Loading...
HomeMy WebLinkAboutGas Piping Schematic( VQOJ9)2?uq `Aub1d7 vo»yD �\Oj e Fitt54-11 on pdolb3 I Qgo z 0 �W > U oC w Ix U , 0 0 L W U S'.} ui !i m w WW N � F ¢o Q`l 6ul}Piuliad '/quno:) apnl OZOZ g 9 NVP 0 0 .an 0 O O O O U O U O to O to O W O Vi O lA O (A C � 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 O o J to lA o N U O o O O O O w O N o o--- IO 3 � G% Er 3 O E T 0 m N N m o Oa Oo �p b N O u N 1NJ W N A [� U N U N V w b O ------------------ J loin g N W VWi V O N T u W N J A 0o A b p O N W g O �Np CI J �-• 0 m N 0 a rC. mm J CO b A O Ai N A w to O U N to W tUA J V pq, c om NN W 9 o N a� Ili N a 9 D A N r N rW N () b �-• A P b N a, o U V O A J N N 4I 4l A U O� m O N A ONE ENO A J O Af A ~ P�}- 9 O lA ^"' w lWJ y OAo oJo G .a T O b ------------ N ---------------- N A .P U lA Q• O� V Co V O O N N��Jl V NNN V� �' � N N G W W O y W w � qyA9�� U o lA A$ Up 01 Y OJ1 N b W i-. �f Q� n d � A IJiI N N O W J a W �„• N W O O O O O m o • O N Y N N� �p.1� N � Np W W W W W W W W a A] ,p A lA lA u v. i-i. r u r N o m yj �. O• �Q V w w }� W VCI .a g N U b U A U D\ to V {A •p q p, W p, to p, J J J w w u "' �"' �'• �-` �+ }ppJ N N s.] IJ W W A O, y r w V N w lA W A O• m �-. O b A r T V U N� N H m �p A� J� U O V V A N �l a J A N O N C J In In C m C y N w VPi V b u V V OW m r r r u u n.r, r r �+ t+ fJ N N N W W W W A A lA lA J O O d D 1a .N-. W W�� b t�f W> N O W V lA v b W U J r N U• J (A A O N a N N 5. O N O 0 0 0 0 o OOO e v o v lY w A lA to O� T V �1 OO 'N W W W A A A lA lA 0 0 0 O N O J O W O w W w W b U� Se+ l3 lNil •N .N O .N b U Jw g N T T pp,, J NN P. O O O O O O O O O O O O O 0 0 0 0 O N J U O a G tl 0 0 m WN U G� W b WWp wN w W y) W W W A A A A A lA to O, O� 1 m b H •' N N W :D U1 A T 00 A s s 00 M Tahlo P.t Pm.unn I nr o....:..am.n..wl N W iw Gpmlry J TrcpOY fawu9lYa� CSlx A tlnmYa e18N pv Xm. P.opw 6N ,'lem°m•+.nap.ere e...nix>mmuwaemreel e..l "•: 7yom (x� F� u 'n r1 .'.m� n+ m N Im.u"° 1 9 mG �,.. :isao - �a __� : . �.... _ _ `m .._-.. `% .._.. L_:._ ._I _ _T s ... a L. C J _ _E,_m »• f! 1m 4 y y m a % a zE a n n N v e e e e a YN! 'b5 L1' ]te xn N9 m IPo IT im ly NI lb 1Z) 1 N n m y a v lm '.n Is LI]6: IJxd� Im" %1'[9_ �- Im 8D aa^ ne mx Bla I61 .W I9x al xd) Sv al Ap IW 1N 1b Im ID 110 1N tm i rail m.:mNry .i9% uem . m i� ills' 9no Lees+ ® ..>m! �ds7� iW.. sa - sat :m xal esl: im, .� s zD. m1 m :m zw� L .Iue Lint .. 1 m .w� i W 6Ve WS 4% SIm D15 340 wf mm t90 mG Ix91 IEV nv.. ISY 1 T NII �:SC'". 19B Ltv f9n S" uu`-'^a.:.YaSi 8S5 NI a4 �w BC C.A !m uY:6'�V3 41 .N W L .. W to412 '1t4c T' L�1.]nmm LbOam'�.mbTa LLoa Y011b®trW mmpsmW �No�enY00FR iavgw�Yps.urbeaMNeM9(lm9.ampFvmNr9TK me'�IFNFamN9mee Iw�491Rmoc EdaLam 6q.b m Tmfle. Gmlm9eeu 63E F 1MV W e m BN p Mve p�rymv to N"l lame m Y 13E 6mO0e 6en1ry12®eN Iv ahe (mi 6N1 •�`^ 1 "39 !�'� r- � i219. .__ JA_'.�_m. W I,�r. r]WJ � L_ v,[ _ L1SG '�.11a. bs � Ep,+ 1Wi. 9 Y® pWY iE• �xZy. Y314 Y'a � I9.. W_ m )ti&1 N! � • y! a+e xn N9 _EB` �I m0 E•�N 1�% 1�. 1yY 1U 9 Ili _. 1W W `B1 � W N 4 61 Ep .) �• Yt]Y9) L � .=V IR ..3Ba1 SW. ]li• LEa.: I i .bl:, 'ILW� INl N - �Im: ISi.:ybf a. _10 m. 141. L% Z3 r Y' e3' )ate 1��4 x^ nm �. iw 1^•Ip 1® BB! E9! rn %E �. ® Rx ®I W xn >� E% %) lMl, N 1m W f4 1'U ipy BeS al M Ia M, aUm J. UM Lx59. _LII: 1pm} SiB'1. _>A � u101. 91. i3=. •SEf ]N� .afe` I. NB mw }f6Y r pJ39 6SL Sel EW ._ Nv _ EI% .. .. 40 ay '._� mv_ 9n ZNr ml iml 1 '-'�'_ _ a m : =F IMp _i•`_: n w6 :.:.T.6 6q •s,'.i )a L..�. ) 1 'TT . f0 C" "5f WJ �i) w �'.1 �L+�'.'.::[: nr+a�e:omi..�ieti___,.._____._.._.�._..._—•-_..___.__....._......_n.,r..e.......,......o.r..,w:,.::w.......®.:mv�.om..e®.®ea olvwma.mY*p.wa�p Ln u�.e.°a.L�aa�,aNda rwm.w.aLme..>mml.m:.mavmam.mm.wxmiy. rwsa�ww.m.Iw�e�.,�aY.mmm wrmmc..w NFo®IMwew�+.1..Gelm j1Ery 1.QAaNN9maehMe.msrl tl4aM0m%.nYm WtlL v NaFunli{sfbd✓Tm'R✓CmmW.aYY 44rFTcrWHmYTI4uuMW®Nfe (anbm.16381cIR glom BN la[W.rmlfm) �'IT v�9� El �J m�i 310 fa'.ilan4v 4a A. �mf� ni.111. u1_N_i1 :W9]�. �•W{�1. 6�. v _rt if ltyL r�1:..9 �3L. iat i4 —et _'. 11d Y?� �Zls Zm IDI v a 1 3 �W. N 01 m N N Im9 iw 8151 MB w +?i w %) m1 1»�•]9 ;�i.1e1 a ' mom_ L Linn wr �� _ zva sv, _ lae m.. me Im °m NB �R Say. Ina w; f® �` _ �m •`s lea w^ ;v � !mL '�!Y L' ems-, tm•• a l—�. 10 ylrfi! �� � '. W n. N' * piv ao, I a fa[ xx F� Vim_ m ! e_ i ilii� % m m w >m z z esx w sm Eu wx b+ m � m m m w y,9; aR !aPe. S Pn OxW ]vl Rv e_b1 yy IBr b 0 Sbt m) elm a 1 mle w) 265 m fII3 m 1 0 IM we pm Bm 6S5 Ba Ttt r6J Er. s4e: a. om a.rm. em memo e. m. �r a v. qp'; c D mmL:.wrawaywrarawcoi..msemrsrFlmmwmuv. w..9.wm. m. �wL ri:ram �. me.eae.lnsp.tlx8mplzm eiu 0. muermlwEl n fasmlM'lEe .^..t ,a — - `y 1 S IW m Im Po m n 4 EeJ b v m a Ny a m u n n fe m t�� ] lytl �34: •2L ai` - 99. Lfw fw; '.�8: IM :1.1 1"% _aL _QL. .1 uzs� LDe use 4a..� a Il% aso w we w .% m w Ja m a zn w m m 1 In^ m +Ie Im lm m m n m n ..1^'wT 4„� s-_r.. 1061 10m +w Yfm 0A ®]t •.eil•')31^_i19 WQ"6n' Wx TO !A" JS!'J0x 'JM' a9' %.'Ym1Yf W' `I m'y4 110 1J9 19"IJL"Im' fIM a ]%0 Dv mB la9 00JB ImB 1m0 16v al Ttl N) 010 S0 SA Y1 ZA ml 34 a0 IYY 4w� Wm Vtm zin zw EIN. xON 193i' iiwl ims lem'1511 NN IZ,_ Mm 119':uy _ .PL R5f .v- 'em !0% .... ....... �_ --... .v..'n r w mom 1mn ewo rm ssa mo m% yls lw emo ei% Jsm N% sDo as we xen sm, I9m Ism I rz a nm nm lw) mx ma m0 w w _=,_I.mFR �'£4T x... ..:.:T ... � "ne =Y ._�.-" �?i �e ^. '�5;. "35t .�. ...:•. t_., ice.. -_ .S.L'... r `" 'P,: .,+�=F 4 P � � n^Fl. $.. .... ;_..x'iF a•=i Wi3.Me.LM1p�YlY6aIL.'9ha0N9etlnh0YnmNd.6+l°ntlL"09�1LL BeYy w�•••v�.s.W nvw w.w•.vim«.ownvawm.vy..ewvwuw^avvw'w� 16,20 9. I 1b OJ 16..1 0 A124.9630 " 0 q`�s I 970.0000' 49, 7°,22' 53" — — x 17.06 5/8°78C �0 0 19.49 I -00 G4�Np0 LS#2391 5C S#2391 C q . 9a4 DaS?raciurz SET5/8°IEC r? c $ 1a 15�loc, m LB#7903 I 19,13 PBOPO I CO EMPEY 35.1' 12.0' m PROPOSED c 120' m120. �� I GREEN ARE �n 11.3' `r 7.0' �^_ 11.3' 10 3• 17,90 x s12 A7,60 �a.o' /T26 Z • •; 13' PEOP0�57YJSYCBS n Im I of Im / CON m o 0 '• PE CID,,\ Il�'7ifUBf �I6[6 I I y I PROPOSE D g`t�p\� 16.3' _ '� DRAINFlEI +-56050F . Wo- N°lh '•` 39.T '.'a ` '\ 40.3 29..1 W �r Q6q `R 35.3' 'i Z D • it'SLL • •75 34.7 "\C� PDOL \ C3 M 18,12 — aOP � D 17.57 17.04 I oPo wiz / I t �y x 18,20 (� 19,94 19,87 Ca,eta3oC x 17.50 x 18.31 w XWOODPEnIca I I �,8.91 16.93 2$— FND4X4°CM 25' drainage & ut Iity easement LS#2391 N 89°30'54" E. 150.02' 14.37 13,96 �14 — — — , ° , — 44 W 8 dome; i Wblack p III's 'I N , W 410 --ug �"bbftl Toplaw. ;Rip- Ftithes -109ud q I'dIjIU'LUIJ L(UUd 'd' -Y.buals�ervi��e'oot!6t!s,foral.Yoveoru,n�d'e�Lgroun applications, • CiIPtibnt#1:,Mead _-to-.bL!rylreddRidUdurb5le powder coa . coating with black pblVeth&neA(5U'&8ome* P,Uf5tibh4#21.At5ovqgrduri"d�optiorf with steel 8" A UGdome ;..All vIlVCs-'and,fIbdf-_ 't - 'd under dome gauges are,cen bre u P Ftdbrtc-dted-td, t-Ne -L&MiE, iafp�t;A Corde, Sectidn -Vill, 5jivig-ibA 1. Bdar,&. -ohiCq.e, i` udes refubllng;em isdions i Widuum.jojptpurgeLd to save time, rficingy aFn'o product t in;YDe�ct(itr�e-dui�reWnisi6r" LA C;O1N`TtA`,I�N!E{iTS 0 LEG WIDTH General Specifications Conforms to the latest edition of the ASME code for Pressure Vessels, 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. ---� WITHDRAWAL VALVE FLOAT LOTICE GAS\ ANODE GAUGE ) ® X CONNECTION FILLER O O I VALVE SERVICE! NAME MULTIVALVE PLATE RELIEF VALVE FITTINGS LAYOUT UNDER DOME AGUG VESSEL DIMENSIONAL INFORMATION All vessels dimensions are approximate WATER OUTSIDE HEAD OVERALL OVERALL LEG LEG WEIGHT QUANTITY FULL PER CAPACITY - DIAMETER TYPE LENGTH HEIGHT WIDTH SPACING LOAD STACK 120 wg. 24" Ellip 5'- 5 13/16" 3' - 0" 10 1/8" 3' - 0" 245 lbs. 96 12 454.2 L 609.6 mm 1671.3mm 911.4 mm 257.2 mm 914.4 mm 111.1 kg. 250 wg. 31.5" Hemi 7' - 2 1/2" 3' - 7 1/2" 12 3/4" 3' - 6" 472 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 1/2" 12 3/4" 4' - 0 1/4" 588 lbs. 45 9 1211.2 L 800.1 mm 2736.9 mm 1104.9 mm 323.9 mm 1225.6 mm 266.7 kg. 500 wg. 37.42" Hemi V -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 wg. 40.96" Hemi 15'- 10 13/16" 4' - 4 5116" 16 1/4" 9' - 0" 1729 lbs. 15 5 3785.0 L 1040A mm 4846.6 mm 1344.6 mm 1 412.8 mm 2743.2 mm 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 currentflows from the soil to the tank, no corrosion occurs. The progress of corrosion is determined by the amount of current flowing between the anode and the cathode and whether the locations of the anode/ cathode remain constant over time. Corrosion rates are generally higher in wet soil environments since the conductivity of the soil promotes the flow of DC current in the corrosion circuit. Corrosion generally exhibits itself on underground tanks in either a general overall rusting or more commonly, a pitting attack. Pit locations may result from metallurgical conditions of the steel suraface or soil variations such as rocks, salts, fertilizer, moisture concentration, oxygen concentration, etc. Preventing Gorrosion Protecting underground tanks from corrosion is easilyachieved bythe use of two commonly applied protection methods: v external coating and cathodic protection. These two methods are complementary -- and should be used in conjunction with the other. An effective external protective coating insulates the steel from the soil environment, thus preventing theflowofcorrosion currentfromtheanodetothe cathode. An effective external coating Gan protect over 99% of the tanksurface area. However, no coating is perfect Damage from construction or soil stresses create tiny defects, which may result in accelerated corrosion at the defect. Cathodic protection prevents corrosion at those defects by applying DC current from an external source, forcing the tank to become cathode. Application of sufficient DC current to the tank will prevent any corrosion from occurring. The two general types of cathodic protection systems are sacrificial and impressed current. Sacrificial systems are used when the amount of current required for the protection is small, such as in underground propane tanks. Impressed current systems are more commonly used for large structures such as large diameter pipelines. Electrical isolation of the tank from metallic piping systems and electrical grounds is critical for the cathodic protection system's effectiveness. How 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 1.25V 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 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 9lb. and 171b. The size designation relatesto the metal weight. 10' of #12 TW insulated wire is attached to the anodes. Anodes are then backfilled in a mixture of gypsum, bentonite, and sodium sulfate to lower the electrical resistance of the anode to soil. The mixture is a low cost, nonhazardous, electrically conductive backfill. The anode and backfill is then packaged in a cotton bag and either a cardboard box or paper bag. Actual shipping weight of these anodes with backfill is 27 lb. and 45 lb. Application Recommendations Magnesium anodes can protect underground tanks in most soil conditions. The H-1 alloyis generally very effective. The following chart providessize and quantity 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' 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. Copperand 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. Soil Type 'r'Feilile,SoilL ay,. Sandy.Loami,_,_, Send, Gravei,Rocky Areas Tank Cap. ' S:fo 5io00 ofi`m cm 5000 to 10000 ohm -cm (gal•j ;ES " �Q��i i?;?Iloy Size Qty. Alloy 120 9# 1 H-1 150 1 " E.01JA 9# 1 1 1 H-1 250 T9'rC 27 H=11 ' 9# 2 H-1 325 t. 9 Z' Sf .H_1� 9# 2 H-1 1000 rlffig �_f 'H`g1" 9# 4tH-11500 41 d d a Fl l 9# 42000 j17# . 31" fHsll 9# 6 'Based on 90% effective external coating, 2 ma&2 current density, and 30- year Anode life. Anode Installation 1. Determine size and quantity of anodes from application chart. 2. When a single anode is Installed, it should be located near the tank center on either side of tank. 3. When multiple anodes are installed, space them evenly around the tank. See examples below. 1 anode 2 anodes 4 anodes O O O 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 feetfrom 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 overto 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.Vedfy 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 insertthe 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 goad solid connection is very important. (DO NOT connect to shroud). STEP 2: Insert the black test lead into the Common jack on the meter, and connect the opposite end of the lead to a charged reference electrode (Ys cell). STEP 3: Remove protective cap from the porous plug at bottom end of electrode. Place porous plug end into native soil (remove grass if necessary) at four locations around the tank (one on each side of the tank, and one at each end of the tank). If difficulty is encountered obtaining readings, moisten soil with water or dig Yz cell deeper into the soil. STEP 4: Record ail four meter readings on an appropriate form. The least of all four readings should be a minimum of-0.850v or more negative. {Note: If any of the four readings are below (less negative) -0.850v then the tank is not fully protected}. Charging Reference Electrode STEP 1: Unscrew and remove porous plug end of new reference electrode. Add deionized or distilled water to the copper sulfate crystals, filling electrode completely. The solution will turn blue in color and there should always be excess crystals at the bottom of the tube. DO NOT USE TAP WATER. STEP 2: Replace porous plug and 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: 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 DSTEB. BTU's per hour. The regulator Is factory set to reduce container pressure to an Intermediate pressure of approximately 10 PSIG. k"�ei4Lt� • Compact design can be connected to a service valve using either a POL adapter or a RegO product pigtail. • Large threaded% F.NPT bonnet vent can easily be piped -away underground installations without the need of glue kits or extra adapters. • Non Adjustable • Large Bow orifice resists freeze ups due to water concentration in LPG vapor. • Design provides for good flow regulation at both high and low container pressures. • Built in relief valve and travel stop comply with NFPA 58 over pressure requirements. • Incorporates W F.NPT downstream pressure tap for an easy Inline check of the regulator's delivery pressure. • Molded diaphragm provides an o-ring type seal between the body and bonnet • Body and bonnet are assembled in the USA using the unique, patented RegUlok seal system. • Fully painted in brilliant red for complete corrosion protection. • Mounting bracket available as an accessory: part number 2302-31. Rga,"vfte-ap8 Body............................................................................................Zinc Bonnet.........................................................................................Zinc Spring........................................................................................ Steel Seat Disc.................................................................Resilient Rubber Diaphragm...........................Integrated Fabric and Synthetic Rubber �u'7��uS��®iTte��'• a;CC;dS�i LV3403TR Par077iapher• INetConnp:G ®®®® [ q--"'connection r lff cd•S Delve PieeSuFe.. Bon6eI&&Pe9tlOn• •' va p or Ca as BTDRk P,Lti nel �� so oil I I Madrnum Dow based on Welpresswe 20 PSIG higherthan the regulator setOng and delivery pressure 20%lower Nan the regulatcrsetling and delivery pressure 20%lower than iha selling. A 4 MAMM 100 Rego Dr. Elon, NC 27244 USA w xegopmduots.cam +1 (336) 649-7707 �'aa:m 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 domestic loads. YeEm- lm • 90 degree right angle inlet to outer connection for meter or standard installations. • Large vent helps to prevent blockage and has''YO 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 an seat disc • Unique bonnet vent profile minimizes vent freeze over when pmpedy installed. • Large molded diaphragm Is extra sensitive to pressure changes. • Built in pressure tap has plugged W F. NPT outlet. Plug can be removed with a 3/16• hex alien wrench. • Select Brown Finish Can mount directly to vapor meter. It Is also suitable for mounting directly to the house piping. It will retrofit into existing installations that are currently using a 90 degree, right angle regulator. r'Lr�QFSi�c �5 Body........................................................................... Die Cast Zinc Bonnet........................................................................ Die Cast Zinc NozzleOrifice......................................................................... Brass Spring...................................................................................... Steel ValveSeat Disc ..................................................... Resilient Rubber Diaphragm ......................... Integrated Fabric and Synthetic Rubber Ua w/a4omting8cacket 1 II I 11 w1 11 1 •11 1,1,1 „I , 1 ir1 OOD Fart Numtier 7n1e4Connection ODU'et rConnechon�` _O`nfice. { 'Srze y Fa__cto Delive.-' , .Pressure ry AdjihT eup Ranggp. Bome$VenU Position V odCe as STlyhr: pare • Maximum 0aw Is based on 10 PSIG Wet and 9' w.e. delivery pressure. •• Mouneng Bracket Included. �q 100 Rego Dc FJon, NC 27244 USA w .mgopmducb.mm +1 (336) 449-7707 9V � An W 761 ES-D-GAC Generac InstaIISmart Job Name _ Job Location Engineer Approval Generac® Flexible Fuel Hines 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) • Flexible Tube Material Annealed 304 Stainless Steel • Flare Nut Material Carbon Steel with Zinc Trivalent Chromate Plating • Flare Adapter Material Carbon Steel with Zinc Trivalent Chromate Plating • PVC Dip Coating Gray Heavy Duty, Antimicrobial, UV Stabilizer , CSA Group Certificate of Compliance to Product Standards ANSI Z21.75/CSA 6.27 — Connectors for Outdoor Gas Appliances and Manufactured Homes Scope states "...Intended for exterior use above ground for making non -rigid connections... between the gas supply and the gas inlet of an appliance for outdoor installation that is not frequently moved after installation." In addition section 1.5.4 states the connector is designed for occasional movement after installation. Repeated bending, flexing or extreme vibration must be avoided. Normal operation of a clothes dryer, rooftop HVAC unit or SIMILAR OUTDOOR APPLIANCE DOES NOT constitute extreme vibration or movement. ANSI Z21.24/GSA 6.10 — Connectors for Gas Appliances s�, (Excluding 60/61 Series) c us Product Configurations Contractor Approval Contractor's P.O. No. Representative SKU For use with Generac stationary outdoor backup/ standby generators. Applicable Codes ANSI Z223.1/NFPA 54 National Fuel Gas Code Section 9.6 International Fuel Gas Code (IFGC) Section 411.1 6149.1 — Natural Gas and Propane Installation Code (CSA Group) Section 6.21 Uniform Mechanical Code (UMC) Section 1313.0 Uniform Plumbing Code (UPC) Section 1212.0 Additional Approvals Commonwealth of Massachusetts Board of State Examiners of Plumbers and Gas Fitters Additional Testing UL2200-2015: Stationary Engine Generator Assemblies Section 66B Vibration Test. Domnnt pmductspedfirations In US customary, units and metic are appmpmate and are pmvidedfurehrence arty. Fwpredse ® ��®��® measurements, please wntact DarmontTedudcal Service. Dormont reserves the fight to change or madly pmductdesign, construction, spedfiradons, or materials wilhoutpdv notice end wahout insuring any obngafon to male such changes and modifications on Darmant pmduds pwicusly orsubsequentysdd. Refer m the owner's manual for warranty bdormaUDn. A WHOM Brand N 7� Minimum Flow Capacity at Specified Pressure Drop Straight Length BTU/hr, NATURAL GAS, 0.64 SG, 1000 BTU/cu.fL CONFIGURATION PRESSURE r' (INCHES WATER COLUIAN) Generae Oonnom' Part Number Pad Number SERIES Nominal l0 in Nominal Lenght In 0.50In 0.75 in 1.00 in 1.25 in 1.5D in 1.75 in 2.00In 10000009793 CAN41-4141-24GEN 41 a/4 24 290,900 356,278 411,395 459,953 503,854 1 544,224 581,800 10000009776 CAN41-4141-48GEN 41 '/4 48 217.000 265,770 306,894 343,107 375,855 405,970 434,000 10000009717 CAN41-0141-72GEN 41 '/4 72 173,900 212,983 254,932 247.960 301,204 325,337 347,800 10DODOOD498 CAN51-5151-24GEN 51 1 24 581,800 712,657 822,789 919,907 1,007.707 1.088,44 11,163,600 10000090499 CAN51-5151-48GEN 51 1 48 442,700 542,195 626,072 699,770 766.779 828,216 885,400 10000000500 CAN51-5151-72GEN 51 1 72 347,800 425.956 491.863 549,920 602,407 650,674 695,600 Straight Length BTU/hr. LP GAS, 1.55 SG, 2500 BTU/cu.ft. 6119 Genemc. Pad Number ION Omani? Part Number SERIES I Nominal ID in Naminal Lenght in 0.50 In 0.75 in PRESSURE 1.OD in (NCHES&TER 1.25 in COLUMN) 1.50 In 1.76 in 2.00 in 10000009793 CAN41.4141.24GEN 1 41 1 r/4 24 465.400 569,996 658,176 735,862 806,096 870,684 930,800 10000009776 CAN41-4141-48GEN 41 a/i 48 344,000 421.312 486.489 543,912 595,825 643.565 688,000 10000009777 CAN414141-72GEN 41 ai 72 278,240 340,773 393,491 439,936 481,926 520,539 556,480 1DODOOD0498 CAN51-5151-24GEN 51 1 24 930,860 1,140,091 1,376,463 1,471,851 1,612,331 1,741,517 1,861,760 10DOOD00499 CAN51-5151-48GEN 51 1 48 708,320 867,511 1,001,716 1,119,952 1,226,846 1,325,145 1,416,640 10000000500 CAN51-5151-72GEN 51 1 72 556,480 1 681,546 786,982 879,872 963,852 1,041,079 1,112,960 Generac part number 10000000498 (Dormont part number CAN51-5151-24GEN) can supply a minimum of 581,800 BTU/hr.of natural gas ® 0.50 in. water column pressure drop to the generator. OMME All installations most completely comply with all-Dormont® manufacturing company warnings and Instructions, national, state and local codes and all applicable ANSI standards. A WA7 M Brand USA T. (800) 367-6668 • F. V24) 733-4808 • Donnont.com Canada: T. (905) 832AO90 - F. (905) 332-7068 - Dormant.ca Latin America: T. (52) 81-1001-8600 • F. (52) 81-80DD-7091 • Donnont.com ES-D-GAC_Generac_lnstallSmart 1703 0 2016 Donnont Maximum Capacity of PE Pipe In Thousands of BTU per Hour of Liquefied Petroleum Gas with a Gas Pressure of 11.0 in. WC and a Pressure Drop of 0.5 In. WC (based on a 1.62 specific grovilygas) NoW 22 20 18 15 13 12 11 10 9 9 8 e 8 7 7 129 113 102 86 76 68 63 58 54 51 48 46 44 42 40 167 747 132 112 99 89 81 75 70 66 63 60 57 54 52 23B 209 188 160 140 126 116 107 700 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 7061 956 810 712 642 557 544 508 478 453 431 417 394 379 25766TUh=ICFH 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 aravlly am) 1192 1073 910 800 720 659 617 07 537 508 484 462 443 425 1545 1391 1779 1037 934 855 792 740 696 659 627 599 574 551 2202 7983 1680 1478 1331 1218 1128 1054 992 939 893 • 853 818 786 3956 3563 3019 2656 2391 2189 2027 1894 7793 1688 1605 1533 1469. 1412 5232 4740 4057 3596 3258 2997 278E 2676 2471 2347 2239 2144 2060 1985 11175 10063 8529 7502 6755 6182 5725 5350 5036 4767 4535 4331 4150 3988 2516BTUh=ICFH Maximum Capacity of PE Pipe In Thousands of BTU per Hour of Liquefied Petroleum Gas Nth a Gas Pressure of 10.0 psi and a Pressure Drop of 1.0 psi (based on a 1.52 specific gravity gas) Ph: 1.800.662.0208 ^ Fax: 615.325.9407 ^ Web: wWW.gastite.com