Page 654 - Bird R.B. Transport phenomena
P. 654

634   Chapter 20  Concentration Distributions with  More Than One Independent  Variable

                           according to Eq. A.7-16. The diffusion  equation for the concentration boundary layer  is then




                           where  Eqs.  A.7-15  and  17  have  been  used.  In  writing  these  equations  it  has  been  as-
                           sumed  that:  (i)  the  x-  and  z-components  of  the  diffusion  flux  are  negligible,  (ii)  the
                           boundary  layer  thickness  is  small  compared  to  the  local  interfacial  radii  of  curvature,
                           and  (iii) the density  and diffusivity  are constant. We  now want  to get  formal  expressions
                           for  the concentration profiles  and  mass  fluxes  for  two  cases  that are  generalizations  of
                           the problems  solved  in §18.5 and  §18.6. When  we  get  the expressions  for  the local  molar
                           flux  at  the  interface,  we  will  find  that  the  dependences  on  the  diffusivity  ({-power  in
                           §18.5 and the f-power  in §18.6) correspond  to cases  (a) and  (b) below.  This turns out to be
                           of  great  importance in the establishment  of  dimensionless  correlations  for  mass  transfer
                           coefficients,  as we  shall  see  in Chapter 22.


     Zero Velocity Gradient at the  Mass Transfer  Surface
                           This situation arises  in a surfactant-free  liquid  flowing around a gas bubble. Here v x  does
                           not  depend  on  y,  and  v  can  be  obtained  from  the equation  of  continuity  given  above.
                                               y
                           Therefore,  for  small  mass-transfer  rates we  can write  general  expressions  for  the  velocity
                           components  as
                                                     v x  = v (x,z)                            (20.3-3)
                                                          5



                           where  у depends  on x and  z. When  this is  used  in  Eq. 20.3-2, we  get  for  the diffusion  in
                           the liquid  phase
                                                     ]_^A__^A.       ^  ^ л                    (20.3-5)
                                                    V              =
                           which  is to be solved  with  the boundary conditions

                           B.C.I:                      atx  = 0,   c A  = 0                    (20.3-6)
                           B.C. 2:                     at у  = 0,  c  = c                      (20.3-7)
                                                                    A   A0
                           B.C.3:                      as у o o ,  CA  -> 0                    (20.3-8)
                                                           ^
                           The nature of  the boundary  conditions suggests that a combination  of  variables  treatment
                           might be appropriate. However,  it is  far  from  obvious  how  to construct an appropriate di-
                           mensionless combination. Hence we  try the following:  let c /c  = fit]), where  17 = y/8 (x,  z),
                                                                          A  A0                 A
                           and 8 (x, z) is the boundary layer  thickness  for  species  A, to be determined later.
                               A
                               When  the indicated combination  of  variables  is introduced into Eq. 20.3-5, the equa-
                           tion becomes



                           with  the  boundary  conditions:  /(0)  =  1  and  /(00)  =  0.  If,  now,  the  coefficient  of  the
                           7]{df/dj])  term  were  a  constant, then  Eq.  20.3-9  would  have  the same  form  as  Eq.  4.1-9,
                           which  we  know  how  to solve.  For convenience we  specify  the constant as

                                                                         =  2                  (20.3-10)

                           Next we  insert the expression  for  у  from  Eq. 20.3-4 and rearrange the equation thus:

                                                             m
                                                     2
                                                                     2
                                                    8
                                                  T" A + I T "  (h-v,) 2  ]8  =  — ^ - ^      (20.3-11)
                                                                      A
                                                  dx  A  \dx    -  5  /  A  v 5
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