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180                              Entropy Analysis in Thermal Engineering Systems


          On the other hand, if the engine is run by fuel combustion, we find the fol-
          lowing relation.

                                            1
                                   ¼ H 0 +                           (11.39)
                                 rev            1 Ψ  ch
                               H
                                e          η
                                            max
          Here, H e denotes the enthalpy of the combustion products calculated at
                  rev
          T e , which designates the minimum theoretical temperature of the combus-
            rev
          tion products exiting the engine. For instance, if methane is used as a fuel,
          the minimum exhaust temperature according to Eq. (11.39) is 313.8K. An
          exit temperature lower than T e would be in violation of the laws of
                                      rev
          thermodynamics.

               11.8 Final notes
               Before closing this final chapter, there remains to make few remarks
          about the limitation of the second law and the application of entropy-based
          analysis.

          11.8.1 Entropy vs exergy

          In principle, there should not be any difference between the design results
          obtained from entropy and exergy analyses. It was repeatedly concluded in
          Sections 11.2–11.4 that the exergy destruction is equivalent to the total
          entropy generation multiplied by the temperature of the coldest reservoir
          (Section 11.2) or of the cold reservoir (Sections 11.3 and 11.4). So, minimi-
          zation of exergy destruction is identical to minimization of total entropy
          generation.
             The simplest explanation for the coincidence of the optimum of the two
          thermodynamic functions would, perhaps, be: exergy is a consequence of
          the first and second laws, but because the first law is an expression of the
          conservation of energy, an exergy-based analysis applied to a steady-state
          process carries a function whose net value is zero. For a system undergoing
          a steady-state process, the first law may be represented with a single function
          as F(E i )¼0, where E i denotes all forms of energy that may appear in a first
          law equation.
             It would then be a matter of preference to employ an entropy- or exergy-
          based analysis when modeling the thermodynamic performance of an energy
          conversion system. A thermodynamic model is primarily built upon the mass
          conservation principle and the first law. If one decides to also include an
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