Page 316 - Principles of Applied Reservoir Simulation 2E
P. 316

Part  V: Technical Supplements  301


             most  natural  gases,  the relationship  \!B g  versus  pressure  will  be  very
             nearly  linear,  especially  at  moderate  to  high  pressures.  Plotting  l/B g
             versus pressure and extrapolating to PMAX should provide more realistic
             values  of  B g  at  higher  pressures.  Interpolating  B g  using  l/B g  versus
             pressure substantially  improves material balance.

       2.    Once the B g versus P curve is fixed, R so versus P and B 0 versus P curves
             must be extrapolated  so as to avoid a negative oil compressibility being
             calculated  over  any  pressure  increment.  To  ensure  that  negative  oil
             compressibilities will not be calculated by the program, the following test
             should be used.  For any pressure  increment P, to P 2, where P 2 > P {, the
             following relationship  should hold:


                    0  *  -     -  B ol)  +                            .
                           v (B 02  ;
                                              5.615
             where the units of B 0, B g, and R so are RB/STB, RCF/SCF, and SCF/ STB,
             respectively. Note that this test applies only to the saturated oil PVT data.

       3 .   The above concepts also apply to the water PVT data. However, for most
             simulations, it can be assumed that R sw = 0.0, thus - AB W/B WAP  approxi-
             mates water  compressibility.



                         28.5 Gas PVT Correlation  Option

       Basic Gas Properties
             Following  Govier  [1975],  real  gas Z-factors  are  computed  using  the
       Dranchuk,  et  al.  [1974] representation  of the  Standing-Katz  Z-factor  charts
        [1942]. This representation  employs the Benedict- Webb-Rubin [1940] eight-
       parameter  equation  of  state  to express  the Z-factor  as a function  of  pseudo-
       critical temperature  T r and pseudo-critical  pressure P r, thus
                               Z  =  Z(P r,  T r)                   (28.2)
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