Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.conf.json
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo): time 0.001388/0.001388, allocations: 81.3 kB / 20.05 MB, free: 1.473 MB / 14.72 MB
"
[Timeout remaining time 180]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo): time 0.001478/0.001478, allocations: 164.4 kB / 23.33 MB, free: 4.465 MB / 14.72 MB
"
[Timeout remaining time 180]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo): time 1.551/1.551, allocations: 177.1 MB / 203.7 MB, free: 9.133 MB / 190.1 MB
"
[Timeout remaining time 178]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo): time 1.062/1.062, allocations: 116 MB / 376.1 MB, free: 7.5 MB / 350.1 MB
"
[Timeout remaining time 179]
Using package ThermofluidStream with version 1.3.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo)
Using package Modelica with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo)
Using package Complex with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo)
Using package ModelicaServices with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo)
Running command: translateModel(ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant,tolerance=1e-06,outputFormat="mat",numberOfIntervals=100,variableFilter="CPUtime|EventCounter|NonlinearSystems.initialization.1..Calls|NonlinearSystems.initialization.1..Iterations|NonlinearSystems.initialization.1..Jacobians|NonlinearSystems.initialization.1..Residues|NonlinearSystems.initialization.2..Calls|NonlinearSystems.initialization.2..Iterations|NonlinearSystems.initialization.2..Jacobians|NonlinearSystems.initialization.2..Residues|NonlinearSystems.initialization.3..Calls|NonlinearSystems.initialization.3..Iterations|NonlinearSystems.initialization.3..Jacobians|NonlinearSystems.initialization.3..Residues|Time|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.H0|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.Hf|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.MM|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.R_s|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.Tlimit|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.ahigh.1.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.ahigh.2.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.ahigh.3.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.ahigh.4.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.ahigh.5.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.ahigh.6.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.ahigh.7.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.alow.1.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.alow.2.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.alow.3.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.alow.4.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.alow.5.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.alow.6.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.alow.7.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.bhigh.1.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.bhigh.2.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.blow.1.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.blow.2.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.H0|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.Hf|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.MM|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.R_s|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.Tlimit|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.ahigh.1.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.ahigh.2.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.ahigh.3.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.ahigh.4.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.ahigh.5.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.ahigh.6.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.ahigh.7.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.alow.1.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.alow.2.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.alow.3.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.alow.4.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.alow.5.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.alow.6.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.alow.7.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.bhigh.1.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.bhigh.2.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.blow.1.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.blow.2.|dropOfCommons.L|dropOfCommons.assertionLevel|dropOfCommons.g|dropOfCommons.instanceNameColor.1.|dropOfCommons.instanceNameColor.2.|dropOfCommons.instanceNameColor.3.|dropOfCommons.k_volume_damping|dropOfCommons.m_flow_reg|dropOfCommons.omega_reg|dropOfCommons.p_min|dropOfCommons.rho_min|eta|fullMedium.L|fullMedium.P|fullMedium.P_nom|fullMedium.P_out|fullMedium.TC|fullMedium.adiabaticModel.eta_is|fullMedium.adiabaticModel.h_in|fullMedium.adiabaticModel.h_out|fullMedium.adiabaticModel.h_out_is|fullMedium.adiabaticModel.p_out|fullMedium.adiabaticModel.s_in|fullMedium.adiabaticModel.state_in.T|fullMedium.adiabaticModel.state_in.p|fullMedium.adiabaticModel.w_t|fullMedium.adiabaticModel.w_t_is|fullMedium.assertionLevel|fullMedium.clip_p_out|fullMedium.dh|fullMedium.dp|fullMedium.dp_fixed|fullMedium.dp_nom|fullMedium.dp_start|fullMedium.dr_corr|fullMedium.etaSpec|fullMedium.eta_actual|fullMedium.eta_fixed|fullMedium.eta_is|fullMedium.h_in|fullMedium.h_out|fullMedium.initM_flow|der.fullMedium.inlet.m_flow.|fullMedium.inlet.m_flow|fullMedium.inlet.r|fullMedium.inlet.state.T|fullMedium.inlet.state.p|fullMedium.m_acceleration_0|fullMedium.m_flow|fullMedium.m_flowStateSelect|fullMedium.m_flow_0|fullMedium.outlet.m_flow|fullMedium.outlet.r|fullMedium.outlet.state.T|fullMedium.outlet.state.p|fullMedium.outletSpec|fullMedium.outletSpec_actual|fullMedium.outletValueSpec|fullMedium.pRatio|fullMedium.pRatio_fixed|fullMedium.p_in|fullMedium.p_min|fullMedium.p_out|fullMedium.p_out_fixed|fullMedium.singularityRegime|fullMedium1.L|fullMedium1.P|fullMedium1.P_in|fullMedium1.P_nom|fullMedium1.TC|fullMedium1.adiabaticModel.eta_is|fullMedium1.adiabaticModel.h_in|fullMedium1.adiabaticModel.h_out|fullMedium1.adiabaticModel.h_out_is|fullMedium1.adiabaticModel.p_out|fullMedium1.adiabaticModel.s_in|fullMedium1.adiabaticModel.state_in.T|fullMedium1.adiabaticModel.state_in.p|fullMedium1.adiabaticModel.w_t|fullMedium1.adiabaticModel.w_t_is|fullMedium1.assertionLevel|fullMedium1.clip_p_out|der.fullMedium1.dp.|fullMedium1.dh|fullMedium1.dp|fullMedium1.dp_fixed|fullMedium1.dp_nom|fullMedium1.dp_start|fullMedium1.dr_corr|fullMedium1.etaSpec|fullMedium1.eta_actual|fullMedium1.eta_fixed|fullMedium1.eta_is|fullMedium1.h_in|fullMedium1.h_out|fullMedium1.initM_flow|der.fullMedium1.inlet.m_flow.|fullMedium1.inlet.m_flow|fullMedium1.inlet.r|fullMedium1.inlet.state.T|fullMedium1.inlet.state.p|fullMedium1.m_acceleration_0|fullMedium1.m_flow|fullMedium1.m_flowStateSelect|fullMedium1.m_flow_0|fullMedium1.outlet.m_flow|fullMedium1.outlet.r|fullMedium1.outlet.state.T|fullMedium1.outlet.state.p|fullMedium1.outletSpec_actual|fullMedium1.pRatio|fullMedium1.pRatio_fixed|fullMedium1.p_in|fullMedium1.p_min|fullMedium1.p_out|fullMedium1.p_out_fixed|fullMedium1.singularityRegime|fullMedium2.L|fullMedium2.P|fullMedium2.P_in|fullMedium2.P_nom|fullMedium2.TC|fullMedium2.adiabaticModel.eta_is|fullMedium2.adiabaticModel.h_in|fullMedium2.adiabaticModel.h_out|fullMedium2.adiabaticModel.h_out_is|fullMedium2.adiabaticModel.p_out|fullMedium2.adiabaticModel.s_in|fullMedium2.adiabaticModel.state_in.T|fullMedium2.adiabaticModel.state_in.p|fullMedium2.adiabaticModel.w_t|fullMedium2.adiabaticModel.w_t_is|fullMedium2.assertionLevel|fullMedium2.clip_p_out|fullMedium2.dh|fullMedium2.dp|fullMedium2.dp_fixed|fullMedium2.dp_nom|fullMedium2.dp_start|fullMedium2.dr_corr|fullMedium2.etaSpec|fullMedium2.eta_actual|fullMedium2.eta_fixed|fullMedium2.eta_is|fullMedium2.h_in|fullMedium2.h_out|fullMedium2.initM_flow|der.fullMedium2.inlet.m_flow.|fullMedium2.inlet.m_flow|fullMedium2.inlet.r|fullMedium2.inlet.state.T|fullMedium2.inlet.state.p|fullMedium2.m_acceleration_0|fullMedium2.m_flow|fullMedium2.m_flowStateSelect|fullMedium2.m_flow_0|fullMedium2.outlet.m_flow|fullMedium2.outlet.r|fullMedium2.outlet.state.T|fullMedium2.outlet.state.p|fullMedium2.outletSpec|fullMedium2.outletSpec_actual|fullMedium2.outletValueSpec|fullMedium2.pRatio|fullMedium2.pRatio_fixed|fullMedium2.p_in|fullMedium2.p_min|fullMedium2.p_out|fullMedium2.p_out_fixed|fullMedium2.singularityRegime|fullMedium3.L|fullMedium3.P|fullMedium3.P_in|fullMedium3.P_nom|fullMedium3.TC|fullMedium3.adiabaticModel.eta_is|fullMedium3.adiabaticModel.h_in|fullMedium3.adiabaticModel.h_out|fullMedium3.adiabaticModel.h_out_is|fullMedium3.adiabaticModel.p_out|fullMedium3.adiabaticModel.s_in|fullMedium3.adiabaticModel.state_in.T|fullMedium3.adiabaticModel.state_in.p|fullMedium3.adiabaticModel.w_t|fullMedium3.adiabaticModel.w_t_is|fullMedium3.assertionLevel|fullMedium3.clip_p_out|fullMedium3.dh|fullMedium3.dp|fullMedium3.dp_fixed|fullMedium3.dp_nom|fullMedium3.dp_start|fullMedium3.dr_corr|fullMedium3.etaSpec|fullMedium3.eta_actual|fullMedium3.eta_fixed|fullMedium3.eta_is|fullMedium3.h_in|fullMedium3.h_out|fullMedium3.initM_flow|der.fullMedium3.inlet.m_flow.|fullMedium3.inlet.m_flow|fullMedium3.inlet.r|fullMedium3.inlet.state.T|fullMedium3.inlet.state.p|fullMedium3.m_acceleration_0|fullMedium3.m_flow|fullMedium3.m_flowStateSelect|fullMedium3.m_flow_0|fullMedium3.outlet.m_flow|fullMedium3.outlet.r|fullMedium3.outlet.state.T|fullMedium3.outlet.state.p|fullMedium3.outletSpec_actual|fullMedium3.pRatio|fullMedium3.pRatio_fixed|fullMedium3.p_in|fullMedium3.p_min|fullMedium3.p_out|fullMedium3.p_out_fixed|fullMed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[Timeout 660]
"Notification: Performance of FrontEnd - Absyn->SCode: time 3.187e-05/3.187e-05, allocations: 6.219 kB / 0.5549 GB, free: 13.55 MB / 478.1 MB
Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant): time 0.7242/0.7242, allocations: 323.4 MB / 0.8707 GB, free: 11.86 MB / 0.6856 GB
Notification: Performance of NFInst.instExpressions: time 0.02685/0.7511, allocations: 15.98 MB / 0.8863 GB, free: 11.85 MB / 0.7012 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.004782/0.7558, allocations: 265.4 kB / 0.8866 GB, free: 11.59 MB / 0.7012 GB
Notification: Performance of NFTyping.typeComponents: time 0.006234/0.7621, allocations: 1.702 MB / 0.8883 GB, free: 9.875 MB / 0.7012 GB
Notification: Performance of NFTyping.typeBindings: time 0.02215/0.7842, allocations: 6.507 MB / 0.8946 GB, free: 3.328 MB / 0.7012 GB
Notification: Performance of NFTyping.typeClassSections: time 0.01376/0.798, allocations: 4.206 MB / 0.8987 GB, free: 15.11 MB / 0.7169 GB
Notification: Performance of NFFlatten.flatten: time 0.01456/0.8125, allocations: 9.008 MB / 0.9075 GB, free: 6.062 MB / 0.7169 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.002429/0.815, allocations: 493.7 kB / 0.908 GB, free: 5.543 MB / 0.7169 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.01656/0.8315, allocations: 6.213 MB / 0.914 GB, free: 15.31 MB / 0.7325 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.004378/0.8359, allocations: 1.674 MB / 0.9157 GB, free: 13.63 MB / 0.7325 GB
Notification: Performance of NFPackage.collectConstants: time 0.001595/0.8375, allocations: 308 kB / 0.916 GB, free: 13.33 MB / 0.7325 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.01479/0.8523, allocations: 4.552 MB / 0.9204 GB, free: 8.773 MB / 0.7325 GB
Notification: Performance of combineBinaries: time 0.01058/0.8629, allocations: 7.893 MB / 0.9281 GB, free: 0.8047 MB / 0.7325 GB
Notification: Performance of replaceArrayConstructors: time 0.005384/0.8683, allocations: 5.058 MB / 0.9331 GB, free: 11.7 MB / 0.7481 GB
Notification: Performance of NFVerifyModel.verify: time 0.001674/0.8699, allocations: 396 kB / 0.9334 GB, free: 11.31 MB / 0.7481 GB
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/Idealized/Processes/AdiabaticThermodynamicModels/BaseClasses/PartialIdealGas.mo:14:5-14:72:writable] Error: Variable ThermodynamicValueSpecification.Fixed not found in scope ThermodynamicModel.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/Idealized/Processes/AdiabaticThermodynamicModels/BaseClasses/PartialIdealGas.mo:22:5-22:72:writable] Error: Variable ThermodynamicValueSpecification.State not found in scope ThermodynamicModel.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/Idealized/Processes/AdiabaticThermodynamicModels/BaseClasses/PartialIdealGas.mo:34:5-34:72:writable] Error: Variable ThermodynamicValueSpecification.State not found in scope ThermodynamicModel.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/Idealized/Processes/AdiabaticThermodynamicModels/BaseClasses/PartialIdealGas.mo:51:5-51:72:writable] Error: Variable ThermodynamicValueSpecification.State not found in scope ThermodynamicModel.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/Idealized/Processes/AdiabaticThermodynamicModels/BaseClasses/PartialIdealGas.mo:14:5-14:72:writable] Error: Variable ThermodynamicValueSpecification.Fixed not found in scope ThermodynamicModel.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/Idealized/Processes/AdiabaticThermodynamicModels/BaseClasses/PartialIdealGas.mo:22:5-22:72:writable] Error: Variable ThermodynamicValueSpecification.State not found in scope ThermodynamicModel.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/Idealized/Processes/AdiabaticThermodynamicModels/BaseClasses/PartialIdealGas.mo:34:5-34:72:writable] Error: Variable ThermodynamicValueSpecification.State not found in scope ThermodynamicModel.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/Idealized/Processes/AdiabaticThermodynamicModels/BaseClasses/PartialIdealGas.mo:51:5-51:72:writable] Error: Variable ThermodynamicValueSpecification.State not found in scope ThermodynamicModel.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/Idealized/Processes/AdiabaticThermodynamicModels/BaseClasses/PartialIdealGas.mo:14:5-14:72:writable] Error: Variable ThermodynamicValueSpecification.Fixed not found in scope ThermodynamicModel.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/Idealized/Processes/AdiabaticThermodynamicModels/BaseClasses/PartialIdealGas.mo:22:5-22:72:writable] Error: Variable ThermodynamicValueSpecification.State not found in scope ThermodynamicModel.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/Idealized/Processes/AdiabaticThermodynamicModels/BaseClasses/PartialIdealGas.mo:34:5-34:72:writable] Error: Variable ThermodynamicValueSpecification.State not found in scope ThermodynamicModel.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/Idealized/Processes/AdiabaticThermodynamicModels/BaseClasses/PartialIdealGas.mo:51:5-51:72:writable] Error: Variable ThermodynamicValueSpecification.State not found in scope ThermodynamicModel.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/Idealized/Processes/AdiabaticThermodynamicModels/BaseClasses/PartialIdealGas.mo:14:5-14:72:writable] Error: Variable ThermodynamicValueSpecification.Fixed not found in scope ThermodynamicModel.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/Idealized/Processes/AdiabaticThermodynamicModels/BaseClasses/PartialIdealGas.mo:22:5-22:72:writable] Error: Variable ThermodynamicValueSpecification.State not found in scope ThermodynamicModel.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/Idealized/Processes/AdiabaticThermodynamicModels/BaseClasses/PartialIdealGas.mo:34:5-34:72:writable] Error: Variable ThermodynamicValueSpecification.State not found in scope ThermodynamicModel.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/Idealized/Processes/AdiabaticThermodynamicModels/BaseClasses/PartialIdealGas.mo:51:5-51:72:writable] Error: Variable ThermodynamicValueSpecification.State not found in scope ThermodynamicModel.
Notification: Performance of FrontEnd: time 0.03959/0.9095, allocations: 22.6 MB / 0.9555 GB, free: 4.906 MB / 0.7637 GB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 724 (680)
 * Number of variables: 724 (724)
Notification: Performance of [SIM] Bindings: time 0.02571/0.9352, allocations: 18.8 MB / 0.9739 GB, free: 1.66 MB / 0.7794 GB
Notification: Performance of [SIM] FunctionAlias: time 0.006835/0.9421, allocations: 4.163 MB / 0.9779 GB, free: 13.87 MB / 0.795 GB
Notification: Performance of [SIM] Early Inline: time 0.442/1.384, allocations: 20.99 MB / 0.9984 GB, free: 63.52 MB / 0.795 GB
Notification: Performance of [SIM] Simplify 1: time 0.007337/1.391, allocations: 3.548 MB / 1.002 GB, free: 62.56 MB / 0.795 GB
Notification: Performance of [SIM] Alias: time 0.03668/1.428, allocations: 19.85 MB / 1.021 GB, free: 57.18 MB / 0.795 GB
Notification: Performance of [SIM] Simplify 2: time 0.005732/1.434, allocations: 3.27 MB / 1.024 GB, free: 56.01 MB / 0.795 GB
Notification: Performance of [SIM] Remove Stream: time 0.003375/1.437, allocations: 1.307 MB / 1.026 GB, free: 55.79 MB / 0.795 GB
Notification: Performance of [SIM] Detect States: time 0.009135/1.446, allocations: 4.753 MB / 1.03 GB, free: 55.26 MB / 0.795 GB
Notification: Performance of [SIM] Events: time 0.00226/1.449, allocations: 0.9253 MB / 1.031 GB, free: 55.14 MB / 0.795 GB
Notification: Performance of [SIM] Partitioning: time 0.01748/1.466, allocations: 6.501 MB / 1.038 GB, free: 54.39 MB / 0.795 GB
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/Math/Nonlinear.mo:645:5-645:69:writable] Warning: Variable $fDER_u of the generated function $fDER0.Modelica.Math.Nonlinear.solveOneNonlinearEquation will be initialized to 0.0 because it could not be proven that it is always assigned before it is used.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/Math/Nonlinear.mo:654:5-654:11:writable] Warning: Variable m of the generated function $fDER0.Modelica.Math.Nonlinear.solveOneNonlinearEquation will be initialized to 0.0 because it could not be proven that it is always assigned before it is used.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/Math/Nonlinear.mo:655:5-655:11:writable] Warning: Variable s of the generated function $fDER0.Modelica.Math.Nonlinear.solveOneNonlinearEquation will be initialized to 0.0 because it could not be proven that it is always assigned before it is used.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/Math/Nonlinear.mo:656:5-656:11:writable] Warning: Variable p of the generated function $fDER0.Modelica.Math.Nonlinear.solveOneNonlinearEquation will be initialized to 0.0 because it could not be proven that it is always assigned before it is used.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/Math/Nonlinear.mo:657:5-657:11:writable] Warning: Variable q of the generated function $fDER0.Modelica.Math.Nonlinear.solveOneNonlinearEquation will be initialized to 0.0 because it could not be proven that it is always assigned before it is used.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/Math/Nonlinear.mo:658:5-658:11:writable] Warning: Variable r of the generated function $fDER0.Modelica.Math.Nonlinear.solveOneNonlinearEquation will be initialized to 0.0 because it could not be proven that it is always assigned before it is used.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/Math/Nonlinear.mo:659:5-659:13:writable] Warning: Variable tol of the generated function $fDER0.Modelica.Math.Nonlinear.solveOneNonlinearEquation will be initialized to 0.0 because it could not be proven that it is always assigned before it is used.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/Math/Nonlinear.mo:654:5-654:11:writable] Warning: Variable $fDER_m of the generated function $fDER0.Modelica.Math.Nonlinear.solveOneNonlinearEquation will be initialized to 0.0 because it could not be proven that it is always assigned before it is used.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/Math/Nonlinear.mo:655:5-655:11:writable] Warning: Variable $fDER_s of the generated function $fDER0.Modelica.Math.Nonlinear.solveOneNonlinearEquation will be initialized to 0.0 because it could not be proven that it is always assigned before it is used.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/Math/Nonlinear.mo:656:5-656:11:writable] Warning: Variable $fDER_p of the generated function $fDER0.Modelica.Math.Nonlinear.solveOneNonlinearEquation will be initialized to 0.0 because it could not be proven that it is always assigned before it is used.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/Math/Nonlinear.mo:657:5-657:11:writable] Warning: Variable $fDER_q of the generated function $fDER0.Modelica.Math.Nonlinear.solveOneNonlinearEquation will be initialized to 0.0 because it could not be proven that it is always assigned before it is used.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/Math/Nonlinear.mo:658:5-658:11:writable] Warning: Variable $fDER_r of the generated function $fDER0.Modelica.Math.Nonlinear.solveOneNonlinearEquation will be initialized to 0.0 because it could not be proven that it is always assigned before it is used.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/Math/Nonlinear.mo:659:5-659:13:writable] Warning: Variable $fDER_tol of the generated function $fDER0.Modelica.Math.Nonlinear.solveOneNonlinearEquation will be initialized to 0.0 because it could not be proven that it is always assigned before it is used.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/Math/Nonlinear.mo:645:5-645:69:writable] Warning: Variable u of the generated function $fDER0.Modelica.Math.Nonlinear.solveOneNonlinearEquation will be initialized to 0.0 because it could not be proven that it is always assigned before it is used.
Error: Internal error NBSorting.tarjan failed to sort system:
System Variables (176/184)
****************************
(1|1)          [ALGB] (1) output Real source9.outlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(2|2)          [DSTA] (1) output Real source4.outlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(3|3)          [ALGB] (1) output Real source3.outlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(4|4)          [ALGB] (1) final Real fullMedium1.adiabaticModel.h_in = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.fullMedium1.adiabaticModel.Medium.specificEnthalpy(fullMedium1.adiabaticModel.state_in) (start = 212805.6215135368, min = -1e10, max = 1e10, nominal = 1e5)
(5|5)          [ALGB] (1) Real $FUN_52.p
(6|6)          [DSTA] (1) final Real fullMedium2.adiabaticModel.h_in = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.fullMedium2.adiabaticModel.Medium.specificEnthalpy(fullMedium2.adiabaticModel.state_in) (start = 212805.6215135368, min = -1e10, max = 1e10, nominal = 1e5)
(7|7)          [ALGB] (1) final Real fullMedium3.adiabaticModel.h_in = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.fullMedium3.adiabaticModel.Medium.specificEnthalpy(fullMedium3.adiabaticModel.state_in) (start = 212805.6215135368, min = -1e10, max = 1e10, nominal = 1e5)
(8|8)          [ALGB] (1) Real fullMedium3.h_out (start = 212805.6215135368, min = -1e10, max = 1e10, nominal = 1e5)
(9|9)          [ALGB] (1) Real sink4.r
(10|10)        [DSTA] (1) Real fullMedium2.h_out (start = 212805.6215135368, min = -1e10, max = 1e10, nominal = 1e5)
(11|11)        [ALGB] (1) Real fullMedium1.h_out (start = 212805.6215135368, min = -1e10, max = 1e10, nominal = 1e5)
(12|12)        [ALGB] (1) Real fullMedium1.P
(13|13)        [ALGB] (1) final Real fullMedium3.adiabaticModel.w_t_is
(14|14)        [DSTA] (1) final Real fullMedium2.adiabaticModel.w_t_is
(15|15)        [ALGB] (1) final Real fullMedium1.adiabaticModel.w_t_is
(16|16)        [ALGB] (1) final Real fullMedium3.adiabaticModel.p_in = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.fullMedium3.adiabaticModel.Medium.pressure(fullMedium3.adiabaticModel.state_in) (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(17|17)        [ALGB] (1) final Real fullMedium2.adiabaticModel.p_in = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.fullMedium2.adiabaticModel.Medium.pressure(fullMedium2.adiabaticModel.state_in) (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(18|18)        [ALGB] (1) Real $FUN_8.p
(19|19)        [ALGB] (1) final Real fullMedium1.adiabaticModel.p_in = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.fullMedium1.adiabaticModel.Medium.pressure(fullMedium1.adiabaticModel.state_in) (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(20|20)        [DSTA] (1) final Real fullMedium.adiabaticModel.h_out_is = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.fullMedium.adiabaticModel.Medium.specificEnthalpy_psX(fullMedium.p_out, fullMedium.adiabaticModel.s_in, {}) (start = 212805.6215135368, min = -1e10, max = 1e10, nominal = 1e5)
(21|21)        [ALGB] (1) Real $FUN_2.p
(22|22)        [ALGB] (1) Real $FUN_49.p
(23|23)        [ALGB] (1) final input Real fullMedium3.adiabaticModel.state_in.T = fullMedium3.inlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(24|24)        [DSTA] (1) Real $FUN_1.p
(25|25)        [DSTA] (1) final input Real fullMedium2.adiabaticModel.state_in.T = fullMedium2.inlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(26|26)        [ALGB] (1) final input Real fullMedium1.adiabaticModel.state_in.T = fullMedium1.inlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(27|27)        [DSTA] (1) Real fullMedium1.P_in_internal
(28|28)        [ALGB] (1) Real fullMedium3.pRatio = fullMedium3.p_out / fullMedium3.p_in
(29|29)        [ALGB] (1) Real fullMedium.dp
(30|30)        [ALGB] (1) Real fullMedium1.pRatio = fullMedium1.p_out / fullMedium1.p_in
(31|31)        [ALGB] (1) output Real source9.outlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(32|32)        [ALGB] (1) final input Real fullMedium3.adiabaticModel.state_in.p = fullMedium3.inlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(33|33)        [DSTA] (1) final input Real fullMedium2.adiabaticModel.state_in.p = fullMedium2.inlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(34|34)        [ALGB] (1) final input Real fullMedium1.adiabaticModel.state_in.p = fullMedium1.inlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(35|35)        [DSTA] (1) output Real source4.outlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(36|36)        [ALGB] (1) output Real source3.outlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(37|37)        [ALGB] (1) Real fullMedium1.dh
(38|38)        [DSTA] (1) Real fullMedium2.dh
(39|39)        [DSTA] (1) final Real fullMedium.adiabaticModel.h_in = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.fullMedium.adiabaticModel.Medium.specificEnthalpy(fullMedium.adiabaticModel.state_in) (start = 212805.6215135368, min = -1e10, max = 1e10, nominal = 1e5)
(40|40)        [ALGB] (1) Real fullMedium3.dh
(41|41)        [ALGB] (1) input Real sink.inlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(42|42)        [ALGB] (1) final Real fullMedium3.adiabaticModel.w_t
(43|43)        [DSTA] (1) final Real fullMedium2.adiabaticModel.w_t
(44|44)        [ALGB] (1) final Real fullMedium1.adiabaticModel.w_t
(45|45)        [DSTA] (1) output Real source.outlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(46|46)        [DSTA] (1) Real fullMedium.p_out (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(47|47)        [ALGB] (1) input Real sink.inlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(48|48)        [ALGB] (1) Real $FUN_9
(49|49)        [ALGB] (1) Real $FUN_15.T
(50|50)        [DSTA] (1) Real $FUN_12.T
(51|51)        [ALGB] (1) Real $FUN_11.T
(52|52)        [ALGB] (1) Real source4.outlet.r
(53|53)        [DSTA] (1) final input Real fullMedium.adiabaticModel.state_in.T = fullMedium.inlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(54|54)        [ALGB] (1) Real $FUN_14
(55|55)        [ALGB] (1) Real $FUN_13
(56|56)        [ALGB] (1) input Real sink9.inlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(57|57)        [ALGB] (1) Real $FUN_10
(58|58)        [ALGB] (1) input Real sink4.inlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(59|59)        [ALGB] (1) input Real sink3.inlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(60|60)        [DISC] (1) Boolean $SEV_9
(61|61)        [ALGB] (1) output Real fullMedium3.outlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(62|62)        [DISC] (1) Boolean $SEV_3
(63|63)        [ALGB] (1) output Real fullMedium2.outlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(64|64)        [DISC] (1) Boolean $SEV_2
(65|65)        [ALGB] (1) output Real fullMedium1.outlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(66|66)        [ALGB] (1) output Real fullMedium3.outlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(67|67)        [DISC] (1) Boolean $SEV_0
(68|68)        [ALGB] (1) output Real fullMedium2.outlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(69|69)        [ALGB] (1) output Real fullMedium1.outlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(70|70)        [ALGB] (1) Real $FUN_15.p
(71|71)        [DSTA] (1) Real $FUN_12.p
(72|72)        [ALGB] (1) Real $FUN_11.p
(73|73)        [ALGB] (1) Real fullMedium1.p_in = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.fullMedium1.Medium.pressure(fullMedium1.inlet.state) (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(74|74)        [DSTA] (1) input Real fullMedium.inlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(75|75)        [DSTA] (1) Real fullMedium2.p_in = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.fullMedium2.Medium.pressure(fullMedium2.inlet.state) (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(76|76)        [ALGB] (1) final Real fullMedium.adiabaticModel.p_in = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.fullMedium.adiabaticModel.Medium.pressure(fullMedium.adiabaticModel.state_in) (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(77|77)        [ALGB] (1) Real fullMedium3.p_in = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.fullMedium3.Medium.pressure(fullMedium3.inlet.state) (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(78|78)        [ALGB] (1) Real $FUN_8.T
(79|79)        [ALGB] (1) Real $FUN_2.T
(80|80)        [DSTA] (1) Real $FUN_1.T
(81|81)        [DSTA] (1) final Real fullMedium.adiabaticModel.w_t
(82|82)        [DSTA] (1) output Real source.outlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(83|83)        [DSTA] (1) final Real fullMedium.adiabaticModel.w_t_is
(84|84)        [ALGB] (1) Real sink9.p = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.sink9.Medium.pressure(sink9.inlet.state) (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(85|85)        [ALGB] (1) input Real fullMedium1.inlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(86|86)        [DSTA] (1) input Real fullMedium2.inlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(87|87)        [ALGB] (1) input Real fullMedium3.inlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(88|88)        [ALGB] (1) Real sink3.p = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.sink3.Medium.pressure(sink3.inlet.state) (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(89|89)        [ALGB] (1) final Real fullMedium3.adiabaticModel.s_in = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.fullMedium3.adiabaticModel.Medium.specificEntropy(fullMedium3.adiabaticModel.state_in) (min = -1e7, max = 1e7, nominal = 1000.0)
(90|90)        [DSTA] (1) final Real fullMedium2.adiabaticModel.s_in = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.fullMedium2.adiabaticModel.Medium.specificEntropy(fullMedium2.adiabaticModel.state_in) (min = -1e7, max = 1e7, nominal = 1000.0)
(91|91)        [ALGB] (1) final Real fullMedium1.adiabaticModel.s_in = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.fullMedium1.adiabaticModel.Medium.specificEntropy(fullMedium1.adiabaticModel.state_in) (min = -1e7, max = 1e7, nominal = 1000.0)
(92|92)        [ALGB] (1) input Real fullMedium3.inlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(93|93)        [DSTA] (1) input Real fullMedium2.inlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(94|94)        [ALGB] (1) Real fullMedium2.outlet.r
(95|95)        [ALGB] (1) input Real fullMedium1.inlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(96|96)        [ALGB] (1) output Real fullMedium.outlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(97|97)        [DSTA] (1) Real fullMedium.dh
(98|98)        [ALGB] (1) Real fullMedium2.dp
(99|99)        [ALGB] (1) Real fullMedium3.dp
(100|100)      [DSTA] (1) Real fullMedium.h_out (start = 212805.6215135368, min = -1e10, max = 1e10, nominal = 1e5)
(101|101)      [ALGB] (1) Real $FUN_52.T
(102|102)      [DSTA] (1) final input Real fullMedium.adiabaticModel.state_in.p = fullMedium.inlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(103|103)      [ALGB] (1) final Real fullMedium3.adiabaticModel.h_out_is = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.fullMedium3.adiabaticModel.Medium.specificEnthalpy_psX(fullMedium3.p_out, fullMedium3.adiabaticModel.s_in, {}) (start = 212805.6215135368, min = -1e10, max = 1e10, nominal = 1e5)
(104|104)      [DSTA] (1) Real fullMedium.p_in = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.fullMedium.Medium.pressure(fullMedium.inlet.state) (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(105|105)      [DSTA] (1) Real fullMedium.h_in = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.fullMedium.Medium.specificEnthalpy(fullMedium.inlet.state) (start = 212805.6215135368, min = -1e10, max = 1e10, nominal = 1e5)
(106|106)      [DER-] (1) Real $DER.fullMedium1.dp
(107|107)      [DSTA] (1) final Real fullMedium2.adiabaticModel.h_out_is = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.fullMedium2.adiabaticModel.Medium.specificEnthalpy_psX(fullMedium2.p_out, fullMedium2.adiabaticModel.s_in, {}) (start = 212805.6215135368, min = -1e10, max = 1e10, nominal = 1e5)
(108|108)      [DSTA] (1) final Real fullMedium.adiabaticModel.s_in = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.fullMedium.adiabaticModel.Medium.specificEntropy(fullMedium.adiabaticModel.state_in) (min = -1e7, max = 1e7, nominal = 1000.0)
(109|109)      [ALGB] (1) final Real fullMedium1.adiabaticModel.h_out_is = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.fullMedium1.adiabaticModel.Medium.specificEnthalpy_psX(fullMedium1.p_out, fullMedium1.adiabaticModel.s_in, {}) (start = 212805.6215135368, min = -1e10, max = 1e10, nominal = 1e5)
(110|110)      [ALGB] (1) output Real fullMedium.outlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(111|111)      [ALGB] (1) Real sink.p = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.sink.Medium.pressure(sink.inlet.state) (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(112|112)      [ALGB] (1) Real fullMedium1.singularityRegime
(113|113)      [ALGB] (1) Real fullMedium2.singularityRegime
(114|114)      [ALGB] (1) Real fullMedium3.singularityRegime
(115|115)      [DDER] (1) Real $DER.fullMedium2.m_flow (StateSelect = avoid)
(116|116)      [ALGB] (1) Real fullMedium3.h_in = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.fullMedium3.Medium.specificEnthalpy(fullMedium3.inlet.state) (start = 212805.6215135368, min = -1e10, max = 1e10, nominal = 1e5)
(117|117)      [ALGB] (1) input Real sink9.inlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(118|118)      [DSTA] (1) Real fullMedium2.h_in = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.fullMedium2.Medium.specificEnthalpy(fullMedium2.inlet.state) (start = 212805.6215135368, min = -1e10, max = 1e10, nominal = 1e5)
(119|119)      [ALGB] (1) Real fullMedium1.h_in = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.fullMedium1.Medium.specificEnthalpy(fullMedium1.inlet.state) (start = 212805.6215135368, min = -1e10, max = 1e10, nominal = 1e5)
(120|120)      [ALGB] (1) Real $FUN_49.T
(121|121)      [ALGB] (1) input Real sink4.inlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(122|122)      [ALGB] (1) Real fullMedium1.p_out (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(123|123)      [ALGB] (1) input Real sink3.inlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(124|124)      [DSTA] (1) Real fullMedium2.p_out (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(125|125)      [ALGB] (1) Real fullMedium3.p_out (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(126|126)      [ALGB] (1) Real $FUN_51
(127|127)      [DSTA] (1) input Real fullMedium.inlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(128|128)      [ALGB] (1) Real $FUN_50
(129|129)      [DSTA] (1) Real fullMedium.P_in_internal
(130|130)      [DDER] (1) output Real $DER.source.outlet.state.T (StateSelect = avoid)
(131|131)      [DDER] (1) output Real $DER.source.outlet.state.p (StateSelect = avoid)
(132|132)      [DDER] (1) output Real $DER.source4.outlet.state.T (StateSelect = avoid)
(133|133)      [DDER] (1) output Real $DER.source4.outlet.state.p (StateSelect = avoid)
(134|134)      [DDER] (1) Real $DER.$FUN_12.T (StateSelect = avoid)
(135|135)      [DDER] (1) Real $DER.$FUN_12.p (StateSelect = avoid)
(136|136)      [DER-] (2) source.Medium.ThermodynamicState $DER.$FUN_1
(137|138)      [DER-] (2) source.outlet.Medium.ThermodynamicState $DER.source.outlet.state
(138|140)      [DDER] (1) input Real $DER.fullMedium2.inlet.state.p (StateSelect = avoid)
(139|141)      [DDER] (1) Real $DER.fullMedium2.p_in (StateSelect = avoid)
(140|142)      [DDER] (1) Real $DER.fullMedium.P_in_internal (StateSelect = avoid)
(141|143)      [DDER] (1) input Real $DER.fullMedium2.inlet.state.T (StateSelect = avoid)
(142|144)      [DDER] (1) Real $DER.fullMedium2.h_in (StateSelect = avoid)
(143|145)      [DDER] (1) Real $DER.fullMedium.dh (StateSelect = avoid)
(144|146)      [DDER] (1) final input Real $DER.fullMedium2.adiabaticModel.state_in.p (StateSelect = avoid)
(145|147)      [DDER] (1) final input Real $DER.fullMedium2.adiabaticModel.state_in.T (StateSelect = avoid)
(146|148)      [DDER] (1) final Real $DER.fullMedium2.adiabaticModel.s_in (StateSelect = avoid)
(147|149)      [DDER] (1) Real $DER.fullMedium2.p_out (StateSelect = avoid)
(148|150)      [DDER] (1) Real $DER.fullMedium2.h_out (StateSelect = avoid)
(149|151)      [DDER] (1) final Real $DER.fullMedium2.adiabaticModel.w_t (StateSelect = avoid)
(150|152)      [DDER] (1) final Real $DER.fullMedium2.adiabaticModel.h_in (StateSelect = avoid)
(151|153)      [DDER] (1) final Real $DER.fullMedium2.adiabaticModel.h_out_is (StateSelect = avoid)
(152|154)      [DDER] (1) final Real $DER.fullMedium2.adiabaticModel.w_t_is (StateSelect = avoid)
(153|155)      [DER-] (2) fullMedium.inlet.Medium.ThermodynamicState $DER.fullMedium.inlet.state
(154|157)      [DER-] (2) final fullMedium.adiabaticModel.Medium.ThermodynamicState $DER.fullMedium.adiabaticModel.state_in
(155|159)      [DER-] (2) source4.Medium.ThermodynamicState $DER.$FUN_12
(156|161)      [DER-] (2) source4.outlet.Medium.ThermodynamicState $DER.source4.outlet.state
(157|163)      [DER-] (2) fullMedium2.inlet.Medium.ThermodynamicState $DER.fullMedium2.inlet.state
(158|165)      [DER-] (2) final fullMedium2.adiabaticModel.Medium.ThermodynamicState $DER.fullMedium2.adiabaticModel.state_in
(159|167)      [DDER] (1) Real $DER.fullMedium1.P_in_internal (StateSelect = avoid)
(160|168)      [DDER] (1) Real $DER.fullMedium2.dh (StateSelect = avoid)
(161|169)      [DDER] (1) Real $DER.$FUN_1.p (StateSelect = avoid)
(162|170)      [DDER] (1) Real $DER.$FUN_1.T (StateSelect = avoid)
(163|171)      [DDER] (1) input Real $DER.fullMedium.inlet.state.p (StateSelect = avoid)
(164|172)      [DDER] (1) Real $DER.fullMedium.p_in (StateSelect = avoid)
(165|173)      [DDER] (1) input Real $DER.fullMedium.inlet.state.T (StateSelect = avoid)
(166|174)      [DDER] (1) Real $DER.fullMedium.h_in (StateSelect = avoid)
(167|175)      [DDER] (1) final input Real $DER.fullMedium.adiabaticModel.state_in.p (StateSelect = avoid)
(168|176)      [DDER] (1) final input Real $DER.fullMedium.adiabaticModel.state_in.T (StateSelect = avoid)
(169|177)      [DDER] (1) final Real $DER.fullMedium.adiabaticModel.w_t_is (StateSelect = avoid)
(170|178)      [DDER] (1) final Real $DER.fullMedium.adiabaticModel.s_in (StateSelect = avoid)
(171|179)      [DDER] (1) Real $DER.fullMedium.p_out (StateSelect = avoid)
(172|180)      [DDER] (1) final Real $DER.fullMedium.adiabaticModel.h_out_is (StateSelect = avoid)
(173|181)      [DDER] (1) final Real $DER.fullMedium.adiabaticModel.h_in (StateSelect = avoid)
(174|182)      [DDER] (1) Real $DER.fullMedium.h_out (StateSelect = avoid)
(175|183)      [DDER] (1) final Real $DER.fullMedium.adiabaticModel.w_t (StateSelect = avoid)
(176|184)      [DSTA] (1) Real fullMedium2.m_flow = fullMedium2.m_flow (StateSelect = default)


System Equations (152/168)
****************************
(1|1)          [SCAL] (1) fullMedium2.outlet.state.T = sink4.inlet.state.T ($RES_SIM_480)
(2|2)          [SCAL] (1) fullMedium2.outlet.state.p = sink4.inlet.state.p ($RES_SIM_481)
(3|3)          [SCAL] (1) fullMedium3.adiabaticModel.s_in = (if noEvent(fullMedium3.adiabaticModel.state_in.T < 1000.0) then 188.9244822140674 * (((-7.04827944) + 626.411601 / fullMedium3.adiabaticModel.state_in.T + 5.30172524 * log(fullMedium3.adiabaticModel.state_in.T) + fullMedium3.adiabaticModel.state_in.T * (0.002503813816 + fullMedium3.adiabaticModel.state_in.T * ((-1.063654364e-7) + fullMedium3.adiabaticModel.state_in.T * ((-2.563329593333333e-10) + 7.1241945025e-14 * fullMedium3.adiabaticModel.state_in.T)))) - 24718.2527 / (fullMedium3.adiabaticModel.state_in.T * fullMedium3.adiabaticModel.state_in.T)) else 188.9244822140674 * (((-26.52669281) + 1788.791477 / fullMedium3.adiabaticModel.state_in.T + 8.29152319 * log(fullMedium3.adiabaticModel.state_in.T) + fullMedium3.adiabaticModel.state_in.T * ((-9.22315678e-5) + fullMedium3.adiabaticModel.state_in.T * (2.43183844e-9 + fullMedium3.adiabaticModel.state_in.T * ((-6.303511039999999e-13) + 1.5825091474999999e-16 * fullMedium3.adiabaticModel.state_in.T)))) - 58848.12095 / (fullMedium3.adiabaticModel.state_in.T * fullMedium3.adiabaticModel.state_in.T))) - 188.9244822140674 * log(9.869232667160129e-6 * fullMedium3.adiabaticModel.state_in.p) ($RES_AUX_880)
(4|4)          [SCAL] (1) fullMedium3.adiabaticModel.h_in = ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"CO2\", 0.0440095, -8.941478544405185e6, 212805.6215135368, 1000.0, {49436.5054, -626.411601, 5.30172524, 0.002503813816, -2.127308728e-7, -7.68998878e-10, 2.849677801e-13}, {-45281.9846, -7.04827944}, {117696.2419, -1788.791477, 8.29152319, -9.22315678e-5, 4.86367688e-9, -1.891053312e-12, 6.330036589999999e-16}, {-39083.5059, -26.52669281}, 188.9244822140674), fullMedium3.adiabaticModel.state_in.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_AUX_881)
(5|5)          [SCAL] (1) fullMedium1.outlet.state.T = sink3.inlet.state.T ($RES_SIM_483)
(6|6)          [SCAL] (1) fullMedium3.adiabaticModel.h_out_is = ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"CO2\", 0.0440095, -8.941478544405185e6, 212805.6215135368, 1000.0, {49436.5054, -626.411601, 5.30172524, 0.002503813816, -2.127308728e-7, -7.68998878e-10, 2.849677801e-13}, {-45281.9846, -7.04827944}, {117696.2419, -1788.791477, 8.29152319, -9.22315678e-5, 4.86367688e-9, -1.891053312e-12, 6.330036589999999e-16}, {-39083.5059, -26.52669281}, 188.9244822140674), ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.fullMedium3.adiabaticModel.Medium.T_ps(fullMedium3.p_out, fullMedium3.adiabaticModel.s_in), true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_AUX_882)
(7|7)          [SCAL] (1) fullMedium1.outlet.state.p = sink3.inlet.state.p ($RES_SIM_484)
(8|8)          [SCAL] (1) fullMedium3.adiabaticModel.w_t = fullMedium3.h_out - fullMedium3.adiabaticModel.h_in ($RES_SIM_92)
(9|9)          [SCAL] (1) source4.outlet.state.T = fullMedium2.inlet.state.T ($RES_SIM_486)
(10|10)        [SCAL] (1) fullMedium1.P_in_internal = -gain.k * fullMedium.P_in_internal ($RES_SIM_213)
(11|11)        [SCAL] (1) fullMedium3.adiabaticModel.w_t_is = fullMedium3.adiabaticModel.h_out_is - fullMedium3.adiabaticModel.h_in ($RES_SIM_93)
(12|12)        [SCAL] (1) source4.outlet.state.p = fullMedium2.inlet.state.p ($RES_SIM_487)
(13|13)        [SCAL] (1) source3.outlet.state.T = fullMedium1.inlet.state.T ($RES_SIM_489)
(14|14)        [RECD] (2) source9.outlet.state = $FUN_49 ($RES_SIM_97)
(15|16)        [SCAL] (1) fullMedium2.dh = fullMedium2.h_out - fullMedium2.h_in ($RES_SIM_291)
(16|17)        [SCAL] (1) $FUN_2.p = fullMedium.p_out ($RES_SIM_990)
(17|18)        [SCAL] (1) $FUN_2.T = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.fullMedium.Medium.T_h(fullMedium.h_out) ($RES_SIM_991)
(18|19)        [SCAL] (1) fullMedium2.adiabaticModel.w_t = if $SEV_3 then fullMedium2.adiabaticModel.w_t_is / fullMedium2.eta_fixed else fullMedium2.adiabaticModel.w_t_is * fullMedium2.eta_fixed ($RES_SIM_297)
(19|20)        [SCAL] (1) fullMedium.p_out = fullMedium.p_in + fullMedium.dp ($RES_SIM_371)
(20|21)        [SCAL] (1) fullMedium1.adiabaticModel.s_in = (if noEvent(fullMedium1.adiabaticModel.state_in.T < 1000.0) then 188.9244822140674 * (((-7.04827944) + 626.411601 / fullMedium1.adiabaticModel.state_in.T + 5.30172524 * log(fullMedium1.adiabaticModel.state_in.T) + fullMedium1.adiabaticModel.state_in.T * (0.002503813816 + fullMedium1.adiabaticModel.state_in.T * ((-1.063654364e-7) + fullMedium1.adiabaticModel.state_in.T * ((-2.563329593333333e-10) + 7.1241945025e-14 * fullMedium1.adiabaticModel.state_in.T)))) - 24718.2527 / (fullMedium1.adiabaticModel.state_in.T * fullMedium1.adiabaticModel.state_in.T)) else 188.9244822140674 * (((-26.52669281) + 1788.791477 / fullMedium1.adiabaticModel.state_in.T + 8.29152319 * log(fullMedium1.adiabaticModel.state_in.T) + fullMedium1.adiabaticModel.state_in.T * ((-9.22315678e-5) + fullMedium1.adiabaticModel.state_in.T * (2.43183844e-9 + fullMedium1.adiabaticModel.state_in.T * ((-6.303511039999999e-13) + 1.5825091474999999e-16 * fullMedium1.adiabaticModel.state_in.T)))) - 58848.12095 / (fullMedium1.adiabaticModel.state_in.T * fullMedium1.adiabaticModel.state_in.T))) - 188.9244822140674 * log(9.869232667160129e-6 * fullMedium1.adiabaticModel.state_in.p) ($RES_AUX_770)
(21|22)        [SCAL] (1) fullMedium1.adiabaticModel.h_in = ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"CO2\", 0.0440095, -8.941478544405185e6, 212805.6215135368, 1000.0, {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), fullMedium1.adiabaticModel.state_in.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_AUX_771)
(22|23)        [RECD] (2) fullMedium3.adiabaticModel.state_in = fullMedium3.inlet.state ($RES_BND_736)
(23|25)        [SCAL] (1) fullMedium1.adiabaticModel.h_out_is = ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"CO2\", 0.0440095, -8.941478544405185e6, 212805.6215135368, 1000.0, {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), ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.fullMedium1.adiabaticModel.Medium.T_ps(fullMedium1.p_out, fullMedium1.adiabaticModel.s_in), true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_AUX_772)
(24|26)        [SCAL] (1) fullMedium2.p_in = fullMedium2.inlet.state.p ($RES_AUX_773)
(25|27)        [SCAL] (1) $FUN_8.p = source3.p0_par ($RES_SIM_998)
(26|28)        [SCAL] (1) fullMedium.P_in_internal = sink.m_flow_fixed * fullMedium.dh ($RES_SIM_375)
(27|29)        [SCAL] (1) fullMedium2.h_in = ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"CO2\", 0.0440095, -8.941478544405185e6, 212805.6215135368, 1000.0, {49436.5054, -626.411601, 5.30172524, 0.002503813816, -2.127308728e-7, -7.68998878e-10, 2.849677801e-13}, {-45281.9846, -7.04827944}, {117696.2419, -1788.791477, 8.29152319, -9.22315678e-5, 4.86367688e-9, -1.891053312e-12, 6.330036589999999e-16}, {-39083.5059, -26.52669281}, 188.9244822140674), fullMedium2.inlet.state.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_AUX_774)
(28|30)        [SCAL] (1) $FUN_8.T = source3.T0_par ($RES_SIM_999)
(29|31)        [SCAL] (1) fullMedium2.adiabaticModel.p_in = fullMedium2.adiabaticModel.state_in.p ($RES_AUX_775)
(30|32)        [SCAL] (1) fullMedium.dh = fullMedium.h_out - fullMedium.h_in ($RES_SIM_377)
(31|33)        [SCAL] (1) fullMedium2.adiabaticModel.s_in = (if noEvent(fullMedium2.adiabaticModel.state_in.T < 1000.0) then 188.9244822140674 * (((-7.04827944) + 626.411601 / fullMedium2.adiabaticModel.state_in.T + 5.30172524 * log(fullMedium2.adiabaticModel.state_in.T) + fullMedium2.adiabaticModel.state_in.T * (0.002503813816 + fullMedium2.adiabaticModel.state_in.T * ((-1.063654364e-7) + fullMedium2.adiabaticModel.state_in.T * ((-2.563329593333333e-10) + 7.1241945025e-14 * fullMedium2.adiabaticModel.state_in.T)))) - 24718.2527 / (fullMedium2.adiabaticModel.state_in.T * fullMedium2.adiabaticModel.state_in.T)) else 188.9244822140674 * (((-26.52669281) + 1788.791477 / fullMedium2.adiabaticModel.state_in.T + 8.29152319 * log(fullMedium2.adiabaticModel.state_in.T) + fullMedium2.adiabaticModel.state_in.T * ((-9.22315678e-5) + fullMedium2.adiabaticModel.state_in.T * (2.43183844e-9 + fullMedium2.adiabaticModel.state_in.T * ((-6.303511039999999e-13) + 1.5825091474999999e-16 * fullMedium2.adiabaticModel.state_in.T)))) - 58848.12095 / (fullMedium2.adiabaticModel.state_in.T * fullMedium2.adiabaticModel.state_in.T))) - 188.9244822140674 * log(9.869232667160129e-6 * fullMedium2.adiabaticModel.state_in.p) ($RES_AUX_776)
(32|34)        [SCAL] (1) fullMedium2.adiabaticModel.h_in = ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"CO2\", 0.0440095, -8.941478544405185e6, 212805.6215135368, 1000.0, {49436.5054, -626.411601, 5.30172524, 0.002503813816, -2.127308728e-7, -7.68998878e-10, 2.849677801e-13}, {-45281.9846, -7.04827944}, {117696.2419, -1788.791477, 8.29152319, -9.22315678e-5, 4.86367688e-9, -1.891053312e-12, 6.330036589999999e-16}, {-39083.5059, -26.52669281}, 188.9244822140674), fullMedium2.adiabaticModel.state_in.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_AUX_777)
(33|35)        [SCAL] (1) fullMedium2.adiabaticModel.h_out_is = ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"CO2\", 0.0440095, -8.941478544405185e6, 212805.6215135368, 1000.0, {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), ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.fullMedium2.adiabaticModel.Medium.T_ps(fullMedium2.p_out, fullMedium2.adiabaticModel.s_in), true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_AUX_778)
(34|36)        [SCAL] (1) source3.outlet.state.p = fullMedium1.inlet.state.p ($RES_SIM_490)
(35|37)        [SCAL] (1) fullMedium1.pRatio = fullMedium1.p_out / fullMedium1.p_in ($RES_BND_541)
(36|38)        [SCAL] (1) fullMedium.pRatio_fixed = fullMedium.p_out / fullMedium.p_in ($RES_BND_509)
(37|39)        [SCAL] (1) fullMedium.outlet.state.T = sink.inlet.state.T ($RES_SIM_495)
(38|40)        [SCAL] (1) fullMedium.outlet.state.p = sink.inlet.state.p ($RES_SIM_496)
(39|41)        [SCAL] (1) $FUN_51 = abs(sink9.m_flow_fixed) ($RES_AUX_937)
(40|42)        [SCAL] (1) fullMedium2.adiabaticModel.w_t = fullMedium2.h_out - fullMedium2.adiabaticModel.h_in ($RES_SIM_300)
(41|43)        [SCAL] (1) $FUN_50 = abs(fullMedium1.P_in_internal) ($RES_AUX_938)
(42|44)        [SCAL] (1) fullMedium2.adiabaticModel.w_t_is = fullMedium2.adiabaticModel.h_out_is - fullMedium2.adiabaticModel.h_in ($RES_SIM_301)
(43|45)        [SCAL] (1) $FUN_14 = abs(fullMedium2.dh) ($RES_AUX_974)
(44|46)        [SCAL] (1) $DER.fullMedium2.m_flow * sink4.L = fullMedium2.outlet.r - sink4.r ($RES_SIM_302)
(45|47)        [SCAL] (1) $FUN_13 = abs(fullMedium1.P_in_internal) ($RES_AUX_975)
(46|48)        [RECD] (2) source4.outlet.state = $FUN_12 ($RES_SIM_303)
(47|50)        [SCAL] (1) source4.L * (-$DER.fullMedium2.m_flow) = source4.outlet.r ($RES_SIM_304)
(48|51)        [SCAL] (1) $FUN_10 = abs(sink3.m_flow_fixed) ($RES_AUX_978)
(49|52)        [SCAL] (1) $FUN_9 = abs(fullMedium1.P) ($RES_AUX_979)
(50|53)        [SCAL] (1) sink.p = sink.inlet.state.p ($RES_AUX_741)
(51|54)        [RECD] (2) fullMedium1.outlet.state = $FUN_11 ($RES_SIM_308)
(52|56)        [SCAL] (1) fullMedium.p_in = fullMedium.inlet.state.p ($RES_AUX_742)
(53|57)        [SCAL] (1) fullMedium.h_in = ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"CO2\", 0.0440095, -8.941478544405185e6, 212805.6215135368, 1000.0, {49436.5054, -626.411601, 5.30172524, 0.002503813816, -2.127308728e-7, -7.68998878e-10, 2.849677801e-13}, {-45281.9846, -7.04827944}, {117696.2419, -1788.791477, 8.29152319, -9.22315678e-5, 4.86367688e-9, -1.891053312e-12, 6.330036589999999e-16}, {-39083.5059, -26.52669281}, 188.9244822140674), fullMedium.inlet.state.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_AUX_743)
(54|58)        [SCAL] (1) fullMedium.adiabaticModel.p_in = fullMedium.adiabaticModel.state_in.p ($RES_AUX_744)
(55|59)        [SCAL] (1) fullMedium.adiabaticModel.s_in = (if noEvent(fullMedium.adiabaticModel.state_in.T < 1000.0) then 188.9244822140674 * (((-7.04827944) + 626.411601 / fullMedium.adiabaticModel.state_in.T + 5.30172524 * log(fullMedium.adiabaticModel.state_in.T) + fullMedium.adiabaticModel.state_in.T * (0.002503813816 + fullMedium.adiabaticModel.state_in.T * ((-1.063654364e-7) + fullMedium.adiabaticModel.state_in.T * ((-2.563329593333333e-10) + 7.1241945025e-14 * fullMedium.adiabaticModel.state_in.T)))) - 24718.2527 / (fullMedium.adiabaticModel.state_in.T * fullMedium.adiabaticModel.state_in.T)) else 188.9244822140674 * (((-26.52669281) + 1788.791477 / fullMedium.adiabaticModel.state_in.T + 8.29152319 * log(fullMedium.adiabaticModel.state_in.T) + fullMedium.adiabaticModel.state_in.T * ((-9.22315678e-5) + fullMedium.adiabaticModel.state_in.T * (2.43183844e-9 + fullMedium.adiabaticModel.state_in.T * ((-6.303511039999999e-13) + 1.5825091474999999e-16 * fullMedium.adiabaticModel.state_in.T)))) - 58848.12095 / (fullMedium.adiabaticModel.state_in.T * fullMedium.adiabaticModel.state_in.T))) - 188.9244822140674 * log(9.869232667160129e-6 * fullMedium.adiabaticModel.state_in.p) ($RES_AUX_745)
(56|60)        [SCAL] (1) fullMedium.adiabaticModel.h_in = ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"CO2\", 0.0440095, -8.941478544405185e6, 212805.6215135368, 1000.0, {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), fullMedium.adiabaticModel.state_in.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_AUX_746)
(57|61)        [SCAL] (1) fullMedium.adiabaticModel.w_t = if $SEV_0 then fullMedium.adiabaticModel.w_t_is / fullMedium.eta_fixed else fullMedium.adiabaticModel.w_t_is * fullMedium.eta_fixed ($RES_SIM_383)
(58|62)        [SCAL] (1) fullMedium.adiabaticModel.h_out_is = ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"CO2\", 0.0440095, -8.941478544405185e6, 212805.6215135368, 1000.0, {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), ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.fullMedium.adiabaticModel.Medium.T_ps(fullMedium.p_out, fullMedium.adiabaticModel.s_in), true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_AUX_747)
(59|63)        [SCAL] (1) $SEV_9 = fullMedium3.p_out >= fullMedium3.adiabaticModel.p_in ($RES_EVT_1077)
(60|64)        [SCAL] (1) fullMedium.adiabaticModel.w_t = fullMedium.h_out - fullMedium.adiabaticModel.h_in ($RES_SIM_386)
(61|65)        [SCAL] (1) fullMedium.adiabaticModel.w_t_is = fullMedium.adiabaticModel.h_out_is - fullMedium.adiabaticModel.h_in ($RES_SIM_387)
(62|66)        [SCAL] (1) $SEV_3 = fullMedium2.p_out >= fullMedium2.adiabaticModel.p_in ($RES_EVT_1071)
(63|67)        [SCAL] (1) source.outlet.state.T = fullMedium.inlet.state.T ($RES_SIM_501)
(64|68)        [SCAL] (1) $SEV_2 = fullMedium1.p_out >= fullMedium1.adiabaticModel.p_in ($RES_EVT_1070)
(65|69)        [SCAL] (1) source.outlet.state.p = fullMedium.inlet.state.p ($RES_SIM_502)
(66|70)        [SCAL] (1) fullMedium2.pRatio_fixed = fullMedium2.p_out / fullMedium2.p_in ($RES_BND_552)
(67|71)        [RECD] (2) fullMedium3.outlet.state = $FUN_52 ($RES_SIM_75)
(68|73)        [SCAL] (1) fullMedium3.p_out = fullMedium3.p_in + fullMedium3.dp ($RES_SIM_77)
(69|74)        [SCAL] (1) fullMedium1.p_out = fullMedium1.p_in + fullMedium1.dp ($RES_SIM_310)
(70|75)        [SCAL] (1) fullMedium3.pRatio = fullMedium3.p_out / fullMedium3.p_in ($RES_BND_671)
(71|76)        [SCAL] (1) $FUN_15.T = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.fullMedium2.Medium.T_h(fullMedium2.h_out) ($RES_SIM_1005)
(72|77)        [SCAL] (1) fullMedium1.singularityRegime = if noEvent($FUN_9 > 2.220446049250313e-16 and $FUN_10 < 2.220446049250313e-16) then 1.0 else 0.0 ($RES_SIM_313)
(73|78)        [SCAL] (1) $FUN_15.p = fullMedium2.p_out ($RES_SIM_1004)
(74|79)        [SCAL] (1) fullMedium1.P = sink3.m_flow_fixed * fullMedium1.dh ($RES_SIM_314)
(75|80)        [SCAL] (1) $FUN_12.T = source4.T0_par ($RES_SIM_1003)
(76|81)        [SCAL] (1) $FUN_12.p = source4.p0_par ($RES_SIM_1002)
(77|82)        [SCAL] (1) fullMedium1.dh = fullMedium1.h_out - fullMedium1.h_in ($RES_SIM_316)
(78|83)        [SCAL] (1) $FUN_11.T = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.fullMedium1.Medium.T_h(fullMedium1.h_out) ($RES_SIM_1001)
(79|84)        [SCAL] (1) ($DER.fullMedium1.dp * fullMedium1.TC) / fullMedium1.dp_nom = (fullMedium1.P_in_internal - fullMedium1.P) / fullMedium1.P_nom ($RES_SIM_317)
(80|85)        [SCAL] (1) $FUN_11.p = fullMedium1.p_out ($RES_SIM_1000)
(81|86)        [RECD] (2) source.outlet.state = $FUN_1 ($RES_SIM_391)
(82|88)        [SCAL] (1) $SEV_0 = fullMedium.p_out >= fullMedium.adiabaticModel.p_in ($RES_EVT_1068)
(83|89)        [SCAL] (1) fullMedium3.outlet.state.T = sink9.inlet.state.T ($RES_SIM_432)
(84|90)        [SCAL] (1) fullMedium3.outlet.state.p = sink9.inlet.state.p ($RES_SIM_433)
(85|91)        [SCAL] (1) source9.outlet.state.T = fullMedium3.inlet.state.T ($RES_SIM_435)
(86|92)        [SCAL] (1) source9.outlet.state.p = fullMedium3.inlet.state.p ($RES_SIM_436)
(87|93)        [SCAL] (1) fullMedium3.singularityRegime = if noEvent($FUN_50 > 2.220446049250313e-16 and $FUN_51 < 2.220446049250313e-16) then 1.0 else 0.0 ($RES_SIM_80)
(88|94)        [SCAL] (1) fullMedium3.dh = (sink9.m_flow_fixed * fullMedium1.P_in_internal) / (4.930380657631324e-32 + sink9.m_flow_fixed ^ 2.0) ($RES_SIM_82)
(89|95)        [SCAL] (1) sink9.p = sink9.inlet.state.p ($RES_AUX_876)
(90|96)        [SCAL] (1) fullMedium3.dh = fullMedium3.h_out - fullMedium3.h_in ($RES_SIM_84)
(91|97)        [SCAL] (1) fullMedium3.p_in = fullMedium3.inlet.state.p ($RES_AUX_877)
(92|98)        [SCAL] (1) fullMedium3.h_in = ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"CO2\", 0.0440095, -8.941478544405185e6, 212805.6215135368, 1000.0, {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), fullMedium3.inlet.state.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_AUX_878)
(93|99)        [SCAL] (1) $FUN_52.T = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.fullMedium3.Medium.T_h(fullMedium3.h_out) ($RES_SIM_1039)
(94|100)       [SCAL] (1) fullMedium3.adiabaticModel.p_in = fullMedium3.adiabaticModel.state_in.p ($RES_AUX_879)
(95|101)       [SCAL] (1) $FUN_52.p = fullMedium3.p_out ($RES_SIM_1038)
(96|102)       [SCAL] (1) $FUN_49.T = source9.T0_par ($RES_SIM_1037)
(97|103)       [SCAL] (1) $FUN_49.p = source9.p0_par ($RES_SIM_1036)
(98|104)       [SCAL] (1) fullMedium3.adiabaticModel.w_t = if $SEV_9 then fullMedium3.adiabaticModel.w_t_is / fullMedium3.eta_fixed else fullMedium3.adiabaticModel.w_t_is * fullMedium3.eta_fixed ($RES_SIM_89)
(99|105)       [RECD] (2) fullMedium2.outlet.state = $FUN_15 ($RES_SIM_282)
(100|107)      [SCAL] (1) fullMedium1.adiabaticModel.w_t = if $SEV_2 then fullMedium1.adiabaticModel.w_t_is / fullMedium1.eta_fixed else fullMedium1.adiabaticModel.w_t_is * fullMedium1.eta_fixed ($RES_SIM_321)
(101|108)      [SCAL] (1) fullMedium2.p_out = fullMedium2.p_in + fullMedium2.dp ($RES_SIM_284)
(102|109)      [SCAL] (1) fullMedium2.outlet.r = source4.outlet.r - $DER.fullMedium2.m_flow * fullMedium2.L ($RES_SIM_285)
(103|110)      [RECD] (2) fullMedium.adiabaticModel.state_in = fullMedium.inlet.state ($RES_BND_721)
(104|112)      [SCAL] (1) fullMedium1.adiabaticModel.w_t = fullMedium1.h_out - fullMedium1.adiabaticModel.h_in ($RES_SIM_324)
(105|113)      [SCAL] (1) fullMedium2.singularityRegime = if noEvent($FUN_13 > 2.220446049250313e-16 and $FUN_14 < 2.220446049250313e-16) then -1.0 else 0.0 ($RES_SIM_287)
(106|114)      [SCAL] (1) fullMedium1.adiabaticModel.w_t_is = fullMedium1.adiabaticModel.h_out_is - fullMedium1.adiabaticModel.h_in ($RES_SIM_325)
(107|115)      [RECD] (2) fullMedium1.adiabaticModel.state_in = fullMedium1.inlet.state ($RES_BND_724)
(108|117)      [RECD] (2) fullMedium2.adiabaticModel.state_in = fullMedium2.inlet.state ($RES_BND_725)
(109|119)      [SCAL] (1) fullMedium2.m_flow = (fullMedium2.dh * fullMedium1.P_in_internal) / (4.930380657631324e-32 + fullMedium2.dh ^ 2.0) ($RES_SIM_289)
(110|120)      [RECD] (2) source3.outlet.state = $FUN_8 ($RES_SIM_329)
(111|122)      [SCAL] (1) $FUN_1.p = source.p0_par ($RES_SIM_988)
(112|123)      [SCAL] (1) $FUN_1.T = source.T0_par ($RES_SIM_989)
(113|124)      [SCAL] (1) sink3.p = sink3.inlet.state.p ($RES_AUX_766)
(114|125)      [SCAL] (1) fullMedium1.p_in = fullMedium1.inlet.state.p ($RES_AUX_767)
(115|126)      [RECD] (2) fullMedium.outlet.state = $FUN_2 ($RES_SIM_369)
(116|128)      [SCAL] (1) fullMedium1.h_in = ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"CO2\", 0.0440095, -8.941478544405185e6, 212805.6215135368, 1000.0, {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), fullMedium1.inlet.state.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_AUX_768)
(117|129)      [SCAL] (1) fullMedium1.adiabaticModel.p_in = fullMedium1.adiabaticModel.state_in.p ($RES_AUX_769)
(118|130)      [SCAL] (1) $DER.fullMedium.adiabaticModel.w_t_is = $DER.fullMedium.adiabaticModel.h_out_is - $DER.fullMedium.adiabaticModel.h_in ($RES_SIM_1080)
(119|131)      [SCAL] (1) $DER.source.outlet.state.T = $DER.fullMedium.inlet.state.T ($RES_SIM_1081)
(120|132)      [SCAL] (1) $DER.source.outlet.state.p = $DER.fullMedium.inlet.state.p ($RES_SIM_1082)
(121|133)      [SCAL] (1) 0.0 = ($DER.fullMedium2.p_out * fullMedium2.p_in - fullMedium2.p_out * $DER.fullMedium2.p_in) / fullMedium2.p_in ^ 2.0 ($RES_SIM_1083)
(122|134)      [SCAL] (1) $DER.source4.outlet.state.T = $DER.fullMedium2.inlet.state.T ($RES_SIM_1084)
(123|135)      [SCAL] (1) $DER.fullMedium1.P_in_internal = -gain.k * $DER.fullMedium.P_in_internal ($RES_SIM_1085)
(124|136)      [SCAL] (1) $DER.source4.outlet.state.p = $DER.fullMedium2.inlet.state.p ($RES_SIM_1086)
(125|137)      [SCAL] (1) $DER.$FUN_12.T = 0.0 ($RES_SIM_1087)
(126|138)      [SCAL] (1) $DER.$FUN_12.p = 0.0 ($RES_SIM_1088)
(127|139)      [SCAL] (1) $DER.fullMedium2.dh = $DER.fullMedium2.h_out - $DER.fullMedium2.h_in ($RES_SIM_1089)
(128|140)      [SCAL] (1) $DER.fullMedium2.adiabaticModel.w_t = if $SEV_3 then ($DER.fullMedium2.adiabaticModel.w_t_is * fullMedium2.eta_fixed) / fullMedium2.eta_fixed ^ 2.0 else $DER.fullMedium2.adiabaticModel.w_t_is * fullMedium2.eta_fixed ($RES_SIM_1090)
(129|141)      [RECD] (2) $DER.source.outlet.state = $DER.$FUN_1 ($RES_SIM_1091)
(130|143)      [SCAL] (1) $DER.fullMedium2.p_in = $DER.fullMedium2.inlet.state.p ($RES_SIM_1092)
(131|144)      [SCAL] (1) $DER.fullMedium.P_in_internal = sink.m_flow_fixed * $DER.fullMedium.dh ($RES_SIM_1093)
(132|145)      [SCAL] (1) $DER.fullMedium2.h_in = $fDER0.ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"CO2\", 0.0440095, -8.941478544405185e6, 212805.6215135368, 1000.0, {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), fullMedium2.inlet.state.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0, $DER.fullMedium2.inlet.state.T, 0.0) ($RES_SIM_1094)
(133|146)      [SCAL] (1) $DER.fullMedium.dh = $DER.fullMedium.h_out - $DER.fullMedium.h_in ($RES_SIM_1095)
(134|147)      [SCAL] (1) $DER.fullMedium2.adiabaticModel.s_in = (if noEvent(fullMedium2.adiabaticModel.state_in.T < 1000.0) then 188.9244822140674 * (((24718.2527 * ($DER.fullMedium2.adiabaticModel.state_in.T * fullMedium2.adiabaticModel.state_in.T + fullMedium2.adiabaticModel.state_in.T * $DER.fullMedium2.adiabaticModel.state_in.T)) / (fullMedium2.adiabaticModel.state_in.T * fullMedium2.adiabaticModel.state_in.T) ^ 2.0 + 5.30172524 * ((1/fullMedium2.adiabaticModel.state_in.T) * $DER.fullMedium2.adiabaticModel.state_in.T) + ($DER.fullMedium2.adiabaticModel.state_in.T * (0.002503813816 + fullMedium2.adiabaticModel.state_in.T * ((-1.063654364e-7) + fullMedium2.adiabaticModel.state_in.T * ((-2.563329593333333e-10) + 7.1241945025e-14 * fullMedium2.adiabaticModel.state_in.T))) + fullMedium2.adiabaticModel.state_in.T * ($DER.fullMedium2.adiabaticModel.state_in.T * ((-1.063654364e-7) + fullMedium2.adiabaticModel.state_in.T * ((-2.563329593333333e-10) + 7.1241945025e-14 * fullMedium2.adiabaticModel.state_in.T)) + fullMedium2.adiabaticModel.state_in.T * ($DER.fullMedium2.adiabaticModel.state_in.T * ((-2.563329593333333e-10) + 7.1241945025e-14 * fullMedium2.adiabaticModel.state_in.T) + fullMedium2.adiabaticModel.state_in.T * (7.1241945025e-14 * $DER.fullMedium2.adiabaticModel.state_in.T))))) - (626.411601 * $DER.fullMedium2.adiabaticModel.state_in.T) / fullMedium2.adiabaticModel.state_in.T ^ 2.0) else 188.9244822140674 * (((58848.12095 * ($DER.fullMedium2.adiabaticModel.state_in.T * fullMedium2.adiabaticModel.state_in.T + fullMedium2.adiabaticModel.state_in.T * $DER.fullMedium2.adiabaticModel.state_in.T)) / (fullMedium2.adiabaticModel.state_in.T * fullMedium2.adiabaticModel.state_in.T) ^ 2.0 + 8.29152319 * ((1/fullMedium2.adiabaticModel.state_in.T) * $DER.fullMedium2.adiabaticModel.state_in.T) + ($DER.fullMedium2.adiabaticModel.state_in.T * ((-9.22315678e-5) + fullMedium2.adiabaticModel.state_in.T * (2.43183844e-9 + fullMedium2.adiabaticModel.state_in.T * ((-6.303511039999999e-13) + 1.5825091474999999e-16 * fullMedium2.adiabaticModel.state_in.T))) + fullMedium2.adiabaticModel.state_in.T * ($DER.fullMedium2.adiabaticModel.state_in.T * (2.43183844e-9 + fullMedium2.adiabaticModel.state_in.T * ((-6.303511039999999e-13) + 1.5825091474999999e-16 * fullMedium2.adiabaticModel.state_in.T)) + fullMedium2.adiabaticModel.state_in.T * ($DER.fullMedium2.adiabaticModel.state_in.T * ((-6.303511039999999e-13) + 1.5825091474999999e-16 * fullMedium2.adiabaticModel.state_in.T) + fullMedium2.adiabaticModel.state_in.T * (1.5825091474999999e-16 * $DER.fullMedium2.adiabaticModel.state_in.T))))) - (1788.791477 * $DER.fullMedium2.adiabaticModel.state_in.T) / fullMedium2.adiabaticModel.state_in.T ^ 2.0)) - 188.9244822140674 * ((1/(9.869232667160129e-6 * fullMedium2.adiabaticModel.state_in.p)) * (9.869232667160129e-6 * $DER.fullMedium2.adiabaticModel.state_in.p)) ($RES_SIM_1096)
(135|148)      [SCAL] (1) $DER.fullMedium2.adiabaticModel.h_in = $fDER0.ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"CO2\", 0.0440095, -8.941478544405185e6, 212805.6215135368, 1000.0, {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), fullMedium2.adiabaticModel.state_in.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0, $DER.fullMedium2.adiabaticModel.state_in.T, 0.0) ($RES_SIM_1097)
(136|149)      [SCAL] (1) $DER.fullMedium2.adiabaticModel.h_out_is = $fDER0.ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"CO2\", 0.0440095, -8.941478544405185e6, 212805.6215135368, 1000.0, {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), ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.fullMedium2.adiabaticModel.Medium.T_ps(fullMedium2.p_out, fullMedium2.adiabaticModel.s_in), true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0, $fDER0.ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.fullMedium2.adiabaticModel.Medium.T_ps(fullMedium2.p_out, fullMedium2.adiabaticModel.s_in, $DER.fullMedium2.p_out, $DER.fullMedium2.adiabaticModel.s_in), 0.0) ($RES_SIM_1098)
(137|150)      [SCAL] (1) 0.0 = ($DER.fullMedium.p_out * fullMedium.p_in - fullMedium.p_out * $DER.fullMedium.p_in) / fullMedium.p_in ^ 2.0 ($RES_SIM_1099)
(138|151)      [SCAL] (1) $DER.fullMedium2.adiabaticModel.w_t = $DER.fullMedium2.h_out - $DER.fullMedium2.adiabaticModel.h_in ($RES_SIM_1100)
(139|152)      [SCAL] (1) $DER.fullMedium2.adiabaticModel.w_t_is = $DER.fullMedium2.adiabaticModel.h_out_is - $DER.fullMedium2.adiabaticModel.h_in ($RES_SIM_1101)
(140|153)      [RECD] (2) $DER.fullMedium.adiabaticModel.state_in = $DER.fullMedium.inlet.state ($RES_SIM_1102)
(141|155)      [RECD] (2) $DER.source4.outlet.state = $DER.$FUN_12 ($RES_SIM_1103)
(142|157)      [RECD] (2) $DER.fullMedium2.adiabaticModel.state_in = $DER.fullMedium2.inlet.state ($RES_SIM_1104)
(143|159)      [SCAL] (1) $DER.fullMedium2.m_flow = (($DER.fullMedium2.dh * fullMedium1.P_in_internal + fullMedium2.dh * $DER.fullMedium1.P_in_internal) * (4.930380657631324e-32 + fullMedium2.dh ^ 2.0) - (2.0 * fullMedium2.dh * $DER.fullMedium2.dh) * fullMedium2.dh * fullMedium1.P_in_internal) / (4.930380657631324e-32 + fullMedium2.dh ^ 2.0) ^ 2.0 ($RES_SIM_1105)
(144|160)      [SCAL] (1) $DER.$FUN_1.p = 0.0 ($RES_SIM_1106)
(145|161)      [SCAL] (1) $DER.$FUN_1.T = 0.0 ($RES_SIM_1107)
(146|162)      [SCAL] (1) $DER.fullMedium.p_in = $DER.fullMedium.inlet.state.p ($RES_SIM_1108)
(147|163)      [SCAL] (1) $DER.fullMedium.h_in = $fDER0.ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"CO2\", 0.0440095, -8.941478544405185e6, 212805.6215135368, 1000.0, {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), fullMedium.inlet.state.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0, $DER.fullMedium.inlet.state.T, 0.0) ($RES_SIM_1109)
(148|164)      [SCAL] (1) $DER.fullMedium.adiabaticModel.s_in = (if noEvent(fullMedium.adiabaticModel.state_in.T < 1000.0) then 188.9244822140674 * (((24718.2527 * ($DER.fullMedium.adiabaticModel.state_in.T * fullMedium.adiabaticModel.state_in.T + fullMedium.adiabaticModel.state_in.T * $DER.fullMedium.adiabaticModel.state_in.T)) / (fullMedium.adiabaticModel.state_in.T * fullMedium.adiabaticModel.state_in.T) ^ 2.0 + 5.30172524 * ((1/fullMedium.adiabaticModel.state_in.T) * $DER.fullMedium.adiabaticModel.state_in.T) + ($DER.fullMedium.adiabaticModel.state_in.T * (0.002503813816 + fullMedium.adiabaticModel.state_in.T * ((-1.063654364e-7) + fullMedium.adiabaticModel.state_in.T * ((-2.563329593333333e-10) + 7.1241945025e-14 * fullMedium.adiabaticModel.state_in.T))) + fullMedium.adiabaticModel.state_in.T * ($DER.fullMedium.adiabaticModel.state_in.T * ((-1.063654364e-7) + fullMedium.adiabaticModel.state_in.T * ((-2.563329593333333e-10) + 7.1241945025e-14 * fullMedium.adiabaticModel.state_in.T)) + fullMedium.adiabaticModel.state_in.T * ($DER.fullMedium.adiabaticModel.state_in.T * ((-2.563329593333333e-10) + 7.1241945025e-14 * fullMedium.adiabaticModel.state_in.T) + fullMedium.adiabaticModel.state_in.T * (7.1241945025e-14 * $DER.fullMedium.adiabaticModel.state_in.T))))) - (626.411601 * $DER.fullMedium.adiabaticModel.state_in.T) / fullMedium.adiabaticModel.state_in.T ^ 2.0) else 188.9244822140674 * (((58848.12095 * ($DER.fullMedium.adiabaticModel.state_in.T * fullMedium.adiabaticModel.state_in.T + fullMedium.adiabaticModel.state_in.T * $DER.fullMedium.adiabaticModel.state_in.T)) / (fullMedium.adiabaticModel.state_in.T * fullMedium.adiabaticModel.state_in.T) ^ 2.0 + 8.29152319 * ((1/fullMedium.adiabaticModel.state_in.T) * $DER.fullMedium.adiabaticModel.state_in.T) + ($DER.fullMedium.adiabaticModel.state_in.T * ((-9.22315678e-5) + fullMedium.adiabaticModel.state_in.T * (2.43183844e-9 + fullMedium.adiabaticModel.state_in.T * ((-6.303511039999999e-13) + 1.5825091474999999e-16 * fullMedium.adiabaticModel.state_in.T))) + fullMedium.adiabaticModel.state_in.T * ($DER.fullMedium.adiabaticModel.state_in.T * (2.43183844e-9 + fullMedium.adiabaticModel.state_in.T * ((-6.303511039999999e-13) + 1.5825091474999999e-16 * fullMedium.adiabaticModel.state_in.T)) + fullMedium.adiabaticModel.state_in.T * ($DER.fullMedium.adiabaticModel.state_in.T * ((-6.303511039999999e-13) + 1.5825091474999999e-16 * fullMedium.adiabaticModel.state_in.T) + fullMedium.adiabaticModel.state_in.T * (1.5825091474999999e-16 * $DER.fullMedium.adiabaticModel.state_in.T))))) - (1788.791477 * $DER.fullMedium.adiabaticModel.state_in.T) / fullMedium.adiabaticModel.state_in.T ^ 2.0)) - 188.9244822140674 * ((1/(9.869232667160129e-6 * fullMedium.adiabaticModel.state_in.p)) * (9.869232667160129e-6 * $DER.fullMedium.adiabaticModel.state_in.p)) ($RES_SIM_1110)
(149|165)      [SCAL] (1) $DER.fullMedium.adiabaticModel.h_in = $fDER0.ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"CO2\", 0.0440095, -8.941478544405185e6, 212805.6215135368, 1000.0, {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), fullMedium.adiabaticModel.state_in.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0, $DER.fullMedium.adiabaticModel.state_in.T, 0.0) ($RES_SIM_1111)
(150|166)      [SCAL] (1) $DER.fullMedium.adiabaticModel.w_t = if $SEV_0 then ($DER.fullMedium.adiabaticModel.w_t_is * fullMedium.eta_fixed) / fullMedium.eta_fixed ^ 2.0 else $DER.fullMedium.adiabaticModel.w_t_is * fullMedium.eta_fixed ($RES_SIM_1112)
(151|167)      [SCAL] (1) $DER.fullMedium.adiabaticModel.h_out_is = $fDER0.ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"CO2\", 0.0440095, -8.941478544405185e6, 212805.6215135368, 1000.0, {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), ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.fullMedium.adiabaticModel.Medium.T_ps(fullMedium.p_out, fullMedium.adiabaticModel.s_in), true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0, $fDER0.ThermofluidStream.Idealized.Tests.Processes.Adiabatic.CompressorConstant.fullMedium.adiabaticModel.Medium.T_ps(fullMedium.p_out, fullMedium.adiabaticModel.s_in, $DER.fullMedium.p_out, $DER.fullMedium.adiabaticModel.s_in), 0.0) ($RES_SIM_1113)
(152|168)      [SCAL] (1) $DER.fullMedium.adiabaticModel.w_t = $DER.fullMedium.h_out - $DER.fullMedium.adiabaticModel.h_in ($RES_SIM_1114)


===================
  Scalar Matching
===================

variable to equation
**********************
	var 1 --> eqn 14
	var 2 --> eqn -1
	var 3 --> eqn 120
	var 4 --> eqn 22
	var 5 --> eqn 101
	var 6 --> eqn 44
	var 7 --> eqn 4
	var 8 --> eqn 8
	var 9 --> eqn -1
	var 10 --> eqn 42
	var 11 --> eqn 112
	var 12 --> eqn 79
	var 13 --> eqn -1
	var 14 --> eqn 19
	var 15 --> eqn 114
	var 16 --> eqn 100
	var 17 --> eqn -1
	var 18 --> eqn 27
	var 19 --> eqn 129
	var 20 --> eqn 62
	var 21 --> eqn 17
	var 22 --> eqn 103
	var 23 --> eqn 24
	var 24 --> eqn 122
	var 25 --> eqn 34
	var 26 --> eqn 116
	var 27 --> eqn 94
	var 28 --> eqn 75
	var 29 --> eqn -1
	var 30 --> eqn 37
	var 31 --> eqn 15
	var 32 --> eqn 23
	var 33 --> eqn 31
	var 34 --> eqn 115
	var 35 --> eqn 9
	var 36 --> eqn 121
	var 37 --> eqn 82
	var 38 --> eqn 45
	var 39 --> eqn 65
	var 40 --> eqn 96
	var 41 --> eqn 39
	var 42 --> eqn 104
	var 43 --> eqn -1
	var 44 --> eqn 107
	var 45 --> eqn 69
	var 46 --> eqn 38
	var 47 --> eqn 40
	var 48 --> eqn 52
	var 49 --> eqn 76
	var 50 --> eqn 80
	var 51 --> eqn 83
	var 52 --> eqn 50
	var 53 --> eqn 60
	var 54 --> eqn -1
	var 55 --> eqn 47
	var 56 --> eqn 89
	var 57 --> eqn 51
	var 58 --> eqn 1
	var 59 --> eqn 5
	var 60 --> eqn 63
	var 61 --> eqn 71
	var 62 --> eqn 66
	var 63 --> eqn 105
	var 64 --> eqn 68
	var 65 --> eqn 54
	var 66 --> eqn 72
	var 67 --> eqn 88
	var 68 --> eqn 106
	var 69 --> eqn 55
	var 70 --> eqn 78
	var 71 --> eqn 81
	var 72 --> eqn 85
	var 73 --> eqn 125
	var 74 --> eqn 56
	var 75 --> eqn 26
	var 76 --> eqn -1
	var 77 --> eqn 97
	var 78 --> eqn 30
	var 79 --> eqn 18
	var 80 --> eqn 123
	var 81 --> eqn -1
	var 82 --> eqn 67
	var 83 --> eqn 61
	var 84 --> eqn 95
	var 85 --> eqn 13
	var 86 --> eqn 29
	var 87 --> eqn 91
	var 88 --> eqn 124
	var 89 --> eqn 3
	var 90 --> eqn 33
	var 91 --> eqn 21
	var 92 --> eqn 92
	var 93 --> eqn 12
	var 94 --> eqn 46
	var 95 --> eqn 36
	var 96 --> eqn 127
	var 97 --> eqn 28
	var 98 --> eqn 108
	var 99 --> eqn 73
	var 100 --> eqn 64
	var 101 --> eqn 99
	var 102 --> eqn 58
	var 103 --> eqn 11
	var 104 --> eqn 20
	var 105 --> eqn 32
	var 106 --> eqn 84
	var 107 --> eqn 35
	var 108 --> eqn 59
	var 109 --> eqn 25
	var 110 --> eqn 126
	var 111 --> eqn 53
	var 112 --> eqn 77
	var 113 --> eqn 113
	var 114 --> eqn 93
	var 115 --> eqn 109
	var 116 --> eqn 98
	var 117 --> eqn 90
	var 118 --> eqn 16
	var 119 --> eqn 128
	var 120 --> eqn 102
	var 121 --> eqn 2
	var 122 --> eqn 74
	var 123 --> eqn 7
	var 124 --> eqn 70
	var 125 --> eqn 6
	var 126 --> eqn 41
	var 127 --> eqn 57
	var 128 --> eqn 43
	var 129 --> eqn 10
	var 130 --> eqn -1
	var 131 --> eqn -1
	var 132 --> eqn -1
	var 133 --> eqn -1
	var 134 --> eqn 137
	var 135 --> eqn 138
	var 136 --> eqn 141
	var 137 --> eqn 142
	var 138 --> eqn -1
	var 139 --> eqn -1
	var 140 --> eqn 136
	var 141 --> eqn 143
	var 142 --> eqn -1
	var 143 --> eqn 134
	var 144 --> eqn 145
	var 145 --> eqn 144
	var 146 --> eqn -1
	var 147 --> eqn 147
	var 148 --> eqn 149
	var 149 --> eqn 133
	var 150 --> eqn 139
	var 151 --> eqn 151
	var 152 --> eqn 148
	var 153 --> eqn 152
	var 154 --> eqn 140
	var 155 --> eqn 153
	var 156 --> eqn 154
	var 157 --> eqn -1
	var 158 --> eqn -1
	var 159 --> eqn 155
	var 160 --> eqn 156
	var 161 --> eqn -1
	var 162 --> eqn -1
	var 163 --> eqn 157
	var 164 --> eqn 158
	var 165 --> eqn -1
	var 166 --> eqn -1
	var 167 --> eqn 135
	var 168 --> eqn 159
	var 169 --> eqn 160
	var 170 --> eqn 161
	var 171 --> eqn 132
	var 172 --> eqn 162
	var 173 --> eqn 131
	var 174 --> eqn 163
	var 175 --> eqn 164
	var 176 --> eqn -1
	var 177 --> eqn 166
	var 178 --> eqn 167
	var 179 --> eqn 150
	var 180 --> eqn 130
	var 181 --> eqn 165
	var 182 --> eqn 146
	var 183 --> eqn 168
	var 184 --> eqn 119

equation to variable
**********************
	eqn 1 --> var 58
	eqn 2 --> var 121
	eqn 3 --> var 89
	eqn 4 --> var 7
	eqn 5 --> var 59
	eqn 6 --> var 125
	eqn 7 --> var 123
	eqn 8 --> var 8
	eqn 9 --> var 35
	eqn 10 --> var 129
	eqn 11 --> var 103
	eqn 12 --> var 93
	eqn 13 --> var 85
	eqn 14 --> var 1
	eqn 15 --> var 31
	eqn 16 --> var 118
	eqn 17 --> var 21
	eqn 18 --> var 79
	eqn 19 --> var 14
	eqn 20 --> var 104
	eqn 21 --> var 91
	eqn 22 --> var 4
	eqn 23 --> var 32
	eqn 24 --> var 23
	eqn 25 --> var 109
	eqn 26 --> var 75
	eqn 27 --> var 18
	eqn 28 --> var 97
	eqn 29 --> var 86
	eqn 30 --> var 78
	eqn 31 --> var 33
	eqn 32 --> var 105
	eqn 33 --> var 90
	eqn 34 --> var 25
	eqn 35 --> var 107
	eqn 36 --> var 95
	eqn 37 --> var 30
	eqn 38 --> var 46
	eqn 39 --> var 41
	eqn 40 --> var 47
	eqn 41 --> var 126
	eqn 42 --> var 10
	eqn 43 --> var 128
	eqn 44 --> var 6
	eqn 45 --> var 38
	eqn 46 --> var 94
	eqn 47 --> var 55
	eqn 48 --> var -1
	eqn 49 --> var -1
	eqn 50 --> var 52
	eqn 51 --> var 57
	eqn 52 --> var 48
	eqn 53 --> var 111
	eqn 54 --> var 65
	eqn 55 --> var 69
	eqn 56 --> var 74
	eqn 57 --> var 127
	eqn 58 --> var 102
	eqn 59 --> var 108
	eqn 60 --> var 53
	eqn 61 --> var 83
	eqn 62 --> var 20
	eqn 63 --> var 60
	eqn 64 --> var 100
	eqn 65 --> var 39
	eqn 66 --> var 62
	eqn 67 --> var 82
	eqn 68 --> var 64
	eqn 69 --> var 45
	eqn 70 --> var 124
	eqn 71 --> var 61
	eqn 72 --> var 66
	eqn 73 --> var 99
	eqn 74 --> var 122
	eqn 75 --> var 28
	eqn 76 --> var 49
	eqn 77 --> var 112
	eqn 78 --> var 70
	eqn 79 --> var 12
	eqn 80 --> var 50
	eqn 81 --> var 71
	eqn 82 --> var 37
	eqn 83 --> var 51
	eqn 84 --> var 106
	eqn 85 --> var 72
	eqn 86 --> var -1
	eqn 87 --> var -1
	eqn 88 --> var 67
	eqn 89 --> var 56
	eqn 90 --> var 117
	eqn 91 --> var 87
	eqn 92 --> var 92
	eqn 93 --> var 114
	eqn 94 --> var 27
	eqn 95 --> var 84
	eqn 96 --> var 40
	eqn 97 --> var 77
	eqn 98 --> var 116
	eqn 99 --> var 101
	eqn 100 --> var 16
	eqn 101 --> var 5
	eqn 102 --> var 120
	eqn 103 --> var 22
	eqn 104 --> var 42
	eqn 105 --> var 63
	eqn 106 --> var 68
	eqn 107 --> var 44
	eqn 108 --> var 98
	eqn 109 --> var 115
	eqn 110 --> var -1
	eqn 111 --> var -1
	eqn 112 --> var 11
	eqn 113 --> var 113
	eqn 114 --> var 15
	eqn 115 --> var 34
	eqn 116 --> var 26
	eqn 117 --> var -1
	eqn 118 --> var -1
	eqn 119 --> var 184
	eqn 120 --> var 3
	eqn 121 --> var 36
	eqn 122 --> var 24
	eqn 123 --> var 80
	eqn 124 --> var 88
	eqn 125 --> var 73
	eqn 126 --> var 110
	eqn 127 --> var 96
	eqn 128 --> var 119
	eqn 129 --> var 19
	eqn 130 --> var 180
	eqn 131 --> var 173
	eqn 132 --> var 171
	eqn 133 --> var 149
	eqn 134 --> var 143
	eqn 135 --> var 167
	eqn 136 --> var 140
	eqn 137 --> var 134
	eqn 138 --> var 135
	eqn 139 --> var 150
	eqn 140 --> var 154
	eqn 141 --> var 136
	eqn 142 --> var 137
	eqn 143 --> var 141
	eqn 144 --> var 145
	eqn 145 --> var 144
	eqn 146 --> var 182
	eqn 147 --> var 147
	eqn 148 --> var 152
	eqn 149 --> var 148
	eqn 150 --> var 179
	eqn 151 --> var 151
	eqn 152 --> var 153
	eqn 153 --> var 155
	eqn 154 --> var 156
	eqn 155 --> var 159
	eqn 156 --> var 160
	eqn 157 --> var 163
	eqn 158 --> var 164
	eqn 159 --> var 168
	eqn 160 --> var 169
	eqn 161 --> var 170
	eqn 162 --> var 172
	eqn 163 --> var 174
	eqn 164 --> var 175
	eqn 165 --> var 181
	eqn 166 --> var 177
	eqn 167 --> var 178
	eqn 168 --> var 183
"
[Timeout remaining time 658]
[Calling sys.exit(0), Time elapsed: 5.3463729321956635]
Failed to read output from testmodel.py, exit status != 0:
1.637602936476469 1.647236608 0.734512653
Calling exit ...
<OMPython.OMCSessionZMQ object at 0x7f1440f891b0>