Page 312 - Subyek Teknik Mesin - Forsthoffers Best Practice Handbook for Rotating Machinery by William E Forsthoffer
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Steam Turbine Best Practices  Best Practice 5 .11
































              Fig 5.11.2   Total train control


              supplied, maintaining the highest possible total train efficiency  are shown. These different energy requirements can represent
              and reliability.                                     either increased pressure ratio requirements (suction strainer
                Figure 5.11.2 presents a process diagram for a steam turbine  blockage exchanger DP, etc.) and/or gas density changes (M.W.
              driven compressor train.                             P or T). As the process head (energy) requirements increase
                Depending on the selected process variable and location, any  from A to B to C, the input flow variable will decrease if the
              PIC or FIC will continuously monitor the selected process  turbo-compressor speed does not change. However, as soon as
              variable, sending its signal as an input to the turbine speed  the monitored process variable, FIC D s flow set point, the
              controller. For this example, assume the set point is a flow  turbine speed controller output will open the turbine inlet
              controller located in the discharge line of the turbo-compressor  throttle valves. This provides more turbine power to increase
              (FIC D ). The process system head (energy) requirements A, B, C  the head (energy) produced by the compressor, to meet the
                                                                   additional process system head requirements, and therefore
                                                                   maintain the desired throughput.
                                                                     Adjusting the speed of the driven equipment is the most
                                                                   efficient control method, since there no control valves are re-
                  The governor is the heart of the control system
                                                                   quired in the system. Therefore only the exact value of head
                  The governor in simple terms compares input signal(s) to a set
                  point and sends an output signal to achieve the desired set  required by the process system is produced by the turbo-
                  point.                                           compressor.
                  An example of a simple governor system is ‘cruise control’ in  Figure 5.11.2 shows the two major protection systems for the
                  a car
                                                                   compressor and steam turbine: the surge protection and turbine
                                                                   overspeed protection systems. The surge system has been
              Fig 5.11.3   Control                                 discussed previously, and the turbine overspeed system will be
















              Fig 5.11.4   A control system analogy. Left: Cruise control. Right: Steam turbine governor. In both cases, load change is inversely related to
              speed change. The controller compares input to set point and changes output appropriately.

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