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Sec. 6.l   Maximizing the Desired Product in  Parallel Reactions   285
                                The rate  of  disappearance  of A  for  this  reaction  sequence is  the  sum of  the
                                rates of formation of U and D:

                                                           -rA = rD + ru                      (6-3)




                                where  cy1  and a2 are positive constants. We  want the rate of  formation of  D,
                                rD, to be high with respect to the rate of  formation of U,  rU. Taking the ratio
                    instantaneous   of these rates [Le., Equation (6-1) to Equation (6-2)], we obtain a rate selectiv-
                       selectivity   ity pammeter, S, which is to be maximized:

                                                       SDU = - - - c,                         (6-5)
                                                             rD  - kD
                                                             ru   k"

                                     6.1.1  Maximizing the Rate Selectivity Parameter S for One Reactant

                 Maximize the rate   In  this  section  we  examine  ways  to  maximize  S, which  is  sometimes
                                referred to as the instantaneous  selectivity, for different reaction orders of  the
                       parameter
                                desired and undesired products.

                  a1 is the order of  Case 1:  a, > a?  For the case where the reaction order of the desired urocluct
                the desired reaction;   is greater ihan the reaction order of  the undesired product, let a be a Gositive
                a2, the undesired
                   of
                        reaction   number that is the difference between these reaction orders:


                                Then


                                                                                               (61-6)


                For  cil > cy2, make   Tal make this ratio as largg as possible, we want to carry out the reaction
                    C,  as large as  in a manner that  will keep me cbncentration of reactant A as high as possible
                        possible   during the reaction. If  the reaction is carried out in the gas phase,  we  should
                                run it without inerts and at high pressures to keep C, high. If the reaction is in
                                the liquid phase, lbe use of diluents should be kept to a minimum.'
                                     A batch or plug-flow reactor should be used in this case, because in these
                                two reactors, the cioncentration of A starts at a high value and drops progressively
                                during the course of the reaction. In a perfectly mixed CSTR, the concentration
                                of reactant within the reactor is always at its lowest value (ie., that of the outlet
                                concentration) and therefore not be chosen under these circumstances.


                                  For a number of liquid-phase reactions, the proper choice of a solvent can enhance selec-
                                  tivity. See, for example, Znd. Eng. Chem., 62(9), 16 (1970). In gas-phase heterogeneous
                                  catalytic reactions, selectivity is an important parameter of any particular catalyst.
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