Cantera
2.2.1
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Pure species representation of carbon dioxide. More...
#include <CarbonDioxide.h>
Public Member Functions | |
double | MolWt () |
Molecular weight [kg/kmol]. More... | |
double | Tcrit () |
Critical temperature [K]. More... | |
double | Pcrit () |
Critical pressure [Pa]. More... | |
double | Vcrit () |
Critical specific volume [m^3/kg]. More... | |
double | Tmin () |
Minimum temperature for which the equation of state is valid. More... | |
double | Tmax () |
Maximum temperature for which the equation of state is valid. More... | |
double | Pp () |
Pressure. Equation P-3 in Reynolds. P(rho, T). More... | |
double | up () |
double | sp () |
entropy. See Reynolds eqn (16) section 2 More... | |
double | Psat () |
Pressure at Saturation. Equation S-2 in Reynolds. More... | |
Public Member Functions inherited from Substance | |
void | setStdState (double h0=0.0, double s0=0.0, double t0=298.15, double p0=1.01325e5) |
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... | |
const char * | name () |
Name of the substance. More... | |
const char * | formula () |
Chemical formula for the substance. More... | |
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 () |
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... | |
Private Member Functions | |
double | ldens () |
Liquid density. Equation D2 in Reynolds. More... | |
double | C (int jm, double, double, double, double) |
double | Cprime (int i, double, double, double) |
Derivative of C(i) More... | |
double | I (int i, double, double) |
double | H (int i, double egrho) |
Additional Inherited Members | |
Protected Member Functions inherited from Substance | |
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 inherited from Substance | |
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 |
Pure species representation of carbon dioxide.
Values and functions are from "Thermodynamic Properties in SI" by W.C. Reynolds
Definition at line 12 of file CarbonDioxide.h.
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Critical specific volume [m^3/kg].
Implements Substance.
Definition at line 298 of file CarbonDioxide.cpp.
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Minimum temperature for which the equation of state is valid.
Implements Substance.
Definition at line 302 of file CarbonDioxide.cpp.
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Maximum temperature for which the equation of state is valid.
Implements Substance.
Definition at line 306 of file CarbonDioxide.cpp.
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Pressure. Equation P-3 in Reynolds. P(rho, T).
Implements Substance.
Definition at line 239 of file CarbonDioxide.cpp.
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internal energy. See Reynolds eqn (15) section 2
u = (the integral from T to To of co(T)dT) + sum from i to N ([C(i) - T*Cprime(i)] + uo
Implements Substance.
Definition at line 187 of file CarbonDioxide.cpp.
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entropy. See Reynolds eqn (16) section 2
Implements Substance.
Definition at line 213 of file CarbonDioxide.cpp.
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Pressure at Saturation. Equation S-2 in Reynolds.
Implements Substance.
Definition at line 256 of file CarbonDioxide.cpp.
References Cantera::fp2str().
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Liquid density. Equation D2 in Reynolds.
Implements Substance.
Definition at line 273 of file CarbonDioxide.cpp.
References Cantera::fp2str().
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C returns a multiplier in each term of the sum in P-3, used in conjunction with C in the function Pp
Definition at line 87 of file CarbonDioxide.cpp.
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Derivative of C(i)
Definition at line 119 of file CarbonDioxide.cpp.
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I = integral from o-rho { 1/(rho^2) * H(i, rho) d rho } ( see section 2 of Reynolds TPSI )
Definition at line 151 of file CarbonDioxide.cpp.
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H returns a multiplier in each term of the sum in P-3. This is used in conjunction with C in the function Pp this represents the product rho^n
Definition at line 174 of file CarbonDioxide.cpp.