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                                                                                                              Section 9.6
                                                                                                           Thermodynamic
                                                             T  mix S/n                             Properties of Ideal Solutions



                                                                                             Figure 9.16
                                                                mix H/n                      Mixing quantities for a two-
                                                                                             component ideal solution as a
                                                                                             function of composition at 25°C.





                                                                mix G/n









                      From     G       H   T    S and (9.44) and (9.46), we find
                             mix     mix      mix
                                      ¢  mix H   0   ideal soln., const. T, P        (9.47)

                  There is no heat of mixing on formation of an ideal solution at constant T and P.
                      From     H       U   P     V at constant P and T and Eqs. (9.45) and (9.47),
                             mix     mix      mix
                  we have    U   0 for forming an ideal solution at constant T and P, as expected from
                           mix
                  the molecular picture.
                      Figure 9.16 plots    G/n,    H/n, and T    S/n for an ideal two-component
                                       mix     mix           mix
                  solution against the B mole fraction x at 25°C, where n   n   n .
                                                  B                   B    C
                  Vapor Pressure
                  If the applied pressure on an ideal liquid solution is reduced until the solution begins
                  to vaporize, we obtain a two-phase system of solution in equilibrium with its vapor.
                  As we shall see, the mole fractions in the vapor phase will generally differ from those
                                                 v
                                          v
                                       v
                  in the liquid phase. Let x , x , . . . , x , . . . be the mole fractions in the vapor phase in
                                       1  2      i
                  equilibrium at temperature T with an ideal liquid solution whose mole fractions are
                    l
                      l
                             l
                  x , x , ..., x , . . . (Fig. 9.17). The vapor pressure is P and equals the sum of the partial
                    1  2     i
                                                                              v
                  pressures of the gases: P   P   P       P      , where P   x P [Eq. (1.23)].
                                           1    2          i             i   i
                  The system’s pressure equals the vapor pressure P. We now derive the vapor-pressure
                  equation for an ideal solution.
                      The condition for phase equilibrium between the ideal solution and its vapor is
                        v
                                                             l
                                                                   v
                    l
                  m   m [Eq. (4.88)] for each substance i, where m and m are the chemical potentials
                    i   i                                    i     i                               x , x , . . . , x , . . .
                                                                                                            y
                                                                                                      y
                                                                                                    y
                  of i in the liquid solution and in the vapor, respectively. We shall assume that the vapor  1  2  i
                  is an ideal gas mixture, which is a pretty good assumption at the low or moderate pres-
                                                                                 v
                  sures at which solutions are usually studied. In an ideal gas mixture, m   m°
                                                                                       v
                                                                                 i    i
                                                v
                  RT ln (P /P°) [Eq. (6.4)], where m° is the chemical potential of pure ideal gas i at T
                          i                     i
                                                                                                    l
                                                                                                      l
                                                                                                            l
                  and P°   1 bar, and P is the partial pressure of i in the vapor in equilibrium with the  x , x , . . . , x , . . .
                                     i                                                              1  2    i
                                                                                l
                                                         v
                                                                      l
                                                                 l
                  solution. Substitution of this expression for m and of m   m*   RT ln x [Eq. (9.42)]
                                                         i       i    i         i
                                      l
                                                                  l
                                                                       v
                  for the ideal solution m into the equilibrium condition m   m gives
                                      i                           i    i                     Figure 9.17
                                                   l
                                                        v
                                                    m   m
                                                   i
                                                        i
                                                                                             An ideal solution in equilibrium
                                    l
                                                   l
                                                         v
                                    m* 1T, P2   RT ln x   m° 1T2   RT ln 1P >P°2     (9.48)  with its vapor (y).
                                   i               i    i             i
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