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Standard Technical Features of BTG System for Supercritical 660 ...

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<strong>Standard</strong> <strong>Technical</strong> <strong>Features</strong> <strong>of</strong> <strong>BTG</strong> <strong>System</strong> <strong>for</strong> <strong>Supercritical</strong> <strong>660</strong>/800 MW Thermal Unitselevations shall be modulated on fuel oil pressure signal whereas theauxiliary air dampers at all other elevations shall be modulated tomaintain the wind box to furnace differential pressure.c) In order to limit the NOx content in flue gas, SADC shall alsoinclude the control <strong>of</strong> over-fire dampers (if provided). The secondaryair damper controls and necessary interlocks to modulate or toopen/close shall be incorporated as per the requirements <strong>of</strong> the boilerdesign.d) Individual position transmitters are to be provided <strong>for</strong> each <strong>of</strong> thesecondary air dampers and the same shall be connected to SADC<strong>System</strong>.iv)Auxiliary Pressure Reducing and De-superheating Station (Aux. PRDS)Control <strong>System</strong>a) Auxiliary PRDS control system shall be provided to control the lowcapacity PRDS (with steam tapping <strong>of</strong>f from CRH line) and the highcapacity PRDS (with steam tapping <strong>of</strong>f from MS line) and coordinatetheir operation under all regimes <strong>of</strong> unit/plant operation.b) Each <strong>of</strong> the aux. PRDS units (i.e. low capacity PRDS and highcapacity PRDS) shall be provided with automatic control loops <strong>for</strong>steam pressure control, steam temperature control and spray waterpressure control. However, facility <strong>for</strong> remote manual control shallalso be provided <strong>for</strong> operation in case the automatic control fails. Thesignals <strong>for</strong> steam pressure and temperature control shall be takenfrom the down-streams <strong>of</strong> pressure reducing valve and desuperheatingstation respectively and their set points shall beadjustable. The spray water pressure control shall regulate thepressure upstreams to the temperature control valve and also basedon feed <strong>for</strong>ward signal from steam temperature control.v) Soot Blower Control <strong>System</strong> (SBCS)a) The soot blowing system shall be fully automatic & sequentiallycontrolled through SG C&I control system. Alternately, a SMARTsoot blowing system based on heat flux sensors and flue gas exittemperature may be implemented with a fall back to sequentialcontrol, if required. The system shall be complete with provision <strong>for</strong>individual operation <strong>of</strong> any soot blower and facility to bypass anysoot blower and shall be provided with following:1. Automatic starting <strong>of</strong> each soot blower in the system.149

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