#include <Sub.h>

Inheritance diagram for Substance:

Public Member Functions
void	setStdState (double h0=0.0, double s0=0.0, double t0=298.15, double p0=1.01325e5)

virtual double	Pp ()=0

double	hp ()
	Enthaply of a single-phase state. More...

double	gp ()
	Gibbs function of a single-phase state. More...

double	prop (propertyFlag::type ijob)

void	set_TPp (double t0, double p0)
	set T and P More...

void	Set (PropertyPair::type XY, double x0, double y0)
	Function to set or change the state for a property pair XY where x0 is the value of first property and y0 is the value of the second property. More...

Information about a substance
virtual double	MolWt ()=0
	Molecular weight [kg/kmol]. More...

virtual double	Tcrit ()=0
	Critical temperature [K]. More...

virtual double	Pcrit ()=0
	Critical pressure [Pa]. More...

virtual double	Vcrit ()=0
	Critical specific volume [m^3/kg]. More...

virtual double	Tmin ()=0
	Minimum temperature for which the equation of state is valid. More...

virtual double	Tmax ()=0
	Maximum temperature for which the equation of state is valid. More...

virtual char *	name ()=0
	Name of the substance. More...

virtual char *	formula ()=0
	Chemical formula for the substance. More...

Properties
double	P ()
	Pressure [Pa]. More...

double	Temp ()
	Temperature [K]. More...

double	v ()
	Specific volume [m^3/kg]. More...

double	u ()
	Internal energy [J/kg]. More...

double	h ()
	Enthalpy [J/kg]. More...

double	s ()
	Entropy [J/kg/K]. More...

double	f ()
	Helmholtz function [J/kg]. More...

double	g ()
	Gibbs function [J/kg]. More...

virtual double	cv ()
	Specific heat at constant volume [J/kg/K]. More...

virtual double	cp ()
	Specific heat at constant pressure [J/kg/K]. More...

virtual double	thermalExpansionCoeff ()

virtual double	isothermalCompressibility ()

Saturation Properties
double	Ps ()

virtual double	dPsdT ()
	The derivative of the saturation pressure with respect to temperature. More...

double	Tsat (double p)
	Saturation temperature at pressure p. More...

double	x ()
	Vapor mass fraction. More...

int	TwoPhase ()
	Returns 1 if the current state is a liquid/vapor mixture, 0 otherwise. More...

Protected Member Functions
virtual double	ldens ()=0

virtual double	Psat ()=0
	Saturation pressure, Pa. More...

virtual double	up ()=0
	Internal energy of a single-phase state. More...

virtual double	sp ()=0
	Entropy of a single-phase state. More...

virtual int	ideal ()

double	vp ()

int	Lever (int itp, double sat, double val, propertyFlag::type ifunc)
	Uses the lever rule to set state in the dome. More...

void	update_sat ()
	Update saturated liquid and vapor densities and saturation pressure. More...

Protected Attributes
double	T

double	Rho

double	Tslast

double	Rhf

double	Rhv

double	Pst

double	m_energy_offset

double	m_entropy_offset

std::string	m_name

std::string	m_formula

Private Member Functions
void	set_Rho (double r0)

void	set_T (double t0)

void	set_v (double v0)

void	BracketSlope (double p)

double	vprop (propertyFlag::type ijob)

void	set_xy (propertyFlag::type if1, propertyFlag::type if2, double X, double Y, double atx, double aty, double rtx, double rty)

Private Attributes
int	kbr

double	Vmin

double	Vmax

double	Pmin

double	Pmax

double	dvbf

double	dv

double	v_here

double	P_here

Detailed Description

Base class from which all pure substances are derived

Definition at line 40 of file Sub.h.

Member Function Documentation

virtual double MolWt ( )

pure virtual

Molecular weight [kg/kmol].

Implemented in HFC134a, CarbonDioxide, hydrogen, methane, nitrogen, Heptane, oxygen, and water.

Referenced by PureFluidPhase::initThermo().

virtual double Tcrit ( )

pure virtual

Critical temperature [K].

Implemented in HFC134a, CarbonDioxide, hydrogen, methane, nitrogen, Heptane, oxygen, and water.

Referenced by PureFluidPhase::critTemperature().

virtual double Pcrit ( )

pure virtual

Critical pressure [Pa].

Implemented in HFC134a, CarbonDioxide, hydrogen, methane, nitrogen, Heptane, oxygen, and water.

Referenced by PureFluidPhase::critPressure(), and PureFluidPhase::initThermo().

virtual double Vcrit ( )

pure virtual

Critical specific volume [m^3/kg].

Implemented in HFC134a, CarbonDioxide, hydrogen, methane, nitrogen, Heptane, oxygen, and water.

Referenced by PureFluidPhase::critDensity().

virtual double Tmin ( )

pure virtual

Minimum temperature for which the equation of state is valid.

Implemented in HFC134a, CarbonDioxide, hydrogen, methane, nitrogen, Heptane, oxygen, and water.

Referenced by Substance::cp(), and Substance::cv().

virtual double Tmax ( )

pure virtual

Maximum temperature for which the equation of state is valid.

Implemented in HFC134a, CarbonDioxide, hydrogen, methane, nitrogen, Heptane, oxygen, and water.

Referenced by Substance::cp(), and Substance::cv().

virtual char* name ( )

pure virtual

Name of the substance.

Implemented in HFC134a, CarbonDioxide, hydrogen, methane, nitrogen, Heptane, oxygen, and water.

virtual char* formula ( )

pure virtual

Chemical formula for the substance.

Implemented in HFC134a, CarbonDioxide, hydrogen, methane, nitrogen, Heptane, oxygen, and water.

double P ( )

Pressure [Pa].

If two phases are present, return the saturation pressure; otherwise return the pressure computed directly from the underlying eos.

Definition at line 28 of file Sub.cpp.

Referenced by Substance::cp(), PureFluidPhase::initThermo(), and PureFluidPhase::pressure().

double Temp ( )

inline

Temperature [K].

Definition at line 95 of file Sub.h.

Referenced by PureFluidPhase::setState_HP(), PureFluidPhase::setState_Psat(), PureFluidPhase::setState_SP(), PureFluidPhase::setState_SV(), and PureFluidPhase::setState_UV().

double v ( )

inline

Specific volume [m^3/kg].

Definition at line 100 of file Sub.h.

Referenced by PureFluidPhase::satPressure(), PureFluidPhase::setPressure(), PureFluidPhase::setState_HP(), PureFluidPhase::setState_Psat(), PureFluidPhase::setState_SP(), PureFluidPhase::setState_SV(), PureFluidPhase::setState_Tsat(), and PureFluidPhase::setState_UV().

double u ( )

inline

Internal energy [J/kg].

Definition at line 105 of file Sub.h.

Referenced by Substance::f(), and PureFluidPhase::intEnergy_mole().

double h ( )

inline

Enthalpy [J/kg].

Definition at line 110 of file Sub.h.

Referenced by PureFluidPhase::enthalpy_mole(), and Substance::g().

double s ( )

inline

Entropy [J/kg/K].

Definition at line 115 of file Sub.h.

Referenced by Substance::cp(), Substance::cv(), PureFluidPhase::entropy_mole(), Substance::f(), and Substance::g().

double f ( )

inline

Helmholtz function [J/kg].

Definition at line 120 of file Sub.h.

References Substance::s(), and Substance::u().

double g ( )

inline

Gibbs function [J/kg].

Definition at line 125 of file Sub.h.

References Substance::h(), and Substance::s().

Referenced by PureFluidPhase::gibbs_mole().

virtual double cv ( )

inlinevirtual

Specific heat at constant volume [J/kg/K].

Definition at line 130 of file Sub.h.

References Substance::s(), Substance::Tmax(), and Substance::Tmin().

Referenced by PureFluidPhase::cv_mole().

virtual double cp ( )

inlinevirtual

Specific heat at constant pressure [J/kg/K].

Definition at line 143 of file Sub.h.

References Substance::P(), Substance::s(), Substance::Set(), Substance::Tmax(), and Substance::Tmin().

Referenced by PureFluidPhase::cp_mole().

double dPsdT ( )

virtual

The derivative of the saturation pressure with respect to temperature.

Definition at line 35 of file Sub.cpp.

double Tsat ( double p )

Saturation temperature at pressure p.

Definition at line 72 of file Sub.cpp.

Referenced by PureFluidPhase::satTemperature().

double x ( )

Vapor mass fraction.

If T >= Tcrit, 0 is returned for v < Vcrit, and 1 is returned if v > Vcrit.

Definition at line 54 of file Sub.cpp.

Referenced by PureFluidPhase::vaporFraction().

int TwoPhase ( )

Returns 1 if the current state is a liquid/vapor mixture, 0 otherwise.

Definition at line 45 of file Sub.cpp.

double hp ( )

inline

Enthaply of a single-phase state.

Definition at line 202 of file Sub.h.

References Substance::up().

Referenced by Substance::gp().

double gp ( )

inline

Gibbs function of a single-phase state.

Definition at line 207 of file Sub.h.

References Substance::hp(), and Substance::sp().

void set_TPp	(	double	t0,
		double	p0
	)

set T and P

Definition at line 567 of file Sub.cpp.

References Cantera::fp2str().

void Set	(	PropertyPair::type	XY,
		double	x0,
		double	y0
	)

Function to set or change the state for a property pair XY where x0 is the value of first property and y0 is the value of the second property.

Definition at line 122 of file Sub.cpp.

References Cantera::fp2str().

Referenced by Substance::cp(), PureFluidPhase::initThermo(), and PureFluidPhase::Set().

virtual double Psat ( )

protectedpure virtual

Saturation pressure, Pa.

Implemented in CarbonDioxide, Heptane, HFC134a, hydrogen, methane, nitrogen, oxygen, and water.

virtual double up ( )

protectedpure virtual

Internal energy of a single-phase state.

Implemented in CarbonDioxide, Heptane, HFC134a, hydrogen, methane, nitrogen, oxygen, and water.

Referenced by Substance::hp().

virtual double sp ( )

protectedpure virtual

Entropy of a single-phase state.

Implemented in CarbonDioxide, Heptane, HFC134a, hydrogen, methane, nitrogen, oxygen, and water.

Referenced by Substance::gp().

int Lever	(	int	itp,
		double	sat,
		double	val,
		propertyFlag::type	ifunc
	)

protected

Uses the lever rule to set state in the dome.

Returns 1 if in dome, 0 if not, in which case state not set.

Definition at line 382 of file Sub.cpp.

void update_sat ( )

protected

Update saturated liquid and vapor densities and saturation pressure.

Definition at line 292 of file Sub.cpp.

References Cantera::fp2str().

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

Public Member Functions

Protected Member Functions

Protected Attributes

Private Member Functions

Private Attributes

Detailed Description

Member Function Documentation