Page 108 - Formation Damage during Improved Oil Recovery Fundamentals and Applications
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90                                                  Thomas Russell et al.


             The final form of the critical retention function versus velocity and
          salinity will not only roughly follow those shown in Fig. 3.8, but will also
          be highly dependent on the form of the particle size distribution.


          3.2.3 Single-phase equations for fines transport
          Mathematical modeling of fines migration typically revolves around a
          continuity equation for the suspended particle concentration. The form
          of this equation is as follows:

             Rate of accumulation 5 Divergence of advective flux
                                     Rate of detachment   Rate of straining:

             Suspended particle transport is given by the sum of the advective and
          diffusive flux. For the purposes of modeling fines migration in petroleum
          reservoirs, diffusive flux is typically negligible and thus is removed for
          convenience. Thus, the continuity equation can be expressed as:
                              @φc       @c   @σ a   @σ s
                                 52 U      2     2     :              (3.22)
                              @t        @x    @t    @t
             This is more commonly given as:
                              @                  @c
                                ½ φc 1 σ a 1 σ s Š 1 U  5 0 ;         (3.23)
                              @t                @x
          where c, σ a ,and σ s are the concentrations of suspended, attached, and
          strained particles, respectively, φ is the porosity of the porous media, U is
          the fluid flow velocity, x is the distance, and t is the time. The porosity
          term arises because the suspended concentration is defined as the volume
          of particles in suspension per pore volume, while the attached and strained
          concentrations are defined similarly but for the bulk rock volume.
             For Eq. (3.23) to be valid, it is necessary here to assume that during
          the transport, detachment, and capture, the particle and fluid volumes are
          additive (Amagat’s law), and c, σ a , and σ s are the volumetric concentra-
          tions. Eq. (3.23) is also valid where the mass concentrations of all particle
          species are negligibly small if compared with the mass of water.
             The straining rate is assumed to be proportional to particle advection
          flux, cU (Bedrikovetsky, 2008; Herzig et al., 1970):

                                    @σ s
                                           ðÞcU;
                                        5 λσ s                        (3.24)
                                     @t
          where λ is the filtration coefficient for straining.
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