Page 600 - Bird R.B. Transport phenomena
P. 600

580  Chapter 18  Concentration Distributions in Solids and in Laminar Flow

                          (c)  Verify  (lengthy!) that the solution

                                                 c  =   *  exp[-(u /2Q) )(s  -  2)]          (18C.1-3)
                                                  A              o    AB
                                                     47Г  J) AB S
                          satisfies the differential  equation above.
                          (d)  Show further  that the following boundary conditions are also satisfied by  Eq. 18C.1-3:



                          B.C. 2:                 ass-*  0,  -4TTS ^  B  -Г^-> W A           (18C.1-5)
                                                                  2
                                                                      dS
                          B.C.3:                  atr  = O,  Ц^  = О                         (18С.1-6)
                                                             оГ
                          Explain the physical  meaning of each of these boundary conditions.
                          (e)  Show how data on c {r, z) for  given v  and ЯЬ  may be plotted, when the preceding solu-
                                                           0
                                              A
                                                                  АВ
                          tion applies, to give a straight line with slope у /2ЯЬ  and intercept In %b .
                                                               о
                                                                    АВ
                                                                                     AB
                    18C2.  Diffusion  and  reaction in  a partially impregnated catalyst.  Consider a catalytic sphere like
                          that in §18.7, except that the active ingredient of the catalyst  is present only in the annular re-
                          gion between r = KR and r = R:
                          In region I (0 < r <  KR),    k"a = 0                              (18C.2-1)
                          In region  II (KR<T<  R),     k"a = constant > 0                   (18C.2-2)
                          Such a situation may arise when the active ingredient is put on the particles after  pelleting, as
                          is done for  many commercial catalysts.
                          (a)  Integrate Eq. 18.7-6 separately  for  the active and inactive regions. Then apply  the appro-
                          priate boundary conditions to evaluate the integration constants, and solve for the concentra-
                          tion profile  in each region. Give qualitative sketches to illustrate the forms  of the  profiles.
                          (b)  Evaluate W , the total molar rate of conversion  of Л in a single particle.
                                       AR
                    18C.3.  Absorption  rate in  a falling  film.  The result in Eq. 18.5-18 may be obtained by  an alternative
                          procedure.
                          (a)  According  to an overall mass balance on the film, the total moles  of A  transferred  per unit
                          time  across  the  gas-liquid  interface  must  be  the  same  as  the  total  molar  rate  of  flow  of  A
                          across the plane z  = L. The latter rate is calculated as  follows:

                                          W A  = lim(W5z; max )(i  f * c \ = dx)  =  V\fo max  f"  c \ dx  (18C.3-1)
                                                                L
                                                              A z
                                                                                A z=L
                                               8->oo    \O  JQ     )        JQ
                          Explain this procedure  carefully.
                          (b)  Insert the solution for c A  in Eq. 18.5-15 into the result  of  (a) to obtain:



                                                                                             (18C.3-2)

                          In the second line, the new variable  и = x/V4® L/v max  has been introduced.
                                                               AB
                          (c)  Change the order of integration in the double integral, to get

                                                                                             (18C.3-3)

                          Explain by  means of  a carefully  drawn  sketch how the limits are chosen for  the integrals The
                          integrals may now be done analytically  to get  Eq. 18.5-18.
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