ9 X4 CN SC Ur cI OAd ure oeJpAHq Dd ISO 614193 8 AI I9 pow sju outuro gt Jojdepy J9 depvy Jo3depy 9qn I sANnssoig IGN AOD ueopooqm oejsupH4 OSOZZ rte 9uogpnsA oq Jajdepe preoqui Oe LOI OAd P9p 9 YUM osn UeD oqny 9107 esoq OLCHTIT pue OTOVTIO LZ C8 97SE OAd T SuTejuoo yry oqny ounssoud SS PPOW juauluio IHd ISO IELIAIEIWN qn inss id 1ojiddepy J o depy Jo3depy s19j3edpy p ueoqug SUIL
301. ar menu selection or by depressing the Alt key while typing in the underlined letter of the selection you want to make Le Alt F would drop down the file menu Hovering the mouse pointer over any of the toolbar icons will display a brief description of what that button does 1 e Add project for creating a new Project Main Menu Notice the blue bar along the top of the screen This is the title bar and gives the name of the screen that you are in In the main screen this bar says Normalization Program The main menu has five selections available File Print Units Window and Help File There are six options in File whose functions are self explanatory Add Project Edit Project Delete Project View Project Export to Excel and Exit Print There are three selections All data Input Data Calculated Data All data will print the entire project 1 e data which is input as well as calculated by the program Input data prints only the data the user is required to input and Calculated data prints only the fields calculated by the program Units This is used to set the default units you want to every time you start a new project These units are set by first selecting the units you want for Pressure Flow Flux and Temperature from their respective drop down boxes You can either select Units and Default from the menu or Click on the Units icon in the toolbar
302. aromatic polyamide urea reverse osmosis thin film with nominal salt rejections over 99 5 and flux rates comparable to the ACMI The X20 membrane shows some fouling resistance characteristics that most other thin film membranes available on the market do not have Nanofiltration Softening Membranes ANM XN45 TS80 XN45 membrane is an aromatic polyamide Advanced Nanofiltration Membrane ANM with nominal solute rejections of 10 30 NaCl and greater than 90 MgSOA and sucrose The XN45 membrane offers high flux rates with high rejection characteristics of multivalent 10ns and organics at typical net driving pressures in the range of 100 psi net TS80 membrane is an semi aromatic polyamide Advanced Nanofiltration Membrane ANM with nominal solute rejections of 90 NaCl and greater than 99 MgSOA and sucrose The TS80 membrane offers high flux rates with high rejection characteristics of multivalent ions and organics at typical net driving pressures in the range of 100 psi net Ultrafiltration Microfiltration Membranes UES0 UEIO TMIO UES50 membrane is a 150 000 MWCO Advanced Ultrafiltration Membrane AUM made from a poly sulfone polymer This membrane has a rejection for Dextran of 100 000 MW of about 90 When tested on clean water at 30 psi the membrane exhibits a flux rate of 40 50 gfd UE10 membrane is a 10 000 MWCO Advanced Ultrafiltration Membrane AUM made from a polysulfone polymer This membran
303. ass Outer Wrap Active Membrane Area 365 ft 33 5 m Recommended Applied Pressure 40 300 psi 3 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 45 20 Length A 40 00 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION A lt 8 ACM LP Low Pressure RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejec
304. ate TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 388 TriSep Engineering Manual TRIS gt ieee ee ELEMENT STORAGE RECOMMENDATIONS FOR XN45 and TS80 MEMBRANE TYPES This document covers all XN45 and TS80 spiral wound NF membrane elements SHORT TERM ELEMENT STORAGE For elements that will be shut down for short periods of time less than 2 3 weeks pretreated feedwater should be flushed through the system daily at low pressure 20 30 psi This will minimize the growth of microbiological organisms and reduce the chance of scaling LONG TERM ELEMENT STORAGE TriSep 8 202 mm and 4 102 mm diameter TS40 and TS80 elements stored in the factory shipping solution will retain the flow salt passage performance for a period of at least twelve 12 months from date of shipment ex works or twelve 12 months following the addition of the sanitizing solution if the elements remain sealed away from direct sunlight and storage temperature must be between 32 F 0 C 113 F 45 C For extended storage times exceeding three 3 months optimum storage temperature must be less than 60 F 15 C If elements are to be stored for periods greater than twelve 12 months consult TriSep Corporation for procedures to minimize long term effects For elements that have been placed in service and will be out of service for more than 2 3 weeks a storage solutio
305. ate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 2NTU ADDIIG300I1 uuuu uuu A degen General Pharmaceutical Element Weight 40 18 Length A 40 00 1 016 Diameter B 7 90 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 047 thick parallel spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION A 8 AUM UF High Temperature Turboclean Element TRI CORPORATION Permeate flow Model GPD m3 day M W C O 8040 N6J1W6 10 000 37 0 10 000 Performance is based on the following test conditions 500 0 ppm Dextran 30 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type AUM Advanced Ultrafiltration Membrane eidele e EE Spiral Wound High Temperature Turboclean Shell Active Membrane Area 252 ft 23 4 m Recommended Applied Pressure 20
306. ate and useful However since any assistance furnished by TriSep with reference to the proper use and disposal of its products is provided without charge and since use conditions and disposal are not within its control TriSep assumes no obligation or liability for such assistance and does not guarantee results from use of such products or other information herein TriSep assumes no liability for results obtained or damages incurred through the application of the presented information and data It 1s the user s responsibility to determine the appropriateness of TriSep s products for the user s specific end uses The total system operation performance is out of the control of TriSep Corporation personnel and we are not on site to monitor the proper operation of our products in the systems TriSep s product performance is affected by such operational variables including but not limited to pretreatment operators and training system breakdowns feedwater changes system components and component changes and other possible variables This warranty applies to all sales of spiral wound elements on or after October 1 2008 1 0 MODELS TriSep X 20 ACM CA XN45 TS80 UE10 UE50 and TM10 membrane elements 1 1 APPLICATIONS The following warranty applies to TriSep spiral wound elements used in water applications Non water applications such as chemical processing food processing or wastewater treatment are not covered by
307. ate connector O rings are in place Place a small amount of Parker Super O Lube or glycerine on the permeate connector O ring Insure that the inside bore of the pressure vessel are clean and free of dirt dust or foreign objects Load elements from feed side of pressure vessel Insert the inboard end connector to the downstream end of the first element side opposite brine seal and load halfway into the pressure vessel Insert the element interconnector into the feed end of the element side with brine seal Make sure the interconnec tor O rings are lubricated with Parker Super O Lube or glycerine While holding the first element connect the downstream end of the next element to the interconnector of the first element Load with brine seal facing installer Push the element stack into the pressure vessel until half of the second element is inside the pressure tube Repeat steps 6 8 until the vessel is loaded When all the elements have been loaded into the vessel push the stack to the downstream side of the pressure vessel until the downstream inboard adapter will connect with the downstream end cap Install the downstream end cap and spacer tube then push the entire membrane stack as far as possible towards the downstream end cap Install the upstream inboard adapter and connect to the upstream end cap Install the upstream end cap and connecting piping Repeat steps 3 12 for the remaining pressure vessels Start the system and run bot
308. ate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 ACM2 TSFA 9 700 36 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Configuration Spiral Wound Fiberglass Outer Wrap Active Membrane Area 365 ft 33 5 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance lt 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1NTU Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permea
309. ater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION 3 8 TS 80 High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 3840 M7P4V6 1 700 6 0 99 00 97 00 Performance is based on the following test conditions 2 000 00 ppm MgSOA 110 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ANM Aromatic Polyamide Advanced Nanofiltration Membrane COMMUN AU OM EEN Spiral Wound Turboclean Shell Active Membrane Area 53 ft 4 9 m Recommended Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 25 GPM 5 6 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity
310. ation TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Zn 8 TS80 Nanofiltration Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 TS83 UWA 11 000 41 0 98 50 97 00 Performance is based on the following test conditions 2 000 0 ppm MgSOA 110 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ANM Aromatic Polyamide Advanced Nanofiltration Membrane ONTO ON I uu aan wa Spiral Wound Fiberglass Outer Wrap Active Membrane Area 400 ft 37 2 m Recommended Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow
311. bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 6 GPM 1 4 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 7 3 2 Length A 40 0 1 016 Diameter B 2 5 63 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION 4 ACM LP Low Pressure RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 ACM5 TWF 2 900 9 0 98 50 97 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 150 0 psi 25 C 15 recovery pH 8 0 30 minutes operation
312. been on line for over 7 months and were cleaned for the first time after 6 months The cleaning restored system to start up conditions with system delta P at only 30 psi The X 20 membrane has exhibited superior silica rejection over the competitors membrane Permeate water silica concentration has dropped from 140 ppb with the competitors elements to 8 ppb with the X 20 This corresponds to a system rejection of 99 2096 running at 7596 recovery and an average element rejection of 99 7596 This has resulted in reducing the regeneration rate of the demineralizer bed and increased the run lengths from 3 million gallons to 15 million gallons The customer is adding Sodium Metabisulfite to control the free chlorine to below 0 1 ppm and allowing a residual of 1 0 ppm chloramine to the RO feed The utility will increase the chloramine concentration to 5 to 10 ppm during the summer months TriSep s X 20 elements have significantly reduced the required cleaning frequency and its superior silica rejection has resulted in longer run times for the demineralizers Overall system costs have dropped due to the reduction in chemical usage and labor costs assoc iated with cleaning TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 362 s TRIS S CORPORATION BULLETIN NO TYPE APPLICATION LOCATION PRODUCTS PROCESS PERFORMANCE CONCLUSIONS APPLICATION BU
313. ble for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION lt 8 TS80 Nanofiltration Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 M7EGT6 8000 30 0 99 00 97 00 Performance is based on the following test conditions 2000 ppm MgSO4 110 psi 25 C 15 recovery pH 8 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ANM Aromatic Polyamide Advanced Nanofiltration Membrane Configuration Spiral Wound Turboclean Shell Active Membrane Area 355 ft 32 6 m Recommended Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity
314. ble for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane eegenen SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION S 9 ACM RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 ACM2 TSA 9 700 36 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane COMM QUIN GIOI L ste uqu La cet T Spiral Wound Fiberglass Outer Wrap Active Membrane Area 365 ft 33 5 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity
315. ccurring in the beginning of the time period slowly leveling off to a constant level A value of 0 025 would correspond to a 209 flux decline over 3 years Larger numbers correspond to higher flux declines The salt passage increase factor SPIF allows you to take into account decreases in element rejection A factor of 2 would correspond to the salt passage doubling in three years Higher numbers would result in more dramatic decreases in element rejections We normally recommend a value of 2 0 for cellulose acetate elements and 1 3 for polyamide elements The only thing left to do to complete the system design is to select the element model you wish to use and determine the array of the system You can also specify permeate back pressures to help in balancing membrane fluxes between passes We have also added interpass concentrate boost pressure This allows a system designer to add a pump or turbocharger between passes to allow for increasing the feed pressure to a second pass There are two ways to select an element Click on the Select button or double click in the box under the Model heading The latter is required if you want to select different elements for different passes When you perform either of the above the element selection window pops up This window allows you to select the element model you wish to use Specification sheets for indi vidual elements may be printed by clicking on the Print Spec Sheets button Custom mode
316. ce is based on the following test conditions 2 000 0 ppm MgSOA 110 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ANM Aromatic Polyamide Advanced Nanofiltration Membrane COMM QUIN GIOI L ste uqu La cet T Spiral Wound Fiberglass Outer Wrap Active Membrane Area 440 ft 40 4 m Recommended Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 50 23 Length A 40 0 1 016 Diameter B 8 5 215 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engine
317. cer The membrane is the part of the element where the separation occurs The membrane can be a RO NF UF or MF type membrane The feed spacer sits between two adjacent membrane faces and acts as a spacer and also a turbulence promoter This function 1s critical to minimizing concentration polarization The permeate carrier fabric acts as the pipe to allow the permeate to exit from the element The other components normally present in a spiral wound element are the permeate tube and the membrane adhesive The permeate tube 1s the pipe through which the permeate can exit the element Water under presure 1s forced through the membrane It travels down the permeate carrier fabric to the permeate tube The permeate tube has holes drilled in it to allow the permeate to enter the inside of the tube Interconnectors with O rings seal the feed water from the permeate water at each end The membrane placed in a spiral element is sealed on three sides The only side not sealed 1s that adjacent to the permeate tube The adhesive creates a sandwich of material between two back sides of the membrane and the permeate carrier fabric The adhesive must form a leak free seal that can hold up to high pressures and possibly high temperatures The feed spacer material Is normally a mesh or netting material made from polypropylene This material is normally about 0 028 0 7 mm to 0 031 0 8 mm thick It must have a relatively low pressure drop at normal operating conditio
318. ct You begin by entering the Project code and Name You proceed to select the units for Pressure Flow Flux and Temperature from their respective drop down boxes If you have already set the units using the Units option you can jump to the Brine Stage depending on what stage you select the input boxes for the Vessels and Elems Vessels will be displayed Conductivity is populated with a default value of 0 5000 and osmotic pressure is populated with 0 0100 Both these can be changed by the user These determine for the program the conversion from conductivity to TDS 1 e a value of 0 5 assumes that a conductivity of 1000 mmhos would equal a TDS of 500 This value can be customized to the particular feed water you have The osmotic pressure value converts TDS to osmotic pressure A value of 0 01 would convert a TDS of 1000 ppm to an osmotic pressure of 10 psi The date format has two options DMY to display date in the dd mm yy format and MDY to display date mm dd yy format There are two check boxes for how delta P is input One is Delta P and the other for InterStage pressure both can be left unchecked or either one of them can be checked When the Delta P box is checked one has to input the Delat P in the grid below for the different stages and the Interstage will be calculated automatically In case the Interstage pressure box is checked one has to input the Interstage values in the grid below for the different stages and Delta P will be automa
319. ction 8040 N117S5 7 100 26 0 99 00 98 00 Performance is based on the following test conditions 2 000 00 ppm NaCl 225 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane ei le le e NEE Spiral Wound Turboclean Shell with FoulGuard Technology Active Membrane Area 270 ft 24 8 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 95 GPM 22 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 2NTU Application Bacteria Concentration Element Weight 40 18 Length A 40 00 1 016 Diameter B 7 90 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 047 thick parallel spacer Permeate flow is clean water flux at standard cond
320. ction are catalyzed by the presence of trivalent metal ions When operating systems near the maximum silica saturation s the presence and concentration of trivalent metal ions should be evaluated Plants designed and operated at or near the maximum specified saturation levels may require special system process features 1 e low pressure feed water flushes upon system shutdown In version 2 0 0 the silica saturation index takes into account pH and temperature Maximum Allowable Saturation Indexes Scale Max Saturation Max Saturation without scale inhibitor with scale inhibitor CaCO3 lt 0 2 6 CaSO4 lt 100 lt 400 SrSO4 lt 100 lt 1 200 BaSO4 lt 100 lt 12 000 CaF2 lt 100 lt 10 000 Silica lt 100 lt 200 Effectiveness of scale inhibitors dosing requirements and feed water chemistry affect maximum saturation indexes Contact chemical company for specific details 6 CUSTOM ELEMENT MODEL NUMBERS Starting the Program New to version 2 0 0 is the ability to add custom model numbers These can be competitors models to allow users to only have one program that they require to compare different element types It can also be used to create custom model that are not on the standard TriSep list TriSep Corporation does not assume any liability for any custom elements that are designed by third parties To input a custom model number go to the main start up screen and click on File Add Custom Model This brings up the RO
321. ctions Design Guidelines Loading Procedure Storage Procedures Troubleshooting Flux rejection recovery How a membrane is made chemistries Membrane performance versus temperature How a Spiral is made Quality Control Procedures Rejection of specific ions by membrane type boron rej System Design guidelines for spiral wound elements Pressure tube element Loading procedure Storing elements by membrane type Troubleshooting spiral wound membrane elements Shipping Information Sizes and weights for standard element pallets TriSep Software Software for system desgin and normalization TROI Projection Software User s Manual ver 2 1 0 TRON Normalization Software users manual ver 1 1 0 Administrative Doing Business with TriSep Spare Parts List List includes adapters connectors and seals TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 275 276 277 284 298 302 308 309 317 324 330 336 338 343 355 371 371 372 373 374 376 381 377 379 382 383 384 388 391 393 395 395 407 411 417 3 A TRIS gt WELCOME TO TRISEP CORPORATION Attached is TriSep Corporation s latest Product Catalog containing current literature in support of our Reverse Osmosis Softening Nanofiltration and Ultrafiltration spiral wound membrane products TriSep has products that are specifically designed for municipal industrial
322. d New and or unused elements must be stored in a cool dry place out of direct sunlight Elements taken out of operation for a period of more than one week must be treated with a suitable biocide Contact TriSep for more information This element is covered under TriSep s Standard Guarantee for Spiral Wound Products If the operating parameters are not followed the guarantee will be void TriSep s maximum total liability for all causes including any breach of warranty or failure to deliver conforming goods shall not exceed the value of the contract TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 34 TurboClean Sanitary Elements The New Standard of Performance TRIS CORPORATION Spiral membrane elements used in sanitary operations such as in the dairy industry for lactose and protein whey separations are required by the USDA to ensure that a percentage of the feed must be free to by pass or flow around the outside of the membrane element to assure this annular area is continuously flushed and that there are no stagnant areas which are not fully exposed to CIP sanitizing procedures Conventional spiral membrane elements have been used historically in water beverage bottled water and dialysis make up water applications These membrane elements use a brine or peripheral seal to prevent feed water from by passing through the ann
323. d Flow 20 GPM 4 5 m3 hr Y M Minimum Brine Flow Permeate Flow Ratio 5 1 VU SH ED Maximum SDI 15 minutes 5 0 appro 4 Maximum Turbidity 1 NTU Application Whey Concentration Il HAT III MI UTIN T MI TM Wi i LAETI i hi Ti l l rif LLL A l AU MI Element Weight 12 5 4 Length A 38 965 Diameter B 3 8 96 Permeate Tube C 0 83 21 2 Units in pounds and inches units in paranthesis in kilograms and millimetes Dim A does not include ATD Mechanical Configuration Sanitary Style Core Tube ATD not included with element Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane End nF I Y i SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION a 3 8 ACM High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 3838 M2D V6 1 300 4 0 99 50 98 50 Performance is based on the following test conditions 2 000 00 ppm NaC
324. d Nanofiltration Membrane Con tigurationi uu a a aaasasan Spiral Wound High Temperature Turboclean Shell Active Membrane Area 70 ft 6 4 m Recommended Applied Pressure Not applicable Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr D M Minimum Brine Flow Permeate Flow Ratio 5 1 u K Di T Maximum SDI 15 minutes 5 0 AppRO Maximum Turbidity 1 NTU A li AMO uu cose DP Lactose Demineralization Element Weight 15 7 Length A 38 00 965 Diameter B 3 9 99 Permeate Tube C 0 83 21 2 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Sanitary Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane Si Y SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep c
325. d Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION 9 ACM RO Element Series TRIS gt CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 ACM3 UWA 12 000 45 0 99 20 98 50 Performance is based on the fol
326. d such as for surface water treatment prior to an RO system or for removal of occysts such as cryptosporidium or giardia The UE10 and UE50 have excellent resistance to a wide range of pH s 2 12 excellent tolerance to chlorine up to 1 000 ppm and other oxidants and excellent thermal stability with the proper element construction up to 140 F 60 C The UE10 and UE50 membranes are not back flushable membranes like the UB50 membrane used in the SpiraSep For applications with high loadings of suspended solids the SpiraSep should be used rather than the UE10 or the UE50 4040 UE10 QSF 4 0 diameter by 40 long 0 75 male O D permeate tube 4040 UE50 QSF 4 0 diameter by 40 long 0 75 male O D permeate tube 8040 UE50 QSA 8 0 diameter by 40 long 1 50 male O D permeate tube TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 250 PRODUCT SPECIFICATION Za 4 AUM Ultrafiltration Element Series TRIS gt CORPORATION Permeate flow Model GPD m3 day M W C O 4040 UE50 QSF 4 400 16 0 100 000 Performance is based on the following test conditions 500 0 ppm Dextran 30 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type AUM Advanced Ultrafiltration Membrane deele D ON MI m denne Spiral Wound Fiberglass Outer Wrap Active Membrane Area
327. diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION A lt 8 ACM RO High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 M4J9W7 15 400 58 0 99 00 98 00 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM LP Fully Aromatic Polyamide Low Pressure Advanced Composite Conn B gs le Spiral Wound Turboclean Shell Active Membrane Area 385 ft 35 4 m Recommended Applied Pressure 50 300 psi 3 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate
328. diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TRIS CORPORATION Permeate flow Model GPD m3 day 7 000 26 0 OPERATIONAL AND DESIGN DATA Membrane Type Oe TN e E Active Membrane Area Recommended Applied Pressure Maximum Applied Pressure Recommended Operating Temperature Feedwater pH Range Chlorine Tolerance Maximum Feed Flow Minimum Brine Flow Permeate Flow Ratio Maximum SDI 15 minutes Maximum Turbidity Element Weight Length A 45 20 40 0 1 016 Diameter B 7 9 200 PRODUCT SPECIFICATION 8 CA RO Element Series Minimum Salt Rejection Average Salt Rejection 8040 SB20 TSA 98 00 97 00 Performance is based on the following test conditions 2 000 0 ppm NaCl 420 0 psi 25 C 15 recovery pH 5 5 30 minutes operation SB Cellulose Ace
329. ding the gas within the coal fissures The extracted ground water is of poor quality making it unsafe for direct environmental discharge Environmental regulations have required coal bed methane producers to treat the produced water to drinking water standards Gamma Ray Type Log AZT Shaliow Water Sand 35 p SClaystone x Figure 1 CBM well schematic For additional information regarding SpiraSep UF membranes please contact Mike Snodgrass at 1 805 964 8003 ext 113 or send e mail to snodgrass trisep com Due to the remote locations of CBM wells overall water recovery is critical in order to reduce disposal costs The Solution For CBM producers to safely discharge the produced water to the environment the salinity must be drastically reduced This is accomplished using a combination of RO SWRO and electric coagulation EC Ultrafiltration is used as pre treatment to remove all particulate matter and provide the RO systems with high quality water The Results Water is extracted from the coal beds and delivered to two SpiraSep 900 ultrafiltration systems with capacities of 500 and 700 gpm 113 and 159 m hr Backwash water from each system is collected and filtered by additional SpiraSep systems bringing the overall recovery of the ultrafiltration process to 9996 Overall system recovery for the UF RO EC process is 92 9596 TRI A Crystal Clear Solufion CORPORATION Trise
330. dwater conditions Individual element s permeate flow may vary 15 Engineered Membrane ee ee SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Zi 8 ACM RO Turboclean Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 M2E6X2 10 250 38 0 99 50 98 50 Performance is based on the following test conditions 2 000 00 ppm NaCl 225 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Configuration Spiral Wound Turboclean Shell Active Membrane Area 390 ft 36 3 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0
331. e 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 19 30 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Desal DuPont Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Zn 8 TS80 Nanofiltration Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 TS80 TSDA 9 000 34 0 99 00 97 00 Performance is based on the following test conditions 2 000 0 ppm MgSOA 110 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ANM Aromatic Polyamide Advanced Nanofiltration Membrane ONTO ON I uu aan wa
332. e 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 15 7 Length A 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane A SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Lum 4 TS80 Nanofiltration Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 TS80 TSF 2 000 7 0 99 00 97 00 Performance is based on the following test conditions 2 000 0 ppm MgSOA 110 0 psi 25 C 15 recovery pH 8 0 30 minutes operation O
333. e 50 300 psi 3 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION lt N 8 TS80 Nanofiltration Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 TS80 UWFA 10 000 37 0 99 00 97 00 Performance is based on the following test conditions 2 000 0 p
334. e TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 387 TriSep Engineering Manual TRIS 3 ELEMENI SIORAGE RECOMMENDATIONS CORPORATION FOR X 20 ACM and ACM LP MEMBRANE TYPES This document covers all X 20 ACM and ACM LP spiral wound RO membrane elements SHORT TERM ELEMENT STORAGE For elements that will be shut down for short periods of time less than 2 3 weeks pretreated feedwater should be flushed through the system daily at low pressure 20 30 psi This will minimize the growth of microbiological organisms and reduce the chance of scaling LONG TERM ELEMENT STORAGE TriSep 8 202 mm and 4 102 mm diameter X 20 ACM and ACM LP elements stored in the factory shipping solution will retain the flow salt passage performance for a period of at least twelve 12 months from date of shipment ex works or twelve 12 months following the addition of the sanitizing solution if the elements remain sealed away from direct sunlight and storage temperature must be between 32 F 0 C 77 F 25 C For extended storage times exceeding three 3 months optimum storage temperature must be less than 60 F 15 C If elements are to be stored for periods greater than twelve 12 months consult TriSep Corporation for procedures to minimize long term effects For elements that have been placed in service and will be out of service
335. e C 0 83 21 2 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Sanitary Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com Lae TRIS gt CORPORATION Permeate flow GPD m3 day Model 3838 N2E U8 1 700 6 0 PRODUCT SPECIFICATION 3 8 XN45 High Temperature Turboclean Element Minimum Salt Rejection Average Salt Rejection 95 00 92 00 Performance is based on the following test conditions 2 000 0 ppm MgSOA 110 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type Configuration Active Membrane Area Recommended Applied Pressure Maximum Applied Pressure Recommended Operating Temperature Feedwater pH Range Chlorine Tolerance Maximum Feed Flow Minimum Brine Flow Pe
336. e Area 116 ft 10 8 m Recommended Applied Pressure Not applicable Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 10 0 ppm Maximum Feed Flow 70 GPM 15 8 m3 hr y M Minimum Brine Flow Permeate Flow Ratio 5 1 S y N Maximum SDI 15 minutes 5 0 APPROV d Maximum T urbuditv 1 NTU APPIC AUO ete een ene ee Milk Fractionation Element Weight 30 14 Length A 38 00 965 Diameter B 6 4 162 Permeate Tube C 1 14 29 0 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Sanitary Style Core Tube Feed Spacer 0 080 thick diamond spacer Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION TRIS CORPORATION 8 ACM RO High Temperature Turboclean Element Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8038 M2C9U8 9400 35 0 99 50 98 50 Performance is based on the following test conditions 2000 ppm NaCl 225 psi 25 C 15 recovery pH 8 30 minutes operatio
337. e I D permeate iube TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 239 r TRIS gt CORPORATION Permeate flow Model GPD m3 day 2540 SB20 TSF 900 1 0 PRODUCT SPECIFICATION 2 5 CA RO Element Series Minimum Salt Rejection Average Salt Rejection 98 00 97 00 Performance is based on the following test conditions 2 000 00 ppm NaCl 420 00 psi 25 C 15 recovery pH 5 50 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type COMMQUPATON ERROR EE Active Membrane Area Recommended Applied Pressure Maximum Applied Pressure Recommended Operating Temperature Feedwater pH Range Chlorine Tolerance Maximum Feed Flow Minimum Brine Flow Permeate Flow Ratio Maximum SDI 15 minutes Maximum Turbiditly Element Weight Length A 7 3 2 40 00 1 016 Diameter B 2 5 63 SB Cellulose Acetate Blend Spiral Wound Fiberglass Outer Wrap 26 ft 2 4 m 100 300 psi 7 21 bar 600 psi 41 bar 50 90 F 10 32 C 5 5 nominal 4 7 0 5 ppm nominal 1 0 ppm max 6 GPM 1 4 m3 hr 5 1 Permeate Tube C
338. e Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 TS80 TSAN 9 000 34 0 99 00 97 00 Performance is based on the following test conditions 2 000 0 ppm MgSOA 110 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ANM Aromatic Polyamide Advanced Nanofiltration Membrane eidele e EE Spiral Wound Fiberglass Outer Wrap Active Membrane Area 365 ft 33 5 m Recommended Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not appl
339. e a significant issue as well The Solution SpiraSep 900 ultrafiltration UF systems provide consistent high quality effluent that exceeds all conventional technologies regardless of inlet water quality Whether For additional information regarding SpiraSep UF membranes please contact Mike Snodgrass at 1 805 964 8003 ext 113 or send e mail to snodgrass trisep com the water source is 1 0 NTU or 1 000 NTU the ultrafiltration membranes will provide high quality effluent and low silt density index SDI values The complete barrier layer provided by the UF membrane removes all particulate matter from your feed water The Results Pre treatment using SpiraSep ultrafiltration membranes will also provide the following benefits o Improved reliability o Improved RO performance o Higher RO flux rates o Lower RO chemical cleaning requirements Reduced footprint Microbial removal Low effluent turbidity 0 1 NTU Low SDI lt 3 0 O O O O lt 2 A A Triseo Corporation A Crystal Clear Solulion IR gt SpiraSeo System Reference List prd E TSS mg l Se Start up Date Location Industrial Wastewater 67 100 500 15 June 2009 Australia Fixed Film Bioreactor 300 500 1000 15 April 2009 Canada Fixed Film Bioreactor 300 500 1000 15 January 2009 Canada Metal Hydroxides 350 50 500 16 May 2009 USA Coal Bed Methane 700 10 20 30 April 2008 USA Surface Water 400 10 20 25 April
340. e e EE Spiral Wound Fiberglass Outer Wrap Active Membrane Area 365 ft 33 5 m Recommended Applied Pressure 50 300 psi 3 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Za 8 TS80 Nanofiltration Element Series TRIS CORPORATION Permeate flow Averag
341. e element specification sheet which can be printed for each element The differential pressure drop across each element is calculated by the following formula Delta P Delta P Coeff Fbar Delta P Exponent Where Delta P pressure drop in psi Delta P Coeff empirical value entered into program Fbar average feed brine flow rate in gpm and Delta P Exponent empirical value entered into program The leak factor assumes a certain by pass leakage for each element A value of 0 001 is equal to a 0 1 leakage Active area is the area in each element NaCl rejection is the rejection of sodium chloride for each element Calc A value is used in permeate flow calculations This value is calculated automatically after you have input the permeate flow area and net driving pressure for each element The Temp Factor is used to correct for variations in permeate flow with temperature The membrane type selects the specific ionic rejections for each type of membrane These can be seen in the calculation section under Modify Ionic Rejections NDP is the net driving pressure in psi at the test conditions for the permeate flow and rejection The remainder of the values on pages 2 4 are self explanatory and are not used in any calculations but only in the printed specifica tion sheet Inputing a Custom Element There are two ways to input a custom element First you can start from scratch and click on the Add Element button I would not recom
342. e event CUSTOMER cancels all or any portion of this contract following the date of acceptance by SELLER CUSTOMER shall be obligated to pay for all fabricated and or purchase of components and all other non recoverable costs pertaining to the project In the event suit is necessary to enforce payment by CUSTOMER whether as a result of cancellation or as a result of nonpayment CUSTOMER agrees to pay all actual attorney s fees out of pocket costs and actual Court costs incurred by SELLER including all out of pocket costs and actual attorney s fees in enforcing any judgment In such event SELLER shall have the exclusive right to institute legal proceedings in either any Court having jurisdiction where the CUSTOMER s materials are installed the place of residence of the CUSTOMER or in any Court of competent jurisdiction in the County of Santa Barbara State of California In the event CUSTOMER institutes legal proceedings against SELLER for whatever reason the Superior Court of the County of Santa Barbara shall have exclusive jurisdiction 10 ASSIGNMENT CUSTOMER may not assign this Agreement or any portion thereof without the express prior written consent of SELLER TriSep Corporation 93 S La Patera Lane Goleta CA 93117 805 954 8003 phone 805 964 1235 fax www trisep com i m RIS F CPAP OR AT F QP Bi GENERAL TriSep provides all data in good faith and believes the information and data contained herein to be accur
343. e has a rejection for Cytochrome C a amino acid with a MW of around 12 000 of about 95 When tested on clean water at 30 psi the membrane exhibits a flux rate of 20 30 gfd TM10 membrane is a 0 2 micron Advanced Microfiltration Membrane AMM made from polyvinylidene fluoride This membrane has a nominal pore size of 0 2 microns When tested on clean water at 10 psi the membrane exhibits a flux rate of 20 30 gfd TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 343 TriSep Flat Sheet Membrane TRIS gt CORPORATION TRISEP CORPORATION MEMBRANE FLAT SHEET SPECIFICATIONS Typical TriSep membranes flux in gallons per square foot per day GFD and salt rejections are listed below Membrane Minimum Flux Nominal Flux Maximum Flux Minimum Salt Nominal Salt Type GFD GFD GFD Rejection Rejection 96 Advanced Composites 1 RO ACMI 20 22 24 99 0 99 5 ACM2 25 28 30 99 0 99 5 ACM3 31 34 SJ 98 5 99 2 ACM4 38 40 45 98 0 99 0 X20 23 25 28 99 0 99 5 Advanced Composites 2 NF XN45 25 30 35 10 0 20 0 TS80 25 30 33 80 0 90 0 Cellulose Acetate Blend 3 RO SB50 24 27 30 94 0 96 0 Ultrafiltration 4 UF UES0 24 27 30 94 0 96 0 UE10 24 21 30 94 0 96 0 Microfiltration 5 MF TM10 24 27 30 94 0 96 0 1 ACM1 ACM2 ACM3 ACM4 and X20 membrane types are provided rolled in approximately 300 ft 91 44 m lengths on a 42 in 106
344. e manufacturer in the world to develop its own line of spiral wound membrane support chemicals Until now RO system users could not be sure if their membrane elements antiscalants cleaners and other support chemicals were compatible Both product lines are normally proprietary and developed and manufactured by different companies Recog nizing this critical fact TriSep s put its experienced R amp D team to work developing a complete chemical line for membrane separation elements Their expertise in the chemistry of membranes and now with the chemicals has allowed TriSep to develop a chemical product line 10096 compatible with current membrane technologies TriSep manufactures a complete range of spiral wound membrane products to accommodate just about any size requirement If your water treatment needs require the use of reverse osmosis Nanofiltration Ultrafiltration or Microfiltration TriSep s experienced professionals can provide you with application specific information and analysis that will assist you in making the optimal decision TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 4 TM i TriSep Web Site TRIS S P CORPORATION Our catalog is intended to answer most of your basic questions If we can assist you with specific questions or other membrane related matters please contact TriSep directly TriSep Corporation s professional staff a
345. e membrane is not fully underood However it seems certain that the chemical nature of the membrane must be such that it will exhibit a preference for water versus dissolved salts at the surface solution interface This may occur by weak chemical bonding of the water to the membrane surface or the water within the membrane structure A concentration gradient is thus formed Pure water either at the interface or within the membrane tends to exclude the solute Transport of the water across the membrane may be through pores physically present in the structure or by diffusion from one bonding site to another within the membrane Both the chemical and the physical nature of the membrane determine its inherent ability to transport water and reject salt Since reverse osmosis membranes are tailored to transport water it follows that dissolved com pounds which are similar in chemical nature to water will also pass readily since they will interact with the membrane in a similar manner More detailed discussion sof reverse osmosis and semipermeable membrans may be found in the literature Mechanical pressure Membrane Membrane Membrane a Osmosis b Osmotic c Reverse equilibrium osmosis TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 373 TriSep Engineering Manual TRI SEP Performance Variables CORPORATION As a first approximation the rate of water
346. e of RO Permeate Water B Start water recirculating through pump and back to tank C Add 2 pounds of TriClean 212CA per every 15 gallons of water in tank Recirculate until completely dissolved D Check pH of solution Range should be between 7 0 and 7 8 unless otherwise specified by membrane manufacturer pH may be raised by adding additional TriClean 212CA or lowered by adding sulfuric acid E Displace water in vessels by diverting Concentrate and Product lines to an appropriate drain and slowly pumping solution into vessels until it is visible coming from the Concentrate line Shutdown the pump and divert Concentrate and Product lines back to cleaning solution tank F Recirculate solution through vessels at appropriate flow and pressure for 30 minutes G Shutdown pump and allow to static soak for 1 hour H Clean additional passes in the same manner while first pass soaks l After soaking recirculate each pass for 30 minutes J Rinse using rinsing method TSR 1 TSC 6 Aggressive Biological and Organic Cleaning NOTE This cleaning is extremely aggressive and may result in some loss of membrane performance A Clean and fill solution tank with proper volume of RO Permeate Water B Start water recirculating through pump and back into the tank during chemical mixing C Add 1 1 pounds of TriClean 213 per every 25 gallons of water in the tank Allow to recirculate until thoroughly mixed D Check pH of solution proper range is b
347. e1 l ae OLWL AN WN d W WOY SENX OZ X SSOUYOIY GOUT elliS 9iqnios 9UueJquuJoe N opioigJo TE o a O BOU eDIOJIO snipey sens E oe mn E Se soysogsy S plio UO on ulu s SE syes snoenby ui9jo4g urunq v aponsed nD VOUT EEUE ee UO Tee LLLA UBSIM ooz 000 L 000 0L 00002 000 00L Je n29 O N eIpJelc Salas OLINL Uong UO ebuey auer oDue 1e n29 O N r OLUL DS EL EJ Ce OI2EIW abuey ESTERI WI Pe ODIN oDuey jeowed IEN 3uouig 3 eue amp eJquiojlN pooueApy uing3 edsg jn desi 371 TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 TriSep Engineering Manual i TRIS S Cross Flow Filtration CORPORATION Cross flow filtration is different from direct or dead end filtration In direct filtration there is a feed stream and a filtered stream Any material that is removed from the feed stream builds up inside the filter The filter then needs to be replaced or back flushed to remove the accumulated sustended e oo of direct filters are cartridge filters bag filters and sand filters In cross flow filtration there is a feed stream a purified or permeate stream and a concentrated or brine stream In cross flow filtration a separation is performed and if everything is working well no material will build up in the filter Material that is removed by the filter ends up in the concent
348. eate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TRIS gt CORPORATION Permeate flow Model GPD m3 day 8040 N7E6X8 14 000 52 0 PRODUCT SPECIFICATION 8 AUM Ultrafiltration Turboclean Element M W C O 100 000 Performance is based on the following test conditions 500 00 ppm Dextran 30 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type Configuration Active Membrane Area Recommended Applied Pressure Maximum Applied Pressure Recommended Operating Temperature Feedwater pH Range Chlorine Tolerance Maximum Feed Flow Minimum Brine Flow Permeate Flow Ratio Maximum SDI 15 minutes Maximum Turbidity PROP 67 0 p NNI RP A Element Weight 40 18 Length A 40 00 1 016 Diameter B 7 90 200 AUM Advanced Ultrafiltration Membrane Spiral Wound Turboclean Shell 260 ft 23 9 m 20 200 psi 1 4 14 bar 600
349. eatment trains array of 37 14 The elements were tested at flux rates and recoveries of 13 5 GFD 7596 recovery and 16 8 GFD 78 596 recovery The increased flux and recovery test was done to simulate conditions when another train was down Each manufacturer s elements were tested for 13 to 16 days treating roughly 400 000 gallons of raw water each Comparisons done at identical operating conditions showed 1 TriSep s ACM4 elements exhibited the lowest feed pressure requirements 2 The highest normalized average TriSep membrane rejection was 99 4096 compared to 99 10 and 98 30 for the other two manufacturer s elements 3 The ACMA exhibited the lowest increase in feed pressure 3 70 after recovering from the increased flux test compared to 5 1096 and 13 3096 4 The ACM4 exhibited no reduction in the normalized membrane productivity after the increased flux test while the competitor s showed 5 and 25 declines respectively 5 Projected system rejection with the 4040 ACM4 TSA was 96 30 Actual system rejection was 98 5096 Pilot test was very successful The low pressure high rejection ACM4 elements provide significant operating cost savings TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 366 um TRIS S CORPORATION BULLETIN NO TYPE APPLICATION CLIENT LOCATION PRODUCT PROCESS CONCLUSIONS APPLICATION BULLETIN
350. ecommended Applied Pressure Not applicable Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 25 GPM 5 6 m3 hr Au A Minimum Brine Flow Permeate Flow Ratio 5 1 S ED Maximum SDI 15 minutes 5 0 appro 4 Maximum Turbidity 1 NTU Application Milk Concentration wi EAR AN AN WA MI MIL WI MI it vi VA A KA LEAL l 1 AEN MANU U d M MUM I a Z n AE Element Weight 12 5 4 Length A 39 984 Diameter B 3 8 96 Permeate Tube C 0 83 21 2 Units in pounds and inches units in paranthesis in kilograms and millimetes Dim A does not include ATD Mechanical Configuration Sanitary Style Core Tube ATD not included with element Feed Spacer 0 065 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane EEN SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003
351. ection over time due to many factors If left unchecked this loss of rejection can quickly lead to a loss of system performance that may result in premature replacement of the membrane elements SOLUTION TriPol 1210 is a specially formulated polymer used to increase the rejection of CA elements This polymer can reduce salt transmission by 20 80 with only a 20 30 loss in permeate flow This product is only effective if the membrane surface is clean As a result a complete membrane cleaning should be performed prior to application of the TriPol 1210 polymer TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 TriSep Corporation Chemical Manual APPLICATION TriPol 1210 should be mixed in a cleaning tank equipped with a mechanical mixer heater low pressure recirculation pump and cartridge or bag filter This polymer works best when applied at a flow rate of 8 10 gpm per 4 pressure tube or 30 40 gpm per 8 pressure tube at a pressure of between 20 50 psi Adjust pH to 8 with ammonium hydroxide Add 1 6 gallons of TriPol 1210 per 100 gallons of RO permeate or DI water Recirculate solution for 15 minutes then flush Can also be added in line by injecting 15 25 ppm discon tinue addition of scale inhibitor during dosing Bring system on line and adjust feedwater pH to 5 3 to 6 0 PACKAGING TriPol 1210 is shipped as a liquid in 5 gallon plas
352. ed Composite Membrane Cong AMON uuu aa E oa akana URS Spiral Wound Fiberglass Outer Wrap Active Membrane Area 88 ft 8 1 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 15 7 Length A 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 78 19 8 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Osmo Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Zem 4 ACM RO Element Series TRIS gt CORPORAT
353. eedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION LA N 8 X 20 Low Fouling RO Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 N1P7T6 9 400 35 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane COMMUN ANON EEN Spiral Wound Turboclean Shell with FoulGuard Technology Active Membrane Area 355 ft 32 6 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maxi
354. eedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane ss SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION ZZ 4 X 20 Low Fouling RO Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 N1E6U5 2 400 9 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane Configuration Spiral Wound Turboclean Shell Active Membrane Area 85 ft 7 9 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity
355. eered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TRIS CORPORATION Permeate flow Model GPD m3 day 8 000 30 0 OPERATIONAL AND DESIGN DATA Membrane Type COM QUT AON RE Active Membrane Area Recommended Applied Pressure Maximum Applied Pressure Recommended Operating Temperature Feedwater pH Range Chlorine Tolerance Maximum Feed Flow Minimum Brine Flow Permeate Flow Ratio Maximum SDI 15 minutes Maximum Turbidity Element Weight Length A 50 23 40 0 1 016 Diameter B 8 3 210 PRODUCT SPECIFICATION 8 3 CA RO Element Series Minimum Salt Rejection Average Salt Rejection 8340 SB20 TSOA 98 00 97 00 Performance is based on the following test conditions 2 000 0 ppm NaCl 420 0 psi 25 C 15 recovery pH 5 5 30 minutes operation SB Cellulose Acetate Blend Spiral Wound Fiberglass Outer Wrap 415 ft 38 1 m 200 500 psi 14 34 bar 600 psi 41 bar 50 90 F 10 32 C 5 5 nominal 4 7 0 5 ppm nominal 1 0
356. el Number AG4040F SG4040F HL4040F SG8040F AG8040F HL8040F DuPont Model Number 2440 2840 2840 Comments Same diameter and permeate tube Same diameter and permeate tube Same diameter and permeate tube Same diameter and permeate tube Same diameter and permeate tube TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 2 7 PRODUCT SPECIFICATION Les 4 ACM RO Element Series TRIS gt CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 ACM2 TSDA 2 450 9 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane ei Te D e DEE Spiral Wound Fiberglass Outer Wrap Active Membrane Area 88 ft 8 1 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Rat
357. elow 11 5 for thin film composite elements and below 7 8 for CA elements unless otherwise specified by membrane manufacturer pH may be lowered by adding sulfuric acid TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 340 emm TriSep Corporation Chemical Manual TRIS gt CORPORATION E Isolate first pass to be cleaned With Concentrate and Product Lines diverted to proper drain slowly run cleaning solution through pressure vessels until all remaining water is out of vessels and cleaning solution is coming out of concentrate line Shutdown pump and divert Concentrate and Product lines to cleaning solution tank F If tank volume is now too low mix additional cleaning solution G Start recirculating the cleaning solution through the vessels at specified flow rate or if different at manufacturer s specified flow rate per vessel Pump pressure should be between 20 and 50 psi Recirculate for 1 hour checking pH periodically H Shutdown pump and allow to static soak for 1 hour while cleaning additional passes l Follow same procedure for cleaning additional passes J After soaking recirculate each pass for 20 minutes K Rinse using rinsing method TSR 1 TSC 7 Biological and Organic Cleaning A Clean and fill solution tank with proper volume of RO Permeate Water B Start water recirculating through pump and back into the tank during chemical
358. embrane Area 26 ft 2 4 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 6 GPM 1 4 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 7 3 2 Length A 40 0 1 016 Diameter B 2 5 63 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Zs 4 ACM RO Element Series TRIS gt CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 ACM2 TSA 2 450 9 0 99 50
359. en replicated by the engineering staff at the facility of one of the largest manufacturers of food and dairy processing equipment in North America By pass flows were reduced by up to 50 using the Turboclean element as opposed to standard net or cage wrapped elements TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 35 TurboClean Hot Water Sanitizable I Membrane Elements TRIS S CORPORATION TriSep TurboClean hot water sanitizable HWS membrane elements are designed for use in dialysis pharmaceutical and beverage applications where sanitization is desired without the use of chemical biocides Typical spiral membrane elements are normally sanitized using chemicals such as chlorine or hydrogen peroxide This biocides can contaminate feed streams 1f not properly rinsed from the system TriSep TurboClean HWS elements can be sanitized at up to 85 C to eliminate the need for these chemical biocides Standard brine seal fiberglass wrapped elements FRP form a stagnant area between the outside of the element and the inside of the pressure tube This stagnant area 1s difficult to sanitize and to insure adequate rinse out of cleaning or sanitizing chemicals 4 a ihi Ery Eg i a D Sine The TurboClean element uses a polypropylene shell to allow a small by pass flow around the outside of the element The TurboClean
360. ended solids the SpiraSep should be used rather than the TM10 4040 TM10 QSA 4 0 diameter by 40 long 0 75 male I D permeate tube 4040 TM10 QXA 4 0 diameter by 40 long 0 75 male I D permeate tube 47 mil parallel spacer 4040 TM10 QXF 4 0 diameter by 40 long 0 75 male O D permeate tube 47 mil parallel spacer 8040 TMIO QXA SOT diameter by 40 long 1 50 male I D permeate tube 47 mil parallel spacer TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 254 TRIS gt CORPORATION Model 4040 TM10 QSA PRODUCT SPECIFICATION 4 AMM Microfiltration Element Series Pore Size 0 2 microns Permeate flow is based on the clean water flux at the following test conditions 10 00 psi 25 C pH 8 00 15 recovery 15 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type Configuration Active Membrane Area Recommended Applied Pressure Maximum Applied Pressure Recommended Operating Temperature Feedwater pH Range Chlorine Tolerance Maximum Feed Flow Minimum Brine Flow Permeate Flow Ratio Maximum SDI 15 minutes
361. ensitive polyamide composite membrane elements APPLICATION TriClean 310 should be mixed in a cleaning tank equipped with a mechanical mixer heater low pressure recirculation pump and cartridge or bag filter This cleaner works best when applied at a temperature of 40 45 C a pH of 2 5 to 3 5 and at a flow rate of 8 10 gpm per 4 pressure tube or 30 40 gpm per 8 pressure tube at a pressure of between 20 50 psi Add 5 gallons of TriClean 310 per 100 gallons of RO permeate or DI water Check and adjust pH if necessary Add sodium hydroxide to increase the pH and add more Tri Clean 310 to decrease the pH Recirculate solution for 1 hour checking pH regularly Shutdown pump and allow to soak for 1 hour After soak recirculate for an additional 20 minutes and then rinse PACKAGING TriClean 310 is shipped as a liquid in 5 gallon plastic pails or 55 gallon plastic drums Pricing is F O B our factory in Goleta CA Salem VA or Duisberg Germany Delivery for most orders is 1 2 days after receipt of order MSDS SHEETS For the most up to date information on MSDS sheets please contact our web site at www trisep com TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 328 TriSep Corporation Chemical Manual s TRIS SE CORPORATION TRICLEAN 510 LIQUID CLEANER e Used to remove organic on Polyamide Composite and CA membrane PROB
362. ep POS EL EES 88 6t C ol ISV Aq opeur Anuo opis c omso o JOYS urepo eu1ojXq 68 8c C6 9v CC CVS GN NC ISV Aq ape LC rg CLOTS C6 8C lais LECtS oqnj 9109 dog 76 8c ddd sju oururo Jo3depy 00 0T OAd LL OI JAd TETI OAd ure pejpAH 86 S6 SSrOt dS 84 A08 VOS C9 IT OAd dS 8H A08 VOS OO Ce ouoj nsA od dS 84H H08 V08 00 ST OAd 08 I OAd 00 ST OAd OO FC OAd SV el JAd 09 I OAd VS TI JAd 86 TI OAd Ge OAd SETT OAd 08 I OAd 9c SE OAd 8c rl OAd 00 LI OAd STS JAd OSEI OAd opooeipAH OETI OAd ure oeJpAH 00 07 OAd 00 81 OAd Od 1498 0 41 OAd 08 I OAd 8 HAd CC IT JAd cel OAd 86 86 SSPOE dS 84 A08 VOS 08 I OAd dS 8H H08 VOS CCCI VYA DAd S0O IELIS U N IPPON Jo3depy Jo3depy 9qn L IMSS s19jedpy p aeoqug SUNIA pue ISTI SVG Soruouis Soruouis sonneutJp H Jejuog Te1jon gj S TS V 2UI 9pO Iejuog e1039n m S TS V SUT 9pO Heys TRIN ONS TS V SUI 9DO 291o1d 9qn oursQ TTUIS SUEN SE IIA LINd s e1ourjA PIO ALIO L ooJeuleg sgurp nedg xiuooud sulysng c4 soruouis WS CH SoTuouis cH soruouisO soruouis oxuo q ORIN ozusq ORIN oddeuy sonneutJp H sonneutJp H jue d 8eA9S Yeppor e A1S PIO Surejs S prnq4 dOnysuieis s prn Sepe SOTUDSOIIAU ulogo Iejuog Te1n3onuS 8S V Sur 3po Iejuog e1njon nS TS V 9UT 9
363. equirements In the last five years the range of applications has expanded widely Starting with systems designed primarily for removal of THM precursors color and hardness from low TDS potable and brackish feed waters many innovative combinations are now being offered They are often described by such terms as Integrated Membrane Systems or Hybrid Systems This trend has been greatly accelerated in the potable water field by increasingly stringent regulatory requirements These requirements now require Turbidity NTU and particulate limits that are almost too low to measure as well as lower disinfection byproduct THM and TOC limits NF can make major contributions to waste water recovery and re use in both municipal and industrial applications Increasingly the quality of the reclaimed generally low TDS waters needs to be improved whether for re injection percolation irrigation boilers and other industrial processes The needs to meet increasingly higher standards include 3 6 log reduction of pathogens limits on Turbidity TDS TOC and chlorine demand TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 217 TriSep TS80 TS83 and XN45 Low Fouling LS Nanofiltration Elements TRIS gt CORPORATION At the other end of the applications scale NF is capable of providing many benefits for Sea Water Very High TDS desalination by bot
364. erature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane y SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Zn 8 ACM RO Element Series TRIS gt CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 ACM2 TSDA 9 700 36 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA
365. ered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TriSep XN45 Composite m Nanofiltration Membrane Elements TRIS gt CORPORATION The XN45 membranes are based on proprietary and patented technology developed by DuPont The unique chemistry of this membrane allows it to have lower organic fouling than standard 344 type NF membranes This membrane is not hydrolyzed or oxidized standard ACM type RO membranes but rather is formulated to naturally have the flow and rejection properties of a NF membrane This makes the XN45 more rogbust and have better chemical resistance than a NF membrane that is made by degrading a RO membrane All XNA45 elements are factory tested on MgSO4 and water solutions The XN45 is typically used in process application where there is a desire to allow monovalent ions to pass through the membrane will rejecting divalent ions or low molecular weight organic molecules such as sugars The XN45 has 20 30 rejection of NaCl and 95 96 rejection of MgSO NF is a membrane process which can be applied to the treatment of a variety of water supplies with many economic and process advantages 2540 XN45 TSF 2 5 diameter by 40 long 0 75 O D male permeate tube protruding permeate tube 4040 XN45 TSF 4 diameter by 40 long 0 75 O D male permeate tube protruding permeate tube 8040 XN45 TSA 8 dia
366. erential pressure and a loss of element rejection If left unchecked this fouling can permanently damage the membrane elements leading to costly and premature mem brane replacement SOLUTION TriClean 212TF removes biological organic and colloidal foulants without damaging sensitive polyamide composite membrane elements TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 APPLICATION TriClean 212TF should be mixed in a cleaning tank equipped with a mechanical mixer heater low pressure recirculation pump and cartridge or bag filter This cleaner works best when applied at a flow rate of 8 10 gpm per 4 pressure tube or 30 40 gpm per 8 pressure tube at a pressure of between 20 50 psi at a pH of 11 5 For silica use at a pH of 12 Use caution as pH s above 12 may damage membrane Add 2 lbs of TriClean 212TF per 15 gallons of RO permeate or DI water Recirculate solution for 1 hour checking pH regu larly Use sulfuric acid to lower pH and add addi tional TriClean 212TF or sodium hydroxide to increase pH Shutdown pump and allow to soak for 1 hour After soak recirculate for an additional 20 minutes and then rinse This solution should be used after a low pH cleaning with TriClean 210 except for emulsified oil fouling in which case the order should be reversed PACKAGING TriClean 212TF is shipped as a powder in 4 Ib 10 x 4 Ib 40 Ib and 100
367. erformance This success has allowed the plant to operate 125 under budget for the year TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 361 s TRIS S CORPORATION BULLETIN NO TYPE APPLICATION CLIENT PRODUCTS BACKGROUND could not tual failure of the PROCESS PERFORMANCE CONCLUSIONS APPLICATION BULLETIN X 20 02 Reverse Osmosis Boiler Feedwater Public Utility 8040 X201 TSA Spiral Wound Element X 20 Membrane TriPol 8510 Advanced Antiscalant Solution The system had experienced ongoing problems with biofouling and organic fouling With competitor s membranes the system was being cleaned monthly Cleaning completely restore the element performance and resulted in the even elements The system s delta P ranged from 70 to 100 psi Raw water is supplied from a shallow lake municipal source SDI 6 Conductivity 270 u mho cm Silica SiO 2 5 4 0 mg L Temperature 50 80 F Pre treatment consists of a multimedia filter 5 0 micron and 1 0 micron cartridge filters nominal sodium bisulfite feeder and TriSep s TriPol 8510 Scale Inhibitor System design consists of 2 parallel trains each with a 4 2 array using 6M vessels Each train is designed to produce 100 gpm of product water The introduction of the X 20 elements resulted in dramatic improvements in system performance The elements have
368. ervable Effect Concentration NOEC No Observable Effect Concentration Do not discharge TriStat 110 into lakes streams ponds or public water unless in accordance with a NPDES permit For guidance contact your regional office of EPA Do not contaminate public waters by cleaning equipment or disposal of wastes TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 332 TriSep Corporation Chemical Manual TRIS CORPORATION TRISTAT 410 SANITARY LIQUID BIOCIDE e Sanitary low temperature steril ant e Peracetic acid hydrogen perox ide base e Suitable for dairy food bever age and potable water mem brane applications PROBLEM In many installations worldwide membranes can accumulate and even promote the growth of bio logical organisms This 1s especially problematic for polyamide membranes which cannot tolerate free chlorine If left unchecked these organisms can quickly lead to a loss of system performance associated with a decrease In permeate flow and increase In differential pressure and a loss of ele ment rejection SOLUTION TriStat 410 1s an non chlorine oxidizing biocide effective against a broad range of bacteria molds fungi and yeasts TriStat 410 should be used on a periodic sanitization basis in applications where traditional biocides are unacceptable APPLICATION TriStat 410 should be mixed in a cleaning
369. es Dim A does not include ATD Mechanical Configuration Sanitary Style Core Tube ATD not included with element Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane EEN SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION a 3 8 XN45 High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 3840 N2D8U8 1750 6 0 95 00 92 00 Performance is based on the following test conditions 2000 ppm MgSO4 110 psi 25 C 15 recovery pH 8 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type XN45 Polyamide Advanced Nanofiltration Membrane Configuration Spiral Wound Turboclean Shell Active Membrane Area 70 ft 6 4 m Recommended Applied Pressure Not applicable Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 5 ppm n
370. essure 1000 psi 69 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 95 GPM 22 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 2 NTU PDDIICAUONL cesia Evaporator Condensate Recovery Element Weight 40 18 Length A 40 00 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 047 thick parallel spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane ip SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION lt 8 X 20 RO High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 N1F3S4 7 100 26 0 99 00 98 00 Performance is based on the followi
371. everse osmosis membranes the following equation may be used The reference temperature is 77 F 25 C TCF e U 1 298 1 7 U 2900 ACM X 20 XN40 and TS80 membranes U 2800 SB50 and SB20 CA membranes T C 273 Temperature Temperature Correction Factor by Membrane Type Fahrenheit Celsius SB CA ACM M X 20 XN40 and TS80 35 1 7 0 50 0 44 40 4 4 0 55 0 49 45 7 2 0 60 0 54 50 10 0 0 65 0 60 55 12 8 0 71 0 66 60 15 6 0 77 0 73 65 18 3 0 83 0 80 70 21 1 0 90 0 88 75 23 9 0 97 0 96 80 26 7 1 05 1 06 85 29 4 1 13 1 15 90 32 2 1 21 1 26 95 35 0 1 30 1 37 TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 381 ER Typical Ionic and Organic Rejections TRIS S CORPORATION For TriSep Membranes Nominal Rejection by Membrane Type Constituent Name SALTS MW X 2OTM ACM ACM LP XN45 Sodium Cyanide NaCN 49 95 95 95 80 10 Sodium Chloride NaCl Silica SiO2 60 99 99 99 86 50 Sodium bicarbonate NaHCO3 84 99 99 99 90 30 Sodium nitrate NaNO3 Ia o 98 Magnesium chloride MgCl 95 997 99 99 93 60 Calcium chloride CACI2 111 99 99 98 95 60 Magnesium sulfate MgSO4 im T 99 E88 9 Calcium Sulfate CaSO4 135 99 oo 99 98 Nominal Rejection by Membrane Type Constituent Name Specific Ions MW X 20TM ACM ACM LP TS
372. feed water at a point where turbulent flow will ensure adequate chemical mixing prior to entering the RO or NF system This is usually done prior to the cartridge filters and high pressure pump Dosing rates vary depending on feedwater quality and recovery but normally run between 2 and 6 ppm For exact dosing use the latest version of TroiWin TriPol 7510 also acts as a dispersant and can be used if there are iron or other metal hydroxides in the feedwater Since this product is anionic In nature care should be taken when using cationic polyelec trolytes in the pretreatment system PERFORMANCE Max Langlier Saturation Index 2 0 Max CaSO4 Saturation 300 Max SrSO4 Saturation 800 Max BaSO4 Saturation 10 000 Max CaF Saturation 8 000 Max CaPO Saturation ELO Silica 100 in the concentrate Levels may be exceeded on occasion Contact TriSep for advice PACKAGING TriPol 7510 is shipped as a liquid in gallon sample sizes 5 gallon 40 Ib plastic pails and 55 500 Ib gallon plastic drums Pricing is F O B our factory in Goleta CA Salem VA or Duisberg Germany Delivery for most orders 1s 1 2 days after receipt of order MSDS SHEETS For the most up to date information on MSDS sheets please contact our web site at www trisep com 312 wm TriSep Corporation Chemical Manual LA A pene TRIS gt CORPORATION APPLICATION TriPol 8510 is metered into the feed water at a TRIPOL 8
373. file You can also print the individual element report from the File menu either in preview or directly to the printer It may take several seconds to load the report generator To get to the second page of the report click on the right arrow button at the top of the screen To get back to the first page click on the left arrow button To scroll through the report click in the scroll bars on the right hand side of the screen or drag the status bar down the page To send the output to a printer click on the printer icon at the top of the page A print window will then pop up indicating the default printer that the report will be sent to If this is not the printer you wish the output to go to exit the report by clicking on the X at the upper right corner of the screen and click on File Printer Setup to select your desired printer This pops up the standard windows printer selection window to allow you to select any printer that is installed on your system If the printer is correct you can specify to print all the pages or a range of pages the number of copies you want to print and whether the pages are collated or not When you have made these selections click OK to begin the printing process If you wish to save the print out to a file for transmission by e mail or to edit it in a text editor the best way is to purchase Adobe Acrobat and print it to a PDF file If you do not have this program click on the inbox button which looks like an en
374. first treated with SpiraSep 950 UF membranes which remove all particulate matter as well as water born microorganisms Effluent from the UF membranes is treated with UV light which provides a combination of both oxidation and reduction processes allowing for effective breakdown of organic compounds For additional information please visit www TriSep com or e mail sales trisep com he Results The 0 03 um membrane reduces turbidity to 0 1 NTU and achieves a 6 log reduction of bacteria An unexpected benefit of the UF system is that the membrane aeration process is able to strip volatile organic compounds VOCs from the water further improving the water quality The UF membranes are sanitized weekly at 80 C 176 F Measured chlorine residuals in the pool water are 1 mg l Figure 1 SpiraSep 950 system s TRIS S CORPORATION BULLETIN NO TYPE APPLICATION CLIENT PRODUCTS BACKGROUND PROCESS PERFORMANCE CONCLUSION APPLICATION BULLETIN X 20 01 Reverse Osmosis Boiler Feedwater Zero Discharge Cogeneration Plant 8040 X201 TSA Spiral Wound Element X 20 Membrane This plant had a history of severe biofouling With the previous manufacturer s elements the system needed to be cleaned every 2 to 3 days based on high Delta P s and a drop in normalized product flow The performance of these elements had steadily declined over time City water feed with
375. fite This solution may cause mild eye irritation and allergic skin reaction Avoid contact with eyes skin and clothing Wash thoroughly after handling Refer to the Material Safety Data Sheet for winterizing solution for details Bags must be opened in a well ventilated area FirstAid In case of eye contact immediately flush eyes with plenty of water for at least 15 minutes Wash skin with soap and water Contact a physician if symptoms persist Follow chemical manufacturer s labeling instructions and warning carefully for any chemical used with the TRISEP elements and or pressure vessel system FLUSHING OF ELEMENTS Prior to operation all new elements and stored elements containing sanitizing solution must be flushed with chlorine free water meeting all RO Guidelines at the brine reject flow rates shown in Table Table RECOMMENDED FLUSHING RATES ELEMENTS Diameter Minimum Brine Rate Pressure Minimum Quantity of Product Element Element Size Inches Vessel gpm lpm Gallons liters 2540 2 5 1 5 1 83 75 284 4040 4 0 5 0 19 0 145 550 8040 8 0 15 0 56 8 500 1893 8060 8 0 18 0 68 2 500 1893 8340 8 3 15 0 56 8 500 1893 8540 8 5 18 0 68 2 500 1893 1 RO feedweater must meet the requirements as detailed in TriSep document Guidelines of Operation and must be chlorine free TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703
376. for all feedwater conditions Individual element s permeate flow may vary 1596 Engineered Membrane nu Y SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION ow NN 8 ACM LP Low Pressure RO Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 M4E6X2 15400 58 0 99 00 98 00 Performance is based on the following test conditions 2000 ppm NaCl 225 psi 25 C 15 recovery pH 8 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM LP Fully Aromatic Polyamide Low Pressure Advanced Composite Configuration Spiral Wound Turboclean Shell Active Membrane Area 390 ft 36 3 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes
377. g 00v 0 MG8 GOU MN OvVOV OEMd 99 Luul d MOG VOSL cINDV 0VE8 VMf cINDV 0vV08 VS L NOV 0r08 4S L INOV 0r0tr TAGOW d3aSslal INANAIV 1d 1dl SOLIDS u eiqui lN J9 eM USryoeJg AGINDS LNAWSAOV 1d3s AAILILAdINNOD TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com e 0105 s ys uorneoiimeds JONpOJd pue sjueuijeJinbaJ uonoeuuoo 10J 921AJ9S JAWOISND uoneJodJjo degu 1961002 seiquuesse 9je d pue Buisnou o Burpeuuoo io sio depe pue jonpoud pjeoqui suinbses Aew sjapow jueuje2e doJ uoneJodJo2 degu 91oN cod 0r09 i I OvOY mm OM 39 Iseind OPOF LO31 3JAS1 L0ZX 0r0r T3qOM d3SI31 FSBREBEIDAH 9eju og JANSSEN S9IJ9S oueJquie N ON Duir jno Jj M07 suiejs S pin 43 HOO soOiuouuso 35 Vd 3H L19 VWd AH LLS VOSL ZINDV 0VES VdO AH 1 0708 Vd AH T 0v08 00r3J0r09SV Vd 00v 0 9S OP V 0 Mg 00v 0 M 8 J10cZ n s Elie 0 v 0cZIN L 00v 0cZIN L d 16288 YH6C88 OOV YH cc88 VMN ZINDV 0708 00r Vd dH SL9 d 1L 09 ANE 0 nS 0 c 0 NLl 10 Z NS OLL NS OLZIN L CORPORATION dilc88 dcc88 S9 HH cc88 dilc8v dHOcCSY YH Legt YH OVO swajshs pinid HOO Vd d4H S L 9 Vd dH S L 9 Vd dH L Lv Vd IH L Lf Vd dH r Lt Vd HH v LV sOluouuso 39 EISE 3J0F08SV 34 40r0rS9S 34 43d0F0rSV CVdO AS T 0v08 oN dO CVdO VH T 0vOY OvOv CVdO sonneueJp H GOU MO OvOV
378. g are vital for successful troubleshooting at this level Also critical is the accuracy of the instrumentation It cannot be over emphasized that before troubleshooting any plant problem the good working order and proper calibration of meters and gauges must first be assured Mara indicating Sampla P Lecalians A crd H Ses igra 2 U Appro mately 1 4 Tubing A Brush Gage 2Al 1ruiesp Shee or osiic bo deg inser lier Figura 1 Praduci Sampling Probe When analysis of the system indicates high salt passage for a particular vessel product conductivity measurements are made for each element to locate the source of the problem Measurements are made by probing the element product water tube at different locations with a plastic or stainless steel tube A product sampling probe is illustrated in Figure 1 Product Sampling Probe The probe can be marked so that the location of the marks correspond to the desired sampling locations in Figure 2 Element Sampling Locations The probe is first inserted to the downstream end of the product water tube to obtain a sample for conductivity measurements It is then withdrawn in increments to obtain a coductivity profile TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 391 TriSep Engineering Manual Y TRISS CORPORATION Feed Frnridici 54 Sompe Point A F sample Point B Downstream M Upstream af el interconnacio
379. ght 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane Sane s hi SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Za 8 X 20 Low Fouling RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 X201 UWAN 10 400 39 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane eidele e EE Spiral Wound Fiberglass Outer Wrap with FoulGuard Technology Active Membrane Area 400 ft 37 2 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature
380. gineered Membrane ku nF I Y i SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION lt 8 ACM RO High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 M2D684 7 200 27 0 99 00 98 00 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane CONTI EE Spiral Wound Turboclean Shell Active Membrane Area 270 ft 24 8 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 95 GPM 22 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Application
381. h degree of sulfate scale inhibition This high tech scale inhibitor contains a blend of an acrylic acid co polymer and an organic phosphonate that gives a high degree of protection especially with high levels of saturation of sulfate scales TriPol 9010 is approved by NSF for use in drinking water at feed concentration of up to 10 ppm TriPol 9110 TriPol 9110 is a high performance scale inhibitor and dispersant that provides the highest level of calcium phosphate scale inhibition commonly found in tertiery waste re use systems that incorporate reverse osmosis systems Developed with a complete understanding of the proprietary membrane chemistries TriPol 9110 is 100 compatible with all membrane types TriPol 9510 TriPol 9510 is a high performance scale inhibitor and dispersant that provides the highest level of silica dispersion as well as excellent control of mineral scales colloids and metal oxides Developed with a complete understanding of the proprietary membrane chemistries TriPol 9510 is 100 compatible with all membrane types TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax e www trisep com 9 00 309 emm TriSep Corporation Chemical Manual u duc TRIS gt CORPORATION Maximum Saturation Allowances for TriPol Antiscalants AntiScalant Maximum Maximum Maximum Maximum Maximum Maximum Maximum Maximum LSI CaSO SrSO 4 BaSO CaF gt Silica CaPO Fe Mn 76
382. h membrane and thermal distillation processes Sea Water contains significant concentrations of bicarbonate alkalinity and divalent ions including magnesium sulfate and calcium For both membrane and thermal systems to achieve higher recoveries one must add acid and or antiscalant The use of these chemicals and controlling their dosage can often present major problems in operation such as brine disposal and biogrowth problems The use of NF as a first stage of a two stage Seawater Membrane System or a NF Distillation Hybrid system means that the second stage be it reverse osmosis or distillation can operate at maximum recovery generally significantly above those ordinarily attainable but with little or no chemical dosing or other pretreatment In addition there is some reduction in the TDS of the feedwater and less fouling of the downstage process TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 218 s TRIS S CORPORATION TriSep TS80 and TS83 Composite Nanofiltration Membrane Elements The TS80 and TS83 nanofiltration NF membranes are based on proprietary and patented technology developed by DuPont The unique chemistry of these membranes allow them to have lower organic fouling than standard 344 type NF membranes These memebrnaes are not hydrolyzed or oxidized standard ACM type RO membranes but rather are formulated to naturally have the f
383. h sides of a semipermeable membrane at equal pressure and tempreature no net flow occurs across the membrane since the chemical potential 1s equal on both sides If a soluble salt is added on one side of the membrane the chemical potential of the water on that side is reduced Osmotic flow from the pure water side to the salt solution side will occur across the membrane Figure a Osmotic Flow until equilibrium of solvent chemical potential is restored The thermodynamic requirement for osmotic equilibrium is that chemical potential of the solvent should be the same on both sides of the membane No such condition 1s imposed on the solute since the membrane prevents its passage Equilibrium occues when the pressure differential from the volume changes on the two sides is equal to the osmotic pressure Figure b Osmotic Equilibrium a solution property which is independent of the membrane The application of external pressure to the solution side which equals the osmotic pressure will also accomplish equilibrium A further increase in pressure will increase the chemical potential of the water in the solution and will cause a reversal of the osmotic flow toward the pure water side Figure c Reverse Osmosis now at a lower solvent chemical potential relative to the solution This een is termed reverse osmosis and is the basis for a precess to desalinate water without phase change The mechanism by which osmosis reverse Osmosis occurs across a semipermeabl
384. h the concentrate and permeate into the drain for 30 minutes to insure adequate flushing of the preservative solution After the system has stabilized take a full set of performance readings TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 386 TriSep Engineering Manual TRIS gt CORPORATION INS TALLING REMOVING ELEMENTS ELEMENT DISPOSAL Dispose of elements by burying in accordance with locally acceptable landfill regulations Do not incinerate USE OF PRODUCT WATER AND DISPOSAL OF BRINE WATER Check local and all applicable health regulations for standards regarding potable water and follow local and all applicable standards regarding effluent discharge CAUTION Follow manufacturers recommendations on containers or in product bulletins for the safe handling of all chemicals and cleaning agents used with TriSep reverse osmosis products The information contained herein is based upon technical data and tests which we believe to be reliable and is intended for use by persons having technical skill at their discretion and risk Since conditions of use are outside TriSep s control we can assume no liability for results obtained or damages incurred through the application of the data presented This information is not intended as a license to operate under or a recommendation to infringe any patent of TriSep or others covering any material or us
385. han dling and mixing powders is undesirable TRICLEAN 217 TriClean 217 can be used to remove manganese dioxide or sulfate scale when used in conjunction with TriClean 211 TRICLEAN 218 TriClean 218 1s a liquid high pH cleaner espe cially formulated for use In the dairy and food industry where daily high pH cleanings and saniti zations are required TRICLEAN 310 Liquid version 40 concentration of TriClean 210 TRICLEAN 510 Cleaner and sanitizer for removing organic material 317 TriSep Corporation Chemical Manual TRIS gt CORPORATION TRICLEAN 210 LOW PH POWDER ACID MEMBRANE CLEANER e Removes iron and metal hydroxide fouling e Removes calcium carbonate scale PROBLEM In many installations worldwide RO membranes can become fouled with calcium carbonate scale and or iron and other metal hydroxide colloids These foulants can quickly lead to a loss of system performance associated with a decrease in permeate flow and increase In differential pres sure and a loss of element rejection If left unchecked this fouling can permanently damage the membrane elements leading to costly and pre mature membrane replacement SOLUTION TriClean 210 removes calcium carbonate scale and iron and metal hydroxide colloids without damaging sensitive polyamide composite mem brane elements Used after a system has exhibited performance loss or as a preventative mainte nance cleaning TriClean 210 sho
386. he Guidelines for Operation of Spiral Wound Elements attached b Fouling and or Scaling d the elements that cause system and or membrane element failures and or damage and or loss of element performance c Physical abuse or misuse of element s c Faulty installation of element s d Alteration of any parts originally supplied by TriSep with element s 5 2 Standard Guidelines All element Warranties are conditioned upon TriSep s determination that shipping storage system design installation operation and maintenance of elements are in accordance with all Guidelines specified by TriSep in the attached Guidelines for Operation Any reviews of system design or inspections of facilities made by TriSep are intended to assist in detection of system faults to subsequently cite matters which were not discovered in such reviews or inspections as violations of Guidelines voiding warranties hereunder 5 3 Additional Equipment TriSep assumes no liability for any additional equipment that may be deemed necessary after plant operation has begun including materials equipment and labor required to install additional elements or pressure vessels 5 4 Warranty Maintenance To maintain the Warranty described herein plant operating records from initial start up date of claim must be maintained and made available to TriSep upon request Documentation must be provided in the detail as specified in 5 5 Below in order to a Verif
387. hen applied at a Aggressive cleaner used to flow rate of 8 10 gpm per 4 pressure tube or 30 40 gpm per 8 pressure tube at a pressure of dee biological SRL MES and between 20 50 psi at a pH of 11 5 for polyamide colloidal fouling on Polyamide membranes and7 8 for CA membranes Add 1 1 Ibs Composite and CA membrane of TriClean 213 per 25 gallons of RO permeate or DI water Recirculate solution for 1 hour check PROBLEM ing pH regularly Use sulfuric acid to lower pH and add additional TriClean 213 to increase pH Shutdown pump and allow to soak for 1 hour After soak recirculate for an additional 20 minutes and then rinse In many installations worldwide polyamide com posite RO and NF membranes can become fouled with biological organic and colloidal foulants These foulants can quickly lead to a loss of system performance associated with a decrease in perme ate flow and increase in differential pressure and PACKAGING a loss of element rejection If left unchecked this IniClean 213 1s shipped as a powder in 40 Ib and fouling can permanently damage the membrane 100 Ib plastic containers Pricing is F O B our elements leading to costly and premature mem factory 1n Goleta CA Salem VA or Duisberg brane replacement Germany Delivery for most orders is 1 2 days after receipt of order SOLUTION TriClean 213 removes biological organic and col MSDS SHEETS loidal foulants when other conventional cleaners Fo
388. icable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Za 8 TS80 Nanofiltration Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 TS80 UWAN 10 000 37 0 99 00 97 00 Performance is based on the following test conditions 2 000 0 ppm MgSOA 110 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ANM Aromatic Polyamide Advanced Nanofiltration Membrane eidele e EE Spiral Wound Fiberglass Outer Wrap Active Membrane Area 400 ft 37 2 m Recommended Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 4 0 Maximum Turbidity
389. icult to predict the rinse out time for these chemicals Standard net wrap sanitary elements have traditionally been used In food and dairy applications Due to the high by pass flow inherent with these designs food and dairy systems incorporate large recirculation pumps to insure a certain minimum flow through the elements These net wrap elements cannot be used in standard 2 1 arrays normally used in water applications The Turboclean element minimized by pass flow to 15 20 of the feed flow This allows the TurboClean element to be used in standard water type applications like dialysis water make up Following are some TriSep TurboClean elements specifically engineered for the dialysis make up water market TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 54 s TRIS gt CORPORATION Permeate flow GPD m3 day Model 3840 N1P3U8 1 750 6 0 PRODUCT SPECIFICATION 3 8 X 20 RO High Temperature Turboclean Element Minimum Salt Rejection Average Salt Rejection 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type CONT GQUPAU OM m Active Membrane Area Recommended Applied Pressure Maximum Ap
390. idual carboxylic acid groups on the surface which have a negative charge Improvements in the 344 membranes have resulted in high flux and high rejection membranes However one of the major problems with the 344 membranes is that they are very susceptible to organic and particulate fouling which results 1n decreased performance and increased operating costs Developed by DuPont and commercialized by TriSep a new fouling resistant RO membrane chemistry was created with the X 20 This new RO membrane commercially known as the X 20 has a different barrier layer which is classified as a fully aromatic polyamide urea This new barrier layer which has residual amino groups on the surface which are neutral at most operating pH s has proven superior in critical areas of reverse osmosis operation including fouling resistant property This property represents a major breakthrough in RO technology The X 20 has been so succesful that many competitors have tried to imitate it These imitations are typically standard 344 membranes with a surface coating The X 20 s low fouling characteristics come from it s unique and patented poly amide urea chemistry This property is built into the polymer backbone and cannot wash off The surface coatings on competitive products lack the durability of the X 20 In summary the benefits seen in system performance when using the X 20 spiral wound elements include significantly lower organic fouling consisten
391. ies TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 ACM2 TSF 2 400 9 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane ele Lett GIOI uu uuu u carte eb T m Spiral Wound Fiberglass Outer Wrap Active Membrane Area 85 ft 7 9 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 15 7 Length A 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean wa
392. ife The system array recovery and instrumentation and the design parameters and components of the system in which the elements s are employed shall be consistent with sound engineering practice TriSep reserves the right to review system design BIOLOGICAL MATTERS e Biological activity inside the element must be controlled during operation so that system water quality and quantity are not affected CHLORINE BROMINE e The total free chlorine and bromine content of all water entering the X 20 ACM TS80 XNASIM element s must be 0 1 mg l The total free chlorine and bromine content of all water entering CA UE10 UE50 and TM10 element s must be lt 1 0 mg l Total free chlorine tolerance for the X 20 and ACM membranes are 1000 ppm hrs when exposed at concentrations less than 1 ppm in the absence of trivalent metals ions on the surface of the membrane The presence of trivalent metal ions such as ferric hydroxide may reduce the oxidation tolerance substantially of all membranes MISCELLANEOUS CHEMICALS e Chemicals which form a water immisible phase in the RO feed or brine must not enter the element Use of cationic anionic or non ionic polyelectrolytic compounds in elements is not permitted unless prior written approval is given by TriSep All water entering the element must be free of strong oxidants such as H505 03 KMn0 CH CO3H Impurities present in chemicals added to the RO feed water
393. igher solute concentration at the membrane surface than in the bulk stream on the membrane surface Reduction of concentration polarization is directly related to cross flow rates in the membrane element Following are a list of TriSep TurboClean products specifically designed for the dairy industry TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 66 PRODUCT SPECIFICATION A NI 3 8 ACM High Temperature Turboclean RO Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection 94 Rejection 94 3838 M2D U8 1700 6 0 99 50 98 50 Performance is based on the following test conditions 2000 ppm NaCl 225 psi 25 C 15 recovery pH 8 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Configuration Spiral Wound Turboclean Shell Active Membrane Area 68 ft 6 2 m Recommended Applied Pressure Not applicable Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Fee
394. iguration Sanitary Style Core Tube Feed Spacer 0 045 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane Ker SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Lum 3 8 XN45 High Temperature Turboclean Element TRI CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 3838 N2F6U8 1700 6 0 95 00 92 00 Performance is based on the following test conditions 2000 ppm MgSOA 110 psi 25 C 15 recovery pH 8 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type XN45 Polyamide Advanced Nanofiltration Membrane Configuration Spiral Wound Turboclean Shell Active Membrane Area 68 ft 6 2 m Recommended Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 5 ppm nominal 1 0 ppm max Maximum
395. ilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane Sane s hi SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Zum 8 ACM LP Low Pressure RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 ACM5 TSAN 11 900 45 0 98 50 97 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 150 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM LP Fully Aromatic Polyamide Low Pressure Advanced Composite Cong AMON uuu aa E oa akana URS Spiral Wound Fiberglass Outer Wrap Active Membrane Area 365 ft 33 5 m Recommended Applied Pressure 50 300 psi 3 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance
396. imum Salt Model GPD m3 day Rejection Rejection 8040 N1P4X8 6 500 24 0 99 00 98 00 Performance is based on the following test conditions 2 000 00 ppm NaCl 225 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane COMMUN AU OM EEN Spiral Wound Turboclean Shell with FoulGuard Technology Active Membrane Area 250 ft 23 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 95 GPM 22 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 2NTU Application General Pharmaceutical Element Weight 40 18 Length A 40 00 1 016 Diameter B 7 90 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Sp
397. inimum Brine Flow Permeate Flow Ratio 5 1 V S y N Maximum SDI 15 minutes 5 0 APPROV d Maximum T urbuditv 1 NTU APPIA UON eee tesco eire A Milk Fractionation Element Weight 30 14 Length A 38 965 Diameter B 7 9 200 Permeate Tube C 1 14 29 0 Units in pounds and inches units in paranthesis in kilograms and millimetes Dim A does not include ATD Mechanical Configuration Filmtec Style Core Tube ATD not included with element Feed Spacer 0 065 thick diamond spacer Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Lo N 8 AUM Ultrafiltration Turboclean Element Series TRIS CORPORATION Model M W C O 8038 N6D4V8 10 000 OPERATIONAL AND DESIGN DATA Membrane Type AUM Advanced Ultrafiltration Membrane Configuration Spiral Wound High Temperature Turboclean Shell Active Membrane Area 355 ft 33 0 m Recommended Applied Pressure Not applicable Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tole
398. inse using rinse method TSR 1 TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 339 emm TriSep Corporation Chemical Manual TRIS gt CORPORATION TSC 3 High pH Cleaning for Thin Film Composite Elements Powder A Clean out solution tank and add appropriate volume of RO Permeate Water B Start water recirculating through pump and back to tank C Add 2 pounds of TriClean 212TF per every 15 gallons of water in tank Recirculate until completely dissolved D Check pH of solution Range should be between 10 5 and 11 5 unless otherwise specified by membrane manufacturer pH may be raised by adding additional TriClean 212TF or lowered by adding sulfuric acid E Displace water in vessels by diverting Concentrate and Product lines to an appropriate drain and slowly pumping solution into vessels until it is visible coming from the Concentrate line Shutdown the pump and divert Concentrate and Product lines back to cleaning solution tank F Recirculate solution through vessels at appropriate flow and pressure for 30 minutes G Shutdown pump and allow to static soak for 1 hour H Clean additional passes in the same manner while first pass soaks l After soaking recirculate each pass for 30 minutes J Rinse using rinsing method TSR 1 TSC 4 High pH Cleaning for Cellulose Acetate Elements Powder A Clean out solution tank and add appropriate volum
399. io 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 15 7 Length A 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 62 15 9 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Desal DuPont Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION _ h 4 TS80 Nanofiltration Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 TS80 TSDA 2 000 7 0 99 00 97 00 Performance is based on the following test conditions 2 000 0 ppm MgSOA 110 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ANM Aromatic Polyamide Advanced Nanofiltration Membrane ONTO ON I uu aan wa Spiral Wound Fiberglass Outer Wrap Active Membrane Area 88 ft 8 2 m Recommended Applied Pressure 40 200
400. ion divert Concentrate and Product lines to appropriate drain Thoroughly rinse out solution tank and fill with RO Permeate or Deionized water C Start pump and begin rinse water through vessels D Rinse for a minimum of 20 minutes E Test pH of water in solution tank and then test pH of Concentrate water F When both pH readings are similar rinse one more tank volume of water through vessels G Rinse additional passes in the same manner H Shutdown pump and go on to next cleaning method or if cleaning is complete go to rinse method TSR 2 TSR 2 RO Start Up A Return RO manifolds to normal operating configuration B Divert Concentrate and Product lines to drain C Start water flowing through RO at city water pressure only DO NOT START PUMP D Allow water to flow through vessels for a minimum of 15 minutes and until all air is out of the system E Start RO pump and adjust pressures and flows to normal operating perameters F Flush to drain for a minimum of 30 minutes G Test pH or Conductivity of Concentrate and Product waters and compare to pre cleaning readings H When pH or Conductivity is similar to pre cleaning readings shutdown RO pump and divert Concentrate and Product lines back to normal operating configuration Restart RO Note Unless otherwise noted in Cleaning Method or recommended by membrane TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax e www tri
401. is bal anced If the analysis is not balanced within 1 a message box will pop on the screen asking if you want to automatically balance the analysis edit it manually or cancel If you click on yes the program will automatically balance the water analysis by either adding sodium Na or chloride Cl to the water analysis depending on whether the analysis requires cations or anions to balance If you click on No you can manually adjust the analysis and then recalculate Note The values of pH Temp and HCO3 will affect the values of CO2 and CO3 So if pH Temp and HCO3 are changed this will affect the anion total In addition to balancing the cations and anions the calculate button also calculates saturation indices the total dissolved solids TDS and the feedwater osmotic pressure in either psi or bar We have added calcium fluoride saturation indexes to version 2 0 0 We have also modified the calculation for silica saturation to include temperature and pH in the calculation TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 398 TriSep Troi Design Program A Manual ver 2 0 0 TRIS CORPORATION Open Analysis When this option is selected you will be prompted to select a file from a drop down list of entered analysis Click on the analysis you wish to edit and then click on OK Alternatively you can double click on the analysis tha
402. is in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Lum 4 X 20 Low Fouling RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 X201 TSA 2 450 9 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane elle e EE Spiral Wound Fiberglass Outer Wrap with FoulGuard Technology Active Membrane Area 88 ft 8 2 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance
403. is section is a copy of our competitive element replacement guide to help you in selecting the proper TriSep element for your element replacement needs TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 347 s ys uomneoiioeds JONpOJd pue si u ui uinb i uornoeuuoo 10J 921AJ9 S JAWOISND uoneJodJjo 2 degsu 19e1u02 sei quiesse ejejd pue Buisnou o Dunoeuuoo 104 sJo1depe pue jonpoud pjeoqui uinb i Aew sjapow jueujeo2e do J uoreJjodJo2 degu 91oN 348 000 02 INL OZE 0 TNL EUM J10cZ n s AOCL NS 0 v 0cZIN L 00v 0cZIN L UNE 0 nS 02 0cZIN L 10 Z NS OLL NS OLZIALL TRIS CORPORATION suu s S pin 3 HOO d 16c88 dH6c88 00vr HH cc88 d 1L 09 dilc88 d cc88 S9 HH cc88 diic8v YHOC8P YH L ck YH Otot suu s S pinid HOO SOIUOWSO 39 Vd SH 1 48 Vd d4H L L9 00t Vd HH SL8 Vd 4H S18 Vd HH SL9 Vd dH L Lv Wd YH LLY Vd dH rL t Vd HH v LV So9Iuouiso 39 OM Ov 08 oror OM 33 Iseinqd UO ZOO J0r09S9S 3J0r08SV 34 40Fr0rSS 34 4d0F0rSV yorseing YsAS9E OEMad 99 Luul d MOG 031 M L947 Y00r 0emg WMN 10ZX 0708 sonneueJp H VS1 L02X 0708 JS L L0ZX 0r0t TAGOW d3aSslal INANAIV 1d321 SOLIDS ueilqui lN ON Buiinod MO VdO AH 1 008 vd AH T 0v08 eVdO CVdO AS T 0v08 Vd CWdO VH T 0r0r OvOV cVdO sonneueJp H 00v 0 9S OP V 0 M8
404. isions must be made to permit installation and operation of at least 10 additional pressure vessels calculated to meet design capacity A thrust ring must be used on the last element in a pressure vessel The pre treatment system must be designed to prevent irreversible organic and or inorganic fouling of the membrane Cleaning shall be initiated at 10 to 15 normalized product flow decline a 15 to 20 increase in normalized system delta P or a 20 decline in normalized salt passage OPERATING CONDITIONS TEMPERATURE AND PRESSURE The product pressure must never exceed the feed or brine pressure The maximum temperature for operation of the element is 45 C For operation outside this limit consult TriSep In all stages the ratio of the brine flow to the product flow must be at least 5 0 per element At all times e g operation cleaning flushing and post treatment the maximum pressure drop per pressure vessel is 60 psi or 15 psi per element whichever is less as determined from routine monitoring on a representative sampling of pressure tubes per stage and per train The elements shall not be exposed to pressure greater than 1000 psi for seawater elements and 600 psi for brackish water elements OPERATING CONDITIONS FLOW RATES Min Brine Max Feed Model No l min gpm l min gpm 4 19 0 5 0 75 6 20 0 8 57 15 0 303 80 0 8 5 57 15 0 322 85 0 TriSep Corporation 93 S La Patera Lane Goleta CA 9
405. items used in the purification and distribution of water The 8040 TS82 TSA membrane element from TriSep is KIWA ATA approved for use in producing drinking water by nanofiltra tion TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 259 TriSep NSF Standard 61 Element Listing RISES CORPORATION NSF ANSI STANDARD 61 Drinking Water System Components Health Effects NOTE Unless otherwise indicated for Materials Certification is only for the Water Contact Material shown in the Listing Click here for a list of Abbreviations used in these Listings Water Water Contact Contact Trade Designation Size Temp Material Reverse Osmosis Element 8040 ACM2 TSAN 1 2 NA CLD 23 MLTPL 8040 ACM2 UWANL 1 2 NA CLD 23 MLTPL 8040 ACM3 TSAN NA CLD 23 MLTPL 8040 ACM3 UWAN NA CLD 23 MLTPL 8040 ACMA TSANT 1 2 NA CLD 23 MLTPL 8040 ACM4 UWAN 1 2 NA CLD 23 MLTPL 8040 ACM5 TSAN NA CLD 23 MLTPL 8040 ACMS UWAN NA CLD 23 MLTPL 8040 TS80 TSAN 1 2 NA CLD 23 MLTPL 8040 TS80 UWANTI 2 NA CLD 23 MLTPL 8040 TS83 TSAN NA CLD 23 MLTPL 8040 TS83 UWAN NA CLD 23 MLTPL 8040 X201 TSAN 1 2 NA CLD 23 MLTPL 8040 X201 UWANL 1 2 NA CLD 23 MLTPL 8040 X20LP TSAN NA CLD 23 MLTPL 8040 X20LP U WAN NA CLD 23 MLTPL 1 2 TRISEP CORPORATION 93 SOUTH LA PATERA GOLETA CA 93117 805 964 8003 Facility GOLETA CA Mechanical Devices Certified for a mini
406. ith FoulGuard Technology Active Membrane Area 355 ft 32 6 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 2 NTU 7 16 0 0121 0 u u nee ee Ultra Pure Water n wo c P m EC od gem KO AT VOIE p N Se aa GC TIE Element Weight 45 20 Length A 40 00 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 1596 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TRIS gt CORPORATION Permeate flow Mode
407. ith the membrane surface providing a scrubbing action due to the high shear rate generated by the liquid gas interface This air lift mechanism not only removes particulate matter from the membrane surface but also purges solids from the element itself Solids are scoured from the membrane surface Air and feedwater travel up through the element w TRI CORPORATION Triseo Corporation A Crystal Clear Solution Advantages of Ultrafiltration UF vs Conventional Pre Treatment Technologies The Challenge For years conventional water treatment technologies such as clarifiers and multimedia filters have been unable to produce high quality effluent consistently especially with poor quality water sources When used for reverse osmosis RO pre treatment conventional treatment technologies often provide poor removal of particulate matter leading to excessive RO membrane fouling Frequent and rapid RO fouling dramatically increases the life cycle costs of a water treatment plant RO membrane life is reduced and cleaning frequency increased when feed water quality declines The high membrane replacement cost and chemical consumption make it difficult to justify the use of a Clarifier or multimedia filter as the main pre treatment technology Conventional treatment technologies also require large footprints occupying valuable space in your facility In the case of clarifiers sludge disposal costs ar
408. itions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TM10 PVDF I Microfiltration Elements TRIS CORPORATION The TM10 microfiltration membrane from TriSep is a 0 2 mircon nominal pore size membrane made from polyvinylidene flouride PVDF This membrane offers very high specific flus rates 5 gfd psi 120Imh bar with a uniform pore distribution This membrane is characterized using a particle counter and bubble point testing This membrane is excellent for removal of suspended solids Dissolved inorganic and organic materials are not rejected by this membrane Typical applications include removal of oocysts such as giardia and cryptosporidium from drinking water pretreatment of surface or wastewaters prior to an RO system or clarification of process and food streams The PVDF chemistry of the TM10 membrane has excellent thermal and chemical properties The mem brane with the appropriate element construction can operate at temperatures of up to 165 F 75 C and over a wide range of pH s 2 12 The membrane is resistant to a wide range of oxidants and can tolerate up to 1 000 ppm of chlorine The TM10 membranes are not back flushable membranes like the UB50 membrane used in the SpiraSep For applications with high loadings of susp
409. itions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Ow NN 8 X 20 RO High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 N118S4 7 100 26 0 99 00 98 00 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane COMMUN ANON EEN Spiral Wound Turboclean Shell with FoulGuard Technology Active Membrane Area 270 ft 24 8 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 95 GPM 22 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes
410. ization program that allows users to create normalized data for flow rejection and differential pressure in a graphical format This allows operators to easily determine if systems are operating at a steady condition Both these programs are available at no charge either by downloading from TriSep s web site or on the TriSep CD TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 394 TriSep Troi Design Program A Manual ver 2 0 0 TRIS CORPORATION 1 INTRODUCTION Welcome to TriSep s Reverse Osmosis Implementation Windows TROIWIN software TROIWIN is an easy to follow straight forward approach to helping you design the water purification system that meets your needs Before the system can be designed and analyzed TROIWIN must have an accurate analysis of your raw water These can be obtained by contacting your local water district or sending a sample of your water to a reputable lab for analysis Just a quick note on terminology At TriSep we use the term pass and stage differently from some other people in the industry In strict chemical engineering terms a stage indicates a change of phase such as in a distillation column We have adopted this same terminology So in our manual and our program a pass indicates a feed brine stage For example a 2 1 array would be a two pass system A stage indicates a permeate stream being fed to another RO sys
411. l 225 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Configuration Spiral Wound High Temperature Turboclean Shell Active Membrane Area 53 ft 4 9 m Recommended Applied Pressure Not applicable Maximum Applied Pressure 1000 psi 69 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 25 GPM 5 6 m3 hr sD A Minimum Brine Flow Permeate Flow Ratio 5 1 u s mp A Maximum SDI 15 minutes 5 0 APPROV e Maximum Turbudtv 1 NTU Application Whey Concentration d Il 1 Leh i KETE at SLA Lh WAL UU Li EEN TAYN V LLL I AN A VON d M i NN M NN C A a UP E 1 mm B A Se d Element Weight 12 5 4 Length A 38 00 965 Diameter B 3 8 96 Permeate Tube C 0 83 21 2 Units in pounds and inches units in paranthesis in kilograms and millimetes Dim A does not include ATD Mechanical Configuration Sanitary Style Core Tube ATD not included with element
412. l Ge ANN AN WA UN d l a AAA AAA Element Weight 12 5 4 Length A 38 75 984 Diameter B 3 8 96 Permeate Tube C 0 83 21 2 Units in pounds and inches units in paranthesis in kilograms and millimetes Dim A does not include ATD Mechanical Configuration Sanitary Style Core Tube ATD not included with element Feed Spacer 0 065 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION ow NN 3 8 X 20 High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 3840 N1C9U8 1750 6 0 99 50 98 50 Performance is based on the following test conditions 2000 ppm NaCl 225 psi 25 C 15 recovery pH 8 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane Configuration Spiral Wound Turboclean Shell with FoulGuard Technology Active Membrane Area 70 ft 6 4 m Recommended Applied Pressure
413. l ae ee eee eee ee AUER LENKA PL LOR LUD KKKWAAKKNKMAAKAUKMU NAA y i AU AWAYYANA AAA NN NW Nt M d ll li II Element Weight Length A 12 5 4 38 965 Units in pounds and inches units in paranthesis in kilograms and millimetes Dim A does not include ATD Diameter B Mechanical Configuration Sanitary Style Core Tube Feed Spacer 3 8 96 0 045 thick diamond spacer PRODUCT SPECIFICATION 3 8 AUM High Temperature UF Turboclean Element M W C O 10 000 AUM Advanced Ultrafiltration Membrane Spiral Wound Turboclean Shell 53 ft 4 9 m Not applicable 600 psi 41 bar 35 140 F 2 60 C 2 11 continuous 10 0 ppm 4 5 m3 hr us one 5 0 1 NTU AT Milk Fractionation Wii d Permeate Tube C 0 83 21 2 ATD not included with element Engineered Membrane EE SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TRIS CORPORATION Model 3838 N6D9V7 PRODUCT SPECIFICATION 3 8 AUM High Temperature UF Turboclean Element M W C O 10 000 OPERATIONAL AND DESIGN DATA Membrane Type Contiigurali iu uuu u Active Membrane Area Typical Element Feed Pressure Maximum Applied Pressure
414. l GPD m3 day 8040 01G8T6 7 000 26 0 PRODUCT SPECIFICATION 8 CA RO Turboclean Element Minimum Salt Rejection Average Salt Rejection 98 00 97 00 Performance is based on the following test conditions 2 000 00 ppm NaCl 420 00 psi 25 C 15 recovery pH 5 50 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type Configuration E Active Membrane Area Recommended Applied Pressure Maximum Applied Pressure Recommended Operating Temperature Feedwater pH Range Chlorine Tolerance Maximum Feed Flow Minimum Brine Flow Permeate Flow Ratio Maximum SDI 15 minutes Maximum Turbidity ADDIIG300I Rm A Element Weight 45 20 Length A 40 00 1 016 Diameter B 7 9 200 SB Cellulose Acetate Blend Spiral Wound Turboclean Shell 350 ft 32 5 m 200 500 psi 14 34 bar 600 psi 41 bar 50 90 F 10 32 C 5 5 nominal 4 7 0 5 ppm nominal 1 0 ppm max 80 GPM 18 m3 hr 5 1 5 0 1 NTU Cooling Water Blowdown Recycle gt a c w DU e i B A Ww A 3 E Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis i
415. l Manual TRIS gt CORPORATION SUPPORT CHEMICALS The following are support chemicals used in the operation of membrane treatment plants These biocides and polymers are specifically formulated to work with cellulose acetate polyamide composite and ultratfiltration mem brane elements TRIPOL 1210 TriPol 1210 is a polymer additive used to enhance the rejection of CA reverse osmosis elements This polymer can reduce salt trans mission by 20 to 8096 while decreasing per meate flow by 20 to 30 TRISTORE 110 TriStore 110 is a premixed preservative solu tion used to store RO NF and UF membrane elements It will prevent biogrowth and offer some freeze protection and should be used for long term element storage TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 330 emm TriSep Corporation Chemical Manual TRIS gt CORPORATION TRISTAT 110 APPLICATION LIQUID BIOCIDE TriStat 110 should be mixed in a cleaning tank equipped with a mechanical mixer heater low pressure recirculation pump and cartridge or bag e Broad spectru m biocide filter This biocide works best when applied at a e Effective on bacteria mold flow rate of 8 10 gpm per 4 pressure tube or fungu S and yeasts 30 40 gpm per 8 pressure tube at a pressure of between 20 50 psi Add 1 gallon of TriStat 110 per PROBLEM 50 gallons of RO permeate or DI water Recirc
416. l attack 1s necessary For economic considerations the membrane should lend itselt to being fabricated into shapes which offer high surface to volume ratios Most flat sheet membranes used in RO applications today are composite membranes The mem brane is coated or cast unto a support sheet typically a non woven polyester film usually about 0 004 0 1 mm thick On top of this layer a thin UF support membrane 0 002 0 05mm thick usually made from polysulfone is applied to the support fabric The final RO membrane 2 000 angstroms thick is then coated on top of the support membrane The TriSep ACM X 20 TS80 and XN45 membranes are made with this process The celluslose acetate SB series RO membranes and the UE and TM10 UF and MF membranes are assymetric membranes This type of membrane is made in a single step It is coated on a polyester support fabric in a single step The surface has a much denser pore structure while the base of the membrane has a more pourous and open structure to minimize pressure drop Figure 3 Feed Water High Pressure RO NF Membrane UF Membrane Non woven support Permeate Low Pressure TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 376 TriSep Engineering Manual TRIS SS How a Spiral is Made CORPORATION Spiral wound elements are made of three main fabrics The membrane permeate carrier fabric and feed spa
417. l numbers are at the bottom of the list with an at the beginning of the model number to indicate that this 1s not a standard TriSep model number A view of the sheet is displayed to the screen which can then be printed or saved in several different file formats Elements are separated by diameter Click on the radio button of the diameter you wish to use Then select the appropriate element and input the number of elements per pressure tube The maximum number of elements per pressure tube is 7 Click OK to select the element Now input the array for the system This is done by specifying the number of tubes per pass A maximum of 4 passes are allowed You can type in the number of tubes per pass or click on the up and down arrows to increment or decrement the number of tubes by one The last two fields that you can input is for the permeate backpressure Depending on the units toggle switch you must input in psi or bar This allows you to balance the permeate flux rates in each pass This is useful on high osmotic pressure feed streams or when using very high flux membrane elements You may also enter a concentrate boost pressure for inter pass boosting This is sometimes used for high osmotic pressure feeds and is a more energy efficient method of balancing permeate fluxes Once all of the required data fields have been input you can click on the Calculate button and do the system design calculation If you have left required fields blank it will
418. l spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane ee ee SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TRIS CORPORATION Permeate flow Model GPD m3 day 8037 O1B3Z6 6 500 24 0 PRODUCT SPECIFICATION 8 CA RO Turboclean Element Minimum Salt Rejection 96 Average Salt Rejection 96 98 00 97 00 Performance is based on the following test conditions 2 000 00 ppm NaCl 420 00 psi 25 C 15 recovery pH 5 50 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type Configuration Active Membrane Area Recommended Applied Pressure Maximum Applied Pressure Recommended Operating Temperature Feedwater pH Range Chlorine Tolerance Maximum Feed Flow Minimum Brine Flow Permeate Flow Ratio Maximum SDI 15 minutes Maximum Turbidity Nolo e Tel e SB Cellulose Acetate B
419. lation STORAGE Min Storage Min Storage Maximum Temp without Temp w 40 Storage Glycerin wt Glycerine Temp 0 C 32 F 15 C S F 30 C 86 F Only glycerin may be used as a freeze protection agent If used the concentration must be 40 wt 2 3 wt sodium metabisulfite or TriSep approved biocide must be used for storage shipping or continuous element shutdowns in excess of 5 days to prevent biological growth TriSep Corporation 93 S La Patera Lane Goleta CA 93117 805 954 8003 phone 805 964 1235 fax www trisep com 416 TRIS gt CORPORATION Spare Parts The following tables contain a listing of spare parts that are available for TriSep membrane elements These include inboard adapters used to adapt the first and last element within a pressure tube to the pressure tube end cap interconnectors used to connect two element permeate tubes together and brine seals and O rings for the elements Most TriSep elements come standard with brine seals interconnectors and interconnector O rings The exceptions are that all Turboclean elements come without a brine seal since they are sanitary elements and do not require one And 2 5 and 3 8 diameter elements are not supplied with interconnectors These must be purchased separately TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 417 WY CS 01 8007 67 01 Suq pue Daat
420. le Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TRIS CORPORATION Permeate flow Model GPD m3 day 4040 N6PAX4 3 100 11 0 PRODUCT SPECIFICATION 4 AUM Ultrafiltration Turboclean Element Series M W C O 10 000 Performance is based on the following test conditions 500 00 ppm PEG 30 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type e Oe ESL OP asco uuu uuu uuu yuana Active Membrane Area Recommended Applied Pressure Maximum Applied Pressure Recommended Operating Temperature Feedwater pH Range Chlorine Tolerance Maximum Feed Flow Minimum Brine Flow Permeate Flow Ratio Maximum SDI 15 minutes Maximum Turbidity PAD DNC AUG DEE AUM Advanced Ultrafiltration Membrane Spiral Wound Turboclean Shell
421. leakage with fewer associated chemicals being used TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 365 A TRIS gt CORPORATION APPLICATION BULLETIN BULLETIN NO ACM 04 TYPE APPLICATION CLIENT LOCATION EQUIPMENT BACKGROUND PROCESS PERFORMANCE CONCLUSIONS Reverse Osmosis Municipal Drinking Water Town of Jupiter Florida U S A 4040 ACM4 TSA Spiral Wound Element ACM Low Pressure Membrane A pilot study was done at the town of Jupiter for their planned expansion of 4 additional 1 5 MGD treatment trains to their current 6 MGD Reverse Osmosis Water Treatment Plant The pilot test was designed to evaluate various membranes treating raw water supplied to the plant TriSep along with two other manufacturer s participated in this pilot study Feedwater was any combination of 7 online Floridian Aquifer supply wells with varying water qualities Conductivity 5 400 9 500 u mho cm Total Hardness 783 1 141mg L as CaCO Bicarbonate HCO 120 mg L as CaCO Pretreatment consisted of 6 10 inch cartridge filters to remove particles larger than 5 0 microns from the raw water Antiscalant dosed at 3 ppm Acid injection used only during increased recovery at 5 10 ppm depending on raw water pH The design is a 2 stage system with a 2 1 array using 6M vessels This design simulated their existing full scale RO tr
422. lean Shell 67 ft 6 2 m 5 200 psi 0 3 14 bar 600 psi 41 bar 35 140 F 2 60 C 2 11 continuous 10 0 ppm 20 GPM 4 5 m3 hr 5 1 5 0 1 NTU Sugar Refining Starch Removal Wii d Permeate Tube C 0 83 21 2 Engineered Membrane EE SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION ow NN 3 8 XN45 High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 3840 N2bE7U8 1 750 6 0 95 00 92 00 Performance is based on the following test conditions 2 000 0 ppm MgSOA 110 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type XN45 Polyamide Advanced Nanofiltration Membrane COMMUN ANON EEN Spiral Wound Turboclean Shell Active Membrane Area 70 ft 6 4 m Recommended Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 5 ppm nominal 1 0 ppm max Maximum Feed Flow
423. lement Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 M2C2T6 9 400 35 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane CONTI EE Spiral Wound Turboclean Shell Active Membrane Area 355 ft 32 6 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU PAO DUCAUO MW se scencinensaascenenttacessscdedenenndeacseddueeacee Pharm Process Water Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Fi
424. lend Spiral Wound Turboclean Shell 340 ft 31 6 m 200 500 psi 14 34 bar 600 psi 41 bar 50 90 F 10 32 C 5 5 nominal 4 7 0 5 ppm nominal 1 0 ppm max 80 GPM 18 m3 hr 5 1 5 0 1 NTU Chemical Waste Water Element Weight Length A 45 20 37 00 939 Diameter B 7 9 200 Permeate Tube C 1 40 35 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Stainless Steel Core Tube 0 031 thick diamond spacer Mechanical Configuration Feed Spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane ni SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Lun 8 X 20 Low Fouling RO Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 N1J8T6 9 400 35 0 99 50 98 50 Performance is based on the following test conditions 2 000 00 ppm NaCl 225 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane CGopnfguraton a k Spiral Wound Turboclean Shell w
425. lerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 4 0 Maximum Turbidity 1 NTU Element Weight 50 23 Length A 40 0 1 016 Diameter B X 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 028 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Za 8 ACM LP Low Pressure RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 ACM5 TSAN 11 900 45 0 98 50 97 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 150 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM LP Fully Aromatic Polyamide Low Pressure Advanced Composite eidel
426. lerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 15 7 Length A 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Zu 4 X 20 Low Fouling RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 X201 TSF 2 400 9 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane CORT QU e e ua eens seca ana iss azu uqa apaq awa
427. les dosing use the latest version of TroiWin TriPol S d sili di t 9010 contains a dispersant and can be used 1f there ibd an ana silica aispersan is iron or other metal hydroxides in the feedwater capability PERFORMANCE 45 en PROBLEM Max Langlier Saturation Index 2 6 I ny Installation ridwide higher permeate ee ae ate pa M from se osmosis RO S ide are eet Satan SEH SC 7 Max BaSO4 Saturation 10 000 often limited by the potential for carbonate and l ae Max CaF Saturation 10 000 sulfate scales This is especially problematic for Silica 100 0 well waters with high dissolved solids where sig nificant amounts of sulfates and alkalinity may be present In many applications the tendency for scale formation has the effect of lowering the system recovery that could adversely effect the system economics 1n the concentrate Levels may be exceeded on occasion Contact TriSep for advice PACKAGING TriPol 9010 is shipped as a liquid in 2 gallon sample sizes 5 gallon 40 Ib plastic pails and 55 500 Ib gallon plastic drums Pricing 1s F O B our factory in Goleta CA Salem VA or Duisberg SOLUTION Germany Delivery for most orders is 1 2 days TriPol 9010 protects and enhances the operation of after receipt of order RO and NF systems by controlling mineral scale formation due to carbonate sulfate and fluoride compounds In most water types proper use of TriPol 9010 can significantly increase allo
428. leta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TRIS CORPORATION Permeate flow Model GPD m3 day 4040 O3P3U5 1 900 7 0 PRODUCT SPECIFICATION 4 CA NF Turboclean Element Series Minimum Salt Rejection Average Salt Rejection 85 00 80 00 Performance is based on the following test conditions 2 000 00 ppm NaCl 225 00 psi 25 C 15 recovery pH 5 50 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type Oe TN e E Active Membrane Area Recommended Applied Pressure Maximum Applied Pressure Recommended Operating Temperature Feedwater pH Range Chlorine Tolerance Maximum Feed Flow Minimum Brine Flow Permeate Flow Ratio Maximum SDI 15 minutes Maximum Turbidity PDD NGAUGM Cellulose Acetate Nanofiltration Membrane Spiral Wound Turboclean Shell 80 ft 7 4 m 200 500 psi 14 34 bar 600 psi 41 bar 50 90 F 10 32 C 5 5 nominal 4 7 0 5 ppm nominal 1 0 ppm max 20 GPM 4 5m3 hr 5 1 5 0 1 NTU Dialysis Make up Water Element Weight Length A 15 7 40 00 1 016 Diameter B
429. liability for all causes including any breach of warranty or failure to deliver conforming goods shall not exceed the value of the contract 3 PREVAILING TERMS AND CONDITIONS Specific provisions provided by SELLER may supersede these terms and conditions However should any of these terms and conditions be contrary to or inconsistent with any terms and conditions contained in any purchase order form or other document between SELLER and CUSTOMER which is prepared by CUSTOMER and whenever executed the provisions hereof shall be controlling and shall supersede the conflicting terms and conditions which are contained in such other document 4 TITLE AND RISK OF LOSS Title to and risk of loss of the goods herein described shall pass to CUSTOMER upon delivery of said goods to a carrier at SELLERS plant Title to and risk of loss of said goods shall pass to CUSTOMER in no other way notwithstanding any agreement to the contrary including but not by the way of limitation any agreement to pay freight express or other transportation of insurance charges 5 TAXES DUTIES AND CLEARANCE EXPENSES CUSTOMER assumes full responsibility including reporting and payment of any and all sales or use taxes import duties or other expenses relating to clearance of the goods herein described at destination or any and all other charges of like nature which may be imposed upon such goods 6 ACCEPTANCE OF GOODS CUSTOMER shall inspect all goods immedia
430. lids SpiraSep process flow diagram A Triseo el rdc TRI gt A Crystal Clear Solution CORPORATION SpiraSep M 900 Submerged Ultrafiltration UF Membranes Features and Benefits Process Description SpiraSep is a patented U S Patent No 6 755 970 submerged negative pressure ultrafiltration UF membrane process complete with backwashing and aeration capabilities The process utilizes spiral wound membranes that remove suspended solids turbidity cryptosporidium and oocysts with the 0 03 um ultrafiltration membrane Perforated Central Tube Permeate Collection Material 2 Membrane b Feed Channel Spacer sf Outer Wrap p Submerged Operation Water is pulled through the membranes using a slight vacuum Air is bubbled up through the element feed channels scouring and scrubbing the surface clean The rigid durable structure of the SpiraSep membrane design eliminates mechanical integrity issues commonly associated with hollow fibers This is a key factor in For additional information regarding SpiraSep UF membranes please contact Mike Snodgrass at 1 805 964 8003 ext 113 or send e mail to snodgrass trisep com maintaining effluent quality over the life of the membrane Advanced Air Scouring Process The SpiraSep filtration process utilizes a unique and innovative air scouring process where air is bubbled up through each element Air bubbles come in direct contact w
431. lied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 2 NTU Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Za 8 X 20 Low Fouling RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 X201 TSAN 9 700 36 0 99 50 98 50
432. lk Fractionation Element Weight 33 15 Length A 38 965 Diameter B 6 3 160 Permeate Tube C 1 14 28 9 Units in pounds and inches units in paranthesis in kilograms and millimetes Dim A does not include ATD Mechanical Configuration Sanitary Style Core Tube ATD not included with element Feed Spacer 0 031 thick diamond spacer Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION LA N 6 3 AUM High Temperature UF Turboclean Element TRIS CORPORATION Model M W C O 6338 N6D4V9 10 000 OPERATIONAL AND DESIGN DATA Membrane Type AUM Advanced Ultrafiltration Membrane Configuration Spiral Wound Turboclean Shell Active Membrane Area 175 ft 16 3 m Recommended Applied Pressure Not applicable Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 10 0 ppm Maximum Feed Flow 70 GPM 15 8 m3 hr sD A Minimum Brine Flow Permeate Flow Ratio 5 1 u s 0 Ma
433. llimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane ri SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Za 8 TS80 Nanofiltration Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 TS80 TSA 9 000 34 0 99 00 97 00 Performance is based on the following test conditions 2 000 0 ppm MgSOA 110 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ANM Aromatic Polyamide Advanced Nanofiltration Membrane COMIC UA OND ME Spiral Wound Fiberglass Outer Wrap Active Membrane Area 365 ft 33 5 m Recommended Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow
434. llowing test conditions 500 0 ppm Dextran 30 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type AUM Advanced Ultrafiltration Membrane ei le le e NEE Spiral Wound High Temperature Turboclean Shell Active Membrane Area 260 ft 23 9 m Recommended Applied Pressure 20 200 psi 1 4 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 10 0 ppm Maximum Feed Flow 95 GPM 22 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU eeler e Pyrogen Free Water Element Weight 40 18 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 047 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 S
435. lmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION LA 8 ACM RO Turboclean Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 M2P4T6 9 400 35 0 99 50 98 50 Performance is based on the following test conditions 2 000 00 ppm NaCl 225 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane COMMUN ANON EEN Spiral Wound Turboclean Shell Active Membrane Area 355 ft 32 6 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr
436. lograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 047 thick parallel spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com Certified Products NSF Standard 60 and 61 PL KIWA ATA RISES kiwa CORPORATION certified A ASSESSMENT ON TOXICOLOGICAL ASPECTS Historically drinking water systems membranes and chemicals were not covered by any governing agency in the United States and in most foreign countries The FDA and USDA in the United States regulated the food dairy beverage bottled water and pharmaceudical markets but did not have jurisdiction over drinking water With the increasing focus on water purity this is rapidly changing Many states in the US now require NSF approved membrane elements and ant scalants Many European countries have their own governmental approval aganecy such as KIWA in the Netherlands NSF International The Public Health and Safety Company a not for profit non governmental organiza tion is the world leader in standards development product certification education and risk management for public health and safety For 60 years NSF has been commit
437. low 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 2 NTU Element Weight 50 23 Length A 40 00 1 016 Diameter B 8 3 210 Permeate Tube C 1 14 29 0 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Osmo Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane ni SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com OPERATING INFORMATION TRIS CORPORATION Recommended operating pressure is given as a guideline and may vary depending on the application feed water quality and temperature Rated permeate flow is based on standard test conditions and may not apply depending on the feed water quality Individual element s permeate flow may vary 15 Design data may be exceeded under certain circumstances Contact TriSep for specific application information and approval Elements are shipped with a preservative therefore the permeate from the first one hour of operation must be discarde
438. low Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 4 0 Maximum Turbidity 1 NTU Element Weight 50 23 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 028 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane y SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION s 9 ACM RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 ACM2 UWAN 10 700 40 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Configuration Spiral Wound Fiberglass Outer Wrap Active Membrane Area 400 ft 37 2
439. low and rejection properties of a NF membrane This makes the TS80 more rogbust and have better chemical resistance than a NF membrane that 1s made by degrading a RO membrane All TS80 elements are factory tested on MgSO4 and water solutions The TS80 is typically used in municipal membrane softening applications It has a higher relative sodium chloride rejection 90 than the XN45 30 The TS80 or its higher flow cousin the TS83 are excellent choices to remove THM precursors color iron and hardness from surface and well waters 2540 TS80 TSF 4040 TS80 TSA 4040 TS80 TSF 4040 TS83 TSF 8040 TS80 TSA 8040 TS80 TSAN 8040 TS80 TSFA 8040 TS80 UWA 8040 TS80 UWAN 8040 TS83 TSA 8040 TS83 TSAN 8040 TS83 UWA 8040 TS83 UWAN 8540 TS83 TSFA 2 5 diameter by 40 long 0 75 O D male permeate tube protruding permeate tube 4 diameter by 40 long 0 75 O D female permeate tube flush cut 4 diameter by 40 long 0 75 O D male permeate tube protruding permeate tube 4 diameter by 40 long 0 75 O D male tube protruding tube higher flow 8 diameter by 40 long 1 50 I D female permeate tube flush cut Same as 8040 TS80 TSA but NSF approved 8 dia by 40 long 1 12 I D female perm tube flush cut Filmtec replacement 8 diameter by 40 long 1 50 I D female permeate tube flush cut 400 ft Same as 8040 TS80 USA but NSF approved 8 diameter by 40 long 1 50 I D female permeate tube flush cut Same as 8040 TS83 TSA b
440. low may vary 1596 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION TRIS gt CORPORATION 8 TS80 Nanofiltration Element Series Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 TS80 UWA 10 000 37 0 99 00 97 00 Performance is based on the following test conditions 2 000 0 ppm MgSOA 110 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ANM Aromatic Polyamide Advanced Nanofiltration Membrane Configuration EE Spiral Wound Fiberglass Outer Wrap Active Membrane Area 400 ft 37 2 m Recommended Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 4 0 Maximum Turbidity 1 NTU EH
441. lowing test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane COMMUN ANON EEN Spiral Wound Fiberglass Outer Wrap Active Membrane Area 400 ft 37 2m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 4 0 Maximum Turbidity 1 NTU Element Weight 50 23 Length A 40 0 1 016 Diameter B X 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 028 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane
442. lowing test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane ONTO ON I uu aan wa Spiral Wound Fiberglass Outer Wrap Active Membrane Area 400 ft 37 2 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 4 0 Maximum Turbidity 1 NTU Element Weight 50 23 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 028 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS
443. lp File There are six options in File whose functions are self explanatory New Analysis Open Analysis Delete Analysis Add Custom Model Print and Exit The Add Custom Model is new for version 2 0 0 Calculations There is currently only one selection under Calculation and that allows you to perform the system design calculation This can not be done unless a water analysis has been input balanced and saved Units This is a toggle switch that allows you to set the units you want to use in the calculations and units you wish to use in the print out It defaults to U S units which will use degrees F for temperature gallons per day gpd and gallons per minute gpm for TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 397 TriSep Troi Design Program A Manual ver 2 0 0 TRIS CORPORATION flow rates and pounds per square inch psi for pressures and gallons per square foot per day gfd for flux rates If you select metric units it will use degrees C for temperature cubic meters per hour m3 hr for flow rates bar for pressures and liters per square meter per hour Imh for flux rates The program will remember the last setting you used so check this before you start a new design As an example if you set the units toggle to metric exit the program and then start the program again the toggle
444. lution by back diffusion Concentration polarization has several negative effects on the desalination process Osmotic pres sure will be greater at the membrane surface than in the bulk soliution reducing the net pressure differential across the membrane AP Az and thereby the water flow Similarly salt flow will increase with the higher localized salt concentration In addition the probablility of exceeding the solubility of sparingly soluble salts at the membrane surface increases and with the possibility of precipitation causing membrane scaling Although these boundary layer pheneomena are indepenent of membrane transport per se their effects can be significant particulary for membranes with high water flow per unit area specific flux TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 375 TriSep Engineering Manual TRIS 3 How a Membrane is Made CORPORATION The membrane chosen for desalination of water by reverse osmosis must be highly permeable to water to achieve high rates of production while being highly impermeable to salts to obtain acceptable product water quality It must also be extremely thin to maximize water flow but strong enough to withstand high pressure Changes in the membranes transport and mechanical properties should be minimal after long exposure to high pressure Likewise resistance of the membrane to chemical and biologica
445. lution tank If tank volume is now too low mix additional cleaning solution Start recirculating the cleaning solution through the vessels at specified flow rate or if different at manufacturer s specified flow rate per vessel Pump pressure should be between 20 and 50 psi Recirculate for 1 hour checking pH periodically If pH goes above 4 0 a new solution will have to be mixed Shutdown pump and allow to static soak for 1 hour while cleaning additional passes Follow same procedure for cleaning additional passes After soaking recirculate each pass for 20 minutes Rinse using rinsing method TSR 1 TSC 2 Sterilization A B C D Clean solution tank and fill with appropriate volume of RO Permeate water Start water recirculating through pump and back to tank Add 1 gallon of TriStat 110 per 50 gallons of water and recirculate until thoroughly mixed To displace water in vessels divert Concentrate and Product lines to drain and slowly pump solution into vessels until it is coming out of Concentrate line Shutdown pump and divert Concentrate and Product lines to cleaning solution tank If tank level is too low mix additional solution Start recirculating solution through vessels at appropriate flows and pressures Recirculate for 20 minutes shutdown pump and allow to static soak for 2 hours Sterilize additional passes in the same manner while first pass soaks After soaking recirculate each pass for 15 minutes R
446. lyamide Advanced Nanofiltration Membrane Configuration Spiral Wound High Temperature Turboclean Shell Active Membrane Area 355 ft 32 6 m Recommended Applied Pressure Not applicable Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 5 ppm nominal 1 0 ppm max Maximum Feed Flow 80 GPM 18 m3 hr iU M Minimum Brine Flow Permeate Flow Ratio 5 1 y 5 Maximum SDI 15 minutes 5 0 OD Maximum Turbdiftv 1 NTU PAD ONC QUO ME Lactose Demineralization i Element Weight 45 20 Length A 38 00 965 Diameter B X 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Dim A does not include ATD Mechanical Configuration Filmtec Style Core Tube ATD not included with element Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane INS ea SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A
447. m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 4 0 Maximum Turbidity 1 NTU Element Weight 50 23 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 028 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane Sane s hi SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION 8 ACM RO Element Series TRIS gt CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 ACM2 UWFA 10 700 40 0 99 50 98 50 Performance is based on the fol
448. m Turbidity 1 NTU Element Weight 7 3 2 Length A 40 0 1 016 Diameter B 2 5 63 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane T SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Za 4 TS80 Nanofiltration Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 TS80 TSA 2 000 7 0 99 00 97 00 Performance is based on the following test conditions 2 000 0 ppm MgSOA 110 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ANM Aromatic Polyamide Advanced Nanofiltration Membrane Configuration Spiral Wound Fiberglass Outer Wrap Active Membrane Area 88 ft 8 1 m Recommended Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressur
449. m sulfate scales Calcium Carbonate Scale Sodium hexametaphosphate SHMP acrylic acids and or acidification can be used to control CaCO3 scaling At low TDS s less than 15 000 ppm the Langelier Saturation Index LSI can be used to indicate saturation At higher TDS levels the Stiff and Davis Saturation Index S and DSI gives a more accurate representation of the solubility of CaCO3 The indexes are set up so that negative values indicate a solution that 1s not saturated while positive values indicate some degree of supersaturation Calcium Flouride Scale In version 2 0 0 calcium flouride scale calculation have been added A value less than 100 indicates a solution that is not saturated while a value greater than 10096 indicates some degree of supersaturation Acrylic acid antiscalent can be used to control calcium flouride scaling TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 403 TriSep Troi Design Program Manual ver 2 0 0 TRIS gt CORPORATION Silica Scale Silica scaling in actual RO systems is dependent on a number of factors The equilibrium value is dependent on the feedwater temperature and pH In actual practice due to the relatively short residence time in a typical RO system the kinetics of the precipitation reaction are normally the limiting factor rather than the equilibrium value The kinetics of the silica precipitation rea
450. may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Jams 8 X 20 Low Fouling RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 X201 TSFA 9 700 36 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane COrnfigural on RET Spiral Wound Fiberglass Outer Wrap with FoulGuard Technology Active Membrane Area 365 ft 33 5 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 2NTU Element Weight 45 20
451. mber 4040 ACMI TSF 4040 ACM2 TSF 4040 ACM3 TSF 4040 ACM4 TSF 4040 ACMS TSF 4040 ACMS5 TWF 4040 TS80 TSF 4040 TS83 TSF 4040 X201 TSF 8040 ACM2 TSFA 8040 ACM2 UWFA 8040 ACMA TSFA 8040 ACM5 UWFA 8040 TS80 UWFA 8040 X201 TSFA TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 Dow Filmtec Dow Filmtec BW30 4040 BW30HP 4040 BW30 LE4040 XLE 4040 XLE 4040 NF90 4040 NF70 4040 BW30 8040 BW30 365 BW30 400 BW30 440 BW30 LE 400 XLE 400 LE 400 LE 440 NF90 400 NF70 400 BW30 365FR Style Elements Comments Same diameter and permeate tube Same diameter and permeate tube Same diameter and permeate tube Same diameter and permeate tube Same diameter and permeate tube Same diameter and permeate tube Same diameter and permeate tube Same diameter and permeate tube Same diameter and permeate tube Same diameter and permeate tube Same diameter and permeate tube Same diameter and permeate tube Same diameter and permeate tube 284 PRODUCT SPECIFICATION 4 ACM RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 ACM1 TSF 1 900 7 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type
452. meate flow may vary 15 Engineered Membrane End nF I Y i SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION ow NN 8 ACM RO High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8038 M2C9V6 7500 28 0 99 00 98 00 Performance is based on the following test conditions 2000 ppm NaCl 225 psi 25 C 15 recovery pH 8 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Configuration Spiral Wound High Temperature Turboclean Shell Active Membrane Area 288 ft 26 8 m Recommended Applied Pressure Not applicable Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 95 GPM 22 m3 hr a p A Minimum Brine Flow Permeate Flow Ratio 5 1 S ED Maximum SDI 15 minutes 5 0 APPROV Maximum Turbidity
453. mem brane fouling rates The type of membrane used for a particular application may also affect the fouling rate The X 20 mem branes generally exhibit lower fouling rates on surface and waste waters than standard composite membranes For further information please refer to the Guidelines for Operation in the TRISEP Engineering Manual Table 2 Flux Guidelines for S WMS Elements Feedwater Source suggested Flux GFD RO UF Permeate 22 28 Deep Wells 18 22 Shallow Wells 16 18 Surface Waters 12 16 Waste Waters 8 12 TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 402 TriSep Troi Design Program A Manual ver 2 0 0 TRIS CORPORATION Beta Factor The Beta Factor is a measure of the relationship between the feed water velocity traveling parallel to the membrane and the permeate water traveling perpendicular or into the membrane This number is also related to the individual element recovery For most large systems the Beta Factor should be less than 1 20 This equates to an individual 40 element recovery of approximately 20 Lower beta factors indicate lower element recoveries For a given system recovery increasing the path length of the system array i e the equivalent number of elements in series decreases the Beta Factor Table 3 gives guidelines for the number of elements In series required to achieve acceptable Be
454. mend this to the casual user There are many fields to input and it is easier to copy the structure and data from an existing model To do this select a standard TriSep element that is close to the new element you wish to create Then click on the Copy Element button This will ask you for a new model number and part number Please note that model numbers must be less than 15 characters in length You can leave the part number blank but it will require a model number Once a copy has been created you can modify the required fields to suit your purposes After you have modified the element you can then select the element in the calculation portion of the program under the Select Element button Custom elements will be listed at the bottom of the element list below all the standard TriSep elements and will be marked with an at the beginning of the model number to indicate that this is a custom model To delete a custom element highlight it then click on the Delete button 7 SHARING THE DATABASES ON A NETWORK TROI needs to be individually installed on each work station but the database can now be shared on the network Copy the Romain mdb Romain ini Elements dat and Elements mdb onto a shared network folder Then on each work station create a database ini file with notepad pointing to the database folder path For example you have a shared folder DataTroi on the network and its mapped to drive M Then you would just type in the M Data
455. meter by 40 long 1 50 I D female permeate tube flush cut 8040 XN45 TSFA 8 dia by 40 long 1 12 I D female permeate tube flush cut Filmtec replacement 8040 XN45 UWA 8 diameter by 40 long 1 50 I D female permeate tube flush cut high area TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 234 PRODUCT SPECIFICATION LA 2 5 XN45 Nanofiltration Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 2540 XN45 TSF 600 2 0 95 00 92 50 Performance is based on the following test conditions 2 000 0 ppm MgSOA 110 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type XN45 Polyamide Advanced Nanofiltration Membrane Configuratio EE Spiral Wound Fiberglass Outer Wrap Active Membrane Area 26 ft 2 4 m Recommended Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 5 ppm nominal 1 0 ppm max Maximum Feed Flow 6 GPM 1 4 m3 hr Minimum
456. mixing C Add 3 gallons of TriClean 214 per every 100 gallons of water in the tank Allow to recirculate until thoroughly mixed D Check pH of solution proper range is below 11 5 for thin film composite elements and below 7 8 for CA elements unless otherwise specified by membrane manufacturer pH may be lowered by adding sulfuric acid E Isolate first pass to be cleaned With Concentrate and Product Lines diverted to proper drain slowly run cleaning solution through pressure vessels until all remaining water is out of vessels and cleaning solution is coming out of concentrate line Shutdown pump and divert Concentrate and Product lines to cleaning solution tank F If tank volume is now too low mix additional cleaning solution G Start recirculating the cleaning solution through the vessels at specified flow rate or if different at manufacturer s specified flow rate per vessel Pump pressure should be between 20 and 50 psi Recirculate for 1 hour checking pH periodically H Shutdown pump and allow to static soak for 1 hour while cleaning additional passes l Follow same procedure for cleaning additional passes J After soaking recirculate each pass for 20 minutes K Rinse using rinsing method TSR 1 TSC 8 Low pH Cleaning A Clean and fill solution tank with proper volume of RO Permeate Water B Start water recirculating through pump and back into the tank during chemical mixing C Add 1 gallon of TriClean 217 per every
457. mmended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 1000 psi 69 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 95 GPM 22 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU PIDBIICAHO uuu m nen ee ee Fruit Juice Must Concentration Element Weight 40 18 Length A 40 00 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 047 thick parallel spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION oe 8 ACM RO Turboclean Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 M2E6T6 9 400 35 0 99 50
458. mum Turbidity 2NTU Application Tea Concentration Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TurboClean Sanitary Elements for Pharmaceudical Applications um TRIS SE CORPORATION TurboClean elements have been used extensively in the pharmaceudical market for USP and WFI water purification and down stream process purification Although not required by law by the FDA contamination of pharmaceudical USP and WFI water can result in contaminated products The sanitary nature of the TurboClean element provides a continous by pass flow around the outside of the element This eliminates the stagnant area normally present on sr n brine seal elements which can result in bio growth that can contaminate the pharmaceudical product This stagnant area is difficult to clean or s
459. mum flow of 1 100 gallons per day conditioning flush with potable water prior to use Serial number 191709 and greater Product requires a 1 hour TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 260 TriSep NSF Standard 60 Chemical Listing TRIS gt CORPORATION ANSI NSF STANDARD 60 Drinking Water Treatment Chemicals Health Effects TRISEP CORPORATION 93 SOUTH LA PATERA LANE GOLETA CA 93117 805 964 8003 Plant at GOLETA CA Miscellaneous Water Supply Products Trade Designation Product Function Max Use TriPol 8500 Reverse Osmosis Antiscalant 4 mg L TriPol 8510 Reverse Osmosis Antiscalant 4 mg L TriPol 9000 Reverse Osmosis Antiscalant 10 mg L TriPol 9005 Reverse Osmosis Antiscalant 10mg L TriPol 9010 Reverse Osmosis Antiscalant 10 mg L TriPol 9013 Reverse Osmosis Antiscalant 10me L Plant at ROANOKE VA Miscellaneous Water Supply Products Trade Designation Product Function Max Use TriPol 9010 Reverse Osmosis Antiscalant 10me L TriPol 9000 Reverse Osmosis Antiscalant 10mg L TriPol 8510 Reverse Osmosis Antiscalant 4mg L TriPol 8500 Reverse Osmosis Antiscalant 4mg L TriPol 9005 Reverse Osmosis Antiscalant 10me L TriPol 9013 Reverse Osmosis Antiscalant 10mg L TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 261 PRODUCT SPECIFICATION 8 AC
460. must not affect the element performance Fouling of the membrane elements by organic materials suspended solids or precipitated scales shall void the warranty Membrane damage caused by chemical compounds e g surfactants solvents soluble oils free oils lipids and high FOR STANDARD WARRANTY SPIRAL WOUND ELEMENTS 3 YEAR STANDARD WARRANTY molecular weight natural polymers shall nullify and void the warranty Failure to maintain the elements in a clean condition unfouled by particulate matter precipitates suspended material or biological growth shall nullify and void the warranty pH The pH in the element must be gt 4 0 for continuous operation The maximum allowable exposure time during operation and cleaning for solutions with a pH between 2 to 4 is 150 hours over the life of the elements Elements must not be exposed to pH 2 0 For continuous operation the pH in the elements must be lt 11 0 up to 40 C and 10 0 up to 45 C The maximum total allowable exposure time during operation and cleaning is 500 hours over the life of the element for solutions with pH 11 0 to 11 9 up to 40 C and with pH 10 0 to 10 9 up to 45 C Elements must not be exposed to pH 711 9 SOLUBILITY LIMITS The Langelier Saturation Index LSI of the brackish water brine dream must be negative except where an approved Antiscalant is used When an approved Antiscalant is used the pressure vessels must be flushed within 15 minutes afte
461. n OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Configuration Spiral Wound High Temperature Turboclean Shell Active Membrane Area 355 ft 32 6 m Recommended Applied Pressure Not applicable Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr a Y M Minimum Brine Flow Permeate Flow Ratio 5 1 K y W Maximum SDI 15 minutes 5 0 appro d Maximum T urbuditv 1 NTU Application Lactose Concentration Element Weight 45 20 Length A 38 965 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Dim A does not include ATD Mechanical Configuration Filmtec Style Core Tube ATD not included with element Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s per
462. n kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 1596 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TriSep ACM Composite RO Membrane Elements AN ACM1 ACM2 ACM3 ACM4 ACM5 TRIS gt CORPORATION TriSep offers five versions of it s popular ACM series reverse osmosis membrane elements The ACM line is the workhorse of theTriSep RO line It delivers high flux and high rejection in a durable and economical membrane The membrane has good combination of chemical resistance and mechanical strength This 1s exhibited by wide operating pH ranges 2 12 some resistance to oxidants such as chlorine up to 2 000 ppm hrs and hydrogen peroxide and pressures up to 1 000 psi 70 bar with the proper construction ACM RO membranes typically have higher salt NaCl rejection than cellulose acetate or nanofiltration membranes but in the ACM4 and ACMS configurations have high specific flux rates and can therefore operate at lower feed pressures ACM RO membranes have the ability to reject a wide range of feed species specifically particulates colloidal and microbiological species
463. n of 2 sodium metabisulfite and 18 glycerine in RO permeate water at a pH of 6 8 should be used for a storage solution This solution should be recirculated through the system for 30 minutes at 60 psi pressure Feed concentrate and permeate valves should be closed after the pump is shut down to keep the storage solution in the pressure tubes FLUSHING PRIOR TO USE TriSep 8 and 4 diameter elements as shipped contain the standard aqueous solution of approximately 396 of Sodium metabisulfite and 1896 glycerine These solutions must be flushed from the elements both concentrate and permeate before the elements are placed in service initially or returned to service from storage Adequate flushing can be achieved with water at a TDS up to 5000 mg l at 100 psi 6 8 bar at the permeate and concentrate rates listed below Be sure that the solubility guidelines for sparingly soluble salts maximum feed flow maximum flux rates and maximum pressure drop are not exceeded Minimum Concentration Rate Minimum Quantity of Permeate Diameter Inches Pressure Vessel US GPM LPM Element US Gallons liters The quality of the flush water is important Flush water must meet the Nanofiltration feedwater guidelines detailed in the TriSep document Guidelines for Operation The flushing procedures given will reduce the total organic carbon TOC to less than 1 mg l in the permeate TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 96
464. nced Ultrafiltration Membrane Spiral Wound Turboclean Shell 41 ft 3 8 m Not applicable 600 psi 41 bar 35 140 F 2 60 C 2 11 continuous 10 0 ppm A 4 5 m3 hr us So 5 0 1 NTU Mt Whey Fractionation A I l M Permeate Tube C 0 83 21 2 ATD not included with element Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION 3 8 TS50 High Temperature Turboclean Element TRIS c HS Ch A T di Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 3840 O8D1U8 1 600 6 0 99 00 98 00 Performance is based on the following test conditions 2 000 00 ppm MgSO4 110 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type TS50 Polyamide Advanced Nanofiltration Membrane Configuration Spiral Wound High Temperature Turboclean Shell Active Membrane Area 70 ft 6 4 m Recommended Applied Pressure Not applicable Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 contin
465. nd spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Z 8 ACM RO Element Series TRIS gt CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 ACM2 UWAN 10 700 40 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane eidele e EE Spiral Wound Fiberglass Outer Wrap Active Membrane Area 400 ft 37 2m7 Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI
466. nd worldwide network of local representatives are always avail able to assist you with all your membrane separation needs This electronic catalog is up to date as of the time of printing However specifications and products are continually changing and the best way to insure you have the most up to date information is to check our web site Our web address is http www trisep com The site contains all of our product information for elements and chemicals along with MSDS sheets for the chemicals Our TroiWin program can be downloaded for no charge In addition we regularly post updates on the element database for TroiWin that you can update You must have TroiWin version 2 0 0 or later for this feature to work This windows program allows you print a spec sheet for any of our elements directly from the program You can also download the most current version of this catalog at any time We will update the catalog several times per year to give you the most current information The web site also has several nice features such as a interactive element and chemical cross reference guide a literature request form e mail and telephone addresses and technical product information Please visit our web site for more information TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 5 TRI SEP A Crystal Clear Solution IR gt IriSep Corporation SpiraSep
467. ndard brine seal elements which can result in bio growth that can contaminate the product This stagnant area is difficult to clean or sanitize in place as there is no flow of cleaning or sanitizing chemicals into this area If cleaning or sanitizing chemicals do get into this area it is difficult to predict the rinse out time for these chemicals Standard net wrap sanitary elements have traditionally been used in food and dairy applications Due to the high by pass flow inherent with these designs food and dairy systems incorporate large recirculation pumps to insure a certain minimum flow through the elements These net wrap elements cannot be used in standard 2 1 arrays normally used in water applications The Turboclean element minimized by pass flow to 15 20 of the feed flow This allows the TurboClean element to be used in standard water type applications like cooling tower recycle Following are some TriSep TurboClean elements specifically engineered for the industrial water market TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 158 PRODUCT SPECIFICATION TRIS CORPORATION 4 X 20 Low Fouling RO Turboclean Element Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 N1L4V5 1 800 6 0 99 00 98 00 Performance is based on the following test conditions 2 000 00 ppm NaCl 225 00 psi 25 C 15 recover
468. nditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION ON 8 5 TS80 Nanofiltration Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8540 TS80 TSFA 10 800 40 0 99 00 97 00 Performance is based on the following test conditions 2 000 0 ppm MgSOA 110 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ANM Aromatic Polyamide Advanced Nanofiltration Membrane E ele Le UT AU ON ee Spiral Wound Fiberglass Outer Wrap Active Membrane Area 440 ft 40 4 m Recommended Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity
469. ne 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Za 8 ACM LP Low Pressure RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 ACM4 UWAN 16 000 60 0 99 00 98 00 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM LP Fully Aromatic Polyamide Low Pressure Advanced Composite Configuration Spiral Wound Fiberglass Outer Wrap Active Membrane Area 400 ft 37 2 m Recommended Applied Pressure 50 300 psi 3 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 4 0 Maximum Turbidity 1 NTU Element Weight 50 23 Length A 40 0 1 016 Diameter B X 7 9 200 Permeate Tube C 1 50 3
470. ne in RO permeate water at a pH of 6 8 should be used for a storage solution This solution should be recirculated through the system for 30 minutes at 60 psi pressure Feed concentrate and permeate valves should be closed after the pump is shut down to keep the storage solution in the pressure tubes FLUSHING PRIOR TO USE TriSep 8 and 4 diameter elements as shipped contain the standard aqueous solution of approximately 3 of Sodium metabisulfite and 18 glycerine These solutions must be flushed from the elements both concentrate and permeate before the elements are placed in service initially or returned to service from storage Adequate flushing can be achieved with water at a TDS 5000 mg l at 400 psi 27 2 bar at the concentrate rates and times listed below Be sure that the solubility guidelines for sparingly soluble salts maximum feed flow maximum flux rates and maximum pressure drop are not exceeded Element Minimum Concentration Rate Minimum Quantity of Permeate Diameter Inches Pressure Vessel US GPM LPM Element US Gallons liters 4 5 19 145 510 8 15 56 8 540 2040 The quality of the flush water is important Flush water must meet the RO feedwater guidelines detailed in the TriSep document Guidelines for Operation The flushing procedures given will reduce the total organic carbon TOC to less than 1 mg l TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 12
471. nes The readings that will be used as Start Up data for the calculation should be taken and logged for reference after the system has operated for 24 to 48 hours from the time of initial start up or start up of newly loaded membranes Temperature Compensation Factor Look up this factor on the Table that is provided on the reverse side Pressure Compensation Factor You calculate the PCF by dividing Start Up Feed Pressure by the Present Feed Pressure reading Start Up PSI Present PSI Example If Start up Feed Pressure was 230 psi and the Present Feed Pressure is 250 psi the calculation would be 230 250 0 92 Pressure Compensation Factor Information required Start up Present Feed Pressure pe eee Product Flow gpm eee Feedwater Temperature eee Sample Calculation Feed Pressure 230 250 Feed Temperature 66 F 71 F Product Flow 40 gpm 39 gpm Temp Correction Factor 1 2 1 1 Temp Corrected Flow 48 40 x 1 2 42 9 89 x 1 1 Pressure Correction Factor 230 250 0 92 Pressure Corrected Flow N A 39 468 42 9 x 0 92 Normalized Flow 48 gpm 39 468 gpm Difference 48 39 468 8 532 gpm Flow Decline 8 532 48 17 775 decline When Flow Decline is 15 or greater it is time to clean membranes If the Flow Decline comes out as a negative number double check your calculations and readings If it is still a negative number check TDS readings and Rejection rates as there is a possibility of O ring or membrane problems TriSep Corp
472. ng test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane ONTO ON I uu aan wa Spiral Wound Turboclean Shell with FoulGuard Technology Active Membrane Area 270 ft 24 8 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 95 GPM 22 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 2NTU PAO DUCAUO MW se scencinensaascenenttacessscdedenenndeacseddueeacee General Food Waste Water Element Weight 40 18 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 047 thick parallel spacer Permeate flow is clean water flux at standard conditions above Not applicable for all f
473. nical Configuration Filmtec Style Core Tube Feed Spacer 0 028 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION 9 ACM RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 ACM3 TSA 11 000 41 0 99 20 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Configuration Spiral Wound Fiberglass Outer Wrap Active Membrane Area 365 ft 33 5 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow
474. ning chemicals have been added to the main menu 5 Administrative documents such as our standard warranty terms and conditions etc have been added to the main menu 6 Operating pH ranges were increased for ACM X 20 TS80 and XN45 product lines from 4 11 to 2 11 For short term cleaning it has been increased to 1 12 if the temperature does not exceed 40 C Maximum exposure should not exceed 500 hours for a pH gt 11 0 and 11 9 We are always working to improve our software and will plan to have a new version available in the next 6 months Keep checking the web site for updates TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 395 TriSep Troi Design Program A Manual ver 2 0 0 TRIS CORPORATION 3 INSTALLATION The hardware requirements to run TROIWIN are an IBM PC compatible type computer 486 or equivalent Windows 95 98 NT 2000 or XP a hard disk with about 10 megabytes of free space a CD a printer and 16 megabytes of memory A color monitor is desirable To install the TROIWIN software onto a hard disk Place the TROIWIN CD into your drive At the Windows Desktop click on Start then click on Run and type in d setup where d Is your CD drive Your CD drive may have a different drive setting than d it may be e or some other letter If you are unsure of the drive letter for your CD click on Browse then double click on
475. nr Innerconnectar ar End Conn ctar or End Connector Figure 2 Element Sampling Locations As the feedwater flows through an element it becomes more concentrated causing the product water concentration to increase The conductivity of a probe sample is the average of product water produced upstream Typically this average conductivity changes 5 to 696 from one element to the next An unusually large deviation from this conductivity profile locates the source of the high salt passage problem Mechanical leaks are generally indicated by a step change in the conductivity profile at Sample Point A of Figure 2 A step change in the conductivity profile at sample Point B can indicate high salt passage from the element and or a mechanical leak UI 10 Probing Technique The tubing is marked to show locations of the interconnectors and the end of the pressure vessel housing By inserting and withdrawing the tube according to the markings permeate samples from various locations within the pressure vessel housing can be obtained By measuring the solute concentration of the samples the location of problem areas can be determined This procedure is illustrated in the figure Probing Technique shown above TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 392 TriSep Engineering Manual TRIS gt CORPORATION SHIPPING INFORMATION DIMENSIONS AND WEIGHT
476. ns Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION 8 ACM LP Low Pressure RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 ACM5 UWAN 12 500 47 0 98 50 97 50 Performance is based on the following test conditions 2 000 00 ppm NaCl 150 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM LP Fully Aromatic Polyamide Low Pressure Advanced Composite Configuratio uu LLULLU uu u uy Ti Spiral Wound Fiberglass Outer Wrap Active Membrane Area 400 ft 37 2 m Recommended Applied Pressure 50 300 psi 3 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes
477. ns around 1 4 psi per element This is especially important on low pressure RO NF UF and MF applications where the feed brine differential pressure can subtract a significant amount of the available net driving pressure Feed spacers that are thicker have lower pressure drops Spacers that are thinner than 0 028 0 7mm are normally not suitable for commercial and industrial spiral wound elements due to the higher pressure drop and increased rick of feed channel plugging Thicker feed spacers up to 0 090 2 3 mm can be used for applications with high suspended solids or high recirculation flow rates The permeate carrier fabric must have a low pressure drop for the permeate flow while being able to withstand high pressures without compaction The material normally used is a knit fabric that is coated with an epoxy resin to give it additional strength This material is normally 0 010 25 mm to 0 016 0 41 mm ice For high pressure applications gt 600 psi 40 bar a special permeate carrier fabric must be used Maximum pressure for most spiral elements is around 1 200 psi 83 bar Be Central Core Tube Permeate Carrier Fabric TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 377 TriSep Engineering Manual us TRIS gt CORPORATION Once the element is wound it needs some device to hold it together to keep it from unraveling This can be done u
478. ns it is a requirement that some of the process fluid must by pass or flow around the outside of the element to insure that this annular area is continuously flushed and that there are no areas in which product can become stagnant or which are not fully exposed to cleaning agents Different manufacturers employ different means of enclosure in an attempt to provide mechanical stability for the element while assuring this by pass flow These methods include a cage wrap or alternatively a net wrap around the outer diameter of the element Either 1s considered soft wrapped and allows a significant amount of the feed flow to by pass around the outside of the element A third method the hard shell TurboClean design by TriSep Corporation incorporates an impermeable hard plastic shell with a machined groove that spirals around the shell from end to end to allow bypass flow In the food and dairy industry membranes are installed in multi stage continuous recirculation systems The variation in the specific permeate flux at different concentration levels changing viscosities and different fouling characteristics of the process streams requires high recirculation flows to insure adequate feed flow through the membrane element A constant velocity over the membrane surface of the process liquid 1s maintained by a recirculation pump in each stage Stages contain a number of pressure vessels all connected in parallel to a main feed manifold
479. nt Series M W C O 100 000 Performance is based on the following test conditions 500 0 ppm Dextran 30 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type Configuration Active Membrane Area Recommended Applied Pressure Maximum Applied Pressure Recommended Operating Temperature Feedwater pH Range Chlorine Tolerance Maximum Feed Flow Minimum Brine Flow Permeate Flow Ratio Maximum SDI 15 minutes Maximum Turbidity AUM Advanced Ultrafiltration Membrane Spiral Wound Fiberglass Outer Wrap 360 ft 33 4 m 20 200 psi 1 4 14 bar 600 psi 41 bar 35 113 F 2 45 C 2 11 continuous 10 0 ppm 80 GPM 18 m3 hr 5 1 Element Weight Length A 45 20 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater cond
480. nthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TurboClean Sanitary Elements for Diary Applications TRIS CORPORATION The TurboClean element can reduce by pass flow by 35 44 when compared to commercially avail able sanitary membrane elements This improves overall hydraulic control in the pressure vessels resulting in energy savings improved membrane life and significant improvements In processing and cleaning efficiency The TurboClean element was developed by TriSep Corporation as a sanitary membrane that uses a hard outer shell A basic design requirement of a sanitary element is that it has no dead zones or non flow areas Conventional spiral wound elements use a brine or peripheral seal to prevent feed water from bypassing through the annular area formed between the pressure vessel inner diameter and the element outer diameter This results in a dead zone or stagnant area between the outside of the element and the inside of the pressure vessel For food and dairy applicatio
481. o Corporation Landfill Leachate Safely Recharged Into Groundwater Supplies Using Ultrafiltration and Reverse Osmosis Case Study Florida USA The Challenge A municipal landfill in southwest Florida was faced with the problem of treating their leachate for safe environmental discharge In Florida all landfill sites must collect any drainage rainfall from the solid waste cells so that it does not penetrate and contaminate the shallow water tables Due to the high suspended solids content and Salinity of the water the wastewater requires extensive treatment before it can be safely re introduced to the water tables The Solution It was determined that ultrafiltration UF and reverse osmosis RO would provide the most effective treatment solution for the landfill A pre existing coagulation filtration system would be utilized as pre treatment to the UF RO system SpiraSep 900 membranes were selected for the ultrafiltration system he Results Raw leachate is collected from a series of solid waste cells and transferred to a holding pond Wastewater is coagulated with ferric chloride and passed through a sand filter Effluent from the sand filter is For additional information regarding SpiraSep UF membranes please contact Mike Snodgrass at 1 805 964 8003 ext 113 or send e mail to snodgrass trisep com fed directly to the SpiraSep ultrafiltration system Typical turbidity levels of the sand filter effluent are lt 4
482. oJo u Q8 3n d PUA cp Lv 10j ouuoo1oju Snid PUA cp t 1oloouuoosz lu 3n d puq 8 8c JOJIOUUOSIOU PO L 3n d puq 0 89 1oj ouuooJo ju ZO Ott 3n d puq S Ic BNI PHOS 11072ouuoo19 u GE OC HOGG IO Z I JOJIOUUOSIOW 6 II suwu OI 8I 6 00 T Or LV lt 18509 OI 06 0T Iv SI Iv vi vv Oc 96 IC vv Oc 96 IC OL I 00 c UU oC CH 61 81 6 00 T OEL LV lt 18509 OI PAA oo S A A A AAA UO UO FHA gn Gei uo on OA d JAd JAd AION 193 AI 1 JAd JAd JAd ouoJj ns odq ouoj ns odq ouoj ns od ouoj ns oq AION ouoj ns od ouoj ns odq JAd JAd JAd AION 193 AI OI d1 09 1 AISI TI 0S1 HI 0S1 qn L 9 107 suoru ur g AICI AISTII AISTI AIII AIII QIASIT QI SIT duct I duct I duct I Cd Lucl TI 0S1 TI 0S1 d1 09 1 OT qn I 9 107 suoru utr g S dout S dogu ag doeut S doSul uondri95s Gq 0SIOI L OSTOI L 8 80I L I 8ecOl L SUMEI Jo oged VXX XXXX 0p 8 600vCII VXX XXXX 0p 8 OCCvcII VXX XXXX 0p S8 CCOVCII VXX XXXX 0p 8 OCOVCII Spo juouropq quinw LI SIN ANZIA WALAN VIC HONI S 8 SIMS OFS8 9 A1S soruouis ueo ooqung o A1S PIO ueo ooqun o A1S PIO duio um dural usrH duro L ysty oqung 314S plo duro L ysty oqung 314S plo ueo ooqunq ueo ooqun OLAI JUJA s SOJT S d
483. of many mathematical equations to take into account changes in temperature flow pressure and feed water quality TRON is designed to make normalizing data a simple task The Windows based software has a simple set up screen to input your specific system variables such as array number of elements per tube units of measure and variables to convert conductivity to TDS and osmotic pressure Individual data points are input into a spreadsheet type matrix The program calculates the normalized values which are displayed in a graphical format Multiple RO systems can be input into the database 2 INSTALLATION The hardware requirements to run TRON are an IBM PC compatible type computer 486 or equivalent Windows 95 98 NT 2000 or XP a hard disk with about 10 megabytes of free space a CD a printer and 64 megabytes of memory A color monitor is desirable To install the TROIN software onto a hard disk Place the TROIWIN TRON CD into your drive Once the CD is inserted it will automatically bring up a Menu screen Click on the menu TRON for Windows Ver 1 1 This will automatically start the setup program In case the Cd does not autostart at the Winows Desktop click on Start and then on Run and type in d normalization setup exe where d is your CD drive Your CD drive may have a different drive designation that 1s it could be assigned to e or s or any other letter If unsure of your drive letter right click on Start and then on Explore
484. ofiltration Membrane CGopnfguraton a k Spiral Wound High Temperature Turboclean Shell Active Membrane Area 70 ft 6 4 m Recommended Applied Pressure Not applicable Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 5 ppm nominal 1 0 ppm max Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Apple AMOI u u usu uo iA Whey Demineralization iQ MD Hn VI ATTI il LWkakkk uukh AN ANA ALI MAPLE H N 1 1 L LL T lh hhh AEN MAU MK l T lata A LA AM I d Element Weight 15 7 Length A 33 00 838 Diameter B 4 2 106 Permeate Tube C 0 83 21 2 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Sanitary Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Pa
485. ograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Lum 8 5 ACM LP Low Pressure RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8540 ACM4 TSFA 17 500 66 0 99 00 98 00 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM LP Fully Aromatic Polyamide Low Pressure Advanced Composite ele el ie le NP Spiral Wound Fiberglass Outer Wrap Active Membrane Area 440 ft 40 4 m Recommended Applied Pressure 50 300 psi 3 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm
486. olyamide Advanced Composite Membrane Oe TN e E Spiral Wound Turboclean Shell Active Membrane Area 355 ft 32 6 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU ADDIIG300I1 uuuu uuu A degen Dialysis Make up Water Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION
487. om PRODUCT SPECIFICATION LS CS 3 9 ACM High Temperature Turboclean RO Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 3940 M2D7U8 1 750 6 0 99 50 98 50 Performance is based on the following test conditions 2 000 00 ppm NaCl 225 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Configuration Spiral Wound High Temperature Turboclean Shell Active Membrane Area 70 ft 6 4 m Recommended Applied Pressure Not applicable Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr sD Minimum Brine Flow Permeate Flow Ratio 5 1 v s ED Maximum SDI 15 minutes 5 0 APPRON Maximum Turbidity 1 NTU olei m Whey Concentration LN l 4 P IK d Element Weight 12 5 4 Length A 38 75 984 Diameter B 3 9 99 Permeate Tube C 0 83 21 2 Units
488. ominal 1 0 ppm max Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU APPIANO c Pa Whey Demineralization i MUI LU AM A LI MAU WW M dl I it MA MU NW WM I Element Weight 15 7 Length A 39 984 Diameter B 3 8 96 Permeate Tube C 0 83 21 2 Units in pounds and inches units in paranthesis in kilograms and millimetes Dim A does not include ATD Mechanical Configuration Sanitary Style Core Tube ATD not included with element Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Ns 3 8 XN45 High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 3840 N2D9U8 1750 6 0 95 00 92 00 Performance is based on the following test conditions 2000 ppm MgSO4 110 psi 25 C 15 recovery pH 8 30 minutes operation OPERATIONAL AND DESIGN DATA
489. on in feed stream The term salt reyection is 100 minus the salt passage Salt passage increases as the applied pressure is decreased This increase results from the lower water flow rate at deduced pressure and consequently less dilution of the salt which continues to flow at a constant rate TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 374 TriSep Engineering Manual TRI Sep Performance Variables CORPORATION Conversion or recovery affects salt passage and product flow As conversion is increased the salt concentration on the feed brine side of the membrane increases causing an increase In salt flow rate as indicated by Equation 2 In addition the higher salt concentraion in the brine can significantly increase the osmotic pressure thereby reducing the water flow rate according to Equation 1 Actual water flow rate and salt rejection are always less than theoretical because of the pheneome non of concentration polarization As water flows through the membrane and as salts are rejected by the membrane a boundary layer is formed near the membrane surface in which the salt concentration exceeds that in the bulk solution This enrichment of the salt concentration is called concentration polarization The thickness of the boundary laryer is dependent upon the stirring or streaming velocity however the salt in the boundary layer must return to the bulk so
490. on pump and cartridge or bag filter This cleaner works best when applied at a flow rate of 8 10 gpm per 4 pressure tube or 30 40 gpm per 8 pressure tube at a pressure of between 20 50 psi at a pH of 7 7 8 Add 2 Ibs of TriClean 212CA per 15 gallons of RO permeate or DI water Recirculate solution for 1 hour checking pH regularly Use sulfuric acid to lower pH and add additional TriClean 212CA or sodium hydrox ide to increase pH Shutdown pump and allow to soak for 1 hour After soak recirculate for an additional 20 minutes and then rinse PACKAGING TriClean 212CA is shipped as a powder in 4 Ib 10 x 4 Ib 40 Ib and 100 Ib plastic containers Pricing is F O B our factory in Goleta CA Salem VA or Duisberg Germany Delivery for most orders is 1 2 days after receipt of order MSDS SHEETS For the most up to date information on MSDS sheets please contact our web site at www trisep com 320 TriSep Corporation Chemical Manual TRIS CORPORATION TRICLEAN 212TF HIGH PH POWDER CLEANER e Used to remove biological organic and colloidal fouling on Polyamide Composite mem brane e Effective for emulsified oil and silica PROBLEM In many installations worldwide polyamide com posite RO and NF membranes can become fouled with biological organic and colloidal foulants These foulants can quickly lead to a loss of system performance associated with a decrease in perme ate flow and increase in diff
491. oration 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 336 m TriSep Corporation Chemical Manual LEA S and TRIS S CORPORATION TEMPERATURE CORRECTION FACTOR Factor 1 22 1 2 1 19 1 17 1 15 1 13 1 11 1 1 1 08 1 06 1 03 1 02 1 00 0 98 0 97 0 96 0 94 0 93 H Q 0 90 Q 89 UR 0 86 0 85 0 84 0 82 0 81 0 80 6 amp 2 1a 35 0 64 4 1 24 35 5 05 9 TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 337 emm TriSep Corporation Chemical Manual TRIS gt CORPORATION PRESCRIBED CLEANINGS Types Of Foulant Prescribed Cleaning In order of use CA Minerals scales metal Oxides TSC 1 TSR 1 TSR 2 px Silts Colloids Organics TSC 3 TSR 1 TSR 2 Silts Colloids Organics TSC 4 TSR 1 TSR 2 x f Scales metals silt Colloids Organics TSC 1 TSR 2 TSC 3 TSR 1 TSR 2 Sp Scales metals silt Colloids Organics TSC 1 TSR 1 TSC 4 TSR 1 TSR 2 x Light Biological TSC 3 TSR 1 TSR 2 X Moderate Biiological with without TSC 1 TSR 1 TSC 2 TSR 1 scales metals and or silt organic colloid TSC 3 TSR 1 TSR 2 Moderate Biological with without TSC 1 TSR 1 TSC 2 TSR 1 scales metals and or silt organic colloid TSC 4 TSR 1 TSR 2 Very Heavy Biological with without TSC 1 TSR 1 TSC 2 TSR 1 scales metals and or silt organic colloid
492. ouoJj ns oq I d I ejo v dr euogj nsA oq dr JAd VOV 8395 V d L ouogj nsA od ed TL JAd VOV ouogj nsAT oq d 83995 V dr ouogj nsAT oq qr ouogj nsA oq av OAd I d L JAd dr JAd OAd I Sd L JAd dr JAd JAd JAd OAd SS 7 odAL OAd SS T ed T JAd JAd OAd c d I OAd I d L JAd vor JAd sra arn JAd dr 61193 AI PPoW Jajdepy qmniI 34nssoaq siojedpvy pavoquy Surrid pue JsrT SUE 1rejuog peamjonas TS v ouropo 1rejuog peamjonas TS v ouiopo SOIUOUIS SoIUOUIS Irejuog peamjons Ts v ouropo 1rejuog pemjons TS y ouropo Irejuog peamjonas TS VUP SOIUOUIS SoIUOUIS Irejuog pemjons TS v ourpopo SOIUOUIS Irejuog pemjons TS v ourpopo Irejuog pemjonjs TS v out opo 1rejuog pemjons TS v ourpopo SOIUOUIS 1rejuog pemyonas S v ouropo exeog 2o101d SoIUOUIS 1rejuog pemjons TS v ouropo ININS K9JO L gurp nedg SoIUOUIS SOIUOUIS oxueq OWN sulojs S pin sjonpolg ejueuruoJrAusq sjonpolg puw omg Jejogq Temon d s TS V Sul spo Irejuog pemjons TS v utlopoO Irejuog pemjonns TS VUP J9 1nj9egjnu Ar oqn Inss id I7cc OI L C C9 0TI L cCOtOI L C 8IvOI L 8l1vOI L T 8080 I L 0901 L C 8080I L C CCE OT L e STVOI L CCeOI L Dab I 81v0I L Dab I 8ITOI L COVIIT L I8cOI L CCCOT L 06cOI L 61 cOI L SILOI L SEO 9LEOI L 89COI L I C LOSOT LL SOU ccOT L H SUIMBIG 989 Jo u
493. out els desur eps desur ais dog uondri5s Gq C I 80I L 6c60I L I v 80I L C 6c601 L C Yt80I L C 6c601 L C Yt80I L C OS80I L C O8ZLOI L OS80I L O8ZOI L 0SIOI L OSTOI L 8 80I L I 8ecOl L SUIMBIG VOXX XXXX 0p 8 CIOIVCII SXX XXXX 0v 8 SS0vCII SXX XXXX 0v 8 CEOVCII HXX XXXx Qpe8 LICVCII HXX XXXX Qpc 8 SIvcII D XX XXXX 0v 8 LICVCII DXX XXXX 0v 8 SIvcII SJIXX XXXX 0pt 8 OSCVCII SJIXX XXXX 0p 8 OSIVCII OJIXX XXXxX 0pec8 IST DAXX XXxXxX Q7E8 OLIVCII VXX XXXX QPE8 600vCII VXX XXXX 0pc 8 OCCVCII VXX XXXX 0p 8 CCOVCII VXX XXXX 0p 8 OCOVCII SPPON uwy quinw Lg SLNHIAAW TM WALA VIC HONI 8 SIMS opes suwy Aurumq snid 10329uu02J93U SUNIA pue jsrT SUE 424 TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax e www trisep com 0703 WY tS 01 8007 67 01 LO cI c AN qn L 9107 TT S 8 0 Or v eqn 9107 TT S 8 0 Or t XX XXXX 0p8tc SSCrCIHI SXX XXXX 0y8t SSCvCII Spo juw SLNAWHATA AALANWVIAd HONI SMIS OF8E JoquinN Med sury O 21 XXX XXXX PSZ I90 cvI XXX XXXX 0PST OOOECII qn L 2107 AMS JUHA ZT 0 qn L 9107 IJUMA 60 Z S 9po A juw SLNAWHATA AALANWVIA HONI 8S Z S H9S 0pSc JoquinN LUS SSUTH O O I pue seas vung SUNIA pue JSr SUE p Jo 38ed 425 TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax e www t
494. outh La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TRIS gt CORPORATION Permeate flow Model GPD m3 day 8340 N6I8Y1 15 000 56 0 PRODUCT SPECIFICATION 8 3 AUM Ultrafiltration Turboclean Element Series M W C O 10 000 Performance is based on the following test conditions 500 00 ppm 10K PEG 30 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type e Oe ESL OP asco uuu uuu uuu yuana Active Membrane Area Recommended Applied Pressure Maximum Applied Pressure Recommended Operating Temperature Feedwater pH Range Chlorine Tolerance Maximum Feed Flow Minimum Brine Flow Permeate Flow Ratio Maximum SDI 15 minutes Maximum Turbidity PAO DNC AUG a PE A Element Weight 50 23 Length A 40 00 1 016 Diameter B 8 30 210 AUM Advanced Ultrafiltration Membrane Spiral Wound Turboclean Shell 372 ft 34 6 m 5 200 psi 0 3 14 bar 600 psi 41 bar 35 140 F 2 60 C 2 11 continuous 10 0 ppm 80 GPM 18 m3 hr 5 1 5 0 1 NTU Enzyme Concentration
495. oval of poly mers and emulsified oil PROBLEM In many installations worldwide RO mem branes can become fouled with sulfate scale polymers and or manganese dioxide These foulants can quickly lead to a loss of system performance associated with a decrease in permeate flow and increase in differential pressure and a loss of element rejection If left unchecked this fouling can permanently damage the membrane elements leading to costly and premature membrane replacement SOLUTION TriClean 211 when used in conjunction with TriClean 210 or TriClean 217 removes sulfate scale polymer fouling and or manganese diox ide without damaging sensitive polyamide com posite membrane elements TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 TriSep Corporation Chemical Manual APPLICATION TriClean 211 should be mixed in a cleaning tank equipped with a mechanical mixer heater low pressure recirculation pump and cartridge or bag filter This cleaner works best when applied at a flow rate of 8 10 gpm per 4 pressure tube or 30 40 gpm per 8 pressure tube at a pressure of between 20 50 psi Add 1 gallon of TriClean 211 per 100 gallons of RO permeate or DI water Recirculate solution for 1 hour check ing pH regularly Shutdown pump and allow to soak for 1 hour After soak recirculate for an additional 20 minutes and then rinse PACKAGING TriClean 21
496. over the newer polyamide membranes for applications with high organic fouling such as wastewaters and waters where biological growth is an issue easily addressed using chlorine There is large installed base of CA membranes in many different applications and the SB series of membrane elements from TriSep can satisfy most retrofitting or new system applications The SB series of membrane elements from TriSep are available in 2 5 4 8 8 3 and 8 5 diameters There are three different membranes offered the SB20 SB50 and SB90 The SB20 offers the highest rejection at 98 while the SB50 offers 20 higher flow at 95 salt rejection The SB90 1s a nanofiltration NF membrane Operating at about twice the flow of the SB20 at 85 90 rejection 2540 SB20 TSF 2 5 diameter by 40 long 0 75 male O D permeate tube 4040 SB20 TSA 4 0 diameter by 40 long 0 75 male I D permeate tube 4040 SB50 TSA 4 0 diameter by 40 long 0 75 male I D permeate tube 4040 SB50 TSF 4 0 diameter by 40 long 0 75 male O D permeate tube 8040 SB20 TSA 8 0 diameter by 40 long 1 50 male I D permeate tube 8040 SB20 TSOA 8 0 diameter by 40 long 1 14 male I D Osmo style permeate tube 8040 SB50 TSA 8 0 diameter by 40 long 1 50 male I D permeate tube 8340 SB20 TSOA 8 3 diameter by 40 long 1 14 male I D Osmo style permeate tube 8540 SB20 TSA 8 5 diameter by 40 long 1 50 male I D permeate tube 8540 SB20 TSA 8 5 diameter by 40 long 1 50 mal
497. ow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU APPICCIU Race ee u u ne HE ee acre Whey Concentration m J C p W w v Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION k 8 ACM RO High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 M2G4T9 9 400 35 0 99 00 98 00 Performance is based on the following test conditions 2 000 00 ppm NaCl 225 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Configuration Spiral Wound High Temperature
498. ow pH cleaning with TriClean 210 or TriClean 310 except for emulsified oil fouling in which case the order should be reversed Please see guielines for operation for Ph and tem prature limits PACKAGING TriClean 214TF is shipped as a liquid in 5 gallon plastic pails or 55 gallon plastic drums Pricing is F O B our factory in Goleta CA Salem VA or Duisberg Germany Delivery for most orders 1s 1 2 days after receipt of order MSDS SHEETS For the most up to date information on MSDS sheets please contact our web site at www trisep com 805 964 8003 805 964 1235 fax www trisep com e 0105 325 TriSep Corporation Chemical Manual TRIS CORPORATION TRICLEAN 217 LOW PH LIQUID CLEANER e Used to remove polymers emulsified oil and manganese dioxide PROBLEM In many installations worldwide polyamide com posite RO and NF membranes can become fouled with polymers emulsified oil or manganese diox ide foulants These foulants can quickly lead to a loss of system performance associated with a decrease In permeate flow and increase in dif ferential pressure and a loss of element rejection If left unchecked this fouling can permanently damage the membrane elements leading to costly and premature membrane replacement SOLUTION TriClean 217 is a low pH cleaner that should be used In conjunction with TriClean 211 This com bination of cleaners will remove polymers emulsi fied oil or mangane
499. p com 0105 116 PRODUCT SPECIFICATION NI 3 8 X 20 High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 3838 N1E8U8 1 700 6 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane E ele let ig e EE Spiral Wound Turboclean Shell with FoulGuard Technology Active Membrane Area 68 ft 6 2 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Applicationi u u u uuasaaa sakha napawakaq Egg Concentration Element Weight 12 5 4 Length A 38 0 965 Diameter B 3 8 96 Permeate Tub
500. p0 o ea J94n33egnu A qn L nss id esse JOOUUOD JOOP SI 0p SutopoO p Jo c oSeq CCLOT L CCLOT L CLCOT L V LI OI L I ZI OI L C L81IOI L I IZCTI AL Cv60I L S9CTI L KE V8cOI L ccecOl L L8LOI L 68t0I L LvVTI L OTLITI L IScOI L 80L0T L I 80Z0I L 06 0I L I 2810I L SIIOI L 6760I L 6IvII L 88IOI L NACH LSCOI L GI e LZ810I L I Z810I L H SUIMBIG S 9po A 3uouro q IOrvCTI VQXx Xxxx 0p08 CLIVCII V Xx Xxxx 0Qv08 060vClHI VQXx XXxX 0v08 C8CVCII VQ Xx XXxX Qp08 9S0ETI I VXX XXXX 0v08 LOtvCII VXX XXXX 0v08 ICEVCII VXX XXXX 0v08 60cr lt ll VXX XXXX 0v08 680vCII VXX XXXX 0v08 60vCII VXX XXXX 0v08 CCOVCI I VXX XXXX 0v08 COVCII VXX XXXX 0v08 CICVCI I VXX XXXX 0v08 Trip VXX XXXX 0v08 SSCVCII VXX XXXX 0v08 OSEVCI I VXX XXXX 0v08 90cr lt ll VXX XXXX 0v08 OrOvCIUI VXX XXXX 0v08 VCOVCI I VXX XXXX 0v08 CECCI I VXX XXXX 0v08 CIIVCII VXX XXXX 0v08 LIOVCII VXX XXXX 0v08 vIOvVCIUI VXX XXXX 0v08 96cvclI VXX XXXX 0v08 8ECVCII VXX XXXX 0v08 SIOVCII VXX XXXX 0v08 LIOTCII VXX XXXX 0v08 IOvCII VXX XXXX 0v08 960vCII VXX XXXX 0v08 S8CrCII VXX XXXX 0v08 LIOvCII VXX XXXX 0v08 P6CVCI I JoquinN yed SLNWIATH AALAWVIA HONI 8 S998 07 08 419 TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax e www trisep com 0703 WV S 01 8007 67 01 LO TCI T 99 Sqn L 3100 IUA 6C LTIS S A S 19 depv qn1 9107 Joydepe pyeoqut oC c
501. plied Pressure Recommended Operating Temperature Feedwater pH Range Chlorine Tolerance Maximum Feed Flow Minimum Brine Flow Permeate Flow Ratio Maximum SDI 15 minutes Maximum Turbidity X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane Spiral Wound Turboclean Shell with FoulGuard Technology 70 ft 6 4 m 100 300 psi 7 21 bar 600 psi 41 bar 35 140 F 2 60 C 2 11 continuous 0 1 ppm 20 GPM 4 5 m3 hr 5 1 5 0 1 NTU PROD NC AUOM uu RERO IRR RR RR ERE Hemodialysis aS s LLLI HE EE j ug a ANN vo Blu MM WO i ili IA I MAAN WW II d VCI AM n Ou MODO LU TU LL M d in LO AM M M M NA d W MI M I OM WAN M 1 dU s SEN 7 A Element Weight 12 5 4 Length A 38 8 984 Diameter B 3 8 96 Permeate Tube C Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Sanitary Style Core Tube 0 031 thick diamond spacer 0 83 21 2 Feed Spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation
502. pm MgSOA 110 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ANM Aromatic Polyamide Advanced Nanofiltration Membrane Configuration Spiral Wound Fiberglass Outer Wrap Active Membrane Area 400 ft 37 2 m Recommended Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 4 0 Maximum Turbidity 1 NTU Element Weight 50 23 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 028 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS
503. pplicable Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 10 0 ppm Maximum Feed Flow 80 GPM 18 m3 hr sD y M Minimum Brine Flow Permeate Flow Ratio 5 1 v s V 0 Maximum SDI 15 minutes 5 0 APPROV d Maximum T urbuditv 1 NTU Application Whey Fractionation Element Weight 50 23 Length A 38 965 Diameter B 7 9 200 Permeate Tube C 1 14 29 0 Units in pounds and inches units in paranthesis in kilograms and millimetes Dim A does not include ATD Mechanical Configuration Filmtec Style Core Tube ATD not included with element Feed Spacer 0 031 thick diamond spacer Engineered Membrane u SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION l 8 AUM Ultrafiltration Turboclean Element Series TRIS CORPORATION Model M W C O 8038 N6D9V9 10 000 OPERATIONAL AND DESIGN DATA Membrane Type AUM Advanced Ultrafiltration Membrane Configuration
504. premises TriSep will have the right to specify reasonable remedies other than replacement repair or addition of element s to restore performance to TriSep specified levels TriSep s Returned Goods Authorization RGA Procedure must be followed for return of element s Element s shipped to TriSep for warranty examination must be shipped freight prepaid Unless specifically agreed to in writing by TriSep prior to shipment all collect and or COD deliveries will be refused by TriSep If the Customer desires replacement element s to replace those alleged to be defective or those returned to TriSep for warranty examination Customer is responsible for providing any needed replacements until warranty examination is complete Element s examined as part of a warranty claim which are found by TriSep to be performing as warranted will be returned to the Customer freight collect with appropriate charges minimum US 100 00 made for TriSep handling inspection testing or analytical services as described in TriSep s RGA Procedure Replacement by the Customer of element s under Extended Element Performance warranties will be at the then current selling price per TriSep s Standard Terms and Conditions plus handling charge for each returned element If in connection with any TriSep inspection and testing of products and or system on the Customer s or end user s premises a claim under the Extended element performance warranty is determined by Tri
505. pressure vessel in a continu ous recirculation stage The vessel was equipped with flow control valves on the feed and concentrate side pressure gauges on feed and concentrate and flow meters to measure the concentrate and permeate flow The tests showed a reduction in feed flow rate of 44 when comparing the TurboClean elements versus conventional soft wrapped elements What effect will this new element design have on the food and dairy industry The hard shell TurboClean energy savings can be as high as 44 of the required recirculation flow and in certain application a corresponding decrease in required cooling energy Improved hydraulic flow control may also lead to increased membrane life and improved membrane cleaning efficiencies Although initial tests tend to support this hypothesis conclusive data is still pending Effects of improved hydraulic flow control may result in improved separation efficiencies since the effect of high by pass flow is to reduce membrane cross flow and increase concentration polarization a higher solute concentration at the membrane surface than in the bulk stream on the membrane surface Reduction of concentration polarization 1s directly related to cross flow rates in the membrane element Following are a list of TriSep TurboClean products specifically designed for the food industry TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trise
506. prompt you to fill in the fields When the system has calculated properly the middle section of the screen will be filled in The View and Print buttons will also change from a grayed out button to the active color button This indicates that the button is now available for use The view button allows a quick look at additional calculated values The view button displays all of the raw feed permeate and concentrate concentrations in ppm and CaCO3 In addition the TDS and pH s are displayed Below these fields the saturation indices are displayed followed by the osmotic pressures Lastly recommended antiscalent model and dosages are given along with dosage of acid or caustic 1f needed TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 400 TriSep Troi Design Program A Manual ver 2 0 0 TRIS CORPORATION There are now two print outs The projection print out and the individual element print out The projection print out gives details on the system design and the feed brine and permeate water analysis The individual element print out gives details on the permeate flow TDS Beta flux and net driving pressure for each element in a system The Print button allows you to print the entire projection To view the print out on the screen select File Print Preview This is a two page report that can be viewed on the screen sent to a printer or saved as a
507. provide freeze protection down to 26 F 3 C For lower temperatures the solution may be added at a ratio of 1 gallon of TriStore to 1 gallon of RO permeate or DI water This will protect the membranes down to a temperature of 19 F 7 C This solution should be replaced every 3 6 months Flush permeate to drain for at least 30 minutes prior to bringing system back on line PACKAGING TriStore 110 is shipped as a liquid in 5 gallon plastic pails or 55 gallon plastic drums Pricing is F O B our factory in Goleta CA Delivery for most orders is 1 2 days after receipt of order MSDS SHEETS For the most up to date information on MSDS sheets please contact our web site at www trisep com TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 335 emm TriSep Corporation Chemical Manual TRIS gt CORPORATION HOW TO DETERMINE WHEN TO CLEAN YOUR MEMBRANES Although there are Flow Normalization calculations that are based on projected membrane performance data system design or operational modifications can hinder the accuracy of these calculations In order to simplify the calculation and to track your system s actual performance this calculation will help to determine present membrane performance vs performance at start up If the calculation determines that Normalized Flow has declined by 10 or more it is time to schedule a cleaning for the membra
508. psi 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 15 7 Length A 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 62 15 9 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Desal DuPont Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Zia 4 X 20 Low Fouling RO Element Series TRI CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 X201 TSDA 2 450 9 0 99 50 98 50 Performance is based on the following test conditions 2 000
509. psi 41 bar 35 113 F 2 45 C 2 11 continuous 10 0 ppm 95 GPM 22 m3 hr 5 1 5 0 1 NTU Beverage Water Make Up Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 047 thick parallel spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TurboClean Sanitary Elements for Dialysis Applications I TRI CORPORATION TurboClean elements have been used extensively in the dialysis make up water market Although not required by law by the FDA contamination of dialysis make up water can result In advarse patient reactions The sanitary nature of the TurboClean element provides a continous by pass flow around the outside of the element This eliminates the stagnant area normally present on standard brine seal elements which can result in bio growth that can contaminate the beverage product This stagnant area 1s difficult to clean or sanitize in place as there is no flow of cleaning or sanitizing chemicals into this area If cleaning or sanitizing chemicals do get into this area it is diff
510. q S 10 99UU09 19 UT SUNI pue jsrT SUE 422 TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax e www trisep com 0703 WY vS 01 8007 67 01 JO c ase 423 OT LOSS CL uv l 9b 7 00 01 OA d w l T7 4081 VOXX XXXX p08 I09LI L VXX XXXX 0p08 UPP Sn d eqng 3109 SS GI F I 97 c 00 0I OAd aO T7 4081 VOXX XXXX p08 09I L VXX XXXX 0p08 tOvYvCII doy 0 doe O I eler 00 SI JAd w6lT 4081 VOXX XXXX p08 OOSTI L VXX XXXX 0p08 CotrclI OWSO S L SHL DT 87 0 Iocl OAd w l T7 4081 VOXX XXXX p08 IScOl L VXX XXXX 0p08 O9IOvCII YOW S L desur OIT 61 c 00 SI OAd uSC T7 4081 juouio g surojs s prn 4 uo0 gt SLCII L VXX XXXX 0p08 CCEVCIT SMH SL d SHI OT LC VES I9 vl JAd GdOOST 0SI juwo SMH p60I L VXX XXXX 0p08 00tvCIT juodn q Teseq doeut T TETES Se EI OAd uSLIL 7 0SI VQxx Xxxx 0Qp08 0StOI L VXX XXXX 0v08 L80rvCII OI YWA oj eseqppuodnq 6p se SI euoj nsAqoqd uCETE 7 SEI VQxx Xxxx 0Qp08 CC6880I L VJXX XXXX 0p08 vo6crclI OI SoTL oj eseqpiuodnq c8 CC L 6 OAd cl I SEI VQxx Xxxx 0Qp08 I c880I L VAXX XXXX 0p08 t6cvcII 1ojoouuooJojUu c T st 9 SAd dO uu ce o 41s ALIO L VE9OI L V LXX XXXX 0p08 6ICHCII Sn d puq ST 9 Iv SI JAd AIII ueo ooqm L9 43S PIO T 6601 L SXX XXXX 0p08 SSOVCIT JojoouuooJo9 u CC OLYI JAd AISTI ueo ooqm L9 43S PIO I v 830I L SXX XXXX 0p08 CtOVCIT Sn d PUA 6t6c LS CI JAd TI
511. qa mau Spiral Wound Fiberglass Outer Wrap with FoulGuard Technology Active Membrane Area 85 ft 7 9 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 2NTU Element Weight 15 7 Length A 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Zee 8 ACM RO Element Series TRIS gt CORPORATION Perme
512. r Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 4 0 Maximum Turbidity 1 NTU TS80 b Technology Element Weight 50 23 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 028 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane Bee SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION 8 TS80 Nanofiltration Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 TS83 TSA 10 000 37 0 98 50 97 00 Performance is based on the following test conditions 2 000 0 ppm MgSOA 110 0 psi 25 C 15 recovery
513. r shutdown to remove the supersaturated salt solutions Recovery ratio shall be consistent with concentration of sparingly soluble salts Membrane scaling caused by failure of the chemical dosing system e g Ca Ba or Sr salts shall nullify and void the warranty IP Ksp for CaSO BaSO SrSO and CaF where IP is the ion product of brine stream Ksp is the solubility product IP CaSO lt 1 0 x 10 or 2 5 x Ksp whichever is larger if TriPol 8510 or TriPol 9010 is used where IP is the ion product of brine stream Ksp is the solubility product IP BaSO lt 70 x Ksp if TriPol 8510 or TriPol 9010 is used where IP is the ion product of brine stream Ksp is the solubility product IP SrSO4 lt 8 Ksp if TriPol 8510 or TriPol 9010 is used where IP is the ion product of brine stream Ksp is the solubility product IP CaF2 lt Ksp if TriPol 8510 or TriPol 9010 is used where IP is ion product of brine stream Ksp is the solubility product The brine silica shall be less than 150 mg l at 25 C unless an antiscalant approved by TriSep is used TriSep Corporation 93 S La Patera Lane Goleta CA 93117 805 954 8003 phone 805 964 1235 fax www trisep com TRIS 2 PAPA 8 T F Q Hi GUIDELINES FOR OPERATION DESIGN Modifications of any TriSep element and or component supplied by TriSep are not permitted unless approved by TriSep in writing In systems having 10 or more pressure vessels prov
514. r Saturation Index 2 6 Max CaSO4 Saturation 400 Max SrSO4 Saturation 1 200 Max BaSO4 Saturation 12 000 Max CaF Saturation 10 000 Silica 200 1n the concentrate Levels may be exceeded on occasion Contact TriSep for advice Silica saturation levels depend on a number of factors including trivalent metal ion concentration pH and tempera ture PACKAGING TriPol 9510 is shipped as a liquid in 2 gallon sample sizes 5 gallon 40 Ib plastic pails and 55 500 Ib gallon plastic drums Pricing is F O B our factory in Goleta CA Salem VA or Duisberg Germany Delivery for most orders is 1 2 days after receipt of order MSDS SHEETS For the most up to date information on MSDS sheets please contact our web site at www trisep com 316 TriSep Corporation Chemical Manual TRIS CORPORATION TriClean Membrane Cleaners TriClean is the only line of membrane cleaners engineered by a leading membrane manufacturer for use with high tech reverse osmosis RO and nanofiltration NF elements Using proprie tary knowledge of membrane chemistry and foul ing characteristics TriSep has developed TriClean cleaners to be compatible with today s membrane chemistries while providing maximum removal of mineral scales silica metal oxides colloids organics and biological fouling TRICLEAN 210 TriClean 210 is a high performance low pH cleaner formulated to remove acid soluble mineral
515. r all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION LS CS 3 8 ACM High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 3840 M2D2V6 1300 4 0 99 50 98 50 Performance is based on the following test conditions 2000 ppm NaCl 225 psi 25 C 15 recovery pH 8 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Configuration Spiral Wound Turboclean Shell Active Membrane Area 53 ft 4 9 m Recommended Applied Pressure Not applicable Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 25 GPM 5 6 m3 hr sD Minimum Brine Flow Permeate Flow Ratio 5 1 v s ED Maximum SDI 15 minutes 5 0 APPRON Maximum Turbidity
516. r by 40 long 0 75 O D male permeate tube protruding permeate tube 4040 ACM5 TWF 4 dia by 40 long 0 75 O D male permeate tube protruding permeate tube 88 ft 8040 ACM5 TSA 8 diameter by 40 long 1 50 I D female permeate tube flush cut 8040 ACM5 TSAN Same as 8040 ACM5 TSA but NSF approved 8040 ACM5 TSFA 8 diameter by 40 long 1 12 I D female permeate tube flush cut Filmtec replacement 8040 ACMS UWA 8 diameter by 40 long 1 50 I D female permeate tube flush cut 400 ft 8040 ACMS UWAN Same as 8040 ACM5 UWA but NSF approved TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 209 PRODUCT SPECIFICATION Ow NN 2 5 ACM LP RO Element Series TRIS gt CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 2540 ACM5 TSF 800 3 0 98 50 97 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 150 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane COMM QUIN GIOI L ste uqu La cet T Spiral Wound Fiberglass Outer Wrap Active Membrane Area 26 ft 2 4 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41
517. r the most up to date information on such as TriClean 212TF have failed This 1s a MSDS sheets please contact our web site at non chlorine oxidizing cleaner which can result in WWww trisep com performance loss of CA and polyamide composite membranes TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 323 emm TriSep Corporation Chemical Manual TRIS gt CORPORATION TRICLEAN 214CA APPLICATION LIQUID HIGH PH TriClean 214CA should be mixed in a cleaning tank equipped with a mechanical mixer heater CLEANER low pressure recirculation pump and cartridge or bag filter This cleaner works best when applied e Used to remove biological at a flow rate of 8 10 gpm per 4 pressure tube or 30 40 gpm per 8 pressure tube at a pressure of OHHO and colloidal fouling E between 20 50 psi at a pH of 7 to 7 8 for CA CA membrane membranes Add 3 gallons of TriClean 214CA per 100 gallons of RO permeate or DI water Recircu PROBLEM late solution for 1 hour checking pH regularly In many installations worldwide polyamide com Use sulfuric acid to lower pH and add additional posite RO and NF membranes can become fouled TriClean 214CA to increase pH Shutdown pump with biological organic and colloidal foulants and allow to soak for 1 hour After soak recirculate These foulants can quickly lead to a loss of system for an additional 20 minutes and then rinse
518. rance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr eD M Minimum Brine Flow Permeate Flow Ratio 5 1 u K Di TAL Maximum SDI 15 minutes 5 0 ApPRON Maximum Turbidity 1 NTU PODIIG AMOI MM Hc Lactose Demineralization Element Weight 15 T Length A 38 75 984 Diameter B 3 9 99 Permeate Tube C 0 83 21 2 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Sanitary Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION lt 4 2 XN45 High Temperature Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4233 N2D8U8 1 700 6 0 95 00 92 00 Performance is based on the following test conditions 2 000 00 ppm MgSOA 110 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type XN45 Polyamide Advanced Nan
519. rance 10 0 ppm Maximum Feed Flow 80 GPM 18 m3 hr sD A Minimum Brine Flow Permeate Flow Ratio 5 1 v s p A Maximum SDI 15 minutes 9 0 APPROV d Maximum Turbudtv 1 NTU ele e Tel EE Milk Fractionation Element Weight 50 23 Length A 38 965 Diameter B 7 9 200 Permeate Tube C 1 14 29 0 Units in pounds and inches units in paranthesis in kilograms and millimetes Dim A does not include ATD Mechanical Configuration Filmtec Style Core Tube ATD not included with element Feed Spacer 0 031 thick diamond spacer Engineered Membrane EE SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Lo N 8 AUM Ultrafiltration Turboclean Element Series TRIS CORPORATION Model M W C O 8038 N6D4V9 10 000 OPERATIONAL AND DESIGN DATA Membrane Type AUM Advanced Ultrafiltration Membrane Configuration Spiral Wound High Temperature Turboclean Shell Active Membrane Area 288 ft 26 8 m Recommended Applied Pressure Not applicable Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature
520. rane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION v 4 ACM RO Element Series TRIS gt CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 ACM2 TSDA 2 450 9 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Cong AMON uuu aa E oa akana URS Spiral Wound Fiberglass Outer Wrap Active Membrane Area 88 ft 8 1 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 15 7 Length A 40 0 1 016
521. rate stream These types of filters are normally operated with a significant cross flow velocity across the membrane surface to prevent fouling or scaling hence the name Cross flow filtration elements come in several forms There are hollow fine fiber based 0 1 mm diameter capillary 1 2 mm diameter fibers tubular 12 mm 25 mm diameter fibers plate and frame and spiral wound configurations Spiral membrane element designs dominate the RO and NF markets due to their high packing density flexible design low cost and excellent performance over a wide range of applications In the newly emerging back flushable UF market capillary membranes are currently dominating the market The SpiraSep element is the first spiral wound entry into this marketplace TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 372 TriSep Engineering Manual TRIS 3 Principles of Reverse Osmosis CORPORATION Osmosis is a natural process involving fluid flow across a membrane which 1s said to be semiper meable A semipermeable membrane is selective in that certain components of a solution usually the solvent can pass through it while others usually dissolved solids cannot The direction of solvent flow is determined by its chemical potential which is a function of pressure temperature and concentration of the dissolved solids If pure water contacts bot
522. rating Temperature Feedwater pH Range Chlorine Tolerance Maximum Feed Flow Minimum Brine Flow Permeate Flow Ratio Maximum SDI 15 minutes Maximum Turbiditly SB Cellulose Acetate Blend Spiral Wound Fiberglass Outer Wrap 350 ft 32 5 m 200 500 psi 14 34 bar 600 psi 41 bar 50 90 F 10 32 C 5 5 nominal 4 7 0 5 ppm nominal 1 0 ppm max 80 GPM 18 m3 hr 5 1 Element Weight Length A 45 20 40 00 1 016 Diameter B 7 9 200 Permeate Tube C 1 14 29 0 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Feed Spacer Osmo Style Core Tube 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TRIS CORPORATION Permeate flow Model GPD m3 day 8 500 32 0 OPERATIONAL AND DESIGN DATA Membrane Type COM QUT AON RE Active Membrane Area
523. rature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 15 7 Length A 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION 4 ACM RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 ACM3 TSF 2 00 10 0 99 20 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type
524. risep com 0703 WV SS 01 800C 6C OT y JO c e3eq SSULI C g s e9s uttq C t p TOT dd IW 998 JXX XXXX 0f0t FZIPZII SSULI C g s e9s oULIq C t p TOT dd J3MI9S vXx xxxx opot 6TIVCIT qn 2100 otusO 9 0 On dd Surq O O I Wat ouisQ LOPHTZII qn L 2107 AMS WHA 9T0 r00 Uda Surq O Ol Lxx xxxx 0rt0r 190 cv1 uc ooqin1 679 0 90 0 200 dd Surd O OT SXX XXXX 0t0t SEOETII emnjeoduro L u8TH 6 8 0 Z1 0 c 00 dd Sun O OTI HXX Xxxx 0p0r 6S0ETII LH ue ooqm p 679 0 80 0 200 dd SUIJ O OT 5XX xxxx 0p0r SCOETII ueo poqmn p As uA cT 0 c 00 dd Sung O OTI SAXX Xxxx 0p0r I90 cvI dural ut oqun p opAs oom cr0 On dd SURI O OT 54Xx xxxx 0por I90 cvI oqn L 2107 A S YI cT OS c 00 Uda Surq O Ol JAXX xxxx oror L9DETHI qn 1 2107 juodn j Teseqq 800 200 dd Sug O OT VGxx xxxx opor SEOETIT qn L 9107 desur cT 0 c 00 Ud Sunp O OI VXX xxxx 0pop IZOETIT eqn 2100 IAS IOUT 60 Z 680 dd fog ouug LXx xxxx opop T00 cIT qn L 9107 soruouis 60 c 6890 dd fes SULIG VOXX Xxxx opop IODETII omnje1oduro L YstH 60 6890 dd fog ouug HXX xxxx opop TOOECIT oqn 2107 JUA 60 c 680 dd fos vung JIXX XxXX 0p0t I00 c 1I oqn 2107 yuodnq eseq 60 7 680 dd fog ouug vqxx xxxx orop T00 c IT qn 2100 desu T 60 c 6890 dd fog ouug vyvxx xxxx 0rt0r IOOETIT Jd JS029 61 193 AI U93UIUIO BIS 69S BIS od KT BIS SPPON Juouors J9quinw JACI
525. rmeate Flow Ratio Maximum SDI 15 minutes Maximum Turbidity Application AWA Element Weight Length A 15 7 38 0 965 Diameter B NW l 1l m 1 mu UU 3 8 96 XN45 Polyamide Advanced Nanofiltration Membrane Spiral Wound Turboclean Shell 68 ft 6 2 m 40 200 psi 3 14 bar 600 psi 41 bar 35 140 F 2 60 C 2 11 continuous 0 5 ppm nominal 1 0 ppm max 20 GPM 4 5 m3 hr 5 1 5 0 1 NTU Coffee Extract Concentration WU UU E p MA 9A Permeate Tube C 0 83 21 2 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Feed Spacer sanitary Style Core Tube 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION 3 8 XN45 High Temperature Turboclean Element TRI gt CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 3838 N2E8V6 1300 4 0 95 00 92 00 Performance is based on
526. s Although TriSep stocks a large variety of inboard adapters In many cases customers want an exact mechanical retofit to their existing elements Most variations in elements center around different permeate tube diameters and or configurations male versus female There are also special element diameters 8 3 and 8 5 that some manufacturers have produced to try and minimize competition To address different permeate tube diameters TriSep makes a variety of elements to exactly retrofit many of our competitors elements In the 4 diameter we offer both the TriSep style permeate tube 0 75 I D female permeate tube as well as the more common Dow Filmtec style permeate tube 0 75 O D male permeate tube In the 8 diameter element TriSep makes a standard TriSep style 1 5 I D female permeate tube which 1s also being adopted by Dow Filmtec on their LE and XLE elements a Dow Filmtec style 1 12 I D female permeate tube and GE Osmonics style 1 19 I D female permeate tube and a Desal DuPont style 1 18 I D female permeate tube In 1991 TriSep purchased the Spiral Wound Assets from E I DuPont de Nemours and Company DuPont had a line of spiral wound elements that had permeate tube dimensions that are the same as the Desal permeate tubes To address different element diameters TriSep makes an 8 3 diameter element to retrofit Osmonics elements as well as 8 5 diameter elements to retrofit Hydranautics style elements Attached
527. s flow These methods include a cage wrap or alternatively a net wrap around the outer diameter of the element Either is considered soft wrapped and allows a significant amount of the feed flow to by pass around the outside of the element A third method the hard shell TurboClean design by TriSep Corporation incorporates an impermeable hard plastic shell with a machined groove that spirals around the shell from end to end to allow bypass flow In the food and dairy industry membranes are installed in multi stage continuous recirculation systems The variation in the specific permeate flux at different concentration levels changing viscosities and different fouling characteristics of the process streams requires high recirculation flows to insure adequate feed flow through the membrane element A constant velocity over the membrane surface of the process liquid 1s maintained by a recirculation pump in each stage Stages contain a number of pressure vessels all connected in parallel to a main feed manifold Conventional sanitary elements have significant clearances between the soft wrap and the inside of the pressure vessel resulting in by pass of feed flow around the element of 40 60 This adds to the required recirculation flow Comparative tests at a major California Cheese producer were performed to compare the by pass flow of the TurboClean element to a standard net wrap element by isolating one
528. s in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION L C38 4 TS80 Nanofiltration Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 TS83 TSF 2 300 8 0 98 00 96 00 Performance is based on the following test conditions 2 000 0 ppm MgSOA 110 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ANM Aromatic Polyamide Advanced Nanofiltration Membrane ele Lett GIOI uu uuu u carte eb T m Spiral Wound Fiberglass Outer Wrap Active Membrane Area 85 ft 7 9 m Recommended Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine To
529. scales such as calcium carbonate metal oxides and sulfate scales from RO and NF membrane elements TRICLEAN 211 TriClean 211 is a cleaner additive used to boost the performance of TriClean 210 or TriClean 217 This surfactant based cleaner should be used when polymer fouling or manganese dioxode fouling are suspected TRICLEAN 212CA TriClean 212CA is specifically formulated as a buffered high pH cleaner for cellulose acetate CA membranes Buffered to a pH of 7 to protect CA membrane from hydrolysis during cleaning this cleaner will remove organic and biological fouling from CA membrane TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 TRICLEAN 212TF TriClean 212TF is a broad spectrum high pH cleaner used for today s high performance polyamide composite membranes This versatile cleaner should be used at a pH of 11 5 to remove biological organic and silt TRICLEAN 213 TriClean 213 is a non chlorine oxidizer that should be used if other cleaners have failed to remove heavy organic or biological fouling Since it 1s an oxidizer performance loss can occur when used with polyamide composite membranes TRICLEAN 214CA This is a 20 concentration liquid version of the TriClean 212CA Use when handling and mixing powders 1s undesirable TRICLEAN 214TF TriClean 214TF is a 50 concentration liquid version of the TriClean 212TF Use when
530. se dioxide foulants without damaging sensitive polyamide composite mem brane elements TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 APPLICATION TriClean 217 should be mixed in a cleaning tank equipped with a mechanical mixer heater low pressure recirculation pump and cartridge or bag filter This cleaner works best when applied at a flow rate of 8 10 gpm per 4 pressure tube or 30 40 gpm per 8 pressure tube at a pressure of between 20 50 psi at a pH of 2 3 Add 1 gallon of TriClean 217 per 25 gallons of RO permeate or DI water and an additional 0 25 gallons of Tri Clean 211 Recirculate solution for 1 hour check ing pH regularly Use sulfuric acid to lower pH and sodium hydroxide to increase pH Shutdown pump and allow to soak for 1 hour After soak recirculate for an additional 20 minutes and then rinse PACKAGING TriClean 217 1s shipped as a liquid in 5 gallon plastic pails or 55 gallon plastic drums Pricing is F O B our factory in Goleta CA Salem VA or Duisberg Germany Delivery for most orders 1s 1 2 days after receipt of order MSDS SHEETS For the most up to date information on MSDS sheets please contact our web site at www trisep com 326 emm TriSep Corporation Chemical Manual TRIS gt CORPORATION APPLICATION TriClean 218 should be mixed in a cleaning tank equipped with a mechanical mixer heater low
531. sed on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane COMM QUIN GIOI L ste uqu La cet T Spiral Wound Fiberglass Outer Wrap Active Membrane Area 88 ft 8 1 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Element Weight 15 7 Length A 40 0 1 016 Diameter B 4 0 101 Permeate Tube C 0 75 19 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane
532. sep com e 0105 342 TRIS gt CORPORATION TRISEP ACM AND ANM MEMBRANES TriSep Flat Sheet Membrane TriSep Corporation offers an expanding line of cellulose acetate blend and thin film polyamide membranes for reverse osmosis and nanofiltration elements applications A general description of the TriSep thin film membranes is presented below TriSep ACM and ANM membranes continue to prove to be of outstanding quality performance high flux and solute rejection All flat sheet membranes are sold wet in 42 wide rolls Reverse Osmosis Advanced Composite Membranes ACM V ACMI ACM2 ACM3 ACM4 ACMS5 X20 In the cases where a product of equal or better performance capabilities tolerances and proven quality we offer the equivalent ACM1 membrane For slightly higher flux requirements while maintaining high salt rejection we offer the equivalent ACM2 membrane ACM3 offers high flux and salt rejection characteristics Like the ACMI and ACM2 membranes the ACM3 is forgiving of system upsets There is not a comparable thin film membrane product available to date by any of the other membrane manufacturers ACMA membrane is a thin film membrane of similar chemistries to the other ACM membranes This is a higher flux membrane than the ACM3 with nominal salt rejections in the 99 0 range ACMS offers the highest flow of any TriSep RO membrane Rejection is 98 5 when tested at 150 psi X20 membrane is a fully
533. sing tape fiberglass reinforced epoxy plastic FRP welded or extruded netting for sanitary applications or a hard shell such as 1s used for the Turboclean element For most commericial and industrial applications that do not require sanitary construction FRP outerwrapping is the most common method This outerwrap must also give the element rigidity and strength to withstand the forces exhibited on the element by the CIC differential pressure or dela P On a typical 8 system the pressure drop on a single tube can be 30 psi bar to 60 psi 4 bar This equates to a force trying to compress the element stack of 1 500 Ibs 685 kg to 3 000 Ibs 1 360 kg Spiral elements are typically loaded into a pressure tube that can withstand the feed pressure required to operate the element To seal the outside of the element to the inside of the pressure tube which is required to force the feed water into the elemnet rather than bypass around the outside a seal carrier or anti telescoping device ATD is attached to each end of the element This serves two purposes One it 1s a place where a brine seal can be placed to seal to the inside of the pressure tube wall and it acts as an antitelescoping device Telescoping happens if you fix either the center or the outside of the element and allow the other to move The ATD must be strong enough to withstand the delta P forces mentioned above without allowing the element to telescope Spiral elements are normally
534. sio Rejection gt 99 80 System Dissolved Solids Rejection gt 99 93 1 Final permeate quality exceeds design specification 2 Substantial cost savings over previous ion exchange system TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 363 um TRIS SE CORPORATION BULLETIN No TYPE CLIENT APPLICATION LOCATION PRODUCT BACKGROUND PROCESS PERFORMANCE CONCLUSIONS APPLICATION BULLETIN ACM 02 Reverse Osmosis Municipal Utility Power Plant Boiler Feedwater Treatment Silica and dissolved solids TDS reduction for low pressure boiler feedwater North Central United States 4040 ACM1 TSA Spiral Wound Element ACM Membrane In June of 1993 FLOCEPT INC of Bloomington MN reloaded two 2 reverse osmosis systems at a municipal utility power plant located in the north central United States with TriSep s Advanced Composite Membrane ACM RO elements for supply of low pressure boiler feedwater The feedwater quality to each reverse osmosis system ranged in conductivity from 690 940 micromhos cm approximately 350 480 mg l as NaCl TDS with average inlet silica SiO concentrations of greater than 21 mg l Permeate quality of both reverse osmosis systems employing TriSep ACM elements has remained constant at 7 10 micromhos cm approximately 3 5 5 mg l as NaCl TDS with NON DETECTABLE silica SiO
535. sire to allow monovalent ions to pass through the membrane will rejecting divalent ions or low molecular weight organic molecules such as sugars NF is a membrane process which can be applied to the treatment of a variety of water supplies with many economic and process advantages NF membranes typically have lower salt NaCl rejection than reverse osmosis membranes but have higher specific flux rates and can therefore operate at lower feed pressures NF membranes have the inherent ability to reject or separate different feed species specifically particulates colloidal and microbiological species hardness sulfate and other multivalent 10ns and soluble low molecular weight 200 Daltons neutral and charged organic compounds These species typically contribute little to osmotic pressures even at high system recoveries This is a property consistent with large molecular weight molecules as 1s the case for THM s trihalomethane precursors or highly hydrated multivalent 10ns such as sulphate magnesium and iron At the same time common monovalent nonhydrated ions such as sodium and chloride which are prevalent in feedwaters are poorly rejected by most NF membranes which also leads to lower osmotic pressures therefore permitting lower net driving pressures NDP This in turn permits designs of nanofiltration systems capable of operation at relatively high specific flux rates and recoveries with low feed pressures and low power r
536. spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION 8 X 20 Low Fouling RO Turboclean Element TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 N1P4T5 7 100 26 0 99 00 98 00 Performance is based on the following test conditions 2 000 00 ppm NaCl 225 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane COrnfigural on RET Spiral Wound Turboclean Shell with FoulGuard Technology Active Membrane Area 270 ft 24 8 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 95 GPM 22 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1
537. stem technologies were not a viable option for followed by ion exchange this project due to the variable water quality associated with surface waters Heavy rainfall or rapid snow melts can elevate turbidity levels quite dramatically and quickly A pre treatment technology that could provide high quality water regardless of inlet quality was needed he Solution Ultrafiltration was an obvious answer to the problem due to the high permeate water quality UF membranes produce However not all UF technologies were applicable for this application due to the potentially high suspended solids levels with the source Figure 1 SpiraSep UF System water Due to the low pressure operation and membrane aeration the SpiraSep membranes were chosen for its low fouling tendencies Cold water temperatures during the water also warranted a robust design that would maintain flow For additional information regarding SpiraSep UF membranes please contact Mike Snodgrass at 1 805 964 8003 ext 113 or send e mail to snodgrass trisep com i A N TRI E CORPORATION Triseo Corporation A Crystal Clear Solution Coal Bed Methane CBM Produced Water Treated Using Submerged Ultrafiltration Membranes Case Study Wyoming USA The Challenge Production of coal bed methane CBM which has become a viable source of natural gas requires the extraction of high salinity water in order to reduce the pressure hol
538. t overall salt rejection of 99 consistently high silica rejection of 99 lower and consistent system delta P system maintainability ease of cleaning and returning performance back to start up conditions system durability and up to 2700 cleaning hours with little loss in performance For your difficult RO applications choose the leader and still the best TriSep s X 20 TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 18 X 20 Low Fouling RO Membrane The Unique Chemistry that just works s TRIS S CORPORATION 2540 X201 TSF 4040 X201 TSA 4040 X201 TSDA 4040 X201 TSF 4040 X201 TWF 8040 X201 TSA 8040 X201 TSAN 8040 X201 TSFA 8040 X201 UWA 8040 X201 UWAN 8040 X201 UNA 8340 X201 TSOA TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 X 20 Model Numbers 2 5 diameter by 40 long 0 75 O D male permeate tube protruding permeate tube 4 diameter by 40 long 0 75 I D female permeate tube flush cut 4 dia by 40 long 0 62 I D female permeate tube flush cut Desal replacement 4 diameter by 40 long 0 75 O D male permeate tube protruding permeate tube 4 dia by 40 long 0 75 O D male perm tube protruding permeate tube high area 8 diameter by 40 long 1 50 I D female permeate tube flush cut Same as 8040 ACM2 TSA but NSF approved 8
539. t you want to edit This will open the analysis and allow you to edit any of the data Once you have finished inputting all of the data on this screen click on the Calculate button to check if the analysis is balanced If the analysis is not balanced within 1 a message box will pop on the screen asking if you want to automatically balance the analysis edit it manually or cancel If you click on yes the program will automatically balance the water analysis by either adding sodium Na or chloride Cl to the water analysis depending on whether the analysis requires cations or anions to balance If you click on No you can manually adjust the analysis and then recalculate Note The values of pH Temp and HCO3 will affect the values of CO2 and CO3 So if pH Temp and HCO3 are changed this will affect the anion total Delete Analysis Once a water analysis file is deleted 1t is permanently removed from your list of files on record in your database Click on the file that you want to delete then click OK Print This will allow you to print out a projection that has previously been calculated and saved It is not necessary to recalculate the design before printing it The program will prompt you to select the projection that you want to print Click on the appropriate file then click on OK Exit Select this option when you are finished using Trisep s Reverse Osmosis Implementation Software and wish to close the program
540. ta Factors at some typical system recoveries Table 3 Element Path Length versus System Recovery Recovery Path Length 50 6 75 12 88 18 Note Path length is defined as the number of 40 elements in series needed to define the array Balanced designs are easily obtained by tapering the number of pressure tubes per pass For six element long tubes approximately 50 of the feedwater is converted to permeate water in each pass Therefore the second pass should have half as many tubes in parallel as the first pass A 50 recovery system would require one pass of six element long tubes 1 e all the tubes could be plumbed in parallel For a 75 recovery system a two pass design would be required 1 e 8 tubes in the first pass feeding 4 tubes in the second pass resulting in a 12 element path length For an 87 5 recovery system a three pass design would be required 1 e 8 tubes in the first pass feeding 4 tubes in the second pass feeding 2 tubes in the third pass resulting in an 18 element path length Saturation Indexes Sulfate Scales The saturation values for the sulfates are expressed as a percentage of the ion product IP divided by the solubility product Ksp A value less than 100 indicates a solution that is not saturated while a value greater than 100 indicates some degree of supersaturation Acrylic acid antiscalent can be used to control sulfate scaling The program lists saturation indices for calcium strontium and bariu
541. tank equipped with a mechanical mixer heater low pressure recirculation pump and cartridge or bag filter This biocide works best when applied at a flow rate of 8 10 gpm per 4 pressure tube or 30 40 gpm per 8 pressure tube at a pressure of between 20 50 psi Solution should be used at a temperature of 20 to 25 C Add 2 gallon of TriStat 410 per 100 gallons of RO permeate or DI water The pH should be between 3 4 Recirculate solu tion for 30 40 minutes and then rinse Dilute 196 solutions loose 50 of the peracetic acid after 7 days Make up dilute solutions fresh the day of use Concentrated solutions do not decay Store in cool dark place for maximum shelf life Spent solution is biodegradable and will decompose to oxygen water and acetic acid PACKAGING TriStat 410 1s shipped as a liquid 1n 5 gallon plastic pails or 55 gallon plastic drums Pricing 1s F O B our factory in Goleta CA Delivery for most orders is 1 2 days after receipt of order Not available for sale in the United States or Canada MSDS SHEETS For the most up to date information on MSDS sheets please contact our web site at www trisep com TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 333 TRIS CORPORATION TRIPOL 1210 MEMBRANE POLYMER TREATMENT e Restores rejection of CA ele ments PROBLEM In many installations worldwide CA membranes can lose rej
542. tate Blend Spiral Wound Fiberglass Outer Wrap 350 ft 32 5 m 200 500 psi 14 34 bar 600 psi 41 bar 50 90 F 10 32 C 5 5 nominal 4 7 0 5 ppm nominal 1 0 ppm max 80 GPM 18 m3 hr 5 1 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TRIS gt CORPORATION Permeate flow Model GPD m3 day 8040 SB20 TSOA 7 000 26 0 PRODUCT SPECIFICATION 8 CA RO Element Series Minimum Salt Rejection Average Salt Rejection 98 00 97 00 Performance is based on the following test conditions 2 000 00 ppm NaCl 420 00 psi 25 C 15 recovery pH 5 50 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type Configuration Active Membrane Area Recommended Applied Pressure Maximum Applied Pressure Recommended Ope
543. te Flow Ratio Maximum SDI 15 minutes Maximum Turbidity PRODUCT SPECIFICATION 8 5 CA RO Element Series Minimum Salt Rejection Average Salt Rejection 8540 SB20 TSA 98 00 97 00 Performance is based on the following test conditions 2 000 0 ppm NaCl 420 0 psi 25 C 15 recovery pH 5 5 30 minutes operation SB Cellulose Acetate Blend Spiral Wound Fiberglass Outer Wrap 440 ft 40 4 m 200 500 psi 14 34 bar 600 psi 41 bar 50 90 F 10 32 C 5 5 nominal 4 7 0 5 ppm nominal 1 0 ppm max 80 GPM 18 m3 hr 5 1 Element Weight Length A 50 23 40 0 1 016 Diameter B 8 5 215 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TRIS gt CORPORATION Permeate flow Model GPD m3 day 10 000 37 0 OPERATIONAL AND DESIGN DATA Membrane Type
544. te Wat 3 to 5 8 to 12 3 Year Salt Passage Increase Factor S P I F Membrane Type 3 Year S P I F Cellulose Acetate Blend SB20 1 5 to 2 0 SB50 Thin Film Composite X 20 1 1 to 1 3 Reverse Osmosis ACM ACM LP Thin Film Composite TS80 1 1 to 1 3 NanoFiltration XN45 TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 383 TriSep Engineering Manual TRIS gt CORPORATION TRISEP ELEMENT LOADING PROCEDURES This document covers information for the safe loading of TriSep elements The information is based on potential safety hazards known to TriSep and is believed to be reliable Users should not rely upon it exclusively as hazards unknown to TriSep can be introduced in specific applications The information is to be accepted and utilized at user s risk Confirmation of its validity and suitability in particular cases should be obtained independently Trisep makes no guarantee of safety and assumes no obligation or liability in connection with this information Please refer to the TriSep Engineering Manual for more detailed loading procedures PROPER EQUIPMENT Wear appropriate gloves safety shoes and safety glasses for all operations discussed in this section CHEMICALS WARNING DO NOT CONTACT FLUID INSIDE PLASTIC BAGS CONTAINING NEW ELEMENTS New or stored elements contain a winterizing solution of approximately 3 of sodium metabisul
545. te flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Zee 8 ACM RO Element Series TRIS gt CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 ACM2 UWFA 10 700 40 0 99 50 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane Configuration Spiral Wound Fiberglass Outer Wrap Active Membrane Area 400 ft 37 2m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance lt 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate
546. ted the Stage 2 tab turns from gray to normal indicating that this project is a two stage system The Recirc and Blend features are not functional when using the two stage feature To design the second stage system click on the Stage 2 tab and input the permeate flow required for the second stage The first input is a check box to indicate if you wish to adjust the second stage pH If you check this box it allows you to adjust the pH on the feed to the second stage If this box 1s un checked the feed pH to the second stage defaults to the permeate pH from the first stage The second stage permeate flow must be less than 95 of the first stage permeate flow Once the permeate flow is input the recovery is automati cally calculated since the permeate flow from the first stage is set which is equal to the feed flow to the second stage Also note that the temperature is grayed out and entry is not allowed Select the element type and array When the Calculate button is pressed the two stage system is automatically calculated The concentrate from the second stage is recycled back to feed the first stage This will be indicated as a recirc flow rate in the first stage system The feed to the first stage is then a blend of the second stage concentrate and the raw feed The first stage recovery is actually the overall two stage system recovery since the con centrate from the second stage is recycled The program will indicate the stage recovery
547. ted to public health safety and protection of ie environment While focusing on food water indoor air and the environment NSF develops national standards provides learning opportunities through its Center for Public Health Education and provides third party conformity assessment services while representing the interests of all stakeholders The primary stakeholder groups include industry the regulatory community and the public at large Listings can be checked on the NSF website at www nsf org Two standards from NSF apply to TriSep products NSF standard 60 is used to test and approve various chemicals that may be added to drinking water for toxicological effects on humans A maximum dose rate is established based on the toxicity and use of the chemicals Two TriSep products have NSF 60 certification the TriPol 8510 and TriPol 9010 antiscalants These can be used as an antiscalant to an RO system at a concentration up to 4 ppm and 10 ppm respectively A number of TriSep membrane elements have been approved under NSF Standard 61 This 1s a relatively new development as in the past NSF would not certify membrane elements as stand alone devices This standard does not validate the performance of the element but tests for any toxicological concerns regarding the leaching any residual chemicals into the permeate water The Netherlands has a governmental agency KIWA that is owned by the local water municipalities This organization tests many
548. tely upon their delivery to the destination stated in the agreement and shall within ten 10 days provide written notice to SELLER at its principal place of business of any claim that the goods do not conform to the terms of the agreement 7 PATENT INFRINGEMENT Except for goods manufactured by SELLER based on specification of drawings furnished by CUSTOMER SELLER shall defend at its expense any suit action or proceedings brought against CUSTOMER based upon any claim that the equipment covered by this order infringes any United States patent which has been issued as of the date of the order and pay any damages and costs awarded therein against CUSTOMER but not to exceed the amount therefore paid to SELLER by CUSTOMER hereunder if promptly notified by CUSTOMER in writing of such Claim and given authority information and assistance by CUSTOMER at SELLER S expense to conduct such defense 8 EXCUSABLE DELAYS SELLER shall not be in default for failure to deliver or delay in delivery arising out of causes beyond its control and without its negligence including but not limited to Acts of God or the public enemy acts of the Government in either its sovereign or contractual capacity fires floods epidemics quarantine restrictions strikes shortages of materials or supplies labor disputes freight embargoes delays in transit consignments lost or damaged by freight agent s and unusually severe weather 9 DEFAULT AND VENUE In th
549. tem So a two stage system would take the permeate from a first system and feed it to a second system to further reduce the permeate TDS 2 WHATS NEW FOR VERSION 2 0 0 Troi version 2 0 0 has now been posted on our web site and is available for distribution This version changes the limits of saturation and dosing for TriSep antiscalants incorporates the new TriSEp Reverse Osmosis Normalization TRON software and incorporates electronic documents for chemical spec sheets admin documents and some technical white papers Some element specifications and new models have also been added to the menu It is not a major revision and it is not necessary for you to upgrade 1 Antisclant saturation indexes have been increase as shown below Saturation Limits for TriPol Antiscalants Max Max Max Max Max Max Max Max LSI CaSO4 SrSOA BaSO4 CaF2 Silica Al Fe Mn ppm ppm 8010 1 0 150 200 200 200 100 0 1 0 1 8510 2 0 400 1 200 12 000 8 000 100 0 5 0 5 9010 2 6 300 800 10 000 10 000 100 0 3 0 3 9510 2 6 400 1 200 12 000 10 000 200 4 0 4 0 2 4040 ACMS TSF 8040 ACM5 TSA and 8040 ACM5 UWA elements have been added to the list of element selections 3 The new version of TRON TriSep s normalization software that allows operators to normalize flow rejection and delta P over time in a graphical format is now linked to the Troi main menu A separate manual fro TRON is included 4 Chemical spec sheets for antiscalants and clea
550. ter flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION 4 ACM RO Element Series TRIS gt CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 ACM3 TSF 2 00 10 0 99 20 98 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM Fully Aromatic Polyamide Advanced Composite Membrane ele el ie le NP Spiral Wound Fiberglass Outer Wrap Active Membrane Area 85 ft 7 9 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes
551. tera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION Zi 6 3 AMM High Temperature MF Turboclean Element TRIS CORPORATION Model Pore Size 6338 N5D9V9 0 2 microns Permeate flow is based on the clean water flux at the following test conditions 10 psi 25 C pH 8 15 recovery 15 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type AMM Advanced Microfiltration Membrane Configuration Spiral Wound Turboclean Shell Active Membrane Area 157 ft 14 7 m Recommended Applied Pressure Not applicable Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 10 0 ppm Maximum Feed Flow 70 GPM 15 8 m3 hr sD A Minimum Brine Flow Permeate Flow Ratio 5 1 v s p A Maximum SDI 15 minutes 5 0 APPROV d Maximum Turbudtv 1 NTU ele e Tel EE Whey Fractionation Element Weight 33 15 Length A 38 965 Diameter B 6 3 160 Permeate Tube C 1 14 28 9 Units in pounds and inches units in paranthesis in kilograms
552. th pattern as shown in the figure below where a maximum TSS value is reached and is then subsequently reduced to the inlet value This reduces the average TSS concentration by 40 5096 compared to traditional submerged designs Membrane backwash C Total Suspended Solids Time ISCO system TSS profile gt f AN SPIRASEP TRI gt Ultrafiltration Membrane Technology CORPORATION Submerged SpiraSep with Aeration SpiraSep Swimming Pool Treatment SpiraSep 125 m3 hr Wastewater TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 13 SPIRASEP Ultrafiltration Membrane Technology v w 4 TRIS CORPORATION l 1 dO LI3HS 133HS LHOIM QaigiHO3d d3Sl31 JO NOISSIW I3d N3LLIM AHL LNOHIIM 31OHM Y SV JO HSINI4 Led NI NOILOQnGIO d33l ANY d3Sl31 JO AldadOdd 31OS 3H1 SI ONIMV3IG SIHL NI Q3NIVINOO NOILVW3OdNI 3HL SONI NI 28 SNOISN3WIQ 1 Tyl 3lyW SINAWWOO TVIIN3GHNOO ANV A3V13l3dO3d ddd ONIONV H TIOL OIl313WO3O 13dslalNI y U ddv Saw OLOF 1VWIO3d 3OV14 333H1 CO 3 VWIO3Q 3OY1d OML y o Hddv ONI L 1vWIO3Q3OVld INO DES QIN38 OEHOVW ees mui zeg 32NV2HTIO1 NMWad ISVMA PO EL S Ne S3HONI NI 34 Y SNOISN3WIQ 3WVN alva ETE ASIMYSHLO SSIINN ONIO IV WG vZOeCll l INIS NOIIV33V INJJAdONdATOd FCCRZIIIL j ONO ONd WGddj O
553. th TriSep s Advanced Composite Membrane ACM RO elements for the supply of 216 000 gallons per day GPD of low pressure boiler feedwater FEED The feedwater quality to each reverse osmosis system ranges in conductivity from 1600 1860 micromhos cm approximately 800 930 mg l as NaCl TDS with average inlet silica SiO concentrations of approximately 19 mg l PERMEATE Permeate quality of both reverse osmosis systems employing the ACM elements remains consistent at 28 30 micromhos cm approximately 13 15 mg l as NaCl TDS Permeate silica SiO concentrations detectable by the client to 1 5 mg l are consistently deter mined to be less than 1 5 mg l TriSep s elements have maintained permeate water quality permeate water flow rates and consistent low operating pressures The ACM membrane continues to perform producing greater than 99 conductivity reduction CR quality permeate water through the system while tolerating a standard quarterly chemical cleaning program CONCLUSION Spiral wound elements manufactured with TriSep membrane operate efficiently atlow pressures 150 250 psi 10 2 17 bar yielding significantly lower passage of silica salt and naturally occurring low molecular weight organic compounds than does cel lulosic and other polyamide composite RO membranes This presents cost savings and operational maintenance advantages by reducing ion exchange resin fouling regeneration frequen cies and silica
554. the following test conditions 2000 ppm MgSOA 110 psi 25 C 15 recovery pH 8 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type XN45 Polyamide Advanced Nanofiltration Membrane Configuration Spiral Wound Turboclean Shell Active Membrane Area 53 ft 4 9 m Recommended Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 5 ppm nominal 1 0 ppm max Maximum Feed Flow 25 GPM 5 6 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU Application Egg Concentration rated l I TP 1 ATTEN AMI 1111111 deM i WAN MAKKA lll vii Iu it ANTE t hh Ve ll 1 VE ANN AA VWAULL ON WA M NM 1 MY WW WM M Element Weight 15 T Length A 38 965 Diameter B 3 8 96 Permeate Tube C 0 83 21 2 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Conf
555. the performance warranty in section 4 3 2 0 TYPE AND LENGTH OF WARRANTIES 2 1 Water Applications X 20 ACM UE10 UE50 CA XN45 TM10 A Initial Performance 24 hours 24 hours B Materials 12 months 12 months and Workmanship C Extended 36 months Contact Element Performance TriSep 2 2 Non Water Applications All elements A Initial Performance 24 hours B Materials 12 months and Workmanship C Extended Contact Element Performance TriSep 3 0 WARRANTY START DATE Warranties for extended element performance commence on the date of plant start up or 3 months after initial shipment date from TriSep s facility whichever occurs first FOR STANDARD WARRANTY SPIRAL WOUND ELEMENTS 3 YEAR STANDARD WARRANTY 4 0 WARRANTIES AND LIABILITIES SPIRAL WOUND PRODUCTS 4 1 Materials and Workmanship TriSep warrants that its spiral element s will be free of mechanical defects as determined by TriSep due to faulty materials or errors In manufacturing workmanship for a period up to twelve 12 months after the Warranty Start Date Claims made under this portion of TriSep s warranty must specify the alleged defect in materials of construction or manufacturing workmanship on which such a claim is based All claims must be documented by the customer for TriSep processing 4 1 1 TriSep Liability TriSep will repair or replace at no charge any element which is found by TriSep to be mechanically defective due to errors in
556. thin the system TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 166 TriSep ACM1 Composite AN RO Membrane Elements TRIS 5 CORPORATION The ACMI offers the highest rejection 99 5 and typically operate at 150 200 psi 10 14 bar The ACM I is preferred in applications with high feedwater TDS 73 000 ppm and or high recovery The lower specific flux of this membrane compared to the ACM4 and ACMS allows for a more balanced hydraulic flow through the system and more balanced permeate flux rates due to the high osmotic pressure of these feedwaters 4040 ACMI TSA 4 diameter by 40 long 0 75 I D female permeate tube flush cut 4040 ACM1 TSF 4 diameter by 40 long 0 75 O D male permeate tube protruding permeate tube 4040 ACMI TWF 4 dia by 40 long 0 75 O D male perm tube protruding perm tube high area 8040 ACMI TSA 8 diameter by 40 long 1 50 I D female permeate tube flush cut 8040 ACMI UWA 8 diameter by 40 long 1 50 I D female permeate tube flush cut high area TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 167 PRODUCT SPECIFICATION Za 4 ACM RO Element Series TRIS gt CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 ACM1 TSA 1 950 7 0 99 50 98 50 Performance is ba
557. tically calculated If your system is equipped with Delta P gauges you want to check Delta P If you have interstage pressure gauges check Interstage If you have neither leave both unchecked We strongly recommend that you have the capability to monitor the Delta P of all stages independently The System start date and the Start NDP are input This can be whatever you would like Normally the start date would be when you replace your elements The start NDP can be 200 psi or the start up NDP The last thing is to input the system array Enter the Stage 1 Vessels and Stage 1 Elem Vessels depending on how many stages you have selected under the Brine Stages dropdown Click on the Add button to start entering the detailed data points on the grid Every time you want to add a set of data to the grid you will need to click on the Add button You can proceed in the grid by using the Enter Key or the tab key A message will popup if a field which requires input or if the input needs to be within a range of values Once all the values required by the user have been input the temperature correction factor NDP osmotic pressure Delta P and the normalized flow and rejection will be calculated You can make changes to any user input values and recalculate the values in the grid by clicking on the recalculate icon on the toolbar TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 07
558. tion 8040 ACM5 UWA 12 500 47 0 98 50 97 50 Performance is based on the following test conditions 2 000 0 ppm NaCl 150 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM LP Fully Aromatic Polyamide Low Pressure Advanced Composite Cong AMON uuu aa E oa akana URS Spiral Wound Fiberglass Outer Wrap Active Membrane Area 400 ft 37 2 m Recommended Applied Pressure 50 300 psi 3 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 4 0 Maximum Turbidity 1 NTU Element Weight 50 23 Length A 40 0 1 016 Diameter B X 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 028 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditio
559. tion 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TRIS gt CORPORATION Model 3840 N6D4V7 OPERATIONAL AND DESIGN DATA Membrane Type Configuration E Active Membrane Area Recommended Applied Pressure Maximum Applied Pressure Recommended Operating Temperature Feedwater pH Range Chlorine Tolerance Maximum Feed Flow Minimum Brine Flow Permeate Flow Ratio Maximum SDI 15 minutes Maximum Turbidity ADDIIG300I Rm A dd ANN MA WA lll ll Il n Wl Element Weight Length A 12 5 4 39 984 Units in pounds and inches units in paranthesis in kilograms and millimetes Dim A does not include ATD Mechanical Configuration Diameter B Sanitary Style Core Tube Feed Spacer 3 8 96 0 065 thick diamond spacer PRODUCT SPECIFICATION 3 8 AUM High Temperature UF Turboclean Element M W C O 10 000 AUM Advanced Ultrafiltration Membrane Spiral Wound Turboclean Shell 41 ft 3 8 m Not applicable 600 psi 41 bar 35 140 F 2 60 C 2 11 continuous 10 0 ppm A 4 5 m3 hr us So
560. ts Certain elements are reopened rinsed wet tested and tolerance checked This operation is logged by Quality Control and the elements are returned to inventory 4 OPERATION PARAMETERS In addition to numerous in line Quality Control inspections of the various phases of element fabrication TriSep maintains a rigorous control of process parameters These controls include daily independent checks of the process variables i e temperature casting speed adhesive ratio etc by a Quality Control representative and machine operator Additionally each of the instruments used in the control and testing of elements and membrane is calibrated on a routine basis TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 380 TriSep Engineering Manual TRISJS gt TEMPERATURE CORRECTION FACTORS sss s FOR TRISEP ELEMENTS Permeate output of a membrane is partially temperature dependent Other factors that may influence membrane permeate flow include driving pressure osmotic pressure differential pressure and pH The dependency of a membrane on temperature will vary between membrane type and manufacturer Below are temperature correction factors for TriSep membranes to assist in estimating the effects of feedwater temperature on permeate flow rates by membrane type To project the estimated effects of temperature alone all other factors constant on permeate flow of TriSep r
561. ty APPIANO c Pa PRODUCT SPECIFICATION 6 3 AUM High Temperature UF Turboclean Element M W C O 10 000 AUM Advanced Ultrafiltration Membrane Spiral Wound Turboclean Shell 225 ft 20 9 m Not applicable 600 psi 41 bar 35 140 F 2 60 C 2 11 continuous 10 0 ppm En 15 8 m3 hr vu S p 5 0 APPROV k 1NTU Whey Fractionation Element Weight Length A 33 15 38 965 Diameter B 6 3 160 Permeate Tube C 1 14 28 9 Units in pounds and inches units in paranthesis in kilograms and millimetes Dim A does not include ATD Mechanical Configuration Sanitary Style Core Tube Feed Spacer 0 031 thick diamond spacer ATD not included with element Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION ow NN 6 4 PE High Temperature UF Turboclean Element TRIS CORPORATION Model M W C O 6438 N9D4V8 10 000 OPERATIONAL AND DESIGN DATA Membrane Type PerSep Advanced Ultrafiltration Membrane Configuration Spiral Wound High Temperature Turboclean Shell Active Membrane Area 210 ft 19 5 m Recommended Applied Pressure
562. uals for our Troi design program as well as the new Tron normalization program TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 1 TRIS CORPORATION The Company SpiraSep X 20 Turboclean ACM ACM1 ACM2 ACM3 ACM4 ACM5 Nanofiltration TS80 TS83 XN45 Cellulose Acetate SB20 SB50 SB90 Ultrafiltration UE10 UE50 Microfiltration TM10 Certifications NSF Elements TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 CONTENTS Introduction to TriSep Backflushable Immersed Ultrafiltration Technology X 20 Low Fouling Composite RO Membrane Elements Sanitary membrane elements Beverage Applications for Turboclean Dialysis Applications for Turboclean Dairy Applications for Turboclean Food Applications for Turboclean Pharmaceudical Applications for Turboclean Industrial Applications for Turboclean ACM Composite RO Membrane Elements Low flow high rejection PA membrane General purpose PA membrane High flow and high rejection PA membrane Low pressure PA membrane Ultra low pressure PA membrane TS80 and XN45 Nanofiltration Membrane Elements Low fouling softening membrane Low fouling process membrane Cellulose Acetate Blend RO Membrane Elements General purpose high rejection CA membrane High flow CA membrane Nanofiltration CA
563. ube Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION LAS NN 4 X 20 Low Fouling RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 4040 X201 TWF 2 400 9 0 99 50 98 50 Performance is based on the following test conditions 2 000 00 ppm NaCl 225 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane CGopnfguraton a k Spiral Wound Fiberglass Outer Wrap with FoulGuard Technology Active Membrane Area 88 ft 8 2 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr Minimum
564. uccessful long term field testing on membrane systems with challenging feed streams TriSep began marketing our membrane support chemicals in January of 1996 Find out how TriPol antiscalents TriClean cleaners and TriStat bio control chemical products can save you money and enhance your membrane system performance Please call your TriSep representative listed on the back of the enclosed brochure for free technical information or to discuss your specific requirements TriPol scale inhibitors are engineered to protect the integrity of the membrane surface and to provide superior control of calcium carbonate calcium sulfate barium sulfate strontium sulfate silica metal oxides colloids calcium fluoride and calcium phosphate TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 308 wm TriSep Corporation Chemical Manual LAS andi TRIS S CORPORATION TriPol Scale Inhibitors TriPol is the first line of high performance scale inhibitors developed by a leading membrane manufacturer spe cifically for use with the latest reverse osmosis RO an nanofiltration NF membranes Using our proprietary knowledge of membrane chemistry design and fouling characteristics TriSep developed scale inhibitors to be 100 compatible with today s high tech membrane chemistries while providing maximum control of the highest levels of the most common membrane foulants
565. uickly lead to a loss of system performance associated with a decrease in perme ate flow and increase in differential pressure and a loss of element rejection If left unchecked this fouling can permanently damage the membrane elements leading to costly and premature mem brane replacement SOLUTION TriClean 214TF is a liquid version of TriClean 212TF used where powdered cleaners are unde sirable to remove biological organic and colloi dal foulants without damaging sensitive polyamide composite membrane elements TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA APPLICATION TriClean 214TF should be mixed in a cleaning tank equipped with a mechanical mixer heater low pressure recirculation pump and cartridge or bag filter This cleaner works best when applied at a flow rate of 8 10 gpm per 4 pressure tube or 30 40 gpm per 8 pressure tube at a pressure of between 20 50 psi at a pH of 11 5 For silica use at a pH of 12 Use caution as pH s above 12 may damage membrane Please see Guidelines For Operation for pH and temperature limits Pg 137 Add 3 gallons of TriClean 214TF per 100 gallons of RO permeate or DI water Recirculate solution for hour checking pH regularly Use sulfuric acid to lower pH and add additional TriClean 214TF to increase pH Shutdown pump and allow to soak for 1 hour After soak recirculate for an additional 20 minutes and then rinse This solution should be used after a l
566. ular area formed between the vessel inner diameter and the membrane element outer diameter This results in a dead or stagnant area between the outside of the membrane element and the inside of the housing that is prone to microbial contamination Cleaning procedures therefore cannot adequately sanitize some areas of conventional membrane elements Different manufactures use different methods of enclosing their elements to maintain mechanical stability and to control the by pass flow Mechanical stability is important in both maintaining the integrity of the membrane element s configuration and maximizing element life The enclosure type used has a major impact on both the element s mechanical stability and its efficiency in controlling by pass flow There are three basic design configurations for enclosing sanitary service elements These three enclosure configurations are commonly designated as cage wrap net wrap and hard shell Controlling by pass flow is critical for two reasons First if the individual element by pass flows are different there is no way of ensuring the membrane elements are operating as designed This can have a detrimental effect on fouling rates and element life Secondly while there must be some by pass flow around the element any excess over the required minimum is a costly waste of power To determine the relative performance of each type of sanitary membrane element tests were conducted first in our factory and th
567. ulate solution for 20minutes shutdown pump and allow to soak for 2 hours After soak recirculate for an additional 20 minutes and then rinse As an on line injectable inject 2 3 ppm on a continuous basis Can be added to high or low pH cleaning solutions at 10 20 ppm Solutions over 50 ppm must be deactivated prior to disposal See below on how to deactivate TriStat 110 In many installations worldwide membranes can accumulate and even promote the growth of bio logical organisms This is especially problematic for polyamide membranes which cannot tolerate free chlorine If left unchecked these organisms can quickly lead to a loss of system performance associated with a decrease in permeate flow and increase in differential pressure and a loss of ele ment rejection PACKAGING SOLUTION TriStat 110 is shipped as a liquid in 2 gallon 10 x 1 2 gallon 5 gallon plastic pails or 55 gallon plastic drums Pricing 1s F O B our factory in Goleta CA Delivery for most orders is 1 2 days after receipt of order Not available for sale in the United States or Canada TriStat 110 is a non oxidizing biocide effective against a broad range of bacteria molds fungi and yeasts TriStat 100 can be used on a periodic sanitization basis or as an on line injectable Not approved for use in food beverage potable water or dairy applications Do not use as an on line injectable for ultrapure water applications as it can MSDS SHEETS le
568. uld be the first step in any cleaning regime APPLICATION TriClean 210 should be mixed In a cleaning tank equipped with a mechanical mixer heater low pressure recirculation pump and cartridge or bag filter This cleaner works best when applied at a temperature of 40 45 C a pH of 2 5 to 3 5 and at a flow rate of 8 10 gpm per 4 pressure tube or 30 40 gpm per 8 pressure tube at a pressure of between 20 50 psi Add 1 5 lbs of TriClean 210 per 10 gallons of RO permeate or DI water Check and adjust pH if necessary Add sodium hydroxide to increase the pH and add more TriClean 210 to decrease the pH Recirculate solution for hour checking pH regularly Shutdown pump and allow to soak for 1 hour After soak recirculate for an additional 20 minutes and then rinse PACKAGING TriClean 210 is shipped as a powder in 4 Ib 10 x 4 Ib 40 Ib or 100 Ib plastic containers Pricing is F O B our factory in Goleta CA Salem VA or Duisberg Germany Delivery for most orders is 1 2 days after receipt of order MSDS SHEETS For the most up to date information on MSDS sheets please contact our web site at www trisep com TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 318 TRIS CORPORATION TRICLEAN 211 CLEANER ADDITIVE e Can be added to TriClean 210 to aid in sulfate scale removal e Surfactant additive to TriClean 217 improves rem
569. uoo ANP st OOP eurpopo y Jo 93ed Vqxxxxxx opor 86CVCI I Vqxxxxxx oyor 6LOVCI I S pocxxxx ovpor v9cvcrT DAXXXXxXX 0p0p SOCvCII S pocxxxx opop 99cvclTT DJIXx Xxxx opop LOCC SXX XXXX 0pOpr 86tvclI SXX XXXX 0pOFr 6ScvcII HXX XXXX 0 0f cICvVCIT XX XXXX 0p0pr 86tvcII XX XXXX 0p0r 09cvcTI SXX XXXX 0pOr OCT HXx Xxxx QpO0v SCCVCII D OXX XXXX 0pOr LSCVCII LXX XXXX 0pOv t60vclI LXX XXXxX 0pOp p80vCcII JIXx XxXX Qp0p PICVCIT JIXx XxXX 0p0p 60vcIT HXX XXXX OPOV P8OVCI I VXX XXXX 0p0Opv 8CEVCII VXX XXXX 0pOv OSOECIT VXX XXXX 0vp0v LIOVCII VXX XXXX 0vr0v OSOVCII VXX XXXX 0p0v STOVCII VXX XXXX 0p0v TEcrcll VXX XXXX 0p0v L60VCTI VXX XXXX 0p0pv 90IvCII VXX XXXX 0p0v vOITCII VXX XXXX 0p0v ILCVCl I VXX XXXX 0p0v O80VCII VXX XXXX 0p0Ov CIOVCII SPO JoquinN juouio q Jed SLNWHIAWTH 9EA LAIAVIG HONI P S9H9S opor 418 TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax e www trisep com 0703 WV CSO 8007 67 01 LO CI C APN eqn 9109 qI SS 9 GI ub l desur OF cs qn 210 1uodnG es q oz z qn 210 1uodnG es q 06 8CS qn 210 1uodnG es q ST SCCS qn 210 1uodnG es q 9C LCS 86 IcIS 6T SE IST Aq pozIwiojsnd qn OWSO LETZTES 6T SE 9L OLS sdeo pue peppnis 06 I IT res Vrses LECES SSEPTIO 9I0vCIO LE CES Jop nous 9 SEH C OLCcvcTII pue 9IOPTCIO IL ces T Surejuoo ITY oqnj ounssoud SS snd 1o1d
570. uous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 20 GPM 4 5 m3 hr 6 H M Minimum Brine Flow Permeate Flow Ratio 5 1 LY K Di CH Maximum SDI 15 minutes 5 0 pu Maximum Turbdiftv 1 NTU PAO ONC QUO BEE Lactose Demineralization Ld Element Weight 15 T Length A 38 75 984 Diameter B X 3 8 96 Permeate Tube C 0 83 21 2 Units in pounds and inches units in paranthesis in kilograms and millimetes Dim A does not include ATD Mechanical Configuration Sanitary Style Core Tube ATD not included with element Feed Spacer 0 031 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION 3 9 TS50 High Temperature Turboclean Element Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 3938 O8D1U8 1 600 6 0 99 00 98 00 Performance is based on the following test conditions 2 000 00 ppm MgSOA 110 00 psi 25 C 15 recovery pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type TS50 Polyamide Advance
571. urbidity 2 NTU Element Weight 45 20 Length A 40 00 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration TriSep Style Core Tube Feed Spacer 0 028 thick diamond spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions Individual element s permeate flow may vary 15 Engineered Membrane End nF I Y i SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com TriSep Cellulose Acetate RO Membranes SB20 SB50 and SB90 A TRIS gt CORPORATION Cellulose acetate CA membranes were the first commercialized RO membranes developed in the late 1960 s CA membranes offered a good combination of rejection fouling resistance and the ability to toler ate continous chlorine up to 1 0 ppm Some of the reasons they lost favor to the new polyamide membranes was the requirement for acidification CA membranes should be operated at a pH of i ere 4 6 to minimize hydrolysis lower rejection 98 versus 99 5 and higher net drive pressure requirements 300 psi 20 bar versus 150 psi 10 bary But in many applications CA membranes operate very well and give long and usefull service lifes They have an advantage
572. ut NSF approved 8 diameter by 40 long 1 50 I D female permeate tube flush cut 400 ft Same as 8040 TS83 USA but NSF approved 8 5 diameter by 40 long 1 12 I D female permeate tube flush cut TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 219 PRODUCT SPECIFICATION LA 2 5 TS80 Nanofiltration Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 2540 TS80 TSF 650 2 0 99 00 97 00 Performance is based on the following test conditions 2 000 0 ppm MgSOA 110 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ANM Aromatic Polyamide Advanced Nanofiltration Membrane COnIGur AU OM EE Spiral Wound Fiberglass Outer Wrap Active Membrane Area 26 ft 2 4 m Recommended Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 6 GPM 1 4 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximu
573. velope with a red arrow pointing into it This will bring up the export window which allows you to specify the type of file you wish to save the report in Depending on the way your system is configured you can select a variety of formats including Excel Word ASCII and other formats We have found that using Rich Text Format seems to work the best for importing into Microsoft Word None of these formats will save the lines that are present on the printout that separates the raw feed permeate and concentrate ions You can also specify a destination which would normally be a Disk File Once you have made these selections the Choose Export File window will pop up This allows you to name the file and specify a folder to save it You can also specify the magnification that is used to view the file Click on the down arrow next to the 100 box and select the desired magnification When you are finished click on the X in the upper right hand corner of the screen to return to the Design Calculation window Two Stage System Calculation TroiWin version 2 0 0 allows two stage system design 1 e permeate staged The operation is very similar to the single stage design with a couple of limitations To create a two stage design click on the 2 Stage button or click on File the Create Two Pass System from the drop down menu The 2 Stage button then becomes gray indicating it is not available for selection Also when the 2 Stage button is selec
574. vidual element s permeate flow may vary 15 Engineered Membrane SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION LA Zi 8 ACM LP Low Pressure RO Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 ACM4 TSAN 14 600 55 0 99 00 98 00 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM LP Fully Aromatic Polyamide Low Pressure Advanced Composite COMTI GUN AU ON M Spiral Wound Fiberglass Outer Wrap Active Membrane Area 365 ft 33 5 m Recommended Applied Pressure 50 300 psi 3 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity
575. w Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 M4C2T6 14 000 52 0 99 00 98 00 Performance is based on the following test conditions 2 000 0 ppm NaCl 225 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ACM LP Fully Aromatic Polyamide Low Pressure Advanced Composite CONTI EE Spiral Wound Turboclean Shell Active Membrane Area 355 ft 32 6 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU PAO DUCAUO MW se scencinensaascenenttacessscdedenenndeacseddueeacee Pharm Process Water Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 12 28 6 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Filmtec Style Core Tube Feed Spacer 0 031 thick
576. wable system recoveries and thus expand the suitability for use in a wider range of applications MSDS SHEETS For the most up to date information on MSDS sheets please contact our web site at www trisep com TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax e www trisep com e 0105 314 TRIS CORPORATION TRIPOL 9110 SCALE INHIBITOR DISPERSANT e Extends useful membrane life e Superior control of calcium phosphate scales PROBLEM In many municipal wastewater installations world wide higher permeate recoveries from reverse osmosis RO systems are often limited by the potential for calcium phosphate scales This 1s especially problematic for municipal waste waters with high phosphate concentrations In many appli cations the tendency for scale formation has the effect of lowering the system recovery that could adversely effect the system economics SOLUTION TriPol 9110 protects and enhances the operation of RO and NF systems by controlling mineral scale formation due to carbonate sulfate fluoride and phosphate compounds In most water types proper use of TriPol 9110 can significantly increase allow able system recoveries and thus expand the suit ability for use in a wider range of applications TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0105 TriSep Corporation Chemical M
577. ware and wish to close the program 4 DISCLAIMER We at TriSep have put much time and energy into making TRON a user friendly program for our customers that is as accurate as possible The output from this program should not be used for warranty purposes and is only as accurate as the input data As with any program certain simplifying assumptions have been made which under certain circumstances may result in calculated values that are not accurate TriSep Corporation assumes no liability for any errors or costs that may result from the use of this program TRON has been extensively tested by our in house engineers and we feel that most of the bugs have been removed However if you experience a problem with your particular copy or hardware please let us know so that we can remedy it for future revisions by sending an e mail to info trisep com Any comments that you may want to make to improve the software will be considered for future modifications Thank you for considering TriSep in your membrane selection process TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com 0703 410 TRIS CORPORATION Administrative Documents The following pages contains severeal adminstrative documents such as our standard warranty and terms and conditions TriSep Corporation 93 S La Patera Lane Goleta CA 93117 USA 805 964 8003 805 964 1235 fax www trisep com e 0105 4
578. will still be set to metric Help Currently the help menu only displays the version of the program Main Toolbar The main toolbar selections are Exit New Open Design Calculation and Delete These correspond to the menu selections listed above File New Analysis Select this option to input a new water analysis You will be prompted for a file code This file code is a unique alphanumeric filed up to 50 characters long under which the file is saved Choose the file code carefully because a file code cannot be changed A duplicate file code entered here will result in an error message and a prompt for another file code To exit at this point click on the Exit toolbar to return to the TROIWIN main menu Once a valid file code is entered the raw water information is entered The feedwater temperature can be entered as either C or F by clicking on the C radio button for C or the F radio button for F All of the fields below pH are for reference purposes only and are not currently used by the program calculations These fields can be left empty The cations and anions can be input as part per million ppm which is equivalent to milligrams per liter mg l milliequavalents meq or ppm as calcium carbonate CaCO3 All ions will be saved as ppm when the water analysis is balanced and saved Once you have finished inputting all of the data on this screen click on the Calculate button to check if the analysis
579. x 805 964 1235 www trisep com PRODUCT SPECIFICATION i 8 TS80 Nanofiltration Element Series TRIS CORPORATION Permeate flow Average Salt Minimum Salt Model GPD m3 day Rejection Rejection 8040 TS83 TSAN 10 000 37 0 98 50 97 00 Performance is based on the following test conditions 2 000 0 ppm MgSOA 110 0 psi 25 C 15 recovery pH 8 0 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type ANM Aromatic Polyamide Advanced Nanofiltration Membrane Configuratio EE Spiral Wound Fiberglass Outer Wrap Active Membrane Area 365 ft 33 5 m Recommended Applied Pressure 40 200 psi 3 14 bar Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 80 GPM 18 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 1 NTU EH We Element Weight 45 20 Length A 40 0 1 016 Diameter B 7 9 200 Permeate Tube C 1 50 38 1 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configur
580. ximum SDI 15 minutes 5 0 APPROV N Maximum Turbidity 1 NTU Application Milk Fractionation Element Weight 30 14 Length A 38 965 Diameter B 6 3 160 Permeate Tube C 1 14 28 9 Units in pounds and inches units in paranthesis in kilograms and millimetes Dim A does not include ATD Mechanical Configuration Sanitary Style Core Tube ATD not included with element Feed Spacer 0 047 thick diamond spacer Engineered Membrane Beet SOLUTIONS TriSep Corporation 93 South La Patera Lane Goleta California 93117 U S A Phone 805 964 8003 Fax 805 964 1235 www trisep com PRODUCT SPECIFICATION A N 6 3 AUM High Temperature UF Turboclean Element TRIS gt CORPORATION Model M W C O 6338 N6D9V7 10 000 OPERATIONAL AND DESIGN DATA Membrane Type AUM Advanced Ultrafiltration Membrane E elle Ur LE Spiral Wound Turboclean Shell Active Membrane Area 138 ft 12 8 m Recommended Applied Pressure Not applicable Maximum Applied Pressure 600 psi 41 bar Recommended Operating Temperature 35 140 F 2 60 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 10 0 ppm Maximum Feed Flow
581. y pH 8 00 30 minutes operation OPERATIONAL AND DESIGN DATA Membrane Type X20 Fully Aromatic Polyamide Urea Advanced Composite Membrane Configuration Spiral Wound Turboclean Shell with FoulGuard Technology Active Membrane Area 65 ft 5 9 m Recommended Applied Pressure 100 300 psi 7 21 bar Maximum Applied Pressure 1000 psi 69 bar Recommended Operating Temperature 35 113 F 2 45 C Feedwater pH Range 2 11 continuous Chlorine Tolerance 0 1 ppm Maximum Feed Flow 25 GPM 5 6 m3 hr Minimum Brine Flow Permeate Flow Ratio 5 1 Maximum SDI 15 minutes 5 0 Maximum Turbidity 2 NTU Application Agricultural Waste Water Element Weight 12 5 4 Length A 40 00 1 016 Diameter B 4 0 101 Permeate Tube C 0 62 15 9 Units in pounds and inches units in paranthesis in kilograms and millimetes Mechanical Configuration Desal DuPont Style Core Tube Feed Spacer 0 047 thick parallel spacer Permeate flow is clean water flux at standard conditions above Not applicable for all feedwater conditions
582. y uninterrupted compliance with Guidelines and b establish liability TriSep s or Customers for element s replaced or repaired under warranty 5 5 Notification and Verification of Performance Deficiency All claims filed hereunder shall be made in writing within thirty 30 days of identifying a deficiency in warranted performance and shall present a detailed analysis of the system and individual element data showing the performance deficiency and must include a The serial number s of the element s involved and b The individual element s documented operating data documented system operating data or defect in materials or workmanship upon which the claim is based Operating data must include permeate and brine flow salt passage operating pressure pressure drop feedwater temperature pH TDS SDI conversion FOR STANDARD WARRANTY SPIRAL WOUND ELEMENTS 3 YEAR STANDARD WARRANTY and elapsed time since start up hours TriSep reserves the right to require additional data as necessary to validate the claims filed After receipt of the notice TriSep will promptly undertake such investigations as in TriSep s opinion are necessary to verify whether a deficiency exists and to establish liability for remedy of any deficiency The Customer may in course of these investigations be requested to return element s to TriSep for examination TriSep may make reasonable tests and inspections on end user s or on the Customer s

TriSep Catalog 11-10-08.indd - liquidfiltration

Contents

Download Pdf Manuals

Related Search

Related Contents