version 3.9-dev
Dumux::FluidSystems::H2ON2Kinetic< Scalar, Policy > Class Template Reference

A two-phase fluid system with two components water \((\mathrm{H_2O})\) Nitrogen \((\mathrm{N_2})\) for non-equilibrium models. TODO: Is this fluid system necessary??

#include <dumux/material/fluidsystems/h2on2kinetic.hh>

Inheritance diagram for Dumux::FluidSystems::H2ON2Kinetic< Scalar, Policy >:

Public Types

using ParameterCache = NullParameterCache
 The type of parameter cache objects. More...
 
using H2O = TabulatedH2O
 The components for pure water. More...
 
using N2 = SimpleN2
 The components for pure nitrogen. More...
 
using Scalar = Scalar
 export the scalar type More...
 

Static Public Member Functions

template<class FluidState >
static Scalar componentEnthalpy (FluidState &fluidState, const int phaseIdx, const int compIdx)
 Return the enthalpy of a component in a phase. More...
 
static Scalar henry (Scalar temperature)
 Return the Henry constant for a component in a phase. \(\mathrm{[Pa]}\). More...
 
static Scalar vaporPressure (Scalar temperature)
 Return the vapor pressure of a component above one phase. \(\mathrm{[Pa]}\). More...
 
static std::string phaseName (int phaseIdx)
 Return the human readable name of a fluid phase. More...
 
static constexpr bool isMiscible ()
 Returns whether the fluids are miscible. More...
 
static constexpr bool isGas (int phaseIdx)
 Return whether a phase is gaseous. More...
 
static bool isIdealMixture (int phaseIdx)
 Returns true if and only if a fluid phase is assumed to be an ideal mixture. More...
 
static constexpr bool isCompressible (int phaseIdx)
 Returns true if and only if a fluid phase is assumed to be compressible. More...
 
static bool isIdealGas (int phaseIdx)
 Returns true if and only if a fluid phase is assumed to be an ideal gas. More...
 
static std::string componentName (int compIdx)
 Return the human readable name of a component. More...
 
static Scalar molarMass (int compIdx)
 Return the molar mass of a component in \(\mathrm{[kg/mol]}\). More...
 
static Scalar criticalTemperature (int compIdx)
 Critical temperature of a component \(\mathrm{[K]}\). More...
 
static Scalar criticalPressure (int compIdx)
 Critical pressure of a component \(\mathrm{[Pa]}\). More...
 
static Scalar kelvinVaporPressure (const FluidState &fluidState, const int phaseIdx, const int compIdx)
 Vapor pressure including the Kelvin equation in \(\mathrm{[Pa]}\). More...
 
static Scalar criticalMolarVolume (int compIdx)
 Molar volume of a component at the critical point \(\mathrm{[m^3/mol]}\). More...
 
static Scalar acentricFactor (int compIdx)
 The acentric factor of a component \(\mathrm{[-]}\). More...
 
static void init ()
 Initialize the fluid system's static parameters generically. More...
 
static void init (Scalar tempMin, Scalar tempMax, unsigned nTemp, Scalar pressMin, Scalar pressMax, unsigned nPress)
 Initialize the fluid system's static parameters using problem specific temperature and pressure ranges. More...
 
static Scalar density (const FluidState &fluidState, int phaseIdx)
 Given a phase's composition, temperature, pressure, and the partial pressures of all components, return its density \(\mathrm{[kg/m^3]}\). More...
 
static Scalar density (const FluidState &fluidState, const ParameterCache &paramCache, int phaseIdx)
 Calculate the density \(\mathrm{[kg/m^3]}\) of a fluid phase. More...
 
static Scalar molarDensity (const FluidState &fluidState, int phaseIdx)
 Calculate the molar density \(\mathrm{[mol/m^3]}\) of a fluid phase. More...
 
static Scalar molarDensity (const FluidState &fluidState, const ParameterCache &paramCache, int phaseIdx)
 Calculate the molar density \(\mathrm{[mol/m^3]}\) of a fluid phase. More...
 
static Scalar viscosity (const FluidState &fluidState, int phaseIdx)
 Calculate the dynamic viscosity of a fluid phase \(\mathrm{[Pa*s]}\). More...
 
static Scalar viscosity (const FluidState &fluidState, const ParameterCache &paramCache, int phaseIdx)
 Calculate the dynamic viscosity of a fluid phase \(\mathrm{[Pa*s]}\). More...
 
static Scalar fugacityCoefficient (const FluidState &fluidState, int phaseIdx, int compIdx)
 Calculate the fugacity coefficient \(\mathrm{[Pa]}\) of an individual component in a fluid phase. More...
 
static Scalar fugacityCoefficient (const FluidState &fluidState, const ParameterCache &paramCache, int phaseIdx, int compIdx)
 Calculate the fugacity coefficient \(\mathrm{[Pa]}\) of an individual component in a fluid phase. More...
 
static Scalar diffusionCoefficient (const FluidState &fluidState, int phaseIdx, int compIdx)
 Calculate the binary molecular diffusion coefficient for a component in a fluid phase \(\mathrm{[mol^2 * s / (kg*m^3)]}\). More...
 
static Scalar diffusionCoefficient (const FluidState &fluidState, const ParameterCache &paramCache, int phaseIdx, int compIdx)
 Calculate the binary molecular diffusion coefficient for a component in a fluid phase \(\mathrm{[mol^2 * s / (kg*m^3)]}\). More...
 
static Scalar binaryDiffusionCoefficient (const FluidState &fluidState, int phaseIdx, int compIIdx, int compJIdx)
 Given a phase's composition, temperature and pressure, return the binary diffusion coefficient \(\mathrm{[m^2/s]}\) for components \(\mathrm{i}\) and \(\mathrm{j}\) in this phase. More...
 
static Scalar binaryDiffusionCoefficient (const FluidState &fluidState, const ParameterCache &paramCache, int phaseIdx, int compIIdx, int compJIdx)
 Given a phase's composition, temperature and pressure, return the binary diffusion coefficient \(\mathrm{[m^2/s]}\) for components \(\mathrm{i}\) and \(\mathrm{j}\) in this phase. More...
 
static Scalar enthalpy (const FluidState &fluidState, int phaseIdx)
 Given a phase's composition, temperature, pressure and density, calculate its specific enthalpy \(\mathrm{[J/kg]}\). More...
 
static Scalar enthalpy (const FluidState &fluidState, const ParameterCache &paramCache, int phaseIdx)
 Given a phase's composition, temperature, pressure and density, calculate its specific enthalpy \(\mathrm{[J/kg]}\). More...
 
static Scalar componentEnthalpy (const FluidState &fluidState, int phaseIdx, int componentIdx)
 Returns the specific enthalpy \(\mathrm{[J/kg]}\) of a component in the specified phase. More...
 
static Scalar thermalConductivity (const FluidState &fluidState, const int phaseIdx)
 Thermal conductivity of a fluid phase \(\mathrm{[W/(m K)]}\). More...
 
static Scalar thermalConductivity (const FluidState &fluidState, const ParameterCache &paramCache, int phaseIdx)
 Thermal conductivity \(\lambda_\alpha \) of a fluid phase \(\mathrm{[W/(m K)]}\). More...
 
static Scalar heatCapacity (const FluidState &fluidState, int phaseIdx)
 Specific isobaric heat capacity \(c_{p,\alpha}\) of a fluid phase \(\mathrm{[J/(kg*K)]}\). More...
 
static Scalar heatCapacity (const FluidState &fluidState, const ParameterCache &paramCache, int phaseIdx)
 Specific isobaric heat capacity \(c_{p,\alpha}\) of a fluid phase \(\mathrm{[J/(kg*K)]}\). More...
 
static constexpr bool isTracerFluidSystem ()
 Some properties of the fluid system. More...
 
static constexpr int getMainComponent (int phaseIdx)
 Get the main component of a given phase if possible. More...
 
static constexpr bool viscosityIsConstant (int phaseIdx)
 Returns true if and only if a fluid phase is assumed to have a constant viscosity. More...
 

Static Public Attributes

static constexpr int numPhases
 Number of phases in the fluid system. More...
 
static constexpr int numComponents
 Number of components in the fluid system. More...
 
static constexpr int liquidPhaseIdx
 index of the liquid phase More...
 
static constexpr int gasPhaseIdx
 index of the gas phase More...
 
static constexpr int phase0Idx
 index of the first phase More...
 
static constexpr int phase1Idx
 index of the second phase More...
 
static constexpr int H2OIdx
 
static constexpr int N2Idx
 
static constexpr int comp0Idx
 index of the first component More...
 
static constexpr int comp1Idx
 index of the second component More...
 
static constexpr int liquidCompIdx
 index of the liquid component More...
 
static constexpr int gasCompIdx
 index of the gas component More...
 

Member Typedef Documentation

◆ H2O

◆ N2

◆ ParameterCache

template<class Scalar , class Policy = H2ON2DefaultPolicy<>>
using Dumux::FluidSystems::H2ON2Kinetic< Scalar, Policy >::ParameterCache = NullParameterCache

◆ Scalar

using Dumux::FluidSystems::Base< Scalar , H2ON2< Scalar, H2ON2DefaultPolicy<> > >::Scalar = Scalar
inherited

Member Function Documentation

◆ acentricFactor()

static Scalar Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::acentricFactor ( int  compIdx)
inlinestaticinherited
Parameters
compIdxThe index of the component to consider

◆ binaryDiffusionCoefficient() [1/2]

static Scalar Dumux::FluidSystems::Base< Scalar , H2ON2< Scalar, H2ON2DefaultPolicy<> > >::binaryDiffusionCoefficient ( const FluidState &  fluidState,
const ParameterCache paramCache,
int  phaseIdx,
int  compIIdx,
int  compJIdx 
)
inlinestaticinherited
Parameters
fluidStateThe fluid state
paramCachemutable parameters
phaseIdxIndex of the fluid phase
compIIdxIndex of the component i
compJIdxIndex of the component j

◆ binaryDiffusionCoefficient() [2/2]

static Scalar Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::binaryDiffusionCoefficient ( const FluidState &  fluidState,
int  phaseIdx,
int  compIIdx,
int  compJIdx 
)
inlinestaticinherited
Parameters
fluidStateThe fluid state
phaseIdxIndex of the fluid phase
compIIdxIndex of the component i
compJIdxIndex of the component j

◆ componentEnthalpy() [1/2]

static Scalar Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::componentEnthalpy ( const FluidState &  fluidState,
int  phaseIdx,
int  componentIdx 
)
inlinestaticinherited
Parameters
fluidStateThe fluid state
phaseIdxThe index of the phase
componentIdxThe index of the component

◆ componentEnthalpy() [2/2]

template<class Scalar , class Policy = H2ON2DefaultPolicy<>>
template<class FluidState >
static Scalar Dumux::FluidSystems::H2ON2Kinetic< Scalar, Policy >::componentEnthalpy ( FluidState &  fluidState,
const int  phaseIdx,
const int  compIdx 
)
inlinestatic
Parameters
fluidStateA container with the current (physical) state of the fluid
phaseIdxThe index of the phase to consider
compIdxThe index of the component to consider

◆ componentName()

static std::string Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::componentName ( int  compIdx)
inlinestaticinherited
Parameters
compIdxThe index of the component to consider

◆ criticalMolarVolume()

static Scalar Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::criticalMolarVolume ( int  compIdx)
inlinestaticinherited
Parameters
compIdxThe index of the component to consider

◆ criticalPressure()

static Scalar Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::criticalPressure ( int  compIdx)
inlinestaticinherited
Parameters
compIdxThe index of the component to consider

◆ criticalTemperature()

static Scalar Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::criticalTemperature ( int  compIdx)
inlinestaticinherited
Parameters
compIdxThe index of the component to consider

◆ density() [1/2]

static Scalar Dumux::FluidSystems::Base< Scalar , H2ON2< Scalar, H2ON2DefaultPolicy<> > >::density ( const FluidState &  fluidState,
const ParameterCache paramCache,
int  phaseIdx 
)
inlinestaticinherited
Parameters
fluidStateThe fluid state
paramCachemutable parameters
phaseIdxIndex of the fluid phase

◆ density() [2/2]

static Scalar Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::density ( const FluidState &  fluidState,
int  phaseIdx 
)
inlinestaticinherited

If Policy::useH2ODensityAsLiquidMixtureDensity() == false, we apply Eq. (7) in Class et al. (2002a) [20]
for the liquid density.

Parameters
fluidStateAn arbitrary fluid state
phaseIdxThe index of the fluid phase to consider

◆ diffusionCoefficient() [1/2]

static Scalar Dumux::FluidSystems::Base< Scalar , H2ON2< Scalar, H2ON2DefaultPolicy<> > >::diffusionCoefficient ( const FluidState &  fluidState,
const ParameterCache paramCache,
int  phaseIdx,
int  compIdx 
)
inlinestaticinherited

Molecular diffusion of a component \(\mathrm{\kappa}\) is caused by a gradient of the chemical potential and follows the law

\[ J = - D \nabla \mu_\kappa \]

where \(\mathrm{\mu_\kappa}\) is the component's chemical potential, \(\mathrm{D}\) is the diffusion coefficient and \(\mathrm{J}\) is the diffusive flux. \(\mathrm{\mu_\kappa}\) is connected to the component's fugacity \(\mathrm{f_\kappa}\) by the relation

\[ \mu_\kappa = R T_\alpha \mathrm{ln} \frac{f_\kappa}{p_\alpha} \]

where \(\mathrm{p_\alpha}\) and \(\mathrm{T_\alpha}\) are the fluid phase' pressure and temperature.

Parameters
fluidStateThe fluid state
paramCachemutable parameters
phaseIdxIndex of the fluid phase
compIdxIndex of the component

◆ diffusionCoefficient() [2/2]

static Scalar Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::diffusionCoefficient ( const FluidState &  fluidState,
int  phaseIdx,
int  compIdx 
)
inlinestaticinherited

Molecular diffusion of a component \(\mathrm{\kappa}\) is caused by a gradient of the chemical potential and follows the law

\[ J = - D \nabla \mu_\kappa \]

where \(\mathrm{\mu_\kappa}\) is the component's chemical potential, \(\mathrm{D}\) is the diffusion coefficient and \(\mathrm{J}\) is the diffusive flux. \(\mathrm{\mu_\kappa}\) is connected to the component's fugacity \(\mathrm{f_\kappa}\) by the relation

\[ \mu_\kappa = R T_\alpha \mathrm{ln} \frac{f_\kappa}{p_\alpha} \]

where \(\mathrm{p_\alpha}\) and \(\mathrm{T_\alpha}\) are the fluid phase' pressure and temperature.

Parameters
fluidStateThe fluid state
phaseIdxIndex of the fluid phase
compIdxIndex of the component

◆ enthalpy() [1/2]

static Scalar Dumux::FluidSystems::Base< Scalar , H2ON2< Scalar, H2ON2DefaultPolicy<> > >::enthalpy ( const FluidState &  fluidState,
const ParameterCache paramCache,
int  phaseIdx 
)
inlinestaticinherited
Parameters
fluidStateThe fluid state
paramCachemutable parameters
phaseIdxIndex of the fluid phase

◆ enthalpy() [2/2]

static Scalar Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::enthalpy ( const FluidState &  fluidState,
int  phaseIdx 
)
inlinestaticinherited
Note
This fluid system neglects the contribution of gas-molecules in the liquid phase. This contribution is probably not big. Somebody would have to find out the enthalpy of solution for this system. ...
Parameters
fluidStateAn arbitrary fluid state
phaseIdxThe index of the fluid phase to consider

◆ fugacityCoefficient() [1/2]

static Scalar Dumux::FluidSystems::Base< Scalar , H2ON2< Scalar, H2ON2DefaultPolicy<> > >::fugacityCoefficient ( const FluidState &  fluidState,
const ParameterCache paramCache,
int  phaseIdx,
int  compIdx 
)
inlinestaticinherited

The fugacity coefficient \(\mathrm{\phi^\kappa_\alpha}\) is connected to the fugacity \(\mathrm{f^\kappa_\alpha}\) and the component's mole fraction \(\mathrm{x^\kappa_\alpha}\) by means of the relation

\[ f^\kappa_\alpha = \phi^\kappa_\alpha\;x^\kappa_\alpha\;p_\alpha \]

Parameters
fluidStateThe fluid state
paramCachemutable parameters
phaseIdxIndex of the fluid phase
compIdxIndex of the component

◆ fugacityCoefficient() [2/2]

static Scalar Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::fugacityCoefficient ( const FluidState &  fluidState,
int  phaseIdx,
int  compIdx 
)
inlinestaticinherited

The fugacity coefficient \(\mathrm{\phi^\kappa_\alpha}\) is connected to the fugacity \(\mathrm{f^\kappa_\alpha}\) and the component's mole fraction \(\mathrm{x^\kappa_\alpha}\) by means of the relation

\[ f^\kappa_\alpha = \phi^\kappa_\alpha\;x^\kappa_\alpha\;p_\alpha \]

Parameters
fluidStateThe fluid state
phaseIdxIndex of the fluid phase
compIdxIndex of the component

◆ getMainComponent()

static constexpr int Dumux::FluidSystems::Base< Scalar , H2ON2< Scalar, H2ON2DefaultPolicy<> > >::getMainComponent ( int  phaseIdx)
inlinestaticconstexprinherited
Parameters
phaseIdxThe index of the fluid phase to consider
Note
This only makes sense if this is not a tracer fluid system (then the bulk component is not balanced)

◆ heatCapacity() [1/2]

static Scalar Dumux::FluidSystems::Base< Scalar , H2ON2< Scalar, H2ON2DefaultPolicy<> > >::heatCapacity ( const FluidState &  fluidState,
const ParameterCache paramCache,
int  phaseIdx 
)
inlinestaticinherited

Given a fluid state, an up-to-date parameter cache and a phase index, this method computes the isobaric heat capacity \(c_{p,\alpha}\) of the fluid phase. The isobaric heat capacity is defined as the partial derivative of the specific enthalpy \(h_\alpha\) to the fluid pressure \(p_\alpha\):

\( c_{p,\alpha} = \frac{\partial h_\alpha}{\partial p_\alpha} \)

Parameters
fluidStaterepresents all relevant thermodynamic quantities of a fluid system
paramCachemutable parameters
phaseIdxIndex of the fluid phase

◆ heatCapacity() [2/2]

static Scalar Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::heatCapacity ( const FluidState &  fluidState,
int  phaseIdx 
)
inlinestaticinherited
Parameters
fluidStaterepresents all relevant thermodynamic quantities of a fluid system
phaseIdxIndex of the fluid phase

Given a fluid state, an up-to-date parameter cache and a phase index, this method computes the isobaric heat capacity \(c_{p,\alpha}\) of the fluid phase. The isobaric heat capacity is defined as the partial derivative of the specific enthalpy \(h_\alpha\) to the fluid pressure \(p_\alpha\):

\( c_{p,\alpha} = \frac{\partial h_\alpha}{\partial p_\alpha} \)

◆ henry()

template<class Scalar , class Policy = H2ON2DefaultPolicy<>>
static Scalar Dumux::FluidSystems::H2ON2Kinetic< Scalar, Policy >::henry ( Scalar  temperature)
inlinestatic
Parameters
temperatureThe given temperature

◆ init() [1/2]

static void Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::init ( )
inlinestaticinherited

If a tabulated H2O component is used, we do our best to create tables that always work.

◆ init() [2/2]

static void Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::init ( Scalar  tempMin,
Scalar  tempMax,
unsigned  nTemp,
Scalar  pressMin,
Scalar  pressMax,
unsigned  nPress 
)
inlinestaticinherited
Parameters
tempMinThe minimum temperature used for tabulation of water \(\mathrm{[K]}\)
tempMaxThe maximum temperature used for tabulation of water \(\mathrm{[K]}\)
nTempThe number of ticks on the temperature axis of the table of water
pressMinThe minimum pressure used for tabulation of water \(\mathrm{[Pa]}\)
pressMaxThe maximum pressure used for tabulation of water \(\mathrm{[Pa]}\)
nPressThe number of ticks on the pressure axis of the table of water

◆ isCompressible()

static constexpr bool Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::isCompressible ( int  phaseIdx)
inlinestaticconstexprinherited

Compressible means that the partial derivative of the density to the fluid pressure is always larger than zero.

Parameters
phaseIdxThe index of the fluid phase to consider

◆ isGas()

static constexpr bool Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::isGas ( int  phaseIdx)
inlinestaticconstexprinherited
Parameters
phaseIdxThe index of the fluid phase to consider

◆ isIdealGas()

static bool Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::isIdealGas ( int  phaseIdx)
inlinestaticinherited
Parameters
phaseIdxThe index of the fluid phase to consider

◆ isIdealMixture()

static bool Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::isIdealMixture ( int  phaseIdx)
inlinestaticinherited

We define an ideal mixture as a fluid phase where the fugacity coefficients of all components times the pressure of the phase are independent on the fluid composition. This assumption is true if Henry's law and Raoult's law apply. If you are unsure what this function should return, it is safe to return false. The only damage done will be (slightly) increased computation times in some cases.

Parameters
phaseIdxThe index of the fluid phase to consider

◆ isMiscible()

static constexpr bool Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::isMiscible ( )
inlinestaticconstexprinherited

◆ isTracerFluidSystem()

static constexpr bool Dumux::FluidSystems::Base< Scalar , H2ON2< Scalar, H2ON2DefaultPolicy<> > >::isTracerFluidSystem ( )
inlinestaticconstexprinherited

If the fluid system only contains tracer components

◆ kelvinVaporPressure()

static Scalar Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::kelvinVaporPressure ( const FluidState &  fluidState,
const int  phaseIdx,
const int  compIdx 
)
inlinestaticinherited

Calculate the decreased vapor pressure due to capillarity

Parameters
fluidStateAn arbitrary fluid state
phaseIdxThe index of the fluid phase to consider
compIdxThe index of the component to consider

◆ molarDensity() [1/2]

static Scalar Dumux::FluidSystems::Base< Scalar , H2ON2< Scalar, H2ON2DefaultPolicy<> > >::molarDensity ( const FluidState &  fluidState,
const ParameterCache paramCache,
int  phaseIdx 
)
inlinestaticinherited

The molar density is defined by the mass density \(\rho_\alpha\) and the component molar mass \(M_\alpha\) after

\[\rho_{mol,\alpha} = \frac{\rho_\alpha}{M_\alpha} \;.\]

Parameters
fluidStateThe fluid state
paramCachemutable parameters
phaseIdxIndex of the fluid phase

◆ molarDensity() [2/2]

static Scalar Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::molarDensity ( const FluidState &  fluidState,
int  phaseIdx 
)
inlinestaticinherited
Parameters
fluidStateThe fluid state
phaseIdxIndex of the fluid phase

◆ molarMass()

static Scalar Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::molarMass ( int  compIdx)
inlinestaticinherited
Parameters
compIdxThe index of the component to consider

◆ phaseName()

static std::string Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::phaseName ( int  phaseIdx)
inlinestaticinherited
Parameters
phaseIdxThe index of the fluid phase to consider

◆ thermalConductivity() [1/2]

static Scalar Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::thermalConductivity ( const FluidState &  fluidState,
const int  phaseIdx 
)
inlinestaticinherited

Use the conductivity of air and water as a first approximation.

Parameters
fluidStateAn arbitrary fluid state
phaseIdxThe index of the fluid phase to consider

◆ thermalConductivity() [2/2]

static Scalar Dumux::FluidSystems::Base< Scalar , H2ON2< Scalar, H2ON2DefaultPolicy<> > >::thermalConductivity ( const FluidState &  fluidState,
const ParameterCache paramCache,
int  phaseIdx 
)
inlinestaticinherited
Parameters
fluidStateThe fluid state
paramCachemutable parameters
phaseIdxIndex of the fluid phase

◆ vaporPressure()

template<class Scalar , class Policy = H2ON2DefaultPolicy<>>
static Scalar Dumux::FluidSystems::H2ON2Kinetic< Scalar, Policy >::vaporPressure ( Scalar  temperature)
inlinestatic
Parameters
temperatureThe given temperature

◆ viscosity() [1/2]

static Scalar Dumux::FluidSystems::Base< Scalar , H2ON2< Scalar, H2ON2DefaultPolicy<> > >::viscosity ( const FluidState &  fluidState,
const ParameterCache paramCache,
int  phaseIdx 
)
inlinestaticinherited
Parameters
fluidStateThe fluid state
paramCachemutable parameters
phaseIdxIndex of the fluid phase

◆ viscosity() [2/2]

static Scalar Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::viscosity ( const FluidState &  fluidState,
int  phaseIdx 
)
inlinestaticinherited

Compositional effects in the gas phase are accounted by the Wilke method. See Reid et al. (1987) [70]
4th edition, McGraw-Hill, 1987, 407-410 5th edition, McGraw-Hill, 20001, p. 9.21/22

Parameters
fluidStateAn arbitrary fluid state
phaseIdxThe index of the fluid phase to consider
Note
Compositional effects for a liquid mixture have to be implemented.

◆ viscosityIsConstant()

static constexpr bool Dumux::FluidSystems::Base< Scalar , H2ON2< Scalar, H2ON2DefaultPolicy<> > >::viscosityIsConstant ( int  phaseIdx)
inlinestaticconstexprinherited
Parameters
phaseIdxThe index of the fluid phase to consider

Member Data Documentation

◆ comp0Idx

constexpr int Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::comp0Idx
staticconstexprinherited

◆ comp1Idx

constexpr int Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::comp1Idx
staticconstexprinherited

◆ gasCompIdx

constexpr int Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::gasCompIdx
staticconstexprinherited

◆ gasPhaseIdx

constexpr int Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::gasPhaseIdx
staticconstexprinherited

◆ H2OIdx

constexpr int Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::H2OIdx
staticconstexprinherited

◆ liquidCompIdx

constexpr int Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::liquidCompIdx
staticconstexprinherited

◆ liquidPhaseIdx

constexpr int Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::liquidPhaseIdx
staticconstexprinherited

◆ N2Idx

constexpr int Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::N2Idx
staticconstexprinherited

◆ numComponents

constexpr int Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::numComponents
staticconstexprinherited

◆ numPhases

constexpr int Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::numPhases
staticconstexprinherited

◆ phase0Idx

constexpr int Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::phase0Idx
staticconstexprinherited

◆ phase1Idx

constexpr int Dumux::FluidSystems::H2ON2< Scalar, H2ON2DefaultPolicy<> >::phase1Idx
staticconstexprinherited

The documentation for this class was generated from the following file: