Page 630 - Bird R.B. Transport phenomena
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610  Chapter 19  Equations of Change for  Multicomponent Systems


                            In  their  experimental arrangement, С was  a  condensable vapor,  which  could  be separated
                            from A and В by lowering the temperature so that С would  be  liquefied.
                               We  want to study  the details  of  the three-component  diffusion  taking place in the  diffu-
                            sion tube of length L, when the apparatus is operated at steady state. Obtain an expression re-
                            lating the concentrations x A]  and x m  at the feed  end  of  the tube to the concentrations x A2  and
                           x B2  at  the product end. This  expression  will  contain the  molar  fluxes  of  the  three  species,
                            which are controlled by the rates of addition of materials in the two entering streams.
                               Use the following  notation for  dimensionless quantities: £ = z/L  for  the  distance  down
                            the tube from  the feed  entrance; r A = 4b AB/4b AC and  r B = 3) ./0)  for the diffusivity  ratios; and
                                                                               вс
                                                                          ль
                            v a  = N L/c3) AB  for the molar fluxes  (with a  = А,  В,  С).
                                 QZ
                            (a)  Shows  that, in terms of  these dimensionless quantities, the Maxwell-Stefan  equations  for
                            the diffusion  are
                                                                        +
                                                                  • Y AB x B  Y A
                                                      Щ   = Y x  + Y x  + Y                    (19D.3-2)
                                                             BA A  BB B   B
                            where У лл  = v  + г (^  л  + y ), У лв  = ^ (г  -  1), and Y A  = ~r v , and the remaining quantities
                                                            л
                                       B
                                                                           A A
                                                  c
                                           л
                                                          л
                            are obtained by interchanging A and B.
                            (b)  By using Laplace transforms, solve Eqs. 19D.3-1 and 2 to get the concentration profiles  for
                            A and В in the tube.
                            (c)  Show that the terminal concentrations are interrelated thus,
                                        _X A {x AU x B} ;0)  X A {x AU x Bl ;p+)expp +  X A (x M ,x B] ;p  ) exp  p  М О ¥ Л О _
                                      X A 2  —  ——   ~r      ;           1             —      \iy\J.D-5)
                                              V+V-         рЛр +  -р-)         рЛр   -р + )
                            in which
                                      V,  =  ШЛА  +  YBB) ±  V(Y^  +  Y BB ) 2  + 4У„У Ь , Л ]  (19D.3-4)
                                      ХлЬли  хви  Р) =  ?*АХ  +  P(YA  ~  x M Y BB  +  x B] Y AB )  +  (Y AP Y B  -  Y BD Y A )  (19D.3-5)
                            A similar expression  may be obtained for x .  Keyes and Pigford' give further results  for spe-
                                                                               (
                                                              B1
                            cial cases.
                     19D.4.  Steady-state  diffusion  from a rotating disk. 7  A large  disk  is rotating with  an angular veloc-
                            ity Vi in an infinite expanse  of liquid  B. The surface  is coated with a material A  that is  slightly
                            soluble in  B. Find the rate at which A  dissolves  in  B. (The solution to this problem can be ap-
                            plied to a disk  of  finite radius R with negligible error.)
                               The fluid  dynamics of this problem was developed by von Karman  and later corrected by
                                                                                    8
                            Cochran.  It was  found that the velocity components can be expressed, except near the edge, as
                                   9
                                              v  = £lrF(Q;  v e =  D,rG(0;  =  Vlh>H(0         (19D.4-1)
                                               r                        v z
                            in which £ = zwOjv.  The functions  F, G, and H have the following  expansions, 8
                                                         2
                                                  F = at-\t -  \Ъ£ Ъ  -  WC                     (19D.4-2)
                                                  G = 1 + Ц  + \a?  + ~(ab -  1)£ 4            (19D.4-3)
                                                  H = -a?  + k  3  + k  4  +  • '  •           (19D.4-4)
                            in  which  a  =  0.510  and  b  =  -0.616.  It  is  further  known  that,  in  the  limit  as  f  —> °°, H —>
                            -0.886, and  F, G, F', and  G' all approach  zero. Also it is known  that the boundary  layer  thick-
                            ness is proportional  to \TvJVL, except near the edge  of the  disk.


                               7
                                 V. G. Levich, Physicochemical Hydrodynamics,  Prentice-Hall,  Englewood  Cliffs,  N.J. (1962), §11.
                               8
                                 T. von Karman, Zeits. f. angew. Math. u. Mech.,1, 244-247 (1921).
                               9
                                 W. G. Cochran,  Proc. Camb. Phil. Soc,  30, 365-375  (1934).
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