Page 160 - Materials Chemistry, Second Edition
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Mass-Balance Concept and Reactor Design                          143



           flow  rate of  50 L/min,  an  off-the-shelf  reactor would  provide  a hydrau-
           lic retention of 5 min and reduce TCE concentration from 200 to 16 ppb.
           However, the discharge limit for TCE is 3.2 ppb. Assuming the reactors are
           of ideal plug flow type and the reaction is first-order, how many reactors
           would you recommend? What would be the TCE concentration in the final
           effluent?

              Solution:
               (a)  Use Equation (4.24) to find out the reaction-rate constant:


                             16
                       C out       −  k ()(5)
                           =     =  e
                       C in  200

                   k = 0.505/min
               (b)  Use Equation (4.29) to find out the final effluent concentration
                   from two PFRs in series:



                       C 2    C 2     C 2    C 1   − (0.505)(5)  − (0.505)(5)  − 5.05
                          =     =        =  e (  )( e   ) =  e
                       C 0   200     C 1   C o 

                   C  = 1.28 ppb (It is less than 3.2 ppb.)
                     out
                   Two PFRs, each with 5-min residence time, would be needed.

              Discussion:
              We can also determine the total residence time needed to reduce the
                final concentration to 3.2 ppb first, and then determine the number
                of PFRs needed.
              Use Equation (4.24) to find out the required residence time

                                           3.2
                                         =     =  e
                                     C out       − (0.505)( )τ
                                     C in  200

              τ = 8.2 min (Two PFRs are needed.)

           4.6.2   Reactors in Parallel

           For reactors in parallel, the reactors share the same influent (the influent is
           split and fed to the reactors). The flow rate to each reactor in parallel can be
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