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Irreversible engines—Open cycles                             113


              8.4.2 Determination of SEG
              To calculate the specific entropy generation, we note that entropy is
              generated due to the following four irreversible processes: compression,
              combustion, expansion, and exhaust cooling. The entropy generation rate
              per molar flowrate of the fuel within the compressor and turbine is simply
              obtained from Eqs. (8.40) and (8.41), respectively.

                                                                         (8.40)
                                        Φ c ¼ S 2  S 1
                                                                         (8.41)
                                        Φ t ¼ S 4  S 3
              The rate of entropy generation per unit molar flowrate of the fuel within the
              combustor is the difference between the entropies of the reactants and the
              products in reaction (8.33)
                                                                         (8.42)
                                       Φ com ¼ S P  S R
              where S P ¼S 3 , which can be computed using Eq. (8.39), and

                                                                         (8.43)
                                S R ¼ s CH 4  + Λs 2,O 2  +3:76Λs 2,N 2
              The last source of entropy generation is the cooling process of the combus-
              tion gases that leave the turbine at temperature T 4 and cool down to the
              ambient temperature. Hence,


                                     Φ L ¼  Q L  + S 5  S 4 Þ            (8.44)
                                               ð
                                          T 0
              where S 4 is determined using Eq. (8.39), and S 5 denotes the entropy of the
              combustion gases at the ambient temperature and pressure. Hence,

                             ½             ð                  Š          (8.45)
                         S 5 ¼ s CO 2  +2s H 2 O + Λ 2Þs O 2  +3:76Λs N 2 T 0 ,p 0
              In Eq. (8.44), Q L denotes the amount of heat rejected by the cycle per unit
              flowrate of the fuel.
                                                                         (8.46)
                                      Q L ¼ HV  W net
              where HV denotes the fuel heating value and W net is the net power produced
              per unit molar flowrate of the fuel burned in the combustor.

                                                                         (8.47)
                                    W net ¼ W t  W c  W fc
              where W c is the air compressor power consumption, W t is the turbine power
              production, and W fc is the power requirement of the fuel compressor.
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