Page 308 - Principles of Applied Reservoir Simulation 2E
P. 308

Part  V: Technical  Supplements  293


       process is expensive and most relative permeability data are obtained on restored
       state cores in the laboratory.
             In principle, three-phase  relative permeability should be used when oil,
       water, and gas are flowing simultaneously. As a practical  matter, the  difficulty
       of accurately measuring three-phase relative permeabilities  often  makes their
       use  meaningless.  It  is  often  sufficient  to  work  with  the  two-phase relative
       permeability curves only.
             Despite their shortcomings, it may be of interest to perform a simulation
       using a set of three-phase relative permeability curves. For this case, WINB4D
       contains an option for computing a three-phase oil relative permeability curve
       using water-oil and gas-oil relative permeability curves. As with most calcula-
       tions of this type, we assume:
             a.   The water relative permeability curve (k^  obtained for a water-oil
                   system  depends only on water saturation, and
             b.   The  gas  relative  permeability curve  (k rg)  obtained  for  a  gas-oil
                  system depends  only on gas saturation.
             The validity of these assumptions depends on such factors as wettability
       and degree of consolidation.  Given the above assumptions, £ w and k rg for water-
       oil and gas-oil  systems, respectively, are also valid for a water-gas-oil  system.
       The three-phase  oil relative permeability k ro3 is calculated as


                 ,      (^row  +  ^rw)  (krog  +  *rp  ,*  _,_  L  \
                 k^  =            -   1     £-  -  (k rw  +  k rg)  (28J)
                                 *row
       where

             k row  -  oil relative permeability for water-oil system
                 =  oil relative permeability for gas-oil system
             k mg
             k* row=  oil relative permeability for water-oil system  evaluated
                    at the oil saturation corresponding to irreducible water
                    saturation
       Equation (28.1) is based  on the work by  Stone  [1973], and it corresponds to
       Model II of Dietrich and Bonder [1976]. For a discussion of alternative models
       of three-phase  oil relative permeability,  see Blunt [1999].
             When the three-phase  calculation is activated, the user must be sure the
       input water-oil and gas-oil relative permeability curves are realistic. For example,
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