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Chapter 9.  The gas turbine as a cogeneration (combined heat and power) plant   177

        temperature is limited, at the level corresponding to (QNU)CG/FCG  = 3/16 as in the basic
        plant, then corresponding limits on A’,  are 27/4 for + = 1.5 and 27/2 for + = 1.2.



        9.5.  Design of gas turbines as cogeneration (CHP) plants

          Both  the  heat  to  work  ratio  kG and  the  various performance parameters such  as
        EUF and FESR  are affected by  the choice of  design parameters within a gas turbine.
        However, for the gas turbine with a WHR, the range of  &-G  that  can be achieved by
        varying these parameters is not large and operation may have to involve firing a WHB,
        or running in parallel with conventional plants, as explained earlier. But some variation
        in kc can be achieved by varying the  ‘internal’ design parameters (e.g. pressure ratio
        and  turbine  inlet  temperature), achieving matched  operation for each  of  the  different
        designs, i.e.  by varying kG to match AD.  Porter and Mastanaiah [2] calculated kc for
        a gas turbine with a WHR supplying process steam at pp, Tp. Plots of the heat to work
        ratio A,-G  against Tp are shown in Fig. 9.7, for a maximum temperature of  1200 K and
        various pressure ratios, and with a limit on the stack temperature and compressor and
        turbine efficiencies of  0.9.
          The EUF and FESR are then simple to derive and typical area plots of the range of EUF
        and  FESR  against  the  derived  &G,  for  gas  turbines  with  varying  practical  design
        parameters, are illustrated in Fig. 9.8.
          It is concluded that such simple gas turbines with WHRs have good energy utilisation at
        kc = I  with respectable FESR. The introduction of a WHB will move the operable area
        to  higher  values of  A,  usually with  comparable EUFs  but  lower FESRs, as has been
        illustrated in the examples calculated in Section 9.2.

        9.6.  Some practical gas turbine cogeneration plants

          There  are  many  gas  turbine CHP plants in  operation for a  range  of  purposes and
        applications. Here we describe the salient features of two such plants, each operating with
        a WHR but also with supplementary firing which can be introduced to meet increased heat
        demands.


        9.6.1. The Beilen CHP plant
          A gas turbine CHP scheme, with a heat recovery steam generator producing process
        steam,  operates  at  the  DOMO  plant  at  Beilen  in  the  Netherlands. The  plant,  which
        produces dairy products, originally took its electric power (up to 3.2 MW) from the grid
        and its heat load was met by two gas-fired boilers with a steam production of  25 t/h  at
        13 bar.
          The  CHP  plant  which  replaced  these  two  separate energy  supplies is  based  on  a
        Ruston  TB  gas  turbine  (rated at  3.65 MW)  which  can  meet  the  electrical demand  of
        3.2 MW and  is  connected to the grid so that excess electrical power can be  sold. By
        providing  full  gas  power, up  to  12 t/h  of  saturated steam can  be  produced  at  191°C
        and  13 bar.  Five  supplementary  gas  burners  can  be  engaged  to  increase  the  steam
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