Page 118 - Advanced Gas Turbine Cycles
P. 118

90                         Advanced gas turbine cycles

          6.2.2. The recuperative STIG plant

             Consider next a recuperative STIG plant (Fig. 6.5, again after Lloyd [2]). Heat is again
          recovered from the gas turbine exhaust: but firstly in a recuperator to heat the compressed
          air, to state 2A before combustion; and secondly in an HRSG, to raise steam S for injection
          into the combustion chamber.
             Again we analyse the open cycle version of this plant, but with a fuel inputf'  (per unit
          air flow) at ambient temperature To, i.e.  a fuel enthalpy flux off'hfo.  For the combustion
          chamber we may now write
               ha2A +fhfO + Shlih  = (1 +f)hg.l + Sh3,                        (6.10)
          and for the parallel calorific value experiment, at temperature To = T,,

               ha0 +fho = f[CVI" + (1 +f)h,,                                  (6.1  I)
          Subtracting Eq. (6. I 1) from Eq. (6.10) yields
               ha2A  - ha0 +frcvlo = (1  +fMg3  - hgo) + S(k3 - hsfA          (6.12)



                                                                              (6.13)















                                        6                     4
                        I1
                   AIR                                      7
                                                                 RECUPERATOR
                                   2


                                     STEAM
                                                                   HRSG




                                                                 EXHAUST



                            Fig. 6.5. STIG plant with additional gadair recuperator.
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