Page 133 - Fundamentals of Reservoir Engineering
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MATERIAL BALANCE APPLIED TO OIL RESERVOIRS                          72

                                      p i                              p



                                  Gascap gas                                               B
                                 mNB   (rb)
                                     oi

                                 Oil + originally
                                 dissolved gas       ∆p

                                                                                C      A



                                  NB    (rb)
                                     oi




                                     (a)                                    (b)

                     Fig. 3.1   Volume changes in the reservoir associated with a finite pressure drop ∆ ∆∆ ∆p;
                                (a) volumes at initial pressure, (b) at the reduced pressure

                     taking all the surface production back down to the reservoir at this lower pressure) then
                     it should fit into the volume A + B + C which is the total volume change of the original
                     HCPV. Conversely, volume A + B + C results from expansions which are allowed to
                     artificially occur in the reservoir. In reality, of course, these volume changes correspond
                     to reservoir fluid which would be expelled from the reservoir as production. Thus the
                     volume balance can be evaluated in reservoir barrels as

                      Underground         =   Expansion of oil + originally dissolved gas (rb)
                      withdrawal (rb)

                                          +   Expansion of gascap gas (rb)

                                          +   Reduction in HCPV due to connate water expansion and
                                              decrease in the pore volume (rb)


                     Before evaluating the various components in the above equation it is first necessary to
                     define the following parameters.

                     N    is the initial oil in place in stock tank barrels
                          = V φ (1−S wc) / B oi stb

                     m    is the ratio

                           initial hydrocarbon volume of the gascap
                             initial hydrocarbon volume of the oil


                     (and, being defined under initial conditions, is a constant)

                     N p  is the cumulative oil production in stock tank barrels, and

                     R p  is the cumulative gas oil ratio
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