Page 563 - Bird R.B. Transport phenomena
P. 563

§18.1  Shell mass balances; boundary conditions
                            §18.2  Diffusion  through a stagnant gas  film

                            §18.3  Diffusion  with  a heterogeneous chemical reaction
                            §18.4  Diffusion  with  a homogeneous chemical reaction
                            §18.5  Diffusion  into a falling liquid  film  (gas  absorption)
                            §18.6  Diffusion  into a falling liquid  film  (solid  dissolution)
                            §18.7  Diffusion  and chemical reaction inside a porous  catalyst
                            §18.8°  Diffusion  in a three-component gas  system




                            In Chapter 2 we  saw  how  a number  of  steady-state  viscous  flow  problems  can be  set up
                            and  solved  by  making  a  shell  momentum  balance. In  Chapter  9  we  saw  further  how
                            steady-state  heat-conduction problems  can be handled by  means  of  a shell energy balance.
                            In this chapter we  show  how  steady-state  diffusion  problems may be formulated  by shell
                            mass balances. The procedure used  here is virtually  the same as  that used  previously:
                                a.  A  mass  balance  is  made  over  a thin shell  perpendicular  to the direction  of  mass
                                  transport, and this shell  balance leads  to a first-order  differential  equation, which
                                  may be solved to get the mass flux distribution.
                               b.  Into  this  expression  we  insert  the relation  between  mass  flux  and concentration
                                  gradient, which  results  in a second-order  differential  equation  for  the concentra-
                                  tion  profile.  The integration constants that appear  in the resulting  expression  are
                                  determined by  the boundary conditions on the concentration and/or mass flux at
                                  the bounding  surfaces.
                               In Chapter  17 we  pointed  out  that several  kinds  of  mass  fluxes  are  in common use.
                            For simplicity,  we  shall  in this chapter use the combined flux  N —that  is, the number  of
                                                                                 A
                            moles  of Л that go through a unit area  in unit time, the unit area being  fixed  in space.  We
                            shall  relate the molar flux to the concentration gradient by  Eq. (D) of  Table  17.8-2, which
                            for  the z-component is

                                                   N Az  =  -c® AB  ^  + x (N Az  + N )         (18.0-1)
                                                                     A
                                                                             Bz
                                                combined  molecular  convective
                                                flux     flux      flux
                            Before  Eq.  18.0-1  is  used,  we  usually  have  to  eliminate  N .  This  can  be  done  only  if
                                                                              Bz
                            something  is  known  beforehand  about  the ratio N /N .  In each  of  the binary  diffusion
                                                                         Az
                                                                      Bz
                                                                                                   543
   558   559   560   561   562   563   564   565   566   567   568