Page 160 - Principles of Applied Reservoir Simulation 2E
P. 160

Part II: Reservoir Simulation  145


             The  molar  flow  equations  were  derived  using  the  conservation  laws
       introduced  in Chapter  15.1. An energy balance  equation can be  found  in the
       thermal recovery literature [Prats, 1982]. The energy balance equation is more
       complex than the flow equations because of the presence of additional nonlinear
       terms. Energy loss to adjacent non-reservoir rock must also be computed. The
       resulting  complexity  requires  substantial  computation to  achieve  an energy
       balance. In many realistic systems, reservoir temperature variation is slight and
       the  energy  balance  equation  can  be  neglected  by  imposing  the isothermal
       approximation. The result is a substantial savings in computation expense with
       a reasonably small loss of accuracy.
             Several  supplemental -  or auxiliary -  equations  must be specified to
       complete the  definition  of the mathematical  problem.  There must be a flow
       equation  for  each  modeled phase.  Commercial  black  oil  and compositional
       simulators are formulated to model up to three phases: oil, water, and gas. The
       inclusion of gas in the water phase can be found in some simulators, though it
       is neglected in most. The ability to model gas solubility in water is useful  for
       CO 2 floods or for modeling geopressured  gas-water reservoirs.  Some black oil
       simulator formulations include a condensate term. It accounts  for liquid yield
       associated with condensate reservoir performance.
             In addition to modeling reservoir structure and PVT data, simulators must
       include rate equations for modeling wells, phase potential calculations, and rock-
       fluid interaction data such as relative permeability curves and capillary pressure
       curves.  Saturation-dependent  rock-fluid interaction data are entered in either
       tabular or analytical form. More sophisticated simulators let the user represent
       different types of saturation change processes, such as imbibition, drainage, and
       hysteresis. Applying such options leads to additional computation and cost,



                         15.3 Well and Facilities  Modeling

             Well and surface facility  models are simplified representations  of real
       equipment [Williamson and Chappelear,  1981]. The well model, for example,
       does not account for flow in the wellbore from the reservoir to the surface. This
       effect can be taken into account by adding a wellbore model. The wellbore model
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