Page 166 - Elements of Chemical Reaction Engineering 3rd Edition
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1 38                                   Isothermal Rqactor Design   Chap. 4

                           For  a  first-order reactioq  the  product  zk  is  often referred to  as  the reaction
                Da  = - Damkohler number.
                     FAO
                                The Damkohler is a dimensionless number that can give us  a quick esti-
                           mate of the degree of conversion that can be achieved in continuous-flow reac-
                           tors. The Damkohler number is the ratio of the rate of reaction of A to the rate
                           of convective transport of A  at the entrance to the reactor. For first- and sec-
                           ond-order irreversible reactions the Damkijhler numbers are





                           and






                           respectively.  It  is important to  know  what  values of  the Dardcohler  number,
                           Da,  give  high  and  low  conversion  in  continuous-flow  reactors. A  value  of
                           Da = 0.1 or less  will usually  give less than  10% conversion  and a value of
               0.1 <Da<  10   Da = 10.0 or greater will usually give greater than 90% conversion.


                           CSTRs in Series.  A first-order reaction with no volume change (v = u,)  is
                           to be carried out in two CSTRs placed in series (Figure 4-3). The effluent con-


                                                         CAI
                            CAO                           XI                           ' cA2
                                                                                         X2







                                                Figure 4-3  Two CSTRs in series.

                           centration of A from reactor 1 is






                           From a mole balance on reactor 2,
                                                      - FA2  - - vO(cAl  -
                                              vz  =
                                                     -'A2        k2CA2

                           Solving for CA2, the concentration exiting the second reactor, we get
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