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                          So far, only elements have been considered. Suppose we want the conventional en-    Section 5.5
                      thalpy of liquid water at  T. The formation reaction is H    1 2 O → H O. Therefore  Temperature Dependence
                                                                               2
                                                                          2
                                                                    2
                                                                                                          of Reaction Heats
                        H° (H O, l)    H° (H O, l)    H° (H , g)    1 2 H° (O , g). Knowing the conventional
                                                                  2
                                         2
                                     m,T
                                                  m,T
                                                      2
                       f
                                                              m,T
                            2
                         T
                      enthalpies H° m,T  for the elements H and O , we use the experimental   H° of H O(l) (de-
                                                                                   2
                                                      2
                                                2
                                                                              T
                                                                            f
                      termined as discussed earlier) to find the conventional H°  of H O(l). Similarly, we can
                                                                  m,T   2
                      find conventional enthalpies of other compounds.
                    5.5          TEMPERATURE DEPENDENCE OF REACTION HEATS
                  Suppose we have determined  H° for a reaction at temperature T and we want  H°
                                                                          1
                  at T . Differentiation of  H°     n H° [Eq. (5.3)] with respect to T gives d  H°/dT
                      2                        i  i  m,i
                      n dH° /dT, since the derivative of a sum equals the sum of the derivatives. (The
                      i  i  m,i
                  derivatives are not partial derivatives. Since P is fixed at the standard-state value 1 bar,
                  H° and  H° depend only on T.) The use of (
H  /
T)   C   [Eq. (4.30)] gives
                    m,i                                     m,i   P    P,m,i
                                          d ¢H°
                                                   a  n  C°    ¢C°                   (5.18)
                                            dT      i  i  P,m,i   P
                  where C°   is the molar heat capacity of substance i in its standard state at the tem-
                          P,m,i
                  perature of interest, and where we defined the standard heat-capacity change  C°
                                                                                          P
                  for the reaction as equal to the sum in (5.18). More informally, if pr and re stand for
                  stoichiometric numbers of moles of products and reactants, respectively, then
                            d ¢H°   d1H°   H° 2   dH° pr  dH°
                                       pr
                                             re
                                                            re
                                                                C°    C°   ¢C°
                             dT         dT         dT     dT      P,pr  P,re     P
                  Equation (5.18) is easy to remember since it resembles (
H/
T)   C .
                                                                        P    P
                      Integration of (5.18) between the limits T and T gives
                                                         1     2
                                                    T 1
                                          ¢H°   ¢H°       T 2  ¢C°  dT              (5.19)*
                                             T 2               P
                                                         T 1
                  which is the desired relation (Kirchhoff’s law).
                      An easy way to see the validity of (5.19) is from the following diagram:
                                                      1a2
                             Standard-state reactants at T S standard-state products at T 2
                                                    2
                                                                        1d2
                                 T   1b2                            c
                                                      1c2
                             Standard-state reactants at T S standard-state products at T 1
                                                    1
                  We can go from reactants to products at T by a path consisting of step (a) or by a path
                                                     2
                  consisting of steps (b)   (c)   (d). Since enthalpy is a state function,  H is indepen-
                  dent of path and  H   H   H   H . The use of  H        T 2  C dT [Eq. (2.79)]
                                    a     b      c     d                 T 1  P
                  to find  H and  H then gives Eq. (5.19).
                           d       b
                      Over a short temperature range, the temperature dependence of  C° in (5.19) can
                                                                              P
                  often be neglected to give  H°    H°   C° (T   T ). This equation is useful if
                                            T 2    T 1    P,T 1  2  1
                  we have C°  data at T only, but can be seriously in error if T   T is not small.
                            P,m       1                                2    1
                      The standard-state molar heat capacity C°  of a substance depends on T only and
                                                        P,m
                  is commonly expressed by a power series of the form
                                                            2
                                          C°    a   bT   cT   dT   3                 (5.20)
                                           P,m
                  where the coefficients a, b, c, and d are found by a least-squares fit of the experimen-
                  tal C°  data. Such power series are valid only in the temperature range of the data
                       P,m
                  used to find the coefficients. The temperature dependence of  C was discussed in
                                                                          P
                  Sec. 2.11 (see Fig. 2.15).
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