Page 218 - Process Modelling and Simulation With Finite Element Methods
P. 218

Simulation and Nonlinear Dynamics         205


          Now pull down the Solve menu and select the Parameters option.  This pops
          up the Solver Parameters dialog window.

           Solver Parameters
              8   Select time stepping tab, set output times 0:0.01:0.5
                  Set time stepping algorithm odel5s
                  Select general tab, set solution form to weak, solver type time
                  dependent
                  Solve
                  Cancel
                  OK
          You  should animate the solution.  The final time should look similar to Figure
          5.14.  Compare with Figure 5.15 which shows the initial condition. The red band
          is the initial slug of unit concentration.  Clearly, the nonuniform streamlines are
          due  to  the  vorticity  generated  by  the  concentration  noise.  The  effect  of
          channeling  of  the  less  viscous  fluid  in  the  slug  eventually  becomes  so
          pronounced  that  the  upstream  and  downstream  more  viscous  fluid  connects
          through  the  slug,  isolating islands of  the  less viscous fluid.  In an immiscible
          fluid, a topological change forming droplets would have had to have occurred.
          Here, the interface remains  smooth due to diffusive  mixing,  so channeling has
          occurred.  The longer the slug, the less likely the complete channeling through
          the slug is to occur in a fixed time.  The trailing front of the slug is stable since it
          has less viscous fluid displaced by more viscous fluid.  As the animation shows,
          it is the instability of the leading front that becomes so pronounced, it eventually
          breaks through  the  slug.  The success  of  this  simulation  in  capturing  unstable
          frontal dynamics , in comparison with the first model in the Darcy’s Law mode,
          is  predicted  solely  on  the  use  of  periodic  horizontal  boundary  conditions.
          Otherwise, the model equations are dynamically equivalent to the built-in modes
          that were used before.
             Figure  5.16  shows  the  formation  of  viscous  fingers just  on  the  leading
          edge  with  accompanying  vorticity  generation.  Otherwise,  the  trailing  edge
          simply  has  diffused  out  somewhat  with  still  uniformity  in  the  cross-stream
          direction.
             Figure 5.17 shows the leading edge gouging out large, broad fingers into the
          slug.  Viscous fingering is not a symmetric process - back-fingering of the more
          viscous fluid into the less viscous displacing fluid does not necessary mirror the
          dynamics  of  forward  fingering.  Here,  the  slug  is  poor  in less  viscous  fluid.
          Figure 5.14 shows that  we eventually  use up the supply of  finger-forming less
          viscous fluid if the slug length is too short in comparison to its breadth.  Figure
          5.17 has much shorter fingers than seen in [ 141 with a long slug.
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