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188                                    Isothermal Reactor  Design   Chap. 4

                           time necessary to reach  steady-state operation  (see Figure 4-13a). Next, semi-   '
                           batch reactors  are discussed.  In each of  these  cases,  we  are interested  in pre-
                           dicting  the  concentration  and  conversion  as  a  function of  time.  Closed-form
                          . analytical solutions to the differential equations arising from the mole balance
                           of these reaction types can be obtained only for zero- and first-order reactions.
           CAo-m
                           ODE solvers must be used for other orders.

                                    -
                           I

                                         CA








                                                    (b)                        (C)
                                Figure 4-13  Semibatch reactors.  [Excerpted by special permission  from Chem.
                                Eng., 63(10) 21 1 (Oct. 1956). Copyright 0 1956 by McGraw-Hill, Inc., New York,
                                NY  10020.1

                                There are two basic types of  semibatch  operations.  In  one type, one of
                           the reactants in the reaction

                                                     A+B-+C+D
                           (e.g., B) is slowly fed to a reactor containing the other reactant (e.g., A), which
                           has already been charged to a reactor such as that shown in Figure 4-13b. This
                           type of  reactor is generally  used  when  unwanted  side reactions  occur  at high
                           concentrations  of  B, or the  reaction  is highly  exothermic.  In  some reactions,
                           the reactant B is a gas and is bubbled  continuously  through  liquid reactant A.
                           Examples of reactions used in this type of semibatch reactor operation include
                           ammonolysis, chlorination, and hydrolysis. The other type of semibatch reactor
                           is shown  schematically  in  Figure 4-13c.  Here  reactants  A  and B  are charged
                           simultaneously and one of the  products  is vaporized  and  withdrawn  continu-
                           ously. Removal of  one of the products in this manner  (e.g., C) shifts the equi-
                           librium  towards  the  right,  increasing  the  final  conversion  above  that  which
                           would be achieved had C not been removed. In addition, removal of one of the
                           products further concentrates the reactant, thereby producing  an increased rate
                           of  reaction  and  decreased  processin   e. This type of reaction  operatioq is
                           called  reactive distilzation. Examples  of  reactions  carried  out in this  type  of
                           reactor  include  acetylation  reactions  and  esteriJication  reactions  in  which
                           water is removed.
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