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196    CHAPTER 9 THERMODYNAMIC PROPERTIES OF IDEAL GASES




             2. The total pressure exerted by a mixture is the sum of the pressures exerted by the
                individual components as each occupies the whole volume of the mixture at the same
                temperature.
             3. The internal energy, enthalpy and entropy of the mixture are respectively equal to the sums of the
                internal energy, enthalpy and entropy of the various components as each occupies the whole
                volume at the temperature of the mixture.



             9.4.3 MIXTURE RELATIONSHIPS
             The total mass, m, of a mixture can be related to the mass of constituents by
                                                                n
                                                               X
                                        m ¼ m a þ m b þ m c þ . ¼  m i                    (9.49)
                                                               i¼1
                From the ideal gas law (Eqn (9.2))
                                                     m
                                         pV ¼ mRT ¼     m w RT ¼ n<T
                                                     m w
             and hence for the individual constituents
                                           pV a ¼ m a R a T ¼ n a <T;

                                           pV b ¼ m b R b T ¼ n b <T;                     (9.50)

                                           pV c ¼ m c R c T ¼ n c <T; etc:
                In Eqn (9.50) V a ¼ volume of constituent a at the pressure and temperature of mixture, and V b and
             V c are similar volumes for constituents b and c. But the total volume, V, is given by
                                                               n
                                                              X
                                        V ¼ V a þ V b þ V c þ . ¼  V i ;                  (9.51)
                                                              i¼1
                                                               n
                                                             X
             and therefore              n ¼ n a þ n b þ n c þ . ¼  n i                    (9.52)
                                                              i¼1
                                     n a
                                Let    ¼ x a ¼ molar fraction of a in the mixture:        (9.53)
                                     n
                Similarly, n b /n ¼ x b and n c /n ¼ x c , etc, with n i /n ¼ x i .

                                                         n
                                                        X
             Therefore                 x a þ x b þ x c þ . ¼  x i ¼ 1                     (9.54)
                                                         i¼1
                It is possible to develop the term for the partial pressure of each constituent from statement (2) of
             the Gibbs–Dalton laws. Then, for constituent a occupying the total volume of the mixture at the
             pressure and temperature of the mixture

                                                 p a V ¼ n a <T                           (9.50)
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