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                      Collecting the expressions for dU, dH, dA, and dG, we have                              Section 4.4
                                                                                                  Thermodynamic Relations for a
                                  dU   T dS   P dV                                                     System in Equilibrium
                                                                                    (4.33)*
                                  dH   T dS   V dP       closed syst., rev. proc.,
                                                     u                               (4.34)
                                  dA   S dT   P dV   P-V work only
                                                                                     (4.35)
                                  dG   S dT   V dP
                                                                                    (4.36)*
                  These are the Gibbs equations. The first can be written down from the first law dU
                  dq   dw and knowledge of the expressions for dw rev  and dq . The other three can be
                                                                     rev
                  quickly derived from the first by use of the definitions of H, A, and G. Thus they need
                  not be memorized. The expression for dG is used so often, however, that it saves time
                  to memorize it.
                      The Gibbs equation dU   TdS   PdV implies that U is being considered a func-
                  tion of the variables S and V. From U   U(S, V), we have [Eq. (1.30)]
                                                0U          0U
                                         dU   a    b  dS   a   b  dV
                                                0S  V       0V  S
                  Since dS and dV are arbitrary and independent of each other, comparison of this equa-
                  tion with dU   TdS   PdV gives

                                          0U              0U
                                         a   b   T,   a     b   P                    (4.37)
                                          0S  V           0V  S
                  A quick way to get these two equations is to first put dV   0 in dU   TdS   PdV to
                  give (
U/
S)   T and then put dS   0 in dU   TdS   PdV to give (
U/
V)   P.
                             V
                                                                                    S
                  [Note from the first equation in (4.37) that an increase in internal energy at constant vol-
                  ume will always increase the entropy.] The other three Gibbs equations (4.34) to (4.36)
                  give in a similar manner (
H/
S)   T,(
H/
P)   V,(
A/
T)   S,(
A/
V)   P,
                                             P
                                                         S
                                                                     V
                                                                                   T
                  and
                                          0G               0G
                                         a   b   S,   a       b   V                  (4.38)
                                          0T  P            0P  T
                      Our aim is to be able to express any thermodynamic property of an equilibrium
                  system in terms of easily measured quantities. The power of thermodynamics is that it
                  enables properties that are difficult to measure to be expressed in terms of easily mea-
                  sured properties. The easily measured properties most commonly used for this purpose
                  are [Eqs. (1.43) and (1.44)]

                                                 1   0V                  1   0V
                            C 1T, P2,   a1T, P2     a  b ,   k1T, P2      a    b    (4.39)*
                             P
                                                 V   0T  P               V   0P  T
                  Since these are state functions, they are functions of T, P, and composition. We are
                  considering mainly constant-composition systems, so we omit the composition depen-
                  dence. Note that a and k can be found from the equation of state V   V(T, P) if this is
                  known.

                  The Euler Reciprocity Relation
                  To relate a desired property to C , a, and k, we use the basic equations (4.25) to (4.31)
                                             P
                  and mathematical partial-derivative identities. Before proceeding, there is another
                  partial-derivative identity we shall need. If z is a function of x and y, then [Eq. (1.30)]
                                          0z         0z
                                   dz   a   b  dx   a  b  dy   M dx   N dy           (4.40)
                                          0x  y      0y  x
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