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HomeMy WebLinkAboutDrawings-DanielW MR1 A 0 mkt=w GAS PIPING INSI"ALLATIONS 'TABLE 402.4(28) SCHEDULE 40 METALLIC PIPE Gas Undiluted Propane Inlet Pressure 11.0 In. w.c. Pressure Drop 0,5 in. w.c. Specific Gravity 1.50 INTENDED USE Pipe sizing between single-msecontl-stage (low pressure) regulator and appliance. PIPE SIZE (inch) Nominal 11, 'h 9 1'Ig 1'h 2 2'1, 3 4 Actual ID 0.622 0.824 1.048 1.380 1.610 2.067 2.469 3.068 4.02E Length (ft) Capacity in Thousands of Btu per Hour 10 291 608 1,150 2,350 3,520 6,790 10,800 19,100 39,000 20 200 418 787 1,620 2,420 4,660 7,430 13,100 26,800 30 160 336 632 1,300 1,940 3,750 5,970 10,600 21,500 40 137 237 541 t,110 1,660 3,210 5,110 9,030 18,400 50 122 255 480 985 1,480 2,840 4,530 8,000 16,300 60 1to 231 434 892 1,340 2,570 4,100 7,250 14,800 80 101 212 400 821 1,230 2,370 3,770 6,670 13,600 100 94 197 372 763 1,140 2,200 3,510 6,21.0 12,700 125 89 193 349 716 1,070 2,070 3,290 5,820 11,900 150 84 175 330 677 1,010 1,950 3,110 5.500 11,200 175 7,1 155 292 600 899 1,730 2,760 4,880 9,950 200 67 140 265 543 814 1,570 2,500 4,420 9,010 250 62 129 243 500 749 1,440 2,300 4,060 8,290 300 58 120 227 465 697 1,340 2,140 3,780 7,7 t0 350 51 107 201 412 618 1,190 1,900 3,350 6,840 400 46 97 182 373 560 1,090 1,720 , 3,040 6,190 450 42 89 167 344 515 991 1,580 2,790 5,700 500 40 83 156 320 479 922 1,470 2,600 5,300 550 37 78 146 300 449 865 1,380 2,440 4,970 --- 600 35 --73 138 283 424 817 1,300 2,300 4,700 650 33 70 131 269 403 776 1,240 2,190 4,460 700 32 66 125 257 385 741 1,180 2,090 4260 750 30 64 120 246 368 709 1,130 2,000 4,080 800 29 61 t15 236 354 681 1090 1,920 3,920 850 28 59 ]1] 227 341 656 1,050 1,850 3,770 900 27 57 107 220 329 634 1,010 t,790 3,640 950 26 55 104 213 319 613 978 1,730 3,530 1,000 25 53 100 206 309 595 948 1,680 3,420 1,100 25 52 97 200 300 578 921 1,630 3,320 1,200. 24 50 95 195 292 562 895 1,580 3,230 1,300 23 48 90 185 277 534 850 1,500 3,070 1,400 22 46 86 L76 264 509 811 1,430 2,930 1,500 21 44 82 169 253 487 777 1,370 2,800 1,600 20 42 79 162 243 468 746 1,320 2,690 1,700 19 40 7fi 156 234 ais 719 1,270 2,590 1,800 19 39 74 151 226 436 694 1,230 2,500 1,900 18 38 71 146 219 422 672 1,190 2,420 2,000 18 37 69 142 212 409 652 1,150 2,350 For ST: 1. inch = 25.4 nun, I font = 304.8 unit, 1 pound per square incli= 6, 895 kl'a, 1-inch water column - 0,2488 kPa, 1 British thermal unit per hour = 0.293 t W, I cubic foot per hour= 0.0283 mph, I degree= 0.01745 rad. Note; All table entries have been rounded to three significant digtts. FLORIDA BUILDING CODE -- FUEL GAS, 0th EDITION (2017) 53 flyeIn0207ICC. ALL RIGHTS RESERVED .A,L... d6yClly r repr.bu'!,,, or 1 1 IT INK TM 1.rb lolau fi0Led, ANY UNAUTHORIZED REPRODUCTION OR DISTRIBUTION IS A VIOLATION OFTHE FEDERAL COPYRIGHT ACT AND THE LICENSE ArnInEMEh^r, AND SUBIEC'I' TO CIVIL AND CRIMINAL PENALTIPS TI TFRPUNDDR. GAS PIPING INSTALLATIONS TABLE 402.4 (32) CORRUGATED STAINLESS STEEL TUBING (CSST) Gas Undiluted Propene Inlef Press m'e 11.0 w In. .c. Pressure Drop 45 in.. Specific Gravity 1.50 INTENDED USE: SIZING BETWEEN S114GLE OR SECOND STAGE (Low Pressure) REGULATOR AND THE APPLIANCE SHUTOFF VALVE TUBE SIZE (EHD) Designation, 13 96 18 19 23 25 30 31 37 39 46 48 60 62 Length (R) Capacity in Thousands of Btu per Hout 5 72 99 181 211 355 426 744 863 1,420 1,638 2,830 3,270 5,780 6,550 10 50 69 129 150 254 303 521 605 971 Is179 1,990 2,320 4,110 4,640 15 39 55 104 121 208 248 422 490 775 972 1,620 1,900 3,370 3,790 20 34 49 91 106 183 216 365 425 661 847 1,400 L,650 2,930 3,290 25 30 42 82 94 164 192 325 379 583 762 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. L53 256 297 449 610 988 1,170 2,090 2,330 50 20 30 58 66 118 137 227 265 397 548 884 1,050 1,870 2,080 60 19 26 53 60 107 126 207 241 359 502 905 961 1,710 1.,900 70 17 25 49 1 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 'IO2 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 fib 75 123 t43 217 324 506 611 1,090 1,210 200 9 14 28 33 60 69 112 129 183 293 438 531. 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 For SI: I inch=25,4m n, I foot=304,8 nuns I pound per square inch =6,895 kPa, I -inch water column - 0 2488 kPa, I British thermal unit per hour =0,2931 W, 1 cubic feet per hour =0.0283 m'/h, I degree =0,01745 rad. Notes: 1. Table includes losses foi four90-degree bends and two end fittings, Tuhing rusts with larger Numbers of bends or fittings shall be increased by an equivalent length of tubing to the following equation', L.= 1.3n where L is additional length ('feet) of tubing and n is the number of additional fittings or heads. 2. EHD-Equivalent Hydraulic Diameter, which is a measure of the relative hydraulic efteieney between different tubing sizes. The greater the value of BHD, the greater the gas capacity ofthe tubing. 3. All table entries have been rounded to three significant digits. FLORIDA BUILDING CODE-- FUEL GAS, 6th EDITION (2017) 57 1 capyr'yhto,un7i .. ALLRIGH'ISMESDIN6D Accmeedtry] illy S1Ivpcjij,r3r,2uIS5su,35AM pursuant Licc-Agno,insintwith lCC, N f Po -ymducti-or d,W Lura I c, Ihtu, d. ANY UNAUTHORIZED REPRODUCTION OR DIS'IR1gUTIOh IS A VIOLATION Of IHB IRDER AL COPYRIGHT AC I AND1 HE LICENSE AGRElp,nerr, AND SUNFICTTO CIVIL AND CRIMINAL P6NALTIE,S' THERRUNDER. GAS PIPING I NS'tALLA'1'IC1NS Gas Undiluted Propane TAk-31..E 402.4(16) Inlet Pressure 11,0 in. w.c. POLYETHYLENE PLASTIC: PIPE Pressure Drop 10,5111. W.C. Specific Gravity 1.50 INTENDED USE PE pipe sizing between integral two -stage regulator attank or second stage (low-pressure regulator) and building. PIPE SIZE (inch) Nominal OD '1 - '14 1 1'h ill, 2 � 3 4 Designation SDR9 SD1111 SDR 11 SDR 10 SDR11 SDR 11 SDR 11 SDR 11 Actual ID 0.660 0.860 1,077 1.328 1.664 1.943 2.8fi4 3.682 Length (ft) Capacity in Thousands of Btu per Noun 10 340 680 1,230 2,130 3,210 5,770 16,000 30,900 20 233 468 844 1,460 2,210 3,970 1.1,000 21,200 30 187 375 677 1,170 1,770 3,180 8,810 77,000 40 160 321 580 1,000 1,520 2,730 7,540 14,600 50 142 285 514 890 1,340 2,420 6,680 12,900 60 10 258 466 807 1,220 2,t90 6,050 11,700 70 119 237 428 742 1,120 2,010 5,570 10,800 86 ll0 221 398 690 1,040V�,470 5,180 10,000 90 103 207 374 648 978 4,860 9,400 100 98 196 353 612 924 4,590 8,900 125 87 I73 313 542 8'19 4,070 7,900 150 78 157 284 491 742 3,690 7,130 175 72 145 261 452 683 3,390 6,560 200 67 135 243 420 635 3,160 6,100 250 60 119 215 373 563 1,010 2,800 5,410 300 54 108 195 338 5,10 916 2,530 4,900 350 50 99 179 311 469 843 2,330 4,510 400 46 92 167 289 436 784 2,170 4,190 450 43 87 157 271 409 736 2,04 0 3,930 500 41 82 148 256 387 695 1,920 3.720 For SI: 1 inch = 25.4 mm, 1 foot =304.8 mill, 1 pound per square inch =6.895 US, I -inch Water Sol umD=0,2488 US, L British thermal unit per Iiouf = 0.2931 W, I cubic Pool per hour = 0.0283 m'di, 1 degree = 0 01745 rad. Note: All table RUHics have been rounded to three significant digits, 60 FLORIDA BUILDING CODE - FUEL_ GAS, 6tlt EDITION (2017) L in L r Co9yrlgN®2F17RC ALL RIGHTS RESERVED. Accessed UyLilly SEA on leu so,mlos'000,AMFnAnmllaLlmneeAgrmmem will, VC. M. finter rapmducdnn m'n murmimi wumm' diWE.Eon -d ..re d. ANY UNAUTHORIZED REPRODUCTION OR DISTRIBUTION IS A VIOLATION OF THE FEDERAL COPYRIGHT ACT AND THE Id GENSE AOREEIMENT, AND SUIFUC'I'10 CIVIL AND CRIMINAL VLN, AL1IRS THEREUNDER. P1PG? ND TUBING SIZING T.- BLF5 Table 15,1(o) PolycL4ylene Plastic Pipe Sizing Peimeeu First -Stage and Second-st ge Repdators: Nominal Outside TDia,.teter (L-3) pas: Uucliluted Propm'e hilet Pressure: 10.0 psi Pressuue prop; 1.10 psi ,Specific �G.ravily: 1.5 `,� Pl .sLic Pipe yy i&i. 3/1 in 1 in. I Vt hi. 1 yg ill. 2 in. Leng+ds SDR 9.33 SDR 11.0 ,SDR 11.00 SDR 10.00 MR) 1,00 SDR 11.00 (ft) (0.660) (0.860) (1,077) (1.328) (1,554) 94 30 2143 4292 774-1 13415 20260 36402 40 1835 3673 6628 11482 17340 31155 50 1626 3256 5874 10176 15368 27612 60 1475 2950 5522 9"20 13924 25019 70 1355 2714 4896 8483 12310 2° ,017 80 1261 2525 4555 7891 11918 21113 90 1183 2369 4274 7404 11182 20091 100 1117 2238 4037 6994 10362 18978 125 990 1983 5578 6199 9361 16820 150 897 1797 5242 5616 8482 15240 175 826 1655 2983 6167 7803 1-1020 200 778 1539 27i5 4807 1 0 13043 225 721 144S 2603 4510 6811 12238 250 681 1363 2459 4260 6434 1156060 275 C46 1294 2336 4046 Gill 10979 300 517 1235 2223 3860 5830 10474 350 567 1136 2050 3551 53G3 9G36 400 523 1057 1907 M04 4989 3965 450 495 992 1739 3100 4681 3411 500 468 937 1690 2928 4422 7945 600 700 421 849 1531 2553 4007 7199 800 390 353 731 1409 2441 3686 6625 900 340 726 582 1311 2271 3429 GTE 1000 322 G4=1 1230 2131 3217 5731 1162 2012 30;i9 5461 1500 258 51, 935 1616 2111 4385 2000 221 443 793 13S3 2089 3753 IRS: Iron pipe size. SDP: &andard dimension rnu Notes: (1) Capacities are in L000 Btu/he. (2) DiVICnSiOnS in parentheses are inside. dicnteter 55-97 9n Ia F, limn Instruction Manual nnrt< 9141 R600 and HSRL Series LP -Gas Regulators March 2006 I SeriesR600 and HSRL kC Failure to follow these instructions or to properly install and maintain this equipment could result in an explosion and/or fire causing property damage and personal injury:`death. Fisher equipment must be installed, operated, and maintained in accordance with federal, state, and local codes and Fisher instructions. The installation in most states must also comply with NFPA No. 54 and 58 standards. Only personnel trained in the proper procedures, codes, standards, and regulations of the LP -gas industry should install and service this equipment. Things to tefi the gas customer.: 1. Show the customer the vent or vent assembly or vent tube. Stress that this opening must remain unobstructed at all times. Tell the customer to check the vent opening after a freezing rain, sleet storm, or snow to make sure ice has hot formed in the vent. 2. Show the customer the shutoff valve on the container. The customer should closethis valve immediately if gas is smelled, appliancerot.,lights fail to stay on or appear higher than usual or any other abnormal situation occurs. 3. Tell the customer 6.call your company to service the regulator if the regulator vents gas or a leak develops in the syster_q,-Only a qualified gas service person should it sfis, 'or service the regulator, Introduction Scope of Manual This instruction manual covers Installation and Maintenance for the R600 and HSRL Series regulators, which includes first stage, second stage, integral and TYPE HSRL Figure 1, Types R622, R642 and HSRL 2 psi (0,14 bar) service regulators used on LP -Gas vapor service applications. They are not to be used on liquid service. Description Second Stage Low Pressure Regulators The Types R622, R642, R662,'and HSRL Series regulators provide low pressure, inches of water column, delivery pressures. They are normally set at 11-inches water column (27 mbar) pressure. They have high capacity internal relief valve construction, The regulators are normally painted PALM GREEN. The units differ in construction and capacity rating. uwyu_l$f1�i2Geyu��aos $onji'll IFISHER-'r a� EMERSON- Process Management N F- cations Pressure Taps Size Restriction Outlet Pressure Standard Set Point R600 Series: 1/8 NFT: #54 (0,055 inch (1,40 mm)) Types R622, R642, R652, and HSRL Series: Drill on outlet and inlet 11-inches w.c. (27 mbar) HSRL Series: None - Type R632:_ First Stage: approximately 10 psi (0,69 bar) Orifice $izes. R600 Series: 7/32-inch (5,55 mm) HSRL Series; 3/8-inch (9,5 mm) Wide Open Co for Relief Sizing R600 Series: 38 HSRL Series: 105 Maximum Allowable Inlet Pressure Types R622H, R632: 250 psig (17,24 bar) Types R622E, R652E: 10 psig (0,69 bar) Types R622, R642, R652, and HSRL Series: 10 paid (0,69 bar) Maximum Emergency Inlet Pressure Types R622H, R632: 250 psig (17,24 bar) Types i�622E, R652E: 15 psig (1,03 bar) Types 1[1622, R642, R652, and HSRL Series: 15 psig (1,03 bar) Temperature Capabilities -20' to 160°F (-29° to 71 °C) Pressure Registration Internal Integral Two -stage Regulator The Type R632 integral two -stage regulator contains a non-adjustable first stage regulator on the inlet. The second stage provides 11-inches water column (27 mbar) outlet pressure. The second stage portion has a high capacity internal relief valve construction. The first stage does not have an internal relief valve. The regulators are normally painted GRAY. First Stage and 2 PSI (0,14 bar) Service Regulators The Types R622H, R622E and R652E regulators are designed for high pressure (pounds per square inch) vapor service. These regulators have high capacity internal relief valves. When used on first stage service, the.Type R622H regulator reduces container pressure .to 10 psig (0,69 bar) for a second stage regulator. On final stage service the regulator reduces container pressure for a high pressure burner. The regulator is normally painted RED. The Type R622E or R652E standard outlet pressure setting is 2 psig (0,14 bar). The regulator is painted PALM GREEN with a WHITE CAP. It is an intermediate stage regulator that reduces 10 psig (0,69 bar) first stage pressure to 2 psig (0,14 bar). They are used on 2 psig (0,14 bar) pressure systems. The Types R622E and R652E are not suitable for first stage service. g tzi.moari _.. econ a e.-.=Inc-es. .c. Types 6 s� (0,14: bar) Type R622H: 10p (0 69 bar), 5 psi (0,35 bar) Outlet Pressure Spring Range Types R622, R642, R652: 7.5 to 9.5-inches w.c. (19 to 24 mbar), 9 to 13-inches w.c. (22 to 32 mbar), 13 to 20-inches w.c, (32 to 50 mbar),, 16 to 40-inches w.c. (40 to 99 mbar) Type R632: First Stage: non-adjustable Second Stage: 9 to 13-inches w,c. (22 to 32 mbar) Types R622E, R652E: 1 to 2.2 psi (0,069 to 0,15 bar) . Type R622H: 8 to 12 psi (0,55 to 0,83 bar), 4 to 6 psi (0,28 to 0,41 bar) HSRL Series: 9 to 13-inches W.G. (22 to 32 mbar) Approximate Weight Types R622H, R632 with P®L inlet: 1.7 pounds (771 grams) Ali Other R600 Series: 1 A pounds (635 grams) HSRL Series: 4.5 pounds (2,04 kg) ) Specifications section, Tables 1 and 2 list the specifications for these regulators. Contact the factory if the regulator is to be used on any service other than LP -gas, natural gas, or air. The following information is located on the spring case: Type nhmber, orifice size, spring range, and date of manufacture. Install aflon A� WARNIf�G4' All vents should be kept open to permit free flow of air in and out of the regulator. Protect vent openings against the entrance of rain, snow, ice formation, paint, mud, insects, or any other foreign material that could plug the vent or vent line. LP -gas may discharge to the atmosphere through the vent. An obstructed vent which limits air or gas flow can cause abnormally high pressure that could result in personal injury or property damage. Failure to use a vent line on Table 9. Relief Valve Specifications TYPE TYPICAL SET POINT NOMINAL RELIEF VALVE START TO DISCHARGE MAXIMUM INLET PRESSURE TO NOT EXCEED OUTLET PRESSURE WITH DISC REMOVED Inlet Pressure Maximum Outlet Pressure .. ___.... .._. _ " psi(0;069'bar) ..__.._.__ -2psig-(0;14-bar)--- R622, R642 _ ----- --- _ .----- -..R652_ ____ R632 250 psig (17,2 bar) R622E 2 psi (0,14 bar) 3.5 psi (0,24 bar) 50 psig (3,4 bar)) 5 psig (0,34 bar) R652E R622H 10 psl (q69 bar) 20 psi (1,37 bar) Not Applicable Table 2. Capacity, Connection Sizes, and Vent Orientation REGULATOR APPLICATION TYPE NUMBER CAPACITY BTUIHR pBTU/HRut INLET CONNECTION OUTLET CONNECTION OUTLET PRESSURE SETTING FT 3SCINCHN1) SCREENED VENOCAT11T STAN ARD LOCATION R622-BCF 875,000 1l2-Inch FNPT 1l2-inch FNPT R842-DFF 900,000 3l4-Inch FNPT 11-inchss w.c. R692-DFF 1,000,000 3l4-inch FNPT 27 mbar ( ) Rfi227CFF 1,400,000 1/2-loch FNPT Second Sta e 9 A Over Inlet R622-DFF 3/4!Inch FNPT R622-CFGXA 1,125,000 1/2-Inch FNPT 3/4-Inch FNPT 18-inches w.c. (45 mbar) HSRL-BFC«r 3/4-inch FNPT 11-inches W.C. 2,100,000 (27 mbar) HSRL-GFCuI 1-inch FNPT 1-inch FNPT � Integral Two -Stage 9 R632-BCF 700,000 1/4-inch FNPT 1/2-Inch FNPT 11-Inches w.c. (27 ruder) First Stage. Dawn Second Stage: Over Inlet R632-HCF FPOL Rfi32-CFF 750,000 114-Inch FNPT 3/4-Inch FNPT' R632-JFF FPOL R622E-BCH 1,250,000 1/2-inch FNPT 1/2-inch FNPT 2 PSI (0,14 bar) Service 2psig (0,14 bar) Over Inlet R622E-DCH 1,500,000 3/4-inch FNPT 3/4-Inch FNPT R652E-DFH 1,400,000 R622H-BGK 2,000,000 1/2-inch FNPT 5 pslg (0,35 bar) ' — " !���"'y' First Stage':' R622H-BGJ 2,100,000 1/2-EFNPT 10 psig (0,69 her) Over Outlet R622H-HGJ FPOL R622H-HGJKA R622H-JGK 5 psig (0,35 bar) 2,250,000 3/4-inch FNPT R622H-JGJ 10 psig (0,69 bar) R622H-DGJ 2,400,000 3/4-inch FNPT 1, Capacltles Based on: Second Stage: 10 psig (0,69 bar) inlet pressure and 2-Inchesw.c. (5 mbar) droop. . Integral Two Stage: 30 psig (2,07 bar) and lunches w.c. (6 mbar) droop. 2 PSI (0,14 bar) SeNIGtr 10 psig (0,69 bar) Inlet pressure and 20% droop. First Stage: 30 psig (2,07 bar) Inlet pressure and 20% droop. 2. Straight globe valve body configuration. Installation Location The installed regulator should be adequately protected from vehicular traffic and damage from other .external sources. install the regulator with the vent pointed — - vertically down, see Figure 2-If-the vent cannot be --- installed in a vertically down position, the regulator must VENT POINTED DOWN be installed under a separate protective cover. installing the regulator with the vent down allows condensation to drain, minimizes the entry of water or other debris from entering the vent, and minimizes vent blockage from freezing precipitation. Ffgure 2. Regulator with Vent Pointed Down Indoor Installations can cause a hazardous accumulation of gas which could result in personal injury or property damage. Never use a Type R622H, R622E or R652E (pounds to pounds) regulator on low pressure (inches of water column) service because personal injury or property damage could occur. The Types R622E and R652E are not suitable for use as a "first stage" regulator. General installation Instructions Before installing the regulator, Check for damage, which might have occurred in shipment. o Check for and remove any dirt or foreign material, which may have accumulated In the regulator body. Replace old pigtails. Blow out any debris, dirt or copper sulfate in the copper tubing and the pipeline. Apply pipe compound to the male threads of the pipe before installing the regulator. Make sure gas flow through the regulator is in the same direction as the arrow on the body. "Inlet" and "outlet" connections are clearly marked. _ ®o not install the regulator in a location where there can be excessive water accumulation or ice formation, such as directly beneath a down spout,, gutter, or roof line of building. Even a protective hood may not provide adequate protection in these instances. Install the regulator so that any gas discharge through the vent or vent assembly is over 3 feet (0,91 meters) horizontally from any building opening below the level of discharge. Install the regulator, high enough above ground level at least 1 B-inches (45 cm) - so that rain splatter cannot freeze in the vent. Regulators S6bledtod..to Hid v✓ -.. Snow CondiAllons Some installations, such as in areas with heavy snowfall, may require a hood or enclosure to protect the regulator from snow load and vent freeze over. Horizonta09y Instailed Requiators Horizontally mounted regulators, such as found in single cylinder installations and ASME tanks, must be installed beneath a protective cover or under the ASME tank dome, refer to Figure 3. If possible, slope or turn the vent down sufficiently to allow any condensation to drain out of the spring case;:, Be careful that the slot in the tank dome or protective cover for the regulator's outlet piping does not expose the vent to the elements. The first stage vent on the Type R632 should be pointed down. Meter installations Type R642 regulators have an angle body that makes it easy to install on to a gas meter instead of piping leading directly into a building. Meter and Type R642 with vent over regulator inlet: Install the regulator per instructions given in the previous section "Installation Location". Figure3. Tanklnstallatton Meter and Type R642 with vent over the regulator outlet and installed over the top of the meter: This installation orientation will put the Type R642 regdlator vent in a vertical down position, but very close to the top of the gas meter. The regulator vent may become blocked during a freezing rain storm or heavy snows. Therefore, some type of protective cover -should be installed over the regulator and meter or vent piping should be installed so that the vent remains open. Meter and Type R642 Regulator Installed Indoors: Pipe the regulator vent per the section "Indoor Installations". Indoor 4tastea9iati®ns By code, regulators installed indoors have limited inlet pressure, and -they require a vent line to the outside of the building, see Figure 4. Avent assembly, such as Fisher Y602 Series, should be used on the end of the vent line. The same installation precautions, previously discussed throughout this manual for the regulator vent, apply to the end of the vent tube assembly. Vent lines must not restrict the gas flow from the regulator's internal relief valve. Vent lines should be at least 3/4-inch NPT pipe or 3/4-inch NPT size, Gray PVC Schedule 40 Rigid Non-metallic Elect(ical Conduit for above Ground. Service, per UL 651. To install the vent line, remove the vent screen and apply a good grade of pipe dope to the male threads of the line. Vent lines should be as straight as possible with a minimum number of bends. TO APPLIANCE VENT LINE BASEMENT FROM FIRST � STAGE REGULATOR VENT ASSEMBLY VENT OPENING MUST BEAT LEAST 3 FEET (0,91 meters) HORIZONTALLY FROM ANY BUILDING OPENING BELOW IT Figure 4. Basement Installation END OF REGULATOR VENT TUBE LOCATED AT TOP INSIDE OF GRACE GROUND DOWNWARD AND HOUSING DOME COVER. SLOPING AWAY FROM HOUSING DOME. THIS PREVENTS WATER COLLECTING AND RUNNING INTO OR STANDING AROUND HOUSING DOME. &INCHES (50,8 MM) ._MINIMUM ._ REGULATORADJUSTMENTCLOSURE CAP MUST BE TIGHT WATER MARK LEFT IN HOUSING DOME AT LEVEL ABOVE REGULATOR VENT, OR END OF VENT TUBE REQUIRES REPLACEMENT OF REGULATOR. THEN CORRECT INSTALLATION. Figure 5, Underground Installation Underground Installaflorts ,CAUTION Type R632 integral regulators require 2 vent tubes, one on the first stage vent . and one on the second stage vent, when- - installed on underground tanks. Failure to use 2 separate vent tubes can result in early regulator failure and/or over pressuring the second stage that could result in fires or personal injury. Regulators installed in the dome of an underground container require a vent tube to prevent water from entering the regulator spring case, see Figure 5. Note: Type R632 integral regulators installed on underground tanks require the use of 2 vent tubes, one for the first stage vent and the other for the second stage vent of the regulator. Remove the vent screen and install a vent tube. ,The vent tube must be run from the regulator vent to above the maximum water table. The vent tube opening must terminate at the extreme top Inside of the dome cover. Make sure the regulator's closing cap is on tightly, and maintain drainage away from the dome at all times. For further information on Underground Installations, contain, __ Fulfillment Services at phone number 866-840-1075 and ask for Item number 000412 "Installation of Underground LP -Gas Systems: Suggested Installation, Inspection,", Adjustment Each regulator is factory set. If it becomes necessary to increase the outlet pressure, remove the closing cap and turn the adjustment screw clockwise. Turn the adjusting screw counterclockwise to decrease the outlet pressure. The first stage portion of the Type R632 integral regulator is non-adjustable. The outlet pressure plug may be removed using a 7/16-inch (11,1 mm) hexagon wrench. The pressure tap is restricted, so the plug can be removed with pressure on the outlet of the regulator. fnstall a pressure gauge to determine the regulator's outlet setting during adjustment, (Actual pressure at the second stage regulator may be less due to line loss.) After setting, reinstall the pipe plug and replace the closing cap. Check the plug for leakage. Inlet pressure may be checked using the inlet pressure gauge tap and a pressure gauge. Remove the plug using a 7/16-inch (11,1 mm) wrench. The pressure tap is restricted, so the plug can be removed with pressure on the inlet of the regulator. Overpressure Protection Some type of overpressure protection is needed if actual inlet pressure can exceed the outlet pressure rating. Overpressuring any portion of this equipment above the f NO limits shown in the Specifications section Due to normal wear or damage that may cause damage to regulator parts, may occur from external sources, leaks in the regulator, or personal injury these regulator's must be inspected and due to bursting of pressure -containing maintained periodically. The frequency parts or explosion of accumulated gas. of inspection and replacement of the regulators depends upon -the _severity of If any portion of the regulator is exposed service conditions or the recL irements of ah ove[p_ressure condinon thatwCeeds----... _--loealr-state,-and- federal -regulations.-Even the limits in the Specifications section, of under ideal conditions, these regulators must be inspected for damage that may should lie replaced after 20 years from have occurred. date of manufacture or sooner should Large volumes of gas may discharge inspection reveal the need. through the regulator vent during internal relief valve operation, which can, if not Visually inspect the regulator each time a gas controlled, result in fire or explosion from delivery is made for: accumulated gas. t The R600 and HSRL Series regulators, except for the first stage of the Type R632, contain internal relief valves. The internal relief valve in all units will give overpressure protection against excessive build-up resulting from seat leakage due to worn parts or chips or foreign material on the orifice. The amount of internal relief protection provided varies with the regulator type and the cause for the overpressure relief valve operation. When the internal relief valve opens, gas escapes to the atmosphere through the regulator's vent. Some type of additional external overpressure protection must be provided if the outlet pressure in an overpressure condition exceeds the inlet pressure rating of the gas system or downstream equipment. Common methods of external overpressure protection include relief valves, monitoring regulators, shutoff devices, and series regulation. Maintenance rxtT� ty �'� trrF� a1 '4d i'i�-'1� 5W_ i,? Wk i ] k 4 .�Y$8" wm5 cm;. To avoid personal injury or equipment damage, do not attempt any maintenance or disassembly without first isolating the regulator from system pressure and relieving all internal pressure. Regulators that have been disassembled for repair must be tested for proper operation before being returned to service, only parts manufactured by Fisher should be used for repairing Fisher regulators. Relight pilot lights according to normal startup procedures, Improper installation, vent not pointed vertically down or under a cover; no vent tube on underground systems. • Plugged or frozen vent. • Wrong regulator or no regulator in the system. • Internal or external corrosion. • Flooded Regulator; water in spring case; regulator submersed on underground tanks • Regulator age. • Any other condition that could, cause the uncontrolled escape of gas. Failure to do the above could result in personal injury or property damage. Vent ®penjng Make sure the regulator vent, vent assembly, or vent tube does not become plugged by mud, insects, ice, snow, paint, etc. The vent screen aids in keeping the vent from becoming plugged, and the screen should be clean and properly installed. Water inside Regulators from Floods, Weather or Rater gable on Underground Systems Replace any regulator that has been flooded or has been submersed below the water table of an underground tank, have had water in their spring case or show evidence of external or internal corrosion. Checking for internal corrosion can be done by removing the closing cap and with the aid of a flashlight observing the condition of the relief valve spring, main spring, and internal spring barrel area. Amore detailed examination will require shutting 600 and HSRL Series LP -Gas Re u9ators down of the gas system and the complete removal of the Reguiai4or Repair dt' screw Closel examine regulators installed a )us ng y with their vent horizontal for signs of corrosion. Correct Regulators that have been disassembled for repair any improper installations. must be tested for proper operation before being returned to service. Only parts manufactured by Fisher should.be used to repair.Elsher.regulaicle. Be_sura to Regulator Re lacement 90 wive the complete type number of the regulator when _ _ Older regulators -are more likely to catastrophically fail - corresponding -with .the factory because of worn or corroded parts. Replace R600 The type number, orifice size, and spring range are and HSRL Series regulators over 20 years of age. on a label attached to the spring barrel. The date of Other service or environmental conditions, may dictate manufacture is stamped on the regulator. Always provide replacement of the regulator before it becomes this information in any correspondence with your Fisher 20 years old. Regulators that are installed on Distributor regarding replacement parts or technical underground systems and in areas that are subject to sea. assistance. If construction changes are made in salt (coastal) atmospheres should be inspected annually the field, be sure that the regulator marking is also for external and internal corrosion and may require changed to reflect the most recent construction. replacement sooner. Refer to Fisher Bulletin LP-32 for additional information. d3s,r. Fisher and Fisher Regulators are marks owned by Fisher Controls Intematlonal, LLC. The Emerson logo is a trademark and s Nlce mark of Emerson Electric Co. All other marks are the property of their respective owners. The contents ofthfsPublication are proser edforinformaflonsheurpwes onty, end while everyal od has been made to ensure thelraccuracy, fbeyare not to be consfinedas murandes orguarommes, expressed orimplled, regarding the products or services d'esadbad herein or their use or applicability. We reserve fire right to modify crlmpmve the designs or spacifioallons of such products at any time without notice. Fisher does not assume responsibility for the selection, use or real nanance of any product. Responsibility, for proper selection, use and maintenance of any Fisher product remains solely with the purchaser. Emerson Process Management Fisher Controls International, LLC. P.O. Box 8004 McKinney, Texas 75070, USA :+ Telephone:1 (469)293-5863 4201 E E S NN Telephone: 1 (469) 293-4201 ©Fisher Controls International, LLC., 2001, 20061 All Rights Reserved Process Management i Z . L1 w ae ry o O15 sty LL i LL 88m °��' hffi r Z {p[o O A ro 16 U d m O 8N N O Q¢ N W O w ry r O y jo 6`rvF 5 itn pz� F m� W a =OJ O N °° i ox �o p M° rc 1 rcw d 3 8 ssa° H8 �t` o vx "_�W NN K �Ua¢�y �� a 3y ¢ u�q u O2 m °o i� V >>rcm auj sa J a o$u p °F c�yuQo ayrv�, yf�a� puow� �w� oW W Q g Q ZOCW W2nz 'z wZW6 N Nv�Cm wU' WO pia) 8 O N t+) �1 W F N F Q m K z z O K u� a U If N rnoi h M� a iw-rc ��`k'W C7 N^ u i �Mgwm3 0 3mk' z�c? y �y�wE oLL ..a M 0 z 0�W (9y RY W �pm OaooZ�Z ~ �K Z �u U> OSZ26FOW WJWU FOU FvV1�6 J2 VUF6W gZ n�'�>u y n C LL ° mFzS J whip wdoQ ���JJ�Fi i pw�6wt4 r w;� oaw� w CY a asEHU a of O >OZoy O 360 2N KKVN 2 n ahe 8� K Z S g a o o LL U m yx o N o E w y o u ° o Ev O� a ��o8� uo'3 O 3� 3 6 w 8 Z°O6 OM>E °ry z og m° zloin 0 °;s��gm W � — o, � g h M I— �o If� ` e LL M lh a w 0 W K W �>W V ry M O06 pW> W WQ Wrw K} e w OUKmM rvrvW Yo wz (7 O O O ¢ Om J Q cl d WKM W �O mU' 4 Wp M o ogo o <g z m Q �a OW o❑ oM W "x L6� Q LL N °°w ° W r �w° U) a % =Ln O VM JpO 2 z a w a III III � V Z i 2 0 Q LL y K Z �o m O $N pF- KN q o o �o OQ v z2 U J a V O9 W Z Nf 3� �LL j a Q o 0 go III III II I � II I I W W J 2 wU 2 Y W ❑ ❑ ❑ W i w Z W o � z O 1M � a W N ] 2 W ❑_ a m W a m Z o 2 t O � O m N w oY CC ® ® 4 O j U O ww z ao oop J Q Q ❑ (O � t0 N W t0 cO a N N W N N 2 N T F- a 4 Q m U w LL p (9 � LL UNDERGROUND L.P,G- STOR46E TANK ! Gq TYPICAL ANCHORING STANDARD DIVISION Notes: vaen nwessuyC® prevent E�oatat aen, or hn rz ae� ,etude melnr i '.;,° 'r 7�S sl ail b are 6art�d usiRg 2 - 'A-K4° auger anchors and 'Vd" P cable. Cable ;:I ,u, u L7serted Li Va A PE mffbrang to PFO&x tale tank, ffom &tct conta'c�t srrU the cab'ic. 2. LOC -� cable approxib:° ,dy W hvmTd ofw(-1ded mm on both ends �aafc Use � (W) galvaav b�c CQamps t® scam caWc to.Ihc a-" fin, 3 _ Pcfer to Stzradaj�d 6.6 for ranitoeadou, coating and, bacYs¢(R. 58-146 PETROLEUM GAS CODE Window air conditioner ,urce of golf a to direct - appliance 0 it (min) (Note 1) =CNote in) 10 ft (min)1) (Note 2) �Crawace opening, compressor window, or exhaust fan (source of ignition) 10 ft(min) 2000 fi'--, (Note 2) or les gal W.C. = 0,3048 M. � Nearest line of adjoining property that can be For SI units, 1 it /� built upon Notes: (1) The relief valve, filling connectlon, and fixed maximum liquid level gauge vent connection at the container must be at least 10 ft from any exterior source of ignition, openings into direct -vent appliances, or mechanical ventilation air intakes. Refer to 6.3.4.4. (2) No part of an underground container can be less than 10 It from an important building online of adjoining property that can be built upon. Refer to 6.3.2.3. FIGURE 1.1(c) Underground ASME Containers. (Figure for illustrative purposes only; code compliance required.) Annex J Sample Ordinance Adopting NFPA 58. This annex is not a ]cart of the requirements of this NFPA document but is included for informational purposes only. J.1 The following sample ordnance is provided to assist a jurisdiction in the adof option this code and is not part. of this code. QRIiI]�ANd,E NO ' EE IT ORDAINED BY THE `[�6verning Gedj] Of TIAE Oaris dzotao.]:;� SECTION 1 That the Liquefied Petroleum Gas'Code and du- oc ixients adopted by,Chapteo 2, three (3) copies of Nvhich are on file and are open to inspection rby the public in the office of the (jurisdiction's" keeper of records] of the (juns'tliction], are :_ hereby adopted and incorporated Into ordinance -as bully as if set 2017 Edition C—.. ".. awo.ea ,� G e,. �®R r A i .. 4 y No R'Bi[15i1i AnaF �J GARAGE L42 sq ft CLO BB 3 KI -------------------- CHE e 3 GREAT ROOM c b B' n Id• Pzn Pm `a• x I]' Pm °ohm, OFFICE A'L'_APPFOYER EDIe PORCH murRiV.-Few e ®rsekdi e = 3,35.2 eq. ft. Total = I sq. fe.1,2T3 ea ftal - 5,593 sq. It. I •'1dr S �I to �IIIQ i e 0 111 BEDROOM I both GARAGE 631 square ft UJlndow Schedule Mark Size Window Description I. T-2' x A'-4' FIXED GLASS - IMPACT 2 SIN LE G - iM AC s 3. 2'-2" -I' SI GLE HUN - PAC 4 T-2" x 4-4° SI GLE UNG- IMPACT 5 V-2' x 6'- " PANEL CASEMENT W/ 2' HIGH TRANSOM ABOV HORIZONTAL ROLLING - IMPACT. FIXED GLAse - IMPACT - ALL Windows to be white ESP aluminum windows with tint. Provide montin s and structural mullions per elevation*. See product approval chart for Window manufacturer information. - ALL windows to wthstand Pressures stated In Permit Information Box on these plans. - ALL windows in bathrooms to be tempered - ALL windows within 18" of finished floor to be tempered unless Impact rated. - varify ell masonry/rough opening sizes prior to ordering windows. Door Schedule Mark Size Door Description A la> 3'-0' X 8'-O" SOLID CORE - WOOD B 3'-0' X 8'-0' PIBERGLASS 2 PANEL C (6) 3'-Ox x W-D° ALUMN IMPACT SLIDING GLASS D 12) 3'-0' x 8-O" ALUMN IMPACT SLIDING GLASS E 2'-6° X 8'-0' FOAM FILLED PIBERGLA35 6 PANEL F (2) 3'-0° X S'-O" SOLID CORE - WOOD G T-8° X 8'-0' 2 PANEL MOP H 2'-6° X e'-0' 2 PANEL MOP d 2'-6° x 8'-0" 2 PANEL MOP POCKET K 4'-O' x W-On 2 PANEL MOP SI-PASS L I8'-O' X 8-0' OVERHEAD GARAGE DOOR - ALL exterior doors Including garage doors to withstand pressures stated in permit mrorma ion box on these plans, - verify all masonry/rough opening sizes prior to ordering windows. - See product approval chart on these plans for exterior door manufacturer information (including garage door) - Provide one exit door (swing type) that la 3'-O" wide minimum and one emergency escape door (not shuttered). If escape door has gglazing then it must be impact resistant and shall NOT be thru garage. This may be the same door if it meets both criteria listed above. Column Schedule Marki _ Size and Descrmtion C-1 16° IC eo�'cZts black Filled %co,br.te and (9 G5 bare vend. m9 cnubro ime And Decorative'I tubes C-a aslEu° nirn1x[pudteww)da.oaaee n�with bar. v®Vert. � I[i"ey lYtVw FLOOR PLAN ✓ rrm TYPICAL NOTES CALF 3/16" = I'-O" v N'rr� : ,�(� t! I. Contractor to verify ALL notes and dimensions pnar to 1, 1.E ^"' tC nuE -" c proceeding with work. 2. Contractor to STRICTLY ,force ALL OSHA Regmremants. = i y W ' S. ALL Lumber to be used as Dear, R.rters, etc... to have a minimum 1,400 P.S.I. fiber street. 4. Me dsilsler metals to touch. S. ALL Concrete seed far slabs shall he 2500 PSI concrete, and ALL Concrete used far verm,ul filled ce11s, continuous. tie beams etc.. to .hall be 3,000 P.S.I. concrete end/ar 4.000 P.S.I. grout mix 6. Drywall at telling. shall he leveled and attached to bottom chord ar bruises with screws. 9. ALL wood in content oth eo,aete shall be pressure treated. S. ALL wall dimensions are nominal and not finished wall or stud dimensont, 9. ALL plumbing fixtures to he low flow. 10. Contractor to Provide Puri I Drum at water heater m accordance with the Pla ids Plumbing Code current edition. ll. Contractor to Provide a 2'-8" wide door at ane bathroom for handicap accessibility requirements. 12, Lowest Finished floor to be set 6y Governing Building Department surveyor to set in field. Sheet 13. Separation between rawdonce and garage shall be per PEC R309.1 end R309.2 9. Door between garage end residence shall be 1-3/8" solid wood - 20 min. fire rated "X" 2 E, The Geroge shall he separated from rawdence and the attic area by 5/8" type drywall to wall .J appplied gg.rage 14. Garage* banenth hawtthle rooms shell be eno... ted from all habitable rooms. OF above by no lass than 5/8" type "X" drywall M. ALL Pleor tc ceiling meembhes shall be protected by 5/8" type "X" drywall Comm It 19-82