15.4 SPECIFIC control system REQUIREMENTS
15.4.1 CONTROL PHILOSPHY OF COAL HANDLING PLANT
a. The control & instrumentation shall be through microprocessor based PLC system for the entire Coal handling plant covering the total functional requirement of sequence control, interlock and protection, monitoring, alarm , data logging etc.
b. The design of the control system and related equipment shall adhere to the principle of Fail safe operation of all system levels i.e the failure of signal, failure of power or failure of any component should not cause a hazardous condition and at the same time prevent occurrence of false trips and provide reliable and efficient operation of the plant under dynamic conditions.
c. The system shall provide an integrated control & monitoring of coal handling plant equipment from a Main CHP Control Room. The control Room operator shall be provided with color graphic displays of the Coal handling plant and with sufficient details to allow proper control and monitoring of the plant function.
d. The entire Coal handling plant will be controlled from the following control points.
i) The overall operation and control of the entire Coal Handling Plant, with acontrol desk and suitable control panel will be provided at the Main CHP Control Room .
The main Control Room of CHP shall have control desk in which the operating station along with CRT and keyboard will be mounted and control panel shall have the CHP mimic, indicating lamps, push buttons meters, totalizer etc. and the alarm fascia windows at the top. CHP main Control Room will house system cabinets in addition to control desk.
The main switchgear will be housed in the main control room building for CHP and located near the crusher house, the I/O cards and the relays for drives and the equipments which are around the crusher house shall be mounted in the system cabinets which are located in the main control room building.
ii) The traveling Trippler and its associated drives shall be controlled from local panel located near the bunker floor MCC room .The system cabinet for remote I/O cards relays and interfacing equipment etc. for the Traveling Trippler drives and equipment shall be located in its MCC room to provide status indication /alarms for traveling Tripler operation in the main CHP control room. The system cabinets shall be suitable for protection class IP-65 .
iii) Similarly Coal unloading operation for wagon rakes near track hopper area shall be controlled from control panel located in the control room with in building near track hopper. The ON/OFF operation of paddle feeders shall be controlled from this panel apart from its local Control Panels. The control room in this building shall be provided with glass panel to have full view of rakes unloading operation
The integrated weigh bridges shall be provided for the measurements of weight for each wagon at wagon trippler complex. Each weighing bridge shall have built in diagnostic and weight measurements software .The weigh bridges shall be controlled from the panel located in control room at Tripler complex..
The remote I/Os relays, interfacing equipment etc. will be located in system cabinets in building at Tripler complex to provide status indication/alarm of the unloading operation in the main control room.
iv) Stacker Reclaimer shall be provided with PLC system. The remote I/O and relays will be provided on operator’s cabin of stacker –re-claimer to indicate Stacker re-claimer operation in the main control room.
e. Following Equipment will come under sequential interlock scheme and can be started / stopped from control desk in the main CHP control room with indication on CRT and mimic panel with fault annunciation facility:
i. All belt conveyors.
ii. Vibrating feeders.
iii. Screens
iv. Crushers
v. Flap Gates.
The sequential control system shall provide stream selection from under ground conveyor of track hopper, from crusher conveyor to stacking yard conveyor, from stacker –re claimer to staking yard conveyor during reclaim mode etc.
However, all the above mentioned equipment will have its local control panels/ station for start / stop and /or any other function required with suitable lockable type local / remote selector switch shall be housed in local panel and placed near drives
f. Following equipment will not generally come under interlock scheme and can be started / stopped / controlled from its local panels shall be provided with status indication and alarms on mimic at control panel in main CHP control room:
i. Belt Weigher :
ii. Bunker Level Indicator:
iii. Paddle Feeder :
iv. Stacker/Reclaimer:
v. Coal Sampling System.
vi. Mobile Trippler :
vii. Magnetic Separator in line.
viii. Ventilation system
ix. Dust extraction System.
x. Dust suppression System.
xi. Vibration monitoring system( for coal crushers)
g. Following equipment will be operated from its local panels without any indication in control desk and mimic.
i. Electric Hoist.
ii. Sump pump
iii. Suspended magnets
h. All equipment systems and accessories supplied shall be from the latest proven product range of a manufacturer.
One communication gateway shall be provided for hooking-up CHPcontrol system with DDCMIS control system located in central control room of power plant.
15.4.2 CONTROL PHILOSPHY OF ASH HANDLING SYSTEM.
15.4.2.1 Control Philosophy.
The control & instrumentation shall be through microprocessor based PLC system for the entire Ash handling plant covering the total functional requirement of sequence control, interlock & protection, monitoring, alarm data logging etc.
The PLC system shall be an integrated control and data acquisition system for providing control & monitoring of Ash handling plant from a Main AHP Control Room. The control room operator shall be provided with colour graphic displays of the Ash handling plant and with sufficient details to allow proper control & monitoring of the plant function. The operation of ash handling plant will be possible in Auto / Semi-auto / manual mode .
The entire Ash Handling plant will be controlled from the following control points:
For overall operation and control of entire Ash Handling Plant with fly ash system, bottom ash system, ash water and slurry pumping system and ash disposal system, a control desk along with control panels mimic will be provided at the Main AHP Control Room.
i) In order to have ease of operation and maintenance, the Central Control Room of AHP shall have control desk in which the operating station along with CRT and keyboard will be mounted and the control panel shall have the AHP mimic, indicating lamps, push buttons, control switches, indicating instruments/recorders etc. the alarm facia windows. AHP Central Control Room will house system cabinets in addition to control desk.
Following Equipment will come under interlock scheme and can be started/stopped from control desk with indication on CRT and mimic panel with fault nnunciation facility:
a. All Pumps/Blowers and Compressors .
b. Bottom Ash system.
c. Fly ash system, comprising of ash extraction from ESP’s & duct hopper to buffer hopper located near ESP’s and fly ash transportation system from buffer hopper to storage silos.
d. Ash slurry disposal system.
e. Bottom ash over flow system comprising of bottom ash over flow water storage tanks, settling tank, ash over flow water pumps, sludge pumps etc.
f. Silo system.
g. All Motorized valves
h. All pneumatic operated valves.
For local operation in the Bottom Ash area one (1) no. Bottom ash control panel/cubical is provided for each unit .this panel shall provide control for clinker grinders, bottom ash discharge valves, jet pumps for ash slurry transport etc.
ii) A control panel/cubicle shall also be provided in MCC room near silo area for fly ash collection system. The panel shall provide control for dry pneumatic ash extraction transportation and unloading system
iii) The system cabinet associated with various local controls shall be located near the local control panels. These cabinets shall accommodate I/O cards, relays, interfacing equipments etc. To provide status indication/ alarms etc. for various drives/ valves /equipments in main AHP control room.
iv) The system cabinets associated with other system/equipment being controlled from main control room shall be located in the main AHP control room. The various local control panels envisaged will be located/installed in different areas for ease of operation of different sub systems. Suitable alarm/annunciation system will be provided to warn of any mal-functioning g of the ash handling system.
v) The control panel shall be provided with adequate nos. of facia type annunciation windows for audio-visual summary fault annunciation purpose.
vi) One communication gateway along with suitable cables shall be provided for hooking up the ash handling control system with DDCMIS control system located in the central control room of the power plant.
vii) All instruments like vacuum/pressure switches, pressure gauges transmitter, level ontrollers, level switches/indicators, level probes, flow indicators and any other special instruments for remote measurements in the main control room shall be provided by the contractors
15.4.3 CONTROL PHILOSPHY OF PLANT WATER SYSTEM.
The control & instrumentation shall be through microprocessor based PLC system for the entire Plant water system covering the total functional requirement of sequence control, interlock & protection, monitoring, alarm data logging etc.
The PLC system shall be an integrated control and data acquisition system for providing control & monitoring of Plant water system from a DM plant Control Room. The control room operator shall be provided with colour graphic displays of the entire system with sufficient details to allow proper control & monitoring of the plant function. The operation of plant water system will be possible in Auto / Semi-auto / manual mode
The entire Plant water system will be controlled from the following control points:
For overall operation and control of entire Plant water system i.e.Raw water system, Chlorination plant for raw water system and DM plant system, a control desk along with control panels mimic will be provided at the DM plant Control Room.
i) In order to have ease of operation and maintenance, the l Control Room of DM plant shall have control desk in which the operating station along with CRT and keyboard will be mounted and the control panel shall have the Plant water system mimic, indicating lamps, push buttons, control switches, indicating instruments/recorders etc. the alarm facia windows. DM Control Room will house system cabinets to accommodate I/O cards ,drive cards, controllers etc. with the associated system.
ii) The following local control panels are envisaged .which are located near their associated system.
a) Raw water system local control panel
b) Chlorination plant local control panel for raw water treatment and CW water treatment
c) Chlorination plant local control panel for potable water system.
d) CW treatment plant local control panel
e) Transfer of acid/Alkali local control panel for DM plant
f) Any other control recommended by contractor
iii) The local control panel shall be provided with adequate nos. of facia type annunciation windows for audio-visual annunciation to warn operator for any mal functioning.
iv) All instruments like vacuum/pressure switches, pressure gauges transmitter, level controllers, level switches/indicators, level probes, flow indicators and any other special instruments for remote measurements in the main control room shall be provided by the contractors
v) The system cabinet associated with various local controls shall be located near the local control panels. These cabinets shall accommodate I/O cards, relays, interfacing equipments etc. to provide status indication/ alarms etc. for various drives/ valves /equipments in DM Plant control room.
a) water level in the sump——– very low
b) Pressure at pump discharge due to accidental closure of valve——- high
c) Winding temp of Motor(for HT drives)——–high
d) Temperature of pumps thrust bearing (HT drives only)———-High
e) Bearing vibration (for HT drives only)———-High
vii) Emergency stop of drives has also been envisaged from the local push button (lockable stay put type) provided near the drive. This local push button will be directly wired to Switchgear/MCC. To monitor the HT/LT drives following minimum signals shall be exchanged between Switch gear/MCC and PLC system:
a. Drive start/stop command.
b. Drive status feedback (ON/OFF)
c. Ready to start.
d. Electrical trips (from SWGR/MCC).
viii) DM plant PLC system shall be provided with suitable communication gateway for monitoring through DDCMIS in central control room
15.4.3.1 SYSTEM DESCRIPTION :
A) RAW WATER SYSTEM CONTROL.
i) The pre treatment plant is controlled from PLC, and the chemical dosing is envisaged only in manual mode from local. The Dosing pumps ,Tank agitator, Sludge pumps and clarifloculator bridge pumps can be operated from remote (i,e.PLC) as well as local control panel.
ii) Drives on the clarifier bridge i.e. rake mechanism drive motor and floculator agitator motor shall be operated from local start/stop push buttons to be located near it.
iii) The clarified water storage sump level is controlled by raw water inlet control valve with respect to the level in the clarified water sump .
iv) All the chemical dosing/solution tank shall be provided with local level indicator and low level switch ,which shall be interlocked with respective dosing pumps i.e the pump shall trip in case of the low level in the respective tank.
v) The sludge sump shall be provided with low and high level switch and selected pump whichever in auto shall start automatically when sludge sump level is high and stop automatically when sump level is low.
B) CHLORINATION PLANT CONTROL.
( control for CW water treatment, Raw water treatment)
i) The chlorination plant shall be controlled manually from local control panel located in chlorination system main control building. The control of all the drives and auxiliaries shall be implemented from this panel. The control panel shall have operators interface devices as selector switches, indicating lamps, push buttons and other required indicators.
ii) The control panel shall also provided control for absorption system to be located in main chlorination building.
iii) Provision shall also be given for local operation of pump/drives from control Box. Emergency trip push buttons shall be provided for all such drives which needs immediate stopping due to any mal- functioning of equipment or due to health/operator hazards. Provision shall be made to operate the booster pumps through selector switch.
iv) Local starting shall be possible through remote/local selector switch on control panel or in MCC. Tripping of / emergency stop of dries motors locally shall be permissible irrespective of position of remote/local selector switch. provision for locking the local stop push buttons after tripping the motors from local push buttons shall be provided.
v) A window based annunciator system shall be provided in local control panel for all major alarms/trip conditions. The annunciation system shall also include alarms for abnormal level conditions in caustic solutions preparation cum recirculation tanks,
vi) The chlorination of potable water system shall be separately carried out through chlorine cylinder .This arrangements is located near by DM plant building .The operation &control is similar to above and operated through a local control panel located there.
C) D.M. PLANT CONTROL.
i) The operation and control of Dematerializing Plant shall be through a PLC in Auto/semi auto mode. However, there shall be provision to changeover to manual operation. The control operation philosophy shall include sequential control like semi-auto/remote-manual/manual , facility like step numbering, step time elapsed time, hold/release push button through CRT, flow of control logic (sequence of various steps) for smooth operation of the entire plant .
ii) DM plant control system shall be designed so that complete Operation, Control & monitoring, interlocks, logic etc. of Raw Water system and associated clarified sump pumps, Raw water chlorination system, service water pumps, CT make up pumps, Potable water pumps control, DM feed pumps etc.shall be provided from DM plant control room
iii) The operator will initiate the operation of regeneration/rinsing/backwashing of a particular ion-exchange unit/filter based on the criteria described below, but the change from one step of the sequence to the next will be automatic. The system will employ a logical system, which will link the various steps such as closing/opening of different valves, starting/stopping of various pumps, which make a sequence.
iv) Filters/lon exchange units will be automatically isolated from the system as follows:
Pressure Sand Filter : On passing predetermined volume of water or high
Differential pressure across the filter bed.
Activated Carbon Filter : On passing predetermined volume of water or on reaching preset residual chlorine level of high
Differential pressure across the filter bed.
Cation : On reaching high sodium leakage or on passing of
Predetermined volume of filtered water whichever
Occurs first.
Anion Unit : On reaching higher conductivity & Silica at
Outlet or on passing of predetermined volume of
Decationised water, whichever occurs fist.
Mixed Bed Unit : On reaching higher conductivity, pH at outlet or
On passing of predetermined volume of deionised
Water or on reaching preset silica level, whichever
Occurs first.
v) As state above, the isolation of the exchanger unit from the system will be displayed on CRT. The operator will then select the particular vessel to be regenerated through option and selected for regeneration. On selecting the option the regeneration cycle shall start automatically. During regeneration, the progress of different sequence/sub-process shall be displayed to the operator in the form of step number as well as step description which is in progress, the set time for that.
vi) The progress of the sequence shall be displayed to the operator through suitable means. The system will incorporate the necessary safety systems, locking systems and manual emergency system. On failure of logic system, in between , the failure shall be annunciated to the operator and all the valves corresponding to that unit, being regenerated shall close automatically.
vii) A graphic depicting the complete plant process operations shall be designed properly and be available on CRT. The graphic shall indicate the different filters, exchanger units, measuring tanks, opening/closing of all valves (motorized and solenoid operated), ON / OFF of different pumps and blowers etc. Color coding shall be used to differentiate lines for different services such as normal water lines, backwash lines, Acid / Alkali lines etc.
viii) Separate conductivity measurement, silica mesurement and pH measurements shall be employed for ensuring the various parameters in the effluent and in the rinse line of caution, anion and mixed bed exchanger units for normal and rinsing operation. The conductivity cell in the rinsing line shall be automatically isolated during the first half of the rinsing cycle and shall be connected automatically during the second half of rinsing cycle when the conductivity is less than 100 micromhos/cm excess over the rinse water conductivity.
ix) Discharge valves of all pumps of the entire plant, connected with semi-auto/remote manual operation shall be pneumatically operated: and all pumps, pneumatically operated valves, drive motors of all the other equipment and other accessories, pneumatic on-off valves, etc. shall be completely suitable for remote manual operation from operating console/panel. All drive motor shall also be provided with arrangement of local stopping. Tripping of drive motors from local panel shall be permissible irrespective of the position of local-remote selection option. Local stop push-button shall be locked after tripping the motor from local.
x) Although the basic demineralising process is semi-automatic in nature, following operations shall be performed manually.
Unloading and Transfer of Acid.
a. Hydrochloric acid will be unloaded from the road tank-cars by operating any one of the acid unloading pumps. Opearation shall be controlled from local panel.
b. Hydrochloric acid, stored in over ground tanks, will be led remote manually by gravity to the acid measuring tanks for cation, mixed bed units to fill up to the desired level. Subsequent transfer of acid from the measuring tanks to the ion-exchanger units as required in regeneration operation is however automatic.
Unloading, Preparation and Transfer of Alkali.
a. Caustic solution will be unloaded from the road tank-cars by operating any one of the Caustic unloading pumps. Operation shall be controlled manually from local panel.
b. Caustic solution, stored in over ground tanks, will be led remote manually by gravity to the caustic measuring tanks for anion, mixed bed units to fill up to the desired level. Subsequent transfer of caustic from the measuring tanks to the ion-exchanger units as required in regeneration operation is however automatic.
c. All operations in items (a) and (b) will be controlled manually from the local panel.
d. Transfer of alkali to the respective measuring tanks for anion and mixed bed exchanger units will be done remote manually. However, subsequent transfer of alkali to respective ion exchanger units will be automatic.
Neutralization of Waste from DM Plant.
a. After completion of regeneration of one cation and one anion exchanger, the waste generated during regenerations will be thoroughly recirculated in the neutralizing pit and if necessary, acid/alkali solution will be added to make the waste slightly alkaline.
b. When required pH of waste solution has been reached, the waste solution will be pumped to the effluent treatment plant area and the effluent shall conform to IS-2490. The pump will automatically be tripped when the level in neutralization pit reaches very low.
c. Priming of pumps operating under suction lift and operations as in (a) and (b) will be done manually. All pump operation shall be controlled from the local panel.
D) CW TREATMENT PLANT CONTROL
(for make up to condenser)
The operation and control philosophy of circulating water treatment plant shall be as below:
i) Sulphuric acid shall be unloaded by two no. unloading pumps into over ground acid storage tanks. Acid shall be subsequently transferred to acid dosing tanks by using above unloading pumps.
ii) The sulphuric acid dosing pumps operation shall be auto and manual from local control panel. In the auto mode ,the rate of acid dosing shall be controlled by auto adjusting of the stroke of the pumps by sensing of ph of circulating water. However the starting and tripping of the dosing pumps shall be controlled by the level switches of the dosing tanks.
iii) During normal operation sulphuric acid dosing pumps shall operate in the auto mode and inject sulphuric acid to maintain the ph of circulating water at desired level so that alkalinity remains with in desired limits.
iv) The operation of other chemical dosing pumps like anti scalant dosing pumps, anti corrosion dosing pumps and biocide dosing shall be manual from local control panel operation of the pumps shall be guided through the level of the respective tanks.
15.4.4 Control philosphy for compressed air system
15.4.4.1 CONTROL PHILOSOPHY.
i) Complete automation of the Compressed Air System and Air drying Plant shall be based on dedicated microprocessor based PLC Control System. The Control System shall be comprising a Processor Unit, Input./Output modules, LCD screen display The PLC l will be housed in local control panel located in compressor room/compartment. .
ii) The local control panel shall house PLC hardware (processors, I/O cards, relays, cables etc) LCD screen , Alarm annunciators configured in PLC. Indication lamps, witches, Start/Stop push buttons, Auxiliary relays, Motor current etc.,through the local control panel, local, manual and automatic operation of the compressed air system shall be carried out for local operation of the system
iii) Each compressor shall be suitable for individual and / or parallel operation with other compressors at any demand rate from zero to maximum capacity . Each compressor shall be suitable for start up and operation of a second or third operating with the first compressor in operation at all load with no instability in performance.
iv) The operating compressor for units shall be on automatic mode .both service air & instrument air is is fed from the same and common compressor. The compressors shall be utilized for On-off/load control as decided by the operator. All necessary instruments /controller and interlock /protection /monitoring and sequential logics controls shall be provided for implementation andare achieved by PLC.
v) Each air dryer shall be provided with independent microprocessor PLC, heater, set of absorber . With a selector switch ,the particular air dryer is selected and then the operation is fully automatic. Start up and shut down permissive interlocks for compressor and air drying plant shall be provided for safe operation of the equipment.
vi) Hooking up with central control room DDCMIS will be done through proper gateway and communication cables.
vii) All process connection and piping materials including pipes, valves, manifolds and fittings as required for connecting all field instruments shall be provided.
15.4.5 CONTROL PHILOSOPHY OF FUEL OIL STORAGE AND HANDLING SYSTEM
i) Two no control panels (Local control panel-1 & Local control panel-2) are envisaged for control and operation for fuel oil unloading, storage & transfer system. Local control panel-1 shall be placed at fuel oil pump house for control and operation of HFO/LSHS & LDOunloading, storage and transfer operation. & Local control panel-2 shall be located in Fuel oil pressuring and heating building for control and operation of HFO/LSHS & LDOday storage tank.
ii) When the unloading header & the piping at the pump suction becomes filled with oil and the steady supply is ensured at the suction pipe the unloading pumps shall be started manually from push buttons in the local control panel-! located in the fuel oil unloading pump house. These pumps shall,however, trip automatically in the event of high level in the respective oil (LDO or HFO/LSHS) storage tank. Standby pump shall start automatically whenever any operating pump trips due to any fault ( echanical / electrical) or discharge header pressure low. The differential pressure across the suction duplex strainer high initiates alarms to change the duplex strainer position.
iii) The transfer pumps to day tank shall be started manually from push buttons in the above local control panel-1. These pumps trip automatically when the level in the source storage tank goes low or the level of respective day oil tank goes high. These pumps will also be prevented from starting in case of low level in the respective source storage tank, or high level in respective day oil tank or high pressure drop across the respective suction strainer. Stand-by pump shall start automatically whenever any operating pump trips due to any fault (mechanical/electrical) or discharge header pressure goes low.
iv) The drain oil pump will start/stop automatically on high/low level initiation. Further there should be provision for alarm also. The standby pump shall also operated automatically in case the operating pumps trip.
v) Local emergency stop push button shall be provided for all electrical drives.
vi) Steam flow to HFO/LSHS storage and day tank floor coil heater shall be controlled by pneumatically operated control valve (ON-OFF type) to maintain the desired oil temperature.
vii) Steam flow to suction heater of HFO/LSHS day tanks shall be regulated through pneumatically operated control valve on the steam supply line to the suction heater and the same shall be actuated from heater outlet oil temperature.
viii) The Local control panel-1 & Local control panel-2 panel shall include start/stop buttons for all drives, status indication etc. and shall also include complete annunciations (alarm & indication) with TEST/ACKNOWLEDGE/RESET push buttons.
ix) One communication gateway shall be provided by hooking up the system with DDCMIS for monitoring from central control room
x) All the instruments shall be supplied as required with all necessary accessories for safe and efficient running of the plant.