Page 162 - Entrophy Analysis in Thermal Engineering Systems
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Entropy and chemical equilibrium                             157


                 Gibbs’s theory is concerned with reversible processes with the surround-
              ing temperature assumed to be the same as the system temperature. Setting
              T s ¼T in our formulation yields G m ¼G, and Eq. (10.10) is accordingly
              expressed in terms of the Gibbs function.

                                                     !
                                    1  X        X
                                         k
                                                 k
                                             f       i     ΔG
                             Φ G ¼         G       G   ¼                (10.13)
                                             j       j
                                        j¼1     j¼1
                                    T                       T
              where Φ G is the entropy generation function that is evaluated for the special
              condition of G m ¼G, and ΔG denotes the net difference in the Gibbs func-
              tion between the initial and final states.
                 Because real processes are irreversible, we have Φ>0 so the right-hand
              side of Eq. (10.10) is always positive. Thus, the change in function G m will
              always be negative, i.e., ΔG m <0. Hence,


                                                                        (10.14)
                                            f    i
                                          G < G
                                           m     m
              In the special case of T s ¼T, one finds G <G . Inequality (10.14) is obtained
                                                f
                                                    i
              by invoking the second law. It is valid for all thermodynamic processes in the
              absence of work, including chemical reactions, which exchange heat with
              the surroundings assumed to be at a constant temperature. It states that
              for a system undergoing an actual process that is initially at an arbitrary
              but known state, the function G m at the final state will always be less than
              that in the initial state regardless of whether the transformation from the ini-
              tial state to the final state is infinitesimal, the system is initially at equilibrium
              or nonequilibrium, or the surrounding temperature, T s , is equal to the sys-
              tem temperature. Any other conclusion drawn from inequality (10.14) relat-
              ing the state of chemical equilibrium to the minimum of G m (or G in the
              special case of T s ¼T) would simply be unjustified.
                 From the discussion thus far, one may deduce that an application of
              Gibbs criterion, Eq. (10.1), may lead to inaccurate predictions of the com-
              position of a reactive system because there exists no strong experimental nor
              analytical foundation for such criterion. Neither the second law nor the
              combined first and second laws suggest that the chemical equilibrium is des-
              ignated by setting the differential of the Gibbs function or G m to zero. In a
              thermodynamic equilibrium, there is no change in the quantity of any spe-
              cies of the system, enthalpy, entropy, etc. The source of mistake is that
              “the change in enthalpy or entropy is zero” is often interpreted as
              “the differential of enthalpy or entropy is zero.” One is then led to look
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