Control Fluid system | |||||||
Control fluid (A fire resistant fluid) is used as operating media for oil operated HP & IP stop / | |||||||
control valves. This control fluid system also supplies control fluid as operating media for LPBP | |||||||
stop & control valves. The control fluid system contains two 100 % capacity pumps with double | |||||||
discharge i.e. LP control fluid delivered at 8 bar pressure from the 1st stage of the pump and HP | |||||||
control fluid delivered at 32 bar pressure from the pump 4th stage, two coolers (one being standby). | |||||||
There is no common filter, each sub system has got its own Duplex or rotating filters. CF | |||||||
tank is provided with two oil vapour exhausters, which extracts non condensable gases from the | |||||||
tank and expels to atmosphere. There is a temperature control valve which Controls oil | |||||||
temperature by controlling oil flow through the cooler. There is an electrical heater provided in the | |||||||
control fluid tank to maintain the oil temperature between 55 and 57ºC. | |||||||
Heater gets ON - If CF temperature in tank < 55ºC or at heater <50ºC. | |||||||
Heater gets OFF- If CF temperature in tank >57ºC or at heater >65ºC. | |||||||
Control fluid regeneration system is provided for removal of acids and ageing products | |||||||
during operation by the continuous filtering through Fuller´s earth and mechanical filters. The | |||||||
mode of operation of this natural earth treatment is based on a ion-exchange reaction. The | |||||||
regeneration system is having two pumps, two filters, two Fuller Earth filters, one heater. | |||||||
FULLER EARTH REPLACEMENT PROCEDURE: | |||||||
F.1 Isolation procedure of fuller earth for replacement :- | |||||||
1 Stop the regeneration pumps and isolate the power supply. | |||||||
2 Close inlet and outlet valves of the fuller earth system. | |||||||
3 Open vent valves of the fuller earth system for depressurization. | |||||||
4 Open drain valve of the fuller earth system for draining. | |||||||
5 Ensure the complete draining of the system. | |||||||
6 Issue PTW on fuller earth system for fuller earth replacement. | |||||||
F.2 Normalization procedure of fuller earth after replacement:- | |||||||
1 Close the drain valves of fuller earth system. | |||||||
2 Crack open the vent valve of fuller earth system. | |||||||
3 Slowly open inlet valve and ensure venting. | |||||||
4 Close the vent valve of fuller earth system after venting. | |||||||
5 Allow it for soaking about 4-5 hours if new fuller-earth is used. | |||||||
6 Open outlet valve of fuller earth system. | |||||||
7 Normalise the regeneration pump power supply. | |||||||
8 Start regeneration pump and check for any abnormality. | |||||||
G PROCEDURE FOR FILTER CHANGE-OVER:- | |||||||
1 Close drain valve of stand-by filter. | |||||||
2 Open vent valve of stand-by filter. | |||||||
3 Open equalizing valve and observe the pressure in the pressure gauge mounted on stand-by | |||||||
filter. Also observe the temperature of the stand-by filter body which will increase. | |||||||
4 Close the vent valve and equalizing valve after ensuring pressure and temperature of the | |||||||
standby filter. | |||||||
5 Slowly change-over the filter by rotating the change-over valve. | |||||||
6 Open the vent for depressurization and check the pressure. | |||||||
7 Open the drain valve of the new stand-by filter and ensure the complete draining (Continuous | |||||||
draining may happen when filter was not properly isolated due to passing in change over valve) | |||||||
PUMP INITIAL STARTING AND STOPPING PROCEDURE: | |||||||
1 All PTWs are returned and Clearance from Turbine Maintenance available | |||||||
2 Pump surroundings are clean & properly illuminated and access to the pump area is adequate. | |||||||
3 No PTW pending in the Governing system (Main and LP Bypass) & lined up. | |||||||
4 Control fluid moisture and acidity values are within limits (Moisture: <1000 ppm (mg/kg) / Acidity : | |||||||
<0.1 mg KOH/Gm). | |||||||
5 CFT level is more than + 100 mm and that CF temp. is more than 20ºC | |||||||
6 Start one control fluid pump and stop it after a few seconds to allow for line filling and venting. | |||||||
7 Then again start the pump and keep in service. | |||||||
8 Check that the HP & LP pressure are more than 32 ksc and 8 ksc respectively. | |||||||
9 Check for any abnormality like Abnormal sound, seal leakage, bearing temp. line leakage, | |||||||
Vibration etc. Stop the pump if any major abnormality is observed. | |||||||
10 Observe the CFT level after starting the pump. If it drops below zero and maintains there, level | |||||||
topping up may be required. | |||||||
11 Similarly check the availability of other pump (Stop the running pump and then start the stand by | |||||||
pump). Check that the HP & LP pressure are more than 32 ksc and 8 ksc respectively. | |||||||
12 Check for any abnormality like Abnormal sound, seal leakage, bearing temp. line leakage, | |||||||
Vibration etc. Stop the pump if any major abnormality is observed. | |||||||
13 Keep any one pump in service. | |||||||
14 Observe for any filter choking. If required changeover and clean the filters. | |||||||
15 Switch on the control fluid heating system and put it in auto. | |||||||
16 Observe the proper operation of the CF temp. control valve for maintaining the temperature. | |||||||
17 Switch ‘ON’ SLC CF system and give ‘Run’ command to complete the start-up | |||||||
TANK DRAINING AND REFILLING PROCEDURE | |||||||
I.1 CONTROL FLUID TANK DRAINING PROCEDURE | |||||||
1 Ensure that the unit is under shutdown and there is no requirement of control fluid system | |||||||
operation. | |||||||
2 Stop the both control fluid pumps and isolate the power supply. | |||||||
3 Stop both CF oil vapour exhausters and isolate the power supply. | |||||||
4 Stop both CF regeneration pumps and isolate the power supply. | |||||||
5 Ensure the availability of empty clean oil barrels or empty standby thoroughly cleaned tank | |||||||
prepared for this purpose for emptying the CF tank. | |||||||
6 Ensure the clearance from TMD for emptying the CF tank.. | |||||||
7 Isolate the deluge valve spray system provided for the system | |||||||
8 Note down the tank level before starting draining. | |||||||
9 TMD is responsible for tank draining into the empty barrels. | |||||||
I.2 CONTROL FLUID TANK FILLING PROCEDURE | |||||||
1 Ensure the correct quality of the control fluid ((Moisture: <1000 ppm (mg/kg) / Acidity : <0.1 mg | |||||||
KOH/Gm). | |||||||
2 Ensure the inspection of the tank is completed and cleanliness of the tank. | |||||||
3 Ensure the CFT drain valve is closed. | |||||||
4 Local level gauge is calibrated if required and charged condition. | |||||||
5 TMD is responsible for tank filling from the barrels. | |||||||
6 Start CFT filling and monitor the level. | |||||||
7 Check the Level switches (Operation & resetting) while filling CFT. | |||||||
8 Fill the CFT level up to 650mm from Top | |||||||
9 Check oil level in the local level gauge and compare with remote level indication, Attend it if any | |||||||
deviation appears.. | |||||||
10 CFT filling completed | |||||||
J CONTROL FLUID PUMP CHANGE OVER | |||||||
1 Check & note down the running pump discharge pressure. | |||||||
2 Check & note down the running pump current at UCB & local breaker panel. | |||||||
3 SLC control fluid in ON condition. | |||||||
4 Start standby control fluid pump from UCB CRT. | |||||||
5 Check the discharge header pressure at local and UCB. Ensure that there is an increase in | |||||||
pressure, which indicates loading condition of the standby pump. | |||||||
6 Check the current of the running standby pump at UCB and local breaker panel. | |||||||
7 Stop the previous running pump after ensuring loading condition of the standby pump. | |||||||
8 Again check the discharge header pressure and current (There may be a dip in discharge | |||||||
pressure). | |||||||
CHECKS AND MONITORING DURING NORMAL RUNNING:- | |||||||
K.1 Local Monitoring: | |||||||
1 Note down CF tank level. CFP discharge pressure, all filters DP, cooler o/l temp, tank temp, | |||||||
Waste fluid tank level. | |||||||
2 Check for any leakages and abnormal sound, foaming condition. | |||||||
K.2 Remote Monitoring: | |||||||
1 CF tank level, cross-check it with local reading. | |||||||
2 CFP discharge pressure, temp after cooler, pump current, see trend of current and pressure to | |||||||
detect foaming condition. | |||||||
3 See the moisture content and acidity from daily planning report and take necessary action if any | |||||||
discrepancy occurs. |
Thursday, May 10, 2018
Control Fluid system
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