Page 95 - Introduction to chemical reaction engineering and kinetics
P. 95

4.3 Dependence of Rate on Concentration  77



                             0.9
                             0.8


                             0.6
                            0
                           e 0 5
                            z
                             0.4
                             0.3
                             0.2
                             0 . 1

                                     1    2    3    4    5     6    7    8    9     1
                                                         MAn
                           Figure  4.3 Comparison of CAICA~  for various orders of reaction in a BR or
                           PP’R (for conditions, see footnote to Table 4.1)


                           to increasing reaction time, t. For a given MA”, cA/cAO increases  with  increasing  order,
                           n.  We note that for IZ  = 0 and  1/2,  cAIcAO  decreases to 0 at  MA0 = 1 and  MAn2 = 2,
                           respectively, whereas for the other values of IZ,  cAIcAO  approaches 0 asymptotically.
                           The former behavior is characteristic for  IZ   <  1; in such cases, the value of  MA,,  for the
                           conditions noted in Figure 4.3 is given from equation 4.3-5 by

                                              MAACdCh    = 0) = l/(l  -  n);  n<l              (4.3-7)

                           We also note that the slope s  of the curves in Figure 4.3 is not the rate of reaction (-Y*),
                           but is related to it by (-rA)  = -s(--I*)~, where ( --I*)~  is the initial rate at MAn = 0
                                          ).  The limiting slope at MA,,  = 0 is  s  = -  1 in every case, as is evident
                           (-@Ah   =  kAcko
                           graphically for  n  = 0, and can be shown in general from equations 4.3-5 and -6.

                           4.3.5.2 CSTR (Constant Density)

                           For an nth-order, constant-density reaction in a CSTR, the combination of equations
                           2.3-12 and 3.4-1 can be rearranged to give a polynomial equation in cA/cAO:

                                                   (-TA)  = kAc1  = (CA0  -  c&t               (4.3-8)

                           from which, using equation 4.3-4 for  MA",   we obtain (for  all  values of n):


                                                                                               (4.3-9)


                             SOhltiOllS   for  CA/CA0 from equation 4.3-9 are given in the third column in Table 4.1.
                           For II = 312 and 3, the result is a cubic equation in (cA/cAo)lc! and CA/CA~,  respectively.
                           The analytical solutions for these are cumbersome expressions, and the equations can
                           be solved numerically to obtain the curves in Figure 4.4.
                             In Figure 4.4, similar to Figure 4.3,  CA/CA~   is plotted as a function of MA,,.  The behav-
                           ior is similar in both figures, but the values of  CA/CA~ for a CSTR are higher than those
                           for a BR or PFR (except for n  = 0, where they are the same). This is an important
                           characteristic in comparing these types of reactors (Chapter 17). Another difference is
                           that  CA/CA~  approaches 0 asymptotically for all values of n > 0, and not just for it 2 1,
                           as in Figure 4.3.
   90   91   92   93   94   95   96   97   98   99   100