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A fully-implicit black-oil flow model. More...
#include <opm/material/densead/Math.hpp>
#include <opm/material/fluidsystems/BlackOilFluidSystem.hpp>
#include <opm/models/blackoil/blackoilboundaryratevector.hh>
#include <opm/models/blackoil/blackoilbrinemodules.hh>
#include <opm/models/blackoil/blackoildarcyfluxmodule.hh>
#include <opm/models/blackoil/blackoildiffusionmodule.hh>
#include <opm/models/blackoil/blackoildispersionmodule.hh>
#include <opm/models/blackoil/blackoilextbomodules.hh>
#include <opm/models/blackoil/blackoilextensivequantities.hh>
#include <opm/models/blackoil/blackoilfoammodules.hh>
#include <opm/models/blackoil/blackoilindices.hh>
#include <opm/models/blackoil/blackoilintensivequantities.hh>
#include <opm/models/blackoil/blackoillocalresidual.hh>
#include <opm/models/blackoil/blackoilmicpmodules.hh>
#include <opm/models/blackoil/blackoilnewtonmethod.hpp>
#include <opm/models/blackoil/blackoilpolymermodules.hh>
#include <opm/models/blackoil/blackoilprimaryvariables.hh>
#include <opm/models/blackoil/blackoilproblem.hh>
#include <opm/models/blackoil/blackoilproperties.hh>
#include <opm/models/blackoil/blackoilratevector.hh>
#include <opm/models/blackoil/blackoilsolventmodules.hh>
#include <opm/models/blackoil/blackoiltwophaseindices.hh>
#include <opm/models/common/multiphasebasemodel.hh>
#include <opm/models/io/vtkblackoilmodule.hpp>
#include <opm/models/io/vtkcompositionmodule.hpp>
#include <opm/models/io/vtkdiffusionmodule.hpp>
#include <sstream>
#include <string>
Go to the source code of this file.
Namespaces | |
namespace | Opm |
This file contains a set of helper functions used by VFPProd / VFPInj. | |
namespace | Opm::Properties::TTag |
The generic type tag for problems using the immiscible multi-phase model. | |
A fully-implicit black-oil flow model.
The black-oil model is a three-phase, three-component model widely used for oil reservoir simulation. The phases are denoted by lower index
The densities of the phases are determined by so-called formation volume factors:
Since the gas and water phases are assumed to be immiscible, this is sufficient to calculate their density. For the formation volume factor of the the oil phase
The composition of the oil phase is given by the gas dissolution factor
This allows to calculate all quantities required for the mass-conservation equations for each component, i.e.
where
By default
although the actual approach which is used can be specified via the FluxModule
property. For example, the velocity model can by changed to the Forchheimer approach by
The primary variables used by this model are: