Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop.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 0.0007714/0.0007714, allocations: 76.16 kB / 9.861 MB, free: 0.8281 MB / 10.45 MB Notification: Performance of NFInstanceAPI.mkTop(): time 0.001068/0.001839, allocations: 443.8 kB / 10.29 MB, free: 404 kB / 10.45 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 0.0008621/0.0008621, allocations: 141.2 kB / 11.17 MB, free: 3 MB / 13.93 MB Notification: Performance of NFInstanceAPI.mkTop(): time 0.001015/0.001877, allocations: 475.6 kB / 11.64 MB, free: 2.531 MB / 13.93 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 0.9027/0.9027, allocations: 177.2 MB / 189.5 MB, free: 5.309 MB / 186.7 MB Notification: Performance of NFInstanceAPI.mkTop(): time 0.07101/0.9737, allocations: 53.66 MB / 243.2 MB, free: 15.57 MB / 250.7 MB " [Timeout remaining time 179] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.1-main/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.1-main/package.mo): time 0.6342/0.6342, allocations: 118.7 MB / 362.6 MB, free: 1.27 MB / 346.7 MB Notification: Performance of NFInstanceAPI.mkTop(): time 0.04629/0.6805, allocations: 35.83 MB / 398.5 MB, free: 13.35 MB / 394.7 MB " [Timeout remaining time 179] Using package ThermofluidStream with version 1.4.1 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.1-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: setCommandLineOptions("--fmiFlags=s:cvode") Running command: "" <> buildModelFMU(ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop,fileNamePrefix="ThermofluidStream_dev_ThermofluidStream_Idealized_Examples_ClausiusRankine_Step1OpenLoop",fmuType="me_cs",version="2.0+3.0",platforms={"static"}) "" <> buildModelFMU(ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop,fileNamePrefix="ThermofluidStream_dev_ThermofluidStream_Idealized_Examples_ClausiusRankine_Step1OpenLoop",fmuType="me_cs",version="2.0+3.0",platforms={"static"}) [Timeout 660] "Notification: Performance of FrontEnd - loaded program: time 1.543e-06/1.543e-06, allocations: 0 / 399.7 MB, free: 12.11 MB / 394.7 MB Notification: Performance of FrontEnd - Absyn->SCode: time 8.175e-06/9.718e-06, allocations: 2.312 kB / 399.7 MB, free: 12.11 MB / 394.7 MB Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop): time 0.01757/0.01758, allocations: 17.65 MB / 417.4 MB, free: 10.38 MB / 410.7 MB Notification: Performance of NFInst.instExpressions: time 0.1711/0.1886, allocations: 16.92 MB / 434.3 MB, free: 0.9883 MB / 410.7 MB Notification: Performance of NFInst.updateImplicitVariability: time 0.0005289/0.1892, allocations: 51.36 kB / 434.3 MB, free: 0.9883 MB / 410.7 MB Notification: Performance of NFTyping.typeComponents: time 0.0003863/0.1895, allocations: 211.5 kB / 434.5 MB, free: 0.9883 MB / 410.7 MB Notification: Performance of NFTyping.typeBindings: time 0.01023/0.1998, allocations: 6.032 MB / 440.6 MB, free: 364 kB / 410.7 MB Notification: Performance of NFTyping.typeClassSections: time 0.001306/0.2011, allocations: 0.7644 MB / 441.3 MB, free: 84 kB / 410.7 MB Notification: Performance of NFFlatten.flatten: time 0.001176/0.2023, allocations: 1.451 MB / 442.8 MB, free: 15.52 MB / 426.7 MB Notification: Performance of NFFlatten.resolveConnections: time 0.0002211/0.2025, allocations: 141.7 kB / 442.9 MB, free: 15.46 MB / 426.7 MB Notification: Performance of NFEvalConstants.evaluate: time 0.003065/0.2055, allocations: 2.04 MB / 445 MB, free: 14.8 MB / 426.7 MB Notification: Performance of NFSimplifyModel.simplify: time 0.0004318/0.206, allocations: 359.2 kB / 445.3 MB, free: 14.68 MB / 426.7 MB Notification: Performance of NFPackage.collectConstants: time 5.879e-05/0.206, allocations: 56.81 kB / 445.4 MB, free: 14.68 MB / 426.7 MB Notification: Performance of NFFlatten.collectFunctions: time 0.01246/0.2185, allocations: 10.42 MB / 455.8 MB, free: 8.625 MB / 426.7 MB Notification: Performance of NFScalarize.scalarize: time 0.0003191/0.2188, allocations: 123.4 kB / 455.9 MB, free: 8.504 MB / 426.7 MB Notification: Performance of NFVerifyModel.verify: time 0.0002223/0.219, allocations: 271.4 kB / 456.2 MB, free: 8.238 MB / 426.7 MB Notification: Performance of NFConvertDAE.convert: time 0.006807/0.2258, allocations: 6.255 MB / 462.4 MB, free: 2.305 MB / 426.7 MB Notification: Performance of FrontEnd - DAE generated: time 1.119e-05/0.2259, allocations: 0 / 462.4 MB, free: 2.305 MB / 426.7 MB Notification: Performance of FrontEnd: time 1.172e-06/0.2259, allocations: 4 kB / 462.4 MB, free: 2.301 MB / 426.7 MB Notification: Performance of Transformations before backend: time 1.283e-05/0.2259, allocations: 0 / 462.4 MB, free: 2.301 MB / 426.7 MB Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 173 * Number of variables: 173 Notification: Performance of Generate backend data structure: time 0.003546/0.2294, allocations: 2.643 MB / 465.1 MB, free: 15.7 MB / 442.7 MB Notification: Performance of prepare preOptimizeDAE: time 3.302e-05/0.2294, allocations: 8.031 kB / 465.1 MB, free: 15.69 MB / 442.7 MB Notification: Performance of preOpt introduceOutputAliases (simulation): time 7.484e-05/0.2295, allocations: 124 kB / 465.2 MB, free: 15.59 MB / 442.7 MB Notification: Performance of preOpt normalInlineFunction (simulation): time 0.0006534/0.2302, allocations: 359.9 kB / 465.6 MB, free: 15.24 MB / 442.7 MB Notification: Performance of preOpt evaluateParameters (simulation): time 0.0006572/0.2308, allocations: 0.6043 MB / 466.2 MB, free: 14.64 MB / 442.7 MB Notification: Performance of preOpt simplifyIfEquations (simulation): time 8.469e-05/0.2309, allocations: 165.4 kB / 466.3 MB, free: 14.46 MB / 442.7 MB Notification: Performance of preOpt expandDerOperator (simulation): time 5.802e-05/0.231, allocations: 74.52 kB / 466.4 MB, free: 14.39 MB / 442.7 MB Notification: Performance of preOpt clockPartitioning (simulation): time 0.0006846/0.2317, allocations: 0.65 MB / 467 MB, free: 13.73 MB / 442.7 MB Notification: Performance of preOpt findStateOrder (simulation): time 1.289e-05/0.2317, allocations: 0 / 467 MB, free: 13.73 MB / 442.7 MB Notification: Performance of preOpt replaceEdgeChange (simulation): time 2.961e-05/0.2317, allocations: 28 kB / 467.1 MB, free: 13.7 MB / 442.7 MB Notification: Performance of preOpt inlineArrayEqn (simulation): time 1.065e-05/0.2317, allocations: 24 kB / 467.1 MB, free: 13.68 MB / 442.7 MB Notification: Performance of preOpt removeEqualRHS (simulation): time 0.0004325/0.2321, allocations: 306.6 kB / 467.4 MB, free: 13.38 MB / 442.7 MB Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.001673/0.2338, allocations: 2.163 MB / 469.6 MB, free: 11.27 MB / 442.7 MB Notification: Performance of preOpt comSubExp (simulation): time 0.0005633/0.2344, allocations: 392.5 kB / 469.9 MB, free: 10.89 MB / 442.7 MB Notification: Performance of preOpt resolveLoops (simulation): time 9.668e-05/0.2345, allocations: 96.56 kB / 470 MB, free: 10.8 MB / 442.7 MB Notification: Performance of preOpt evalFunc (simulation): time 0.1856/0.4201, allocations: 96.7 MB / 0.5534 GB, free: 10.2 MB / 0.5261 GB Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 3.366e-05/0.4202, allocations: 47.05 kB / 0.5535 GB, free: 10.14 MB / 0.5261 GB Notification: Performance of pre-optimization done (n=47): time 2.565e-06/0.4202, allocations: 0 / 0.5535 GB, free: 10.14 MB / 0.5261 GB Notification: Performance of matching and sorting (n=47): time 0.001198/0.4214, allocations: 0.6062 MB / 0.5541 GB, free: 9.523 MB / 0.5261 GB Notification: Performance of inlineWhenForInitialization (initialization): time 2.155e-05/0.4214, allocations: 55.91 kB / 0.5541 GB, free: 9.457 MB / 0.5261 GB Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.0004044/0.4218, allocations: 0.65 MB / 0.5548 GB, free: 8.914 MB / 0.5261 GB Notification: Performance of collectPreVariables (initialization): time 1.899e-05/0.4218, allocations: 37.64 kB / 0.5548 GB, free: 8.871 MB / 0.5261 GB Notification: Performance of collectInitialEqns (initialization): time 0.0001331/0.4219, allocations: 314.8 kB / 0.5551 GB, free: 8.598 MB / 0.5261 GB Notification: Performance of collectInitialBindings (initialization): time 7.46e-05/0.422, allocations: 171.7 kB / 0.5553 GB, free: 8.438 MB / 0.5261 GB Notification: Performance of simplifyInitialFunctions (initialization): time 9.043e-05/0.4221, allocations: 111.6 kB / 0.5554 GB, free: 8.336 MB / 0.5261 GB Notification: Performance of setup shared object (initialization): time 6.705e-05/0.4222, allocations: 333.3 kB / 0.5557 GB, free: 8.016 MB / 0.5261 GB Notification: Performance of preBalanceInitialSystem (initialization): time 6.818e-05/0.4222, allocations: 49.28 kB / 0.5557 GB, free: 7.969 MB / 0.5261 GB Notification: Performance of partitionIndependentBlocks (initialization): time 0.0001308/0.4224, allocations: 224.8 kB / 0.556 GB, free: 7.691 MB / 0.5261 GB Notification: Performance of analyzeInitialSystem (initialization): time 0.0002405/0.4226, allocations: 336.2 kB / 0.5563 GB, free: 7.305 MB / 0.5261 GB Notification: Performance of solveInitialSystemEqSystem (initialization): time 3.787e-06/0.4226, allocations: 0 / 0.5563 GB, free: 7.305 MB / 0.5261 GB Notification: Performance of matching and sorting (n=69) (initialization): time 0.0003718/0.423, allocations: 379.5 kB / 0.5566 GB, free: 6.93 MB / 0.5261 GB Notification: Performance of prepare postOptimizeDAE: time 1.339e-05/0.423, allocations: 4 kB / 0.5566 GB, free: 6.926 MB / 0.5261 GB Notification: Performance of postOpt simplifyComplexFunction (initialization): time 8.366e-06/0.423, allocations: 8 kB / 0.5566 GB, free: 6.918 MB / 0.5261 GB Notification: Performance of postOpt tearingSystem (initialization): time 0.0001885/0.4232, allocations: 62.45 kB / 0.5567 GB, free: 6.855 MB / 0.5261 GB Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0002369/0.4234, allocations: 131.8 kB / 0.5568 GB, free: 6.727 MB / 0.5261 GB Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.0007225/0.4242, allocations: 1.35 MB / 0.5582 GB, free: 5.301 MB / 0.5261 GB Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.0002149/0.4244, allocations: 71.48 kB / 0.5582 GB, free: 5.23 MB / 0.5261 GB Notification: Performance of postOpt collapseArrayExpressions (initialization): time 2.732e-05/0.4244, allocations: 20 kB / 0.5582 GB, free: 5.211 MB / 0.5261 GB Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 23 * Number of states: 0 () * Number of discrete variables: 5 (pump.outlet.state.phase,flowResistance.outlet.state.phase,turbine.outlet.state.phase,waterSource.outlet.state.phase,steamGenerator.outlet.state.phase) * Number of discrete states: 0 () * Number of clocked states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (64): * Single equations (assignments): 63 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (not torn): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems (#iteration vars, #inner vars, density): 1 system {(1,5,100.0%)} * Non-linear torn systems (#iteration vars, #inner vars): 0 systems Notification: Performance of prepare postOptimizeDAE: time 0.0001279/0.4245, allocations: 148.5 kB / 0.5584 GB, free: 5.055 MB / 0.5261 GB Notification: Performance of postOpt lateInlineFunction (simulation): time 6.579e-05/0.4246, allocations: 69.34 kB / 0.5584 GB, free: 4.988 MB / 0.5261 GB Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.0008333/0.4254, allocations: 0.9506 MB / 0.5594 GB, free: 4.039 MB / 0.5261 GB Notification: Performance of postOpt inlineArrayEqn (simulation): time 1.46e-05/0.4254, allocations: 23.97 kB / 0.5594 GB, free: 4.016 MB / 0.5261 GB Notification: Performance of postOpt constantLinearSystem (simulation): time 2.144e-06/0.4254, allocations: 4 kB / 0.5594 GB, free: 4.012 MB / 0.5261 GB Notification: Performance of postOpt simplifysemiLinear (simulation): time 4.649e-06/0.4254, allocations: 0 / 0.5594 GB, free: 4.012 MB / 0.5261 GB Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.001193/0.4266, allocations: 1.445 MB / 0.5608 GB, free: 2.641 MB / 0.5261 GB Notification: Performance of postOpt simplifyComplexFunction (simulation): time 4.278e-06/0.4266, allocations: 0 / 0.5608 GB, free: 2.641 MB / 0.5261 GB Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.0001507/0.4268, allocations: 83.89 kB / 0.5609 GB, free: 2.559 MB / 0.5261 GB Notification: Performance of postOpt removeConstants (simulation): time 0.000131/0.4269, allocations: 130.9 kB / 0.561 GB, free: 2.43 MB / 0.5261 GB Notification: Performance of postOpt tearingSystem (simulation): time 0.0001432/0.4271, allocations: 73 kB / 0.5611 GB, free: 2.359 MB / 0.5261 GB Notification: Performance of postOpt inputDerivativesUsed (simulation): time 1.691e-05/0.4271, allocations: 8 kB / 0.5611 GB, free: 2.352 MB / 0.5261 GB Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 0.0006302/0.4277, allocations: 1.331 MB / 0.5624 GB, free: 0.9336 MB / 0.5261 GB Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 1.222e-06/0.4277, allocations: 4.031 kB / 0.5624 GB, free: 0.9297 MB / 0.5261 GB Notification: Performance of postOpt symbolicJacobian (simulation): time 0.0005573/0.4283, allocations: 0.7332 MB / 0.5631 GB, free: 196 kB / 0.5261 GB Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 5.223e-05/0.4283, allocations: 22.08 kB / 0.5631 GB, free: 176 kB / 0.5261 GB Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0001343/0.4285, allocations: 12 kB / 0.5631 GB, free: 164 kB / 0.5261 GB Notification: Performance of postOpt findZeroCrossings (simulation): time 4.051e-05/0.4285, allocations: 36.42 kB / 0.5632 GB, free: 128 kB / 0.5261 GB Notification: Performance of postOpt collapseArrayExpressions (simulation): time 1.488e-05/0.4285, allocations: 11.94 kB / 0.5632 GB, free: 116 kB / 0.5261 GB Notification: Performance of sorting global known variables: time 0.0002446/0.4288, allocations: 370.1 kB / 0.5635 GB, free: 15.78 MB / 0.5417 GB Notification: Performance of sort global known variables: time 7e-08/0.4288, allocations: 3.938 kB / 0.5636 GB, free: 15.78 MB / 0.5417 GB Notification: Performance of remove unused functions: time 0.002384/0.4311, allocations: 1.625 MB / 0.5651 GB, free: 14.15 MB / 0.5417 GB Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 2 * Number of states: 1 (flowResistance.inlet.m_flow) * Number of discrete variables: 10 ($cse1.phase,$cse1.region,$cse2.phase,$cse2.region,$cse3.phase,$cse3.region,$cse6.phase,$cse6.region,$cse7.phase,$cse7.region) * Number of discrete states: 0 () * Number of clocked states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (47): * Single equations (assignments): 41 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 5 * When equations: 0 * If-equations: 0 * Equation systems (not torn): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems (#iteration vars, #inner vars, density): 1 system {(1,5,100.0%)} * Non-linear torn systems (#iteration vars, #inner vars): 0 systems Notification: Performance of Backend phase and start with SimCode phase: time 0.004296/0.4354, allocations: 3.216 MB / 0.5683 GB, free: 11.08 MB / 0.5417 GB Notification: Performance of simCode: created initialization part: time 0.0004514/0.4359, allocations: 441.1 kB / 0.5687 GB, free: 10.65 MB / 0.5417 GB Notification: Performance of simCode: created event and clocks part: time 1.071e-05/0.4359, allocations: 12 kB / 0.5687 GB, free: 10.64 MB / 0.5417 GB Notification: Performance of simCode: created simulation system equations: time 0.0002428/0.4361, allocations: 327.3 kB / 0.569 GB, free: 10.31 MB / 0.5417 GB Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.001044/0.4372, allocations: 0.5627 MB / 0.5696 GB, free: 9.785 MB / 0.5417 GB Notification: Performance of simCode: created linear, non-linear and system jacobian parts: time 0.004674/0.4419, allocations: 4.935 MB / 0.5744 GB, free: 4.855 MB / 0.5417 GB Notification: Performance of simCode: some other stuff during SimCode phase: time 0.0001189/0.442, allocations: 209.6 kB / 0.5746 GB, free: 4.629 MB / 0.5417 GB Notification: Performance of simCode: alias equations: time 0.0003627/0.4423, allocations: 255 kB / 0.5748 GB, free: 4.391 MB / 0.5417 GB Notification: Performance of simCode: all other stuff during SimCode phase: time 0.0006706/0.443, allocations: 0.6553 MB / 0.5755 GB, free: 3.73 MB / 0.5417 GB Notification: Performance of SimCode: time 5.51e-07/0.443, allocations: 0 / 0.5755 GB, free: 3.73 MB / 0.5417 GB Notification: Performance of FMU documentation: time 0.2673/0.7103, allocations: 91.36 MB / 0.6647 GB, free: 191.4 MB / 0.6042 GB Notification: FMU-only work: backend 0.0006109, simCode 0.00181, templates 0 Notification: Performance of buildModelFMU: Generate the FMI files: time 0.06288/0.7732, allocations: 1.338 MB / 0.666 GB, free: 190 MB / 0.6042 GB Notification: Building FMU for platform 'static' (1/1). Notification: Finished FMU for platform 'static' (1/1). Notification: Performance of buildModelFMU: Generate platform static: time 5.11/5.883, allocations: 34.19 kB / 0.666 GB, free: 190 MB / 0.6042 GB " [Timeout remaining time 654] (rm -f ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop.pipe ; mkfifo ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop.pipe ; head -c 1048576 < ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop.pipe >> ../files/ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop.sim & (cd run_OMSimulator && /home/hudson/saved_omc/OMSimulator/install/bin/OMSimulator --resultFile=../ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat --stripRoot --tempDir=temp_ThermofluidStream_dev_ThermofluidStream_Idealized_Examples_ClausiusRankine_Step1OpenLoop_fmu --startTime=0 --stopTime=1 --stepSize=0.01 --mode=me --timeout=240 --tolerance=1e-06 ../ThermofluidStream_dev_ThermofluidStream_Idealized_Examples_ClausiusRankine_Step1OpenLoop.fmu) > ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop.pipe 2>&1) [Timeout 252.0] diffSimulationResults("ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat","/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_ref.mat","",relTol=0.003,relTolDiffMinMax=0.003,rangeDelta=0.001) [Timeout 660] "Error: Could not read variable CPUtime in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat. Warning: Get data of variable CPUtime from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed! Error: Could not read variable EventCounter in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat. Warning: Get data of variable EventCounter from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed! Error: Could not read variable dropOfCommons.instanceNameColor[1] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat. Warning: Get data of variable dropOfCommons.instanceNameColor[1] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed! Error: Could not read variable dropOfCommons.instanceNameColor[2] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat. Warning: Get data of variable dropOfCommons.instanceNameColor[2] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed! Error: Could not read variable dropOfCommons.instanceNameColor[3] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat. Warning: Get data of variable dropOfCommons.instanceNameColor[3] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed! Error: Could not read variable flowResistance.mu_in in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat. Warning: Get data of variable flowResistance.mu_in from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed! Error: Could not read variable flowResistance.rho_in in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat. Warning: Get data of variable flowResistance.rho_in from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed! Error: Could not read variable steamGenerator.outletSpec_actual in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat. Warning: Get data of variable steamGenerator.outletSpec_actual from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed! Error: Could not read variable waterSink.p in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat. Warning: Get data of variable waterSink.p from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed! Error: Could not read variable waterSink.r in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat. Warning: Get data of variable waterSink.r from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed! " [Timeout remaining time 660] Not compared, constant in the reference and not in the result: dropOfCommons.instanceNameColor[1],dropOfCommons.instanceNameColor[2],dropOfCommons.instanceNameColor[3],flowResistance.mu_in,flowResistance.rho_in,steamGenerator.outletSpec_actual "" Variables in the reference: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,efficiency.displayVariablefinal,efficiency.showNumber,efficiency.significantDigits,flowResistance.D_h,flowResistance.L,flowResistance.L_value,flowResistance.a,flowResistance.areaCross,flowResistance.areaCrossInput,flowResistance.areaHydraulic,flowResistance.b,flowResistance.clip_p_out,flowResistance.dp,flowResistance.dp_ref_color,flowResistance.dr_corr,flowResistance.h_in,flowResistance.h_out,flowResistance.initM_flow,der(flowResistance.inlet.m_flow),flowResistance.inlet.m_flow,flowResistance.inlet.r,flowResistance.inlet.state.T,flowResistance.inlet.state.d,flowResistance.inlet.state.h,flowResistance.inlet.state.p,flowResistance.inlet.state.phase,flowResistance.l,flowResistance.m_acceleration_0,flowResistance.m_flow,flowResistance.m_flowStateSelect,flowResistance.m_flow_0,flowResistance.mu_in,flowResistance.outlet.m_flow,flowResistance.outlet.r,flowResistance.outlet.state.T,flowResistance.outlet.state.d,flowResistance.outlet.state.h,flowResistance.outlet.state.p,flowResistance.outlet.state.phase,flowResistance.p_in,flowResistance.p_min,flowResistance.p_out,flowResistance.perimeter,flowResistance.perimeterInput,flowResistance.phi,flowResistance.pressureDropSignificantDigits,flowResistance.r,flowResistance.rho_in,flowResistance.rho_min,flowResistance.shape,pump.L,pump.P,pump.P_nom,pump.TC,pump.adiabaticModel.eta_is,pump.adiabaticModel.h_in,pump.adiabaticModel.h_out,pump.adiabaticModel.h_out_is,pump.adiabaticModel.p_out,pump.adiabaticModel.s_in,pump.adiabaticModel.state_in.T,pump.adiabaticModel.state_in.d,pump.adiabaticModel.state_in.h,pump.adiabaticModel.state_in.p,pump.adiabaticModel.state_in.phase,pump.adiabaticModel.w_t,pump.adiabaticModel.w_t_is,pump.assertionLevel,pump.clip_p_out,pump.dh,pump.dp,pump.dp_fixed,pump.dp_nom,pump.dp_start,pump.dr_corr,pump.etaSpec,pump.eta_actual,pump.eta_fixed,pump.eta_is,pump.h_in,pump.h_out,pump.initM_flow,der(pump.inlet.m_flow),pump.inlet.m_flow,pump.inlet.r,pump.inlet.state.T,pump.inlet.state.d,pump.inlet.state.h,pump.inlet.state.p,pump.inlet.state.phase,pump.m_acceleration_0,pump.m_flow,pump.m_flowStateSelect,pump.m_flow_0,pump.outlet.m_flow,pump.outlet.r,pump.outlet.state.T,pump.outlet.state.d,pump.outlet.state.h,pump.outlet.state.p,pump.outlet.state.phase,pump.outletSpec,pump.outletSpec_actual,pump.outletValueSpec,pump.pRatio,pump.pRatio_fixed,pump.p_in,pump.p_min,pump.p_out,pump.p_out_fixed,pump.singularityRegime,steamGenerator.L,steamGenerator.P,steamGenerator.Q_flow,steamGenerator.T_out_fixed,steamGenerator.assertionLevel,steamGenerator.clip_p_out,steamGenerator.dT,steamGenerator.dT_fixed,steamGenerator.dh,steamGenerator.dh_fixed,steamGenerator.dp,steamGenerator.dr_corr,steamGenerator.du,steamGenerator.h_in,steamGenerator.h_out,steamGenerator.h_out_fixed,steamGenerator.initM_flow,der(steamGenerator.inlet.m_flow),steamGenerator.inlet.m_flow,steamGenerator.inlet.r,steamGenerator.inlet.state.T,steamGenerator.inlet.state.d,steamGenerator.inlet.state.h,steamGenerator.inlet.state.p,steamGenerator.inlet.state.phase,steamGenerator.m_acceleration_0,steamGenerator.m_flow,steamGenerator.m_flowStateSelect,steamGenerator.m_flow_0,steamGenerator.outlet.m_flow,steamGenerator.outlet.r,steamGenerator.outlet.state.T,steamGenerator.outlet.state.d,steamGenerator.outlet.state.h,steamGenerator.outlet.state.p,steamGenerator.outlet.state.phase,steamGenerator.outletSpec,steamGenerator.outletSpec_actual,steamGenerator.outletValueSpec,steamGenerator.p,steamGenerator.p_in,steamGenerator.p_inf,steamGenerator.p_min,steamGenerator.p_out,steamGenerator.q,steamGenerator.rho_in,steamGenerator.rho_out,steamGenerator.singularityRegime,steamGenerator.systemSpec,steamGenerator.u_in,steamGenerator.u_out,steamGenerator.v_in,steamGenerator.v_out,steamGenerator.w_amb,steamGenerator.w_exp,steamGenerator.w_exp_net,turbine.L,turbine.P,turbine.P_nom,turbine.TC,turbine.adiabaticModel.eta_is,turbine.adiabaticModel.h_in,turbine.adiabaticModel.h_out,turbine.adiabaticModel.h_out_is,turbine.adiabaticModel.p_out,turbine.adiabaticModel.s_in,turbine.adiabaticModel.state_in.T,turbine.adiabaticModel.state_in.d,turbine.adiabaticModel.state_in.h,turbine.adiabaticModel.state_in.p,turbine.adiabaticModel.state_in.phase,turbine.adiabaticModel.w_t,turbine.adiabaticModel.w_t_is,turbine.assertionLevel,turbine.clip_p_out,turbine.dh,turbine.dp,turbine.dp_fixed,turbine.dp_nom,turbine.dp_start,turbine.dr_corr,turbine.etaSpec,turbine.eta_actual,turbine.eta_fixed,turbine.eta_is,turbine.h_in,turbine.h_out,turbine.initM_flow,der(turbine.inlet.m_flow),turbine.inlet.m_flow,turbine.inlet.r,turbine.inlet.state.T,turbine.inlet.state.d,turbine.inlet.state.h,turbine.inlet.state.p,turbine.inlet.state.phase,turbine.m_acceleration_0,turbine.m_flow,turbine.m_flowStateSelect,turbine.m_flow_0,turbine.outlet.m_flow,turbine.outlet.r,turbine.outlet.state.T,turbine.outlet.state.d,turbine.outlet.state.h,turbine.outlet.state.p,turbine.outlet.state.phase,turbine.outletSpec,turbine.outletSpec_actual,turbine.outletValueSpec,turbine.pRatio,turbine.pRatio_fixed,turbine.p_in,turbine.p_min,turbine.p_out,turbine.p_out_fixed,turbine.singularityRegime,waterSink.L,der(waterSink.inlet.m_flow),waterSink.inlet.m_flow,waterSink.inlet.r,waterSink.inlet.state.T,waterSink.inlet.state.d,waterSink.inlet.state.h,waterSink.inlet.state.p,waterSink.inlet.state.phase,waterSink.p,waterSink.p0,waterSink.p0_par,waterSink.r,waterSource.L,waterSource.T0,waterSource.T0_par,waterSource.h0,waterSource.h0_par,der(waterSource.outlet.m_flow),waterSource.outlet.m_flow,waterSource.outlet.r,waterSource.outlet.state.T,waterSource.outlet.state.d,waterSource.outlet.state.h,waterSource.outlet.state.p,waterSource.outlet.state.phase,waterSource.p0,waterSource.p0_par Variables in the result:der(flowResistance.inlet.m_flow),der(flowResistance.outlet.m_flow),der(pump.inlet.m_flow),der(pump.m_flow),der(pump.outlet.m_flow),der(steamGenerator.inlet.m_flow),der(steamGenerator.m_flow),der(steamGenerator.outlet.m_flow),der(turbine.inlet.m_flow),der(turbine.m_flow),der(turbine.outlet.m_flow),der(waterSink.inlet.m_flow),der(waterSource.outlet.m_flow),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,efficiency.displayVariable,efficiency.displayVariablefinal,efficiency.number,efficiency.showNumber,efficiency.significantDigits,efficiency.use_numberPort,flowResistance.D_h,flowResistance.L,flowResistance.L_value,flowResistance.a,flowResistance.areaCross,flowResistance.areaCrossInput,flowResistance.areaHydraulic,flowResistance.b,flowResistance.clip_p_out,flowResistance.computeL,flowResistance.considerInertance,flowResistance.displayInstanceName,flowResistance.displayParameters,flowResistance.dp,flowResistance.dp_ref_color,flowResistance.dr_corr,flowResistance.h_in,flowResistance.h_out,flowResistance.initM_flow,flowResistance.inlet.m_flow,flowResistance.inlet.r,flowResistance.inlet.state.T,flowResistance.inlet.state.d,flowResistance.inlet.state.h,flowResistance.inlet.state.p,flowResistance.inlet.state.phase,flowResistance.l,flowResistance.m_acceleration_0,flowResistance.m_flow,flowResistance.m_flowStateSelect,flowResistance.m_flow_0,flowResistance.outlet.m_flow,flowResistance.outlet.r,flowResistance.outlet.state.T,flowResistance.outlet.state.d,flowResistance.outlet.state.h,flowResistance.outlet.state.p,flowResistance.outlet.state.phase,flowResistance.p_in,flowResistance.p_min,flowResistance.p_out,flowResistance.perimeter,flowResistance.perimeterInput,flowResistance.phi,flowResistance.pressureDropSignificantDigits,flowResistance.pressureDropUnit,flowResistance.r,flowResistance.rho_min,flowResistance.shape,flowResistance.showPressureDrop,pump.L,pump.P,pump.P_in_internal,pump.P_nom,pump.TC,pump.adiabaticModel.eta_is,pump.adiabaticModel.h_in,pump.adiabaticModel.h_out,pump.adiabaticModel.h_out_is,pump.adiabaticModel.p_in,pump.adiabaticModel.p_out,pump.adiabaticModel.s_in,pump.adiabaticModel.state_in.T,pump.adiabaticModel.state_in.d,pump.adiabaticModel.state_in.h,pump.adiabaticModel.state_in.p,pump.adiabaticModel.state_in.phase,pump.adiabaticModel.w_t,pump.adiabaticModel.w_t_is,pump.assertionLevel,pump.clip_p_out,pump.considerInertance,pump.dh,pump.displayInstanceName,pump.displayParameters,pump.dp,pump.dp_fixed,pump.dp_nom,pump.dp_start,pump.dr_corr,pump.enableFilter,pump.etaSpec,pump.eta_fixed,pump.eta_is,pump.h_in,pump.h_out,pump.iconIsCompression,pump.iconType,pump.initM_flow,pump.inlet.m_flow,pump.inlet.r,pump.inlet.state.T,pump.inlet.state.d,pump.inlet.state.h,pump.inlet.state.p,pump.inlet.state.phase,pump.m_acceleration_0,pump.m_flow,pump.m_flowStateSelect,pump.m_flow_0,pump.outlet.m_flow,pump.outlet.r,pump.outlet.state.T,pump.outlet.state.d,pump.outlet.state.h,pump.outlet.state.p,pump.outlet.state.phase,pump.outletSpec,pump.outletValueSpec,pump.pRatio,pump.pRatio_fixed,pump.p_in,pump.p_min,pump.p_out,pump.p_out_fixed,pump.powerSignal,pump.showEfficiency,pump.showOutletSpecification,pump.showPowerDirection,pump.singularityRegime,pump.specifyOutlet,steamGenerator.L,steamGenerator.P,steamGenerator.Q_flow,steamGenerator.T_in,steamGenerator.T_out,steamGenerator.T_out_fixed,steamGenerator.assertionLevel,steamGenerator.clip_p_out,steamGenerator.considerInertance,steamGenerator.dT,steamGenerator.dT_fixed,steamGenerator.dh,steamGenerator.dh_fixed,steamGenerator.displayInstanceName,steamGenerator.displayParameters,steamGenerator.dp,steamGenerator.dr_corr,steamGenerator.du,steamGenerator.h_in,steamGenerator.h_out,steamGenerator.h_out_fixed,steamGenerator.heatFlowSignal,steamGenerator.iconIsHeating,steamGenerator.iconType,steamGenerator.initM_flow,steamGenerator.inlet.m_flow,steamGenerator.inlet.r,steamGenerator.inlet.state.T,steamGenerator.inlet.state.d,steamGenerator.inlet.state.h,steamGenerator.inlet.state.p,steamGenerator.inlet.state.phase,steamGenerator.isCycle,steamGenerator.m_acceleration_0,steamGenerator.m_flow,steamGenerator.m_flowStateSelect,steamGenerator.m_flow_0,steamGenerator.outlet.m_flow,steamGenerator.outlet.r,steamGenerator.outlet.state.T,steamGenerator.outlet.state.d,steamGenerator.outlet.state.h,steamGenerator.outlet.state.p,steamGenerator.outlet.state.phase,steamGenerator.outletSpec,steamGenerator.outletValueSpec,steamGenerator.p_in,steamGenerator.p_inf,steamGenerator.p_min,steamGenerator.p_out,steamGenerator.q,steamGenerator.rho_in,steamGenerator.rho_out,steamGenerator.showHeatFlowDirection,steamGenerator.showOutletSpecification,steamGenerator.singularityRegime,steamGenerator.specifyOutlet,steamGenerator.systemSpec,steamGenerator.u_in,steamGenerator.u_out,steamGenerator.v_in,steamGenerator.v_out,steamGenerator.w_amb,steamGenerator.w_exp,steamGenerator.w_exp_net,time,turbine.L,turbine.P,turbine.P_in_internal,turbine.P_nom,turbine.TC,turbine.adiabaticModel.eta_is,turbine.adiabaticModel.h_in,turbine.adiabaticModel.h_out,turbine.adiabaticModel.h_out_is,turbine.adiabaticModel.p_in,turbine.adiabaticModel.p_out,turbine.adiabaticModel.s_in,turbine.adiabaticModel.state_in.T,turbine.adiabaticModel.state_in.d,turbine.adiabaticModel.state_in.h,turbine.adiabaticModel.state_in.p,turbine.adiabaticModel.state_in.phase,turbine.adiabaticModel.w_t,turbine.adiabaticModel.w_t_is,turbine.assertionLevel,turbine.clip_p_out,turbine.considerInertance,turbine.dh,turbine.displayInstanceName,turbine.displayParameters,turbine.dp,turbine.dp_fixed,turbine.dp_nom,turbine.dp_start,turbine.dr_corr,turbine.enableFilter,turbine.etaSpec,turbine.eta_fixed,turbine.eta_is,turbine.h_in,turbine.h_out,turbine.iconIsCompression,turbine.iconType,turbine.initM_flow,turbine.inlet.m_flow,turbine.inlet.r,turbine.inlet.state.T,turbine.inlet.state.d,turbine.inlet.state.h,turbine.inlet.state.p,turbine.inlet.state.phase,turbine.m_acceleration_0,turbine.m_flow,turbine.m_flowStateSelect,turbine.m_flow_0,turbine.outlet.m_flow,turbine.outlet.r,turbine.outlet.state.T,turbine.outlet.state.d,turbine.outlet.state.h,turbine.outlet.state.p,turbine.outlet.state.phase,turbine.outletSpec,turbine.outletValueSpec,turbine.pRatio,turbine.pRatio_fixed,turbine.p_in,turbine.p_min,turbine.p_out,turbine.p_out_fixed,turbine.powerSignal,turbine.showEfficiency,turbine.showOutletSpecification,turbine.showPowerDirection,turbine.singularityRegime,turbine.specifyOutlet,waterSink.L,waterSink.considerInertance,waterSink.displayInertance,waterSink.displayInstanceName,waterSink.displayP,waterSink.displayParameters,waterSink.displayPressure,waterSink.inlet.m_flow,waterSink.inlet.r,waterSink.inlet.state.T,waterSink.inlet.state.d,waterSink.inlet.state.h,waterSink.inlet.state.p,waterSink.inlet.state.phase,waterSink.p0_par,waterSink.pressureFromInput,waterSource.L,waterSource.T0_par,waterSource.considerInertance,waterSource.displayH,waterSource.displayInertance,waterSource.displayInstanceName,waterSource.displayMassFractions,waterSource.displayP,waterSource.displayParameters,waterSource.displayPressure,waterSource.displayT,waterSource.displayTemperature,waterSource.displayXi,waterSource.enthalpyFromInput,waterSource.h0_par,waterSource.outlet.m_flow,waterSource.outlet.r,waterSource.outlet.state.T,waterSource.outlet.state.d,waterSource.outlet.state.h,waterSource.outlet.state.p,waterSource.outlet.state.phase,waterSource.p0_par,waterSource.pressureFromInput,waterSource.setEnthalpy,waterSource.temperatureFromInput,waterSource.xiFromInput filterSimulationResults("ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat", "/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop.diff.mat", vars={"waterSink.r", "waterSink.p"}, removeDescription=false) [Timeout 660] "Error: Could not read variable waterSink.r in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat. " [Timeout remaining time 660] Failed to write the differing variables of ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat to /var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop.diff.mat: "" filterSimulationResults("/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_ref.mat", "/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop.diff.ref.mat", vars={"waterSink.r", "waterSink.p"}, removeDescription=false) [Timeout 660] "" [Timeout remaining time 660] (rm -f ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-cvode.pipe ; mkfifo ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-cvode.pipe ; head -c 1048576 < ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-cvode.pipe >> /var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-cvode.sim & (cd run_OMSimulator-cs-cvode && /home/hudson/saved_omc/OMSimulator/install/bin/OMSimulator --resultFile=../ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-cvode_res.mat --stripRoot --tempDir=temp_ThermofluidStream_dev_ThermofluidStream_Idealized_Examples_ClausiusRankine_Step1OpenLoop_OMSimulator-cs-cvode_fmu --startTime=0 --stopTime=1 --stepSize=0.01 --mode=cs --timeout=240 --tolerance=1e-06 ../ThermofluidStream_dev_ThermofluidStream_Idealized_Examples_ClausiusRankine_Step1OpenLoop_OMSimulator-cs-cvode.fmu) > ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-cvode.pipe 2>&1) [Timeout 252.0] diffSimulationResults("ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-cvode_res.mat","/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_ref.mat","",relTol=0.003,relTolDiffMinMax=0.003,rangeDelta=0.001) [Timeout 660] "Error: Could not read variable CPUtime in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-cvode_res.mat. Warning: Get data of variable CPUtime from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-cvode_res.mat failed! Error: Could not read variable EventCounter in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-cvode_res.mat. Warning: Get data of variable EventCounter from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-cvode_res.mat failed! Error: Could not read variable dropOfCommons.instanceNameColor[1] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-cvode_res.mat. Warning: Get data of variable dropOfCommons.instanceNameColor[1] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-cvode_res.mat failed! Error: Could not read variable dropOfCommons.instanceNameColor[2] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-cvode_res.mat. Warning: Get data of variable dropOfCommons.instanceNameColor[2] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-cvode_res.mat failed! Error: Could not read variable dropOfCommons.instanceNameColor[3] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-cvode_res.mat. Warning: Get data of variable dropOfCommons.instanceNameColor[3] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-cvode_res.mat failed! Error: Could not read variable flowResistance.mu_in in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-cvode_res.mat. Warning: Get data of variable flowResistance.mu_in from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-cvode_res.mat failed! Error: Could not read variable flowResistance.rho_in in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-cvode_res.mat. Warning: Get data of variable flowResistance.rho_in from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-cvode_res.mat failed! Error: Could not read variable steamGenerator.outletSpec_actual in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-cvode_res.mat. Warning: Get data of variable steamGenerator.outletSpec_actual from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-cvode_res.mat failed! Error: Could not read variable waterSink.p in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-cvode_res.mat. Warning: Get data of variable waterSink.p from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-cvode_res.mat failed! Error: Could not read variable waterSink.r in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-cvode_res.mat. Warning: Get data of variable waterSink.r from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-cvode_res.mat failed! " [Timeout remaining time 660] Not compared, constant in the reference and not in the result: dropOfCommons.instanceNameColor[1],dropOfCommons.instanceNameColor[2],dropOfCommons.instanceNameColor[3],flowResistance.mu_in,flowResistance.rho_in,steamGenerator.outletSpec_actual "" Variables in the reference: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,efficiency.displayVariablefinal,efficiency.showNumber,efficiency.significantDigits,flowResistance.D_h,flowResistance.L,flowResistance.L_value,flowResistance.a,flowResistance.areaCross,flowResistance.areaCrossInput,flowResistance.areaHydraulic,flowResistance.b,flowResistance.clip_p_out,flowResistance.dp,flowResistance.dp_ref_color,flowResistance.dr_corr,flowResistance.h_in,flowResistance.h_out,flowResistance.initM_flow,der(flowResistance.inlet.m_flow),flowResistance.inlet.m_flow,flowResistance.inlet.r,flowResistance.inlet.state.T,flowResistance.inlet.state.d,flowResistance.inlet.state.h,flowResistance.inlet.state.p,flowResistance.inlet.state.phase,flowResistance.l,flowResistance.m_acceleration_0,flowResistance.m_flow,flowResistance.m_flowStateSelect,flowResistance.m_flow_0,flowResistance.mu_in,flowResistance.outlet.m_flow,flowResistance.outlet.r,flowResistance.outlet.state.T,flowResistance.outlet.state.d,flowResistance.outlet.state.h,flowResistance.outlet.state.p,flowResistance.outlet.state.phase,flowResistance.p_in,flowResistance.p_min,flowResistance.p_out,flowResistance.perimeter,flowResistance.perimeterInput,flowResistance.phi,flowResistance.pressureDropSignificantDigits,flowResistance.r,flowResistance.rho_in,flowResistance.rho_min,flowResistance.shape,pump.L,pump.P,pump.P_nom,pump.TC,pump.adiabaticModel.eta_is,pump.adiabaticModel.h_in,pump.adiabaticModel.h_out,pump.adiabaticModel.h_out_is,pump.adiabaticModel.p_out,pump.adiabaticModel.s_in,pump.adiabaticModel.state_in.T,pump.adiabaticModel.state_in.d,pump.adiabaticModel.state_in.h,pump.adiabaticModel.state_in.p,pump.adiabaticModel.state_in.phase,pump.adiabaticModel.w_t,pump.adiabaticModel.w_t_is,pump.assertionLevel,pump.clip_p_out,pump.dh,pump.dp,pump.dp_fixed,pump.dp_nom,pump.dp_start,pump.dr_corr,pump.etaSpec,pump.eta_actual,pump.eta_fixed,pump.eta_is,pump.h_in,pump.h_out,pump.initM_flow,der(pump.inlet.m_flow),pump.inlet.m_flow,pump.inlet.r,pump.inlet.state.T,pump.inlet.state.d,pump.inlet.state.h,pump.inlet.state.p,pump.inlet.state.phase,pump.m_acceleration_0,pump.m_flow,pump.m_flowStateSelect,pump.m_flow_0,pump.outlet.m_flow,pump.outlet.r,pump.outlet.state.T,pump.outlet.state.d,pump.outlet.state.h,pump.outlet.state.p,pump.outlet.state.phase,pump.outletSpec,pump.outletSpec_actual,pump.outletValueSpec,pump.pRatio,pump.pRatio_fixed,pump.p_in,pump.p_min,pump.p_out,pump.p_out_fixed,pump.singularityRegime,steamGenerator.L,steamGenerator.P,steamGenerator.Q_flow,steamGenerator.T_out_fixed,steamGenerator.assertionLevel,steamGenerator.clip_p_out,steamGenerator.dT,steamGenerator.dT_fixed,steamGenerator.dh,steamGenerator.dh_fixed,steamGenerator.dp,steamGenerator.dr_corr,steamGenerator.du,steamGenerator.h_in,steamGenerator.h_out,steamGenerator.h_out_fixed,steamGenerator.initM_flow,der(steamGenerator.inlet.m_flow),steamGenerator.inlet.m_flow,steamGenerator.inlet.r,steamGenerator.inlet.state.T,steamGenerator.inlet.state.d,steamGenerator.inlet.state.h,steamGenerator.inlet.state.p,steamGenerator.inlet.state.phase,steamGenerator.m_acceleration_0,steamGenerator.m_flow,steamGenerator.m_flowStateSelect,steamGenerator.m_flow_0,steamGenerator.outlet.m_flow,steamGenerator.outlet.r,steamGenerator.outlet.state.T,steamGenerator.outlet.state.d,steamGenerator.outlet.state.h,steamGenerator.outlet.state.p,steamGenerator.outlet.state.phase,steamGenerator.outletSpec,steamGenerator.outletSpec_actual,steamGenerator.outletValueSpec,steamGenerator.p,steamGenerator.p_in,steamGenerator.p_inf,steamGenerator.p_min,steamGenerator.p_out,steamGenerator.q,steamGenerator.rho_in,steamGenerator.rho_out,steamGenerator.singularityRegime,steamGenerator.systemSpec,steamGenerator.u_in,steamGenerator.u_out,steamGenerator.v_in,steamGenerator.v_out,steamGenerator.w_amb,steamGenerator.w_exp,steamGenerator.w_exp_net,turbine.L,turbine.P,turbine.P_nom,turbine.TC,turbine.adiabaticModel.eta_is,turbine.adiabaticModel.h_in,turbine.adiabaticModel.h_out,turbine.adiabaticModel.h_out_is,turbine.adiabaticModel.p_out,turbine.adiabaticModel.s_in,turbine.adiabaticModel.state_in.T,turbine.adiabaticModel.state_in.d,turbine.adiabaticModel.state_in.h,turbine.adiabaticModel.state_in.p,turbine.adiabaticModel.state_in.phase,turbine.adiabaticModel.w_t,turbine.adiabaticModel.w_t_is,turbine.assertionLevel,turbine.clip_p_out,turbine.dh,turbine.dp,turbine.dp_fixed,turbine.dp_nom,turbine.dp_start,turbine.dr_corr,turbine.etaSpec,turbine.eta_actual,turbine.eta_fixed,turbine.eta_is,turbine.h_in,turbine.h_out,turbine.initM_flow,der(turbine.inlet.m_flow),turbine.inlet.m_flow,turbine.inlet.r,turbine.inlet.state.T,turbine.inlet.state.d,turbine.inlet.state.h,turbine.inlet.state.p,turbine.inlet.state.phase,turbine.m_acceleration_0,turbine.m_flow,turbine.m_flowStateSelect,turbine.m_flow_0,turbine.outlet.m_flow,turbine.outlet.r,turbine.outlet.state.T,turbine.outlet.state.d,turbine.outlet.state.h,turbine.outlet.state.p,turbine.outlet.state.phase,turbine.outletSpec,turbine.outletSpec_actual,turbine.outletValueSpec,turbine.pRatio,turbine.pRatio_fixed,turbine.p_in,turbine.p_min,turbine.p_out,turbine.p_out_fixed,turbine.singularityRegime,waterSink.L,der(waterSink.inlet.m_flow),waterSink.inlet.m_flow,waterSink.inlet.r,waterSink.inlet.state.T,waterSink.inlet.state.d,waterSink.inlet.state.h,waterSink.inlet.state.p,waterSink.inlet.state.phase,waterSink.p,waterSink.p0,waterSink.p0_par,waterSink.r,waterSource.L,waterSource.T0,waterSource.T0_par,waterSource.h0,waterSource.h0_par,der(waterSource.outlet.m_flow),waterSource.outlet.m_flow,waterSource.outlet.r,waterSource.outlet.state.T,waterSource.outlet.state.d,waterSource.outlet.state.h,waterSource.outlet.state.p,waterSource.outlet.state.phase,waterSource.p0,waterSource.p0_par Variables in the result:der(flowResistance.inlet.m_flow),der(flowResistance.outlet.m_flow),der(pump.inlet.m_flow),der(pump.m_flow),der(pump.outlet.m_flow),der(steamGenerator.inlet.m_flow),der(steamGenerator.m_flow),der(steamGenerator.outlet.m_flow),der(turbine.inlet.m_flow),der(turbine.m_flow),der(turbine.outlet.m_flow),der(waterSink.inlet.m_flow),der(waterSource.outlet.m_flow),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,efficiency.displayVariable,efficiency.displayVariablefinal,efficiency.number,efficiency.showNumber,efficiency.significantDigits,efficiency.use_numberPort,flowResistance.D_h,flowResistance.L,flowResistance.L_value,flowResistance.a,flowResistance.areaCross,flowResistance.areaCrossInput,flowResistance.areaHydraulic,flowResistance.b,flowResistance.clip_p_out,flowResistance.computeL,flowResistance.considerInertance,flowResistance.displayInstanceName,flowResistance.displayParameters,flowResistance.dp,flowResistance.dp_ref_color,flowResistance.dr_corr,flowResistance.h_in,flowResistance.h_out,flowResistance.initM_flow,flowResistance.inlet.m_flow,flowResistance.inlet.r,flowResistance.inlet.state.T,flowResistance.inlet.state.d,flowResistance.inlet.state.h,flowResistance.inlet.state.p,flowResistance.inlet.state.phase,flowResistance.l,flowResistance.m_acceleration_0,flowResistance.m_flow,flowResistance.m_flowStateSelect,flowResistance.m_flow_0,flowResistance.outlet.m_flow,flowResistance.outlet.r,flowResistance.outlet.state.T,flowResistance.outlet.state.d,flowResistance.outlet.state.h,flowResistance.outlet.state.p,flowResistance.outlet.state.phase,flowResistance.p_in,flowResistance.p_min,flowResistance.p_out,flowResistance.perimeter,flowResistance.perimeterInput,flowResistance.phi,flowResistance.pressureDropSignificantDigits,flowResistance.pressureDropUnit,flowResistance.r,flowResistance.rho_min,flowResistance.shape,flowResistance.showPressureDrop,pump.L,pump.P,pump.P_in_internal,pump.P_nom,pump.TC,pump.adiabaticModel.eta_is,pump.adiabaticModel.h_in,pump.adiabaticModel.h_out,pump.adiabaticModel.h_out_is,pump.adiabaticModel.p_in,pump.adiabaticModel.p_out,pump.adiabaticModel.s_in,pump.adiabaticModel.state_in.T,pump.adiabaticModel.state_in.d,pump.adiabaticModel.state_in.h,pump.adiabaticModel.state_in.p,pump.adiabaticModel.state_in.phase,pump.adiabaticModel.w_t,pump.adiabaticModel.w_t_is,pump.assertionLevel,pump.clip_p_out,pump.considerInertance,pump.dh,pump.displayInstanceName,pump.displayParameters,pump.dp,pump.dp_fixed,pump.dp_nom,pump.dp_start,pump.dr_corr,pump.enableFilter,pump.etaSpec,pump.eta_fixed,pump.eta_is,pump.h_in,pump.h_out,pump.iconIsCompression,pump.iconType,pump.initM_flow,pump.inlet.m_flow,pump.inlet.r,pump.inlet.state.T,pump.inlet.state.d,pump.inlet.state.h,pump.inlet.state.p,pump.inlet.state.phase,pump.m_acceleration_0,pump.m_flow,pump.m_flowStateSelect,pump.m_flow_0,pump.outlet.m_flow,pump.outlet.r,pump.outlet.state.T,pump.outlet.state.d,pump.outlet.state.h,pump.outlet.state.p,pump.outlet.state.phase,pump.outletSpec,pump.outletValueSpec,pump.pRatio,pump.pRatio_fixed,pump.p_in,pump.p_min,pump.p_out,pump.p_out_fixed,pump.powerSignal,pump.showEfficiency,pump.showOutletSpecification,pump.showPowerDirection,pump.singularityRegime,pump.specifyOutlet,steamGenerator.L,steamGenerator.P,steamGenerator.Q_flow,steamGenerator.T_in,steamGenerator.T_out,steamGenerator.T_out_fixed,steamGenerator.assertionLevel,steamGenerator.clip_p_out,steamGenerator.considerInertance,steamGenerator.dT,steamGenerator.dT_fixed,steamGenerator.dh,steamGenerator.dh_fixed,steamGenerator.displayInstanceName,steamGenerator.displayParameters,steamGenerator.dp,steamGenerator.dr_corr,steamGenerator.du,steamGenerator.h_in,steamGenerator.h_out,steamGenerator.h_out_fixed,steamGenerator.heatFlowSignal,steamGenerator.iconIsHeating,steamGenerator.iconType,steamGenerator.initM_flow,steamGenerator.inlet.m_flow,steamGenerator.inlet.r,steamGenerator.inlet.state.T,steamGenerator.inlet.state.d,steamGenerator.inlet.state.h,steamGenerator.inlet.state.p,steamGenerator.inlet.state.phase,steamGenerator.isCycle,steamGenerator.m_acceleration_0,steamGenerator.m_flow,steamGenerator.m_flowStateSelect,steamGenerator.m_flow_0,steamGenerator.outlet.m_flow,steamGenerator.outlet.r,steamGenerator.outlet.state.T,steamGenerator.outlet.state.d,steamGenerator.outlet.state.h,steamGenerator.outlet.state.p,steamGenerator.outlet.state.phase,steamGenerator.outletSpec,steamGenerator.outletValueSpec,steamGenerator.p_in,steamGenerator.p_inf,steamGenerator.p_min,steamGenerator.p_out,steamGenerator.q,steamGenerator.rho_in,steamGenerator.rho_out,steamGenerator.showHeatFlowDirection,steamGenerator.showOutletSpecification,steamGenerator.singularityRegime,steamGenerator.specifyOutlet,steamGenerator.systemSpec,steamGenerator.u_in,steamGenerator.u_out,steamGenerator.v_in,steamGenerator.v_out,steamGenerator.w_amb,steamGenerator.w_exp,steamGenerator.w_exp_net,time,turbine.L,turbine.P,turbine.P_in_internal,turbine.P_nom,turbine.TC,turbine.adiabaticModel.eta_is,turbine.adiabaticModel.h_in,turbine.adiabaticModel.h_out,turbine.adiabaticModel.h_out_is,turbine.adiabaticModel.p_in,turbine.adiabaticModel.p_out,turbine.adiabaticModel.s_in,turbine.adiabaticModel.state_in.T,turbine.adiabaticModel.state_in.d,turbine.adiabaticModel.state_in.h,turbine.adiabaticModel.state_in.p,turbine.adiabaticModel.state_in.phase,turbine.adiabaticModel.w_t,turbine.adiabaticModel.w_t_is,turbine.assertionLevel,turbine.clip_p_out,turbine.considerInertance,turbine.dh,turbine.displayInstanceName,turbine.displayParameters,turbine.dp,turbine.dp_fixed,turbine.dp_nom,turbine.dp_start,turbine.dr_corr,turbine.enableFilter,turbine.etaSpec,turbine.eta_fixed,turbine.eta_is,turbine.h_in,turbine.h_out,turbine.iconIsCompression,turbine.iconType,turbine.initM_flow,turbine.inlet.m_flow,turbine.inlet.r,turbine.inlet.state.T,turbine.inlet.state.d,turbine.inlet.state.h,turbine.inlet.state.p,turbine.inlet.state.phase,turbine.m_acceleration_0,turbine.m_flow,turbine.m_flowStateSelect,turbine.m_flow_0,turbine.outlet.m_flow,turbine.outlet.r,turbine.outlet.state.T,turbine.outlet.state.d,turbine.outlet.state.h,turbine.outlet.state.p,turbine.outlet.state.phase,turbine.outletSpec,turbine.outletValueSpec,turbine.pRatio,turbine.pRatio_fixed,turbine.p_in,turbine.p_min,turbine.p_out,turbine.p_out_fixed,turbine.powerSignal,turbine.showEfficiency,turbine.showOutletSpecification,turbine.showPowerDirection,turbine.singularityRegime,turbine.specifyOutlet,waterSink.L,waterSink.considerInertance,waterSink.displayInertance,waterSink.displayInstanceName,waterSink.displayP,waterSink.displayParameters,waterSink.displayPressure,waterSink.inlet.m_flow,waterSink.inlet.r,waterSink.inlet.state.T,waterSink.inlet.state.d,waterSink.inlet.state.h,waterSink.inlet.state.p,waterSink.inlet.state.phase,waterSink.p0_par,waterSink.pressureFromInput,waterSource.L,waterSource.T0_par,waterSource.considerInertance,waterSource.displayH,waterSource.displayInertance,waterSource.displayInstanceName,waterSource.displayMassFractions,waterSource.displayP,waterSource.displayParameters,waterSource.displayPressure,waterSource.displayT,waterSource.displayTemperature,waterSource.displayXi,waterSource.enthalpyFromInput,waterSource.h0_par,waterSource.outlet.m_flow,waterSource.outlet.r,waterSource.outlet.state.T,waterSource.outlet.state.d,waterSource.outlet.state.h,waterSource.outlet.state.p,waterSource.outlet.state.phase,waterSource.p0_par,waterSource.pressureFromInput,waterSource.setEnthalpy,waterSource.temperatureFromInput,waterSource.xiFromInput filterSimulationResults("ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-cvode_res.mat", "/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-cvode.diff.mat", vars={"waterSink.r", "waterSink.p"}, removeDescription=false) [Timeout 660] "Error: Could not read variable waterSink.r in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-cvode_res.mat. " [Timeout remaining time 660] Failed to write the differing variables of ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-cvode_res.mat to /var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-cvode.diff.mat: "" filterSimulationResults("/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_ref.mat", "/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-cvode.diff.ref.mat", vars={"waterSink.r", "waterSink.p"}, removeDescription=false) [Timeout 660] "" [Timeout remaining time 660] (rm -f ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-euler.pipe ; mkfifo ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-euler.pipe ; head -c 1048576 < ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-euler.pipe >> /var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-euler.sim & (cd run_OMSimulator-cs-euler && /home/hudson/saved_omc/OMSimulator/install/bin/OMSimulator --resultFile=../ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-euler_res.mat --stripRoot --tempDir=temp_ThermofluidStream_dev_ThermofluidStream_Idealized_Examples_ClausiusRankine_Step1OpenLoop_OMSimulator-cs-euler_fmu --startTime=0 --stopTime=1 --stepSize=0.01 --mode=cs --timeout=240 --tolerance=1e-06 ../ThermofluidStream_dev_ThermofluidStream_Idealized_Examples_ClausiusRankine_Step1OpenLoop_OMSimulator-cs-euler.fmu) > ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_OMSimulator-cs-euler.pipe 2>&1) [Timeout 252.0] OMSimulator-cs-euler timed out simulating the FMU (rm -f ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy.pipe ; mkfifo ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy.pipe ; head -c 1048576 < ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy.pipe >> /var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy.sim & (cd run_fmpy && python3 -m fmpy simulate --output-file ../ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy_res.csv --output-variables 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 efficiency.displayVariablefinal efficiency.showNumber efficiency.significantDigits flowResistance.D_h flowResistance.L flowResistance.L_value flowResistance.a flowResistance.areaCross flowResistance.areaCrossInput flowResistance.areaHydraulic flowResistance.b flowResistance.clip_p_out flowResistance.dp flowResistance.dp_ref_color flowResistance.dr_corr flowResistance.h_in flowResistance.h_out flowResistance.initM_flow 'der(flowResistance.inlet.m_flow)' flowResistance.inlet.m_flow flowResistance.inlet.r flowResistance.inlet.state.T flowResistance.inlet.state.d flowResistance.inlet.state.h flowResistance.inlet.state.p flowResistance.inlet.state.phase flowResistance.l flowResistance.m_acceleration_0 flowResistance.m_flow flowResistance.m_flowStateSelect flowResistance.m_flow_0 flowResistance.mu_in flowResistance.outlet.m_flow flowResistance.outlet.r flowResistance.outlet.state.T flowResistance.outlet.state.d flowResistance.outlet.state.h flowResistance.outlet.state.p flowResistance.outlet.state.phase flowResistance.p_in flowResistance.p_min flowResistance.p_out flowResistance.perimeter flowResistance.perimeterInput flowResistance.phi flowResistance.pressureDropSignificantDigits flowResistance.r flowResistance.rho_in flowResistance.rho_min flowResistance.shape pump.L pump.P pump.P_nom pump.TC pump.adiabaticModel.eta_is pump.adiabaticModel.h_in pump.adiabaticModel.h_out pump.adiabaticModel.h_out_is pump.adiabaticModel.p_out pump.adiabaticModel.s_in pump.adiabaticModel.state_in.T pump.adiabaticModel.state_in.d pump.adiabaticModel.state_in.h pump.adiabaticModel.state_in.p pump.adiabaticModel.state_in.phase pump.adiabaticModel.w_t pump.adiabaticModel.w_t_is pump.assertionLevel pump.clip_p_out pump.dh pump.dp pump.dp_fixed pump.dp_nom pump.dp_start pump.dr_corr pump.etaSpec pump.eta_actual pump.eta_fixed pump.eta_is pump.h_in pump.h_out pump.initM_flow 'der(pump.inlet.m_flow)' pump.inlet.m_flow pump.inlet.r pump.inlet.state.T pump.inlet.state.d pump.inlet.state.h pump.inlet.state.p pump.inlet.state.phase pump.m_acceleration_0 pump.m_flow pump.m_flowStateSelect pump.m_flow_0 pump.outlet.m_flow pump.outlet.r pump.outlet.state.T pump.outlet.state.d pump.outlet.state.h pump.outlet.state.p pump.outlet.state.phase pump.outletSpec pump.outletSpec_actual pump.outletValueSpec pump.pRatio pump.pRatio_fixed pump.p_in pump.p_min pump.p_out pump.p_out_fixed pump.singularityRegime steamGenerator.L steamGenerator.P steamGenerator.Q_flow steamGenerator.T_out_fixed steamGenerator.assertionLevel steamGenerator.clip_p_out steamGenerator.dT steamGenerator.dT_fixed steamGenerator.dh steamGenerator.dh_fixed steamGenerator.dp steamGenerator.dr_corr steamGenerator.du steamGenerator.h_in steamGenerator.h_out steamGenerator.h_out_fixed steamGenerator.initM_flow 'der(steamGenerator.inlet.m_flow)' steamGenerator.inlet.m_flow steamGenerator.inlet.r steamGenerator.inlet.state.T steamGenerator.inlet.state.d steamGenerator.inlet.state.h steamGenerator.inlet.state.p steamGenerator.inlet.state.phase steamGenerator.m_acceleration_0 steamGenerator.m_flow steamGenerator.m_flowStateSelect steamGenerator.m_flow_0 steamGenerator.outlet.m_flow steamGenerator.outlet.r steamGenerator.outlet.state.T steamGenerator.outlet.state.d steamGenerator.outlet.state.h steamGenerator.outlet.state.p steamGenerator.outlet.state.phase steamGenerator.outletSpec steamGenerator.outletSpec_actual steamGenerator.outletValueSpec steamGenerator.p steamGenerator.p_in steamGenerator.p_inf steamGenerator.p_min steamGenerator.p_out steamGenerator.q steamGenerator.rho_in steamGenerator.rho_out steamGenerator.singularityRegime steamGenerator.systemSpec steamGenerator.u_in steamGenerator.u_out steamGenerator.v_in steamGenerator.v_out steamGenerator.w_amb steamGenerator.w_exp steamGenerator.w_exp_net turbine.L turbine.P turbine.P_nom turbine.TC turbine.adiabaticModel.eta_is turbine.adiabaticModel.h_in turbine.adiabaticModel.h_out turbine.adiabaticModel.h_out_is turbine.adiabaticModel.p_out turbine.adiabaticModel.s_in turbine.adiabaticModel.state_in.T turbine.adiabaticModel.state_in.d turbine.adiabaticModel.state_in.h turbine.adiabaticModel.state_in.p turbine.adiabaticModel.state_in.phase turbine.adiabaticModel.w_t turbine.adiabaticModel.w_t_is turbine.assertionLevel turbine.clip_p_out turbine.dh turbine.dp turbine.dp_fixed turbine.dp_nom turbine.dp_start turbine.dr_corr turbine.etaSpec turbine.eta_actual turbine.eta_fixed turbine.eta_is turbine.h_in turbine.h_out turbine.initM_flow 'der(turbine.inlet.m_flow)' turbine.inlet.m_flow turbine.inlet.r turbine.inlet.state.T turbine.inlet.state.d turbine.inlet.state.h turbine.inlet.state.p turbine.inlet.state.phase turbine.m_acceleration_0 turbine.m_flow turbine.m_flowStateSelect turbine.m_flow_0 turbine.outlet.m_flow turbine.outlet.r turbine.outlet.state.T turbine.outlet.state.d turbine.outlet.state.h turbine.outlet.state.p turbine.outlet.state.phase turbine.outletSpec turbine.outletSpec_actual turbine.outletValueSpec turbine.pRatio turbine.pRatio_fixed turbine.p_in turbine.p_min turbine.p_out turbine.p_out_fixed turbine.singularityRegime waterSink.L 'der(waterSink.inlet.m_flow)' waterSink.inlet.m_flow waterSink.inlet.r waterSink.inlet.state.T waterSink.inlet.state.d waterSink.inlet.state.h waterSink.inlet.state.p waterSink.inlet.state.phase waterSink.p waterSink.p0 waterSink.p0_par waterSink.r waterSource.L waterSource.T0 waterSource.T0_par waterSource.h0 waterSource.h0_par 'der(waterSource.outlet.m_flow)' waterSource.outlet.m_flow waterSource.outlet.r waterSource.outlet.state.T waterSource.outlet.state.d waterSource.outlet.state.h waterSource.outlet.state.p waterSource.outlet.state.phase waterSource.p0 waterSource.p0_par --start-time 0 --stop-time 1 --timeout 240 --relative-tolerance 1e-06 --interface-type ModelExchange --solver CVode --output-interval 0.01 ../ThermofluidStream_dev_ThermofluidStream_Idealized_Examples_ClausiusRankine_Step1OpenLoop.fmu) > ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy.pipe 2>&1) [Timeout 252.0] diffSimulationResults("ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy_res.csv","/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_ref.mat","",relTol=0.003,relTolDiffMinMax=0.003,rangeDelta=0.001) [Timeout 660] "Error: Could not read variable CPUtime in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy_res.csv. Warning: Get data of variable CPUtime from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy_res.csv failed! Error: Could not read variable EventCounter in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy_res.csv. Warning: Get data of variable EventCounter from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy_res.csv failed! Error: Could not read variable dropOfCommons.instanceNameColor[1] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy_res.csv. Warning: Get data of variable dropOfCommons.instanceNameColor[1] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy_res.csv failed! Error: Could not read variable dropOfCommons.instanceNameColor[2] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy_res.csv. Warning: Get data of variable dropOfCommons.instanceNameColor[2] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy_res.csv failed! Error: Could not read variable dropOfCommons.instanceNameColor[3] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy_res.csv. Warning: Get data of variable dropOfCommons.instanceNameColor[3] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy_res.csv failed! Error: Could not read variable flowResistance.mu_in in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy_res.csv. Warning: Get data of variable flowResistance.mu_in from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy_res.csv failed! Error: Could not read variable flowResistance.rho_in in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy_res.csv. Warning: Get data of variable flowResistance.rho_in from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy_res.csv failed! Error: Could not read variable steamGenerator.outletSpec_actual in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy_res.csv. Warning: Get data of variable steamGenerator.outletSpec_actual from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy_res.csv failed! Error: Could not read variable waterSink.p in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy_res.csv. Warning: Get data of variable waterSink.p from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy_res.csv failed! Error: Could not read variable waterSink.r in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy_res.csv. Warning: Get data of variable waterSink.r from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy_res.csv failed! " [Timeout remaining time 660] Not compared, constant in the reference and not in the result: dropOfCommons.instanceNameColor[1],dropOfCommons.instanceNameColor[2],dropOfCommons.instanceNameColor[3],flowResistance.mu_in,flowResistance.rho_in,steamGenerator.outletSpec_actual "" Variables in the reference: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,efficiency.displayVariablefinal,efficiency.showNumber,efficiency.significantDigits,flowResistance.D_h,flowResistance.L,flowResistance.L_value,flowResistance.a,flowResistance.areaCross,flowResistance.areaCrossInput,flowResistance.areaHydraulic,flowResistance.b,flowResistance.clip_p_out,flowResistance.dp,flowResistance.dp_ref_color,flowResistance.dr_corr,flowResistance.h_in,flowResistance.h_out,flowResistance.initM_flow,der(flowResistance.inlet.m_flow),flowResistance.inlet.m_flow,flowResistance.inlet.r,flowResistance.inlet.state.T,flowResistance.inlet.state.d,flowResistance.inlet.state.h,flowResistance.inlet.state.p,flowResistance.inlet.state.phase,flowResistance.l,flowResistance.m_acceleration_0,flowResistance.m_flow,flowResistance.m_flowStateSelect,flowResistance.m_flow_0,flowResistance.mu_in,flowResistance.outlet.m_flow,flowResistance.outlet.r,flowResistance.outlet.state.T,flowResistance.outlet.state.d,flowResistance.outlet.state.h,flowResistance.outlet.state.p,flowResistance.outlet.state.phase,flowResistance.p_in,flowResistance.p_min,flowResistance.p_out,flowResistance.perimeter,flowResistance.perimeterInput,flowResistance.phi,flowResistance.pressureDropSignificantDigits,flowResistance.r,flowResistance.rho_in,flowResistance.rho_min,flowResistance.shape,pump.L,pump.P,pump.P_nom,pump.TC,pump.adiabaticModel.eta_is,pump.adiabaticModel.h_in,pump.adiabaticModel.h_out,pump.adiabaticModel.h_out_is,pump.adiabaticModel.p_out,pump.adiabaticModel.s_in,pump.adiabaticModel.state_in.T,pump.adiabaticModel.state_in.d,pump.adiabaticModel.state_in.h,pump.adiabaticModel.state_in.p,pump.adiabaticModel.state_in.phase,pump.adiabaticModel.w_t,pump.adiabaticModel.w_t_is,pump.assertionLevel,pump.clip_p_out,pump.dh,pump.dp,pump.dp_fixed,pump.dp_nom,pump.dp_start,pump.dr_corr,pump.etaSpec,pump.eta_actual,pump.eta_fixed,pump.eta_is,pump.h_in,pump.h_out,pump.initM_flow,der(pump.inlet.m_flow),pump.inlet.m_flow,pump.inlet.r,pump.inlet.state.T,pump.inlet.state.d,pump.inlet.state.h,pump.inlet.state.p,pump.inlet.state.phase,pump.m_acceleration_0,pump.m_flow,pump.m_flowStateSelect,pump.m_flow_0,pump.outlet.m_flow,pump.outlet.r,pump.outlet.state.T,pump.outlet.state.d,pump.outlet.state.h,pump.outlet.state.p,pump.outlet.state.phase,pump.outletSpec,pump.outletSpec_actual,pump.outletValueSpec,pump.pRatio,pump.pRatio_fixed,pump.p_in,pump.p_min,pump.p_out,pump.p_out_fixed,pump.singularityRegime,steamGenerator.L,steamGenerator.P,steamGenerator.Q_flow,steamGenerator.T_out_fixed,steamGenerator.assertionLevel,steamGenerator.clip_p_out,steamGenerator.dT,steamGenerator.dT_fixed,steamGenerator.dh,steamGenerator.dh_fixed,steamGenerator.dp,steamGenerator.dr_corr,steamGenerator.du,steamGenerator.h_in,steamGenerator.h_out,steamGenerator.h_out_fixed,steamGenerator.initM_flow,der(steamGenerator.inlet.m_flow),steamGenerator.inlet.m_flow,steamGenerator.inlet.r,steamGenerator.inlet.state.T,steamGenerator.inlet.state.d,steamGenerator.inlet.state.h,steamGenerator.inlet.state.p,steamGenerator.inlet.state.phase,steamGenerator.m_acceleration_0,steamGenerator.m_flow,steamGenerator.m_flowStateSelect,steamGenerator.m_flow_0,steamGenerator.outlet.m_flow,steamGenerator.outlet.r,steamGenerator.outlet.state.T,steamGenerator.outlet.state.d,steamGenerator.outlet.state.h,steamGenerator.outlet.state.p,steamGenerator.outlet.state.phase,steamGenerator.outletSpec,steamGenerator.outletSpec_actual,steamGenerator.outletValueSpec,steamGenerator.p,steamGenerator.p_in,steamGenerator.p_inf,steamGenerator.p_min,steamGenerator.p_out,steamGenerator.q,steamGenerator.rho_in,steamGenerator.rho_out,steamGenerator.singularityRegime,steamGenerator.systemSpec,steamGenerator.u_in,steamGenerator.u_out,steamGenerator.v_in,steamGenerator.v_out,steamGenerator.w_amb,steamGenerator.w_exp,steamGenerator.w_exp_net,turbine.L,turbine.P,turbine.P_nom,turbine.TC,turbine.adiabaticModel.eta_is,turbine.adiabaticModel.h_in,turbine.adiabaticModel.h_out,turbine.adiabaticModel.h_out_is,turbine.adiabaticModel.p_out,turbine.adiabaticModel.s_in,turbine.adiabaticModel.state_in.T,turbine.adiabaticModel.state_in.d,turbine.adiabaticModel.state_in.h,turbine.adiabaticModel.state_in.p,turbine.adiabaticModel.state_in.phase,turbine.adiabaticModel.w_t,turbine.adiabaticModel.w_t_is,turbine.assertionLevel,turbine.clip_p_out,turbine.dh,turbine.dp,turbine.dp_fixed,turbine.dp_nom,turbine.dp_start,turbine.dr_corr,turbine.etaSpec,turbine.eta_actual,turbine.eta_fixed,turbine.eta_is,turbine.h_in,turbine.h_out,turbine.initM_flow,der(turbine.inlet.m_flow),turbine.inlet.m_flow,turbine.inlet.r,turbine.inlet.state.T,turbine.inlet.state.d,turbine.inlet.state.h,turbine.inlet.state.p,turbine.inlet.state.phase,turbine.m_acceleration_0,turbine.m_flow,turbine.m_flowStateSelect,turbine.m_flow_0,turbine.outlet.m_flow,turbine.outlet.r,turbine.outlet.state.T,turbine.outlet.state.d,turbine.outlet.state.h,turbine.outlet.state.p,turbine.outlet.state.phase,turbine.outletSpec,turbine.outletSpec_actual,turbine.outletValueSpec,turbine.pRatio,turbine.pRatio_fixed,turbine.p_in,turbine.p_min,turbine.p_out,turbine.p_out_fixed,turbine.singularityRegime,waterSink.L,der(waterSink.inlet.m_flow),waterSink.inlet.m_flow,waterSink.inlet.r,waterSink.inlet.state.T,waterSink.inlet.state.d,waterSink.inlet.state.h,waterSink.inlet.state.p,waterSink.inlet.state.phase,waterSink.p,waterSink.p0,waterSink.p0_par,waterSink.r,waterSource.L,waterSource.T0,waterSource.T0_par,waterSource.h0,waterSource.h0_par,der(waterSource.outlet.m_flow),waterSource.outlet.m_flow,waterSource.outlet.r,waterSource.outlet.state.T,waterSource.outlet.state.d,waterSource.outlet.state.h,waterSource.outlet.state.p,waterSource.outlet.state.phase,waterSource.p0,waterSource.p0_par Variables in the result:time,flowResistance.inlet.m_flow,der(flowResistance.inlet.m_flow),flowResistance.dp,flowResistance.dr_corr,flowResistance.h_in,flowResistance.m_flow,flowResistance.p_out,flowResistance.phi,pump.adiabaticModel.h_out_is,pump.adiabaticModel.s_in,pump.adiabaticModel.state_in.d,pump.adiabaticModel.w_t,pump.adiabaticModel.w_t_is,pump.dh,pump.dp,pump.dr_corr,pump.h_in,pump.outlet.r,pump.pRatio,pump.singularityRegime,steamGenerator.P,steamGenerator.Q_flow,steamGenerator.dT,steamGenerator.dp,steamGenerator.dr_corr,steamGenerator.du,steamGenerator.h_in,steamGenerator.outlet.r,steamGenerator.q,steamGenerator.rho_in,steamGenerator.rho_out,steamGenerator.singularityRegime,steamGenerator.u_in,steamGenerator.u_out,steamGenerator.v_in,steamGenerator.v_out,steamGenerator.w_amb,steamGenerator.w_exp,steamGenerator.w_exp_net,turbine.adiabaticModel.h_out_is,turbine.adiabaticModel.s_in,turbine.adiabaticModel.state_in.T,turbine.adiabaticModel.w_t,turbine.adiabaticModel.w_t_is,turbine.dh,turbine.dp,turbine.dr_corr,turbine.h_in,turbine.outlet.r,turbine.outlet.state.T,turbine.outlet.state.d,turbine.pRatio,turbine.singularityRegime,waterSink.inlet.r,waterSink.inlet.state.T,waterSink.inlet.state.d,waterSource.outlet.r,dropOfCommons.L,dropOfCommons.g,dropOfCommons.k_volume_damping,dropOfCommons.m_flow_reg,dropOfCommons.omega_reg,dropOfCommons.p_min,dropOfCommons.rho_min,flowResistance.D_h,flowResistance.L,flowResistance.L_value,flowResistance.a,flowResistance.areaCross,flowResistance.areaCrossInput,flowResistance.areaHydraulic,flowResistance.b,flowResistance.dp_ref_color,flowResistance.inlet.state.p,flowResistance.l,flowResistance.m_acceleration_0,flowResistance.m_flow_0,flowResistance.p_in,flowResistance.p_min,flowResistance.perimeter,flowResistance.perimeterInput,flowResistance.r,flowResistance.rho_min,pump.L,pump.P_nom,pump.TC,pump.adiabaticModel.eta_is,pump.adiabaticModel.p_out,pump.adiabaticModel.state_in.T,pump.adiabaticModel.state_in.p,pump.dp_fixed,pump.dp_nom,pump.dp_start,pump.eta_fixed,pump.eta_is,pump.inlet.state.T,pump.inlet.state.p,pump.m_acceleration_0,pump.m_flow_0,pump.outlet.state.p,pump.pRatio_fixed,pump.p_in,pump.p_min,pump.p_out,pump.p_out_fixed,steamGenerator.L,steamGenerator.T_out_fixed,steamGenerator.dT_fixed,steamGenerator.dh_fixed,steamGenerator.h_out_fixed,steamGenerator.inlet.state.p,steamGenerator.m_acceleration_0,steamGenerator.m_flow_0,steamGenerator.outlet.state.p,steamGenerator.p_in,steamGenerator.p_inf,steamGenerator.p_min,steamGenerator.p_out,turbine.L,turbine.P_nom,turbine.TC,turbine.adiabaticModel.eta_is,turbine.adiabaticModel.p_out,turbine.adiabaticModel.state_in.p,turbine.dp_fixed,turbine.dp_nom,turbine.dp_start,turbine.eta_fixed,turbine.eta_is,turbine.inlet.state.p,turbine.m_acceleration_0,turbine.m_flow_0,turbine.outlet.state.p,turbine.pRatio_fixed,turbine.p_in,turbine.p_min,turbine.p_out,turbine.p_out_fixed,waterSink.L,waterSink.p0_par,waterSource.L,waterSource.T0_par,waterSource.h0_par,waterSource.outlet.state.T,waterSource.outlet.state.p,waterSource.p0_par,der(pump.inlet.m_flow),der(steamGenerator.inlet.m_flow),der(turbine.inlet.m_flow),der(waterSink.inlet.m_flow),der(waterSource.outlet.m_flow),efficiency.showNumber,flowResistance.h_out,flowResistance.inlet.r,flowResistance.inlet.state.T,flowResistance.inlet.state.d,flowResistance.inlet.state.h,flowResistance.outlet.m_flow,flowResistance.outlet.r,flowResistance.outlet.state.T,flowResistance.outlet.state.d,flowResistance.outlet.state.h,flowResistance.outlet.state.p,pump.P,pump.adiabaticModel.h_in,pump.adiabaticModel.h_out,pump.adiabaticModel.state_in.h,pump.h_out,pump.inlet.m_flow,pump.inlet.r,pump.inlet.state.d,pump.inlet.state.h,pump.m_flow,pump.outlet.m_flow,pump.outlet.state.T,pump.outlet.state.d,pump.outlet.state.h,steamGenerator.dh,steamGenerator.h_out,steamGenerator.inlet.m_flow,steamGenerator.inlet.r,steamGenerator.inlet.state.T,steamGenerator.inlet.state.d,steamGenerator.inlet.state.h,steamGenerator.m_flow,steamGenerator.outlet.m_flow,steamGenerator.outlet.state.T,steamGenerator.outlet.state.d,steamGenerator.outlet.state.h,turbine.P,turbine.adiabaticModel.h_in,turbine.adiabaticModel.h_out,turbine.adiabaticModel.state_in.d,turbine.adiabaticModel.state_in.h,turbine.h_out,turbine.inlet.m_flow,turbine.inlet.r,turbine.inlet.state.T,turbine.inlet.state.d,turbine.inlet.state.h,turbine.m_flow,turbine.outlet.m_flow,turbine.outlet.state.h,waterSink.inlet.m_flow,waterSink.inlet.state.h,waterSink.inlet.state.p,waterSource.outlet.m_flow,waterSource.outlet.state.d,waterSource.outlet.state.h,flowResistance.outlet.state.phase,pump.outlet.state.phase,steamGenerator.outlet.state.phase,turbine.outlet.state.phase,waterSource.outlet.state.phase,dropOfCommons.assertionLevel,efficiency.significantDigits,flowResistance.initM_flow,flowResistance.m_flowStateSelect,flowResistance.pressureDropSignificantDigits,flowResistance.shape,pump.assertionLevel,pump.etaSpec,pump.initM_flow,pump.m_flowStateSelect,pump.outletSpec,pump.outletValueSpec,steamGenerator.assertionLevel,steamGenerator.initM_flow,steamGenerator.m_flowStateSelect,steamGenerator.outletSpec,steamGenerator.outletValueSpec,steamGenerator.systemSpec,turbine.assertionLevel,turbine.etaSpec,turbine.initM_flow,turbine.m_flowStateSelect,turbine.outletSpec,turbine.outletValueSpec,flowResistance.inlet.state.phase,pump.adiabaticModel.state_in.phase,pump.inlet.state.phase,steamGenerator.inlet.state.phase,turbine.adiabaticModel.state_in.phase,turbine.inlet.state.phase,waterSink.inlet.state.phase,efficiency.displayVariablefinal,flowResistance.clip_p_out,pump.clip_p_out,steamGenerator.clip_p_out,turbine.clip_p_out filterSimulationResults("ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy_res.csv", "/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy.diff.mat", vars={"waterSink.r", "waterSink.p"}, removeDescription=false) [Timeout 660] "Error: Could not read variable waterSink.r in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy_res.csv. " [Timeout remaining time 660] Failed to write the differing variables of ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy_res.csv to /var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy.diff.mat: "" filterSimulationResults("/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_ref.mat", "/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy.diff.ref.mat", vars={"waterSink.r", "waterSink.p"}, removeDescription=false) [Timeout 660] "" [Timeout remaining time 660] (rm -f ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy-fmi3-cs-cvode.pipe ; mkfifo ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy-fmi3-cs-cvode.pipe ; head -c 1048576 < ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy-fmi3-cs-cvode.pipe >> /var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy-fmi3-cs-cvode.sim & (cd run_fmpy-fmi3-cs-cvode && python3 -m fmpy simulate --output-file ../ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy-fmi3-cs-cvode_res.csv --output-variables 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 efficiency.displayVariablefinal efficiency.showNumber efficiency.significantDigits flowResistance.D_h flowResistance.L flowResistance.L_value flowResistance.a flowResistance.areaCross flowResistance.areaCrossInput flowResistance.areaHydraulic flowResistance.b flowResistance.clip_p_out flowResistance.dp flowResistance.dp_ref_color flowResistance.dr_corr flowResistance.h_in flowResistance.h_out flowResistance.initM_flow 'der(flowResistance.inlet.m_flow)' flowResistance.inlet.m_flow flowResistance.inlet.r flowResistance.inlet.state.T flowResistance.inlet.state.d flowResistance.inlet.state.h flowResistance.inlet.state.p flowResistance.inlet.state.phase flowResistance.l flowResistance.m_acceleration_0 flowResistance.m_flow flowResistance.m_flowStateSelect flowResistance.m_flow_0 flowResistance.mu_in flowResistance.outlet.m_flow flowResistance.outlet.r flowResistance.outlet.state.T flowResistance.outlet.state.d flowResistance.outlet.state.h flowResistance.outlet.state.p flowResistance.outlet.state.phase flowResistance.p_in flowResistance.p_min flowResistance.p_out flowResistance.perimeter flowResistance.perimeterInput flowResistance.phi flowResistance.pressureDropSignificantDigits flowResistance.r flowResistance.rho_in flowResistance.rho_min flowResistance.shape pump.L pump.P pump.P_nom pump.TC pump.adiabaticModel.eta_is pump.adiabaticModel.h_in pump.adiabaticModel.h_out pump.adiabaticModel.h_out_is pump.adiabaticModel.p_out pump.adiabaticModel.s_in pump.adiabaticModel.state_in.T pump.adiabaticModel.state_in.d pump.adiabaticModel.state_in.h pump.adiabaticModel.state_in.p pump.adiabaticModel.state_in.phase pump.adiabaticModel.w_t pump.adiabaticModel.w_t_is pump.assertionLevel pump.clip_p_out pump.dh pump.dp pump.dp_fixed pump.dp_nom pump.dp_start pump.dr_corr pump.etaSpec pump.eta_actual pump.eta_fixed pump.eta_is pump.h_in pump.h_out pump.initM_flow 'der(pump.inlet.m_flow)' pump.inlet.m_flow pump.inlet.r pump.inlet.state.T pump.inlet.state.d pump.inlet.state.h pump.inlet.state.p pump.inlet.state.phase pump.m_acceleration_0 pump.m_flow pump.m_flowStateSelect pump.m_flow_0 pump.outlet.m_flow pump.outlet.r pump.outlet.state.T pump.outlet.state.d pump.outlet.state.h pump.outlet.state.p pump.outlet.state.phase pump.outletSpec pump.outletSpec_actual pump.outletValueSpec pump.pRatio pump.pRatio_fixed pump.p_in pump.p_min pump.p_out pump.p_out_fixed pump.singularityRegime steamGenerator.L steamGenerator.P steamGenerator.Q_flow steamGenerator.T_out_fixed steamGenerator.assertionLevel steamGenerator.clip_p_out steamGenerator.dT steamGenerator.dT_fixed steamGenerator.dh steamGenerator.dh_fixed steamGenerator.dp steamGenerator.dr_corr steamGenerator.du steamGenerator.h_in steamGenerator.h_out steamGenerator.h_out_fixed steamGenerator.initM_flow 'der(steamGenerator.inlet.m_flow)' steamGenerator.inlet.m_flow steamGenerator.inlet.r steamGenerator.inlet.state.T steamGenerator.inlet.state.d steamGenerator.inlet.state.h steamGenerator.inlet.state.p steamGenerator.inlet.state.phase steamGenerator.m_acceleration_0 steamGenerator.m_flow steamGenerator.m_flowStateSelect steamGenerator.m_flow_0 steamGenerator.outlet.m_flow steamGenerator.outlet.r steamGenerator.outlet.state.T steamGenerator.outlet.state.d steamGenerator.outlet.state.h steamGenerator.outlet.state.p steamGenerator.outlet.state.phase steamGenerator.outletSpec steamGenerator.outletSpec_actual steamGenerator.outletValueSpec steamGenerator.p steamGenerator.p_in steamGenerator.p_inf steamGenerator.p_min steamGenerator.p_out steamGenerator.q steamGenerator.rho_in steamGenerator.rho_out steamGenerator.singularityRegime steamGenerator.systemSpec steamGenerator.u_in steamGenerator.u_out steamGenerator.v_in steamGenerator.v_out steamGenerator.w_amb steamGenerator.w_exp steamGenerator.w_exp_net turbine.L turbine.P turbine.P_nom turbine.TC turbine.adiabaticModel.eta_is turbine.adiabaticModel.h_in turbine.adiabaticModel.h_out turbine.adiabaticModel.h_out_is turbine.adiabaticModel.p_out turbine.adiabaticModel.s_in turbine.adiabaticModel.state_in.T turbine.adiabaticModel.state_in.d turbine.adiabaticModel.state_in.h turbine.adiabaticModel.state_in.p turbine.adiabaticModel.state_in.phase turbine.adiabaticModel.w_t turbine.adiabaticModel.w_t_is turbine.assertionLevel turbine.clip_p_out turbine.dh turbine.dp turbine.dp_fixed turbine.dp_nom turbine.dp_start turbine.dr_corr turbine.etaSpec turbine.eta_actual turbine.eta_fixed turbine.eta_is turbine.h_in turbine.h_out turbine.initM_flow 'der(turbine.inlet.m_flow)' turbine.inlet.m_flow turbine.inlet.r turbine.inlet.state.T turbine.inlet.state.d turbine.inlet.state.h turbine.inlet.state.p turbine.inlet.state.phase turbine.m_acceleration_0 turbine.m_flow turbine.m_flowStateSelect turbine.m_flow_0 turbine.outlet.m_flow turbine.outlet.r turbine.outlet.state.T turbine.outlet.state.d turbine.outlet.state.h turbine.outlet.state.p turbine.outlet.state.phase turbine.outletSpec turbine.outletSpec_actual turbine.outletValueSpec turbine.pRatio turbine.pRatio_fixed turbine.p_in turbine.p_min turbine.p_out turbine.p_out_fixed turbine.singularityRegime waterSink.L 'der(waterSink.inlet.m_flow)' waterSink.inlet.m_flow waterSink.inlet.r waterSink.inlet.state.T waterSink.inlet.state.d waterSink.inlet.state.h waterSink.inlet.state.p waterSink.inlet.state.phase waterSink.p waterSink.p0 waterSink.p0_par waterSink.r waterSource.L waterSource.T0 waterSource.T0_par waterSource.h0 waterSource.h0_par 'der(waterSource.outlet.m_flow)' waterSource.outlet.m_flow waterSource.outlet.r waterSource.outlet.state.T waterSource.outlet.state.d waterSource.outlet.state.h waterSource.outlet.state.p waterSource.outlet.state.phase waterSource.p0 waterSource.p0_par dropOfCommons.instanceNameColor --start-time 0 --stop-time 1 --timeout 240 --relative-tolerance 1e-06 --interface-type CoSimulation --output-interval 0.01 ../ThermofluidStream_dev_ThermofluidStream_Idealized_Examples_ClausiusRankine_Step1OpenLoop_fmpy-fmi3-cs-cvode.fmu) > ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy-fmi3-cs-cvode.pipe 2>&1) [Timeout 252.0] diffSimulationResults("ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy-fmi3-cs-cvode_res.csv","/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_ref.mat","",relTol=0.003,relTolDiffMinMax=0.003,rangeDelta=0.001) [Timeout 660] "Error: Could not read variable CPUtime in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy-fmi3-cs-cvode_res.csv. Warning: Get data of variable CPUtime from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy-fmi3-cs-cvode_res.csv failed! Error: Could not read variable EventCounter in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy-fmi3-cs-cvode_res.csv. Warning: Get data of variable EventCounter from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy-fmi3-cs-cvode_res.csv failed! Error: Could not read variable dropOfCommons.instanceNameColor[1] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy-fmi3-cs-cvode_res.csv. Warning: Get data of variable dropOfCommons.instanceNameColor[1] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy-fmi3-cs-cvode_res.csv failed! Error: Could not read variable dropOfCommons.instanceNameColor[2] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy-fmi3-cs-cvode_res.csv. Warning: Get data of variable dropOfCommons.instanceNameColor[2] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy-fmi3-cs-cvode_res.csv failed! Error: Could not read variable dropOfCommons.instanceNameColor[3] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy-fmi3-cs-cvode_res.csv. Warning: Get data of variable dropOfCommons.instanceNameColor[3] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy-fmi3-cs-cvode_res.csv failed! Error: Could not read variable flowResistance.mu_in in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy-fmi3-cs-cvode_res.csv. Warning: Get data of variable flowResistance.mu_in from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy-fmi3-cs-cvode_res.csv failed! Error: Could not read variable flowResistance.rho_in in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy-fmi3-cs-cvode_res.csv. Warning: Get data of variable flowResistance.rho_in from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy-fmi3-cs-cvode_res.csv failed! Error: Could not read variable steamGenerator.outletSpec_actual in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy-fmi3-cs-cvode_res.csv. Warning: Get data of variable steamGenerator.outletSpec_actual from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy-fmi3-cs-cvode_res.csv failed! Error: Could not read variable waterSink.p in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy-fmi3-cs-cvode_res.csv. Warning: Get data of variable waterSink.p from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy-fmi3-cs-cvode_res.csv failed! Error: Could not read variable waterSink.r in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy-fmi3-cs-cvode_res.csv. Warning: Get data of variable waterSink.r from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy-fmi3-cs-cvode_res.csv failed! " [Timeout remaining time 660] Not compared, constant in the reference and not in the result: dropOfCommons.instanceNameColor[1],dropOfCommons.instanceNameColor[2],dropOfCommons.instanceNameColor[3],flowResistance.mu_in,flowResistance.rho_in,steamGenerator.outletSpec_actual "" Variables in the reference: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,efficiency.displayVariablefinal,efficiency.showNumber,efficiency.significantDigits,flowResistance.D_h,flowResistance.L,flowResistance.L_value,flowResistance.a,flowResistance.areaCross,flowResistance.areaCrossInput,flowResistance.areaHydraulic,flowResistance.b,flowResistance.clip_p_out,flowResistance.dp,flowResistance.dp_ref_color,flowResistance.dr_corr,flowResistance.h_in,flowResistance.h_out,flowResistance.initM_flow,der(flowResistance.inlet.m_flow),flowResistance.inlet.m_flow,flowResistance.inlet.r,flowResistance.inlet.state.T,flowResistance.inlet.state.d,flowResistance.inlet.state.h,flowResistance.inlet.state.p,flowResistance.inlet.state.phase,flowResistance.l,flowResistance.m_acceleration_0,flowResistance.m_flow,flowResistance.m_flowStateSelect,flowResistance.m_flow_0,flowResistance.mu_in,flowResistance.outlet.m_flow,flowResistance.outlet.r,flowResistance.outlet.state.T,flowResistance.outlet.state.d,flowResistance.outlet.state.h,flowResistance.outlet.state.p,flowResistance.outlet.state.phase,flowResistance.p_in,flowResistance.p_min,flowResistance.p_out,flowResistance.perimeter,flowResistance.perimeterInput,flowResistance.phi,flowResistance.pressureDropSignificantDigits,flowResistance.r,flowResistance.rho_in,flowResistance.rho_min,flowResistance.shape,pump.L,pump.P,pump.P_nom,pump.TC,pump.adiabaticModel.eta_is,pump.adiabaticModel.h_in,pump.adiabaticModel.h_out,pump.adiabaticModel.h_out_is,pump.adiabaticModel.p_out,pump.adiabaticModel.s_in,pump.adiabaticModel.state_in.T,pump.adiabaticModel.state_in.d,pump.adiabaticModel.state_in.h,pump.adiabaticModel.state_in.p,pump.adiabaticModel.state_in.phase,pump.adiabaticModel.w_t,pump.adiabaticModel.w_t_is,pump.assertionLevel,pump.clip_p_out,pump.dh,pump.dp,pump.dp_fixed,pump.dp_nom,pump.dp_start,pump.dr_corr,pump.etaSpec,pump.eta_actual,pump.eta_fixed,pump.eta_is,pump.h_in,pump.h_out,pump.initM_flow,der(pump.inlet.m_flow),pump.inlet.m_flow,pump.inlet.r,pump.inlet.state.T,pump.inlet.state.d,pump.inlet.state.h,pump.inlet.state.p,pump.inlet.state.phase,pump.m_acceleration_0,pump.m_flow,pump.m_flowStateSelect,pump.m_flow_0,pump.outlet.m_flow,pump.outlet.r,pump.outlet.state.T,pump.outlet.state.d,pump.outlet.state.h,pump.outlet.state.p,pump.outlet.state.phase,pump.outletSpec,pump.outletSpec_actual,pump.outletValueSpec,pump.pRatio,pump.pRatio_fixed,pump.p_in,pump.p_min,pump.p_out,pump.p_out_fixed,pump.singularityRegime,steamGenerator.L,steamGenerator.P,steamGenerator.Q_flow,steamGenerator.T_out_fixed,steamGenerator.assertionLevel,steamGenerator.clip_p_out,steamGenerator.dT,steamGenerator.dT_fixed,steamGenerator.dh,steamGenerator.dh_fixed,steamGenerator.dp,steamGenerator.dr_corr,steamGenerator.du,steamGenerator.h_in,steamGenerator.h_out,steamGenerator.h_out_fixed,steamGenerator.initM_flow,der(steamGenerator.inlet.m_flow),steamGenerator.inlet.m_flow,steamGenerator.inlet.r,steamGenerator.inlet.state.T,steamGenerator.inlet.state.d,steamGenerator.inlet.state.h,steamGenerator.inlet.state.p,steamGenerator.inlet.state.phase,steamGenerator.m_acceleration_0,steamGenerator.m_flow,steamGenerator.m_flowStateSelect,steamGenerator.m_flow_0,steamGenerator.outlet.m_flow,steamGenerator.outlet.r,steamGenerator.outlet.state.T,steamGenerator.outlet.state.d,steamGenerator.outlet.state.h,steamGenerator.outlet.state.p,steamGenerator.outlet.state.phase,steamGenerator.outletSpec,steamGenerator.outletSpec_actual,steamGenerator.outletValueSpec,steamGenerator.p,steamGenerator.p_in,steamGenerator.p_inf,steamGenerator.p_min,steamGenerator.p_out,steamGenerator.q,steamGenerator.rho_in,steamGenerator.rho_out,steamGenerator.singularityRegime,steamGenerator.systemSpec,steamGenerator.u_in,steamGenerator.u_out,steamGenerator.v_in,steamGenerator.v_out,steamGenerator.w_amb,steamGenerator.w_exp,steamGenerator.w_exp_net,turbine.L,turbine.P,turbine.P_nom,turbine.TC,turbine.adiabaticModel.eta_is,turbine.adiabaticModel.h_in,turbine.adiabaticModel.h_out,turbine.adiabaticModel.h_out_is,turbine.adiabaticModel.p_out,turbine.adiabaticModel.s_in,turbine.adiabaticModel.state_in.T,turbine.adiabaticModel.state_in.d,turbine.adiabaticModel.state_in.h,turbine.adiabaticModel.state_in.p,turbine.adiabaticModel.state_in.phase,turbine.adiabaticModel.w_t,turbine.adiabaticModel.w_t_is,turbine.assertionLevel,turbine.clip_p_out,turbine.dh,turbine.dp,turbine.dp_fixed,turbine.dp_nom,turbine.dp_start,turbine.dr_corr,turbine.etaSpec,turbine.eta_actual,turbine.eta_fixed,turbine.eta_is,turbine.h_in,turbine.h_out,turbine.initM_flow,der(turbine.inlet.m_flow),turbine.inlet.m_flow,turbine.inlet.r,turbine.inlet.state.T,turbine.inlet.state.d,turbine.inlet.state.h,turbine.inlet.state.p,turbine.inlet.state.phase,turbine.m_acceleration_0,turbine.m_flow,turbine.m_flowStateSelect,turbine.m_flow_0,turbine.outlet.m_flow,turbine.outlet.r,turbine.outlet.state.T,turbine.outlet.state.d,turbine.outlet.state.h,turbine.outlet.state.p,turbine.outlet.state.phase,turbine.outletSpec,turbine.outletSpec_actual,turbine.outletValueSpec,turbine.pRatio,turbine.pRatio_fixed,turbine.p_in,turbine.p_min,turbine.p_out,turbine.p_out_fixed,turbine.singularityRegime,waterSink.L,der(waterSink.inlet.m_flow),waterSink.inlet.m_flow,waterSink.inlet.r,waterSink.inlet.state.T,waterSink.inlet.state.d,waterSink.inlet.state.h,waterSink.inlet.state.p,waterSink.inlet.state.phase,waterSink.p,waterSink.p0,waterSink.p0_par,waterSink.r,waterSource.L,waterSource.T0,waterSource.T0_par,waterSource.h0,waterSource.h0_par,der(waterSource.outlet.m_flow),waterSource.outlet.m_flow,waterSource.outlet.r,waterSource.outlet.state.T,waterSource.outlet.state.d,waterSource.outlet.state.h,waterSource.outlet.state.p,waterSource.outlet.state.phase,waterSource.p0,waterSource.p0_par Variables in the result:time,flowResistance.inlet.m_flow,der(flowResistance.inlet.m_flow),flowResistance.dp,flowResistance.dr_corr,flowResistance.h_in,flowResistance.m_flow,flowResistance.p_out,flowResistance.phi,pump.adiabaticModel.h_out_is,pump.adiabaticModel.s_in,pump.adiabaticModel.state_in.d,pump.adiabaticModel.w_t,pump.adiabaticModel.w_t_is,pump.dh,pump.dp,pump.dr_corr,pump.h_in,pump.outlet.r,pump.pRatio,pump.singularityRegime,steamGenerator.P,steamGenerator.Q_flow,steamGenerator.dT,steamGenerator.dp,steamGenerator.dr_corr,steamGenerator.du,steamGenerator.h_in,steamGenerator.outlet.r,steamGenerator.q,steamGenerator.rho_in,steamGenerator.rho_out,steamGenerator.singularityRegime,steamGenerator.u_in,steamGenerator.u_out,steamGenerator.v_in,steamGenerator.v_out,steamGenerator.w_amb,steamGenerator.w_exp,steamGenerator.w_exp_net,turbine.adiabaticModel.h_out_is,turbine.adiabaticModel.s_in,turbine.adiabaticModel.state_in.T,turbine.adiabaticModel.w_t,turbine.adiabaticModel.w_t_is,turbine.dh,turbine.dp,turbine.dr_corr,turbine.h_in,turbine.outlet.r,turbine.outlet.state.T,turbine.outlet.state.d,turbine.pRatio,turbine.singularityRegime,waterSink.inlet.r,waterSink.inlet.state.T,waterSink.inlet.state.d,waterSource.outlet.r,dropOfCommons.L,dropOfCommons.g,dropOfCommons.k_volume_damping,dropOfCommons.m_flow_reg,dropOfCommons.omega_reg,dropOfCommons.p_min,dropOfCommons.rho_min,flowResistance.D_h,flowResistance.L,flowResistance.L_value,flowResistance.a,flowResistance.areaCross,flowResistance.areaCrossInput,flowResistance.areaHydraulic,flowResistance.b,flowResistance.dp_ref_color,flowResistance.inlet.state.p,flowResistance.l,flowResistance.m_acceleration_0,flowResistance.m_flow_0,flowResistance.p_in,flowResistance.p_min,flowResistance.perimeter,flowResistance.perimeterInput,flowResistance.r,flowResistance.rho_min,pump.L,pump.P_nom,pump.TC,pump.adiabaticModel.eta_is,pump.adiabaticModel.p_out,pump.adiabaticModel.state_in.T,pump.adiabaticModel.state_in.p,pump.dp_fixed,pump.dp_nom,pump.dp_start,pump.eta_fixed,pump.eta_is,pump.inlet.state.T,pump.inlet.state.p,pump.m_acceleration_0,pump.m_flow_0,pump.outlet.state.p,pump.pRatio_fixed,pump.p_in,pump.p_min,pump.p_out,pump.p_out_fixed,steamGenerator.L,steamGenerator.T_out_fixed,steamGenerator.dT_fixed,steamGenerator.dh_fixed,steamGenerator.h_out_fixed,steamGenerator.inlet.state.p,steamGenerator.m_acceleration_0,steamGenerator.m_flow_0,steamGenerator.outlet.state.p,steamGenerator.p_in,steamGenerator.p_inf,steamGenerator.p_min,steamGenerator.p_out,turbine.L,turbine.P_nom,turbine.TC,turbine.adiabaticModel.eta_is,turbine.adiabaticModel.p_out,turbine.adiabaticModel.state_in.p,turbine.dp_fixed,turbine.dp_nom,turbine.dp_start,turbine.eta_fixed,turbine.eta_is,turbine.inlet.state.p,turbine.m_acceleration_0,turbine.m_flow_0,turbine.outlet.state.p,turbine.pRatio_fixed,turbine.p_in,turbine.p_min,turbine.p_out,turbine.p_out_fixed,waterSink.L,waterSink.p0_par,waterSource.L,waterSource.T0_par,waterSource.h0_par,waterSource.outlet.state.T,waterSource.outlet.state.p,waterSource.p0_par,der(waterSource.outlet.m_flow),flowResistance.outlet.m_flow,pump.outlet.m_flow,steamGenerator.outlet.m_flow,turbine.outlet.m_flow,waterSource.outlet.m_flow,pump.inlet.m_flow,pump.m_flow,steamGenerator.inlet.m_flow,steamGenerator.m_flow,turbine.inlet.m_flow,turbine.m_flow,waterSink.inlet.m_flow,der(pump.inlet.m_flow),der(steamGenerator.inlet.m_flow),der(turbine.inlet.m_flow),der(waterSink.inlet.m_flow),efficiency.showNumber,flowResistance.h_out,flowResistance.inlet.state.h,flowResistance.outlet.state.h,turbine.adiabaticModel.h_out,turbine.h_out,turbine.outlet.state.h,waterSink.inlet.state.h,flowResistance.outlet.state.p,waterSink.inlet.state.p,pump.P,pump.inlet.state.d,waterSource.outlet.state.d,pump.adiabaticModel.h_in,pump.adiabaticModel.state_in.h,pump.inlet.state.h,waterSource.outlet.state.h,steamGenerator.inlet.r,pump.outlet.state.T,steamGenerator.inlet.state.T,pump.adiabaticModel.h_out,pump.h_out,pump.outlet.state.h,steamGenerator.inlet.state.h,turbine.inlet.r,steamGenerator.dh,pump.outlet.state.d,steamGenerator.inlet.state.d,steamGenerator.outlet.state.d,turbine.adiabaticModel.state_in.d,turbine.inlet.state.d,turbine.P,steamGenerator.outlet.state.T,turbine.inlet.state.T,steamGenerator.h_out,steamGenerator.outlet.state.h,turbine.adiabaticModel.h_in,turbine.adiabaticModel.state_in.h,turbine.inlet.state.h,flowResistance.inlet.r,flowResistance.inlet.state.T,flowResistance.inlet.state.d,flowResistance.outlet.r,flowResistance.outlet.state.T,flowResistance.outlet.state.d,pump.inlet.r,flowResistance.outlet.state.phase,pump.outlet.state.phase,steamGenerator.outlet.state.phase,turbine.outlet.state.phase,waterSource.outlet.state.phase,efficiency.significantDigits,flowResistance.pressureDropSignificantDigits,waterSink.inlet.state.phase,steamGenerator.inlet.state.phase,turbine.adiabaticModel.state_in.phase,turbine.inlet.state.phase,flowResistance.inlet.state.phase,pump.adiabaticModel.state_in.phase,pump.inlet.state.phase,dropOfCommons.assertionLevel,flowResistance.initM_flow,flowResistance.m_flowStateSelect,flowResistance.shape,pump.assertionLevel,pump.etaSpec,pump.initM_flow,pump.m_flowStateSelect,pump.outletSpec,pump.outletValueSpec,steamGenerator.assertionLevel,steamGenerator.initM_flow,steamGenerator.m_flowStateSelect,steamGenerator.outletSpec,steamGenerator.outletValueSpec,steamGenerator.systemSpec,turbine.assertionLevel,turbine.etaSpec,turbine.initM_flow,turbine.m_flowStateSelect,turbine.outletSpec,turbine.outletValueSpec,efficiency.displayVariablefinal,flowResistance.clip_p_out,pump.clip_p_out,steamGenerator.clip_p_out,turbine.clip_p_out filterSimulationResults("ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy-fmi3-cs-cvode_res.csv", "/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy-fmi3-cs-cvode.diff.mat", vars={"waterSink.r", "waterSink.p"}, removeDescription=false) [Timeout 660] "Error: Could not read variable waterSink.r in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy-fmi3-cs-cvode_res.csv. " [Timeout remaining time 660] Failed to write the differing variables of ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy-fmi3-cs-cvode_res.csv to /var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy-fmi3-cs-cvode.diff.mat: "" filterSimulationResults("/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_ref.mat", "/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_fmpy-fmi3-cs-cvode.diff.ref.mat", vars={"waterSink.r", "waterSink.p"}, removeDescription=false) [Timeout 660] "" [Timeout remaining time 660] [Calling sys.exit(0), Time elapsed: 9.143716713413596]