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P. 68

§2.4  Flow Through an Annulus  53

                          To  check whether the flow is laminar, we calculate the Reynolds number
                                           D(v )p  4(w/p)p
                                       Re =   z
                                                    TTD/JL
                                           4( 0.00398 -К-)(2.54  ^  X  12 ^  ) ( ^  ^  Y  1.261
                                            \       min/\    m.     ft/  \60  s  /V



                                          =  2.41 (dimensionless)                              (2.3-24)
                          Hence the flow is indeed laminar. Furthermore, the entrance length is
                                            L e  = 0.035D Re = (0.035)(0.1/12X2.41)  = 0.0007 ft  (2.3-25)
                          Hence, entrance effects  are not important, and the viscosity  value given  above has been calcu-
                          lated properly.

      EXAMPLE 2.3-2       Obtain an expression  for  the mass rate of flow w  for an ideal gas  in laminar flow in a long cir-
                          cular tube. The flow is presumed  to be isothermal. Assume  that the pressure change through
     Compressible Flow  in  t ^  e  ^ ^ е  j  s  n o t  v e r v  i g  e /  s o  that the viscosity  can be regarded a constant throughout.
                              и
                                          ar
     a Horizontal  Circular
     Tube6
                          SOLUTION
                          This  problem  can  be  solved  approximately  by  assuming  that the Hagen-Poiseuille equation
                           (Eq.  2.3-21) can be applied  over a small length dz of the tube as  follows:

                                                                                               ( 2 3  2 6 )
                                                                                                 -
                          To eliminate p in favor  of p, we use the ideal gas  law  in the form pip  = p /p ,  where p  and p 0
                                                                                               0
                                                                                    o
                                                                                      o
                          are the pressure and density at z = 0. This gives
                                                                 ( )
                           The  mass rate of flow w is the same  for  all z. Hence Eq. 2.3-27 can be integrated  from z = 0 to
                          z = L to give

                                                               ^                               (23-28)

                           Since p\-p\  = (p  + p )(p  -  p ), we get  finally
                                               0
                                                   L
                                            L
                                         0
                                                           «*>-rf**                             .
                                                                                              (23 29)
                           where  p  av g  =  \(p  + p )  is  the  average  density  calculated  at  the  average  pressure  /? avg  =
                                         0
                                            L
                           l(Po + Pi)-
     §2.4 FLOW THROUGH AN ANNULUS
                           We  now  solve  another  viscous  flow  problem  in  cylindrical  coordinates,  namely  the
                           steady-state  axial  flow  of  an  incompressible  liquid  in  an  annular  region  between  two
                           coaxial cylinders  of radii KR and R as shown  in Fig. 2.4-1. The fluid is  flowing  upward  in



                              6
                               L. Landau and E. M. Lifshitz, Fluid Mechanics, Pergamon, 2nd edition (1987), §17, Problem 6. A
                           perturbation solution  of this problem was obtained by R. K. Prud'homme, T. W. Chapman, and J.  R.
                           Bowen, Appl. Sci. Res, 43, 67-74 (1986).
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