Page 398 - Modelling in Transport Phenomena A Conceptual Approach
P. 398

378       CHAPTER 9.  STEADY MICROSCOPIC BALANCES WITH GEN.

              4. The concentration of  dZ3 does not interfere with the diffusion of  A through
                 f?, i.e.,  A molecules, for the most part, hit molecules l? and hardly ever hit
                 molecules AB. This is known as the pseudo-binary behavior.

               Since CA = CA(Z), Table C.8 in Appendix C indicates that the only non-zero
            molar flux component is NA. and it is given by

                                                                             (9.42)

            For  a differential volume element of  thickness A2, as shown in Figure 9.14,  Q.
            (9.41) is expressed as

                               NA, 1% A - NA, lz+Az A + %A A Az = 0          (9.43)
            Dividing Eq. (9.43) by AAz and taking the limit as Az + 0 gives


                                                                             (9.44)


                                                                             (9.45)

            The use of Eq. (5.3-26)  gives the rate of  depletion of  species A per unit volume as

                                          %A=-kCA                            (9.46)
            Substitution of  Eqs.  (9.42) and (9.4-6)  into Eq. (9.45) yields


                                                                             (9.47)

            The boundary conditions associated with the problem are

                                     at  z = 0    CA =CA,                    (9.48)

                                     at  z=L      -- -0                      (9.49)
                                                  dCA
                                                   dz
            The value of CA,  in Eq. (9.48) can be determined from  Henry’s law.  The boundary
            condition given by Eq. (9.49) indicates that since species A cannot diffuse through
            the bottom of  the container, i.e.,  impermeable wall, then, the molar flux and the
            concentration gradient of  species A are zero.
               The physical significance and the order of magnitude of the terms in Eq. (9.47)
            are given in Table 9.2.  Therefore, the ratio of  the rate of  reaction to the rate of
            diffusion is given by

                              Rate of reaction  -   IccAo   - k L2
                                             -
                                                           --
                              Rate of  diffusion   DABCAo/L2   DAB          (9.410)
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