Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2.conf.json
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"[<interactive>:1:22-1:33:writable] Warning: Modelica only supports 32-bit signed integers! Transforming: 13743895347 into a real
[<interactive>:1:1-1:33:writable] Error: Class GC_set_max_heap_size not found in scope <global scope> (looking for a function or record).
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo): time 0.0005075/0.0005075, allocations: 0 / 0, free: 0 / 0
"
[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 0.0004243/0.0004243, allocations: 0 / 0, free: 0 / 0
"
[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 0.3332/0.3332, allocations: 0 / 0, free: 0 / 0
"
[Timeout remaining time 180]
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 0.2074/0.2074, allocations: 0 / 0, free: 0 / 0
"
[Timeout remaining time 180]
Using package ThermofluidStream with version 1.4.0 (/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: "" <> buildModelFMU(ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2,fileNamePrefix="ThermofluidStream_dev_ThermofluidStream_Idealized_Tests_Processes_Adiabatic_Prescribed2",fmuType="me_cs",version="3.0",platforms={"wasm"})
"" <> buildModelFMU(ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2,fileNamePrefix="ThermofluidStream_dev_ThermofluidStream_Idealized_Tests_Processes_Adiabatic_Prescribed2",fmuType="me_cs",version="3.0",platforms={"wasm"}) [Timeout 660]
"Notification: Performance of FrontEnd - loaded program: time 2.715e-06/2.715e-06, allocations: 0 / 0, free: 0 / 0
Notification: Performance of FrontEnd - Absyn->SCode: time 1.592e-05/1.863e-05, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2): time 0.3303/0.3303, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFInst.instExpressions: time 0.02053/0.3508, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFInst.updateImplicitVariability: time 0.002223/0.353, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFTyping.typeComponents: time 0.003701/0.3567, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFTyping.typeBindings: time 0.009185/0.3659, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFTyping.typeClassSections: time 0.004462/0.3704, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFFlatten.flatten: time 0.003855/0.3742, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFFlatten.resolveConnections: time 0.0008339/0.3751, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFEvalConstants.evaluate: time 0.003941/0.379, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFSimplifyModel.simplify: time 0.002085/0.3811, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFPackage.collectConstants: time 0.0002427/0.3813, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFFlatten.collectFunctions: time 0.00594/0.3873, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFScalarize.scalarize: time 0.0004774/0.3878, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFVerifyModel.verify: time 0.00111/0.3889, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFConvertDAE.convert: time 0.007222/0.3961, allocations: 0 / 0, free: 0 / 0
Notification: Performance of FrontEnd - DAE generated: time 0.0002776/0.3964, allocations: 0 / 0, free: 0 / 0
Notification: Performance of FrontEnd: time 8.065e-06/0.3964, allocations: 0 / 0, free: 0 / 0
Notification: Performance of Transformations before backend: time 4.034e-05/0.3964, allocations: 0 / 0, free: 0 / 0
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 199
 * Number of variables: 199
Notification: Performance of Generate backend data structure: time 0.008952/0.4054, allocations: 0 / 0, free: 0 / 0
Notification: Performance of prepare preOptimizeDAE: time 0.0001462/0.4055, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt introduceOutputAliases (simulation): time 0.0008155/0.4063, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.001156/0.4075, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt evaluateParameters (simulation): time 0.00418/0.4117, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0005189/0.4122, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt expandDerOperator (simulation): time 0.0003854/0.4126, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt clockPartitioning (simulation): time 0.005382/0.418, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt findStateOrder (simulation): time 7.395e-05/0.418, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.0002722/0.4183, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt inlineArrayEqn (simulation): time 4.445e-05/0.4183, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.004709/0.4231, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.01166/0.4347, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt comSubExp (simulation): time 0.005189/0.4399, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt resolveLoops (simulation): time 0.001908/0.4418, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt evalFunc (simulation): time 0.001887/0.4437, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 0.002671/0.4464, allocations: 0 / 0, free: 0 / 0
Notification: Performance of pre-optimization done (n=78): time 0.0001528/0.4465, allocations: 0 / 0, free: 0 / 0
Notification: Performance of matching and sorting (n=78): time 0.006707/0.4532, allocations: 0 / 0, free: 0 / 0
Notification: Performance of inlineWhenForInitialization (initialization): time 0.0001227/0.4533, allocations: 0 / 0, free: 0 / 0
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.003044/0.4564, allocations: 0 / 0, free: 0 / 0
Notification: Performance of collectPreVariables (initialization): time 0.0003481/0.4567, allocations: 0 / 0, free: 0 / 0
Notification: Performance of collectInitialEqns (initialization): time 0.0008805/0.4576, allocations: 0 / 0, free: 0 / 0
Notification: Performance of collectInitialBindings (initialization): time 0.0004642/0.4581, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simplifyInitialFunctions (initialization): time 0.0009066/0.459, allocations: 0 / 0, free: 0 / 0
Notification: Performance of setup shared object (initialization): time 0.0002788/0.4593, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preBalanceInitialSystem (initialization): time 0.001944/0.4612, allocations: 0 / 0, free: 0 / 0
Notification: Performance of partitionIndependentBlocks (initialization): time 0.002147/0.4634, allocations: 0 / 0, free: 0 / 0
Notification: Performance of analyzeInitialSystem (initialization): time 0.003833/0.4672, allocations: 0 / 0, free: 0 / 0
Notification: Performance of solveInitialSystemEqSystem (initialization): time 1.607e-05/0.4672, allocations: 0 / 0, free: 0 / 0
Notification: Performance of matching and sorting (n=98) (initialization): time 0.006141/0.4733, allocations: 0 / 0, free: 0 / 0
Notification: Performance of prepare postOptimizeDAE: time 0.0001962/0.4735, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 2.289e-05/0.4736, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt tearingSystem (initialization): time 3.989e-05/0.4736, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.001326/0.4749, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 2.88e-05/0.475, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.001051/0.476, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.0002779/0.4763, allocations: 0 / 0, free: 0 / 0
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 10
 * Number of states: 0 ()
 * Number of discrete variables: 25 (isentropicEfficiency.count,$PRE.isentropicEfficiency.count,isentropicEfficiency.T_start,$PRE.isentropicEfficiency.T_start,massFlowRate.count,$PRE.massFlowRate.count,massFlowRate.T_start,$PRE.massFlowRate.T_start,pressureRatio.count,$PRE.pressureRatio.count,pressureRatio.T_start,$PRE.pressureRatio.T_start,inletTemperature.count,$PRE.inletTemperature.count,inletTemperature.T_start,$PRE.inletTemperature.T_start,inletPressure.count,$PRE.inletPressure.count,inletPressure.T_start,$PRE.inletPressure.T_start,$whenCondition1,$whenCondition2,$whenCondition3,$whenCondition4,$whenCondition5)
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for initialization (93):
 * Single equations (assignments): 88
 * Array equations: 0
 * Algorithm blocks: 5
 * Record equations: 0
 * When equations: 0
 * If-equations: 0
 * Equation systems (not torn): 0
 * Torn equation systems: 0
 * Mixed (continuous/discrete) equation systems: 0
Notification: Performance of prepare postOptimizeDAE: time 0.001589/0.4779, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0007207/0.4786, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.005948/0.4845, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt inlineArrayEqn (simulation): time 2.68e-05/0.4846, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt constantLinearSystem (simulation): time 2.409e-05/0.4846, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt simplifysemiLinear (simulation): time 3.31e-05/0.4846, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.003506/0.4881, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 1.16e-05/0.4882, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.001218/0.4894, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt tearingSystem (simulation): time 2.319e-05/0.4894, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt inputDerivativesUsed (simulation): time 0.0002235/0.4896, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 1.554e-05/0.4896, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 4.759e-06/0.4896, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt symbolicJacobian (simulation): time 0.007154/0.4968, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt removeConstants (simulation): time 0.001725/0.4985, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.0005522/0.4991, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0009848/0.5001, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt findZeroCrossings (simulation): time 0.0008748/0.5009, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt collapseArrayExpressions (simulation): time 0.0002585/0.5012, allocations: 0 / 0, free: 0 / 0
Notification: Performance of sorting global known variables: time 0.001803/0.503, allocations: 0 / 0, free: 0 / 0
Notification: Performance of sort global known variables: time 4.087e-05/0.503, allocations: 0 / 0, free: 0 / 0
Notification: Performance of remove unused functions: time 0.002802/0.5058, allocations: 0 / 0, free: 0 / 0
Notification: Model statistics after passing the back-end for simulation:
 * Number of independent subsystems: 1
 * Number of states: 1 (firstOrder.y)
 * Number of discrete variables: 15 ($whenCondition5,$whenCondition4,$whenCondition3,$whenCondition2,$whenCondition1,inletPressure.T_start,inletPressure.count,inletTemperature.T_start,inletTemperature.count,pressureRatio.T_start,pressureRatio.count,massFlowRate.T_start,massFlowRate.count,isentropicEfficiency.T_start,isentropicEfficiency.count)
 * Number of discrete states: 5 (inletPressure.count,inletTemperature.count,pressureRatio.count,massFlowRate.count,isentropicEfficiency.count)
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for simulation (78):
 * Single equations (assignments): 68
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 0
 * When equations: 10
 * If-equations: 0
 * Equation systems (not torn): 0
 * Torn equation systems: 0
 * Mixed (continuous/discrete) equation systems: 0
Notification: Performance of Backend phase and start with SimCode phase: time 0.01042/0.5163, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: created initialization part: time 0.00474/0.521, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: created event and clocks part: time 1.676e-05/0.521, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: created simulation system equations: time 0.002122/0.5231, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.004607/0.5277, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: created linear, non-linear and system jacobian parts: time 0.03553/0.5633, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: some other stuff during SimCode phase: time 0.001426/0.5647, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: alias equations: time 0.001747/0.5664, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: all other stuff during SimCode phase: time 0.002332/0.5688, allocations: 0 / 0, free: 0 / 0
Notification: Performance of SimCode: time 0.0008334/0.5696, allocations: 0 / 0, free: 0 / 0
Notification: Performance of FMU modelDescription.xml: time 0.01378/0.5834, allocations: 0 / 0, free: 0 / 0
Notification: Performance of FMU model kernel: time 0.007765/0.5912, allocations: 0 / 0, free: 0 / 0
Notification: Performance of FMU translated model: time 0.05273/0.6439, allocations: 0 / 0, free: 0 / 0
Notification: Performance of FMU component link: time 1.462e-05/0.6439, allocations: 0 / 0, free: 0 / 0
Notification: Performance of FMU precompile: time 1.996e-05/0.6439, allocations: 0 / 0, free: 0 / 0
Notification: Performance of FMU write (0.2 MB unzipped): time 0.0002649/0.6442, allocations: 0 / 0, free: 0 / 0
Notification: Building FMU for platform 'wasm' (1/1).
Notification: Finished FMU for platform 'wasm' (1/1).
"
[Timeout remaining time 659]
simulate(ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2,startTime=0,stopTime=1,tolerance=1e-06,numberOfIntervals=100,outputFormat="mat",variableFilter="CPUtime|EventCounter|P|T_in|Time|adiabaticModel.eta_is|adiabaticModel.h_in|adiabaticModel.h_out|adiabaticModel.h_out_is|adiabaticModel.p_out|adiabaticModel.s_in|adiabaticModel.state_in.T|adiabaticModel.state_in.p|adiabaticModel.w_t|adiabaticModel.w_t_is|dh|dp|dp1.P|dp1.P_in|dp1.P_nom|dp1.TC|dp1.adiabaticModel.eta_is|dp1.adiabaticModel.h_in|dp1.adiabaticModel.h_out|dp1.adiabaticModel.h_out_is|dp1.adiabaticModel.p_out|dp1.adiabaticModel.s_in|dp1.adiabaticModel.state_in.T|dp1.adiabaticModel.state_in.p|dp1.adiabaticModel.w_t|dp1.adiabaticModel.w_t_is|dp1.assertionLevel|dp1.clip_p_out|dp1.dh|dp1.dp|dp1.dp_fixed|dp1.dp_nom|dp1.dp_start|dp1.dr_corr|dp1.etaSpec|dp1.eta_actual|dp1.eta_fixed|dp1.eta_is|dp1.eta_prescribed|dp1.h_in|dp1.h_out|dp1.initM_flow|dp1.inlet.m_flow|dp1.inlet.r|dp1.inlet.state.T|dp1.inlet.state.p|dp1.m_acceleration_0|dp1.m_flow|dp1.m_flowStateSelect|dp1.m_flow_0|dp1.outlet.m_flow|dp1.outlet.r|dp1.outlet.state.T|dp1.outlet.state.p|dp1.outletSpec|dp1.outletSpec_actual|dp1.outletSpec_prescribed|dp1.outletValueSpec|dp1.pRatio|dp1.pRatio_fixed|dp1.p_in|dp1.p_min|dp1.p_out|dp1.p_out_fixed|dp1.singularityRegime|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|energyFlowSource.E_flow|energyFlowSource.E_flow_out|eta_is|firstOrder.T|der.firstOrder.y.|firstOrder.initType|firstOrder.k|firstOrder.u|firstOrder.y|firstOrder.y_start|h_in|h_out|inletPressure.T_start|inletPressure.amplitude|inletPressure.count|inletPressure.nperiod|inletPressure.offset|inletPressure.period|inletPressure.startTime|inletPressure.y|inletTemperature.T_start|inletTemperature.amplitude|inletTemperature.count|inletTemperature.nperiod|inletTemperature.offset|inletTemperature.period|inletTemperature.startTime|inletTemperature.y|isentropicEfficiency.T_start|isentropicEfficiency.amplitude|isentropicEfficiency.count|isentropicEfficiency.nperiod|isentropicEfficiency.offset|isentropicEfficiency.period|isentropicEfficiency.startTime|isentropicEfficiency.y|m_flow|massFlowRate.T_start|massFlowRate.amplitude|massFlowRate.count|massFlowRate.nperiod|massFlowRate.offset|massFlowRate.period|massFlowRate.startTime|massFlowRate.y|outletPressure.y|pOut1.P|pOut1.P_in|pOut1.P_nom|pOut1.TC|pOut1.adiabaticModel.eta_is|pOut1.adiabaticModel.h_in|pOut1.adiabaticModel.h_out|pOut1.adiabaticModel.h_out_is|pOut1.adiabaticModel.p_out|pOut1.adiabaticModel.s_in|pOut1.adiabaticModel.state_in.T|pOut1.adiabaticModel.state_in.p|pOut1.adiabaticModel.w_t|pOut1.adiabaticModel.w_t_is|pOut1.assertionLevel|pOut1.clip_p_out|pOut1.dh|pOut1.dp|pOut1.dp_fixed|pOut1.dp_nom|pOut1.dp_start|pOut1.dr_corr|pOut1.etaSpec|pOut1.eta_actual|pOut1.eta_fixed|pOut1.eta_is|pOut1.eta_prescribed|pOut1.h_in|pOut1.h_out|pOut1.initM_flow|pOut1.inlet.m_flow|pOut1.inlet.r|pOut1.inlet.state.T|pOut1.inlet.state.p|pOut1.m_acceleration_0|pOut1.m_flow|pOut1.m_flowStateSelect|pOut1.m_flow_0|pOut1.outlet.m_flow|pOut1.outlet.r|pOut1.outlet.state.T|pOut1.outlet.state.p|pOut1.outletSpec|pOut1.outletSpec_actual|pOut1.outletSpec_prescribed|pOut1.outletValueSpec|pOut1.pRatio|pOut1.pRatio_fixed|pOut1.p_in|pOut1.p_min|pOut1.p_out|pOut1.p_out_fixed|pOut1.singularityRegime|pRatio|pRatio1.P|pRatio1.P_in|pRatio1.P_nom|pRatio1.TC|pRatio1.adiabaticModel.eta_is|pRatio1.adiabaticModel.h_in|pRatio1.adiabaticModel.h_out|pRatio1.adiabaticModel.h_out_is|pRatio1.adiabaticModel.p_out|pRatio1.adiabaticModel.s_in|pRatio1.adiabaticModel.state_in.T|pRatio1.adiabaticModel.state_in.p|pRatio1.adiabaticModel.w_t|pRatio1.adiabaticModel.w_t_is|pRatio1.assertionLevel|pRatio1.clip_p_out|pRatio1.dh|pRatio1.dp|pRatio1.dp_fixed|pRatio1.dp_nom|pRatio1.dp_start|pRatio1.dr_corr|pRatio1.etaSpec|pRatio1.eta_actual|pRatio1.eta_fixed|pRatio1.eta_is|pRatio1.eta_prescribed|pRatio1.h_in|pRatio1.h_out|pRatio1.initM_flow|pRatio1.inlet.m_flow|pRatio1.inlet.r|pRatio1.inlet.state.T|pRatio1.inlet.state.p|pRatio1.m_acceleration_0|pRatio1.m_flow|pRatio1.m_flowStateSelect|pRatio1.m_flow_0|pRatio1.outlet.m_flow|pRatio1.outlet.r|pRatio1.outlet.state.T|pRatio1.outlet.state.p|pRatio1.outletSpec|pRatio1.outletSpec_actual|pRatio1.outletSpec_prescribed|pRatio1.outletValueSpec|pRatio1.pRatio|pRatio1.pRatio_fixed|pRatio1.p_in|pRatio1.p_min|pRatio1.p_out|pRatio1.p_out_fixed|pRatio1.singularityRegime|p_in|p_out|power.y|pressureDifference.y|pressureRatio.T_start|pressureRatio.amplitude|pressureRatio.count|pressureRatio.nperiod|pressureRatio.offset|pressureRatio.period|pressureRatio.startTime|pressureRatio.y|sink.inlet.m_flow|sink.inlet.r|sink.inlet.state.T|sink.inlet.state.p|sink1.inlet.m_flow|sink1.inlet.r|sink1.inlet.state.T|sink1.inlet.state.p|sink2.inlet.m_flow|sink2.inlet.r|sink2.inlet.state.T|sink2.inlet.state.p|source.T0|source.T0_par|source.T0_var|source.h0|source.h0_par|source.outlet.m_flow|source.outlet.r|source.outlet.state.T|source.outlet.state.p|source.p0|source.p0_par|source.p0_var|source1.T0|source1.T0_par|source1.T0_var|source1.h0|source1.h0_par|source1.outlet.m_flow|source1.outlet.r|source1.outlet.state.T|source1.outlet.state.p|source1.p0|source1.p0_par|source1.p0_var|source2.T0|source2.T0_par|source2.T0_var|source2.h0|source2.h0_par|source2.outlet.m_flow|source2.outlet.r|source2.outlet.state.T|source2.outlet.state.p|source2.p0|source2.p0_par|source2.p0_var|state_in.T|state_in.p",fileNamePrefix="ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2",simflags=" -alarm=240  -emit_protected -lv LOG_STATS -startTime=0 -stopTime=1 -tolerance=1e-06 -stepSize=0.01 -r=ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat",resimulateExecutable="ThermofluidStream_dev_ThermofluidStream_Idealized_Tests_Processes_Adiabatic_Prescribed2.fmu") [Timeout 240]
""
[Timeout remaining time 240]
diffSimulationResults("ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat","/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_ref.mat","/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2.diff",relTol=0.003,relTolDiffMinMax=0.003,rangeDelta=0.001) [Timeout 660]
"Error: Could not read variable CPUtime in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat.
Warning: Get data of variable CPUtime from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat failed!
Error: Could not read variable EventCounter in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat.
Warning: Get data of variable EventCounter from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat failed!
Error: Could not read variable dp1.P_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat.
Warning: Get data of variable dp1.P_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat failed!
Error: Could not read variable dp1.TC in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat.
Warning: Get data of variable dp1.TC from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat failed!
Error: Could not read variable dp1.dp_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat.
Warning: Get data of variable dp1.dp_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat failed!
Error: Could not read variable dp1.dp_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat.
Warning: Get data of variable dp1.dp_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat failed!
Error: Could not read variable dp1.dp_start in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat.
Warning: Get data of variable dp1.dp_start from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat failed!
Error: Could not read variable dp1.eta_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat.
Warning: Get data of variable dp1.eta_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat failed!
Error: Could not read variable dp1.pRatio_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat.
Warning: Get data of variable dp1.pRatio_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat failed!
Error: Could not read variable dp1.p_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat.
Warning: Get data of variable dp1.p_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat failed!
Error: Could not read variable pOut1.P_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat.
Warning: Get data of variable pOut1.P_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat failed!
Error: Could not read variable pOut1.TC in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat.
Warning: Get data of variable pOut1.TC from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat failed!
Error: Could not read variable pOut1.dp_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat.
Warning: Get data of variable pOut1.dp_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat failed!
Error: Could not read variable pOut1.dp_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat.
Warning: Get data of variable pOut1.dp_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat failed!
Error: Could not read variable pOut1.dp_start in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat.
Warning: Get data of variable pOut1.dp_start from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat failed!
Error: Could not read variable pOut1.eta_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat.
Warning: Get data of variable pOut1.eta_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat failed!
Error: Could not read variable pOut1.pRatio_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat.
Warning: Get data of variable pOut1.pRatio_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat failed!
Error: Could not read variable pOut1.p_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat.
Warning: Get data of variable pOut1.p_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat failed!
Error: Could not read variable pRatio1.P_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat.
Warning: Get data of variable pRatio1.P_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat failed!
Error: Could not read variable pRatio1.TC in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat.
Warning: Get data of variable pRatio1.TC from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat failed!
Error: Could not read variable pRatio1.dp_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat.
Warning: Get data of variable pRatio1.dp_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat failed!
Error: Could not read variable pRatio1.dp_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat.
Warning: Get data of variable pRatio1.dp_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat failed!
Error: Could not read variable pRatio1.dp_start in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat.
Warning: Get data of variable pRatio1.dp_start from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat failed!
Error: Could not read variable pRatio1.eta_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat.
Warning: Get data of variable pRatio1.eta_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat failed!
Error: Could not read variable pRatio1.pRatio_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat.
Warning: Get data of variable pRatio1.pRatio_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat failed!
Error: Could not read variable pRatio1.p_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat.
Warning: Get data of variable pRatio1.p_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_res.mat failed!
"
[Timeout remaining time 660]
Reference file matches
simulate(ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2,startTime=0,stopTime=1,tolerance=1e-06,numberOfIntervals=100,outputFormat="mat",variableFilter="CPUtime|EventCounter|P|T_in|Time|adiabaticModel.eta_is|adiabaticModel.h_in|adiabaticModel.h_out|adiabaticModel.h_out_is|adiabaticModel.p_out|adiabaticModel.s_in|adiabaticModel.state_in.T|adiabaticModel.state_in.p|adiabaticModel.w_t|adiabaticModel.w_t_is|dh|dp|dp1.P|dp1.P_in|dp1.P_nom|dp1.TC|dp1.adiabaticModel.eta_is|dp1.adiabaticModel.h_in|dp1.adiabaticModel.h_out|dp1.adiabaticModel.h_out_is|dp1.adiabaticModel.p_out|dp1.adiabaticModel.s_in|dp1.adiabaticModel.state_in.T|dp1.adiabaticModel.state_in.p|dp1.adiabaticModel.w_t|dp1.adiabaticModel.w_t_is|dp1.assertionLevel|dp1.clip_p_out|dp1.dh|dp1.dp|dp1.dp_fixed|dp1.dp_nom|dp1.dp_start|dp1.dr_corr|dp1.etaSpec|dp1.eta_actual|dp1.eta_fixed|dp1.eta_is|dp1.eta_prescribed|dp1.h_in|dp1.h_out|dp1.initM_flow|dp1.inlet.m_flow|dp1.inlet.r|dp1.inlet.state.T|dp1.inlet.state.p|dp1.m_acceleration_0|dp1.m_flow|dp1.m_flowStateSelect|dp1.m_flow_0|dp1.outlet.m_flow|dp1.outlet.r|dp1.outlet.state.T|dp1.outlet.state.p|dp1.outletSpec|dp1.outletSpec_actual|dp1.outletSpec_prescribed|dp1.outletValueSpec|dp1.pRatio|dp1.pRatio_fixed|dp1.p_in|dp1.p_min|dp1.p_out|dp1.p_out_fixed|dp1.singularityRegime|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|energyFlowSource.E_flow|energyFlowSource.E_flow_out|eta_is|firstOrder.T|der.firstOrder.y.|firstOrder.initType|firstOrder.k|firstOrder.u|firstOrder.y|firstOrder.y_start|h_in|h_out|inletPressure.T_start|inletPressure.amplitude|inletPressure.count|inletPressure.nperiod|inletPressure.offset|inletPressure.period|inletPressure.startTime|inletPressure.y|inletTemperature.T_start|inletTemperature.amplitude|inletTemperature.count|inletTemperature.nperiod|inletTemperature.offset|inletTemperature.period|inletTemperature.startTime|inletTemperature.y|isentropicEfficiency.T_start|isentropicEfficiency.amplitude|isentropicEfficiency.count|isentropicEfficiency.nperiod|isentropicEfficiency.offset|isentropicEfficiency.period|isentropicEfficiency.startTime|isentropicEfficiency.y|m_flow|massFlowRate.T_start|massFlowRate.amplitude|massFlowRate.count|massFlowRate.nperiod|massFlowRate.offset|massFlowRate.period|massFlowRate.startTime|massFlowRate.y|outletPressure.y|pOut1.P|pOut1.P_in|pOut1.P_nom|pOut1.TC|pOut1.adiabaticModel.eta_is|pOut1.adiabaticModel.h_in|pOut1.adiabaticModel.h_out|pOut1.adiabaticModel.h_out_is|pOut1.adiabaticModel.p_out|pOut1.adiabaticModel.s_in|pOut1.adiabaticModel.state_in.T|pOut1.adiabaticModel.state_in.p|pOut1.adiabaticModel.w_t|pOut1.adiabaticModel.w_t_is|pOut1.assertionLevel|pOut1.clip_p_out|pOut1.dh|pOut1.dp|pOut1.dp_fixed|pOut1.dp_nom|pOut1.dp_start|pOut1.dr_corr|pOut1.etaSpec|pOut1.eta_actual|pOut1.eta_fixed|pOut1.eta_is|pOut1.eta_prescribed|pOut1.h_in|pOut1.h_out|pOut1.initM_flow|pOut1.inlet.m_flow|pOut1.inlet.r|pOut1.inlet.state.T|pOut1.inlet.state.p|pOut1.m_acceleration_0|pOut1.m_flow|pOut1.m_flowStateSelect|pOut1.m_flow_0|pOut1.outlet.m_flow|pOut1.outlet.r|pOut1.outlet.state.T|pOut1.outlet.state.p|pOut1.outletSpec|pOut1.outletSpec_actual|pOut1.outletSpec_prescribed|pOut1.outletValueSpec|pOut1.pRatio|pOut1.pRatio_fixed|pOut1.p_in|pOut1.p_min|pOut1.p_out|pOut1.p_out_fixed|pOut1.singularityRegime|pRatio|pRatio1.P|pRatio1.P_in|pRatio1.P_nom|pRatio1.TC|pRatio1.adiabaticModel.eta_is|pRatio1.adiabaticModel.h_in|pRatio1.adiabaticModel.h_out|pRatio1.adiabaticModel.h_out_is|pRatio1.adiabaticModel.p_out|pRatio1.adiabaticModel.s_in|pRatio1.adiabaticModel.state_in.T|pRatio1.adiabaticModel.state_in.p|pRatio1.adiabaticModel.w_t|pRatio1.adiabaticModel.w_t_is|pRatio1.assertionLevel|pRatio1.clip_p_out|pRatio1.dh|pRatio1.dp|pRatio1.dp_fixed|pRatio1.dp_nom|pRatio1.dp_start|pRatio1.dr_corr|pRatio1.etaSpec|pRatio1.eta_actual|pRatio1.eta_fixed|pRatio1.eta_is|pRatio1.eta_prescribed|pRatio1.h_in|pRatio1.h_out|pRatio1.initM_flow|pRatio1.inlet.m_flow|pRatio1.inlet.r|pRatio1.inlet.state.T|pRatio1.inlet.state.p|pRatio1.m_acceleration_0|pRatio1.m_flow|pRatio1.m_flowStateSelect|pRatio1.m_flow_0|pRatio1.outlet.m_flow|pRatio1.outlet.r|pRatio1.outlet.state.T|pRatio1.outlet.state.p|pRatio1.outletSpec|pRatio1.outletSpec_actual|pRatio1.outletSpec_prescribed|pRatio1.outletValueSpec|pRatio1.pRatio|pRatio1.pRatio_fixed|pRatio1.p_in|pRatio1.p_min|pRatio1.p_out|pRatio1.p_out_fixed|pRatio1.singularityRegime|p_in|p_out|power.y|pressureDifference.y|pressureRatio.T_start|pressureRatio.amplitude|pressureRatio.count|pressureRatio.nperiod|pressureRatio.offset|pressureRatio.period|pressureRatio.startTime|pressureRatio.y|sink.inlet.m_flow|sink.inlet.r|sink.inlet.state.T|sink.inlet.state.p|sink1.inlet.m_flow|sink1.inlet.r|sink1.inlet.state.T|sink1.inlet.state.p|sink2.inlet.m_flow|sink2.inlet.r|sink2.inlet.state.T|sink2.inlet.state.p|source.T0|source.T0_par|source.T0_var|source.h0|source.h0_par|source.outlet.m_flow|source.outlet.r|source.outlet.state.T|source.outlet.state.p|source.p0|source.p0_par|source.p0_var|source1.T0|source1.T0_par|source1.T0_var|source1.h0|source1.h0_par|source1.outlet.m_flow|source1.outlet.r|source1.outlet.state.T|source1.outlet.state.p|source1.p0|source1.p0_par|source1.p0_var|source2.T0|source2.T0_par|source2.T0_var|source2.h0|source2.h0_par|source2.outlet.m_flow|source2.outlet.r|source2.outlet.state.T|source2.outlet.state.p|source2.p0|source2.p0_par|source2.p0_var|state_in.T|state_in.p",fileNamePrefix="ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2",simflags=" -alarm=240  -emit_protected -lv LOG_STATS -startTime=0 -stopTime=1 -tolerance=1e-06 -stepSize=0.01 -r=ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_me_res.mat -s fmi3:me:daskr",resimulateExecutable="ThermofluidStream_dev_ThermofluidStream_Idealized_Tests_Processes_Adiabatic_Prescribed2.fmu") [Timeout 240]
""
[Timeout remaining time 240]
diffSimulationResults("ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_me_res.mat","/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_ref.mat","/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_me.diff",relTol=0.003,relTolDiffMinMax=0.003,rangeDelta=0.001) [Timeout 660]
"Error: Could not read variable CPUtime in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_me_res.mat.
Warning: Get data of variable CPUtime from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_me_res.mat failed!
Error: Could not read variable EventCounter in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_me_res.mat.
Warning: Get data of variable EventCounter from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_me_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[1] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_me_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[1] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_me_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[2] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_me_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[2] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_me_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[3] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_me_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[3] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_me_res.mat failed!
Error: Could not read variable inletPressure.T_start in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_me_res.mat.
Warning: Get data of variable inletPressure.T_start from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_me_res.mat failed!
Error: Could not read variable inletPressure.count in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_me_res.mat.
Warning: Get data of variable inletPressure.count from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_me_res.mat failed!
Error: Could not read variable inletTemperature.T_start in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_me_res.mat.
Warning: Get data of variable inletTemperature.T_start from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_me_res.mat failed!
Error: Could not read variable inletTemperature.count in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_me_res.mat.
Warning: Get data of variable inletTemperature.count from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_me_res.mat failed!
Error: Could not read variable isentropicEfficiency.T_start in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_me_res.mat.
Warning: Get data of variable isentropicEfficiency.T_start from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_me_res.mat failed!
Error: Could not read variable isentropicEfficiency.count in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_me_res.mat.
Warning: Get data of variable isentropicEfficiency.count from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_me_res.mat failed!
Error: Could not read variable massFlowRate.T_start in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_me_res.mat.
Warning: Get data of variable massFlowRate.T_start from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_me_res.mat failed!
Error: Could not read variable massFlowRate.count in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_me_res.mat.
Warning: Get data of variable massFlowRate.count from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_me_res.mat failed!
Error: Could not read variable pressureRatio.T_start in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_me_res.mat.
Warning: Get data of variable pressureRatio.T_start from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_me_res.mat failed!
Error: Could not read variable pressureRatio.count in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_me_res.mat.
Warning: Get data of variable pressureRatio.count from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_me_res.mat failed!
"
[Timeout remaining time 660]
""

Variables in the reference:CPUtime,EventCounter,P,T_in,Time,adiabaticModel.eta_is,adiabaticModel.h_in,adiabaticModel.h_out,adiabaticModel.h_out_is,adiabaticModel.p_out,adiabaticModel.s_in,adiabaticModel.state_in.T,adiabaticModel.state_in.p,adiabaticModel.w_t,adiabaticModel.w_t_is,dh,dp,dp1.P,dp1.P_in,dp1.P_nom,dp1.TC,dp1.adiabaticModel.eta_is,dp1.adiabaticModel.h_in,dp1.adiabaticModel.h_out,dp1.adiabaticModel.h_out_is,dp1.adiabaticModel.p_out,dp1.adiabaticModel.s_in,dp1.adiabaticModel.state_in.T,dp1.adiabaticModel.state_in.p,dp1.adiabaticModel.w_t,dp1.adiabaticModel.w_t_is,dp1.assertionLevel,dp1.clip_p_out,dp1.dh,dp1.dp,dp1.dp_fixed,dp1.dp_nom,dp1.dp_start,dp1.dr_corr,dp1.etaSpec,dp1.eta_actual,dp1.eta_fixed,dp1.eta_is,dp1.eta_prescribed,dp1.h_in,dp1.h_out,dp1.initM_flow,dp1.inlet.m_flow,dp1.inlet.r,dp1.inlet.state.T,dp1.inlet.state.p,dp1.m_acceleration_0,dp1.m_flow,dp1.m_flowStateSelect,dp1.m_flow_0,dp1.outlet.m_flow,dp1.outlet.r,dp1.outlet.state.T,dp1.outlet.state.p,dp1.outletSpec,dp1.outletSpec_actual,dp1.outletSpec_prescribed,dp1.outletValueSpec,dp1.pRatio,dp1.pRatio_fixed,dp1.p_in,dp1.p_min,dp1.p_out,dp1.p_out_fixed,dp1.singularityRegime,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,energyFlowSource.E_flow,energyFlowSource.E_flow_out,eta_is,firstOrder.T,der(firstOrder.y),firstOrder.initType,firstOrder.k,firstOrder.u,firstOrder.y,firstOrder.y_start,h_in,h_out,inletPressure.T_start,inletPressure.amplitude,inletPressure.count,inletPressure.nperiod,inletPressure.offset,inletPressure.period,inletPressure.startTime,inletPressure.y,inletTemperature.T_start,inletTemperature.amplitude,inletTemperature.count,inletTemperature.nperiod,inletTemperature.offset,inletTemperature.period,inletTemperature.startTime,inletTemperature.y,isentropicEfficiency.T_start,isentropicEfficiency.amplitude,isentropicEfficiency.count,isentropicEfficiency.nperiod,isentropicEfficiency.offset,isentropicEfficiency.period,isentropicEfficiency.startTime,isentropicEfficiency.y,m_flow,massFlowRate.T_start,massFlowRate.amplitude,massFlowRate.count,massFlowRate.nperiod,massFlowRate.offset,massFlowRate.period,massFlowRate.startTime,massFlowRate.y,outletPressure.y,pOut1.P,pOut1.P_in,pOut1.P_nom,pOut1.TC,pOut1.adiabaticModel.eta_is,pOut1.adiabaticModel.h_in,pOut1.adiabaticModel.h_out,pOut1.adiabaticModel.h_out_is,pOut1.adiabaticModel.p_out,pOut1.adiabaticModel.s_in,pOut1.adiabaticModel.state_in.T,pOut1.adiabaticModel.state_in.p,pOut1.adiabaticModel.w_t,pOut1.adiabaticModel.w_t_is,pOut1.assertionLevel,pOut1.clip_p_out,pOut1.dh,pOut1.dp,pOut1.dp_fixed,pOut1.dp_nom,pOut1.dp_start,pOut1.dr_corr,pOut1.etaSpec,pOut1.eta_actual,pOut1.eta_fixed,pOut1.eta_is,pOut1.eta_prescribed,pOut1.h_in,pOut1.h_out,pOut1.initM_flow,pOut1.inlet.m_flow,pOut1.inlet.r,pOut1.inlet.state.T,pOut1.inlet.state.p,pOut1.m_acceleration_0,pOut1.m_flow,pOut1.m_flowStateSelect,pOut1.m_flow_0,pOut1.outlet.m_flow,pOut1.outlet.r,pOut1.outlet.state.T,pOut1.outlet.state.p,pOut1.outletSpec,pOut1.outletSpec_actual,pOut1.outletSpec_prescribed,pOut1.outletValueSpec,pOut1.pRatio,pOut1.pRatio_fixed,pOut1.p_in,pOut1.p_min,pOut1.p_out,pOut1.p_out_fixed,pOut1.singularityRegime,pRatio,pRatio1.P,pRatio1.P_in,pRatio1.P_nom,pRatio1.TC,pRatio1.adiabaticModel.eta_is,pRatio1.adiabaticModel.h_in,pRatio1.adiabaticModel.h_out,pRatio1.adiabaticModel.h_out_is,pRatio1.adiabaticModel.p_out,pRatio1.adiabaticModel.s_in,pRatio1.adiabaticModel.state_in.T,pRatio1.adiabaticModel.state_in.p,pRatio1.adiabaticModel.w_t,pRatio1.adiabaticModel.w_t_is,pRatio1.assertionLevel,pRatio1.clip_p_out,pRatio1.dh,pRatio1.dp,pRatio1.dp_fixed,pRatio1.dp_nom,pRatio1.dp_start,pRatio1.dr_corr,pRatio1.etaSpec,pRatio1.eta_actual,pRatio1.eta_fixed,pRatio1.eta_is,pRatio1.eta_prescribed,pRatio1.h_in,pRatio1.h_out,pRatio1.initM_flow,pRatio1.inlet.m_flow,pRatio1.inlet.r,pRatio1.inlet.state.T,pRatio1.inlet.state.p,pRatio1.m_acceleration_0,pRatio1.m_flow,pRatio1.m_flowStateSelect,pRatio1.m_flow_0,pRatio1.outlet.m_flow,pRatio1.outlet.r,pRatio1.outlet.state.T,pRatio1.outlet.state.p,pRatio1.outletSpec,pRatio1.outletSpec_actual,pRatio1.outletSpec_prescribed,pRatio1.outletValueSpec,pRatio1.pRatio,pRatio1.pRatio_fixed,pRatio1.p_in,pRatio1.p_min,pRatio1.p_out,pRatio1.p_out_fixed,pRatio1.singularityRegime,p_in,p_out,power.y,pressureDifference.y,pressureRatio.T_start,pressureRatio.amplitude,pressureRatio.count,pressureRatio.nperiod,pressureRatio.offset,pressureRatio.period,pressureRatio.startTime,pressureRatio.y,sink.inlet.m_flow,sink.inlet.r,sink.inlet.state.T,sink.inlet.state.p,sink1.inlet.m_flow,sink1.inlet.r,sink1.inlet.state.T,sink1.inlet.state.p,sink2.inlet.m_flow,sink2.inlet.r,sink2.inlet.state.T,sink2.inlet.state.p,source.T0,source.T0_par,source.T0_var,source.h0,source.h0_par,source.outlet.m_flow,source.outlet.r,source.outlet.state.T,source.outlet.state.p,source.p0,source.p0_par,source.p0_var,source1.T0,source1.T0_par,source1.T0_var,source1.h0,source1.h0_par,source1.outlet.m_flow,source1.outlet.r,source1.outlet.state.T,source1.outlet.state.p,source1.p0,source1.p0_par,source1.p0_var,source2.T0,source2.T0_par,source2.T0_var,source2.h0,source2.h0_par,source2.outlet.m_flow,source2.outlet.r,source2.outlet.state.T,source2.outlet.state.p,source2.p0,source2.p0_par,source2.p0_var,state_in.T,state_in.p

Variables in the result:P,T_in,__zc_0,__zc_1,__zc_10,__zc_11,__zc_12,__zc_13,__zc_2,__zc_3,__zc_4,__zc_5,__zc_6,__zc_7,__zc_8,__zc_9,adiabaticModel.eta_is,adiabaticModel.h_in,adiabaticModel.h_out,adiabaticModel.h_out_is,adiabaticModel.p_in,adiabaticModel.p_out,adiabaticModel.s_in,adiabaticModel.state_in.T,adiabaticModel.state_in.p,adiabaticModel.w_t,adiabaticModel.w_t_is,der(firstOrder.y),dh,dp,dp1.L,dp1.P,dp1.P_in,dp1.P_in_internal,dp1.P_nom,dp1.TC,dp1.adiabaticModel.eta_is,dp1.adiabaticModel.h_in,dp1.adiabaticModel.h_out,dp1.adiabaticModel.h_out_is,dp1.adiabaticModel.p_in,dp1.adiabaticModel.p_out,dp1.adiabaticModel.s_in,dp1.adiabaticModel.state_in.T,dp1.adiabaticModel.state_in.p,dp1.adiabaticModel.w_t,dp1.adiabaticModel.w_t_is,dp1.assertionLevel,dp1.clip_p_out,dp1.considerInertance,dp1.dh,dp1.displayInstanceName,dp1.displayParameters,dp1.dp,dp1.dp_fixed,dp1.dp_nom,dp1.dp_start,dp1.dr_corr,dp1.enableFilter,dp1.etaSpec,dp1.eta_fixed,dp1.eta_is,dp1.eta_prescribed,dp1.h_in,dp1.h_out,dp1.iconIsCompression,dp1.iconType,dp1.initM_flow,dp1.inlet.m_flow,dp1.inlet.r,dp1.inlet.state.T,dp1.inlet.state.p,dp1.m_acceleration_0,dp1.m_flow,dp1.m_flowStateSelect,dp1.m_flow_0,dp1.outlet.m_flow,dp1.outlet.r,dp1.outlet.state.T,dp1.outlet.state.p,dp1.outletSpec,dp1.outletSpec_prescribed,dp1.outletValueSpec,dp1.pRatio,dp1.pRatio_fixed,dp1.p_in,dp1.p_min,dp1.p_out,dp1.p_out_fixed,dp1.powerSignal,dp1.showEfficiency,dp1.showOutletSpecification,dp1.showPowerDirection,dp1.singularityRegime,dp1.specifyOutlet,dropOfCommons.L,dropOfCommons.assertionLevel,dropOfCommons.considerInertance,dropOfCommons.displayColor,dropOfCommons.displayInstanceNames,dropOfCommons.displayParameters,dropOfCommons.g,dropOfCommons.k_volume_damping,dropOfCommons.m_flow_reg,dropOfCommons.omega_reg,dropOfCommons.p_min,dropOfCommons.rho_min,energyFlowSource.E_flow,energyFlowSource.E_flow_out,eta_is,firstOrder.T,firstOrder.initType,firstOrder.k,firstOrder.u,firstOrder.y,firstOrder.y_start,h_in,h_out,inletPressure.amplitude,inletPressure.nperiod,inletPressure.offset,inletPressure.period,inletPressure.startTime,inletPressure.y,inletTemperature.amplitude,inletTemperature.nperiod,inletTemperature.offset,inletTemperature.period,inletTemperature.startTime,inletTemperature.y,isentropicEfficiency.amplitude,isentropicEfficiency.nperiod,isentropicEfficiency.offset,isentropicEfficiency.period,isentropicEfficiency.startTime,isentropicEfficiency.y,m_flow,massFlowRate.amplitude,massFlowRate.nperiod,massFlowRate.offset,massFlowRate.period,massFlowRate.startTime,massFlowRate.y,outletPressure.y,pOut1.L,pOut1.P,pOut1.P_in,pOut1.P_in_internal,pOut1.P_nom,pOut1.TC,pOut1.adiabaticModel.eta_is,pOut1.adiabaticModel.h_in,pOut1.adiabaticModel.h_out,pOut1.adiabaticModel.h_out_is,pOut1.adiabaticModel.p_in,pOut1.adiabaticModel.p_out,pOut1.adiabaticModel.s_in,pOut1.adiabaticModel.state_in.T,pOut1.adiabaticModel.state_in.p,pOut1.adiabaticModel.w_t,pOut1.adiabaticModel.w_t_is,pOut1.assertionLevel,pOut1.clip_p_out,pOut1.considerInertance,pOut1.dh,pOut1.displayInstanceName,pOut1.displayParameters,pOut1.dp,pOut1.dp_fixed,pOut1.dp_nom,pOut1.dp_start,pOut1.dr_corr,pOut1.enableFilter,pOut1.etaSpec,pOut1.eta_fixed,pOut1.eta_is,pOut1.eta_prescribed,pOut1.h_in,pOut1.h_out,pOut1.iconIsCompression,pOut1.iconType,pOut1.initM_flow,pOut1.inlet.m_flow,pOut1.inlet.r,pOut1.inlet.state.T,pOut1.inlet.state.p,pOut1.m_acceleration_0,pOut1.m_flow,pOut1.m_flowStateSelect,pOut1.m_flow_0,pOut1.outlet.m_flow,pOut1.outlet.r,pOut1.outlet.state.T,pOut1.outlet.state.p,pOut1.outletSpec,pOut1.outletSpec_prescribed,pOut1.outletValueSpec,pOut1.pRatio,pOut1.pRatio_fixed,pOut1.p_in,pOut1.p_min,pOut1.p_out,pOut1.p_out_fixed,pOut1.powerSignal,pOut1.showEfficiency,pOut1.showOutletSpecification,pOut1.showPowerDirection,pOut1.singularityRegime,pOut1.specifyOutlet,pRatio,pRatio1.L,pRatio1.P,pRatio1.P_in,pRatio1.P_in_internal,pRatio1.P_nom,pRatio1.TC,pRatio1.adiabaticModel.eta_is,pRatio1.adiabaticModel.h_in,pRatio1.adiabaticModel.h_out,pRatio1.adiabaticModel.h_out_is,pRatio1.adiabaticModel.p_in,pRatio1.adiabaticModel.p_out,pRatio1.adiabaticModel.s_in,pRatio1.adiabaticModel.state_in.T,pRatio1.adiabaticModel.state_in.p,pRatio1.adiabaticModel.w_t,pRatio1.adiabaticModel.w_t_is,pRatio1.assertionLevel,pRatio1.clip_p_out,pRatio1.considerInertance,pRatio1.dh,pRatio1.displayInstanceName,pRatio1.displayParameters,pRatio1.dp,pRatio1.dp_fixed,pRatio1.dp_nom,pRatio1.dp_start,pRatio1.dr_corr,pRatio1.enableFilter,pRatio1.etaSpec,pRatio1.eta_fixed,pRatio1.eta_is,pRatio1.eta_prescribed,pRatio1.h_in,pRatio1.h_out,pRatio1.iconIsCompression,pRatio1.iconType,pRatio1.initM_flow,pRatio1.inlet.m_flow,pRatio1.inlet.r,pRatio1.inlet.state.T,pRatio1.inlet.state.p,pRatio1.m_acceleration_0,pRatio1.m_flow,pRatio1.m_flowStateSelect,pRatio1.m_flow_0,pRatio1.outlet.m_flow,pRatio1.outlet.r,pRatio1.outlet.state.T,pRatio1.outlet.state.p,pRatio1.outletSpec,pRatio1.outletSpec_prescribed,pRatio1.outletValueSpec,pRatio1.pRatio,pRatio1.pRatio_fixed,pRatio1.p_in,pRatio1.p_min,pRatio1.p_out,pRatio1.p_out_fixed,pRatio1.powerSignal,pRatio1.showEfficiency,pRatio1.showOutletSpecification,pRatio1.showPowerDirection,pRatio1.singularityRegime,pRatio1.specifyOutlet,p_in,p_out,power.y,pressureDifference.y,pressureRatio.amplitude,pressureRatio.nperiod,pressureRatio.offset,pressureRatio.period,pressureRatio.startTime,pressureRatio.y,sink.L,sink.considerInertance,sink.displayInstanceName,sink.displayParameters,sink.inlet.m_flow,sink.inlet.r,sink.inlet.state.T,sink.inlet.state.p,sink.r,sink1.L,sink1.considerInertance,sink1.displayInstanceName,sink1.displayParameters,sink1.inlet.m_flow,sink1.inlet.r,sink1.inlet.state.T,sink1.inlet.state.p,sink1.r,sink2.L,sink2.considerInertance,sink2.displayInstanceName,sink2.displayParameters,sink2.inlet.m_flow,sink2.inlet.r,sink2.inlet.state.T,sink2.inlet.state.p,sink2.r,source.L,source.T0_par,source.T0_var,source.considerInertance,source.displayH,source.displayInertance,source.displayInstanceName,source.displayMassFractions,source.displayP,source.displayParameters,source.displayPressure,source.displayT,source.displayTemperature,source.displayXi,source.enthalpyFromInput,source.h0_par,source.outlet.m_flow,source.outlet.r,source.outlet.state.T,source.outlet.state.p,source.p0_par,source.p0_var,source.pressureFromInput,source.setEnthalpy,source.temperatureFromInput,source.xiFromInput,source1.L,source1.T0_par,source1.T0_var,source1.considerInertance,source1.displayH,source1.displayInertance,source1.displayInstanceName,source1.displayMassFractions,source1.displayP,source1.displayParameters,source1.displayPressure,source1.displayT,source1.displayTemperature,source1.displayXi,source1.enthalpyFromInput,source1.h0_par,source1.outlet.m_flow,source1.outlet.r,source1.outlet.state.T,source1.outlet.state.p,source1.p0_par,source1.p0_var,source1.pressureFromInput,source1.setEnthalpy,source1.temperatureFromInput,source1.xiFromInput,source2.L,source2.T0_par,source2.T0_var,source2.considerInertance,source2.displayH,source2.displayInertance,source2.displayInstanceName,source2.displayMassFractions,source2.displayP,source2.displayParameters,source2.displayPressure,source2.displayT,source2.displayTemperature,source2.displayXi,source2.enthalpyFromInput,source2.h0_par,source2.outlet.m_flow,source2.outlet.r,source2.outlet.state.T,source2.outlet.state.p,source2.p0_par,source2.p0_var,source2.pressureFromInput,source2.setEnthalpy,source2.temperatureFromInput,source2.xiFromInput,state_in.T,state_in.p,time
simulate(ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2,startTime=0,stopTime=1,tolerance=1e-06,numberOfIntervals=100,outputFormat="mat",variableFilter="CPUtime|EventCounter|P|T_in|Time|adiabaticModel.eta_is|adiabaticModel.h_in|adiabaticModel.h_out|adiabaticModel.h_out_is|adiabaticModel.p_out|adiabaticModel.s_in|adiabaticModel.state_in.T|adiabaticModel.state_in.p|adiabaticModel.w_t|adiabaticModel.w_t_is|dh|dp|dp1.P|dp1.P_in|dp1.P_nom|dp1.TC|dp1.adiabaticModel.eta_is|dp1.adiabaticModel.h_in|dp1.adiabaticModel.h_out|dp1.adiabaticModel.h_out_is|dp1.adiabaticModel.p_out|dp1.adiabaticModel.s_in|dp1.adiabaticModel.state_in.T|dp1.adiabaticModel.state_in.p|dp1.adiabaticModel.w_t|dp1.adiabaticModel.w_t_is|dp1.assertionLevel|dp1.clip_p_out|dp1.dh|dp1.dp|dp1.dp_fixed|dp1.dp_nom|dp1.dp_start|dp1.dr_corr|dp1.etaSpec|dp1.eta_actual|dp1.eta_fixed|dp1.eta_is|dp1.eta_prescribed|dp1.h_in|dp1.h_out|dp1.initM_flow|dp1.inlet.m_flow|dp1.inlet.r|dp1.inlet.state.T|dp1.inlet.state.p|dp1.m_acceleration_0|dp1.m_flow|dp1.m_flowStateSelect|dp1.m_flow_0|dp1.outlet.m_flow|dp1.outlet.r|dp1.outlet.state.T|dp1.outlet.state.p|dp1.outletSpec|dp1.outletSpec_actual|dp1.outletSpec_prescribed|dp1.outletValueSpec|dp1.pRatio|dp1.pRatio_fixed|dp1.p_in|dp1.p_min|dp1.p_out|dp1.p_out_fixed|dp1.singularityRegime|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|energyFlowSource.E_flow|energyFlowSource.E_flow_out|eta_is|firstOrder.T|der.firstOrder.y.|firstOrder.initType|firstOrder.k|firstOrder.u|firstOrder.y|firstOrder.y_start|h_in|h_out|inletPressure.T_start|inletPressure.amplitude|inletPressure.count|inletPressure.nperiod|inletPressure.offset|inletPressure.period|inletPressure.startTime|inletPressure.y|inletTemperature.T_start|inletTemperature.amplitude|inletTemperature.count|inletTemperature.nperiod|inletTemperature.offset|inletTemperature.period|inletTemperature.startTime|inletTemperature.y|isentropicEfficiency.T_start|isentropicEfficiency.amplitude|isentropicEfficiency.count|isentropicEfficiency.nperiod|isentropicEfficiency.offset|isentropicEfficiency.period|isentropicEfficiency.startTime|isentropicEfficiency.y|m_flow|massFlowRate.T_start|massFlowRate.amplitude|massFlowRate.count|massFlowRate.nperiod|massFlowRate.offset|massFlowRate.period|massFlowRate.startTime|massFlowRate.y|outletPressure.y|pOut1.P|pOut1.P_in|pOut1.P_nom|pOut1.TC|pOut1.adiabaticModel.eta_is|pOut1.adiabaticModel.h_in|pOut1.adiabaticModel.h_out|pOut1.adiabaticModel.h_out_is|pOut1.adiabaticModel.p_out|pOut1.adiabaticModel.s_in|pOut1.adiabaticModel.state_in.T|pOut1.adiabaticModel.state_in.p|pOut1.adiabaticModel.w_t|pOut1.adiabaticModel.w_t_is|pOut1.assertionLevel|pOut1.clip_p_out|pOut1.dh|pOut1.dp|pOut1.dp_fixed|pOut1.dp_nom|pOut1.dp_start|pOut1.dr_corr|pOut1.etaSpec|pOut1.eta_actual|pOut1.eta_fixed|pOut1.eta_is|pOut1.eta_prescribed|pOut1.h_in|pOut1.h_out|pOut1.initM_flow|pOut1.inlet.m_flow|pOut1.inlet.r|pOut1.inlet.state.T|pOut1.inlet.state.p|pOut1.m_acceleration_0|pOut1.m_flow|pOut1.m_flowStateSelect|pOut1.m_flow_0|pOut1.outlet.m_flow|pOut1.outlet.r|pOut1.outlet.state.T|pOut1.outlet.state.p|pOut1.outletSpec|pOut1.outletSpec_actual|pOut1.outletSpec_prescribed|pOut1.outletValueSpec|pOut1.pRatio|pOut1.pRatio_fixed|pOut1.p_in|pOut1.p_min|pOut1.p_out|pOut1.p_out_fixed|pOut1.singularityRegime|pRatio|pRatio1.P|pRatio1.P_in|pRatio1.P_nom|pRatio1.TC|pRatio1.adiabaticModel.eta_is|pRatio1.adiabaticModel.h_in|pRatio1.adiabaticModel.h_out|pRatio1.adiabaticModel.h_out_is|pRatio1.adiabaticModel.p_out|pRatio1.adiabaticModel.s_in|pRatio1.adiabaticModel.state_in.T|pRatio1.adiabaticModel.state_in.p|pRatio1.adiabaticModel.w_t|pRatio1.adiabaticModel.w_t_is|pRatio1.assertionLevel|pRatio1.clip_p_out|pRatio1.dh|pRatio1.dp|pRatio1.dp_fixed|pRatio1.dp_nom|pRatio1.dp_start|pRatio1.dr_corr|pRatio1.etaSpec|pRatio1.eta_actual|pRatio1.eta_fixed|pRatio1.eta_is|pRatio1.eta_prescribed|pRatio1.h_in|pRatio1.h_out|pRatio1.initM_flow|pRatio1.inlet.m_flow|pRatio1.inlet.r|pRatio1.inlet.state.T|pRatio1.inlet.state.p|pRatio1.m_acceleration_0|pRatio1.m_flow|pRatio1.m_flowStateSelect|pRatio1.m_flow_0|pRatio1.outlet.m_flow|pRatio1.outlet.r|pRatio1.outlet.state.T|pRatio1.outlet.state.p|pRatio1.outletSpec|pRatio1.outletSpec_actual|pRatio1.outletSpec_prescribed|pRatio1.outletValueSpec|pRatio1.pRatio|pRatio1.pRatio_fixed|pRatio1.p_in|pRatio1.p_min|pRatio1.p_out|pRatio1.p_out_fixed|pRatio1.singularityRegime|p_in|p_out|power.y|pressureDifference.y|pressureRatio.T_start|pressureRatio.amplitude|pressureRatio.count|pressureRatio.nperiod|pressureRatio.offset|pressureRatio.period|pressureRatio.startTime|pressureRatio.y|sink.inlet.m_flow|sink.inlet.r|sink.inlet.state.T|sink.inlet.state.p|sink1.inlet.m_flow|sink1.inlet.r|sink1.inlet.state.T|sink1.inlet.state.p|sink2.inlet.m_flow|sink2.inlet.r|sink2.inlet.state.T|sink2.inlet.state.p|source.T0|source.T0_par|source.T0_var|source.h0|source.h0_par|source.outlet.m_flow|source.outlet.r|source.outlet.state.T|source.outlet.state.p|source.p0|source.p0_par|source.p0_var|source1.T0|source1.T0_par|source1.T0_var|source1.h0|source1.h0_par|source1.outlet.m_flow|source1.outlet.r|source1.outlet.state.T|source1.outlet.state.p|source1.p0|source1.p0_par|source1.p0_var|source2.T0|source2.T0_par|source2.T0_var|source2.h0|source2.h0_par|source2.outlet.m_flow|source2.outlet.r|source2.outlet.state.T|source2.outlet.state.p|source2.p0|source2.p0_par|source2.p0_var|state_in.T|state_in.p",fileNamePrefix="ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2",simflags=" -alarm=240  -emit_protected -lv LOG_STATS -startTime=0 -stopTime=1 -tolerance=1e-06 -stepSize=0.01 -r=ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_cs_res.mat -s fmi3:cs",resimulateExecutable="ThermofluidStream_dev_ThermofluidStream_Idealized_Tests_Processes_Adiabatic_Prescribed2.fmu") [Timeout 240]
""
[Timeout remaining time 240]
diffSimulationResults("ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_cs_res.mat","/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_ref.mat","/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_cs.diff",relTol=0.003,relTolDiffMinMax=0.003,rangeDelta=0.001) [Timeout 660]
"Error: Could not read variable CPUtime in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_cs_res.mat.
Warning: Get data of variable CPUtime from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_cs_res.mat failed!
Error: Could not read variable EventCounter in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_cs_res.mat.
Warning: Get data of variable EventCounter from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_cs_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[1] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_cs_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[1] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_cs_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[2] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_cs_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[2] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_cs_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[3] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_cs_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[3] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_cs_res.mat failed!
Error: Could not read variable inletPressure.T_start in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_cs_res.mat.
Warning: Get data of variable inletPressure.T_start from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_cs_res.mat failed!
Error: Could not read variable inletPressure.count in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_cs_res.mat.
Warning: Get data of variable inletPressure.count from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_cs_res.mat failed!
Error: Could not read variable inletTemperature.T_start in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_cs_res.mat.
Warning: Get data of variable inletTemperature.T_start from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_cs_res.mat failed!
Error: Could not read variable inletTemperature.count in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_cs_res.mat.
Warning: Get data of variable inletTemperature.count from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_cs_res.mat failed!
Error: Could not read variable isentropicEfficiency.T_start in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_cs_res.mat.
Warning: Get data of variable isentropicEfficiency.T_start from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_cs_res.mat failed!
Error: Could not read variable isentropicEfficiency.count in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_cs_res.mat.
Warning: Get data of variable isentropicEfficiency.count from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_cs_res.mat failed!
Error: Could not read variable massFlowRate.T_start in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_cs_res.mat.
Warning: Get data of variable massFlowRate.T_start from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_cs_res.mat failed!
Error: Could not read variable massFlowRate.count in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_cs_res.mat.
Warning: Get data of variable massFlowRate.count from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_cs_res.mat failed!
Error: Could not read variable pressureRatio.T_start in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_cs_res.mat.
Warning: Get data of variable pressureRatio.T_start from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_cs_res.mat failed!
Error: Could not read variable pressureRatio.count in file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_cs_res.mat.
Warning: Get data of variable pressureRatio.count from file ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.Prescribed2_cs_res.mat failed!
"
[Timeout remaining time 660]
Reference file matches
[Calling sys.exit(0), Time elapsed: 2.187339562107809]