No preview available
HomeMy WebLinkAboutPROPANE TANK PAPERWORK_.ST. LUCIE COUNTY BUILDING DIVISION REVIEWED FOR CO REVIEWED BY IANCE DATE _ PLANS AND PERMIT MUST BE KEPT ON J013 OR NO INSPECTION WILL BE MADE. fa - 0 Z 1/8" GALV. CABLE W/ (2)HDG CLAMPS TO ANCHOR (PULLED TIGHT) — _ J` RECEIVED 0 C 1 0 9 2018 Y, uuve County, Permitting �9- 'E_ copy. 118 GALLON LP GAS TANK (3) BX16X3" CMU BLOCK, HELICAL ANCHORS 5/8"X40" SINGLE 6 HELIX HELICAL ANCHOR NOTE: 1 PAIR 700#/ANCHOR 118 GALLON MAX ABOVEGROUND HOLD DOWN DETAIL PROVIDE (2) 118 GALLON TANKS 1701 mtaeY all Avenue i y ll veto Beach, Florida32960 GENERAL NOTES: 1. ANCHORS SHALL BE INSTALLED PER ANCHOR MANUFACTURER TO ACHIEVE STATED LOAD CAPACITY. CAPACITY VARIES WITH SOIL TYPE. VERIFY ANCHOR CAPACITY WITH SOIL TYPE �r''j1e11sej, - ENCOUNTERED. � ! ®� 2. CHECK FOR UNDERGROUND UTILITIES PRIOR TO ANCHOR INSTALLATION S,,��o°e°o� FqR°A°®p 3. LOCATION OF TANK RELATIVE TO ADJACENT STRUCTURES AND FEATURES IS DEPENDENT UPON E N Soo �� s LOCAL CODES AND IS THE `RESPONSIBILITY OF OTHERS, ° ®o�Q 4. THE TANK AS SHOWN. HAS BEEN DESIGNED TO PREVENT FLOTATION, COLLAPSE, OR LATERAL o MOVEMENT DURING THE BASE FLOOD EVENT. No 40111 °®. 5. 4" ANCHORS SHALL BE LOAD TESTED AFTER .INSTALLATION 6. WIND LOAD DESIGN CRITERIA �a ow m 160 MPH; EXPOSURE "GCpi N/A; Cf = 0.6 ° W m D'; - 0° STATE OF m o Oa o �o i ® AA °° F e o © COPYRIGHT 2018 - FARLEY ENGINEERING, LLC F ° < o R r oll� COMO OIL AND PROPANE FARLEY ENGINEERING LLC I "IfmSll Consulting Engineer #40111 - CA28108 r 52 9/16" R3/4" TYP. 4 PLCS. . z 0 0 0 a 0 1 W. 1 23 1/8" LU c O;D ` 1! �I 11.0". I OUTAGE 30" O.D. 39 2.11/16 X 4.5/8 D1 R4 1/4" "DIAMOND" OPENING R3 7/8" TYP. 2 PLCS. M1 457 1" TYP: 22' 15 11/16" 13' - - O.D. 1 I / R5 3/16 3:1 /4' X B" OPENING 1 2' 1 A SG CPLNG. 45 5/8" NOTES: 1. INSIDE OF THE TANK TO BE CLEAN, DRY & FREE OF RUST, SLAG & OTHER FOREIGN PARTICULATE MATTER. 2. FOR NON -CORROSIVE SERVICE. 3. SLEEVE & PROTECTIVE COVER (FOR TOP OF . GUARD) TO BE PUT ON TANK AFTER PRODUCTION. 4. ATTACH NAMEPLATE TO GUARD WITH SEAL WELD. 6. INSTALL SIGHT GAUGE DIAL AS SHOWN IN DETAIL A. 7. SEE DT DETAIL FOR CORRECT LENGTH OF DIP TUBE. S T 0 R DP DW E1 CF DP I DW DW DW C1042 A C1043 D C1046 D C1045 A Como Oil and Propane 1701 Commerce Avenue Vera Beach, FL 329GO 6 A 1 RECEIVED . PREFERED FLOAT LOCATION (±15') A I SG OCT U 9 2018 ST. Lucie County,, PermittinO 10.7/16"±3/32" DT. DETAIL VIEW D=D DETAIL A ..SPECIFICATIONS mtefrotn.APPSS\dw9\6o0D\ O.D.30 LGTH.45:5/8 SH.. q rR MAWP 250 PSI ® 650 T HD. RT- MDMT-20 TO 250 PSI GAL.118 S.A.32.7 DNT TEST PSI Wr.278# cu.Fr.i6.1 420# ASME: DOMESTIC XRAY CORR ALW sH HD STORAGE TANK CRN L4886.5C CODE: ASME SECTION VIE DN.I, DRAWN BY DATE WELD DETAILS: M-1932 LATEST EDITION & ADDENDA �C sca E NONE AMP BY DEATDRAWING N0. STD. TOLERANCES (UNLESS .OTHERWISE NOTED): M-2461 Jp 6762 f . 77, e a , e e a e a Example 3 Determine the sizes of piping or tubing required for the 2 PSI I-P-Gas installation shown. Total first stage piping length a 26 feet; first stage regulator setting Is 10psig (use Table 1 or 2 @ 30 feet) a, Total 2 PSI Piping Length = 19 ft. (use Table 4 @ 20 ft. or Table 6 @ 20 ft.) From as to a, demand= 338,000 BTU use 3/B'I CSST or 1/2" copper tubing or 1/2" pipe From Regulator a to each appliance; From a to b, demand= 65,000 BTU; length = 25 ft. (Table 5), use 1/;' CSST , From a to c, demand= 200,000 BTU; length = 30 ft. (Table 5) use 1" CSST From a to d, demand= 38,000 BTU; length = 21 ft.* (Table 5) use 3/8" CSST - *use 25 ft. column From a to e, demand= 35,000 BTU; length = 40 ft. (Table 5) Range Use 1/2" CSST 63,000 First Stage 26 Regulator 19 j 1� or pp ggg �gry�p pg p�q + Feet �Feet7 calvI® VF&151&Y11L'aE1YF�ANE � ..�.cs:a�«:ia. ..... 1701 Commerce Avenue Vero peach, Florida32960 as /PSI Second Stage Regulator I.tne Pressnire Regalator _ Furnace j e 200,000 J c `30 Feet 25 21. Feet Feet 12. Inches 40 Feet Clothes Dryer ( L 36,000 e Table-1 - First Stage Tubing or Pipe Sizing.' 10 PSIG Inlet with a 1 PSIG Pressure Drop (Between First and Second Stage Regulators) 1-:- 1- -f 0 ri 1/1.n of n:..iiL i4crl 1 o-rZm-a Mr-ncl lRacorl nn 1 Fin Rnacifir. Gravity Gas) d Water Heater 38,000 of Pipe.0'r, Copper tubing, 1011 20 1 30 140 50 LengthSize 60 70 80 90 100 126 150 175 200 1 250 300 1 350 1 400 Copper Tubing '/e' 513 352 283 242 215 194 179 166 156 147 131 118 109 101 90 81 75 70 (O.D.) %z" 1,060 727 584 500 443 461 369 343 322 304 270 244 225 209 185 168 155 144 -- z 5/° 2,160 .1,480' 1,190 1,020 901 816 751 699 655 619 549 497 457 426 377 342 314 292 3,760 2,580 2,080 1,780 1,570 1,430 1,310 `1,220 1,150 1,080 959 B69 799 744 659 597 549' 511 Pipe Size Y," 5,330 3,670 2,940 2,520 .2,230 2,020 1,860 1.1,730 1,630 1,540 1360 1230 1130 .1,060 935 847 779 725 1/," 3,320 2,280 1,830 1,570 1,390 1,260 1,160 1 1,080 1 1,010 956 1 848 768, 706 657 .582 1 52B 486 452 3/4" 6,950 4,780 1 3,840 3,280 2.910 2,640 2,430 2,260 2.120 2,000 1,770 -1,610 1,48.0 1,370 1,220 1,100 1,020 945 1" 13,100 9,000 7,220 6,180 5,480 4,970 4,570 4,250 3,990 3,770 3,340 3,020 2,780 2,590 2,290 2,080 1,910 1,780 11/4" 26,900 18,500 .14,800. 12,700 11,300 10.200 9,360 8,730 8,190 7,730 . 6,850 6,210 5,710, 5,320 4,710 4,270 3,530 3,650 1'%x 40,300 27,700 22,200 19,000 16,900 15,300 14,100 13.100 12,300 11,600 10,300 9,300 8,560 7,960 7,060 6,400 .5,880 5,470 2" 77,600 53,300 42,800 36,600 32,500 29,400 27.100 25,200 23,600 22,300 19,800 17,900 16,500 1 15,300 13,600 12,300 11,300 10,500 ' Notes: Total length of piping from outlet of first stage regulator to inlet of second stage regulator (or to inlet or second stage regulator illnrle3t away/ 1) To allow 2 PSIG pressure drop, multiply total gas demand by 0.707 and use capacities from table. 2) For different first stage pressures, multiply total gas demand by the following factor and use capacities from table. Example: 1,000,000 BTU load at 5 PSI: 1,000,000 (1.12)=1,120,000 BTU then use chart based on 1,120,000 BTU First Stage Pressure PSIG Multiply By Data Calculated per NFPA# 54 and NFPA # 58 20 0,844 15 0,912 5 1.120 Table 2 - First Stage Polyethylene Plastic Tubing or Pipe Sizing' 10 PSIG Inlet with a 1 PSIG Pressure Drop (Between First end Second Stage Regulators) - Maximum capacity of polyethylene pipe or tubing in thousands of BTU/lir of undiluted LP -Gases (Propane) leased on 1.50 Soecific Gravitv Gas) . .. :.. . . - .. . . plastic Lonoth of bing,or pipe N SDR 10 20 30 40 50 60 70 BO 90 100 125. 150 175. 200 225 250 275 300 350 400 '/T 7.00 762 653 578 524 482 448 421 397 352 319 294 273 256. 242 230 219 202 18B 9.33 2,140 'T,840 1,630 1,470 1,360 • 1,260 1,180 1,120 990 897 826 778 721 681 646 617 567 528 a/. 11.00 2,390 3,670 3,260 2,950 2,710 2,530 2,370 2,240 990 897 826 778 721 681 646 617 567 528 1 T 11.00 5,230 4,470 3,960 3,590 3,300 3,070 2,880 2,720 2,410 2,190 2,010 1,870 1,760 1,660 1,580 1,500 1,360 1,290 1 11.00 7,740 6,630 5,870 5,320 4,900- 4,560 4,270 '4,040 3,580' '3,240 2,980 2,780 2,600 2,460 2.340 2,230 2,050 1,910 I% 11.00 13 420. 11,480 10 180 9,221 1,411 7,890 . 7,400 _ 6,990 6,200 5,620 5,170 4,810 - 4,510 4,260 4,050 3,860 3,550 3,300 1% 11.00 20,300 17'00 15,400 13,900 12,800 1 11,900 11,200 10,600 9,360 8,480 7,800 7,260 6,810 6,430 6,110 5;631 5,360 4,990 2 _ 11,00 36,400 31.200`27,600_25,000 23,000_21400 20,100_19,000-16_800^^15;200,14.000 �3�,000«^12`200: 11,600 11,000 10,470 9,. 8,970 T = Tube Size First Stage Pressure PSIG Multiply By Data Calculated per NFPA# 54 and NFPA# 58 20 0.844 15 0.912 5 1.120 AUZZ 100 Rego Dr, P.O. Box 247 Elon, NC 27244 USA www.regoproducts.com Phone (336) 449-7707 Fax (336) 449-6594 13 Table +.- Socond Stage or Integral-Tvgin•Stage Tubing or Pipe U12ing 994n: Water Column Inlet with a 0°05-In. iNater Column prop __ a..f.. .... 1� sw,.,,-d� of RT1 11hr of I InrliII ftPrI I P-G9SeS Maxlrnum capacityar P'Pu ut lu-1ll,_,II,IkrVUao.,. k k♦ 4 I° 10 20 30 40 60 . 60 F 70 1 80 90 100 Us 150 175 200 250. 300 350 400 4-5 31 25 21 19 17 16 15 14 13- 11 10 NA NA NA NA NA NA Copper^/a" 93 64 51 44 39 35 32 30 28 27 24 21 - 20 18 16 15 1A 13 Tuning a/a" 968 - 129 104 89 79 71 66 61 57 54 48 44 . 40 37 33 30 28 26 p 3/a" 3 8` 226 182 165 138 125 115 107 100 95 84 76 70 . 65 58 52 48 45 (0 W , 467 321, 258 220 95 177 163' 152 '142 134 119 108 99 92 82 74 68 63 291 200 160 137 122 110 NA 101 NA 94 89 84 74 67 62 58 51 46 608 418 336 287 255 231 NA 210 NA 197 185 175 155 140 127 101 97 Pipe 1" 1.150 787 632 541 480 434 NA 400 NA 372 349 330 292 265 243 2 227 201 182 Size 1'/a" 2 350 1 620 1,300 1,110 985 892 NA 821 NA 763 716 677 600 543 500 465 412 373 1' m" 3 520 2 420 1,940 .1,660 1,480 1 340 NA 1,230 N 140 1,070 1 010 899 814 749 697 618 560 6 720 4 660 3 760 3 210 2 840 2,570 NA 2,370 NA 2 200 2,070 1 960 1 730 1 570 1,440 1,340 1 190 1,080 2" _ � __ _.__ ._ _--I!-- a..4i-+ �... n., nnta Cairulated nor NFPA# 54 and NFPA# 58 Note: Total ler)gtti of piping Train �t ouuyr IGyuta UU w oFF!.... ........ Table 4 - lWaxIMUM Capacity of CSST 2 PSiG. and a Pressure Drop of 9 PSIG (Between 2 psig Service and 1_ine Pressure Regulator) rn_,.c.. --% tm-,-,4 nn 1 rn Cnanifin rZra\rifi, r�a51 In Thousands of b l ulnr oT unauumu L.r-aaaGa r I V aL�, ..� �, •� C--• - - - - - _ - - p f 1 °1 1 at 1 1 tt l it tl 11 426 262 238 203 181' 147 140 124- 101 66 77. 69 60 .53 r s�13 e 15 558 347 316 271 243 196 189 169 137 118 105 96 82 72 18 927 591 540 469 420 344 333 s 298 245 213 191 173 151 135 �a 19 1.110 701 640 554 496 406 393 350 287 248 222 203 175 158 - 23 1,740 1,120 1,030 896 806 663 G42 578 1*1 11 415 .373 1 343 298 268 319 3�4 25 2,170 1,380 1,270 1,100 . 986 809 1 760 1 703 1 675 501 1 448 411. 355 30 4.100' 2,560 2.330 -2,010 1,790 1,460 1 1,410,.; 1,260 1,111-, .880 785 716 616 550 31 4,790 2,950 2,690 2,320 2,070 1,690 1,630'`` 1,450 1,160. 1020 910_ 829 716 638 ' Notes: (1).T6ble does not include effect of pressure drop across the line regulator. If regulator loss exceeds 1/2 psi (based on 13-in. water_column outlet pressure): -- DO NOT USE THIS TABLE, Consult with regulator manufacturer for pressure drops and capacity factors. Pressure drops across a regulator may very with flow rate. (2.) C�fUTION: Capacities shown in table can exceed maximum .capacity for a selected regulator. Consult with regulator or tubing manufacturer for guidance. (3) Table includes losses for four 90-degree bends and two end flSings. Tubing runs with q larger number of bends and/or fittings shall be increased by an equivalent . lengt) of tuing according 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. *°FI-'D - Equivalent Hydraulic Diameter - A measure of the relative hydraulic effiencly between different tubing sizes. The greater the value of EHp, the greater the gas capacity of the tubing:pate Calculated per NFPA# 54 and NFPA# 58 TabI6 5 - Maximum Capacity of CSST " (Between 114nl Water Column and a Pressure Drop of 0.054m Water Column Seooad Stage (Low Pressure) Regulatorarid Appliance ShutoffUalve) in Thousands of 13TU/hr of undiluted LP -Gases (Propane) ttsasea on Lac JrItlLN/G v,gv,LX , oar - - - n3/B" 13 72 :' SD 39 34 30 28 23 20 19 -17 15 15 14. ' 11 9 6 8 15 99 69 55 49 42 39 33 .30 26 25 23 22 20, 15 1 14 12 11 18 181 .129 104 91 82 74 64 58 53 49 45 44 41 31 1 28 25 23 /�" - 19 211 150 121 106 94 87 Z4 66 60 57 52 50 47 36 1 33- 30 26 23' 355 254 208 183 184 151 131 118 107 1 99 94 . 90 85 . 66 60 53 50 V4" 25 426; 303 1 248 216 192 177 153 137 1 126 117. 109 102 98 75 69 61 57 . 744 521 422 365 326 297._ 256 227 207 191 178 169 159 123 112 99 90 1 .30 31 863 605 490 425 . 379 344 297 265 241 222 208 197 186 143 129 117 107 Table includes losses for four 90-degree bends and two and Min9s. Tubing runs with a latgernumber afbends and/orflttingsshio hl increased. by bands. Ibrigrh of ttibin� according to the following equation: L-1.3n Where L is additional length (it) of tubing and n is the number of additional fittings and/or bends. . 4".EHD - Equlvalent Hydraulic Diameter -A measure of the relative hydraulic effenciy betweOn different tubing sizes, The greater the value of EHD, the greater the gas capacity ofthe tubins., Data Calculated per-NFPA# 54. and NFPA# 58 Table 6 r Copper Tubing or Schedule 40 Pipe Sizing ° 2 PSIG Inlet with a 1 PSIG Pressure Prop (Between 2 PSIG Service and I.ine Pressure Regulator) d n 1 60 S ecific Gravity Gas n Thousands ° _ of STU/hr of undiluted LP Gases (Pre ane ase o . p 1 i +► f ./ 0 .l 11 t6 3/0° 413' 2B4 228 195 ' 173 157 .144 134 126 119 276 259 245 1 11 { tl 1 11 I 1 I .1 \ 1 105 217 .'95 197 88 181 . 82 168 72 149 . fib 135 .60 124. 56 116 53 109 50 103 47 97 45 43 93 89 41 86 Copper Tubing '1" 852 585 470 402 356 323 297 °° 1 790 1,190 966 81B 725 857 605 562 628' 498 442 400 368 - 343 304 : 275 253 235 221, 209 19B 189 1B1 174 (O.D,) 3/e" 3030 2.080' 1,670 1,430 1,270 1.160 1,060 983 922 871 772 700 644 1 599 1 531 481 442 411 386 365 1 346 330 1 316 30 %" 4300 2,950 2370 2,D30 1,800 1,630 1500 1,390 1,310 1,240 1.100 992 913. 849 763 682 62B. 584 548 517 491 469 449 431 'h" 2680 1,840. 1,4110 1.260 1,120 1,010 934 .869 815 770 682 818 569 529 469 425 391 364 341 322 306 292 280 269 5590 3,850 3090 2,640 2;340 2120 1 950 1,820 1,700 1,610 1,430 1290 1,190 1,110 981 869 817 760 714, 674 $40 611 585 562 Pipe 1 10,600 7.240 5 820 4,960 4.410 4700073 680 .3,420 3,210 3,030 2,690 2,440 2,240 2,080 1 860 1 670 1,540 1,411 1,350 1,270 1 10 1,160 1,100 1,060 + Size 11/4" 21,600 14900 11,900 10,200 9,060 8,210 7,55D 7,020` 6.690 6,230 5,250 5,000 4.600 4.280 3790 3.440 3,160 2940 2,760 2,610 2,480 2,360 2,260 2,170 00 217,900 15 300 13 600 12,300 11,300 10,500 9.080' 9..' 1'/a" 32 2 300 8,270 -7 490 6,890 6,410 6.680 15,150 4,74D 4,410. 4,130 3,910 3,710 3,540 3,390 3,260 2° 6240D 42900 34,500 29,50D 26100 2370D 21,800 20,300 19,000 18,000 15,90014A00 13,3D0 12,300 _ 10 00 9920 9,120 t.. innn 8,490 nTl 7,960 uhr 7,520. 7140 6,820 6,530 6,270 Ni � ..Note: Maximum undiluted propane capacities iistea are basso on a c-psrg 5ULL1119 --1" a :-F �I r W��.� �•�r•' K+r��•��- ••• •--_ _ , _...._ Data Calculated per NFPA# 64 and NFPA# 58 �xksd.-e