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Single-Phase  Formation  Damage  by Fines Migration  and Clay  Swelling  187

                                                        Surface
                                                        deposits





















             Figure  10-2. Pore surface  deposition  in a core  (after  Civan,  1994; reprinted
             by  permission  of  the  U.S. Department  of  Energy;  after  Civan  1992  SPE;
             reprinted  by  permission  of  the  Society  of  Petroleum  Engineers).


             somewhere  along  the  tube,  by  a  single  particle  to  stop  the  flow  through
             that particular tube. Therefore,  the  cross-sectional  areas  of  the individual
             tubes, A h, do  not change. But, the number of tubes, N np,  open  for  the flow
             is  reduced  as  depicted  in  Figure  10-3.  The  area  of  the  tubes  eliminated
             from  service  is  given  by:

                                                                        (10-12)
                A p=N pA h
             The  number of tubes plugged  is estimated  by the  ratio  of the  total  volume
             of  pore  throat  blocking  particles  to  the  volume of  a  single  particle  of  the
             critical  size.



                                                                       (10-13)



             The  critical  particle  size,  d,  is  defined  as  the  average  size  of  the  critical
                                         f
             pore  constrictions  in  the  core. d  is  the  volume  fraction  of  particles  in
             the  flowing  phase,  having  sizes  comparable  or  greater  than  d.  p p  is  the
             particle  grain  density.  p p/  is  the  mass  concentration  of  particles  in  the
             flowing  suspension  of particles.  Because A h  is a constant, Eq.  10-7  leads
             to  the  following  permeability  to  open  flow  area  relationship:
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