Page 662 - Bird R.B. Transport phenomena
P. 662

642  Chapter 20  Concentration Distributions with More Than One Independent Variable

       SOLUTION             Rewriting  Eq. 20.1-66 with  a boundary  layer  thickness  function  8(u, w, t) leads  by  analogous
                            steps  to the relation

                                                                                2
                                                5(w,w?,f)=  *®AB\  [s(u,w,t)/s{u,w,t)] dt       (20.4-21)
                                                         V     Jo
                            and  the corresponding generalizations  of  Eqs. 20.1-71 and 72:
                                                                      z
                                                                                                (20.4-22)
                                                                                2
                                                                l[s{u,w,~t)/s(u,w,t)] d~t
                                                                                 _ \ - 1 / 2
                                                                  ' >
                                             N ,o  = CAO  I ^ T  ( 7  I  [ s ( w  w  f)/s(w '  w > ^  d ~ f  (20.4-23)
                                               A
                                                     \  TTf  \t  J o              )
                            These  solutions,  unlike  Eq.  20.1-71  and  Eq.  20.1-72,  include  the  spatial  variations  of  the
                            boundary  layer  thickness  and  interfacial  molar  flux  N  that  occur  in  nonuniform  flows.
                                                                         Az0
                            Local stretching  of  the interface  (as at stagnation  loci) thins the boundary  layer  and enhances
                            N .  Local interfacial  shrinkage  (at separation  loci) diminishes N , but also  ejects  stale  fluid
                              Az0                                               Az0
                            from  the boundary  layer,  allowing  its  mixing  into the interior  of  the same  phase.  Observa-
                            tions  of  mass  transfer  enhancement by  such  mixing  have  been  interpreted by  some  workers
                            as  "surface  renewal/ 7  even  though creation  of  new  surface  elements  in an existing  surface  is
                            not  permitted in continuum fluid  mechanics.
                                These  results,  and  others  for  negligible  v ,  are  obtainable  conveniently  by  introducing
                                                                 z0
                            the  following new variables  into Eq. 20.4-19:
                                                                     =
                                                 Z  = zs(u, w, t)  and  r • =  s\u,  w, w, t)dt  (20.4-24,25)
                                                                          s\u,
                                                                       Jo Jo
                            In the absence  of  chemical reactions, the resulting  differential  equation  for  the concentration
                            function  c (u, w, Z, T) becomes
                                    A
                                                            5  =  ^«§J                          (20.4-26)

                            This is a generalization  of Fick's second law  to an asymptotic relation  for  forced  convection in
                            free-surface  flows.


        EXAMPLE 20.4-2      Show  how  to generalize  Example  20.1-2  to flow  systems,  by  using  Eq. 20.4-26 for  the two re-
                            action-free zones.
       Gas  Absorption  with
       Rapid  Reaction  and  SOLUTION
       Interfacial  Deformation
                            Using Eq. 20.4-26, we  get the following replacements for  Eqs. 20.1-26 and 27:
                                                    ^  = ЯЬ А5  д -Ц  for 0 <  Z <  Z R         (20.4-27)

                                                                           z <
                                                                                                -~
                                                    S  = % s  §    for ZR  ~  °°              (20 4 28)
                            Now  the reaction plane z  = z R  of  the original  example  is  a  time-dependent surface,  Z  = Z ,  or
                                                                                                     R
                            z (u,  w, t) = Z /s(u,  w, t). The initial and boundary conditions remain as before, subject  to this
                                       R
                             R
                            generalization  of the reaction-front location.
                                The  solutions  for c  and c  then take the forms  in Eqs. 20.1-35 and 36, with z/Vf  replaced
                                               A    B
                            by  Z/VT,  and  z /Vt  by  Vy.  The latter constant is  again  given  by  Eq. 20.1-37.  The enhance-
                                         R
                            ment  of the absorption rate by the chemical reaction accordingly  parallels  the expressions  that
                            will be given in Eq. 22.5-10, and simplified  in Eqs. 22.5-11  through 13.
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