Emerson Type 92B Self Powered Control Valve Data Sheet
2015-03-30
: Emerson Emerson-Type-92B-Self-Powered-Control-Valve-Data-Sheet-681409 emerson-type-92b-self-powered-control-valve-data-sheet-681409 emerson pdf
Open the PDF directly: View PDF .
Page Count: 16
Download | |
Open PDF In Browser | View PDF |
Bulletin 71.2:92B September 2014 Type 92B Pressure Reducing Valve • Extended Diaphragm Service Life • Two-Path Control • Elevated Actuator • Resilient Seats • Bellows Stem Guide • Double Post Stem Guide W8264 • Standard ANSI Face-to-Face Life D101342X012 Figure 1. Type 92B Pressure Reducing Valve www.fisherregulators.com Bulletin 71.2:92B Introduction The Type 92B Pressure Reducing Valve is the standard steam valve for industry. The Type 92B is designed to provide decades of continuous service. It can withstand dirty operating environments while providing accurate and stable pressure control. The Type 92B is applied as a main Pressure Reducing Valve in industrial process heating applications such as heat exchangers, evaporators, digesters and reactors. Commercial applications include Pressure Reducing Valves for meter runs found in district energy systems, hot water heat exchangers, absorption chillers and boiler deaerator tanks. The Type 92B is rated for inlet pressure up to 300 psig / 20.7 bar and inlet temperatures to 600°F / 316°C. Maximum controlled outlet pressure is 250 psig / 17.2 bar. A large actuator and heavy main spring ensures high accuracy and stability over its entire steam flow range. A safety override pilot is available for the Type 92B pressure reducing valve. The Type 92B pilot is used in a series installation with the Type 6492HM safety override pilot installed on the upstream valve. The Type 6492HM safety override pilot senses pressure downstream of the second valve and prevents pressure from rising above safe operating pressure in the event the downstream valve fails. This system is approved by ASME B31.1-1989, 122.14.2.A and can replace an ASME safety valve when vent piping is not practical and upstream steam pressure does not exceed 400 psig / 27.6 bar. Local codes and standards may require approval by an appropriate authority prior to installation. Features • Extended Diaphragm Service Life—Two-ply construction and dual flex points increases cycle life compared to conventional designs. Stainless steel material ensures satisfactory operation at high steam temperatures. • Resilient Seats—Valve seats are individually lapped for tight shutoff. Beveled seats ensure easy in-line lapping. Plug and valve seats are constructed of hardened stainless steel which reduces wire drawing in wet steam applications. • Standard ANSI Face-to-Face—NPT, CL125 FF, CL150 RF, CL250 RF and CL300 RF end connections are ANSI standard face-to-face dimensions. The Type 92B main valve is also available with PN 16/25/40 RF end connections. • Bellows Stem Guide—Pilot bellows reduces sticking from scale build-up due to boiler carryover. • Elevated Actuator—Plugging from scale and rust is reduced as condensate will not pool in critical areas. • Two-Path Control—Downstream pressure registers under main valve and pilot diaphragms improving response time. • Double Post Stem Guide—Top and bottom seat guides with Inconel® bushings eliminate lateral plug instability and premature stem wear. W1322-3A Figure 2. Typical Type 92B Construct Inconel® is a mark owned by Special Metals Corporation. 2 Bulletin 71.2:92B pipe plug or tube fitting directly over orifice for ease of accessibility bleed orifice - easily cleaned with wire diaphragms and diaphragm plate diaphragms case guide bushing pilot spring case pilot pressure setting spring bellows and bellows retainer lower spring seat orifice check valve assembly pilot valve stem and plug valve plug and seat ring bottom flange valve stem guide pilot valve spring reducing valve spring tion 3 Bulletin 71.2:92B Specifications This section lists the specifications for the Type 92B Pressure Reducing Valve. The following information is stamped on the nameplate of Type 92B: Type Number, Maximum Outlet Pressure, Maximum Inlet Pressure and Maximum Temperature. Available Configurations Pilot-operated globe-style pressure reducing valve with post guiding and flow-to-close valve plug action. Body Sizes and End Connection Styles See Table 1 Body Ratings and Maximum Inlet Pressures(1) See Table 3 Minimum Differential Pressures Required for Full Stroke(1) 20 psig / 1.4 bar with Stainless steel spring; 10 psig / 0.69 bar with Inconel® spring Maximum Outlet (Casing) Pressure Cast iron: 150 psig / 10.3 bar or body rating limits, whichever is lower Steel/Stainless steel: 300 psig / 20.7 bar or body rating limits, whichever is lower Outlet Pressure Ranges(1) See Table 2 Flow Coefficients See Table 5 Flow Capacities See Table 6 Pressure Registration External Maximum Temperature Capabilities(1) See Table 3 Downstream Control Line Connections NPS 1 and 1-1/2 / DN 25 and 40: 1/4 NPT NPS 2 / DN 50: 3/8 NPT NPS 3 and 4 / DN 80 and 100: 1/2 NPT Approximate Weights See Table 7 Construction Materials Main Valve Body, Bottom Flange, Diaphragm Case and Diaphragm Plate: Cast iron, WCC Steel or CF8M Stainless steel Construction Materials (continued) Main Valve (continued) Bottom Flange Gasket: Cast iron: Composition; Steel/Stainless steel: Graphite Diaphragms: Stainless steel Valve Plug: 410 or 416 Stainless steel Seat Ring: 416 Stainless steel (standard), 316 Stainless steel (seal weld option) Valve Plug Guide Bushing: 17-4PH Stainless steel Spring: 17-7PH Stainless steel or Inconel® Bleed Orifice Fitting: 416 Stainless steel Pipe Fittings: Steel or Stainless steel Type 92B Pilot Mounting Parts Cast iron: Copper tubing and brass fittings Steel Body: Stainless steel tubing and corrosion resistant steel fittings Stainless steel Body: Stainless steel tubing and fittings ype 92B Pilot T Body and Spring Case: Cast iron, WCC steel, CF8M Stainless steel Diaphragm Plate Assembly: Aluminum, Steel and Stainless steel Diaphragm Gasket: Cast iron: Composition; Steel/Stainless steel: Graphite Diaphragm, Valve Guide, and Valve Spring: Stainless steel Valve Stem and Orifice: 416 Stainless steel Bellows and Bellows Retainer: Bronze (standard) or 321 Stainless steel (high temperature/Stainless steel pilot construction) Spring: Steel for standard spring and Stainless steel for high temperature spring Upper Spring Seat: Plated steel for standard construction and Stainless steel for high temperature spring Lower Spring Seat: Aluminum or Carbon steel Screen: 304 Stainless steel Check Valve Assembly: Stainless steel internal with copper housing or all Stainless steel 1. The pressure/temperature limits in this Bulletin or any applicable standard limitation should not be exceeded. Inconel® is a mark owned by Special Metals Corporation. 4 Bulletin 71.2:92B Table 1. Body Sizes and End Connection Styles END CONNECTION STYLES BODY SIZES, NPS / DN 1 / 25 Cast iron Body NPT 1-1/2 and 2 / 40 and 50 NPT, CL125 FF and CL250 RF NPT, SWE(1), CL150 RF, CL300 RF and PN 16/25/40 RF Steel and Stainless steel Body 3 and 4 / 80 and 100 CL125 FF and CL250 RF CL150 RF, CL300 RF, PN 16 RF and PN 25/40 RF 1. Available in steel bodies only. Table 2. Outlet Pressure Ranges PILOT TYPE OUTLET PRESSURE SPRING WIRE DIAMETER SPRING FREE LENGTH PART NUMBER COLOR CODE 63.5 66.5 62.0 1E395627022 1D7455T0012 1E395727192 Yellow Green Black 2.50 2.62 2.44 63.5 66.5 62.0 1E395627022 1D7455T0012 1E395727192 Yellow Green Black 2.50 2.50 63.5 63.5 14B9943X012 14B9942X022 Unpainted Unpainted psig bar In. mm In. mm Low-Pressure 2 to 6 5 to 15 13 to 25 0.14 to 0.41 0.34 to 1.0 0.90 to 1.7 0.207 0.234 0.283 5.26 5.94 7.19 2.50 2.62 2.44 High-Pressure 15 to 30 25 to 75 70 to 150 1.0 to 2.1 1.7 to 5.2 4.8 to 10.3 0.207 0.234 0.281 5.26 5.94 7.14 High Temperature 15 to 100 80 to 250 1.0 to 6.9 5.5 to 17.2 0.282 0.375 7.16 9.53 Table 3. Maximum Inlet Pressures and Temperatures BODY MATERIAL MAXIMUM TEMPERATURE psig bar °F °C NPT 250 17.2 406 208 CL125 FF 125 8.6 353 178 CL250 RF 250 17.2 406 208 NPT 300 20.7 450 232 SWE 300 20.7 450 232 CL150 RF 185 12.8 450 232 CL300 RF 300 20.7 600 316(1) PN 16/25/40 RF (NPS 1, 1-1/2, 2 and 3 / DN 25, 40, 50 and 80) 300 20.7 600 316(1) PN 16 RF (NPS 4 / DN 100) 185 12.8 450 232 PN 25/40 RF (NPS 4 / DN 100) 300 20.7 600 316(1) 232 Cast iron Steel Stainless steel MAXIMUM INLET PRESSURE END CONNECTION NPT 300 20.7 450 CL150 RF 175 12.1 450 232 CL300 RF 300 20.7 600 316(1) PN 16/25/40 RF (NPS 1, 1-1/2, 2 and 3 / DN 25, 40, 50 and 80) 300 20.7 600 316(1) PN 16 RF (NPS 4 / DN 100) 175 12.1 450 232 PN 25/40 RF (NPS 4 / DN 100) 300 20.7 600 316(1) 1. 450°F / 232°C with standard seat ring, 600°F / 316°C with seal weld option. Table 4. Minimum Differential Pressures for Safety Override System TYPE 6492HM 6492HTM SPRING RANGE SPRING COLOR MINIMUM PRESSURE AT WHICH MONITORING PILOT CAN BE SET psig bar 10 to 30 0.69 to 2.1 Yellow 10 psig / 0.69 bar over normal downstream pressure 25 to 75 1.7 to 5.2 Green 10 psig / 0.69 bar over normal downstream pressure 70 to 150 4.8 to 10.3 Black 15 psig / 1.0 bar over normal downstream pressure 15 to 100 1.0 to 6.9 Unpainted 10 psig / 0.69 bar over normal downstream pressure 80 to 250 5.5 to 17.2 Unpainted 25 psig / 1.7 bar over normal downstream pressure 5 Bulletin 71.2:92B CONTROL LINE PILOT SPRING ORIFICE PILOT CONTROL LINE MAIN VALVE DIAPHRAGM PILOT DIAPHRAGM PILOT VALVE PLUG VALVE PLUG MAIN VALVE SPRING PILOT SUPPLY LINE E0672 INLET PRESSURE OUTLET PRESSURE ATMOSPHERIC PRESSURE LOADING PRESSURE Figure 3. Type 92B Operational Schematic Principle of Operation Refer to Figure 3. Compression of the pilot spring pushes diaphragm down and holds pilot valve plug open. Outlet pressure is changed by varying the amount of pilot spring compression. When steam enters the inlet of the valve, it also enters the pilot supply line and flows through the open pilot valve to the top of the main diaphragm. The force created by this steam pressure on the diaphragm overcomes the force of the main valve spring opening the valve plug and allowing steam to flow downstream. Downstream pressure registers under the main diaphragm through the control line and tends to balance the diaphragm. Steam from the downstream system also registers under the pilot diaphragm through line. Pressure forces the diaphragm upward, permitting the pilot valve plug to move toward the closed position. Flow of steam to the top of the main diaphragm is thereby reduced and the pressure on main diaphragm drops due to the bleed through the orifice. The main valve moves toward the closed position, allowing only enough steam flow to satisfy downstream requirements. 6 When steam demand increases, the downstream pressure decreases below the setting of the pilot spring. The pilot opens to increase the pressure on the main diaphragm. The main valve opens to increase the flow downstream. Conversely, if the steam demand decreases, the downstream pressure increases and the pilot reacts to decrease the pressure on top of the main diaphragm. The main valve throttles toward the closed position and the steam flow decreases. Thus, through the combination of pilot and main valve operation, control of the downstream steam pressure is maintained. An internal check valve is included in all Type 92B pilots to limit differential pressure on the main valve diaphragm. In the event of a large decrease in downstream pressure, the check valve opens to relieve diaphragm loading pressure to the downstream system. The check valve cartridge assembly has a factory setting to limit differential pressure across the diaphragm to approximately 40 psid / 2.8 bar d. If diaphragm differential pressure reaches approximately 40 psid / 2.8 bar d, the check valve opens to relieve diaphragm loading pressure into the downstream Bulletin 71.2:92B TYPE 92B PILOT (B) TYPE 92B MAIN VALVE TYPE 92B PILOT (C) TYPE 92B MAIN VALVE TYPE 6492HM SAFETY OVERRIDE PILOT (A) E0794 INLET PRESSURE OUTLET PRESSURE ATMOSPHERIC PRESSURE LOADING PRESSURE INTERMEDIATE PRESSURE Figure 4. Safety Override System Schematic system, thereby preventing a high differential across the diaphragm which might otherwise cause diaphragm damage. The check valve closes and normal operation resumes when the differential pressure across the diaphragm is reduced to the proper level. Safety Override System Refer to Figure 4. Once placed in operation, the upstream Type 92B pilot (B) senses the intermediate pressure between both valves and the Type 6492HM (A) pilot senses pressure downstream of the second valve. As demand for flow increases, intermediate pressure will fall causing the Type 92B pilot to open. As the Type 92B pilot opens, loading pressure to the main valve increases, opening the main valve. The Type 6492HM (A) safety override pilot remains open because its setpoint is above the setpoint of the downstream valve. In the unlikely event that the downstream valve fails open, downstream pressure will rise above the downstream valve’s setpoint. This pressure is sensed by the Type 6492HM (A) safety override pilot. As downstream pressure increases the Type 6492HM (A) safety override pilot closes, reducing loading pressure to the upstream main valve, which positions the main valve to maintain desired downstream override pressure. In the event that the upstream valve fails, the downstream valve will prevent downstream pressure from rising above safe operating levels. It is recommended to install some type of warning system, such as a sentinel relief valve, to warn the operator that a valve has failed in the system. This will prevent prolonged operation with one valve, which could cause valve trim wear and noise associated with operation at high differential pressures. 7 Bulletin 71.2:92B Installation Installation of the Type 92B is dependent on the application. As a minimum, a typical steam pressure reducing station must include a 3-valve bypass, inlet drip leg, inlet strainer (and steam separator if required) and relief valve per ASME Section VIII code. A safety override pressure reducing station can be installed in the event a relief valve is not practical as per ASME B16.122.14 standards, subject to local codes and regulations. Positioning and Mounting The Type 92B regulators are intended to be installed with their diaphragm case above the pipeline so that condensate will not collect in the cases. In order to obtain the performance given in this bulletin, connect the downstream end of the control line into a straight run of pipe. The connection should be located at least 6 pipe diameters from the valve body outlet in an unswaged pipeline or 10 pipe diameters from the swage in a swaged pipeline. The Type 92B pilot should also be installed with the adjusting screw pointing up and the control line should be sloped with a downward pitch to ensure drainage of condensate. The body should be installed so the flow is in the same direction as the arrow on the body. Note that the Type 92B pilot may be installed on either side of the body. Overpressure Protection and Relief Valve Sizing Overpressure protection is required when piping and components downstream of a steam regulating valve have a maximum allowable working pressure (MAWP) that is lower than the upstream supply pressure to the regulating valve. In some cases, the regulating valve itself may have a lower outlet pressure rating than its inlet pressure rating, which will require overpressure protection. 8 Governing codes and standards define the type and design of overpressure protection. When full flow relief valves are specified, they must relieve a maximum specified flow at a pressure not to exceed that specified by applicable codes. In North America, the governing code for most steam regulating valve installations is ASME Boiler Code, Section VIII, which may be amended by local codes or variances. The issue in sizing stream relief valves is quantifying its maximum flow rate. Maximum flow conditions may occur under many conditions, so the entire steam system must be analyzed to make sure the maximum relief valve flow is accurate. Failure to do so may cause overpressure. In applications where it is determined that the steam regulating valve creates maximum flow to the relief valve, several issues must be resolved prior to quantifying the flow to the relief valve. 1. There must be general agreement on the failure mode of the regulating valve. The Emerson Process Management Regulator Technologies, Inc. (Emerson™) provides wide-open regulating coefficients to assist with sizing steam relief valves. The coefficients assume that the valve plug is at maximum travel and still in its normal orientation. Contact your local Sales Office prior to relief valve sizing in the event that there is disagreement with the mode of failure. 2. Maximum steam flow must be calculated at the pressure obtained at the relief valve’s full-open condition. This pressure is typically larger than a relief valve’s set pressure. This pressure must be used as the outlet pressure of the steam regulating valve when calculating the maximum flow through the regulating valve. 3. Maximum steam flow should be calculated from the manufacturer’s recommended procedure. The Emerson recommends using either the Fisher® steam sizing equation or IEC sizing procedure. Bulletin 71.2:92B BLOCK VALVE INITIAL PRESSURE GAUGE REDUCED PRESSURE GAUGE SENSING LINE BLOCK VALVE BLOCK VALVE TYPE 92B STRAINER TRAP E0706 TYPE 92B SINGLE-STAGE INSTALLATION REDUCED PRESSURE GAUGE BLOCK VALVE BLOCK VALVE INITIAL PRESSURE GAUGE SENSING LINE STRAINER REDUCED PRESSURE GAUGE BLOCK VALVE TRAP BLOCK VALVE TYPE 92B SENSING LINE STRAINER BLOCK VALVE TYPE 92B TRAP E0707 TYPE 92B SINGLE-STAGE PARALLEL INSTALLATION BLOCK VALVE INITIAL PRESSURE GAUGE BLOCK VALVE INTERMEDIATE PRESSURE GAUGE BLOCK VALVE REDUCED PRESSURE GAUGE SENSING LINE SENSING LINE BLOCK VALVE TRAP STRAINER PRIMARY TYPE 92B BLOCK VALVE TRAP SECONDARY TYPE 92B E0708 TYPE 92B TWO-STAGE INSTALLATION Figure 5. Type 92B Typical Installations 9 Bulletin 71.2:92B TYPE 92B MAIN VALVE TYPE 6492HM SAFETY OVERRIDE PILOT TYPE 92B MAIN VALVE TYPE 92B PILOT TYPE 92B PILOT Top View TYPE 92B MAIN VALVE TYPE 92B MAIN VALVE TYPE 92B PILOT TYPE 92B PILOT TYPE 6492HM SAFETY OVERRIDE PILOT Side View Figure 6. Safety Override System Installation Example: Example Calculation: RELIEF VALVE SET: 15 psig / 1.0 bar FULL OPEN: 25 psig / 1.7 bar Qmax(lb/hr) = 10 psig / 0.69 bar 100 psig / 6.9 bar, 338°F / 170°C relief valve where: Determine the maximum valve flow capacity at wide-open failure. CSP1 1 + 0.00065 Tsh SIN 3417 ΔP C1 P1 CS = 74 ΔP = 75 psia / 5.2 bar C1 = 35 Tsh = 0°F P1 = 114.7 psia / 7.9 bar DEG where: Q = Steam flow rate, lb/hr P1 = Absolute inlet pressure, psia (P1 gauge + 14.7) Cs = Wide-open gas sizing coefficient, see Table 5 C1 = Flow coefficient, see Table 5 Tsh = Degrees of steam superheat at inlet, °F ΔP = Pressure drop across regulator, psia 10 75 DEG 114.7 Qmax = 8,330 lb/hr / 3778 kg/hr NPS 2 / DN 50 TYPE 92B Qmax(lb/hr) = 74 x 114.7 3417 SIN 1 + 0.00065 x 0 35 Bulletin 71.2:92B Table 5. Main Valve Coefficients FLOW COEFFICIENTS BODY SIZE Regulating Coefficients IEC SIZING COEFFICIENTS Wide-Open Coefficients C1 Km NPS DN Cg Cs Cv Cg Cs Cv 1 1-1/2 25 40 330 560 16.5 28 9.4 16 480 921 24 46 13.7 26.3 35 35 2 3 4 50 80 100 960 2000 2700 48 100 135 27.4 57.1 77.1 1481 3042 4515 74 152 225 42.3 86.9 129 35 35 35 FL XT FD 0.80 0.80 0.89 0.89 0.78 0.78 0.24 0.25 0.80 0.80 0.80 0.89 0.89 0.89 0.78 0.78 0.78 0.28 0.26 0.20 Table 6. Capacities(1) INLET PRESSURE OUTLET PRESSURE psig bar psig bar 25 1.7 5 10 15 0.34 0.69 1.0 660 600 525 299 272 238 1060 1080 935 481 490 424 2060 2080 1860 934 943 844 3800 3850 3260 1724 1746 1479 4940 5000 4520 2241 2268 2050 3.4 5 10 20 30 40 0.34 0.69 1.4 2.1 2.8 1080 1080 1080 928 710 490 490 490 421 322 1830 1890 1860 1760 1660 830 857 844 798 753 3300 3390 3290 2940 2590 1497 1538 1492 1334 1175 6500 6650 6500 5740 4980 2948 3016 2948 2604 2259 8960 9110 8810 7730 6650 4064 4132 3996 3506 3016 5 10 20 0.34 0.69 1.4 1500 1500 1500 680 680 680 2510 2620 2720 1138 1188 1234 4610 4700 4770 2091 2132 2164 9080 9180 9290 4119 4164 4214 10,900 11,200 11,300 4944 5080 5126 30 40 50 60 2.1 2.8 3.4 4.1 1470 1380 1240 1020 667 626 562 463 2680 2640 2380 2120 1216 1198 1080 962 4680 4590 4370 4160 2123 2082 1982 1887 8880 8470 7680 6900 4028 3842 3484 3130 10,800 10,200 9240 8280 4899 4627 4191 3756 5 10 20 0.34 0.69 1.4 1900 1920 1920 862 871 871 3400 3440 3460 1542 1560 1569 5710 5870 5900 2590 2663 2676 11,500 11,700 11,800 5216 5307 5352 16,100 16,400 16,400 7303 7439 7439 40 60 80 2.8 4.1 5.5 1920 1700 1330 871 771 603 3500 3330 2860 1588 1510 1297 5930 5650 4960 2690 2563 2250 11,800 11,000 9670 5352 4990 4386 16,500 15,200 13,000 7484 6895 5897 5 10 20 0.34 0.69 1.4 2310 2340 2340 1048 1061 1061 4140 4170 4230 1878 1892 1919 6950 7010 7080 3152 3180 3211 13,900 14,100 14,100 6305 6396 6396 19,600 19,800 19,800 8890 8981 8981 40 60 80 100 2.8 4.1 5.5 6.9 2340 2340 2100 1630 1061 1061 952 739 4280 4400 4100 3250 1941 1996 1860 1474 7080 7250 6750 5400 3211 3289 3062 2449 14,200 14,400 13,700 11,300 6441 6532 6214 5126 19,800 19,800 18,500 15,600 8981 8981 8392 7076 20 40 60 1.4 2.8 4.1 2770 2770 2770 1256 1256 1256 5000 5070 5110 2268 2300 2318 8220 8260 8300 3728 3747 3765 16,700 16,700 16,800 7575 7575 7620 23,600 23,700 23,800 10,705 10,750 10,796 80 100 120 5.5 6.9 8.3 2770 2360 1950 1256 1070 884 4980 4600 4090 2259 2086 1855 8130 7740 7070 3688 3511 3207 15,900 15,200 13,700 7212 6895 6214 23,500 21,700 18,600 10,660 9843 8437 20 40 60 1.4 2.8 4.1 3610 3610 3610 1637 1637 1637 6480 6500 6520 2939 2948 2957 10,700 10,800 10,900 4854 4899 4944 21,900 21,900 22,000 9934 9934 9979 29,500 31,000 31,200 13,381 14,062 14,152 80 100 120 150 5.5 6.9 8.3 10.3 3610 3610 3280 2790 1637 1637 1488 1266 6550 6250 6300 6070 2971 2835 2858 2753 11,000 10,700 10,500 10,200 4990 4854 4763 4628 22,500 21,700 20,700 19,700 10,206 9843 9390 8936 31,300 30,700 29,700 28,300 14,198 13,926 13,472 12,837 50 75 100 125 150 200 5.2 6.9 8.6 10.3 13.8 CAPACITIES IN lb/h / kg/h OF SATURATED STEAM (BASED ON 10 PERCENT DROOP) Body Size NPS 1 / DN 25 NPS 1-1/2 / DN 40 NPS 2 / DN 50 NPS 3 / DN 80 NPS 4 / DN 100 1. Printed capacities are for the Type 92B with electropneumatic loading system. 11 Bulletin 71.2:92B Table 6. Capacities(1) (continued) INLET PRESSURE OUTLET PRESSURE psig psig bar 20 40 60 1.4 2.8 4.1 4460 4460 4460 2023 2023 2023 7850 7920 8100 3561 3592 3674 13,000 13,200 13,300 5897 5988 6033 27,200 27,300 27,300 12,338 12,383 12,383 37,300 37,800 38,500 16,919 17,146 17,464 80 100 120 150 5.5 6.9 8.3 10.3 4460 4460 4160 4050 2023 2023 1887 1837 8130 8150 7860 6780 3688 3697 3565 3075 13,400 13,400 12,700 11,500 6078 6078 5761 5216 27,400 27,500 26,300 23,000 12,429 12,474 11,930 10,433 38,700 38,800 37,000 31,000 17,554 17,600 16,783 14,062 20 40 60 1.4 2.8 4.1 5190 5190 5180 2354 2354 2350 8810 8810 8790 3996 3996 3987 15,100 15,100 15,000 6849 6849 6804 31,400 31,400 31,400 14,243 14,243 14,243 42,400 42,400 42,300 19,234 19,234 19,187 80 100 120 150 5.5 6.9 8.3 10.3 5150 5110 5040 4900 2336 2318 2286 2223 8740 8670 8550 8310 3964 3933 3878 3769 14,900 14,800 14,600 14,200 6759 6713 6623 6441 31,200 30,900 30,500 29,700 14,152 14,016 13,835 13,472 42,100 41,800 41,200 40,000 19,096 18,960 18,688 18,144 175 200 250 12.1 13.8 17.2 4730 4510 3830 2146 2046 1737 8030 7650 6510 3642 3470 2953 13,700 13,100 11,100 6214 5942 5035 28,600 27,300 23,200 12,973 12,383 10,524 38,700 36,800 31,400 17,554 16,692 14,243 250 300 bar 17.2 21.0 CAPACITIES IN lb/h / kg/h OF SATURATED STEAM (BASED ON 10 PERCENT DROOP) Body Size NPS 1 / DN 25 NPS 1-1/2 / DN 40 NPS 2 / DN 50 NPS 3 / DN 80 NPS 4 / DN 100 1. Printed capacities are for the Type 92B with electropneumatic loading system. Table 7. Approximate Weights BODY MATERIAL Cast iron Steel or Stainless steel 1. Add 5 lbs / 2 kg for low-pressure pilot. 12 APPROXIMATE WEIGHTS WITH HIGH-PRESSURE PILOT(1) BODY SIZE END CONNECTION STYLES NPS DN lbs kg NPT 1 1-1/2 2 25 40 50 55 73 105 25 33 48 CL125 FF 1-1/2 2 3 4 40 50 80 100 77 110 175 243 35 50 79 110 CL250 RF 1-1/2 2 3 4 40 50 80 100 83 115 190 263 38 52 86 119 NPT 1 1-1/2 2 25 40 50 65 89 122 29 40 55 CL150 RF, PN 16 RF 1 1-1/2 2 3 4 25 40 50 80 100 77 95 132 220 285 35 43 60 100 129 CL300 RF, PN 16/25/40 RF, PN 25/40 RF 1 1-1/2 2 3 4 25 40 50 80 100 82 102 137 225 305 37 46 62 102 138 Bulletin 71.2:92B F - DOWNSTREAM CONTROL LINE CONNECTION, NPT c e n g l 1/2 A A npt F - DOWNSTREAM CONTROL LINE CONNECTION, NPT c E n g l b A flanged Figure 7. Dimensions Table 8. Dimensions DIMENSIONS BODY SIZE A NPT NPS DN L CL125 FF(1) and CL150 RF CL250 RF(1) and CL300 RF PN 16 RF C PN 25/40 RF E G F NPT In. mm In. mm In. mm In. mm In. mm In. mm In. mm N In. mm In. 1 1-1/2 2 25 40 50 6.50 8.00 9.25 165 203 235 7.25 8.75 10.00 184 222 254 7.75 9.25 10.50 197 235 267 7.75 9.06 10.25 197 230 260 7.75 9.06 10.25 197 230 260 9.25 10.38 11.88 235 264 302 6.81 7.00 7.75 173 178 197 1/4 1/4 3/8 3.25 3.81 4.12 82.6 96.8 105 2.81 3.94 3.91 3 4 80 100 ------- ------- 11.75 13.88 298 353 12.50 14.50 317 368 11.81 13.56 300 344 12.21 13.88 310 353 13.88 14.88 353 378 8.94 10.12 227 257 1/2 1/2 5.19 6.44 132 164 5.50 6.38 mm LowPressure Pilot HighPressure/ High Temp Pilot In. mm In. mm 260 272 286 8.38 8.81 9.38 213 224 238 308 333 10.25 11.25 260 286 71.4 10.25 100(2) 10.69 99.3 11.25 140 162 12.12 13.12 1. Cast iron flanges are not available for the NPS 1 / DN 25 body. 2. 3.44 in. / 87 mm NPT bodies. 13 Bulletin 71.2:92B Ordering Guide Inlet Steam Conditions (Select One) Steel ≤ 125 psig / 8.6 bar; 353°F / 178°C ≤ 175 psig / 12.1 bar; 450°F / 232°C CL150 RF Flanged ≤ 185 psig / 12.8 bar; 450°F / 232°C CL300 RF Flanged ≤ 250 psig / 17.2 bar; 406°F / 208°C ≤ 300 psig / 20.7 bar; 450°F / 232°C ≤ 300 psig / 20.7 bar; 600°F / 316°C Main Valve Body Size and Material (Select One) Cast Iron NPS 1 / DN 25 NPT (NPS 1, 1-1/2 and 2) PN 16/25/40 RF (NPS 1, 1-1/2, 2 and 3 / DN 25, 40, 50 and 80) PN 16 RF (NPS 4 / DN 100) PN 25/40 RF (NPS 4 / DN 100) Stainless steel NPT (NPS 1, 1-1/2 and 2) CL150 RF Flanged NPS 1-1/2 / DN 40 CL300 RF Flanged NPS 2 / DN 50 NPS 3 / DN 80 NPS 4 / DN 100 Steel NPS 1 / DN 25 PN 16/25/40 RF (NPS 1, 1-1/2, 2 and 3 / DN 25, 40, 50 and 80) PN 16 RF (NPS 4 / DN 100) PN 25/40 RF (NPS 4 / DN 100) Main Valve Spring (Select One) 17-7PH Stainless steel (standard)*** NPS 1-1/2 / DN 40 NPS 2 / DN 50 Inconel® (optional)** NPS 3 / DN 80 Pilot Material (Select One) NPS 4 / DN 100 Stainless steel NPS 1 / DN 25 NPS 1-1/2 / DN 40 NPS 2 / DN 50 NPS 3 / DN 80 NPS 4 / DN 100 Cast iron Steel Stainless steel Pilot Type and Spring Range (Select One) High-Pressure 15 to 30 psig / 1.0 to 2.1 bar, Yellow 25 to 75 psig / 1.7 to 5.2 bar, Green End Connection Style (Select One) 70 to 150 psig / 4.8 to 10.3 bar, Black Cast Iron Low-Pressure NPT (NPS 1, 1-1/2 and 2) CL125 FF Flanged (NPS 1-1/2, 2, 3 and / DN 40, 50, 80 and 100) 2 to 6 psig / 0.14 to 0.41 bar, Yellow 5 to 15 psig / 0.34 to 1.0 bar, Green 13 to 25 psig / 0.90 to 1.7 bar, Black CL250 RF Flanged (NPS 1-1/2, 2, 3 and 4 / DN 40, 50, 80 and 100) - continued Inconel is a mark owned by Special Metals Corporation. ® 14 Bulletin 71.2:92B Ordering Guide (continued) High Temperature Type 6492HTM Pilot Spring Range 15 to 100 psig / 1.0 to 6.9 bar, Unpainted 15 to 100 psig / 1.0 to 6.9 bar, Unpainted 80 to 250 psig / 5.5 to 17.2 bar, Unpainted 80 to 250 psig / 5.5 to 17.2 bar, Unpainted Pilot Mounting Position (Select One) Main Valve Replacement Parts Kit (Optional) Facing inlet side of main valve with diaphragm case up, pilot is mounted: On left side with pilot adjusting screw pointed up Yes, send one main valve replacement parts kit to match this order. Replacement Pilot (Optional) On right side with pilot adjusting screw pointed up Yes, send one replacement pilot to match this order. Options (Select One) Pilot Replacement Parts Kit (Optional) Standard Adjusting Screw Sealed Adjusting Screw Yes, send one pilot replacement parts kit to match this order. Handwheel Safety Override System (Optional) Type 6492HM Pilot Spring Range 10 to 30 psig / 0.69 to 2.1 bar, Yellow 25 to 75 psig / 1.7 to 5.2 bar, Green 70 to 150 psig / 4.8 to 10.3 bar, Black Steam Specification Worksheet Application: Tag Number: Valve Type: Direct-Operated Pilot-Operated Pressure Loaded Differential Iron Stainless steel Body Material: Steel Inlet/Outlet End Connection Style: CL150 RF Flange CL125 FF Flange CL250 RF Flange CL300 RF Flange PN 16/25/40 RF NPT Inlet/Outlet Pipe Size: Regulators Quick Order Guide *** ** * Readily Available for Shipment Allow Additional Time for Shipment Special Order, Constructed from Non-Stocked Parts. Consult your local Sales Office for Availability. Availability of the product being ordered is determined by the component with the longest shipping time for the requested construction. Steam Conditions: Inlet Pressure (psig / bar) Inlet Temperature (°F / °C) Outlet Pressure (psig / bar) Maximum In. / mm Normal Minimum Flow (lb/h or kg/h) Performance Required: Accuracy Requirements: ≤ 10% ≤ 20% ≤ 30% ≤ 40% 15 Bulletin 71.2:92B Industrial Regulators Natural Gas Technologies TESCOM Emerson Process Management Regulator Technologies, Inc. Emerson Process Management Regulator Technologies, Inc. Emerson Process Management Tescom Corporation USA - Headquarters McKinney, Texas 75070 USA Tel: +1 800 558 5853 Outside U.S. +1 972 548 3574 USA - Headquarters McKinney, Texas 75070 USA Tel: +1 800 558 5853 Outside U.S. +1 972 548 3574 USA - Headquarters Elk River, Minnesota 55330-2445, USA Tels: +1 763 241 3238 +1 800 447 1250 Asia-Pacific Shanghai 201206, China Tel: +86 21 2892 9000 Asia-Pacific Singapore 128461, Singapore Tel: +65 6770 8337 Europe Selmsdorf 23923, Germany Tel: +49 38823 31 287 Europe Bologna 40013, Italy Tel: +39 051 419 0611 Europe Bologna 40013, Italy Tel: +39 051 419 0611 Chartres 28008, France Tel: +33 2 37 33 47 00 Asia-Pacific Shanghai 201206, China Tel: +86 21 2892 9499 Middle East and Africa Dubai, United Arab Emirates Tel: +971 4811 8100 Middle East and Africa Dubai, United Arab Emirates Tel: +971 4811 8100 For further information visit www.fisherregulators.com The Emerson logo is a trademark and service mark of Emerson Electric Co. All other marks are the property of their prospective owners. Fisher is a mark owned by Fisher Controls International LLC, a business of Emerson Process Management. The contents of this publication are presented for informational purposes only, and while every effort has been made to ensure their accuracy, they are not to be construed as warranties or guarantees, express or implied, regarding the products or services described herein or their use or applicability. We reserve the right to modify or improve the designs or specifications of such products at any time without notice. Emerson Process Management Regulator Technologies, Inc. does not assume responsibility for the selection, use or maintenance of any product. Responsibility for proper selection, use and maintenance of any Emerson Process Management Regulator Technologies, Inc. product remains solely with the purchaser. ©Emerson Process Management Regulator Technologies, Inc., 1980, 2014; All Rights Reserved
Source Exif Data:
File Type : PDF File Type Extension : pdf MIME Type : application/pdf PDF Version : 1.4 Linearized : Yes XMP Toolkit : Adobe XMP Core 5.3-c011 66.145661, 2012/02/06-14:56:27 Create Date : 2014:09:17 21:12:34+08:00 Metadata Date : 2014:09:17 21:12:40+08:00 Modify Date : 2014:09:17 21:12:40+08:00 Creator Tool : Adobe InDesign CS6 (Windows) Instance ID : uuid:3b0940d4-2845-4e5f-a63d-6ddf8da172a1 Original Document ID : adobe:docid:indd:5bae2888-cb05-11df-af5e-bd741ad5fc2a Document ID : xmp.id:F48E32316C3EE4118FA4C4C6299FEF86 Rendition Class : proof:pdf Derived From Instance ID : xmp.iid:F38E32316C3EE4118FA4C4C6299FEF86 Derived From Document ID : xmp.did:22B44474A5DAE3119DA6EFB44156A7E2 Derived From Original Document ID: adobe:docid:indd:5bae2888-cb05-11df-af5e-bd741ad5fc2a Derived From Rendition Class : default History Action : converted History Parameters : from application/x-indesign to application/pdf History Software Agent : Adobe InDesign CS6 (Windows) History Changed : / History When : 2014:09:17 21:12:34+08:00 Format : application/pdf Producer : Adobe PDF Library 10.0.1 Trapped : False Page Count : 16 Creator : Adobe InDesign CS6 (Windows)EXIF Metadata provided by EXIF.tools