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MATERIAL BALANCE APPLIED TO OIL RESERVOIRS                          76

                           reservoir. In the case of an oil reservoir, however, the situation is generally more
                           complex since below the bubble point two phases, oil and gas, will co-exist and,
                           due to the gravity difference between the phases, will tend to segregate. As a
                           result, the point at which the average pressure should be determined will vary
                           with time. Precisely how the volume averaged reservoir pressure can be
                           determined from the analysis of pressure tests in wells will be detailed in
                           Chapter 7.


              3.3    THE MATERIAL BALANCE EXPRESSED AS A LINEAR EQUATION

                     Since the advent of sophisticated numerical reservoir simulation techniques, the
                     Schilthuis material balance equation has been regarded by many engineers as being of
                     historical interest only; a technique used back in the nineteen forties and fifties when
                     people still used slide-rules. It is therefore interesting to note that as late as 1963-4,
                     Havlena and Odeh presented two of the most interesting papers ever published on the
                     subject of applying the material balance equation and interpreting the results. Their
                            4,5
                     papers,  described the technique of interpreting the material balance as the equation
                     of a straight line, the first paper describing the technique and the second illustrating the
                     application to reservoir case histories.

                     To express equ. (3.7) in the way presented by Havlena and Odeh requires the
                     definition of the following terms

                           F  =  N p (B o  +  (R p     R s)  B g)  +  W p B w   (rb)                 (3.8)


                     which is the underground withdrawal;

                           E o  =  (B o − B oi) + (R si − R s) B g                  (rb/stb)         (3.9)

                     which is the term describing the expansion of the oil and its originally dissolved gas;

                                     B
                           E =  B oi      g  − 1                            (rb / stb)              (3.10)
                            g
                                     B gi

                     describing the expansion of the gascap gas, and

                                                cS   + c
                           E f,w  =  (1 m) B oi    w  wc  f     ∆ p         (rb / stb)              (3.11)
                                      +
                                                 1 −  S wc
                     for the expansion of the connate water and reduction in the pore volume. Using these
                     terms the material balance equation can be written as

                                                                                                    (3.12)
                           F  =  N(E o+mE g+E f,w) + W eB w

                     Havlena and Odeh have shown that in many cases equ. (3.12) can be interpreted as a
                     linear function. For instance, in the case of a reservoir which has no initial gascap,
                     negligible water influx and for which the connate water and rock compressibility term
                     may be neglected; the equation can be reduced to
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