Page 642 - Bird R.B. Transport phenomena
P. 642

622   Chapter 20  Concentration Distributions with  More Than One Independent Variable

                                  t == 0                          t> 0
                                  z,        Semi-infinite medium  z ,
                                             in  region z > 0. The
                                             mass transfer  surface
                                            Sit)  changes with time
                                                uniformly.     ^
                                   ^   ^                                    /  ^


                                    уУ^       У       ^ y ^     ^
                                                                       C A  ~  c A0
                                    atz  = 0
                                                                       atz  = 0
                           Fig.  20.1-4.  Time-dependent diffusion  across  a mass  transfer  interface
                           Sit)  that is changing  with  time. The liquid  B, in the region  above  the
                           plane z = 0, has a velocity  distribution  v x  = +\ax, v y  = +\ay, and
                           v 2  = -az,  where a = d In S/dt.





                           Since Eq. 20.1-62 is solved by  the method  of combination  of variables,  the same technique can
                           be tried here. We  postulate

                                                                                              (20.1-66)

                           Substitution  of  this trial solution into Eq. 20.1-65 gives

                                                                                              (20.1-67)

                           If we  set the expression  within  the brackets  equal  to unity, then we  accomplish  two things: (i)
                           we  obtain  an  equation  for  g  that  has  the  same  form  as  Eq.  4.1-9,  to  which  the  solution  is
                           known;  (ii) we  get an equation  for 8 as a function  of t:

                                                                                              (20.1-68)

                           This equation may be integrated  to give
                                                     г  sum)
                                                         d(SSf  = №    S4t)dt                 (20.1-69)
                                                    Jo            AB
                           The  lower  limit  on the  left  side  is  chosen  so  as  to ensure  that c A  = 0 initially  throughout the
                           fluid.  This choice then leads to

                                                                          2
                                                    S(t)  =J43) ]  [S(t)/S(t)] dt             (20.1-70)
                                                            AB
                           and  we  get  finally  for the concentration  profiles

                                                 £*- =  !-erf       Z -                       (20.1-71)
                                                 C
                                                  A0                        2
                                                                M f  [S(t)/SU)] dt
                           The interfacial mass flux is then obtained by differentiating  Eq. 20.1-71 to get
                                                                           Л-1/2
                                                    = c A                                     (20.1-72)
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