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HomeMy WebLinkAboutProduct Review® ®e0 o MO hiNO�_Y. UB• ; r• Ranked Nl by PERC in ovarJI performance F LL , DU�?Rh,D"QneMu�rer duper. urab Tboo-oat i , Zi�i Oreb, ri o�rA o�iegrourid7 POWLi!�l�aQneCure?n"i vicorcna sy`stiempropert�eszinc�utle Zink nct�epox� p`iimer - e d'orrrerin black, p ftg;, ;.c' oi�� i Me-) •> s4gr, ffr�dt W14tC;ptertac01 gal�van2edlstee� ��•�up�rior7cd6Gosibn)an:d�e�ge�dtot'ecf�6n} . " •} Paf��ii;'pendingjtot'mcil`atedprimeGand'fopcoai;' c Duaf service options for above: or. underground applications • Option 91: Beady -to -bury - red- oxide. durable powder coating with black • polyethylene.AGUG dome' _� v , I • Option 42: Aboveground option with steel 8" AGUG dome r j • All valves,and float gauges are centered under dome • � ' • r' Fabricated to the latest;A.S.M.E, Code, Section V[II; Division 1 i • Registered with the Nadoiial Boarc[' Y • 1171licluid level'outagevalve orifrcereducesrefueling•emissionsI T ._,w Vacuum pre-purged.to save t1 ee,,. money and product I I Applicable federdr stater orlodalr-egulaffons may contain specificrequiremenls for NaTA �iN R i protective coafingg and cathddic profec[idn: Tfie purchaser arid'irisfallerare, responsible ring• . . -. fdredmpliance with all fed'e'raf state; fdc'!Aand NFPA•ihdustryrdgurafidfis: Cathodic protedtTdntis,required and doating)mustbedon tinuous an'd tAbIferrdpeed and must j comply with an focal, state ornafional'dbde: F TRINITY Containing Our Worlds EnergyT" Q I 1 IL W rOUTSIDE 4_ Q IL � > 0 DIAMETER o CL 0 0 0 LEG WIDTH General Specifications Conforms to the latest edition of the ASME code for Pressure Vessels, Section VIII, Division 1. Complies with NFPA 58. Rated at 250 psig from -200 F. to 125' F. Ali tanks may be evacuated to a full (14.7 psi) vacuum. Vessel Finish: Coated with epoxy red powder. ( Tanks coated with the epoxy powder must be buried). For Aboveground use, tanks may be coated with 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. M MDA1 I I C:Kl 'Tu -- WITHDRAWAL VALVE NOTICE FLOAT `\� ANODE GAUGE (5 CONNECTION ' ® ' FILLER ' '_VALVE I � � O 1 1 , ,� 9 SERVICE / NAME MULTIVALVE PLATE �� RELIEF VALVE FITTINGS LAYOUT UNDER DOME AGUG VESSEL DIMENSIONAL INFORMATION All vessels dimensions are approximate WATER OUTSIDE HEAD OVERALL OVERALL LEG LEG WEIGHT QUANTITY CAPACITY DIAMETER TYPE LENGTH I HEIGHT I WIDTH SPACING FULL PER I LOAD STACK 120 wg. 24" Ellip 5' - 5 13/16" 3' - 0" 10 1/8" . 3' - 0" 245 lbs. 96 12 454.2 L 609.6 mm 1671.3mm 911.4 mm 257.2 mm 914.4 mm 111.1 kg. 250 wg. 31.5" Hem! 7'- 2 1/211 3' - 7 1/2" 12 3/4" 3' - 6" 472 lbs. 63 9 946.3 L 800.1 mm 2197.1 mm 1104.9 mm 323.9 mm 1066.8 mm 214.1 kg. 320 wg. 31.5" Hemi 8' -11 3/4" 3' - 7 1/2" 12 3/4" 4' - 0 1/4" 588 lbs. 45 9 1211.2 L 800.1 mm 2736.9 mm 1104.9 mm 323.9 mm 1225.6 mm 266.7 kg. 500 wg. 37.42' Hem! 9' -10" 4' -1 7/16" 15" 5' - 0" 871 lbs. 30 6 1892.5 L- 950.5 mm 2997.2 mm -1255:7 mm -381.0 mm 1524.0 mm 395.1 kg 1000 wg. 40.96" Hem! 15' -10 13/16" 4' - 4 5/16" 16 1/4" 9' - 0" 1729 lbs. 15 5 3785.0 L 1040.4 mm 4846.E mrn 1344.E mm 412.8 mm 2743.2 mm 784.3 kg Rev: Jan. 27, 2016 Why Wanks Corrode Underground steel tanks corrode due to an electrochemical reaction between the tank and the surrounding soil. The process of corrosion 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 flows from the soil to the tank, no corrosion occurs. The progress of corrosion is determined by the amount of current flowing between the anode and the cathode and whether the locations of the anode/ cathode remain constant overtime. Corrosion rates are generally higher in wet soil environments since the conductivity of the soil promotes the flow of DC current in the corrosion circuit. Corrosion generally exhibits 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 suraface or soil variations such as rocks, salts, fertilizer, moisture concentration, oxygen concentration, etc. Preventing Corrosion Protecting underground tanks from corrosion is easily achieved by the use of two commonly applied protection methods: external coating and cathodic protection. These two methods are complementary and should be used in conjunction with the other. An effective external protective coating insulates the steel from the soil environment, thus preventing the flow of corrosion currentfrom the anode to the cathode. An effective external coating can protect over99% of the tank surface area. However, no coating is perfect. Damage from construction or soil stresses create tiny defects, which may result in accelerated corrosion at the defect. Cathodic protection prevents corrosion at those defects by applying DC current from an external source, forcing the tank to become cathode. Application of sufficient DC current to the tank will prevent any 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. How Sacrificial Cathodic Protection Works Sacrificial systems work by creating a galvanic connection between two 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-1.80V. By connecting the two metals together, the difference of 1 to 1.25V volts results in current flow to the tank that overcomes the natural corrosion cells that exist on the tank. 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 two primary alloys are designed as H-1 (or AZ63) 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 412 TW insulated wire is attached to the anodes. Anodes are then backfilled in a mixture of gypsum, bentonite, 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 quantity recommendations forvarious sizetanks based on conservative design assumptions. This chart covers soil conditions up to 10,000 ohm -centimeter resistivity. Resistivities higher than 10,000 ohm -centimeter generally represent very dry soils. 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 50' in length, the tank 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 couple that will accelerate corrosion of the steel tank when directly connected to copper piping. Generally, copper piping does not require cathodic protection. J silsl `. Sand, Gravel, Rocky Soil Type ' ; zd` ;5 Areas Tank Cap. 5000 to 10000 ohm -cm #Size 4fw_-...... • rj sty" i. alloy` 1.. Size Qty. Alloy (9a1) 120 f; ;9 v ` ti1S'..,.H"1 9# 1 H-1 150 q1;'' 9# 1 H-1 250 ;;4 1 i ` H`1i; 9# 2 H-1 3259#°� j;�i; H`,1.: 9# 2 H-1 500 f;:g1"S Ak -J 9# 2 H-1 1000 1500 2000 9# "Based on 90% effective external coating, 2 malft2 current density, and SO- yearAnode life. Anode Installation. 1. Determine size and quantity 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. 3. When multiple anodes are installed, space them evenly around the tank. See examples below. 7 anode 2 anodes 4 anodes C:Jrj C c O O O C 4.Anodes are shipped in either cardboard boxes or multi -wall paper sacks. 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 over to 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 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 testing of the tank can include measurement of anode output and verification of performance. 10.Verify performance of the anode using an appropriate test procedure. MJechanlcel Conneoflon Under Dome Cathodic Pro$ecfuon Testing Procedure Equipment deeded: Digital Voltmeter, Red Test Lead Min.12' Long & Black Lead Mina 2' Long, Reference Electrode (Copper/Copper Sulphate Half -Cell) 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 fill pipe multivalve. A good solid connection is very important. (DO NOT connect to shroud). STEP2: Insertthe blacktest lead into the Common jack on the meter, and connect the opposite and of the lead to a charged reference electrode (%2 cell). STEP 3: 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 %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 Deference Electrode STEP 1: Unscrew and remove porous plug end of new reference electrode. Add .deionized 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 and 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. Caution: Do not allow electrode to contact oil, road salts, or other substances that may contaminate the solution by absorption through porous plod. Do not allow electrode to freeze. Distributed By: Ideal for use as a first stage regulator on any domestic size ASME or DOT container in propane gas installations requiring up to 1,500,000 LISTED BTU's per hour. The regulator is factory set to reduce container pressure to an intermediate pressure of approximately 10 PSIG. • Compact design can be connected to a service valve using either a POL adapter or a RegO product pigtail. • Large threaded Y.' F.NPT bonnet vent can easily be piped -away underground installations without the need of glue kits or extra adapters. • Non Adjustable " Large flow orifice resists freeze ups due to water concentration in LPG vapor. • Design provides for good flow regulation at both high and low container pressures. • Built in relief valve and travel stop comply with NFPA 58 over pressure requirements. " Incorporates %a" F NPT downstream pressure tap for an easy inline check of the regulator's delivery pressure. • Molded diaphragm provides an o-ring type seal between the body and bonnet. Body and bonnet are assembled in the USA using the unique, patented RegUlok seal system. Fully painted in brilliant red for complete corrosion protection. • Mounting bracket available as an accessory: part number 2302-31. PUNO-elff'.1 AS Body............................................................................................Zinc Bonnet......................................................................................... Zino Spring........................................................................................ Steel Seat Disc.................................................................Resilient Rubber Diaphragm...........................Integrated Fabric and Synthetic Rubber a ILVM03TR r -,� � - Tom.. r � i � �• •{J 3.56" FLOW PROPANE LV3403TRV9 ''Y,"• F NPT I %" F NPT I 7/3z" I 10 PSIG Over9:0Outlet — '- 1,5D0,000 I Maximum flow based on inlet pressure 20 PSIG higher than the regulator setting and delivery pressure 20% lower than the regulator setting and delivery pressure 20 % lower than the setting. It 14 ZOO Ed 0. 100 Rego Dr. Eton, NC 27244 USA www.ragoprDducts.com +1 (336) 449-7707 Designed to .reduce first stage pressure of 5 to 20 PSIG down to burner pressure, normally 11" w.c. Ideal for medium 'commercial installations, vapor meter installations and normal domestic loads. yeah s �'? • 90 degree right angle inlet to outer connection for meter or standard installations. • Large vent helps to prevent blockage and has'/<" F. NPT for vent piping. With 15 PSIG inlet pressure, regulator is designed to not pass more than 2 PSIG with the seat disc removed. • Replaceable valve orifice and valve seat. • Straight line valve closure reduces wear on seat disc • Unique bonnet vent profile minimizes vent freeze over when properly installed. • Large molded diaphragm is extra sensitive to pressure changes. • Built in pressure tap has plugged %' F. NPT outlet. Plug can be removed with a 3/16" hex allen wrench. • Select Brown Finish Can mount directly to vapor meter. It is also suitable for mounting directly to the house piping. It will retrofit into existing installations that are currently using a 90 degree, right angle regulator. t it tfM.T-,FA— Body........................................................................... Die Cast Zinc Bonnet........................................................................ Die Cast Zinc. Nozzle Orifice......................................................................... Brass Spring...................................................................................... Steel Valve Seat Disc ..................................................... Resilient Rubber Diaphragm ......................... Integrated Fabric and Synthetic Rubber III 51/,.. 1 Z E 2.2 °11 U L CFli/nr. I BTUthr. L M N wg/ftr ounlbng8fracket 100 15D 200 250 3W 350 4DO 450 50D 250,OD0 5DD,000 750,000 1,000,DDO 1,250,ODD LV4403B66RA 11" w.c. at 10 — - ---.— -- — — -- ` — -- — — L�l441}3B66F2AB"' F. NPT '/<" F. NPT 3/16" PSIG Inlet 9" to 13" w.c. Over Inlet 1,000,000 f - - - ]-- - - I I Maximum flow is based on 10 PSIG inlet and 9' w.c. derivery pressure. '• Mounting Bracket Included. 100 Rego Dr. Elan, NC 27244 USA www.rBgDproducts.com +1 (336) 449-7707 M CI /- A21 Job Name _ Job Location Engineer Approval _ UM Flexible Fuel Lines The flexible connection between the gas supply and the gas inlet of a Generac° Stationary Outdoor Backup/Standby Generator Features o Operating Temperature -40°F to 150°F (-40°C to 65.6°C) o Operating Pressure MAX 0.5psi (3.45 kPa) o Hydrostatic Burst Pressure MIN 250psi (1725 kPa) o Flexible Tube Material Annealed 304 Stainless Steel o Flare Nut Material Carbon Steel with Zinc Trivalent Chromate Plating o Flare Adapter Material Carbon Steel with Zinc Trivalent Chromate Plating v PVC Dip Coating Gray Heavy Duty, Antimicrobial, UV Stabilizer CSA Group Certificate of Compliance to Product Standards ANSI 721.75/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 bending, flexing or extreme vibration must be avoided. Normal operation 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 ��° (Excluding 60/61 Series) c us Product Configurations ES-D-GAC_Gen erac—InstallSmart Contractor Approval Contractor's P.O. No Representative SKU For use with Generac'!stationary outdoor backup/ standby generators. Applicable Codes ANSI Z223.1/NFPA 54 National Fuel Gas Code Section 9.6 International Fuel Gas Code (IFGC) Section 411.1 B149.1 — 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 Plumbers and Gas Fitters Additional Testing UL2200-2015: Stationary Engine Generator Assemblies Section 66B Vibration Test. DDnnnnt produet specifications in U.S. customary units and metric are appm)dmate and are provided for reference only. For precise D64MOnt' measurements, please Contact DormontTechniral Service. Donnont reserves the right to change or modify product design, construction, specifications, or materials without prior notice and without incurring any obligation to make such changes and modifications on Dormant products previously or subsequently sold. Refer to the owner's manual for warranty information. A WAS Brand Minimum Flow Capacity at Specified Pressure Drop Straight Length BTU/hr. NATURAL GAS, 0.64 SG, 1000 BTU/cu.ft. r r Generac° Part Number Dormont' Part Number SERIES Nominal ID in Nominal Lenght in 0.50 in 0.75 in 1.00 in 1.25In 1.5D in 1.75 in 2.00 in 10000009793 CAN41-4141-24GEN 41 1/4 24 290,900 356,278 411,395 459,953 503,854 1 544,224 581,800 10000009776 CAN41-4141-48GEN 41 3/4 48 217,000 265,770 306,884 343,107 375,855 405,970 434,000 10000009777 CAN41-4141-72GEN 41 3/4 72 173,900 212,983 254,932 247,960 301,204 325,337 347,800 10000000498 GAN51-5151-24GEN 51 1 24 581,800 712,557 822,789 919,907 1,007,707 1,088,448 1,163,600 10000000499 CAN51-5151-48GEN 51 1 48 442,700 542,195 626,072 699,970 766,779 828,216 885,400 10000000500 CAN51-5151-72GEN' 51 1 72 347,800 425,966 491,863 549,920 602,407 650,674 695,600 Straight Length BTU/hr. LP GAS, 1.55 SG, 2500 BTU/cu.ft. r r Generac° Part Number Dormont* Part Number SERIES Nominal ID in Nominal Lenght In 0.50 In 0.75 In 1.00In 1.25In 1.50 In 1.75In 2.00 in 10000009793 CAN41-4141-24GEN 41 3/4 24 465,400 569,996 658,175 735,862 806,096 870,684 1 930,800 10000009776 CAN41-4141-48GEN 41 % 48 344,000 421,312 486,489 543,912 595,825 6431565 6881000 10000009777 CAN41-4141-72GEN 41 3/ 72 278,240 340,773 393,491 439,936 481,926 520,539 556,480 10000000498 CAN51-5151-24GEN 51 1 24 930,880 1,140,091 1,316,463 1,471,851 1,612,331 1,741,517 1,851,760 10000000499 CAN51-5151-48GEN 51 1 48 708,320 867,511 1,001,716 1,119,952 1,226,846 1,325,145 1,416,640 10000000500 CAN51-5151-72GEN 51 1 72 556,480 681,546 786,982 879,872 963,852 1,041,079 1,112,960 Generac part number 10000000498 (Dormont part number CAN51-5151-24GEN) can supply a minimum of 581,800 BTU/hr.of natural gas Q 0.50 in. water column pressure drop to the generator. All installations must completely comply with all Dormont® manufacturing company warnings and instructions, national, state and local codes and all applicable ANSI standards. 0 A WATTS Brand USA: T: (800) 367-666B o R (724) 733-4808 a Dormontcom Canada: T: (905) 332-409D a F: (905) 332-7068 o Dormont.ca Latin America: T. (52) 81-1001-8600 o F: (52) 81-8000-7091 - Dormont.com ES-D-GAC-Generac InStaIISmart 1703 © 2016 Dormont i Maximum Capacity of PE Pipe in Thousands of BTU per Hour of Liquefied Petroleum Gas with a Gas Pressured of . id . WC specific Pre u j Drop of 0.5 in. C 187 125 99 84 74 67 �-- 56 325 50 286 45 257 41 235 218 29 4 1 1073 720 571 484 425 383 421 370 333 305 283 264 49 249 219 197 1391 934 740 1054 627 893 551 786 .497 708 600 528 475 435 403 376 354 636 311 560 280 504 1983 3563 1331 2391 1894 1605 1412 1272 1078 948 854 1232 781 1133 723 1054 676 989 934 828 750 4724 3247 2608 2232 1978 1792 1534 3044�eb�� 1359 211 2207 2044 1910 1797 1581 1424 10063 6755 5351 4535 3989 3592 10 9 9 8 8 8 7 7 22 129 20 113 18 15 102 86 13 12 11 76 68 63 58 64 51 48 63 46 60 44 57 42 54 40 52 167 147 132 112 99 89 81 75 70 .66 140 126 116 107 100 94 89 85 81 78 75 238 427 209 376 188 160 338 287 252 227 208 192 180 169 160 269 255 152 244 146 233 140 224 134 216 642 569 516 441 810 391 354 326 303 286 712 642 587 544 508 478 453 431 471 1207 1061 956 2516BTUh=1CFH BTU er Hour of Liquefied in pSiPetroleum Gas Cawithia Maximum Gas P esssureT f 20 psi and a Pressure Drop 1 0 (based on a 1.52 specific grovity gas) 1�� l� 3j9 1- 4- 8 77�9 702 595 3418 523 3007 471 2707 437 2478 �vv 2295 3ic 2144 JOI 2018 �+�+� 1775 - 1599 11300 7586 6008 - 5092 4479 5807 4033 5229 4432 3898 3510 '3213 2975 2780 2617 2302 2073 14652 20877 9835 14014 7790 11100 6602 9408 8276 7461 6315 5555 5002 4570 4239 3962 3729 6700 3280 5894 2953 6307 37514 25183 • 19946 16905 14869 13389 11348 9982 12496 8988 11322 B226 10417 7618 9691 7119 9092 8589 7612 6897. 43429 29848 23969 20515 18182 16474 37820 14100 32054 28194 25388 23234 21517 20108 18926 16647 14990 105963 71131 66339 47750 42000 115 106 99 93 88 84 80 77 74 236 207 187 158 139 125 910 800 720 659 611 571 537 508 484 462 443 425 1355 1757 1192 1545 1073 1391 1179 1037 934 855 792 740 696 659. 627 599 853 874 818 551 786 2503 2202 1983 1680 1478 1331 1218 1128 1054 992 939 2027 1894 1783 1688 893 1605 1533 1469. 1412 4498 3956 3563 3019 2656 2391' 2189 4057 3596 3258 2997 2788 2616 2471 2347 2239 2144 2060 1985 5903 12705 5232 11175 4740 10063 8529 7502 6755 6182 5725 5360 5036 4767 4535 43312514150 98 l Maximum CapacityPE s of a Hour of Liquefied Gas a Gof as Pressure of 10 0 psi and Pressure Drop fr 1 0 (based on a 1.59 specific gravity gas) 2476 1662 1316 1116 981 884 749 659 593 543 503 470 2701 442 2542 389 2236 3 2014 14234 9555 7568 6414 5642 5080 4306 5583 3787 4910 3410 4422 3121 4047 2890' 3747 3502 3296 2899 2611 18455 26296 12388 17652 9812 13981 8316 11849 7315 10423 6587 9385 7954 6997 6300 5766 5340 4990 4697, 4131 3720 47252 31720 25123 21293 18729 16865 14294 12572 11321 10361 12943 9595 12041 8967 11297 8440 10671 7423 9458 6685 8569 53960 37087 29782 25489 22591 20469 47640 17519 40376 15527 35514 14068 31980 29267 27104 25329 23840 20970 18882- 133476 89601 70967 60148 52905 / /1 11 11 .11 • 11 - • •ON Nis :/1 A •11 111 1/ 11 11 11 1� 1/ 297 261 235 199 175 158 144 134 125 118 111 640 106 609 101 582 97 557 93 536 1707 1501 1352 1146 1008 907 830 769 997 719 932 676 877 830 790 754 723 695 2213 1946 1753 2497 1485 2116 1306 1862 1176 1676 1077 1534 1421 -1328 1250 1183 1125 1075 1030 990 3153 5665 2773 4983 4487 3803 3345 3012 -2757 2553 2386 2246 2126 2916 2022 2782 1931 2664 1851 2560 1779 2466 7334 6500 5890 5041 4468 4048 3724 7787 3465 7212 3251 6739 3071 6343 6005 5712 64552515227 024 16004 14077 12676 10743 9449 8509 1 Ph: 1.800.662.0208 a Fax: 615.325.9407 a Web: www.gastite.corn