#include <PvtConstCompr.hpp>

Inheritance diagram for Opm::PvtConstCompr:

Public Types
enum	PhaseIndex { Aqua = 0, Liquid = 1, Vapour = 2 }

Public Member Functions
	PvtConstCompr ()

void	initFromWater (Opm::DeckKeywordConstPtr pvtwKeyword)

void	initFromOil (Opm::DeckKeywordConstPtr pvcdoKeyword)

	PvtConstCompr (double visc)
	Create a PVT object with a given viscosity that assumes all fluid phases to be incompressible. More...

virtual	~PvtConstCompr ()

virtual void	mu (const int n, const int pvtRegionIdx, const double p, const double , const double , double *output_mu) const
	Viscosity as a function of p, T and z. More...

virtual void	mu (const int n, const int pvtRegionIdx, const double p, const double , const double , double output_mu, double output_dmudp, double *output_dmudr) const

virtual void	mu (const int n, const int pvtRegionIdx, const double p, const double , const double , const PhasePresence , double output_mu, double output_dmudp, double output_dmudr) const

virtual void	B (const int n, const int pvtRegionIdx, const double p, const double , const double , double *output_B) const
	Formation volume factor as a function of p, T and z. More...

virtual void	dBdp (const int n, const int pvtRegionIdx, const double p, const double , const double , double output_B, double output_dBdp) const
	Formation volume factor and p-derivative as functions of p and z. More...

virtual void	b (const int n, const int pvtRegionIdx, const double p, const double , const double , double output_b, double output_dbdp, double *output_dbdr) const

virtual void	b (const int n, const int pvtRegionIdx, const double p, const double , const double , const PhasePresence , double output_b, double output_dbdp, double output_dbdr) const

virtual void	rsSat (const int n, const int , const double , double output_rsSat, double output_drsSatdp) const
	Solution gas/oil ratio and its derivatives at saturated conditions as a function of p. More...

virtual void	rvSat (const int n, const int , const double , double output_rvSat, double output_drvSatdp) const
	Vapor oil/gas ratio and its derivatives at saturated conditions as a function of p. More...

virtual void	R (const int n, const int , const double , const double , double output_R) const
	Solution factor as a function of p and z. More...

virtual void	dRdp (const int n, const int , const double , const double , double output_R, double *output_dRdp) const
	Solution factor and p-derivative as functions of p and z. More...

void	setPhaseConfiguration (const int num_phases, const int *phase_pos)

Static Public Attributes
static const int	MaxNumPhases = 3

Protected Attributes
int	num_phases_

int	phase_pos_ [MaxNumPhases]

Detailed Description

Class for constant compressible phases (PVTW or PVCDO). The PVT properties can either be given as a function of pressure (p) and surface volume (z) or pressure (p) and gas resolution factor (r). Also, since this class supports multiple PVT regions, the concrete table to be used for each data point needs to be specified via the pvtTableIdx argument of the respective method. For all the virtual methods, the following apply: pvtTableIdx, p, r and z are expected to be of size n, size n, size n and n*num_phases, respectively. Output arrays shall be of size n, and must be valid before calling the method.

Member Enumeration Documentation

enum Opm::BlackoilPhases::PhaseIndex

inherited

Enumerator
Aqua
Liquid
Vapour

Constructor & Destructor Documentation

Opm::PvtConstCompr::PvtConstCompr ( )

inline

Opm::PvtConstCompr::PvtConstCompr ( double visc )

inlineexplicit

Create a PVT object with a given viscosity that assumes all fluid phases to be incompressible.

virtual Opm::PvtConstCompr::~PvtConstCompr ( )

inlinevirtual

Member Function Documentation

virtual void Opm::PvtConstCompr::B	(	const int	n,
		const int *	pvtRegionIdx,
		const double *	p,
		const double *	T,
		const double *	z,
		double *	output_B
	)		const

inlinevirtual

Formation volume factor as a function of p, T and z.

Implements Opm::PvtInterface.

virtual void Opm::PvtConstCompr::b	(	const int	n,
		const int *	pvtRegionIdx,
		const double *	p,
		const double *	T,
		const double *	r,
		double *	output_b,
		double *	output_dbdp,
		double *	output_dpdr
	)		const

inlinevirtual

The inverse of the volume factor b = 1 / B as a function of p, T and r. The fluid is considered saturated if r >= rsSat(p).

Implements Opm::PvtInterface.

virtual void Opm::PvtConstCompr::b	(	const int	n,
		const int *	pvtRegionIdx,
		const double *	p,
		const double *	T,
		const double *	r,
		const PhasePresence *	cond,
		double *	output_b,
		double *	output_dbdp,
		double *	output_dpdr
	)		const

inlinevirtual

The inverse of the volume factor b = 1 / B as a function of p, T and r. State condition determined by 'cond'.

Implements Opm::PvtInterface.

virtual void Opm::PvtConstCompr::dBdp	(	const int	n,
		const int *	pvtRegionIdx,
		const double *	p,
		const double *	T,
		const double *	z,
		double *	output_B,
		double *	output_dBdp
	)		const

inlinevirtual

Formation volume factor and p-derivative as functions of p and z.

Implements Opm::PvtInterface.

virtual void Opm::PvtConstCompr::dRdp	(	const int	n,
		const int *	pvtRegionIdx,
		const double *	p,
		const double *	z,
		double *	output_R,
		double *	output_dRdp
	)		const

inlinevirtual

Solution factor and p-derivative as functions of p and z.

Implements Opm::PvtInterface.

void Opm::PvtConstCompr::initFromOil ( Opm::DeckKeywordConstPtr pvcdoKeyword )

inline

void Opm::PvtConstCompr::initFromWater ( Opm::DeckKeywordConstPtr pvtwKeyword )

inline

virtual void Opm::PvtConstCompr::mu	(	const int	n,
		const int *	pvtRegionIdx,
		const double *	p,
		const double *	T,
		const double *	z,
		double *	output_mu
	)		const

inlinevirtual

Viscosity as a function of p, T and z.

The PVT properties can either be given as a function of pressure (p), temperature (T) and surface volume (z) or pressure (p), temperature (T) and gas resolution factor (r). For all the virtual methods, the following apply:

pvtRegionIdx is an array of size n and represents the index of the PVT table which should be used to calculate the output. NULL can also be passed and is interpreted such that the first table should be used for the output
p, r and z are expected to be of size n, size n and n*num_phases, respectively.
Output arrays shall be of size n, and must be valid before calling the method.

Implements Opm::PvtInterface.

virtual void Opm::PvtConstCompr::mu	(	const int	n,
		const int *	pvtRegionIdx,
		const double *	p,
		const double *	T,
		const double *	r,
		double *	output_mu,
		double *	output_dmudp,
		double *	output_dmudr
	)		const

inlinevirtual

Viscosity as a function of p, T and r. The fluid is considered saturated if r >= rsSat(p).

Implements Opm::PvtInterface.

virtual void Opm::PvtConstCompr::mu	(	const int	n,
		const int *	pvtRegionIdx,
		const double *	p,
		const double *	T,
		const double *	r,
		const PhasePresence *	cond,
		double *	output_mu,
		double *	output_dmudp,
		double *	output_dmudr
	)		const

inlinevirtual

Viscosity as a function of p, T and r. State condition determined by 'cond'.

Implements Opm::PvtInterface.

virtual void Opm::PvtConstCompr::R	(	const int	n,
		const int *	pvtRegionIdx,
		const double *	p,
		const double *	z,
		double *	output_R
	)		const

inlinevirtual

Solution factor as a function of p and z.

Implements Opm::PvtInterface.

virtual void Opm::PvtConstCompr::rsSat	(	const int	n,
		const int *	pvtRegionIdx,
		const double *	p,
		double *	output_rsSat,
		double *	output_drsSatdp
	)		const

inlinevirtual

Solution gas/oil ratio and its derivatives at saturated conditions as a function of p.

Implements Opm::PvtInterface.

virtual void Opm::PvtConstCompr::rvSat	(	const int	n,
		const int *	pvtRegionIdx,
		const double *	p,
		double *	output_rvSat,
		double *	output_drvSatdp
	)		const

inlinevirtual

Vapor oil/gas ratio and its derivatives at saturated conditions as a function of p.

Implements Opm::PvtInterface.

void Opm::PvtInterface::setPhaseConfiguration	(	const int	num_phases,
		const int *	phase_pos
	)

inherited

Parameters

[in]	num_phases	The number of active phases.
[in]	phase_pos	Array of BlackpoilPhases::MaxNumPhases integers, giving the relative positions of the three canonical phases A, L, V in order to handle arbitrary two-phase and three-phase situations.

Member Data Documentation

const int Opm::BlackoilPhases::MaxNumPhases = 3

staticinherited

Referenced by Opm::Equil::isConstPc(), Opm::Equil::PcEq::PcEq(), Opm::Equil::PcEqSum::PcEqSum(), Opm::Equil::phaseSaturations(), Opm::phaseUsageFromDeck(), Opm::Equil::Miscibility::RsSatAtContact::RsSatAtContact(), Opm::Equil::Miscibility::RsVD::RsVD(), Opm::Equil::Miscibility::RvSatAtContact::RvSatAtContact(), Opm::Equil::Miscibility::RvVD::RvVD(), Opm::Equil::satFromDepth(), Opm::Equil::satFromPc(), Opm::Equil::satFromSumOfPcs(), and Opm::ExplicitArraysFluidState::setIndex().

int Opm::PvtInterface::num_phases_

protectedinherited

int Opm::PvtInterface::phase_pos_[MaxNumPhases]

protectedinherited

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

PvtConstCompr.hpp

Public Types

Public Member Functions

Static Public Attributes

Protected Attributes

Detailed Description

Member Enumeration Documentation

Constructor & Destructor Documentation

Member Function Documentation

Member Data Documentation