2 GP-2000 : Trouble Shooting Cause of problems 1: s related to other factors 2: s on the pressure reducing valve A : Reduced pressure exceed specified set pressure. B : Reduced pressure does not reach the set pressure. C : Unstable operation
3 s caused by other factors Outlet pressure increase / decrease Fact example Pressure gauge is broken Replace the pressure gauge
4 s caused by other factors Outlet pressure increase Fact example Outlet pressure increase By-pass valve has leakage Replace isolation valve
5 s caused by other factors does not reach the set pressure Fact example Rising pipe at outlet side without trap Condensate at outlet side Condensate Decrease the size of piping
6 s caused by other factors does not reach the set pressure Fact example Conditions: *Inlet : 0.5MPa, pipe size 50A Outlet : 0.2MPa, pipe size 50A Steam capacity : 600 kg/h Pipe size at outlet side is too small!! *0.5MPa Pipe size 50A, Velocity : 35.6 m/s *0.2MPa Pipe size 50A, Velocity : 130 m/s High velocity leads to have pressure loss Velocity : m/s 50A Bigger size 65A
7 s caused by other factors does not reach the set pressure Fact example Conditions: *Decrease in outlet pressure Globe Valve *Globe valve is installed after PRV The pressure loss is caused by Globe valve. The flow capacity of globe valve was cannot handle the steam capacity. *Should install gate valve which has less pressure loss comparing to globe valve. *Select proper size of valve after PRV.
8 s caused by other factors does not reach the set pressure Condensate in the piping and bottom diaphragm case Fact example *The pressure at bottom diaphragm cannot increase because of condensate. *Discharge condensate by opening the plug at bottom diaphragm case.
9 To avoid Scale problem Make sure the strainer is installed before PRV Proposal : When scale problem Screen mesh are recommended when installing in front of PRV
10 To avoid Scale problem Proposal : When scale problem Flushing is required when 1Change of piping system 2Modifying the piping 3installing new piping Existing piping -Scales or corrosion exist
11 To avoid Water hammer Proposal : Installing separator and steam trap
12 To avoid Water hammer Proposal : Installing slow start-up station Slow start-up station prevents water hammer automatically when starting the system.
13 GP-2000 : Trouble Shooting related to product A. Reduced pressure exceed specified set pressure. Maintenance procedure Case 1-A : Check if Orifice B at Tee is clogged? Case 2-A : Check if foreign material stuck and scratch at pilot valve or seat. Case 3-A : Check if foreign material stuck and scratch at main valve and valve seat. Case 4-A : Check if Pilot diaphragm is damaged? Case 5-A : Check if External sensing pipe is not installed?
14 Case 1-A : Check if Orifice B at Tee is clogged? Phenomenon Clogging orifice B by scales causes high pressure to bottom diaphragm case, and pressure at diaphragm case stays and cannot release from Orifice B. Clogging orifice B caused by the collection of scales at the bottom diaphragm case because of accumulation of condensate. Clogged TEE Orifice A 1: Check the existence of condensate at the bottom diaphragm case by opening plug at the bottom diaphragm case. Orifice B Orifice C Pressure 2: Concerning the condensate, please check if steam trap and separator is installed or not.
15 Case 2-A : Check if foreign material stuck and scratch at pilot valve or seat. Phenomenon Increase in outlet pressure!! because pilot valve force to open by scale Leakage because valve cannot close completely Have to change pilot assembly Parts kit no. Size Consists of Q'ty Pilot valve assembly 1 KS A-200A Pilot valve gasket 1 Pilot diaphragm 2 Pilot valve
16 Case 3-A : Check if foreign material stuck and scratch at main valve and valve seat. Phenomenon Increase in outlet pressure!! because main valve tends to open by scales Leakage because valve cannot close completely Main valve Valve seat Lapping procedure is required Parts kit no. Size Consists of Q'ty KS A Main valve 1 KS A Top body gasket 1 KS A Bottom body gasket 1 KS A Main valve spring 1 KS A Spacer gasket* 1 KS A *For size 50A-125A KS A KS A KS A KS A-200A
17 Case 3-A : Check if foreign material stuck and scratch at main valve or seat. Solution : Lapping procedure Step 1) Put lapping powder to the valve seating surface. Recommended lapping powder: Fujimi incorp. Green silicon carbide #2000 or #4000. Please mix together with green silicon carbide or oil before usage. Step 2) Set the main valve to the valve seat. Step 3) -a: Turn the main valve clockwise and counterclockwise. Pressing the main valve down slightly. -b: Change the main valve position and repeat above procedure. Step 4) Continue lapping until the main valve and valve seat fit tightly. (Time for lapping differs in main valve and valve seat condition.) Step 5) Wipe out lapping powder completely on main valve and valve seat by soft cloth.
18 Case 2 / 3 -A : Check if foreign material stuck and scratch at GP-2000 Inspection method : Steam leakage of GP-2000 Step 1 : loosen lock nut of adjusting screw and loosen screw until feel the load has been removed. Step 2 : Loosen joint A & B and slowly open stop valve a little. Inspect whether steam leaks out of joint A & B. Adjusting screw Joint A By-pass Pressure gauge Drain separator Ball valve Stop valve Pressure gauge Safety valve Joint B Stop valve Stop valve Blow Strainer Stop valve Steam Trap Reducer Flow indicator GP-2000 Reducer Stop valve
19 Case 2 / 3 -A : Check if foreign material stuck and scratch at GP-2000 Inspection method : Steam leakage of GP-2000 Case A : If steam leaks out of joint A, there may be foreign materials between the pilot valve & seat. Case B : If steam leaks out of joint B, there may be foreign materials between the main valve & seat. area Steam Steam area Steam Steam
20 Case 4-A : Check if pilot diaphragm is damaged. Phenomenon Pilot diaphragm Cannot decrease into set pressure! because of broken pilot diaphragm Pilot valve always opens because the pressure at bottom pilot diaphragm cannot push up diaphragm to adjust into the set pressure. Have to change pilot diaphragm accordance with the procedure
21 Case 4-A : Check if pilot diaphragm is damaged. Procedure of changing pilot diaphragm Step 1: Prepare a new pilot diaphragm. (Using spare parts kit described on page 7). Step 2: Apply liquid sealant to the periphery of the bottom sealing surface of pilot diaphragm. (NEVER-SEEZ standard grade, made by BOSTIC is recommended as a liquid sealant). Regular Grade Anti Seize The "original" anti-seize compound and extreme pressure lubricant formulated with copper, graphite, aluminum and other ingredients to protect metal parts against rust, corrosion and seizure up to 1800ºF. Fine metallic and graphite particles in special grease protect parts even in high heat, high pressure and corrosive environments. Ford ESE-M12A4-A, Garrett Engine Div. PCS5724, Pratt & Whitney PWA and tested to MIL-A-907.
22 Case 5-A : Check if External sensing pipe is installed? Phenomenon Installing without external sensing pipe Without external sensing pipe, the pilot valve keeps opening by the adjusting spring force. Pilot valve will not sense and adjust the reducing pressure. Install the external sensing pip.
23 Fact Example: Reduced pressure exceed specified set pressure. Fact example Installing rising gradient Installed in round shape Because of accumulation of condensate at pilot, the pressure transmission to bottom pilot diaphragm is cut off. Install the external sensing pipe in down slope position not to have accumulation of condensate.
24 Fact Example: Reduced pressure exceed specified set pressure. Fact example Conditions: *Mixing valve is only used once a day. *Outlet pressure: 0.3MPa Piping Drawing 30M Mixing Valve *Outlet pressure increases up to 0.4MPa after 24 hours, and safety valve blows. *Accumulation of condensate is cause because of not using for a long period of time. *Water back flow in the piping system. *Scales stuck at the PRV. *Installing check valve solved the problem, and install trap close to PRV.
25 GP-2000 : Trouble Shooting related to product B. Pressure does not reach the set pressure. Maintenance procedure Case 1-B : Check if Pilot valve assembly is stuck with dirt? Case 2-B : Check if main diaphragm is damaged? Case 3-B : Check if Screen is clogged? Case 4-B : Check if Orifice C at Tee is clogged? Case 5-B : Check if External sensing pipe is clogged? Case 6-B : Check if Nominal size is too small for the steam capacity?
26 Case 1-B : Check if pilot valve assembly is stuck with dirt? Phenomenon Outlet pressure cannot control!! because defect on pilot valve Leakage will be caused and valve cannot open completely because of dirt.
27 Case 1-B : Check if pilot valve assembly is stuck with dirt? Inspection method Step 1 : Turn the pilot valve assembly upside down and place it on a table. Change the parts as pilot assembly Step 2 : Hold valve seat by fingers, depress the assembly strongly and check whether valve seat moves. Pilot assembly Parts kit no. Size Consists of Q'ty Pilot valve assembly 1 KS A-200A Pilot valve gasket 1 Pilot diaphragm 2 *Please also change pilot diaphragm at the same time.
28 Case 2-B : Check if main diaphragm is damaged? Phenomenon 1: With broken diaphragm, the pressure cannot push up the diaphragm because the pressure runs through the diaphragm. 1: Scale problem -Scales go into diaphragm case 2: Diaphragm cannot push up the main valve via retainer and spindle 2: Water hammer -On-off valve or too much condensate in the piping system 3: Outlet pressure will be Zero.
29 Case 2-B : Check if main diaphragm is damaged? 1: Scale problem Solution by Modification Scale moves into diaphragm case Equalizing line *Please make sure strainer (60 80 mesh) is installed before PRV.
30 Case 2-B : Check if main diaphragm is damaged? Proposal : to avoid water hammer 2: Water hammer Ⅰ Ⅱ Ⅰ. On-off valve should be installed in front of PRV Ⅱ. Proper location (more than 3M away from PRV)
31 Case 3-B : Check if screen is clogged? Phenomenon *Steam cannot flow because the integral strainer is clogged Steam cannot go through strainer because of too much scales Clean up or change the integral strainer
32 Case 4-B : Check if Orifice C at Tee is clogged? TEE Phenomenon Orifice A Clogged Orifice B Orifice C Steam cannot flow to the bottom diaphragm case and cannot push up the diaphragm to lift up the main valve Blow inside of the tee with compressed air. Pressure does not reach the set pressure
33 Case 5-B : Check if external sensing pipe is clogged? Phenomenon Clogged The pressure inside of external sensing pipe cannot escape because of scales, Lots of scales inside of the piping Blow inside of the external sensing pipe with compressed air.
34 Case 6-B : Check if Nominal size is too small for the steam capacity Fact example Large steam capacity Too much steam capacity to PRV Velocity Reduced Pressure *Select proper size of PRV *Steam velocity should be 20 to 40 m/s
35 Fact Example: Pressure does not reach the set pressure. Fact example Installing normal position Orifice A (5mm) Installing wrong side up Orifice C Orifice B (4mm) Orifice B Orifice C (3mm) Orifice A Required pressure cannot flow to bottom diaphragm, and diaphragm does not move to open main valve Assemble with right position
36 GP-2000 : Trouble Shooting related to product C. Unstable operation Maintenance procedure Case 1-C : Pressure reduction ratio is too big Case 2-C : Nominal size is too large
37 s caused by other factors Unstable operation Fact example Inlet pressure 2.0MPa Outlet pressure 0.05MPa *Pressure reduction ratio is 40 : 1 *Reduction ratio must be less than 20 : 1 Two-stage reduction 3M or more
38 s caused by other factors Unstable operation Fact example Tank Vibration problem Conditions: *Flow rate: 30 kg/h *GP A & OB-30 25A *P1: 0.4MPa, P2: 0.2MPa
39 s caused by other factors Unstable operation Vibration is caused because *Rated flow of GP-2000 : 600kg/h and Flow rate : 30kg/h is only 5% of rated flow. *When the flow becomes lower than 30 kg/h vibration is occurred. Reduced Pressure *Should install proper size of PRV. *Installing GP A or GD-30 15A to solve the problem. *Select proper size of the valve between 30 to 80 % of rated flow.
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