Page 663 - Bird R.B. Transport phenomena
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§20.5  'Taylor  Dispersion"  in Laminar Tube Flow  643

                                                                                 Fig. 20.5-1.  Sketch  show-
                                   I           Parabolic velocity                ing the axial  spreading  of
                            Pulse  I '  z  =  0  profile  in a circular tube  z = L  a concentration pulse in
                           injected  '                 \                         Taylor dispersion  in a
                            here
                                                                                 circular tube.



                                                           t =  l/<v z >






      §20.5  "TAYLOR    DISPERSION" IN LAMINAR        TUBE FLOW

                           Here  we  discuss  the  transport  and  spreading  of  a  solute  "pulse''  of  material  A  intro-
                           duced  into  fluid  В in  steady  laminar  flow  through  a  long,  straight  tube  of  radius  R, as
                           shown  in Fig. 20.5-1. A pulse  of mass  m A  is introduced at the inlet 2 = 0 over  a very short
                           period  near  time  t  =  0, and  its  progress  through  the tube  is  to be  analyzed  in the  long-
                           time limit. Problems  of  this type  arise  frequently  in process  control (see Problem 20C.4),
                                                     1
                           medical diagnostic procedures,  and in a variety  of environmental applications.  2
                               A  short distance downstream  from  the inlet, the 0-dependence  of  the mass  fraction
                           distribution will die out. Then the diffusion  equation for a> (r, z, t) in Poiseuille  flow  with
                                                                             A
                           constant \x, p, and ЯЬ  takes the  form
                                             АВ
                                                                                               (20.5-1)

                           This equation is to be solved with  the boundary conditions

                           B.C. 1 and 2:          at  r  = 0 and at r  = R,  -^  = 0           (20.5-2)
                                                                        oY
                           which  express  the radial symmetry  of  the mass  fraction  profile  and  the impermeability  of
                           the tube wall to diffusion.  For this long-time analysis  it is not necessary  to specify  the exact
                           shape  of  the pulse  injected  at  t  =  0. No exact  analytical  solution  is  available  for  the  mass
                           fraction  profile  u> {r,  z, t)—even  if  an  initial  condition were  clearly  formulated—but  Tay-
                                           A
                           lor ' 3 4  gave  a  useful  approximate  analysis  that we  summarize  here. This  involves  getting
                           from  Eq. 20.5-1 a partial differential  equation for the cross-sectional  average  mass  fraction
                                                       Г27Г  (R
                                                            o) r  dr d6
                                                              A
                                                      Jp  JQ
                                                                    =  —    (o r  dr           (20.5-3)
                                                                             A
                                                             rdrdB
                           which  can then be solved to describe  the behavior  at long  times.



                               1  J. B. Bassingthwaighte  and C. A. Goresky, in Section 2, Volume  3 of Handbook of Physiology, 2nd
                           edition, American Physiological  Society, Bethesda, Md. (1984).
                               2  P. С  Chatwin and C.  ML Allen, Ann.  Rev. Fluid Mech., 17,119-150  (1985); В. Е. Logan,
                           Environmental  Transport  Processes, Wiley-Interscience, New York  (1999), Chapters 10 and 11; J. H.
                           Seinfeld, Advances  in Chemical Engineering, Academic Press, New York  (1983), pp. 209-299.
                               3
                                G. I. Taylor, Proc. Roy. Soc. A219,186-203  (1953).
                               4
                                G. I. Taylor, Proc. Roy. Soc,  A225, 473^77  (1954).
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