Page 118 - Entrophy Analysis in Thermal Engineering Systems
P. 118

Irreversible engines—Open cycles                             111


















              Fig. 8.2 Schematic of a gas turbine cycle.



              Chapter 7. Here, we will also account for the temperature dependence of
              the specific heat of the gaseous species as well as the fuel combustion in
              the pressurized air coming from the compressor. The fuel is methane
              (CH 4 ) that is compressed from the ambient pressure and temperature
              to the combustor pressure. The analysis begins by calculating the molar
              enthalpy and entropy flows per unit molar flowrate of the fuel at the inlet
              and outlet of the components.

              8.4.1 Enthalpy and entropy flows
              The compressor outlet temperature under isentropic condition is obtained by

                                                  γ c  1
                                               p 2
                                      T 2s ¼ T 1   γ c                   (8.29)
                                               p 1
              where γ c denotes the average specific heat ratio of the air across the
              compressor.
                 The isentropic efficiency of the compressor defined in terms of
              enthalpies as

                                             h 2s  h 1
                                         η ¼                             (8.30)
                                          c
                                             h 2  h 1
              allows us to determine the air temperature at the compressor outlet. The
              enthalpy and entropy of the air at the entrance and the exit of the compressor
              are calculated as follows.

                                        ð              Þ                 (8.31)
                                   H j ¼ Λh O 2  +3:76Λh N 2 j
                                       ð               Þ                 (8.32)
                                   S j ¼ Λs O 2  +3:76Λs N 2 j
   113   114   115   116   117   118   119   120   121   122   123