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Home My WebLink AboutGAS PIPING SCHEMATICSCANNED S Lu6j6 Count/ BOARD OF COUNTY COMMISSIONERS TANK FLl SIZE [.AS PIPIAI 1 2] [L4] L31 FL5 1.21 [L6] [A1] [A3] TANK SIZE: S"d GALS. APPLICANCE — TYPE/SIZE Al e A2 —fi A3 A4 A5 A6 [A4] [L8] PLANNING & DEVELOPMENT SERVICES DEPARTMENT Building and Code Regulation Division RECEIVED MAY 17 2018 [L10]FILE COPY [A5] i BTU BTU I BTU BTU BTU j BTU ST. LUCIE COUNTY BUILDING DIVISION REVIEWED FOR COM �.1A �9CE REVIEWED BY DATE -1 PLANS AND PERMIT MUST BE KEPT ON JOB On NO INSPECTION WILL BE MAD- E-t S as- oY 'rb PIPING LENGTH & SIZE . (PIPE SIZE WAS TAKEN FROM L1 FT. 3 INCH DIA. THE 264448C FUEL GAS CODE - L2 FT. 3 INCH DIA. T49I F 4Cl (_�) L3 FT. INCH DIA. L4 FT. INCH DIA. L5 FT. INCH DIA. L6 FT. INCH DIA. L7 FT. INCH DIA. L8 FT. INCH DIA. L9 FT. INCH DIA. L10 FT. INCH DIA. 1-11 FT. INCH DIA. L12 FT. INCH DIA. Revised 7122/14 i7o-oQkCA urc le Website: www.stiucleco.gov 2300 Virginia Avenue - Fort Pierce, FL. 34982-5652 Phone (772) 462-1553 FAX (772) 462-1578 -- q J S Ja RS a <J -� co -- NSA `'" c BOUNDARY SURVEY prepared for Joe Grenadier 4 NOT TO SCALE. Y PNWP L•1[SI CC•. Y!C U BI.S I . a TRACT i { '�J hnu•u r L Set 112' Iran MLEA C and 'RL5 0391 Ca _ _(TYPICAN S89° i4' 54'.E. 50. 00 mi = cable Splice Box t0"UT TY'AND OR0.1N GE EASEMENT- 35e I '4 uOCLnE xG1uC0� { 199 I CD •[[AII o� 14 [5.i 61, 163 I 5 / 0uul u111 l V 3 t i`T TTi ' I I I I I I0i zo cc Forseoarde Elevation • 52. B' O o Lot 4 w Lot 5 Lot 6 u.l Q) Lo roan �Jkcvt��r@ I V o I Z 12. 35' 16 1 \ 2.00 65' phone Splice Bex l` R=355.00' 25g• A-24e2= ' water Ser�lee� i I R•305 p=1' 36 A•1( Fodnd PK 'PCP 22 of 0r\ A \P m121.35' G�\1�•1 i—PTun1 j fl I $tt 1 From 54NOce. /� of Crete T ��'®��C ) 91, A-0m. M onnuci4. nt T &- —{glen — — — -- _ f0' UT LITY AND DRAINAGE EASEMENT• SB9' i4' 54' E 40.00'I o Valley Oo{{eT — L POI NC 1 ANA COURT SB_•E 612.66' BEfiRlfib_ BASIS — —7� (FOflNERLY INTEflNATIONAL CIRCLE) 40.00' p. B• 23, PGS. 26 TO 26C (60' Right -of -Nay) I t1re Hydrant Maximum Capacity of PE Plpe in Thousands of BTU per Hour of Lioue(led Petroleum Gels With a C-a, Pressure of 11,0 in, WC and a pressure Drop of 0 ^-' IS in. WC �_�� (based on a 1:62 spa6lito gravity aanl 1073 1391 720 934 671 740 484 425 67 383 325 o 1286 1983 131 1054 627 893 786. 370 3663 4724 2391 3247 11394 2608 1605 1412 708 7272 600 1078 528 1946 10063 6755 6351 2232 4535 1978 3989 7792 7534 11359 3592 3044 !2678 129 167 113 147 102 732 8V to 6 76 12 11 66 63 238 427 209 376 788 338 112 140 81 116 12252 642 1207 569 1061 516 287 447 391 7 208 54 3 54 326 956 810 712 642 587 587 Maximum Capacity of PE Pipe In Thousands with a Gas Pressure of 2,0 psi c (based an a 1,52 an, 257 236 -- 204 10 29 119 26 333 475 306 435 283 264 249 219 152 197 854 781 403 723 376 376 384 311 280 1232 1133 1054 989 938 560 828 504 2411 „°i, 2207 2044 1910 1797 1581 750 1424 58 54. bl 48 I70 63 46 44 42 40 1D6 100 192 180 169 160 60 57 81 54 78 62 76 1544 508 803 285269 255 478 152 244 233 224 216 463 431 417 394 379 )f BTU per Hour of Liquefled petroleum Gas 516BTUh_1CFH d a Pressure Drop or 1,0 .111rr M-1h. _. psi 11300 14652 758b 6008 5092 //y479 702 69& 23 20877 9836 14014 7790 11100 6602 9408 807 5229 443 4432 3007 25183 19946 16905 8275 14869 7451 }451 �qs3qs88595837514 43429 106963 29848 71131 23969 56339 20516 78182 16474 1136 14100 2 12496 47750 - 42000 37820 32054 2879d 1366 1192 1073 910 WI 125 116 1767 2503 1545 2202 1391 1179 1037 934 855 4498 3956 1983 1680 7478 1331 3563 3019 2656 1218 5903 12705 5232 11176 2391 4740 4067 3596 3288 2189 2997 10063 8829 7602 6765 6182 Maximum Capciclfy of PE Pipe In Thousands with a Gas Pressure of 10.0 psi (based on a 1.62 soe 2707 2478 2296 2144 J71 309 278 3510 6002 3218 4578 2975 4239 2780 2617 2302, 2073 8988 8226 7618 3962 7119 3729 6700 3280 2953 11322 26388 10417 23234 9691 9092 8689 5894 7612 8307 6897 21617 20108 18924 16647 14990 611 571 537 792 740 508 484 62 80 77 443. 74 428 696 1128 7054' 992 659 939 627 893 599 574 551 !027 .1894 178818 3 !788 2616 1688 1605 883 1533 1469 71 2471 726 6350 5036 2347 4767 2239 4535 2744 2060 1985 4331 4150 .3988 f BTU per Hour of Ltquefled Petroleum Gas5168TUh;1CFH f a Pressure Drop of 1.0 psi c gravity goa) 14234 9556 7568 ' ' V 6414. vol 6642 U64 749 6�` 5g 43 ° ° 6153 8496 26296 17652 17652 9812 13981 8316 7315 6080 6687 4306 6683- 3787 4910 3410 4422 3121 2840 2701 2542 2236 350 2614 47252 31720 25123 11849 21293 10423 18729 9385 16865 7954 6997 6300 4047 .6766 3747 3747 3502 3502 3 32�6 223 2611 53960 133476 37087 89601 29782 70967 25489 60148 22591 20469 14294 17619 12672 12522 11321 11321 70361 9640 8967 06 4697 413 1 71 23 3720 82905 47640 40376 3-6514 31980 12943 29267 12041 ]1297 10671 94 588569 6b85 27104 26329 238g0 20970 1882 1601 1352 1146 1008 907 2273 213 3163 1946 2773 1753 1485 1306 1176 830 1077 8665 4983 2497 4487 2116 3803 1862 1676 1534 7334 6500 6890 5041 3345 4468 3012' 2757 76004 14077 12676 10743 9449 4048 8509 3724 7787 Ph: 1-800.662,0208 Fc1x; 615,326,9407 a Web: WWwgastlte.com I134 769 125 719 118 1 1'101 �� 97 �� 93 997 932 676 877 640 609 0 682 557 536 '1421 7328 1250 1883 11 1� 5 723 695 2853 7212 2386 3251 2246 3077 2126 2022 1931 030 185, 990 779 7212 6739 6343 2916 6005 2782 5712 2664 2560 2466 545.5 6227 5024 25168TUh=1CP141 r 0 ®O0 Fg��rr�y,�xs� I V Q�IUJ 11Cl�Ol'n , s:�f -�I •Sy��e��;,} �k � � �•:s- � �� • '� ,_ £ a . ,v � . �' �� d�Y'"• t -: `F t�.Y�� 1 {tn �}v t: Y"�`�,L t�ti :•'i C ytF'} •a. y Runuad a1 by PERC < ° 7. •• in avarall partorinanao Innldnp r -� E i" .•". 'No{ ;< ... 3yy,-' , 3 .��,.�• '" .', rorProlooftCoaftsappliad 2'•71 •' ;., an Underground PropmraTanks t „ w z F., . r,t tD�'4 �� tyZ�in r7y r nva :n k �� '�`4 tG. cx'ya t. ..a>.,......�;. - .•,.u`tln x�I�r�N "£ -�r �� 3�i.t�'�lW� rv. tir�.�� •Y?S dt °r f 1� t Y`Z' ,� +t t { �.'n'�i,� ,4 C�+ ' • I .,. C;. ."' ..,. C" 2,. ..:>i_ ... nA�vP ..c �,v ' h ,,tb i. )1�V F C u�}fl Iy t }t• ?cl r�'^C,p �-��. a-�Y ..'• ROUDLY FINISHED WHTm � ��}tir-�t�'-�w-?E,�-��+�• ' ;*ai r-Ts� ,'1• h�$f�`'�a.��rtr.'3�n �r,�� G.�t Z� _'��:� � f�] (��f �(�pyJ/��Qf� �f r,:,.CL�'�✓ryi.'YSd.L 4 rv' y...'l �" ' UE U tl Wl § l! - IJ lJ §LLLtllr"111i 15't7�6 8"-dome•in,black plastic or white gplVanized stebl; i { IPiU:Il W RM- - O:ne .;k1t6ftsa fil Durable Topcoaf. ;uvthlZinc`Rich+tPrimer{an�Aovegrtound+ iPOWD:URA'l&LE Curen� Two�eoatl.sys#e im+;properties�inelucie: -4 Zinc;i;[ci�iel axypriiiPer ra 5uertd`ufaule�TGlCff�4lyesteaopeo?ti ' '.':� Superiorteor+:ositin�5nilketlgeiproteeton. • . ' �•;Patenivtie+�dri"c�;:formulai'edrprimer antl�+fopca�l • Dual service options for above or underground applications • Option #1 Ready -to -bury red oxide durable powder coating with black • polyethylene AGUG dome* • Option #2i 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 Vill, Division 1 • Registered with the National Board • tt72 liquid -level outage valve orifice reduces refueling emissions • Vacuum pre -purged to save time, money and product 'Applicable federal, state, or local'regula lions may contain specific requirements for protective coatings and cathodic protection. The purchaser and installer are responsible for compliance with all federal, state, local and NFPA industry regulations. Cathodic protection isirequired and coating must be continuous and uninterrupted and must comply with,an local, state or national code. www.ToiiityContainers.com Call Toll Free: 688-558-8265 -A �' TRINITY Co»fairting OurWeiJd's�eY , VVILJ I n General Specifications Conforms to thtest editio e lan of the ASME code for Pressure Vessels, Section Vlll, Division I. Complies with NFPA 58. Rated at 250 psig from -200 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 FLOAT ,' NOTICEVALVE GAUGE I ANODE CONNECTION 'L,,-FILLER O OVALVE MULRVICE / ' TIVALVE NAME __-�- PLATE RELIEF VALVE FITTINGS LAYOUT UNDER DOME AGUG VESSEL DIMENSIONAL INFORMATION All Vessels dimensions are approximate WATER CAPACITY OUTSIDE DIAMETER HEAD TYPE OVERALL LENGTH OVERALL LEG LEG WEIGHT QUANTITY 120 w HEIGHT WIDTH SPACING FULL PER . 454.2E 24 609.6 mm Ellip 5,- 5 13/16" 1671.3mm 3' - 0° 10 1/8" 3' - 0" 245 Ibs. LOAD STAC 250 wg, 31,5" Heml 7' - 2 1/2" 911,4 mm 257,2 mm 914.4 mm 111.1 kg, 96 12 L 800.1 mm 2197.1 mm 3 - 7 1/2I' 1104.9 mm 12 3/4 � _ „ 72Ibs. 63 g 20 w. 3g. 31,5" Heml 8' -11 3/4" 3' - 7 1/2" 323.9 mm 1066,8 mm 2 1g 1211,2 L 800.1 mm 2736 ,9 m" m 1104,9 mm 12 314" 4' - 0 114" 588 Ibs. 45 g 500 w9• 37.42" Heml 9' -10 323.9 mm 1225.6 mm 266.7 kg, 1892.5 L 950.5 mm 2997.2 mm 4' -1 7/16" 1255.7 mm 15" 381.0 mm 5' - Oil 871 Ibs. 30 .6 1000 wg, 3785.0 L 40.96" Hemi 15' -10 13/16" 4' - 4 5/16" 16 1/4" 1524.0 mm 395.1 kg 1040.4 mm 4846.E mm 1344.E mm 412,8 rnm 9' - 0" 2743.2 1729 Ibs. 15 5 mm 784.3 ka Rev; Jan, 27, 2016 1 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 conductivit circuit. y of the soil promotes the flow of DC current in the corrosion 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 r1' 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 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 over 99% 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 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. 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 -0,150 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 islwell 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 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 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 conditions. The H-1 alloy. is generally very effective. The following chart provides size and quantityrecommendations 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. Copper and steel create a galvanic couple that will accelerate �corrosfon of the steel tank when directly connected to copper piping. 'Generally, copper piping does not require cathodic protection. I 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. (i)0 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 (Y 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 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 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. 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_ Soil Type „77!1esolls;;:Clay San(!Vlbam� , Tank Cap. 5 to 5000 o(im-cm (gal.) Size Qty. Alloy 120 9# 150 9# 250 9# 325 9# 500 17# 1600 17# 1500 17# 2000 17# 1 I . H-1 Sand, Gravel, Rocky Areas 5000 to 10000 ohm -cm -1 -1 -1-11111 §SlzeAloy 'Based on 90% effective external coating, 2 ma/ft2 current density, and 30- yearAnode 11fe. 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. B.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 becoated 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. ideal for use as a first stage regulator on any domestic size A installations requiring up to 1.500,000 BTU's per hour. The reg Pressure to an intermediate pressure of approximately 10 PSIG. is factory set to r- propane gas educe container �" FNPT YV RNPT • t,Vsgoa�'t;vg /3x" 10 PSIG Over Outlet Maximum Dow based ur iNet pressure 20 Pete higher than the regulator selling and del 9:00 , 1,500,000 sailing end delivery pressure 20 Pressure lower than the selling. ry pressure 20% lower than the regulalar 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 i high pressu`re burners for applications like Industrial furnaces or boilers. Also Incorporated In multiple cylinder Installations. When used for final stage pressure contrcl With NFPA Pamphlet 88. , must either Incorporate integral renervalve or separate relief valve should be specified in accordance " Maximum flow based on inlet pressure 20 PSIG higher then the regulator selling and delivery e 9 8 9 ry pressure 20% lower than the selling. Designed to reduce first stage pressure of 5 to 20 PS1G down to burner pressure, normally 11" wc. Ideal for medium commercial installations, multiple cylinder Installations and normal domestic loads. 11'aIceRlt� ��ii��li'a�tt�il«rn an 10 PSIG Inlet and 9° txc. delivery pressure. The LV34036R Back Mount Regulator is de burner pressure normally signed to reduce first stage pressure of 6-10 PSIG down to 11" w.c. Designed as a second stage regulator for smaller applications with flow requirements up to 450,000 BTU/hr, and are ideal for homes, mobile homes, and cottages. ��'�Qilrglln� i>Im�mrrri;�t�su®r� '/z" F NPT " I -AFT I 11" W.C. At 10 L\!�403$ri6R s/e'� l= AIp7 7/3a„ PSIG Inlet Maximum now 16 based on-10 PSIG inlet and 9" W.C. delivery pressure. 9° to W.C. I Over inlet