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HomeMy WebLinkAbouttank specc ABOVEGROUND/UNDERGROUND DOMESTIC TANKS 120 - 2.000 vvg 8” dome in black plastic or white galvanized steel. 19 NEW! 7ROU�LY F1NEIS&.500 WITH SHERWI'N- WILL IAI VIS. POVJDURA'_, OneCure Super Durable Topcoat with Zinc Rich Primer on Aboveground POVJOURA OneCure T!;ro coal system properties include: 7;r: • SUIT_r !�llf;:I1�C i (:�(,�r�i�!_ - �„f IUl/r �1;:: • 5u11!'r!r�r r,ptlL''�•i ;:uG �_Ci:r U!OItC(u�!1 • F.::•.'=r,t (;:i;��!it_i trnrui?Ic!I I;!u;!� r �:!.C: I'JI) I • Dual sPJN,Ge oetio^us for aoove or undergrounc •Dotion # 1- Pp-ady-to-bury red oxide durable povlid--r coatir, th lac k. • p»Ijethylsne .ACU a dour • Option r : �b�v_ground cptio'n with steel 8- AGUG dome • Allvalaes and float gauges are :entered under dome • Fabricated to rre lawst A,S.M.E. Code, section Vlll, DMsion 1 . Fiegis'tered "nth the t4ational Board • #,`72 liquid level outage valve orifice reduces refueling emissions • Vacuum pre -purged to save time. money and pFodu t 4pprmabW_ ,C,dp stat`, or local regulations may containspeclfcrequinmenisfor C O Pfd TA t M E R S Protective :oa!ing5 and caihod!cprote�on- The purchaserandinstallerare respgnsibic for campliance vott; ail federal, state, local and NFPA industry regujations Cathodic Fritaining Our . • - • protection is r=qu,reo and coating mustbe continuo), and uninterrupted and must co m. ply i r'h en local, tate or national code. .v�,^nl.TrinityContainers.com Cali Toll Free: 888-558-8265 Aug=TRINITY. Containing Our World's Energy'" General Specifications Conforms to the latest edition of the ASME code for Pressure Ves", Section Vill, 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. WfFHDRAWAL VALVE FLOAT .'/ LPn \`� GAUGE ANODE 6-coNrJEcrloN FILLER VALVE SERVICE/ NAME MULTiVALVE PLATE RELIEF VALVE FJTTINGS LAYOUT UNDER DOME f � All vessels dimensions are approximate r. _ o � C7 S W w QJ HEAD J n OUTSIDE LEG WEIGHT DIAMETER 0 n 0 TYPE LENGTH F WIDTH SPACING 0 F FULL PER LEG WIDTH General Specifications Conforms to the latest edition of the ASME code for Pressure Ves", Section Vill, 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. WfFHDRAWAL VALVE FLOAT .'/ LPn \`� GAUGE ANODE 6-coNrJEcrloN FILLER VALVE SERVICE/ NAME MULTiVALVE PLATE RELIEF VALVE FJTTINGS LAYOUT UNDER DOME Rev: Jan. 27, 2016 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 ---j LOAD STACK 120 wg. 24" Ellip 5'- 5 13116" 3'. 0" 10 1/8" 31-011 245 tbs. 96 12 454.2 L 609.6 mrn 1671.3mm 911.4 mm 257.2 mm 914.4 mm 111.1 kg. 250 wg. 31.5" Hemi 7' - 2 1/2" X- 7 112" 12 3/4" 3' - 6" 4721bs. 63 9 946.3 L 800.1 mm 2197.1 mm 1104.9 mm 323.9 mm 9066,8 mm 214.1 kg. 320 wg. 31.5" Hemi 8'- 11 3/4" 3'- 7 1/2" 12 3/4" 4' - D 114" 5881bs. 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 9y-1011 0" 4'-1 7/16" 15" 5' - D" 871 lbs. 30 6 1892.5.1- 950.5 m1 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 5116" 16 1/4" 9' - 0" 1729 lbs. 15 5 3785.01. 1040-4 mm 43^, 5,6 m;;� 1344.6 mm ^.- (2.S mm 2743.2 mtii 784.3 kg Rev: Jan. 27, 2016 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 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 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 surface or soil variations such as rocks, salts, fertilizer, moisture concentration, oxygen concentration, etc. Preventing Corrosion Protecting underground tanks from corrosion is easily achieved bythe use of two com m only applied protection . methods: external coating and cathodic protection. These two methods are complementarybxm,n 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 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 atthe 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 tankwill 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. Now 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 flowto the tankthat 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 th e 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 ib, and 45 lb. Application Recommendations Magnesium anodes can protect underground tanks in most soil condiffons. The H-1 alloy is generailyvery 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-cenfimeter resistivity. Resistivitles 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 resistivibes 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 extemally 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 Forlile Soils, Clay, Sandy Loam sand, Gravel, Rocky Areas Tank cap. (gal-) 3 to 5090 ohm -cm Size ©ty. Alloy 5000 to 10000 ohm -cm Size Oty. Alloy 120 91 1 H-1 91 1 H-1 150 91 1 14-1 9# 1 H-1 250 W i H-1 9# 2 H-1 325 91 1 11-1 9# 2 H-1 500 170 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 2000 17� 3 H-1 9# 6 H-1 -Based on 90% effective external coaling, 2 ma/f12 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. 1 anode 2 anodes 4 -anodes 4.Anodes are shipped in either cardboard boxes or multi -wall papersacks. Remove outer container and bury the cloth bagged anode. If anode is supplied in plastic bag, remove plastic bag before installing. 5. Install anodes approximately two to three feet from the tank and at least as deep as the center line of the tank. Anodes work best in locations with permanent moisture, so generally the deeper the better. 6.After placing the anode, stretch out the anode connection wire and extend 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: lnsertthe blacktest lead into the Common jack on the meter, and connect the opposite end of the lead to a charged reference electrode (1/2 cel)). 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 % 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. f Note: If any of the four readings are below (less negative) -O.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: 1112011-5000 Loss of Pressure Freeze-up inside the regulator. 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 bent where free flow of the LP -Gas is restricted. These freeze -ups can occur when the moisture, gas flow and temperature combine to create a hazardous condition. Freeze -ups can occur at temperatures above 32`F. Action Required: All LP -Gas should be checked for moisture content prior to delivery to consumers and proper amounts of anhydrous methanol added if the gas cannot be returned to the supplier. Any container suspected of having excessive moisture should be treated With the proper amount of methanol. Customer Safety Since regulators are often used by consumers without previous knowledge of the hazards of LP -Gas, and the LP -Gas dealers are the only ones who have direct contact with the consumers, It is the dealer's responsibility to make sure that his customers are properly instructed in safety matters relating to their installation. At the very minimum, it is desirable that these customers: 1. Know the odor of LP -Gas and what to do in case they smell gas. Use the NPGA "Scratch in Sniff" leaflet. 2. Are instructed to never tamper with the system. 3. Know that when protective hoods are used to enclose regulators and/or valves, that these hoods must be closed, but not locked. 4. Keep snow drifts from covering regulators. 5. Know the location of the cylinder or tank shut-off valve in emergencies. Underground Installations 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 j 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. I Refer to NPGA No. 401. R Regulator adjustment closure cap must be tight. End of regulator vent or vent tube i Grade ground downward and to be located above the highest away around housing dome. probable water level. This prevents water collecting and running into or standing 2 to 6 inches arounddome. minimum. 6 inches minimum / (18 inches minimum if subject to vehicular traffic). Note: Water mark left in housing dome at level above regulator vent, or end of vent tube requires replacement of regulator. Then correct installation. General Warning All RegO Products are mechanical devices that will eventually become inoperative due to wear, contaminants, corrosion and aging of components made of materials such as metal and rubber. As a general recommendation,Regulators should be replaced in accordance with all of the recommendations outlined in this safety warning. The recommended service life of a regulator is one of many factors that must be considered in determining when to replace a regulator. The environment and conditions of use will determine the sane service life of these products. Periodic inspection and maintenance are essential. Because RegO Products have a long and proven record of quality and service, LP -Gas dealers may forget the hazards that can occur because a regulator is used beyond its safe service life. Life of a regulator is determined by the environment in which it "lives." The LP -Gas dealer knows better than anyone what this environment is. NOTE: There is a developing trend in state legislation and in proposed national legislation to make the owners of products responsible for replacing products before they reach the end of their safe useful life. LP -Gas dealers should be aware of legislation which could affect them. AEGj7 100 RegO Dr. Elon, NC 27244 USA www.regoproducts.com +1 (336) 449-7707 Ok First Stage Regulator with Relief Valve and Pressure Tap - e regulator is truly the heart of an LP -Gas installation. It must .:-pensate for variations in tank pressure from as low as 8 PSIG �3 10 PSIG - and still deliver a steady flow of LP -Gas at 11" w_c. n consuming appliances. The regulator must deliver this pressure !Wle a variable load from intermittent use of the appliances. zagh a single -stage system may perform adequately in many -_�X_Oations, the use of a two-stage system offers the ultimate in pin - j -=t regulation. Two-stage regulation can result in a more profitable -P-Gas operation for the dealer resulting from less maintenance and `twer installation callbacks - and there is no better time than now for `stalling RegO Regulators in two-stage systems. k : auriform Appliance Pressure 1?�e installation of a two-stage system - one high pressure regulator a: 1e container to compensate for varied inlet pressures, and one :w pressure regulator at the building to supply a constant delivery pessure to the appliances - helps ensure maximum efficiency 37d trouble-free operation year-round. It is important to note that ahiie pressure at the appliances can vary up to 4" w.c. using single- sl✓ge systems, two-stage systems keep pressure variations within 1- w.c. New high -efficiency appliances require this closer pressure omitrol for proper ignition and stable, efficient operation. In fact, one major manufacturer requires the use of two-stage systems with their Jppliances. Reduced Freeze-ups/Service Calls R egulator freeze-up occurs when moisture in the gas condenses and ;,-ezes on cold surfaces of the regulator nozzle. The nozzle becomes chilled when high pressure gas expands across it into the regulator body. This chilling action is more severe in single -stage systems as gas expands from tank pressure to 11" w.c. through a single regulator nozzle. Size The System Correctly Prior to installing your two-stage system, be sure the system pipe and tubing is properly sized. Proper sizing will help ensure constant delivery pressure to the appliances during fluctuating loads at all times. Just as important, be sure the RegO Regulators you choose are capable of handling the desired load. This is another advantage of two-stage systems - they are capable of handling much more BTU's/hr. than single -stage systems. The RegO "LP -Gas Serviceman'S MaiIueJ" provides ccinplote infr�nnation on pipo sizing and proper regulator selection. Two-stage systems can greatly reduce the possibility of freeze -ups and resulting service calls as the expansion of gas from tank pressure to 11" w.c. is divided into two steps, with less chilling effect at each regulator. In addition, after the gas exits the first -stage regulator and enters the first -stage transmission line, it picks up heat from the line, further reducing the possibility of second -stage freeze-up. Service calls for pilot outages and electronic ignition system failures are also reduced as a result of more uniform appliance pressure from two-stage systems. Economy of Installation In a single -stage system, transmission line piping between the container and the appliances must be large enough to accommodate the required volume of gas at 11" w.c. In contrast, the line between the first and second stage regulators in two-stage systems can be much smaller as it delivers gas at 10 PSIG to the second -stage regulator. Often the savings in piping cost will pay for the second regulator. As an additional benefit, single -stage systems can be easily converted to two-stage systems using existing supply lines when they prove inadequate to meet added loads. This is the least expensive and best method of correcting the problem. Allowance for Future Appliances A high degree of flexibility is offered in new installations of two- stage systems. Appliances can be added later to the present load - provided the high pressure regulator can handle the increase - by the addition of a second low pressure regulator. Since appliances can be regulated independently, demands from other parts of the installation will not affect their individual performances. Replace Pigtails If you are replacing an old regulator, remember to replace the copper pigtail. The old pigtail may contain corrosion which can restrict flow. In addition, corrosion may flake off and wedge between the regulator orifice and seat disc - preventing proper lock-up. ' Req» First Stage RegWators witih Bunt -in Relief Valves First Stage Regulator with Relief Valve and Pressure Tap With no first stage relief valve, propane liquid may form here... Resulting in sudden pressure surge due to flashing into vapor here! First stage relief can prevent liquid from forming in first stage piping during periods with no gas demand! I 1 Pressure at which liquid can form at various temperatures. Vapor Pressures of LP -Gases C9 n. N N d a -40 -20 0 20 40 60 80 100 120 Temperature °F. The Problem Many modem LP -Gas appliances are equipped with pilotless ignition systems. Water heaters and older appliances use pilot lights, but it has become a common practice for energy conscious homeowners to shut=off the pilot when leaving home for extended periods of time. In each instance, there is no gas demand at all for extended periods. The Consequences If the first stage regulator fails to lock-up tight, usually as a result of a worn seat disc or foreign material lodged between nozzle and seat disc, pressure will build-up in the first stage piping — possibly to a level that approaches tank pressure. Combining this with warm ambient temperatures and cool ground, propane liquid may form in the first stage piping. When gas demand resumes, this liquid may pass through the second stage regulator into the appliances and furnace. NOTE the second stage regulator will not relieve the pressure in first stage piping. The rapid vaporization of the liquid may cause a rapid pressure surge that could seriously damage critical components of the appliance and furnace controls. I A fire or explosion could occur as a consequence. The Solution RegO LV4403 Series First Stage Regulators with Built -In Relief Valves reduce the possibility of this serious hazard in two stage applications. The built-in relief valve is designed to vent as needed and reduce the possibility of first stage piping pressure from becoming high enough to form liquid. ® �� 100 Rego Dr. Elon, NC 27244 USA vnvw.regoproducts.com +1 (336) 449-7707 11 Ideal for use as a first stage regulator on any domestic size ASME or vosra, DOT container in propane gas installations requiring up to 1,500,OOb BTU's per hour. The regulator is factory set to reduce container �L pressure to an intermediate pressure of approximately 10 PSIG. ' 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. Provides accurate first stage regulation in two-stage bulk tank systems. Reduce tank pressure to an intermediate pressure of 5 to 10 PSIG. Also used to supply high pressure burners for applications like industrial furnaces or boilers. Also incorporated in multiple cylinder installations. LV4403SR4 /„ P 5 .1-5 LV4403TR4 NPT '/a" P 10 5-10 1100�LV4403SR9 NPT 5 1-5 LV4403TR9 �" 10 5-10 Yes 2,50D,000 LV4403SR96 F. POL %4" 5 1-5 LV4403TR96 F NPT 10 5-1 D '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. Designed to reduce first stage pressure of 5 to 20 PSIG down to burner pressure, normally 11" w.c. Ideal for medium commercial installations, multiple cylinder installations and normal domestic loads. LV4403134 . %" LV4403B46 %" F NPT 11" w.c. at LV4403840 428 10 PSIG LV4403566 '/." F. NPT Drill Inlet LV4403B66R' '�" F NPT Backmount design " Maximum now based on 10 PSIG inlet and 9" w.c. delivery pressure 9" to 13" I Over Inlet I 935,000 W.C. LV3403TH LV4403Series LV4403S seane= Job Name Job Location Engineer _ Approval _ Donncant Supr=Safu® Flexible Gas Appliance Connectors 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) Operating Pressure MAX 0.5psi (3.45 kPa) Hydrostatic Burst Pressure MIN 250psi (1725 kPa) e Flepble Tube Material Annealed 304 Stainless Steel Flare Nut Material Carbon Steel with Zinc Trivalent Chromate Plating o Flare Adapter Material Carbon Steel with Zinc Trivalent Chromate Plating CSA Group Certificate of Compliance to Product Standards ANSI 221.75/CSA 6.27 - Connectors for Outdoor Gas Appliances and Manufactured Homes Scope states "...intended for exterior use above ground for making non -rigid connections... between the gas supply and the gas inlet of an appliance for outdoor installation that is not frequently moved after Installation." In addition section 1.5.4 states the connector is designed for occasional movement after installation. Repeated bend- ing, flexing or extreme vibration must be avoided. Normal opera- tion of a clothes dryer, rooftop HVAC unit or SIMILAR OUTDOOR APPLIANCE DOES NOT constitute extreme vibration or movement. ANSI Z21.24/CSA 6.10 - Connectors for Gas Appliances (Excluding 60/61 Series) �A• c us Product Configurations OL4835A CAN30-3131-14GL 30 OL4836A CAN40 4141-14GL 40 OL4836C CAN60-6161-15GL 60 "CAN" Mfg indicates product supplied with bat English and French instructions for C All installations must completely comply with all Dormont manufacturing company warnings and lnstructions, national, state and local codes and all applicable ansi standards. Contractor Approval Contractor's P.O. No, Representative SKU ES-D-GAC_Generator Generac - ,� fy { For use with Generac stationary outdoor backup/ standby generators. Series 30, 40 and 60 Applicable Codes ANSI Z223.1/NFPA 54 National Fuel Gas Code Section 9.6 International Fuel Gas Code (IFGC) Section 411.1 8149.1 - 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 668 Vibration Test. Dormont product specifications in U.S. customary units end metric are appm)dmate and are prov ded for reference only For precise measure- ments, please Cutdact DormontTechdcal Service. Dummnt rresenres the right to change or moldy product design, construction, specifications, or materials without prior notice and without incurring any obligation to make such changes and modifications on Dormont products previously or subsNuenty sold. haler to the owner's manual for warranty information. Yz 14 I/ 14 15 1)6fmon - A WATTS Brand Maximum Capacity of PE Pipe in Thousands of BTU per Hour of Uquefled Petroleum Gas with a Gas Pressure of 11.0dn. WC and a Pressure Drop of 0:5 in, WC (based on a 1.52 specific gravity gas) 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 f 427 376 338 287 252 227 208 192 180 169 160 752 146 140 134 642 569 516 441 391 354 326 303 285 269 255 244 233 224 216 1207 1061 956 810 712 642 587 544 508 478 - 453 431 411 394 379 133476 89601 70967 60148 52905 47640 40376 (based on a 7.52 specific gravity gas) 3198D 29267 27104 25329 25 7 6BTUh= 7 CFH 20970 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) Tubing Length (ft) 60 J 70 j :O 1 90 1 IN 1 125 1 150 196 1319 l0 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 67DO 5894 5307 43429 29848 23969 20515 18182 16474 14100 12496 11322 10477 9691 9092 8589 7612 6897 105963 71131 56339 47750 42000 37820 32054 28194 25388 23234 21517 20108 18926 16647 14990 236 207 187 158 139 125 175 106 99 93 88 bA bu // /4 1355 1192 1073 910 800 720 659 631 577 537 508 484 462 443 425 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 6756 6182 5725 5350 5036 4767 4535 4331 4150 3988 9595 8967 8440 7423 6685 53960 37087 2516BTUh=7CFH 25489 22591 20469 Maximum Capacity of PE Pipe in Thousands of BTU per Hour of liquefied Petroleum Gas 12943 72041 11297 10671 with a Gas Pressure of 70.0 psi and a Pressure drop of 1.0 psi 133476 89601 70967 60148 52905 47640 40376 (based on a 7.52 specific gravity gas) 3198D 29267 27104 25329 23840 20970 2476 1707 1662 1316 1116 981 884 749 659 593 543. 503 4/u 442 389 3bu 14234 9555 7568 6414 5642 5080 4306 3787 3470 3121 2890 2701 2542 2236 2014 18455 12388 9812 8316 7315 6587 5583 4910 4422 4047 3747 3502 3296 2899 2611 26296 17652 73981 17849 10423 9385 7954 6997 6300 5766 5340 4990 4697 4737 3720 47252 31720 25123 21293 18729 76865 14294 12572 11321 10361 9595 8967 8440 7423 6685 53960 37087 29782 25489 22591 20469 17579 1 15527 14068 12943 72041 11297 10671 9458 8569 133476 89601 70967 60148 52905 47640 40376 35514 3198D 29267 27104 25329 23840 20970 8882 18882- 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 83D 790 754 723 695 3153 2773 2497 2116 7862 1676 1534 1421 7328 1250 1183 1125 1075 1030 990 5665 4983 4487 3803 3345 3D12 2757 2553 2386 2246 2126 2022 1931 1857 1779 7334 6500 5890 5047 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 2576BT1Jh=7CFH i Ph: 1.800.662.0208 e Far.: 615.325.9407 a Web: www.gastife.com