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HomeMy WebLinkAboutProject Information, gas schematic • PLANNING & DEVELOPMENT BOARD OF SERVICES DEPARTMENT COUNTY COMMISSIONERS o o Building and Code Regulation Division GAS PIPING SCHEMATIC [A2] [A4] [A6] [L4] [L8] [1.12] TANK L1 1.3 L5 L7 L9 L11 SIZE [L2] [L6] [L10] [Al] [A3] [AS] BUILDINjq DIVISION �3EVI iFOR OoeREVIEWED BY �.�-- TANK SIZE: GALS. DATEPLANS A7 MUST BE KEPT ON JOB OR APPLICANC —TYPE/SIZE NO INSPECTION WILL BE MADE Al er. 5C&OOd BBTU TU 76 A3 BTU A4 BTU A5 BTU A6 BTU PIPING LENGTH & SIZE (PIPE SIZE WAS TAKEN FROM L1 100 FT. ri INCH DIA. THE 2014 FBC FUEL GAS CODE- L2_ I. FT. &'vINCH DIA. TABLE 402(�,�e 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. „ � r ,�, p ` L10 FT. INCH DIA. ' �'U L11 FT. INCH DIA. L12 FT. INCH DIA. Website:www st ucieco ov I i .4 2300 Virginia Avenue-Fort Pierce,FL. 34982-5652 Phone(772)462-1553 FAX(772)462-1578 Revised 7/22/14 t, 2-0 . _2-(e) �s 3 O Pv O/ - --- - -- - -- i 31 Z. Table N-5 Elevated Pressure 2 psig Maximum Capacity of OmegaFlexTracPipe CSST in Cubic Feet per Hour(CFH)of Natural Gas(1000 BTU per cubic foot approx) Gas Pressure:. 2 psig Pressure Drop: . .1.0 psi: _ (Based on a 0.60 Specific Gravity Gas) Tubing Length(feet) 3/8" 15 410 353 286 246 220 200 172 154 139 128 124 120 112 107 94 87 75 67 61 53 47 43 40 38 36 34 33 31 30 29 28 1/2 19, 965 700 567 ..493 . 444 406 353 317 290 269 260 252 238 '226 203 186 162 1451 '133 116 104 95 88 83 78 74 -71 68_ 65 63 61j _. 3/4" 25 2430 1734 1423 1237 1110 1015 883 792 724 672 650 630 595 565 507 464 403 361 331 287 258 236 219 205 193 184 175 168 162 156 151 • 1" 31 4220 3004 2463 2139 1917 1753 1522 1365 1248 1157 1118,1084 1023 971. 871 796 691 ' 620 567 492 441 403 374-. 350 �30 314= 299 287 276 <266 257.r, 1114 39 7969 5670 4646 4034 3615 3305 2870 2572 2352 2180 2108 2042 1927 1830 1640 1499 1302 1167 1067 926 830 759 703 659 622 590 563 540 519 500 484 1Irr 46 13626 9599 7820 6762 6041. 5509 4763 4255 3881 3590 3467. 3355 3161 2997 2678 2442 2111.1886.1720 1487 1329 1212 1121y`:1048 987 936 892 853. 820 789 652`; 2" 62 0546 121637 17684 15326 13715 12526 10855 1971S 188721 8217 7940 1768917251 6881 6158 15624 4874 4362 3983 3452 3089 2821 2613 2445 2306 2188 2087 1998 1920 1851 1788 see notes below' EHD t:111=ient Hydraulic Diameter)A theoretical size which reflects the hydraulic performance of the tubing.It is not a true physical measure.This number is used to compare individual sizes between different manufactures. Pressure drop across a regulator will vary with flow rate FGP-REG3 has a 3/4 PSI pressure drop at a flow of 250 cubic feet per hour.regulator the higher the EHD number the greater the flow opacity of the piping. Table does not lncludeeffed of pressure drop across the line regulator.CAImON: Capacities shown In table may exceed the maximum opacity for a sleeted regulatar. Table N-SA Elevated Pressure 2 psig Maximum Capacity of OmegaFlex TracPipe CSST in Cubic Feet per Hour(CFH)of Natural Gas(1000 BTU per cubic foot approx) Gas Pressure: 2 . psig Pressure Drop: 1.5 psi (Based on a 0.60 Specific Gravity Gas) 1110111001111111 Tubing Length(feet) 1 15 20 25 30 4 0 50 60 70 75 81 •I 100 125 150 200 250 300 +04 500 600 700 800 • 0 1000 1100 1200 1300 1400 1500 • 3/8" 15 495 438 354 305 271 24 189 171 158 153 148 139 131 117 106 91 81 74 64 57 53 49 46 43 41 40 38 37 35 34 1/2" 19 1174 855 690 600 542 49 _� 385, 353' 327 317 307 290 275 247 126 197 177 162' 141 126 116 107;t:101 95 90`. ;86 83, 79 77 74. ij 3/4" 25 2960 2112 1734 1507 1352 12 1W5( 965 883 819 792 767 724 688 617 565 491 440 403 350 .314 287 267 250 236 224 214 205 197 190 184 337 325 314 1'. 31 5148 3687 3004 2609 2339 213 1665 1522 1412 1365 1322 1248 1.185 1062 971 843.,756 691 600' S38 492 4% ,427 403' 383; 365 350• IU4' 39 9725 6919 5670 4923 4412 40 . 35 3139 2870 2661 2572 2492 2352 2233 2001 1830 1589 1424 1302 1130 1013 926 858 804 759 720 688 659 633 611 590 11/' 46 16725 11782 9599 8300 7415. 6 584 5223 4763 4406 4255' 4119 3881 3679 3287 2997 2592 2315 2111 1826 1631 1487 1376 :1286 1212 1149 7095 1048 1006 '969 936`: P' 62 P7374 26473 21637 18751 6781.15 11886 10855 10054 9715 1940818872 8419 7534 6881 15963 5337 4874 4224 3780 3452 3197 2992 2821 2677 2553 2445 2350 2265 2188 Notes:Tables above include lossesfor four 9D•degree bends and two en in ubing runs with larger numbers of bends and/or fittings shall be increased by the equivalent length of tubing to the following equation: L=13n where Lis the additional length of tubing and n is the number of i - fittings and/or bends.Table does not include effect of pressure drop across the line regulator.If regulator loss exceeds 1/4 PSI(basedone inch outlet pressure) Do notuse this chart pressure drop acrassa regulator will vary with flown OREG3 has 1/4 PSI pressure drop at a flow of 145 cubic feet per hour.CAUTION: Capacitlesshown in table mayexceed the maximum opacity fora selected regulator.