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HomeMy WebLinkAboutPROPANE TANK PAPERWORKHills THIS VESSEL IS OF LIOUEFII E-x I E 11 of TOP VIEW THESTORAGE GAS ONLY d w' J SIDE ELEVATION NOTE: TANK MUST BE INSTALLED LEVEL, WITH ALL LEGS IN SAME PLANE TO ASSURE EVEN DISTRIBUTION OF LOADAND OPTIMIZE ACCURACY OF GAUGE DEVICE FI TING6 MARK I Ctt. I SIZE ttPE ____ SERVICE QTY. Ul. LUGIrlk/Tnrpp�- FITTING LAYOUT SEE D-01 FOR ANY UNSPECIFIED WELD DETAILS DE6CRInION OPTIONAL )ME BRACKET FOR UG GREEN ONLY LONG. WELD SEAM .-..y long seam END VIEW loc. to TIES leg weld PART NUMBER: 0102502X DWG. NO. REV. BY: DESCRIPTION DATE; ;ERTIFIED BY: QUALITY STEEL CORPORATION aEYEuva Ms • RiDPNlO ax-vrEsr,IwDal ur MAXALLV.Y.NRKIR 250 PSI Ar 400 •F. m"I, -F. AT 250 1 P61 `�Y vnpnnn 0.nSIDa DG. SHMM 1. LIFTING LUGS OESINGED FOR TOTAL LIFTING WEIGHT OF 8000.. 2. TOTAL EMPTY WEIGHTIS 480M 3. ALL DIMENSIONSARE IN INCHES UNLESS OTHERWISE SPECIFIED 4. COMPLETETANKDRIEDTOREMOVEALLMOIMRE S. EXTERIOROFTANKTOBEGRITBLASTED 6. PAINT PER SHOP ORDER T. VACUUM PURGE TANK 8. DIMENSION ARE SUBJECT TO CHANGEW4THOUT NOTICE. (NON -PRESSURE RETAINING COMPONENTS ONLY) S. THREADS OF ALL FITTINGS TO BE OCATED WITH COMPOUND SUITABLE FOR USE NTH LP GAS 10. FLOAT GAUGE TO BE INSTALLED WITH FLOAT ARM 45' OFF LONGITUDINAL CENTERLINE OF TANK REGULATOREMCKET I E1 I z; I RaotTlimLIEFVALVE 01f14113 QUALITY STEEL CORPORATION DIPTUEELENGTH=&V'FOR6Q%ol 2i I pM I UPDATECOMPANYANDDATAPLATE 01,1144 HINOEANDRAWORDOMEBMOKST9 16f0O, D18,1 PR ple CHANOEFITTIND LOCATION OetlOtl9 YPD4imt]1ELLMWYWE99pN0.MfiPUTE. ANODEATTPCHMENT p-t)y p4 M'J smzE04ss MAmocp)mom Dip4f18 uP reounavAcmaioep• 01/03/00 WRAC fr TWV M.0 7A a V-Y STANDARD AGOG 250 GROLM Lift °GAL / ; IW TAW��%r p Kso l a Z !\/I'ox go ftyiV. ®w � � rsu GAL-. � f Nominal Ualseale D)ameteerr. � Detwecn Fa'atSiage and Serond Sege 0 PLO& Pipe (2io. mi 0 7I9R(8ft) SDR 9.33 SDR 11.0 (0.660) (0,860) 30 ' 2143 4292 40 1835 3673 50 1626 B256 60 1413 - 2950 70 1355 2714 1 aq 90 `; 125 150 , { 175 200 x.;. 225 250 275 '. 300 350 .r 400 550000 ' 600 700 u. goo G' 900 1000 1-hL SDR I1.00 7744 6628 5874 5322 4896 Gm Min. SDR 10.00 MUM 13416 11482 10176 9220 .803 Min., SDR 11A0 (1,554) 20260 17340 15368 13924 ' 12810 1261 2525 4555 7891 1183 2369 17 11918 1117 y238 990 4274 6994 11182 10562 897 179y 3578 3242 6199 5616 g� 8482 826 778 721 681 646 617 567 528 495 468 424 390 363 340 322 2fibSD.00 (1.943) 36402 31155 27612 25619 23017 • 21413 20091 18978 16820 15240 1653 1539 2775 5167 7803 14020 1443 2603 4807 4510 7259 13043 2459 4260 6811 6434 12238 1294 2336 4046 6111 11560 10979 1235 i�IJS6 2228 2050 3860 5830 10474 1057 1907 3551 3304 5363 4989 9636 992 9 1789 100 8 1690 23928 �2 1; 7945 849 781 1531 1409 2653 4007 7199 726 1311 2271 2271 3689 6623 64 �4 1230 2131 3217 6161 5781 1162 2012 3039 5461 150000 258 221 517 933 1616 443 798 2441 4385 1383 2089 3753 IpS_ Imn pipe eve.WIL. Standard dimension ratio Notes . .7 (1) C padtim are in 1000 Bm/hr. (2) Dtmendons m parentheses are inside diameter. .. L .4 G"u M �oM E S Co�TRhT�� O-AEOWAJ EA*w 'R. 0 kk 2014 Emllon WIF 'ANSI Z223.1-53 PIPE SIZING Table 6.3 (h) Corrugated Stainless Steel Tubing (CSST) :]�W-OkOR C?as L�E -ro rj"?Ac 54-53 Gas: Undiluted Propane Ides Pressure: 11.0 in. w.c. Pressure Drop: 0.5 in. w.c. Specific Gravity: 1.50 [. �t ''INTENDED:USE.(SSY'S .. .Between_S o-or irondS Premue)t, for and ]indCe ShutaffValve fa!'6..- .� tam, (Im'- ,Regina . APP.... . 11 Tube Size (EIID) Mass Designation: 13 15 IB 19 1 23 Y5 30 31 37 39 46 96 60 6Y Length (it) Capacity in thousands of But per Hour 5 72 99 181 211 355 426 7411425 863 1,420 1,638 2,830 3,270 5,780 6,550 10 50 69 129 150 254 303 521605 971 1,179 1,990 2,320 4,110 4,640 15 39 55 104 121 208 248 422490 775 972 1,620 1,900 3,370 3,790 20 34 49 91 106 183 216 365 661 847 1.400 1,650 2,930 3,290 25 30 42 82 94 164 192 525 379 583 762 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 40 23 33 64 74 131 153 256 297 449 610 988 1,170 2,090 2,330 50 20 30 58 66 118 137 227 265 397 548 894 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 99 117 191 222 330 466 745 890 1,590 1,760 80 15 23 45 52 94 109 178 208 307 438 696 833 1,490 1,650 90 15 22 44 50 90 102 169 197 286 414 656 787 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 75 123 143 217 324 506 611 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 57 90 107 147 234 357 434 777 854 EEiD: Equivalent hyyddraulic diameter. A measure of the relative hydraulic efciency between different tubing sixes. The greater the value ofEHD, the greater the gas capacity of the tubing. Notes: (1) Table includes losses for four 90 degree bends and rwo end fittings. Tubing runs with larger numbers of bends and/or fittings shag 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. HomEo(jjqE1 e A<cLE,uz co�AC: ID�R CGA S> . Co,�,pANE 1 2015 Edition