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3.6 THE VARIATION OF ENTHALPY WITH PRESSURE AT CONSTANT TEMPERATURE  59

              For isothermal processes, dT = 0 , and Equation (3.42) can be rearranged to
                                  0H        0U          0V
                                a    b  = ca   b  + P da  b  + V              (3.43)
                                  0P  T     0V  T       0P  T
              Using Equation (3.19) for (0U>0V) T ,

                                 0H         0P    0V
                                 a  b  = Ta   b  a   b  + V
                                 0P  T      0T  V  0P  T
                                                0V
                                        = V - Ta  b  = V(1 - Tb)              (3.44)
                                                0T  P
              The second formulation of Equation (3.44) is obtained through application of the cyclic
              rule [Equation (3.7)]. This equation is applicable to all systems containing pure sub-
              stances or mixtures at a fixed composition, provided that no phase changes or chemical
              reactions take place. The quantity (0H>0P) T  is evaluated for an ideal gas in Example
              Problem 3.8.



               EXAMPLE PROBLEM 3.8
              Evaluate (0H>0P) T  for an ideal gas.

              Solution
              (0P>0T) = (0[nRT>V]>0T) = nR>V   and (0V>0P) = (d[nRT>P]>dP)  =
                     V
                                                         T
                                      V
                                                                           T
              -nRT>P 2  for an ideal gas. Therefore,
               0H         0P    0V            nR    nRT            nRT nRT
              a   b  = Ta   b a    b + V = T     a -    b + V =-            + V = 0
               0P  T      0T  V  0P  T        V      P 2            P nRT
              This result could have been derived directly from the definition H = U + PV . For an
              ideal gas, U = U(T)  only and PV = nRT . Therefore, H = H(T)  for an ideal gas
              and (0H>0P) = 0 .
                        T

                 Because Example Problem 3.8 shows that H is only a function of T for an ideal gas,
                                       T f           T f
                                ¢H =     C (T)dT = n   C P,m (T)dT            (3.45)
                                          P
                                       3             3
                                       T i           T i
              for an ideal gas. Because H is only a function of T, Equation (3.45) holds for an ideal
              gas even if P is not constant. This result is also understandable in terms of the potential
              function of Figure 1.10. Because ideal gas molecules do not attract or repel one
              another, no energy is required to change their average distance of separation (increase
              or decrease P).
                 Equation (3.44) is next applied to several types of systems. We have seen that
              (0H>0P) = 0  for an ideal gas. For liquids and solids, 1 W Tb  for T 6 1000 K  as
                     T
              can be seen from the data in Table 3.1. Therefore, for liquids and solids,
              (0H>0P) L V  to a good approximation, and dH can be written as
                     T
                                       dH L C  dT + V dP                      (3.46)
                                              P
              for systems that consist only of liquids or solids.



               EXAMPLE PROBLEM 3.9
              Calculate the change in enthalpy when 124 g of liquid methanol initially at 1.00 bar
              and 298 K undergoes a change of state to 2.50 bar and 425 K. The density of liquid
                                                   –3
              methanol under these conditions is 0.791 g cm , and C P, m  for liquid methanol is
                         –1
                    –1
              81.1 J K mol .
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