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Home My WebLink AboutDRAWING7003 S -Tw zo z -2- ap<- U� RECEIVED J U N 13 2018 _... _ - ST..kucie Gbunty,•Petmkting -✓v /��/ �� U 5•L i '' - .r' ' IL Ll cr } , . •.� .,._ � _ ( '� � ' Ate' - `� " _ ' •i �.s.__....: w_:__-.:....t_:..Y.—.::.:-...:.....sue - -�-�—_i__..._...___:.--..�:__........:_! ..._..,_._•_•______i �r A ft: 7003 /07)r Z6� RECEIVED J U N 13 2018 ... ...... ... ST.tijcie Cou0y.j Permitting "u < . . . ............... Zoe, q/ _/Otl Mpe/W I sr. Ar < 4�1 1 X. Ab� . . . ........... BOARD OF COUNTY COMMISSIONERS TANK SIZE [A1] GAS PIPING SCHEMATIC [A3] TANK SIZE:., V GALS. APPLICANCE — TYPE/SIZE /'I r'lwrl [A4] [L8] L11 I., I I[L10] [AS] l�S BTU 'BTU BTU BTU BTU BTU PLANNING & DEVELOPMENT SERVICES DEPARTMENT Building and Code Regulation Division [A6] LRECEIVE-D-- [1.12] 3 ?F;rs: ,t._ .�,rr•`, `_'_I PIPINGLENGTH ENGTH & SIZE (PIPE SIZE WAS TAKEN FROM L1 FT. INCH DIA. THE 2014 {1 �VJFBC FUEL GAS CODE — L2 FT. INCH DIA. TABLE 402) 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. L11 FT. INCH DIA. L12 FT. INCH DIA. Website: www.stluoieco.00v 2300 Virginia Avenue - Fort Pierce, FL. 34982-5652 Phone ;(772) 462-1553 FAX (772) 462A 578 Revised 7/22/14 GAS PIPING INSTALLATIONS Gas Undiluted Propane TABLE 402.4(29) Inlet Pressure 10.0 psi SEMIRIGID COPPER TUBING Pressure Drop 1.0 psi Specific Gravity 1.50 INTENDED USE Sizing between first stage (high-pressure regulator) and second stage (low-pressure regulator). TUBE SIZE (in.) Nominal ACR '/ g 1, '/ 9 '1 A '/9 1'I , 1'/ 3 - - Outside 0.375 0.500 0.625 0.750 0.875 1.125 1.375 1.625 2.125 Inside 0.305 0.402 0527 0.652 0.745 0.995 1.245 1.481 1.959 Length (it) Capacity in Thousands of Btu per Hour 10 513 1,060 2,150 3,760 5,330 11,400 20,500 32,300 67,400 20 352 727 1,430 2,580 3,670 7,830 14,100 22,200 46,300 30 283 584 1,190 7,080 2,940 6.290 11,300 17.900 37,200 40 242 500 1.020 1,780 2,520 5,380 9,690 15,300 31,800 50 215 443 901 1,570 2,230 4,770 8,590 13,500 28.200 60 194 401 816 1,430 2,020 4,3220 7,780 12,300 25,600 70 179 369 751 1,310 1,860 3,980 7,160 11.300 23,500 80 166 343 699 1,220 1,730 3.700 6,660 10.500 21,900 90 156 322 655 1,150 1,630 3,470 6,250 9,850 20,500 100 147 304 619 1,080 1,540 3,280 5,900 9,310 19,400 125 131 270 549 959 1,360 2,910 5,230 8,250 17,200 150 113 1 244 497 869 1,230 1 2,630 4,740 7,470 15,600 175 109 1 225 457 799 1,130 1 2,420 4360 6,880 14,300 200 101 209 426 744 1,060 2,250 4,060 6,400 13,300 250 90 185 377 659 935 2,000 3.600 3,670 11,800 300 81 168 342 1 597 847 1,810 3,260 5,140 10,700 350 75 l55 314 549 779 1,660 3,000 4,730 9,840 400 70 144 292 511 725 1,550 2,790 4,400 9,160 450 65 135 274 480 680 1,450 2,620 4,130 8,590 500 62 127 259 453 643 1,370 2,470 3,900 8,120 550 59 121 246 430 610 1,300 2,350 3,700 7,710 600 56 115 235 410 532 1,240 2,240 3,530 7,350 650 54 111 225 393 558 1,190 2,140 3,380 7,040 700 51 106 216 378 536 1,140 2,060 3.250 6,770 750 50 102 208 364 516 1,100 1,980 3,130 6,520 300 43 99 201 351 499 1,060 1,920 3,020 6,290 850 46 96 195 340 482 1,030 1,850 2.920 6,090 900 45 93 189 330 468 1,000 1,800 2,940 5,910 950 44 90 183 320 454 970 1,750 2.750 5,730 1,000 42 88 178 311 442 944 1,700 2,680 5,580 1,100 40 83 169 296 420 896 1,610 2,540 5,300 1,200 38 79 161 282 400 855 1,540 2,430 5,050 1,300 37 76 155 270 383 819 1,470 2,320 4,840 1,400 35 73 148 260 368 787 1,420 2,230 4,650 1,500 34 1 70 143 250 355 758 1,360 2,150 4,, 1,600 33 1 68 138 241 343 732 1,320 2.080 4,330 1,700 32 66 134 234 331 708 1,270 2,010 4,190 1,800 31 64 130 227 321 687 1,240 1,930 4,060 1,900 30 63 126 1 220 312 667 1,200 1,890 1 3,940 2,000 29 60 122 214 304 648 1,170 1,840 1 3,830 For SI: 1 inch = 25.4 mm, 1 foot = 304.8 mm, 1 pound per square inch = 6,895 kPa, 1-inch water column = 0.24M KFa, I British thermal unit per hoar = 0.2931 W, 1 cubic foot per hour = 0.0283 m'/h, 1 degree = 0.01745 rad. Notes: 1. Table capacities are based on Type K copper tubing inside diameter (shown), which has the smallest inside diameter of the copper tubing products. 2. All table entries have been rounded to three significant digits. RECEIVED JUN 13 2018 FLORIDA BUILDING CODE - FUEL GAS, 5th EDITION (2014) 4.30 ST. Lucie County Permitting PIPE AND TUBING SIZING TABLES 58-97 ble 15.1(o) Polyethylene Plastic Pipe Sizing Between First -Stage and Second -Stage gulators: Nominal Outside Diameter OPS) Gas: Undiluted Propane Enlet Pressure: 10.0 psi Pressure Drop: 1.0 psi Specific Gravity: 1.52 astir Pipe '/2 in. 3/4 in. 1 in. 11/4 in. V/2 in. 2 in. Length SD18 9.33 SID1811.0 S1DR 11.00 SDR 10.00 SYDR 11.00 SDR 11.00 (it) (0.660) (0.860) (1.077) (1.328) (1.554) (1.943) 30 2143 4292 7744 13416 20260 36402 40 1835 3673 6628 11482 17340 31155 50 1626 3256 5874 10176 15368 27612 60 1473 2950 5322 9220 13924 25019 70 1355 2714 4896 8483 12810 23017 80 1261 2525 4555 7891 11918 21413 90 1183 2369 4274 7404 11182 20091 100 1117 2238 4037 6994 10562 18978 125 990 1983 3578 6199 9361 16820 150 897 1797 3242 5616 8482 15240 175 826 1653 2983 5167 7803 14020 200 778 1539 2775 4807 7259 13043 225 721 1443 2603 4510 6811 12238 250 681 1363 2459 4260 6434 11560 275 646 1294 2336 4046 6111 10979 300 617 1235 2228 3860 5830 10474 350 567 1136 2050 3551 5363 9636 400 528 1057 1907 3304 4989 8965 450 495 992 1789 3100 4681 8411 500 468 937 1690 2928 4422 7945 600 424 849 1531 2653 4007 7199 700 390 781 1409 2441 3686 6623 x 800 363 726 1311 2271 3429 6161 ' 900 340 682 1230 2131 3217 5781 1000 322 644 1162 2012 3039 5461 1500 258 517 933 1616 2441 4385 2000 221 443 798 1383 2089 3753 �S: Iron pipe size. SDP- Standard dimension ratio. votes: �l) Capacities are in 1000 Btu/hr. j2) Dimensions in parentheses are inside diameter. 2014 Edition I PIPE AND TUBING SIZING TABLES - 58-89 blg 15.1(d) Pipe Sizing Between First -Stage and Second -Stage Regulators: Nominal Pipe ;e, Schedule 80 Gas: Undiluted Propane Inlet Pressure: 10.0 psi Pressure Drop- 1.0 psi Specific Gravid. 1,52 Pipe Length 1/2 in. 3/4 in. 1 in, 11/4 in. 11/2 in, 2 in. 3 in. 31/2 in. 4 in. (gt) 0.546 0.742 0.957 1.278 1.5 1.939 2.9 3.364 3.826 30 1309 2927 5706 12185 18548 36368 104539 154295 216246 40 1121 2505 4884 1.0429 15875 31127 89472 132057 185079 50 993 2221 4328 9243 14069 27587 79297 117039 164032 60 900 2012 3922 8375 12748 24996 71849 106046 148625 70 828 1851 3608 7705 11728 22996 66100 97561 136733 80 770 1722 3357 7168 10911 21393 61494 90762 127204 90 723 1616 3149 6725 10237 20073 57697 85159 119351 s 100 683 1526 2975 6353 9670 18960 54501 80440 112738 150 548 1226 2389 5105 7765 15236 43766 64596 90539 f 200 469 1049 2045 4366 6646 13031 37458 55286 77484 c 250 416 930 1812 3870 5890 11549 33198 48999 68673 e 300 377 842 1642 3506 5337 10465 30080 44397 62223 350 347 775 1511 3226 4910 9627 27673 40844 57244 400 322 721 1405 3001 4568 8956 25745 37998 53255 450 303 676 1318 2816 4286 8403 24155 35652 49967 V. 500 286 639 1245 2660 4048 7938 22817 33677 47199 t 600 259 579 1128 2410 3668 7192 20674 30514 42765 . 700 238 533 1038 2217 3375 6617 19020 28072 39344 t 800 222 495 966 2062 3139 6156 17694 26116 36602 ' 900 208 465 906 1935 2946 5776 16602 24504 34342 f 1000 196 439 856 1828 2782 5456 15682 23146 32439 fr`1500 158 353 687 1468 2234 4381 12593 18587 26050 2000 135 302 588 1256 1912 3750 10778 15908 22295 dotes: jl) Capacities are in 1000 Btu/hr. 0f To convert to capacities at a gauge pressure of 5 psi setting with 10 percent (0.5 psig) pressure drop, uldply values by 0.606. To convert to capacities at a gauge pressure of 15 psi with 10 percent (1.5 psig) O) sure drop, multiply values by 1.380. 2014 Edition �,W A rwomm0, 8 a, m "MmMrto R k '"117 M4 cl, m cKi llt� cl� m m L- G11 %z V�z 4 C6 co C6 .6 G4 04 G4 Go C-4 an m C14 a, MCD to m 00 to m I- v 00 00 OD 00 M C. m CD 0) V� CD " 00 C) U) 1� d4 cc) ko X0 cl co ID 00 10 �c Ll E- LO g CD (D 00 M M cf) 14 V r� ko 00 00 a Vi C� 4 k C=� Lr! - 5! 0c) Ci c7i Cli 0) r"i Vi C� oc� �i m cn oo GNL C� ol� 00 cl L- L"% IR tR ,d4 cn :� M. OD n cl C� Ci xn cn V m CO kR CI In (n OD r- to to m v -IV co m .0 m m C11 cq .... I 04 - - — - — — — — — et C04 'm )o 00 Lo 10 m m cn, c (D 00 X' M .0 m t- L- 00 C) 0) 00 CO 10 =5 m V. C4 m 00 tO (3) CC) C4 V 10 " M 4 10 a, -n 10 CO I- Ct ra-I 1.00 ral)0 10 LV 10 C*l " CO'o cl, 10 C�l .0 OPP !� 1. 'mo OD Lq n l3i C Vi oc� OCL n R Lq Ci 0) to -1 -1 cc! CR �a LL� -1 -1 ol -� -1 ;i CD CD C> 0) chi m r. P. 10 M LO m -q� v M .0 .0 Cf I Cf C4 - - - — — — - — — — — — — — — ti — — — — — I r- 0000 tt-- IMO tD IMO to- 10 10 1� to ;8 'MI to m v 0)'r w r, m v .1, C) 00 .0 a)- cq GV In 10 n cl� Ci " V' CL lc� It CN� C� "V CV Q OD I - UD M M �n S' - G-4 M 0 toG'l -i I-i C=� C� oo �o " M S� 8 M 0) (M 00 .0 0) to CD 00 r- t, r- 00 M M CD 'D 'D to to m m m m G4 C4 C'I — -V�Crin — — - - — . — — — — — 0 O Cl L- 00 v 11 Cq A 0, 0 m m M LO C4 Go 00 r, 00 C4 CD b F, 10 .0 ID M I- t, cl v to m C, MrC4 " C� L- Lo m MC4 C't LO m to -M on CD 10 CC) CD rto M CD 0) m m r rto Go tD to LO uo >o cn 00 �o m m v v v -q� :;; M k- d. co D .0 LO co Cl) m cq en CC) o to C6 t6 cF cF cF .5i A C, 00 0) IN 10 an LD �b " on Go C4 C, 00 to cn mm M to 00 C) m m co -,v SO Cl "r on to C) m" m en 0) to v CD C. w .0 m m Of C4 v �! 0) mv co 'd, to mm CD ;! i� m C� rl� Iq C'l G'j li cli I-i C� m 00 r r- to LO xn v v w " o m m mv -14 v co m co m cli CD comMMm m rb m" C4 " cq GN CNI 11) " C) C4 a, t- 00 UD v .0 oo C4 00 lt+ v 00 W C. -IV -Q� t- Cl 00 'Ir - m g p B to 00 LO "r m 00 M m 04 g M t- O .0 t- "r m m 00 to C4 O IN 0) m r'D 'o m M m 'd. n co co C4 CV C4 CI O Of ODD r-- �m 10 V- Mr-� aq CK? M GN V 00 r .44 m " :$ ai (D OD 0) M to C) 00 r- 0) 00 to cn m �4 m .44 cn to " m to co m 00 m m M L- to -.1, m to m m m m m C11 C4 Cl C) 0) cn cn 00 00 00 OD t- 10 10 a m -0 to m Gov 'In �! IMD :� 00, 00 1"- ,; 00 m to c. C� w al to .0 m C, t- 'D 0 g 00 �o -W 'n 0 ctI m 00 r� r- 'D v m C4 C4 — —M m m v q, on a) n m m " Cq " Gm G4 00 CD 0 0 CD m 0 0 0 CD 0 = 1- 00 C� 2 m 0 m CD 0 G CD C> CD C) CD• 0 o o CD o CD CD C� c, m CD �o (CIE'll 8 CS, 18 C, C� oCD bn C4 m co v �o .0 QD Im 00 00 C) m 0 �Sn VICE, L'., 'o L, 00 0) CD 4taL I - - - 1 AidTSI Z223.1-39 PIPE SIZING 54-39 Table 6.2 (P) Corrugated Stainless Steel 'Tubing (CSST) lGas:Natural Inlet Presthan 2 psi Pressure D. w.c.Specific Gr � r ,�.� t`s'� x -fir �r �� ?,.� IIVTENDEDUSiE,TmhaLSuPP1YPressureo x � u► wc.or rea r r� M_», �� x ?_., M1 �� V Tube Size (EHD) Flow Designation: 13 15 18 19 23 25 30 31 37 46 48F60 62 Length (ft) Capacity in Cubic Feet of Gas per Hour 5 120 160 277 327 529 649 1,180 1,370 2,140 4,430 5,010 8,800 10,100 10 83 112 197 231 380 462 828 958 1,530 3,200 3,560 6,270 7,160 15 67 90 161 189 313 379 673 778 1,250 2,540 2,910 5,140 5,850 20 57 78 140 164 273 329 580 672 1,090 2,200 2,530 4,460 5,070 25 51 69 125 147 245 295 518 599 978 1,960 2,270 4,000 4,540 30 46 63 115 134 225 270 471 546 895 1,790 2,070 3,660 4,140 40 39 54 100 116 196 234 407 471 778 1,550 1,800 3,180 3,590 50 35 48 89 104 176 210 363 421 698 1,380 1,610 2,850 3,210 60 2 44 82 95 161 192 330 383 639 1,260 1,470 2,600 2,930 70 41 76 88 150 178 306 355 593 1,170 1,360 2,420 2,720 80 126 38 71 82 141 167 285 331 555 1,090 1,280 2,260 2,540 90 36 67 77 133 157 268 311 524 1,030 1,200 2,140 2,400 100 4 34 63 73 126 149 254 295 498 974 1,140 2,030 2,280 150 150 19 27 52 60 104 122 206 240 409 793 936 1,660 1,860 200 17 23 45 52 91 106 178 207 355 686 812 1,440 1,610 250 15 21 40 46 82 95 159 184 319 613 728 1,290 1,440 300 13 19 37 42 75 87 144 168 234 559 665 1,180 1,320 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 L is 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. 2012 Edition f Maximum Capacitiy of WARD FLEX@/WAR D FLEX@ II CSST in Thousands of BTU (KBTU) for Propane Gas (LPG) Table A-18 Gas Pressure of: 0.5 psi or Less Pressure Drop of: 3.0 , inches W.C. /ti—H Igo r Size 16A , 15A ','.20A `.; 25A 32A; 38A 50A 3/8" • 1/2"1,1=1/4"'` 1-1/2" ..• 2;. -' EHD 15`. 19 25.. ,! 30 ;37,x qg 5 253 517 ;ts 1026 1868 '3270 7926 14690 10 177 365 •.`' 73QI 1309 r 2342; 5632 y' 1059E 15 142 299 599' 1064 1927 4611 20 123 259 520' 917 °' 1678_ 4001 25 109' 232 466 819 507 3585 30 10Q 212 : 'f427 745 `:a1380 3277 ;631,2 40 ..855 183 • '643 ; ,� ,Vr O1" 2844 5512 50 76 164 332 5741 307,9 2547 60 70' 150 ;? 304 522 <<_' 98$ 2328"4553 70 �5 :65 139 ' , '24f' 482 k 917 2158 ;` 4233 80 6,0. 130 ,°; 264 45186Q 2020 3976 90 .'67 122 .;248 424 ez'•,8i-2 1906 ;:,; 37,61; ii 100 ; 54 115 �'- v2a6 402 ; `°+.Z73 1810 '`• 7 3579 -E 125 '., 47. 104 .` -, -212 357 °=.-' 693' 1620 3222 m 150 ; 43 95 1 193 326 '' 635' 1481 -� 200 ',.36 82 '.,.168, 281 1 :,'558 1285 • 2581' . .6 250 ' 33 73 " ; 150 251 `' ,497 1152 ,.2324 H 300 30 66 ',, 138 228 , :455 1053 ., � 2131 400 25: 58 1,1.> u120 196 500 22 52 ,'t t107 175 , ; ;355 819 ` 1676 600 21 47 98; 160 ;325 748:'.;` 1,536 700 19 44 147 „ .'302 692 800 it 41 1.' 85' 138 ;;;-283 648,7 1342 900 ;16 38 81° 130,,_ 268' 612 1000.,F16 36 ` r '-76 123 254' 582 `' 1208 1100 14 35117 243 555 '#k1156 1200 14` 33 112 ,, 233' 5311,,; F11g8 1300 r14', 32 66 107 ,'•,; 224 511 :, 1400 13 30 ' ;65 103 ;'' 216 492 ,106Z . vu 1031` 150013 30 '62 100 : 209 476 Table includes losses for four 90 degree bends and 2 end fittings. To compute flow capacity for tubing runs with a larger number of bends and/or fittings, add the appropriate number of feet to the actual run length using the following formula: L =1.3 (n) L = Numbers of feet to be added to actual run length. n = Number of bends and/or fittings over six ss «,wRnr--Lc"' nuunnnnnnnnnnnnuuuunmm�mmnnmm�numuunnnnunn