Page 141 - Bird R.B. Transport phenomena
P. 141

§4.2  Solving  Flow Problems Using a Stream Function  125

                    To get  the pressure  distribution, we  substitute  these velocity  components into the r- and
                 ^-components  of  the Navier-Stokes  equation  (given  in Table  B.7). After  some tedious manip-
                 ulations we  get
                                            fi7W






                 These equations may be integrated  (cf.  Eqs. 3.6-38 to 41), and, when use is made of the bound-
                 ary  condition that as r —»  °°  the modified  pressure  9? tends to p 0  (the pressure  in the plane z =
                 0 far  from  the sphere), we  get

                                        p  = p  - pgz - I {~){jj  cos в               (4.2-17)
                                             0

                 This is the same as the pressure  distribution given  in Eq. 2.6-4.
                    In  §2.6 we  showed  how  one can integrate the pressure  and  velocity  distributions  over
                 the sphere  surface  to get  the drag  force.  That method  for  getting  the  force  of  the fluid  on
                 the  solid  is  general.  Here we  evaluate  the  "kinetic  force"  F  by  equating  the rate  of  doing
                                                                 k
                 work  on  the sphere  (force  X  velocity)  to  the  rate  of  viscous  dissipation  within  the  fluid,
                 thus

                                      F k *  =  ~\    (TiVv)rrfr  sin  Ш&ф           (4.2-18)
                                       v
                                             Jo  Jo  JR
                 Insertion  of the function  (—T:VV) in spherical coordinates from  Table  B.7 gives









                 Then the velocity  profiles  from  Eqs. 4.2-13 and  14 are substituted  into Eq. 4.2-19. When  the in-
                 dicated differentiations  and integrations (lengthy!) are performed, one finally  gets

                                                 F  = бтг/jiV^R                      (4.2-20)
                                                  k
                 which is  Stokes'  law.
                    As  pointed out in  §2.6, Stokes 7  law  is  restricted  to Re <  0.1. The expression  for  the drag
                 force  can be improved  by  going  back and including  the  [v •  Vv]  term. Then use  of  the method
                 of matched asymptotic expansions leads to the following result 4

                                                                         3
                                             2
                    F  = бтг/Ai^RIl  + re Re + T^ Re (ln  \ Re + у  + |  In 2 -  fi)+  ^  Re  In  \ Re + О (Re )]
                                                                                      3
                     k
                                                                                     (4.2-21)
                 where  у  = 0.5772 is Euler's constant. This expression  is good up to Re of about 1.





                     1. Proudman and J. R. A. Pearson, /. Fluid Mech. 2, 237-262  (1957); W. Chester and  D. R. Breach,
                    4
                 /. Fluid. Mech. 37, 751-760  (1969).
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