Page 294 - Reservoir Formation Damage
P. 294

274    Reservoir Formation Damage

               in  which  (3  is  an  empirically  determined  coefficient.
                  For  constant  rate  filtration,  Eq.  12-11  subject  to  Eq.  12-14 can  be
               integrated  numerically  for  varying  shear-stress  T s. When  the  shear-stress
               is  constant  or  does  not  vary  significantly,  an  analytical  solution  can  be
               obtained  as  (Civan,  1999a):

                    =  (Aq-B)t                                           (12-42)


               in  which  fi  = 0  because  T = 0  for  static  conditions  and  5^0  because
                t * 0  for dynamic  conditions.  The cumulative  filtrate  volume  is given by,
               for  both  the  static  and  dynamic  filtration


                  Q = qt                                                  (12-43)
               Then,  the  pressure  difference  (p c-p e)  or  the  slurry  injection  pressure
                p c, when  the back  pressure  at the  effluent  side  of  the porous  filter  media
                   is  prescribed,  can  be  calculated  by  Eq.  12-19.  The  following con-
                p e
               ventional  filtration  equation  (Hermia,  1982; de  Nevers,  1992) can  be
               derived  by  invoking  Eq.  12-43 into  Eq.  12-40:


                                                                         (12-44)
                  Q         q 0

               Radial   Filter  Cake  Model

                  A  schematic  of  the  formation  of  a filter  cake  over  the  sand  face  during
               over-balanced  mud  circulation  in  a  wellbore  is  shown  in  Figure  12-3.
               Figure  12-4 is a quadrant  areal view  of the problem.  The radii  of the mud
               slurry  side  cake  surface,  the  sand  face  over  which  the  cake  is  built  up,
               and  the  external  surface considered  for  the region  of influence  are  denoted
                      r
               by  r c, w  an d  r e, respectively.  The formation  thickness  is  h.
                  The  particle  mass  balance  equation  is  given  by  (Civan,  1994, 1998a)

                                                                         (12-45)


               The  filter  cake  thickness  is  given  by

                  5 = r, -                                               (12-46)

                   is  given  by  Eq.  12-9. The  slurry  shear-stress  at  the  cake  surface  is
                R ps
               given  by  the  Rabinowitsch-Mooney  equation  (Metzner  and  Reed, 1955)
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