Loading...
HomeMy WebLinkAboutFuel Specs_ - L 1 t 1 m=uphuralTucaa't4 Y ,, .�jr-�•,�{�l[� /f�S {�* {/r•}p�l •__K.. £ (5- xPd)Ui(DIJi une , rd YI,t.wiIEYL�Lsys.LG i d!i'dfr C �Jetfies �r inieft�pQxy Pmer_, - =k $" �Qirl;£ Cil bciGL�It�[� O rhl a SlipeoduCaile TC�[l Ayes tee tapcoft ��lvan�ed s _ j Super�ar cQCroSfot) agdEec�t�e m ec�ran rl _ f?atenf pending facmul t d prEmeriff c�topcaa } { 3 F 4t . Rual service: optrons for above oC undergroundf appficatW!§, _ ." Qptror i#1 Ready to-buryfred ozrdedural?le�powder cpattng witii,blaCRr •, polyeth &A_ie AGUGicfome" • _Optroi�2 Aboveground optionwrth steel 8' AG(J Gi dome •Alf valves and float gauges are centered underdome �'� ��4 � ®�Fabncatedto ih_ef'atesiA"SFM EGode„Sectian��Vlil Divis�on-1' 5` u RegisteredViihithe Nab board •` #72rirgriiclFlevelFoutageva(ve artf ce reduces refueling emrssigns„ TRINIT Y • Vacuumfpre paved to sa�re_fime; money�and product- � rApplrcable /ederaJA state, or local regula.rons m`ay contain specrequ�rement� For } protertrve coafrngsrand cathodre protec ton The purchaser and installerarer espdrsrble s r. _. for'complranceTwrtli a`fl�rederal; state, lo`eand?VFP�t,rnditstry regUlatrons`_Cafhodic:r • s • • pr®tact on rs requrred and co�irng rrjustbegconanuousand�lrnmfzr_rup%d"and must coiijp(�wrfhran*Iocalsfa`tenreiafional,code� _ t Containing OLk ftrld`S Enerayy' Q = i I 0 Z = LU (' J 0 -< 0 OUTSIDE a DIAMETER o o LEG WIDTH general Specificef`ions Conforms to the latest edition of the ASME code for Pressute Vessels, Section Vill, Division t. Complies with NFPA R. Rated at 250 psig from -20' F. to 1-250 F. All tanks may be evacuated to a full (14.7 psi) vacuum. Vessel 51riish: Coated with epoxy red powder. (Tanks coated with fhe epoxy powder must be buried). For Aboveground use, tanks may be coated with TGIC powder, _ Appliicabl-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. -- WITHDRAWAL VALVE FLOAT NtfIICSE ANODE GAUGEANODE FILLER ,-VALVE 0 SERVICE! NAVtE 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 HEIGHT WIDTH SPACING FULL PER LOAD STACK 120 wg. 24" Ellip 5' - 5 13/16" 3' - 0" 10 1/8" 3' - 0" 245 lbs. 96 12 454.2 L 609.8 mm 1671.3mm 911.4 mm 257.2 mm 914.4 mm 111.1 kg. 250wg. 31.5" Hem! 7'- 2 112" 3' - 7 1/2" 12 3/4" 3' - 6" 472 lbs. 63 9 9466.3 L 8D0.1 mm 2197.1 mm 1104.9 mm 323.9 mm 1065,8 mm 214.1 kg. 320 wg. 31.5" Hem! 8' -11 3/4" T - 7 1/2" 12 314" 4' - 0 1/4" 588 tbs. 45 9 1211.2 L 800.1 MIn 273-13 m>n 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"h871lbs. 30 6 1892c5 L . 95D,5 mm -2997.2 mm 1255.7 mm 381.0 mm 1524.0 mm kg _40.96" Hemi 15' - 10 13I16" 4' - 4 5/16" 16 114" 9'- 0"lbs. 15 537K0 L 104D:4 mm 4841344.Emm 412.8 mm 2743.2 rnm kg Rev; Jan. 27, 2016 WhY Tanks Corrode Underground steel tanks corrode due to an electrochcrrtical 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 flout/ 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 currentflaws from the soil to the tank, no corrosion occurs. T he 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 pining attack, pit locations may Rspit 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 IWO 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 current from the anode to the cathode. An effective extiarnalcoatfngcan Protect over 99%ofthe tank surface area. However, no coating is perfect Damage from construction or soil stresses create tidy 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 catitode. Application of sufficient DC current to the tank will prevent any corrosion front 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 electricai rou ti 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 1.25Vvolts results in current flawto. the tank that overcomes the natural corrosion cells that exist on the tank. With this current available to the tank, no corrosion occurs. Magnesium Modes 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 iotential 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 TW insulated wire is attached to the anodes. Anodes are then backfilied 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 sizeand quantity recommendations forvarioussizetanks 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. g n s is cntical for the cath— odic rotection s ystem's --- effectiveness--- -- - p l If another metallic material such as copper is used'#or service piping, - -- - - -- - -- - - - -- - -- - ---- - - the Pipe should be electrically isolated from the tank at the fill pipe - -- — connection. Copperandsteeicreateagalvaniccouple that will accelerate dw sairiffaial Cathodic Protection lAltrrlrs corrosion of the steel tank when directly connected to copper i in Sacrificial systems work by creating a galvanic connection between two Generally, copper piping does not require cathodic protection. p p g mechantal C al>aV0. tli i�ab Domes Cathridic Ptal'ection Te,31fl&o Procedure Equipment Headed: Digital Voltmeter, Red Test Lead Min. 12' Long & Black Lead Min. 2' Long, Reference Electrode (Copper/Copper Sulphate Half -Cell) MP 1: Using a dlgital 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). STEP 2: Insertthe black test lead into the Codlmon jack on the meter, and connect the apposite end of the lead to a charged reference electrode (1l cell). S 3 EP 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 1�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). Chrargiirig Reference Electrode STEP 1: UnsareW and remove porous plug end of new reference electrode. Add deionized or distilled water to the copper sulfate crystals, filling electrode completely. The solution v✓ill 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. Caution: Do not allow electrode to contact ell, road salts, or other substances that may contaminate the solutien by absorption through parous plug. ©o net allow electrode to freeze. Soil Type�-0 �utls,ja ay e Sa ad, Gravel, Rocky Areas Tank Cap.: odeg_'m ! 5QQD to a-DQDD ❑hm-cn (9a1,) ]zef D Afla size My. Alloy 120`' 9# 1 H-1 150 '- 7- W 1 H-1 250 9# 2 H 1 9# 5QD 1 114. 1000a 15ao -_ fiF1_, 9# A H-1 2oDa s H-1 Based on 90% effective extemal coating, 2 malft2 current density, and 30- 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 9 � C� (�' 4.Anodes are shipped in either cardboard boxes or multi -wall papersacks. 'Remove outer container and burythe 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. S.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.. & 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. Ideal for use as a first stage regulator on any domestic size ASM;= 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 PStG. Compact design can be connected to a service valve using either a POL adapter or a RegO product pigtail. Large threaded %" 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 W F.NPT downstream pressure tap for an easy inline.check of the reguiator'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 Reglllok seal system. Fully painted In brilliant red,for complete corrosion protection. • Mounting bracket available as an accessory: part number 2302-31. Body............................................................................................Zinc Bonnet.........................................................................................Zinc spring................................................................. ...... Steel ................. Seat Disc ........................... ....... .......... ...... -............. Resilient Rubber Diaphragm ...... --- ...............Integrated Fabric and Synthetic Rubber I.UM03TE 3.56' FLOW FROFAKE LV3403TRet - LV3403TRV9 %" F.NPT 1" RN Tw 10 PSIS Over Ou 9 oD. 1,500r000 Maximum flow based on inlet pressure 20 PSIG hlgher than the regulator setting and delivery pressure 20% lower than the regulalorsetting and delivery pressure 20%.lower Than the satOng. A14- _- 34 t?% 1f30 Rego or. Elon, NG 27244 USA —gv.regoproducts.com +1 (336) 449-7707 - Designed to reduce first stage pressure of 5 to 20 PSIG dawn to burner pressure, normally 1'I" w.c. Ideal for .medium commercial installations, vapor meter installations and normal domestic loads, go degree right angle inlet to outer connection for metet or standard installations. Large vent helps to prevent blockage and has Ile' 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 'dlaphra'gm is extra sensitive to pressure changes. • Built in pressure tap has plugged %F NPT outlet, Plug can be removed with a 3116' hex ailen 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. Body..................................................................... Die Cast Zinc Bonnet........................................................................ Die Cast Zinc Nozzle Orifice .......................... :........................... .............. ..... Brass Spring...................................................................................... Steel Valv.'e Seat Disc ............. ................. ............. ........ Resilient Rubber Diaphragm ......................... Integrated Fabric and Synthetic Rubber .� A ,ssuw or�R �yyq'Zi 7� G 9�yX G. O �vl 1 0 1*1 90 h �:uf.)3'ia�mai9�gias= s9cag LV440386sRA — — _-- -'/<" NPT- _ - '/< F NPT 3/16" 11" W.C. at 10 9" l0 13" w.c_ Over inlet 1,OD0,000 LvaaosBssrlaB� F PSIG inlet -- — — — T4aximumfow Is based on 10 Psir, inlet and T w.c. delivery pressure. " Mounting Bracket included. 100 Rego Dr, Elon, NC 27244 C75A vnvw:regopmducLs.corn *; (336) 4:9-7707 � off--'r�-s. 5Y23 Job Name Job Location Engineer Approval .,Gene Flexible Fuel s 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 150°F (40°C to 65.6°C) a Operating Pressure MAX 0.5psi (3.45 kPa) a Hydrostatic Burst Pressure MIN 250psi (-f725 kPa) a Flexible Tube Material Annealed 304 Stainless Steel m Flare Nut Material Carbon Steel with Zinc Trivalent Chromate Plating a Flare Adapter Material Carbon Steel with Zinc Trvalent Chromate Plating a PVC -Dip Coating Gray Heavy Duty, Antimicrobial, UV Stabilizer GSA Croup Ceriificat3e of Compliance to Product ;standards ANSI 721.75/CSA 6.27 — Connectors for Out -door '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) o us Product Configurations ES-D-GAG Generac_lneiallSmart CointractoT Approval Contractor's P.O. No. Representative SKU For use with Generac stationary outdoor backup/ standby generators. Applicable Codes ANSI 2228.1/NFPA 54 National Fuel Gas Code Section 9.6 International Fuel Gas Code (IFGC) Section 411.1. 3149.1 — 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 Additiorial Approvals Commonwealth of Massachusetts Board of State Examiners of Plumbers and Gas Fitters Additional Testing UL2200-2015: Stationary Engine Generator Assemblies Seotion 66B Vibration Test. f Domtottt Rmductspecif cations in U.S. Customary uniisand metres are appmldmate and are provided for reference mly. For precise meastremeris, please contact Dormant Technical Service. Dormant reserves the right io change or modify pwdud design, consb5lion, - -- Df-M-- on specffrcatlons, a materials wtihout prior notice and x dhout incurring any obligation to make such changes and mWications on Donnont Product previously or subsequently sold. Refer to the awaer's manual for w�rranty Information. A WATTS Brand Minimum Flow Capacity at Specified Pressure D(rop Straight Length BTU/hr. NATURAL GAS, 0.64 SG, 1000 BTUku.ft. Genelto Pad Number DonnoW Part Number SERIES Hammel ID in Nominal Lenghi in 0 50In 0.75 In 1.00 In 1-251n 1.5D in 1.75 in 2.00 in 1DODOOD9793 CAN414141-24GEN 41 3/ 24 290,900 { 356,278 411395 4501,953 503,854 544,224 581,800 1000OOD9.775 CAN41-4141-48GEN 41 3/4 48 217,000 265,779 306,884 343,107 375,855 405,970 434,000 TOOOOD09777 CAN41-4141-72GE14 41 3/ 72 173,900 212,983 254,932 247,960 301,2D4 325,337 347,800 10000900498 CAN51-5151-24GEN 51 1 24 581,800 712,557 822,789 919,907 1,007,707 1,088,448 1,163,600 iDD00D00499 { CAN51-5151-48GEN 51 1 48 442,700 542,195 626,072 699,970 766,779 828,216 885,4DO v0d0da500 CAN51-5151-72GEN 51 1 72 347,800 425,966 491,863 549,920 602,407 650,574 695,600 Straight Length BTU/hr. LP GAS, 1.55 SG, 2500 BTU/cu t. Genme Part Number Dormont° Part Number SERIESNominal ID in Nomibal Lenpbt in 0.0 in 0.75 in - 1.00 in 1.251n i.501n 1.75 in 2 00 in 10000ODD793 CAN41-4141-24GEN 41 3/ 24 465,400 569,996 658,175 735,862 806,095 870,694 930,900 10600009776 CAN41-4141-48GEN 41 3/ 48 344,000 421,31.2 486,489 543;912 595,825 643,565 688,000 10411OD09777 CAN41-4141-72GEN 41 3/ 72 278,240 340,773 393,491 439,936 481,926 520,539 556,480 10DOODOD498 CAN51-5151-24GEN 51 1 24 930,880 1,140,091 1,316,463 1,471,851 1,612,331 f,741,517 1,861,760 1DDDDQPD499 C4151-5151-48GEN 51 1 48 708,320 867,511 1,001,716 1,119,952 1,226,846 1325,145 1,415,640 10DOD000580 CAN51-5151-726EN 51 1 72 556,480 681,546 786,982 879,872 953,852 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. MMM All installations must completely comply with all DormontO man0fachiring carirpany w2mings -and instructions, national, state and local codes and all applicable ANSI standards, ---- ---A WATTS Brand - - _... _ USA: T; (800) 367-6663 • R (724) 733--4808 • Dormont;com - - - - Canada: T: (905) 332-4D9D - F; (905) 332-7068 - Dormontca Latin America: T. (52) 81-1001-8600 • R (52) 81-8DOO-7091 • Donnont.eam ES'Q-GAG Generac_InstaliSmart 1703 © 2016 Dorm ont Uri MOXIi MM COPUcii� of PL ripe- in Thous cinds of BTU per Hour of LfquOed Rafrolcum Gas brl, C: vies {'1&s$ulc— Of 11.0 in'l,"Ic and a Piti�.riur� Drop Oi C.&h.WC (based on a 1.52 specific gravlVy,gm) 187 125 99 $4 74 67 56 50 45 4738 1073 720 571 464 425 383 325 286 257 235 218 204 192. 769 152 1391 934 740 627 551 497 421 370 333 305 283 264 249 219. 197 1983 1331 1054 893 786 708 6D0 528 475 435 403 376 354 311 280 3563 2-397 1894 1605 141-2 1272 1078 948 854 781 723 676 636 560 504 4724 3247 2608 2232 1978 1792 134 7359 1232 1133 1054 989 934 828 1DD63 6755 5351 453 SW 3592 3044 _-2678 2411 22D7 2044 1910 1797 1581 .7..60 7424 22 129 20 113 78 102 15 86 73 76 72 77 iD 9 68 63 58 54 9 51 8 48 8 46 8 44 7 42 7 40 167 23B 147 209 132 188 112 160 99 140 89 81 75 70 126 116 107 7DD 66 94 63 89 60 85 57 81 54 78 52 75 427 642 376 569 338 .536 287 441 262 391 227 208 192 18D 334 326 $03 285 169 269 16D 255 152 244 146 233 140 . 224 134 1207 1061 956 810 712 642 587 544 508 478 453 481 411 394 216 379 MOXlmum CcfPciclfy of PE Pipe in Thousands of 73T!i per Hour of Liquefied Petroleum Grw 2516B7Uh-1 CFH with c Gas Pressure of 2.0 psi and a Pressure iDrop of 1.0 psi (based on a 1.62 specirio gravity gas) 966 1379 1046 SSb 779 7Q2 595 523 471 431 399 373 351 309 11300 14652 7586 6008 • 5092 4479 4033 3418 3DD7 2707 2478 2295 2144 21)]B 1775 278 1699 20577 9835 14014 779D 177bD 66D2 94D8 5807 8275 6229 7451 4432 3898 3510 3213 2975 2780 2617 23Q2 2073 37514 25183 19946 169D5 74869 13389 6315 17348 5555 9982 5002 8988 4578 822.6 4239 7618 3.9.62 7119 3729 3280 2953 43429 2Q848 23969 20515 78-782 16474 14100 12496 11322 10417 9691 9092 6700 8589 5894 7612 53D7 105963 71131 56339 47750 42000 37B20 32054 28194 253BB 23234 27517 20.108 18926 76 47 6897 7499D Iov izo 115 106 99 93 8$ 84 80 - 77 74 1355 1192 1073 910 800 720 659 671 57.1 537 508 484 462 443 425 77-57 1545 1391 1179 7037 934 855 792 740 696 659 627 599 04 557 2503 2202 1983 168D 1478 1331 1218 1128 1054 992 939 893 • B53 818 786 4498 3986 3563 3019 2656 2391 2789 2027 1894 1783 7658 1605 7533 1469. 7472 5903 5232 4740 4057 3596 3268 2997 2788 2676 2477 2347 2239 2744 2060 7985 727D5 17175 logtb3 8529 7502 6755 6782 5725 5350 5036 4767 4536 4331 4750 3988 Max !Mum Crapactfy or PE Pipe in TilouscrYda of BTU per 146ar of Liquefies! Pei roieum Gas5768TUh_7 CF7# With a Gas Pressure of 10.0 psi rnd a Pressure Drop of 7.0 psi (based on a 1.62 specific gravlly gps) 2476 1662 7316 1116 981 884 749 659 593 543 503 470 442 389 350 14234 9555 7568 6474 5642 508D 43D6 3787 3410 3727 2890 2701 2s42 2236 2074 78455 12388 9872 8316 7375 6587 553 4910 4422 4047 3747 3502 3296 2899 2611 26296 17652 13981 11849 10423 9385 7954 6997 .0300 5766 5340 4990 4697 4131 3720 1147252 31720 25123 27293 15729 16B65 14294 12572 11321 10361 96.96 8967 8440 7423 6685 1 5396D 37087 29782 25489 22591 20469 77519 :15527 14068 72943 12041 11297 70677 9458 B569 1133476 89607 70967 60148 52905 47640 40376 35514 319BO 29267 271D4 25329 23840 20970 18882 a n a ➢9 a ➢1 e➢ c➢ ➢a se ee as eaa o➢ �D➢ ➢a 297 261 235 199 775 158 144 734 125 778 au 7707 150] 1352 J146 7008 907 830 171 1Qb 107 970 769 719 676 640 609 582 557 393 6 2213 1946 1753 1485 1306 .1176 7077 997 932 877 83D 790 754 723 695 3153 2773 2497 2116 186.2 7676 1534 1.421 1328 1250 1183 1125 .7075 7030 990 5665 4983 4187 3803 3345 8.012 2757 2b53 2386 2246 2726 2022 7031 1857 7779 _7384 .- _f DD _ .SggD - 5041 .-4468- -4048 --3`72a 3465 --3251 3071 2916 -2782- --26- 4 - '2560 .24bb 760D4 14077 1-?.676 10743 9449 8509 7787 7212 6739 6343 6005 5712 5455 5227 5D24 25] 6H7.11h=7 CFH Ph 7.800.662.02D8 ° Pcl%: 615.325.9407 n Web: wwwgcistilo.co m