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5707 Spruce LP table
Maximurn Capacity of PE Pipe in Thousands of BTU per Hour of Liquefied Petroleum Got wail, a Ccs Pr lire of 11.0 in. WC and a Pressufe Drop of 0.5 in, WC (bated on a 1.62 5pec*c grovilV gm) 187 125 99 64 74 67 56 50 45 41 38 Sri 33 29 26 :073 720 671 484 425 383 325 286 257 235 218 204 192 169 152 391 934 740 627 551 497 421 370 &M 3135 2$.3 264 244 210 197 :983 1331 1054 893 756 7x..08 6W 528 475 435 4f33 376 354 311 280 3W 2391 1894 1605 1412 1772 1078 948 1354 761 723 676 &36 5W 504 4724 32247 266 22232 1976 1742 3563+1 1359 1232 1133 1054 9e9 9u 828 7501 1303 6756 5351 4535 3989 3592 9M4 267,8 2411 2207 2044 19110 1797 1581 1424 Z2 2G T8 15 13 1 10 9 9 B 471 8 7 7 129 113 102 86 76 68 753 58 54 51 48 46 Oil 42 40 T 167 132 112 99 89 81 75 70 66 63 60 57 54 52 2v c 2019 1188 160 140 121 116 107 1 CO 44 89 96 81 78 78 427 376 338 287 252 227 206 192 T80 169 160 152 144. 140 1.34 642 W 516 441 341 354 325 30.3 2865 269 255 244 233 224 214 1297 1061 956 010 712 642 587 544 X48 478 453 43' 411 344 379 T0417 901 9D92 8,589 7612 in Thousontjs of BTU per Hour of Liquefied 105963 7T 131 56330 2516BROhs 1 CFH 3788 xir'r'furr :'apxacW €5f IE € ipe in Thouscrids of BTU per Hour of Liquefied R+eftaeum Gas =`44 25388 23234 21517 201106 with 0 6x711 F°re ure of 2.0 psi and a Pressure Drop of 1.0 psi i (t,� an a 1.52 s4ecrhe gaa.f y gas) on a 1.52 specMc grtrAV gcM) 25T6BTU4--1CiiIkj., IV456 1319 1045 1186 779 126 1T5 106 999 749 X23 471 431 509 - 1192 =>74 2719 113M 7586 60M 5[342 4479 403.3 -418 31)137 2707 2476 2296 2144 2Oi43 '75 1599 I 62 9835 774(} 66M X477 5229 44.32 3898 3510 3213 2475 2780 2€517 786 2073 24877 1401.4 111100 4.408 4275 7451 6318 55M 50M 4678 4239 3962 3729 3280 24'53 3761+4 25383 19946 16905 14869 13389 11358 4982 SW 8726 7618 7119 6700 5894 SW7 43429' 29M 23969 20515 18162 164714 14100 12446 I1:322 T0417 901 9D92 8,589 7612 in Thousontjs of BTU per Hour of Liquefied 105963 7T 131 56330 47750 470M 3788 with a Gas Pxessure of 10.01 psi and a Nessure Drop of 1.10 psi =`44 25388 23234 21517 201106 18926 16647 i 236 2D7 187 158 139 126 1T5 106 999 749 84 80 7. 74% 34661 1192 1073 910 WO 720 659 6111 •57T .s] 578 484 467 443 425 1757 15+45 1;391 117x? 1037 934 856 742 740 696 659 61=27 599 574 5..51 2503 2702 19+83 1680 147'8 1331 1218 1126 11 942 939 893 853 618 786 X98 3456 3,563 3014 21556 2391 21 E9 2627 1894 1783 1688 16015 1: 3 1469 1412 5 5232 474{7 41357 3596 3258 2q97 2788 .2616 2471 2347 2239 2144 2(7fd.1 1486 12735 11176 1 GG63 8514 7,9M 675;4 6782 5725 53513 _FC36 4767 46M 4331 4150 3WF 20,762 25484 72591 2M69 17514 15627 14068 12M 2516BTUh=1( 1fH 106171 h+loxil'r`rum Cap+7city of RE Pipe in Thousontjs of BTU per Hour of Liquefied Petroleum Gas (17601 70967 €1148 52905 47W with a Gas Pxessure of 10.01 psi and a Nessure Drop of 1.10 psi 35,514 31980 29267 271 N 25324 23M 2CO70 18&72 (t,� an a 1.52 s4ecrhe gaa.f y gas) 1416 1662 13 Tb 1116 981 16$ 749 659 593 543 503 4717 442 M9 ;156 14234 9555 7568 6414 -%42 907 6 3787 3410 317E 2eW 2701 2542 2236 2014 184% 32.3M6 9012 8316 7315 6587 56W 4910 4422 40417 3747 3507 3296 2849 2611 76246 77652 13% ! 1860 10723 9365 7954 6997 6300 5766 5340 499(1 4697 4131 372fl 47252 31720 25123 21243 18729 16865 14244. 12,72 11321 1[1361 9W 867 8440 78,'23 6685 53960 37387 20,762 25484 72591 2M69 17514 15627 14068 12M 1204, 11297 106171 9458 8569 1334761 (17601 70967 €1148 52905 47W .413.376 35,514 31980 29267 271 N 25324 23M 2CO70 18&72 Ph: 1.800.662.D208 + FOX- 615.326.9407 * Weo' www.ggSi,te.COM � :%61 235 140 16$ 144 134 125 119 ill 106 1131 97 57;3 i1+ 1501 1352 1 907 RP 719 676 641 409 582 557 536 I W6 1753 14- 1176 1077 997 932 877 &30 790 75.4 723 i 53 2773 241W 2136 1 ' 576 1' ?:4 1421 1328 1254 1 183 1125 7075 16361 990 ''565 4483 4487 SaW 3.345 3012 2757 2553 2.386 22416 2126 T(771 1851 1779 33+4 6600 5$4L'I W4? 4468 4048 3724 U65 3251 7071 2916 2782 2564 25W 2466 -Oa4 14977 12676 101743 94451 8-x;19 7787 7212 67:9 636&3 6W5 5712 5+455 5227 51124 25T6BTU4--1CiiIkj., Ph: 1.800.662.D208 + FOX- 615.326.9407 * Weo' www.ggSi,te.COM �