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44  Principles  of Applied  Reservoir Simulation



                              Qi  =



        where Q i is the cumulative pore volume of injected water. The slope of the water
        fractional  flow  curve with respect  to water  saturation  evaluated  at the water
        saturation at breakthrough gives Q ( at breakthrough.

        Effects  of Capillary Pressure and Gravity
             In the absence  of capillary pressure and gravity effects,  the flood front
        propagates as a "sharp" step function, or piston-like displacement. The presence
        of capillary pressure  leads to the imbibition of water ahead of the front. This
        causes a change in the behavior of produced fluid ratios. Rather than an abrupt
        increase  in  WOR  associated  with  piston-like  displacement,  the  WOR  will
        increase gradually as the leading edge of the mobile water reaches the well and
        is produced. In addition, the WOR will begin to increase sooner than it would
        have in the absence of capillary pressure.  By contrast, gravity causes high S w
        values to lag behind the front. The result is a smeared or "dispersed" flood front.


                             5.3 Miscible  Displacement

             Buckley-Leverett theory treats the displacement of one fluid by another
        under immiscible, piston-like conditions. An immiscible displacement  occurs
        when the  displaced  and displacing  fluids  do not mix. The result  is a readily
        discernible  interface between the two fluids. In a miscible  displacement, the
        fluids mix and the interfacial tension approaches zero at the interface. A miscible
        displacement  system is described  by a convection-dispersion  (C-D) equation.
        As an illustration, consider the one-dimensional C-D equation for the concentra-
       tion C of the displacing fluid:
                                2
                               d C     BC   dC
                             n
                             D       v    = —                       f5  16\
                               dx 2    dx    dt                     IJ 10J
                                                                      '
       We assume here that dispersion D and velocity v are real, scalar constants. The
                                           2
       diffusion  term  has  the  Fickian  form  D'd C/dx 2  and  the  convection  term  is
       vdC/dx.  When the diffusion  term is much larger than the convection term, the
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