Page 28 - PVT Property Correlations
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Introduction Chapter | 1  9


                                  Hydrocarbon  Hydrocarbon
                                  vapor phase  liquid phase  Water phase
                                  (gas phase)  (oil phase)
                      Component 1     X           X

                      Component 2     X           X
                      Component 3     X           X

                      ……              X           X

                      ……              X           X
                      Surface water                           X

             FIGURE 1.6 Relation of fluid components and reservoir phases for compositional models.

             the relations between the surface components, and their existence in the res-
             ervoir gas and oil phases. In this model, all hydrocarbon components (or
             pseudocomponents) produced on surface are assumed to have existed in
             either the reservoir gas or oil phases, or both.
                The preparation of PVT data for compositional models requires the use
             of EOS programs and is beyond the scope of this book. Compositional PVT
             models are needed to handle fluids that change composition significantly
             with different recovery processes. Applications of compositional models
             include (1) tracking the hydrocarbon components in the production stream
             (rather than merely volumes of gas and oil produced), (2) gas cycling in rich
             gas condensate reservoirs, (3) miscible and near miscible processes, (4) cases
             with severe compositional gradient (e.g., near-critical fluids with large com-
             positional variation versus depth), and (5) separator conditions changes dur-
             ing reservoir depletion. Some commercial reservoir simulators allow
             changing black-oil PVT data (oil formation volume factor and solution gas-
             oil ratio) when separator conditions change during the simulation run. The
             extension of these corrections to MBO simulation were presented by Ibrahim
             et al. (2011).


             NOMENCLATURE

             B g   gas formation volume factor, rcf/scf
             B o   oil formation volume factor, rbbl/STB
             CGR   condensate gas ratio
             CVD   constant volume depletion
             EOS   equation of state
             GOC   gas oil contact
                   equilibrium constant for component (i)
             K i
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