Page 45 - Introduction to chemical reaction engineering and kinetics
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2.2 Batch Reactor (BR) 27

      2.2.2  Material Balance; Interpretation of  ri

                           Consider a reaction represented by A + . . . -+  products taking place in a batch reactor,
                           and focus on reactant A. The general balance equation, 1.51, may then be written as a
                           material balance for A with reference to a specified control volume (in Figure 2.1, this
                           is the volume of the liquid).
                             For a batch reactor, the only possible input and output terms are by reaction, since
                           there is no flow in or out. For the reactant A in this case, there is output but not input.
                           Equation 1.5-1 then reduces to


                                     rate offormation of  A  by reaction = rate of accumulation of  A

                           or, in mol s-l, sayr,

                                                       (-rA)V   =  -dnAldt,                    (2.2-1)

                           where V is the volume of the reacting system (not necessarily constant), and nA  is the
                           number of moles of A at time  t. Hence the interpretation of  r, for a batch reactor in
                           terms of amount nA  is


                                                     (-rA)   =  -(l/V)(dnAldt)                (2.2-2)


                             Equation 2.2-2 may appear in various forms, if nA is related to other quantities (by
                           normalization), as follows:

                             (1) If A is the limiting reactant, it may be convenient to  normalize  nA  in terms of  fA,
                                 the fractional conversion of A, defined by


                                                                                              (2.2-3) j
                                                  fA = @A0 - nA)inAo     WV

                                 where  n&, is the initial amount of A;  fA   may vary between 0 and 1. Then equation
                                 2.2-2  becomes



                                                     cerA)  =  (nA,lV)(dfAldt)                (2.2-4)  ~

                             (2) Whether A is the limiting reactant or not, it may be convenient to normalize by
                                 means of the extent of reaction, 5, defined for any species involved in the reac-
                                 tion by


                                                   d[  = dnilvi;  i = 1,2, . . . , N         (2.2-5) 1



                           ‘Note that the rate of formation of A is rA,  as defined in section 1.4; for a reactant, this is a negative quantity. The
                           rate of disappearance of A is (-r.&   a positive quantity. It is this  quantity that is used subsequently in balance
                           equations and rate laws for a reactant. For a product,  the  rate of formation, a positive quantity, is used. The
                           symbol  rA  may be used generically in the text to stand for “rate of reaction of A” where the  sign is irrelevant
                           and correspondingly for any other substance, whether reactant or product.
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