Page 222 - Introduction to chemical reaction engineering and kinetics
P. 222

204  Chapter 8: Catalysis and Catalytic Reactions

                            The second boundary condition is not known definitely, but is consistent with reactant A
                            not penetrating the impermeable face at z = 1. From equations  8.512a  to c,

                                                        Cl  = edl(e+  + e+)                   (8.5-12d)
                                                        C2  = eb/(e+  +  e-+)                 (8.5-12e)

                            Then equation 8.5-12a becomes, on substitution for  C,  and  C,:
                                                    e-4(1-Z)  + &l-Z)
                                               e=      e4  + e-4    =  cosh[4(1 - z)l          (8.5-13)
                                                                         cash  4

                            where  cosh4 = (e+  + e&‘)/2.
                              Figure 8.10(b)  shows a plot of  $ = cAIcAS as a function of  z,  the fractional distance
                            into the particle, with the Thiele modulus  #I  as parameter. For  4  = 0, characteristic of a
                            very porous particle, the concentration of A remains the same throughout the particle. For
                            4  = 0.5, characteristic of a relatively porous particle with almost negligible pore-diffusion
                            resistance,  cA  decreases slightly as z +  1. At the other extreme, for  4  = 10, characteristic
                            of relatively strong pore-diffusion resistance,  CA  drops rapidly as z increases, indicating
                            that reaction takes place mostly in the outer part (on the side of the permeable face) of the
                            particle, and the inner part is relatively ineffective.
                              The effectiveness factor  77,  defined in equation 8.5-5, is a measure of the effectiveness of
                            the interior surface of the particle, since it compares the observed rate through the particle
                            as a whole with the intrinsic rate at the exterior surface conditions; the latter would occur
                            if there were no diffusional resistance, so that all parts of the interior surface were equally
                            effective (at cA = c&.  To obt ain q,  since all A entering the particle reacts (irreversible
                            reaction), the observed rate is given by the rate of diffusion across the permeable face at
                            z = 0:


                                                  rate with diff. resist.  =  (-I-~)  observed
                                             77=  rate with no diff. resist.  (-rJ  intrinsic

                                           =  rate of diffusion of A at z = 0  = (NA  at z = O)A,
                                               total rate of reaction at cAs  (- RA)int
                                              =  -D,A,(dc,/dx),=,    _  -D,c,(d$ldz),=,

                                                    LAckACAs      -      L2k,Ck,




                            That is,






                            where  tanh4  =  sinh@cosh$  =  (e#’ -  e&)l(e’#  +  e-4).

                              Note that 7 -+ 1 as r#~  --+ 0 and 77 -+ l/$ as 4 -+  large. (Obtaining the former result
                            requires an application of  L’HBpital’s  rule, but the latter follows directly from tanh  4  -+
                            1 as  4  -+  large.) These limiting results are shown in Figure 8.11, which is a plot of 17  as a
                            function of  4  according to equation 8.5-14, with both coordinates on logarithmic scales.
                            The two limiting results and the transition region between may arbitrarily be considered
                            as three regions punctuated by the points marked by G and H:
                                                                                                           !I
   217   218   219   220   221   222   223   224   225   226   227