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        Emerson Type 1290 Vapor Recovery Regulator Data Sheet
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1.      Steel    Stainless Steel                              Vent Assembly  Select One   O Spring Case Up  Type Y602 11      O Spring Case Down  Type Y602 1                    Parts Kits    Replacement Parts Kit  Optional   O Yes  send one replacement parts kit to match this  order for each unit     Quick Change Trim Package  Optional   Yes  send one main valve Quick Change Trim  Package to match this order                 Wireless Position Monitor Mounting Kit  Optional   Yes  send one mounting kit for mounting the  Topworx    4310 or the Fisher   4320 wireless  position monitor                 Specification Worksheet    Application Specifications   Tank Size  Pump In Rate   Pump Out Rate  Blanketing Gas  Type and Specific Gravity           Pressure Requirements  Please Designate Units    Maximum Inlet Pressure  Pimax    Minimum Inlet Pressure  D    Control Pressure Setting  P3    Maximum Flow IO               Accuracy Requirements   0 25 inch w c    0 60 mbar  1 inch w c    2 mbar   L Other    Other Specifications   Is a vapor recovery regulator required  O Yes No  Special Material Requirements  L Ductile Iron L Steel    Stainless Steel Hastelloy   C Other  Other Requirements           0 5 inch w c    1 mbar  2 inches w c    5 mbar                                                                                                    Bulletin 74 2 1290    Industrial Regulators    Emerson Process Management  Regulator Technologies  Inc     USA   Headquarters   McKinney  Texas 75069
2.    where     C    gas sizing coefficient from Table 5    g    C    C C  or 35 from Table 5    G   gas specific gravity  air   1 0   P    absolute inlet pressure  psia  add 14 7 psi  to gauge inlet pressure to obtain absolute  inlet pressure   Q   flow rate  SCFH  T   absolute temperature in   R of gas at inlet       F   460        Bulletin 74 2 1290    Table 8  Materials Compatibility  continued        FLUID INFORMATION          Fluid    Acetic Acid  30    Acetone   Alcohol  Ethyl   Alcohol  Methyl   Ammonia  Anhydrous     Material  a Fluorocarbon Perfluorelastomer Ethylenepropylene  Neoprene  CR  Nitrile  NBR   FKM   FFKM  y  EPDM        Ammonia  Gas  Hot   Benzene   Brine  Calcium Chloride   Butadiene Gas   Butane  Gas    Butane  Liquid        Carbon Tetrachloride  Chlorine  Dry   Chlorine  Wet    Coke Oven Gas  Ethyl Acetate       Ethylene Glycol  Freon 11   Freon 12  Freon 22  Freon 114       Gasoline   Hydrogen Gas  Hydrogen Sulfide  Dry   Hydrogen Sulfide  Wet   Jet Fuel  JP 4        Natural Gas   Natural Gas   H S  Sour Gas   Nitric Acid  20     Nitric Acid  50 to 100    Nitrogen    Oil  Fuel    Propane   Sulfur Dioxide   Sulfuric Acid  to 50    Sulfuric Acid  50 to 100            Water  Ambient   Water  at 200  F   93  C   Water  Sea           orolmtmtmolsomtszlomssmoliskEozxloooooimpzsmorzomlzsfrzmo    mroiootkflzoomblzootsfitottktklomgooolrfosooiottom    FF DESFPONOO FONAN OIF SSSO SFSEWDOFSIDONQNIANINNQANSOD SESPSS          D gt  gt  rrrrrl rrrorlrandoryr vou    Oo
3.   Cast Iron  or   CL600 RF i 3  BODY SIZE D G Stainless Stainless  CL150 RF CL300 RF Steel or  NPT s Cast Iron Steel or Cast Iron Steel or  Steel or Steel Stainless Steel Steel  Stainless   or Stainless Steel  Steel Steel  NPS DN Inch   mm   Inch   mm   Inch   mm   Inch   mm   Inch   mm   Inch   mm   Inch   mm   Inch   mm   Inch   mm   Inch   mm  1 25 8 25   210   7 25   184   7 75   197   8 25   210   3 88   99   8 62   219  12 00  305  10 50  267   3 00   76   2 44   62  2 50 11 25  286  10 00   254  10 50  267  11 25  286   4 56   116   9 12   232   13 31  338   11 81  300   3 12   79   3 12   79  3 80            11 75  298  12 50  317   13 25  337   5 31   135  11 25  286   16 50  419   14 00  356   3 88   99   3 88   99  4 100            13 88  353   14 50  368  15 50  394   6 50   165   12 62  321   19 12  486   16 88  429   5 12   130   5 12   130  6 150           17 75  451   18 62  473   20 00  580   7 25   184   13 69  348   20 44  519   19 19  487   6 38   162   6 62   168  8x6   200 x 150              21 40  544   22 40  569  24 00  610   9 76   248   15 02  382   20 25  514   23 25  591   6 62   168   6 62   168  12 x 6  300 x 150               29 00  737   30 50  775  32 25  819   9 76   248   15 02  382               23 25  591              6 62   168                                                                   Bulletin 74 2 1290    Ordering Guide    Construction  Select One   O Standard  O NACE                Type EGR Main Valve    Main Valve Body Size  S
4.  0 11 050 11 630 316 332 35 0  300 x 150 2   S        PIPING STYLE  2 1 Line Size to Body Size Piping  BODY SIZE  S 7 7 S  NPS  DN Standard Linear Cage Drilled Hole Whisper Trim Cage  C  C C  C  C  C  Km  Regulating   Wide Open   Regulating  Wide Open Regulating   Wide Open   Regulating   Wide Open  1 25 568 598 17 2 18 1 33 0 529 557 15 6 16 4 34 0  2 50 2050 2160 59 6 62 8 34 4 1830 1930 52 3 55 1 35 1  3 80 4410 4650 128 135 34 4 3630 3830 106 110 34 2  41100 6940 7310 198 209 35 0 6020 6340 171 180 35 2  6 150 12 100 12 800 381 404 31 7 9240 9730 291 306 31 7 0 80  8x6   200 x 150 17 370 18 280 543 571 32 0 10 020 10 550 286 301 35 0  12x6 19 900 20 950 622 655 32 0 10 380 10 930 297 312 35 0  300 x 150  Table 6  Flow Rate Conversions  Gas Flow Required to Displace Blanketing Gas with Pump in of Liquid   MULTIPLY MAXIMUM PUMP RATE IN TO OBTAIN    SCFH air required           2  To convert to Nm     h  multiply SCFH by 0 0268        1  For liquids with a flash point below 100  F   38  C or normal boiling point below 300  F   149  C  multiply the above calculated outbreathing requirement by 2 0        Note    The Type 1290 Vapor Recovery Regulator  is not intended to be used as an ASME  certified relief device for overpressure  protection  It is to be used as part of   the gas blanketing system to control the  outflow of blanketing gas under normal  conditions and to collect vessel vapors  for the vapor recovery system  You  should provide alternate methods of  emergency ove
5.  11 5 0 79 11 0 76 10 0 69 9 0 62 8 5 0 59 Light Blue  12 5   0 86 12   0 83 11 0 76 10   0 69 10 5   0 72 Black          Table 4  Flow Capacities for Type 1290 Vapor Recovery Regulators       BUILDUP OVER    CAPACITIES IN SCFH   Nm  h OF 0 97 SPECIFIC GRAVITY NITROGEN                                                             nor   PILOT   contROL CONTROL    DOWNSTREAM  Type   SPRING   PRESSURE   PRESSURE TO VACUUM NPS 1   DN 25   NPS 2   DN 50   NPS 3   DN 80   NPS AT DN 100  NPS 6   DN 150  COLOR WIDE OPEN    PRESSURE Body Body Body Body Body  Greter Eege lew Palo bar 600   16 1 2300 61 6   4900 131 7600 204   14 600 391   Y291AL  Black a ae 0 80 mbar   22 PSig  0 17 bar  5600 150   19 900 533   43 100   1155   66 900   1793   124 500   3337     5 psig 0 34 bar   7300 196   25 800 691   55 700  1493   86 700  2324   160 600   4304   EEN E oO psig  Ober 700   18 8 2700 72 4   5900 158 9200 247   17 700 474   eri 0 80 mbar   22 PSig  0 17 bar  5700 153   10 000  268   43 200   1158   67 000  1796   126 700   3396   SS 5 psig 0 34 bar   7400 198   25 900 694   55 800  1495   86 800   2326   160 800   4309   S 2inches w c      0 25 inch w c      _ 2 belo bar 1100   29 5 3900   105 8400 225   13 000 348   25 000  670   Ste 0 60 mbar   25psig 0 17 ber  5800 155   20 200 541   43 500  1166   67 600   1812   127 700   3422   5 psig 0 34 bar   7400 198   26 000 697   56 000  1501   87 200   2337   161 500   4328   DREES 1500   40 2 5300 142   11 500 308   17 800 477   34 200 917  
6.  1872  USA  Tel   1 800 558 5853   Outside U S   1 972 548 3574    Asia Pacific  Shanghai 201206  China  Tel   86 21 2892 9000    Europe  Bologna 40013  Italy  Tel   39 051 419 0611    Middle East and Africa  Dubai  United Arab Emirates  Tel   971 4811 8100    For further information visit www fisherregulators com    Natural Gas Technologies    Emerson Process Management  Regulator Technologies  Inc     USA   Headquarters   McKinney  Texas 75069 1872  USA  Tel   1 800 558 5853   Outside U S   1 972 548 3574    Asia Pacific  Singapore 128461  Singapore  Tel   65 6770 8337    Europe   Bologna 40013  Italy  Tel   39 051 419 0611  Chartres 28008  France  Tel   33 2 37 33 47 00    TESCOM    Emerson Process Management  Tescom Corporation    USA   Headquarters  Elk River  Minnesota 55330 2445  USA  Tels   1 763 241 3238    1 800 447 1250    Europe  Selmsdorf 23923  Germany  Tel   49 38823 31 287    Asia Pacific  Shanghai 201206  China  Tel   86 21 2892 9499    The Emerson logo is a trademark and service mark of Emerson Electric Co  All other marks are the property of their prospective owners  Fisher is a mark owned by Fisher Controls International LLC     a business of Emerson Process Management     The contents of this publication are presented for informational purposes only  and while every effort has been made to ensure their accuracy  they are not to be construed as warranties or  guarantees  express or implied  regarding the products or services described herein or their use o
7.  SFEPPSY WEOyryrliryrrron  ekKKKAE KK KKH Ke KK erte ar be Ke e OK KKK KK KKH KK KKK KKK ed  ODFkFrrIOkFFDIkFFODOIODOO OD FOI FD ODIOOODkObtFkOO    OFF FlIFODDFIOObtFIm ti bFFFOlIkOm DIS    Hydrochloric Acid  Aerated                          DStbtklbktrFklbbbFbIbIkbbIbbbFbibbFFbIbbFFbIbbFFFl Hastelloy   CH                            Chromic Acid Sulfuric Acid  Aerated    Citric Acid l Sulfuric Acid  Air Free    Coke Oven Gas Sulfurous Acid   Copper Sulfate Trichloroethylene   Ether Water  Boiler Feed    Ethyl Chloride Water  Distilled    Ethylene Water  Sea    Ethylene Glycol l Zinc Chloride   Formaldehyde Zinc Sulfate   Formic Acid l        Freon  Wet  l                     Freon  Dry  l             Gasoline  Refined                      Glucose                          1  Monel  is a mark owned by Special Metals Corporation   2  Hastelloy   C is a mark owned by Haynes International  Inc        A   Best possible selection  A  Recommended    B  Minor to moderate effect  Proceed with caution     C  Unsatisfactory  L L   Information lacking         continued       at 0  C and 1 01325 bar  of 0 97 specific gravity  nitrogen  For gases of other specific gravities  multiply  the given capacity of nitrogen by 0 985  and divide by  the square root of the appropriate specific gravity of  the gas required  To determine regulating capacities  at pressure settings not given or to determine  wide open flow capacities  use the following formula     Q   520    3417  AP  GT Gran C  VP  pee 
8.  age 0 60 mbar   22 PSig 0 17 bar  5800 155   20 500 549   44 100  1182   68 500   1836   129 400   3468   5 psig  0 34 bar   7500 201   26 300 705   56 600  1517   88 100  2361   162 200   4347   lee fil 2 PSI9 0 bar 2100 56 3   7400 198   16 000 429   24 800 665   47 600  1276   Unpainted 1  o mbar 0 60 mbar   22 PSig  0 17 bar  6000 161   21 000 563   45 300  1214   70 400   1887   132 800   3559      5 psig   0 34 bar   7600 204   26 800 718   57 700  1546   89 800   2407   166 200   4454   Ban Geo ewe eebe  b pein Ee 2900 77 7   10 100 271   21 800 584   33 800 906   64 900  1739  E 0 80 mbar   128 PSig  0 17 bar  6300 169   22 000 590   47 400   1270   73 600  1972   138 700   3717   5 psig   0 34 bar   7900 212   27 800 745   59 800  1603   93 100  2495   172 400   4620   ES 0 05 psig   0 psig   0 bar 4000 107   14 100 378   30 500 817   47 200 1265   90 300   2420   Yellow darbar E 2 5 psig 0 17 bar  6800 182   23 900 641   51 400 1378   79 900 2141   150 100   4023   5 psig 0 34 bar   8100 217   28 700 769   61 800  1656   96 200   2578   177 200   4749   See 0 15 psig   0 psig   0 bar 7000 188   24 700 662   53 200 1426   82 500 2211   155 800 4175   fod ha Ae 2 5 psig  0 17 ber  8700 233   30 600  820   66 000  1769   102 700   2752   190 700   5111   ear   5 psig  0 34 bar   9600 257   34 100 914   73 400  1967   114 600   3071   209 100   5604   a 5 psig   0 15 psig   0 psig   0 bar 9100 244   31 900 855   68 600   1838   106 700   2860   199 500   5347   GE tes 
9. 1AL Pilot    Body  Spring Case Assembly  and Diaphragm  Casing Material  Select One    O Ductile lron      O Stainless Steel                   Control Pressure Range  Select One     Type Y291AL  0 5 to 1 5 inches w c    1 to 4 mbar  Black       Type Y291A   1 0 to 2 5 inches w c    2 to 6 mbar  Orange      2 to 7 inches w c    5 to 17 mbar  Red      4 to 14 inches w c    10 to 35 mbar  Unpainted     12 to 28 inches w c    30 to 70 mbar  Yellow      1 to 2 5 psig   0 07 to 0 17 bar  Green      2 5 to 4 5 psig   0 17 to 0 31 bar  Light Blue     4 5 to 7 psig   0 31 to 0 48 bar  Black       Diaphragm Material  Select One    O Nitrile  NBR       O Fluorocarbon  FKM      O Nitrile  NBR  with Polytetrafluoroethylene  PTFE   diaphragm protector                                                                     O ring and Seal Material  Select One   Nitrile  NBR       Fluorocarbon  FKM     Ethylenepropylene  EPDM     Perfluoroelastomer  FFKM                                       Regulators Quick Order Guide  Readily Available for Shipment       7  Allow Additional Time for Shipment       BR Special Order  Constructed from Non Stocked Parts   Consult Your local Sales Office for Availability           Availability of the product being ordered is determined by the component with the  longest shipping time for the requested construction           Bulletin 74 2 1290    Type Y291A or Y291AL Pilot  continued     Closing Cap Material  Select One   Type Y291AL   Zinc   Type Y291A   Plastic  
10. 2 5 psig   0 17 bar  10 200 273   36 300 973   78 100  2093   121 600   3259   224 000   6003   5 psig   0 34 bar   _11 000 295   39 000   1045   83 900   2249   131 000   3511   327 400   8774   7 psig   0 20 psig   Opsig Obar   10 800 289   38 200   1024   82 200   2203   127 900   3428   237 100   6354   Black E ER 2 5 psig 0 17 bar  11 700 314   41 600 1115   89 500   2399   139 700   3744   255 300   6842   5 psig   0 34 bar  _12 300 330   43 800   1174   94 200   2525   147 300   3948   265 100   7105          1  Increased capacity is available at higher buildups           Table 5  Flow Coefficients    Bulletin 74 2 1290                                                                                                                                                                            U S  GPM  U S  GPH  Barrels hour  Barrels day       0 1337    0 2340    PIPING STYLE  Line Size Equals Body Size Piping  BODY SIZE  P F A reas  NPS  DN Linear Cage Drilled Hole Whisper Trim    Cage  C  C  Cy C   C  C  Kn  Regulating   Wide Open   Regulating  Wide Open Regulating   Wide Open   Regulating   Wide Open  1 25 600 632 16 8 17 7 35 7 576 607 16 7 17 6 34 5  2 50 2280 2400 63 3 66 7 36 0 1970 2080 54 7 57 8 36 0  3 80 4630 4880 132 139 35 1 3760 3960 107 113 35 0  4 100 7320 7710 202 213 36 2 6280 6610 180 190 34 8  6 150 12 900 13 600 397 418 32 5 9450 9950 295 310 32 0 0 80  8x6   200 x 150 18 480 19 450 578 608 32 0 10 660 11 220 305 321 35 0  12  6 21 180 22 290 662 697 32
11. 7022   0 25 inch w c    0 60 mbar 0 100 2 70 3 75 95 0   Y291A 12 to 28 inches w c    30 to 70 mbar Yellow 1B537027052 1 4 inch w c    3 mbar 0 114 2 90 4 31 109  1 0 to 2 5 psig   0 07 to 0 17 bar Green 1B537127022 2 8 inch w c    7 mbar 0 156 4 00 4 06 103   2 5 to 4 5 psig   0 17 to 0 31 bar Light blue   1B537227022 4 2 inch w c    10 mbar 0 187 4 80 3 94 100   4 5 to 7 psig   0 31 to 0 48 bar Black 1B537327052 5 5 inch w c    14 mbar 0 218 5 40 3 98 101   1  Spring ranges based on pilot being installed with the spring case pointed down   2  Do not use Fluorocarbon  FKM  diaphragm with this spring at diaphragm temperatures lower than 60  F   16  C   3  When using a Fluorocarbon  FKM  diaphragm  the minimum outlet pressure is 2 inches w c    5 mbar   4  When using a Fluorocarbon  FKM  diaphragm  the minimum outlet pressure is 2 5 inches w c    6 mbar           Table 3 Maximum Main Valve Inlet Pressures                                                       MAXIMUM INLET PRESSURES  psig   bar  PILOT TYPE Type 1098 EGR Main Valve with Green Spring SPRING COLOR  NPS 6  8 x 6  or 12 x 6   NPS 1  DN 25 NPS 2 7 DN 50 NPS 3  DN 80 NPS 4  DN 100 DN 150  200 x 150  or 300 x 150   Y291AL 5 5   0 38 5 0 35 4 0 28 3 0 21 3 5   0 24 Black  5 5   0 38 5 0 35 4 0 28 3 0 21 3 5   0 24 Orange  5 5   0 38 5 0 35 4 0 28 3 0 21 3 5   0 24 Red  6 5   0 45 6 0 41 5 0 35 4 0 28 4 5 0 31 Unpainted   Y291A 7 5 0 52 7 0 48 6 0 41 5 0 35 4 5 0 31 Yellow  8 5 0 59 8 0 55 7 0 48 6 0 41 5 5   0 38 Green 
12. AL 8 psig   0 55 bar 13 psig   0 90 bar Black  8 psig   0 55 bar 13 psig   0 90 bar Orange  8 psig   0 55 bar 13 psig   0 90 bar Red  9 psig   0 62 bar 14 psig   0 97 bar Unpainted  Y291A 10 psig   0 69 bar 14 psig   0 97 bar Yellow  11 psig   0 76 bar 15 psig   1 0 bar Green  14 psig   0 97 bar 18 psig   1 2 bar Light blue  15 psig   1 0 bar 20 psig   1 4 bar Black                Type Y291A or Y291AL Pilot Orifice Diameter  3 8 inch   9 5 mm    Flow Capacities  See Table 4       Flow Coefficients  See Table 5    Control Line Connection  1 2 NPT    Exhaust Line Connection  3 4 NPT    Supply Pressure and Spring Case Connections  1 4 NPT    Orifice Diameters and Travels             BODY SIZE PORT DIAMETER TRAVEL  NPS DN Inch mm Inch mm  1 25 1 5 16 33 3 4 19  2 50 2 3 8 60 1 1 8 29  3 80 3 3 8 86 1 1 2 38  4 100 4 3 8 111 2 51  6 150 7 3 16 183 2 51  8x6 200 x 150 7 3 16 183 2 51  12x6 300 x 150 7 3 16 183 2 51                      Material Temperature Capabilities   Nitrile  NBR     20 to 180  F    29 to 82  C  Fluorocarbon  FKM    For Inches w c  Setpoints  40 to 300  F   4 to 149  C  For psig Setpoints  0 to 300  F    18 to 149  C  Ethylenepropylene  EPDM     20 to 275  F    29 to 135  C  Perfluoroelastomer  FFKM     20 to 300  F    29 to 149  C    Approximate Weights  NPS 1   DN 25  85 pounds   39 kg  NPS 2 7 DN 50  100 pounds   45 kg  NPS 3  DN 80  145 pounds   66 kg  NPS 4 7 DN 100  195 pounds   88 kg  NPS 6  DN 150  380 pounds   172 kg  NPS 8 x 6  DN 200 x 150  740 pound
13. Bulletin 74 2 1290    May 2013    Type 1290 Vapor Recovery Regulator       Figure 1  Type 1290 Vapor Recovery Valve    Features    Quick Change Trim Package     Tested trim  packages can be ordered and stocked ahead of time  for fast replacement     Easy In Line Maintenance     Top entry design  reduces maintenance time and manpower  requirements  trim parts can be inspected  cleaned     and replaced without removing the body from the line     In Service Travel Inspection     Standard travel  indicator assembly with protective cover permits  periodic inspection of plug travel without removing  regulator from service     High Accuracy     Total proportional band of  0 25 inch w c    0 62 mbar or less at lower  set pressures     Proven Technology     Time proven regulator  technology has been adapted to meet the  specific requirements of vapor recovery   depadding  applications     www fisherregulators com    Introduction    The Type 1290 vapor recovery regulator controls vessel  blanketing gas pressure when the vessel is being filled  with fluid or when ambient temperature causes the vapor  gas to expand  The system monitors the increasing  blanket pressure and throttles open to pass excess  blanketing gas into a vapor disposal or reclamation system  thus controlling the desired set pressure of the vessel     The vapor recovery regulator is not intended to   be used as anASME certified relief device for  overpressure protection  It is to be used as part of  the gas blanketing 
14. Sizing Problem for Vapor  Recovery Applications     E Prasat bea elas a Ieee 1000 barrels  Pumpin Capacity                   20 GPM  75 7 Ipm  Inlet Pressure Source 60 psig   4 1 bar nitrogen  Desired Blanket Setpoint         0 5 inch w c    1 mbar  Desired Vapor Recovery Setpoint      2 inches w c   5 mbar  Vapor Recovery Vacuum Source    5 inches Hg  169 mbar  FIUIG bike bi ne edo Eet shoe Alaaa Hexane  Boiling Point 155  F   68  C    Vessel Capacity    1  From Table 6 the desired air flow rate due to  pump in equals 20 GPM x 8 021 x 2   320 SCFH   8 58 Nm  h air     From Table 7 the desired air flow rate   1000 SCFH    26 8 Nm  h air due to thermal heating     Total required flow rate   1000 SCFH air     320 SCFH   1320 SCFH   35 4 Nm  V h air  This  converts to nitrogen requirements of 1340 SCFH    35 9 Nm h     Capacity Information    Table 4 gives typical nitrogen regulating capacities at  selected inlet pressures and outlet pressure settings   Flows are in SCFH  at 60  F and 14 7 psia  and Nm  h    Table 8  Materials Compatibility    Bulletin 74 2 1290       CORROSION INFORMATION       Material     o  o  oO o  g _ 5 SE be 3    Fluid a   OF ol sw lal    amp   eoj  8  oY 1 5 8  KG  ES IS   s a a   so  2  o 13s Slsg  lecl     2 CINE        O Slo El E lo    8 alez 63 5  bi GI     Acetic Acid  Air Free   Acetic Acid Vapors  Acetone   Acetylene   Alcohols    Aluminum Sulfate  Ammonia  Ammonium Chloride  Ammonium Nitrate  Ammonium Sulfate    Fluid    Hydrochloric Acid  Air Fr
15. e Spring Range  Select One        60 psig   4 1 bar maximum drop  Green         Main Valve Spring       Steel     Inconel   X 750  NACE                   O ring and Seal Material  Select One        Nitrile  NBR      Fluorocarbon  FKM     Ethylenepropylene  EPDM     Perflouroelastomer  FFKM                                Type 1098 Actuator    Lower Diaphragm Case Material  Select One        Steel     Stainless Steel               Bonnet Material  Select One        Steel     Stainless Steel               O ring Material  Select One        Nitrile  NBR      Fluorocarbon  FKM     Ethylenepropylene  EPDM                 kk       Diaphragm Material  Select One        O Nitrile  NBR      O Fluorocarbon  FKM     O Ethylenepropylene  EPDM                   Type 95H Supply Pressure Regulator  Body Material  Select One        kkk    Cast Iron  Steel     Stainless Steel                      Spring Case Material  Select One        kkk    Cast Iron  Steel     Stainless Steel                      Valve Plug Material  Select One        O 416 Stainless Steel with Nitrile  NBR       O 416 Stainless Steel with Fluorocarbon  FKM      O 316 Stainless Steel with Neoprene  CR   NACE     O 316 Stainless Steel with Fluorocarbon  FKM                      Ordering Guide  continued     Type 95H  continued     Outlet Pressure Range  Select One   15 to 30 psig   1 0 to 2 1 bar  Yellow       Diaphragm Material  Select One   Neoprene  CR      Fluorocarbon  FKM                               Type Y291A or Y29
16. ee   Hydrogen   Hydrogen Peroxide  Hydrogen Sulfide  Liquid   Magnesium Hydroxide    Methanol   Methyl Ethyl Ketone  Natural Gas   Nitric Acid   Petroleum Oils  Refined        Material     o Olu  o  3 Sls S2    gt   AENEAM  so    ELE   clg 2   Sa     S o  L  2 eB  aL S2IHGD  e  Zoe D Elie    5 a     S  o8 s  bi Kik       Ammonium Sulfite    Phosphoric Acid  Air Free        Calcium Chloride  Alkaline   Carbon Dioxide  Dry   Carbon Dioxide  Wet   Carbon Disulfide    Sodium Acetate  Sodium Carbonate  Sodium Chloride  Sodium Chromate    Beer Phosphoric Acid Vapors    Benzene  Benzol  Potassium Chloride   Benzoic Acid Potassium Hydroxide   Boric Acid Propane   Butane Silver Nitrate       Carbon Tetrachloride  Carbonic Acid  Chlorine Gas  Dry   Chlorine Gas  Wet   Chlorine  Liquid     Sodium Hydroxide  Stearic Acid   Sulfur   Sulfur Dioxide  Dry   Sulfur Trioxide  Dry           OO FIDDOOOltttttikOkFOlItOOOOikOtttzitOOr SO       OODFIODNINO  SYSPPOFI FOFYPO  SFUDOO FOSFSPY SFOYFFPrO     POWDYFIFWODOO SFSEPSYSISFWOSrPwoYr Srrrwar rrrrr rrrro   POWDFSF SFPWDOO  SFSPYESYS FOFTryr  rworrr rworrr   gt rrrroa     DONONDIDWDNONOAON WBSFUWVOAD FWOODSrTD FWDNNAO FOFYKrYKrI FOWFO     POFYP SFPOWDO  FSFSEPOFISFrSrSTO  SFPWDOBD FOSPYrHr FOrFrOA    vr SFFFlbbkbFlkbFbFFlkFbFFlbbktr lb kFFlb FD FD Hastelloy   C        OFFOUD FWDSFSFO  WOFSFLOINNOSFOD SFOSDFIONONSFDO ONOSOSFO  SSSPOIO  OFPFWDINODFSPO DWOFIONONO NINDFSFOND FOFDFINIFWOINQINQNFO  SYSEYPIO  OFrFEFWIDSEYSFSYSIFWOSFWDO NONOWDAD SSESPOYVP
17. elect One   NPS 1   DN 25      NPS 2   DN 50      NPS 3  DN 80      NPS 47 DN 100      NPS 6  DN 150     NPS 8 x 6   DN 200 x 150    NPS 12 x 6  DN 300 x 150     Main Valve Body Material  Select One   Cast lron      WCC Steel      CF8M Stainless steel  NACE       Main Valve End Connection Style  Select One                                                                       Cast Iron Body  NPT  NPS 1 and 2  DN 25 and 50 only      CL125 FF     CL250 RF       WCC Steel or CF8M Stainless Steel Body   NPT  NPS 1 and 2   DN 25 and 50 only       SWE  NPS 1 and 2  DN 25 and 50 only     CL150 RF      CL300 RF      CL600 RF      BWE 40     BWE 80    PN 16 25 40  please specify rating    Main Valve Body Flange Material  Select One   Cast Iron      WCC Steel      CF8M Stainless Steel  NACE       Percent Travel or Travel Stop  Select One   O 100 percent  standard       O 70 percent  NPS 2   DN 50 only      O 40 percent  Not available for NPS 1 and 2    DN 25 and 50      O 30 percent  NPS 2   DN 50 only       Main Valve Cage Type and Material  Select One   Linear  CF8M Stainless Steel  NACE       Whisper Trim    Cage  416 Stainless steel  Whisper Trim Cage  316 Stainless steel  NACE   Quick Opening  Cast Iron   Quick Opening  Steel  for NPS 6   DN 150 body only                                                                                                                                         1  Inconel   is a mark owned by Special Metals Corporation     Type EGR  continued   Main Valv
18. n maintains a higher loading  pressure on the bottom of the Type 1098 actuator  The  pressure differential across the main valve diaphragm  moves the diaphragm upward causing the main valve  to open which allows the blanket gas to flow out to   the vapor recovery system vacuum source  hence  controlling the vessel blanket pressure     When the vessel blanket gas pressure begins to stabilize   the pilot spring throttles the pilot disk closed  This allows  the loading pressure source to fill both sides of the   Type 1098 actuator through the fixed restriction  This  equalizes the pressure acting on the diaphragm  thus  allowing the main valve spring to close the main valve plug     Sizing Blanketing Systems    When sizing a gas vapor recovery regulator system  you  must consider the volume of blanketing gas that must be  displaced from the vessel when either filling the vessel  with liquid  pump in  or the expansion of vapors inside  the vessel during atmospheric thermal heating     Using the established procedures from American  Petroleum Institute Standard 2000  API 2000   determine  the flow rate for outbreathing     1  Determine the flow rate of blanketing gas  displaced when liquid is being pumped into the  vessel  see Table 6      2  Determine the gas flow rate due to outbreathing  caused by atmospheric thermal heating  see Table 7      3  Add the requirements of 1 and 2 and select a vapor  recovery regulator size based on total capacity  required from Table 4     Sample 
19. nt is Below 100  F   38  C or  Normal Boiling Point is Equal to or Above 300  F   149  C Normal Boiling Point is Below 300  F   149  C  60 2500 9500 40   1 07 60   1 61  100 4200 16 000 60   1 61 100   2 68  500 21 000 79 500 300   8 04 500   13 4  1000 42 000 159 000 600   16 1 1000   26 8  2000 84 000 318 000 1200   32 2 2000   53 6  3000 126 000 477 000 1800   48 2 3000   80 4  4000 168 000 636 000 2400   64 3 4000   107  5000 210 000 795 000 3000   80 4 5000   134  10 000 420 000 1 590 000 6000   161 10 000   268  15 000 630 000 2 385 000 9000   241 15 000   402  20 000 840 000 3 180 000 12 000   322 20 000   536  25 000 1 050 000 3 975 000 15 000   402 24 000   643  30 000 1 260 000 4 769 000 17 000   456 28 000   750  35 000 1 470 000 5 564 000 19 000   509 31 000   831  40 000 1 680 000 6 359 000 21 000   563 34 000   911  45 000 1 890 000 7 154 000 23 000   616 37 000   992  50 000 2 100 000 7 949 000 24 000   643 40 000   1072  60 000 2 520 000 9 539 000 27 000   724 44 000   1179  70 000 2 940 000 11 298 000 29 000   777 48 000   1286  80 000 3 360 000 12 718 000 31 000   831 52 000   1394  90 000 3 780 000 14 308 000 34 000   911 56 000   1501  100 000 4 200 000 15 897 000 36 000   965 60 000   1608  120 000 5 040 000 19 077 000 41 000   1099 68 000   1822  140 000 5 880 000 22 256 000 45 000   1206 75 000   2010  160 000 6 720 000 25 436 000 50 000   1340 82 000   2198  180 000 7 560 000 28 615 000 54 000   1447 90 000   2412             The small fixed restrictio
20. p TF DD FOIOO DO D  PPPIPPPPP PPPPP PPPPPIPPPPPJIPPPPP PPPPPPJPPPRPPRP       A   Best possible selection  A  Recommended  B  Minor to moderate effect  Proceed with caution        Installation    Install the regulator using a straight run of pipe the  same size or larger than the regulator body  Flow  through the regulator body is indicated by the flow  arrow cast  stamped  or riveted on the body  If   a block valve is required  install a full flow valve  between the regulator and the blanketed vessel   For proper operation at low setpoint ranges  the  regulators should be installed with the pilot spring  case barrel pointed down     C  Unsatisfactory    L   Information lacking    Ordering information    Refer to the Specifications section on page 2   Carefully review the description of each specification  and specify the desired selection on the Ordering  Guide page wherever there is a choice to be made                       1 2 NPT  CONTROL LINE  CONNECTION                 Bulletin 74 2 1290    16 06            EXHAUST LINE    408    1 4 NPT GAUGE           N    TRIM REMOVAL  CLEARANCE       TAP CONNECTION                 SIZE 40  ACTUATOR                                  hee 11 56    3 4 NPT   294  TYPE Y291A PILOT  y  TYPE 95H      B2442 1 13 12    La 333 gl AR ACTUATOR  REMOVAL  CLEARANCE  SUPPLY PRESSURE  CONNECTION   1 4 NPT   Inch    mm  Figure 3  Type 1290 Dimensional Drawing  Table 9  Type 1290 Dimensions  DIMENSIONS  Z AR  CL125 FF CL250 FF  MAIN VALVE Cast Iron  or
21. r applicability  We reserve the right to modify or improve the designs or specifications of such    products at any time without notice     Emerson Process Management Regulator Technologies  Inc  does not assume responsibility for the selection  use or maintenance of any product  Responsibility for proper selection  use and    maintenance of any Emerson Process Management Regulator Technologies  Inc  product remains solely with the purchaser       Emerson Process Management Regulator Technologies  Inc   1994  2013  All Rights Reserved       ZS    EMERSON     
22. rpressure protection     The Type 1290 vapor recovery regulator responds to  any changes in the blanket gas pressure and throttles  open or closed to control the flow of the blanket gas  out of the vessel  A vacuum source on the outlet of  the regulator is usually necessary to ensure flow of low  pressure blanket gas out of the vessel into a vapor    recovery system  The higher the vacuum pressure of  the vacuum source  the higher the flow capacity of the  vapor recovery regulator     The pressure of the blanket gas registers under   the diaphragm of the pilot  A Type 95H regulator  provides a constant loading pressure source to the  Type 1098 EGR main valve actuator  When the pilot  is closed  the loading pressure fills both sides of the  Type 1098 actuator through a fixed restriction     The Type 1098 EGR main valve spring keeps the  main valve plug tightly shut off  When the vessel  blanket gas pressure reaches the setting of the   pilot spring  the pilot diaphragm moves  opening   the pilot valve disk and exhausting some of the   Type 1098 EGR   s actuator loading pressure through  the pilot orifice  This typically happens when the vessel  is being filled with liquid        Bulletin 74 2 1290    Table 7  Gas Flow Required for Thermal Heating  Outbreathing  per API 2000  Interpolate for intermediate sizes                                   VESSEL CAPACITY SCFH   Nm  h AIR FLOW RATE REQUIRED  Barrels Gallons Liters Flash Point is Equal to or Above 100  F   38  C or Flash Poi
23. s   336 kg  NPS 12 x 6  DN 300 x 150  1265 pounds   574 kg       1  End connections for other than U S  standards can usually be provided  Consult your local Sales Office   2  The pressure temperature limits in this Bulletin and any applicable standard or code limitation should not be exceeded     blanket gas out of the vessel into a vapor disposal or  reclamation system  The higher the vacuum pressure  of the vacuum source  the higher the flow capacity of  the vapor recovery regulator     Principle of Operation    The Type 1290 vapor recovery regulator serves as  a vessel vapor recovery system  The Type 1290    regulator controls vessel blanketing gas pressure  when the vessel is being filled with fluid or   when ambient temperature causes the vapor gas  to expand     The system monitors the increasing blanket pressure  and throttles open to pass excess blanketing gas into  a vapor recovery system thus controlling the desired   set pressure of the vessel     Bulletin 74 2 1290        TYPE 1098 EGR    d MAIN VALVE         VAPOR RECOVERY  VACUUM SOURCE               CONTROL LINE                              Mga ga N           Vil         FIXED  RESTRICTION                                                   SETPOINT  ADJUSTMENT           EXHAUST LINE    VAPOR PRESSURE       TYPE 95H SUPPLY  REGULATOR        E0063    C  ATMOSPHERIC PRESSURE    LOADING PRESSURE    M INTERMEDIATE PRESSURE    E VACUUM PRESSURE  EZ TANK PRESSURE    Figure 2  Operational Schematic    Table 1  Construc
24. system to control the outflow of  blanketing gas under normal conditions and to collect  vessel vapors for the vapor disposal or reclamation  system  You should provide alternate methods of  emergency overpressure protection per the American  Petroleum Institute Standard 2000  API 2000      The vapor recovery regulator responds to any changes  in the blanket gas pressure and throttles open or  closed to control the flow of the blanket gas out of the  vessel  A vacuum source on the outlet of the regulator  is usually necessary to ensure flow of low pressure    ZS    EMERSON     D101964x012    Bulletin 74 2 1290    Specifications    Body Size and End Connection Styles          MAIN VALVE END CONNECTION STYLE          BODY SIZE   NPS DN WCC Steel or  SEH CF8M Stainless Steel  1or2  NPT  CL125 FF or  NPT  SWE  BWE  CL150 RF   25 or 50 CL250 RF flanged Ee  9 or PN 16 25 40 flanged  3  4  or 6  CL125 FF or BWE  CL150 RF  CL300 RF     80  100  or 150    CL250 RF flanged    CL600 RF  or PN 16 flanged       8x6or12x6   200 x 150 or 300 x 150          BWE  CL150 RF   CL300 RF  CL600 RF   or PN 25 flanged       Construction Materials    See Table 1    Maximum Main Valve Inlet Pressures      See Table 3    Maximum Differential Pressure  35 psi   2 4 bar    Control Pressure Ranges                    See Table 2  Type 95H Supply Pressure Settings  TYPE 1098 EGR MAIN VALVE WITH  PILOT GREEN SPRING  NPS   DN SPRING  TYPE 1  2 3  or 4  6 or8x6  COLOR  25  50  80  or 100 150 or 200 x 150  Y291
25. tion Materials                            ion              MAIN VALVE  SIZE 40 PILOT SUPPLY  Body and Plug and Spring Cage ACTUATOR REGULATOR  Body Flange Seat Ring  Cast iron 416 oe Steel Cast iron Steel Ductile iron Cast iron  WCC Steel   476 SES Steel Steel Steel Ductile iron WCC Steel  316 Stainless  CF8M 316 Stainless   Inconel   steel Stainless dier  CF8M Stainless  CF8M Stainless  Stainless steel steel X 750 Whisper steel steel  Trim    Cage    1  Special construction materials are offered for your system compatibility  Contact your local Sales Office for additional information   Inconel   is a mark owned by Special Metals Corpora       DIAPHRAGMS    Nitrile  NBR      Fluorocarbon  FKM    or Ethylenepropylene     EPDM        O RINGS AND SEALS    Nitrile  NBR    Fluorocarbon  FKM    Ethylenepropylene   EPDM   or  Perfluoroelastomer   FFKM           Bulletin 74 2 1290    Table 2  Control Pressure Ranges                                           PILOT SPRING  SPRING PART BUILDUP TO SCENE SPRA S TREE   1  DIAMETER LENGTH  TYPE CONTROL PRESSURE RANGES COLOR NUMBER WIDE OPEN   Inch mm Inch mm  Y291AL 0 5 to 1 5 inches w c    1 to 4 mbar   Black 1B413627222   0 25 inch w c    0 60 mbar 0 075 1 90 2 19 56 0  1 to 2 5 inches w c    2 to 6 mbar     Orange   1B558527052   0 25 inch w c    0 60 mbar 0 072 1 83 3 78 96 0  2 to 7 inches w c    5 to 17 mbar    4  Red 1B653827052   0 25 inch w c    0 60 mbar 0 085 2 20 3 63 92 0  4 to 14 inches w c    10 to 35 mbar Unpainted   1B65392
    
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