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               Chapter 10                experimental activity coefficient data, so the values of these parameters implicitly
               Nonideal Solutions        incorporate the effects of ion pairing. Some workers have used the Pitzer equations
                                         together with explicit allowance for ion pairing to obtain better results than given by
                                         the Pitzer equations with ion pairing ignored [see Pitzer (1991), pp. 294, 306, 307].
                                         When this is done, the Pitzer parameters are modified from their usual values.
                                             The Pitzer and Meissner equations do not explicitly consider ion pairing and so
                                         one calculates I in these equations by assuming each strong electrolyte is present
                                                       m
                                         solely as ions, and these equations are designed to yield the experimentally observed
                                                           †
                                         activity coefficient  g   .
                                             A review of ion pairing concluded that “ion pairs can be treated as real species in
                                         the solution” and that “when at least one of the ion partners has a charge larger than
                                         1, ion pairing can be a reality in most solvents” [Y. Marcus and G. Hefter, Chem. Rev.,
                                         106, 4585 (2006)].


                                          10.9          STANDARD-STATE THERMODYNAMIC PROPERTIES
                                                        OF SOLUTION COMPONENTS
                                         To deal with chemical equilibrium in solution, we want to tabulate standard-state ther-
                                         modynamic properties of substances in solution. How are such properties determined?

                                         Nonelectrolyte Solutions
                                         For nonelectrolyte solutions where Convention I is used, the standard states are the
                                         pure substances, and we know how to determine standard-state properties of pure sub-
                                         stances (see Chapter 5).
                                             For solid and gaseous solutes, the molality scale is most commonly used. The
                                         standard Gibbs energy of formation and standard enthalpy of formation of substance
                                         i in solution at temperature T are defined by
                                                             ¢ G°1i, sln2   m° 1T, P°2   G° 1T2            (10.78)
                                                              f
                                                                                        elem
                                                                            m,i
                                                                 T

                                                             ¢ H°1i, sln2   H° 1T, P°2   H° 1T2            (10.79)
                                                                            m,i
                                                                T
                                                              f
                                                                                        elem

                                         where i, sln indicates substance i in solution in some particular solvent, m° and H° m,i
                                                                                                        m,i
                                         are the molality-scale standard-state partial molar Gibbs energy and enthalpy of i in
                                         solution, and G° elem  and H° elem  are the standard-state Gibbs energy and enthalpy of the
                                         pure, separated elements needed to form 1 mole of i. One way to determine standard-
                                         state molality-scale thermodynamic properties is from solubility data—the fact that m i
                                         in a saturated solution equals m* enables us to relate properties in solution to pure-
                                                                     i
                                         substance properties. The following example shows how this is done.
                                         EXAMPLE 10.4 Standard-state properties of a solute
                                            The molality of a saturated solution of sucrose in water at 25°C and 1 bar is
                                            6.05 mol/kg. Vapor-pressure measurements and the Gibbs–Duhem equation give
                                            g (C H O )   2.87 in the saturated solution. For pure sucrose at 25°C,   G°
                                                                                                          f
                                                      11
                                                12
                                                   22
                                             m
                                             1544 kJ/mol,   H°   2221 kJ/mol, and S°   360 J/(mol K). At 25°C and
                                                                                   m
                                                           f
                                            1 bar, the differential heat of solution of sucrose in water at infinite dilution is

                                            5.9 kJ/mol. Find   G° ,   H° , and S° 298  for C H O (aq).
                                                                                          11
                                                                                       22
                                                                                    12
                                                              298
                                                            f
                                                                   f
                                                                     298
                                               Using the phase-equilibrium condition of equality of chemical potentials, we
                                            equate m of pure sucrose to m of sucrose in the saturated solution. m of sucrose in
                                            solution is given by m   m°   RT ln (g m /m°) [Eq. (10.28)], and we have
                                                              i
                                                                                  i
                                                                              m,i
                                                                   m,i
                                                       G* 1T, P°2   m° 1T, P°2   RT ln 1g m,i,sat m i,sat >m°2  (10.80)
                                                         m,i
                                                                     m,i
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