Page 666 - Bird R.B. Transport phenomena
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646  Chapter 20  Concentration Distributions with More Than One Independent Variable

                              100,000




                               10,000
                                                            Taylor's
                                                           solution in
                                                           Eq.  20.5-15
                                1000


                            Q  S
                            ll  13
                           Ей    100

                                                           Taylor solution :
                                                             with  Aris 1  ;
                                                            modification  ;
                                  10       =  Equations
                                           I (48) and  (50) \  in Eq. 20.5-15  \
                                           :  of  Ref.  6

                                    diffusion
                                  0.01      0.1      1.0       10       100
                                               Dimensionless time
                                                   ® AB t/R 2
                          Fig.  20.5-2.  Sketch showing  the limits  of the Taylor  (Eq. 20.3-15)
                          and Aris (Eq. 20.5-19) expressions  for the axial  dispersion
                          coefficient.  This figure  is patterned after  one in Ref. 6.

                           is an important extension  of  Eq. 20.5-15. From this result, we  see that molecular  diffusion
                           enhances  the axial  dispersion  when  the Peclet number  Pe  = R(v )/^ AB  is  less  than  V48
                                                                                 z
                           and  inhibits axial  dispersion  at larger  Peclet numbers, where Taylor's  mode of transport
                           predominates.
                              The ranges  of validity  of  the Taylor and Aris dispersion  formulas  have been studied
                                                               6
                                                                                          7
                           thoroughly by  finite  difference  calculations  and by  orthogonal collocation.  Figure 20.5-
                           2 shows  the useful  ranges  of  Eq. 20.5-15 and  19. The latter formula  has been widely  used
                                                                                8
                           for  measurements  of  binary  diffusivities,  and  an extension  of  it  has been used  to mea-
                           sure ternary diffusivities  in liquids.
                              Several  further  investigations  on  convective  dispersion  will  be  mentioned  here.
                           Coiled tubes give reduced longitudal dispersion, as shown by  the experiments  of  Koutsky
                           and Adler 9  and analyzed  for laminar flow by Nunge, Lin, and Gill.  This effect  is impor-
                                                                                   10
                           tant  in  chemical reactor design  and  in  diffusivity  measurements, where  coiling  is  often
                           necessary  to get enough tube length into a compact apparatus.
                              Extra-column  dispersion, caused  by  the pump and connecting tubing  of chromato-
                           graphic  systems,  was  investigated  by  Shankar  and  Lenhoff 11  with  detailed  predic-


                               V. Ananthakrishnan, W. N. Gill, and A. J. Barduhn, AlChE  Journal  11,1063-1072  (1965).
                              6
                              7
                                J. C. Wang  and W.  E. Stewart, AIChE  Journal, 29,493-497  (1983).
                               Ph. W. M. Rutten, Diffusion in Liquids, Delft University  Press, Delft, The Netherlands (1992).
                              8
                               J. A. Koutsky  and  R. J. Adler,  Can. J. Chem. Eng., 42, 239-246  (1964).
                              4
                              10
                                R. J. Nunge, T. S. Lin, and W. N. Gill, /. Fluid Mech., 51,363-382  (1972).
                              11
                                A. Shankar and A.  M. Lenhoff,  /. Chromatography, 556, 235-248  (1991).
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