Page 165 - Bird R.B. Transport phenomena
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Problems  149
                   in  which e, the porosity, is the ratio of pore volume to total volume, and к is the permeability of
                   the  porous medium. The velocity  v 0  in these equations is  the superficial velocity,  which  is de-
                   fined  as the volume rate of  flow  through a unit cross-sectional area  of the solid  plus fluid,  av-
                   eraged  over a small region  of space—small  with respect to the macroscopic dimensions in the
                   flow  system, but large  with  respect to the pore size. The density  and pressure  are  averaged
                   over a region available  to flow  that is large with respect to the pore size. Equation 4C.3-2 was
                   proposed empirically  to describe the slow seepage  of fluids  through granular media.
                       When  Eqs. 4C.3-1 and 2 are combined we  get

                                                                                       (4C.3-3)

                   for  constant viscosity and permeability. This equation and the equation  of  state describe the
                   motion  of a fluid  in a porous medium. For most purposes we may write the equation of state as
                                                         m
                                                    p  =  Po p e^                      (4C.3-4)
                   in  which p  is the fluid  density at unit pressure, and the following  parameters have been given: 6
                           0
                   1.  Incompressible liquids   m = 0   /3 = 0
                   2.  Compressible liquids     m = 0   /3 Ф 0
                   3.  Isothermal expansion of gases  /3 = 0  m-\
                   4.  Adiabatic expansion  of gases  /3 = 0  m = C /C  =  \/y
                                                             v
                                                                p
                   Show that Eqs. 4C.3-3 and 4 can be combined and simplified  for these four  categories to give
                   (for  gases it is customary to neglect the gravity terms since they are small compared with the
                   pressure terms):
                   Casel.                   V p  = 0                                   (4С.З-5)
                                             2

                   Case 2.                  ( ^ )  Ц- = V p  -  (V  •  p /3g)           (4C.3-6)
                                                                2
                                                       2
                   Case 3.                  ( ^ ^  j  ^  = V p 2                       (4C.3-7)
                                                        2
                   Case 4.                  /(m + \)e^ \  ^    ^
                                                    /m
                                                            =  у 2  ( 1 +т)/т         (4Q  3 g )
                   Note that Case 1 leads to Laplace's equation, Case 2 without the gravity  term leads  to the heat-
                   conduction or diffusion equation, and Cases 3 and 4 lead to nonlinear equations. 7

              4C.4  Radial flow through a porous medium  (Fig. 4C.4).  A  fluid  flows  through a porous cylindri-
                   cal  shell  with  inner and  outer radii  R }  and  R , respectively.  At  these  surfaces,  the pressures
                                                        2
                   are  known to be p  and p , respectively.  The length of the cylindrical shell is h.
                                       2
                                 x
                             Porous medium  Fluid


                                                                w = mass
                                                               rate of flow
                                              ]          J               Fig.4C4.  Radial flow
                                \        \    I                          through a porous
                              Pressure p }  Pressure p 2                 medium.


                       в
                        М. Muskat, Flow of Homogeneous  Fluids Through Porous Media,  McGraw-Hill  (1937).
                       7  For the boundary condition at a porous surface that bounds a moving fluid, see G. S. Beavers and
                   D. D. Joseph, J. Fluid Mech., 30,197-207 (1967) and G. S. Beavers, E. M. Sparrow, and B. A. Masha, AIChE
                   Journal, 20, 596-597 (1974).
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