Reverse Osmosis User`s Manual
Contents
1. j FIGURE 1A ENGF 108 REV A 01 11 2011 AXEON Water Technologies NUMBER IDENTIFICATION Solenoid Valve Turns On Off Feed Water 10 Micron Sediment Removes particulates 5 Micron Sediment Removes particulates Pressure Gauge Measures feed pressure Pressure Gauge Measures pressure after filters Pressure Gauge Measures pump pressure Pressure Gauge Measures concentrate pressure Computer Control Controls RO system 9 Recycle Valve Recycles concentrate back to feed If Applicable 10 Concentrate Valve Controls flow of concentrate waste water to the drain 11 RO Pump amp Motor Pressurizes RO System 12 Throttle Valve Controls flow of the pump 13 Flow Meter Measures flow of permeate water 14 Flow Meter Measures flow of concentrate waste water 15 Flow Meter Measures flow of concentrate recycle water If Applicable 16 Pressure Switch Turns the Pump off at 15 PSI feed pressure 17 Permeate check Valve Protects membranes from back pressure 18 Pressure Vessels Houses Membrane Elements O GE Iw or 16 ENGF 108 REV A 01 11 2011 AXEON Water Technologies 3 PERMEATE RECYCLE FLOW METER FLOW METER CONCENTRATE FILTER IN FLOW METER 4 PRESSURE GAUGE 0 100 PSI FILTER OUT 5 PRESSURE GAUGE 0 100 PSI PUMP PRESSURE GAUGE 0 300 PSI COMPUTER 8 pre LEE RATE nem U2. 202306 PUMP 5HP 208 230 480V CR5 15 204914 VALVE SOLENOID N C UL 220V 1 FNPT 2200 39 HOUSING FILTER BAG 2 FNPT 18 FSI 200640 CART SEDIMENT POLYPRO 4 5 x 20 1 MIC 203649 HOUSING FILTER BLK BLU 4 5 x 20 1 FNPT 200994 VALVE GLOBE SS 3 4 FNPT 200527 HOUSING MEM PVC 4040 1 2 P x 1 2 200379 5 iss MEM HF1 4040 SYSTEMS 204036 MANIFOLD DELRIN 11 HOLE 3 4 IN 1 2 OUT 200900 METER FLOW 0 20GPM 1 x 1 MNPT 202307 GAUGE BKM FILL 0 100PSI BAR 2 5 DIA 200904 GAUGE BKM FILL 0 300PSI BAR 2 5 DIA 200967 VALVE CHECK PVC 1 FNPT x 1 FNPT 203263 CONT COMP ROTROL S 150 220V 3PH 200906 SWITCH PRESS LOW N O 15 30 1 4 FNPT 200598 SNAP RING DELRIN 4 200597 END PLUG CLOSED GTX 4 1 2 FNPT 200596 END PLUG OPEN GTX 4 1 2 FNPT 200588 CLAMP SADDLE NYLON BLK 4 PVC FRP 48 2011 AXEON Water Technologies DT 10000 FLOW DIAGRAM ODA I Londoud QN3931 108M4S 2011 AXEON Water Technologies IDM I SINYHANIM 070 FELL MANU ove NOHDIN OL S 7 5 dH 0 INANIS ENGF 108 REV A 01 11 DT 15000 FLOW DIAGRAM PI PI 0 100 0 100 4040 MEMBRANES 1 1 1 1 1 1 1 1 ARRAY 10 MICRON BAG FILTER SYMBOL LEGEND 50 ENGF 1
3. pH Range Short Term Cleaning 30 Min 1 13 Maximum Operating Temperature 113 F 45 C Maximum Feed Water Turbidity 1 NTU Maximum Operating Pressure 600 psi 41 bar Maximum Feed Silt Density Index 5 SDI Minimum Concentrate Flow Rate 5 1 Chlorine Tolerance ppm pH Range Continuous Operation 2 11 Product Specifications Applied Permeate Nominal Salt Applied Permeate Nominal Salt Description Pressure Flow Rate Rejection Part Numb psi bor gpd m3 d X psi bar gpd m3 d 200386 100 6 89 225 0 85 98 5 200389 HF4 4014 100 689 600 2 27 200387 100 6 89 400 1 51 98 5 200390 HF4 4021 100 689 1000 3 79 200388 HF4 2540 100 6 89 850 3 22 98 5 200391 HF4 4040 100 6 89 2500 9 46 Test Parameters 550 TDS Filtered 5 Micron De Chlorinated Softened City Feed Water 77 Degrees F 15 Permeate Recovery 6 5 7 0 pH Range at the Specified Operating Pressure Data Taken After 30 Minutes of Operation Maximum Pressure drop for each element is 10 psi Minimum salt rejection is 96 Permeate flow for individual elements may vary 20 Part Number Description Pressure Flow Rate Rejection n Dimensions inch mm Description A B lt D A B c Description wm Maran A604 110794 0750909 awa Uwe 211594 ug 0751909 398003 wu zsu o 110798 awa mao 080 111794 075909
4. 2011 AXEON Water Technologies FLUSHING THE SYSTEM The system should be flushed weekly to remove sediment from the surface of the membranes To manually flush the system follow the preceding steps 1 The system must be operating during the flush procedure 2 Fully open the concentrate valve Figure 1B Page 16 3 Allow the system to run for 10 to 20 minutes 4 After 10 to 20 minutes close the concentrate valve to its previous setting Ensure the proper concentrate flow rate is going to the drain 5 The system is now ready to operate PREPARING UNIT FOR STORAGE OR SHIPMENT Prior to shipping or storing your system the system should be cleaned with an appropriate cleaner flushed with water and protected from biological attack with an appropriate solution for membrane elements The membrane housing s and plumbing lines of the system must be completely drained Any water remaining in the plumbing of a system may freeze causing serious damage Preparing system for storage 1 Totally immerse the elements in the membrane housing in a solution of 2 Memstor venting the air outside of the pressure vessels Use the overflow technique circulate the Memstor solution in such a way that the remaining air in the system is minimized after the recirculation is completed After the pressure vessel is filled the Memstor solution should be allowed to overflow through an opening located higher than the upper end of the highest pressure ve
5. 355110031 Under certain conditions the presence of free chlorine and other oxidizing agents will cause premature membrane failure Since oxidation damage is not covered under warranty the manufacturer recommends removing residual free chlorine by pretreatment prior to membrane exposure Wet tested membrane elements must be kept sealed and moist when in storage Drying out may occur and damage the membrane permanently Prevent elements from freezing or being exposed to direct sunlight Wet tested elements are vacuum sealed in a polyethylene bag containing 1 0 sodium meta bi sulfite and then packaged in a cardboard box Discard the permeate for the first twenty four hours of operation The permeate flow product water flow varies with feed water temperature For membrane warranty information please contact the manufacturer The manufacturer believes the information and data contained herein be accurate and useful The information and data are offered in good faith but without guarantee as conditions and methods of use of products are beyond the manufacturer s control The manufacturer assumes no liability for results obtained or damages incurred through the application of the presented information and data It is the user s responsibility to determine the appropriateness of these products for the user s specific end uses z AXEO P 800 320 4074 760 723 5417 W www axeonwater com 760 728 5062 E sales axeonwater com 541 Indus
6. CONCENTRATE 0 300 PSI VALVE 5 RECYCLE VALVE SEMEN 4 5 x20 10 MICRON SEDIMENT BAG FILTER THROTTLE VALVE FRONT VIEW FIGURE 1B 3 4 CONCENTRATE LINE TO CONCENTRATE VALVE LB BA Il S MICRON 7 DEDA SEDIMENT r1 4 5 xe0 WU 10 MICRON i SEDIMENT SOLENOID BAG FILTER VALVE o e 5 BACK VIEW FIGURE 1C 17 ENGF 108 REV A 01 11 2011 AXEON Water Technologies 7 1 PERMEATE CHECK VALVE fl 2 INLET LINE FROM WATER SOURCE 1 PERMEATE LINE OUT TO USE LEFT VIEW FIGURE 1D 8 PRESSURE VESSELS 27 40 beaches PUMP amp MOTOR 11 1 FEED WATER TO INLET OF PUMP 1 CONCENTRATE LINE OUT TO DRAIN RIGHT VIEW FIGURE 1E 18 ENGF 108 REV A 01 11 2011 AXEON Water Technologies LOW PRESSURE SWITCH 1 PERMEATE CHECK VALVE PERMEATE TDS PROBE 1 CONCENTRATE 1 PERMEATE LINE OUT TO DRAIN LINE OUT TO USE BACK CUTAWAY VIEW FIGURE 1F Note A portion of the frame has been removed to expose components 19 ENGF 108 REV A 01 11 2011 AXEON Water Technologies DT 10000 MEMBRANE FLOW DIAGRAM 1 l s a q EL Sal SEN 1 Ae 1 TE VAN Note Black arrows r
7. PUMP 3HP 1PH 208 230 480V Pre ds 204914 VALVE SOLENOID UL 220V 1 DEM lisses 200739 HOUSING FILTER BAG 2 FNPT 18 FSI dan lisses 200640 CART SEDIMENT POLYPRO 4 5 x 20 1 MIC 203649 HOUSING FILTER BLK BLU 4 5 20 1 FNPT Z sd o 200994 VALVE GLOBE SS 3 4 FNPT Os 200527 HOUSING MEM PVC 4040 1 2 P x 1 2 C FNPT MT 200379 MEM HF1 4040 SYSTEMS petr an 204036 MANIFOLD DELRIN 11 HOLE 3 4 IN 1 2 OUT TO LOS 200900 METER FLOW PM 0 20GPM 1 x 1 MNPT lee 202307 GAUGE BKM FILL 0 100PSI BAR 2 5 DIA Pass SE 200904 GAUGE BKM FILL 0 300PSI BAR 2 5 DIA Sa hs 200967 VALVE CHECK PVC 1 FNPT x 1 FNPT repe ese lise 203263 CONT COMP ROTROL S 150 220V 3PH 200906 SWITCH PRESS LOW N O 15 30 1 4 FNPT 12 200598 SNAP RING DELRIN 4 200597 END PLUG CLOSED GTX 4 1 2 FNPT 200596 END PLUG OPEN GTX 4 1 2 FNPT lee lan 200588 CLAMP SADDLE NYLON BLK 4 PVC FRP ENGF 108 REV A 01 11 46 2011 AXEON Water Technologies No Qty DT 15000 SYSTEM PART LIST PartNo Description EN TE 200792 PUMP 3HP 1PH 208 230 480V Pre ds 204914 VALVE SOLENOID UL 220V 1 DEM lisses 200739 HOUSING FILTER BA
8. 63 7 17 6 294 70 9 21 6 1 124 78 1 25 6 0 982 85 3 29 6 0 874 567 13 7 A91 63 9 177 1 290 71 1 21 7 1 120 78 3 25 7 0 979 85 5 29 7 0 871 56 8 13 8 486 64 0 17 8 285 71 2 21 8 116 78 4 25 8 0 977 85 6 29 8 0 869 57 0 13 9 480 64 2 17 9 281 714 21 9 1 112 78 6 25 9 0 974 85 8 29 9 0 866 oF PC x 9 5 32 Corrected Flow Rate Measured Flow Rate Feed Water Temp 36 ENGF 108 REV A 01 11 2011 AXEON Water Technologies If a system is rated to produce 5 of permeate water 77 F The same system will produce more water at a higher temperature It will also produce less water at a lower temperature Use the temperature correction table to obtain the correct flow Example 5 59 F 5 1 42 3 52 5 77 F 5 1 5 gpm 5 84 F 5 0 89 5 62 SERVICE ASSISTANCE If service assistance is required please complete the following process Contact your local dealer or distributor Prior to making the call have the following information available system installation date serial number daily log sheets current operating parameters e g flow operating pressures pH etc and a detailed description of the problem 37 ENGF 108 REV A 01 11 2011 AXEON Water Technologies OPERATION Company Location Week Of System Serial Date of Start Up Date of Last Cleaning Date Time Hour
9. 8 0 921 53 4 11 9 594 60 6 15 9 376 67 8 19 9 193 75 0 23 9 1 038 82 2 27 9 0 918 53 6 12 0 1 588 60 8 16 0 371 68 0 20 0 1 189 75 2 24 0 1 035 82 4 28 0 0 915 53 8 12 1 1 582 61 0 16 1 366 68 2 20 1 185 75 4 24 1 1 031 82 6 28 1 0 913 54 0 12 2 576 61 2 16 2 36 68 4 20 2 180 75 6 24 2 1 028 82 8 28 2 0 910 54 1 12 3 1 570 61 3 16 3 1 356 68 5 20 3 1 176 75 7 24 3 1 024 82 9 28 3 0 908 54 3 12 4 1 564 61 5 16 4 1 351 68 7 20 4 1 172 75 9 24 4 1 021 83 1 28 4 0 905 54 5 12 5 558 617 16 5 347 68 9 20 5 168 76 1 24 5 017 83 3 28 5 0 902 54 7 12 6 553 61 9 16 6 342 69 1 20 6 164 76 3 24 6 1 014 83 5 28 6 0 900 54 9 12 7 1 547 62 1 16 7 1 337 69 3 20 7 1 160 76 5 24 7 1 010 83 7 28 7 0 897 55 0 12 8 1 541 62 2 16 8 332 69 4 20 8 156 76 6 24 8 007 83 8 28 8 0 894 55 2 12 9 536 62 4 16 9 327 69 6 20 9 152 76 8 24 9 1 003 84 0 28 9 0 892 55 4 13 0 530 62 6 17 0 1 323 69 8 21 0 1 148 77 0 25 0 000 84 2 29 0 0 889 55 6 13 1 524 62 8 17 1 318 70 0 21 1 144 772 25 1 0 997 84 4 29 1 0 887 55 8 13 2 519 63 0 17 2 313 70 2 21 2 140 77 4 25 2 0 994 84 6 29 2 0 884 55 9 13 3 513 63 1 17 3 308 70 3 21 3 1 136 77 5 25 3 0 991 847 29 3 0 882 56 1 13 4 508 63 3 17 4 304 70 5 21 4 132 77 7 25 4 0 988 84 9 29 4 0 879 56 3 13 5 502 63 5 17 5 299 70 7 21 5 128 77 9 25 5 0 985 85 1 29 5 0 877 56 5 13 6 1 496
10. RR CREDE RR 39 3 ENGF 108 REV A 01 11 2011 AXEON Water Technologies INTRODUCTION Your DT Series system is a durable piece of equipment which with proper care will last for many years This User s Manual outlines installation operation maintenance and troubleshooting details vital to the sustained performance of your system The test results which are included with this User s Manual indicate your system s permeate product and concentrate waste test results If your system is altered at the site of operation or if the feed water conditions change please contact your local dealer or distributor to determine the proper recovery for your application CAUTION gt NOTE IN ORDER TO MAINTAIN THE MANUFACTURER S WARRANTY AN OPERATING LOG MUST BE MAINTAINED AND COPIES WILL NEED TO BE SENT TO YOUR LOCAL DEALER OR DISTRIBUTOR FOR REVIEW CAUTION gt NOTE PRIOR TO OPERATING OR SERVICING THE REVERSE OSMOSIS SYSTEM THIS USER S MANUAL MUST BE READ AND FULLY UNDERSTOOD KEEP THIS AND OTHER ASSOCIATED INFORMATION FOR FUTURE REFERENCE AND FOR NEW OPERATORS OR QUALIFIED PERSONNEL NEAR THE SYSTEM SAFETY The Safety section of this User s Manual outlines the various safety headings used throughout this manual s text and are enhanced and defined below NOTE INDICATES STATEMENTS THAT PROVIDE FURTHER INFORMATION AND CLARIFICATION CAUTION CAUTION INDICATES STATEMENTS THAT ARE USED TO IDENTIFY CONDITIONS OR PRAC
11. bar amp NF4 Membranes Operating Pressure 77 Degrees F 25 Degrees C Recovery as stated 7 0 pH Data taken after 30 minutes of operation Low temperatures and high feed water TDS levels will significantly affect system s production capabilities Computer projections should be run for individual applications which do not meet or exceed minimum and maximum operating limits NOTE HIGHER TDS AND OR LOWER TEMPERATURES WILL REDUCE THE SYSTEM S PRODUCTION REJECTION RECOVERY amp FLOW RATES DT Series reverse osmosis systems are designed to produce permeate water at the capacities indicated by the suffix in the system s name under the conditions listed above For example the DT 10000 produces 10000 gallons per day of permeate water at the listed operating test conditions The amount of total dissolved solids TDS rejected by the membrane is expressed as a percentage For example a 98 5 rejection rate means that 98 5 of total dissolved ENGF 108 REV A 01 11 2011 AXEON Water Technologies solids do not pass through the membrane To calculate the rejection use the following formula Rejection Feed TDS Product TDS Feed TDS x 100 Example 98 5 550 8 25 550 x 100 A NOTE ALL TDS FIGURES MUST BE EXPRESSED IN THE SAME UNITS TYPICALLY PARTS PER MILLION PPM OR MILLIGRAMS PER LITER MG L DT Series reverse osmosis systems are designed to reject up to 98 5 NaCl unless computer projecti
12. directions should be observed for installation of each element into each housing Figure 4 Page 30 As time progresses the efficiency of the membrane will be reduced In general the salt rejection does not change significantly until two or three years after installation when operated on properly pretreated feed water The permeate flow rate will begin to decline slightly after one year of operation but can be extended with diligent flushing and cleaning of the system A high pH and or precipitation of hardness can cause premature loss in rejection REPLACING THE MEMBRANE ELEMENT CAUTION gt WARNING THE BRINE SEAL MUST BE IN THE SAME POSITION FOR EACH MEMBRANE ELEMENT HOUSING SO MARK EACH HOUSING PRIOR TO REMOVING THE MEMBRANE ELEMENTS THE BRINE SEAL IS A RUBBER SEAL THAT PROTRUDES ON ONE SIDE OF THE MEMBRANE AND IS ALWAYS ON THE FEED SIDE OF THE MEMBRANE ELEMENT 29 ENGF 108 REV A 01 11 2011 AXEON Water Technologies Remove one membrane element at a time from the membrane element housings from the top of the housing Long nose pliers may be necessary to pull the old membrane element out of the membrane element housing Lubricate the brine seal with non petroleum based lubricant Silicone DC 111 Install the brine seal side of the membrane element first Figure 4 Page 30 When the housings have a direction of flow from bottom to top the brine seal should be located at the bottom of the housing Ata slight an
13. of Operation Filter inlet pressure psi Filter outlet Pressure psi Concentrate Pressure psi Pump Discharge Pressure psi Feed Flow gpm Permeate Flow gpm Concentrate Flow gpm Recovery Feed Temperature Feed TDS ppm Permeate TDS ppm Rejection Feed PH Permeate PH Scale Inhibitor Feed ppm Iron mg L Free Chlorine mg L Hardness gpg CaCO3 ENGF 108 REV A 01 11 38 2011 AXEON Water Technologies DRAWINGS FIGURE 5 2011 AXEON Water Technologies ENGF 108 REV A 01 11 FIGURE 6 2011 AXEON Water Technologies 40 ENGF 108 REV A 01 11 17 16 FIGURE 7 41 ENGF 108 REV A 01 11 2011 AXEON Water Technologies FIGURE 8 42 ENGF 108 REV A 01 11 2011 AXEON Water Technologies e 2 FIGURE 9 43 2011 AXEON Water Technologies ENGF 108 REV A 01 11 gt 8 e gt ns UD Note A portion of the frame has been removed to expose components FIGURE 10 44 2011 AXEON Water Technologies ENGF 108 REV A 01 11 5 CN e Te Note A portion of the frame has been removed to expose components FIGURE 11 2011 AXEON Water Technologies 45 ENGF 108 REV A 01 11 No Qty DT 10000 SYSTEM PART LIST PartNo Description EN TE 200792
14. 00 should be adjusted until it produces about 10000 GPD or 6 94 GPM of permeate product water at 77 F Design flow might be achieved below 150 PSI GPM GPD 1440 Example 6 94 10000 1440 24 ENGF 108 REV A 01 11 2011 AXEON Water Technologies DESIGN BASIS FOR DT 10000 DT 15000 DT 20000 Specifications Models DT 10000 DT 15000 DT 20000 Design Configuration Single Pass Feed Water Source City or Well Water City or Well Water City or Well Water Standard Recovery Rate 55 Rejection and Flow Rates Nominal Sal Rejection 98 5 Permeate Flow gpm lpm 13 89 52 57 Minimum Feed Flow gpm lpm 29 00 109 77 Maximum Feed Flow gpm 33 00 124 91 Connections Membranes Membrane Zeie Membrane Quantity Membrane Size 55 Recovery with Optional Concentrate Recycle Up to 75 Up to 75 Up to 75 Vessels Vessel 2222 Vessel Quan ob E Pumps Pump Type Motor HP 51547 RPM 60 DOT 3250 2900 Electrical 220 50HZ 1PH 220 50HZ 1PH 220V 60HZ 3PH 220V 60HZ 3PH 220 50HZ 3PH Voltage Options 220 50HZ 3PH 220 50HZ 3PH 380 50HZ 1PH 380V SOHZ 1PH 380 50HZ 1PH 460V 60HZ 3PH 460V 60HZ 3PH 460V 60HZ 3PH Voltage Amp Draw 220V 60Hz 220 50 Hz 380V 50 Hz 460V 60 Hz Systems Dimensions LxWxH inch cm Weight Tb kg Product Flow rates are based on equipment test parameters Does not include operating space requirements WARNING NEV
15. 08 REV A 01 11 2011 AXEON Water Technologies DT 20000 FLOW DIAGRAM 4 1000084 QN3931 108 5 I Di SSH 01 51 2011 AXEON Water Technologies ENGF 108 REV A 01 11 TANK LUW LVL 2011 AXEON Water Technologies 220V 60Hz 1 PHASE ELECTRICAL SCHEMATIC S 150 TANK HI LVL PRE TREAT 227 LPS age INLET LE 7 5 RI RO PUMP 40 CAUTION DISCONNECT AND BRANCH PROTECTION IS REQUIRED ON THE POWER FEEDING THIS PANEL 52 ENGF 108 REV A 01 11 220V 50 60Hz 3 PHASE ELECTRICAL SCHEMATIC S 150 lla INLET FLUSH VALVE VALVE L zen vac CAUTIONI DISCONNECT AND BRANCH PROTECTION IS REQUIRED ON THE POWER FEEDING THIS PANEL 53 2011 AXEON Water Technologies ENGF 108 REV A 01 11 MAIN POWER CONNECT APPROVED DISCONNECT 54 CAUTION DISCONNECT AND BRANCH PROTECTION IS REQUIRED ON THE POWER FEEDING THIS PANEL 460V 60Hz 3 PHASE ELECTRICAL SCHEMATIC S 150 2011 AXEON Water Technologies ENGF 108 REV A 01 11 55 ENGF 108 REV A 01 11 2011 AXEON Water Technologies
16. 150 psi 27 ENGF 108 REV A 01 11 2011 AXEON Water Technologies Example 98 5 550 8 25 550 x 100 Rejection Feed TDS Product TDS Feed TDS x 100 ADJUSTING THE THROTTLE VALVE To decrease the pressure turn the handle clockwise To increase the pressure turn the handle counter clockwise Figure 3 Page 27 DECREASE PRESSURE INCREASE PRESSURE FIGURE 3 28 ENGF 108 REV A 01 11 2011 AXEON Water Technologies MEMBRANE REMOVAL amp REPLACEMENT Replacing membranes in the pressure vessels is an easy process if you have the proper information and tools at hand Please refer to the following instructions when removing and replacing membrane elements CAUTION gt WARNING ALL PRESSURE GAUGES MUST READ ZERO BEFORE PROCEEDING BEFORE ATTEMPTING DISCONNECT THE POWER FROM THE SYSTEM AND BLEED ALL WATER PRESSURE FROM THE SYSTEM 1 Remove the end caps from the top of the membrane housings This is done by removing the white snap ring of the membrane housing 2 Remove the membrane bag containing the membrane element from the shipping box WEAR GLOVES FOR THE FOLLOWING STEPS IN ORDER NOT TO CONTAMINATE THE MEMBRANE 3 Cut the bag open as close as possible to the seal at the end of the bag so the bag may be re used if necessary 4 Make sure that all parts are clean and free from dirt Examine the brine seal and permeate tube for nicks or cuts Replace the O rings or brine seal if damaged 5 Flow
17. 18 1 272 71 8 22 1 105 79 0 26 1 0 968 50 4 10 2 698 57 6 14 2 464 64 8 18 2 267 72 0 22 2 101 792 26 2 0 965 50 5 10 3 692 57 7 14 3 459 64 9 18 3 1 262 72 1 22 3 097 79 3 26 3 0 962 50 7 10 4 1 686 57 9 14 4 453 65 1 18 4 258 72 3 22 4 093 79 5 26 4 0 959 50 9 10 5 679 58 1 14 5 448 65 3 18 5 1 254 72 5 22 5 1 090 79 7 26 5 0 957 51 1 10 6 673 58 3 14 6 1 443 65 5 18 6 1 249 727 22 6 1 086 79 9 26 6 0 954 51 3 10 7 1 667 58 5 147 1 437 65 7 18 7 1 245 72 9 22 7 082 80 1 26 7 0 951 51 4 10 8 660 58 6 14 8 432 65 8 18 8 240 73 0 22 8 078 80 2 26 8 0 948 51 6 19 9 654 58 8 14 9 1427 66 0 18 9 1 236 73 2 22 9 075 80 4 26 9 0 945 51 8 11 0 1 648 59 0 15 0 1422 66 2 19 0 1 232 73 4 23 0 071 80 6 27 0 0 943 52 0 11 1 642 59 2 15 1 417 66 4 19 1 1 227 73 6 23 1 1 067 80 8 27 1 0 940 52 2 11 2 636 59 4 15 2 1 41 66 6 19 2 1 223 73 8 23 2 064 81 0 27 2 0 937 52 3 11 3 630 59 5 15 3 406 66 7 19 3 219 73 9 23 3 060 81 1 27 3 0 934 52 5 11 4 1 624 59 7 15 4 1 40 66 9 19 4 214 74 1 23 4 1 056 81 3 27 4 0 932 52 7 11 5 618 59 9 15 5 396 67 1 19 5 210 74 3 23 5 1 053 81 5 27 5 0 929 52 9 11 6 611 60 1 15 6 39 67 3 19 6 1 206 74 5 23 6 1 049 81 7 27 6 0 926 53 1 117 1 605 60 3 15 7 1 386 67 5 19 7 1 201 747 23 7 1 045 81 9 27 7 0 924 53 2 11 8 Deg 60 4 15 8 1 38 67 6 19 8 1 197 74 8 23 8 1 042 82 0 27
18. 3 F 45 C Maximum Feed Water Turbidity 1 NTU Maximum Operating Pressure 600 psi 41 bar Maximum Feed Silt Density Index 5 SDI Minimum Concentrate Flow Rate 5 1 Chlorine Tolerance ppm pH Range Continuous Operation 2 11 Product Specifications Applied Permeate Nominal Salt Description Pressure Flow Rate Rejection psi bar gpd m3 d psi bar gpd m3 d Par Number 700483 2000079 40 50 200404 Wi aois 7093 5 40 50 200402 2521 70 4 83 350 1 33 40 50 200405 NF3 4021 70 4 83 1000 3 79 40 50 200403 NF3 2540 70 4 83 850 3 22 40 50 200406 NF3 4040 70 483 2500 9 46 40 50 Test Parameters 550 TDS Filtered 5 Micron De Chlorinated Softened City Feed Water 77 Degrees F 15 Permeate Recovery 6 5 7 0 pH Range the Specified Operating Pressure Data Taken After 30 Minutes of Operation Maximum Pressure drop for each element is 10 psi Minimum salt rejection is 96 Permeate flow for individual elements may vary 20 Applied eate Nominal Salt Part Description Pressure Rejection Dimensions inch m Description A D A B c D B 9 wan upsa 110794 07501909 246098 110798 0750909 39511003 110998 028865 246099 216054 110734 975009 3951101 111794 0751009 24698 weg 11794 97509 355 100 Under ce
19. Clean with high pH cleaner Chlorine Oxidation Check Chlorine feed equipment and de chlorination system Abrasion of membrane by Crystalline Material Improve pretreatment Check all filters for media leakage ENGF 108 REV A 01 11 34 2011 AXEON Water Technologies ABNORMAL PERMEATE FLOW Permeate flow should be within 20 of the rated production after correcting the feed water temperatures above or below 77 F Check your permeate flow meter to determine the permeate flow rate A NOTE TO DETERMINE THE TEMPERATURE CORRECTION FACTOR LOCATE THE TEMPERATURE CORRECTION TABLE IN THIS USER S MANUAL AND FOLLOW THE DIRECTIONS 35 ENGF 108 REV A 01 11 2011 AXEON Water Technologies TEMPERATURE CORRECTION FACTORS FOR MEMBRANE Find the temperature correction factor TCF from the table below Divide the rated permeate flow at 77 F by the temperature correction factor The result is the permeate flow at the desired temperature See example on the next page Temperature Correction Factor Temperature Correction Factor Temperature Correction Factor Temperature Correction Factor Temperature Correction Factor Temperature Temperature Temperature SF C Temperature F C Temperature F C 50 0 10 0 14 57 2 14 0 1 64 4 18 0 71 6 22 0 109 78 8 26 0 0 971 50 2 10 1 705 57 4 14 1 469 64 6
20. ER EXCEED THE MAXIMUM PRESSURE RATING OF YOUR SYSTEM 25 ENGF 108 REV A 01 11 2011 AXEON Water Technologies OPERATING DO s amp DON Ts DO e Change the cartridge filters regularly e Monitor the system and keep a daily log e Run the system as much as possible on a continuous basis e Adjust the system recovery to the recommended value e Always feed the pump with filtered water DON T e Permit chlorine to enter or be present in the feed water e Shut down the system for extended periods e Close the throttle valve completely e Operate the system with insufficient feed flow e Operate the pump dry OPERATION amp MAINTENANCE The reverse osmosis process causes the concentration of impurities The impurities may precipitate come out of solution when their concentration reaches saturation levels A NOTE PRECIPITATION CAN SCALE OR FOUL MEMBRANES AND MUST BE PREVENTED Check your feed water chemistry and pre treat the water and or reduce the system s recovery as required If necessary consult with your local dealer or distributor 26 ENGF 108 REV A 01 11 2011 AXEON Water Technologies PRE FILTER PRESSURE GAUGES These gauges measure the feed water pressure when it enters and exits the pre filters A pressure differential of 10 15 psi or more on the two pressure gauges indicates that the pre filters require servicing For example if the inlet pressure is 40 psi the filter should be changed when the outlet pre
21. ERSE OSMOSIS PERMEATE WATER WILL TYPICALLY BE 1 2 POINTS LOWER THAN THE FEED WATER PH A LOW PH CAN BE VERY AGGRESSIVE TO SOME PLUMBING MATERIALS SUCH AS COPPER PIPING CONCENTRATE WASTE WATER CONNECTION Locate the 1 connection labeled concentrate and attach to a drain Run the concentrate line to an open drain in a free and unrestricted manner no backpressure CAUTION gt CAUTION ANY RESTRICTIONS OR BLOCKAGE IN THE DRAIN LINE CAN CAUSE BACKPRESSURE WHICH WILL INCREASE THE SYSTEM S OPERATING PRESSURE THIS CAN RESULT IN DAMAGE TO THE SYSTEM S MEMBRANES AND COMPONENTS ELECTRICAL The motor used on the DT Series systems are pump and motor combination The motor is available in 220 380 460 Volt 50 60 Hertz 1 Phase 3 phase Each DT Series system is equipped with a 5 foot electrical cord Ensure that the electrical circuit supplying the system is compatible with the requirements of the specific DT model you are installing ENGF 108 REV A 01 11 2011 AXEON Water Technologies A NOTE IT S RECOMMENDED THAT A LICENSED ELECTRICIAN WIRE YOUR SYSTEM IN ACCORDANCE WITH LOCAL AND NATIONAL ELECTRICAL CODES NEC CAUTION gt WARNING TO REDUCE THE RISK OF ELECTRICAL SHOCK THE INCOMING POWER SUPPLY MUST INCLUDE A PROTECTIVE EARTH GROUND DT Series systems are typically controlled with a liquid level switch in a storage tank The liquid level switch turns the system on when the water level in the tank drops and off whe
22. Fallbrook CA 92028 WATER TECHNOLOGIES AXEON is a registered trademark of AXEON Water Technologies 01 11 22011 AXEON Water Technologies 13 ENGF 108 REV A 01 11 2011 AXEON Water Technologies NF4 OPTIONAL AXEON NF4 Series Reverse Osmosis Membrane Elements AXEON NF4 Membrane Elements are one of the industries most reliable and highest performing nanofiltration elements AXEON membranes are available in all standard commercial sizes and feature a protective ABS shell Advanced membrane technology and manufacturing processes ensure high quality and performance allowing for improved system performance All elements are shipped dry for an extended shelf life and easier handling Membrane elements are 100 vacuum integrity tested and may also be ordered as individually wet tested Operating Limits Membrane Type Polyamide Thin Film pH Range Short Term Cleaning 30 Min 1 13 Maximum Operating Temperature 113 F 45 C Maximum Feed Water Turbidity 1 NTU Maximum Operating Pressure 600 psi 41 bar Maximum Feed Silt Density Index 5 501 Minimum Concentrate Flow Rate 5 1 Chlorine Tolerance ppm pH Range Continuous Operation 2 11 Product Specifi Applied Permeate Nominal Salt MgSO Description Pressure Flow Rate Rejection Rejection Applied Permeate Nominal Sall MgSO Part Description Pressure Flow Rate Rejection Rejection Number Part psi bar m3
23. G 2 FNPT 18 FSI dan lisses 200640 CART SEDIMENT POLYPRO 4 5 x 20 1 MIC 203649 HOUSING FILTER BLK BLU 4 5 20 1 FNPT 200994 VALVE GLOBE SS 3 4 FNPT Tarbes 200527 HOUSING MEM PVC 4040 1 2 1 2 FNPT 200379 HF1 4040 SYSTEMS an 204036 MANIFOLD DELRIN 11 HOLE 3 4 IN 1 2 OUT TO LOS 200900 METER FLOW PM 0 20GPM 1 x 1 MNPT lee 202307 GAUGE BKM FILL 0 100PSI BAR 2 5 DIA Pass SE 200904 GAUGE BKM FILL 0 300PSI BAR 2 5 DIA ON 200967 VALVE CHECK PVC 1 FNPT x 1 FNPT LE sonder lise 203263 CONT COMP ROTROL S 150 220V 3PH TS Fee 200906 SWITCH PRESS LOW N O 15 30 1 4 FNPT eos 200598 SNAP RING DELRIN 4 b t e Din 200597 END PLUG CLOSED GTX 4 1 2 FNPT o iod B dede 200596 END PLUG OPEN GTX 4 1 2 FNPT sens dB eins 200588 CLAMP SADDLE NYLON BLK 4 PVC FRP ENGF 108 REV A 01 11 47 2011 AXEON Water Technologies Item No Qty Br ER 2 17757 due lisse Dh ZO dou CAFES EEN 10 B oux En 10 dr Oise See lasse jt Tod lue lisse dos dedos Ost 20 s 1 E 10 10 20 ENGF 108 REV A 01 11 DT 20000 SYSTEM PART LIST PartNo Description
24. Reverse Osmosis User s Manual Model DT 10000 DT 15000 DT 20000 s ie 4 DT 20000 Pictured This Page Left Blank XEON Water Technologies Table of Contents INTRODUCTION sis ertt eee ene isli 4 SAFETY inti ike 4 FEED WATER 8 OPERATION 5 REJECTION RECOVERY 8 FLOW RATES 7 5 SYSTEM REQUIREMENTS 8 OPERATION 6 MEMBRANE ELEMENT SS unis nine 9 DT 10000 DT 15000 DT 20000 SYSTEM IDENTIFICATION ener 15 DT 10000 MEMBRANE FLOW DIAGRAM 20 DT 15000 MEMBRANE FLOW DIAGRAM 21 DT 20000 MEMBRANE FLOW DIAGRAM eee eee eee een ER R K R R Kn 22 SYSTEM PURGING eroe ite 23 INITIAL START UP cS 24 DESIGN BASIS FOR DT 10000 DT 15000 20000 25 OPERATING DO s amp DON TS ed eene ate ne A eine ih ae IA ern 26 OPERATION amp MAINTENANCE atteste taste ito e Ces e et idee e n 26 MEMBRANE REMOVAL amp REPLACEMENT sass 29 FEUSHING TEIE SYSTEM een rare eh t reo d tr gc Ev ette eee 32 PREPARING UNIT FOR STORAGE OR SHIPMENT ire 32 REVERSE OSMOSIS 5 34 TEMPERATURE CORRECTION FACTORS FOR 36 OPERATION otii ttt eo tete Hem ate e 38 DRAWINGS etna ub gehe tuat a ooo ON
25. TICES THAT COULD RESULT IN EQUIPMENT OR OTHER PROPERTY DAMAGE WARNING INDICATES STATEMENTS THAT ARE USED TO IDENTIFY CONDITIONS OR PRACTICES THAT COULD RESULT IN INJURY OR LOSS OF LIFE FAILURE TO FOLLOW WARNINGS COULD RESULT IN SERIOUS INJURY OR EVEN DEATH ENGF 108 REV A 01 11 2011 AXEON Water Technologies CAUTION DO NOT UNDER ANY CIRCUMSTANCE REMOVE ANY CAUTION WARNING OR OTHER DESCRIPTIVE LABELS FROM THE SYSTEM FEED WATER amp OPERATION SPECIFICATIONS Nothing has a greater effect on a reverse osmosis system than the feed water quality NOTE IT IS VERY IMPORTANT TO MEET THE MINIMUM FEED WATER REQUIREMENTS FAILURE TO DO SO WILL CAUSE THE MEMBRANES TO FOUL AND VOID THE MANUFACTURER S WARRANTY OPERATING LIMITS Maximum Feed Temperature F C 105 40 96 Maximum Free Chlorine ppm 0 Minimum Feed Temperature F 40 4 44 Maximum TDS ppm 2000 Maximum Ambient Temperature F 120 48 89 Maximum Hardness gpg 15 Minimum Ambient Temperature F 35 1 66 Maximum pH Continuous 1 3 Minimum Feed Pressure psi 35 2 41 Maximum pH Cleaning 30 Min 12 Maximum Operating Pressure psi bar Minimum pH Cleaning 30 Min 2 Nam SDI Rating SD Maximum Tid NTU Test Parameters 550 TDS Filtered 5 Micron DeChlorinated Softened City Feed Water 35 psi 2 41 bar Feed Pressure 150 psi 10 34 bar HF1 Membranes 100 psi 6 89 bar HF4 Membranes or 70 psi 4 83
26. a P wees psi bar gpd m3 d u 20007 NF4 2514 701489 2001074 80 90 98 200410 NF4 4014 701483 40011 30 90 20040 NF4 2521 2501098 80290 NF4 4021 701453 9501540 80 90 200109 2510 701483 eso 257 80290 NFA 2040 70 aea 200017 80290 8 Test Parameters 550 TDS Filtered 5 Micron De Chlorinated Softened City Feed Water 77 Degrees F 15 Permecte Recovery 6 5 7 0 pH Range at the Specified Operating Pressure Data Taken After 30 Minutes of Operation Maximum Pressure drop for each element is 10 psi Minimum salt rejection is 96 Permeate flow for individual elements may vary 20 Dimensions inch mm Description A Description B D A B c D Nr4 2514 14 355 6 1 1 27 94 075 19 05 2 4 60 96 4 4014 14 3556 1117794 075 19 05 3 95 100 3 NF4 2521 21 533 4 1 1 27 94 075 19 05 2 4 60 96 21 533 4 1 1 27 94 0 75 19 05 3 95 100 3 NF4 2540 40 1016 0 1 1 27 94 075 19 05 40 1016 0 1 1 27 94 0 75 19 05 3 95 100 3 Under certain conditions the presence of free chlorine and other oxidizing agents will cause premature membrane failure Since oxidation damage is not covered under warranty the manufacturer recommends removing residual free chlorine by pretreatment prior to membrane exposure Wet tested membrane
27. amp meter to check the motor amp draw Concentrate valve might be damage Replace Needle Valve Leaks Fix any visible leaks Low Permeate Flow Low inlet flow Adjust concentrate valve Cold feed water See temperature correction sheet Low operating pressure See low inlet pressure Defective membrane brine seal Inspect amp or replace brine seal Fouled or Scaled membrane Clean membranes High permeate flow Damaged product tube o rings Inspect and or replace Damaged or oxidized membrane Replace membrane Exceeding maximum feed water temperature See temperature correction sheet Poor permeate quality Low operating pressure See low inlet pressure Damage product tube o rings Inspect and or replace Damaged or oxidized membrane Replace membrane Membrane fouling Metal Oxide Fouling Improve pretreatment to remove metals Clean with Acid Cleaners Colloidal Fouling Optimize pretreatment for colloid removal Clean with high pH anionic cleaners Scaling CaSO4 CaSO3 BaSO4 SiO2 Increase acid addition and antiscalant dosage for CaVO3 and CaCO4 Reduce recovery Clean with Acid Cleaners Biological Fouling Shock dosage of Sodium Bi Sulfate Continuous feed of Sodium Bi Sulfate at reduced pH Chlorination and de chlorination Replace cartridge filters Organic Fouling Activated Carbon or other pretreatment
28. e 1 Figure 2 Page 22 5 Turn the feed water on and let the system purge until no visible bubbles appear from concentrate flow meter 14 Figure 1B Page 16 6 Fully open the throttle valve 12 Counter Clockwise Figure 1B Page 16 gt Lever Inline Lever Offset Operating Position Bypass Position FIGURE 2 23 ENGF 108 REV A 01 11 2011 AXEON Water Technologies Ure ONS 10 11 INITIAL START UP Keep the permeate water line to drain for this procedure Fully open the concentrate valve 10 Counter Clockwise Figure 1B Page 16 Fully close the recycle valve 9 Clockwise If Applicable Figure 1B Page 16 Fully open the throttle valve 12 Counter Clockwise Figure 1B Page 16 Return position of the bypass white lever inline on the solenoid valve 1 Figure 1B Page 16 Turn the RO system on 8 and adjust the concentrate waste valve 10 recycle valve 9 If Applicable and the throttle valve to the designed flow and pressure Figure 1B Page 16 Inspect the system for leaks Allow the system to run for one hour to flush the preservative solution from the system After one hour shut down the system Re direct the permeate water back to the tank and then turn the system back on Record the readings daily for a week and after a week record the readings once a week Adjust the pump throttle valve and concentrate valve until the correct flow is achieved For example DT 100
29. elements mus be kept sealed and moist when in storage Drying out may occur and damage the membrane permanently Prevent elements from freezing or being exposed to direct sunlight Wet tested elements are vacuum sealed in a polyethylene bag containing 1 0 sodium metabisulfite and then packaged in a cardboard box Discard the permeate for the first twenty four hours of operation The permeate flow product water Row varies with feed water temperature For membrane warranty information please contact the manufacturer The manufacturer believes the information and data contained herein lo be accurate and useful The information and data are offered in good faith but without guarantee as conditions and methods of use of products are beyond the manufacturer s control The manufacturer assumes no liability for results obtained or damages incurred through the application of the presented information and data It is the user s responsibility to determine the appropriateness of these products for the user s specific end uses AXEO P 800 320 4074 760 723 5417 W www axeonwater com 760 728 5062 E sales axeonwater com 541 Industrial Way Suite 1 Fallbrook 92028 WATER TECHNOLOGIES AXEON is a registered trademark of AXEON Water Technologies 01 11 2011 AXEON Water Technologies 14 ENGF 108 REV A 01 11 2011 AXEON Water Technologies DT 10000 DT 15000 DT 20000 SYSTEM IDENTIFICATION j
30. epresent concentrate water and white arrows represent permeate FIGURE 1G water 2011 AXEON Water Technologies 20 ENGF 108 REV A 01 11 DT 15000 MEMBRANE FLOW DIAGRAM mys HEN 1 3 WS 8 7 Le SK VS Note Black arrows represent concentrate water and white arrows represent permeate FIGURE 1H water 21 2011 AXEON Water Technologies ENGF 108 REV A 01 11 DT 20000 MEMBRANE FLOW DIAGRAM GET N 5 2 on RA VAL 680 pR NESS Tan MITT EE Nj Var e Us p GPS props B D P 1 A f 2 FIGURE 11 Note Black arrows represent concentrate water and white arrows represent permeate water 22 ENGF 108 REV A 01 11 2011 AXEON Water Technologies SYSTEM PURGING Carefully inspect your system before initial start up Check that all plumbing and electrical connections are not loose or have not come undone during shipment A User s Manual Test Results and Filter Housing Wrench will accompany your DT Series reverse osmosis system A NOTE LEAVE THE POWER TO THE SYSTEM OFF FOR THIS PROCEDURE Redirect permeate water to the drain for this procedure Fully open the concentrate valve 10 Counter Clockwise Figure 1B Page 16 Fully close the recycle valve 9 Clockwise If Applicable Figure 1B Page 16 Offset the position of the bypass white lever on the solenoid valv
31. gle insert the membrane while slightly rotating the element being careful not to tear or flip the brine seal A slow twisting motion should be used to insert the membrane element to ensure the brine seal stays in place Re lube the brine seal if necessary With a smooth and constant motion push the membrane element into the housing so the brine seal enters the housing without coming out of the brine seal groove Re install the end caps by gently twisting the end cap while pushing it onto the housing Ensure that you do not pinch or fatigue any O rings while re installing the end plug Push the end plug on until the outer diameter of the plug is flush with the outer diameter of the membrane housing Insert the snap ring until it is fully seated Install the locking clip if available Reconnect any fittings that may have been disconnected when the membrane element housings were disassembled To Start Up the system please refer to the Initial Start Up section of this manual See Page 23 A CAUTION WET MEMBRANES ARE SHIPPED IN A PRESERVATIVE SOLUTION THE MEMBRANES MUST BE FLUSHED FOR AT LEAST 1 HOUR TO REMOVE THE PRESERVATIVE FROM THE MEMBRANE DISCARD ALL OF THE PERMEATE AND CONCENTRATE WHICH IS PRODUCED DURING THE FLUSH PERIOD 30 ENGF 108 REV A 01 11 2011 AXEON Water Technologies FIGURE 3 FIGURE 4 View from the right side of DT 10000 DT 15000 DT 20000 reverse osmosis system 31 ENGF 108 REV A 01 11
32. ity Feed Water 77 Degrees F 15 Permeate Recovery 6 5 7 0 pH Range at the Specified Operating Pressure Data Taken After 30 Minutes of Operation Maximum Pressure drop for each element is 10 psi Minimum salt rejection is 96 Permeate flow for individual elements may vary 20 D Dimensions uu Bes Description LETS MES 1162790 07511999 9510931 21 533 4 1 1 27 94 0 75 19 05 3 95 100 3 40 10160 1 1 27 94 0 75 19 05 3 95 100 3 Under certain conditions the presence of free chlorine and other oxidizing agents will cause premature membrane failure Since oxidation damage is not covered under warranty the manufacturer recommends removing residual free chlorine by pretreatment prior to membrane exposure Wel tested membrane elements must be kept sealed and mois when in storage Drying out may occur and damage the membrane permanently Prevent elements from freezing or being exposed to direct sunlight Wet tested elements are vacuum sealed in a polyethylene bag containing 1 0 sodium metabisulfite and then packaged in a cardboard box Discard the permeate for the first twenty four hours of operation The permeate flow product water Row varies with feed water temperature For membrane warranty information please contact the manufacturer The manufacturer believes the information and dala contained herein to be accurate and useful The information and data are offered in good faith but wi
33. membranes unless otherwise specified General membrane element performance characteristics are listed below ENGF 108 REV A 01 11 2011 AXEON Water Technologies HF1 STANDARD HF Series Reverse Osmosis Membrane Elements AXEON HF1 Membrane Elements are one of the industries most reliable and highest performing reverse osmosis elements AXEON membranes are available in all standard commercial sizes and feature a protective ABS shell Advanced membrane technology and manufacturing processes ensure high quality and performance allowing for improved system performance All elements are shipped dry for an extended shelf life and easier handling Membrane elements are 100 vacuum integrity tested and may also be ordered as individually wet tested Operating Limits Membrane Type Polyamide Thin Film pH Range Short Term Cleaning 30 Min 1 13 5 Maximum Operating Temperature 113 F 45 C Maximum Feed Water Turbidity 1 NTU Maximum Operating Pressure 600 psi 41 bar Maximum Feed Silt Density Index 5 SDI Minimum Concentrate Flow Rate 5 1 Chlorine Tolerance O ppm pH Range Continuous Operation 2 11 Product Specifications Applied Permeate Nominal Sali Part Applied Permeale Nominal Salt Number Part Number Description Pressure Flow Rate eden psi bar gpd m3 d Description Pressure Flow Rate Rejection psi bar gpd m3 d Test Parameters 550 TDS Filte
34. n the tank is full Liquid level switches can be obtained by your local dealer or distributor If a liquid level switch is to be used install it at this time PRE FILTRATION DT Series systems supplied with a 10 Micron FSI Bag Filter and a 4 5 x 20 5 Micron polypropylene sediment filter Change the cartridge once a month or when a 10 15 psi differential exists between the pre filter Ask your local dealer or distributor about Pre Filtration systems if required NOTE THE SYSTEM MUST BE OPERATED ON FILTERED WATER ONLY PUMP The pump type used on the DT Series systems are multi stage centrifugal carbon steel pumps These pumps are also available as an option in stainless steel Follow these guidelines to ensure proper operation of the pump e The pump must NEVER be run dry Operating the pump without sufficient feed water will damage the pump e ALWAYS feed the pump with filtered water The pump is susceptible to damage from sediment and debris ENGF 108 REV A 01 11 2011 AXEON Water Technologies e If any damage occurs to your system s pump a re build kit may be available Contact your local dealer or distributor and inform them of your system s model and pump size MOUNTING The free standing system should be bolted down in compliance with local regulation standards or securely fastened MEMBRANE ELEMENTS DT Series reverse osmosis systems come pre loaded with Thin Film Composite TFC HF1 High Flow Low Energy
35. nd useful The information and data are offered in good faith but without guarantee as conditions and methods of use of products are beyond the manufacturer s control The manufacturer assumes no liability for results obtained or damages incurred through the application of the presented information and data II is the user s responsibility to determine the appropriateness of these products for the user s specific end uses 800 320 4074 760 723 5417 W www axeonwater com 760 728 5062 E sales axeonwater com 541 Industrial Way Suite 1 Fallbrook 92028 WATER TECHNOLOGIES AXEON is a registered trademark of Water Technologies 01 11 22011 AXEON Water Technologies 10 ENGF 108 REV A 01 11 2011 AXEON Water Technologies HF4 OPTIONAL AXEON Series Reverse Osmosis Membrane Elements AXEON HF4 Membrane Elements are one of the industries most reliable and highest performing reverse osmosis elements AXEON membranes are available in all standard commercial sizes and feature a protective ABS shell Advanced membrane technology and manufacturing processes ensure high quality and performance allowing for improved system performance All elements are shipped dry for an extended shelf life and easier handling Membrane elements are 100 vacuum integrity tested and may also be ordered as individually wet tested Operating Limits Membrane Polyamide Thin Film
36. ons have been provided or stated otherwise The amount of permeate water recovered for use is expressed as a percentage To calculate recovery use the following formula Recovery Product Water Flow Rate Feed Water Flow Rate x 100 Example 46 6 94 15 x 100 A NOTE ALL FLOW RATES MUST BE EXPRESSED IN THE SAME UNITS TYPICALLY GALLONS PER MINUTE GPM SYSTEM REQUIREMENTS amp OPERATION GUIDELINES PLUMBING The membranes and high pressure pumps used on DT Series systems require a continuous flow of water with a minimum feed pressure of 35 psi not to exceed 105 F FEED WATER CONNECTION 1 Locate the 2 FNPT feed water inlet on the 18 FSI bag filter housing Figure 1A Page 14 2 Attach the inlet piping to the 2 FNPT feed water inlet 3 Be certain that all of the components of the feed water are soluble at the concentrations attained in the system ENGF 108 REV A 01 11 2011 AXEON Water Technologies NOTE FEED LINE MUST BE MINIMUM 1 INCH PERMEATE PRODUCT WATER CONNECTION Locate the 1 connection labeled permeate and attach to storage tank Ensure that the permeate water can flow freely with no backpressure Backpressure can cause irreversible damage to the membrane elements The 1 permeate line can be run to the holding tank with PVC fittings or other FDA approved materials This is so the material being used does not dissolve into the permeate water A CAUTION THE PH OF THE REV
37. red 5 Micron De Chlorinated Softened City Feed Water 77 Degrees F 15 Permeate Recovery 6 5 7 0 pH Range at the Specified Operating Pressure Data Taken After 30 Minutes of Operation Maximum Pressure drop for each element is 10 psi Minimum salt rejection is 96 Permeate flow for individual elements may vary 20 Dimensions inch mm Description B c D Description Hs 111790 TE 11754 aon 2164 1184 0751008 3951009 ees penes Tsa 075009 Lee 114 sta 395103 Under certain conditions the presence of free chlorine and other oxidizing agents will cause premature membrane failure Since oxidation damage is not covered under warranty the manufacturer recommends removing residual free chlorine by pretreatment prior to membrane exposure Wet tested membrane elements must be kept sealed and moist when in storage Drying out may occur and damage the membrane permanently Prevent elements from freezing or being exposed to direct sunlight Wet tested elements are vacuum sealed in a polyethylene bag containing 1 0 sodium mete bisulfite and then packaged in a cardboard box Discard the permeate for the first hwenty four hours of operation The permeate flow product water flow varies with feed water lemperature For membrane warranty information please contact the manufacturer The manufacturer believes the information and data contained herein to be accurate a
38. rtain conditions the presence of free chlorine and other oxidizing agents will cause premature membrane failure Since oxidation damage is not covered under warranty the manufacturer recommends removing residual free chlorine by pretreatment prior to membrane exposure Wet tested membrane elements must be kept sealed and moist when in storage Drying out may occur and damage the membrane permanently Prevent elements from freezing or being exposed to direct sunlight Wet tested elements are vacuum sealed in a polyethylene bag containing 1 0 sodium met bisulfite and then packaged in a cardboard box Discard the permeate for the first twenty four hours of operation The permeate flow product water flow varies with feed water temperature For membrane warranty information please contact the manufacturer The manufacturer believes the information and data contained herein to be accurate and useful The information and data are offered in good faith but without guarantee as conditions and methods of use of products are beyond the manufacturer s control The manufacturer assumes no liability for results obtained or damages incurred through the application of the presented information and data It is the user s responsibility to determine the appropriateness of these products for the user s specific end uses Ru i Y AXEO P 800 320 4074 760 723 5417 W www axeonwater com 760 728 5062 E sales axeonwater com 541 Industrial Way Suite 1
39. ssel being filled 2 Separate the preservation solution from the air outside by closing all valves Any contact with oxygen will oxidize the Memstor 3 Check the pH once a week When the pH becomes 3 or lower change the preservation solution 4 Repeat this process at least once a month During the shutdown period the plant must be kept frost free or the temperature must not exceed 113 F 45 C Preparing unit for shipment 32 ENGF 108 REV A 01 11 2011 AXEON Water Technologies 5 Disconnect the inlet concentrate pre filter and permeate plumbing 6 Drain all water from the pre filter cartridge housings by unscrewing the housings removing the pre filter cartridges and drain the water from the housings 7 Disconnect the tubing from the connectors on the permeate and concentrate inlets and outlets 8 Fully open the concentrate valve 9 Drain the flow meters 10 Allow the system to drain for a minimum eight hours or until the opened ports quit dripping 11 After draining is complete reconnect all of the plumbing 33 ENGF 108 REV A 01 11 2011 AXEON Water Technologies REVERSE OSMOSIS TROUBLESHOOTING SYMPTOMS POSSIBLE CAUSES CORRECTIVE ACTION Low Inlet Pressure Low supply pressure Increase Inlet Pressure Cartridge filters plugged Change Filters Solenoid valve malfunction Replace Sol Valve and or Coil Motor may not be drawing correct current Use clamp on
40. ssure is 30 psi or below PERMEATE PRODUCT FLOW METER amp CONCENTRATE WASTE FLOW METER These flow meters indicate the flow rates of the permeate and concentrate water The measurements when added together also indicate the feed water flow rate or total flow rate if the system is not equipped with a concentrate recycle valve A CAUTION EXCESSIVE RECYCLING MAY CAUSE PREMATURE FOULING OR SCALING OF THE MEMBRANE ELEMENTS LOW PRESSURE SWITCH The low pressure switch shuts off the system when the feed water pressure drops below 15 PSI preventing damage to the pump The system restarts automatically when there is a constant pressure of 35 PSI or more A If you notice the pressure fluctuating and the system cycling off and on turn the system off and ensure that proper feed flow and pressure are available to the system PUMP THROTTLE VALVE This valve is installed as a standard feature on the DT Series reverse osmosis systems It provides an adjustment for pump pressure which will vary as the required system pressure changes As the feed water temperature decreases and or the feed water TDS increases the system will require a higher operating pressure to produce the specified permeate flow DT system installed in Florida may provide the specified permeate flow of 6 94 gpm at 100 psi however the same system installed in Maine much colder feed water may require 150 psi to produce the same amount of permeate Never exceed
41. thout guarantee as conditions and methods of use of products are beyond the manufacturer s control The manufacturer assumes no liability for results obtained or damages incurred through the application of the presented information and dota It is the user s responsibility to determine the appropriateness of these products for the user s specific end uses AXEO 800 320 4074 760 723 5417 W www axeonwater com 760 728 5062 E sales axeonwater com 541 Industrial Way Suite 1 Fallbrook CA 92028 WATER TECHNOLOGIES AXEON is a registered trademark of AXEON Water Technologies 01 11 2011 AXEON Water Technologies 12 ENGF 108 REV A 01 11 2011 AXEON Water Technologies NF3 OPTIONAL AXEON NF3 Series Reverse Osmosis Membrane Elements AXEON NF3 Membrane Elements are one of the industries most reliable and highest performing nanofiltration elements AXEON membranes are available in all standard commercial sizes and feature a protective ABS shell Advanced membrane technology and manufacturing processes ensure high guality and performance allowing for improved system performance All elements are shipped dry for an extended shelf life and easier handling Membrane elements are 100 vacuum integrity tested and may also be ordered as individually wet tested Operating Limits Membrane Type Polyamide Thin Film pH Range Short Term Cleaning 30 Min 1 13 Maximum Operating Temperature 11
42. trial Way Suite 1 Fallbrook CA 92028 WATER TECHNOLOGIES AXEON is a registered trademark of AXEON Water Technologies 01 11 2011 AXEON Water Technologies 11 ENGF 108 REV 01 11 2011 AXEON Water Technologies HF5 OPTIONAL AXEON HF5 Series Reverse Osmosis Membrane Elements AXEON HF5 Membrane Elements are the only element on the market that operates at a pressure of 80 psi meaning more energy savings membranes are available in all standard 4 inch commercial sizes and feature a protective tape wound exterior HF5 Membrane Elements are the best choice to counter the negative effects of cold temperatures on reverse osmosis production All elements are shipped dry for an extended shelf life and easier handling Membrane elements are 100 vacuum integrity tested and may also be ordered as individually wet tested Operating Limits Membrane Type Polyamide Thin Film pH Range Short Term Cleaning 30 Min 1 13 Maximum Operating Temperature 113 F 45 C Maximum Feed Water Turbidity 1 NTU Maximum Operating Pressure 400 psi 27 58 bar Maximum Feed Silt Density Index 5 SDI Minimum Concentrate Flow Rate 5 1 Chlorine Tolerance ppm pH Range Continuous Operation 2 1 Product Specifications m Applied Permeate Nominal Salt ar Number Description Pressure Flow Rate Rejection psi bar gpd m3 d Test Parameters 550 TDS Filtered 5 Micron De Chlorinated Softened C
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