#include <PvtLiveGas.hpp>

Inheritance diagram for Opm::PvtLiveGas:

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

Public Member Functions
	PvtLiveGas (const std::vector< Opm::PvtgTable > &pvtgTables)

virtual	~PvtLiveGas ()

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

virtual void	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

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

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

virtual void	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_dbdr) const

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

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

virtual void	dRdp (const int n, const int pvtRegionIdx, const double p, const double z, 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 Member Functions
int	getTableIndex_ (const int *pvtTableIdx, int cellIdx) const

double	evalB (double press, const double *surfvol, int pvtTableIdx) const

void	evalBDeriv (double press, const double *surfvol, int pvtTableIdx, double &B, double &dBdp) const

double	evalR (double press, const double *surfvol, int pvtTableIdx) const

void	evalRDeriv (double press, const double *surfvol, int pvtTableIdx, double &R, double &dRdp) const

double	miscible_gas (const double press, const double *surfvol, const int pvtTableIdx, const int item, const bool deriv=false) const

double	miscible_gas (const double press, const double r, const PhasePresence &cond, const int pvtTableIdx, const int item, const int deriv=0) const

Protected Attributes
std::vector< std::vector < std::vector< double > > >	saturated_gas_table_

std::vector< std::vector < std::vector< std::vector < double > > > >	undersat_gas_tables_

int	num_phases_

int	phase_pos_ [MaxNumPhases]

Detailed Description

Class for miscible wet gas (with vaporized oil in vapour phase). 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: 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.

Member Enumeration Documentation

enum Opm::BlackoilPhases::PhaseIndex

inherited

Enumerator
Aqua
Liquid
Vapour

Constructor & Destructor Documentation

Opm::PvtLiveGas::PvtLiveGas ( const std::vector< Opm::PvtgTable > & pvtgTables )

virtual Opm::PvtLiveGas::~PvtLiveGas ( )

virtual

Member Function Documentation

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

virtual

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

Implements Opm::PvtInterface.

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

virtual

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

Implements Opm::PvtInterface.

virtual void Opm::PvtLiveGas::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_dbdr
	)		const

virtual

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

Implements Opm::PvtInterface.

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

virtual

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

Implements Opm::PvtInterface.

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

virtual

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

Implements Opm::PvtInterface.

double Opm::PvtLiveGas::evalB	(	double	press,
		const double *	surfvol,
		int	pvtTableIdx
	)		const

protected

void Opm::PvtLiveGas::evalBDeriv	(	double	press,
		const double *	surfvol,
		int	pvtTableIdx,
		double &	B,
		double &	dBdp
	)		const

protected

double Opm::PvtLiveGas::evalR	(	double	press,
		const double *	surfvol,
		int	pvtTableIdx
	)		const

protected

void Opm::PvtLiveGas::evalRDeriv	(	double	press,
		const double *	surfvol,
		int	pvtTableIdx,
		double &	R,
		double &	dRdp
	)		const

protected

int Opm::PvtLiveGas::getTableIndex_	(	const int *	pvtTableIdx,
		int	cellIdx
	)		const

inlineprotected

double Opm::PvtLiveGas::miscible_gas	(	const double	press,
		const double *	surfvol,
		const int	pvtTableIdx,
		const int	item,
		const bool	deriv = `false`
	)		const

protected

double Opm::PvtLiveGas::miscible_gas	(	const double	press,
		const double	r,
		const PhasePresence &	cond,
		const int	pvtTableIdx,
		const int	item,
		const int	deriv = `0`
	)		const

protected

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

virtual

Viscosity as a function of p, T and z.

Implements Opm::PvtInterface.

virtual void Opm::PvtLiveGas::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

virtual

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

Implements Opm::PvtInterface.

virtual void Opm::PvtLiveGas::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

virtual

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

Implements Opm::PvtInterface.

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

virtual

Solution factor as a function of p and z.

Implements Opm::PvtInterface.

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

virtual

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

Implements Opm::PvtInterface.

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

virtual

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

std::vector< std::vector<std::vector<double> > > Opm::PvtLiveGas::saturated_gas_table_

protected

std::vector< std::vector<std::vector<std::vector<double> > > > Opm::PvtLiveGas::undersat_gas_tables_

protected

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

PvtLiveGas.hpp

Public Types

Public Member Functions

Static Public Attributes

Protected Member Functions

Protected Attributes

Detailed Description

Member Enumeration Documentation

Constructor & Destructor Documentation

Member Function Documentation

Member Data Documentation