Page 278 - Advanced Thermodynamics for Engineers, Second Edition
P. 278

12.8 THE VAN’T HOFF RELATIONSHIP         267




                  The ratios of the amounts of substance in the equilibrium products are defined by the equilibrium
               constant,
                                                 	                1=2 1=2
                                                  p p 0         an  p
                                                       CO 2       P  0  :
                                        K p r                 ¼                            (12.89)
                                                     	     1=2    1=2  1=2
                                           ¼
                                              p p 0   p p 0     bc  p
                                                   CO      O 2       P
                  Hence,
                                                         2
                                                  2
                                                              2
                                                 b c  p P  K ¼ a ;                         (12.90)
                                                         p r
                                                    p 0 n P
               and, from the atomic balances, this can be written in terms of a as
                                                   1
                                                  2        p P  2    2
                                                              K ¼ a                        (12.91)
                                                   2       p 0 n P
                                           ð1:1   aÞ  ð1   aÞ   p r
                  The previous calculations showed that the temperature of the products which satisfies the gov-
                                                                 ¼ 13:1488. These values will be used to
               erning equations is T P ¼ 2950 K; which gives a value of K p r
               demonstrate this example. Then
                                           2  	           2   3  	 p P  13:1488   2
                              1:21   2:2a þ a   1:21a   2:2a þ a              ¼ a :        (12.92)
                                                                 p 0 n P  2
                  It is possible to evaluate the ratio p P =p 0 n P from the perfect gas relationship, giving
                                          p P  p R T P  8:5   2950
                                                                ¼ 12:009
                                             ¼      ¼
                                         p 0 n P  n R T R  3:48   600
                  This enables a cubic equation in a to be obtained
                                                             2
                                                                      3
                                     95:532   269:23a þ 251:65a   78:953a ¼ 0              (12.93)
                  The solution to this equation is a ¼ 0.8506, and hence the chemical equation becomes
                              1
                      1:1CO þ ðO 2 þ 3:76N 2 Þ/0:8506CO 2 þ 0:2494CO þ 0:0747O 2 þ 1:88N 2  (12.94)
                              2
               which is the same as that obtained previously. The advantage of this approach is that it is possible to
               derive a set of simultaneous equations which define the equilibrium state, and these can be easily
               solved by a computer program. The disadvantage is that it is not possible to use the intuition that most
               engineers can adopt to simplify the solution technique. It must be recognised that the full range of
               iteration was not used in this demonstration, and the solution obtained from the original method was
               simply used for the first ‘iteration’.

               12.8 THE VAN’T HOFF RELATIONSHIP BETWEEN EQUILIBRIUM
                      CONSTANT AND HEAT OF REACTION
               It has been shown that, Eqn (12.54)

                                               1 	   0     0     0     0
                                                  y a m þ y b m   y c m   y d m :          (12.95)
                                              <T
                                       ln K p r  ¼   a     b     c     d
   273   274   275   276   277   278   279   280   281   282   283