Page 167 - Modeling of Chemical Kinetics and Reactor Design
P. 167

Reaction Rate Expression  137

                              improved by incorporating a method that favors the required reaction
                              over the unwanted reaction.


                                     HOMOGENEOUS CATALYZED REACTIONS


                                A catalyzed reaction can be expressed as
                                     
                                     k 1
                                         P
                                 A →      (uncatalyzed)                                (3-112)
                                 AC  →      PC      (catalyzed)                        (3-113)
                                        
                                              +
                                  +
                                        k 2
                              where C and P represent the catalyst and product respectively.  The
                              reaction rates for a constant volume batch system (i.e., constant
                              density) are:


                                 − ( r  )=−   dC A   = kC
                                   A               1  A                                (3-114)
                                          dt
                                               1

                                 − ( r  )=−   dC A   = kC C                           (3-115)
                                   A
                                          dt      2  A  C
                                               2
                                The overall rate of disappearance of reactant A is:


                                 −  dC A  = kC A  + k C C C                             (3-116)
                                                   A
                                                2
                                          1
                                   dt
                                The catalyst concentration remains unchanged and integrating
                              Equation 3-116 with the boundary conditions: t = 0, C  = C AO  and
                                                                                  A
                              t = t, C  = C A
                                     A
                                   C A  dC   t
                                             ∫
                                 −  ∫    A  = (k 1  + k C C )dt
                                                    2
                                       C A                                              (3-117)
                                  C AO       0
                                     C
                                 −ln  A  =(k 1  + k C C ) =t  Kt                        (3-118)
                                                2
                                    C AO
                              where K = k  + k C .
                                          1    2 C
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