Contents - Index
All built-in thermophysical property functions are listed below in alphabetical order. Not all of these functions are applicable to all substances.
ACENTRICFACTOR COMPRESSIBILITYFACTOR CONDUCTIVITY
CP CV DEBYE_T
DENSITY DEWPOINT DIPOLE
ELECTRICAL_RESISTIVITY EK_LJ EMISSIVITY
ENTHALPY ENTHALPY_FORMATION ENTHALPY_FUSION
ENTHALPY_VAPORIZATION ENTROPY FLUIDTYPE$
FREEZINGPT FUGACITY HENRYCONSTANT_WATER
HIGHERHEATINGVALUE HUMRAT INTENERGY
INTK ISENTROPICEXPONENT ISIDEALGAS
ISOTHERMALCOMPRESS KINEMATICVISCOSITY LINEAREXPCOEF
LOWERHEATINGVALUE MASSFRACTION MOLARMASS
MOLARMASS_SOLN NORMALBOILINGPT PHASE$
PRANDTL PRESSURE P_CRIT
POISSONSRATIO P_SAT QUALITY
RELHUM SIGMA_LJ SOUNDSPEED
SPECHEAT SURFACETENSION TEMPERATURE
T_CRIT THERMALDIFFUSVITY TOTALTHERMALEXP
T_SAT T_TRIPLE ULTIMATESTRESS
VISCOSITY VOLUME V_CRIT
VOLEXPCOEF WETBULB YIELDSTRESS
The first argument of all built-in thermophysical property functions is the name of the substance. This argument is a string that may be provided as a string constant (enclosing quote marks are optional) or a string variable that contains the name of the fluid. The fluid may be any of the built-in fluids provided with EES, any of ideal gas fluids provided with the NASA ideal gas data base, or any of the fluids in the Brine fluids or Incompressible substances libraries. EES also allows User-Supplied Property Data.
Arguments are separated with the list separator character, which is a comma for the U.S. numerical format and a semicolon for the European numerical format.
It may appear that some substances in the built-in property data base, e.g., N2 and Nitrogen, CO2 and CarbonDioxide, H2O and Steam (or Water), are duplicated, but this is not true. Whenever a chemical symbol notation (e.g., N2, CO2, CH4) is used, the substance is modeled as an ideal gas and the enthalpy and entropy values are based on JANAF table references. The JANAF table reference for enthalpy is based on the elements having a specific molar enthalpy value of 0 at 298 K (537 R). The entropy of these substances is based on the Third Law of Thermodynamics. Whenever the substance name is spelled out (e.g., Steam (or Water), Nitrogen, R12, CarbonDioxide, Methane, etc.) the substance is modeled as a real fluid with subcooled, saturated, and superheated phases. Exceptions to this rule occur for Air and AirH2O, both of which are modeled as ideal gases. AirH2O is the notation for air-water vapor mixtures, i.e., psychometrics. Additional information concerning the methods, reference states, and ranges of applicability for the thermophysical properties are provided in the manual.
All arguments in thermophysical property functions, aside from the substance name, are identified by a single case-insensitive letter followed by an equal sign. Arguments must be separated with commas and may be in any order, provided that the substance name is first. The value or algebraic expression representing the value of the argument follows the equal sign. The letters that are recognized in function arguments and their meaning are:
B= wet-bulb temperature (only for substance AIRH2O)
C=mass concentration in % (only for Brines)
D=dew-point temperature (only for substance AIRH2O)
Q=quality (only for NH3H2O. Use X for quality for real fluids)
R=relative humidity (only for substance AIRH2O)
U=specific internal energy
V=specific volume (=1/density)
W=humidity ratio (only for substance AIRH2O)
X=quality (for real fluids, mass fraction for NH3H2O, otherwise not applicable)
Many of the thermodynamic functions can take alternate sets of arguments. For example, the ENTHALPY function for steam can be accessed with temperature and pressure as arguments; alternatively, the same function could be accessed with entropy and quality as arguments. In general, any valid set of arguments can be supplied for thermodynamic functions.
EES does not require the function argument to have a known value. For example:
h1 = ENTHALPY(Steam,T=T1,P=P1)
will return the value of h1 corresponding to known temperature and pressure, T1 and P1. If, however, the value of h1 is known, but T1 is unknown, the same equation will return the appropriate value of the temperature. Alternatively, the temperature could be found by:
T1 = TEMPERATURE(Steam,h=h1,P=P1)
The latter method is preferable in that the iterative calculations implemented for steam are less likely to have convergence difficulty.
EES built-in fluid data base
NASA Ideal gas data base