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) | |
| Function to invert temperatures | |
| Base properties of T dependent medium | |
| Returns state record, given pressure and temperature | |
| Returns state record, given pressure and temperature | |
| Returns state record as function of p and T | |
| Returns state record, given pressure and specific enthalpy | |
| Returns state record as function of p and h | |
| Returns state record, given pressure and specific entropy | |
| Returns state record as function of p and s | |
| Return thermodynamic state so that it smoothly approximates: if x > 0 then state_a else state_b | |
| Specific heat capacity at constant volume (or pressure) of medium | |
| Specific heat capacity at constant volume (or pressure) of medium | |
| Return dynamic viscosity as a function of the thermodynamic state record | |
| Return thermal conductivity as a function of the thermodynamic state record | |
| Compute specific entropy | |
| Return specific entropy as a function of the thermodynamic state record | |
| Compute specific enthalpy from temperature | |
| Compute specific enthalpy from temperature | |
| Compute specific enthalpy from pressure and temperature | |
| Return density as function of temperature | |
| Return temperature as a function of the thermodynamic state record | |
| Return pressure as a function of the thermodynamic state record | |
| Return density as a function of the thermodynamic state record | |
| Return specific enthalpy as a function of the thermodynamic state record | |
| Return specific internal energy as a function of the thermodynamic state record | |
| Compute temperature from pressure and specific enthalpy | |
| Compute temperature from pressure and specific enthalpy | |
| 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 |
| Critical, triple, molecular and other standard data of fluid | |
| Minimal variable set that is available as input argument to every medium function | |
| Return the Prandtl number | |
| Return specific Gibbs energy | |
| Return specific Helmholtz energy | |
| Alias for deprecated name | |
| Alias for deprecated name | |
| Return isentropic exponent | |
| Return isentropic enthalpy | |
| Return velocity of sound | |
| Return overall the isobaric expansion coefficient beta | |
| Alias for isobaricExpansionCoefficient for user convenience | |
| Return overall the isothermal compressibility factor | |
| Alias of isothermalCompressibility for user convenience | |
| Return density derivative w.r.t. pressure at const specific enthalpy | |
| Return density derivative w.r.t. specific enthalpy at constant pressure | |
| Return density derivative w.r.t. pressure at const temperature | |
| Return density derivative w.r.t. temperature at constant pressure | |
| Return density derivative w.r.t. mass fraction | |
| Return the molar mass of the medium | |
| Return specific enthalpy from p, T, and X or Xi | |
| Return specific enthalpy from p, T, and X or Xi | |
| Return density from p, T, and X or Xi | |
| Return temperature from p, h, and X or Xi | |
| Return density from p, h, and X or Xi | |
| Return temperature from p,s, and X or Xi | |
| Return density from p, s, and X or Xi | |
| Return specific enthalpy from p, s, and X or Xi | |
| Type for mass flow rate with medium specific attributes | |
| Type for absolute pressure with medium specific attributes | |
| Type for density with medium specific attributes | |
| Type for dynamic viscosity with medium specific attributes | |
| Type for enthalpy flow rate with medium specific attributes | |
| Type for mass fraction with medium specific attributes | |
| Type for mole fraction with medium specific attributes | |
| Type for molar mass with medium specific attributes | |
| Type for molar volume with medium specific attributes | |
| Type for isentropic exponent with medium specific attributes | |
| Type for specific energy with medium specific attributes | |
| Type for specific internal energy with medium specific attributes | |
| Type for specific enthalpy with medium specific attributes | |
| Type for specific entropy with medium specific attributes | |
| Type for specific heat capacity with medium specific attributes | |
| Type for surface tension with medium specific attributes | |
| Type for temperature with medium specific attributes | |
| Type for thermal conductivity with medium specific attributes | |
| Type for Prandtl number with medium specific attributes | |
| Type for velocity of sound with medium specific attributes | |
| Type for unspecified, mass-specific property transported by flow | |
| Type for conserved integral of unspecified, mass specific property | |
| Type for flow rate of unspecified, mass-specific property | |
| Type for isobaric expansion coefficient with medium specific attributes | |
| Type for dipole moment with medium specific attributes | |
| Type for partial derivative of density with respect to pressure with medium specific attributes | |
| Type for partial derivative of density with respect to enthalpy with medium specific attributes | |
| Type for partial derivative of enthalpy with respect to pressure with medium specific attributes | |
| Type for partial derivative of density with respect to temperature with medium specific attributes | |
| Type for partial derivative of temperature with respect to pressure with medium specific attributes | |
| Saturation properties of two phase medium | |
| Validity limits for fluid model | |
| Phase of the fluid: 1 for 1-phase, 2 for two-phase, 0 for not known, e.g., interactive use | |
| The most basic version of a record used in several degrees of detail | |
| The ideal gas version of a record used in several degrees of detail | |
| The two phase fluid version of a record used in several degrees of detail | |