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Home My WebLink AboutPROJECT INFORMATION-rue,) lwn t 4's IN oe— RECEIVED APR 2 5 2018 ST, t�wdp!, -:40-oly, it azi zo Ina r\ 111-120a, z Le 0 a. - NO, 00 ct Lp L 5 r L L)qi-161 @ I I "- 15 1 wo, 6 -3- pa iTe, v ZE L�41vs"O- L'v TRU I-jv wv 7 079 1 0&9 U o550917 V dO 7V3S IMI" VN15140 .y V� YOA348hS VGiyo-' S31doo 3,qL hfojko.Gy ONV dVH A34W75 .31MA m 017VA ION -79 V -.o3y3'U OWS ,VoyVbLjLjWo qYO Poll P V- -og (Jiga la) NIP oll arivos bmcivllf) ,b/F , . S, -(%)j-a) I . hG I 'If -A Nog yojvvSnsiv1 3VIL - 7VNOLi YN Z/1 lcrlld3d ANV%,up Siassa=nS -9;1 tVNViT 7VNUIJVIY'-LSYQDM "3 SufijSSD JO/ . PUD 37Yt6qdiYf 'UV'qly 7 fo rvu� SISVJB)Yj J12q) -Tuou V/OtdV-1 Mp 3i�169dnl -'SAfOLiV 7 Ar�ujyAi ino auf W1161HOW ws �wa -yo iv-:151vo.,Oj �;,Vop-qo do SNO4100Y .9 'Llyvd VMN ,Yns (H SdVH AM i go ,UgVd 6MINDAF JR1 VVHL 831� 0 7VO37 X 49 L73WN211V Afolld'W-F30. MIS S537 SO 389ly layyqV *P.o 210 j:w 38vhos g-Irl,61 -,V-Vyv ;/78&V -.03" P�gopo-ZWO'f . 9, , . . . '91 A80 17007J NI s3n 3115 sluL JNOZ No avvio-f4wivi ONY . 497VOS SVA .'d,V dYN V)W G�OWOMr is -40 :YOV21931 tiq.72GH lqOH5 S*18*6 VVV ol awq I JV do HV101�3H c3nnss sv-lcwAg ti 42NO71�3'.90P`? Y013� .99, Nd AMO �NV AI Vld 0� U59V:10N 3WH N0393H MOW Sj�O�y 8010M� . SllV3paSv3.yoj avoW (3ans r M 9m?ld3a 7�y -40 �x W -90 Jf7OHLM OMOJ2q� SV volAfo s3,?AqY -WSV -U It - V jo ILGIOS 1� c1m; O.L I*taovpoy *M W 3 Maximum COPa0ltV Of PE Pipe In Thousands ofjBTU per - Hour of Uquefled Petroleum Gas with a Gas Pressure of 11.0 In. WC and a Pressure Drop of 0.5 In. WC (based an a 1.62 sperlhc =2� , gravIty gas) 00 .50 4-5— 4-1 �38 1073 720 571 i�4 425 383 325 2�6 257 1391 33 29 ' 26 , 235 218 934 740 627 651 497 421 3' '?0 333 305 283 1983 1331 1054 893 204 264 192 249 16,?9 152 15 3563 2391 786 708 600 528 475 435 403 1894 1605 1412 1272 1078 9� 376 364 219 311 197 80 2870 4724 .8 8,94 781 723 3247 2608 2232 1978 1792 1534 1�69 .1232 1133 1054 10063 6755 6351 676 989 636 560 504 0� 4635 3989 3592 3044 26178 2411 2207 2044 934 1910 828 710 1797 1581 1424 22 13 12 I 129 167 113 147 1 10 9 9 102 86 76 68 63 56 54 51 132 112 48 46 44 238 209 99 89 81 76 70 66 laa 160 140 126 116 63 60 57 42 54 40 52 427 642 376 569 100 94 338 287 252 227 208 19� 180 169 516 441 89 160 88 182 81 146 78 76 1207 1061 391 354 326 30� 285 269 956 810 712 642 587 54� 255 244 233 140 224 134 216 608 478 453 431 411 394 379 MaXIMUM Capacity of pE pipe In Thousands of BTU per Hour Of Liquefied Petroleum 2516STUh=ICFH with 0 Gqs Pressure of 2.0 psi and d Pressure Gas Drop (based an a 1.62 spec)fic 6rovitV of 1.0 psi gas) �-MN, 1966 11800 1 19 7586 11111-114:F1111! WIR1111 11 11-011111ROA 1045 88A 702 Mr,15 4/1 431 6008 5092 4479 399 373 351 W9 �09 14652 9835 4033 3418 3007 2707 2478 7790 6602 5807 5229 4432 3896 2296 2144 2018 1775 278 '27. 1599 "9 20877 14014 3810 3213 11100 9408 8275 7461 6316 5556 5002 2975 278o 2617 �0 2302 2.7� 2073 37514 43429 26183 29848 4578 19946 16905 14869 13389 11348 998� 8988 8226 23969. 4239 7618 3962 7119 3729 9 3280 29. 2053 105963 71131 20515 18182 16474 14100 12496 11322 10417 56339 47750 42000 37820 32054 28194 9691 9092"78589 6700 5894 7612 68307 .07 6197 25388 23234 21617 20108 18926 16647 149 901 236 OMAN 207 187 58 1.39 125 1 8 106 1355 1787 1192 1W 99 93 1073 910 800 720 659 611 571 637 1391 1179 06 608 84 484 so 462 74 2603 2202 1037 934 866 792 740 696 1983 1680 1478 1331 1218 659 627 599 443 874 428 651 4498 3956 1128 1054 3563 3019 2656 2391 2189 2027 1894 893 818 786 8903 12708 5232 11175 1979823 4740 4067 3596 3258 2997 2788 2616 2471 10063 8529 7602 1939 688 M47 1605 2239 1533 2144 1469 2061) 1412 6785 6182 .572.5 -53,W 8036 4767 4535 4331 4150 1985 3988 Maximum CaPacify of PE Pipe I n Thousands 2816BTUh=]CFH of BTU per Hour of Liquefied Petroleum with a Gas Pressure of 10.0 psi and a Pressure Drop of 1.0 psi Gas (based on a 1.62 apeciffe gr6vlty gas) —r47—C 14234 1662 95M 1316 1116 981 884 749 "659 5093 7668 6414 jin3 470 442 18465 12388 6642 60BO 4306 3787 3410 3121 9812 8316 7318 6687 5583 2890 2701 2542 389 2236 7i,: 350 2014 < 26296 17652 4910 4422 4047 13981 11849 10423 300 9385 7954 6997 6 3747 3502 . 306 2899 z.,j 2611 47252 53960 31720 37087 5766 25123 21293 18729 16865 14294 12872 11321 10361 29782 5340 9595 4990 8967 4697 4131 3720 133476 89601 25489 22591 20469 17519 15527 14068 12943 70967 60148 52905 47640 40376 12041 11297 8440 10671 7423 9458 6685 8569 35514 31980 - - - 29267 271.04 26329 23840 20970 18882 297 26 235 175 158 1 4 134 125 1707 1501 118 1362 1146 1008 907 830 769 719 676 lub 101 97 — 9-3 2213 3153 1946 2773 1753 1485 1306 1176 1077 997 932 877 640 830 609 790 682 857 836 6665 4983 2497 2116 1862, 1676 1534 1421 1328 1250 4487 3803 3345 3012 1183 1125 754 1075 723 1030 695 990 7334 6500 2757 2553 2386 2246 8890 5041 4468 4048 3724 3465 32al 2126 2022 1931 1851 1779 16004 14077 3071 12676 10743 9449 8609 7787 7212 6739 6343 2916 2782 2664 2560 2466 60os 5712 5455 5227 6024 2516BTUh=ICFH Ph: 1.800.662-0208 FaX 615.325,9407 0 Web: WWW.gastlte.corn 7 ABOVEG.ROUND/UNDERGROUND DOMESTIC TANKS'' 120 - 2,000 Wg 9_ 8" dome in black plastic or whitel galvanized steel CONTAINERS NEW! POWDURAO 0neCureP Super Durable Topcoat with Zinc Rich Primer on Aboveground POWDURAO OneCurem Two coat systern properties include: • Zinc rich epoxy primer • Super durable TGIC polyester topcoat • Superior corrosion and edge protection • Patent pending formulated primer and topcoat • Dual service Options for above or Underground applications • Option IN: Ready -to -bury red oxide durable powder coating with black • polyethylene AGUG dorne' • Option #2: Aboveground option with steel 8" AGUG dome • All valves and float gauges are centered under dome • Fabricated to the latest A.S.M.E. Code, Section V111, Division 1 • Registered with the National Board • 472 liquid level Outage valve orifice reduces refueling emissions • Vacuum pre -purged to save time, money and product '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 if/ fedoral, state. loraland NrPA industry r�qijlniionn_ Cothodic protection is required and coating must be continuous and uninterrupted and must colliply will' at) local, state Or national code. www.TrinityContainers.com,--,CalI Toll Free: 888-558-8265 TRINITY n � �JA-. a Containing Our World's Energy'" Generg�� 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 (14.1 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, FILLER (Cy-r,VALVE FITTINGS LAYOUT UNDER DOME Rev: Jan. 27,2016 Why Tanks corrode Underground steel tanks corrode due to an electrach between the tank and the surrounding soil. The Process of col Occurs due to -small voltage differences on the steel surface that In the flow of DO current from one to flows from the tank into the soil cation to another. Where o; corrosion occurs.. This location is the anode In a corrosion circuit. Where current flows from the soil tank, 00 corrosion occurs. The progress of corrosion Is determin the amount Of current flowing between the anode and the cathod Whether the locations of the anode/ cathode remain constant over Corrosion rates are generally higher in wet soil enviro . conductivity of the soil promote$ the flow of DO ourre nments sInc circuit. nt in the com Gorroslon generally ixhlbits It'llt on underground tanks In elti, general overall rusting or more Commonly, a Pitting attack. pit, v may result from metallurgical conditions of the steel a aj variations such as rocks, salts, fertilizer, urface or concentration, etc. moisture concentsratfon, OXI different metals, The most common anode materW Is magnesium action Which when ,oslon coupled to steel results In -DO current now from result Magnesium to the Steel, The open circuit Potential at the s about irrent -0.50 volts referenced to a copper sulfate electrode. Thestseelel circuit malled Potential of magnesium Is about .1.55V to - p '0 the two metals together, the difference of I to 1. 1.8ov, By connecting the 25V volts results In current �d b flaw to the tank that overcomes the natural corrosion 0811s; that exist on , Y the tank. With this current available to the tank, no corrosion occurs. , and �lma ' - Magnesium Anodes I the There are a variety of anode sizes and alloys used for cathodic Ion Protection. The two primary at High Potential, The toys are designed as H-1 (or AZ63) and and has an open circ H-1 alloy is Produced from recycled magnesium uit Potential of approximately — I.M. This alloy is W811 suited for:Protection of underground Propane tanks. The High 'oil3nS Potential alloy is 99% Pure magnesium having an open circuit potential i' up to -1-8V- This alloy should be used for soil applications over 10,0oo �n Ohm -cm resistivity. NeventIng corrosion Protecting undergroun, tanks from corrosion 11, 82311Yachleved bythe us(' Of two Commonly applied protection . Methods: external coating and Cathodic Protection. These two methods are Complementary and should be used in Gonjunction with . the )ther, An Affn,,m Mating Insulates the st va 081 from the'soll external protective environment, thus preventing he flow of corrosion Current from the anode to the cathode Aneffective Xtemal Coating can Protect overg.9% Of the tanksurfa 0 co"'n" Damage from construc ce area. However, ny defects, V'uh6jrC'heonaY result tion or soil stresses create In accelerated corrosion at the defect. Ithodic protection prevents corrosion at those defects by applying ' durrent fr6m an external' source, f6rolng the tank to bicome thOde. Application of -sufficient DO current to the tank will prevent any rrOslon from Occurring. Th dems are Sacrificial and 1 0 two general tYP6S Of cathodic Protection mPressed current Sacrificial system$ a. ,d When the amount Of current required -for. the PrOtBotlon Is small, ih. as in Undpr9round Propane tanks. Impressed current systems more 10mmonly Used for large structures ,lines, "'ItriCal Isolation- of the tank from Such as large diameter electrical ' metallic piping I grounds Is -critical for the cathodic Protection systems ItIveness,. System's '88crifIC181 Cathodic Proliollon works :, ificial systerns.work by creating a galvanto c" .0nnOctlon between two The two most Common anode sizes Used for underground propane tanks are 9 lb, and I 71b. The size designation relates to the Metal weight 10' Of #12 7W Insulated wire is attached to the anodes, Anodes are then backfilled in 8 mixture at gypsum, bentonite, and sodium sulfate to lower the electrical resistance of the anode to soil. The ml ure I a low cost, nonhazardous, electrically conductive backfill. xt S backfill Is then Packaged In a Cotton bag and th0anodeand Paper bag. Actual shipping Weight at these either a cardboard box or lb. and 45 lb. anodes with backfill is 27 ApplIcallon Fi0cOmMendatIons MagROSIUM anodes can Protect underground tanks 1 condiffons..The H-1 alloy is n most soil Provid gsnerallYverY effective, The to 86 Size and quantltYMCOMMendatlons IlOwIng chart on conservative design assumptions, Th forvarlous sizetanks based Is chart covers soil conditions up to 10,000 Ohm -centimeter resistivity. ResistIvItles higher than 10,000 Ohm -centimeter generally represent very dry soil$. Verification of �011 resistivity can be Performed through soil analysis. Contact us for design reco notations In locations where 10,000 Ohm- mme CM, or If there Is no effective Wqrn so" reststivitles exceed at coating on the tank, The. Propane service line from the tank to the house 11so considered In the cathodic protection design, unless,the service line Is Plastic, All underground steel pipe shoul must be a corrosion resistant material. The servl d be externally coated with isolated at the house With an In. ce fine should be electrically 1� to$ , sulating fitting or union, If service Pipe S than 50'In length, the tank anodes will Provide sufficient current :,a protect both tank and pipe, For longer lengths Of Pipe, an additional Inode May be required at the house connections. �� another metallic Material such as copper is used for service Piping, ),e PIPO should be electricatly isolated from the tank at the Jinnection. Copperandsteel create fill pipe )rros a galvanic couple that will accelerate "on of the Steel tank when directly connected to copper piping. 11 nerallY, Copper Piping does not require cathodic Protection, 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 lack of the meter and select the 2 or 20 volt DO scale. Clip red test lead connector to an uncoated metallic area of the tank, preferably to the fill Pips MultivalVe. A good solid connection is (DO NOT connect to shroud). very Important. STEP 2: Insert the blacktest lead Into the Common lack I on the meter, and connect the OPPOSite end Of the lead to a charged reference electrode (X call). STEP 3: Remove protective cap from -the Porous Plug at bottom end of electrode. Place porous Plug and Into native $oll (remove grass if necessary) at four locations around the tank (one on each side of the tank, and one at each end of the tank). If difficulty Is encountered obtaining readings, Molsten soil With water or dig the soil. ya Cell deeper Into STEP 4: Record all four'meter readings on an appropriate form. The least of all four readings should be a minimum of -0-850v or more n8gatIve. (Note: If any Of the four readings are below (less negative) -0-850v then the tank Is not fully Protectedj. Charging Rejerence Electrode STEP 1: Unscrew and remove Porous Plug end of new reference electrode, Add delonized or distilled water to the Copper sulfate crystals, filling electrode completely. color and there should always be The solution will turn blue In excess crystals at the bottom of the. tube. DO NOT USE TAP WATER. STEP 2: Replace porous Plug end of electrode and place in an upright Position so that the porous Plug end Is facing In the down positlon and let stand for\1 hour before Use, This will al 0 to become completely saturated before use. I W the porous Plug 'O'011on' '00 not allow electrade.to 0017100t 011, road salts, oF other Substance$. that may contaminate the solution by absorption throll-qh porousplu-a. #0 not allow electrode in I'll Type Fertile sails, clay, Sandy Loam Tank Cap. (gall) 5 to agoo ohm.em Saco to 10000 hm-oml size QtY. Alloy size QtY. Alloy 120 160 H-1 .9# H-1 250 H-1 9# 1 H-1 9# 9# H-1 2 N.1 325 Soo 9# H-1 17# H-1 9# 9# 000 17# 2 N., 9# 2 H-1 4 H-1 1500 2000 17# 2 H-1 17# 3, 9# 4 H-1 H-1 'Based an 90% 8#ectivO 646mal Mating, 2 YearAnode life. M&W current density, and' so - 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. Sea examples below. I anode 2 anodes 4 ainodes� IMF,. 4-Anodes are shipped In either cardboard boxes or multi-wal PaperSacks. Remove OUter container and bury the lothbagg'st anode. If anode Is SUPPIlod In plastic bag, remo 0 before Installing. ve plastic bag 5. Install anodes approximately two to three feet fr . om the tank a nd at least as deep as the center line of the tank. Anodes work best In locations with permanent moisture, so generall the better. Y the deeper O.After placing the anode, stretch out the anode connection W1 I re and extend over to a cOnn action point on the tank fill pipe. , 7. Cover the anode with approximately six inches Of backfill ar d 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 electrlca� resistance connection Examples are threaded stud on the'l tank fill Pipe or any ac;8ssibIG metallic connection point to th6 tank. All connections should be,coated with a mo material. isture-proof 9. Ideally, the'tank Connection is made In the area of the'tank fill i PIP8 within the covered dome. With access to the anode w1re,j subsequent testing Of the tank can Include measurement of, anode Output and verification of performance. 10-Verlfy performance of the anode Using an appropriate te$ procedure, t Ideal for use as a first stage regulator on any'dornestic SlZe AS I ME or DOT container in Propane gas Installations requiring Up to i,s6o,oao BTU's per hour. The regulator Is factory set to reduce container Pressure to an Intermediate pressure of approximately 10 pSld. Ordering Information I O�er Outlet Lv3403TRV-91 Y4" F.NPT I W F.NPT I YV I P10 ar Ou�� MOXIMUM flow based an inlet pressure 20 PSIG higher than the SIG 9:00 1,500,000 '�'M��LV3403TR regulator setting and ;e—iivery srurs 20% lower than the regulator salting and delivery pressure 20% lower than the selling. I Provides accurate first stage regulation in twO-stage bulk tank systems, Reduce tank Pressure to an Intermediate Pressure of 6 to 1 10 I PSIG. Also used to supply high Pressure bumers for applications like industrial furnaces or boilers. Also Incorporated in multiple cylln6er installations. I information LV44 138N_�- 0 Y. F. NPT LV44 3TIR4 403S 44V4 jkR9 %12"' F. NPT L-1 U I Lv4403TR9 Y4" 5 LV4403SR96 F POL 10 PT .11, 5 LV4403TR96 F . N When used for final stage Pressure contrDl. must either incorporate 10 vWlh NFPA Pamphlet 58. Integral relief valve Maximum flow based an Inlet pressure 20 PSIG higher than the regulator setting and d Designed to reduce first stage pressure Of 5 to 20 PSIG down to burner pressure, normally 11" W.C. Ideal for medium commerciall Installations, multiple cylinder Installations and normal domestic fonds. Ordering InforMation LV4403CE34 Y210 113B46 YT F - NPT LV4403846R- #28 1 11" W.C. atio C) ia� w LV4403866 Y4" F NPT Drill PSIG PT LV44 03 B66111": NPT Inlet 114:111nount design maximum flow based an 10 PSIG Inlet and 9'W.C. delivery pressure, IT Yes I 2,500,00o Metal relief valve should be SPSCIlled In Occordance, pressure 20% lower than the setting. 91, td 13" Over Inlet I 935,OC)o LV4403 Series LV4403B Series 14