Opm::BinaryCoeff::Brine_CO2< Scalar, H2O, CO2, verbose > Class Template Reference
Binary coefficients for brine and CO2. More...
#include <Brine_CO2.hpp>
Static Public Member Functions | |
| template<class Evaluation , class CO2Params > | |
| static OPM_HOST_DEVICE Evaluation | gasDiffCoeff (const CO2Params ¶ms, const Evaluation &temperature, const Evaluation &pressure, bool extrapolate=false) |
| Binary diffusion coefficent [m^2/s] of water in the CO2 phase. More... | |
| template<class Evaluation > | |
| static OPM_HOST_DEVICE Evaluation | liquidDiffCoeff (const Evaluation &, const Evaluation &) |
| Binary diffusion coefficent [m^2/s] of CO2 in the brine phase. More... | |
| template<class Evaluation , class CO2Params > | |
| static OPM_HOST_DEVICE void | calculateMoleFractions (const CO2Params ¶ms, const Evaluation &temperature, const Evaluation &pg, const Evaluation &salinity, const int knownPhaseIdx, Evaluation &xlCO2, Evaluation &ygH2O, const int &activityModel, bool extrapolate=false) |
| Returns the mol (!) fraction of CO2 in the liquid phase and the mol_ (!) fraction of H2O in the gas phase for a given temperature, pressure, CO2 density and brine salinity. More... | |
| template<class Evaluation > | |
| static OPM_HOST_DEVICE Evaluation | henry (const Evaluation &temperature, bool extrapolate=false) |
Henry coefficent ![$\mathrm{[N/m^2]}$](form_8.png) for CO2 in brine. | |
| template<class Evaluation , class CO2Params > | |
| static OPM_HOST_DEVICE Evaluation | fugacityCoefficientCO2 (const CO2Params ¶ms, const Evaluation &temperature, const Evaluation &pg, const Evaluation &yH2O, const bool highTemp, bool extrapolate=false, bool spycherPruess2005=false) |
| Returns the fugacity coefficient of the CO2 component in a water-CO2 mixture. More... | |
| template<class Evaluation , class CO2Params > | |
| static OPM_HOST_DEVICE Evaluation | fugacityCoefficientH2O (const CO2Params ¶ms, const Evaluation &temperature, const Evaluation &pg, const Evaluation &yH2O, const bool highTemp, bool extrapolate=false, bool spycherPruess2005=false) |
| Returns the fugacity coefficient of the H2O component in a water-CO2 mixture. More... | |
Detailed Description
template<class Scalar, class H2O, class CO2, bool verbose = true>
class Opm::BinaryCoeff::Brine_CO2< Scalar, H2O, CO2, verbose >
Binary coefficients for brine and CO2.
Member Function Documentation
◆ calculateMoleFractions()
template<class Scalar , class H2O , class CO2 , bool verbose = true>
template<class Evaluation , class CO2Params >
|
inlinestatic |
Returns the mol (!) fraction of CO2 in the liquid phase and the mol_ (!) fraction of H2O in the gas phase for a given temperature, pressure, CO2 density and brine salinity.
Implemented according to "Spycher and Pruess 2005" applying the activity coefficient expression of "Duan and Sun 2003" and the correlations for pure water given in "Spycher, Pruess and Ennis-King 2003"
- Parameters
-
params Parameters to use temperature the temperature [K] pg the gas phase pressure [Pa] salinity the salinity [kg NaCl / kg solution] knownPhaseIdx indicates which phases are present xlCO2 mole fraction of CO2 in brine [mol/mol] ygH2O mole fraction of water in the gas phase [mol/mol] activityModel Activity model to use extrapolate True to use extrapolation
◆ fugacityCoefficientCO2()
template<class Scalar , class H2O , class CO2 , bool verbose = true>
template<class Evaluation , class CO2Params >
|
inlinestatic |
Returns the fugacity coefficient of the CO2 component in a water-CO2 mixture.
(given in Spycher, Pruess and Ennis-King (2003))
- Parameters
-
params Parameters to use temperature the temperature [K] pg the gas phase pressure [Pa] yH2O mole fraction of water highTemp True to use high temperature extrapolate True to use extrapolation spycherPruess2005 True to Spycher-Pruess (2005) model
◆ fugacityCoefficientH2O()
template<class Scalar , class H2O , class CO2 , bool verbose = true>
template<class Evaluation , class CO2Params >
|
inlinestatic |
Returns the fugacity coefficient of the H2O component in a water-CO2 mixture.
(given in Spycher, Pruess and Ennis-King (2003))
- Parameters
-
params Parameters to use temperature the temperature [K] pg the gas phase pressure [Pa] yH2O mole fraction of water highTemp True to use high temperature extrapolate True to use extrapolation spycherPruess2005 True to Spycher-Pruess (2005) model
◆ gasDiffCoeff()
template<class Scalar , class H2O , class CO2 , bool verbose = true>
template<class Evaluation , class CO2Params >
|
inlinestatic |
Binary diffusion coefficent [m^2/s] of water in the CO2 phase.
According to "Diffusion of Water in Liquid and Supercritical Carbon Dioxide: An NMR Study",Bin Xu et al., 2002
- Parameters
-
params Parameters to use temperature the temperature [K] pressure the phase pressure [Pa] extrapolate True to use extrapolation
◆ liquidDiffCoeff()
template<class Scalar , class H2O , class CO2 , bool verbose = true>
template<class Evaluation >
|
inlinestatic |
Binary diffusion coefficent [m^2/s] of CO2 in the brine phase.
- Parameters
-
temperature the temperature [K] pressure the phase pressure [Pa]
The documentation for this class was generated from the following file:
- opm/material/binarycoefficients/Brine_CO2.hpp
