Page 286 - Reservoir Formation Damage
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266   Reservoir Formation Damage

                Linear  Filter  Cake  Model

                  A  schematic  of  the  formation  of  a  filter  cake  over  a  hydraulically
                created  fracture is  shown in Figure  12-1. Figure  12-2 shows  the simplified,
                one-dimensional  linear  cake  filtration problem  considered  in this  section.
               The  locations  of  the  mud  slurry  side  cake  surface  and  the  slurry  and
               effluent  side  surfaces of  the porous  medium  are denoted,  respectively, by
               x c, x w, and x e. Consistent  with laboratory  tests using core  plugs, the  cross-
                sectional  area  is denoted  by a  and the core  length  by L = x e -  x w.
                  The  mass  balance  of  particles  in  the  filter  cake  is  given  by  (Civan,
                1996,  1998a)


                                                                           (12-1)

               where  p p  is  the  particle  density,  t  is  time, e 5 is  the  volume  fraction of
               particles  of  the  cake  that  can  be  expressed  as  a  function  of  the  porosity
                   of  the  cake  as
                <|> c

                                                                           (12-2)
                  e,= l-<t> c
               and  R ps  is  the  net  mass  rate  of  deposition  of  particles  of  the  slurry  to
               form  the  cake  given  by  (Civan,  1998b,  1999a,b)

                  RPS  = k du cc p-k e(e s  p,)  (T, -t cr)u(i s  -T cr )  (12-3)


               The  first  term  on  the  right  of  Eq.  12-3  expresses  the  rate  of  particle
               deposition  as  being  proportional  to  the  mass  of  particles  carried  toward
               the filter by the filtration  volumetric  flux  u c, normal to the filter surface,
               given  by


                  u c = q/a                                                (12-4)

               where  q  is the carrier  fluid  filtration flow rate  and  a  is the  area  of the  cake
               surface.  c p  is the  mass  of particles  contained  per  unit volume  of the  carrier
               fluid  in  the  slurry.  k d  is  the  deposition  rate  coefficient. The  second  term on
               the right  of Eq.  12-3 expresses  the rate  of erosion  of the cake  particles  from
               the  cake  surface on the  slurry side.  Erosion  takes place only when the  shear-
               stress i s applied  by the slurry to the cake  surface exceeds  a minimum  critical
               shear  stress  i cr  necessary  for detachment  of particles  from  the  cake  surface.
               The  shear-stress  is  given  by  (Metzner  and  Reed, 1955)
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