![[Jenkins]](/jenkins/static/e6f1148a/images/svgs/logo.svg){kind=logo}
Regression
simulation_libraries_3rdParty_TestMedia.TestFlueGas.mos (from (result.xml))
Stacktrace
Output mismatch (see stdout for details)
Standard Output
+ TestFlueGas.mos [instantiate/check/simulate] ... equation mismatch [time: 18]
==== Log C:\Windows\TEMP/omc-rtest-OpenModelica/simulation/libraries/3rdParty/TestMedia/TestFlueGas.mos_temp3724/log-TestFlueGas.mos
true
""
true
""
"function Modelica.Math.asin \"Inverse sine (-1 <= u <= 1)\"
input Real u;
output Real y(quantity = \"Angle\", unit = \"rad\", displayUnit = \"deg\");
external \"C\" y = asin(u);
end Modelica.Math.asin;
function Modelica.Math.log \"Natural (base e) logarithm (u shall be > 0)\"
input Real u;
output Real y;
external \"C\" y = log(u);
end Modelica.Math.log;
function Modelica.Media.IdealGases.Common.DataRecord \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord res;
end Modelica.Media.IdealGases.Common.DataRecord;
function Modelica.Media.IdealGases.Common.DataRecord$Ar \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord$Ar\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord$Ar res;
end Modelica.Media.IdealGases.Common.DataRecord$Ar;
function Modelica.Media.IdealGases.Common.DataRecord$C2H2_vinylidene \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord$C2H2_vinylidene\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord$C2H2_vinylidene res;
end Modelica.Media.IdealGases.Common.DataRecord$C2H2_vinylidene;
function Modelica.Media.IdealGases.Common.DataRecord$C2H4 \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord$C2H4\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord$C2H4 res;
end Modelica.Media.IdealGases.Common.DataRecord$C2H4;
function Modelica.Media.IdealGases.Common.DataRecord$C2H5OH \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord$C2H5OH\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord$C2H5OH res;
end Modelica.Media.IdealGases.Common.DataRecord$C2H5OH;
function Modelica.Media.IdealGases.Common.DataRecord$C2H6 \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord$C2H6\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord$C2H6 res;
end Modelica.Media.IdealGases.Common.DataRecord$C2H6;
function Modelica.Media.IdealGases.Common.DataRecord$C3H6_propylene \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord$C3H6_propylene\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord$C3H6_propylene res;
end Modelica.Media.IdealGases.Common.DataRecord$C3H6_propylene;
function Modelica.Media.IdealGases.Common.DataRecord$C3H8 \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord$C3H8\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord$C3H8 res;
end Modelica.Media.IdealGases.Common.DataRecord$C3H8;
function Modelica.Media.IdealGases.Common.DataRecord$C4H10_n_butane \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord$C4H10_n_butane\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord$C4H10_n_butane res;
end Modelica.Media.IdealGases.Common.DataRecord$C4H10_n_butane;
function Modelica.Media.IdealGases.Common.DataRecord$C4H8_1_butene \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord$C4H8_1_butene\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord$C4H8_1_butene res;
end Modelica.Media.IdealGases.Common.DataRecord$C4H8_1_butene;
function Modelica.Media.IdealGases.Common.DataRecord$C5H10_1_pentene \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord$C5H10_1_pentene\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord$C5H10_1_pentene res;
end Modelica.Media.IdealGases.Common.DataRecord$C5H10_1_pentene;
function Modelica.Media.IdealGases.Common.DataRecord$C5H12_n_pentane \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord$C5H12_n_pentane\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord$C5H12_n_pentane res;
end Modelica.Media.IdealGases.Common.DataRecord$C5H12_n_pentane;
function Modelica.Media.IdealGases.Common.DataRecord$C6H12_1_hexene \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord$C6H12_1_hexene\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord$C6H12_1_hexene res;
end Modelica.Media.IdealGases.Common.DataRecord$C6H12_1_hexene;
function Modelica.Media.IdealGases.Common.DataRecord$C6H14_n_hexane \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord$C6H14_n_hexane\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord$C6H14_n_hexane res;
end Modelica.Media.IdealGases.Common.DataRecord$C6H14_n_hexane;
function Modelica.Media.IdealGases.Common.DataRecord$C6H6 \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord$C6H6\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord$C6H6 res;
end Modelica.Media.IdealGases.Common.DataRecord$C6H6;
function Modelica.Media.IdealGases.Common.DataRecord$C7H14_1_heptene \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord$C7H14_1_heptene\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord$C7H14_1_heptene res;
end Modelica.Media.IdealGases.Common.DataRecord$C7H14_1_heptene;
function Modelica.Media.IdealGases.Common.DataRecord$C7H16_n_heptane \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord$C7H16_n_heptane\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord$C7H16_n_heptane res;
end Modelica.Media.IdealGases.Common.DataRecord$C7H16_n_heptane;
function Modelica.Media.IdealGases.Common.DataRecord$C8H10_ethylbenz \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord$C8H10_ethylbenz\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord$C8H10_ethylbenz res;
end Modelica.Media.IdealGases.Common.DataRecord$C8H10_ethylbenz;
function Modelica.Media.IdealGases.Common.DataRecord$C8H18_n_octane \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord$C8H18_n_octane\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord$C8H18_n_octane res;
end Modelica.Media.IdealGases.Common.DataRecord$C8H18_n_octane;
function Modelica.Media.IdealGases.Common.DataRecord$CH3OH \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord$CH3OH\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord$CH3OH res;
end Modelica.Media.IdealGases.Common.DataRecord$CH3OH;
function Modelica.Media.IdealGases.Common.DataRecord$CH4 \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord$CH4\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord$CH4 res;
end Modelica.Media.IdealGases.Common.DataRecord$CH4;
function Modelica.Media.IdealGases.Common.DataRecord$CL2 \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord$CL2\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord$CL2 res;
end Modelica.Media.IdealGases.Common.DataRecord$CL2;
function Modelica.Media.IdealGases.Common.DataRecord$CO \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord$CO\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord$CO res;
end Modelica.Media.IdealGases.Common.DataRecord$CO;
function Modelica.Media.IdealGases.Common.DataRecord$CO2 \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord$CO2\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord$CO2 res;
end Modelica.Media.IdealGases.Common.DataRecord$CO2;
function Modelica.Media.IdealGases.Common.DataRecord$F2 \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord$F2\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord$F2 res;
end Modelica.Media.IdealGases.Common.DataRecord$F2;
function Modelica.Media.IdealGases.Common.DataRecord$H2 \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord$H2\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord$H2 res;
end Modelica.Media.IdealGases.Common.DataRecord$H2;
function Modelica.Media.IdealGases.Common.DataRecord$H2O \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord$H2O\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord$H2O res;
end Modelica.Media.IdealGases.Common.DataRecord$H2O;
function Modelica.Media.IdealGases.Common.DataRecord$He \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord$He\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord$He res;
end Modelica.Media.IdealGases.Common.DataRecord$He;
function Modelica.Media.IdealGases.Common.DataRecord$N2 \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord$N2\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord$N2 res;
end Modelica.Media.IdealGases.Common.DataRecord$N2;
function Modelica.Media.IdealGases.Common.DataRecord$N2O \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord$N2O\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord$N2O res;
end Modelica.Media.IdealGases.Common.DataRecord$N2O;
function Modelica.Media.IdealGases.Common.DataRecord$NH3 \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord$NH3\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord$NH3 res;
end Modelica.Media.IdealGases.Common.DataRecord$NH3;
function Modelica.Media.IdealGases.Common.DataRecord$NO \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord$NO\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord$NO res;
end Modelica.Media.IdealGases.Common.DataRecord$NO;
function Modelica.Media.IdealGases.Common.DataRecord$NO2 \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord$NO2\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord$NO2 res;
end Modelica.Media.IdealGases.Common.DataRecord$NO2;
function Modelica.Media.IdealGases.Common.DataRecord$Ne \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord$Ne\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord$Ne res;
end Modelica.Media.IdealGases.Common.DataRecord$Ne;
function Modelica.Media.IdealGases.Common.DataRecord$O2 \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord$O2\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord$O2 res;
end Modelica.Media.IdealGases.Common.DataRecord$O2;
function Modelica.Media.IdealGases.Common.DataRecord$SO2 \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord$SO2\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord$SO2 res;
end Modelica.Media.IdealGases.Common.DataRecord$SO2;
function Modelica.Media.IdealGases.Common.DataRecord$SO3 \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.DataRecord$SO3\"
input String name;
input Real MM(quantity = \"MolarMass\", unit = \"kg/mol\", min = 0.0);
input Real Hf(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real H0(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6);
input Real Tlimit(quantity = \"ThermodynamicTemperature\", unit = \"K\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0, displayUnit = \"degC\");
input Real[7] alow;
input Real[2] blow;
input Real[7] ahigh;
input Real[2] bhigh;
input Real R(quantity = \"SpecificHeatCapacity\", unit = \"J/(kg.K)\");
output DataRecord$SO3 res;
end Modelica.Media.IdealGases.Common.DataRecord$SO3;
function Modelica.Media.IdealGases.Common.SingleGasNasa.FluidConstants \"Automatically generated record constructor for Modelica.Media.IdealGases.Common.SingleGasNasa.FluidConstants\"
input String iupacName;
input String casRegistryNumber;
input String chemicalFormula;
input String structureFormula;
input Real molarMass(min = 0.001, max = 0.25, nominal = 0.032, quantity = \"MolarMass\", unit = \"kg/mol\");
input Real criticalTemperature(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
input Real criticalPressure(min = 0.0, max = 1e8, nominal = 1e5, start = 1e5, quantity = \"Pressure\", unit = \"Pa\", displayUnit = \"bar\");
input Real criticalMolarVolume(min = 1e-6, max = 1e6, nominal = 1.0, quantity = \"MolarVolume\", unit = \"m3/mol\");
input Real acentricFactor;
input Real meltingPoint(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
input Real normalBoilingPoint(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
input Real dipoleMoment(min = 0.0, max = 2.0, unit = \"debye\", quantity = \"ElectricDipoleMoment\");
input Boolean hasIdealGasHeatCapacity = false;
input Boolean hasCriticalData = false;
input Boolean hasDipoleMoment = false;
input Boolean hasFundamentalEquation = false;
input Boolean hasLiquidHeatCapacity = false;
input Boolean hasSolidHeatCapacity = false;
input Boolean hasAccurateViscosityData = false;
input Boolean hasAccurateConductivityData = false;
input Boolean hasVapourPressureCurve = false;
input Boolean hasAcentricFactor = false;
input Real HCRIT0(min = -1e8, max = 1e8, nominal = 1e6, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
input Real SCRIT0(min = -1e6, max = 1e6, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
input Real deltah(min = -1e8, max = 1e8, nominal = 1e6, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
input Real deltas(min = -1e6, max = 1e6, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
output FluidConstants res;
end Modelica.Media.IdealGases.Common.SingleGasNasa.FluidConstants;
function Modelica.Media.IdealGases.Common.SingleGasNasa.h_T \"Compute specific enthalpy from temperature and gas data; reference is decided by the
refChoice input, or by the referenceChoice package constant by default\"
input Modelica.Media.IdealGases.Common.DataRecord data \"Ideal gas data\";
input Real T(quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0) \"Temperature\";
input Boolean exclEnthForm = true \"If true, enthalpy of formation Hf is not included in specific enthalpy h\";
input enumeration(ZeroAt0K, ZeroAt25C, UserDefined) refChoice = Modelica.Media.IdealGases.Common.SingleGasNasa.Choices.ReferenceEnthalpy.ZeroAt0K \"Choice of reference enthalpy\";
input Real h_off(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6) = 0.0 \"User defined offset for reference enthalpy, if referenceChoice = UserDefined\";
output Real h(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6) \"Specific enthalpy at temperature T\";
algorithm
h := smooth(0, (if T < data.Tlimit then data.R * (T * (data.blow[1] + data.alow[2] * log(T) + T * (data.alow[3] + T * (0.5 * data.alow[4] + T * (0.3333333333333333 * data.alow[5] + T * (0.25 * data.alow[6] + 0.2 * data.alow[7] * T))))) - data.alow[1]) / T else data.R * (T * (data.bhigh[1] + data.ahigh[2] * log(T) + T * (data.ahigh[3] + T * (0.5 * data.ahigh[4] + T * (0.3333333333333333 * data.ahigh[5] + T * (0.25 * data.ahigh[6] + 0.2 * data.ahigh[7] * T))))) - data.ahigh[1]) / T) + (if exclEnthForm then -data.Hf else 0.0) + (if refChoice == Modelica.Media.Interfaces.PartialMedium.Choices.ReferenceEnthalpy.ZeroAt0K then data.H0 else 0.0) + (if refChoice == Modelica.Media.Interfaces.PartialMedium.Choices.ReferenceEnthalpy.UserDefined then h_off else 0.0));
end Modelica.Media.IdealGases.Common.SingleGasNasa.h_T;
function Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants \"Automatically generated record constructor for Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants\"
input String iupacName;
input String casRegistryNumber;
input String chemicalFormula;
input String structureFormula;
input Real molarMass(min = 0.001, max = 0.25, nominal = 0.032, quantity = \"MolarMass\", unit = \"kg/mol\");
input Real criticalTemperature(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
input Real criticalPressure(min = 0.0, max = 1e8, nominal = 1e5, start = 1e5, quantity = \"Pressure\", unit = \"Pa\", displayUnit = \"bar\");
input Real criticalMolarVolume(min = 1e-6, max = 1e6, nominal = 1.0, quantity = \"MolarVolume\", unit = \"m3/mol\");
input Real acentricFactor;
input Real meltingPoint(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
input Real normalBoilingPoint(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
input Real dipoleMoment(min = 0.0, max = 2.0, unit = \"debye\", quantity = \"ElectricDipoleMoment\");
input Boolean hasIdealGasHeatCapacity = false;
input Boolean hasCriticalData = false;
input Boolean hasDipoleMoment = false;
input Boolean hasFundamentalEquation = false;
input Boolean hasLiquidHeatCapacity = false;
input Boolean hasSolidHeatCapacity = false;
input Boolean hasAccurateViscosityData = false;
input Boolean hasAccurateConductivityData = false;
input Boolean hasVapourPressureCurve = false;
input Boolean hasAcentricFactor = false;
input Real HCRIT0(min = -1e8, max = 1e8, nominal = 1e6, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
input Real SCRIT0(min = -1e6, max = 1e6, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
input Real deltah(min = -1e8, max = 1e8, nominal = 1e6, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
input Real deltas(min = -1e6, max = 1e6, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
output FluidConstants res;
end Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants;
function Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants$CO \"Automatically generated record constructor for Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants$CO\"
input String iupacName;
input String casRegistryNumber;
input String chemicalFormula;
input String structureFormula;
input Real molarMass(min = 0.001, max = 0.25, nominal = 0.032, quantity = \"MolarMass\", unit = \"kg/mol\");
input Real criticalTemperature(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
input Real criticalPressure(min = 0.0, max = 1e8, nominal = 1e5, start = 1e5, quantity = \"Pressure\", unit = \"Pa\", displayUnit = \"bar\");
input Real criticalMolarVolume(min = 1e-6, max = 1e6, nominal = 1.0, quantity = \"MolarVolume\", unit = \"m3/mol\");
input Real acentricFactor;
input Real meltingPoint(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
input Real normalBoilingPoint(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
input Real dipoleMoment(min = 0.0, max = 2.0, unit = \"debye\", quantity = \"ElectricDipoleMoment\");
input Boolean hasIdealGasHeatCapacity = false;
input Boolean hasCriticalData = false;
input Boolean hasDipoleMoment = false;
input Boolean hasFundamentalEquation = false;
input Boolean hasLiquidHeatCapacity = false;
input Boolean hasSolidHeatCapacity = false;
input Boolean hasAccurateViscosityData = false;
input Boolean hasAccurateConductivityData = false;
input Boolean hasVapourPressureCurve = false;
input Boolean hasAcentricFactor = false;
input Real HCRIT0(min = -1e8, max = 1e8, nominal = 1e6, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
input Real SCRIT0(min = -1e6, max = 1e6, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
input Real deltah(min = -1e8, max = 1e8, nominal = 1e6, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
input Real deltas(min = -1e6, max = 1e6, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
output FluidConstants$CO res;
end Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants$CO;
function Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants$CO2 \"Automatically generated record constructor for Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants$CO2\"
input String iupacName;
input String casRegistryNumber;
input String chemicalFormula;
input String structureFormula;
input Real molarMass(min = 0.001, max = 0.25, nominal = 0.032, quantity = \"MolarMass\", unit = \"kg/mol\");
input Real criticalTemperature(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
input Real criticalPressure(min = 0.0, max = 1e8, nominal = 1e5, start = 1e5, quantity = \"Pressure\", unit = \"Pa\", displayUnit = \"bar\");
input Real criticalMolarVolume(min = 1e-6, max = 1e6, nominal = 1.0, quantity = \"MolarVolume\", unit = \"m3/mol\");
input Real acentricFactor;
input Real meltingPoint(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
input Real normalBoilingPoint(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
input Real dipoleMoment(min = 0.0, max = 2.0, unit = \"debye\", quantity = \"ElectricDipoleMoment\");
input Boolean hasIdealGasHeatCapacity = false;
input Boolean hasCriticalData = false;
input Boolean hasDipoleMoment = false;
input Boolean hasFundamentalEquation = false;
input Boolean hasLiquidHeatCapacity = false;
input Boolean hasSolidHeatCapacity = false;
input Boolean hasAccurateViscosityData = false;
input Boolean hasAccurateConductivityData = false;
input Boolean hasVapourPressureCurve = false;
input Boolean hasAcentricFactor = false;
input Real HCRIT0(min = -1e8, max = 1e8, nominal = 1e6, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
input Real SCRIT0(min = -1e6, max = 1e6, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
input Real deltah(min = -1e8, max = 1e8, nominal = 1e6, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
input Real deltas(min = -1e6, max = 1e6, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
output FluidConstants$CO2 res;
end Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants$CO2;
function Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants$H2 \"Automatically generated record constructor for Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants$H2\"
input String iupacName;
input String casRegistryNumber;
input String chemicalFormula;
input String structureFormula;
input Real molarMass(min = 0.001, max = 0.25, nominal = 0.032, quantity = \"MolarMass\", unit = \"kg/mol\");
input Real criticalTemperature(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
input Real criticalPressure(min = 0.0, max = 1e8, nominal = 1e5, start = 1e5, quantity = \"Pressure\", unit = \"Pa\", displayUnit = \"bar\");
input Real criticalMolarVolume(min = 1e-6, max = 1e6, nominal = 1.0, quantity = \"MolarVolume\", unit = \"m3/mol\");
input Real acentricFactor;
input Real meltingPoint(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
input Real normalBoilingPoint(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
input Real dipoleMoment(min = 0.0, max = 2.0, unit = \"debye\", quantity = \"ElectricDipoleMoment\");
input Boolean hasIdealGasHeatCapacity = false;
input Boolean hasCriticalData = false;
input Boolean hasDipoleMoment = false;
input Boolean hasFundamentalEquation = false;
input Boolean hasLiquidHeatCapacity = false;
input Boolean hasSolidHeatCapacity = false;
input Boolean hasAccurateViscosityData = false;
input Boolean hasAccurateConductivityData = false;
input Boolean hasVapourPressureCurve = false;
input Boolean hasAcentricFactor = false;
input Real HCRIT0(min = -1e8, max = 1e8, nominal = 1e6, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
input Real SCRIT0(min = -1e6, max = 1e6, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
input Real deltah(min = -1e8, max = 1e8, nominal = 1e6, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
input Real deltas(min = -1e6, max = 1e6, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
output FluidConstants$H2 res;
end Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants$H2;
function Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants$H2O \"Automatically generated record constructor for Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants$H2O\"
input String iupacName;
input String casRegistryNumber;
input String chemicalFormula;
input String structureFormula;
input Real molarMass(min = 0.001, max = 0.25, nominal = 0.032, quantity = \"MolarMass\", unit = \"kg/mol\");
input Real criticalTemperature(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
input Real criticalPressure(min = 0.0, max = 1e8, nominal = 1e5, start = 1e5, quantity = \"Pressure\", unit = \"Pa\", displayUnit = \"bar\");
input Real criticalMolarVolume(min = 1e-6, max = 1e6, nominal = 1.0, quantity = \"MolarVolume\", unit = \"m3/mol\");
input Real acentricFactor;
input Real meltingPoint(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
input Real normalBoilingPoint(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
input Real dipoleMoment(min = 0.0, max = 2.0, unit = \"debye\", quantity = \"ElectricDipoleMoment\");
input Boolean hasIdealGasHeatCapacity = false;
input Boolean hasCriticalData = false;
input Boolean hasDipoleMoment = false;
input Boolean hasFundamentalEquation = false;
input Boolean hasLiquidHeatCapacity = false;
input Boolean hasSolidHeatCapacity = false;
input Boolean hasAccurateViscosityData = false;
input Boolean hasAccurateConductivityData = false;
input Boolean hasVapourPressureCurve = false;
input Boolean hasAcentricFactor = false;
input Real HCRIT0(min = -1e8, max = 1e8, nominal = 1e6, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
input Real SCRIT0(min = -1e6, max = 1e6, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
input Real deltah(min = -1e8, max = 1e8, nominal = 1e6, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
input Real deltas(min = -1e6, max = 1e6, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
output FluidConstants$H2O res;
end Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants$H2O;
function Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants$N2 \"Automatically generated record constructor for Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants$N2\"
input String iupacName;
input String casRegistryNumber;
input String chemicalFormula;
input String structureFormula;
input Real molarMass(min = 0.001, max = 0.25, nominal = 0.032, quantity = \"MolarMass\", unit = \"kg/mol\");
input Real criticalTemperature(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
input Real criticalPressure(min = 0.0, max = 1e8, nominal = 1e5, start = 1e5, quantity = \"Pressure\", unit = \"Pa\", displayUnit = \"bar\");
input Real criticalMolarVolume(min = 1e-6, max = 1e6, nominal = 1.0, quantity = \"MolarVolume\", unit = \"m3/mol\");
input Real acentricFactor;
input Real meltingPoint(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
input Real normalBoilingPoint(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
input Real dipoleMoment(min = 0.0, max = 2.0, unit = \"debye\", quantity = \"ElectricDipoleMoment\");
input Boolean hasIdealGasHeatCapacity = false;
input Boolean hasCriticalData = false;
input Boolean hasDipoleMoment = false;
input Boolean hasFundamentalEquation = false;
input Boolean hasLiquidHeatCapacity = false;
input Boolean hasSolidHeatCapacity = false;
input Boolean hasAccurateViscosityData = false;
input Boolean hasAccurateConductivityData = false;
input Boolean hasVapourPressureCurve = false;
input Boolean hasAcentricFactor = false;
input Real HCRIT0(min = -1e8, max = 1e8, nominal = 1e6, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
input Real SCRIT0(min = -1e6, max = 1e6, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
input Real deltah(min = -1e8, max = 1e8, nominal = 1e6, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
input Real deltas(min = -1e6, max = 1e6, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
output FluidConstants$N2 res;
end Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants$N2;
function Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants$O2 \"Automatically generated record constructor for Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants$O2\"
input String iupacName;
input String casRegistryNumber;
input String chemicalFormula;
input String structureFormula;
input Real molarM
...[truncated 63164 chars]...
, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
input Real dipoleMoment(min = 0.0, max = 2.0, unit = \"debye\", quantity = \"ElectricDipoleMoment\");
input Boolean hasIdealGasHeatCapacity = false;
input Boolean hasCriticalData = false;
input Boolean hasDipoleMoment = false;
input Boolean hasFundamentalEquation = false;
@@ -597,29 +597,29 @@
input Boolean hasSolidHeatCapacity = false;
input Boolean hasAccurateViscosityData = false;
input Boolean hasAccurateConductivityData = false;
input Boolean hasVapourPressureCurve = false;
input Boolean hasAcentricFactor = false;
-input Real HCRIT0(min = -100000000.0, max = 100000000.0, nominal = 1000000.0, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
-input Real SCRIT0(min = -1000000.0, max = 1000000.0, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
-input Real deltah(min = -100000000.0, max = 100000000.0, nominal = 1000000.0, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
-input Real deltas(min = -1000000.0, max = 1000000.0, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
+input Real HCRIT0(min = -1e8, max = 1e8, nominal = 1e6, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
+input Real SCRIT0(min = -1e6, max = 1e6, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
+input Real deltah(min = -1e8, max = 1e8, nominal = 1e6, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
+input Real deltas(min = -1e6, max = 1e6, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
output FluidConstants res;
end Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants;
function Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants$CO \"Automatically generated record constructor for Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants$CO\"
input String iupacName;
input String casRegistryNumber;
input String chemicalFormula;
input String structureFormula;
input Real molarMass(min = 0.001, max = 0.25, nominal = 0.032, quantity = \"MolarMass\", unit = \"kg/mol\");
-input Real criticalTemperature(min = 1.0, max = 10000.0, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
-input Real criticalPressure(min = 0.0, max = 100000000.0, nominal = 100000.0, start = 100000.0, quantity = \"Pressure\", unit = \"Pa\", displayUnit = \"bar\");
-input Real criticalMolarVolume(min = 1e-06, max = 1000000.0, nominal = 1.0, quantity = \"MolarVolume\", unit = \"m3/mol\");
+input Real criticalTemperature(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
+input Real criticalPressure(min = 0.0, max = 1e8, nominal = 1e5, start = 1e5, quantity = \"Pressure\", unit = \"Pa\", displayUnit = \"bar\");
+input Real criticalMolarVolume(min = 1e-6, max = 1e6, nominal = 1.0, quantity = \"MolarVolume\", unit = \"m3/mol\");
input Real acentricFactor;
-input Real meltingPoint(min = 1.0, max = 10000.0, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
-input Real normalBoilingPoint(min = 1.0, max = 10000.0, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
+input Real meltingPoint(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
+input Real normalBoilingPoint(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
input Real dipoleMoment(min = 0.0, max = 2.0, unit = \"debye\", quantity = \"ElectricDipoleMoment\");
input Boolean hasIdealGasHeatCapacity = false;
input Boolean hasCriticalData = false;
input Boolean hasDipoleMoment = false;
input Boolean hasFundamentalEquation = false;
@@ -627,29 +627,29 @@
input Boolean hasSolidHeatCapacity = false;
input Boolean hasAccurateViscosityData = false;
input Boolean hasAccurateConductivityData = false;
input Boolean hasVapourPressureCurve = false;
input Boolean hasAcentricFactor = false;
-input Real HCRIT0(min = -100000000.0, max = 100000000.0, nominal = 1000000.0, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
-input Real SCRIT0(min = -1000000.0, max = 1000000.0, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
-input Real deltah(min = -100000000.0, max = 100000000.0, nominal = 1000000.0, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
-input Real deltas(min = -1000000.0, max = 1000000.0, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
+input Real HCRIT0(min = -1e8, max = 1e8, nominal = 1e6, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
+input Real SCRIT0(min = -1e6, max = 1e6, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
+input Real deltah(min = -1e8, max = 1e8, nominal = 1e6, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
+input Real deltas(min = -1e6, max = 1e6, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
output FluidConstants$CO res;
end Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants$CO;
function Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants$CO2 \"Automatically generated record constructor for Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants$CO2\"
input String iupacName;
input String casRegistryNumber;
input String chemicalFormula;
input String structureFormula;
input Real molarMass(min = 0.001, max = 0.25, nominal = 0.032, quantity = \"MolarMass\", unit = \"kg/mol\");
-input Real criticalTemperature(min = 1.0, max = 10000.0, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
-input Real criticalPressure(min = 0.0, max = 100000000.0, nominal = 100000.0, start = 100000.0, quantity = \"Pressure\", unit = \"Pa\", displayUnit = \"bar\");
-input Real criticalMolarVolume(min = 1e-06, max = 1000000.0, nominal = 1.0, quantity = \"MolarVolume\", unit = \"m3/mol\");
+input Real criticalTemperature(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
+input Real criticalPressure(min = 0.0, max = 1e8, nominal = 1e5, start = 1e5, quantity = \"Pressure\", unit = \"Pa\", displayUnit = \"bar\");
+input Real criticalMolarVolume(min = 1e-6, max = 1e6, nominal = 1.0, quantity = \"MolarVolume\", unit = \"m3/mol\");
input Real acentricFactor;
-input Real meltingPoint(min = 1.0, max = 10000.0, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
-input Real normalBoilingPoint(min = 1.0, max = 10000.0, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
+input Real meltingPoint(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
+input Real normalBoilingPoint(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
input Real dipoleMoment(min = 0.0, max = 2.0, unit = \"debye\", quantity = \"ElectricDipoleMoment\");
input Boolean hasIdealGasHeatCapacity = false;
input Boolean hasCriticalData = false;
input Boolean hasDipoleMoment = false;
input Boolean hasFundamentalEquation = false;
@@ -657,29 +657,29 @@
input Boolean hasSolidHeatCapacity = false;
input Boolean hasAccurateViscosityData = false;
input Boolean hasAccurateConductivityData = false;
input Boolean hasVapourPressureCurve = false;
input Boolean hasAcentricFactor = false;
-input Real HCRIT0(min = -100000000.0, max = 100000000.0, nominal = 1000000.0, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
-input Real SCRIT0(min = -1000000.0, max = 1000000.0, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
-input Real deltah(min = -100000000.0, max = 100000000.0, nominal = 1000000.0, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
-input Real deltas(min = -1000000.0, max = 1000000.0, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
+input Real HCRIT0(min = -1e8, max = 1e8, nominal = 1e6, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
+input Real SCRIT0(min = -1e6, max = 1e6, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
+input Real deltah(min = -1e8, max = 1e8, nominal = 1e6, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
+input Real deltas(min = -1e6, max = 1e6, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
output FluidConstants$CO2 res;
end Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants$CO2;
function Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants$H2 \"Automatically generated record constructor for Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants$H2\"
input String iupacName;
input String casRegistryNumber;
input String chemicalFormula;
input String structureFormula;
input Real molarMass(min = 0.001, max = 0.25, nominal = 0.032, quantity = \"MolarMass\", unit = \"kg/mol\");
-input Real criticalTemperature(min = 1.0, max = 10000.0, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
-input Real criticalPressure(min = 0.0, max = 100000000.0, nominal = 100000.0, start = 100000.0, quantity = \"Pressure\", unit = \"Pa\", displayUnit = \"bar\");
-input Real criticalMolarVolume(min = 1e-06, max = 1000000.0, nominal = 1.0, quantity = \"MolarVolume\", unit = \"m3/mol\");
+input Real criticalTemperature(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
+input Real criticalPressure(min = 0.0, max = 1e8, nominal = 1e5, start = 1e5, quantity = \"Pressure\", unit = \"Pa\", displayUnit = \"bar\");
+input Real criticalMolarVolume(min = 1e-6, max = 1e6, nominal = 1.0, quantity = \"MolarVolume\", unit = \"m3/mol\");
input Real acentricFactor;
-input Real meltingPoint(min = 1.0, max = 10000.0, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
-input Real normalBoilingPoint(min = 1.0, max = 10000.0, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
+input Real meltingPoint(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
+input Real normalBoilingPoint(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
input Real dipoleMoment(min = 0.0, max = 2.0, unit = \"debye\", quantity = \"ElectricDipoleMoment\");
input Boolean hasIdealGasHeatCapacity = false;
input Boolean hasCriticalData = false;
input Boolean hasDipoleMoment = false;
input Boolean hasFundamentalEquation = false;
@@ -687,29 +687,29 @@
input Boolean hasSolidHeatCapacity = false;
input Boolean hasAccurateViscosityData = false;
input Boolean hasAccurateConductivityData = false;
input Boolean hasVapourPressureCurve = false;
input Boolean hasAcentricFactor = false;
-input Real HCRIT0(min = -100000000.0, max = 100000000.0, nominal = 1000000.0, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
-input Real SCRIT0(min = -1000000.0, max = 1000000.0, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
-input Real deltah(min = -100000000.0, max = 100000000.0, nominal = 1000000.0, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
-input Real deltas(min = -1000000.0, max = 1000000.0, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
+input Real HCRIT0(min = -1e8, max = 1e8, nominal = 1e6, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
+input Real SCRIT0(min = -1e6, max = 1e6, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
+input Real deltah(min = -1e8, max = 1e8, nominal = 1e6, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
+input Real deltas(min = -1e6, max = 1e6, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
output FluidConstants$H2 res;
end Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants$H2;
function Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants$H2O \"Automatically generated record constructor for Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants$H2O\"
input String iupacName;
input String casRegistryNumber;
input String chemicalFormula;
input String structureFormula;
input Real molarMass(min = 0.001, max = 0.25, nominal = 0.032, quantity = \"MolarMass\", unit = \"kg/mol\");
-input Real criticalTemperature(min = 1.0, max = 10000.0, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
-input Real criticalPressure(min = 0.0, max = 100000000.0, nominal = 100000.0, start = 100000.0, quantity = \"Pressure\", unit = \"Pa\", displayUnit = \"bar\");
-input Real criticalMolarVolume(min = 1e-06, max = 1000000.0, nominal = 1.0, quantity = \"MolarVolume\", unit = \"m3/mol\");
+input Real criticalTemperature(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
+input Real criticalPressure(min = 0.0, max = 1e8, nominal = 1e5, start = 1e5, quantity = \"Pressure\", unit = \"Pa\", displayUnit = \"bar\");
+input Real criticalMolarVolume(min = 1e-6, max = 1e6, nominal = 1.0, quantity = \"MolarVolume\", unit = \"m3/mol\");
input Real acentricFactor;
-input Real meltingPoint(min = 1.0, max = 10000.0, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
-input Real normalBoilingPoint(min = 1.0, max = 10000.0, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
+input Real meltingPoint(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
+input Real normalBoilingPoint(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
input Real dipoleMoment(min = 0.0, max = 2.0, unit = \"debye\", quantity = \"ElectricDipoleMoment\");
input Boolean hasIdealGasHeatCapacity = false;
input Boolean hasCriticalData = false;
input Boolean hasDipoleMoment = false;
input Boolean hasFundamentalEquation = false;
@@ -717,29 +717,29 @@
input Boolean hasSolidHeatCapacity = false;
input Boolean hasAccurateViscosityData = false;
input Boolean hasAccurateConductivityData = false;
input Boolean hasVapourPressureCurve = false;
input Boolean hasAcentricFactor = false;
-input Real HCRIT0(min = -100000000.0, max = 100000000.0, nominal = 1000000.0, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
-input Real SCRIT0(min = -1000000.0, max = 1000000.0, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
-input Real deltah(min = -100000000.0, max = 100000000.0, nominal = 1000000.0, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
-input Real deltas(min = -1000000.0, max = 1000000.0, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
+input Real HCRIT0(min = -1e8, max = 1e8, nominal = 1e6, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
+input Real SCRIT0(min = -1e6, max = 1e6, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
+input Real deltah(min = -1e8, max = 1e8, nominal = 1e6, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
+input Real deltas(min = -1e6, max = 1e6, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
output FluidConstants$H2O res;
end Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants$H2O;
function Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants$N2 \"Automatically generated record constructor for Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants$N2\"
input String iupacName;
input String casRegistryNumber;
input String chemicalFormula;
input String structureFormula;
input Real molarMass(min = 0.001, max = 0.25, nominal = 0.032, quantity = \"MolarMass\", unit = \"kg/mol\");
-input Real criticalTemperature(min = 1.0, max = 10000.0, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
-input Real criticalPressure(min = 0.0, max = 100000000.0, nominal = 100000.0, start = 100000.0, quantity = \"Pressure\", unit = \"Pa\", displayUnit = \"bar\");
-input Real criticalMolarVolume(min = 1e-06, max = 1000000.0, nominal = 1.0, quantity = \"MolarVolume\", unit = \"m3/mol\");
+input Real criticalTemperature(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
+input Real criticalPressure(min = 0.0, max = 1e8, nominal = 1e5, start = 1e5, quantity = \"Pressure\", unit = \"Pa\", displayUnit = \"bar\");
+input Real criticalMolarVolume(min = 1e-6, max = 1e6, nominal = 1.0, quantity = \"MolarVolume\", unit = \"m3/mol\");
input Real acentricFactor;
-input Real meltingPoint(min = 1.0, max = 10000.0, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
-input Real normalBoilingPoint(min = 1.0, max = 10000.0, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
+input Real meltingPoint(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
+input Real normalBoilingPoint(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
input Real dipoleMoment(min = 0.0, max = 2.0, unit = \"debye\", quantity = \"ElectricDipoleMoment\");
input Boolean hasIdealGasHeatCapacity = false;
input Boolean hasCriticalData = false;
input Boolean hasDipoleMoment = false;
input Boolean hasFundamentalEquation = false;
@@ -747,29 +747,29 @@
input Boolean hasSolidHeatCapacity = false;
input Boolean hasAccurateViscosityData = false;
input Boolean hasAccurateConductivityData = false;
input Boolean hasVapourPressureCurve = false;
input Boolean hasAcentricFactor = false;
-input Real HCRIT0(min = -100000000.0, max = 100000000.0, nominal = 1000000.0, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
-input Real SCRIT0(min = -1000000.0, max = 1000000.0, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
-input Real deltah(min = -100000000.0, max = 100000000.0, nominal = 1000000.0, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
-input Real deltas(min = -1000000.0, max = 1000000.0, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
+input Real HCRIT0(min = -1e8, max = 1e8, nominal = 1e6, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
+input Real SCRIT0(min = -1e6, max = 1e6, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
+input Real deltah(min = -1e8, max = 1e8, nominal = 1e6, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
+input Real deltas(min = -1e6, max = 1e6, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
output FluidConstants$N2 res;
end Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants$N2;
function Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants$O2 \"Automatically generated record constructor for Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants$O2\"
input String iupacName;
input String casRegistryNumber;
input String chemicalFormula;
input String structureFormula;
input Real molarMass(min = 0.001, max = 0.25, nominal = 0.032, quantity = \"MolarMass\", unit = \"kg/mol\");
-input Real criticalTemperature(min = 1.0, max = 10000.0, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
-input Real criticalPressure(min = 0.0, max = 100000000.0, nominal = 100000.0, start = 100000.0, quantity = \"Pressure\", unit = \"Pa\", displayUnit = \"bar\");
-input Real criticalMolarVolume(min = 1e-06, max = 1000000.0, nominal = 1.0, quantity = \"MolarVolume\", unit = \"m3/mol\");
+input Real criticalTemperature(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
+input Real criticalPressure(min = 0.0, max = 1e8, nominal = 1e5, start = 1e5, quantity = \"Pressure\", unit = \"Pa\", displayUnit = \"bar\");
+input Real criticalMolarVolume(min = 1e-6, max = 1e6, nominal = 1.0, quantity = \"MolarVolume\", unit = \"m3/mol\");
input Real acentricFactor;
-input Real meltingPoint(min = 1.0, max = 10000.0, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
-input Real normalBoilingPoint(min = 1.0, max = 10000.0, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
+input Real meltingPoint(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
+input Real normalBoilingPoint(min = 1.0, max = 1e4, nominal = 300.0, start = 300.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
input Real dipoleMoment(min = 0.0, max = 2.0, unit = \"debye\", quantity = \"ElectricDipoleMoment\");
input Boolean hasIdealGasHeatCapacity = false;
input Boolean hasCriticalData = false;
input Boolean hasDipoleMoment = false;
input Boolean hasFundamentalEquation = false;
@@ -777,14 +777,14 @@
input Boolean hasSolidHeatCapacity = false;
input Boolean hasAccurateViscosityData = false;
input Boolean hasAccurateConductivityData = false;
input Boolean hasVapourPressureCurve = false;
input Boolean hasAcentricFactor = false;
-input Real HCRIT0(min = -100000000.0, max = 100000000.0, nominal = 1000000.0, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
-input Real SCRIT0(min = -1000000.0, max = 1000000.0, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
-input Real deltah(min = -100000000.0, max = 100000000.0, nominal = 1000000.0, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
-input Real deltas(min = -1000000.0, max = 1000000.0, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
+input Real HCRIT0(min = -1e8, max = 1e8, nominal = 1e6, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
+input Real SCRIT0(min = -1e6, max = 1e6, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
+input Real deltah(min = -1e8, max = 1e8, nominal = 1e6, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
+input Real deltas(min = -1e6, max = 1e6, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
output FluidConstants$O2 res;
end Modelica.Media.Interfaces.PartialMixtureMedium.FluidConstants$O2;
function Modelica.SIunits.Conversions.from_degC \"Convert from Celsius to Kelvin\"
input Real Celsius(quantity = \"ThermodynamicTemperature\", unit = \"degC\") \"Celsius value\";
@@ -797,16 +797,16 @@
input String iupacName;
input String casRegistryNumber;
input String chemicalFormula;
input String structureFormula;
input Real molarMass(min = 0.001, max = 0.25, nominal = 0.032, quantity = \"MolarMass\", unit = \"kg/mol\");
-input Real criticalTemperature(start = 500.0, nominal = 500.0, min = 1.0, max = 10000.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
-input Real criticalPressure(start = 1000000.0, nominal = 1000000.0, min = 0.0, max = 100000000.0, quantity = \"Pressure\", unit = \"Pa\", displayUnit = \"bar\");
-input Real criticalMolarVolume(min = 1e-06, max = 1000000.0, nominal = 1.0, quantity = \"MolarVolume\", unit = \"m3/mol\");
+input Real criticalTemperature(start = 500.0, nominal = 500.0, min = 1.0, max = 1e4, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
+input Real criticalPressure(start = 1e6, nominal = 1e6, min = 0.0, max = 1e8, quantity = \"Pressure\", unit = \"Pa\", displayUnit = \"bar\");
+input Real criticalMolarVolume(min = 1e-6, max = 1e6, nominal = 1.0, quantity = \"MolarVolume\", unit = \"m3/mol\");
input Real acentricFactor;
-input Real meltingPoint(start = 500.0, nominal = 500.0, min = 1.0, max = 10000.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
-input Real normalBoilingPoint(start = 500.0, nominal = 500.0, min = 1.0, max = 10000.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
+input Real meltingPoint(start = 500.0, nominal = 500.0, min = 1.0, max = 1e4, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
+input Real normalBoilingPoint(start = 500.0, nominal = 500.0, min = 1.0, max = 1e4, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
input Real dipoleMoment(min = 0.0, max = 2.0, unit = \"debye\", quantity = \"ElectricDipoleMoment\");
input Boolean hasIdealGasHeatCapacity = false;
input Boolean hasCriticalData = false;
input Boolean hasDipoleMoment = false;
input Boolean hasFundamentalEquation = false;
@@ -814,74 +814,74 @@
input Boolean hasSolidHeatCapacity = false;
input Boolean hasAccurateViscosityData = false;
input Boolean hasAccurateConductivityData = false;
input Boolean hasVapourPressureCurve = false;
input Boolean hasAcentricFactor = false;
-input Real HCRIT0(start = 300000.0, nominal = 100000.0, min = -100000000.0, max = 100000000.0, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
-input Real SCRIT0(min = -1000000.0, max = 1000000.0, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
-input Real deltah(start = 300000.0, nominal = 100000.0, min = -100000000.0, max = 100000000.0, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
-input Real deltas(min = -1000000.0, max = 1000000.0, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
+input Real HCRIT0(start = 3e5, nominal = 1e5, min = -1e8, max = 1e8, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
+input Real SCRIT0(min = -1e6, max = 1e6, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
+input Real deltah(start = 3e5, nominal = 1e5, min = -1e8, max = 1e8, quantity = \"SpecificEnergy\", unit = \"J/kg\") = 0.0;
+input Real deltas(min = -1e6, max = 1e6, nominal = 1000.0, quantity = \"SpecificEntropy\", unit = \"J/(kg.K)\") = 0.0;
output FluidConstants res;
end TestMedia.TestModels.TestFlueGas.Medium.FluidConstants;
function TestMedia.TestModels.TestFlueGas.Medium.ThermodynamicState \"Automatically generated record constructor for TestMedia.TestModels.TestFlueGas.Medium.ThermodynamicState\"
-input Real p(start = 1000000.0, nominal = 1000000.0, min = 0.0, max = 100000000.0, quantity = \"Pressure\", unit = \"Pa\", displayUnit = \"bar\");
-input Real T(start = 500.0, nominal = 500.0, min = 1.0, max = 10000.0, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
+input Real p(start = 1e6, nominal = 1e6, min = 0.0, max = 1e8, quantity = \"Pressure\", unit = \"Pa\", displayUnit = \"bar\");
+input Real T(start = 500.0, nominal = 500.0, min = 1.0, max = 1e4, quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\");
input Real[6] X(quantity = \"MassFraction\", unit = \"kg/kg\", min = 0.0, max = 1.0, nominal = 0.1);
output ThermodynamicState res;
end TestMedia.TestModels.TestFlueGas.Medium.ThermodynamicState;
function TestMedia.TestModels.TestFlueGas.Medium.density \"Return density of ideal gas\"
input TestMedia.TestModels.TestFlueGas.Medium.ThermodynamicState state \"thermodynamic state record\";
-output Real d(quantity = \"Density\", unit = \"kg/m3\", displayUnit = \"g/cm3\", min = 0.0, max = 100000.0, start = 10.0, nominal = 10.0) \"Density\";
+output Real d(quantity = \"Density\", unit = \"kg/m3\", displayUnit = \"g/cm3\", min = 0.0, max = 1e5, start = 10.0, nominal = 10.0) \"Density\";
algorithm
d := state.p / (state.T * (296.8033869505308 * state.X[1] + 4124.487568704486 * state.X[2] + 296.8383547363272 * state.X[3] + 259.8369938872708 * state.X[4] + 461.5233290850878 * state.X[5] + 188.9244822140674 * state.X[6]));
end TestMedia.TestModels.TestFlueGas.Medium.density;
function TestMedia.TestModels.TestFlueGas.Medium.h_TX \"Return specific enthalpy\"
input Real T(quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\", min = 1.0, max = 6000.0, start = 288.15, nominal = 300.0) \"Temperature\";
input Real[:] X(quantity = \"MassFraction\", unit = \"kg/kg\", min = 0.0, max = 1.0, nominal = 0.1) = {0.768, 0.0, 0.0, 0.232, 0.0, 0.0} \"Independent Mass fractions of gas mixture\";
input Boolean exclEnthForm = true \"If true, enthalpy of formation Hf is not included in specific enthalpy h\";
input enumeration(ZeroAt0K, ZeroAt25C, UserDefined) refChoice = Modelica.Media.Interfaces.PartialMedium.Choices.ReferenceEnthalpy.ZeroAt0K \"Choice of reference enthalpy\";
-input Real h_off(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1000000.0) = 0.0 \"User defined offset for reference enthalpy, if referenceChoice = UserDefined\";
-output Real h(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1000000.0) \"Specific enthalpy at temperature T\";
+input Real h_off(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6) = 0.0 \"User defined offset for reference enthalpy, if referenceChoice = UserDefined\";
+output Real h(quantity = \"SpecificEnergy\", unit = \"J/kg\", nominal = 1e6) \"Specific enthalpy at temperature T\";
algorithm
-h := X * {Modelica.Media.IdealGases.Common.SingleGasNasa.h_T(Modelica.Media.IdealGases.Common.DataRecord(\"N2\", 0.0280134, 0, 309498.4543111511, 1000, {22103.71497, -381.846182, 6.08273836, -0.00853091441, 1.384646189e-05, -9.62579362e-09, 2.519705809e-12}, {710.846086, -10.76003744}, {587712.406, -2239.249073, 6.06694922, -0.00061396855, 1.491806679e-07, -1.923105485e-11, 1.061954386e-15}, {12832.10415, -15.86640027}, 296.8033869505308), T, exclEnthForm, refChoice, h_off), Modelica.Media.IdealGases.Common.SingleGasNasa.h_T(Modelica.Media.IdealGases.Common.DataRecord(\"H2\", 0.00201588, 0, 4200697.462150524, 1000, {40783.2321, -800.918604, 8.21470201, -0.01269714457, 1.753605076e-05, -1.20286027e-08, 3.36809349e-12}, {2682.484665, -30.43788844}, {560812.801, -837.150474, 2.975364532, 0.001252249124, -3.74071619e-07, 5.936625200000001e-11, -3.6069941e-15}, {5339.82441, -2.202774769}, 4124.487568704486), T, exclEnthForm, refChoice, h_off), Modelica.Media.IdealGases.Common.SingleGasNasa.h_T(Modelica.Media.IdealGases.Common.DataRecord(\"CO\", 0.0280101, -3946262.098314536, 309570.6191695138, 1000, {14890.45326, -292.2285939, 5.72452717, -0.008176235030000001, 1.456903469e-05, -1.087746302e-08, 3.027941827e-12}, {-13031.31878, -7.85924135}, {461919.725, -1944.704863, 5.91671418, -0.0005664282830000001, 1.39881454e-07, -1.787680361e-11, 9.62093557e-16}, {-2466.261084, -13.87413108}, 296.8383547363272), T, exclEnthForm, refChoice, h_off), Modelica.Media.IdealGases.Common.SingleGasNasa.h_T(Modelica.Media.IdealGases.Common.DataRecord(\"O2\", 0.0319988, 0, 271263.4223783392, 1000, {-34255.6342, 484.700097, 1.119010961, 0.00429388924, -6.83630052e-07, -2.0233727e-09, 1.039040018e-12}, {-3391.45487, 18.4969947}, {-1037939.022, 2344.830282, 1.819732036, 0.001267847582, -2.188067988e-07, 2.053719572e-11, -8.193467050000001e-16}, {-16890.10929, 17.38716506}, 259.8369938872708), T, exclEnthForm, refChoice, h_off), Modelica.Media.IdealGases.Common.SingleGasNasa.h_T(Modelica.Media.IdealGases.Common.DataRecord(\"H2O\", 0.01801528, -13423382.81725291, 549760.6476280135, 1000, {-39479.6083, 575.5731019999999, 0.931782653, 0.00722271286, -7.34255737e-06, 4.95504349e-09, -1.336933246e-12}, {-33039.7431, 17.24205775}, {1034972.096, -2412.698562, 4.64611078, 0.002291998307, -6.836830479999999e-07, 9.426468930000001e-11, -4.82238053e-15}, {-13842.86509, -7.97814851}, 461.5233290850878), T, exclEnthForm, refChoice, h_off), Modelica.Media.IdealGases.Common.SingleGasNasa.h_T(Modelica.Media.IdealGases.Common.DataRecord(\"CO2\", 0.0440095, -8941478.544405185, 212805.6215135368, 1000, {49436.5054, -626.411601, 5.30172524, 0.002503813816, -2.127308728e-07, -7.68998878e-10, 2.849677801e-13}, {-45281.9846, -7.04827944}, {117696.2419, -1788.791477, 8.291523189999999, -9.22315678e-05, 4.86367688e-09, -1.891053312e-12, 6.330036589999999e-16}, {-39083.5059, -26.52669281}, 188.9244822140674), T, exclEnthForm, refChoice, h_off)};
+h := X * {Modelica.Media.IdealGases.Common.SingleGasNasa.h_T(Modelica.Media.IdealGases.Common.DataRecord(\"N2\", 0.0280134, 0, 309498.4543111511, 1000, {22103.71497, -381.846182, 6.08273836, -0.00853091441, 1.384646189e-5, -9.62579362e-9, 2.519705809e-12}, {710.846086, -10.76003744}, {587712.406, -2239.249073, 6.06694922, -6.1396855e-4, 1.491806679e-7, -1.923105485e-11, 1.061954386e-15}, {12832.10415, -15.86640027}, 296.8033869505308), T, exclEnthForm, refChoice, h_off), Modelica.Media.IdealGases.Common.SingleGasNasa.h_T(Modelica.Media.IdealGases.Common.DataRecord(\"H2\", 0.00201588, 0, 4.200697462150524e6, 1000, {40783.2321, -800.918604, 8.21470201, -0.01269714457, 1.753605076e-5, -1.20286027e-8, 3.36809349e-12}, {2682.484665, -30.43788844}, {560812.801, -837.150474, 2.975364532, 0.001252249124, -3.74071619e-7, 5.9366252e-11, -3.6069941e-15}, {5339.82441, -2.202774769}, 4124.487568704486), T, exclEnthForm, refChoice, h_off), Modelica.Media.IdealGases.Common.SingleGasNasa.h_T(Modelica.Media.IdealGases.Common.DataRecord(\"CO\", 0.0280101, -3.946262098314536e6, 309570.6191695138, 1000, {14890.45326, -292.2285939, 5.72452717, -0.008176235030000001, 1.456903469e-5, -1.087746302e-8, 3.027941827e-12}, {-13031.31878, -7.85924135}, {461919.725, -1944.704863, 5.91671418, -5.664282830000001e-4, 1.39881454e-7, -1.787680361e-11, 9.62093557e-16}, {-2466.261084, -13.87413108}, 296.8383547363272), T, exclEnthForm, refChoice, h_off), Modelica.Media.IdealGases.Common.SingleGasNasa.h_T(Modelica.Media.IdealGases.Common.DataRecord(\"O2\", 0.0319988, 0, 271263.4223783392, 1000, {-34255.6342, 484.700097, 1.119010961, 0.00429388924, -6.83630052e-7, -2.0233727e-9, 1.039040018e-12}, {-3391.45487, 18.4969947}, {-1.037939022e6, 2344.830282, 1.819732036, 0.001267847582, -2.188067988e-7, 2.053719572e-11, -8.193467050000001e-16}, {-16890.10929, 17.38716506}, 259.8369938872708), T, exclEnthForm, refChoice, h_off), Modelica.Media.IdealGases.Common.SingleGasNasa.h_T(Modelica.Media.IdealGases.Common.DataRecord(\"H2O\", 0.01801528, -1.342338281725291e7, 549760.6476280135, 1000, {-39479.6083, 575.573102, 0.931782653, 0.00722271286, -7.34255737e-6, 4.95504349e-9, -1.336933246e-12}, {-33039.7431, 17.24205775}, {1.034972096e6, -2412.698562, 4.64611078, 0.002291998307, -6.836830479999999e-7, 9.426468930000001e-11, -4.82238053e-15}, {-13842.86509, -7.97814851}, 461.5233290850878), T, exclEnthForm, refChoice, h_off), Modelica.Media.IdealGases.Common.SingleGasNasa.h_T(Modelica.Media.IdealGases.Common.DataRecord(\"CO2\", 0.0440095, -8.941478544405185e6, 212805.6215135368, 1000, {49436.5054, -626.411601, 5.30172524, 0.002503813816, -2.127308728e-7, -7.68998878e-10, 2.849677801e-13}, {-45281.9846, -7.04827944}, {117696.2419, -1788.791477, 8.29152319, -9.22315678e-5, 4.86367688e-9, -1.891053312e-12, 6.330036589999999e-16}, {-39083.5059, -26.52669281}, 188.9244822140674), T, exclEnthForm, refChoice, h_off)};
end TestMedia.TestModels.TestFlueGas.Medium.h_TX;
function TestMedia.TestModels.TestFlueGas.Medium.setState_pTX \"Return thermodynamic state as function of p, T and composition X\"
-input Real p(quantity = \"Pressure\", unit = \"Pa\", displayUnit = \"bar\", min = 0.0, max = 100000000.0, start = 1000000.0, nominal = 1000000.0) \"Pressure\";
-input Real T(quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\", min = 1.0, max = 10000.0, start = 500.0, nominal = 500.0) \"Temperature\";
+input Real p(quantity = \"Pressure\", unit = \"Pa\", displayUnit = \"bar\", min = 0.0, max = 1e8, start = 1e6, nominal = 1e6) \"Pressure\";
+input Real T(quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\", min = 1.0, max = 1e4, start = 500.0, nominal = 500.0) \"Temperature\";
input Real[:] X(quantity = \"MassFraction\", unit = \"kg/kg\", min = 0.0, max = 1.0, nominal = 0.1) = {0.768, 0.0, 0.0, 0.232, 0.0, 0.0} \"Mass fractions\";
output TestMedia.TestModels.TestFlueGas.Medium.ThermodynamicState state;
algorithm
state := if size(X, 1) == 6 then TestMedia.TestModels.TestFlueGas.Medium.ThermodynamicState(p, T, X) else TestMedia.TestModels.TestFlueGas.Medium.ThermodynamicState(p, T, cat(1, X, {1.0 - sum(X)}));
end TestMedia.TestModels.TestFlueGas.Medium.setState_pTX;
function TestMedia.TestModels.TestFlueGas.Medium.specificEnthalpy \"Return specific enthalpy\"
input TestMedia.TestModels.TestFlueGas.Medium.ThermodynamicState state \"thermodynamic state record\";
-output Real h(quantity = \"SpecificEnergy\", unit = \"J/kg\", min = -100000000.0, max = 100000000.0, start = 300000.0, nominal = 100000.0) \"Specific enthalpy\";
+output Real h(quantity = \"SpecificEnergy\", unit = \"J/kg\", min = -1e8, max = 1e8, start = 3e5, nominal = 1e5) \"Specific enthalpy\";
algorithm
h := TestMedia.TestModels.TestFlueGas.Medium.h_TX(state.T, {state.X[1], state.X[2], state.X[3], state.X[4], state.X[5], state.X[6]}, true, Modelica.Media.Interfaces.PartialMedium.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0);
end TestMedia.TestModels.TestFlueGas.Medium.specificEnthalpy;
class TestMedia.TestModels.TestFlueGas
-Real state.p(quantity = \"Pressure\", unit = \"Pa\", displayUnit = \"bar\", min = 0.0, max = 100000000.0, start = 1000000.0, nominal = 1000000.0) \"Absolute pressure of medium\";
-Real state.T(quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\", min = 1.0, max = 10000.0, start = 500.0, nominal = 500.0) \"Temperature of medium\";
+Real state.p(quantity = \"Pressure\", unit = \"Pa\", displayUnit = \"bar\", min = 0.0, max = 1e8, start = 1e6, nominal = 1e6) \"Absolute pressure of medium\";
+Real state.T(quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\", min = 1.0, max = 1e4, start = 500.0, nominal = 500.0) \"Temperature of medium\";
Real state.X[1](quantity = \"MassFraction\", unit = \"kg/kg\", min = 0.0, max = 1.0, nominal = 0.1) \"Mass fractions (= (component mass)/total mass m_i/m)\";
Real state.X[2](quantity = \"MassFraction\", unit = \"kg/kg\", min = 0.0, max = 1.0, nominal = 0.1) \"Mass fractions (= (component mass)/total mass m_i/m)\";
Real state.X[3](quantity = \"MassFraction\", unit = \"kg/kg\", min = 0.0, max = 1.0, nominal = 0.1) \"Mass fractions (= (component mass)/total mass m_i/m)\";
Real state.X[4](quantity = \"MassFraction\", unit = \"kg/kg\", min = 0.0, max = 1.0, nominal = 0.1) \"Mass fractions (= (component mass)/total mass m_i/m)\";
Real state.X[5](quantity = \"MassFraction\", unit = \"kg/kg\", min = 0.0, max = 1.0, nominal = 0.1) \"Mass fractions (= (component mass)/total mass m_i/m)\";
Real state.X[6](quantity = \"MassFraction\", unit = \"kg/kg\", min = 0.0, max = 1.0, nominal = 0.1) \"Mass fractions (= (component mass)/total mass m_i/m)\";
-Real p(quantity = \"Pressure\", unit = \"Pa\", displayUnit = \"bar\", min = 0.0, max = 100000000.0, start = 1000000.0, nominal = 1000000.0);
-Real h(quantity = \"SpecificEnergy\", unit = \"J/kg\", min = -100000000.0, max = 100000000.0, start = 300000.0, nominal = 100000.0);
-Real d(quantity = \"Density\", unit = \"kg/m3\", displayUnit = \"g/cm3\", min = 0.0, max = 100000.0, start = 10.0, nominal = 10.0);
-Real T(quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\", min = 1.0, max = 10000.0, start = 500.0, nominal = 500.0);
+Real p(quantity = \"Pressure\", unit = \"Pa\", displayUnit = \"bar\", min = 0.0, max = 1e8, start = 1e6, nominal = 1e6);
+Real h(quantity = \"SpecificEnergy\", unit = \"J/kg\", min = -1e8, max = 1e8, start = 3e5, nominal = 1e5);
+Real d(quantity = \"Density\", unit = \"kg/m3\", displayUnit = \"g/cm3\", min = 0.0, max = 1e5, start = 10.0, nominal = 10.0);
+Real T(quantity = \"ThermodynamicTemperature\", unit = \"K\", displayUnit = \"degC\", min = 1.0, max = 1e4, start = 500.0, nominal = 500.0);
equation
T = 300.0 + 300.0 * time;
-p = 100000.0;
+p = 1e5;
state = TestMedia.TestModels.TestFlueGas.Medium.setState_pTX(p, T, {0.768, 0.0, 0.0, 0.232, 0.0, 0.0});
d = TestMedia.TestModels.TestFlueGas.Medium.density(state);
h = TestMedia.TestModels.TestFlueGas.Medium.specificEnthalpy(state);
end TestMedia.TestModels.TestFlueGas;
"
@@ -889,12 +889,52 @@
"Check of TestMedia.TestModels.TestFlueGas completed successfully.
Class TestMedia.TestModels.TestFlueGas has 12 equation(s) and 12 variable(s).
2 of these are trivial equation(s)."
""
record SimulationResult
-resultFile = "TestMedia.TestModels.TestFlueGas_res.mat",
-simulationOptions = "startTime = 0.0, stopTime = 1.0, numberOfIntervals = 500, tolerance = 1e-06, method = 'dassl', fileNamePrefix = 'TestMedia.TestModels.TestFlueGas', options = '', outputFormat = 'mat', variableFilter = '.*', cflags = '', simflags = ''",
-messages = "LOG_SUCCESS | info | The initialization finished successfully without homotopy method.
-LOG_SUCCESS | info | The simulation finished successfully.
-"
+resultFile = "",
+simulationOptions = "startTime = 0.0, stopTime = 1.0, numberOfIntervals = 500, tolerance = 1e-6, method = 'dassl', fileNamePrefix = 'TestMedia.TestModels.TestFlueGas', options = '', outputFormat = 'mat', variableFilter = '.*', cflags = '', simflags = ''",
+messages = "Failed to build model: TestMedia.TestModels.TestFlueGas"
end SimulationResult;
-""
+"Error: Error building simulator. Build log: make: Entering directory '/c/dev/jenkins/ws/Windows/OM_Win/TESTSU~1/SIMULA~1/LIBRAR~1/3rdParty/TESTME~1/TESTFL~2.MOS'
+clang -municode -O0 -DOM_HAVE_PTHREADS -Wno-parentheses-equality -falign-functions -mstackrealign -msse2 -mfpmath=sse -I\"C:/dev/jenkins/ws/Windows/OM_Win/build/include/omc/c\" -I\"C:/dev/jenkins/ws/Windows/OM_Win/build/include/omc\" -I. -DOPENMODELICA_XML_FROM_FILE_AT_RUNTIME -DOMC_MODEL_PREFIX=TestMedia_TestModels_TestFlueGas -DOMC_NUM_MIXED_SYSTEMS=0 -DOMC_NUM_LINEAR_SYSTEMS=0 -DOMC_NUM_NONLINEAR_SYSTEMS=0 -DOMC_NDELAY_EXPRESSIONS=0 -DOMC_NVAR_STRING=0 -c -o TestMedia.TestModels.TestFlueGas.o TestMedia.TestModels.TestFlueGas.c
+clang -municode -O0 -DOM_HAVE_PTHREADS -Wno-parentheses-equality -falign-functions -mstackrealign -msse2 -mfpmath=sse -I\"C:/dev/jenkins/ws/Windows/OM_Win/build/include/omc/c\" -I\"C:/dev/jenkins/ws/Windows/OM_Win/build/include/omc\" -I. -DOPENMODELICA_XML_FROM_FILE_AT_RUNTIME -DOMC_MODEL_PREFIX=TestMedia_TestModels_TestFlueGas -DOMC_NUM_MIXED_SYSTEMS=0 -DOMC_NUM_LINEAR_SYSTEMS=0 -DOMC_NUM_NONLINEAR_SYSTEMS=0 -DOMC_NDELAY_EXPRESSIONS=0 -DOMC_NVAR_STRING=0 -c -o TestMedia.TestModels.TestFlueGas_functions.o TestMedia.TestModels.TestFlueGas_functions.c
+clang -municode -O0 -DOM_HAVE_PTHREADS -Wno-parentheses-equality -falign-functions -mstackrealign -msse2 -mfpmath=sse -I\"C:/dev/jenkins/ws/Windows/OM_Win/build/include/omc/c\" -I\"C:/dev/jenkins/ws/Windows/OM_Win/build/include/omc\" -I. -DOPENMODELICA_XML_FROM_FILE_AT_RUNTIME -DOMC_MODEL_PREFIX=TestMedia_TestModels_TestFlueGas -DOMC_NUM_MIXED_SYSTEMS=0 -DOMC_NUM_LINEAR_SYSTEMS=0 -DOMC_NUM_NONLINEAR_SYSTEMS=0 -DOMC_NDELAY_EXPRESSIONS=0 -DOMC_NVAR_STRING=0 -c -o TestMedia.TestModels.TestFlueGas_records.o TestMedia.TestModels.TestFlueGas_records.c
+clang -municode -O0 -DOM_HAVE_PTHREADS -Wno-parentheses-equality -falign-functions -mstackrealign -msse2 -mfpmath=sse -I\"C:/dev/jenkins/ws/Windows/OM_Win/build/include/omc/c\" -I\"C:/dev/jenkins/ws/Windows/OM_Win/build/include/omc\" -I. -DOPENMODELICA_XML_FROM_FILE_AT_RUNTIME -DOMC_MODEL_PREFIX=TestMedia_TestModels_TestFlueGas -DOMC_NUM_MIXED_SYSTEMS=0 -DOMC_NUM_LINEAR_SYSTEMS=0 -DOMC_NUM_NONLINEAR_SYSTEMS=0 -DOMC_NDELAY_EXPRESSIONS=0 -DOMC_NVAR_STRING=0 -c -o TestMedia.TestModels.TestFlueGas_01exo.o TestMedia.TestModels.TestFlueGas_01exo.c
+clang -municode -O0 -DOM_HAVE_PTHREADS -Wno-parentheses-equality -falign-functions -mstackrealign -msse2 -mfpmath=sse -I\"C:/dev/jenkins/ws/Windows/OM_Win/build/include/omc/c\" -I\"C:/dev/jenkins/ws/Windows/OM_Win/build/include/omc\" -I. -DOPENMODELICA_XML_FROM_FILE_AT_RUNTIME -DOMC_MODEL_PREFIX=TestMedia_TestModels_TestFlueGas -DOMC_NUM_MIXED_SYSTEMS=0 -DOMC_NUM_LINEAR_SYSTEMS=0 -DOMC_NUM_NONLINEAR_SYSTEMS=0 -DOMC_NDELAY_EXPRESSIONS=0 -DOMC_NVAR_STRING=0 -c -o TestMedia.TestModels.TestFlueGas_02nls.o TestMedia.TestModels.TestFlueGas_02nls.c
+clang -municode -O0 -DOM_HAVE_PTHREADS -Wno-parentheses-equality -falign-functions -mstackrealign -msse2 -mfpmath=sse -I\"C:/dev/jenkins/ws/Windows/OM_Win/build/include/omc/c\" -I\"C:/dev/jenkins/ws/Windows/OM_Win/build/include/omc\" -I. -DOPENMODELICA_XML_FROM_FILE_AT_RUNTIME -DOMC_MODEL_PREFIX=TestMedia_TestModels_TestFlueGas -DOMC_NUM_MIXED_SYSTEMS=0 -DOMC_NUM_LINEAR_SYSTEMS=0 -DOMC_NUM_NONLINEAR_SYSTEMS=0 -DOMC_NDELAY_EXPRESSIONS=0 -DOMC_NVAR_STRING=0 -c -o TestMedia.TestModels.TestFlueGas_03lsy.o TestMedia.TestModels.TestFlueGas_03lsy.c
+clang -municode -O0 -DOM_HAVE_PTHREADS -Wno-parentheses-equality -falign-functions -mstackrealign -msse2 -mfpmath=sse -I\"C:/dev/jenkins/ws/Windows/OM_Win/build/include/omc/c\" -I\"C:/dev/jenkins/ws/Windows/OM_Win/build/include/omc\" -I. -DOPENMODELICA_XML_FROM_FILE_AT_RUNTIME -DOMC_MODEL_PREFIX=TestMedia_TestModels_TestFlueGas -DOMC_NUM_MIXED_SYSTEMS=0 -DOMC_NUM_LINEAR_SYSTEMS=0 -DOMC_NUM_NONLINEAR_SYSTEMS=0 -DOMC_NDELAY_EXPRESSIONS=0 -DOMC_NVAR_STRING=0 -c -o TestMedia.TestModels.TestFlueGas_04set.o TestMedia.TestModels.TestFlueGas_04set.c
+clang -municode -O0 -DOM_HAVE_PTHREADS -Wno-parentheses-equality -falign-functions -mstackrealign -msse2 -mfpmath=sse -I\"C:/dev/jenkins/ws/Windows/OM_Win/build/include/omc/c\" -I\"C:/dev/jenkins/ws/Windows/OM_Win/build/include/omc\" -I. -DOPENMODELICA_XML_FROM_FILE_AT_RUNTIME -DOMC_MODEL_PREFIX=TestMedia_TestModels_TestFlueGas -DOMC_NUM_MIXED_SYSTEMS=0 -DOMC_NUM_LINEAR_SYSTEMS=0 -DOMC_NUM_NONLINEAR_SYSTEMS=0 -DOMC_NDELAY_EXPRESSIONS=0 -DOMC_NVAR_STRING=0 -c -o TestMedia.TestModels.TestFlueGas_05evt.o TestMedia.TestModels.TestFlueGas_05evt.c
+clang -municode -O0 -DOM_HAVE_PTHREADS -Wno-parentheses-equality -falign-functions -mstackrealign -msse2 -mfpmath=sse -I\"C:/dev/jenkins/ws/Windows/OM_Win/build/include/omc/c\" -I\"C:/dev/jenkins/ws/Windows/OM_Win/build/include/omc\" -I. -DOPENMODELICA_XML_FROM_FILE_AT_RUNTIME -DOMC_MODEL_PREFIX=TestMedia_TestModels_TestFlueGas -DOMC_NUM_MIXED_SYSTEMS=0 -DOMC_NUM_LINEAR_SYSTEMS=0 -DOMC_NUM_NONLINEAR_SYSTEMS=0 -DOMC_NDELAY_EXPRESSIONS=0 -DOMC_NVAR_STRING=0 -c -o TestMedia.TestModels.TestFlueGas_06inz.o TestMedia.TestModels.TestFlueGas_06inz.c
+LLVM ERROR: out of memory
+Allocation failed
+PLEASE submit a bug report to https://github.com/llvm/llvm-project/issues/ and include the crash backtrace, preprocessed source, and associated run script.
+Stack dump:
+0. Program arguments: C:\\\\OMDevUCRT\\\\tools\\\\msys\\\\ucrt64\\\\bin\\\\clang.exe -municode -O0 -DOM_HAVE_PTHREADS -Wno-parentheses-equality -falign-functions -mstackrealign -msse2 -mfpmath=sse -IC:/dev/jenkins/ws/Windows/OM_Win/build/include/omc/c -IC:/dev/jenkins/ws/Windows/OM_Win/build/include/omc -I. -DOPENMODELICA_XML_FROM_FILE_AT_RUNTIME -DOMC_MODEL_PREFIX=TestMedia_TestModels_TestFlueGas -DOMC_NUM_MIXED_SYSTEMS=0 -DOMC_NUM_LINEAR_SYSTEMS=0 -DOMC_NUM_NONLINEAR_SYSTEMS=0 -DOMC_NDELAY_EXPRESSIONS=0 -DOMC_NVAR_STRING=0 -c -o TestMedia.TestModels.TestFlueGas_06inz.o TestMedia.TestModels.TestFlueGas_06inz.c
+1. C:/OMDevUCRT/tools/msys/ucrt64/include/psdk_inc/intrin-impl.h:1732:2: current parser token 'if'
+2. C:/OMDevUCRT/tools/msys/ucrt64/include/psdk_inc/intrin-impl.h:1725:107: parsing function body '_InterlockedCompareExchange64'
+3. C:/OMDevUCRT/tools/msys/ucrt64/include/psdk_inc/intrin-impl.h:1725:107: in compound statement ('{}')
+Exception Code: 0xC000001D
+0x00007FFB4C80B736 <unknown module>
+0x00007FFB89B3E6D5 <unknown module>
+0x00000011315F9F50 <unknown module>
+0x00007FFB49860000 <unknown module>
+0x0000000000000016 <unknown module>
+clang: error: clang frontend command failed due to signal (use -v to see invocation)
+clang version 17.0.6
+Target: x86_64-w64-windows-gnu
+Thread model: posix
+InstalledDir: C:/OMDevUCRT/tools/msys/ucrt64/bin
+clang: note: diagnostic msg:
+********************
+
+PLEASE ATTACH THE FOLLOWING FILES TO THE BUG REPORT:
+Preprocessed source(s) and associated run script(s) are located at:
+clang: note: diagnostic msg: C:/Windows/TEMP/TestMedia-23e377.c
+clang: note: diagnostic msg: C:/Windows/TEMP/TestMedia-23e377.sh
+clang: note: diagnostic msg:
+
+********************
+make: *** [<builtin>: TestMedia.TestModels.TestFlueGas_06inz.o] Error 1
+make: Leaving directory '/c/dev/jenkins/ws/Windows/OM_Win/TESTSU~1/SIMULA~1/LIBRAR~1/3rdParty/TESTME~1/TESTFL~2.MOS'
+RESULT: 2
+"
''
Equation mismatch: omc-diff says:
Failed 'T' '"'
Line 894: Text differs:
expected: resultFile = "TestMedia.TestModels.TestFlueGas_res.mat",
got: resultFile = "",
== 1 out of 1 tests failed [simulation/libraries/3rdParty/TestMedia/TestFlueGas.mos_temp3724, time: 31]