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HomeMy WebLinkAboutGAS PIPING SCHEMATICBOARD OF COUNTY COMMISSIONERS [A2] TANK[ILILTIp SIZE [A1] TANK SIZE: -LE(L GALS, APPLICANCE - TYPE/SIZE Al r e�lercnl A2 A3 A4 A5 A6 V��Bt7tlV�� lay SR LucbI CauMy PLANNING & DEVELOPMENT SERVICES DEPARTMENT Building and Code Regulation Division [A4] [A6] [L12] L61 rREVIEINED 8o5 Zvi% Lucl AUNTY ] BUILDINGE�lt9{E©o� YNSAND PERMIT E KEPT ON JOB OR CTION WILL B E_ BTU BTUmml BT PIPING LENGTH & SIZE FT. 3 4 INCH DIA. (PIPE SIZE WAS TAKEN FROM LI L3 FT' FT INCH DIA. (3DE- L4—FT. FT. • L5 INCH DIA. INCH DIA. �� 0-017 F�L (Gu�l Gas Cod-e_ INCH DIA. � INCH DIA. L7 . FT. T L8 ,INCH DIA. FT• L9 FT. INCH DIA. L10 FT. INCH DIA. INCH DIA. L11 FT.' L12 INCH DIA. FT. _ INCH DIA, Revised 7/22/14 i Website: wwwAtiucieco ^ov 2300 Virginia Avenue - Fort Pierce, FL. 34982-5652 Phone (772) 462-1553 'FAX (772) 462-1578 ,6\7 CJ vIA S5` 31� Pot Maximum Capacity of PE Pipe In Thousands of BTU per Hour of Liquefied Petroleum Gas with a Gas Pressure o't 11.0 in. WC and a Pressure Drop of 0.6 in. WC (based on a 7.52 specific gravity gas) MEZURIM 1073 720 571 484 425 a1 56 1 50 45 e 383 325 i286 257 41 38 35 33 29 26 1391 934 740 627 561 497 421 235 218 204 192 169 152 1983 1331 1054 893 786 11 708 600 j1528 4�5 305 283 264 249 219 197 3563 2391 1894 1605 1412 1272 1078 948 854 435 403 376 1354 311 280 4724 3247 2608 2232 1978 1792 1534 1359 151 81 103 676 934 828 504 781 523 676 636 560 504 10063 6755 6351 4535 3989 13592 3044 i 2678 223 1133 2044 1910 1797 1581 1750 4 e 24 C os 22 20 18 15 13 '11 •�° eee °e oe ee 129 113 102 86 76 8 3 ]0 9 °° ee 68 63 9 8 8 8 7 7 167 147 132 112 99 ; 89 81 75 7p 51 48 96 44 42 40 238 209 188 160 140 126 116 107 bb 63 69 b1 54 52 427 376 338 287 252 100 94 89 85 81 78 76 642 569 516 441 391 ; 354 326 I W3 286 269 255 244 2146 33 140 134 1207 1061 956 810 712� 642 587 544 508 478 453 24 224 216 411 394 379 Maximum Capacity of PE Pipe In Thousands of BTU per Hour of Liquefied Petroleum Gas 5168TUh=iCFH with a Gas Pressure of 2,0 psif and a Pressure drop of 1.0 psi ° (based on a 1.52 specific gravity gas) ° • o 1966 ]319 1045 886 779; 702 5951 523 471 11300 7586 6008 5D92 431 399 373 351 309 279 ]4652' 9835 7796 6602 5807 5229 4432 3898 3510 3213 2975 2144 2018 1775 7599 37514 14083 i1100 9408 8276 7451 6316 5555 5002 4578 4239 3962 3729 3280 2953 37514 25183 19946 16906 14869 13389 11348 9982 8988 8226 7 278D 2617 2302 2953 0596 71131 23969 20s1547750 18182 16474 14100 12496 11322 10417 9691 9092 8589 7612 6897 105963 71131 56339 47750 42000 37820 32054 28194 208B 23234 21517 20108 18926 16612 5307 ° 47 14990 ee '1° ee .ee ee :ee 236 207 187 168 139 125 115 106 9g eee 10 " ee 'e ae 1365 1192 1073 910 800 126 616 611 571 59-3 37 88 84 80 77 74 1757 1545 1391 1179 1037 934 855 608 484 462 443 2503 2202 1983 1680 7478 1331 1218 1128 1054 992 939 893 853 425 4498 3956 3563 3019 2656 2391 2189 2027 1894 1783 1688 1605 1533 1469 14�2 270 5232 4)06 6755 3196 3258 2997 2788 2616 2471 2688 1605 1633 469 1412 12706 1117b 10063 8529 7s02 6755 6T82 5725 6350 2471 4767 4535 4331 4150 3988 Maxlrnum Capacity of FE Pipe In Thousands of BTU per Hour of Liquefied Petroleum Gas 516BTUh=1CFH with a Gas Pressure of 10.0, psi and a Pressure Drop of 1.0 psi (based on a 7152 speclQc gravity gas) e 2476 14234 ]662 1316 1116981 684 7.4e9 65- a9 ° 0ya 0 195557568 6414 5642 6080 4306 3787 3�i84519812 8316 4103121 2890 2701 2642 2236 2583 4910 4422 407 3747 1426296 17652 1301 47252 10423 9385 7954 6997 6300 3592 2601123 21293 18729 40 899 991 5 14294 4697 4131 372953960 37087 29782 25489 221 10361 9596 8967 4697 69 17519 6685 15527 74068 12943 12D41 11297 10671 9458 8569 133476 89601 70967 60148 b2905 47640 40376 35514 31980 29267 27704 26297 10671 9458 1889 e ea o ee ee • - o 297 261 11 •/e +e :ee 235 �199 158 •1e eee ee ee ee 1707 1601 1352 1146 ;10 8 l44 134 125 118 111 106 0e ee 93 2213 1946 1763 1485 1306 907 830 769 719 676 640 609 582 567 3 3153 2773 2497 2116 I1862 1676 1534 1421 1328 1250 1183 1125 1075 103 695 932 877 830 790 754 523 7334 6500 5890 3803 13345 3012 ;2757 2553 2386 2246 2126 2022 1931 1851 17�9 7334 6500 5890 5041 1 4468 . 4048 3724 3465 3251 3071 2916 2782 2664 2851 2476 16004 14077. 12676 10743 1 9449 8509 '7787 7212 3251 3071 6005 5712 2664 5227 2466 5024 Ph: 1.800.662.0208 • 2516BTUh=1 CFH Fax: 615.325.9407 p Web; WwW gastlte.com I 7 B-OUND-A-R-Y .SURVEY y� 6�..50 5u pRPjIJP,, UGC P 0T UMU PEUMPnoA! • u0aamri LOr f, EOITAYS REFOGE; ALtiYAPOWG 70 171E HAT nIERt'OF, AS REO�ROEON nORMA. LN' TJ; PAGE m Or 7NE PUBLIC R£G DS Or SE LOGE COON7Y• 5-0 • S7?tWMS NOIES ' 7. LANOS S/OBN y2111W R— NOT A—AGIED FOR EASLtfER75 AND/gV I{77775 O'-.WAY OF R£c44O ExYfPT AS 91ow av pl£ RFCQ:M PAT 7� c` lF ANY. BO24WL5 rf1 a9 ALWCOIT r0 7w 57m OERG4We\9•FOO)ING$ Cf- .4ALCLWf7EEOMLVSBOOaOn'AIN BLN1Y1'µ S:PR615Y£7R76aR'£/{S R/aNTr6FAN PAAYSISB7aL1EDLi NS VLEGI5AGP fNNAaWL? VN£m1 \ \ 1AnL lC£R-6'a �llr b17FD,. fF6WCRY iBMAIII ROM AIW S 5,7E AREA' 471A72 SCYL4RE fEET. S LEGAL OEMWIlaV fDR1 Z* BY QIOfr 7. A00I77aV5 a4 ' OE,EnONS W SLRkEYMAPS aP ARPa47S BY OnkR RNN R1F. SQVVVG PARTY a4 PARFES IS PR No M1TTfOLIT NR?7EiV L'at5Er7T a"' nI1' SGMNG PARTY a° PAR71£S $ BEARGVG$ ANX AND a•SrANXS S Y01W NE78LW ARE BASED aV PLAT• e or MOM M101w NEREa1 a -:WY• LS 1AVT APAWZW BY VJIS SORb£Y. ` ®�• o snel'EraRs cf MMA nau' SL47YEY7LAP'ANO ' . ,i Cit REPa9r aP Ilk' GOP/ES' nrfa£o� ARE�Nor W7nour TNF 9GNA)GWE AND INE asmNu BAWD SEAL PiA fLa?49A swkz W tdr• z to a4 /✓JAug AND YAPPER. �I /. . _ G - - !`LICEMD rFi SAL 1.V1D S.WYE,'a4 ui J0 Na *uA srA T£ a' fzaelBA . ice" : �f `��•• � `G:i•.i .: J•: � f01.6 - _ "d;,� 4asl • a'. LOT 1 cn o � � � . • .; om ', :' �' frown .s.• ol c Rjn%.Z3: .`�� �., J�yC� (! iE7',7. _• O B9 ic• .'.^:,�'".���. �• s: Qom .• ' •S•• cl N N \ �. iT �1.•�> I�yC�:I�•�.ti.� 'Y� p �V� IIVE -� 1. 4! •.�}{S,`�� •'sn' t:� •�i. � V/� 1. l / io 4r=� f?��t_ �: •,�wa EAR GRAPHIC SCALE /otn ya•awAm �1' i'• 't ir4Y';Ef y � ._. • � .r o�, - � m Feet) 20 1L LOT 2'>. a. r3�g9 lmh a f Roo s BLOOMS T '1� --E� ,2� , f'� �, PROFESSIONAL LAND F rE' s B 41 SURVEYORS, INC. JOB NO. 364 LB. 018. REVISIONS 641 NE SPENCER STREET ' JENSEN BEACH, FLORIDA 34957 PRONE 772-631-8935 � �„�,�,;,� PREPARED FOR SHERD D. /FERN o i L fa Rf, asG APLAOLSGPf COWANY. 12737 S. lND/AN-Rll/ER DRl!/E a ST. LUCK" .COUNTYFL , OR/DA f7BE:/rrfunpvAt nnE,a�aQaoA•tvc 1-31 lu, use as a Tirs; stage regulator on any domestic size ASME or DOT container in propane gas installations requiring up to 1,500,000 BTU's per hour. The regulator is factory set to reduce container Pressure to an Intermediate pressure of approximately 10 PSIG., Ordering Information LV34o3TRV9 ,,„ F.NPT I %" F.NPT X" I PS10IG over Outlet 1 500,000 I �. LV3403TR 9 00 Maximum flow based on inlet pressure 20 PSIG higher than the regulator setting and delivery pressure 20% lower than the regulator setting and delivery pressure 200,E lower than the setting. Provides accurate first stage regulation in two -stage bulk tank systems. Reduce tank pressure to an intermediate pressure of 5 to 10 PSIG. Also used to supply high pressure bumers for applications like industrial furnaces or boilers. Also incorporated in multiple cylinder installations. Ordering InforMation LV403SR4 LV4403TR4 F. NPT LV4403SR9 ''/" F. NPT LV4403TR9 '/a LV403SR96 F. POL'F.NPT 3" ' When used for final stage pressure control, must either Incorporate With NFPA Pamphlet 58. Maximum flaw based on inlet pressure 20 PSIG higher than the rea Yes 1 2,500,000 'gral relief valve or separate relief valve should be specified in accordance i [or setting and delivery pressure 20% lower than the setting. i Designed to reduce first stage pressure of 5 to 20 PSIG down to Installations, o medium multipl cyl nder nstal ationsand normal omest domestic loads. information LV44031S4 2„ LV4403B46 %" F. NPT LV4403B46R' 11" W.C. #28 at 10 9" to 13" Over LV4403B66 '," F. NPT Drill PSIG W.C. Inlet 3/<" F. NPT LV4403866R" Inlet • Saclanount design '• Maximum flow based an 10 PSIG inlet and 9° w.c. delivery pressure. 935,000 LV4403 Series LV4403B Series 9 i 14 IVIcaximumI Cclpaolty of PE pipe In Thousands! of BTU per Hour of Llcluefled Petroleum Gagith q Gas ; rassure, of 11.0 In. WC and a Pressure Drop of 0.5 in. WC iar.a—(based on a 1.62 sciaclRc gravity gas) n��-,• 1073 1391 720 934 4 571 571 0 484 �y I 42- 07 383 56 325 - 50 286 5 257 � 1 ap 3b 33 29 26 1391 13 10 627 893 561 I 497 421 370 333 305 305 218 283 264. 264 192 169 152. 3563 2391 7894 1605 1412 1272 1078 528 948 854 435 403 376 354 354 219 311 197 280 10063 006 6765 6755 5351 5351 2235 4636 1989 3989 1792 3592 1634 1359 1232 1133 1054 989 934 3044 2678 2411 2207 2044 1910 1797 828 1581 7804 50 1424 22 129 113 16 15 00 13 Ma / 12 oo 11 1 10 •11 /Ie /1 01 0 00 /1 167 147 102 132 86 112 76 99 68 63 68 9 54 9 51 8 48 8 46 8 7 7 . 238 427 209 376 188 338 160 i40 89 126 81 116 75 107 70 100 d6 63 60 44 57 42 54 40.. 52 642 1207 569 816 287 441 391 391 354 354 208 326 192 303 180 94 169 89 160 86 81 78 140 • 75 1061 956 610 712 642 587 544 286 508 269 476 255 244 233 134. Maximum Capacity of PE PI 463 431 411 5168TUh=1CFH 394 394 3216 379 79 in Thousands of BTU per Hour with a Gas Pressure of 2,0 of Liquefied petroleum Gas psl and (based on a 1.52 specifle a Pressure Drop of 1,0 psi gravity gas) 17300 7586 6008 SD92 /u2 995 523 47� 431 399 e1 1 '14652 9835 7790 6602 8807 5229 4432 �, 3898 351007 �0 3213 2975 2 404 351 309 278 20877 14014 11100 9408 8275 522 6432 2018 1775 ]b99 37614 29848 19969 16515 181 13389 11348; 9982 8988 8226 7618 74578 4239969 63729 00 28 5307 0596 71131 23969 77-50 18182 7820 14100' 12496 11322 10417 9691 9092 6689 7612 be97 105963 71131 56339 d7750 42000 37820 82054� 28194 25388 23234 21617 20108 18926 16647 14990 01 1 /e .lo ° ° o 236 207 E 168 139 .lo a1 t11 •11 Ilo 126 11$ I 106 99 93 881 84e Io ee Io 1365 1192 7073 910 80D 720 80 77 74 1757 1846 1391 1179 1037 934 8792 55 611 740 . 537 608 484 462 2503 2202 1983 1680 1478 1831 1218 696 669 b27 599 443 42b 4498 1128 1054 992 939 893 853 574 551 3232 3740 30i9 2656 2391 99 2027 1894 1783 16e8 1605 1633 1818 469 1412 5903 5232 .47A0 4D57 3696 3258 2997 2788 2fi16 2471 2347 2239 263 12705 11175 10063 8529 7502 6755, 6182 i 8725 6350 5036 4767 4635 4331 ' 2060 ]985 1Mal-Imum Capoe fy of PE pipe in Thousands of BTU per Hour of Liquefied Petroleum Gas 415D 3988 28169TUh=1CFH with a Gas Pressure of 10.0 pst ctnd o Pressure Drop or 1.0 psi _ (based on a 1.82 speclRc gravlly gas) 14234 ,vvz 9555 1516 7568 1176 6414 981 884 ��W 749 ! 659 593 ' :e •e °1 18455 12388 9812 8316 5642 7315 6080 6587 4306 3787 3410 3121 2890 2 00 2702 2542 350 26296 47252 17652 31720 13981 11849 10423 9385 5583 7954 4910 6997 4422 6300 4041 3747 3&96 23 2236 2899 2014 261] 53960 133476 37087 25123 29782 21293 25489 18729 22691 16865 20469 14294 17519! 12572 -11321• .6765, 10361 5340 9596 4990 8967 . 4606 8440 89601 70967 60148 62905 47640 40376i 16527 366i4 14068 12943 12041 11297 10671 9423 9468 31980 29267 27104 26297 23840 6689 1889 1707 1601 1362 1746 1�008 907 i4q 134 125 2213 3163 1946 2713 1753 1485 1306 1176 10707 769 997 779 932 6665 4983 2497 4487 2116 3803 1862 1676 1534 7421 1328 07 3345 3012 4048 2787 2553 2386 16004 7407 12676 10743 9449 8609 3724 7787 3465 7212 326 1 i 6739 Ph: 1.800.662.0208 ° Fax: 615.325,9407 ° Web: www.gastlte.col I '676 640 609 682 557 536 877 830 '790 754 723 695 1260 1183 1126 1075 1030 990 076 29126 27782 6343 6905 5712 2664 5455 2560 5227 2466 5024 7