Page 111 - Bird R.B. Transport phenomena
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96  Chapter 3  The Equations of Change for  Isothermal Systems

                          This  is  an  "equidimensional  equation/'  which  may  be  solved  by  assuming  a  trial  solution
                          / = r" (see Eq. C.l-14). Substitution  of this trial solution into Eq. 3.6-51 gives  ;/ = 1, -2. The so-
                          lution  of  Eq. 3.6-51 is then
                                                           /=С,г  + ^                          (3.6-52)

                          so that
                                                     v^r, в)  =   •  —  } sin  I               (3.6-53)

                                                                                    3
                          Application  of  the boundary  conditions shows that  Cj  = 0 and  C  = (1R . Therefore  the  final
                                                                               2
                          expression  for  the velocity  distribution  is
                                                                v  sin (                       (3.6-54)
                          Next we evaluate the torque needed to maintain the rotation of the sphere. This will be the in-
                          tegral, over  the sphere surface,  of the tangential force  (т \ )Я  sin в(1в(1ф exerted  on the  fluid
                                                                             2
                                                                       гф г=к
                          by a solid  surface  element, multiplied by  the lever arm R sin в for  that element:
                                              7\  =  \ llT  V  (r )\ r=R  (R sin  $)R  sin  вйвйф
                                                                      2
                                                         r(l
                                                  Jo  Jo
                                                   Г2тт  Гтт
                                                                         2
                                                        (3/хП sin  6)(R sin  0)R  sin  вйвйф
                                                  Jo  Jo
                                                            si
                                                         Г sin ed6
                                                              3
                                                         Jo
                                                                                               (3.6-55)
                          In going from  the first  to the second  line, we  have used  Table  B.I, and in going from  the sec-
                          ond  to the third line we  have  done the integration over  the range  of  the ф variable.  The inte-
                          gral  in the third line is |.
                              As  the angular  velocity  increases, deviations  from  the "primary  flow"  of  Eq. 3.6-54 occur.
                          Because  of  the centrifugal  force  effects,  the  fluid  is  pulled  in  toward  the poles  of  the  sphere
                          and  shoved  outward  from  the equator  as  shown  in  Fig.  3.6-8.  To  describe  this  "secondary
                          flow/'  one has to include the  [v •  Vv]  term in the equation  of  motion. This can be done by  the
                          use  of a stream-function method. 6














                                                     Fig. 3.6-8.  Rough sketch showing  the secondary  flow
                                                     which appears around a rotating sphere as the Reynolds
                                                     number is  increased.


                              6  See, for example, the development by  O. Hassager  in  R. B. Bird, R. C. Armstrong, and O.  Hassager,
                           Dynamics  of Polymeric Liquids, Vol.  1., Wiley-Interscience, New  York, 2nd edition (1987), pp. 31-33. See also
                           L. Landau and  E. M. Lifshitz,  Fluid Mechanics, Pergamon, Oxford,  2nd edition (1987), p. 65; and  L. G. Leal,
                           Laminar Flow and Convective Transport Processes, Butterworth-Heinemann, Boston  (1992), pp. 180-181.
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