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Part II: Reservoir Simulation  127


       Both saturated and undersaturated curves are included as functions of pressure
        only. Phase changes occur at the saturation pressures. Single-phase oil becomes
       two-phase  gas-oil when pressure drops below the bubble point pressure (P 6),
        and single-phase gas becomes two-phase gas condensate when pressure drops
       below the dew point pressure  (P d).
             Simulators  run  most  efficiently  when  fluid  property  data  are smooth
        curves. Any discontinuity in a curve can cause numerical difficulties. Ordinarily,
       realistic fluid properties are smooth functions of pressure except at points where
       phase transitions occur. As a practical matter, it is usually wise to plot input PVT
        data to verify the smoothness of the data. Most simulators reduce the nonlinearity
                                                                 to interpo-
        of the gas formation volume factor B g by using the inverse b g = l/B g
        late gas properties.
             Oil properties from a laboratory must usually be corrected  for use in a
        black  oil simulator  [Moses,  1986]. Flow in the  reservoir  is a relatively slow
       process that corresponds to a differential process in the laboratory. A differential
        process  is one  in which pressures  are  allowed to  change  in relatively small
        increments. For comparison, a flash process allows pressures in the experiment
        to change by relatively large increments. The production of oil up the wellbore
       to surface facilities is considered a flash process.  Oil is flashed to the  surface
       through several pressure and temperature regimes. The corrections applied to
        oil property data are designed to adjust  the data to more adequately represent
        fluids as they flow differentially in the reservoir prior to being flashed to surface
        conditions. The corrections alter solution gas-oil ratio and oil formation volume
        factor. The effect of the correction is illustrated by the case study in Chapter 20,
        The oil property correction  is often significant.
             Water  properties  must  also  be  entered  in  a  simulator.  Ideally  water
       properties should be measured by performing laboratory analyses on produced
       water samples. If samples are not available, correlations are often  sufficiently
       accurate for describing the behavior of water.
             In the absence of reliable fluid data for one or more of the reservoir fluids,
       it may be necessary to use correlations. McCain [ 1991 ] reviewed the state of the
       art in the use of correlations to describe fluid properties. New correlations for
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