Page 237 - Modeling of Chemical Kinetics and Reactor Design
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Reaction Rate Expression  207

                                • A = 0.015999
                                • B = –0.26711 × 10 –2
                                • Correlation Coefficient = 0.99991

                                                                      –1
                                The rate constant k  = –B = 0.00267 sec . Figure 3-25 gives a plot
                                                  1
                              of ln C  versus time t (min).
                                     A

                                                        Example 3-11
                                A gas decomposition reaction with stoichiometry 2A  → 2B + C
                                                                             2
                              follows a second order rate law  r mol m(  /  3  s • ) =  kC , where C  is the
                                                            d
                                                                              A
                                                                                        A
                                                            3
                              reactant concentration in mol/m . The rate constant k varies with the
                              reaction temperature according to the Arrhenius law:
                                  (
                                 k m mol s) =  k exp   − E  
                                     3
                                          •
                                                O
                                                       RT
                                         3
                              where k (m /mol•s) = pre-exponential factor
                                     O
                                         E(J/mol) = reaction activation energy
                                               R = gas constant
                                (1) Suppose the reaction is performed in a batch reactor of constant
                                         3
                              volume V(m ) at a constant temperature T(K), beginning with pure A
























                                                Figure 3-25. Plot of ln C  versus t.
                                                                     A
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