.BuildingSystems.Media.Specialized.Water.TemperatureDependentDensity

Information

This medium package models liquid water.

The mass density is computed using a 3rd order polynomial, which yields the density as a function of temperature as shown in the figure below. Note, however, that computing density as a function of temperature can lead to considerably slower computing time compared to using BuildingSystems.Media.Water in which the density is a constant. We therefore recommend to use BuildingSystems.Media.Water for typical building energy simulations.

Mass density as a function of temperature

For the specific heat capacities at constant pressure and at constant volume, a constant value of 4184 J/(kg K), which corresponds to 20°C is used. The figure below shows the relative error of the specific heat capacity that is introduced by this simplification. Using a constant value for the specific heat capacity allows to compute temperature from enthalpy without having to solve an implicit equation, and therefore leads to faster simulation.

Relative variation of specific heat capacity with temperature

Thermal conductivity is calculated as a function of temperature as shown in the figure below. The correlation used to calculate the thermal conductivity is

λ(T) = λ(298.15 K) ⋅ (-1.48445+4.12292⋅(T/298.15)-1.63866⋅(T/298.15)2),

where λ(298.15 K) = 0.6065 W/(m ⋅ K) is the adopted standard value of the thermal conductivity of water at 298.15 K and 0.1 MPa.

Thermal conductivity as a function of temperature

Dynamic viscosity is calculated as the product of density and kinematic viscosity, both temperature dependent. However, the kinematic viscosity has its own temperature dependent correlation, implemented at BuildingSystems.Media.Specialized.Water.TemperatureDependentDensity.kinematicViscosity. Results of the kinematic viscosity as a function of temperature are shown in the figure below.

Kinematic viscosity as a function of temperature

The enthalpy is computed using the convention that h=0 if T=0 °C.

Limitations

Phase changes are not modeled.

Contents

NameDescription
 FluidConstants
 ThermodynamicStateThermodynamic state variables
 BasePropertiesBase properties
 densityReturn the density
 dynamicViscosityReturn the dynamic viscosity
 specificEnthalpyReturn the specific enthalpy
 enthalpyOfLiquidReturn the specific enthalpy of liquid
 specificInternalEnergyReturn the specific enthalpy
 specificEntropyReturn the specific entropy
 specificGibbsEnergyReturn the specific Gibbs energy
 specificHelmholtzEnergyReturn the specific Helmholtz energy
 isentropicEnthalpyReturn the isentropic enthalpy
 isobaricExpansionCoefficientReturn the isobaric expansion coefficient
 isothermalCompressibilityReturn the isothermal compressibility factor
 density_derp_TReturn the partial derivative of density with respect to pressure at constant temperature
 density_derT_pReturn the partial derivative of density with respect to temperature at constant pressure
 density_derXReturn the partial derivative of density with respect to mass fractions at constant pressure and temperature
 specificHeatCapacityCpReturn the specific heat capacity at constant pressure
 specificHeatCapacityCvReturn the specific heat capacity at constant volume
 thermalConductivityReturn the thermal conductivity
 pressureReturn the pressure
 temperatureReturn the temperature
 molarMassReturn the molar mass
 setState_dTXReturn thermodynamic state from d, T, and X or Xi
 setState_phXReturn the thermodynamic state as function of pressure p, specific enthalpy h and composition X or Xi
 setState_pTXReturn the thermodynamic state as function of p, T and composition X or Xi
 setState_psXReturn the thermodynamic state as function of p, s and composition X or Xi

Revisions


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