This model calculates medium properties for water in the liquid, gas and two phase regions according to the IAPWS/IF97 standard, i.e., the accepted industrial standard and best compromise between accuracy and computation time. For more details see Modelica.Media.Water.IF97_Utilities. Three variable pairs can be the independent variables of the model:
Variable | Unit | Description |
T | K | temperature |
u | J/kg | specific internal energy |
d | kg/m^3 | density |
p | Pa | pressure |
h | J/kg | specific enthalpy |
In some cases additional medium properties are needed. A component that needs these optional properties has to call one of the functions listed in Modelica.Media.UsersGuide.MediumUsage.OptionalProperties and in Modelica.Media.UsersGuide.MediumUsage.TwoPhase.
Many further properties can be computed. Using the well-known Bridgman's Tables, all first partial derivatives of the standard thermodynamic variables can be computed easily.
Extends from Interfaces.PartialTwoPhaseMedium (Base class for two phase medium of one substance).
Name | Description |
---|---|
ThermodynamicState | thermodynamic state |
ph_explicit | true if explicit in pressure and specific enthalpy |
dT_explicit | true if explicit in density and temperature |
pT_explicit | true if explicit in pressure and temperature |
BaseProperties | Base properties of water |
density_ph | Computes density as a function of pressure and specific enthalpy |
temperature_ph | Computes temperature as a function of pressure and specific enthalpy |
temperature_ps | Compute temperature from pressure and specific enthalpy |
density_ps | Computes density as a function of pressure and specific enthalpy |
pressure_dT | Computes pressure as a function of density and temperature |
specificEnthalpy_dT | Computes specific enthalpy as a function of density and temperature |
specificEnthalpy_pT | Computes specific enthalpy as a function of pressure and temperature |
specificEnthalpy_ps | Computes specific enthalpy as a function of pressure and temperature |
density_pT | Computes density as a function of pressure and temperature |
setDewState | set the thermodynamic state on the dew line |
setBubbleState | set the thermodynamic state on the bubble line |
dynamicViscosity | Dynamic viscosity of water |
thermalConductivity | Thermal conductivity of water |
surfaceTension | Surface tension in two phase region of water |
pressure | return pressure of ideal gas |
temperature | return temperature of ideal gas |
density | return density of ideal gas |
specificEnthalpy | Return specific enthalpy |
specificInternalEnergy | Return specific internal energy |
specificGibbsEnergy | Return specific Gibbs energy |
specificHelmholtzEnergy | Return specific Helmholtz energy |
specificEntropy | specific entropy of water |
specificHeatCapacityCp | specific heat capacity at constant pressure of water |
specificHeatCapacityCv | specific heat capacity at constant volume of water |
isentropicExponent | Return isentropic exponent |
isothermalCompressibility | Isothermal compressibility of water |
isobaricExpansionCoefficient | isobaric expansion coefficient of water |
velocityOfSound | Return velocity of sound as a function of the thermodynamic state record |
isentropicEnthalpy | compute h(p,s) |
density_derh_p | density derivative by specific enthalpy |
density_derp_h | density derivative by pressure |
bubbleEnthalpy | boiling curve specific enthalpy of water |
dewEnthalpy | dew curve specific enthalpy of water |
bubbleEntropy | boiling curve specific entropy of water |
dewEntropy | dew curve specific entropy of water |
bubbleDensity | boiling curve specific density of water |
dewDensity | dew curve specific density of water |
saturationTemperature | saturation temperature of water |
saturationTemperature_derp | derivative of saturation temperature w.r.t. pressure |
saturationPressure | saturation pressure of water |
dBubbleDensity_dPressure | bubble point density derivative |
dDewDensity_dPressure | dew point density derivative |
dBubbleEnthalpy_dPressure | bubble point specific enthalpy derivative |
dDewEnthalpy_dPressure | dew point specific enthalpy derivative |
setState_dTX | Return thermodynamic state of water as function of d and T |
setState_phX | Return thermodynamic state of water as function of p and h |
setState_psX | Return thermodynamic state of water as function of p and s |
setState_pTX | Return thermodynamic state of water as function of p and T |
setSmoothState | Return thermodynamic state so that it smoothly approximates: if x > 0 then state_a else state_b |
Inherited | |
smoothModel | true if the (derived) model should not generate state events |
onePhase | true if the (derived) model should never be called with two-phase inputs |
FluidLimits | validity limits for fluid model |
FluidConstants | extended fluid constants |
fluidConstants | constant data for the fluid |
SaturationProperties | Saturation properties of two phase medium |
FixedPhase | phase of the fluid: 1 for 1-phase, 2 for two-phase, 0 for not known, e.g. interactive use |
setSat_T | Return saturation property record from temperature |
setSat_p | Return saturation property record from pressure |
saturationPressure_sat | Return saturation temperature |
saturationTemperature_sat | Return saturation temperature |
saturationTemperature_derp_sat | Return derivative of saturation temperature w.r.t. pressure |
molarMass | Return the molar mass of the medium |
specificEnthalpy_pTX | Return specific enthalpy from pressure, temperature and mass fraction |
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 |
setState_pT | Return thermodynamic state from p and T |
setState_ph | Return thermodynamic state from p and h |
setState_ps | Return thermodynamic state from p and s |
setState_dT | Return thermodynamic state from d and T |
setState_px | Return thermodynamic state from pressure and vapour quality |
setState_Tx | Return thermodynamic state from temperature and vapour quality |
vapourQuality | Return vapour quality |
ThermoStates | Enumeration type for independent variables |
mediumName="unusablePartialMedium" | 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, 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=false | = true if medium contains the equation X = reference_X |
reference_p=101325 | 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.SIunits.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) |
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 |
prandtlNumber | Return the Prandtl number |
heatCapacity_cp | alias for deprecated name |
heatCapacity_cv | alias for deprecated name |
beta | alias for isobaricExpansionCoefficient for user convenience |
kappa | alias of isothermalCompressibility for user convenience |
density_derp_T | Return density derivative wrt pressure at const temperature |
density_derT_p | Return density derivative wrt temperature at constant pressure |
density_derX | Return density derivative wrt mass fraction |
density_pTX | Return density from p, T, and X or Xi |
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 |
MassFlowRate | Type for mass 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 resect to pressure with medium specific attributes |
DerDensityByEnthalpy | Type for partial derivative of density with resect to enthalpy with medium specific attributes |
DerEnthalpyByPressure | Type for partial derivative of enthalpy with resect to pressure with medium specific attributes |
DerDensityByTemperature | Type for partial derivative of density with resect to temperature with medium specific attributes |
Choices | Types, constants to define menu choices |
constant Boolean ph_explicit "true if explicit in pressure and specific enthalpy";
constant Boolean dT_explicit "true if explicit in density and temperature";
constant Boolean pT_explicit "true if explicit in pressure and temperature";
redeclare record extends ThermodynamicState "thermodynamic state" SpecificEnthalpy h "specific enthalpy"; Density d "density"; Temperature T "temperature"; AbsolutePressure p "pressure"; end ThermodynamicState;
Type | Name | Default | Description |
---|---|---|---|
Advanced | |||
Boolean | preferredMediumStates | false | = true if StateSelect.prefer shall be used for the independent property variables of the medium |
redeclare replaceable model extends BaseProperties( h(stateSelect=if ph_explicit and preferredMediumStates then StateSelect.prefer else StateSelect.default), d(stateSelect=if dT_explicit and preferredMediumStates then StateSelect.prefer else StateSelect.default), T(stateSelect=if (pT_explicit or dT_explicit) and preferredMediumStates then StateSelect.prefer else StateSelect.default), p(stateSelect=if (pT_explicit or ph_explicit) and preferredMediumStates then StateSelect.prefer else StateSelect.default)) "Base properties of water" Integer phase(min=0, max=2, start=1,fixed=false) "2 for two-phase, 1 for one-phase, 0 if not known"; SaturationProperties sat(Tsat(start=300.0), psat(start=1.0e5)) "saturation temperature and pressure"; equation MM = fluidConstants[1].molarMass; if smoothModel then if onePhase then phase = 1; if ph_explicit then assert(((h < bubbleEnthalpy(sat) or h > dewEnthalpy(sat)) or p > fluidConstants[1].criticalPressure), "With onePhase=true this model may only be called with one-phase states h < hl or h > hv!" + "(p = " + String(p) + ", h = " + String(h) + ")"); else if dT_explicit then assert(not ((d < bubbleDensity(sat) and d > dewDensity(sat)) and T < fluidConstants[1].criticalTemperature), "With onePhase=true this model may only be called with one-phase states d > dl or d < dv!" + "(d = " + String(d) + ", T = " + String(T) + ")"); else assert(true,"no events for pT-model"); end if; end if; else phase = 0; end if; else if ph_explicit then phase = if ((h < bubbleEnthalpy(sat) or h > dewEnthalpy(sat)) or p > fluidConstants[1].criticalPressure) then 1 else 2; elseif dT_explicit then phase = if not ((d < bubbleDensity(sat) and d > dewDensity(sat)) and T < fluidConstants[1].criticalTemperature) then 1 else 2; else phase = 1; //this is for the one-phase only case pT end if; end if; if dT_explicit then p = pressure_dT(d, T, phase); h = specificEnthalpy_dT(d, T, phase); sat.Tsat = T; sat.psat = saturationPressure(T); elseif ph_explicit then d = density_ph(p, h, phase); T = temperature_ph(p, h, phase); sat.Tsat = saturationTemperature(p); sat.psat = p; else h = specificEnthalpy_pT(p, T); d = density_pT(p, T); sat.psat = p; sat.Tsat = saturationTemperature(p); end if; u = h - p/d; R = Modelica.Constants.R/fluidConstants[1].molarMass; h = state.h; p = state.p; T = state.T; d = state.d; phase = state.phase; end BaseProperties;
Type | Name | Default | Description |
---|---|---|---|
AbsolutePressure | p | Pressure [Pa] | |
SpecificEnthalpy | h | Specific enthalpy [J/kg] | |
FixedPhase | phase | 0 | 2 for two-phase, 1 for one-phase, 0 if not known |
Type | Name | Description |
---|---|---|
Density | d | Density [kg/m3] |
redeclare function density_ph "Computes density as a function of pressure and specific enthalpy" extends Modelica.Icons.Function; input AbsolutePressure p "Pressure"; input SpecificEnthalpy h "Specific enthalpy"; input FixedPhase phase=0 "2 for two-phase, 1 for one-phase, 0 if not known"; output Density d "Density"; algorithm d := IF97_Utilities.rho_ph(p, h, phase); end density_ph;
Type | Name | Default | Description |
---|---|---|---|
AbsolutePressure | p | Pressure [Pa] | |
SpecificEnthalpy | h | Specific enthalpy [J/kg] | |
FixedPhase | phase | 0 | 2 for two-phase, 1 for one-phase, 0 if not known |
Type | Name | Description |
---|---|---|
Temperature | T | Temperature [K] |
redeclare function temperature_ph "Computes temperature as a function of pressure and specific enthalpy" extends Modelica.Icons.Function; input AbsolutePressure p "Pressure"; input SpecificEnthalpy h "Specific enthalpy"; input FixedPhase phase=0 "2 for two-phase, 1 for one-phase, 0 if not known"; output Temperature T "Temperature"; algorithm T := IF97_Utilities.T_ph(p, h, phase); end temperature_ph;
Type | Name | Default | Description |
---|---|---|---|
AbsolutePressure | p | Pressure [Pa] | |
SpecificEntropy | s | Specific entropy [J/(kg.K)] | |
FixedPhase | phase | 0 | 2 for two-phase, 1 for one-phase, 0 if not known |
Type | Name | Description |
---|---|---|
Temperature | T | Temperature [K] |
redeclare function temperature_ps "Compute temperature from pressure and specific enthalpy" extends Modelica.Icons.Function; input AbsolutePressure p "Pressure"; input SpecificEntropy s "Specific entropy"; input FixedPhase phase=0 "2 for two-phase, 1 for one-phase, 0 if not known"; output Temperature T "Temperature"; algorithm T := IF97_Utilities.T_ps(p, s, phase); end temperature_ps;
Type | Name | Default | Description |
---|---|---|---|
AbsolutePressure | p | Pressure [Pa] | |
SpecificEntropy | s | Specific entropy [J/(kg.K)] | |
FixedPhase | phase | 0 | 2 for two-phase, 1 for one-phase, 0 if not known |
Type | Name | Description |
---|---|---|
Density | d | density [kg/m3] |
redeclare function density_ps "Computes density as a function of pressure and specific enthalpy" extends Modelica.Icons.Function; input AbsolutePressure p "Pressure"; input SpecificEntropy s "Specific entropy"; input FixedPhase phase=0 "2 for two-phase, 1 for one-phase, 0 if not known"; output Density d "density"; algorithm d := IF97_Utilities.rho_ps(p, s, phase); end density_ps;
Type | Name | Default | Description |
---|---|---|---|
Density | d | Density [kg/m3] | |
Temperature | T | Temperature [K] | |
FixedPhase | phase | 0 | 2 for two-phase, 1 for one-phase, 0 if not known |
Type | Name | Description |
---|---|---|
AbsolutePressure | p | Pressure [Pa] |
redeclare function pressure_dT "Computes pressure as a function of density and temperature" extends Modelica.Icons.Function; input Density d "Density"; input Temperature T "Temperature"; input FixedPhase phase=0 "2 for two-phase, 1 for one-phase, 0 if not known"; output AbsolutePressure p "Pressure"; algorithm p := IF97_Utilities.p_dT(d, T, phase); end pressure_dT;
Type | Name | Default | Description |
---|---|---|---|
Density | d | Density [kg/m3] | |
Temperature | T | Temperature [K] | |
FixedPhase | phase | 0 | 2 for two-phase, 1 for one-phase, 0 if not known |
Type | Name | Description |
---|---|---|
SpecificEnthalpy | h | specific enthalpy [J/kg] |
redeclare function specificEnthalpy_dT "Computes specific enthalpy as a function of density and temperature" extends Modelica.Icons.Function; input Density d "Density"; input Temperature T "Temperature"; input FixedPhase phase=0 "2 for two-phase, 1 for one-phase, 0 if not known"; output SpecificEnthalpy h "specific enthalpy"; algorithm h := IF97_Utilities.h_dT(d, T, phase); end specificEnthalpy_dT;
Type | Name | Default | Description |
---|---|---|---|
AbsolutePressure | p | Pressure [Pa] | |
Temperature | T | Temperature [K] | |
FixedPhase | phase | 0 | 2 for two-phase, 1 for one-phase, 0 if not known |
Type | Name | Description |
---|---|---|
SpecificEnthalpy | h | specific enthalpy [J/kg] |
redeclare function specificEnthalpy_pT "Computes specific enthalpy as a function of pressure and temperature" extends Modelica.Icons.Function; input AbsolutePressure p "Pressure"; input Temperature T "Temperature"; input FixedPhase phase=0 "2 for two-phase, 1 for one-phase, 0 if not known"; output SpecificEnthalpy h "specific enthalpy"; algorithm h := IF97_Utilities.h_pT(p, T); end specificEnthalpy_pT;
Type | Name | Default | Description |
---|---|---|---|
AbsolutePressure | p | Pressure [Pa] | |
SpecificEntropy | s | Specific entropy [J/(kg.K)] | |
FixedPhase | phase | 0 | 2 for two-phase, 1 for one-phase, 0 if not known |
Type | Name | Description |
---|---|---|
SpecificEnthalpy | h | specific enthalpy [J/kg] |
redeclare function specificEnthalpy_ps "Computes specific enthalpy as a function of pressure and temperature" extends Modelica.Icons.Function; input AbsolutePressure p "Pressure"; input SpecificEntropy s "Specific entropy"; input FixedPhase phase=0 "2 for two-phase, 1 for one-phase, 0 if not known"; output SpecificEnthalpy h "specific enthalpy"; algorithm h := IF97_Utilities.h_ps(p, s, phase); end specificEnthalpy_ps;
Type | Name | Default | Description |
---|---|---|---|
AbsolutePressure | p | Pressure [Pa] | |
Temperature | T | Temperature [K] | |
FixedPhase | phase | 0 | 2 for two-phase, 1 for one-phase, 0 if not known |
Type | Name | Description |
---|---|---|
Density | d | Density [kg/m3] |
redeclare function density_pT "Computes density as a function of pressure and temperature" extends Modelica.Icons.Function; input AbsolutePressure p "Pressure"; input Temperature T "Temperature"; input FixedPhase phase=0 "2 for two-phase, 1 for one-phase, 0 if not known"; output Density d "Density"; algorithm d := IF97_Utilities.rho_pT(p, T); end density_pT;
Type | Name | Default | Description |
---|---|---|---|
SaturationProperties | sat | saturation point | |
FixedPhase | phase | 1 | phase: default is one phase |
Type | Name | Description |
---|---|---|
ThermodynamicState | state | complete thermodynamic state info |
redeclare function extends setDewState "set the thermodynamic state on the dew line" algorithm state := ThermodynamicState( phase= phase, p= sat.psat, T= sat.Tsat, h= dewEnthalpy(sat), d= dewDensity(sat)); end setDewState;
Type | Name | Default | Description |
---|---|---|---|
SaturationProperties | sat | saturation point | |
FixedPhase | phase | 1 | phase: default is one phase |
Type | Name | Description |
---|---|---|
ThermodynamicState | state | complete thermodynamic state info |
redeclare function extends setBubbleState "set the thermodynamic state on the bubble line" algorithm state := ThermodynamicState( phase= phase, p= sat.psat, T= sat.Tsat, h= bubbleEnthalpy(sat), d= bubbleDensity(sat)); end setBubbleState;
Type | Name | Default | Description |
---|---|---|---|
ThermodynamicState | state | thermodynamic state record |
Type | Name | Description |
---|---|---|
DynamicViscosity | eta | Dynamic viscosity [Pa.s] |
redeclare function extends dynamicViscosity "Dynamic viscosity of water" algorithm eta := IF97_Utilities.dynamicViscosity(state.d, state.T, state.p, state. phase); end dynamicViscosity;
Type | Name | Default | Description |
---|---|---|---|
ThermodynamicState | state | thermodynamic state record |
Type | Name | Description |
---|---|---|
ThermalConductivity | lambda | Thermal conductivity [W/(m.K)] |
redeclare function extends thermalConductivity "Thermal conductivity of water" algorithm lambda := IF97_Utilities.thermalConductivity(state.d, state.T, state.p, state.phase); end thermalConductivity;
Type | Name | Default | Description |
---|---|---|---|
SaturationProperties | sat | saturation property record |
Type | Name | Description |
---|---|---|
SurfaceTension | sigma | Surface tension sigma in the two phase region [N/m] |
redeclare function extends surfaceTension "Surface tension in two phase region of water" algorithm sigma := IF97_Utilities.surfaceTension(sat.Tsat); end surfaceTension;
Type | Name | Default | Description |
---|---|---|---|
ThermodynamicState | state | thermodynamic state record |
Type | Name | Description |
---|---|---|
AbsolutePressure | p | Pressure [Pa] |
redeclare function extends pressure "return pressure of ideal gas" algorithm p := state.p; end pressure;
Type | Name | Default | Description |
---|---|---|---|
ThermodynamicState | state | thermodynamic state record |
Type | Name | Description |
---|---|---|
Temperature | T | Temperature [K] |
redeclare function extends temperature "return temperature of ideal gas" algorithm T := state.T; end temperature;
Type | Name | Default | Description |
---|---|---|---|
ThermodynamicState | state | thermodynamic state record |
Type | Name | Description |
---|---|---|
Density | d | Density [kg/m3] |
redeclare function extends density "return density of ideal gas" algorithm d := state.d; end density;
Type | Name | Default | Description |
---|---|---|---|
ThermodynamicState | state | thermodynamic state record |
Type | Name | Description |
---|---|---|
SpecificEnthalpy | h | Specific enthalpy [J/kg] |
redeclare function extends specificEnthalpy "Return specific enthalpy" extends Modelica.Icons.Function; algorithm h := state.h; end specificEnthalpy;
Type | Name | Default | Description |
---|---|---|---|
ThermodynamicState | state | thermodynamic state record |
Type | Name | Description |
---|---|---|
SpecificEnergy | u | Specific internal energy [J/kg] |
redeclare function extends specificInternalEnergy "Return specific internal energy" extends Modelica.Icons.Function; algorithm u := state.h - state.p/state.d; end specificInternalEnergy;
Type | Name | Default | Description |
---|---|---|---|
ThermodynamicState | state | thermodynamic state record |
Type | Name | Description |
---|---|---|
SpecificEnergy | g | Specific Gibbs energy [J/kg] |
redeclare function extends specificGibbsEnergy "Return specific Gibbs energy" extends Modelica.Icons.Function; algorithm g := state.h - state.T*specificEntropy(state); end specificGibbsEnergy;
Type | Name | Default | Description |
---|---|---|---|
ThermodynamicState | state | thermodynamic state record |
Type | Name | Description |
---|---|---|
SpecificEnergy | f | Specific Helmholtz energy [J/kg] |
redeclare function extends specificHelmholtzEnergy "Return specific Helmholtz energy" extends Modelica.Icons.Function; algorithm f := state.h - state.p/state.d - state.T*specificEntropy(state); end specificHelmholtzEnergy;
Type | Name | Default | Description |
---|---|---|---|
ThermodynamicState | state | thermodynamic state record |
Type | Name | Description |
---|---|---|
SpecificEntropy | s | Specific entropy [J/(kg.K)] |
redeclare function extends specificEntropy "specific entropy of water" algorithm if dT_explicit then s := IF97_Utilities.s_dT(state.d, state.T, state.phase); elseif pT_explicit then s := IF97_Utilities.s_pT(state.p, state.T); else s := IF97_Utilities.s_ph(state.p, state.h, state.phase); end if; end specificEntropy;
In the two phase region this function returns the interpolated heat capacity between the liquid and vapour state heat capacities.
Error:Found no end-tag in HTML-documentationExtends from (Return specific heat capacity at constant pressure).
Type | Name | Default | Description |
---|---|---|---|
ThermodynamicState | state | thermodynamic state record |
Type | Name | Description |
---|---|---|
SpecificHeatCapacity | cp | Specific heat capacity at constant pressure [J/(kg.K)] |
redeclare function extends specificHeatCapacityCp "specific heat capacity at constant pressure of water" algorithm if dT_explicit then cp := IF97_Utilities.cp_dT(state.d, state.T, state.phase); elseif pT_explicit then cp := IF97_Utilities.cp_pT(state.p, state.T); else cp := IF97_Utilities.cp_ph(state.p, state.h, state.phase); end if;end specificHeatCapacityCp;
Type | Name | Default | Description |
---|---|---|---|
ThermodynamicState | state | thermodynamic state record |
Type | Name | Description |
---|---|---|
SpecificHeatCapacity | cv | Specific heat capacity at constant volume [J/(kg.K)] |
redeclare function extends specificHeatCapacityCv "specific heat capacity at constant volume of water" algorithm if dT_explicit then cv := IF97_Utilities.cv_dT(state.d, state.T, state.phase); elseif pT_explicit then cv := IF97_Utilities.cv_pT(state.p, state.T); else cv := IF97_Utilities.cv_ph(state.p, state.h, state.phase); end if; end specificHeatCapacityCv;
Type | Name | Default | Description |
---|---|---|---|
ThermodynamicState | state | thermodynamic state record |
Type | Name | Description |
---|---|---|
IsentropicExponent | gamma | Isentropic exponent [1] |
redeclare function extends isentropicExponent "Return isentropic exponent" algorithm if dT_explicit then gamma := IF97_Utilities.isentropicExponent_dT(state.d, state.T, state. phase); elseif pT_explicit then gamma := IF97_Utilities.isentropicExponent_pT(state.p, state.T); else gamma := IF97_Utilities.isentropicExponent_ph(state.p, state.h, state. phase); end if; end isentropicExponent;
Type | Name | Default | Description |
---|---|---|---|
ThermodynamicState | state | thermodynamic state record |
Type | Name | Description |
---|---|---|
IsothermalCompressibility | kappa | Isothermal compressibility [1/Pa] |
redeclare function extends isothermalCompressibility "Isothermal compressibility of water" algorithm if dT_explicit then kappa := IF97_Utilities.kappa_dT(state.d, state.T, state.phase); elseif pT_explicit then kappa := IF97_Utilities.kappa_pT(state.p, state.T); else kappa := IF97_Utilities.kappa_ph(state.p, state.h, state.phase); end if; end isothermalCompressibility;
Type | Name | Default | Description |
---|---|---|---|
ThermodynamicState | state | thermodynamic state record |
Type | Name | Description |
---|---|---|
IsobaricExpansionCoefficient | beta | Isobaric expansion coefficient [1/K] |
redeclare function extends isobaricExpansionCoefficient "isobaric expansion coefficient of water" algorithm if dT_explicit then beta := IF97_Utilities.beta_dT(state.d, state.T, state.phase); elseif pT_explicit then beta := IF97_Utilities.beta_pT(state.p, state.T); else beta := IF97_Utilities.beta_ph(state.p, state.h, state.phase); end if; end isobaricExpansionCoefficient;
Type | Name | Default | Description |
---|---|---|---|
ThermodynamicState | state | thermodynamic state record |
Type | Name | Description |
---|---|---|
VelocityOfSound | a | Velocity of sound [m/s] |
redeclare function extends velocityOfSound "Return velocity of sound as a function of the thermodynamic state record" algorithm if dT_explicit then a := IF97_Utilities.velocityOfSound_dT(state.d, state.T, state.phase); elseif pT_explicit then a := IF97_Utilities.velocityOfSound_pT(state.p, state.T); else a := IF97_Utilities.velocityOfSound_ph(state.p, state.h, state.phase); end if; end velocityOfSound;
Type | Name | Default | Description |
---|---|---|---|
AbsolutePressure | p_downstream | downstream pressure [Pa] | |
ThermodynamicState | refState | reference state for entropy |
Type | Name | Description |
---|---|---|
SpecificEnthalpy | h_is | Isentropic enthalpy [J/kg] |
redeclare function extends isentropicEnthalpy "compute h(p,s)" algorithm h_is := IF97_Utilities.isentropicEnthalpy(p_downstream, specificEntropy( refState), 0); end isentropicEnthalpy;
Type | Name | Default | Description |
---|---|---|---|
ThermodynamicState | state | thermodynamic state record |
Type | Name | Description |
---|---|---|
DerDensityByEnthalpy | ddhp | Density derivative wrt specific enthalpy [kg.s2/m5] |
redeclare function extends density_derh_p "density derivative by specific enthalpy" algorithm ddhp := IF97_Utilities.ddhp(state.p, state.h, state.phase); end density_derh_p;
Type | Name | Default | Description |
---|---|---|---|
ThermodynamicState | state | thermodynamic state record |
Type | Name | Description |
---|---|---|
DerDensityByPressure | ddph | Density derivative wrt pressure [s2/m2] |
redeclare function extends density_derp_h "density derivative by pressure" algorithm ddph := IF97_Utilities.ddph(state.p, state.h, state.phase); end density_derp_h;
Type | Name | Default | Description |
---|---|---|---|
SaturationProperties | sat | saturation property record |
Type | Name | Description |
---|---|---|
SpecificEnthalpy | hl | boiling curve specific enthalpy [J/kg] |
redeclare function extends bubbleEnthalpy "boiling curve specific enthalpy of water" algorithm hl := IF97_Utilities.BaseIF97.Regions.hl_p(sat.psat); end bubbleEnthalpy;
Type | Name | Default | Description |
---|---|---|---|
SaturationProperties | sat | saturation property record |
Type | Name | Description |
---|---|---|
SpecificEnthalpy | hv | dew curve specific enthalpy [J/kg] |
redeclare function extends dewEnthalpy "dew curve specific enthalpy of water" algorithm hv := IF97_Utilities.BaseIF97.Regions.hv_p(sat.psat); end dewEnthalpy;
Type | Name | Default | Description |
---|---|---|---|
SaturationProperties | sat | saturation property record |
Type | Name | Description |
---|---|---|
SpecificEntropy | sl | boiling curve specific entropy [J/(kg.K)] |
redeclare function extends bubbleEntropy "boiling curve specific entropy of water" algorithm sl := IF97_Utilities.BaseIF97.Regions.sl_p(sat.psat); end bubbleEntropy;
Type | Name | Default | Description |
---|---|---|---|
SaturationProperties | sat | saturation property record |
Type | Name | Description |
---|---|---|
SpecificEntropy | sv | dew curve specific entropy [J/(kg.K)] |
redeclare function extends dewEntropy "dew curve specific entropy of water" algorithm sv := IF97_Utilities.BaseIF97.Regions.sv_p(sat.psat); end dewEntropy;
Type | Name | Default | Description |
---|---|---|---|
SaturationProperties | sat | saturation property record |
Type | Name | Description |
---|---|---|
Density | dl | boiling curve density [kg/m3] |
redeclare function extends bubbleDensity "boiling curve specific density of water" algorithm if ph_explicit or pT_explicit then dl := IF97_Utilities.BaseIF97.Regions.rhol_p(sat.psat); else dl := IF97_Utilities.BaseIF97.Regions.rhol_T(sat.Tsat); end if; end bubbleDensity;
Type | Name | Default | Description |
---|---|---|---|
SaturationProperties | sat | saturation property record |
Type | Name | Description |
---|---|---|
Density | dv | dew curve density [kg/m3] |
redeclare function extends dewDensity "dew curve specific density of water" algorithm if ph_explicit or pT_explicit then dv := IF97_Utilities.BaseIF97.Regions.rhov_p(sat.psat); else dv := IF97_Utilities.BaseIF97.Regions.rhov_T(sat.Tsat); end if; end dewDensity;
Type | Name | Default | Description |
---|---|---|---|
AbsolutePressure | p | pressure [Pa] |
Type | Name | Description |
---|---|---|
Temperature | T | saturation temperature [K] |
redeclare function extends saturationTemperature "saturation temperature of water" algorithm T := IF97_Utilities.BaseIF97.Basic.tsat(p); end saturationTemperature;
Type | Name | Default | Description |
---|---|---|---|
AbsolutePressure | p | pressure [Pa] |
Type | Name | Description |
---|---|---|
Real | dTp | derivative of saturation temperature w.r.t. pressure |
redeclare function extends saturationTemperature_derp "derivative of saturation temperature w.r.t. pressure" algorithm dTp := IF97_Utilities.BaseIF97.Basic.dtsatofp(p); end saturationTemperature_derp;
Type | Name | Default | Description |
---|---|---|---|
Temperature | T | temperature [K] |
Type | Name | Description |
---|---|---|
AbsolutePressure | p | saturation pressure [Pa] |
redeclare function extends saturationPressure "saturation pressure of water" algorithm p := IF97_Utilities.BaseIF97.Basic.psat(T); end saturationPressure;
Type | Name | Default | Description |
---|---|---|---|
SaturationProperties | sat | saturation property record |
Type | Name | Description |
---|---|---|
DerDensityByPressure | ddldp | boiling curve density derivative [s2/m2] |
redeclare function extends dBubbleDensity_dPressure "bubble point density derivative" algorithm ddldp := IF97_Utilities.BaseIF97.Regions.drhol_dp(sat.psat); end dBubbleDensity_dPressure;
Type | Name | Default | Description |
---|---|---|---|
SaturationProperties | sat | saturation property record |
Type | Name | Description |
---|---|---|
DerDensityByPressure | ddvdp | saturated steam density derivative [s2/m2] |
redeclare function extends dDewDensity_dPressure "dew point density derivative" algorithm ddvdp := IF97_Utilities.BaseIF97.Regions.drhov_dp(sat.psat); end dDewDensity_dPressure;
Type | Name | Default | Description |
---|---|---|---|
SaturationProperties | sat | saturation property record |
Type | Name | Description |
---|---|---|
DerEnthalpyByPressure | dhldp | boiling curve specific enthalpy derivative [J.m.s2/kg2] |
redeclare function extends dBubbleEnthalpy_dPressure "bubble point specific enthalpy derivative" algorithm dhldp := IF97_Utilities.BaseIF97.Regions.dhl_dp(sat.psat); end dBubbleEnthalpy_dPressure;
Type | Name | Default | Description |
---|---|---|---|
SaturationProperties | sat | saturation property record |
Type | Name | Description |
---|---|---|
DerEnthalpyByPressure | dhvdp | saturated steam specific enthalpy derivative [J.m.s2/kg2] |
redeclare function extends dDewEnthalpy_dPressure "dew point specific enthalpy derivative" algorithm dhvdp := IF97_Utilities.BaseIF97.Regions.dhv_dp(sat.psat); end dDewEnthalpy_dPressure;
Type | Name | Default | Description |
---|---|---|---|
FixedPhase | phase | 0 | 2 for two-phase, 1 for one-phase, 0 if not known |
Density | d | density [kg/m3] | |
Temperature | T | Temperature [K] | |
MassFraction | X[:] | reference_X | Mass fractions [kg/kg] |
Type | Name | Description |
---|---|---|
ThermodynamicState | state | thermodynamic state record |
redeclare function extends setState_dTX "Return thermodynamic state of water as function of d and T" algorithm state := ThermodynamicState( d=d, T=T, phase=0, h=specificEnthalpy_dT(d,T), p=pressure_dT(d,T)); end setState_dTX;
Type | Name | Default | Description |
---|---|---|---|
FixedPhase | phase | 0 | 2 for two-phase, 1 for one-phase, 0 if not known |
AbsolutePressure | p | Pressure [Pa] | |
SpecificEnthalpy | h | Specific enthalpy [J/kg] | |
MassFraction | X[:] | reference_X | Mass fractions [kg/kg] |
Type | Name | Description |
---|---|---|
ThermodynamicState | state | thermodynamic state record |
redeclare function extends setState_phX "Return thermodynamic state of water as function of p and h" algorithm state := ThermodynamicState( d=density_ph(p,h), T=temperature_ph(p,h), phase=0, h=h, p=p); end setState_phX;
Type | Name | Default | Description |
---|---|---|---|
FixedPhase | phase | 0 | 2 for two-phase, 1 for one-phase, 0 if not known |
AbsolutePressure | p | Pressure [Pa] | |
SpecificEntropy | s | Specific entropy [J/(kg.K)] | |
MassFraction | X[:] | reference_X | Mass fractions [kg/kg] |
Type | Name | Description |
---|---|---|
ThermodynamicState | state | thermodynamic state record |
redeclare function extends setState_psX "Return thermodynamic state of water as function of p and s" algorithm state := ThermodynamicState( d=density_ps(p,s), T=temperature_ps(p,s), phase=0, h=specificEnthalpy_ps(p,s), p=p); end setState_psX;
Type | Name | Default | Description |
---|---|---|---|
FixedPhase | phase | 0 | 2 for two-phase, 1 for one-phase, 0 if not known |
AbsolutePressure | p | Pressure [Pa] | |
Temperature | T | Temperature [K] | |
MassFraction | X[:] | reference_X | Mass fractions [kg/kg] |
Type | Name | Description |
---|---|---|
ThermodynamicState | state | thermodynamic state record |
redeclare function extends setState_pTX "Return thermodynamic state of water as function of p and T" algorithm state := ThermodynamicState( d=density_pT(p,T), T=T, phase=1, h=specificEnthalpy_pT(p,T), p=p); end setState_pTX;
Type | Name | Default | Description |
---|---|---|---|
Real | x | m_flow or dp | |
ThermodynamicState | state_a | Thermodynamic state if x > 0 | |
ThermodynamicState | state_b | Thermodynamic state if x < 0 | |
Real | x_small | Smooth transition in the region -x_small < x < x_small |
Type | Name | Description |
---|---|---|
ThermodynamicState | state | Smooth thermodynamic state for all x (continuous and differentiable) |
redeclare function extends setSmoothState "Return thermodynamic state so that it smoothly approximates: if x > 0 then state_a else state_b" import Modelica.Media.Common.smoothStep; algorithm state :=ThermodynamicState( p=smoothStep(x, state_a.p, state_b.p, x_small), h=smoothStep(x, state_a.h, state_b.h, x_small), d=density_ph(smoothStep(x, state_a.p, state_b.p, x_small), smoothStep(x, state_a.h, state_b.h, x_small)), T=temperature_ph(smoothStep(x, state_a.p, state_b.p, x_small), smoothStep(x, state_a.h, state_b.h, x_small)), phase=0); end setSmoothState;