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HomeMy WebLinkAboutproduct app�>��f ���� old �`:'•����,,77� r_ Ranked 11 by PERC ✓t In ovcall pafann;I far Pmte_-tfI ranking CeaCnas Undcr.,3mand applied' T.inks on Pmrano F3 as ��� � ; • f a -• C +w - �•r'rY:aR.r.:"�� "..".a"^'�w T•-----.-.�:.,,.,. . "�, w �r^;""t.i �� }y. o" dame in Black plastic orwhite, galvanized steel. 1 �� A =.ia _ •�. I agarI �IM Y4'Wr;pO Ids yF"itF•Z°��{"Us'F FVVY,.; is� S .• �'�.a 'i�E R`'� 1YtF � ^fir+ - �'I Ilul',,�lu��"�", I��I ICI • I ,� - o �P•_^C+.Fi o ;�'/ J1 Jred aiFri9J'-a0!=P:,..dcr - .. �t`�f =� -a:"✓i :C]`v ]r:�•� �5711. vP$^! ise .., C3'Jr;j - ',.(_".� `, ^.c' •j 1t,3 r.� ;ra r.Ats'c. r•?r_! _ _ = 7�{_. `Z jrra d : t: 11r!�St.%+ S rrl E. C C J S e ri.?�•;4-,,=J P u b = r:a,roriaI 13c jr c =72 b:au If 14 J?( outage .?!t? 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ForAboveground use, tanks may be coated Y& TGIC powder. Applicable federal, state or local regulations may contain specific requirements for protective coatings and cathodic protection. The purchaser and installer are responsible for compliance with all federal, state or local regulations, --�' WSDRAWAL VALVE FLOAT-- .'/ . GAUGE �ANODE �-CONNECTION © , FILER VALVE SERVICE MULTIVALVE NAME PLATE RELIEF VALVE F) T TINGS LAYOUT UNDER DOME All vessels dimensions are approximate WATER CAPACITY OUTSIDE HEAD OVERALL OVERALL LEG LEG WEIGHT QUANTITY DIAMETER TYPE LENGTH HEIGHT WIDTH SPACING FULL PER 120 lvg, 454.2 L 24" E11lp 5' - 5 13/16" 3' 0" 10 1/8" 3, _ 0„ 245 lbs. LOAD STACK 96 12 609.E mrri 1671.3mm 911.4 mm 257.2 mm 914.4 mm 111.1 kg. 1 Wg. . 31.5" He►n! 7' - 2 1/2" 3' - 7 112" 12 3/4" 3' - 6" 472 lbs. 63 9 946.3 L 800. i tnm 2197.1 mm 1104.9 mm 323.9 mm 1066.8 mm 214.1 kg. 320 wg. 31.5" Hem! 8' -11 3/4" 3' - 7 1/2" 12 3/4" 4' - 0 1 /4" 5881bs. 45 g .1211.2 L 800.1 mm 2736.9 mm 1104.9 nun 323.9 min 1225,6 mm 266.7 kg, 500 Wg. 1892.5 L 37,42" 950.5 Hem! 91.1011 4' - 1 7116" 15" 5' - 0" 87.1 lbs. 30 6 mm 2997.2 mm 1255.7 mm 381.0 mm 15244O mm 395.1 kg 1000 Wg. 40,96" Hemi 16' -10 13116" 4' - 4 5116" 16 1/4" 9'1729 lbs. 4.. 15 5 �� Rev: Jan, 27, 2016 M Why Tanks Corrode Underground steel tanks corrode due to an electrochemical reaction between the tank and the surrounding soil. The process of corroslon occurs due to small voltage differences on the steel surface that result in the flow of DC current from one location to another. Where current flows from the tank into the soil corrosion occurs. This location is called the anode in a corrosion circuit. Where current floods froin the soil to the tank, no corrosion occurs. The progress of corrosion is determined by the amount of current flovving between the anode and the cathode and whetherthe locations of the anode/ cathode remain constant overtime, Corrosion rates are generally higher in vvet soil environments since the conductivity of the soil promotes the flow of DC current in the corrosion circuit. Corrosion generally erhfbits itself on underground tanks in either a general overall rusting or more commonly, a pitting attack Pit locations may result from metallurgical conditions of the steel surface or soil variations such as rocks, salts, fertilizer, moisture concentration, oxygen ;oncentration, etc. Preuenting Corrosion Protecting underground tanks from corrosion is easilyachieved bythe use of two commonly applied protection methods: external coating and cathodic protection. These two methods are complementary �: --•. and should be used in " conjunction %k th the other. An effective external protective coating insulates the steel from the soil environment, thus preventing thelflow ofcorrosion current from the anode tothe cathode, Aneffective extemal coating can protect over 99% of the tank surface area. However; no coating is perfect. Damage from construction orsofl stresses create tiny defects, which may result in accelerated corrosion atthe defect. Cathodic protection prevents corrosion at those defects by applying DC current from an external source, forcing the tank to become cathode. Application ofsufficient DCcurrenttothe tankwillpreventany corrosion from occurring. The two general types of cathodic protection systems are sacrificial and impressed current. Sacrificial systems are used when the amount of current required for the protection is small, such as -in underground propane tanks. impressed current systems are more commonly used for large structures such as large diameter pipelines. Electrical isolation of the tank from metallic piping systems and electrical'grounds is critical for the cathodic protection system's effectiveness. H®urlearrificiel Cathodir Protection works Sacrificial systems work by creating a yalvanic connection beivieen tvvo different metals. The most common anode material is magnesium, which when coupled to steel results in DC current flow from the magnesium to the steel. The open circuit potential of steel is about -0.50 volts referenced to a copper sulfate electrode. The open circuit potential of magnesium is about -1.55V to -1.8K By connecting the two metals together, the difference of 1 to 1 r5Vvolts results in current flaw to the tank-ihat overcomes the natural corrosion cells that exist on thetank. With this current available to the tank, no corrosion occurs. Magnesium Anodes There are a variety of anode sizes and alloys used for cathodic protection. The trio primary alloys are designed as H-1 (orAZ63) and High Potential. The H-1 alloy is produced from recycled magnesium and has an open circuit potential of approximately-1.55V. This alloy is well suited for protection of underground propane tanks. The High Potential alloy is 99% pure magnesium having an open circuit potential up to -1.8V. This alloy should be used for soil applications over 10,000 ohm -cm resistivity. The two most common anode sizes used for underground propane tanks are 9 lb, and 171b. The size designation relates to the metal weight. 10' of -#12 TVV insulated wire is atfached to the anodes. Anodes are then backfIlled in a mixture of gypsum, bentode, and sodium sulfate to lower the electrical resistance of the anode to soil. The mixture is a low cost, nonhazardous, electrically conductive backfill. The anode and backfill is then packaged In a cotton bag and either a cardboard box or paper bag. Actual shipping weight of these anodes with backfill is 27 lb, and 45 lb. Application Recommendations Magnesium anodes can protect underground tanks in most soil conditions. The H-1 alloy is generally very effective. The following chart provides size and quantityrecommendations forvarious size tanks based on conservative design assumptions. This chart covers soil conditions up to 10,000 ohm -centimeter resistivity. Resistiviiies higher than 10,000 ohm -centimeter generally represent very dry sells. Verification of soil resistivity can be performed through soil analysis. Contact us for design recommendations in locations where soil resistivities exceed 10,000 ohm -cm, or if there is no effective external coating on the tank. The propane service line from the tank to the house also must be considered in the cathodic protection design, unless the service line is plastic. All underground steel pipe should be externally coated with a corrosion resistant material. The service line should be electrically isolated at the house with an insulating fitting or union. if service pipe is less than Win length, the tanic anodes will provide sufficient current to protect both tank and pipe. For longer lengths of pipe, an additional anode may be required at the house connections. If another metallic material such as copper is used for service piping, the pipe should be electrically isolated from the tank at the fill pipe connection. Copper and steel create a galvanic couplethatwvill accelerate corrosion of the steel tank when dirertly connected to copper piping. Generaliy, copper piping does not require cathodic protection. 'Based on 90% effective external coating, 2 ma/ft2 current density, and 30- yearAnode life. poude Installation 1. Determine size and quant w of -anodes from application chart. 2.When a single anode is installed, it should be located near the tank center on either side of tank. 8.When multiple anodes are installed, space them evenly around the tank. See examples below. 1 anode 2 anodes 4-anodes 4.Anodes are shipped in either cardboard boxes or mulfl-wall papersacks. Remove outer container and bury the cloth bagged anode. If anode is supplied in plastic bag, remove plastic bag before installing. 5. Install anodes approximately two to three feet from the tank and at least as deep as the center line of the tank. Anodes work best in locations with permanent moisture, so generally the deeper the better. 6.After placing the anode, stretch out the anode connection wire and extend overto a connection point on the tank -fill pipe. 7. Cover the anode with approximately six inches of backfill and pour 5 gallons of water on the anode to saturate the prepared backfill. Water is necessary to activate the anode. 8. Connect the anode wire to the tank with a low electrical resistance connection. Examples are threaded stud on the j tank fill pipe or any accessible metallic connection point to the tank. All connections should be coated with a moisture -proof material. 9. Ideally, the tank connection is made in the area of the tank fill pipe within the covered dome. With access to the anode wire, subsequent testfng of the tank can include measurement of anode output and verification of performance. R.Verify performance of the anode using an appropriate test procedure. Mec*aaicag COVIR6611011 Undar Dome Whodic PY0*28cii®a osging procedue Equipment Needed: Digital Voltmeter, Red Test Lead AA!n. 12' Long & Black Lead Min. 2' Long, Reference Electrode (Copper/Copper Sulphate Half -Ceti) STEP 1: Using a digital voltmeter insert the red test lead into the Volt jack of the meter and select the 2 or 20 volt DC scale. Clip red test lead connector to an uncoated metallic area of the tank, preferably to the rill pipe multivalve. A good solid connection is very important. (DO NOTconnectto shroud). STEP 2: lnsertthe blacktest lead intothe Common jack on the meter, and connect the opposite end of the lead to a charged reference electrode (% cell). STEP S: Remove protective cap from the porous plug at bottom end of electrode. Place porous plug end into native soil (remove grass if necessary) at four, locations around the tank (one on each side of the tank, and one at each end of the tank). If difficulty is encountered obtaining readings, moisten soil with water or dig Y/2 cell deeper into the soil. STEP 4: Record all four meter readings on an appropriate form. The least of all four readings should be a minimum of-0.850v or more negative. {Note: If any of the four readings are below (less negative) -0.850v then the tank is not fully protected}. Charging Reference Elecirode STEP 1: Unscrew and remove porous plug end of new reference electrode. Add delonized or distilled water to the copper sulfate crystals, filling electrode completely. The solution will turn blue in color and there should always be excess crystals at the bottom of the tube. DO NOT USE TAP WATER. STEP 2: Replace porous plug end of electrode and place in an upright position so that the porous plug end Is facing in the down position and let stand for 1 hour before use. This will allow the porous plug to become completely saturated before use. Cauflon: Do not allow electrode to contact oil, road salts, or othar Substances fhat may contaminate the solution by • absorption through porous plug. Do flat allow electrode to freeze. Distributed By: Loss of Pressure Freeze-up inside the regulator. t his will prevent the regulator from regulating properly. Regulator freeze -ups occur because. there Is excessive moisture in the gas. Freeze -ups can also occur in pigtails that are kinked or bent where free flow of the LP -Gas is restricted. These freeze -ups can occur when the moisture, gas flow and temperature combine to create a hazardous condition. Freeze -ups can occur at temperatures above 32'F Action Required: All LP -Gas should be checked for moisture content prior to delivery to consumers and proper amounts of anhydrous methanol added if the gas cannot be returned to the supplier. Any container suspected of having excessive moisture should be treated with the proper amount of methanol. Customer Safety Since- regulators are often used by consumers without previous knowledge of the hazards of LP -Gas, and the LP -Gas dealers are the only ones who have direct contact with the consumers, It is the dealer's responsibility to make sure that his customers are properly instructed in safety matters relating to their installation. At the very minimum, it is desirable that these customers: 1, Know the odor of LP -Gas and what to do in case they smell gas. Use the NPGA "Scratch 'n Sniff" leaflet. 2. Are instructed to never tamper with the system. 3. Know that when protective hoods are used to enclose regulators and/or valves, that these hoods must be closed, but not locked. Keep snow drifts from covering regulators. . Know the location of the cylinder or tank shut-off valve in emergencies. Underground installations , Special hazards can occur if regulators are not properly installed in J underground systems. Water, dirt, mud and insects can get into the regulator if the bonnet cap is not tightly In place and the vent is not protected with a proper vent tube, opening above any potential water level. Most problems occur because the waterproof dome on the buried storage tank does not extend above the ground level sufficiently to keep out water and mud. Refer to iVPGA No. 401. Regulator adjustment closure cap mustbe tight. Wle Grade round downward and to be Ice led a r vent a highvens! 9 to be lcpted above the highest away around housing dome. probable tvaterievel. This prevents water collecting and running into ors zndin_a /" 2 to 6inches around dame. u � minimum. I I 61nches minimum (t a inches minimum If subject to vehiculartrafic), Note: Water mark left in housing dome at level above regulator vent, or and of vent tube requires replacement of regulator. Then correct installation. General Warning All RegO Products are mechanical devices that will eventually become inoperative due to wear, contaminants, corrosion and aging of components made of materials such as metal and rubber. As a general recommendation,Regulators should be replaced In accordance with ail of the recommendations outlined in this safety warning. The recommended service life of a regulator is one of many factors -that must be considered in determining when to replace a regulator. The environment and conditions of use will determine the safe service life of these products. Periodic inspection and maintenance are essential. Because RegO Products have a long and proven record of quality and service, LP -Gas dealers may forget the hazards that can occur because a regulator is used beyond its safe service life. Life of a regulator is determined by the environment in which it 'lives." The LP -Gas dealer knows better than anyone what this environment is. NOTE: There is a developing trend in state legislation and in proposed national legislation to make the owners of products responsible for replacing products before they reach the end of their safe useful life. LP -Gas dealers should be aware of legislation which could affect them. F 7 '=� '�• 100 Rego Dr. Eton, PIC 27244 USA µv,-a.rerri:mduc!s.com =1 (336) 449-7707 First Stage Regulator with Relief valve and First Stage Piping 7-re regulator is truly the heart of an LP -Gas installation. It must .=-pensate for variations in tank pressure from as low as 8 PSlts 90 PSIG — and still deliver a steady flow of LP -Gas at 11" tuc. zonsuming appliances. The regulator must deliverthis pressure ,az pl a variable load from intermittent use of the appliances. :;sgh a single -stage system may perform adequately in many —.a�ialions, the use of a two -stage system offers the ultimate in pin- ;='t regulation. Two -stage regulation can result in a more profitable F-GM operation for the dealer resulting from less maintenance and installation callbacks — and there is no better time than now for ailing RegO Regulators in two -stage systems. 'f a, orm Appliance Pressure installation of a two -stage system — one high pressure regulator _: Tfe container to compensate for varied inlet pressures, and one =:a pressure regulator at the building to supply a constant delivery ;'mssure to the appliances — helps ensure maximum efficiency and trouble -free operation year-round. It is important to note that *5e pressure at the appliances can vary up to ?" w.c. using single- laae systems, two -stage systems keep pressure variations within ?" tv.c. New high -efficiency appliances require this closer pressure control for proper ignition and stable, efficient operation. In fact, one -rajor manufacturer requires the use of two -stage systems with their appliances. Reduced Freeze-ups/Service Calls Regulator freeze-up occurs when moisture in the gas condenses and i,eezes on cold surfaces of the regulator nozzle. The nozzle becomes chilled when high pressure gas expands across it into the regulator body. This chilling action is more severe in single -stage systems as gas expands from tank pressure to 11" w.c. through a single regulator nozzle. Size The System Correctly Prior to installing your two -stage system, be sure the system pipe and tubing Is properly sized. Proper sizing will help ensure constant delivery pressure to the appliances during fluctuating loads at all times. Just as Importarit, be sure the RegO Regulators you choose are capable of handling the desired load. This is another advantage of tyro -stage systems — they are capable of handling much more BTU'slhr. than single -stage systems. The RegO "LP -Gas b1111(:idill0+i'3 Manual" i f'-vid'J.. cc.wlplofi: and proper regulator selection. Two -stage systems can greatly reduce the possibility of teeze-ups and resulting service calls as the expansion of gas from tank pressure to 11" w.c. is divided into two steps, with less chilling effect at each regulator. In addition, after the gas exits the [first -stage regulator and enters the first -stage transmission line, it picks up heat from the line, further reducing the possibility of second -stage freeze-up. Service calls for pilot outages and electronic ignition system failures are also reduced as a result of more uniform appliance pressure from two -stage systems. Economy of Installation In a single -stage system, transmission line piping between the container and the appliances must be large enough to accommodate the required volume of gas at 11" iv.c. In contrast, the line between the first and second stage regulators in two -stage systems can be much smaller as it delivers gas at 10 PSIG to the second -stage regulator. Oven the savings In piping cost Will pay for the second regulator. As an additional benefit, single -stage systems can be easily converted to two -stage systems using existing supply lines when they prove inadequate to meet added loads. This is the least expensive and best method of correcting the problem. Allowance for Future Appliances A high degree of flexibility is offered in new installations of two - stage systems. Appliances can be added later to the present load — provided the high pressure regulator can handle the increase — by the addition of a second low pressure regulator. Since appliances can be regulated independently, demands from other parts of the installation will not affect their individual performances. Replace Pigtails if you are replacing an old regulator, remember to replace the copper pigtail. The old pigtail may contain corrosion which can restrict flow. In addition, corrosion may flake off and wedge between the regulator orifice and seat disc —.preventing proper lock -up. ` First Stage Regulator with Relief Valve and Pressure Second Stage Tap Regulator with Large Vent �. and Pressure Tap / ,— To Appliances/Furnace First Stage Piping With no first stage relief valve, a propane liquid may form here... 70° F 120 PSIG 40' F. 72 PSIG Resulting in sudden pressure surge due to flashing into vapor here! 80' F. 140 PSIG 50° F. 85 PSIG First stage relief can prevent liquid from forming in first stage piping 9o, F. 165 P51G 60, F. 102 PSIG during periods with no gas demand! I I Pressure at which liquid can form at various temperatures. Vapor Pressures of LP -Gases t9 a r W N P L a -40 -20 0 20 40 60 80 1CO 12D Temperature T. The Problem Many modem LP -Gas appliances are equipped with plio Vass ignition systems. Water heaters and older. appliances use pilot lights, but it has become a common practice for energy conscious homeowners to Shut-off the pilot when leaving home for extended periods of time. in each instance, there is no gas demand at all for extended periods. The Consequences If the first stage regulator falls to lock -up tight, usually as a result of a wpm seat disc or foreign material lodged between nozzle and seat disc, pressure % dl build-up in the first stage piping — possibly to a level that approaches tank pressure. Combining this with warm ambient temperatures and cool ground, propane liquid may form in the first stage piping. When gas demand resumes, this liquid may pass through the second nt,go mquietor into the appliances and furnace. NOT E •- the second stage regulator will not relieve the pressure in first stage piping. The rapid vaporization of the liquid may cause a rapid pressure surge that could seriously damage critical components of the appliance and furnace controls. I Afire or explosion could occur as a consequence. The Solution RegO LV4403 Series First Stage Regulators with Built -In Relief Valves reduce the possibility of this serious hazard in Iwo stage applications. The built -In relief valve is designed to vent as needed and reduce the possibility of flrsf stage piping pressureb from becoming high enough to form liquid. [9 Ra i DO Rego Dr. Scn, i<C 27244 USA vnv:r�.regcproducts.com +1 (33e) 449 7707 ^� Ideal for use as a first stage regulator on any domestic size ASME or ops4; DOT container in propane gas installations requiring up to 1,500,000,, BTU's per hour. The regulator is factory set to reduce container =L pressure to an intermediate pressure of approximately 10 PSIG. ' Maximum pour based on inlet pressure 20 PSIG higher than the regWalor selling and delivery pressure 2051 Imar then the regubterselting and dely ery pressure 205S Icwer than the acting. Provides accurate first stage regulation in hvo-stage bulk tank eflsh systems. Reduce tank pressure to an intermediate pressure of 5 to 10 !Ug PSIG. Also used to supply high pressure burners for applications like Industrial furnaces or boilers. Also incorporated In multiple cylinder Installations. Irl-- . F. 6 — 1-5 NPT ' ya" F. 10 5-10 NPT 5 1-5 10 5-10 Yes 2,500,000 POL /" 5 1-5 • F.NPT 10 5-10 When used for final stage pressure control, must either Incorporate Integral relief valve or separate relief valve should be speed In accordance wi6ti NFPAPamphlet 50. Maximum flow based on Inlet pressure 20 PSIG higher than the regulator setting and delivery pressure 20% lower than the selling. Designed to reduce first stage pressure of 5 to 20 PSIG down to rusL� burner pressure, normally 11' w.c. Ideal for medium commercial installations, multiple cylinder Installations and normal domestic �L loads. LV4403B4 Y" LV44031346 %" F NPT 8 1 0 PSI at 9" to 13" LY4403B46R' 10 PSIG Over Inlet 935,000 E.Vr,403666 3/0 F NPT Drill Inlet W.C. d tJ94D8PEtiR' Y.i= NPT 'aadonourt design "Maximum fiax based on 10 PSIG inte_l and 9' w.a derwerypressure. I WING37A I MM03Beaies Job Name Job Location Engineer Approval <+• ram- R � � � � The flexible connection between the gas supply and the gas inlet of a Generac° Stationary Outdoor Backup/Standby Generator. Features " Operating Temperature -40°F to 150OF (40°C to 65.6"C) o Operating Pressure MAX 0.5psL (3.45 kpa) ° Hydrostatic Burst Pressure MIN 250ps► (1725 kPa) o Flexible Tube Material Annealed 304 Stainless Steel ° Flare Nut Material Carbon Steel with Zinc Trivalent Chromate Plating ° Flare Adapter Material Carbon Steel with Zinc Trivalent Chromate Plating CSA Group Certificate of Cornpliance to Product Standards ANSI Z21.75/CSA 6.27 — Connectors for Outdoor Gas Appliances and Manufactured Homes Scope states "...intended for exterior use above ground for making non -rigid connections... between the gas supply and the gas inlet of an appliance for outdoor installation that is not frequently moved after installation." in addition section 1.5.4 states the connector is designed for occasional movement after installation. Repeated bend- ing, flexing or extreme vibration must be avoided. Normal opera- tion of a clothes dryer, rooftop HVAC unit or SIMILAR OUTDOOR APPLIANCE DOES NOT constitute extreme vibration or movement, ANSI Z21.24/CSA 6.10 — Connectors for Gas Appliances (&"cluding 60161 Series) CIA' c us Product Configurations All installations must completey On Ply tnth all Dornont manDlacturing company svarufngs and Instructions national, stair end local codes and all applicable ansl standards. ES-D-GAC Generator—Generac Contractor Approval Contractor's P.O. No, Representative SKID �� E air+• r � For use With Generac stationary outdoor backup/ standby generators, Series 30, 40 and 60 Applicable Codes ANSI Z223.1/tirFPA 54 National Fuel Gas Code Section 9.6 International Fuel Gas Code (IFGC) Section 411.1 13149.1— Natural Gas and Propane Installation Code (CSA Group) Section 6.21 Uniform Mechanical Code (UMC) Section' 1313.0 Uniform Plumbing Code (UPC) Section 1212.0 Additional Approvals Commonwealth of Massachusetts Board of State Examiners of Plumber and Gas Fitters Additional Vesting UI2200 2015; StafionaryEnaine Generator Assemblies Section 668 Vibration Test Damront product specMcstsns in D.s are apprmdmare and arz pv ?;ed{arrcis z,1:1a only rn,-pncisn mrasyc- imens,p;aasaeorra tDcmontrechric.-ISM0 mtherighttoChange ormodyproduotdesneoLor matadatwthutpriorn°5coard ya�ten,spedfcatians,wrra9 E4 W919ai ra 15W such changes awd ito6imU'ons on Dormant products PwArisly or satrsrquanty sold. tinter to the ovmsrs martial for vr rartyinloimalfan. ��' �� � ff`�° r;.'"�e• yea, [}� A tl MYTTa Brand 3 M40,tlr` LIV-41 CCMCMIN Of P3 P109 it 771ousand3 of 07U Sa ar Hour of DclusiPed Pavolol.rrrl Gas V116a Cc Pressure cl 11.0"1r�. MYC and rj Pressum Drop o� D:o in. "aye (based an.a 1.52 weclfic.grav, W RCIs) 187 125 99 84 74 67 56 50 45' 41 38 1073 720 571 484 425 383 325 286 257 235 218 1391 934 740 627 551 497 421 370 333 305 283 7983 7337 1054 893 786 708 600 528 475 435 403 3563 2391 1894 1605 1412 1272 1075 948 854 781 .723 4724 3247 2608 2232 1978 1792 1534 1359 1232 1133 1054 10063 6755 5357 4535 3989 3592 3044 2678 241.1 2207 2644 22 20 718 15 13 12 11 10 9 9 8 8 8 7 7 129 l73 102 86 76 68 63E 58 54 51 48 46 44 42 40 767 147 132 112 99 69 87 75 70 66 63 60 57 54 52 238 209 188 760 140 126 116 107 700 94 89 85 81 78 75 427 376 338 . 287 252 227 208 192 180 169 160 752 146 140 134 642 569 ` 516 441 391 354 326 303 285 269 255 244 233 224 216 1207 7061 956 810 712 642 587 544 '508" 478 453 431 411 394 379 2516BTUh=1 CFH Mcltlrl�uria Capaci111y of P5 A1ce In Thousands of 810 per How olLiquerlsd-Pstrolsum Gas z lih a Gas or89a"ing 012.0 psi and a Ressure PrbP 0H.0 psi (based on a 1.52specificgrovily gas) 11300 7586 6008 • 5092 4479 4033 3418 3007 2707 2478 2295 2144 2018 1775 1599 14652 9836 7790 6602 5807 5229 4432 3898 3510 3213 2975 2780 2617 2302 2073 20877 14014 11100 9408 8275 7451 6315 5555 5002 4578 4239 3962 3729 3280 2953 37514 2_5183 19946 .16905 14869 13389 1T348 9982 8988 8226 7618 7119 6700 5894 5307 43429 29848 23969 20515 18182 16474 14100, 12496 11322 1041.7 9691 9092 8589 7612 6897 105963 71731 56339 47750 42000 87820 32054' 28194 25388 23234 21517 20103 78926. 76647 74990 236 207 187 158 139 125 175 106 99 93 88 84 80 7 74- 1355 1192 1073 910 800 720 659 611 571 537 508 484 462 443 425 7757 1545 1391 1179 1037 934 855 792 740 696 659 627 599 574 551 2503 ' 2202 1983 1680 1478 1331 1218 1128 1054 , 992 939 893 853 818 786 4498 3956 3563 3019 2656 2391 2189 " 2027 1894 1783 1686 1605 1533 1469. 1472 5903 5232 4740 4057 3596 3258 2997 2758 2616 2471 2347 2239 2144 2060 1985 727D5 11175 IDD63 9529 7502 6756 6182 5725 5350 5036 4767 4535 4331 4150 3988 2516BTUh,1CFH iVlaMit7tuM C0pael,'y cf PE P7pe in Thousands of BTU per Fleur cf i.iqualied Pbtrofeum Gas ivllh a9 Gas Prsssurm of 70.0 PM drill a Pressure Drop of 1.0Iasi (based on a 1.5Zspecl7c aravily gas) -2476 7662 1316 1116 981 884 749 659 593 543. 603 '470 442 389 390 14234 0555 7568 6414 5642 5080 4306 3787 3470 3721 2890 2701 2542 2236 2014 18455 12388 9812 8316 7315 6587 5563 4970 4422 4047 3747 3602 3296 2899 2611 26296 17652 78981 17849 10423 9385 7954 6997 6300 5766 5340 4990 4697 4137 3720 47252 3172D 25723 21293 18729 16865 14294 12572 77321 10361 9595 8967 8440 7423 6685 53960 37087 29782 25489 22591 20469 17619 :15527 14068 12943 12041 11297 10671 9458 8569 133476 89601 70967 60148 52905 47640. 40376 35574 31980 29267 27104 25329 23840 20970 78882" 297 261 235 199 175 158 144 134 725 118' 111 706 707 97 93 1707 1501 1352 1146 1008 907 830 769 719 676 640 609 582 557 636 2218 1946 1753 1485 1306 1176 1077 997 932 877 830 790 754 723 695 3153 2773 2497 2716 1862 7676 1534 7421 1328 7250 7183 7125 1075 7030 990 5665 4983 4487 . 3803 3345 3012 2757 2553 2386 2246 2126 2022 1931 1851 7779 7334 6500 5890 5047 4463 4048 3724 3465 3251 3071 2916 2782 2664 2560 2466 16004 14077 12676 10743 9449 8609 7787 7212 6739 6343 6006 6112 5455 5227 5024 2516BTUh=7 CFH� Ph: 1,800,662.0208 o Fax: 615,3251*94707 o bleb: tww%gasiife.com