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58     CHAPTER 3 The Importance of State Functions: Internal Energy and Enthalpy

                                            To obtain Equation (3.37), both sides of Equation (3.36) have been divided by dT, and
                                         the ratio dV/dT has been converted to a partial derivative at constant P. Equation (3.19)
                                         has been used in the last step. Using Equation (3.9) and the cyclic rule, one can simplify
                                         Equation (3.37) to

                                                                                           0V  2
                                                                                         a   b
                                                                    0P     0V              0T  P
                                                          = C + Ta     b  a  b
                                                                                    V
                                                       C P    V                  = C - T
                                                                    0T  V  0T  P         a  0V b
                                                                                           0P  T
                                                                     b 2                       b 2
                                                       C = C + TV    or  C    P, m  = C V, m  + TV        (3.38)
                                                        P
                                                                                              m
                                                              V
                                                                     k                          k
                                         Equation (3.38) provides another example of the usefulness of the formal theory of
                                         thermodynamics in linking seemingly abstract partial derivatives with experimentally
                                         available data. The difference between C P, m  and C V, m  can be determined at a given tem-
                                         perature knowing only the molar volume, the isobaric volumetric thermal expansion
                                         coefficient, and the isothermal compressibility.
                                            Equation (3.38) is next applied to ideal and real gases, as well as liquids and
                                         solids, in the absence of phase changes and chemical reactions. Because  b  and k
                                         are always positive for real and ideal gases,  C - C 7 0  for these substances.
                                                                                  P
                                                                                       V
                                         First, C - C V  is calculated for an ideal gas, and then it is calculated for liquids
                                                P
                                         and solids. For an ideal gas, (0U>0V) = 0  as shown in Example Problem 3.3, and
                                                                        T
                                            0P     0V        nR   nR
                                         Ta   b  a   b  = Ta    ba   b = nR  so that Equation (3.37) becomes
                                            0T  V  0T  P      V    P
                                                                     C - C = nR                           (3.39)
                                                                       P
                                                                            V
                                         This result was stated without derivation in Section 2.4. The partial derivative (0V>0T)  =
                                                                                                            P
                                         Vb  is much smaller for liquids and solids than for gases. Therefore, generally
                                                                        0U          0V
                                                               C W ca      b  + Pda   b                   (3.40)
                                                                 V
                                                                        0V  T       0T  P
                                         so that C L C V  for a liquid or a solid. As shown earlier in Example Problem 3.2, it is
                                                P
                                         not feasible to carry out heating experiments for liquids and solids at constant volume
                                         because of the large pressure increase that occurs. Therefore, tabulated heat capacities
                                         for liquids and solids list C P, m  rather than C V, m .


                                                    The Variation of Enthalpy with Pressure
                                         3.6 at Constant Temperature
                                         In the previous section, we learned how H changes with T at constant P. To calculate
                                         how H changes as both P and T change, (0H>0P) T  must be calculated. The partial
                                         derivative  (0H>0P) T  is less straightforward to determine in an experiment than
                                         (0H>0T) P . As will be seen, for many processes involving changes in both P and T,
                                         (0H>0T) dT W (0H>0P) dP    and the pressure dependence of H can be neglected
                                                                T
                                                 P
                                         relative to its temperature dependence. However, the knowledge that (0H>0P) T  is not
                                         zero is essential for understanding the operation of a refrigerator and the liquefaction of
                                         gases. The following discussion is applicable to gases, liquids, and solids.
                                            Given the definition H = U + PV , we begin by writing dH as

                                                                 dH = dU + P dV + V dP                    (3.41)
                                         Substituting the differential forms of dU and dH,
                                                           0H                   0U
                                                   C dT + a   b  dP = C  dT + a    b  dV + PdV + VdP
                                                                        V
                                                    P
                                                            0P  T               0V  T
                                                                                 0U
                                                                     = C  dT + ca   b  + PddV + V dP      (3.42)
                                                                        V
                                                                                 0V  T
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