Page 180 - Process Modelling and Simulation With Finite Element Methods
P. 180

Extended Multiphysics                167

          Exercise 4.4

          Alter  the  initial  condition  so  that  U(tO)=  sheetu(x)+0.02*sin(31.4159265*~).
          Does this oscillation grow or decay?  What effect does the buffer tank have on
          the oscillation?

          4.5  Bioreactor Kinetics

          Recall that in 33.4, we treated heterogeneous reaction in a porous catalyst pellet,
          with  a variation  on the treatment in the Model Library  [9].  In this  section, we
          will try a different variation.  In this section, a similar approach will be used to
          model  reaction  of  a  passive  scalar  occurring  in  a  single  cell.  The  reaction
          lunetics will be taken as typical of bioreactors - Langmuir-Hinshelwood:






          where r  is the rate  of  disappearance  by  reaction,  which  only occurs  within  the
          cell.  d represents  the  finite  capacity  of  the  cell  to  hold  the  substrate
          concentration, which saturates at a value controlled by this parameter. The usual
          rate  controlling  step, however,  is  the  transfer of  the nutrient  from the  medium
          across the cell membrane.  The overall mass transfer process is usually modelled
          with a first order resistance, with the flux j given by

                                                                      (4.10)

          At  steady  state,  the  rate  of  disappearance  by  reaction  is  equal  to  the  flux  of
          nutrient across the cell membrance, i.e.

                                                                      (4.1 1)


          Thus, the  boundary  condition  on mass  transport  on the  cell  wall  involves  the
          concentration  ci on  the  boundary  and  the  concentration  within  the  cell  itself,
          which is taken to be uniform.  So the extended multiphysics here is to treat c, in
          an  additional  0-D  space  with  reaction  occurring  only  there,  and  coupling
          between  the two spaces through the flux into the cell and through the boundary
          condition  (4.10).  Equation  (4.11)  can  be  seen  as  modeling  the  cell  as  a
          continuously  stirred  tank  reactor  (CSTR)  with  effective  influx  given  by  the
          integral, and irreversible  reaction.  The boundary  condition  (4.10) is ubiquitous
          in the  chemical  engineering  literature,  nevertheless,  to the authors’  knowledge,
          this  is  the  first  hgher  dimensional  model  that  incorporates  it  as  a  boundary
          condition in a non-trivial way.  If ci is constant, (4.10) represents a simple mass
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