Page 202 - Reservoir Formation Damage
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184   Reservoir Formation Damage

                  An  evaluation  and  comparison  of  six  selected  models  bearing  direct
                relevance  to  formation  damage  prediction  for  petroleum  reservoirs  are
                carried  out. The  modeling  approaches  and  assumptions  are  identified,
                interpreted,  and compared.  These  models  are applicable  for  special  cases
                involving  single-phase  fluid  systems  in  laboratory  core  tests.
                  Porous  media is  considered  in two parts:  (1)  the flowing phase,  denoted
                by  the  subscript /,  consists  of  a  suspension  of  fine  particles  flowing
                through  and (2) the  stationary  phase, denoted  by the  subscript  s,  consists
                of  the  porous  matrix  and  the  particles  retrained.



                              The  Thin   Slice Algebraic  Model

                Model   Formulation

                  Wojtanowicz  et  al.  (1987,  1988) considered  a  thin  slice  of  a  porous
                material  and analyzed the  various  formation damage  mechanisms assum-
                ing  one  distinct  mechanism  dominates  at  a  certain  condition.  Porous
                medium  is visualized as having tortuous pathways represented  by N h  tubes
                of  the  same  mean hydraulic equivalent diameter,  D h, located  between  the
                inlet  and  outlet  ports  of  the  core  as  depicted  in  Figure  10-1.  The  cross-
                sectional  area  of  the  core  is A and  the  length  is  L.  The  tortuosity  factor
                for  the tubes  is defined  as the ratio of the  actual  tube  length  to the  length
                of  the  core.
                  -c = L h/L                                               (10-1)

                The  cross-sectional  area  of  the  hydraulic  tubes  are  approximated  by

                                                                           (10-2)


                in  which  C l  is  an  empirical  shape  factor  that  incorporates  the  effect  of
                deviation  of  the  actual  perimeter  from  a  circular  perimeter.
                  As  a suspension of fine  particles  flows  through the porous media, tubes
                having  narrow  constrictions  are  plugged  and  put  out  of  service.  If  the
                number  of nonplugged tubes  at  any  given time  is  denoted  by  N np  and  the
                plugged  tubes  by  N p,  then  the  total  number of  tubes  is  given  by:

                          +N
                  N,  = N  p  "n                                           (10-3)
                       ly  T
                  ^ h
                The  area  open  for  flow  is  given  by
                                                                           (10-4)
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