Binary coefficients for brine and CO2.  
#include <dumux/material/binarycoefficients/brine_co2.hh>
|  | 
| static Scalar | gasDiffCoeff (Scalar temperature, Scalar pressure) | 
|  | Binary diffusion coefficient \(\mathrm{[m^2/s]}\) of water in the CO2 phase. 
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|  | 
| static Scalar | liquidDiffCoeff (Scalar temperature, Scalar pressure) | 
|  | Binary diffusion coefficient \(\mathrm{[m^2/s]}\) of CO2 in the brine phase. 
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|  | 
| static void | calculateMoleFractions (const Scalar temperature, const Scalar pg, const Scalar salinity, const int knownPhaseIdx, Scalar &xlCO2, Scalar &ygH2O) | 
|  | 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. 
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|  | 
| static Scalar | fugacityCoefficientCO2 (Scalar T, Scalar pg) | 
|  | Returns the fugacity coefficient of the CO2 component in a water-CO2 mixture (given in Spycher, Pruess and Ennis-King (2003) [spycher2003] ) 
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|  | 
| static Scalar | fugacityCoefficientH2O (Scalar T, Scalar pg) | 
|  | Returns the fugacity coefficient of the H2O component in a water-CO2 mixture (given in Spycher, Pruess and Ennis-King (2003) [spycher2003] ) 
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|  | 
◆ calculateMoleFractions()
template<class Scalar, class CO2, bool verbose = true> 
  
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          | static void Dumux::BinaryCoeff::Brine_CO2< Scalar, CO2, verbose >::calculateMoleFractions | ( | const Scalar | temperature, |  
          |  |  | const Scalar | pg, |  
          |  |  | const Scalar | salinity, |  
          |  |  | const int | knownPhaseIdx, |  
          |  |  | Scalar & | xlCO2, |  
          |  |  | Scalar & | ygH2O ) |  | inlinestatic | 
 
Implemented according to Spycher and Pruess (2005) [spycher2005] 
 applying the activity coefficient expression of Duan and Sun (2003) [duan2003] 
 and the correlations for pure water given in Spycher, Pruess and Ennis-King (2003) [spycher2003] 
- Parameters
- 
  
    | temperature | the temperature \(\mathrm{[K]}\) |  | pg | the gas phase pressure \(\mathrm{[Pa]}\) |  | salinity | the salinity \(\mathrm{[kg \ NaCl / kg \ solution]}\) |  | knownPhaseIdx | indicates which phases are present |  | xlCO2 | mole fraction of CO2 in brine \(\mathrm{[mol/mol]}\) |  | ygH2O | mole fraction of water in the gas phase \(\mathrm{[mol/mol]}\) |  
 
 
 
◆ fugacityCoefficientCO2()
template<class Scalar, class CO2, bool verbose = true> 
 
- Parameters
- 
  
    | T | the temperature \(\mathrm{[K]}\) |  | pg | the gas phase pressure \(\mathrm{[Pa]}\) |  
 
 
 
◆ fugacityCoefficientH2O()
template<class Scalar, class CO2, bool verbose = true> 
 
- Parameters
- 
  
    | T | the temperature \(\mathrm{[K]}\) |  | pg | the gas phase pressure \(\mathrm{[Pa]}\) |  
 
 
 
◆ gasDiffCoeff()
template<class Scalar, class CO2, bool verbose = true> 
 
According to B. Xu et al. (2002) [xu2003] 
 
- Parameters
- 
  
    | temperature | the temperature \(\mathrm{[K]}\) |  | pressure | the phase pressure \(\mathrm{[Pa]}\) |  
 
 
 
◆ liquidDiffCoeff()
template<class Scalar, class CO2, bool verbose = true> 
 
- Parameters
- 
  
    | temperature | the temperature \(\mathrm{[K]}\) |  | pressure | the phase pressure \(\mathrm{[Pa]}\) |  
 
 
 
The documentation for this class was generated from the following file: