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Single-Phase Formation Damage by Fines Migration and Clay Swelling  229

             where

                a  = 0 when  u<u f.                                   (10-188)


             where  u c  is  the  critical  flux  below  which  mobilization  does  not  occur.

             Case  2—Particle  Deposition  in  Plugging  Pathways.  To  verify  their
             plugging  rate  equation,  they  considered  sand  packs  and  suspension  of
             glass  particles  of various  sizes.  They  estimated  the  effective  pore  diameter
             of  the  passages  between  the  closest  packing  of  sand  grains  as  the  grain
             diameter,  d g,  divided  by  6.5,  dg/6.5.
               The  data  of  sand grain  and  glass  particle  sizes  as well  as  the  estimated
             effective  pore  diameter  to  particle  diameter  ratio  are  presented  in
             Table  10-2.  They  measured  the  pressure  difference  across  the  sand  pack
             as  a function  of  the pore  volume of  the  suspension  of glass  beads  injected
             at  a  constant  rate.  They  classified  the  deposition  type  as  indicated  in
             Table  10-2  based  on  the  observed  variation  of  the  pressure  difference.
             The  deposition  process  was considered  mainly as the pore  surface  deposi-
             tion  when  the  variation  of the pressure  difference  was  small,  and  indicated
             by  "5"'  in  Table  10-2.  The  deposition  was  considered  due  to  the  pore
             throat  plugging,  when  the  pressure  difference  indicated  a  monotonic
             increase  and indicated  by  "P"  in Table  10-2.  A rise  in pressure  difference



                                          Table 10-2
                     Deposition of 5- to  10-jo.m Glass Beads in Sandpacks*
             Sand Grain     Effective     Glass Bead
              Diameter      Pore Size      Diameter
                                                                     Deposition
                 d g           d s            d f
                (um)          (urn)         (um)          d s/d f      Type**
             840 to 2000      218f         5 to 10        29.lt,        S
             840 to 2000      218          8 to 25        13.2          S
             420 to  840       97          5 to 10        12.9          S
             420 to  840       97          8 to 25         5.9          SandP
             250 to  297       42          5 to  10        5.6          SandP
             250 to  297       42          8 to 10         2.6          FC
             177 to  210       30          5 to 10         4.0          P
             104 to  124       18          5 to 10         2.4          FC

              * After Gruesbeck and Collins,  1982 SPE; reprinted by permission  of the Society of Petroleum Engineers.
             **S = surface, P = plugging, FC = filter  cake
              t  = (1/2) (840  + 2000) / 6.5 = 218 for closest packing of spheres
              ^ = 2187 [(1/2) (5+10)] = 29.1
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