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§6.3  Friction Factors for  Flow around Spheres  187


                               1U
                                    \
                                      \
                               10 3
                                           \
                                             \  \
                             )n factor /  о  о   \  s



                            ."5  ю                           UP  to  a b n n f  TCP> — f\ X  1 Г)3.
                                                           s   i/
                                                         / N ч
                                         1
                                     Stokes  law  asymptote  f=^-
                               1.0
                                                                             -   ——• 55ИВ—
                               0.1
                                10 _ 3 2  5 10 _ 2 2  5  l  2  5  1 Q  2  5  ^  2  2  5  ^  5 ] ( ) 6
                                                     Reynolds number  Re = Dv x  р//л

                           Fig. 6.3-1.  Friction factor  (or drag  coefficient)  for spheres moving  relative  to a
                            fluid  with a velocity  v .  The definition of/is  given  in Eq. 6.1-5. [Curve taken
                                             x
                            from  С. Е. Lapple, "Dust and Mist Collection/' in Chemical Engineers  Handbook,
                            (J. H. Perry, ed.), McGraw-Hill, New York, 3rd edition (1950), p. 1018.]

                            is both simple and useful.  It is important to remember that
                                                 f -  0.44  for  5  X 10 2  <  Re <  1 X  10 5  (6.3-17)

                            which  covers  a  remarkable  range  of  Reynolds  numbers.  Eq.  6.3-17 is  sometimes  called
                            Newton's  resistance  law; it  is  handy  for  a  seat-of-the-pants  calculation. According  to this,
                            the drag  force  is proportional to the square  of the approach velocity  of the  fluid.
                               Many extensions  of  Fig. 6.3-1  have  been made, but  a systematic  study  is beyond  the
                            scope  of  this  text.  Among  the  effects  that  have  been  investigated  are  wall  effects 3  (see
                            Prob.  6C.2), fall  of  droplets  with  internal circulation,  hindered  settling  (i.e., fall  of  clus-
                                                                        4
                            ters  of  particles 5  that  interfere  with  one  another), unsteady  flow, 6  and  the  fall  of  non-
                            spherical  particles.  7

       EXAMPLE   6.3-1      Glass  spheres  of  density  p  sph  =  2.62  g/cm 3  are  to be  allowed  to  fall  through  liquid  CC1  at
                                                                                                    4
                            20°C in an experiment  for  studying  human reaction times  in making  time observations  with
      Determination  of  the  stopwatches  and more elaborate devices.  At  this temperature the relevant  properties  of CC1
      Diameter  of  availing  are p  =  1.59  g/cm  3  and /л = 9.58  millipoises.  What  diameter should  the spheres  be to have a 4
      Sphere                terminal velocity  of about 65 cm/s?



                                 J. R. Strom and  R. C. Kintner, AIChE  Journal, 4,153-156 (1958).
                               3
                               4
                                L. Landau and  E. M. Lifshitz,  Fluid Mechanics,  Pergamon, Oxford,  2nd edition  (1987), pp.  65-66;
                            S. Hu and  R. C. Kintner, AIChE  Journal, 1,42-48  (1955).
                                 С. Е. Lapple, Fluid and Particle Mechanics,  University  of Delaware  Press, Newark,  Del. (1951),
                               5
                            Chapter  13; R. F. Probstein, Physicochemical Hydrodynamics,  Wiley, New  York, 2nd edition  (1994), §5.4.
                               6
                                R. R. Hughes and  E. R. Gilliland, Chem.  Eng. Prog., 48,497-504  (1952);  L. Landau and  E. M.  Lifshitz,
                            Fluid Mechanics,  Pergamon, Oxford,  2nd edition  (1987), pp. 90-91.
                                E. S. Pettyjohn  and  E. B. Christiansen, Chem.  Eng. Prog., 44,147  (1948); H. A. Becker, Can. J. Chem.
                               7
                            Eng., 37, 885-891  (1959); S. Kim  and  S. J. Karrila, Microhydrodynamics: Principles and Selected Applications,
                            Butterworth-Heinemann, Boston  (1991), Chapter 5.
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