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HomeMy WebLinkAboutProducts Review; Domestic Tanks-.,...r��ti��pC.-�'z5��r;•�'ac.IB"bet'�15�'s<-',.•.:� � ux,y,�.as.r•+-.�s r,�, ,°�:`%•�r' ,..,,�$: ;,u.,- .ae. .. _ -n i-. - a A MU R0 / D: R ROUND`== SST MANME)c .x�Pxrk.d=.3aV-'MR'e- a ..+C+asK.[ +. :�+ryas:�1►*W-W;aR.a%tas+,W#.�d._MKriixibk�st... _a w..+-s+wa,rw .. :xr,�"'.: ..-�•S.t.+-,q,.=•a; x a x,s.-e.a�Ya�s..twvo�a.. .. �,.�.,,,r..�'ru,wruacs.s=.-w.�dy�t+xw•e.�-rser'r�+.r!�IMM�wa>wna+ w ti- ..,a.�t,.n...x.. ,. ,.s .._.,a,o-... w ' J :21ND�.R®O�n�C'u�SuMr. Drab"T pcoat4 . ' v vih nc�ich(Pnmer . • P�QIIIDU 16 bll r "t103,wog [ at system pmper�eS include ° ---- �.., --- ,�- � a ;�qj, r, - �.;!7��n��r�c"h�epox�jiprliners''� . �„- ^ • ` _ i , �8�'•dome!n bl•a a �� s:� �;�5u erfi u�ve T I>;� o�fiesi�e�top�c6a�• ,. ' ,� ° x �galua 2ed�`s Bell' --.. ; rtrrco �osaon;,andedge�pr�otecan'' T " , ,� „ - eta � , ° C��Pafei�tk�pefi'ding�formuJated�nme►�a�d��iopcoat� ` " a ° P , , ` Dual.s i;vide opffons•fdrabov,'e'6r•andergrbund applications) Option,4,1;:.Ready4o :puyred'i gXid'e: d'urabfe powder, coating`Wth-black; a *;polyethylene AGIJG;dome' Option#2-',Abo\ra& ddptionlwithi steelc8' AGUG,tlome: _ ei All,,val,ves•and float, gauges;aroc- nfered- under dome' •) -Code, Section VIII,. Division' 1 ' d' i Regisferediwitfirthe;.Nafional B~dardl i, #721iquiF, id ifdovalve) Of, ifice (educes g;n refuelineris9 Adns •. '' ' • Vacuurn.pre purged'to save=time; money and product `Applicable+federal;=state,;ror, local{regulaifbns'may cdnraih specific ),dquiremenis for <a pr'`otectwe,cbatings and cathodic protection The•purchaser•andiFrnstaller )re responsibfex . for compbance�with all�federaP sta B Flocalland'NF. PA,irirlustry`, regulatron's Cathodfc _ • • ' ' • protectronti'jTequfred andlcoofmg�musir'be,eontihuous aridlunfriterrupted;andxmust' i comply)w, tAa'hlocal;;stdte7or`nafional}ddde`:, v �' ' �vwvw,,� nni,�'� C;�orta�ners cg'm:CallfToll;;F,:,ree5t.�8=558;.$265 •� cam-- 1 Q 1 I 1 ' Z) 0 W cWc C .J o OUTSIDE � o DIAMETER 0 o F- 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 -20' F. to 125' F. All 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. nll=AI 1 I LKlr"r J � WITHDRAWAL --� X'-" ,I� VALVE FLOAT Lall NOTICE �` ANODE GAUGE � CONNECTION p� ' FILLER I 0 0�VALVE I 1 Q I SERVICE / NAME MULTIVALVE PLATE RELIEF VALVE FITTINGS LAYOUT UNDER DOME IAGUG VESSEL DIMENSIONAL INFORMATION I 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. 2411 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" Hemi 7'- 2 1/2" 3' - 7 1/2" 12 3/4" 3' - 6" 472 Ibs. 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 3/41, 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" Hemi 9'- 10" 4' -1 7/16" 1511 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" Hemi 15' -10 13/16" 4' - 4 5/16" 16 1/4" 9' - 0" _ 1729 lbs. 15 5 3785.0 L 1 1040.4 mm 4846.6-mm 1344.6 mm 1 412.8 mm 2743.2 mm 784.3 kg Rev: Jan. 27, 2016 1'!-.� t �... _ ..7. ,.�.. �r L-> 1 ..: s 1 �„g• _ .te . TPA .:....... _ Why Tanks 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 currentflows 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 over time. 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. rrevennng 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 current from the anode to the cathode. An effective external coating can protect over 99% 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. Flow 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 1.25Vvolts 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 #12 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. Soil Type (9pi9s„evlay, �S�h0-y" 6am�y v :; Sand, Gravel, Rocky Areas Tank Cap. (9al•)FA I ;.,`.toi5000 o�imscinZ 5000 to 10000 ohm -cm MML QyAlloyll� Size Qty. Alloy 120# a;? 1) 9# 1 H-1 150 °v�9#' E>1 w : �Fff- 9# 1 H-1 250 9 E. H 117 9# 2 H-1 325' 9# 2 H-1 500'� 9# 2 H-1 1000 rtjri H1; 9# 4 H-1 15007%#�'2 �'1�_, 9# 4 H-1 2000 �;1 � 1_ f;Hc1r 9# 6 H-1 'Based on 90% effective external coating, 2 malft2 current density, and 30- year Anode 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. 1 anode 2 anodes 4 anodes C C � 0 0 0 CDO C C 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. Mechanical Connection Under Dome Cathodic Protection Testing Procedure Equipment Needed: Digital Voltmeter, Red Test Lead Min. 12' Long & Black Lead Min. 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). STEP 2: Insert the black test 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 Y2 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 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 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 oil, road salts, or other substances that may contaminate the solution by absorption through porous plug. Do not allow electrode to freeze. Distributed By: k71�nJ�a7i °�G3r�%Fl 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 BTU's per hour. The regulator is factory set to reduce container pressure to an intermediate pressure of approximately 10 PSIG. a 1 'fib ��c-^aiISR:t:. i•=rw • Compact design can be connected to a service valve using either a POL adapter or a RegO product pigtail. • Large threaded W RNPT 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" RNPT 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. NEW Body............................................................................................Zinc Bonnet.........................................................................................Zinc Spring........................................................................................ Steel Seat Disc.................................................................Resilient Rubber Diaphragm...........................Integrated Fabric and Synthetic Rubber llht1'aP1r•��ilmo iiF:aSd�i n t9,,." '�f PN, q U�a LISTED LV3403TR FLOW PROPANE ` __.._—"^-�i artNtimbec 1 I >'_ .�^—_-- ---•--�'--� ']'� !Inle,C[ o echon cyl{ , >-�__--- ) ! icE`- �^,�--.`.--__'•r .�r. Outle.Eonnechon fI - ry [ .�_ .-�"j(""�. O'�fice;Stze . ! I•`dCtOLY�� ��— •1 - °° etUenbEosi6onl _ �--'--• -i c Vapor�Ca��aaLyBTU%'hr Prapane� 1 • 11 111 t • 11 Maximum flow based on inlet pressure 20 PSIG higher than the regulator setting and delivery pressure 20 / lower inan tno reguistor setung ano aesvery pressure zu r lower man ine semng. A14 MAN emu. 100 Rego Dr. Elon, NC 27244 USA www.regoproducts.com +1 (336) 449-7707 AFY 9-aa (DY,tt 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 domesticloads. Fealnues • 90 degree right angle inlet to outer connection for meter or standard installations. • Large vent lielps to prevent blockage and has 3/4" 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 alien 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. W't Rern Ri cg Body............................... :........................................... Die Cast Zinc Bonnet........................................................................ Die Cast Zinc NozzleOrifice......................................................................... Brass Spring...................................................................................... Steel Valve Seat Disc ..................................................... Resilient Rubber Diaphragm ......................... Integrated Fabric and Synthetic Rubber OA. Il�i��`�; e- w/MonntiingRzacket �,N013 I I A 15 PSIG Inlet g 5 PSIG Inlet t ° 8 PSIG Inlet c '1 PSIG nlet C rift.. 0 50 100 150 200 250 300 350 400 450 .500 B1Umr. 250,000, 500,000 750,000 1,000,000 1,250,000 yPr�essuce% Vap Cap"autyBT�[I/,hr[ALIX •F. 1®® NPIF ®®PSIG Inlet 111 111 Maximum flow is based on 10 PSIG inlet and 9° w.c. delivery pressure. "Mounting Bracket Included. 100 Rego Dr. Elon, NC 27244 USA www.regoproducts.com +1 (336) 449-7707�/� AZl Job Name Contractor Job Location Approval Engineer Contractor's P.O. No. Approval Representative SKU Generaco f ,y6. Flexible Feel Lines The flexible connection between the gas supply and the gas inlet of a Generac° Stationary Outdoor Backup/Standby Generator Features a 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) a Flexible Tube Material Annealed 304 Stainless Steel a Flare Nut Material Carbon Steel with Zinc Trivalent Chromate Plating • Flare Adapter Material Carbon Steel with Zinc Trivalent Chromate Plating • PVC Dip Coating Gray Heavy Duty, Antimicrobial, UV Stabilizer' CSA Group Certificate of Compliance 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 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 S�° (Excluding 60/61 Series) c us Product Configurations ES-D-GAC_Gen erac_I nstallSmart For use with Generac 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. DDrmont product specifications in U.S. customary units and metric are appm)dmate and are provided for reference only. For precise D6fmont® measurements, please contact Dormant Technical Service. Dormant 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 WATTS Brand Minimum Flow Capacity at Specified Pressure Drop Straight Length BTU/hr. NATURAL GAS, 0.64 SG, 1000 BTU/cu.ft. CONFIGURATIOND•i• i Generac° Part Number 0ormont° Part Number SERIES Nominal ID in Nominal Lenght I in 0.50 in 1 0.75 In 1.00 in 1.25 In 1.50 in 1.751n 2.00 in 10000009793 CAN41-4141-24GEN 1 41 3/4 1 24 290,900 1 356,278 411,395 459,953 503.854 544,224 581,800 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 % 72 173,900 212,983 254,932 247,960 301,204 325,337 347,800 10000000498 CAN51-5151-24GEN 51 1 24 581,800 712,557 822,789 919,907 1,007,707 1,088,448 1,163,600 10900000499 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. CONFIGURATION P•O• INCHES WATER COLUMN) Generac° Part Number Dormont, Part Number SERIES Nominal ID in Nominal Lenght in . 0.50 In 0.75 in 1.OD in 1.25 In 1.50 in 1.75 in 2.00 In 10000009793 CAN41-4141-24GEN 41 3/4 24 465,400 569,996 658,175 735,862 806,096 870,684 930,800 10000009776 CAN41-4141-48GEN 41 3/4 48 344,000 421,312 486,489 543,912 595,825 1 643,565 688,000 10000009777 CAN41-4141-72GEN 41 3/4 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 1,861,760 100000D0499 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 1 51 1 72 556,480 681,546 786,982 1 879,872 1 963,852 1.041.079 1,112,960 EXAMPLE Generac part number 10000000498 (Dormont part number CAN51-5151-24GEN) can supply a minimum of 581,800 BTU/hr.of natural gas @ 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. A WATTS Brand USA: T: (800) 367-6668 • F: (724) 733-4808 • Dormont.com Canada: T: (905) 332-4090 • R (905) 332-7068 • Dormont.ca Latin America: T. (52) 81-1001-8600 • F: (52) 81-8000-7091 • Dormont.com ES-D-GAC_Generac IhstallSmart 1703 © 2016 Dormont Maximum Capacity of PE Pipe in Thousands of BTU per Hour of LiquEirled Petroleum Gas with c1 Gras Pressure of 11.0 in. VVC and a Pressure Drop of 0,5,1n.1t'VC (based on a 7.52 specific grovitygas) zu 15 Ib . Ad 12 11 10 9 9 8 8 8 7 7 113 102 86 76 68 63 58 54 51 48 46 44 '42 40 147 132 112 99 89 81 75 70 66 63 60 57 54 52 209 188 160 140 126 116 107 100 94 89 85 81 78 75 376 338 287 262 227 208 192 180 169 ' 160 152 146 140 . 134 569 516 441 391 354 326 303 285 269 255 244 233 224 216 1061 956 810 712 642 587 544 508 478 453 431 411' 394 379 2516BTUh, 7 CFH Maximum Capacity of PE Pipe in Thousands of BTU per Hour of Liquefied Petroleum Gas with a Gas Pressure of 2.0 psi and a Pressure Drop of 1.0 psi (based on a 1.52 specific gravity gas) 17UU 101Y iu4a 000 //v /uz 595 623 471 437 399 373 351 309 278 11300 7586 6008 5092 4479 4033 3418 3007 2707 2478 2295 2144 2018 1775 1599 14652 9835 7790 6602 5807 5229 4432• 3898 3570 3273 2975 2780 2617 2302 2073 20877 14014 11100 94DB 8275 7451 6315' 5555 5002 4578 4239 3962 3729 3280 2953 37514 25183 19246 16905 14869 13389 77348 9982 8988 8226 7618 7119 6700 5894 5307 43429 29848 23969 20515 18782 16474 14100 12496 11322 10477 9691 9092 8589 7612 6897 105963 71131 56339 47760 42000 37B20 32054 28194 25388 23234 21517 20108 18926 ' 76647 14990 —f 1WI luo joy izo 110 IUD yy 93 88 84 80 77 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 1.128 1054 992 939 893 • 853 818 786 4498 3956 3563 3019 ' 2656 2397 2189 • 2027 1894 1783 1688 1605 1533 7469• 1412 5903 5232 4740 4057 3596 3258 2997 2788 2616 2477 2347 2239 2144 206D 1985 12705 11176 1OD63 8529 7502 6755 6182 5725 5350 5036 4767 4535 4331 4150 3988 2516BTUh=7CFH Maximum Capacity of PE Pipe in Thousands of BTU per Hour of Liquefied Petroleum Gas with a Gas Pressure of 10.0 psi and a Pressure Drop of 1.0 psi (based on a 1.62 specific gravity gas) ZWo 1002 1316 1116 987 884 749 659 593 543 503 470 442 389 0 14234 9555 7568 6414 5642 5080 4306 3787 347.0 3121 2590 2707 2542 2236 2014 18455 12388 9812 8316 7315 6587 5583 4910 4422 4047 3747 3602 3296 2899 . 2611 26296 17652 13981 11849 10423 9385 7954 6997 6300 5766 5340 4990 4697 4131 3720 47252 31720 25123 21293 18729. 16865 14294 12572 11321 10361 9595 8967 8440 7423 6685 53960 37087 29782 25489 22591 20469 17579 115527 14068 12948 12041 11297 10671 9458 8569 133476 89607 70967 60148 52905 47640 40376 35514 31980 29267 27104 25329 23840 20970 18882- 7707 1501 LVu- 1352 177 1146 IIJ 7008 JOo 907 144 830 AM 769 1z5 719 118 676 111 64D 106 609 101 582 97 93 2213 1946 1753 .1485 1306 1176 7077 997 932 877 830 790 754 557 723 536 695 3153 2773 2497 2116 1862 7676 1534 7421 1328 1250 1183 1725 1075 1030 990 E665 4983 4487 3803 3345 3012 2757 2553 2386 2246 2726 2022 1931 1857 1779 7334 6500 5890 5047 4468 -4048 3724 3465 3257 3077 2916 2782 2664 2560 2466 16004 14077 12676 10743 9449 .8509 7787 7212 6739 6343 6005 5772 5456 5227 5024 2516BTUh-1CFH . Ph: 1.800.662.0208 a Fax: 615.325.9407 o Web: www.gctstlte.com