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HomeMy WebLinkAboutArce tankAll APPLICABLE INFO MUST BE COMPLETED FOR APPLICATION TO BE ACCEPTED Date .: ;J Planning and Development Services Building and Code Regulation Division 2300 Virginia Avenue, Fort Pierce FL 34982 Phone: (772) 462-1553 Fax: (772) 462-1578 Permit Number: Building Permit Application Commercial Residential E� PERMIT TYPE; a PROPOSED IMPROVEMENT LOCATION: r Address: f { i`rt Z4n e c+ A `e-rGC Fzclr,; d Property Tax ID#: f rC 7 - 6,0 7 Lot No.� Site Plan Name: rce- 6 G 5 Block No. Project Name: DETAILED DESCRIPTION OF WORK: I CONSTRUCTION INFORMATION: Additional work to be performed under this permit— check all that apply: _Mechanical — Gas Tank as Piping _ Shutters _ Windows/Doors Electric _ Plumbing _Sprinklers Total Sq. Ft of Construction: Cost of Construction: $ 000 Generator Roof Pitch Sq. Ft. of First Floor: Utilities: —Sewer —Septic Building Height: OWNER/LESSEE: CONTRACTOR: Name �;_ i,�i_�_�;r�A.rGP _ Dame:Blake Cowdell Address: '% �n G e- Company: Energized Gas City: + `CrC State: _Z�_z Zip Code: Fax: Phone No. Address:1786 SW Biltmore St City: Port ST Lucie State: EL Zip Code: 34984 Fax: Phone No7727778133 E-Mail: Fill in fee simple Title Holder on next page ( if different from the Owner listed above) E-Mail energizedgenerators@gmail.com State or County License LG34747 it value or construction is !�[SUU or more, a RECORDED Notice of Commencement is required. If value of HVAC is $7,500 or more, a RECORDED Notice of Commencement is required. SUPPLEMENTAL CONSTRUCTION LIEN LAW INFORMATION: DESIGNER/ENGINEER: Not Applicable Name: MORTGAGE COMPANY: Not Applicable Name: Address: Address: City: State: Zip: Phone City: State: Zip: Phone: FEE SIMPLE TITLE HOLDER: Not Applicable Name: BONDING COMPANY: Not Applicable Name: Address: Address: City: City: Zip: Phone: Zip: Phone: OWNER/ CONTRACTOR AFFIDVIT: Application is hereby made to obtain a permit to do the work and installation as indicated. I certify that no work or installation has commenced prior to the issuance of a permit. St. Lucie County makes no representation that is granting a permit will authorize the permit holder to build the subject structure which is in conflict with any applicable Home Owners Association rules, byiaws or and covenants that may restrict or prohibit such structure. Please consult with your Home Owners Association and review your deed for any restrictions which may apply. In consideration of the granting of this requested permit, I do hereby agree that I will, in all respects, perform the work in accordance with the approved plans, the Florida Building Codes and St. Lucie County Amendments. The following building permit applications are exempt from undergoing a full concurrency review: room additions, accessary structures, swimming pools, fences, walls, signs, screen rooms and accessory uses to another non-residential use "WARNING TO OWNER" YOUR FAILURE TO RECORD A NOTICE OF COMMENCEMENT MAY RESULT IN YOUR PAYING TWICE FOR IMPROVEMENTS TO YOUR PROPERTY. A NOTICE OF COMMENCEMENT MUST BE RECORDED AND POSTED ON THE JOB SITE BEFORE THE FIRST INSPECTION. IF YOU INTEND TO OBTAIN FINANCING, CONSULT WITH YOUR LENDER OF COMMENCEMENT." O�'R AN ATTORNEY BEFORE RECORDING YOUR RJ/ ?�� Jotaiw jNOTICE 7 Signature of Owner/ Lessee/Contractor as Agent for Owner STATE OF FLORI COUNTY OF X Th�y forgoing inst ument was acknowledg d before me thin ,day of 20 y _ NO l 0 4 � I cif' �_Y � � Signature of Contractor/License Holder STATE OF FLORI A COUNTY OF The f oing mstr ment was acknowledge before me this ay of j 20, 2` by � lJi � L 1 �� P Name of person making tement. Personalty Known OR Produced Identification Type of Identification Produced ,i f (Signature ?u 3°dl& 2*946 *� �F ¢j(PIRES: June 27, 2022 Commissio my AC M*Mft� Name of person making statement. Personally Known OR Produced Identification Type of Identification Produced f (Signature of N Commission No DA3WiEl E GOIJ(; t1• FS ,: :,: IFYCEsMIISSIUi�#�32945 EX-PIRCB: Ji.r;e 27, 2022 •':!?�P'c'ar 8.1Vd Thai Neay t uLbc UiNWwIftas REVIEWS FRONT COUNTER ZONING REVIEW SUPERVISOR REVIEW PLANS REVIEW VEGETATION REVIEW SEATURTLE REVIEW MANGROVE REVIEW DATE RECEIVED DATE COMPLETED Energized Gas Inc Ctopane and cAratatcd 6tco 8pecialat Proposal / Agreement George Arce 9414 Bunting Lane Fort Pierce, FL, 34951 772-461-4448 BeverlyArce56@gmail.com March 171", 2020 1) Supply and install (1) customer owned 500 gallon underground LP tank with gas line to generator and final connect 2) Obtain all permits & inspections needed 3) Price includes backfilling and removing dirt 4) Price does NOT include filling the tank with propane NOTE: Tank and line to be installed by Thompson Gas or the sum o :4, 000.00 1786 SW Biltmore St, Port ST Lucie, FL, 34984 *Licensed & insured FL34747 Toll Free 855-PROGAS4 *Treasure Coast 772-777-8133 *Palm Beach 561-752-0214 *Fax 772-318-6673 TERMS: Charges & Payments: Charges are due in full at time services are rendered unless otherwise stated below. Contractor may charge and customer agrees to pay a late fee for all past due payments, such fees not to exceed the maximum allowed rate by applicable law. Customer shall be responsible and agrees to pay for all charges billed, applicable taxes, applicable legal fees and other charges/fees. Proposal/Contract pricing good for 30 days from Proposal/Contract date $800.00 is due @Signing $2,000.00 is due @ Tank Installation $1,200.00 is due @ Completion We appreciate the opportunity you have extended us to quote on this work and would like to thank you in advance for your consideration. Authorized signature: complete the work in terms ouGtined above� , 4, Signatfire Roger Lussier Acceptance of Proposal (printed name), authorize Energized Gas to accordance with the above specifications and conditions. I agree to pay as per Date This agreement shall be construed under the laws of the State of Florida. This agreement contains the entire understanding of the parties and supersedes all previous verbal or written agreements: there are no other agreements, representations or warranties not set forth herein. If any conflicts exist in this agreement between terms which are printed and those which are typed or written, the typed or written language shall govern. Page 2 of 3 Ca 0 0 ed as `,Z— ol i� r f ,e / » � 7 G � �f /© \ \ � / D � r ... N-�.. � - t3 � _ �- - �a a ,x P _] lt�� �fisupe ura��Topcaa . r rF ti', i' _ VlllI zinc Ricfa P�rimer}orbav run 1`_T_m sE +3 7ow WI =; f B 7 c►Of p�xy�primer- _ 8" dome �n f�laeh{�astic o._ui 5upe tlueaile TiC polyester tapcoa _ ga�,uar z l tees$ p�riaiU7-- n an 1ed9 ra e # r - - • - ' , ` �Paf�r�tp�ndtng�"formufatetlEpri�eranditapcoa#•'•� - , F — ------------ Y SI dual sere+ce opi[ans for above:©r� unclegrouncl appiica#tuns . k •` 4pt►ori#i Ready ta.pury red;oXtdecfurable pbuvder coating uvrt#t biactc s' r. • paCyethyW AGlJG,dome` i •: Optlon;#`2..Abovegrounci optron:►nr+tF� steel 8'..AGUG+dome_ ~ If' All valves aknd float gauges are centered untler:'c[ome Fabricated to,the latest:" M.E . Code,;5�2'ct7or Vi11, Division .t i. Regrstered wi'ti��lVa#�ona! 8oad �72 llqurdrlevef o+tage valve orrfice reduces refi�ekng,ernissEons -� • l►acuurrr re ur etl to save trine rr�Qne and raducf P_ P g "A ` pliCatile federal s pptattn ar locafFregatronrmay con#art specrfrc requirements for prgtectrve coatrngslanticatho6'rc pro aroThepurchaser and installer are resp¢ns�61e 1 s for compharrce vrrthtal! ferleraf ysta#e, !o IVFPA rrraf%stryregulations: Cathodic p4td-c ron�l5 requfreii andfcoat g u . e ntrnuausiand'unfnterrupt2d°and rircist ' `_ comply w�th+an laeal�,state or, r"ratrorralrcode- -- — �� L] 0 C7 CO LLi ul 2 � 0 Q 0 wa- W 0 0 0 r 0 THIMYY I -C, �wa Containing Our World's Fnargy'" OUTSIDE DIAMETER 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. Ail 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. -- WITHDRAWAL VALVE - FLOAT •` N0710E1\. LP. gas • ANODE GAUGE CONNECTION r l FILLER O 6, -VALVE 1 � , SERVICE 1 NAME MULTJVALVE PLATE /� RELIEF VALVE FITTINGS LAYOUT UNDER DOME AGUG VESSEL DIMENSIONAL INFORMATION All vessels dimensions are approximate WATER HEAD OVERALL OVERALL LEG LEG WEIGHT QUANTITY CAPACITY. TYPE LENGTH HEIGHT WIDTH SPACING FULL PER FDIAMETER LOAD STACK 120 wg.Ellip 5'- 5 13I16" 3'-0" 1Q 118" 3' - 0" 245 Ibs. 96 12 454.2 L 1671.3mm 911.4 mm 257.2 mm 914.4 mm 11-1.1 kg. 250 W9. 31.5" Hemi 7' - 2 112" T - 7 112n 12 314" 3' - 6" 472 lbs. 63 9 946.3 L 800.1 mm 2197.1 mm 1104.9 mm 323.9 mm 1066.8 mm 214.1 kg. 320 wg_ 31.5" Hemi 8' - 11 314" 3' _ 7 112" 12 314" 4' 0 114" 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. 54]0 v�g- 37:42" Hemi 9' -10" 4' - 1 7/16" 15" 5' - 0" 871 lbs. 30 6 1892.5 L 950.5 mm 2997.2 mm 1255.7 mm 381.0 mm 1524.0 mm 395.1 kg 1000 W9- ' 40.96" Hemi 15' -10 13116" 4' - 4 5116" 16 114" 9' _ 0" 1729 lbs. 15 5 3785.0 L 1040.4 mm 4846.6 mm 1344.6 mm 412.8 mm. 2743.2 mm 784.3 kg Rev: Jan. 27, 2616 why Tanks Corrode Underground steel tanks corrode due to an electrochemical reaction between the tank and the surrounding soil. The process of corrosion occurs duo to small voltage differences on the steel surface that result in the flow of UG current from ono location to another. Where current flows from the tank into the soil corrosion occurs. This location is tailed the anode in a corrosion circuit. Where current flows from the soil to the tank, no corrosion occurs. The progress of corrosion is determined by the amount of current flowing between the anode and the cathode and whether the locations of the anode/ cathode remain constant overtime. Corrosion rates are generally higher in wet soil environments since the conductivity of the soil promotes the flow of DC current in the corrosion circuit. Corrosion generally exhibits itself on underground tanks in either a general overall rusting or more commonly, a pitting attack. Pit locations may result from metallurgical conditions of the steel suraface or soil variations such as rocks, salts, fertilizer, moisture concentration, oxygen concentration, etc. - Preventing Corrosion Protecting underground tanks from corrosion is easily achieved by the use of two commonly applied protection methods: external coating and cathodic protection. These two methods are complementary and should be used in conjunction with the other. An a fective 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 orsoil 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 electdcal grounds is critical for the cathodic protection system's effectiveness. Now Sacrificial Galhodie Protection Works Sacrificial systems work by creafirig a galvanic connection between two different metals. The most common anode material is magnesium, which when coupled to steel results in DC current flow from the magnesium to the steel. The open circuit potential of steel is about -0.50 volts referenced to a copper sulfate electrode. The open circuit potential of magnesium is about -1.55V to-1.80V. By connecting the two metals together, the difference of 1 to 1.25V volts results in current flow to the tank that overcomes the natural corrosion cells that exist on the tank. With this current available to the tank, no corrosion occurs. Magnesium Anodes There are a variety of anode sizes and alloys used for cathodic protection. The two primary alloys are designed as H-1 (or AZ63) and Nigh 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 backffll 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. Rppifcation 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 quanfity recommendations forvarious size tanks 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' 1n 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 thatwill accelerate corrosion of the steel tank when directly connected to copper piping, Generally, copper piping does not require cathodic protection. SaiE T��pe E ffi 5 ���, ,.' Sand, Bratrel, Rochy Areas Tank Cap. (gal.) to €0000 ohm -cm iz� (1.ty<: .Alloy Size n,, Ahoy 150 60; 1 H-1 9# 1 H-1 250 BIJ 1 H-I 9# 2 H-1 325 i# 1 H-1 9# 2 H-1 5007 1 H-1 9# 2 H-1 10007 - _ 2 . - . - -H-� 9# 4 HAt500 13# 2 H-1 91 4 H-1 2000 - 1*. I 3 . H-1 90 *Based on 90% effective external coating, 2 ma/ft2 current density, and 30- yearAnode fife. Anode Installation 1. Determine size and quantity of anodes from application chart. 2. When a single anode is installed, it should he located near the tank center on either side of tank. 3.When. multiple anodes are installed, space them evenly around the tank. See examples below. 7 anode 2 anodes 4 anodes c , cDO c 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. G.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. Mor,hanical oat nacHon Under loome Cathodic Protection Testing Procedure Equipment deeded: 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 lack 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 multivaive. A good solid connection is very important. (DO NOT connect to shroud). STEP?: insert the black test lead into the Common jack on the motor, and connect the opposite end of the lead to a charged reference electrode Ch 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) atfour 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 deeperinto 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 Elecfrude STEP 1: Unscrew and remove porous plug end of new reference electrode. Add delonized 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 electrade to contact nil, road salts, ar other substances that may contaminate the solution by absarption through porous plug. Do not allow electrode to freeze. Distributed By: r�='�rI_ tlsd;5���w-�i Ideal for use as a first stage regulator on any domestic size ASME or }� DOT container in propane gas installations requiring up to 1,500,000 LISTED BTU's per hour. The regulator is factory set to reduce container pressure to an intermediate pressure of approximately 10 PSIG. Compact design can be connected to a service valve using either a POL adapter or a RegO product pigtail. Large threaded Y? F NPT bonnet vent can easily be piped -away underground installations without the need of glue kits or extra adapters. Non Adjustable Large flow orifice resists freeze ups due to water concentration in LPG vapor. • Design provides for good flow regulation at both high and low container pressures. jBuilt 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 regulator's delivery pressure. • Molded diaphragm provides an o-ring, type seal between the bony 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 23D2-31. RE Body............................................................................................Zinc Bonnet........................................ .............................................Zinc Spring... ............... --................................... .............................. Steel Seat Disc ....................................... Resilient Rubber Diaphragm...........................Integrated Fabric and Synthetic Rubber 61WN, 250.W6 SV°p✓J )ARa 1l .� f.5o1P� VSRVCC F OWPROPANE LV3403TR Over Outlet LV34037TRV9 1 1" FNPT W FNPT 7132, 10 PSIG 9:00 1,500,DDD " Maximum flow based on inlet pressure 20 PSIG higher than the regulator selling and delivery pressure 20% lower than fhe regulator setting and deliverypressure 20% lower than the setting. A14 16 MM 100 RagO Dr. Eton, NG 27244 LFSA www.regoproducts.corrr +i (335) 449-7707 31WIM"CReft.I 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 dornestio loads. TW 90 degree right angle inlet to outer connection for meter or standard installations_ Large vent helps to prevent blockage and has W 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 W F. HPT outlet. Plug can be removed with a 311W hex alien wrench. Select Brown Finish W01-a�AK 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 Valve Seat Disc ..................................................... Resilient Rubber Diaphragm ......................... Integrated Fabric and Synthetic Rubber MY 2 10 ��l ❑ L U BTUAY. 5+/4„ C WIfflonn ingSMckee LV4403E66RA / 1' F. NPT 3/4" F. NPT 3116" 11" yr c• at 1{l 9" to 13" W.C. Over Inlet 1,000,000 L1l4403B56RA8*T PSIG Inlet • Maximum 0ow is based on 10 PSIG inlat and W w.c. delivery pressure. *' Mouuting Bracket included. py ?DO Rsg6 Dn Elon, NC 27244 USA w .regoproducts.com +1 (336) 449-7707 10ME� .421 Job Name _ Job Location Engineer Approval Contractor Approval Contractor's PO, No. Representative SKU ES-D-GAG Generac installSmart Li1� racy r cr>,�3LLT.."rCj Flexible Fuel Lines The flexible connection between the gas supply and the gas inlet - of a Generac® Stationary Outdoor Backup/Standby Generator Features o Operating Temperature -407 to 150°F (-40'C to 65.6°C) Operating Pressure MAX 0.5psi (3.45 kPa) a Hydrostatic Burst Pressure MIN 250psi (1725 kPa) a ReAble Tube Material Annealed 304 Stainless Steel a Flare Nut Material Carbon Steel with Zinc Trivalent Chromate Plating o Flare Adapter Material Carbon Steel with Zinc Trivalent Chromate Plating . PVC Dip Coating Gray Heavy Duty, Antimicrobial, UV Stabilizer CSA Group Certifijcato of Compliance to Product Standards ANSI 721.75/CSA 6.27 — Connectors for Outdoor Gas Appliances and Manufactured Homes Scope states "...intended for exterior use above ground for making non -rigid connections... between the gas supply and the gas inlet of an appliance for outdoor installation that is not frequently moved after installation." In addition section 1.5.4 states the connector is designed for occasional movement after installation. Repeated bending, flexing or extreme vibration must be avoided. Normal operation of a clothes dryer, rooftop HVAC unit or SIMILAR OUTDOOR APPLIANCE DOES NOT constitute extreme vibration or movement. ANSI Z21.24/CSA 6.10 — Connectors for Gas Appliances �PB (Excluding 60/61 Series) P c us Product Configurations For use with Generac stationary outdoor backup/ standby generators. Applicable Codes ANSI 7223.1/NFPA 54 National Fuel Gas Code Section 9.6 intemational Fuel Gas Code (1FGC) Section 411.1• B149.1 — Natural Gas and Propane Installation Code (CSA Group) Section 6,21 Uniform Mechanical Code (UMQ Section 1313.0 Uniform Plumbing Code fUPC) 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 €lormont prodact spRditations in U& cusbmary m b and metric are approximate and are provided for reference only. For precise measurements, please corltactl)= Afechnical Service_ Durment reserves the right to change ormeddy pmduddedgn, construction; specifications, ormatedals without prior nice and Yftt thn :Wng anyubligation to make such changes and modrfications'on Durmunf products previously orsubsequerify sold. Refer to the owner's manual for t awanty info ma5Da D6fA9OfiE A WAS Brand Maximum Capacity of PE Pipe in Thousands of BTU per. Hour or L qu-:E�fled PM-Toleam Gas wi i t G vies ProssQr2 of T 1.0 in. WC and ci Piessura Drop of 0.5- i€1.1MC (bases( an a 7.52 specific gravffil-9 s) l.0 113 IV 102 Ja 86 is 76 )G id lu 68 63 58 y 54 y 8 51 48 8 46 8 44 7 42 7 40 747 209 132 188 112 160 99 140 89 B1 75 126 116 107 70 IDD 66 63 94 89 60 85 57 81 54 78 52 75 376 569 338 516 287 441 252 391 227 208 192 354 326 303 180 285 169 160 269 255 152 244 146 233 140 224 184 2T6 1061 956 810 712 642 587 544 508 478 453 431 411 394 379 2516BTUh= T CFH f"10)(imurn Capacity of PE Pipe in Thousands of BT U per dour of Liquefied Petroleum vas with as Gas Pressure of 2.0 psi and a Pressure Drop of 7.0 psi (based on a 1.52 specirc gravfiy gas) 1966 1319 1045 886 779 702 595 523 471 43T 399 373 - 351 309 278 11300 7586 6008 - 5092 4479 4033 3418 3007 2707 2478 2295 2144 2018 1775 1599 14652 9835 7790 66D2 5807 5229 4482 3898 3510 3213 2976 2780 2617 2302 2073 2DB77 14014 11100 9408 8275 7457 6375 5555 5002 4578 4239 3962 3729 3280 2953 37514 25T83 19946 169D5 74869 13389 TT348 9982 8988 8226 7618 7119 670D 5894 5307 43429 29848 23969 20515 18182 76474 14TOD 12496 17322 10417 9691 9092 8569 7672 6897 105963 71131 66339 47750 42000 37820 32054 28194 25388 23234 21517 20108 T8926 76647 14990 ­ 107 I Gi.7 I l a J UD vy Y5 88 84 80 77 74 1192 1073 910 800 720 659 611 571 537 508 484 462 443 425 7545 1391 1T79 1037 934 855 792 740 696 659 627 599 574 551 2202 1983 168D 1478 1331 1218 1128 1064 992 939 893 853 818 786 3956 3563 3OT9 2656 2391 2789 2027 1894 1783 1688 1605 1533 1469. 7412 5232 4740 4057 3596 325E 2997 2788 2616 2471 2347 2239 2144 2060 1985 11175 1DD63 8529 75D2 6755 6182 5725 5350 5036 4767 4535 4331 4T50 3988 2516BTUh-1CFH Maximum COPOC Ty of PE Pipe in Thousands of BTLJ per Hour of Liquefied Petroleum Gas with a Gass Pressure of 70.0 psi and a Pressure Drop of 1.0 psi (based on a 1.52 specific gravijV gas) 1 2476 1662 1316 1116 981 884 749 659659 543 503 470 442 389 350 14234 9555 7568 6414 5642 5080 4306 3787 341.0 3121 289D 2707 2542 2-236 2014 -18455 12388 9812 8316 7315 6587 5583 A910 4422 4047 3747 3502 3296 2899 2611 26296 17652 13987 11849 10423 9385 7954 6997 63DD 5766 6340 4990 4697 4731 3720 47252 31720 25T23 21293 18729 76865 14294 12572 11321 1036T 9595 8967 8440 7423 6685 53960 37087 29782 25489 22591 20469 T7519 :15527 14068 12943 12041 11297 10677 9458 8569 133476 89601 70967 60748 52905 47640 40376 35514 31980 29267 27104 25329 23840 20970 18682- 7707 7507 1352 1746 2213 1946 - 17M 1485 3153 2773 2497 2716 5665 4983 4487 3803 7334 6500 5890 504T 16004 14077 12676 10743 134 T25 ITS 711 1D6 769 719 676 640 609 997 932 - 877 - 880 — 79D 1421 1328 1250 1183 €125 2553 2386 2246 2726 2022 3465 3251 3071 29T6 2782 7212 6739 6343 6005 5712 101 97 582 557 754 - - - 723 1075 1030 1931 7857 ]2466 2664 2560 5455 5227 2516BTUh=1 Ph: 1.800-662,0205 o FQX: 615.325.9407 o Web: wtvw.gasfife.com