Page 665 - Bird R.B. Transport phenomena
P. 665

§20.5  'Taylor  Dispersion"  in Laminar Tube Flow  645

                     The  total mass  flow  of  A  through  a  plane  of  constant z  (that  is, the  flow  relative  to
                  the  average  velocity  (v )) is
                                     z
                                                           [н



                                            «-!?««                                   (205-13.
                                                 482)    dz
                  Next  we  note  that,  with  the  assumption  of  p  =  constant,  p(co (v ))  =  (p )(v )  and
                                                                          A
                                                                             z
                                                                                      z
                                                                                    A
                                   n
                             V
                  p(co v )  ~  (PA AZ)  =  ( Az)- (Replacing  v  by  v  is  allowed  here because, with  axial  mol-
                     A z                          z    Az
                  ecular  diffusion  neglected,  species  A  and  В are  moving  with  the  same  axial  speed).
                  Therefore  when  Eq.  20.5-13  is  divided  by  TTR, 2  we  obtain  the  averaged  mass  flux
                  expression
                                    (n )  = (p )(v )  ~ K ^  = (p )(v )  - K ^       (20.5-14)
                                                             A
                                                                z
                                            A
                                     Az
                                               z
                  relative  to stationary  coordinates. Here К  is  an  axial dispersion coefficient,  given  by  Tay-
                  lor's analysis  as
                  This  formula  indicates  that  axial  dispersion  (in the range  Pe  > >  1 considered  so  far)  is
                  enhanced by  the radial variation  of  v  and reduced by  radial  molecular  diffusion.
                                                 z
                      Although  Eq. 20.5-14  has the form  of  Fick's law  in Eq. (C) of Table  17.8-2, the present
                  equation  does  not include any  axial  molecular  diffusion.  Also  it  should  be  emphasized
                  that К is not a property  of  the  fluid mixture, but depends on R and (v ) as well as on Я1 .
                                                                                          АВ
                                                                            z
                      Next we  write  the equation  of  continuity  of  Eq. 19.1-6, averaged  over  the tube  cross
                  section, as
                                               j (pA)=  -Ji^Az)                      (20.5-16)
                                                t
                  When  the expression  for  the mass  flux  of  A  from  Eq. 20.5-14  is  inserted, we  get  the  fol-
                  lowing  axial dispersion equation'.


                                         ^(PA)  +  (V )-J-(PA)  =  KA  (PA)          (20.5-17)
                                                   Z
                                         dt          dZ       $2T
                  This  equation  can be  solved  to get  the shape  of  the  traveling  pulse  resulting  from  a 8-
                  function  input of  a mass  m A  of solute A  into a stream  of otherwise  pure B:

                                                                                     (20.5-18)

                  This can be used  along with  Eq. 20.5-15  to extract 4L  from  data on the concentrations in
                                                              AB
                  the  traveling  pulse.  In  fact,  this  is  probably  the best  method  for  reasonably  quick  mea-
                  surements  of liquid  diffusivities.
                      Taylor's  development  laid  the foundation  for  an extensive  literature on convective  dis-
                  persion.  However,  it remained  to study  the approximations  made  and  to determine their
                                    5
                  range  of validity.  Aris  gave a detailed  treatment of dispersion  in tubes and ducts, covering
                  the  full  range of t and including diffusion  in the z and в directions. His long-time asymptote






                      5
                       R. Aris, Proc. Roy.  Soc,  A235 r  67-77  (1956).
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