model gp10f cast steel carbon steel
Transkript
SDS U2404-08 MODEL GP10F CAST STEEL CARBON STEEL MECHANICAL PUMP WITH RETROFITTABLE MECHANISM FOR CONDENSATE REMOVAL AND RECOVERY Features Pump for a wide range of applications. Ideal for condensate removal from vented receivers and sump drainage. 1. Handles high-temperature condensate without cavitation. 2. No electric power or additional level controls required, hence INTRINSICALLY SAFE. 3. Pump will operate with a low filling head. 4. Durable nickel-based alloy compression coil spring. 5. All internal parts are suspended from the trap cover and can be removed upward in one piece. 6. High quality stainless steel internals and hardened working surfaces ensure reliability. Patented Specifications Model GP10F Flanged DIN 2501 PN 40* Screwed BSP DIN 2999* DN 80 × DN 50 3 ⁄4” 1” 10.5 220 0.3 – 10.5 0.5 bar less than motive medium pressure used approximately 30 Saturated Steam, Compressed Air, Nitrogen Steam Condensate, Water Pumped Medium Inlet & Outlet Connection Motive Medium & Pump Exhaust Pumped Medium: Inlet × Outlet Size Motive Medium Inlet Pump Exhaust Outlet PMO Maximum Operating Pressure (barg) TMO Maximum Operating Temperature (°C) Motive Medium Pressure Range (barg) Maximum Allowable Back Pressure Volume of Each Discharge Cycle (ℓ) Motive Medium** Pumped Medium*** * Other standards available ** Do not use with toxic, flammable or otherwise hazardous fluids. *** Do not use for fluids with specific gravities under 0.85 or over 1, or for toxic, flammable or otherwise hazardous fluids. PRESSURE SHELL DESIGN CONDITIONS (NOT OPERATING CONDITIONS): Maximum Allowable Pressure (barg) PMA: 10.5 Maximum Allowable Temperature (°C) TMA: 220 CAUTION No. Description ① Body ② Cover ③ Cover Gasket ④ ⑤ ⑥ ⑦ To avoid abnormal operation, accidents or serious injury, DO NOT use this product outside of the specification range. Local regulations may restrict the use of this product to below the conditions quoted. DIN1) Material 2) Carbon Steel HII Cast Steel A216 Gr.WCB 2) Fluorine Resin PTFE Stainless Steel Float SUS316L/SUS304 Stainless Steel Snap-action Unit Stainless Steel SUS440C/ Motive Medium Intake SUS303 Valve Intake Valve Unit Valve Seat Stainless Steel SUS440C Stainless Steel SUS440C/ Exhaust Exhaust Valve Valve SUS303 Unit Valve Seat Stainless Steel SUS420F Carbon Steel S25C Drain Plug Carbon Steel C22.8 Flange Assembly 3) 4) Check Valve 4) CKF3MG Stainless Steel A351 Gr.CF8 ⑧ ⑨ ⑩ 1) Equivalent materials 2) Option: Stainless Steel 3) Consisting of bolts, nuts, butt-weld flange, gaskets 4) ASTM/AISI1) 1.0425 1.1811 PTFE 1.4404/ 1.4301 — 1.4125/ 1.4305 1.4125 1.4125/ 1.4305 A415 Gr.60 — PTFE AISI316L/ AISI304 — AISI440C/ AISI303 AISI440C AISI440C AISI303/ 1.4028 1.1158 1.0460 1.4312 AISI420F AISI1025 A105 — Shown on reverse 1 bar = 0.1 MPa Dimensions ¡GP10F H3 GP10F Motive Medium Inlet 3/4” BSP Flanged* (mm) L H H1 H2 H3 L1 L2 L3 810 782 230 512 40 600 115 95 φW Weight (kg) 400 82 * DIN 2501 PN 40, threaded connections: DIN 2999 female, other standards available Plug 1/2” BSP H H2 Pump Exhaust Outlet 1” BSP H1 L2 L1 L Pumped Medium Outlet DN 50 PN 40 Pumped Medium Inlet DN 80 PN 40 CKF3MG flangeless Check Valve DN 80 L3 CKF3MG flangeless Check Valve DN 50 W Discharge Capacity ¡Correction Factor CKF3MG DN 80 check valve at inlet, DN 50 at outlet, filling head 1070 mm For GP10F with check valve CKF3MG, installed with filling head other than 1070 mm (minimum filling head: 860 mm) 9 1700 Motive Medium: Saturated Steam Motive Steam Pressure: barg Condensate Temperature: 90 °C 8 7 1600 6 5 4 3 1.5 2 2 4 3 6 8 1 0 0 1 2 3 4 5 6 7 10 8 Filling Head (mm) Discharge Capacity (t/h) 10 9 1500 1400 1300 1200 1100 1070 1000 Discharge Capacity (t/h) 10 900 860 0.7 9 Motive Medium: Compressed Air Motive Air Pressure: barg Condensate Temperature: 20 °C 8 7 1.0 1.2 ¡Illustration of Filling Head and Pressures 6 5 4 Condensate Receiver 1.5 3 2 2 4 3 6 10 8 Pm 1 0 0 1 2 3 4 5 6 7 8 9 Filling Head P2 1 bar = 0.1 MPa System Back Pressure (barg) NOTE: ¡ To achieve the above capacities with the standard GP10F configuration, TLV CKF3MG check valves (supplied with the GP10F) must be used at the pumped medium inlet and outlet. ¡ Motive medium pressure minus back pressure must be greater than 0.5 bar. ¡In closed system applications, the motive medium must be compatible with the liquid being pumped. If a non-condensible gas such as air or nitrogen is used as the motive medium, consult TLV for assistance. ¡A strainer must be installed at the motive medium and pumped medium inlets. GP10F ¡The Discharge Capacity is determined by the motive medium, motive medium pressure (Pm) and back pressure (P2). Make sure that: Discharge Capacity ×correction factor > required flow rate SDS U2404-08 Size of Receiver / Reservoir The receiver/reservoir must have a capacity sufficient to store the condensate produced during the PowerTrap operation and discharge. A receiver will generally be larger than a reservoir because it must handle the condensate both as a liquid and as flash steam, and separate one from the other so that only condensate is sent to the PowerTrap. ① Size of Receiver (flash steam is involved) (Length: 1 m) Flash steam up to kg/h 25 50 75 100 150 200 300 400 500 700 800 1000 1100 1400 1500 Receiver diameter mm 80 100 125 150 200 200 250 300 350 400 450 500 500 550 600 ② Size of Reservoir (flash steam is not involved) Amount of condensate kg/h Vent pipe diameter mm 25 50 50 80 80 100 125 125 150 200 200 200 250 250 250 300 or less 400 500 600 800 1000 1500 2000 3000 4000 5000 6000 7000 8000 9000 10000 Reservoir diameter (mm) and length (m) 40 1.2 m 1.5 2.0 50 0.7 1.0 1.2 1.5 2.0 80 0.5 0.6 0.8 1.0 1.5 2.0 100 0.5 0.7 1.0 1.3 2.0 150 0.6 0.9 1.2 1.4 1.7 2.0 200 250 0.5 0.7 0.8 1.0 1.2 1.3 1.5 1.7 0.5 0.6 0.7 0.8 0.9 1.0 Reservoir length can be reduced by 50% when the motive pressure (Pm) divided by the back pressure (P2) equals 2 or greater (when Pm ÷ P2 ≧ 2). ③ If flash steam is condensed before it enters the receiver/reservoir, compare tables ① and ② and choose the larger of the two sizes. Steam or Air Consumption (Motive Medium) Air Consumption 7 7 6 Steam Consumption 5 4 3 2 1 1 2 3 5 7 (per 1 tonne condensate)* 10 9 9 Air Consumption (m3) (per 1 tonne condensate) Steam Consumption (kg) 20 10 1 bar = 0.1 MPa Back Pressure (barg) * Equivalent consumption of air at 20 °C under atmospheric pressure Cycle Counter (option) Two types of counter can be installed on the GP10F to monitor the number of pumping cycles and help to determine the timing of maintenance, or estimate the volume of pumped condensate. LED LCD ¡C1CF – (Counter Unit Type): Self-contained standalone unit. Includes an LCD counter display and an operation indicator LED. ¡C1SF – (Terminal Box Type): Designed for use with remote monitoring equipment and systems. See the Cycle Counter SDS for further details. C1CF C1SF SDS U2404-08 System Packages (Open Systems) Single System Package 1188 1076 Exhaust Outlet DN 100 PN 16 Discharge Capacity: see discharge capacity graph (no correction factor required) Maximum Allowable Flash Steam: 500 kg/h Tank Size: 100ℓ Pumped Medium Inlet DN 80 PN 16 868 φ356 250 412 86 Type M1 Motive Medium Inlet 3/4” BSP 1333 1524 864 320 Pumped Medium Outlet DN 50 PN 40 275 GP10F 1100 1362 212 238 450 900 Twin System Package With small condensate loads, PowerTrap ① operates alone. As condensate loads increase, PowerTraps ① and ② operate together. 868 B Pumped Medium Inlet DN 80 PN 16 412 86 Discharge Capacity: double discharge capacity in graph (no correction factor required) Maximum Allowable Flash Steam: 1000 kg/h Tank Size: 230ℓ Pumped Medium Inlet DN 100 PN 16 1188 1076 Exhaust Outlet DN 150 PN 16 460 Type L2 ② Standards: Flanged connections: DIN 2501 Screwed connections: DIN 2999 Other standards available Units: mm F ① Pumped Medium Outlet DN 50 PN 40 GP10F 275 Pumped Medium Outlet DN 50 PN 40 1100 1424 864 320 Discharge Capacity: double discharge capacity in graph (no correction factor required) Maximum Allowable Flash Steam: 1500 kg/h Tank Size: 330ℓ Motive Medium Inlet 3/4” BSP H Type E2 212 238 238 212 900 Dimensions Type L2 E2 H 1724 1823 F 1524 1623 φB 560 660 SDS U2404-08 Rev. 7/2013 Products for intended use only. Specifications subject to change without notice.
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Specifications
Pump/ Trap with built-in steam trap for a wide
range of applications: drainage of heat
exchangers, flash steam recovery systems and
non-vented receivers such as low-pressure
stages of turbines and ...
model gt10l cast iron cast steel
SDS U2404-06 Rev. 9/2015
Products for intended use only.
Specifications subject to change without notice.
steam trap
* PRESSURE SHELL DESIGN CONDITIONS (NOT OPERATING CONDITIONS)
1 bar = 0.1 MPa
** This Rating Graph is based on Allowable Stress Values of ASTM-Materials at each temperature.
free float® steam trap
Maximum Allowable Pressure (barg) PMA: 120 Maximum Allowable Temperature (°C) TMA: 425 (JH7RH-B), 530 (JH7RH-P, JH7RH-W)
Model
Connection
Size
Orifice No.
Maximum Operating Press. (barg) PMO
Maximu...
free float® steam trap
2. Differential pressure is the difference between the inlet and outlet pressure of the trap.
3. Capacities are based on continuous discharge of condensate 6 °C below saturated steam temperature.