1,2-Propylene glycol, 47% mixture with water
Extends from TableBased (Incompressible medium properties based on tables).
Name | Description |
---|---|
Inherited | |
enthalpyOfT=true | True if enthalpy is approximated as a function of T only, (p-dependence neglected) |
densityOfT=size(tableDensity, 1) > 1 | True if density is a function of temperature |
T_min=Cv.from_degC(-30) | Minimum temperature valid for medium model |
T_max=Cv.from_degC(100) | Maximum temperature valid for medium model |
T0=273.15 | Reference Temperature |
h0=0 | Reference enthalpy at T0, reference_p |
s0=0 | Reference entropy at T0, reference_p |
MM_const=0.1 | Molar mass |
npol=2 | Degree of polynomial used for fitting |
npolDensity=npol | Degree of polynomial used for fitting rho(T) |
npolHeatCapacity=npol | Degree of polynomial used for fitting Cp(T) |
npolViscosity=npol | Degree of polynomial used for fitting eta(T) |
npolVaporPressure=npol | Degree of polynomial used for fitting pVap(T) |
npolConductivity=npol | Degree of polynomial used for fitting lambda(T) |
neta=size(tableViscosity, 1) | Number of data points for viscosity |
tableDensity=[-30, 1066; -20, 1062; -10, 1058; 0, 1054; 20, 1044; 40, 1030; 60, 1015; 80, 999; 100, 984] | Table for rho(T) |
tableHeatCapacity=[-30, 3450; -20, 3490; -10, 3520; 0, 3560; 20, 3620; 40, 3690; 60, 3760; 80, 3820; 100, 3890] | Table for Cp(T) |
tableViscosity=[-30, 0.160; -20, 0.0743; -10, 0.0317; 0, 0.0190; 20, 0.00626; 40, 0.00299; 60, 0.00162; 80, 0.00110; 100, 0.00081] | Table for eta(T) |
tableVaporPressure=[0, 500; 20, 1.9e3; 40, 5.3e3; 60, 16e3; 80, 37e3; 100, 80e3] | Table for pVap(T) |
tableConductivity=[-30, 0.397; -20, 0.396; -10, 0.395; 0, 0.395; 20, 0.394; 40, 0.393; 60, 0.392; 80, 0.391; 100, 0.390] | Table for lambda(T) |
TinK=false | True if T[K],Kelvin used for table temperatures |
hasDensity=not (size(tableDensity, 1) == 0) | True if table tableDensity is present |
hasHeatCapacity=not (size(tableHeatCapacity, 1) == 0) | True if table tableHeatCapacity is present |
hasViscosity=not (size(tableViscosity, 1) == 0) | True if table tableViscosity is present |
hasVaporPressure=not (size(tableVaporPressure, 1) == 0) | True if table tableVaporPressure is present |
invTK=if size(tableViscosity, 1) > 0 then (if TinK then 1 ./ tableViscosity[:, 1] else 1 ./ Cv.from_degC(tableViscosity[:, 1])) else fill(0, neta) | |
poly_rho=if hasDensity then Polynomials.fitting(tableDensity[:, 1], tableDensity[:, 2], npolDensity) else zeros(npolDensity + 1) | |
poly_Cp=if hasHeatCapacity then Polynomials.fitting(tableHeatCapacity[:, 1], tableHeatCapacity[:, 2], npolHeatCapacity) else zeros(npolHeatCapacity + 1) | |
poly_eta=if hasViscosity then Polynomials.fitting(invTK, Math.log(tableViscosity[:, 2]), npolViscosity) else zeros(npolViscosity + 1) | |
poly_pVap=if hasVaporPressure then Polynomials.fitting(tableVaporPressure[:, 1], tableVaporPressure[:, 2], npolVaporPressure) else zeros(npolVaporPressure + 1) | |
poly_lam=if size(tableConductivity, 1) > 0 then Polynomials.fitting(tableConductivity[:, 1], tableConductivity[:, 2], npolConductivity) else zeros(npolConductivity + 1) | |
invertTemp | Function to invert temperatures |
BaseProperties | Base properties of T dependent medium |
setState_pTX | Returns state record, given pressure and temperature |
setState_dTX | Returns state record, given pressure and temperature |
setState_pT | Returns state record as function of p and T |
setState_phX | Returns state record, given pressure and specific enthalpy |
setState_ph | Returns state record as function of p and h |
setState_psX | Returns state record, given pressure and specific entropy |
setState_ps | Returns state record as function of p and s |
setSmoothState | Return thermodynamic state so that it smoothly approximates: if x > 0 then state_a else state_b |
specificHeatCapacityCv | Specific heat capacity at constant volume (or pressure) of medium |
specificHeatCapacityCp | Specific heat capacity at constant volume (or pressure) of medium |
dynamicViscosity | Return dynamic viscosity as a function of the thermodynamic state record |
thermalConductivity | Return thermal conductivity as a function of the thermodynamic state record |
s_T | Compute specific entropy |
specificEntropy | Return specific entropy as a function of the thermodynamic state record |
h_T | Compute specific enthalpy from temperature |
h_T_der | Compute specific enthalpy from temperature |
h_pT | Compute specific enthalpy from pressure and temperature |
density_T | Return density as function of temperature |
temperature | Return temperature as a function of the thermodynamic state record |
pressure | Return pressure as a function of the thermodynamic state record |
density | Return density as a function of the thermodynamic state record |
specificEnthalpy | Return specific enthalpy as a function of the thermodynamic state record |
specificInternalEnergy | Return specific internal energy as a function of the thermodynamic state record |
T_ph | Compute temperature from pressure and specific enthalpy |
T_ps | Compute temperature from pressure and specific enthalpy |
specificEnthalpyOfT | Return specific enthalpy from pressure and temperature, taking the flag enthalpyOfT into account |
ThermoStates=if enthalpyOfT then Modelica.Media.Interfaces.Choices.IndependentVariables.T else Modelica.Media.Interfaces.Choices.IndependentVariables.pT | Enumeration type for independent variables |
mediumName="Glycol-Water 47%" | Name of the medium |
substanceNames={mediumName} | Names of the mixture substances. Set substanceNames={mediumName} if only one substance. |
extraPropertiesNames=fill("", 0) | Names of the additional (extra) transported properties. Set extraPropertiesNames=fill("",0) if unused |
singleState=true | = true, if u and d are not a function of pressure |
reducedX=true | = true if medium contains the equation sum(X) = 1.0; set reducedX=true if only one substance (see docu for details) |
fixedX=true | = true if medium contains the equation X = reference_X |
reference_p=1.013e5 | Reference pressure of Medium: default 1 atmosphere |
reference_T=298.15 | Reference temperature of Medium: default 25 deg Celsius |
reference_X=fill(1/nX, nX) | Default mass fractions of medium |
p_default=101325 | Default value for pressure of medium (for initialization) |
T_default=Modelica.Units.Conversions.from_degC(20) | Default value for temperature of medium (for initialization) |
h_default=specificEnthalpy_pTX(p_default, T_default, X_default) | Default value for specific enthalpy of medium (for initialization) |
X_default=reference_X | Default value for mass fractions of medium (for initialization) |
C_default=fill(0, nC) | Default value for trace substances of medium (for initialization) |
nS=size(substanceNames, 1) | Number of substances |
nX=nS | Number of mass fractions |
nXi=if fixedX then 0 else if reducedX then nS - 1 else nS | Number of structurally independent mass fractions (see docu for details) |
nC=size(extraPropertiesNames, 1) | Number of extra (outside of standard mass-balance) transported properties |
C_nominal=1.0e-6*ones(nC) | Default for the nominal values for the extra properties |
FluidConstants | Critical, triple, molecular and other standard data of fluid |
ThermodynamicState | Minimal variable set that is available as input argument to every medium function |
prandtlNumber | Return the Prandtl number |
specificGibbsEnergy | Return specific Gibbs energy |
specificHelmholtzEnergy | Return specific Helmholtz energy |
heatCapacity_cp | Alias for deprecated name |
heatCapacity_cv | Alias for deprecated name |
isentropicExponent | Return isentropic exponent |
isentropicEnthalpy | Return isentropic enthalpy |
velocityOfSound | Return velocity of sound |
isobaricExpansionCoefficient | Return overall the isobaric expansion coefficient beta |
beta | Alias for isobaricExpansionCoefficient for user convenience |
isothermalCompressibility | Return overall the isothermal compressibility factor |
kappa | Alias of isothermalCompressibility for user convenience |
density_derp_h | Return density derivative w.r.t. pressure at const specific enthalpy |
density_derh_p | Return density derivative w.r.t. specific enthalpy at constant pressure |
density_derp_T | Return density derivative w.r.t. pressure at const temperature |
density_derT_p | Return density derivative w.r.t. temperature at constant pressure |
density_derX | Return density derivative w.r.t. mass fraction |
molarMass | Return the molar mass of the medium |
specificEnthalpy_pTX | Return specific enthalpy from p, T, and X or Xi |
specificEntropy_pTX | Return specific enthalpy from p, T, and X or Xi |
density_pTX | Return density from p, T, and X or Xi |
temperature_phX | Return temperature from p, h, and X or Xi |
density_phX | Return density from p, h, and X or Xi |
temperature_psX | Return temperature from p,s, and X or Xi |
density_psX | Return density from p, s, and X or Xi |
specificEnthalpy_psX | Return specific enthalpy from p, s, and X or Xi |
MassFlowRate | Type for mass flow rate with medium specific attributes |
AbsolutePressure | Type for absolute pressure with medium specific attributes |
Density | Type for density with medium specific attributes |
DynamicViscosity | Type for dynamic viscosity with medium specific attributes |
EnthalpyFlowRate | Type for enthalpy flow rate with medium specific attributes |
MassFraction | Type for mass fraction with medium specific attributes |
MoleFraction | Type for mole fraction with medium specific attributes |
MolarMass | Type for molar mass with medium specific attributes |
MolarVolume | Type for molar volume with medium specific attributes |
IsentropicExponent | Type for isentropic exponent with medium specific attributes |
SpecificEnergy | Type for specific energy with medium specific attributes |
SpecificInternalEnergy | Type for specific internal energy with medium specific attributes |
SpecificEnthalpy | Type for specific enthalpy with medium specific attributes |
SpecificEntropy | Type for specific entropy with medium specific attributes |
SpecificHeatCapacity | Type for specific heat capacity with medium specific attributes |
SurfaceTension | Type for surface tension with medium specific attributes |
Temperature | Type for temperature with medium specific attributes |
ThermalConductivity | Type for thermal conductivity with medium specific attributes |
PrandtlNumber | Type for Prandtl number with medium specific attributes |
VelocityOfSound | Type for velocity of sound with medium specific attributes |
ExtraProperty | Type for unspecified, mass-specific property transported by flow |
CumulativeExtraProperty | Type for conserved integral of unspecified, mass specific property |
ExtraPropertyFlowRate | Type for flow rate of unspecified, mass-specific property |
IsobaricExpansionCoefficient | Type for isobaric expansion coefficient with medium specific attributes |
DipoleMoment | Type for dipole moment with medium specific attributes |
DerDensityByPressure | Type for partial derivative of density with respect to pressure with medium specific attributes |
DerDensityByEnthalpy | Type for partial derivative of density with respect to enthalpy with medium specific attributes |
DerEnthalpyByPressure | Type for partial derivative of enthalpy with respect to pressure with medium specific attributes |
DerDensityByTemperature | Type for partial derivative of density with respect to temperature with medium specific attributes |
DerTemperatureByPressure | Type for partial derivative of temperature with respect to pressure with medium specific attributes |
SaturationProperties | Saturation properties of two phase medium |
FluidLimits | Validity limits for fluid model |
FixedPhase | Phase of the fluid: 1 for 1-phase, 2 for two-phase, 0 for not known, e.g., interactive use |
Basic | The most basic version of a record used in several degrees of detail |
IdealGas | The ideal gas version of a record used in several degrees of detail |
TwoPhase | The two phase fluid version of a record used in several degrees of detail |