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. |
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Heater gets ON - If CF temperature in tank < 55ºC or
at heater <50ºC. |
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Heater gets OFF- If CF temperature in tank >57ºC or at
heater >65ºC. |
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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. |
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FULLER EARTH REPLACEMENT PROCEDURE: |
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F.1 Isolation procedure of fuller earth for replacement
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1 Stop the regeneration pumps and isolate the power
supply. |
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2 Close inlet and outlet valves of the fuller earth
system. |
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3 Open vent valves of the fuller earth system for
depressurization. |
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4 Open drain valve of the fuller earth system for
draining. |
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5 Ensure the complete draining of the system. |
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6 Issue PTW on fuller earth system for fuller earth
replacement. |
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F.2 Normalization procedure of fuller earth after
replacement:- |
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1 Close the drain valves of fuller earth system. |
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2 Crack open the vent valve of fuller earth system. |
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3 Slowly open inlet valve and ensure venting. |
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4 Close the vent valve of fuller earth system after
venting. |
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5 Allow it for soaking about 4-5 hours if new
fuller-earth is used. |
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6 Open outlet valve of fuller earth system. |
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7 Normalise the regeneration pump power supply. |
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8 Start regeneration pump and check for any abnormality. |
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G PROCEDURE FOR FILTER CHANGE-OVER:- |
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1 Close drain valve of stand-by filter. |
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2 Open vent valve of stand-by filter. |
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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. |
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5 Slowly change-over the filter by rotating the
change-over valve. |
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6 Open the vent for depressurization and check the
pressure. |
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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) |
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PUMP INITIAL STARTING AND STOPPING PROCEDURE: |
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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). |
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5 CFT level is more than + 100 mm and that CF temp. is
more than 20ºC |
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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. |
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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. |
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10 Observe the CFT level after starting the pump. If it
drops below zero and maintains there, level |
topping up may be required. |
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11 Similarly check the availability of other pump (Stop
the running pump and then start the stand by |
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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. |
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13 Keep any one pump in service. |
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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. |
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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 |
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TANK DRAINING AND REFILLING PROCEDURE |
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I.1 CONTROL FLUID TANK DRAINING PROCEDURE |
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1 Ensure that the unit is under shutdown and there is no
requirement of control fluid system |
operation. |
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2 Stop the both control fluid pumps and isolate the power
supply. |
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3 Stop both CF oil vapour exhausters and isolate the
power supply. |
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4 Stop both CF regeneration pumps and isolate the power
supply. |
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5 Ensure the availability of empty clean oil barrels or
empty standby thoroughly cleaned tank |
prepared for this purpose for emptying the CF tank. |
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6 Ensure the clearance from TMD for emptying the CF
tank.. |
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7 Isolate the deluge valve spray system provided for the
system |
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8 Note down the tank level before starting draining. |
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9 TMD is responsible for tank draining into the empty
barrels. |
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I.2 CONTROL FLUID TANK FILLING PROCEDURE |
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1 Ensure the correct quality of the control fluid
((Moisture: <1000 ppm (mg/kg) / Acidity : <0.1 mg |
KOH/Gm). |
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2 Ensure the inspection of the tank is completed and
cleanliness of the tank. |
3 Ensure the CFT drain valve is closed. |
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4 Local level gauge is calibrated if required and charged
condition. |
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5 TMD is responsible for tank filling from the barrels. |
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6 Start CFT filling and monitor the level. |
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7 Check the Level switches (Operation & resetting)
while filling CFT. |
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8 Fill the CFT level up to 650mm from Top |
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9 Check oil level in the local level gauge and compare
with remote level indication, Attend it if any |
deviation appears.. |
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10 CFT filling completed |
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J CONTROL FLUID PUMP CHANGE OVER |
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1 Check & note down the running pump discharge
pressure. |
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2 Check & note down the running pump current at UCB
& local breaker panel. |
3 SLC control fluid in ON condition. |
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4 Start standby control fluid pump from UCB CRT. |
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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. |
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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). |
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CHECKS AND MONITORING DURING NORMAL RUNNING:- |
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K.1 Local Monitoring: |
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1 Note down CF tank level. CFP discharge pressure, all
filters DP, cooler o/l temp, tank temp, |
Waste fluid tank level. |
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2 Check for any leakages and abnormal sound, foaming
condition. |
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K.2 Remote Monitoring: |
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1 CF tank level, cross-check it with local reading. |
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2 CFP discharge pressure, temp after cooler, pump
current, see trend of current and pressure to |
detect foaming condition. |
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3 See the moisture content and acidity from daily
planning report and take necessary action if any |
discrepancy occurs. |
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