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HomeMy WebLinkAboutSwain specs ABOVEGROUND/UNDERGROUND DOMESTIC BANKS 120 - 2.000 I.vg V - r 77 NEW! POVJDURA'-,OneCure •' Super Durable Topcoat with Zinc Rich Primer on AboveOr©und ! POVIDURA OneCure Tvio coal system properties include: I - 8" dome in black plastic or white Sul?_r galvanized steel. • F::.cfil (i•11:';;1'.;I ir•ill�l:i�l_il I,�lCfcl iaVr IUIJ:�il • Dual sr-i ice.00t,0Ts for aoove or undsrgrount J�=„�- . ;otion'#1-Ready-to-bury red oxide durable po:•:-I -eating v.,Jth black • �»lyethyl¢neAGUG dom=' • Option#2:A.bovagr -jnd cptio'n vrith steel 8-AGUG • Allvatv?c and float gauges are:entered under dome • abricated to cha lawsti,.S.M.E Code.Section Vtll. D vision 1 egis'tarad ,nth the National Board • '?2 liquid revel outage valve orifice reduces refueling ernissions • Vacuum p{e-pijrgeri to save Ume,money and preduAt 4pplfcab1-federal,staff,orlocalregulations may contain specificrequir?ment--to- CONTAINERS protective aatings and ralh odic protectron-The purchaserand ins-taller ar res�pn for compliance v,01�ail federal,state,local and NFPA industry regulationz.GaModic . . - • protection r=quir-Pa and coating must be continuous and uninterrupted and must comply .;,i-;,3nlocal, ate or nation al code. ,; v)- l.TrinityContalners.com Call Toil Free: MR-558-8265 TRINITY . AGUG DOMESTIC Containing Our World%Energy- OVERALL LENGTH DOME It OUTSIDED1AMErERIf LEG WIDTH LEG SPACING Generai Specifications -----� WITHDRAWAL Conforms to the latest edition of the ASME code for / VALVE Pressure Vesw,Section Vill, Division 1.Complies wit FLOAT LP ANODE NFPA 58. GAUGE CONNECTION 1 r ,1 Rated at 250 prig from-2I)°F.to 125°F.All tanks maybe ® ,-FILLER evacuated to a full(14.7 psi)vacuum. O , Vessel Finish:Coated with epoxy red powder.(Tanks coated / . with the epoxy powder must be buried).For Aboveground use, SERVICE/__�/ " tanks may be coated with TGIC powder. MULTIVALVE �, NME i PLATE Applicable federal,state or local regulations may contain RELIEF specific requirements for protective coatings and cathodic VALVE protection.The purchaser and installer are responsible for compliance with all federal,state or local regulations. FITTINGS LAYOUT UNDER DOME AGOG 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 I STACK 120 wg. 24" Ellip 5'-5 13/16" T-0" 10 1/8" 3'-0" 245 tbs. 96 1 12 454.2 L 609.6 MM 1671.3mm 1 911.4 mm 257.2 mm' 914.4 mm I 111.1 kg. 250 wg. 31.5" Hemi 7'-2 1/2" 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" Hem! 8'-11 314" 3'-7 112" 12 3/4" 4'-D 1/4" 586 lbs. 45 9 .1211.2 L 800.1 mm 2736.9 mm 1104.9 mm 323.9 mm 1225,6 mm 266.7 kg. J]*t Hemi 9'-10" 4'-1 7116" 15" 5'-D" 871 lbs. 30 6 2997.2 mm 1255.7 mm 381.0 mm 1524.0 mm 395.1 kg Hemi 15'-10 13116" 4'-4 5116" 16 1/4" 9'-0" 1729 Ibs. 15 5 4846.6 mm 1344.E nim 41?.o nim 2743.2 rui; 784.3 kg Rev, Jan.27,2016 a Why Tanks Corrode different metals. The most common anode material is magnesium, Underground steel tanks corrode due to an electrochemical reaction which when coupled to steel results in DC current flow from the between the tank and the surrounding soil. The process of corrosion magnesium to the steel. The open circuit potential of steel is about occurs due to small voltage differences on the steel surface that result -0.50 volts referenced to a copper sulfate electrode. The open circuit in the flow of DC current from one location to another. Where current potential of magnesium is about-1.55V to-1.80V. By connecting the flows from the tank into the soil corrosion occurs. This location is called two metals together,the difference of 1 to 1.25V volts results in current the anode in a corrosion circuit. Where current flows from the soil to the flow to the tank that overcomes the natural corrosion cells that exist on tank,no corrosion occurs. The progress of corrosion is determined by the tank. With this current available to the tank,no corrosion occurs. the amount of current flowing between the anode and the cathode and whether the locations of the anode/cathode remain constant over time. Magnesium Anodes Corrosion rates are generally higher in wet soil environments since the There are a variety of anode sizes and alloys used for cathodic conductivity of the soil promotes the flow of DC current in the corrosion protection. The two primary alloys are designed as H-1 (or AZ63)and circuit. High Potential. The H-1 alloy is produced from recycled magnesium and has an open circuit potential of approximately—1.55V. This alloy Corrosion generally exhibits itself on underground tanks in either a is well suited for protection of underground propane tanks. The High general overall rusting or more commonly,a pitting attack. Pit locations Potential alloy is 99%pure magnesium having an open circuit potential may result from metallurgical conditions of the steel surface or soil up to-1.8V. This alloy should be used for soil applications over 10,000 variations such as rocks,salts,fertilizer,moisture concentration,oxygen ohm-cm resistivity concentration,etc. The two most common anode sizes used for underground propane Preventing Corrosion tanks are 9 lb.and 171b. The size designation relates to the metal weight. Protecting underground 10' of#12 TW insulated wire is attached to the anodes. Anodes are tanks from corrosion is then backfilled in a mixture of gypsum, bentonite,and sodium sulfate easily achieved bythe use to lower the electrical resistance of the anode to soil. The mixture is a of two com m only applied low cost,nonhazardous,electrically conductive backfill. The anode and protection . methods: backfill is then packaged in a cotton bag and either a cardboard box or external coating and paper bag. Actual shipping weight of these anodes viith backfill is 27 cathodic protection. lb.and 45 lb. These two methods are complementary Application Recommendations and should be used in Magnesium anodes can protect underground tanks in most soil conjunction with the conditions. The H-1 alloy is generally very effective. The following chart other. An effective provides size and quantity recommendations forvarious size tanks based external protective on conservative design assumptions. This chart covers soil conditions coating insulates the steel from the soil environment,thus preventing up to 10,000 ohm-centimeter resistivity. Resistivitles higher than the flow of corrosion current from the anode to the cathode. An effective 10,DOD Dhm-centimeter generally represent very dry soils. Verification external coating can protect over99%of the tank surface area. However; of soil resistivity can be performed through soil analysis. Contact us no coating is perfect. Damage from construction or soil stresses create for design recommendations in locations where soil resistivities exceed tiny defects,which may result in accelerated corrosion at the defect. 10,000 ohm-cm,or if there is no effective external coating on the tank. Cathodic protection prevents corrosion at those defects by applying The propane service line from the tank to the house also must be DC current from an external source, forcing the tank to become considered in the cathodic protection design, unless the service line cathode. Application of sufficient DC current to the tank will prevent any is plastic. All underground steel pipe should be extemally coated with corrosion from occurring. The two general types of cathodic protection a corrosion resistant material. The service line should be electrically systems are sacrificial and impressed current. Sacrificial systems are isolated at the house with an insulating fitting or union. if service pipe used when the amount of current required for the protection is small, is less than 50'in length,the tank anodes will provide sufficient current such as in underground propane tanks. Impressed current systems to protect both tank and pipe. For longer lengths of pipe,an additional are more commonly used for large structures such as large diameter anode may be required at the house connections. pipelines. Electrical isolation of the tank from metallic piping systems and electrical grounds is critical for the cathodic protection system's if another metallic material such as copper is used for service piping, effectiveness. the pipe should be electrically isolated from the tank at the fill pipe connection. Copper and steel create a galvanic couple that will accelerate Hc)w Sacrificial Cathodic Protection Works corrosion of the steel tank when directly connected to copper piping_. Sacrificial systems work by creating a galvanic connection between two Generally,copper piping does not require cathodic protection. rliie Soils,Clay, Sand, Gravel,Rocky Mechanical Connection Under Dome Soil Type Sandy Learn Areas r. Tank Cap. 510 5090 ohm-cm 5000 to 10000 ohm-cm (gal-) Size ©ty. Alloy Size Oty. Allay 1 120 91 1 H-1 91 1 H-1 150 9 1 14-1 9# 1 H-1 9 il t H-1 9# 2 H-1 2' 325 � 325 9#1 i H-1 9# 2 H-1 500 170 1 1 H-1 9# 2 H-1 ^---� 1000 17� 2 H-1 9# 4 H-1 1500 17# 2 H-1 9# 4 H-1 Cathodic Protection Testing Procedure 2000 17 3I H-1 9# 6 H-1 Equipment Needed: Digital Voltmeter, Red Test Lead Min. 12'Long =Based on 90%effective external coating,2 maM current density,and 30- & Black Lead Min. 2' Long, Reference Electrode (Copper/Copper yearAnode life. Sulphate Half-Cell) Anode Installation STEP 1:Using a digital voltmeter insertthe red test lead into the Volt 1.Determine size and quantity of anodes from application chart. jack of the meter and select the 2 or 20 volt DC scale. Clip red test 2.When a single anode is installed, it should be located near the lead connector to an uncoated metallic area of the tank, preferably tank center on either side of tank. to the fill pipe multivalve. A good solid connection is very important. 3.When multiple anodes are installed, space them evenly around (DO NOT connect to shroud). the tank, See examples below. STEP 2:lnsertthe blacktest lead into the Common jack on the meter, and connect the opposite end of the lead to a charged reference 1 anode 2 anodes 4.anodes electrode(Y22 cell). _40 C-�10 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 `— - V tank, and one at each end of the tank), If difficulty is encountered obtaining readings, moisten soil with water or dig%cell deeper into 4.Anodes are shipped in either cardboard boxes or multi-wall the soil. paper sacks. Remove outer container and burythe cloth bagged STEP 4:Record all four meter readings on an appropriate form. The anode. If anode is supplied in plastic bag, remove plastic bag least of all four readings should be a minimum of-0.850v or more before installing. negative, (Note:If any of the four readings are below(less negative) 5.Install anodes approximately two to three feet from the tank and -O.850v then the tank is not fully protected}. at least as deep as the center line of the tank. Anodes work best in locations with permanent moisture, so generally the deeper Charging Reference Electrode the better. 6.After placing the anode,stretch out the anode connection wire STEP 1: Unscrew and remove porous plug end of new reference and extend over to a connection point on the tank fill pipe. electrode. Add deionized or distilled water to the copper sulfate 7.Cover the anode with approximately six inches of backfill and crystals, filling electrode completely. The solution will turn blue in pour 5 gallons of water on the anode to saturate the prepared color and there should always be excess crystals at the bottom of backfill. Water is necessary to activate the anode, the tube. DO NOT USE TAP WATER. 8.Connect the anode wire to the tank with a low electrical STEP 2:Replace porous plug end of electrode and place in an upright resistance connection. Examples are threaded stud on the position so that the porous plug end is facing in the down position tank fill pipe or any accessible metallic connection point to the and let stand for 1 hour before use. This will allow the porous plug tank. All connections should be coated with a moisture-proof to become completely saturated before use. material. Caution:Do not allow electrode to contact oil,road salts, or Other 9.Ideally, the tank connection is made in the area of the tank fill substances that may contaminate the solution by,absorption pipe within the covered dome. With access to the anode wire, through porous plug. Do not allow electrode to freeze. subsequent testing of the tank can include measurement of anode output and verification of performance. Distributed By: 10.Verify performance of the anode using an appropriate test procedure. Tulsa HQ: :.. :11 mesaproducts. com 1112011-5000 J Loss of Pressure Underground Installatiops Freeze-up inside the regulator. Special hazards can occur if regulators are not property installed in ' 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. lce Refer to NPGA No.401. Ri Regulator adjustment closure cap must be tight. 1 End of regulator vent or vent tube Grade ground downward and to away around housing dome. probable bleated above the highest i This prevents water collecting prable water level. and running into orstanding 2 to 6 inches t around dome. i minimum. This 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 6 inches minimum l bent where free flow of the LP-Gas is restricted. These freeze-ups (18 inches minimum if ' can occur when the moisture,gas flow and temperature combine to subject to vehicular traffic). create a hazardous condition.Freeze-ups can occur at temperatures above 32`F Action Required:AJ)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 Note: Water mark left in housing dome at level container suspected of having excessive moisture should be treated above regulator vent, or end of vent tube requires with the proper amount of methanol. replacement of regulator.Then correct installation. i Customer Safety General Warning Since regulators are often used by consumers without previous knowledge of the hazards of LP-Gas,and the LP-Gas dealers are the All RegO Products are mechanical devices that will eventually only ones who have direct contact with the consumers, become inoperative due to wear, contaminants, corrosion It is the dealer's responsibility to make sure that his and aging of components made of materials such as metal hould customers are properly instructed in safety matters relating and rubber.As a general rec with all atihe r egul recotors mmendations to their installation. be replaced in accordance with all of the recommendations outlined in this safety warning. The recommended service life of a regulator is one of many factors that must be At the very minimum,it is desirable that these customers: considered in determining when to replace a regulator. I 1. Know the odor of LP-Gas and what to do in case they smell gas.Use the NPGA"Scratch'n Sniff"leaflet. The environment and conditions of use will determine the safe 1 2. Are instructed to never tamper with the system. service life of these products. Periodic inspection and maintenance 3. Know that when protective hoods are used to enclose are essential. regulators and/or valves, that these hoods must be closed, Because RegO Products have a long and proven record of quality but not locked. and service, LP-Gas dealers may forget the hazards that can occur 4. Keep snow drifts from covering regulators. because a regulator is used beyond its safe service life. Life of a g. Know the location of the cylinder or tank shut-off valve in regulator is determined by the environment in which it"lives."The emergencies. 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. 100 Rego Dr.Elon,NC 27244 USA www.regoproducts.com +1(336)449-7707 �r First Stage Regulator with Relief Valve and Pressure Tap Second Stage - l Regulator with Large Vent and I Pressure Tap To Appliances/Furnace First Stage Piping Two-stage systems can greatly reduce the possibility of freeze-ups Y e regulator is truly the heart of an LP-Gas installation. It must and resulting service calls as the expansion of gas from tank pressure _•,-pensate for variations in tank pressure from as low as 8 PS1G to 11"w.c. is divided into two steps, with less chilling effect at each V a 22 PSIG-and still deliver a steady flow of LP Gas at 11"w_ . regulator.In addition,after the gas exits the first-stage regulator and n consuming appliances.The regulator must deliver this pressure enters the first-stage transmission line,it picks up heat from the line, further reducing the possibility of second-stage freeze-up. te a variable toad from intermittent use of the appliances. Service calls for pilot outages and electronic ignition system failures zaagh a single-stage system may perform adequately in many are also reduced as a result of more uniform appliance pressure from 2tions,the use of a two-stage system offers the ultimate in pin- two-stage systems. ;_='t regulation.Two-stage regulation can result in a more profitable _P G'as operation for the dealer resulting from less maintenance and Economy of Installation err installation callbacks-and there is no better time than now for In a single-stage system, transmission line piping between the —(ling Rego Regulators in two-stage systems, container and the appliances must be large enough to accommodate - the required volume of gas at 11"w.c. In contrast, the line between = imform Appliance Pressure the first and second stage regulators in two-stage systems can be 'tte installation of a two-stage system-one high pressure regulator much smaller as it delivers gas at 10 PSIG to the second-stage a!the container to compensate for varied inlet pressures, and one regulator. Often the savings in piping cost will pay for the second x i pressure regulator at the building to supply a constant delivery regulator. z ` ;r=ssure to the appliances - helps ensure maximum efficiency As an additional benefit, single-stage systems can be easily s`d froubie-free operation year-round. It is important to note that converted to two-stage systems using existing supply lines when they a4e pressure at the appliances can vary up to 4"w.c. using single- prove inadequate to meet added loads. This is the least expensive age systems, two-stage systems keep pressure variations within and best method of correcting the problem. 1-w.c. New high-efficiency appliances require this closer pressure rzvitrol for proper ignition and stable, efficient operation. In fact, one Allowance for Future Appliances major manufacturer requires the use of two-stage systems with their A high degree of flexibility is offered in new installations of two- appliances. stage systems.Appliances can be added later to the present load- Reduced Freeze-upslService Calls provided the high pressure regulator can handle the increase-by the addition of a second low pressure regulator.Since appliances can be R egulator freeze-up occurs when moisture in the gas condenses and regulated independently,demands from other parts of the installation ..ezes on cold surfaces of the regulator nozzle.The nozzle becomes will not affect their individual performances. 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 Replace Pigtails and tubing is properly sized. Proper sizing will help ensure constant If you are replacing an old regulator, remember to replace the delivery pressure to the appliances during fluctuating loads at all copper pigtail. The old pigtail may contain corrosion which can times. Just as important,be sure the RegO Regulators you choose restrict flow. In addition, corrosion may flake off and wedge are capable of handling the desired load.This is another advantage between the regulator orifice and seat disc-preventing proper of two-stage systems - they are capable of handling much lock-up. more BTU's/hr. than single-stage systems. The RegO "LP-Gas Servicemen's h4a11ue;l"provides ccrnplete infrxin2tion �m pipo sizing and proper regulator selection. 7 Mquire First Stage Regulators with Built-M Relief Valves First Stage Regulator r with Relief Valve and Pressure Tap Second Stage I Regulator with Large Vent 1 and Pressure Tap r To Appliances/Furnace I / First Stage Piping I With no first stage relief valve, propane liquid may form here... 70'F. 120 PSIG 40'F. 72 PSIG Resulting in sudden pressure surge due to flashing into vapor here! 8D'F. 140 PSIG SO-F. 86 PSIG First stage relief can prevent liquid from forming in firs f stage piping 90-F. 165 PSIG 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 250 200 '. c� n 150 Propane N m 100 I I 5D I Butane -40 -20 0 20 40 60 80 100 120 Temperature'F. The Problem Many modem LP-Gas appliances are equipped with pilotless ignition stage regulator will not relieve the pressure in first stage piping. systems. Water heaters and older appliances use pilot lights, but it The rapid vaporization of the liquid may cause a rapid pressure surge has become a common practice for energy conscious homeowners to that could seriously damage critical components of the appliance and shut-off the pilot when leaving home for extended periods of time. In furnace controls. each instance,there is no gas demand at all for extended periods. Afire or explosion could occur as a consequence. The Consequences If the first stage regulator fails to lock-up tight, usually as a result The Solution of a worn seat disc or foreign material lodged between nozzle and RegO LV4403 Series First Stage Regulators with Built-Jn Relief seat disc, pressure will build-up in the first stage piping—possibly Valves reduce the possibility of this serious hazard in two stage to a level that approaches tank pressure. Combining this with warm applications.The built-in relief valve is designed to vent as needed ambient temperatures and cool ground,propane liquid may form in and reduce the possibility of first stage piping pressure from the first stage piping. becoming high enough to form liquid. When gas demand resumes,this liquid may pass through the second stage regulator into the appliances and furnace. NOTE—the second a NOZJF617 100 Rego Dr.Elon,NC 27244 USA www.regoproducts.com +1(336)449-7707 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,OOb BTU's per hour. The regulator is factory set to reduce container UL pressure to an intermediate pressure of approximately 10 PSIG. • LV3403TR7/"FNPT W F.NPT /az" 10 PSIG Over Outlet 1,500,000 LV3403TRV9 9:00 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. LV3403TH Provides accurate first stage regulation in two-stage bulk tank ops ln� systems.Reduce tank pressure to an intermediate pressure of 5 to 10 �L PSIG.Also used to supply high pressure burners for applications like industrial furnaces or boilers.Also incorporated in multiple cylinder installations. • LV4403SR4 7F. 5 .1 5 LV4403TR4 V2-F 10 5-10 LV4403SR9NPT 5 1-5 LV4403TR9 �� 10 5 10Yes 2,500,D00 LV4403SR96 F % 5 1-5 LV4403TR96RN 10 5-10 'When used for final stage pressure control,must either incorporate integral relief valve or separate relief valve should be specified in accordance with NFPA Pamphlet 58. Maximum flow based on inlet pressure 20 PSIG higher than the regulator setting and delivery pressure 20%lower than the setting. LV4403 Series ! • ! 1 • ' ! !FTV RM Designed to reduce first stage pressure of 5 to 20 PSIG down to o1s1k burner pressure, normally 11" w.c. Ideal for medium commercial �L installations, multiple cylinder installations and normal domestic loads. • I J• LV440384 . %" LV4403B48 /"F.NPT 11"w.c. at LV4403846ft #28 10 PSIG79"tolYver Inlet 935,0003/<"F. NPT Drill Inlet LV4403866 LV44=66R' '�"F. NPT L®44038 Series Backmount design "Maximum flow based on 10 PSIG inlet and T w.c.delivery pressure. i ES-D-GAG_Generator Cenerac For Use with Generac Stationary Outdoor 8tandby Generators Job Name Contractor Job Location Approval Engineer Contractor's P.O.No, Approval Representative SKU ®errnent Supr=Safe® Flexible Gas Appliance = ; Connecters k . The flexible connection between the gas supply and the gas inlet +! " of a Genera&Stationary Outdoor Backup/Standby Generator. Features For use with Generac stationary outdoor backup/ o Operating Temperature -40°F to 150°F(-40-C to 65.6DC) standby generators. e Operating Pressure MAX 0.5psi(3.45 kPa) o Hydrostatic Burst Pressure MIN 250psi(1725 kPa) a Rebble Tube Material Annealed 304 Stainless Steel Flare Nut Material Carbon Steel with Zinc Trivalent Chromate Plating Series 30,40 and 60 Flare Adapter Material Carbon Steel with Zinc Trivalent Chromate Plating Applicable Codes GSA Group Certificate of Compliance to ANSI Z223.1/NFPA 54 National Fuel Gas Code Section 9.6 Product Standards Intemational Fuel Gas Code(IFGC)Section 411.1 ANSI Z21.75/CSA 6.27—Connectors for Outdoor Gas Appliances B149.1 —Natural Gas and Propane Installation Code and Manufactured Homes (CSA Group)Section 6.21 Scope states"...intended for exterior use above ground for making Uniform Mechanical Code(UMC)Section 1313.0 non-rigid connections...between the gas supply and the gas inlet Uniform Plumbing Code(UPC)Section 1212.0 of an appliance for outdoor installation that is not frequently moved after installation."In addition section 1.5.4 states the connector is Additional Approvals designed for occasional movement after installation.Repeated band- pp ing,flexing or extreme vibration must be avoided.Normal opera- Commonwealth of Massachusetts Board of State Examiners ton of a clothes dryer, rooftop HVAC unit or SIMILAR OUTDOOR of Plumbers and Gas Fitters APPLIANCE DOES NOT constitute extreme vibration or movement, ANSI Z21.24/CSA 6.10—Connectors for Gas Appliances Additional Testing (Excluding 60161 Series) UL2200-2015:Stationary Engine Generator Assemblies CIA` Section 668 Vibration Test. c us Product Configurations LE NPT) In In in r'n OL4835A CAN30-3131-14GL 30 '/ % Yz 14 OL4836A CAN40-4141-14GL 40 % 1 % 14 OL4836C CM60-6161-15GL 60 1 l 1 e: 1-'le 15 "CAN"prefix indicates product supplied with both English and French instructions for Canada Ali installations must completely comply with all Dormont manufacturing company warnings and Instructions,national,state and local codes and all applicable ansi standards. Dormontproduct specifications in U.S.customary units and metric are appropmate and am pmvided for reference only For precise measure- 1)6fmont ® mends,please contact DormoatTechdcal service.Domant reserves the dght to change or moTO product deslgn,construction,specifications, or materials wrttrout prior notice and without incurring any obligation to make such changes and modifications on Dormant produces previously or subsequently sold.eteter to the owner's manual for warranty information. A WATFS Brand L�LP GAS SIZING TABLES FOP PC P P Maximum Capa+rrf�r of PE Pips in Thousands of BTU per Hour of Liquefied Petroleum Gas with a Gas Pressure of 11,04n.WC and a Pressure Drop of 0:5 in,WC (based on a 1.52 specific gravity gas) • 1 ! ! .! ! ! 187 125 99 84 74 67 56 50 45 47 38 35 33 29 26 1073 720 571 484 425 383 325 286 257 235 218 204 192 169 152 1391 934 740 627 551 497 421 370 333 305 283 264 249 219 197 1983 1331 1054 893 786 708 600 528 475 435 403 376 354 311 280 3563 2391 1894 1605 1472 1272 1078 948 854 781 723 676 636 560 504 4724 3247 2608 2232 1978 1792 1534 1359 1232 1133 1054 989 934 828 750 10063 6755 5351 4535 3989 3592 3044 2678 2411 2207 2044 1970 1797 1581 7424 11 / 11 ! .!! 11 :11 •11 111 11 • •! !! 11 22 20 18 15 13 12 11 10 9 9 8 8 8 7 7 129 113 102 86 76 68 63 58 54 51 48 46 44 42 40 167 147 132 112 99 89 81 75 70 66 63 60 57 54 52 238 209 188 760 140 126 116 107 100 94 89 85 81 78 75 427 376 338 287 252 227 208 192 180 169 160 152 146 140 134 642 569 516 441 391 354 326 303 285 269 255 244 233 224 216 1207 1061 956 810 712 642 587 544 508 478 453 431 411 394 379 25 7 6BTUh=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 Drbp of 1.0 psi (based on a 1.52 specific gravity gas) 196 1310 1046 886 779 702 595 523 471 431 399 373 351 309 278� 11300 7586 6008 - 5092 4479 4033 3418 30D7 2707 2478 2295 2144 2018 1775 1599 14652 9835 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 25183 19946 16905 14869 13389 11348 9982 8988 8226 7618 7119 6700 5894 5307 43429 29848 23969 20515 18182 16474 14100 12496 11322 10417 9691 9092 8589 7612 68 77 105963 71131 56339 47750 4200D 37820 32054 28194 25388 23234 21517 20108 18926 16647 14990 / / // / 1/ .// !/ .11 •/! 111 // // 1/ .11 11 236 207 187 158 139 726 115 106 99 93 88 84 80 77 74 1355 1192 1073 910 800 720 659 611 577 537 508 484 462 443 425 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 1688 1605 1533 1469. 1472 5903 5232 4740 4057 3596 3258 2997 2788 2616 2471 2347 2239 2144 2060 1985 127D5 11175 10063 8529 7502 6755 6182 5725 5350 5036 4767 4535 4331 4150 3988 2516BTUh=1CFH Maximum Capacity of PE Pipe in Thousands of BTU per Hour of liquefied Petroleum Gas with a Gas Pressure of 70.0 psi and a Pressure drop of 1.0 psi (based on a 7.52 specific gravity gas) 2476 1662 1316 1116 981 884 749 659 593 543 603 470 442 380 350 74234 9555 7566 6414 5642 5080 4306 3787 3470 3121 2890 2707 2542 2236 2014 18455 12388 9812 8316 M15 6587 5583 4910 4422 4047 3747 3502 3296 2899 2611 26296 17652 73981 11849 10423 9385 7954 6997 63DO 5766 5340 4990 4697 4731 3720 47252 31720 25123 21293 18729 16865 14294 12572 11321 10361 9595 8967 8440 7423 6685 53960 37087 29782 25489 22591 20469 17579 15527 14068 72943 72041 11297 10671 9458 8569 133476 89601 70967 60148 529D5 47640 40376 35514 3798D 29267 27104 25329 23840 20970 18882- 11 / / // rr 297 261 2 5 199 175 156 144 134 125 118 111 106 101 97 93 1707 1501 1352 1146 1008 907 830 769 719 676 640 609 582 557 536 2213 1946 1753 1485 1306 1176 1077 997 932 877 830 790 754 723 695 3153 2773 2497 2716 7862 1676 1534 1421 7328 1250 1183 1125 1075 1030 990 5665 4983 4487 3803 3345 3D12 2757 2553 2386 2246 2726 2022 1931 1857 1 7334 6500 5890 5041 4468 4048 3724 3465 3251 3071 2916 2782 2664 2560 2466 16004 14077 72676 10743 9449 8509 7787 7212 6739 6343 6005 5712 5455 5227 5024 2576BTUh=7CFH Ph: 1.800.662.0208 o Far.:615.325.9407 Web:www.gastife.com 7