Page 582 - Bird R.B. Transport phenomena
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562  Chapter 18  Concentration Distributions in Solids and in Laminar Flow
                                                               Fig. 18.6-1.  Solid A dissolving into a falling  film
                                                               of liquid  B, moving  with a fully  developed  para-
                            Near wall                Parabolic  bolic velocity  profile.
                                                      velocity
                            v ~№)y                   profile of
                             z
                                                      fluid В
                                         Insoluble
                                         '  wall

                                          -Slightly soluble
                                           wall made of A

                                           с  = saturation
                                            А0
                                            concentration
                                           - c A (y,  z)
                                                       =
                                                     c A


      §18.6  DIFFUSION INTO A FALLING LIQUID FILM
             (SOLID DISSOLUTION)       1
                            We now  turn to a falling  film  problem that is different  from  the one discussed  in the pre-
                            vious  section.  Liquid  В is  flowing  in laminar  motion down  a  vertical  wall  as  shown  in
                            Fig. 18.6-1. The film  begins  far  enough up the wall so that v  depends only on у  for z  >  0.
                                                                             z
                            For 0 <  z <  L the wall is made  of  a species  A  that is slightly  soluble  in B.
                               For  short  distances  downstream,  species  A  will  not  diffuse  very  far  into the  falling
                            film.  That is, A  will be present only in a very thin boundary  layer  near the solid  surface.
                            Therefore the diffusing  A  molecules will experience  a velocity  distribution that is charac-
                            teristic  of  the falling  film  right  next  to the wall, у  =  0. The velocity  distribution  is  given
                            in Eq. 2.2-18.  In the present situation cos 0 =  1, and x  = 8  — y, and

                                                                                                (18.6-1)


                            At  and  adjacent  to the wall  (y/8) 2  «  (y/8),  so that for  this problem the velocity  is, to a
                            very  good  approximation, v z  =  (pg8//x)y  =  ay. This  means  that Eq.  18.5-6, which  is  ap-
                            plicable here, becomes  for  short distances  downstream


                                                         *£-9»^                                 08.6-2,

                            where  a = pg8//x.  This  equation  is to be solved  with  the boundary  conditions
                            B.C.I:                      at 2 =  0,  c A  = 0                    (18.6-3)
                            B.C. 2:                     at у  = 0,  c  = c                      (18.6-4)
                                                                    A   A0
                            B.C.3:                      aty=°o,     c  = 0                      (18.6-5)
                                                                    A
                            In the second boundary condition, c A0  is the solubility  of A  in  B. The third boundary con-
                            dition  is  used  instead  of  the  correct  one  (дс /ду  =  0  at  у  =  8), since  for  short  contact
                                                                  А
                            times  we  feel  intuitively  that  it will  not make  any  difference.  After  all,  since  the mole-


                               1
                                 H. Kramers and P. J. Kreyger, Chem. Eng. Sci., 6,42-48 (1956); see also R. L. Pigford, Chem. Eng.
                            Prog. Symposium Series No. 17, Vol. 51, pp. 79-92 (1955) for the analogous heat-conduction problem.
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