Page 167 - Bird R.B. Transport phenomena
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Problems  151

                                      Fig. 4D.3. Rotating disk  in a circular tube.























              4D.3  Flows in  the  disk-and-tube system (Fig. 4D.3). 9
                    (a)  A  fluid  in a circular tube is caused  to move tangentially by  a tightly  fitting  rotating disk  at
                    the liquid  surface  at z = 0; the bottom of the tube is located at z = L. Find the steady-state  veloc-
                    ity  distribution v (r, z), when  the angular  velocity  of  the disk  is  П. Assume  that creeping  flow
                                 e
                    prevails  throughout, so that there is no secondary flow. Find the limit of the solution as L —>  «>.
                    (b)  Repeat the problem  for  the unsteady  flow.  The fluid  is  at rest  before  t  =  0, and the  disk
                    suddenly  begins  to rotate with  an angular  velocity  ft  at t  = 0. Find the velocity  distribution
                    v (r, z, t) for a column of fluid  of height  L. Then find  the solution for the limit as L  —>  oo.
                     Q
                    (c)  If the disk  is oscillating  sinusoidally  in the tangential direction with amplitude П , obtain
                                                                                       о
                    the velocity  distribution in the tube when the "oscillatory  steady state" has been attained. Re-
                    peat the problem for a tube of infinite length.
              4D.4  Unsteady annular  flows. 10
                    (a)  Obtain a solution to the Navier-Stokes equation for the start-up of axial annular flow by a
                    sudden impressed  pressure gradient. Check your result against  the published  solution.
                    (b)  Solve the Navier-Stokes equation for the unsteady tangential flow in an annulus. The  fluid
                    is at rest  for  t <  0. Starting at t  = 0 the outer cylinder begins  rotating with  a constant angular
                    velocity  to cause laminar flow  for  t >  0. Compare your result with the published solution. 11
              4D.5  Stream functions  for  steady three-dimensional flow.
                    (a)  Show  that the velocity  functions  pv  =  [V  X A]  and pv  =  [(Vi/^)  X  (V^ )] both satisfy  the
                                                                               2
                    equation  of  continuity identically  for  steady  compressible  flow.  The functions  ф  ф  and  A
                                                                                     и  ъ
                    are arbitrary, except that their derivatives  appearing in  (V • pv) must  exist.
                    (b)  Show  that, for  the conditions  of  Table  4.2-1, the vector  A  has  the magnitude  -рфк 3  and
                    the direction of the coordinate normal to v. Here h  is the scale  factor  for  the third coordinate
                                                            3
                    (see §A.7).
                    (c)  Show  that the streamlines  corresponding  to Eq. 4.3-2  are given  by  the intersections  of  the
                    surfaces  ф  = constant and ф  = constant. Sketch such a pair of surfaces  for the flow in Fig. 4.3-1.
                            х
                                          2
                    (d)  Use Stokes'  theorem  (Eq. A.5-4)  to obtain an expression  in terms  of  A  for  the mass  flow
                    rate through a surface  S bounded by a closed curve  C. Show that the vanishing  of v on С does
                    not imply  the vanishing  of A on С

                       9
                         W. Hort, Z. tech. Phys., 10, 213 (1920); С. Т. Hill, J. D. Huppler, and R. B. Bird, Chem. Engr. ScL, 21,
                    815-817(1966).
                       10
                         W. Miiller, Zeits. fur angew. Math.  u. Mech., 16, 227-228 (1936).
                       11
                         R. B. Bird and C. F. Curtiss, Chem. Engr. Sri, 11,108-113 (1959).
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