Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso.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 0.00112/0.00112, allocations: 76.16 kB / 9.861 MB, free: 0.8281 MB / 10.45 MB
Notification: Performance of NFInstanceAPI.mkTop(<interactive>): time 0.001616/0.002736, 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 0.001118/0.001118, allocations: 141.2 kB / 11.17 MB, free: 3 MB / 13.93 MB
Notification: Performance of NFInstanceAPI.mkTop(<interactive>): time 0.001434/0.002552, 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 0.9148/0.9148, allocations: 177.2 MB / 189.5 MB, free: 5.32 MB / 186.7 MB
Notification: Performance of NFInstanceAPI.mkTop(<interactive>): time 0.07624/0.991, allocations: 53.66 MB / 243.2 MB, free: 15.58 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 0.6505/0.6505, allocations: 118.7 MB / 362.6 MB, free: 1.285 MB / 346.7 MB
Notification: Performance of NFInstanceAPI.mkTop(<interactive>): time 0.05189/0.7024, allocations: 35.84 MB / 398.5 MB, free: 13.36 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.Examples.Utilities.Tests.BoilerEspresso,fileNamePrefix="ThermofluidStream_dev_ThermofluidStream_Examples_Utilities_Tests_BoilerEspresso",fmuType="me_cs",version="2.0+3.0",platforms={"static"})
"" <> buildModelFMU(ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso,fileNamePrefix="ThermofluidStream_dev_ThermofluidStream_Examples_Utilities_Tests_BoilerEspresso",fmuType="me_cs",version="2.0+3.0",platforms={"static"}) [Timeout 660]
"Notification: Performance of FrontEnd - loaded program: time 1.803e-06/1.803e-06, allocations: 0 / 399.7 MB, free: 12.11 MB / 394.7 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 1.873e-05/2.053e-05, allocations: 2.312 kB / 399.7 MB, free: 12.1 MB / 394.7 MB
Notification: Performance of NFInst.instantiate(ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso): time 0.02095/0.02097, allocations: 21.69 MB / 421.4 MB, free: 6.32 MB / 410.7 MB
Notification: Performance of NFInst.instExpressions: time 0.1798/0.2008, allocations: 14.7 MB / 436.1 MB, free: 1.047 MB / 410.7 MB
Notification: Performance of NFInst.updateImplicitVariability: time 0.000993/0.2017, allocations: 76.38 kB / 436.2 MB, free: 1.047 MB / 410.7 MB
Notification: Performance of NFTyping.typeComponents: time 0.0007003/0.2024, allocations: 391 kB / 436.6 MB, free: 1.047 MB / 410.7 MB
Notification: Performance of NFTyping.typeBindings: time 0.004147/0.2066, allocations: 2.607 MB / 439.2 MB, free: 0.6406 MB / 410.7 MB
Notification: Performance of NFTyping.typeClassSections: time 0.006794/0.2134, allocations: 3.991 MB / 443.2 MB, free: 15.87 MB / 426.7 MB
Notification: Performance of NFFlatten.flatten: time 0.002334/0.2157, allocations: 3.045 MB / 446.2 MB, free: 14.6 MB / 426.7 MB
Notification: Performance of NFFlatten.resolveConnections: time 0.0005683/0.2163, allocations: 495.2 kB / 446.7 MB, free: 14.26 MB / 426.7 MB
Notification: Performance of NFEvalConstants.evaluate: time 0.003947/0.2202, allocations: 3.123 MB / 449.8 MB, free: 12.68 MB / 426.7 MB
Notification: Performance of NFSimplifyModel.simplify: time 0.000947/0.2212, allocations: 0.867 MB / 450.7 MB, free: 12.25 MB / 426.7 MB
Notification: Performance of NFPackage.collectConstants: time 0.000202/0.2214, allocations: 185.8 kB / 450.9 MB, free: 12.25 MB / 426.7 MB
Notification: Performance of NFFlatten.collectFunctions: time 0.008552/0.2299, allocations: 7.546 MB / 458.4 MB, free: 6.797 MB / 426.7 MB
Notification: Performance of NFScalarize.scalarize: time 0.000244/0.2302, allocations: 346.6 kB / 458.8 MB, free: 6.457 MB / 426.7 MB
Notification: Performance of NFVerifyModel.verify: time 0.0005567/0.2307, allocations: 0.6082 MB / 459.4 MB, free: 5.848 MB / 426.7 MB
Notification: Performance of NFConvertDAE.convert: time 0.005821/0.2366, allocations: 5.426 MB / 464.8 MB, free: 0.6758 MB / 426.7 MB
Notification: Performance of FrontEnd - DAE generated: time 1.211e-05/0.2366, allocations: 0 / 464.8 MB, free: 0.6758 MB / 426.7 MB
Notification: Performance of FrontEnd: time 1.492e-06/0.2366, allocations: 0 / 464.8 MB, free: 0.6758 MB / 426.7 MB
Notification: Performance of Transformations before backend: time 3.136e-05/0.2366, allocations: 0 / 464.8 MB, free: 0.6758 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: 388
 * Number of variables: 388
Notification: Performance of Generate backend data structure: time 0.00463/0.2412, allocations: 3.878 MB / 468.7 MB, free: 12.88 MB / 442.7 MB
Notification: Performance of prepare preOptimizeDAE: time 3.346e-05/0.2413, allocations: 8.031 kB / 468.7 MB, free: 12.87 MB / 442.7 MB
Notification: Performance of preOpt introduceOutputAliases (simulation): time 0.0001609/0.2414, allocations: 234.2 kB / 468.9 MB, free: 12.69 MB / 442.7 MB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.001185/0.2426, allocations: 0.6109 MB / 469.5 MB, free: 12.08 MB / 442.7 MB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.001295/0.2439, allocations: 0.9883 MB / 470.5 MB, free: 11.08 MB / 442.7 MB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 7.961e-05/0.244, allocations: 124.5 kB / 470.6 MB, free: 10.96 MB / 442.7 MB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.0001616/0.2441, allocations: 171.7 kB / 470.8 MB, free: 10.79 MB / 442.7 MB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.001987/0.2461, allocations: 1.719 MB / 472.5 MB, free: 8.984 MB / 442.7 MB
Notification: Performance of preOpt findStateOrder (simulation): time 3.14e-05/0.2462, allocations: 7.938 kB / 472.5 MB, free: 8.977 MB / 442.7 MB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 8.878e-05/0.2463, allocations: 64 kB / 472.6 MB, free: 8.914 MB / 442.7 MB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 4.89e-05/0.2463, allocations: 50.86 kB / 472.6 MB, free: 8.863 MB / 442.7 MB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.001359/0.2477, allocations: 0.7507 MB / 473.4 MB, free: 8.109 MB / 442.7 MB
Warning: The model contains alias variables with redundant start and/or conflicting nominal values. It is recommended to resolve the conflicts, because otherwise the system could be hard to solve. To print the conflicting alias sets and the chosen candidates please use -d=aliasConflicts.
Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.004038/0.2517, allocations: 4.221 MB / 477.6 MB, free: 3.984 MB / 442.7 MB
Notification: Performance of preOpt comSubExp (simulation): time 0.001174/0.2529, allocations: 0.8643 MB / 478.5 MB, free: 3.152 MB / 442.7 MB
Notification: Performance of preOpt resolveLoops (simulation): time 0.000277/0.2532, allocations: 254.1 kB / 478.7 MB, free: 2.91 MB / 442.7 MB
Notification: Performance of preOpt evalFunc (simulation): time 0.1228/0.376, allocations: 70.02 MB / 0.5359 GB, free: 12.96 MB / 0.5105 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 0.001321/0.3773, allocations: 0.8279 MB / 0.5367 GB, free: 12.13 MB / 0.5105 GB
Notification: Performance of pre-optimization done (n=132): time 2.515e-06/0.3773, allocations: 0 / 0.5367 GB, free: 12.13 MB / 0.5105 GB
Notification: Performance of matching and sorting (n=132): time 0.003011/0.3803, allocations: 1.673 MB / 0.5383 GB, free: 10.45 MB / 0.5105 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 7.014e-05/0.3804, allocations: 201.2 kB / 0.5385 GB, free: 10.21 MB / 0.5105 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.0007671/0.3812, allocations: 1.027 MB / 0.5395 GB, free: 9.367 MB / 0.5105 GB
Notification: Performance of collectPreVariables (initialization): time 6.275e-05/0.3812, allocations: 53.7 kB / 0.5396 GB, free: 9.309 MB / 0.5105 GB
Notification: Performance of collectInitialEqns (initialization): time 0.0002836/0.3815, allocations: 0.5781 MB / 0.5401 GB, free: 8.781 MB / 0.5105 GB
Notification: Performance of collectInitialBindings (initialization): time 0.0002324/0.3817, allocations: 481.2 kB / 0.5406 GB, free: 8.34 MB / 0.5105 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.0002443/0.382, allocations: 253.6 kB / 0.5408 GB, free: 8.117 MB / 0.5105 GB
Notification: Performance of setup shared object (initialization): time 8.678e-05/0.3821, allocations: 360.2 kB / 0.5412 GB, free: 7.785 MB / 0.5105 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0002451/0.3823, allocations: 220.2 kB / 0.5414 GB, free: 7.555 MB / 0.5105 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.0003944/0.3827, allocations: 0.6349 MB / 0.542 GB, free: 6.801 MB / 0.5105 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.000643/0.3834, allocations: 0.7332 MB / 0.5427 GB, free: 6.008 MB / 0.5105 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 5.14e-06/0.3834, allocations: 4 kB / 0.5427 GB, free: 6.004 MB / 0.5105 GB
Notification: Performance of matching and sorting (n=172) (initialization): time 0.001004/0.3844, allocations: 0.9588 MB / 0.5437 GB, free: 5.008 MB / 0.5105 GB
Notification: Performance of prepare postOptimizeDAE: time 4.726e-05/0.3844, allocations: 68.58 kB / 0.5437 GB, free: 4.93 MB / 0.5105 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 1.102e-05/0.3844, allocations: 9.75 kB / 0.5437 GB, free: 4.922 MB / 0.5105 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.0004292/0.3849, allocations: 182.2 kB / 0.5439 GB, free: 4.734 MB / 0.5105 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0007265/0.3856, allocations: 351.5 kB / 0.5442 GB, free: 4.391 MB / 0.5105 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.002525/0.3881, allocations: 5.194 MB / 0.5493 GB, free: 14.86 MB / 0.5261 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.0005217/0.3886, allocations: 151 kB / 0.5495 GB, free: 14.71 MB / 0.5261 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 6.296e-05/0.3887, allocations: 48.05 kB / 0.5495 GB, free: 14.67 MB / 0.5261 GB
Notification: Performance of preBalanceInitialSystem (initialization_lambda0): time 0.0003967/0.3891, allocations: 318.3 kB / 0.5498 GB, free: 14.34 MB / 0.5261 GB
Notification: Performance of partitionIndependentBlocks (initialization_lambda0): time 0.0003771/0.3895, allocations: 0.6306 MB / 0.5504 GB, free: 13.6 MB / 0.5261 GB
Notification: Performance of analyzeInitialSystem (initialization_lambda0): time 0.0006036/0.3901, allocations: 0.7252 MB / 0.5511 GB, free: 12.81 MB / 0.5261 GB
Notification: Performance of solveInitialSystemEqSystem (initialization_lambda0): time 3.818e-06/0.3901, allocations: 240 / 0.5511 GB, free: 12.81 MB / 0.5261 GB
Notification: Performance of matching and sorting (n=172) (initialization_lambda0): time 0.0009735/0.391, allocations: 0.9561 MB / 0.5521 GB, free: 11.82 MB / 0.5261 GB
Notification: Performance of prepare postOptimizeDAE: time 3.104e-05/0.3911, allocations: 68.48 kB / 0.5521 GB, free: 11.74 MB / 0.5261 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 5.82e-06/0.3911, allocations: 4 kB / 0.5521 GB, free: 11.73 MB / 0.5261 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.0003711/0.3915, allocations: 185.2 kB / 0.5523 GB, free: 11.55 MB / 0.5261 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0006898/0.3921, allocations: 347.5 kB / 0.5526 GB, free: 11.21 MB / 0.5261 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.002294/0.3944, allocations: 5.188 MB / 0.5577 GB, free: 5.668 MB / 0.5261 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.0004603/0.3949, allocations: 127.3 kB / 0.5578 GB, free: 5.543 MB / 0.5261 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 5.916e-05/0.395, allocations: 43.98 kB / 0.5579 GB, free: 5.5 MB / 0.5261 GB
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 25
 * Number of states: 0 ()
 * Number of discrete variables: 22 (source.outlet.state.phase,flowResistance.outlet.state.phase,tanValve1.outlet.state.phase,flowResistance1.outlet.state.phase,tanValve2.outlet.state.phase,flowResistance2.outlet.state.phase,PID2.I.local_reset,PID1.I.local_reset,boilerEspresso.phaseSeparator2_1.state_out[1].phase,boilerEspresso.phaseSeparator2_1.state_out[2].phase,tanValve.outlet.state.phase,pulse1.count,$PRE.pulse1.count,pulse1.T_start,$PRE.pulse1.T_start,pulse.count,$PRE.pulse.count,pulse.T_start,$PRE.pulse.T_start,boilerEspresso.phaseSeparator2_1.medium.phase,$whenCondition1,$whenCondition2)
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for initialization (154):
 * Single equations (assignments): 148
 * Array equations: 0
 * Algorithm blocks: 2
 * Record equations: 0
 * When equations: 0
 * If-equations: 0
 * Equation systems (not torn): 0
 * Torn equation systems: 4
 * Mixed (continuous/discrete) equation systems: 0
Notification: Torn system details for strict tearing set:
 * Linear torn systems (#iteration vars, #inner vars, density): 4 systems
   {(1,3,100.0%), (1,3,100.0%), (1,7,100.0%), (1,3,100.0%)}
 * Non-linear torn systems (#iteration vars, #inner vars): 0 systems
Notification: Performance of prepare postOptimizeDAE: time 0.0001894/0.3951, allocations: 277.4 kB / 0.5581 GB, free: 5.223 MB / 0.5261 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.000141/0.3953, allocations: 143.8 kB / 0.5583 GB, free: 5.082 MB / 0.5261 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.001997/0.3973, allocations: 2.257 MB / 0.5605 GB, free: 2.824 MB / 0.5261 GB
Notification: Performance of postOpt inlineArrayEqn (simulation): time 2.87e-05/0.3973, allocations: 51.92 kB / 0.5605 GB, free: 2.773 MB / 0.5261 GB
Notification: Performance of postOpt constantLinearSystem (simulation): time 4.538e-06/0.3973, allocations: 4 kB / 0.5605 GB, free: 2.77 MB / 0.5261 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 1.141e-05/0.3973, allocations: 12 kB / 0.5605 GB, free: 2.758 MB / 0.5261 GB
Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.003037/0.4004, allocations: 3.328 MB / 0.5638 GB, free: 15.62 MB / 0.5417 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 5.851e-06/0.4004, allocations: 4 kB / 0.5638 GB, free: 15.62 MB / 0.5417 GB
Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.0005316/0.4009, allocations: 243.7 kB / 0.564 GB, free: 15.38 MB / 0.5417 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.000332/0.4012, allocations: 279.9 kB / 0.5643 GB, free: 15.11 MB / 0.5417 GB
Notification: Performance of postOpt tearingSystem (simulation): time 0.000569/0.4018, allocations: 470.5 kB / 0.5647 GB, free: 14.64 MB / 0.5417 GB
Notification: Performance of postOpt inputDerivativesUsed (simulation): time 5.905e-05/0.4019, allocations: 43.92 kB / 0.5648 GB, free: 14.6 MB / 0.5417 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 0.002613/0.4045, allocations: 5.856 MB / 0.5705 GB, free: 8.387 MB / 0.5417 GB
Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 2.184e-06/0.4045, allocations: 0 / 0.5705 GB, free: 8.387 MB / 0.5417 GB
Notification: Performance of postOpt symbolicJacobian (simulation): time 0.001751/0.4062, allocations: 1.902 MB / 0.5724 GB, free: 6.473 MB / 0.5417 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.0001192/0.4063, allocations: 47.88 kB / 0.5724 GB, free: 6.426 MB / 0.5417 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0003878/0.4067, allocations: 67.89 kB / 0.5725 GB, free: 6.359 MB / 0.5417 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 0.0001562/0.4069, allocations: 125 kB / 0.5726 GB, free: 6.234 MB / 0.5417 GB
Notification: Performance of postOpt collapseArrayExpressions (simulation): time 4.855e-05/0.4069, allocations: 31.97 kB / 0.5726 GB, free: 6.203 MB / 0.5417 GB
Notification: Performance of sorting global known variables: time 0.0003889/0.4073, allocations: 0.5681 MB / 0.5732 GB, free: 5.703 MB / 0.5417 GB
Notification: Performance of sort global known variables: time 6e-08/0.4073, allocations: 0 / 0.5732 GB, free: 5.703 MB / 0.5417 GB
Notification: Performance of remove unused functions: time 0.003196/0.4105, allocations: 1.817 MB / 0.575 GB, free: 3.883 MB / 0.5417 GB
Notification: Model statistics after passing the back-end for simulation:
 * Number of independent subsystems: 5
 * Number of states: 10 (boilerEspresso.phaseSeparator2_1.M,boilerEspresso.phaseSeparator2_1.U_med,tanValve.inlet.m_flow,flowResistance1.inlet.m_flow,firstOrder1.y,flowResistance2.inlet.m_flow,firstOrder2.y,firstOrder3.y,PID2.I.y,PID1.I.y)
 * Number of discrete variables: 29 ($cse2.region3boundary,$cse4.region3boundary,$cse5.phase,$cse5.region,$cse6.phase,$cse6.region,$cse9.phase,$cse9.region,$cse10.phase,$cse10.region,$cse13.phase,$cse13.region,$cse16.phase,$cse16.region,$cse18.phase,$cse18.region,$cse19.phase,$cse19.region,$cse23.phase,$cse23.region,$cse24.region3boundary,$cse25.region3boundary,$whenCondition2,$whenCondition1,boilerEspresso.phaseSeparator2_1.medium.phase,pulse.T_start,pulse.count,pulse1.T_start,pulse1.count)
 * Number of discrete states: 2 (pulse1.count,pulse.count)
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for simulation (134):
 * Single equations (assignments): 114
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 11
 * When equations: 4
 * If-equations: 0
 * Equation systems (not torn): 0
 * Torn equation systems: 5
 * Mixed (continuous/discrete) equation systems: 0
Notification: Torn system details for strict tearing set:
 * Linear torn systems (#iteration vars, #inner vars, density): 4 systems
   {(1,3,100.0%), (1,3,100.0%), (1,3,100.0%), (1,7,100.0%)}
 * Non-linear torn systems (#iteration vars, #inner vars): 1 system
   {(1,5)}
Notification: Performance of Backend phase and start with SimCode phase: time 0.005233/0.4158, allocations: 3.692 MB / 0.5786 GB, free: 284 kB / 0.5417 GB
Notification: Performance of simCode: created initialization part: time 0.002156/0.4179, allocations: 2.568 MB / 0.5811 GB, free: 13.57 MB / 0.5573 GB
Notification: Performance of simCode: created event and clocks part: time 1.493e-05/0.4179, allocations: 16 kB / 0.5811 GB, free: 13.55 MB / 0.5573 GB
Notification: Performance of simCode: created simulation system equations: time 0.0007867/0.4187, allocations: 1.075 MB / 0.5821 GB, free: 12.45 MB / 0.5573 GB
Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.00154/0.4203, allocations: 0.8518 MB / 0.583 GB, free: 11.65 MB / 0.5573 GB
Notification: Performance of simCode: created linear, non-linear and system jacobian parts: time 0.008785/0.429, allocations: 9.148 MB / 0.5919 GB, free: 2.562 MB / 0.5573 GB
Notification: Performance of simCode: some other stuff during SimCode phase: time 0.000308/0.4293, allocations: 438 kB / 0.5923 GB, free: 2.105 MB / 0.5573 GB
Notification: Performance of simCode: alias equations: time 0.001111/0.4305, allocations: 0.9958 MB / 0.5933 GB, free: 1.125 MB / 0.5573 GB
Notification: Performance of simCode: all other stuff during SimCode phase: time 0.001443/0.4319, allocations: 1.362 MB / 0.5946 GB, free: 15.76 MB / 0.573 GB
Notification: Performance of SimCode: time 6.51e-07/0.4319, allocations: 0 / 0.5946 GB, free: 15.76 MB / 0.573 GB
Notification: Performance of FMU documentation: time 0.2853/0.7172, allocations: 105.5 MB / 0.6976 GB, free: 147 MB / 0.6042 GB
Notification: FMU-only work: backend 0.001853, simCode 0.003463, templates 0
Notification: Performance of buildModelFMU: Generate the FMI files: time 0.06129/0.7785, allocations: 1.327 MB / 0.6989 GB, free: 145.6 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 4.692/5.471, allocations: 18.56 kB / 0.6989 GB, free: 145.6 MB / 0.6042 GB
"
[Timeout remaining time 654]
(rm -f ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso.pipe ; mkfifo ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso.pipe ; head -c 1048576 < ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso.pipe >> ../files/ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso.sim & (cd run_OMSimulator && /home/hudson/saved_omc/OMSimulator/install/bin/OMSimulator --resultFile=../ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_res.mat --stripRoot --tempDir=temp_ThermofluidStream_dev_ThermofluidStream_Examples_Utilities_Tests_BoilerEspresso_fmu --startTime=0 --stopTime=1000 --stepSize=1 --mode=me --timeout=240 --tolerance=1e-06 ../ThermofluidStream_dev_ThermofluidStream_Examples_Utilities_Tests_BoilerEspresso.fmu) > ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso.pipe 2>&1) [Timeout 252.0]
diffSimulationResults("ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_res.mat","/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_ref.mat","",relTol=0.003,relTolDiffMinMax=0.003,rangeDelta=0.001) [Timeout 660]
"Error: Could not read variable pulse.T_start in file ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_res.mat.
Warning: Get data of variable pulse.T_start from file ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_res.mat failed!
Error: Could not read variable pulse.count in file ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_res.mat.
Warning: Get data of variable pulse.count from file ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_res.mat failed!
Error: Could not read variable pulse1.T_start in file ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_res.mat.
Warning: Get data of variable pulse1.T_start from file ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_res.mat failed!
Error: Could not read variable pulse1.count in file ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_res.mat.
Warning: Get data of variable pulse1.count from file ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_res.mat failed!
"
[Timeout remaining time 660]
""

Variables in the reference:PID1.I.y,PID2.I.y,boilerEspresso.phaseSeparator2_1.M,boilerEspresso.phaseSeparator2_1.U_med,firstOrder1.y,firstOrder2.y,firstOrder3.y,pulse.T_start,pulse.count,pulse1.T_start,pulse1.count,source.outlet.m_flow,tanValve1.inlet.m_flow,tanValve2.inlet.m_flow

Variables in the result:PID1.Dzero.k,PID1.Dzero.y,PID1.FFzero.k,PID1.FFzero.y,PID1.I.initType,PID1.I.k,PID1.I.u,PID1.I.use_reset,PID1.I.use_set,PID1.I.y,PID1.I.y_start,PID1.Nd,PID1.Ni,PID1.P.k,PID1.P.u,PID1.P.y,PID1.Td,PID1.Ti,PID1.addFF.k1,PID1.addFF.k2,PID1.addFF.u1,PID1.addFF.u2,PID1.addFF.y,PID1.addI.k1,PID1.addI.k2,PID1.addI.k3,PID1.addI.u1,PID1.addI.u2,PID1.addI.u3,PID1.addI.y,PID1.addP.k1,PID1.addP.k2,PID1.addP.u1,PID1.addP.u2,PID1.addP.y,PID1.addPID.k1,PID1.addPID.k2,PID1.addPID.k3,PID1.addPID.u1,PID1.addPID.u2,PID1.addPID.u3,PID1.addPID.y,PID1.addSat.k1,PID1.addSat.k2,PID1.addSat.u1,PID1.addSat.u2,PID1.addSat.y,PID1.controlError,PID1.controllerType,PID1.gainPID.k,PID1.gainPID.u,PID1.gainPID.y,PID1.gainTrack.k,PID1.gainTrack.u,PID1.gainTrack.y,PID1.homotopyType,PID1.initType,PID1.k,PID1.kFF,PID1.limiter.homotopyType,PID1.limiter.strict,PID1.limiter.u,PID1.limiter.uMax,PID1.limiter.uMin,PID1.limiter.y,PID1.strict,PID1.u_m,PID1.u_s,PID1.wd,PID1.withFeedForward,PID1.wp,PID1.xd_start,PID1.xi_start,PID1.y,PID1.yMax,PID1.yMin,PID1.y_start,PID2.Dzero.k,PID2.Dzero.y,PID2.FFzero.k,PID2.FFzero.y,PID2.I.initType,PID2.I.k,PID2.I.u,PID2.I.use_reset,PID2.I.use_set,PID2.I.y,PID2.I.y_start,PID2.Nd,PID2.Ni,PID2.P.k,PID2.P.u,PID2.P.y,PID2.Td,PID2.Ti,PID2.addFF.k1,PID2.addFF.k2,PID2.addFF.u1,PID2.addFF.u2,PID2.addFF.y,PID2.addI.k1,PID2.addI.k2,PID2.addI.k3,PID2.addI.u1,PID2.addI.u2,PID2.addI.u3,PID2.addI.y,PID2.addP.k1,PID2.addP.k2,PID2.addP.u1,PID2.addP.u2,PID2.addP.y,PID2.addPID.k1,PID2.addPID.k2,PID2.addPID.k3,PID2.addPID.u1,PID2.addPID.u2,PID2.addPID.u3,PID2.addPID.y,PID2.addSat.k1,PID2.addSat.k2,PID2.addSat.u1,PID2.addSat.u2,PID2.addSat.y,PID2.controlError,PID2.controllerType,PID2.gainPID.k,PID2.gainPID.u,PID2.gainPID.y,PID2.gainTrack.k,PID2.gainTrack.u,PID2.gainTrack.y,PID2.homotopyType,PID2.initType,PID2.k,PID2.kFF,PID2.limiter.homotopyType,PID2.limiter.strict,PID2.limiter.u,PID2.limiter.uMax,PID2.limiter.uMin,PID2.limiter.y,PID2.strict,PID2.u_m,PID2.u_s,PID2.wd,PID2.withFeedForward,PID2.wp,PID2.xd_start,PID2.xi_start,PID2.y,PID2.yMax,PID2.yMin,PID2.y_start,boilerEspresso.UA_HX,boilerEspresso.UA_heat,boilerEspresso.V,boilerEspresso.heatport_HX.Q_flow,boilerEspresso.heatport_HX.T,boilerEspresso.heatport_heat.Q_flow,boilerEspresso.heatport_heat.T,boilerEspresso.inlet.m_flow,boilerEspresso.inlet.r,boilerEspresso.inlet.state.T,boilerEspresso.inlet.state.d,boilerEspresso.inlet.state.h,boilerEspresso.inlet.state.p,boilerEspresso.inlet.state.phase,boilerEspresso.p.y,boilerEspresso.p1.y,boilerEspresso.p_0,boilerEspresso.p_out,boilerEspresso.phaseSeparator2_1.A,boilerEspresso.phaseSeparator2_1.L,boilerEspresso.phaseSeparator2_1.M,boilerEspresso.phaseSeparator2_1.M_0,boilerEspresso.phaseSeparator2_1.M_outlets,boilerEspresso.phaseSeparator2_1.Q_flow,boilerEspresso.phaseSeparator2_1.T_start,boilerEspresso.phaseSeparator2_1.U,boilerEspresso.phaseSeparator2_1.U_med,boilerEspresso.phaseSeparator2_1.V,boilerEspresso.phaseSeparator2_1.V_par,boilerEspresso.phaseSeparator2_1.W_v,boilerEspresso.phaseSeparator2_1.density_derp_h_from_media,boilerEspresso.phaseSeparator2_1.density_derp_h_set,boilerEspresso.phaseSeparator2_1.displayInstanceName,boilerEspresso.phaseSeparator2_1.displayParameters,boilerEspresso.phaseSeparator2_1.h_0,boilerEspresso.phaseSeparator2_1.h_start,boilerEspresso.phaseSeparator2_1.heatPort.Q_flow,boilerEspresso.phaseSeparator2_1.heatPort.T,boilerEspresso.phaseSeparator2_1.init_method,boilerEspresso.phaseSeparator2_1.initialize_Xi,boilerEspresso.phaseSeparator2_1.initialize_energy,boilerEspresso.phaseSeparator2_1.initialize_pressure,boilerEspresso.phaseSeparator2_1.inlet.m_flow,boilerEspresso.phaseSeparator2_1.inlet.r,boilerEspresso.phaseSeparator2_1.inlet.state.T,boilerEspresso.phaseSeparator2_1.inlet.state.d,boilerEspresso.phaseSeparator2_1.inlet.state.h,boilerEspresso.phaseSeparator2_1.inlet.state.p,boilerEspresso.phaseSeparator2_1.inlet.state.phase,boilerEspresso.phaseSeparator2_1.k_volume_damping,boilerEspresso.phaseSeparator2_1.l_0,boilerEspresso.phaseSeparator2_1.liquid_level,boilerEspresso.phaseSeparator2_1.liquid_level_pipe1,boilerEspresso.phaseSeparator2_1.liquid_level_pipe2,boilerEspresso.phaseSeparator2_1.m_flow_assert,boilerEspresso.phaseSeparator2_1.medium.MM,boilerEspresso.phaseSeparator2_1.medium.R_s,boilerEspresso.phaseSeparator2_1.medium.T,boilerEspresso.phaseSeparator2_1.medium.T_degC,boilerEspresso.phaseSeparator2_1.medium.X[1],boilerEspresso.phaseSeparator2_1.medium.d,boilerEspresso.phaseSeparator2_1.medium.h,boilerEspresso.phaseSeparator2_1.medium.p,boilerEspresso.phaseSeparator2_1.medium.p_bar,boilerEspresso.phaseSeparator2_1.medium.phase,boilerEspresso.phaseSeparator2_1.medium.preferredMediumStates,boilerEspresso.phaseSeparator2_1.medium.sat.Tsat,boilerEspresso.phaseSeparator2_1.medium.sat.psat,boilerEspresso.phaseSeparator2_1.medium.standardOrderComponents,boilerEspresso.phaseSeparator2_1.medium.state.T,boilerEspresso.phaseSeparator2_1.medium.state.d,boilerEspresso.phaseSeparator2_1.medium.state.h,boilerEspresso.phaseSeparator2_1.medium.state.p,boilerEspresso.phaseSeparator2_1.medium.state.phase,boilerEspresso.phaseSeparator2_1.medium.u,boilerEspresso.phaseSeparator2_1.outlet[1].m_flow,boilerEspresso.phaseSeparator2_1.outlet[1].r,boilerEspresso.phaseSeparator2_1.outlet[1].state.T,boilerEspresso.phaseSeparator2_1.outlet[1].state.d,boilerEspresso.phaseSeparator2_1.outlet[1].state.h,boilerEspresso.phaseSeparator2_1.outlet[1].state.p,boilerEspresso.phaseSeparator2_1.outlet[1].state.phase,boilerEspresso.phaseSeparator2_1.outlet[2].m_flow,boilerEspresso.phaseSeparator2_1.outlet[2].r,boilerEspresso.phaseSeparator2_1.outlet[2].state.T,boilerEspresso.phaseSeparator2_1.outlet[2].state.d,boilerEspresso.phaseSeparator2_1.outlet[2].state.h,boilerEspresso.phaseSeparator2_1.outlet[2].state.p,boilerEspresso.phaseSeparator2_1.outlet[2].state.phase,boilerEspresso.phaseSeparator2_1.p_start,boilerEspresso.phaseSeparator2_1.pipe1_high,boilerEspresso.phaseSeparator2_1.pipe1_low,boilerEspresso.phaseSeparator2_1.pipe2_high,boilerEspresso.phaseSeparator2_1.pipe2_low,boilerEspresso.phaseSeparator2_1.useHeatport,boilerEspresso.phaseSeparator2_1.usePreferredMediumStates,boilerEspresso.phaseSeparator2_1.use_hstart,boilerEspresso.phaseSeparator2_1.x_0,boilerEspresso.steam_out.m_flow,boilerEspresso.steam_out.r,boilerEspresso.steam_out.state.T,boilerEspresso.steam_out.state.d,boilerEspresso.steam_out.state.h,boilerEspresso.steam_out.state.p,boilerEspresso.steam_out.state.phase,boilerEspresso.thermalConductor.G,boilerEspresso.thermalConductor.Q_flow,boilerEspresso.thermalConductor.dT,boilerEspresso.thermalConductor.port_a.Q_flow,boilerEspresso.thermalConductor.port_a.T,boilerEspresso.thermalConductor.port_b.Q_flow,boilerEspresso.thermalConductor.port_b.T,boilerEspresso.thermalConductor1.G,boilerEspresso.thermalConductor1.Q_flow,boilerEspresso.thermalConductor1.dT,boilerEspresso.thermalConductor1.port_a.Q_flow,boilerEspresso.thermalConductor1.port_a.T,boilerEspresso.thermalConductor1.port_b.Q_flow,boilerEspresso.thermalConductor1.port_b.T,boilerEspresso.water_out.m_flow,boilerEspresso.water_out.r,boilerEspresso.water_out.state.T,boilerEspresso.water_out.state.d,boilerEspresso.water_out.state.h,boilerEspresso.water_out.state.p,boilerEspresso.water_out.state.phase,boilerEspresso.x_0,boilerEspresso.y_out,der(PID1.I.y),der(PID1.addPID.u3),der(PID2.I.y),der(PID2.addPID.u3),der(boilerEspresso.inlet.m_flow),der(boilerEspresso.phaseSeparator2_1.M),der(boilerEspresso.phaseSeparator2_1.U_med),der(boilerEspresso.phaseSeparator2_1.inlet.m_flow),der(boilerEspresso.phaseSeparator2_1.outlet[1].m_flow),der(boilerEspresso.phaseSeparator2_1.outlet[2].m_flow),der(boilerEspresso.steam_out.m_flow),der(boilerEspresso.water_out.m_flow),der(firstOrder1.y),der(firstOrder2.y),der(firstOrder3.y),der(flowResistance.inlet.m_flow),der(flowResistance.outlet.m_flow),der(flowResistance1.inlet.m_flow),der(flowResistance1.outlet.m_flow),der(flowResistance2.inlet.m_flow),der(flowResistance2.outlet.m_flow),der(sink.inlet.m_flow),der(sink1.inlet.m_flow),der(source.outlet.m_flow),der(tanValve.inlet.m_flow),der(tanValve.m_flow),der(tanValve.outlet.m_flow),der(tanValve.u),der(tanValve1.inlet.m_flow),der(tanValve1.m_flow),der(tanValve1.outlet.m_flow),der(tanValve1.u),der(tanValve2.inlet.m_flow),der(tanValve2.m_flow),der(tanValve2.outlet.m_flow),der(tanValve2.u),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,firstOrder1.T,firstOrder1.initType,firstOrder1.k,firstOrder1.u,firstOrder1.y,firstOrder1.y_start,firstOrder2.T,firstOrder2.initType,firstOrder2.k,firstOrder2.u,firstOrder2.y,firstOrder2.y_start,firstOrder3.T,firstOrder3.initType,firstOrder3.k,firstOrder3.u,firstOrder3.y,firstOrder3.y_start,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,flowResistance1.D_h,flowResistance1.L,flowResistance1.L_value,flowResistance1.a,flowResistance1.areaCross,flowResistance1.areaCrossInput,flowResistance1.areaHydraulic,flowResistance1.b,flowResistance1.clip_p_out,flowResistance1.computeL,flowResistance1.considerInertance,flowResistance1.displayInstanceName,flowResistance1.displayParameters,flowResistance1.dp,flowResistance1.dp_ref_color,flowResistance1.dr_corr,flowResistance1.h_in,flowResistance1.h_out,flowResistance1.initM_flow,flowResistance1.inlet.m_flow,flowResistance1.inlet.r,flowResistance1.inlet.state.T,flowResistance1.inlet.state.d,flowResistance1.inlet.state.h,flowResistance1.inlet.state.p,flowResistance1.inlet.state.phase,flowResistance1.l,flowResistance1.m_acceleration_0,flowResistance1.m_flow,flowResistance1.m_flowStateSelect,flowResistance1.m_flow_0,flowResistance1.outlet.m_flow,flowResistance1.outlet.r,flowResistance1.outlet.state.T,flowResistance1.outlet.state.d,flowResistance1.outlet.state.h,flowResistance1.outlet.state.p,flowResistance1.outlet.state.phase,flowResistance1.p_in,flowResistance1.p_min,flowResistance1.p_out,flowResistance1.perimeter,flowResistance1.perimeterInput,flowResistance1.phi,flowResistance1.pressureDropSignificantDigits,flowResistance1.pressureDropUnit,flowResistance1.r,flowResistance1.rho_min,flowResistance1.shape,flowResistance1.showPressureDrop,flowResistance2.D_h,flowResistance2.L,flowResistance2.L_value,flowResistance2.a,flowResistance2.areaCross,flowResistance2.areaCrossInput,flowResistance2.areaHydraulic,flowResistance2.b,flowResistance2.clip_p_out,flowResistance2.computeL,flowResistance2.considerInertance,flowResistance2.displayInstanceName,flowResistance2.displayParameters,flowResistance2.dp,flowResistance2.dp_ref_color,flowResistance2.dr_corr,flowResistance2.h_in,flowResistance2.h_out,flowResistance2.initM_flow,flowResistance2.inlet.m_flow,flowResistance2.inlet.r,flowResistance2.inlet.state.T,flowResistance2.inlet.state.d,flowResistance2.inlet.state.h,flowResistance2.inlet.state.p,flowResistance2.inlet.state.phase,flowResistance2.l,flowResistance2.m_acceleration_0,flowResistance2.m_flow,flowResistance2.m_flowStateSelect,flowResistance2.m_flow_0,flowResistance2.outlet.m_flow,flowResistance2.outlet.r,flowResistance2.outlet.state.T,flowResistance2.outlet.state.d,flowResistance2.outlet.state.h,flowResistance2.outlet.state.p,flowResistance2.outlet.state.phase,flowResistance2.p_in,flowResistance2.p_min,flowResistance2.p_out,flowResistance2.perimeter,flowResistance2.perimeterInput,flowResistance2.phi,flowResistance2.pressureDropSignificantDigits,flowResistance2.pressureDropUnit,flowResistance2.r,flowResistance2.rho_min,flowResistance2.shape,flowResistance2.showPressureDrop,prescribedHeatFlow.Q_flow,prescribedHeatFlow.T_ref,prescribedHeatFlow.alpha,prescribedHeatFlow.port.Q_flow,prescribedHeatFlow.port.T,prescribedHeatFlow1.Q_flow,prescribedHeatFlow1.T_ref,prescribedHeatFlow1.alpha,prescribedHeatFlow1.port.Q_flow,prescribedHeatFlow1.port.T,pulse.amplitude,pulse.nperiod,pulse.offset,pulse.period,pulse.startTime,pulse.width,pulse.y,pulse1.amplitude,pulse1.nperiod,pulse1.offset,pulse1.period,pulse1.startTime,pulse1.width,pulse1.y,realExpression.y,realExpression1.y,realExpression2.y,sink.L,sink.considerInertance,sink.displayInertance,sink.displayInstanceName,sink.displayP,sink.displayParameters,sink.displayPressure,sink.inlet.m_flow,sink.inlet.r,sink.inlet.state.T,sink.inlet.state.d,sink.inlet.state.h,sink.inlet.state.p,sink.inlet.state.phase,sink.p0_par,sink.pressureFromInput,sink1.L,sink1.considerInertance,sink1.displayInertance,sink1.displayInstanceName,sink1.displayP,sink1.displayParameters,sink1.displayPressure,sink1.inlet.m_flow,sink1.inlet.r,sink1.inlet.state.T,sink1.inlet.state.d,sink1.inlet.state.h,sink1.inlet.state.p,sink1.inlet.state.phase,sink1.p0_par,sink1.pressureFromInput,source.L,source.T0_par,source.considerInertance,source.displayH,source.displayInertance,source.displayInstanceName,source.displayMassFractions,source.displayP,source.displayParameters,source.displayPressure,source.displayT,source.displayTemperature,source.displayXi,source.enthalpyFromInput,source.h0_par,source.outlet.m_flow,source.outlet.r,source.outlet.state.T,source.outlet.state.d,source.outlet.state.h,source.outlet.state.p,source.outlet.state.phase,source.p0_par,source.pressureFromInput,source.setEnthalpy,source.temperatureFromInput,source.xiFromInput,tanValve.L,tanValve.clip_p_out,tanValve.considerInertance,tanValve.displayInstanceName,tanValve.displayParameters,tanValve.dp,tanValve.dr_corr,tanValve.h_in,tanValve.h_out,tanValve.initM_flow,tanValve.inlet.m_flow,tanValve.inlet.r,tanValve.inlet.state.T,tanValve.inlet.state.d,tanValve.inlet.state.h,tanValve.inlet.state.p,tanValve.inlet.state.phase,tanValve.invertInput,tanValve.m_acceleration_0,tanValve.m_flow,tanValve.m_flowStateSelect,tanValve.m_flow_0,tanValve.m_flow_ref,tanValve.outlet.m_flow,tanValve.outlet.r,tanValve.outlet.state.T,tanValve.outlet.state.d,tanValve.outlet.state.h,tanValve.outlet.state.p,tanValve.outlet.state.phase,tanValve.p_in,tanValve.p_min,tanValve.p_out,tanValve.p_ref,tanValve.relativeLeakiness,tanValve.u,tanValve1.L,tanValve1.clip_p_out,tanValve1.considerInertance,tanValve1.displayInstanceName,tanValve1.displayParameters,tanValve1.dp,tanValve1.dr_corr,tanValve1.h_in,tanValve1.h_out,tanValve1.initM_flow,tanValve1.inlet.m_flow,tanValve1.inlet.r,tanValve1.inlet.state.T,tanValve1.inlet.state.d,tanValve1.inlet.state.h,tanValve1.inlet.state.p,tanValve1.inlet.state.phase,tanValve1.invertInput,tanValve1.m_acceleration_0,tanValve1.m_flow,tanValve1.m_flowStateSelect,tanValve1.m_flow_0,tanValve1.m_flow_ref,tanValve1.outlet.m_flow,tanValve1.outlet.r,tanValve1.outlet.state.T,tanValve1.outlet.state.d,tanValve1.outlet.state.h,tanValve1.outlet.state.p,tanValve1.outlet.state.phase,tanValve1.p_in,tanValve1.p_min,tanValve1.p_out,tanValve1.p_ref,tanValve1.relativeLeakiness,tanValve1.u,tanValve2.L,tanValve2.clip_p_out,tanValve2.considerInertance,tanValve2.displayInstanceName,tanValve2.displayParameters,tanValve2.dp,tanValve2.dr_corr,tanValve2.h_in,tanValve2.h_out,tanValve2.initM_flow,tanValve2.inlet.m_flow,tanValve2.inlet.r,tanValve2.inlet.state.T,tanValve2.inlet.state.d,tanValve2.inlet.state.h,tanValve2.inlet.state.p,tanValve2.inlet.state.phase,tanValve2.invertInput,tanValve2.m_acceleration_0,tanValve2.m_flow,tanValve2.m_flowStateSelect,tanValve2.m_flow_0,tanValve2.m_flow_ref,tanValve2.outlet.m_flow,tanValve2.outlet.r,tanValve2.outlet.state.T,tanValve2.outlet.state.d,tanValve2.outlet.state.h,tanValve2.outlet.state.p,tanValve2.outlet.state.phase,tanValve2.p_in,tanValve2.p_min,tanValve2.p_out,tanValve2.p_ref,tanValve2.relativeLeakiness,tanValve2.u,time
filterSimulationResults("ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_res.mat", "/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso.diff.mat", vars={"source.outlet.m_flow", "pulse1.count", "pulse1.T_start", "pulse.count", "pulse.T_start", "firstOrder3.y", "boilerEspresso.phaseSeparator2_1.U_med", "boilerEspresso.phaseSeparator2_1.M", "PID2.I.y", "PID1.I.y"}, removeDescription=false) [Timeout 660]
"Error: Could not read variable pulse1.count in file ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_res.mat.
"
[Timeout remaining time 660]
Failed to write the differing variables of ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_res.mat to /var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso.diff.mat:
""
filterSimulationResults("/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_ref.mat", "/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso.diff.ref.mat", vars={"source.outlet.m_flow", "pulse1.count", "pulse1.T_start", "pulse.count", "pulse.T_start", "firstOrder3.y", "boilerEspresso.phaseSeparator2_1.U_med", "boilerEspresso.phaseSeparator2_1.M", "PID2.I.y", "PID1.I.y"}, removeDescription=false) [Timeout 660]
""
[Timeout remaining time 660]
(rm -f ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_OMSimulator-cs-cvode.pipe ; mkfifo ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_OMSimulator-cs-cvode.pipe ; head -c 1048576 < ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_OMSimulator-cs-cvode.pipe >> /var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_OMSimulator-cs-cvode.sim & (cd run_OMSimulator-cs-cvode && /home/hudson/saved_omc/OMSimulator/install/bin/OMSimulator --resultFile=../ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_OMSimulator-cs-cvode_res.mat --stripRoot --tempDir=temp_ThermofluidStream_dev_ThermofluidStream_Examples_Utilities_Tests_BoilerEspresso_OMSimulator-cs-cvode_fmu --startTime=0 --stopTime=1000 --stepSize=1 --mode=cs --timeout=240 --tolerance=1e-06 ../ThermofluidStream_dev_ThermofluidStream_Examples_Utilities_Tests_BoilerEspresso_OMSimulator-cs-cvode.fmu) > ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_OMSimulator-cs-cvode.pipe 2>&1) [Timeout 252.0]
diffSimulationResults("ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_OMSimulator-cs-cvode_res.mat","/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_ref.mat","",relTol=0.003,relTolDiffMinMax=0.003,rangeDelta=0.001) [Timeout 660]
"Error: Could not read variable pulse.T_start in file ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_OMSimulator-cs-cvode_res.mat.
Warning: Get data of variable pulse.T_start from file ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_OMSimulator-cs-cvode_res.mat failed!
Error: Could not read variable pulse.count in file ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_OMSimulator-cs-cvode_res.mat.
Warning: Get data of variable pulse.count from file ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_OMSimulator-cs-cvode_res.mat failed!
Error: Could not read variable pulse1.T_start in file ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_OMSimulator-cs-cvode_res.mat.
Warning: Get data of variable pulse1.T_start from file ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_OMSimulator-cs-cvode_res.mat failed!
Error: Could not read variable pulse1.count in file ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_OMSimulator-cs-cvode_res.mat.
Warning: Get data of variable pulse1.count from file ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_OMSimulator-cs-cvode_res.mat failed!
"
[Timeout remaining time 660]
""

Variables in the reference:PID1.I.y,PID2.I.y,boilerEspresso.phaseSeparator2_1.M,boilerEspresso.phaseSeparator2_1.U_med,firstOrder1.y,firstOrder2.y,firstOrder3.y,pulse.T_start,pulse.count,pulse1.T_start,pulse1.count,source.outlet.m_flow,tanValve1.inlet.m_flow,tanValve2.inlet.m_flow

Variables in the result:PID1.Dzero.k,PID1.Dzero.y,PID1.FFzero.k,PID1.FFzero.y,PID1.I.initType,PID1.I.k,PID1.I.u,PID1.I.use_reset,PID1.I.use_set,PID1.I.y,PID1.I.y_start,PID1.Nd,PID1.Ni,PID1.P.k,PID1.P.u,PID1.P.y,PID1.Td,PID1.Ti,PID1.addFF.k1,PID1.addFF.k2,PID1.addFF.u1,PID1.addFF.u2,PID1.addFF.y,PID1.addI.k1,PID1.addI.k2,PID1.addI.k3,PID1.addI.u1,PID1.addI.u2,PID1.addI.u3,PID1.addI.y,PID1.addP.k1,PID1.addP.k2,PID1.addP.u1,PID1.addP.u2,PID1.addP.y,PID1.addPID.k1,PID1.addPID.k2,PID1.addPID.k3,PID1.addPID.u1,PID1.addPID.u2,PID1.addPID.u3,PID1.addPID.y,PID1.addSat.k1,PID1.addSat.k2,PID1.addSat.u1,PID1.addSat.u2,PID1.addSat.y,PID1.controlError,PID1.controllerType,PID1.gainPID.k,PID1.gainPID.u,PID1.gainPID.y,PID1.gainTrack.k,PID1.gainTrack.u,PID1.gainTrack.y,PID1.homotopyType,PID1.initType,PID1.k,PID1.kFF,PID1.limiter.homotopyType,PID1.limiter.strict,PID1.limiter.u,PID1.limiter.uMax,PID1.limiter.uMin,PID1.limiter.y,PID1.strict,PID1.u_m,PID1.u_s,PID1.wd,PID1.withFeedForward,PID1.wp,PID1.xd_start,PID1.xi_start,PID1.y,PID1.yMax,PID1.yMin,PID1.y_start,PID2.Dzero.k,PID2.Dzero.y,PID2.FFzero.k,PID2.FFzero.y,PID2.I.initType,PID2.I.k,PID2.I.u,PID2.I.use_reset,PID2.I.use_set,PID2.I.y,PID2.I.y_start,PID2.Nd,PID2.Ni,PID2.P.k,PID2.P.u,PID2.P.y,PID2.Td,PID2.Ti,PID2.addFF.k1,PID2.addFF.k2,PID2.addFF.u1,PID2.addFF.u2,PID2.addFF.y,PID2.addI.k1,PID2.addI.k2,PID2.addI.k3,PID2.addI.u1,PID2.addI.u2,PID2.addI.u3,PID2.addI.y,PID2.addP.k1,PID2.addP.k2,PID2.addP.u1,PID2.addP.u2,PID2.addP.y,PID2.addPID.k1,PID2.addPID.k2,PID2.addPID.k3,PID2.addPID.u1,PID2.addPID.u2,PID2.addPID.u3,PID2.addPID.y,PID2.addSat.k1,PID2.addSat.k2,PID2.addSat.u1,PID2.addSat.u2,PID2.addSat.y,PID2.controlError,PID2.controllerType,PID2.gainPID.k,PID2.gainPID.u,PID2.gainPID.y,PID2.gainTrack.k,PID2.gainTrack.u,PID2.gainTrack.y,PID2.homotopyType,PID2.initType,PID2.k,PID2.kFF,PID2.limiter.homotopyType,PID2.limiter.strict,PID2.limiter.u,PID2.limiter.uMax,PID2.limiter.uMin,PID2.limiter.y,PID2.strict,PID2.u_m,PID2.u_s,PID2.wd,PID2.withFeedForward,PID2.wp,PID2.xd_start,PID2.xi_start,PID2.y,PID2.yMax,PID2.yMin,PID2.y_start,boilerEspresso.UA_HX,boilerEspresso.UA_heat,boilerEspresso.V,boilerEspresso.heatport_HX.Q_flow,boilerEspresso.heatport_HX.T,boilerEspresso.heatport_heat.Q_flow,boilerEspresso.heatport_heat.T,boilerEspresso.inlet.m_flow,boilerEspresso.inlet.r,boilerEspresso.inlet.state.T,boilerEspresso.inlet.state.d,boilerEspresso.inlet.state.h,boilerEspresso.inlet.state.p,boilerEspresso.inlet.state.phase,boilerEspresso.p.y,boilerEspresso.p1.y,boilerEspresso.p_0,boilerEspresso.p_out,boilerEspresso.phaseSeparator2_1.A,boilerEspresso.phaseSeparator2_1.L,boilerEspresso.phaseSeparator2_1.M,boilerEspresso.phaseSeparator2_1.M_0,boilerEspresso.phaseSeparator2_1.M_outlets,boilerEspresso.phaseSeparator2_1.Q_flow,boilerEspresso.phaseSeparator2_1.T_start,boilerEspresso.phaseSeparator2_1.U,boilerEspresso.phaseSeparator2_1.U_med,boilerEspresso.phaseSeparator2_1.V,boilerEspresso.phaseSeparator2_1.V_par,boilerEspresso.phaseSeparator2_1.W_v,boilerEspresso.phaseSeparator2_1.density_derp_h_from_media,boilerEspresso.phaseSeparator2_1.density_derp_h_set,boilerEspresso.phaseSeparator2_1.displayInstanceName,boilerEspresso.phaseSeparator2_1.displayParameters,boilerEspresso.phaseSeparator2_1.h_0,boilerEspresso.phaseSeparator2_1.h_start,boilerEspresso.phaseSeparator2_1.heatPort.Q_flow,boilerEspresso.phaseSeparator2_1.heatPort.T,boilerEspresso.phaseSeparator2_1.init_method,boilerEspresso.phaseSeparator2_1.initialize_Xi,boilerEspresso.phaseSeparator2_1.initialize_energy,boilerEspresso.phaseSeparator2_1.initialize_pressure,boilerEspresso.phaseSeparator2_1.inlet.m_flow,boilerEspresso.phaseSeparator2_1.inlet.r,boilerEspresso.phaseSeparator2_1.inlet.state.T,boilerEspresso.phaseSeparator2_1.inlet.state.d,boilerEspresso.phaseSeparator2_1.inlet.state.h,boilerEspresso.phaseSeparator2_1.inlet.state.p,boilerEspresso.phaseSeparator2_1.inlet.state.phase,boilerEspresso.phaseSeparator2_1.k_volume_damping,boilerEspresso.phaseSeparator2_1.l_0,boilerEspresso.phaseSeparator2_1.liquid_level,boilerEspresso.phaseSeparator2_1.liquid_level_pipe1,boilerEspresso.phaseSeparator2_1.liquid_level_pipe2,boilerEspresso.phaseSeparator2_1.m_flow_assert,boilerEspresso.phaseSeparator2_1.medium.MM,boilerEspresso.phaseSeparator2_1.medium.R_s,boilerEspresso.phaseSeparator2_1.medium.T,boilerEspresso.phaseSeparator2_1.medium.T_degC,boilerEspresso.phaseSeparator2_1.medium.X[1],boilerEspresso.phaseSeparator2_1.medium.d,boilerEspresso.phaseSeparator2_1.medium.h,boilerEspresso.phaseSeparator2_1.medium.p,boilerEspresso.phaseSeparator2_1.medium.p_bar,boilerEspresso.phaseSeparator2_1.medium.phase,boilerEspresso.phaseSeparator2_1.medium.preferredMediumStates,boilerEspresso.phaseSeparator2_1.medium.sat.Tsat,boilerEspresso.phaseSeparator2_1.medium.sat.psat,boilerEspresso.phaseSeparator2_1.medium.standardOrderComponents,boilerEspresso.phaseSeparator2_1.medium.state.T,boilerEspresso.phaseSeparator2_1.medium.state.d,boilerEspresso.phaseSeparator2_1.medium.state.h,boilerEspresso.phaseSeparator2_1.medium.state.p,boilerEspresso.phaseSeparator2_1.medium.state.phase,boilerEspresso.phaseSeparator2_1.medium.u,boilerEspresso.phaseSeparator2_1.outlet[1].m_flow,boilerEspresso.phaseSeparator2_1.outlet[1].r,boilerEspresso.phaseSeparator2_1.outlet[1].state.T,boilerEspresso.phaseSeparator2_1.outlet[1].state.d,boilerEspresso.phaseSeparator2_1.outlet[1].state.h,boilerEspresso.phaseSeparator2_1.outlet[1].state.p,boilerEspresso.phaseSeparator2_1.outlet[1].state.phase,boilerEspresso.phaseSeparator2_1.outlet[2].m_flow,boilerEspresso.phaseSeparator2_1.outlet[2].r,boilerEspresso.phaseSeparator2_1.outlet[2].state.T,boilerEspresso.phaseSeparator2_1.outlet[2].state.d,boilerEspresso.phaseSeparator2_1.outlet[2].state.h,boilerEspresso.phaseSeparator2_1.outlet[2].state.p,boilerEspresso.phaseSeparator2_1.outlet[2].state.phase,boilerEspresso.phaseSeparator2_1.p_start,boilerEspresso.phaseSeparator2_1.pipe1_high,boilerEspresso.phaseSeparator2_1.pipe1_low,boilerEspresso.phaseSeparator2_1.pipe2_high,boilerEspresso.phaseSeparator2_1.pipe2_low,boilerEspresso.phaseSeparator2_1.useHeatport,boilerEspresso.phaseSeparator2_1.usePreferredMediumStates,boilerEspresso.phaseSeparator2_1.use_hstart,boilerEspresso.phaseSeparator2_1.x_0,boilerEspresso.steam_out.m_flow,boilerEspresso.steam_out.r,boilerEspresso.steam_out.state.T,boilerEspresso.steam_out.state.d,boilerEspresso.steam_out.state.h,boilerEspresso.steam_out.state.p,boilerEspresso.steam_out.state.phase,boilerEspresso.thermalConductor.G,boilerEspresso.thermalConductor.Q_flow,boilerEspresso.thermalConductor.dT,boilerEspresso.thermalConductor.port_a.Q_flow,boilerEspresso.thermalConductor.port_a.T,boilerEspresso.thermalConductor.port_b.Q_flow,boilerEspresso.thermalConductor.port_b.T,boilerEspresso.thermalConductor1.G,boilerEspresso.thermalConductor1.Q_flow,boilerEspresso.thermalConductor1.dT,boilerEspresso.thermalConductor1.port_a.Q_flow,boilerEspresso.thermalConductor1.port_a.T,boilerEspresso.thermalConductor1.port_b.Q_flow,boilerEspresso.thermalConductor1.port_b.T,boilerEspresso.water_out.m_flow,boilerEspresso.water_out.r,boilerEspresso.water_out.state.T,boilerEspresso.water_out.state.d,boilerEspresso.water_out.state.h,boilerEspresso.water_out.state.p,boilerEspresso.water_out.state.phase,boilerEspresso.x_0,boilerEspresso.y_out,der(PID1.I.y),der(PID1.addPID.u3),der(PID2.I.y),der(PID2.addPID.u3),der(boilerEspresso.inlet.m_flow),der(boilerEspresso.phaseSeparator2_1.M),der(boilerEspresso.phaseSeparator2_1.U_med),der(boilerEspresso.phaseSeparator2_1.inlet.m_flow),der(boilerEspresso.phaseSeparator2_1.outlet[1].m_flow),der(boilerEspresso.phaseSeparator2_1.outlet[2].m_flow),der(boilerEspresso.steam_out.m_flow),der(boilerEspresso.water_out.m_flow),der(firstOrder1.y),der(firstOrder2.y),der(firstOrder3.y),der(flowResistance.inlet.m_flow),der(flowResistance.outlet.m_flow),der(flowResistance1.inlet.m_flow),der(flowResistance1.outlet.m_flow),der(flowResistance2.inlet.m_flow),der(flowResistance2.outlet.m_flow),der(sink.inlet.m_flow),der(sink1.inlet.m_flow),der(source.outlet.m_flow),der(tanValve.inlet.m_flow),der(tanValve.m_flow),der(tanValve.outlet.m_flow),der(tanValve.u),der(tanValve1.inlet.m_flow),der(tanValve1.m_flow),der(tanValve1.outlet.m_flow),der(tanValve1.u),der(tanValve2.inlet.m_flow),der(tanValve2.m_flow),der(tanValve2.outlet.m_flow),der(tanValve2.u),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,firstOrder1.T,firstOrder1.initType,firstOrder1.k,firstOrder1.u,firstOrder1.y,firstOrder1.y_start,firstOrder2.T,firstOrder2.initType,firstOrder2.k,firstOrder2.u,firstOrder2.y,firstOrder2.y_start,firstOrder3.T,firstOrder3.initType,firstOrder3.k,firstOrder3.u,firstOrder3.y,firstOrder3.y_start,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,flowResistance1.D_h,flowResistance1.L,flowResistance1.L_value,flowResistance1.a,flowResistance1.areaCross,flowResistance1.areaCrossInput,flowResistance1.areaHydraulic,flowResistance1.b,flowResistance1.clip_p_out,flowResistance1.computeL,flowResistance1.considerInertance,flowResistance1.displayInstanceName,flowResistance1.displayParameters,flowResistance1.dp,flowResistance1.dp_ref_color,flowResistance1.dr_corr,flowResistance1.h_in,flowResistance1.h_out,flowResistance1.initM_flow,flowResistance1.inlet.m_flow,flowResistance1.inlet.r,flowResistance1.inlet.state.T,flowResistance1.inlet.state.d,flowResistance1.inlet.state.h,flowResistance1.inlet.state.p,flowResistance1.inlet.state.phase,flowResistance1.l,flowResistance1.m_acceleration_0,flowResistance1.m_flow,flowResistance1.m_flowStateSelect,flowResistance1.m_flow_0,flowResistance1.outlet.m_flow,flowResistance1.outlet.r,flowResistance1.outlet.state.T,flowResistance1.outlet.state.d,flowResistance1.outlet.state.h,flowResistance1.outlet.state.p,flowResistance1.outlet.state.phase,flowResistance1.p_in,flowResistance1.p_min,flowResistance1.p_out,flowResistance1.perimeter,flowResistance1.perimeterInput,flowResistance1.phi,flowResistance1.pressureDropSignificantDigits,flowResistance1.pressureDropUnit,flowResistance1.r,flowResistance1.rho_min,flowResistance1.shape,flowResistance1.showPressureDrop,flowResistance2.D_h,flowResistance2.L,flowResistance2.L_value,flowResistance2.a,flowResistance2.areaCross,flowResistance2.areaCrossInput,flowResistance2.areaHydraulic,flowResistance2.b,flowResistance2.clip_p_out,flowResistance2.computeL,flowResistance2.considerInertance,flowResistance2.displayInstanceName,flowResistance2.displayParameters,flowResistance2.dp,flowResistance2.dp_ref_color,flowResistance2.dr_corr,flowResistance2.h_in,flowResistance2.h_out,flowResistance2.initM_flow,flowResistance2.inlet.m_flow,flowResistance2.inlet.r,flowResistance2.inlet.state.T,flowResistance2.inlet.state.d,flowResistance2.inlet.state.h,flowResistance2.inlet.state.p,flowResistance2.inlet.state.phase,flowResistance2.l,flowResistance2.m_acceleration_0,flowResistance2.m_flow,flowResistance2.m_flowStateSelect,flowResistance2.m_flow_0,flowResistance2.outlet.m_flow,flowResistance2.outlet.r,flowResistance2.outlet.state.T,flowResistance2.outlet.state.d,flowResistance2.outlet.state.h,flowResistance2.outlet.state.p,flowResistance2.outlet.state.phase,flowResistance2.p_in,flowResistance2.p_min,flowResistance2.p_out,flowResistance2.perimeter,flowResistance2.perimeterInput,flowResistance2.phi,flowResistance2.pressureDropSignificantDigits,flowResistance2.pressureDropUnit,flowResistance2.r,flowResistance2.rho_min,flowResistance2.shape,flowResistance2.showPressureDrop,prescribedHeatFlow.Q_flow,prescribedHeatFlow.T_ref,prescribedHeatFlow.alpha,prescribedHeatFlow.port.Q_flow,prescribedHeatFlow.port.T,prescribedHeatFlow1.Q_flow,prescribedHeatFlow1.T_ref,prescribedHeatFlow1.alpha,prescribedHeatFlow1.port.Q_flow,prescribedHeatFlow1.port.T,pulse.amplitude,pulse.nperiod,pulse.offset,pulse.period,pulse.startTime,pulse.width,pulse.y,pulse1.amplitude,pulse1.nperiod,pulse1.offset,pulse1.period,pulse1.startTime,pulse1.width,pulse1.y,realExpression.y,realExpression1.y,realExpression2.y,sink.L,sink.considerInertance,sink.displayInertance,sink.displayInstanceName,sink.displayP,sink.displayParameters,sink.displayPressure,sink.inlet.m_flow,sink.inlet.r,sink.inlet.state.T,sink.inlet.state.d,sink.inlet.state.h,sink.inlet.state.p,sink.inlet.state.phase,sink.p0_par,sink.pressureFromInput,sink1.L,sink1.considerInertance,sink1.displayInertance,sink1.displayInstanceName,sink1.displayP,sink1.displayParameters,sink1.displayPressure,sink1.inlet.m_flow,sink1.inlet.r,sink1.inlet.state.T,sink1.inlet.state.d,sink1.inlet.state.h,sink1.inlet.state.p,sink1.inlet.state.phase,sink1.p0_par,sink1.pressureFromInput,source.L,source.T0_par,source.considerInertance,source.displayH,source.displayInertance,source.displayInstanceName,source.displayMassFractions,source.displayP,source.displayParameters,source.displayPressure,source.displayT,source.displayTemperature,source.displayXi,source.enthalpyFromInput,source.h0_par,source.outlet.m_flow,source.outlet.r,source.outlet.state.T,source.outlet.state.d,source.outlet.state.h,source.outlet.state.p,source.outlet.state.phase,source.p0_par,source.pressureFromInput,source.setEnthalpy,source.temperatureFromInput,source.xiFromInput,tanValve.L,tanValve.clip_p_out,tanValve.considerInertance,tanValve.displayInstanceName,tanValve.displayParameters,tanValve.dp,tanValve.dr_corr,tanValve.h_in,tanValve.h_out,tanValve.initM_flow,tanValve.inlet.m_flow,tanValve.inlet.r,tanValve.inlet.state.T,tanValve.inlet.state.d,tanValve.inlet.state.h,tanValve.inlet.state.p,tanValve.inlet.state.phase,tanValve.invertInput,tanValve.m_acceleration_0,tanValve.m_flow,tanValve.m_flowStateSelect,tanValve.m_flow_0,tanValve.m_flow_ref,tanValve.outlet.m_flow,tanValve.outlet.r,tanValve.outlet.state.T,tanValve.outlet.state.d,tanValve.outlet.state.h,tanValve.outlet.state.p,tanValve.outlet.state.phase,tanValve.p_in,tanValve.p_min,tanValve.p_out,tanValve.p_ref,tanValve.relativeLeakiness,tanValve.u,tanValve1.L,tanValve1.clip_p_out,tanValve1.considerInertance,tanValve1.displayInstanceName,tanValve1.displayParameters,tanValve1.dp,tanValve1.dr_corr,tanValve1.h_in,tanValve1.h_out,tanValve1.initM_flow,tanValve1.inlet.m_flow,tanValve1.inlet.r,tanValve1.inlet.state.T,tanValve1.inlet.state.d,tanValve1.inlet.state.h,tanValve1.inlet.state.p,tanValve1.inlet.state.phase,tanValve1.invertInput,tanValve1.m_acceleration_0,tanValve1.m_flow,tanValve1.m_flowStateSelect,tanValve1.m_flow_0,tanValve1.m_flow_ref,tanValve1.outlet.m_flow,tanValve1.outlet.r,tanValve1.outlet.state.T,tanValve1.outlet.state.d,tanValve1.outlet.state.h,tanValve1.outlet.state.p,tanValve1.outlet.state.phase,tanValve1.p_in,tanValve1.p_min,tanValve1.p_out,tanValve1.p_ref,tanValve1.relativeLeakiness,tanValve1.u,tanValve2.L,tanValve2.clip_p_out,tanValve2.considerInertance,tanValve2.displayInstanceName,tanValve2.displayParameters,tanValve2.dp,tanValve2.dr_corr,tanValve2.h_in,tanValve2.h_out,tanValve2.initM_flow,tanValve2.inlet.m_flow,tanValve2.inlet.r,tanValve2.inlet.state.T,tanValve2.inlet.state.d,tanValve2.inlet.state.h,tanValve2.inlet.state.p,tanValve2.inlet.state.phase,tanValve2.invertInput,tanValve2.m_acceleration_0,tanValve2.m_flow,tanValve2.m_flowStateSelect,tanValve2.m_flow_0,tanValve2.m_flow_ref,tanValve2.outlet.m_flow,tanValve2.outlet.r,tanValve2.outlet.state.T,tanValve2.outlet.state.d,tanValve2.outlet.state.h,tanValve2.outlet.state.p,tanValve2.outlet.state.phase,tanValve2.p_in,tanValve2.p_min,tanValve2.p_out,tanValve2.p_ref,tanValve2.relativeLeakiness,tanValve2.u,time
filterSimulationResults("ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_OMSimulator-cs-cvode_res.mat", "/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_OMSimulator-cs-cvode.diff.mat", vars={"source.outlet.m_flow", "pulse1.count", "pulse1.T_start", "pulse.count", "pulse.T_start", "firstOrder3.y", "boilerEspresso.phaseSeparator2_1.U_med", "boilerEspresso.phaseSeparator2_1.M", "PID2.I.y", "PID1.I.y"}, removeDescription=false) [Timeout 660]
"Error: Could not read variable pulse1.count in file ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_OMSimulator-cs-cvode_res.mat.
"
[Timeout remaining time 660]
Failed to write the differing variables of ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_OMSimulator-cs-cvode_res.mat to /var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_OMSimulator-cs-cvode.diff.mat:
""
filterSimulationResults("/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_ref.mat", "/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_OMSimulator-cs-cvode.diff.ref.mat", vars={"source.outlet.m_flow", "pulse1.count", "pulse1.T_start", "pulse.count", "pulse.T_start", "firstOrder3.y", "boilerEspresso.phaseSeparator2_1.U_med", "boilerEspresso.phaseSeparator2_1.M", "PID2.I.y", "PID1.I.y"}, removeDescription=false) [Timeout 660]
""
[Timeout remaining time 660]
(rm -f ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_OMSimulator-cs-euler.pipe ; mkfifo ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_OMSimulator-cs-euler.pipe ; head -c 1048576 < ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_OMSimulator-cs-euler.pipe >> /var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_OMSimulator-cs-euler.sim & (cd run_OMSimulator-cs-euler && /home/hudson/saved_omc/OMSimulator/install/bin/OMSimulator --resultFile=../ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_OMSimulator-cs-euler_res.mat --stripRoot --tempDir=temp_ThermofluidStream_dev_ThermofluidStream_Examples_Utilities_Tests_BoilerEspresso_OMSimulator-cs-euler_fmu --startTime=0 --stopTime=1000 --stepSize=1 --mode=cs --timeout=240 --tolerance=1e-06 ../ThermofluidStream_dev_ThermofluidStream_Examples_Utilities_Tests_BoilerEspresso_OMSimulator-cs-euler.fmu) > ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_OMSimulator-cs-euler.pipe 2>&1) [Timeout 252.0]
OMSimulator-cs-euler timed out simulating the FMU
(rm -f ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy.pipe ; mkfifo ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy.pipe ; head -c 1048576 < ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy.pipe >> /var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy.sim & (cd run_fmpy && python3 -m fmpy simulate --output-file ../ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy_res.csv --output-variables PID1.I.y PID2.I.y boilerEspresso.phaseSeparator2_1.M boilerEspresso.phaseSeparator2_1.U_med firstOrder1.y firstOrder2.y firstOrder3.y pulse.T_start pulse.count pulse1.T_start pulse1.count source.outlet.m_flow tanValve1.inlet.m_flow tanValve2.inlet.m_flow --start-time 0 --stop-time 1000 --timeout 240 --relative-tolerance 1e-06 --interface-type ModelExchange --solver CVode --output-interval 1 ../ThermofluidStream_dev_ThermofluidStream_Examples_Utilities_Tests_BoilerEspresso.fmu) > ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy.pipe 2>&1) [Timeout 252.0]
diffSimulationResults("ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy_res.csv","/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_ref.mat","",relTol=0.003,relTolDiffMinMax=0.003,rangeDelta=0.001) [Timeout 660]
"Error: Could not read variable pulse.T_start in file ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy_res.csv.
Warning: Get data of variable pulse.T_start from file ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy_res.csv failed!
Error: Could not read variable pulse.count in file ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy_res.csv.
Warning: Get data of variable pulse.count from file ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy_res.csv failed!
Error: Could not read variable pulse1.T_start in file ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy_res.csv.
Warning: Get data of variable pulse1.T_start from file ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy_res.csv failed!
Error: Could not read variable pulse1.count in file ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy_res.csv.
Warning: Get data of variable pulse1.count from file ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy_res.csv failed!
"
[Timeout remaining time 660]
""

Variables in the reference:PID1.I.y,PID2.I.y,boilerEspresso.phaseSeparator2_1.M,boilerEspresso.phaseSeparator2_1.U_med,firstOrder1.y,firstOrder2.y,firstOrder3.y,pulse.T_start,pulse.count,pulse1.T_start,pulse1.count,source.outlet.m_flow,tanValve1.inlet.m_flow,tanValve2.inlet.m_flow

Variables in the result:time,PID1.I.y,PID2.I.y,boilerEspresso.phaseSeparator2_1.M,boilerEspresso.phaseSeparator2_1.U_med,firstOrder1.y,firstOrder2.y,firstOrder3.y,source.outlet.m_flow,tanValve1.inlet.m_flow,tanValve2.inlet.m_flow
filterSimulationResults("ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy_res.csv", "/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy.diff.mat", vars={"source.outlet.m_flow", "pulse1.count", "pulse1.T_start", "pulse.count", "pulse.T_start", "firstOrder3.y", "boilerEspresso.phaseSeparator2_1.U_med", "boilerEspresso.phaseSeparator2_1.M", "PID2.I.y", "PID1.I.y"}, removeDescription=false) [Timeout 660]
"Error: Could not read variable pulse1.count in file ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy_res.csv.
"
[Timeout remaining time 660]
Failed to write the differing variables of ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy_res.csv to /var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy.diff.mat:
""
filterSimulationResults("/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_ref.mat", "/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy.diff.ref.mat", vars={"source.outlet.m_flow", "pulse1.count", "pulse1.T_start", "pulse.count", "pulse.T_start", "firstOrder3.y", "boilerEspresso.phaseSeparator2_1.U_med", "boilerEspresso.phaseSeparator2_1.M", "PID2.I.y", "PID1.I.y"}, removeDescription=false) [Timeout 660]
""
[Timeout remaining time 660]
(rm -f ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy-fmi3-cs-cvode.pipe ; mkfifo ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy-fmi3-cs-cvode.pipe ; head -c 1048576 < ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy-fmi3-cs-cvode.pipe >> /var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy-fmi3-cs-cvode.sim & (cd run_fmpy-fmi3-cs-cvode && python3 -m fmpy simulate --output-file ../ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy-fmi3-cs-cvode_res.csv --output-variables PID1.I.y PID2.I.y boilerEspresso.phaseSeparator2_1.M boilerEspresso.phaseSeparator2_1.U_med firstOrder1.y firstOrder2.y firstOrder3.y pulse.T_start pulse.count pulse1.T_start pulse1.count source.outlet.m_flow tanValve1.inlet.m_flow tanValve2.inlet.m_flow --start-time 0 --stop-time 1000 --timeout 240 --relative-tolerance 1e-06 --interface-type CoSimulation --output-interval 1 ../ThermofluidStream_dev_ThermofluidStream_Examples_Utilities_Tests_BoilerEspresso_fmpy-fmi3-cs-cvode.fmu) > ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy-fmi3-cs-cvode.pipe 2>&1) [Timeout 252.0]
diffSimulationResults("ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy-fmi3-cs-cvode_res.csv","/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_ref.mat","",relTol=0.003,relTolDiffMinMax=0.003,rangeDelta=0.001) [Timeout 660]
"Error: Could not read variable pulse.T_start in file ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy-fmi3-cs-cvode_res.csv.
Warning: Get data of variable pulse.T_start from file ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy-fmi3-cs-cvode_res.csv failed!
Error: Could not read variable pulse.count in file ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy-fmi3-cs-cvode_res.csv.
Warning: Get data of variable pulse.count from file ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy-fmi3-cs-cvode_res.csv failed!
Error: Could not read variable pulse1.T_start in file ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy-fmi3-cs-cvode_res.csv.
Warning: Get data of variable pulse1.T_start from file ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy-fmi3-cs-cvode_res.csv failed!
Error: Could not read variable pulse1.count in file ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy-fmi3-cs-cvode_res.csv.
Warning: Get data of variable pulse1.count from file ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy-fmi3-cs-cvode_res.csv failed!
"
[Timeout remaining time 660]
""

Variables in the reference:PID1.I.y,PID2.I.y,boilerEspresso.phaseSeparator2_1.M,boilerEspresso.phaseSeparator2_1.U_med,firstOrder1.y,firstOrder2.y,firstOrder3.y,pulse.T_start,pulse.count,pulse1.T_start,pulse1.count,source.outlet.m_flow,tanValve1.inlet.m_flow,tanValve2.inlet.m_flow

Variables in the result:time,PID1.I.y,PID2.I.y,boilerEspresso.phaseSeparator2_1.M,boilerEspresso.phaseSeparator2_1.U_med,firstOrder1.y,firstOrder2.y,firstOrder3.y,source.outlet.m_flow,tanValve1.inlet.m_flow,tanValve2.inlet.m_flow
filterSimulationResults("ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy-fmi3-cs-cvode_res.csv", "/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy-fmi3-cs-cvode.diff.mat", vars={"source.outlet.m_flow", "pulse1.count", "pulse1.T_start", "pulse.count", "pulse.T_start", "firstOrder3.y", "boilerEspresso.phaseSeparator2_1.U_med", "boilerEspresso.phaseSeparator2_1.M", "PID2.I.y", "PID1.I.y"}, removeDescription=false) [Timeout 660]
"Error: Could not read variable pulse1.count in file ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy-fmi3-cs-cvode_res.csv.
"
[Timeout remaining time 660]
Failed to write the differing variables of ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy-fmi3-cs-cvode_res.csv to /var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy-fmi3-cs-cvode.diff.mat:
""
filterSimulationResults("/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_ref.mat", "/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Examples.Utilities.Tests.BoilerEspresso_fmpy-fmi3-cs-cvode.diff.ref.mat", vars={"source.outlet.m_flow", "pulse1.count", "pulse1.T_start", "pulse.count", "pulse.T_start", "firstOrder3.y", "boilerEspresso.phaseSeparator2_1.U_med", "boilerEspresso.phaseSeparator2_1.M", "PID2.I.y", "PID1.I.y"}, removeDescription=false) [Timeout 660]
""
[Timeout remaining time 660]
[Calling sys.exit(0), Time elapsed: 9.227524439804256]