Page 124 - Bird R.B. Transport phenomena
P. 124

Problems  109

                       I Fluid in                      (d)  Write out all the nonzero components of т for this flow.
                                                       (e)  Repeat the problem for concentric spheres.
                            Radial flow outward
                              between disks
                                                       3B.12  Pressure  distribution  in  incompressible  fluids.
                                                       Penelope  is  staring  at a beaker  filled  with  a liquid, which
                                                       for  all practical purposes can be considered as incompress-
                                                       ible; let its  density  be p .  She tells  you  she  is  trying  to un-
                                                                         0
                                                       derstand how the pressure in the liquid  varies  with depth.
                                                       She has taken the origin  of coordinates at the liquid-air in-
                                                       terface, with the positive z-axis pointing away  from the liq-
      Fig. 3B.10.  Outward radial flow  in the space between  two  uid. She says to you:
      parallel, circular disks.
                                                          "If  I  simplify  the  equation  of  motion  for  an incom-
                                                       pressible  liquid  at rest, I get 0 =  -dp/dz  -  pog. I can solve
      (b)  Show  how  the  equation  of  continuity  enables  one to  this  and  get  p  =  p  -  pogz.  That seems  reasonable—the
                                                                      alm
      simplify  the equation of motion to give         pressure increases with increasing depth.
                                                          "But, on the other hand, the equation  of  state  for  any
                                                       fluid  is p  = p(p, T), and  if the system  is at constant temper-
                                                       ature, this just  simplifies  top  = p(p). And, since the fluid  is
      in which ф = rv r  is a function  of z only. Why  is ф indepen-  incompressible,  p  =  p(p ),  and  p  must  be  a  constant
                                                                           0
      dent  of r?                                      throughout the fluid!  How can that be?"
      (c)  It can be  shown  that no solution exists  for  Eq.  3B.10-1  Clearly  Penelope needs  help. Provide  a useful  expla-
      unless  the nonlinear term containing ф is  omitted. Omis-  nation.
      sion  of  this  term  corresponds  to  the  "creeping  flow  as-  3B.13  Flow of  a fluid through a sudden contraction.
      sumption." Show that for creeping flow, Eq. 3B.10-1 can be  (a)  An incompressible liquid  flows  through a sudden con-
      integrated with respect to r to give
                                                       traction  from  a pipe  of  diameter D l  into a pipe  of  smaller
                                                       diameter  D . What  does  the Bernoulli equation predict  for
                                                                2
                 о =                         (зв.10-2)  9>i -  2P, the  difference  between  the  modified  pressures
                                                              2
                                                       upstream  and  downstream  of  the  contraction? Does  this
      (d)  Show that further integration with respect to z gives  result agree with experimental  observations?
                                                       (b)  Repeat  the  derivation  for  the  isothermal  horizontal
                v ix, z) =                   (3B.10-3)  flow  of an ideal gas through a sudden contraction.
                       2/лг In  (r /r )
                 r
                              2  }
                                                       3B.14  Torricelli's equation  for  efflux  from  a tank (Fig.
      (e)  Show that the mass flow rate is
                                                       3B.14).  A large  uncovered tank is  filled  with  a liquid  to a
                                                       height h. Near the bottom of  the tank, there is  a hole that
                                             (3B.10-4)  allows  the  fluid  to  exit  to  the  atmosphere.  Apply
                             In (r /r,)
                                2
                                                       Bernoulli's equation to a streamline that extends from the
      (f)  Sketch the curves  0>(r) and v (r, z).      surface  of  the  liquid  at  the  top  to  a  point  in  the  exit
                               r
      3B.11  Radial flow between  two  coaxial cylinders.  Con-
      sider  an  incompressible  fluid,  at  constant temperature,
      flowing  radially  between  two  porous  cylindrical  shells
      with inner and outer radii KR and R.                               Liquid  surface
      (a)  Show that the equation of continuity leads  to v  =  C/r,       at which
                                              r                          = 0 and  p  =
      where С is a constant.                                                      р л1т
      (b)  Simplify  the components of  the equation  of  motion to     Typical streamline
      obtain the following  expressions  for the  modified-pressure
      distribution:

                                =
                dr   ~^Tr     1в °   dz  =  0  (3B.11-1)                 Fluid exit at which
                                                                           ^2 = Afflux  a n d
      (c)  Integrate the expression  for dty/dr  above to get                V  = Patm
                             H^-O                      Fig.  3B.14.  Fluid draining from a tank. Points 1 " and "2"
                                                                                           "
               9>(r) -  Ш)  = Ь               (3B.11-2)  are on the same streamline.
   119   120   121   122   123   124   125   126   127   128   129