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Chapter 4.  Cycle eficiency with turbine cooling (cooling flow rates specified)   49

       remain  substantially valid  for  open  cycles  with  combustion, i.e.  for  those  involving
       real gases with variable composition and specific heats varying with temperature.
         The  arguments of  this  section  are  developed sequentially, starting with  internally
       reversible cycles and then considering irreversibilities. Here we concentrate on the gas
       turbine with simple closed or open cycle (CHT, CBT).


       4.2.1.  Cooling of  intentally reversible cycles

       4.2.1.1.  Cycle [CHTIRC, with single step cooling
         Consider first a cycle with reversible compression and expansion, but one in which,
       after a unit flow of the compressed gas has been heated externally, it is cooled by mixing
       with the remaining compressor delivery air (+) before entering the turbine in the internal
       cycle, which is otherwise reversible (Fig. 4.1 shows the T,s chart). This single step of
       cooling is representative of cooling the nozzle guide vanes of the first stage in a real gas
       turbine plant, reducing the rotor inlet temperature from T3 = T,,  to T5 = Tfit.
         We assume low velocity (constant pressure) mixing of the ‘extra’ cooling gas mass flow
       (+) at absolute temperature T2 with the gas stream (of unit mass flow), which has been
       heated to the maximum temperature T3 = TB. From the steady flow energy equation, if
       both streams have the same specific heat (c,), it follows that
                                                                           (4.1)

       where T5 is the resulting temperature in the mixed stream, before it is expanded through
       the  turbine.  The  turbine  work  output  is  now  WT = (1 + +)cpT5[(l - (l/x)],  and  the


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        Fig. 4.1. Temperature-entropy diagram for single-step cooling-reversible  cycle [CHTI,  (after Ref. [5]).
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