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HomeMy WebLinkAboutGas Piping SchematicsW i LL IAM. BOARD OFR PLANNING & DEVELOPMENT COUNTY Ewell SERVICES DEPARTMENT COMMISSIONERS o . Building and Code Regulation Division GAS PIPING SCHEMATIC TANK SIZE: GAL�XrST�G S. E1CIcr. APPLICANC —TYPEISIZE Al E BTU Q4 N �� §Z ' 2 BTU NEU�AA R 1I 1 /b+rDO BTU A5 . BTU' ' A6 BTU E^�,1 u1� /OL6STS/ CE)ClE72�oR PIPING LENGTH Ll & SIZE 11 bL I� (PIPE SIZE WAS TAKEN FROM f ��L2 O' FT. INCH DIA NCH DIA.TABLE AeLE4o2THE 2014 eCF(5�+UEL scoDE- E L3 FT. INCH DIA. L5 FT. INCH DIA. N. L5 F7', 1_6 FT. INCH DIA. LT FT. INCH DIA. DER/OR — /Ne✓ 1_8 FT. INCH DIA. 1_9 FT. INCH DIA. L10 FT. INCH DIA. L11 FT. INCH DIA. 1_12 FT. INCH DIA. Website: www sgucteco oov 230D )Arginla Avenue - Fort Pierce, FL. 34982-5652 Phone (772) 462-1553 FAX (772) 462-1578 Revised 7/22/14 56116 LIQUEFIED PETROLEUM GAS CODE Table16.l(n) L'alpetligtene+lslasticpipe_.`'IPS Ir�110� AS I�� 0 6 / Undiluted • Gas: Propane Inlet Pressure: 10.0 prig •' Pressure Drop: 1.0 psig Specific Gravity: 1.52 Plastic Pipe % in. SDR '/ in. SDR 11 1 in. SDR 11 1% in. SDR 11 It/2 in. SDR 11 ' 2 in. SDR 11 Length(ft) 9.33(0.660) (0.860) (1.007) (1 328) (1.554) (1.943) INTENiIEI)�iJ 1zu1g Betw_ een F1rst= ]ke Stage Pressure Regulator:and Secondstagel(I ow' Pressure),1" 0r ;C!F, —�130 2140 2390 7740 13420 20300 1 36400 40 1840 6630 11480 17300 „ 31200 50 1630 3260 5870 10180 15400 27600 60 1470 2950 5320 9220 13900 25000 70 1360 2710 4900 8480 12800 23000 80 1260 2530 4560 7890 11900 21400 90 1180 2370 4270 7400 11200 1 20100 100 1120 2240 4040 6990 106.00 4• 19000 125 990 990 3580 6200 9360 16800 150 897 897 3240 5620 8480 15200 175 826 826 2980 5170 7800•„ 14000 200 778 778 2780 4810 7260 13000 225 721 721. 2600 4510 6810 12200 250 681 681 2460 4260 6430 11600 275 646 646 2340 4050 6110 11000 300 617 617 2230 3860 5830 10470 350 567 567 2050 3550 5360 9540 400 528 528 1910 3300 4990 8970 450 495 495 992 3100 4680 8410 500 468 468 937 2930 4420 7950 600 424 424 849 2650 4010 7200 700 390 390 781 2440 3690 6620 800 363 363 726 2270 3430 6160 900 340 340 ST. LUoftoUN 2130 3220 5780 1000 322 322 UILDI<fB�IVI,1 N 2010 3040 5460 1500 258 258 REVAMED 933 1616 4390 2000 221 221 OR,C y g 498 1383 3750 yyII��S: ipe Size. REVIEWED DR:t�ndar t o q ote . DATE ' PLAN®ND I EI IT ties m, o q�l . hr. MUST MQ KL"PT ON JOB OR (2) Dimensions in D eses areyediamete . NQ IN13PROTION I L {)K MAb2 HoACO Wtl ER . C0wpvkCv GAS rid CO3,1>Ao?A146 2017 Edition AK Ap, (;,w THIS VESSEL IS DESIGNED FOR THE STORAGE OF LIQUEFIED PETROLEUM GAS ONLY SX )S=103- �r K I 2 TOP VIE_ SIDE ELEVATION NOTE TANK MUST BE INSTALLED LEVEL, WTM ALL LESS IN SANE PLANE TO ASSURE EVEN DISTRIBUTION OF LOAD AND OPTIMIZE ACCURACY OF( UCF OFVICF MI rvm ANY UNSPECIFIED WELD DETAILS JIY VIf11V1. HOLES (4) PLACES FITTING LAYOUT \` OPTIONAL _ DOME BRACKET FOR US GREEN ONLY NG. WELD SEAM • May vary loop seem ENGVIEW I4atomis618gx lE MARK OW. SQ TYPE SERMCE MAW( Ott. DMNMON OY%LND. REGOFITTINGS A 1 t mEm [xmmaT P,EUuvA0,Et t SHEIL031CXB7X11011/14-SMt<G B 1 t MRS, om. TGALGE 2 p HEADS-3T I.0.%6185-IONMI:SA114C C . 1 -im m U7S?w FlLLVAW 3 3 NFTINGWGS D-0 E 1 W4 MFL6 FI=55585145 MALT VALVE 4 3 TMMIEW D-3 F 1 14 BQ]SplllT CIIEI4WK 5 1 DOME D-5 WOW) 1 11N JOIFLG. 6 T 1 1 D4TAPIATE REGl6AMR BRPLNET D-50 0.10 e 1 dPTDITE LEMMI.1nr Fogmxg4vF B ] MWANDWISPORDOMEBPOfJ(ET5 D14 o-t0. IW 10 1 PN[OEATTACNMEM D-17 G�s�:i�Rr� rl T I CERTIFIED BY: QUALITY STEEL CC DEVDA�O.IO.RAQR. W.W6T%y�t w%Mla«.wlwLw�ss 25OPSI Il `rl N M F 20 •F. AT 250 m YFA MT U W. W4IN. ammmm NFA07 W �LTR PART NO: 0105002x_ WY. BY: pF5LNP110N PATE 1. LIFTING WGS DESINGE)FORTOTAL UFRNG WEIGHT OF IWW. 2. TOTALEMPTY WEIGHTIS I) O . 3. ALLDIMENSIONS ARE IN NGHES UNLESS OTHMWSE SPECIFIED 4. COMPLETETANKDRIEDTOREMOVEALLMOISTURE 5. ALLWIOROFTNDCAPAEGRTI LASTED O%IMATE 6. EXTERIOROFTANKTOBE GRR &ASTER T. VACUUM PURSE ORDER 8. VACUUM PURGETANK e. DIMENSIONARE RETAINING CHANGE NT S ONL NOTICE (NON -PRE SSURE RETAININGO BE COMPONENTS ONLY) tO.THREADS OFALLENTNGSTO BE COATED WITH COMPOUND SURABLE FOR USE WRH INSTALLED GAS 11.FLOXTLONGI UDINALAUSE O BERUNEO WTM FLOAT ARM 45' OFF LONGIil101NAL CENTERLINE OF TANK y43� 600 WG.ABOVEIUNDERGROUND 1t5M PROPANETANK-TYPE IQ5(FORMERLY AWT-SA) f1/121K1 f]ACD] OI1LV13 QUALITY STEEL CORPORATION a3nen4 wnm4 D ^F O1Iwl DG o.. RAC I TWV 1 23 X.5( AGUG STANDARD pROLO 15AL A/i/l�ri� t TANK r - rMof X1� - b �`/` • ,. Soo GAL. -- �,�. Lp -"GAS-- - �,�, ANSI 2223.1-53 PIPE SIZING 54-53 _ Table &3 (h) Corrugated Stainless Steel Tubing (CSST) Gas: Undiluted Propane Ides Pressure: 3I.01n. w.c. Pressure Drop: 0.5 in. w.c. Specific Graviln 1.50 1`Ti: I.YSfI •..._... ..o "v'..� '. \'.fin ♦...V1j 1.1 T e 'S' iY L SL "`l y' � GSSTS"'.BenveedSu�gte or SecondSt�ge(ImwPresnuel liegWetm tmd,AppBabee ShutoffYalv'ey: , _ ,i II47T1iDUSE. Ei1 Tube Size (IM) Flow Designation 13 15 18 19 23 30 31 37 39. 96 98 60 62 Length (ft) Capad is Thousands of Btu per Hour _ 5 72 99 181 211 355 426 744 863 1.420 1,638 2.830 3.270 5,780 6,550 10 50 69 129 150 254 303 521 605 971 1,179 1,990 2,320 4,110 4,640 15 39 55 104 121 208 248 422 490 775 972 1,620 1,900 3,370 3,790 20 34 49 91 106 18S 216 365 425 661 847 1,400 1,650 2.930 '3,290 25 30 42 82 94 164 192 325 379 593 762 1,250 1.480 2,630 2.940 30 28 39 74 87 151 177 297 344 528 698 1,140 1,350 2,400 2,680 90 23 33 64 74 131 153 256 297 449 610 988 1,170) 2,090 2,330 50 20 So 58 66 118 137 227 265 397 548 884 1.050 1,870 2,080 -�60 19 26 53 60 107 126 207 241 359 502 805 961 1,710 1,900 70 17 25 49 57 99 1 191 222 330 466 745 890 1,590 1,760 80 15 23 45 52 94 109 178 208 307 458 696 833 1,490 1,650 90 15 22 44 50 90 In 169 197 286 414 656 787 1,400 1,550 100 14 20 41 47 85 98 159 186 270 393 621 746 1,330 1.480 150 11 15 31 36 66 75 123 143 217 324 506 fill 1,090 1,210 200 9 14 28 33 60 69 112 129 183 283 438 531 948 1,050 250 8 12 25 30 53 61 99 117 163 254 390 476 850 934 300 8 11 23 26 50 1 57 90 107 147 234 357 439 1 777 854 EHD: Equivalent hydraulic diameter. A measure of the relative hydraulic efficiency between different tubing sizes. The greater the value of EHD, the greater the gas capacity of the tubing. ' Notes: (1) Table includes losses for four 90 degree bends and two end fittings. Tubing runs with larger numbers of bends and/or fittings shall be increased by an equivalent length of tubing to the following equation: L=1.3n, where Lis additional length (ft) of tubing and n is the number of additional fittings and/or bends. (2) All table entries are rounded to 3 significant digits. HoMEOONEIR •tjjLLiAA d,,R61,4 3-A CoNTNACTR (GAS) : 4'� 1a CO- °P"'E 2015 Edition 4e lb,,C 'tj �t "G 9OKe:oWt%JEK 1r & �,j„�--ate q,r4 Co w. poga,krj -fwfj?WE IA SOTS aa-3,wv CNA El