Page 74 - Bird R.B. Transport phenomena
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§2.6  Creeping Flow Around a Sphere  59

                           proaches the fixed  sphere vertically  upward  in the z direction with  a uniform  velocity  v .
                                                                                                    x
                           For this problem, "creeping  flow"  means that the Reynolds number  Re = Dv^p/ /л is less
                           than  about  0.1.  This  flow  regime  is  characterized  by  the  absence  of  eddy  formation
                           downstream  from  the sphere.
                               The velocity  and pressure  distributions  for  this creeping flow are found  in Chapter 4
                           to be
                                                           -K                                   (2.6-1)





                                                 .,=4-1     •i /     4 W  J                     (2.6-2)




                                                              V  = 0                            (2.6-3)



                                                                3
                                                   P   Po  Pgz-           c o s                 (2.6-4)
                                                                2 R   \y/

                           In the last  equation the quantity p  is  the pressure  in the plane z  = 0 far  away  from  the
                                                        0
                           sphere. The term  -pgz  is the hydrostatic pressure  resulting  from  the weight  of the  fluid,
                           and the term containing v x  is the contribution of the fluid  motion. Equations 2.6-1,2, and
                           3  show  that  the  fluid  velocity  is  zero  at  the  surface  of  the sphere.  Furthermore, in  the
                           limit as r -»  °°,  the fluid  velocity  is in the z direction with uniform magnitude p ; this  fol-
                                                                                             M
                           lows from  the fact  that v z  = v r  cos в  -  v e  sin  0, which  can be derived  by using  Eq. A.6-33,
                           and v  = v  = 0, which follows  from  Eqs. A.6-31 and 32.
                                x   y
                               The components of the stress  tensor т in spherical coordinates may be obtained  from
                           the velocity  distribution above  by using  Table B.I. They are


                                                                                                (2.6-5)




                                                                                                (2.6-6)


                           and  all  other  components  are  zero.  Note  that  the  normal  stresses  for  this  flow  are
                           nonzero, except at r  = R.
                               Let us  now  determine the force  exerted  by  the  flowing  fluid  on the sphere.  Because
                           of  the symmetry  around  the z-axis, the resultant  force  will be  in  the z direction. There-
                           fore  the  force  can be  obtained  by  integrating  the z-components  of  the normal and  tan-
                           gential  forces  over  the sphere  surface.


      Integration of  the  Normal Force
                           At  each point on the surface  of  the sphere  the fluid  exerts  a force  per  unit area  — (p +
                           r )\ r=R  on  the  solid,  acting  normal  to  the  surface.  Since  the  fluid  is  in  the  region  of
                            rr
                           greater  r  and  the  sphere  in  the  region  of  lesser  r,  we  have  to  affix  a  minus  sign  in
                           accordance with  the sign  convention established  in §1.2. The z-component of  the  force
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