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264    Op erations


             manual mode, the plant operator watches a dial with a rotating pointer. The pointer will
             rotate passing zero at the top of the dial. Zero on the dial indicates when the frequency
             of the generator and the line are equal. There are usually two lights located above the dial
             that light up when the pointer is at or within a few degrees of zero. The plant operator
             uses a knob below the dial to slow the rotation of the pointer. When the pointer is rotat-
             ing very slowly and it reaches zero on the dial, the operator will turn a switch which then
             locks in the frequency of the generator with the line frequency. It should be noted that on
             most control systems, if the operator turns the switch when the frequency is not in sync
             and the pointer is not at the zero point on the dial the control system will not allow the
             generator to attempt a frequency lock and problems will persist until corrected.

             Bootstrapping
             In power plants, bootstrapping refers to methods for black starting a main generator. In
             large utility plants, there may be a diesel engine generator which allows a small CTG to
             start and synchronize to the diesel generator to provide enough power to start the main
             generator. In a combined cycle plant, a diesel engine generator may allow a standby
             boiler to be fired which supplies steam to the STG. The STG would then be paralleled
             to the diesel generator to provide enough power to a CTG. In many cases bootstrapping
             will allow for a smaller, more economical diesel engine generator to be utilized.

             Restart
             Each time the CTG or engine-generator is shutdown or trips off unexpectedly the prime
             mover equipment and the internals in the HRSG (or hot water heat recovery unit) are
             subjected to thermal stress. This is true for both shutdown and start-up operation.
             The plant operator must wait for the unit to go through a warm-up cycle after a start
             is initiated. If the engine or CTG trips off, the plant operator must quickly assess
             whether there is a serious problem that will cause the unit to be down for an extended
             period. The engine will require a rolldown period that is programmed into the control
             system. The rolldown period may be 10 minutes or longer depending on the size of the
             unit. If the reason for the trip can be reset quickly, the plant operator can gain a permis-
             sive to initiate a restart without further delay. If the CTG or engine generator is down for
             an extended period, the warm-up cycle will take at least an hour and sometimes much
             longer depending on the plant size and on how long equipments/systems have been off.


        Decisions on Plant Optimization
             Plant optimization opportunities depend on a number of factors including CHP electric
             and thermal capacity versus facility loads; the various plant production and use options
             for electricity, heating, and cooling; the level and sophistication of plant metering, mon-
             itoring, and controls; the data and analysis available (see Chap. 17); and the knowledge
             and experience of the plant operators. For example, if a CHP has been designed and
             constructed to be fully base loaded thermally and electrically all of the time, then there
             are no decisions on plant optimization, as compared to CHP plant that needs to be
             adjusted to varying electrical and thermal loads. On the other hand, for example, a
             combined cycle CHP plant with duct firing can adjust the amount of steam production
             and power produced in an STG. The more computer-tabulated and displayed metering
             and monitoring that a CHP possesses, the easier it is to understand and optimize a CHP
             plant (see Chaps. 17 and 18).
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