Page 244 - Bird R.B. Transport phenomena
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228  Chapter 7  Macroscopic Balances for Isothermal Flow Systems

                       7B.8  Change in liquid height with time (Fig. 7.1-1).
                            (a)  Derive Eq. 7.1-4 by using integral calculus.
                            (b)  In Example 7.1-1, obtain the expression  for the liquid height h as a function  of time t.
                            (c)  Make a graph  of Eq. 7.1-8 using dimensionless quantities. Is this  useful?
                       7B.9  Draining of a cylindrical tank with exit pipe (Fig. 7B.9).
                            (a)  Rework  Example  7.1-1, but  with  a  cylindrical  tank  instead  of  a  spherical  tank.  Use  the
                            quasi-steady-state  approach;  that  is,  use  the  unsteady-state  mass  balance  along  with  the
                            Hagen-Poiseuille equation  for the laminar  flow in the pipe.
                            (b)  Rework the problem for turbulent  flow in the pipe.
                                                 2
                                           128fiLR ,
                            Answer:  (a) t ei     In  1 + S
                                             PgD 4
















                                          Fig. 7B.9.  A cylindrical tank with a long pipe attached. The fluid  surface
                                          and pipe exit are open to the atmosphere.

                      7B.10  Efflux time for draining a conical tank (Fig. 7B.10).  A conical tank, with dimensions given in
                            the figure, is initially  filled  with a liquid. The liquid  is allowed  to drain out by gravity. Deter-
                            mine the efflux  time. In parts (a)-(c) take the liquid in the cone to be the "system."
                            (a)  First use an unsteady macroscopic mass balance to show that the exit velocity is
                                                             V
                                                              2=-- 2J-                          (7B.10-1)
                            (b)  Write the unsteady-state  mechanical  energy balance  for  the system. Discard  the  viscous
                            loss term and the term containing the time derivative  of the kinetic energy, and  give reasons
                            for doing so. Show that this leads to
                                                             = V2g(z  -  z 2)                  (7B.10-2)
                                                           v 2







                            Liquid  surface
                               at time t

                                                                      Fig. 7B.10.  A conical container  from
                                                                      which a fluid  is allowed to drain. The
                                                                      quantity r is the radius  of the liquid  sur-
                                                                      face at height z, and r is the radius of
                                                                 = z 2
                                                                      the cone at some arbitrary height z.
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