 Dune | |
  FieldTraits< Opm::DenseAd::Evaluation< ValueType, numVars > > | |
 Opm | |
  BinaryCoeff | |
   Air_Mesitylene | Binary coefficients for water and mesitylene |
   Air_Xylene | Binary coefficients for water and xylene |
   Brine_CO2 | Binary coefficients for brine and CO2 |
   H2O_Air | Binary coefficients for water and nitrogen |
   H2O_CO2 | Binary coefficients for water and CO2 |
   H2O_Mesitylene | Binary coefficients for water and mesitylene |
   H2O_N2 | Binary coefficients for water and nitrogen |
   H2O_Xylene | Binary coefficients for water and xylene |
  DenseAd | |
   Evaluation | Represents a function evaluation and its derivatives w.r.t |
   Evaluation< ValueT, 1 > | |
   Evaluation< ValueT, 10 > | |
   Evaluation< ValueT, 11 > | |
   Evaluation< ValueT, 12 > | |
   Evaluation< ValueT, 2 > | |
   Evaluation< ValueT, 3 > | |
   Evaluation< ValueT, 4 > | |
   Evaluation< ValueT, 5 > | |
   Evaluation< ValueT, 6 > | |
   Evaluation< ValueT, 7 > | |
   Evaluation< ValueT, 8 > | |
   Evaluation< ValueT, 9 > | |
  FluidSystems | |
   BlackOil | A fluid system which uses the black-oil model assumptions to calculate termodynamically meaningful quantities |
    ParameterCache | The type of the fluid system's parameter cache. |
   BrineCO2 | A two-phase fluid system with water and CO2 |
    ParameterCache | |
   H2OAir | A fluid system with a liquid and a gaseous phase and water and air as components |
    ParameterCache | |
   H2OAirMesitylene | A fluid system with water, gas and NAPL as phases and water, air and mesitylene (DNAPL) as components |
    ParameterCache | |
   H2OAirXylene | A fluid system with water, gas and NAPL as phases and water, air and NAPL (contaminant) as components |
    ParameterCache | |
   H2ON2 | A two-phase fluid system with water and nitrogen as components |
   H2ON2LiquidPhase | A liquid-phase-only fluid system with water and nitrogen as components |
    ParameterCache | The type of the fluid system's parameter cache. |
   SinglePhase | A fluid system for single phase models |
    ParameterCache | The type of the fluid system's parameter cache. |
   Spe5 | The fluid system for the oil, gas and water phases of the SPE5 problem |
    ParameterCache | The type of the fluid system's parameter cache. |
   TwoPhaseImmiscible | A fluid system for two-phase models assuming immiscibility and thermodynamic equilibrium |
    ParameterCache | |
  IAPWS | |
   Common | Implements relations which are common for all regions of the IAPWS '97 formulation |
   Region1 | Implements the equations for region 1 of the IAPWS '97 formulation |
   Region2 | Implements the equations for region 2 of the IAPWS '97 formulation |
   Region4 | Implements the equations for region 4 of the IAPWS '97 formulation |
  EnsureFinalized | Default implementation for asserting finalization of parameter objects |
  MathToolbox | |
  ReturnEval_ | |
  Spline | Class implementing cubic splines |
   ComparatorX_ | Helper class needed to sort the input sampling points |
  Tabulated1DFunction | Implements a linearly interpolated scalar function that depends on one variable |
  TridiagonalMatrix | Provides a tridiagonal matrix that also supports non-zero entries in the upper right and lower left |
  UniformTabulated2DFunction | Implements a scalar function that depends on two variables and which is sampled on an uniform X-Y grid |
  UniformXTabulated2DFunction | Implements a scalar function that depends on two variables and which is sampled uniformly in the X direction, but non-uniformly on the Y axis- |
  Air | A simple class implementing the fluid properties of air |
  Brine | A class for the brine fluid properties |
  CO2 | A class for the CO2 fluid properties |
  Component | Abstract base class of a pure chemical species |
  DNAPL | A simple implementation of a dense non-aqueous phase liquid (DNAPL) |
  H2O | Material properties of pure water |
  LNAPL | A simple implementation of a LNAPL, e.g |
  Mesitylene | Component for Mesitylene |
  N2 | Properties of pure molecular nitrogen |
  NullComponent | A component that only throws exceptions |
  SimpleCO2 | A simplistic class representing the fluid properties |
  SimpleH2O | A simple version of pure water |
  TabulatedComponent | A generic class which tabulates all thermodynamic properties of a given component |
  Unit | A component where all quantities are fixed at 1.0 |
  Xylene | Component for Xylene |
  Constants | A central place for various physical constants occuring in some equations |
  CompositionFromFugacities | Calculates the chemical equilibrium from the component fugacities in a phase |
  ComputeFromReferencePhase | Computes all quantities of a generic fluid state if a reference phase has been specified |
  ImmiscibleFlash | Determines the pressures and saturations of all fluid phases given the total mass of all components |
  MMPCAuxConstraint | Specifies an auxiliary constraint for the MiscibleMultiPhaseComposition constraint solver |
  MiscibleMultiPhaseComposition | Computes the composition of all phases of a N-phase, N-component fluid system assuming that all N phases are present |
  NcpFlash | Determines the phase compositions, pressures and saturations given the total mass of all components |
  MathToolbox< Opm::DenseAd::Evaluation< ValueT, numVars > > | |
  PengRobinson | Implements the Peng-Robinson equation of state for liquids and gases |
  PengRobinsonMixture | Implements the Peng-Robinson equation of state for a mixture |
  PengRobinsonParams | Stores and provides access to the Peng-Robinson parameters |
  PengRobinsonParamsMixture | The mixing rule for the oil and the gas phases of the SPE5 problem |
  BrooksCorey | Implementation of the Brooks-Corey capillary pressure <-> saturation relation |
  BrooksCoreyParams | Specification of the material parameters for the Brooks-Corey constitutive relations |
  EclDefaultMaterial | Implements the default three phase capillary pressure law used by the ECLipse simulator |
  EclDefaultMaterialParams | Default implementation for the parameters required by the default three-phase capillary pressure model used by Eclipse |
  EclEpsConfig | Specifies the configuration used by the endpoint scaling code |
  EclEpsGridProperties | Collects all grid properties which are relevant for end point scaling |
  EclEpsScalingPointsInfo | This structure represents all values which can be possibly used as scaling points in the endpoint scaling code |
  EclEpsScalingPoints | Represents the points on the X and Y axis to be scaled if endpoint scaling is used |
  EclEpsTwoPhaseLaw | This material law takes a material law defined for unscaled saturation and converts it to a material law defined on scaled saturations |
  EclEpsTwoPhaseLawParams | A default implementation of the parameters for the material law adapter class which implements ECL endpoint scaleing |
  EclHysteresisConfig | Specifies the configuration used by the ECL kr/pC hysteresis code |
  EclHysteresisTwoPhaseLaw | This material law implements the hysteresis model of the ECL file format |
  EclHysteresisTwoPhaseLawParams | A default implementation of the parameters for the material law which implements the ECL relative permeability and capillary pressure hysteresis |
  EclMaterialLawManager | Provides an simple way to create and manage the material law objects for a complete ECL deck |
  EclMultiplexerMaterial | Implements a multiplexer class that provides all three phase capillary pressure laws used by the ECLipse simulator |
  EclMultiplexerMaterialParams | Multiplexer implementation for the parameters required by the multiplexed three-phase material law |
  EclStone1Material | Implements the second phase capillary pressure/relperm law suggested by Stone as used by the ECLipse simulator |
  EclStone1MaterialParams | Default implementation for the parameters required by the three-phase capillary pressure/relperm Stone 2 model used by Eclipse |
  EclStone2Material | Implements the second phase capillary pressure/relperm law suggested by Stone as used by the ECLipse simulator |
  EclStone2MaterialParams | Default implementation for the parameters required by the three-phase capillary pressure/relperm Stone 2 model used by Eclipse |
  EclTwoPhaseMaterial | Implements a multiplexer class that provides ECL saturation functions for twophase simulations |
  EclTwoPhaseMaterialParams | Implementation for the parameters required by the material law for two-phase simulations |
  EffToAbsLaw | This material law takes a material law defined for effective saturations and converts it to a material law defined on absolute saturations |
  EffToAbsLawParams | A default implementation of the parameters for the adapter class to convert material laws from effective to absolute saturations |
  LinearMaterial | Implements a linear saturation-capillary pressure relation |
  LinearMaterialParams | Reference implementation of params for the linear M-phase material material |
  NullMaterialTraits | A generic traits class which does not provide any indices |
  TwoPhaseMaterialTraits | A generic traits class for two-phase material laws |
  ThreePhaseMaterialTraits | A generic traits class for three-phase material laws |
  NullMaterial | Implements a dummy linear saturation-capillary pressure relation which just disables capillary pressure |
  NullMaterialParams | Reference implementation of params for the linear M-phase material material |
  PLScanningCurve | Represents a scanning curve in the Parker-Lenhard hysteresis model |
  ParkerLenhard | Implements the Parker-Lenhard twophase p_c-Sw hysteresis model |
  ParkerLenhardParams | Default parameter class for the Parker-Lenhard hysteresis model |
  PiecewiseLinearTwoPhaseMaterial | Implementation of a tabulated, piecewise linear capillary pressure law |
  PiecewiseLinearTwoPhaseMaterialParams | Specification of the material parameters for a two-phase material law which uses a table and piecewise constant interpolation |
  RegularizedBrooksCorey | Implementation of the regularized Brooks-Corey capillary pressure / relative permeability <-> saturation relation |
  RegularizedBrooksCoreyParams | Parameters that are necessary for the regularization of the Brooks-Corey capillary pressure model |
  RegularizedVanGenuchten | Implementation of the regularized van Genuchten's capillary pressure / relative permeability <-> saturation relation |
  RegularizedVanGenuchtenParams | Parameters that are necessary for the regularization of VanGenuchten "material law" |
  SplineTwoPhaseMaterial | Implementation of a tabulated capillary pressure and relperm law which uses spline curves as interpolation functions |
  SplineTwoPhaseMaterialParams | Specification of the material parameters for a two-phase material law which uses a table and spline-based interpolation |
  ThreePhaseParkerVanGenuchten | Implementation of three-phase capillary pressure and relative permeability relations proposed by Parker and van Genuchten |
  ThreePhaseParkerVanGenuchtenParams | Specification of the material params for the three-phase van Genuchten capillary pressure model |
  VanGenuchten | Implementation of the van Genuchten capillary pressure - saturation relation |
  VanGenuchtenParams | Specification of the material parameters for the van Genuchten constitutive relations |
  CompositionalFluidState | Represents all relevant thermodynamic quantities of a multi-phase, multi-component fluid system assuming thermodynamic equilibrium |
  CompositionalFluidState< Scalar, FluidSystem, true > | |
  CompositionalFluidState< Scalar, FluidSystem, false > | |
  FluidStateExplicitCompositionModule | Module for the modular fluid state which stores the phase compositions explicitly in terms of mole fractions |
  FluidStateImmiscibleCompositionModule | Module for the modular fluid state which provides the phase compositions assuming immiscibility |
  FluidStateNullCompositionModule | Module for the modular fluid state which does not store the compositions but throws std::logic_error instead |
  FluidStateExplicitDensityModule | Module for the modular fluid state which stores the densities explicitly |
  FluidStateNullDensityModule | Module for the modular fluid state which does not the densities but throws std::logic_error instead |
  FluidStateExplicitEnthalpyModule | Module for the modular fluid state which stores the enthalpies explicitly |
  FluidStateNullEnthalpyModule | Module for the modular fluid state which does not store the enthalpies but returns 0 instead |
  FluidStateExplicitFugacityModule | Module for the modular fluid state which stores the phase fugacity coefficients explicitly |
  FluidStateImmiscibleFugacityModule | Module for the modular fluid state which stores the phase fugacity coefficients explicitly assuming immiscibility |
  FluidStateNullFugacityModule | Module for the modular fluid state which does not store the fugacities but throws std::logic_error instead |
  FluidStateExplicitPressureModule | Module for the modular fluid state which stores the pressures explicitly |
  FluidStateNullPressureModule | Module for the modular fluid state which does not the pressures but throws std::logic_error instead |
  FluidStateExplicitSaturationModule | Module for the modular fluid state which stores the saturations explicitly |
  FluidStateNullSaturationModule | Module for the modular fluid state which does not the saturations but throws std::logic_error instead |
  FluidStateExplicitTemperatureModule | Module for the modular fluid state which stores the temperatures explicitly |
  FluidStateEquilibriumTemperatureModule | Module for the modular fluid state which stores the temperatures explicitly and assumes thermal equilibrium |
  FluidStateNullTemperatureModule | Module for the modular fluid state which does not the temperatures but throws std::logic_error instead |
  FluidStateExplicitViscosityModule | Module for the modular fluid state which stores the viscosities explicitly |
  FluidStateNullViscosityModule | Module for the modular fluid state which does not the viscosities but throws std::logic_error instead |
  ImmiscibleFluidState | Represents all relevant thermodynamic quantities of a multi-phase, multi-component fluid system assuming thermodynamic equilibrium |
  ImmiscibleFluidState< Scalar, FluidSystem, true > | |
  ImmiscibleFluidState< Scalar, FluidSystem, false > | |
  ModularFluidState | Represents all relevant thermodynamic quantities of a multi-phase, multi-component fluid system assuming thermodynamic equilibrium |
  NonEquilibriumFluidState | Represents all relevant thermodynamic quantities of a multi-phase, multi-component fluid system not assuming thermodynamic equilibrium |
  NonEquilibriumFluidState< Scalar, FluidSystem, true > | |
  NonEquilibriumFluidState< Scalar, FluidSystem, false > | |
  PressureOverlayFluidState | This is a fluid state which allows to set the fluid pressures and takes all other quantities from an other fluid state |
  SaturationOverlayFluidState | This is a fluid state which allows to set the fluid saturations and takes all other quantities from an other fluid state |
  SimpleModularFluidState | Represents all relevant thermodynamic quantities of a multi-phase, multi-component fluid system assuming thermodynamic equilibrium |
  TemperatureOverlayFluidState | This is a fluid state which allows to set the fluid temperatures and takes all other quantities from an other fluid state |
  BaseFluidSystem | The base class for all fluid systems |
   ParameterCache | The type of the fluid system's parameter cache |
  ConstantCompressibilityOilPvt | This class represents the Pressure-Volume-Temperature relations of the oil phase without dissolved gas and constant compressibility/"viscosibility" |
  ConstantCompressibilityWaterPvt | This class represents the Pressure-Volume-Temperature relations of the gas phase without vaporized oil |
  DeadOilPvt | This class represents the Pressure-Volume-Temperature relations of the oil phase without dissolved gas |
  DryGasPvt | This class represents the Pressure-Volume-Temperature relations of the gas phase without vaporized oil |
  GasPvtMultiplexer | This class represents the Pressure-Volume-Temperature relations of the gas phase in the black-oil model |
  GasPvtThermal | This class implements temperature dependence of the PVT properties of gas |
  LiveOilPvt | This class represents the Pressure-Volume-Temperature relations of the oil phas with dissolved gas |
  OilPvtMultiplexer | This class represents the Pressure-Volume-Temperature relations of the oil phase in the black-oil model |
  OilPvtThermal | This class implements temperature dependence of the PVT properties of oil |
  SolventPvt | This class represents the Pressure-Volume-Temperature relations of the "second" gas phase in the of ECL simulations with solvents |
  WaterPvtMultiplexer | This class represents the Pressure-Volume-Temperature relations of the water phase in the black-oil model |
  WaterPvtThermal | This class implements temperature dependence of the PVT properties of water |
  WetGasPvt | This class represents the Pressure-Volume-Temperature relations of the gas phas with vaporized oil |
  GasPhase | Represents the gas phase of a single (pseudo-) component |
  LiquidPhase | Represents the liquid phase of a single (pseudo-) component |
  NullParameterCache | A parameter cache which does nothing |
  ParameterCacheBase | The base class of the parameter caches of fluid systems |
  Spe5ParameterCache | Specifies the parameter cache used by the SPE-5 fluid system |
  DummyHeatConductionLaw | Implements a dummy law for heat conduction to which isothermal models can fall back to |
  FluidHeatConduction | Implements a heat conduction law which just takes the conductivity of a given fluid phase |
  FluidHeatConductionParams | Parameters for the heat conduction law which just takes the conductivity of a given fluid phase |
  Somerton | Implements the Somerton law of heat conductivity in a porous medium |
  SomertonParams | The default implementation of a parameter object for the Somerton heatconduction law |
  IdealGas | Relations valid for an ideal gas |
 HairSplittingFluidState | This is a fluid state which makes sure that only the quantities allowed are accessed |