Page 330 - Modeling of Chemical Kinetics and Reactor Design
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300    Modeling of Chemical Kinetics and Reactor Design

                                                        Example 5-6
                                Consider the reaction scheme

                                             
                                    
                                 A←→  →         C
                                     k 1
                                             k 3
                                         B
                                     k 2
                                       k 5  k 4                                         (5-115)




                                          D

                              in a constant volume batch reactor under isothermal conditions, and
                                                               –1
                                                                             –1
                                                                                            –1
                              with the rate constants k  = 0.4 hr , k  = 0.1 hr , k  = 0.16 hr ,
                                                                                  3
                                                                    2
                                                      1
                                                             –1
                                          –1
                              k  = 0.08 hr , and k  = 0.13 hr . The original compositions in the
                               4
                                                  5
                              batch are:
                                C  = 7 gmol/l
                                  A
                                C  = 2.0 gmol/l
                                  B
                                C  = 0 gmol/l
                                  C
                                C  = 0.5 gmol/l
                                  D
                                Determine the concentrations of each component as a function of
                              time for 2 hours. 1
                              Solution

                                From the reaction scheme, it can be assumed the rate equations are
                              first order. The rate of disappearance of component A is:


                                 − ( r A  ) net  =−  dC A  = kC A  − k C B              (5-116)
                                                          2
                                                   1
                                             dt
                                The rate of disappearance of component B is:



                              1 D. M. Himmelblau and K. B. Bischoff, Process Analysis & Simulation-Deterministic Systems,
                              John Wiley, 1968.
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