Slam Shut Valves SBC 782

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Slam Shut Valves SBC 782

SBC 782 > Slam shut valves Introduction SBC 782 is a compact safety device (SAV) which quickly intercepts gas flow whenever the pressure under monitoring reaches preset limits, or whenever manually required by operator on site or through a remote command (optional device). SBC 782 Fig.1

Main Features SBC 782 is a slamshut valve with self operated actuation and manual resetting. It is an ideal product for distribution, transmission networks, industrial and chemical engineering applications. SBC 782 is suitable for natural gas and all noncorrosive gaseous media. Its top entry design allows an easy maintenance without removing the body from the pipeline. Main features: Intervention for overpressure and/or underpressure; Manual pushbutton control at installation point; 3 way solenoid valve for remote control (available on request); Manual resetting; Internal bypass for pressure equalization before resetting Possibility of application of devices for remote signal information (contact switches or proximity switches); SBC 782 Designed With Your Needs In Mind Compact Design High Accuracy Easy Maintenance Low Operation Cost Top Entry Third Party Certified Safety Device Fast Response Time Integral ByPass

Main Features Design pressure: 18,9 bar (274 psi) for class 150 51,7 bar (749,6 psi) for class 300 (up to size 4" only) > 102 bar (1479 psi) for class 600 (up to size 4" only) Design temperature: 20 C to +60 C (14 to + 140 F) Ambient temperature: 20 C to + 60 C (4 to + 140 F) Range of intervention for overpressure Who: 0,02 to 100 bar ( 8"w.c. to 1450 psi ) Range of intervention for underpressure Whu: Who: 0,01 to 88 bar( 4"w.c. to 1276 psi ) Accuracy class AG: ± 5% Available size: class 150 DN 1 2 2" 1/2 3 4 6" 8" 10 class 300 & 600 DN 1" 2" 3" 4" Flanging: class ANSI 150 ANSI 300 ANSI 600 RF or RTJ according to ANSI16.5 and PN16 according to ISO 7005 Materials Body Valve seat Steam Plug Diaphragm Seals Disengagement device Compression fitting Cast steel ASTM A352 LCC for class 300 and 600 ASTM A216 WBC for class 150 and PN16 Steel + rubber AISI 416 Stainless steel AISI 416 Stainless steel Ruberized canvas Nitril rubber Housing in light alloy, with stainless steel mechanism According to DIN 2353 in zincplated carbon steel The characteristics listed above are referred to standard products. Special characteristics and materials for specific applications may be supplied upon request.

SBC 782 Calculation of the pressure drop The following formula can be used to calculate pressure losses of the slam shut valve in fully open position: Δp = K G x Pu (KG 2 x Pu 2 ) 4Q 2 2 x KG Δp = pressure loss in bar Pu = absolute inlet pressure in bar Q = flow rate inlet Stm 3 /h KG = flow coefficient Pressure loss calculated as above is referred to natural gas with specific gravity of 0.61 (air=1) temperature of 15 C at valve inlet, for gases with different specific gravity S and temperatures t C, pressure loss can still be calculated with the above formula, replacing the value of the flow coefficent in the table with: KG1 = KG x S 175.8 x ( 273.16 + t ) Table 1: KG valve coefficient Nominal diameter (mm) Size (inches) KG coefficient 25 1" 510 50 2" 1970 65 2" 1/2 3550 3" 4390 100 4" 7120 150 6" 147 200 8" 230 250 10" 32506

SBC 782 > Slam shut valves Table 2 lists the correction factors Fc for a number of gases at 15 C. Table 2: Correction factors FC Type of gas Air Propane Butane Nitrogen Oxygen Carbon dioxide Relative density 1.0 1.53 2.0 0.97 1.14 1.52 Fc Factor 0.78 0.63 0.55 0.79 0.73 0.63 Caution: in order to get optimal performance, to avoid premature erosion phenomena and limit noise emissions, it is recommended to check that the gas speed at the outlet flange does not exceed 50 m/sec. The gas speed at the outlet flange may be calculated by means of the following formula: V Q = 345.92 x 2 DN where: V = gas speed in m/sec Q = gas flow rate in Stm3/h 1 0.002 x x 1 + Pd Pd DN = nominal size of regulator in mm Pd = outlet pressure in barg. Table 3: Pressure switches Type Overpressure range (OPSO). Underpressure range (UPSO). Press. in bar 101M 0,02 to 1 0,01 to 0,26 102M 0,2 to 5,5 0,04 to 0,8 103M 2 to 22 0,2 to 8 104M 7,5 to 45 1,6 to 18 105M 30 to 90 3 to 44 102MH 0,2 to 5,5 2,8 to 55 103MH 2 to 22 8 to 19 104MH 7,5 to 45 18 to 41 105MH 30 to 90 3 to 44 Installation To ensure proper operation and declared performance, the followings should be observed when installing the SBC782 slam shut valves: a) filtering: the gas flowing in the piping must be adequately filtered. It is also recommended that the piping upstream the regulator is clean and avoids impurities; b) sensing line: for correct operation, the sensing line nipple must be appropriately positioned. Between the valve and the downstream takeoff there must be a lenght of straight pipe four times the diameter of the outlet pipe; beyond the takeoff, there must be a further lenght of pipe twice the same diameter.

Overal dimensions in mm Size (mm) Inches S Ansi 150/PN 16 S Ansi 300 S Ansi 600 a b d e f g h H 25 1" 183 197 210 100 215 130 2 315 50 2 254 267 286 130 240 160 330 370 65 2 " 1/2 277 140 270 1 3 420 3 298 317 336 150 315 200 425 465 100 4 352 368 394 190 300 250 440 490 150 6 451 225 375 275 560 600 200 8 543 265 450 320 625 715 250 10 673 340 530 440 730 870 Weights in Kgf ANSI 150/PN16 ANSI 300 ANSI 600 21 22 23 37 40 42 45 Face to face dimensions S according to IEC 5343 and EN 334 51 54 57 79 154 255 430

Pietro Fiorentini S.p.A. via E.Fermi 8/10 I36057 Arcugnano (VI) Italy Tel. +39 0444 968.511 Fax. +39 0444 960.468 via Rosellini 1 I20124 Milano Italy Tel. +39 02 696.14.21 Fax. +39 02 688.04.57 www.fiorentini.com The data are not binding. We reserve the right to make eventual cheanges without prior notice. CTs512E May 2010