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HomeMy WebLinkAboutSpecs-BortnickInstruction MCK2141Manual R600 and HSRL Series LP -Gas Regulators March 2006 R600 and HSRL Series Instruction Manual W WARNING Failure to follow these instructions or to properly install and maintain this equipment could result in an explosion and/or fire causing property damage and personal injury4s death. Fisher equipment must be installed, operated, and maintained in accordance with federal, state, and local codes and Fisher instructions. The Installation in most states must also comply with NFPA No. 54 and 58 standards. Only personnel trained in the proper procedures, codes, standards, and regulations of the LP -gas industry should install and service this equipment. U Things to tell the gas customer: 1. Show the customer the vent or vent assembly or vent tube. Stress that this opening must remain unobstructed at all times. Tell the customer to check the vent opening after a freezing rain, sleet storm, or snow to make sure ice has not formed in the vent. 2. Show the customer the shutoff valve on the container. TYPEHSRL The customer should close this valve immediately if gas Figure 1. Types R622, R642 and HSRL is smelled, appliance pCt lights fail to stay on or appear higher than usual or any other abnormal situation occurs. 2 psi (0,14 bar) service regulators used on LP -Gas 3. Tell the customer to.call your company to service the vapor service applications. They are not to be used regulator if the regulator vents gas or a leak develops on liquid service. in the system,„Only a qualified gas service person should Insrlgfi;' or service the regulator. Description Introduction Second Stage Low Pressure Regulators, Scope of Manual This instruction manual covers Installation and Maintenance for the R600 and HSRL Series regulators, which includes first stage, second stage, integral and The Types R622, R642, R652, and HSRL Series regulators provide low pressure, inches of water column, delivery pressures. They are normally set at 11-inches water column (27 mbar) pressure. They have high capacity internal relief valve construction. The regulators are normally painted PALM GREEN. The units differ in construction and.,capacity rating. FISHER' [www.FISHERregulators.com/l-pi i EMERSON.. Process Management R600 and HSRL Series LP -Gas Regulators Specifications Pressure Taps Size Restriction R600 Series: 1/8 NPT: #54 (0.055 inch (1,40 mm)) Drill on outlet and inlet HSRL Series: None Orifice Sizes R600 Series: 7/32-inch (5,55 mm) HSRL Series: 3/8-inch (9,5 mm) Wide Open C. for Relief Sizing R600 Series: 38 HSRL Series: 105 Maximum Allowable Inlet Pressure Types R622H, R632: 250 psig (17,24 bar) Types R622E, R652E: 10 psig (0,69 bar) Types R622, R642, R652, and HSRL Series: 10 psig (0,69 bar) Maximum Emergency Inlet Pressure Types R622H, R632: 250 psig (17,24 bar) Types R622E, R652E: 15 psig (1,03 bar) Types R622, R642, R652, and HSRL Series: 15 psig (1,03 bar) Temperature Capabilities -20' to 160°F (-29° to 71 °C) Pressure Registration Internal Integral Two -stage Regulator The Type R632 integral two -stage regulator contains anon -adjustable first stage regulator on the inlet. The second stage provides 11-inches water column (27 mbar) outlet pressure. The second stage portion has a high capacity internal relief valve construction. The first stage does not have an internal relief valve. The regulators are normally painted GRAY. First Stage and 2 PSI (0,14 bar) Service. Regulators Outlet Pressure Standard Set Point Types R622, R642, R652, and HSRL Series: 11-inches w.c. (27 mbar) Type R632: First Stage: approximately 10 psi (0,69 bar) Second Stage: 11-inches w.c. (27 mbar) Types R622E, R652E: 2 psi (0,14 bar) Type R622H: 10 psi (0,69 bar), 5 psi (0,35 bar) Outlet Pressure Spring Range Types R622, R642, R652: 7.5 to 9.5-inches w.c. (19 to 24 mbar), 9 to 13-inches w.c. (22 to 32 mbar), 13 to 20-inches w.c. (32 to 50 mbar), 16 to 40-inches w.c. (40 to 99 mbar) Type R632: First Stage: non-adjustable Second Stage: 9 to 13-inches w.c. (22 to 32 mbar) Types R622E, R652E: 1 to 2.2 psi (0,069 to 0,15 bar) Type R622H: 8 to 12 psi (0,55 to 0,83 bar), 4 to 6 psi (0,28 to 0,41 bar) HSRL Series: 9 to 13-inches w.c. (22 to 32 mbar) Approximate Weight Types R622H, R632 with POL Inlet: 1.7 pounds (771 grams) All Other R600 Series: 1.4 pounds (635 grams) HSRL Series: 4.5 pounds (2,04 kg) Specifications Specifications section, Tables 1 and 2 list the specifications for these regulators. Contact the factory if the regulator is to be used on any service other than LP -gas, natural gas, or air. The following information is located on the spring case: Type number, orifice size, spring range, and date of manufacture. Installation The Types R622H, R622E and R652E regulators are designed for high pressure (pounds per square inch) I vapor service. These regulators have high capacity I WARNING internal relief valves. When used on first stage service, the Type R622H regulator reduces container pressure to 10 psig (0,69 bar) for a second stage regulator. On final stage service the regulator reduces container pressure for a high pressure burner. The regulator is normally painted RED. The Type R622E or R652E standard outlet pressure setting is 2 psig (0,14 bar). The regulator is painted PALM GREEN with a WHITE CAP. It is an intermediate stage regulator that reduces 10 psig (0,69 bar) first stage pressure to 2 psig (0,14 bar). They are used on 2 psig (0,14 bar) pressure systems. The Types R622E and R652E are not suitable for first stage service. All vents should be kept open to permit free flow of air in and out of the regulator. Protect vent openings against the entrance of rain, snow, ice formation,.paint, mud, insects, or any other foreign material that could plug the vent or vent line. LP -gas may discharge to the atmosphere through the vent. An obstructed vent which limits air or gas flow can cause abnormally high pressure that could result in personal injury or property damage. Failure to use a vent line on R600 and HSRL Series LP -Gas Regulators Table 1, Relief Valve Specifications TYPE TYPICAL SET POINT NOMINALRELIEF VALVE MAXIMUM INLET PRESSURE TO NOT EXCEED OUTLET PRESSURE WITH DISC REMOVED START DISCHARGE Inlet Pressure Maximum Outlet Pressure HSRL 11-inches w.c. (27 mbar) 1 psi (0,069 bar) 15 psig (1,03 bar) 2 psig (0,14 bar) R622, R642 50 psig (3,4 bar) R652 R632 250 psig (17,2 bar)) R622E 2 psi (0,14 bar) 3.5 psi (0,24 bar) 50 psig (3,4 bar) 5 psig (0,34 bar) R652E R622H 10 psi (0,69 bar) 20 psi (1,37 bar) Not Applicable Table Z Capacity, Connection Sizes, and Vent Orientation REGULATOR APPLICATION TYPETPCROPANE(" NUMBERBTU APACITY INLET .CONNECTION OUTLET CONNECTION OUTLET PRESSURE SETTING 3/4-INCH NPT SCREENED VENTSTANDARD LOCATION R622-BCF 675,000 1/2-I1ch FNPT 1/2-inch FNPT R642-DFF 900,000 3/4-inch FNPT 11-Inches w.c. R652-DFF 1,000,000 Second Stage 3/4-Inch FNPT (27 mbar) Over Inlet R622-CFF 1,400,000 1/2-Inch FNPT �R622-DFF ' 3/4'-inch FNPT R622-CFGXA 1,125,000 1/2-Inch FNPT 18-inches w.c. inch FNPT (45 mbar) HSRL-BFCI'1 2,100,000 3/4-Inch FNPT 11-inches w.c. (27 mbar) HSRL-CFCI4 1-Inch FNPT 1-Inch FNPT Integral Two -Stage R632-13CF 700,000 1/4-inch FNPT 1/2-Inch FNPT 11inches ( (27 mbar) First Stage: Down Second Stage; Over Inlet R632-HCF FPOL R632-CFF 750,000 1/4-inch FNPT 3/4-Inch FNPT Rfi32JFF FPOL 2 PSI rybar) Service R622E-BCH L250,000 1l2-inch FNPT 1/2-inch FNPT 2 psig (0,14 bar) Over Inlet R622E-DCH 1,500,000 3/4-Inch FNPT 314-inch FNPT R652E-DFH 1,400,c00 R622H-BGK 2.000,000 1/2-inch FNPT 5 psig (0,35 bar) - R622H-BGJ .aK 2.100,000 1/2-inch FNPT 10 psig (0,69 bar) - R622HHGJ R622H-HGJKA First Stage""' FPOL Over Outlet R622H-JGK 2,250,000 314-Inch FNPT 5 psig (0,35 bar) R622H-JGJ 10 psig (0,69 bar) R622H-OGJ 2,40g000 3l4-inch FNPT 1. Capacities Based on: Second Stage: 10 psig (0,69 bar) Inlet pressure and 2-Inches w.c. (5 mbar) droop. Integral Two Stage: 30 psig (2,07 bar) and 24nches we. (5 mbar) droop. 2 PSI (0,14 bar) Service: 10 psig (0,69 bar) inlet pressure and 20%droop. First Stage: 30 psig (2,07 bar) Inlet pressure and 20%droop. 2. Straight globe valve body conllgumtion. R600 and HSRL Series LP -Gas Regulators Installation Location • The installed regulator should be adequately protected from vehicular traffic and damage from other external sources. - Install the regulator with the vent pointed vertically down, see Figure 2. If the vent cannot be installed in a vertically down position, the regulator must VENT POINTED DOWN be installed under a separate protective cover. Installing the regulator with the vent down allows condensation to drain, minimizes the entry of water or other debris from entering the vent, and minimizes vent blockage from freezing precipitation. Figure 2. Regulator with Vent Pointed Down Indoor Installations can cause a hazardous accumulation of gas which could result in personal injury or property damage. Never use a Type R622H, R622E or R652E (pounds to pounds) regulator on low pressure (inches of water column) service because personal injury or property damage could occur. The Types R622E and R652E are not suitable for use as a "first stage" regulator. General Installation Instructions Before installing the regulator, • Check for damage, which might have occurred in shipment. • Check for and remove any dirt or foreign material, which may have accumulated in the regulator body. • Replace old pigtails. Blow out any debris, dirt or copper sulfate in the copper tubing and the pipeline. - Apply pipe compound to the male threads of the pipe before installing the regulator. - Make sure gas flow through the regulator is in the same direction as the arrow on the body. "Inlet' and "Outlet" connections are clearly marked. - Do not install the regulator in a location where there can be excessive water accumulation or ice formation, such as directly beneath a down spout, gutter, or roof line of building. Even a protective hood may not provide adequate protection in these instances. • Install the regulator so that any gas discharge through the vent or vent assembly is over 3 feet (0,91 meters) horizontally from any building opening below the level of discharge. - Install the regulator high enough above ground level at least 18-inches (45 cm) - so that rain splatter cannot freeze in the vent. Regulators Subjected to Heavy Snow Conditions Some installations, such as in areas with heavy snowfall, may require a hood or enclosure to protect the regulator from snow load and vent freeze over. Horizontally Installed Regulators Horizontally mounted regulators, such as found in single cylinder installations and ASME tanks, must be installed beneath a protective cover or under the ASME tank dome, refer to Figure 3. If possible, slope or turn the vent down sufficiently to allow any condensation to drain out of the spring case.:. Be careful that the slot in the tank dome or protective cover for the regulator's outlet piping does not expose the vent to the elements. The first stage vent on the Type R632 should be pointed down. Meter Installations Type R642 regulators have an angle body that makes it easy to install on to a gas meter instead of piping leading directly into a building. Meter and Type R642 with vent over regulator inlet: Install the regulator per instructions given in the previous section "Installation Location". R600 and HSRL Series LP -Gas Regulators Figure 3. Tank Installation Meter and Type 11642;with vent over the regulator outlet and installed over the top of the meter: This installation orientation will put the Type R642 regulator vent in a vertical down position, but very close to the top of the gas meter. The regulator vent may become blocked during a freezing rain storm or heavy snows. Therefore, some type of protective cover should be installed over the regulator and meter or vent piping should be installed so that the vent remains open. Meter and Type R642 Regulator Installed Indoors: Pipe the regulator vent per the section,"Indoor Installations Indoor Installations By code, regulators installed indoors have limited inlet pressure, and they require a vent line to the outside of the building, see Figure 4. A vent assembly, such as Fisher Y602 Series, should be used on the end of the vent line. The same installation precautions, previously discussed throughout this manual for the regulator vent, apply to the end of the vent tube assembly. Vent lines must not restrict the gas flow from the regulator's internal relief valve. Vent lines should be at least 3/4-inch NPT pipe or 3/4-inch NPT size, Gray PVC Schedule 40 Rigid Non-metallic Electrical Conduit for above Ground Service, per UL 651. To install the vent line, remove the vent screen and apply a good grade of pipe dope to the male threads of the line. Vent lines should be as straight as possible with a minimum number of bends. To APPLIANCE VENT LINE BASEMENT FROM FIRST - STAGE REGULATOR VENTASSEMBLY VENT OPENING MUST BE AT LEAST 3 FEET (0,91 meters) HORIZONTALLY FROM ANY BUILDING OPENING BELOW IT Figure 4. Basement Installation R600 and HSRL Series LP -Gas Regulators END OF REGULATOR VENT TUBE GRADE GROUND DOWNWARD AND LOCATED AT TOP INSIDE OF HOUSING DOME COVER. SLOPING AWAY FROM HOUSING DOME. THIS PREVENTS WATER COLLECTING - AND RUNNING INTO OR STANDING AROUND HOUSING DOME. 2-INCHES (50,8 mm) MINIMUM REGULATOR ADJUSTMENT CLOSURE CAP MUST BE TIGHT WATER MARK LEFT IN HOUSING DOME AT LEVEL Y / ABOVE REGULATOR VENT, OR END OF VENT TUBE REQUIRES REPLACEMENT OF REGULATOR. THEN CORRECT INSTALLATION. Figure 5. Underground Installation Underground Installations Type R632 integral regulators require 2 vent tubes, one on the first stage vent and one on the second stage vent, when installed on underground tanks. Failure to use 2 separate vent tubes can result in early regulator failure and/or over pressuring Ufa second stage that could result in fires`ar personal injury. Regulators installed in the dome of an underground container require a vent tube to prevent water from entering the regulator spring case, see Figure 5. Note: Type R632 integral regulators installed on underground tanks require the use of 2 vent tubes, one for the first stage vent and the other for the second stage vent of the regulator. Remove the vent screen and install a vent tube. The vent tube must be run from the regulator vent to above the maximum water table. The vent tube opening must terminate at the extreme top inside of the dome cover. Make sure the regulator's closing cap is on tightly, and maintain drainage away from the dome at all times. For further information on Underground Installations, contact Aero Fulfillment Services at phone number 866-840-1075 and ask for Item number 000412 "Installation of Underground LP -Gas Systems: Suggested Installation, Inspection,". Adjustment Each regulator is factory set. If it becomes necessary to increase the outlet pressure, remove the closing cap and turn the adjustment screw clockwise. Turn the adjusting screw counterclockwise to decrease the outlet pressure. The first stage portion of the Type R632 integral regulator is non-adjustable. The outlet pressure plug may be removed using a 7/16-inch (11,1 mm) hexagon wrench. The pressure tap is restricted, so the plug can be removed with pressure on the outlet of the regulator. Install a pressure gauge to determine the regulator's outlet setting during adjustment, (Actual pressure at the second stage regulator may be less due to line loss.) After setting, reinstall the pipe plug and replace the closing cap. Check the plug for leakage. Inlet pressure may be checked using the inlet pressure gauge tap and a pressure gauge. Remove the plug using a 7/16-inch (11,1 mm) wrench. The pressure tap is restricted, so the plug can be removed with pressure on the inlet of the regulator. Overpressure Protection 00 WARNING Some type of overpressure protection is needed if actual inlet pressure can exceed the outlet pressure rating. Overpressuring any portion of this equipment above the R600 and HSRL Series LP -Gas Regulators limits shown in the Specifications section may cause damage to regulator parts, leaks in the regulator, or personal injury due to bursting of pressure -containing parts or explosion of accumulated gas. If any portion of the regulator is exposed to an overpressure condition that exceeds the limits in the Specifications section, it must be inspected for damage that may have occurred. Large volumes of gas may discharge through the regulator vent during internal relief valve operation, which can, if not controlled, result In fire or explosion from accumulated gas. The R600 and HSRL Series regulators, except for the first stage of the Type R632, contain internal relief valves. The Internal relief valve in all units will give overpressure protection against excessive build-up resulting from seat leakage due to worn parts or chips or foreign materia1`6n'2the orifice. The amount of internal relief protection,, provided varies with the regulator type and the cause for' the overpressure relief valve operation. When the internal relief valve opens, gas escapes to the atmosphere through the regulator's vent. Some type of additional external overpressure protection must be provided if the outlet pressure in an overpressure condition exceeds the inlet pressure rating of the gas system or downstream equipment. Common methods of external overpressure protection include relief valves, monitoring regulators, shutoff devices, and series regulation. Maintenance To avoid personal injury or equipment damage, do not attempt any maintenance or disassembly without first isolating the regulator from system pressure and relieving all internal pressure. Regulators that have been disassembled for repair must be tested for proper operation before being returned to service. Only parts manufactured by Fisher should be used for repairing Fisher regulators. Relight pilot lights according to normal startup procedures. Due to normal wear or damage that may occur from external sources, these regulators must be inspected and maintained periodically. The frequency of inspection and replacement of the regulators depends upon the severity of service conditions or the requirements of local, state, and federal regulations. Even under ideal conditions, these regulators should be replaced after 20 years from date of manufacture or sooner should inspection reveal the need. Visually inspect the regulator each time a gas delivery is made for: • Improper installation, vent not pointed vertically down or under a cover; no vent tube on underground systems. • Plugged or frozen vent. • Wrong regulator or no regulator in the system. • Internal or external corrosion.' • Flooded Regulator; water in spring case; regulator submersed on underground tanks • Regulator age. • Any other condition that could cause the uncontrolled escape of gas. Failure to do the above could result in personal injury or property damage. Vent Opening Make sure the regulator vent, vent assembly, or vent tube does not become plugged by mud, insects, ice, snow, paint, etc. The vent screen aids in keeping the vent from becoming plugged, and the screen should be clean and Properly installed. Water inside Regulators from Floods, Weather or Water Table on Underground Systems Replace any regulator that has peen flooded or has been submersed below the water table of an underground tank, have had water in their spring case or show evidence of external or internal corrosion. Checking for internal corrosion can be done by removing the closing cap and with the aid of a flashlight observing the condition of the relief valve spring, main spring, and internal spring barrel area. A more detailed examination will require shutting R600 and HSRL Series LP -Gas Reaulators down of the gas system and the complete removal of the adjusting screw. Closely examine regulators installed with their vent horizontal for signs of corrosion. Correct any improper installations. Regulator Replacement Older regulators are more likely to catastrophically fail because of worn or corroded parts. Replace R600 and HSRL Series regulators over 20 years of age. Other service or environmental conditions may dictate replacement of the regulator before it becomes 20 years old. Regulators that are installed on underground systems and In areas that are subject to sea salt (coastal) atmospheres should be inspected annually for external and Internal corrosion and may require replacement sooner. Refer to Fisher Bulletin LP-32 for additional information. Regulator Repair Regulators that have been disassembled for repair must be tested for proper operation before being returned to service. Only parts manufactured by Fisher should be used to repair Fisher regulators. Be sure to give the complete type number of the regulator when corresponding with the factory. The type number, orifice size, and spring range are on a label attached to the spring barrel. The date of manufacture is stamped on the regulator. Always provide this information in any correspondence with your Fisher Distributor regarding replacement parts or technical assistance. If construction changes are made in the field, be sure that the regulator marking is also changed to reflect the most recent construction. EM Fisher and Fisher Regulators are marks owned by Fisher Controls International, LLC, The Emerson logo Is a trademark and service mark of Emerson Electric Co. All other marks are the property of their respective owners. The contents ofthlspublMatlon arepmsentedforinformationalpurposes only, andwhile eveiveflodhas Issueless to ensure Ihelraccuracy,theyerenotto bec'onsfruedas wermntles orgua2ntees, expressed or Implied, regarding the products or servlcas described herein or their use or applicability, We reserve the right to modify orlmprove the designs or specifications of such products at any time without notice. Fisher does not assume responsibility for the selection, use or maintenance of any product. Responslbllity for proper selection, use and maintenance of any Fisher product remains solely with the purchaser. Emerson Process Management Fisher Controls International, LLC. P.O. Box 8004 McKinney, Texas 75070, USA Telephone: 1 (800) 588-5853� Telephone:1 (469)293-4201 EMERSON.. ®Fisher Controls International, LLC., 2001, 2006; All Rights Reserved , Process Management GAS PIPING INSTALLATIONS TABLE 402.4(28) SCHEDULE 40 METALLIC PIPE Gas Undiluted Propane Inlet Pressure no In. w.0. Pressure Drop 10.5 Specific Gravity 1.50 INTENDED USE Pipe sizing between single -or second -stage (low pressure) regulator and appliance. PIPE SIZE (inch) Nominal '/z - '14 1 1'/4 1'12 2 2'/z 3 4 Actual ID 0.622 0.824 1.049 1.380 1,610 2.067 2.469 3.068 4.026 Length (ft) Capacity In Thousands of Btu per Hour 10 291 608 1,150 2,350 3,520 6,790 10,800 19,100 39,000 20 200 418 787 1,620 2,420. 4,660 7,430 13,100 26,800 30 t60 336 632 1,300 1,940 3,750 5,970 10,600 21,500 40 137 287 541 1,110 1,660 3,210 5,110 9,030 18,400 50 122 255 480 985 1,480 2,840 4,530 8,000 16,300 60 110 231 434 892 1,340 2,570 4,100 7,250 14,800 80 101 212 400 821 1,230 2,370 3,770 6,670 13,600 100 94 197 372 763 1,140 2,200 3,510 6,210 12,700 125 89 185 349 716 1,070 2,070 3,290 5,820 11,900 150 84 175 330 677 1,010 1,950 3,110 5,500 11,200 175 74 155 292 600 899 1,730 2,760 4,880 9,950 200 67 140 265 543 814 1,570 2,500 4,420 9,010 250 62 129 243 500 749 1,440 2,300 4,060 8,290 300 58 120 227 465 697 1,340 2,140 3,780 7,710 350 51 107 201 412 618 1,190 1,900 3,350 6,840 400 46 97 1.82 373 560 1,080 1,720 3,040 6,190 450 42 89 167 344 515 991 1,580 2,790 5,700 500 40 83 156 320 479 922 1,470 2,600 5,300 550 37 78 146 300 449 865 1,380 2,440 4,970 600 35 73 138 283 424 817 1,300 2,300 4,700 650 33 70 131 269 403 776 1,240 2,190 4,460 700 32 66 125 257 385 741 1,180 2,090 4,260 750 30 64 120 246 368 709 1,130 2,000 4,080 800 29 61 115 236 354 681 - 1,090 1,920 3,920 850 28 59 Ill 227 341 656 1,050 1,850 3,770 900 27 57 107 220 329 634 1,010 1,790 3,640 950 26 55 104 213 319 613 978 1,730 3,530 1,000 25 53 100 206 309 595 948 1,680 3,420 1,100 25 52 97 200 300 578 921 1,630 3,320 1,200 24 50 95 195 292 562 895 1,580 3,230 1.,300 23 48 90 185 277 534 850 1,500 3,070 1,400 22 46 86 176 264 509 811 1,430 2,930 1,500 21 44 82 169 253 487 777 1,370 2,800 1,600 20 42 79 162 243 468 746 1,320 2,690 1,700 19 40 76 156 234 451 719 1,270 2,590 1,800 19 39 74 151 226 436 694 1,230 2,500 1,900 18 38 71 146 219 422 672 1,190 2,420 2,000 18 37 69 142 212 409 652 1,150 2,350 For SI: 1 inch = 25.4 mm, 1 foot= 304.8 mm, 1 pound per square inch = 6.895 kPa, 1-inch water column = 0.2488 kPa, I British rlrermal unit per hour= 0,2931 W, 1 cubic foot per hour =0,0283 ms/h, I degree = 0.01745 rid. Note: All Cable entries have been rounded Co three significant digits. FLORIDA BUILDING CODE - FUEL GAS, 7th EDITION (2020) 53 58-116 LIQUEFIED PETROLEUM GAS CODE - 4 Table 16.1 (n) Polyethylene Plastic Pipe —IPS Undiluted Gas: Propane Inlet Pressure: 10.0 psig Pressure Drop: 1.0 psig - Specific Gravity: 1.52 Plastic Pipe - - •- Length r/2 in. SDR 9.33 3/4 in. SDR 11 1 in. SDR 11 1%, in. SDR 11 I'/2 in. SDR 11 2 in. SDR 11 (fft) (0.660) (0.860) (1.007) (1.328) (1.554) (1.943) LVTENDED USE: SizingBetween Pirsf Stage Pressure Regidator and SecondStage (Lgw;Pressttre)Regrdattir'- 30 '•2140 2390 7740 13420 20301 36400 40 1840 3670 6630 11480 17300 31200 50 1630 3260 5870 10180 15400 27600 60 1470 2950 5320 9220 13900 25000 70 1360 2710 4900 8480 12800 23000 80 1260 2530 4560 7890 11900 21400 90 1180 2370 4270 7400 11200 20100 100 1120 2240 4040 6990 1Q600 19000 125 990 990 3580 6200 .. 9360 16800 150 897 897 - 3240 5620 8480 15200 175 826 826 - 2980 5170 7800 14000 200 778 778 2780 4810 - 7260 13000 225 721 721 2600 -4510 6810 1220Q 250 681 681 2460 4260 _ 6430 11600 275 646 646 2340 4050 6110 11000 300 617 617 2230 3860 5830 10476 350 567 567 20503550 5360 9640 400 528 528 1910 3300 4990 8970 450 495 495 992 3100 4680 8410 500 468 468 937 2930 4420 7950 600 700 424 396 424 -390 849 781 2650 2440 4010 -3690 7200 6620 800 363 363 726 2270 3430 6160 900 340 340 682 2130 3220 5780 1000 322 322 644 2010 3040 5460 1500 258 258 517 933 1616 4390 2000 221 221 443 498. 1383 3750 lFd: Iron Yipe Size, SDR: Standard Dimension Ratio Notes: (1) Capacities are in 1000 Btu/hr. (2) Dimensions in parentheses are inside diameter. i 2020 Edition Shaded teat= Revisions. �'= Textdeletions and figure/[able revisions. •'= Section de,telions. W = New material. Asa �noi �v— MagnesiUMTM L��]� Soil Anodes High Potential Magnesium SuperMag High Potential Magnesium An- odes from Galvotec Alloys, Inc. offers typi- cal high workingldriving potentials of -1.70 volts or better vs. coppericopper sulfate ref- erence electrode, providing more current output per pound than AZ- 63 alloy magne- sium anodes. This alloy is the best choice for engineered systems in high resistivity soils. Laboratory- Testing Our modern laboratory is equipped with the best state of the art equipment available. Our technicians and inspectors are well trained and experienced. AChemical Analy- sis is provided for every heat. Each heat is analyzed throughout production to insure consistency. Electrochemical testing is per- formed routinely on randomly selected heats as a quality assurance procedure, utilizing the ASTM-G-97 test method. Production - Quality Control Our production facilities offer the best pos- sible working environment available in the industry. Our personnel are experienced in all phases of the foundry operation. Quality Control in our foundry begins on the foundry floor, where the first line of inspection is the casting and molding crew, our lab techni- cians, inspectors and managers completes the quality team. Our quality control staff carefully monitors raw material, core mate- rials, packaging and all aspects of produc- tion. Laboratory and field investigations prove that Galvotec SuperMag anodes per- form consistently. Packaging- Availability Anodes are supplied in backfill to meet the customers' specifications. The typical back - fill material consists of 75% gypsum, 20% bentonite and 5% sodium sulfate. Standard sizes and shapes are warehoused. Anodes are available packaged and unpackaged with or without leads as per customers' specifications. Nominal weights and dimensions Rev ovos SO 9UUI G �\ Magnesium � H-1 Soil Anodes ReGI5TCR611 FIRM Galvotec Alloys produces the H-1 Alloys, ASTM AZ63. The standard sizes can be found in the following chart. E2 PRODUCT Weight Anode Dimensions NO. BARE PKDG. Width (W) Height (H) Length (L) Diameter (D) Overall Length (OIL) Ibs kg Ibs kg in mm in mm In mm In mm in mm GA-MG-3 H-1 3 1.4 8 3.6 3 76 3 76 5.0 127 5.25 133 8.00 203 GA-MG-5 H-1 5 2.3 13 5.9 3 76 3 76 8.0 229 5.25 133 11.25 286 GA-MG-9 H-1 9 4.1 27 12.2 3 76 3 76 14.0 336 5.25 133 20.00 508 GA-MG-12 H-1 12 5.4 32 14.5 4 102 4 102 12.0 305 7.50 191 18.00 457 GA-MG-17 H-1 17 7.7 45 29.4 4 102 4 102 17.0 432 7.50 191 24.00 610 GA-MG-32 H-1 32 14.5 68 30.8 5 127 5 127 20.5 521 8.50 216 28.00 711 GA-MG-50 H-1 1 50 22.7 100 45.4 1 7 178 7 178 1 16.0 406 1 10.00 254 24.00 610 Other shapes, sizes and weights available on request. H i L ♦ W Backfill Leatl Wire-� tiOtt®11 Bag OL - Alloy Compositions Grade "A" Grade "B" Grade "C Element % % Aluminum 5.3-6.7 5.3-6.7 5.0-7.0 Zinc 2.5-3.5 2.5-3.5 2.0-4.0 Manganese (Min) 0.15 0.15 0.10 Impurities Iron (Max.) 0.003 0.003 0,003 Nickel (Max.) 0,002 0.003 0.003 Copper (Max.) 0.02 0.05 0.10 Silicon (Max.) 0.10 0.30 0.30 Other (Max.) 0.30 0.30 0,30 Magnesium Balance Balance Balance Packaged Anc are prepack it either bags or cardboard cartons in low resistivity, quick wetting, prepared backfill consisting of 75% hydratred gypsum, 20% bentonite, sodium sulphate. and 5% Connecting Wire: Standard 10 feet of solid or stranded #12 AWG Copper Lead Wire/THWN/THNN. Typical Electrochemical Properties Amps/Hrs./Lb. 500-540 Efficiency 50-54% Closed Circuit Potential -1.45 to -1.55v (Copper/Copper Sulfate) Open Circuit Potential -1.50 to -1.60v (Copper/Copper Sulfate) NOTE: While statements contained herein are believed to be accurate, they are offered as suggestions only and no warranty or representation is intended. Galvotec Alloys products are sold subject to the terms and conditions appearing on our printed order acknowledgment. _ Nominal weights and dimensions REV 02103 ° Z z $ c o ry O C y a °z LL omo�A r z �p5� F 3 a a�i S o N U d J F ¢ 0 2 X 'LyCa w w w o o V O N r a 3W z o �o. w0 o� U ��. 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Whcn rlc sar- to prevent f%oaratiml, or w['-n mgeC £, UndcrgmmaA t.,l^ ;::. snail bc anc ared uss�g 4 - ° 4° auger &mhors and 'io° sty[ cable. Cab[c r;i ail inscrtcd [!'i 'A' PE mbiftg to PTOCOV Lk tahk CMul dhtct conracc vn'U� the caU[e. 2. LOCMf cable sppmxsmately 14' hiw.74d of wcldcd s . on [ oyl cads ark Use 4 gafvalftd 9 cAbl,c damps Eo mmm caU1c ta. titc for, 3 _ I-fer Ea SLanda d 6.6 for cRnk Iocadoa, coateng z�7d bsaffjEf.. ANNEX I 58-149 For SI units, 1 ft = 0.3048'm. �� Nearest line of adjoining property that can be / built upon Notes: (1) The rellef valve, filling connection, and fixed': maximum liquid level gauge vent connection at the container must be at least 10 ft from any exterior source of ignition, openings into direct -vent appliances, or mech2nical ventilation air intakes. [later to 6.4.4.4. (2) No part of an underground container can be less than 10 it from an important building or line of adjoining property that can be built upon. Refer to Table 6.4.1,1, T,WFIGURE I.I (c) Underground ASME Containers. (Figure for illustrative,purposes only; code cormpliaiwe required.) ShlrlollleXi=Revisions. 2o=Teztdeletions and Figure/table revisions. •=Sec[iondeletions. iltl=New material. 2020 Edition