Page 271 - Introduction to Petroleum Engineering
P. 271

258                                          PRODUCTION PERFORMANCE
           The value of N is determined by using production data and assuming a water influx
           model for water influx W . By contrast, solving Equation 13.11 for W  gives
                               e                                  e
                              WB  w  NB  oi  B o  N B o  W B w           (13.13)
                                                  p
                                                        p
                                e
           The value of W  can be estimated using production data and a value of N from volu-
                       e
           metric analysis.

              Example 13.5  Water Influx
              Calculate water influx W  using the material balance equation for an oil–
                                   e
                                   (
              water  system:  WB w  NB oi  B )  N B o  W B .  We have the  estimate
                            e
                                                    p
                                                      w
                                              p
                                         o
                              .
              OOIP  N   N    85  MMSTB where N  is from volumetric analysis. Initial
                         vol                   vol
                             .
                                                               /
                                    /
                                                        .
              oil FVF is  B oi  1 347  RB STB. Oil FVF  B o  1 348  RB STB when 46
              MSTB oil has been produced. Water FVF is approximately constant and has
                           .
                                /
              the value B  10  RB STB. No water production has been reported.
                       w
              Answer
                                                              (
              No reported water production implies W  = 0 so that WB w  NB oi  B )  N B .
                                                                         p
                                                                           o
                                                                    o
                                                       e
                                             p
                                                                         .
                                            (
              Substituting values into  WB w  NB oi  B )  N B  gives  WB w  765
                                                       p
                                     e
                                                                  e
                                                  o
                                                         o
                       .
              MSTB 62 02  MSTB so that W  54.37 MSTB.
                                       e
           13.4.2  Schilthuis Material Balance Equation
           Schilthuis (1936) presented a general material balance equation that accounted for
           oil, water, and gas in the system. The general material balance equation is derived
           by assuming that the system is an isothermal system in pressure equilibrium. It is
           also based on the assumption that the distribution of oil, water, and gas phases does
           not affect tank model results. Following the discussion by Fanchi (2010b), we write
           the general material balance equation as
                                    B    B      BS     B   B
                   N B t  B ti  NmB ti  gc  gi  N  tiwio  tw  twi
                                       B gi     1  S wio  B twwi
                      mB S         B          1      m
                         iwig B
                     N   t     t w  t wi  N               Bc p          (13.14)
                                                           if
                                                           t
                       1  S wig  B t wi    1  S wio  1  S wiig
                     NB    NR B     G B   G B    G B     W   W W  W B
                      p  o  p  so  g  ps  g  pc  gc  i  g  e  i   p  w
           The terms in Equation 13.7 and associated units are specified in  Table  13.2.
           Application of the general material balance equation presumes that fluid property
           data from fluid samples are representative of reservoir fluids and that production,
           injection, and pressure data are reliable.
   266   267   268   269   270   271   272   273   274   275   276