Equation of state for HFC-134a.  
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#include <HFC134a.h>
Equation of state for HFC-134a. 
Implements the equation of state given in Tillner-Roth and Baehr [47]. 
Definition at line 17 of file HFC134a.h.
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| double  | MolWt () override | 
|   | Molecular weight [kg/kmol].  
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| double  | Tcrit () override | 
|   | Critical temperature [K].  
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| double  | Pcrit () override | 
|   | Critical pressure [Pa].  
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| double  | Vcrit () override | 
|   | Critical specific volume [m^3/kg].  
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| double  | Tmin () override | 
|   | Minimum temperature for which the equation of state is valid.  
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| double  | Tmax () override | 
|   | Maximum temperature for which the equation of state is valid.  
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| double  | Pp () override | 
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| double  | fp () | 
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| double  | up () override | 
|   | Internal energy of a single-phase state.  
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| double  | sp () override | 
|   | Entropy of a single-phase state.  
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| double  | Psat () override | 
|   | Saturation pressure, Pa.  
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| void  | setStdState (double h0=0.0, double s0=0.0, double t0=298.15, double p0=1.01325e5) | 
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| virtual double  | Pp ()=0 | 
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| double  | hp () | 
|   | Enthalpy of a single-phase state.  
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| double  | gp () | 
|   | Gibbs function of a single-phase state.  
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| double  | prop (propertyFlag::type ijob) | 
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| void  | set_TPp (double t0, double p0) | 
|   | set T and P  
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| 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.  
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| const char *  | name () | 
|   | Name of the substance.  
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| const char *  | formula () | 
|   | Chemical formula for the substance.  
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| double  | P () | 
|   | Pressure [Pa].  
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| double  | Temp () | 
|   | Temperature [K].  
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| double  | v () | 
|   | Specific volume [m^3/kg].  
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| double  | u () | 
|   | Internal energy [J/kg].  
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| double  | h () | 
|   | Enthalpy [J/kg].  
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| double  | s () | 
|   | Entropy [J/kg/K].  
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| double  | f () | 
|   | Helmholtz function [J/kg].  
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| double  | g () | 
|   | Gibbs function [J/kg].  
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| virtual double  | cv () | 
|   | Specific heat at constant volume [J/kg/K].  
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| virtual double  | cp () | 
|   | Specific heat at constant pressure [J/kg/K].  
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| virtual double  | thermalExpansionCoeff () | 
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| virtual double  | isothermalCompressibility () | 
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| double  | Ps () | 
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| virtual double  | dPsdT () | 
|   | The derivative of the saturation pressure with respect to temperature.  
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| double  | Tsat (double p) | 
|   | Saturation temperature at pressure p.  
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| double  | x () | 
|   | Vapor mass fraction.  
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| int  | TwoPhase (bool strict=false) | 
|   | Returns 1 if the current state is a liquid/vapor mixture, 0 otherwise.  
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| double  | ldens () override | 
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| virtual double  | ldens ()=0 | 
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| virtual double  | Psat ()=0 | 
|   | Saturation pressure, Pa.  
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| virtual double  | up ()=0 | 
|   | Internal energy of a single-phase state.  
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| virtual double  | sp ()=0 | 
|   | Entropy of a single-phase state.  
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| virtual int  | ideal () | 
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| double  | vp () | 
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| int  | Lever (int itp, double sat, double val, propertyFlag::type ifunc) | 
|   | Uses the lever rule to set state in the dome.  
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| void  | update_sat () | 
|   | Update saturated liquid and vapor densities and saturation pressure.  
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◆ HFC134a()
◆ MolWt()
◆ Tcrit()
◆ Pcrit()
◆ Vcrit()
◆ Tmin()
Minimum temperature for which the equation of state is valid. 
Implements Substance.
Definition at line 193 of file HFC134a.cpp.
 
 
◆ Tmax()
Maximum temperature for which the equation of state is valid. 
Implements Substance.
Definition at line 197 of file HFC134a.cpp.
 
 
◆ Pp()
◆ fp()
◆ up()
◆ sp()
◆ Psat()
◆ ldens()
The documentation for this class was generated from the following files: