Page 172 - Process Modelling and Simulation With Finite Element Methods
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Extended Multiphysics                159
          4.13 for both velocity  vectors and concentration is indicative of the long-lived
          nature  of  the  transient  intermediate  approach  to  uniform  mixing.  It  makes  a
          mockery of  “steady-state’’ analysis, since it is not clear that steady state is ever
          achieved in finite time nor is it clear that the uniformly mixed  state will result
          at all.
             Fick’s  law,  which models  the  non-equilibrium transport  of  species, would
          have  us  believe  that  the  equilibrium  endgame  has  concentration  uniformly
          diffused  everywhere  from  a  steady  source.  In  fact,  there  are  two  greater
          complications that preclude this.  The first is that it is not concentration that is
          diffusing at all,  but  rather  chemical potential,  and  in an external  gravitational
          field.  At equilibrium, these two potentials must be balanced.  So a permanent
          concentration gradient is  maintained against  a gravitational field.  This fact  is
          responsible for the difference in composition between air at sea level and at Mile
          High  Stadium.  In a buffer tank, it is probably meaningless,  as the gradient in
          concentration  is  minute.  The  second  complication  that  is  probably  more
          important  in most  chemical  plants  is that  few  solutions are exactly  ideal,  and
          many  show  significant  volume change on mixing.  Zimmerman  [7] has  shown
          that non-ideal  solutions can have the structure of  their  stratification  selected on
          chemical equilibrium grounds, and that only ideal solutions can ever be expected
          to form uniform mixtures at equilibrium.
             The second observation is of  the form of the velocity profile established -
          recirculation  layer  over  a  current.  This  is  exactly  the  form  postulated  by
          Zimmerman  [4] for which the lumped  parameter model of imperfect mixing in
          the buffer  tank  was derived, equations (4.6).  Figure 4.14 shows the idealized
          flow configuration for a denser current driving an upper recirculating layer.  The
          lumped  parameter  model  presumes  that  the  recirculation  is  strong  enough
          that the upper layer becomes well mixed, according to a theory of Batchelor [S],
          and  thus  a  single  Concentration  characterizes  it.  In  fact,  it  seems  that  the
          upper  recirculation  is  weak,  yet  the  concentration  gradients  are  small  in the
          upper layer,

                               a
                          w oil-in-fresh   r  ! ~u





                            Fi  Ci
                                                      FC
                                                  -0     0
                                                     outlet
                                Lx

                Figure 4.14  Plug flow across the tank bottom driving an upper recirculation layer.
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