Page 155 - Physical Chemistry
P. 155

lev38627_ch04.qxd  2/29/08  3:13 PM  Page 136





                136
               Chapter 4                     From the Gibbs equations for dU, dH, and dG, expressions for the variations in U,
               Material Equilibrium      H, and G with respect to T, P, and V were found in terms of the readily measured prop-
                                         erties C , a, and k. Application of the Euler reciprocity relation to dG   SdT
                                                P
                                         VdP gives (
S/
P)   (
V/
T) ; (
S/
V) is found similarly from the Gibbs equa-
                                                                      P
                                                                              T
                                                         T
                                         tion for dA. These relations allow calculation of  U,  H, and  S for arbitrary changes
                                         of state.
                                             For a system (open or closed) in mechanical and thermal equilibrium with P-V
                                                                                     a
                                                                                         a
                                         work only, one has dG   SdT   VdP      m dn , where the chemical poten-
                                                                                a
                                                                                   i
                                                                                         i
                                                                                     i
                                                                               a
                                                                                         a
                                                                                      a
                                         tial of substance i in phase a is defined as m   10G >0n 2  a .  This expression for
                                                                               i
                                                                                         i T,P,n j i
                                         dG applies during an irreversible chemical reaction or transport of matter between
                                         phases.
                                             The condition for equilibrium between phases is that, for each substance i, the
                                                                                                           a
                                                                                                                b
                                         chemical potential m must be the same in every phase in which i is present: m   m .
                                                                                                                i
                                                           i
                                                                                                           i
                                         The condition for reaction equilibrium is that   n m   0, where the n ’s are the reac-
                                                                                 i
                                                                                     i
                                                                                   i
                                                                                                    i
                                         tion’s stoichiometric numbers, negative for reactants and positive for products. The
                                         chemical potentials are the key properties in chemical thermodynamics, since they
                                         determine phase and reaction equilibrium.
                                             Important kinds of calculations dealt with in this chapter include:
                                         •   Calculation of  U,  H, and  S for changes in system temperature and pressure
                                             and calculation of  G and  A for isothermal processes (Sec. 4.5).
                                         •   Calculation of C   C , (
U/
V) , (
H/
P) , (
S/
T ) , (
S/
P) , etc., from read-
                                                                                                  T
                                                                V
                                                           P
                                                                         T
                                                                                  T
                                                                                          P
                                             ily measured properties (C , a, k) (Sec. 4.4).
                                                                   P
                                             Although this has been a long, mathematical chapter, it has presented concepts and
                                         results that lie at the heart of chemical thermodynamics and that will serve as a foun-
                                         dation for the remaining thermodynamics chapters.
                                         FURTHER READING
                                         Zemansky and Dittman, chaps. 9, 14; Denbigh, chap. 2; Andrews (1971), chaps. 13, 15,
                                         20, 21; Van Wylen and Sonntag, chap. 10; Lewis and Randall, App. 6; McGlashan,
                                         chaps. 6, 8.
               PROBLEMS
               Section 4.3                                       boiling point of 80.1°C and 1 atm; (c) adiabatic expansion of
               4.1  True or false? (a) The quantities U, H, A, and G all have  0.100 mol of a perfect gas into vacuum (Joule experiment) with
               the same dimensions. (b) The relation  G   H   T  S is  initial temperature of 300 K, initial volume of 2.00 L, and final
               valid for all processes. (c) G   A   PV. (d) For every closed  volume of 6.00 L.
               system in thermal and mechanical equilibrium and capable of
               only P-V work, the state function G is minimized when material  Section 4.4
               equilibrium is reached. (e) The Gibbs energy of 12 g of ice at  4.3  Express each of the following rates of change in terms of
               0°C and 1 atm is less than the Gibbs energy of 12 g of liquid  state functions. (a) The rate of change of U with respect to tem-
               water at 0°C and 1 atm. (f ) The quantities SdT, TdS, VdP, and  perature in a system held at constant volume. (b) The rate of
                2
                 VdP all have dimensions of energy.              change of H with respect to temperature in a system held at con-
                1
                                                                 stant pressure. (c) The rate of change of S with respect to tem-
               4.2  Calculate  G,  A, and  S univ  for each of the following  perature in a system held at constant pressure.
               processes and state any approximations made: (a) reversible
               melting of 36.0 g of ice at 0°C and 1 atm (use data from Prob.  4.4  The relation (
U/
S)   T [Eq. (4.37)] is notable because
                                                                                     V
               2.49); (b) reversible vaporization of 39 g of C H at its normal  is relates the three fundamental thermodynamic state functions
                                                    6
                                                  6
   150   151   152   153   154   155   156   157   158   159   160