Cantera
2.3.0
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#include <Sub.h>
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... | |
const char * | name () |
Name of the substance. More... | |
const char * | formula () |
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 Attributes | |
int | kbr |
double | Vmin |
double | Vmax |
double | Pmin |
double | Pmax |
double | dvbf |
double | dv |
double | v_here |
double | P_here |
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pure virtual |
Molecular weight [kg/kmol].
Implemented in RedlichKwong, leekesler, HFC134a, CarbonDioxide, hydrogen, methane, nitrogen, Heptane, oxygen, and water.
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pure virtual |
Critical temperature [K].
Implemented in RedlichKwong, leekesler, HFC134a, CarbonDioxide, hydrogen, methane, nitrogen, Heptane, oxygen, and water.
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pure virtual |
Critical pressure [Pa].
Implemented in RedlichKwong, leekesler, HFC134a, CarbonDioxide, hydrogen, methane, nitrogen, Heptane, oxygen, and water.
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pure virtual |
Critical specific volume [m^3/kg].
Implemented in RedlichKwong, leekesler, HFC134a, CarbonDioxide, hydrogen, methane, nitrogen, Heptane, oxygen, and water.
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pure virtual |
Minimum temperature for which the equation of state is valid.
Implemented in RedlichKwong, leekesler, HFC134a, CarbonDioxide, hydrogen, methane, nitrogen, Heptane, oxygen, and water.
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pure virtual |
Maximum temperature for which the equation of state is valid.
Implemented in RedlichKwong, leekesler, HFC134a, CarbonDioxide, hydrogen, methane, nitrogen, Heptane, oxygen, and water.
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inline |
double P | ( | ) |
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inline |
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inline |
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inline |
Entropy [J/kg/K].
Definition at line 109 of file Sub.h.
Referenced by Substance::f(), and Substance::g().
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inline |
Helmholtz function [J/kg].
Definition at line 114 of file Sub.h.
References Substance::s(), and Substance::u().
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inline |
Gibbs function [J/kg].
Definition at line 119 of file Sub.h.
References Substance::h(), and Substance::s().
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virtual |
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virtual |
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virtual |
double Tsat | ( | double | p | ) |
double x | ( | ) |
int TwoPhase | ( | ) |
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inline |
Enthaply of a single-phase state.
Definition at line 156 of file Sub.h.
References Substance::up().
Referenced by Substance::gp().
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inline |
Gibbs function of a single-phase state.
Definition at line 161 of file Sub.h.
References Substance::hp(), and Substance::sp().
void Set | ( | PropertyPair::type | XY, |
double | x0, | ||
double | y0 | ||
) |
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protectedpure virtual |
Saturation pressure, Pa.
Implemented in RedlichKwong, CarbonDioxide, Heptane, HFC134a, leekesler, hydrogen, methane, nitrogen, oxygen, and water.
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protectedpure virtual |
Internal energy of a single-phase state.
Implemented in RedlichKwong, CarbonDioxide, Heptane, leekesler, HFC134a, hydrogen, methane, nitrogen, oxygen, and water.
Referenced by Substance::hp().
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protectedpure virtual |
Entropy of a single-phase state.
Implemented in RedlichKwong, CarbonDioxide, Heptane, leekesler, HFC134a, hydrogen, methane, nitrogen, oxygen, and water.
Referenced by Substance::gp().
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protected |
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protected |