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190                                    Isothermal  Reactor Design   Chap. 4

                                4.7.2  Semibatch Reactors
                                   \
                                Of  the two types of  semibatch reactors described earlier, we focus atten-
                           tion primarily  on the one  with  constant molar  feed. A  schematic diagram  of
                           this semibatch reactor is shown in Figure 4-14. We shall consider the elemen-
                           tary liquid-phase reaction

                                                        A+B-+C











                                                 Figure 4-14  Semibatch reactor.

                            in  which  reactant B  is  slowly added  to  a vat  containing  reactant A. A  mole.
                            balance on species A yields
                                                                  - r   rate of   1
                                                                  -
                                                                    1 accumulation       (4-5 1)




                                There are three variables that can be used to formulate  and solve semi-
                            batch reactor problems: the concentration, Cj, the number of moles, Nj, and the
                            conversion. X.

                            Writing  the  Semibatch  Reactor  Equations  in  Terms  of  Concentrations.
                            Recalling that the number of moles of A is just the product of concentration of
                            A, CA, and the volume % we can rewrite Equation (4-51) as

                                                                                         (4-52)


                            We  note that since the reactor  is being filled, the volume, % varies with time.
                            The reactor volume at any time t can be found from an overall mass balance
                            of  all species:
                                                         generation.  =[ accumulation rateof  I
                                                      + [  rate of
                                         [r;;]   -                                       (4-5.3)
                                                                   -    d(PV)
                                          POUO  -  0   +    0      -      dt

                            For a constant-density system,  po = p , and
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