Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ClaRa_dev_ClaRa.Examples.SteamCycle_01.conf.json loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/SMArtInt main/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/SMArtInt main/package.mo): time 0.0115/0.0115, allocations: 1.784 MB / 21.64 MB, free: 2.82 MB / 18.57 MB " [Timeout remaining time 180] 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 0.001069/0.001069, allocations: 87.41 kB / 25.48 MB, free: 6.422 MB / 18.57 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 0.001738/0.001738, allocations: 167.5 kB / 28.89 MB, free: 3.387 MB / 18.57 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 0.9885/0.9885, allocations: 177.2 MB / 209.3 MB, free: 2.234 MB / 186.7 MB " [Timeout remaining time 179] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa main/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa main/package.mo): time 0.7154/0.7154, allocations: 102.4 MB / 368.3 MB, free: 0.7734 MB / 330.8 MB " [Timeout remaining time 179] Using package ClaRa with version 1.9.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 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) Using package SMArtInt with version 1.0.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/SMArtInt main/package.mo) Running command: translateModel(ClaRa.Examples.SteamCycle_01,tolerance=1e-05,outputFormat="mat",numberOfIntervals=5032,variableFilter="PID_NDVW3.I.y|PID_NDVW3.resetValueI|PID_NDVW3.resetValueID|PID_NDVW3.resetValueP|PID_NDVW3.smoothPIDInput.y_aux|PID_NDVW3.smoothPIDOutput.y_aux|PID_NDVW3.smoothPIDOutput1.y_aux|PID_preheaterLP3.I.y|PID_preheaterLP3.resetValueI|PID_preheaterLP3.resetValueID|PID_preheaterLP3.resetValueP|PID_preheaterLP3.smoothPIDInput.y_aux|PID_preheaterLP3.smoothPIDOutput.y_aux|PID_preheaterLP3.smoothPIDOutput1.y_aux|PID_preheaterLP4.I.y|PID_preheaterLP4.resetValueI|PID_preheaterLP4.resetValueID|PID_preheaterLP4.resetValueP|PID_preheaterLP4.smoothPIDInput.y_aux|PID_preheaterLP4.smoothPIDOutput.y_aux|PID_preheaterLP4.smoothPIDOutput1.y_aux|PI_Pump_cond.I.y|PI_Pump_cond.resetValueI|PI_Pump_cond.resetValueID|PI_Pump_cond.resetValueP|PI_Pump_cond.smoothPIDInput.y_aux|PI_Pump_cond.smoothPIDOutput.y_aux|PI_Pump_cond.smoothPIDOutput1.y_aux|PI_preheater1.I.y|PI_preheater1.resetValueI|PI_preheater1.resetValueID|PI_preheater1.resetValueP|PI_preheater1.smoothPIDInput.y_aux|PI_preheater1.smoothPIDOutput.y_aux|PI_preheater1.smoothPIDOutput1.y_aux|PI_valveControl_preheater_HP.I.y|PI_valveControl_preheater_HP.resetValueI|PI_valveControl_preheater_HP.resetValueID|PI_valveControl_preheater_HP.resetValueP|PI_valveControl_preheater_HP.smoothPIDInput.y_aux|PI_valveControl_preheater_HP.smoothPIDOutput.y_aux|PI_valveControl_preheater_HP.smoothPIDOutput1.y_aux|Time|condenser.shell.h_liq|condenser.shell.h_vap|condenser.shell.p_vap|condenser.shell.volume_vap|condenser.tubes.h|condenser.tubes.p|condenser.wall.U.[0-9,]+.|downComer_feedWaterTank.h.[0-9,]+.|downComer_feedWaterTank.p.[0-9,]+.|feedWaterTank.volume.h_liq|feedWaterTank.volume.h_vap|feedWaterTank.volume.p_vap|feedWaterTank.volume.volume_vap|feedWaterTank.wall.U.[0-9,]+.|inertia.phi|join_HP.h|join_HP.p|join_IP3.h|join_IP3.p|join_LP1.h|join_LP1.p|join_LP2.h|join_LP2.p|join_LP_main.h|join_LP_main.p|join_preheater_LP3.h|join_preheater_LP3.p|measurement.y|preheater_HP.shell.h_liq|preheater_HP.shell.h_vap|preheater_HP.shell.p_vap|preheater_HP.shell.volume_vap|preheater_HP.tubes.h|preheater_HP.tubes.p|preheater_HP.wall.U.[0-9,]+.|preheater_LP1.shell.h_liq|preheater_LP1.shell.h_vap|preheater_LP1.shell.p_vap|preheater_LP1.shell.volume_vap|preheater_LP1.tubes.h|preheater_LP1.tubes.p|preheater_LP1.wall.U.[0-9,]+.|preheater_LP2.shell.h_liq|preheater_LP2.shell.h_vap|preheater_LP2.shell.p_vap|preheater_LP2.shell.volume_vap|preheater_LP2.tubes.h|preheater_LP2.tubes.p|preheater_LP2.wall.U.[0-9,]+.|preheater_LP3.shell.h_liq|preheater_LP3.shell.h_vap|preheater_LP3.shell.p_vap|preheater_LP3.shell.volume_vap|preheater_LP3.tubes.h|preheater_LP3.tubes.p|preheater_LP3.wall.U.[0-9,]+.|preheater_LP4.shell.h_liq|preheater_LP4.shell.h_vap|preheater_LP4.shell.p_vap|preheater_LP4.shell.volume_vap|preheater_LP4.tubes.h|preheater_LP4.tubes.p|preheater_LP4.wall.U.[0-9,]+.|split_IP2.h|split_IP2.p|split_LP3.h|split_LP3.p|steamGenerator.h_HP|steamGenerator.h_IP|steamGenerator.heatRelease.x_scaled.[0-9,]+.|steamGenerator.p_HP|steamGenerator.p_IP",fileNamePrefix="ClaRa_dev_ClaRa.Examples.SteamCycle_01") translateModel(ClaRa.Examples.SteamCycle_01,tolerance=1e-05,outputFormat="mat",numberOfIntervals=5032,variableFilter="PID_NDVW3.I.y|PID_NDVW3.resetValueI|PID_NDVW3.resetValueID|PID_NDVW3.resetValueP|PID_NDVW3.smoothPIDInput.y_aux|PID_NDVW3.smoothPIDOutput.y_aux|PID_NDVW3.smoothPIDOutput1.y_aux|PID_preheaterLP3.I.y|PID_preheaterLP3.resetValueI|PID_preheaterLP3.resetValueID|PID_preheaterLP3.resetValueP|PID_preheaterLP3.smoothPIDInput.y_aux|PID_preheaterLP3.smoothPIDOutput.y_aux|PID_preheaterLP3.smoothPIDOutput1.y_aux|PID_preheaterLP4.I.y|PID_preheaterLP4.resetValueI|PID_preheaterLP4.resetValueID|PID_preheaterLP4.resetValueP|PID_preheaterLP4.smoothPIDInput.y_aux|PID_preheaterLP4.smoothPIDOutput.y_aux|PID_preheaterLP4.smoothPIDOutput1.y_aux|PI_Pump_cond.I.y|PI_Pump_cond.resetValueI|PI_Pump_cond.resetValueID|PI_Pump_cond.resetValueP|PI_Pump_cond.smoothPIDInput.y_aux|PI_Pump_cond.smoothPIDOutput.y_aux|PI_Pump_cond.smoothPIDOutput1.y_aux|PI_preheater1.I.y|PI_preheater1.resetValueI|PI_preheater1.resetValueID|PI_preheater1.resetValueP|PI_preheater1.smoothPIDInput.y_aux|PI_preheater1.smoothPIDOutput.y_aux|PI_preheater1.smoothPIDOutput1.y_aux|PI_valveControl_preheater_HP.I.y|PI_valveControl_preheater_HP.resetValueI|PI_valveControl_preheater_HP.resetValueID|PI_valveControl_preheater_HP.resetValueP|PI_valveControl_preheater_HP.smoothPIDInput.y_aux|PI_valveControl_preheater_HP.smoothPIDOutput.y_aux|PI_valveControl_preheater_HP.smoothPIDOutput1.y_aux|Time|condenser.shell.h_liq|condenser.shell.h_vap|condenser.shell.p_vap|condenser.shell.volume_vap|condenser.tubes.h|condenser.tubes.p|condenser.wall.U.[0-9,]+.|downComer_feedWaterTank.h.[0-9,]+.|downComer_feedWaterTank.p.[0-9,]+.|feedWaterTank.volume.h_liq|feedWaterTank.volume.h_vap|feedWaterTank.volume.p_vap|feedWaterTank.volume.volume_vap|feedWaterTank.wall.U.[0-9,]+.|inertia.phi|join_HP.h|join_HP.p|join_IP3.h|join_IP3.p|join_LP1.h|join_LP1.p|join_LP2.h|join_LP2.p|join_LP_main.h|join_LP_main.p|join_preheater_LP3.h|join_preheater_LP3.p|measurement.y|preheater_HP.shell.h_liq|preheater_HP.shell.h_vap|preheater_HP.shell.p_vap|preheater_HP.shell.volume_vap|preheater_HP.tubes.h|preheater_HP.tubes.p|preheater_HP.wall.U.[0-9,]+.|preheater_LP1.shell.h_liq|preheater_LP1.shell.h_vap|preheater_LP1.shell.p_vap|preheater_LP1.shell.volume_vap|preheater_LP1.tubes.h|preheater_LP1.tubes.p|preheater_LP1.wall.U.[0-9,]+.|preheater_LP2.shell.h_liq|preheater_LP2.shell.h_vap|preheater_LP2.shell.p_vap|preheater_LP2.shell.volume_vap|preheater_LP2.tubes.h|preheater_LP2.tubes.p|preheater_LP2.wall.U.[0-9,]+.|preheater_LP3.shell.h_liq|preheater_LP3.shell.h_vap|preheater_LP3.shell.p_vap|preheater_LP3.shell.volume_vap|preheater_LP3.tubes.h|preheater_LP3.tubes.p|preheater_LP3.wall.U.[0-9,]+.|preheater_LP4.shell.h_liq|preheater_LP4.shell.h_vap|preheater_LP4.shell.p_vap|preheater_LP4.shell.volume_vap|preheater_LP4.tubes.h|preheater_LP4.tubes.p|preheater_LP4.wall.U.[0-9,]+.|split_IP2.h|split_IP2.p|split_LP3.h|split_LP3.p|steamGenerator.h_HP|steamGenerator.h_IP|steamGenerator.heatRelease.x_scaled.[0-9,]+.|steamGenerator.p_HP|steamGenerator.p_IP",fileNamePrefix="ClaRa_dev_ClaRa.Examples.SteamCycle_01") [Timeout 800] "Notification: Performance of FrontEnd - loaded program: time 1.193e-06/1.193e-06, allocations: 0 / 415.1 MB, free: 2.207 MB / 378.8 MB Notification: Performance of FrontEnd - Absyn->SCode: time 1.742e-05/1.862e-05, allocations: 6.312 kB / 415.1 MB, free: 2.199 MB / 378.8 MB Notification: TILMedia requested package Modelica of version 4.0.0. Modelica 4.1.0 is used instead which states that it is fully compatible without conversion script needed. Notification: Automatically loaded package TILMedia 1.9.0 ClaRa due to usage. Notification: Performance of NFInst.instantiate(ClaRa.Examples.SteamCycle_01): time 0.4521/0.4521, allocations: 287.2 MB / 0.6858 GB, free: 8.656 MB / 0.573 GB Notification: Performance of NFInst.instExpressions: time 0.4466/0.8987, allocations: 107 MB / 0.7903 GB, free: 3.996 MB / 0.6355 GB Notification: Performance of NFInst.updateImplicitVariability: time 0.04872/0.9474, allocations: 1.4 MB / 0.7917 GB, free: 3.996 MB / 0.6355 GB [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa main/StaticCycles/Triple.mo:33:3-33:182:writable] Warning: Connector steamSignal is not balanced: The number of potential variables (3) is not equal to the number of flow variables (0). [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa main/Basics/Interfaces/CycleSumModel.mo:3:3-3:52:writable] Warning: Connector cycleSumPort is not balanced: The number of potential variables (0) is not equal to the number of flow variables (4). [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa main/StaticCycles/Triple.mo:33:3-33:182:writable] Warning: Connector steamSignal is not balanced: The number of potential variables (3) is not equal to the number of flow variables (0). [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa main/Basics/Interfaces/CycleSumModel.mo:3:3-3:52:writable] Warning: Connector cycleSumPort is not balanced: The number of potential variables (0) is not equal to the number of flow variables (4). Notification: Performance of NFTyping.typeComponents: time 0.053/1, allocations: 25.22 MB / 0.8163 GB, free: 3.375 MB / 0.6355 GB Notification: Performance of NFTyping.typeBindings: time 0.1056/1.106, allocations: 43.38 MB / 0.8587 GB, free: 4.449 MB / 0.6512 GB Notification: Performance of NFTyping.typeClassSections: time 0.06866/1.175, allocations: 36.33 MB / 0.8941 GB, free: 11.83 MB / 0.6824 GB Notification: Performance of NFFlatten.flatten: time 0.1431/1.318, allocations: 127.8 MB / 1.019 GB, free: 10.31 MB / 0.7918 GB Notification: Performance of NFFlatten.resolveConnections: time 0.7349/2.053, allocations: 46.8 MB / 1.065 GB, free: 16.64 MB / 0.8075 GB Notification: Performance of NFEvalConstants.evaluate: time 0.253/2.306, allocations: 122.8 MB / 1.185 GB, free: 4.141 MB / 0.8232 GB Notification: Performance of NFSimplifyModel.simplify: time 0.07313/2.379, allocations: 41.27 MB / 1.225 GB, free: 4.121 MB / 0.8232 GB Notification: Performance of NFPackage.collectConstants: time 0.03001/2.409, allocations: 8.294 MB / 1.233 GB, free: 3.945 MB / 0.8232 GB Notification: Performance of NFFlatten.collectFunctions: time 0.06161/2.471, allocations: 16.33 MB / 1.249 GB, free: 5.918 MB / 0.8388 GB Notification: Performance of NFScalarize.scalarize: time 0.04499/2.516, allocations: 27.54 MB / 1.276 GB, free: 13.97 MB / 0.8544 GB Notification: Performance of NFVerifyModel.verify: time 0.07645/2.592, allocations: 28.22 MB / 1.303 GB, free: 9.578 MB / 0.87 GB Notification: Performance of NFConvertDAE.convert: time 0.1396/2.732, allocations: 73.24 MB / 1.375 GB, free: 6.652 MB / 0.9325 GB Notification: Performance of FrontEnd - DAE generated: time 5.581e-06/2.732, allocations: 0 / 1.375 GB, free: 6.652 MB / 0.9325 GB Notification: Performance of FrontEnd: time 1.573e-06/2.732, allocations: 0 / 1.375 GB, free: 6.652 MB / 0.9325 GB Notification: Performance of Transformations before backend: time 0.00344/2.735, allocations: 0 / 1.375 GB, free: 6.652 MB / 0.9325 GB Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 14182 * Number of variables: 14182 Notification: Performance of Generate backend data structure: time 0.7358/3.471, allocations: 83.32 MB / 1.456 GB, free: 195.9 MB / 0.9328 GB Notification: Performance of prepare preOptimizeDAE: time 3.592e-05/3.471, allocations: 10.53 kB / 1.456 GB, free: 195.9 MB / 0.9328 GB Notification: Performance of preOpt normalInlineFunction (simulation): time 0.0301/3.501, allocations: 9.141 MB / 1.465 GB, free: 195.9 MB / 0.9328 GB Notification: Performance of preOpt evaluateParameters (simulation): time 0.0934/3.594, allocations: 42.78 MB / 1.507 GB, free: 178.9 MB / 0.9328 GB Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.002983/3.597, allocations: 3.169 MB / 1.51 GB, free: 177 MB / 0.9328 GB Notification: Performance of preOpt expandDerOperator (simulation): time 0.01111/3.608, allocations: 4.585 MB / 1.515 GB, free: 173.9 MB / 0.9328 GB Notification: Performance of preOpt clockPartitioning (simulation): time 0.1151/3.724, allocations: 101.6 MB / 1.614 GB, free: 71.78 MB / 0.9328 GB Notification: Performance of preOpt findStateOrder (simulation): time 0.001481/3.725, allocations: 466.1 kB / 1.614 GB, free: 71.59 MB / 0.9328 GB Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.008215/3.733, allocations: 2.043 MB / 1.616 GB, free: 70.86 MB / 0.9328 GB Notification: Performance of preOpt inlineArrayEqn (simulation): time 0.002326/3.736, allocations: 2.956 MB / 1.619 GB, free: 68.21 MB / 0.9328 GB Notification: Performance of preOpt removeEqualRHS (simulation): time 0.07672/3.812, allocations: 34.24 MB / 1.653 GB, free: 37.88 MB / 0.9328 GB 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 0.698/4.51, allocations: 342.1 MB / 1.987 GB, free: 29.43 MB / 1.058 GB Notification: Performance of preOpt comSubExp (simulation): time 0.06713/4.577, allocations: 44.8 MB / 2.03 GB, free: 14.92 MB / 1.058 GB Notification: Performance of preOpt resolveLoops (simulation): time 0.02276/4.6, allocations: 11.11 MB / 2.041 GB, free: 10.7 MB / 1.058 GB Notification: Performance of preOpt evalFunc (simulation): time 0.005704/4.606, allocations: 1.907 MB / 2.043 GB, free: 10.58 MB / 1.058 GB Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 0.4518/5.058, allocations: 45.47 MB / 2.088 GB, free: 278.5 MB / 1.058 GB Notification: Performance of preOpt simplifyInStream (simulation): time 0.03088/5.089, allocations: 5.862 MB / 2.093 GB, free: 278.5 MB / 1.058 GB Notification: Performance of pre-optimization done (n=7067): time 0.0002054/5.089, allocations: 0 / 2.093 GB, free: 278.5 MB / 1.058 GB Notification: Performance of matching and sorting (n=7074): time 0.2841/5.373, allocations: 96.15 MB / 2.187 GB, free: 235 MB / 1.058 GB Notification: Performance of inlineWhenForInitialization (initialization): time 0.004782/5.378, allocations: 36.5 MB / 2.223 GB, free: 190.3 MB / 1.058 GB Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.08744/5.465, allocations: 51.96 MB / 2.274 GB, free: 152.9 MB / 1.058 GB Notification: Performance of collectPreVariables (initialization): time 0.007679/5.473, allocations: 0.848 MB / 2.274 GB, free: 152.6 MB / 1.058 GB Notification: Performance of collectInitialEqns (initialization): time 0.01968/5.492, allocations: 20.13 MB / 2.294 GB, free: 138.2 MB / 1.058 GB Notification: Performance of collectInitialBindings (initialization): time 0.02017/5.513, allocations: 25.2 MB / 2.319 GB, free: 116.5 MB / 1.058 GB Notification: Performance of simplifyInitialFunctions (initialization): time 0.03254/5.545, allocations: 16.43 MB / 2.335 GB, free: 106.5 MB / 1.058 GB Notification: Performance of setup shared object (initialization): time 2.911e-05/5.545, allocations: 305.1 kB / 2.335 GB, free: 106.2 MB / 1.058 GB Notification: Performance of preBalanceInitialSystem (initialization): time 0.03208/5.577, allocations: 15.91 MB / 2.35 GB, free: 93.96 MB / 1.058 GB Notification: Performance of partitionIndependentBlocks (initialization): time 0.0386/5.616, allocations: 53.25 MB / 2.402 GB, free: 31.38 MB / 1.058 GB [/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelica/OMCompiler/Compiler/BackEnd/BackendEquation.mo:2571:7-2571:76:writable] Error: Internal error function solveEquation failed Error: Initialization problem is structural singular. Please, check the initial conditions. Notification: Performance of analyzeInitialSystem (initialization): time 0.4975/6.113, allocations: 65.54 MB / 2.466 GB, free: 239.4 MB / 1.058 GB Notification: Performance of solveInitialSystemEqSystem (initialization): time 0.000739/6.114, allocations: 162.1 kB / 2.467 GB, free: 239.4 MB / 1.058 GB Notification: Performance of matching and sorting (n=11691) (initialization): time 0.1278/6.242, allocations: 49.55 MB / 2.515 GB, free: 234.6 MB / 1.058 GB Notification: Performance of prepare postOptimizeDAE: time 0.0004359/6.242, allocations: 279.7 kB / 2.515 GB, free: 234.3 MB / 1.058 GB Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.003394/6.246, allocations: 1.974 MB / 2.517 GB, free: 232.8 MB / 1.058 GB Notification: Performance of postOpt tearingSystem (initialization): time 0.1629/6.409, allocations: 34.82 MB / 2.551 GB, free: 208.9 MB / 1.058 GB Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.03397/6.443, allocations: 12.83 MB / 2.564 GB, free: 199.1 MB / 1.058 GB Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.04509/6.488, allocations: 83.31 MB / 2.645 GB, free: 119.3 MB / 1.058 GB Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.04535/6.533, allocations: 2.339 MB / 2.647 GB, free: 118.2 MB / 1.058 GB Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.009563/6.543, allocations: 2.558 MB / 2.65 GB, free: 116.5 MB / 1.058 GB Warning: Assuming fixed start value for the following 66 variables: inertia.phi:VARIABLE(start = 0.0 unit = \"rad\" fixed = true ) \"Absolute rotation angle of component\" type: Real steamGenerator.h_IP:VARIABLE(start = steamGenerator.h_RH_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy before IP injector\" type: Real steamGenerator.p_IP:VARIABLE(min = 0.0 start = steamGenerator.p_RH_start unit = \"Pa\" fixed = true nominal = 1e5 ) \"Pressure at hot reheat outlet\" type: Real steamGenerator.h_HP:VARIABLE(start = steamGenerator.h_LS_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy before HP injector\" type: Real steamGenerator.p_HP:VARIABLE(min = 0.0 start = steamGenerator.p_LS_start unit = \"Pa\" fixed = true nominal = 1e5 ) \"Live steam pressure\" type: Real condenser.tubes.h:VARIABLE(start = condenser.tubes.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 protected = true ) \"spec. enthalpy state\" type: Real condenser.tubes.p:VARIABLE(min = 0.0 start = condenser.tubes.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real condenser.shell.h_liq:VARIABLE(start = condenser.shell.h_liq_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of liquid phase\" type: Real condenser.shell.h_vap:VARIABLE(start = condenser.shell.h_vap_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of vapour phase\" type: Real condenser.shell.p_vap:VARIABLE(min = 0.0 start = condenser.shell.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"Vapour pressure\" type: Real feedWaterTank.volume.h_liq:VARIABLE(start = feedWaterTank.volume.h_liq_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of liquid phase\" type: Real feedWaterTank.volume.h_vap:VARIABLE(start = feedWaterTank.volume.h_vap_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of vapour phase\" type: Real feedWaterTank.volume.p_vap:VARIABLE(min = 0.0 start = feedWaterTank.volume.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"Vapour pressure\" type: Real join_LP1.h:VARIABLE(start = join_LP1.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real join_LP1.p:VARIABLE(min = 0.0 start = join_LP1.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real join_HP.h:VARIABLE(start = join_HP.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real join_HP.p:VARIABLE(min = 0.0 start = Turbine_HP1.p_out_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real preheater_HP.tubes.h:VARIABLE(start = preheater_HP.tubes.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 protected = true ) \"spec. enthalpy state\" type: Real preheater_HP.tubes.p:VARIABLE(min = 0.0 start = preheater_HP.tubes.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real preheater_HP.shell.h_liq:VARIABLE(start = preheater_HP.shell.h_liq_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of liquid phase\" type: Real preheater_HP.shell.h_vap:VARIABLE(start = preheater_HP.shell.h_vap_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of vapour phase\" type: Real preheater_HP.shell.p_vap:VARIABLE(min = 0.0 start = preheater_HP.shell.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"Vapour pressure\" type: Real preheater_LP1.tubes.h:VARIABLE(start = preheater_LP1.tubes.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 protected = true ) \"spec. enthalpy state\" type: Real preheater_LP1.tubes.p:VARIABLE(min = 0.0 start = preheater_LP1.tubes.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real preheater_LP1.shell.h_liq:VARIABLE(start = preheater_LP1.shell.h_liq_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of liquid phase\" type: Real preheater_LP1.shell.h_vap:VARIABLE(start = preheater_LP1.shell.h_vap_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of vapour phase\" type: Real preheater_LP1.shell.p_vap:VARIABLE(min = 0.0 start = preheater_LP1.shell.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"Vapour pressure\" type: Real join_LP_main.h:VARIABLE(start = join_LP_main.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real join_LP_main.p:VARIABLE(min = 0.0 start = join_LP_main.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real split_IP2.h:VARIABLE(start = split_IP2.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real split_IP2.p:VARIABLE(min = 0.0 start = split_IP2.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real join_IP3.h:VARIABLE(start = join_IP3.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real join_IP3.p:VARIABLE(min = 0.0 start = join_IP3.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real join_LP2.h:VARIABLE(start = join_LP2.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real join_LP2.p:VARIABLE(min = 0.0 start = join_LP2.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real split_LP3.h:VARIABLE(start = split_LP3.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real split_LP3.p:VARIABLE(min = 0.0 start = split_LP3.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real preheater_LP2.tubes.h:VARIABLE(start = preheater_LP2.tubes.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 protected = true ) \"spec. enthalpy state\" type: Real preheater_LP2.tubes.p:VARIABLE(min = 0.0 start = preheater_LP2.tubes.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real preheater_LP2.shell.h_liq:VARIABLE(start = preheater_LP2.shell.h_liq_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of liquid phase\" type: Real preheater_LP2.shell.h_vap:VARIABLE(start = preheater_LP2.shell.h_vap_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of vapour phase\" type: Real preheater_LP2.shell.p_vap:VARIABLE(min = 0.0 start = preheater_LP2.shell.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"Vapour pressure\" type: Real preheater_LP3.tubes.h:VARIABLE(start = preheater_LP3.tubes.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 protected = true ) \"spec. enthalpy state\" type: Real preheater_LP3.tubes.p:VARIABLE(min = 0.0 start = preheater_LP3.tubes.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real preheater_LP3.shell.h_liq:VARIABLE(start = preheater_LP3.shell.h_liq_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of liquid phase\" type: Real preheater_LP3.shell.h_vap:VARIABLE(start = preheater_LP3.shell.h_vap_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of vapour phase\" type: Real preheater_LP3.shell.p_vap:VARIABLE(min = 0.0 start = preheater_LP3.shell.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"Vapour pressure\" type: Real preheater_LP4.tubes.h:VARIABLE(start = preheater_LP4.tubes.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 protected = true ) \"spec. enthalpy state\" type: Real preheater_LP4.tubes.p:VARIABLE(min = 0.0 start = preheater_LP4.tubes.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real preheater_LP4.shell.h_liq:VARIABLE(start = preheater_LP4.shell.h_liq_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of liquid phase\" type: Real preheater_LP4.shell.h_vap:VARIABLE(start = preheater_LP4.shell.h_vap_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of vapour phase\" type: Real preheater_LP4.shell.p_vap:VARIABLE(min = 0.0 start = preheater_LP4.shell.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"Vapour pressure\" type: Real join_preheater_LP3.h:VARIABLE(start = join_preheater_LP3.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real join_preheater_LP3.p:VARIABLE(min = 0.0 start = join_preheater_LP3.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real downComer_feedWaterTank.h[1]:VARIABLE(start = downComer_feedWaterTank.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [3] downComer_feedWaterTank.h[2]:VARIABLE(start = downComer_feedWaterTank.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [3] downComer_feedWaterTank.h[3]:VARIABLE(start = downComer_feedWaterTank.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [3] downComer_feedWaterTank.p[1]:VARIABLE(min = 0.0 start = downComer_feedWaterTank.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [3] downComer_feedWaterTank.p[2]:VARIABLE(min = 0.0 start = downComer_feedWaterTank.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [3] downComer_feedWaterTank.p[3]:VARIABLE(min = 0.0 start = downComer_feedWaterTank.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [3] PID_NDVW3.switch_OnOff.u2:DISCRETE(flow=false fixed = true ) \"Connector of Boolean input signal\" type: Boolean PID_preheaterLP3.switch_OnOff.u2:DISCRETE(flow=false fixed = true ) \"Connector of Boolean input signal\" type: Boolean PID_preheaterLP4.switch_OnOff.u2:DISCRETE(flow=false fixed = true ) \"Connector of Boolean input signal\" type: Boolean PI_preheater1.switch_OnOff.u2:DISCRETE(flow=false fixed = true ) \"Connector of Boolean input signal\" type: Boolean PI_valveControl_preheater_HP.switch_OnOff.u2:DISCRETE(flow=false fixed = true ) \"Connector of Boolean input signal\" type: Boolean PI_Pump_cond.switch_OnOff.u2:DISCRETE(flow=false fixed = true ) \"Connector of Boolean input signal\" type: Boolean Warning: The initial conditions are over specified. The following 1 initial equations are redundant, so they are removed from the initialization system: steamGenerator.heatRelease.y = steamGenerator.QF_setl_. Notification: Performance of preBalanceInitialSystem (initialization_lambda0): time 0.05194/6.594, allocations: 17.17 MB / 2.667 GB, free: 104.5 MB / 1.058 GB Notification: Performance of partitionIndependentBlocks (initialization_lambda0): time 0.04241/6.637, allocations: 52.97 MB / 2.718 GB, free: 42.12 MB / 1.058 GB [/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelica/OMCompiler/Compiler/BackEnd/BackendEquation.mo:2571:7-2571:76:writable] Error: Internal error function solveEquation failed Error: Initialization problem is structural singular. Please, check the initial conditions. Notification: Performance of analyzeInitialSystem (initialization_lambda0): time 0.5391/7.176, allocations: 64.63 MB / 2.782 GB, free: 204.8 MB / 1.073 GB Notification: Performance of solveInitialSystemEqSystem (initialization_lambda0): time 0.0008145/7.177, allocations: 162.6 kB / 2.782 GB, free: 204.8 MB / 1.073 GB Notification: Performance of matching and sorting (n=11691) (initialization_lambda0): time 0.1302/7.307, allocations: 48.91 MB / 2.829 GB, free: 202.6 MB / 1.073 GB Notification: Performance of prepare postOptimizeDAE: time 0.000529/7.308, allocations: 282.1 kB / 2.83 GB, free: 202.5 MB / 1.073 GB Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.003425/7.311, allocations: 1.982 MB / 2.832 GB, free: 202.5 MB / 1.073 GB Notification: Performance of postOpt tearingSystem (initialization): time 0.1364/7.447, allocations: 28.23 MB / 2.859 GB, free: 200.7 MB / 1.073 GB Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.03061/7.478, allocations: 12.83 MB / 2.872 GB, free: 200.7 MB / 1.073 GB Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.03872/7.517, allocations: 85.34 MB / 2.955 GB, free: 127.4 MB / 1.073 GB Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.04218/7.559, allocations: 2.476 MB / 2.957 GB, free: 127.4 MB / 1.073 GB Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.00961/7.568, allocations: 2.529 MB / 2.96 GB, free: 127.4 MB / 1.073 GB Warning: Assuming fixed start value for the following 66 variables: inertia.phi:VARIABLE(start = 0.0 unit = \"rad\" fixed = true ) \"Absolute rotation angle of component\" type: Real steamGenerator.h_IP:VARIABLE(start = steamGenerator.h_RH_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy before IP injector\" type: Real steamGenerator.p_IP:VARIABLE(min = 0.0 start = steamGenerator.p_RH_start unit = \"Pa\" fixed = true nominal = 1e5 ) \"Pressure at hot reheat outlet\" type: Real steamGenerator.h_HP:VARIABLE(start = steamGenerator.h_LS_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy before HP injector\" type: Real steamGenerator.p_HP:VARIABLE(min = 0.0 start = steamGenerator.p_LS_start unit = \"Pa\" fixed = true nominal = 1e5 ) \"Live steam pressure\" type: Real condenser.tubes.h:VARIABLE(start = condenser.tubes.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 protected = true ) \"spec. enthalpy state\" type: Real condenser.tubes.p:VARIABLE(min = 0.0 start = condenser.tubes.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real condenser.shell.h_liq:VARIABLE(start = condenser.shell.h_liq_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of liquid phase\" type: Real condenser.shell.h_vap:VARIABLE(start = condenser.shell.h_vap_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of vapour phase\" type: Real condenser.shell.p_vap:VARIABLE(min = 0.0 start = condenser.shell.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"Vapour pressure\" type: Real feedWaterTank.volume.h_liq:VARIABLE(start = feedWaterTank.volume.h_liq_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of liquid phase\" type: Real feedWaterTank.volume.h_vap:VARIABLE(start = feedWaterTank.volume.h_vap_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of vapour phase\" type: Real feedWaterTank.volume.p_vap:VARIABLE(min = 0.0 start = feedWaterTank.volume.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"Vapour pressure\" type: Real join_LP1.h:VARIABLE(start = join_LP1.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real join_LP1.p:VARIABLE(min = 0.0 start = join_LP1.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real join_HP.h:VARIABLE(start = join_HP.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real join_HP.p:VARIABLE(min = 0.0 start = Turbine_HP1.p_out_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real preheater_HP.tubes.h:VARIABLE(start = preheater_HP.tubes.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 protected = true ) \"spec. enthalpy state\" type: Real preheater_HP.tubes.p:VARIABLE(min = 0.0 start = preheater_HP.tubes.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real preheater_HP.shell.h_liq:VARIABLE(start = preheater_HP.shell.h_liq_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of liquid phase\" type: Real preheater_HP.shell.h_vap:VARIABLE(start = preheater_HP.shell.h_vap_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of vapour phase\" type: Real preheater_HP.shell.p_vap:VARIABLE(min = 0.0 start = preheater_HP.shell.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"Vapour pressure\" type: Real preheater_LP1.tubes.h:VARIABLE(start = preheater_LP1.tubes.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 protected = true ) \"spec. enthalpy state\" type: Real preheater_LP1.tubes.p:VARIABLE(min = 0.0 start = preheater_LP1.tubes.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real preheater_LP1.shell.h_liq:VARIABLE(start = preheater_LP1.shell.h_liq_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of liquid phase\" type: Real preheater_LP1.shell.h_vap:VARIABLE(start = preheater_LP1.shell.h_vap_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of vapour phase\" type: Real preheater_LP1.shell.p_vap:VARIABLE(min = 0.0 start = preheater_LP1.shell.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"Vapour pressure\" type: Real join_LP_main.h:VARIABLE(start = join_LP_main.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real join_LP_main.p:VARIABLE(min = 0.0 start = join_LP_main.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real split_IP2.h:VARIABLE(start = split_IP2.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real split_IP2.p:VARIABLE(min = 0.0 start = split_IP2.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real join_IP3.h:VARIABLE(start = join_IP3.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real join_IP3.p:VARIABLE(min = 0.0 start = join_IP3.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real join_LP2.h:VARIABLE(start = join_LP2.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real join_LP2.p:VARIABLE(min = 0.0 start = join_LP2.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real split_LP3.h:VARIABLE(start = split_LP3.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real split_LP3.p:VARIABLE(min = 0.0 start = split_LP3.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real preheater_LP2.tubes.h:VARIABLE(start = preheater_LP2.tubes.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 protected = true ) \"spec. enthalpy state\" type: Real preheater_LP2.tubes.p:VARIABLE(min = 0.0 start = preheater_LP2.tubes.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real preheater_LP2.shell.h_liq:VARIABLE(start = preheater_LP2.shell.h_liq_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of liquid phase\" type: Real preheater_LP2.shell.h_vap:VARIABLE(start = preheater_LP2.shell.h_vap_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of vapour phase\" type: Real preheater_LP2.shell.p_vap:VARIABLE(min = 0.0 start = preheater_LP2.shell.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"Vapour pressure\" type: Real preheater_LP3.tubes.h:VARIABLE(start = preheater_LP3.tubes.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 protected = true ) \"spec. enthalpy state\" type: Real preheater_LP3.tubes.p:VARIABLE(min = 0.0 start = preheater_LP3.tubes.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real preheater_LP3.shell.h_liq:VARIABLE(start = preheater_LP3.shell.h_liq_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of liquid phase\" type: Real preheater_LP3.shell.h_vap:VARIABLE(start = preheater_LP3.shell.h_vap_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of vapour phase\" type: Real preheater_LP3.shell.p_vap:VARIABLE(min = 0.0 start = preheater_LP3.shell.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"Vapour pressure\" type: Real preheater_LP4.tubes.h:VARIABLE(start = preheater_LP4.tubes.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 protected = true ) \"spec. enthalpy state\" type: Real preheater_LP4.tubes.p:VARIABLE(min = 0.0 start = preheater_LP4.tubes.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real preheater_LP4.shell.h_liq:VARIABLE(start = preheater_LP4.shell.h_liq_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of liquid phase\" type: Real preheater_LP4.shell.h_vap:VARIABLE(start = preheater_LP4.shell.h_vap_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of vapour phase\" type: Real preheater_LP4.shell.p_vap:VARIABLE(min = 0.0 start = preheater_LP4.shell.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"Vapour pressure\" type: Real join_preheater_LP3.h:VARIABLE(start = join_preheater_LP3.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real join_preheater_LP3.p:VARIABLE(min = 0.0 start = join_preheater_LP3.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real downComer_feedWaterTank.h[1]:VARIABLE(start = downComer_feedWaterTank.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [3] downComer_feedWaterTank.h[2]:VARIABLE(start = downComer_feedWaterTank.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [3] downComer_feedWaterTank.h[3]:VARIABLE(start = downComer_feedWaterTank.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [3] downComer_feedWaterTank.p[1]:VARIABLE(min = 0.0 start = downComer_feedWaterTank.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [3] downComer_feedWaterTank.p[2]:VARIABLE(min = 0.0 start = downComer_feedWaterTank.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [3] downComer_feedWaterTank.p[3]:VARIABLE(min = 0.0 start = downComer_feedWaterTank.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [3] PID_NDVW3.switch_OnOff.u2:DISCRETE(flow=false fixed = true ) \"Connector of Boolean input signal\" type: Boolean PID_preheaterLP3.switch_OnOff.u2:DISCRETE(flow=false fixed = true ) \"Connector of Boolean input signal\" type: Boolean PID_preheaterLP4.switch_OnOff.u2:DISCRETE(flow=false fixed = true ) \"Connector of Boolean input signal\" type: Boolean PI_preheater1.switch_OnOff.u2:DISCRETE(flow=false fixed = true ) \"Connector of Boolean input signal\" type: Boolean PI_valveControl_preheater_HP.switch_OnOff.u2:DISCRETE(flow=false fixed = true ) \"Connector of Boolean input signal\" type: Boolean PI_Pump_cond.switch_OnOff.u2:DISCRETE(flow=false fixed = true ) \"Connector of Boolean input signal\" type: Boolean Warning: The initial conditions are over specified. The following 1 initial equations are redundant, so they are removed from the initialization_lambda0 system: steamGenerator.heatRelease.y = steamGenerator.QF_setl_. Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 2583 * Number of states: 0 () * Number of discrete variables: 52 ($PRE.PID_NDVW3.time_lag_I_activation.entryTime,$PRE.PID_NDVW3.switch_OnOff.u2,$PRE.PID_preheaterLP3.time_lag_I_activation.entryTime,$PRE.PID_preheaterLP3.switch_OnOff.u2,$PRE.PID_preheaterLP4.time_lag_I_activation.entryTime,$PRE.PID_preheaterLP4.switch_OnOff.u2,$PRE.PI_preheater1.time_lag_I_activation.entryTime,$PRE.PI_preheater1.switch_OnOff.u2,$PRE.PI_valveControl_preheater_HP.time_lag_I_activation.entryTime,$PRE.PI_valveControl_preheater_HP.switch_OnOff.u2,$PRE.PI_Pump_cond.time_lag_I_activation.entryTime,$PRE.PI_Pump_cond.switch_OnOff.u2,valveControl_preheater_HP.pressureLoss.normIsValid,valve_HP.pressureLoss.normIsValid,valve_IP2.pressureLoss.normIsValid,PTarget.nextEventScaled,PTarget.nextEvent,$PRE.PTarget.nextEvent,PTarget.last,PTarget.b,PTarget.a,PID_NDVW3.I_activation.y,PID_NDVW3.time_lag_I_activation.entryTime,PID_NDVW3.switch_OnOff.u2,PID_preheaterLP3.I_activation.y,PID_preheaterLP3.time_lag_I_activation.entryTime,PID_preheaterLP3.switch_OnOff.u2,PID_preheaterLP4.I_activation.y,PID_preheaterLP4.time_lag_I_activation.entryTime,PID_preheaterLP4.switch_OnOff.u2,PI_preheater1.I_activation.y,PI_preheater1.time_lag_I_activation.entryTime,PI_preheater1.switch_OnOff.u2,PI_valveControl_preheater_HP.I_activation.y,PI_valveControl_preheater_HP.time_lag_I_activation.entryTime,PI_valveControl_preheater_HP.switch_OnOff.u2,PI_Pump_cond.I_activation.y,PI_Pump_cond.time_lag_I_activation.entryTime,PI_Pump_cond.switch_OnOff.u2,$whenCondition1,$whenCondition2,$whenCondition3,$whenCondition4,$whenCondition5,$whenCondition6,$whenCondition7,$whenCondition8,$whenCondition9,$whenCondition10,$whenCondition11,$whenCondition12,$whenCondition13) * Number of discrete states: 0 () * Number of clocked states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (7738): * Single equations (assignments): 7129 * Array equations: 0 * Algorithm blocks: 1 * Record equations: 537 * When equations: 0 * If-equations: 0 * Equation systems (not torn): 19 * Torn equation systems: 52 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details (not torn): * Constant Jacobian (size): 0 systems * Linear Jacobian (size,density): 0 systems * Non-linear Jacobian (size): 19 systems {1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1} * Without analytic Jacobian (size): 0 systems Notification: Torn system details for strict tearing set: * Linear torn systems (#iteration vars, #inner vars, density): 21 systems {(1,1,100.0%), (4,3,87.5%), (1,5,100.0%), (4,3,87.5%), (1,1,100.0%), (4,3,87.5%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (4,3,87.5%), (1,4,100.0%), (1,1,100.0%), (4,3,87.5%), (1,1,100.0%), (4,3,87.5%), (1,1,100.0%), (4,3,87.5%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%)} * Non-linear torn systems (#iteration vars, #inner vars): 31 systems {(1,1), (1,1), (5,14), (1,6), (1,2), (1,3), (1,1), (1,6), (1,13), (1,3), (1,3), (1,1), (5,13), (1,21), (1,2), (1,7), (1,1), (5,14), (1,1), (5,14), (1,1), (5,14), (2,5), (1,80), (1,6), (1,6), (1,3), (1,3), (1,4), (1,3), (1,80)} Notification: Performance of prepare postOptimizeDAE: time 0.01837/7.587, allocations: 4.668 MB / 2.965 GB, free: 126 MB / 1.073 GB Notification: Performance of postOpt lateInlineFunction (simulation): time 0.01763/7.604, allocations: 5.023 MB / 2.969 GB, free: 122.8 MB / 1.073 GB Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.1126/7.717, allocations: 99.11 MB / 3.066 GB, free: 57.36 MB / 1.073 GB Notification: Performance of postOpt inlineArrayEqn (simulation): time 0.0006624/7.718, allocations: 0.6007 MB / 3.067 GB, free: 56.76 MB / 1.073 GB Notification: Performance of postOpt constantLinearSystem (simulation): time 0.0001282/7.718, allocations: 176 kB / 3.067 GB, free: 56.59 MB / 1.073 GB Notification: Performance of postOpt simplifysemiLinear (simulation): time 0.03735/7.755, allocations: 20 MB / 3.086 GB, free: 36.68 MB / 1.073 GB Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.6353/8.391, allocations: 122.9 MB / 3.207 GB, free: 234.1 MB / 1.105 GB Notification: Performance of postOpt simplifyComplexFunction (simulation): time 0.002875/8.393, allocations: 1.345 MB / 3.208 GB, free: 234.1 MB / 1.105 GB Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.01824/8.412, allocations: 5.7 MB / 3.213 GB, free: 234.1 MB / 1.105 GB Notification: Performance of postOpt tearingSystem (simulation): time 0.1518/8.563, allocations: 31.99 MB / 3.245 GB, free: 232.7 MB / 1.105 GB Notification: Performance of postOpt inputDerivativesUsed (simulation): time 0.007738/8.571, allocations: 1.158 MB / 3.246 GB, free: 232.7 MB / 1.105 GB Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 0.02663/8.598, allocations: 64.89 MB / 3.309 GB, free: 174.6 MB / 1.105 GB Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 6.888e-05/8.598, allocations: 218.8 kB / 3.309 GB, free: 174.6 MB / 1.105 GB Notification: Performance of postOpt symbolicJacobian (simulation): time 0.09504/8.693, allocations: 61.04 MB / 3.369 GB, free: 129.7 MB / 1.105 GB Notification: Performance of postOpt removeConstants (simulation): time 0.03734/8.73, allocations: 12.83 MB / 3.382 GB, free: 124.2 MB / 1.105 GB Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.01911/8.749, allocations: 0.998 MB / 3.382 GB, free: 123.8 MB / 1.105 GB Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.03346/8.783, allocations: 1.163 MB / 3.384 GB, free: 123.3 MB / 1.105 GB Notification: Performance of postOpt findZeroCrossings (simulation): time 0.008945/8.792, allocations: 2.971 MB / 3.387 GB, free: 122.1 MB / 1.105 GB Notification: Performance of postOpt collapseArrayExpressions (simulation): time 0.004096/8.796, allocations: 1.143 MB / 3.388 GB, free: 121.3 MB / 1.105 GB Notification: Performance of sorting global known variables: time 0.0361/8.832, allocations: 25.68 MB / 3.413 GB, free: 101.7 MB / 1.105 GB Notification: Performance of sort global known variables: time 3.9e-07/8.832, allocations: 0 / 3.413 GB, free: 101.7 MB / 1.105 GB Notification: Performance of remove unused functions: time 0.1048/8.937, allocations: 29.34 MB / 3.441 GB, free: 75.14 MB / 1.105 GB Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 639 * Number of states: 133 (PI_Pump_cond.smoothPIDInput.y_aux,PI_Pump_cond.smoothPIDOutput.y_aux,PI_Pump_cond.smoothPIDOutput1.y_aux,PI_Pump_cond.resetValueI,PI_valveControl_preheater_HP.smoothPIDInput.y_aux,PI_valveControl_preheater_HP.smoothPIDOutput.y_aux,PI_valveControl_preheater_HP.smoothPIDOutput1.y_aux,PI_valveControl_preheater_HP.resetValueI,PI_preheater1.smoothPIDInput.y_aux,PI_preheater1.smoothPIDOutput.y_aux,PI_preheater1.smoothPIDOutput1.y_aux,PI_preheater1.resetValueI,PID_preheaterLP4.smoothPIDOutput1.y_aux,PID_preheaterLP4.resetValueI,PID_preheaterLP3.smoothPIDOutput1.y_aux,PID_preheaterLP3.resetValueI,PID_NDVW3.smoothPIDOutput1.y_aux,PID_NDVW3.resetValueI,steamGenerator.h_IP,steamGenerator.p_IP,steamGenerator.h_HP,steamGenerator.p_HP,steamGenerator.heatRelease.x_scaled[1],steamGenerator.heatRelease.x_scaled[2],condenser.tubes.h,condenser.tubes.p,condenser.shell.h_liq,condenser.shell.h_vap,condenser.shell.volume_vap,condenser.shell.p_vap,condenser.wall.U[1],condenser.wall.U[2],condenser.wall.U[3],feedWaterTank.volume.h_liq,feedWaterTank.volume.h_vap,feedWaterTank.volume.volume_vap,feedWaterTank.volume.p_vap,feedWaterTank.wall.U[1],feedWaterTank.wall.U[2],feedWaterTank.wall.U[3],PI_Pump_cond.resetValueP,PI_Pump_cond.resetValueID,PI_Pump_cond.I.y,join_LP1.h,join_LP1.p,join_HP.h,join_HP.p,preheater_HP.tubes.h,preheater_HP.tubes.p,preheater_HP.shell.h_liq,preheater_HP.shell.h_vap,preheater_HP.shell.volume_vap,preheater_HP.shell.p_vap,preheater_HP.wall.U[1],preheater_HP.wall.U[2],preheater_HP.wall.U[3],preheater_LP1.tubes.h,preheater_LP1.tubes.p,preheater_LP1.shell.h_liq,preheater_LP1.shell.h_vap,preheater_LP1.shell.volume_vap,preheater_LP1.shell.p_vap,preheater_LP1.wall.U[1],preheater_LP1.wall.U[2],preheater_LP1.wall.U[3],PI_valveControl_preheater_HP.resetValueP,PI_valveControl_preheater_HP.resetValueID,PI_valveControl_preheater_HP.I.y,measurement.y,join_LP_main.h,join_LP_main.p,PI_preheater1.resetValueP,PI_preheater1.resetValueID,PI_preheater1.I.y,split_IP2.h,split_IP2.p,join_IP3.h,join_IP3.p,join_LP2.h,join_LP2.p,split_LP3.h,split_LP3.p,preheater_LP2.tubes.h,preheater_LP2.tubes.p,preheater_LP2.shell.h_liq,preheater_LP2.shell.h_vap,preheater_LP2.shell.volume_vap,preheater_LP2.shell.p_vap,preheater_LP2.wall.U[1],preheater_LP2.wall.U[2],preheater_LP2.wall.U[3],preheater_LP3.tubes.h,preheater_LP3.tubes.p,preheater_LP3.shell.h_liq,preheater_LP3.shell.h_vap,preheater_LP3.shell.volume_vap,preheater_LP3.shell.p_vap,preheater_LP3.wall.U[1],preheater_LP3.wall.U[2],preheater_LP3.wall.U[3],preheater_LP4.tubes.h,preheater_LP4.tubes.p,preheater_LP4.shell.h_liq,preheater_LP4.shell.h_vap,preheater_LP4.shell.volume_vap,preheater_LP4.shell.p_vap,preheater_LP4.wall.U[1],preheater_LP4.wall.U[2],preheater_LP4.wall.U[3],join_preheater_LP3.h,join_preheater_LP3.p,PID_preheaterLP4.resetValueP,PID_preheaterLP4.resetValueID,PID_preheaterLP4.I.y,PID_preheaterLP4.smoothPIDInput.y_aux,PID_preheaterLP4.smoothPIDOutput.y_aux,PID_preheaterLP3.resetValueP,PID_preheaterLP3.resetValueID,PID_preheaterLP3.I.y,PID_preheaterLP3.smoothPIDInput.y_aux,PID_preheaterLP3.smoothPIDOutput.y_aux,PID_NDVW3.resetValueP,PID_NDVW3.resetValueID,PID_NDVW3.I.y,PID_NDVW3.smoothPIDInput.y_aux,PID_NDVW3.smoothPIDOutput.y_aux,downComer_feedWaterTank.h[1],downComer_feedWaterTank.h[2],downComer_feedWaterTank.h[3],downComer_feedWaterTank.p[1],downComer_feedWaterTank.p[2],downComer_feedWaterTank.p[3],inertia.phi) * Number of discrete variables: 36 ($whenCondition13,$whenCondition12,$whenCondition11,$whenCondition10,$whenCondition9,$whenCondition8,$whenCondition7,$whenCondition6,$whenCondition5,$whenCondition4,$whenCondition3,$whenCondition2,$whenCondition1,PI_Pump_cond.switch_OnOff.u2,PI_Pump_cond.time_lag_I_activation.entryTime,PI_Pump_cond.I_activation.y,PI_valveControl_preheater_HP.switch_OnOff.u2,PI_valveControl_preheater_HP.time_lag_I_activation.entryTime,PI_valveControl_preheater_HP.I_activation.y,PI_preheater1.switch_OnOff.u2,PI_preheater1.time_lag_I_activation.entryTime,PI_preheater1.I_activation.y,PID_preheaterLP4.switch_OnOff.u2,PID_preheaterLP4.time_lag_I_activation.entryTime,PID_preheaterLP4.I_activation.y,PID_preheaterLP3.switch_OnOff.u2,PID_preheaterLP3.time_lag_I_activation.entryTime,PID_preheaterLP3.I_activation.y,PID_NDVW3.switch_OnOff.u2,PID_NDVW3.time_lag_I_activation.entryTime,PID_NDVW3.I_activation.y,PTarget.a,PTarget.b,PTarget.last,PTarget.nextEvent,PTarget.nextEventScaled) * Number of discrete states: 18 (PID_NDVW3.switch_OnOff.u2,PID_preheaterLP3.switch_OnOff.u2,PID_preheaterLP4.switch_OnOff.u2,PI_preheater1.switch_OnOff.u2,PI_valveControl_preheater_HP.switch_OnOff.u2,PI_Pump_cond.switch_OnOff.u2,PTarget.nextEvent,PTarget.last,PTarget.nextEventScaled,PTarget.b,PTarget.a,$whenCondition1,PID_NDVW3.toPU.y,PID_preheaterLP3.toPU.y,PID_preheaterLP4.toPU.y,PI_preheater1.toPU.y,PI_valveControl_preheater_HP.toPU.y,PI_Pump_cond.toPU.y) * Number of clocked states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (3483): * Single equations (assignments): 3028 * Array equations: 0 * Algorithm blocks: 1 * Record equations: 384 * When equations: 6 * If-equations: 0 * Equation systems (not torn): 2 * Torn equation systems: 62 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details (not torn): * Constant Jacobian (size): 0 systems * Linear Jacobian (size,density): 0 systems * Non-linear Jacobian (size): 2 systems {1, 1} * Without analytic Jacobian (size): 0 systems Notification: Torn system details for strict tearing set: * Linear torn systems (#iteration vars, #inner vars, density): 33 systems {(1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (4,3,87.5%), (1,1,100.0%), (1,1,100.0%), (4,3,87.5%), (1,1,100.0%), (1,5,100.0%), (4,3,87.5%), (1,1,100.0%), (4,3,87.5%), (1,1,100.0%), (1,5,100.0%), (1,1,100.0%), (1,1,100.0%), (4,3,87.5%), (1,1,100.0%), (1,1,100.0%), (1,5,100.0%), (1,1,100.0%), (1,1,100.0%), (1,5,100.0%), (1,1,100.0%), (1,1,100.0%), (4,3,87.5%), (4,3,87.5%), (1,5,100.0%), (1,1,100.0%), (1,5,100.0%), (1,5,100.0%), (1,1,100.0%)} * Non-linear torn systems (#iteration vars, #inner vars): 29 systems {(1,8), (1,3), (1,6), (1,4), (3,8), (1,6), (1,4), (1,3), (1,14), (1,2), (1,10), (3,8), (1,6), (1,29), (3,8), (3,8), (1,4), (1,4), (3,8), (1,4), (1,6), (1,5), (1,4), (1,4), (1,4), (1,4), (1,4), (1,4), (1,4)} Notification: Performance of Backend phase and start with SimCode phase: time 0.01146/8.948, allocations: 3.363 MB / 3.445 GB, free: 73.89 MB / 1.105 GB [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa main/Basics/ControlVolumes/FluidVolumes/VolumeVLE_L3_TwoZonesNPort.mo:130:3-130:139:writable] Warning: Variable $DER.preheater_LP3.shell.volume_vap has attribute stateSelect=StateSelect.always, but can't be selected as a state. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa main/Basics/ControlVolumes/FluidVolumes/VolumeVLE_L3_TwoZonesNPort.mo:130:3-130:139:writable] Warning: Variable $DER.preheater_LP2.shell.volume_vap has attribute stateSelect=StateSelect.always, but can't be selected as a state. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa main/Basics/ControlVolumes/FluidVolumes/VolumeVLE_L3_TwoZonesNPort.mo:130:3-130:139:writable] Warning: Variable $DER.preheater_LP1.shell.volume_vap has attribute stateSelect=StateSelect.always, but can't be selected as a state. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa main/Basics/ControlVolumes/FluidVolumes/VolumeVLE_L3_TwoZonesNPort.mo:130:3-130:139:writable] Warning: Variable $DER.preheater_HP.shell.volume_vap has attribute stateSelect=StateSelect.always, but can't be selected as a state. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa main/Basics/ControlVolumes/FluidVolumes/VolumeVLE_L3_TwoZonesNPort.mo:130:3-130:139:writable] Warning: Variable $DER.feedWaterTank.volume.volume_vap has attribute stateSelect=StateSelect.always, but can't be selected as a state. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa main/Basics/ControlVolumes/FluidVolumes/VolumeVLE_L3_TwoZonesNPort.mo:130:3-130:139:writable] Warning: Variable $DER.preheater_LP4.shell.volume_vap has attribute stateSelect=StateSelect.always, but can't be selected as a state. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa main/Basics/ControlVolumes/FluidVolumes/VolumeVLE_L3_TwoZonesNPort.mo:130:3-130:139:writable] Warning: Variable $DER.condenser.shell.volume_vap has attribute stateSelect=StateSelect.always, but can't be selected as a state. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa main/Basics/ControlVolumes/FluidVolumes/VolumeVLE_L3_TwoZonesNPort.mo:130:3-130:139:writable] Warning: Variable $DER.preheater_LP3.shell.volume_vap has attribute stateSelect=StateSelect.always, but can't be selected as a state. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa main/Basics/ControlVolumes/FluidVolumes/VolumeVLE_L3_TwoZonesNPort.mo:130:3-130:139:writable] Warning: Variable $DER.preheater_LP2.shell.volume_vap has attribute stateSelect=StateSelect.always, but can't be selected as a state. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa main/Basics/ControlVolumes/FluidVolumes/VolumeVLE_L3_TwoZonesNPort.mo:130:3-130:139:writable] Warning: Variable $DER.preheater_LP1.shell.volume_vap has attribute stateSelect=StateSelect.always, but can't be selected as a state. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa main/Basics/ControlVolumes/FluidVolumes/VolumeVLE_L3_TwoZonesNPort.mo:130:3-130:139:writable] Warning: Variable $DER.preheater_HP.shell.volume_vap has attribute stateSelect=StateSelect.always, but can't be selected as a state. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa main/Basics/ControlVolumes/FluidVolumes/VolumeVLE_L3_TwoZonesNPort.mo:130:3-130:139:writable] Warning: Variable $DER.feedWaterTank.volume.volume_vap has attribute stateSelect=StateSelect.always, but can't be selected as a state. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa main/Basics/ControlVolumes/FluidVolumes/VolumeVLE_L3_TwoZonesNPort.mo:130:3-130:139:writable] Warning: Variable $DER.preheater_LP4.shell.volume_vap has attribute stateSelect=StateSelect.always, but can't be selected as a state. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa main/Basics/ControlVolumes/FluidVolumes/VolumeVLE_L3_TwoZonesNPort.mo:130:3-130:139:writable] Warning: Variable $DER.condenser.shell.volume_vap has attribute stateSelect=StateSelect.always, but can't be selected as a state. Notification: Performance of simCode: created initialization part: time 0.494/9.442, allocations: 101.6 MB / 3.544 GB, free: 253.7 MB / 1.136 GB Notification: Performance of simCode: created event and clocks part: time 0.00308/9.445, allocations: 0.9378 MB / 3.545 GB, free: 253.6 MB / 1.136 GB Notification: Performance of simCode: created simulation system equations: time 0.03899/9.484, allocations: 29.58 MB / 3.574 GB, free: 237.4 MB / 1.136 GB Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.08557/9.57, allocations: 14.89 MB / 3.588 GB, free: 236.4 MB / 1.136 GB Notification: Performance of simCode: created linear, non-linear and system jacobian parts: time 0.2115/9.781, allocations: 122.5 MB / 3.708 GB, free: 184.2 MB / 1.136 GB Notification: Performance of simCode: some other stuff during SimCode phase: time 0.0308/9.812, allocations: 14.61 MB / 3.722 GB, free: 182.4 MB / 1.136 GB Notification: Performance of simCode: alias equations: time 0.05781/9.87, allocations: 16.34 MB / 3.738 GB, free: 177.8 MB / 1.136 GB Notification: Performance of simCode: all other stuff during SimCode phase: time 0.07162/9.942, allocations: 20.41 MB / 3.758 GB, free: 162.4 MB / 1.136 GB Notification: Performance of SimCode: time 2.144e-06/9.942, allocations: 0 / 3.758 GB, free: 162.4 MB / 1.136 GB Notification: Performance of Templates: time 2.426/12.37, allocations: 1.069 GB / 4.827 GB, free: 257.3 MB / 1.198 GB " [Timeout remaining time 788] make -j1 -f ClaRa_dev_ClaRa.Examples.SteamCycle_01.makefile [Timeout 800] (rm -f ClaRa_dev_ClaRa.Examples.SteamCycle_01.pipe ; mkfifo ClaRa_dev_ClaRa.Examples.SteamCycle_01.pipe ; head -c 1048576 < ClaRa_dev_ClaRa.Examples.SteamCycle_01.pipe >> ../files/ClaRa_dev_ClaRa.Examples.SteamCycle_01.sim & ./ClaRa_dev_ClaRa.Examples.SteamCycle_01 -abortSlowSimulation -alarm=240 -emit_protected -lv LOG_STATS > ClaRa_dev_ClaRa.Examples.SteamCycle_01.pipe 2>&1) [Timeout 240] diffSimulationResults("ClaRa_dev_ClaRa.Examples.SteamCycle_01_res.mat","/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/ReferenceFiles/ClaRa/ReferenceResults/ClaRa.Examples.SteamCycle_01.mat","",relTol=0.003,relTolDiffMinMax=0.003,rangeDelta=0.001) [Timeout 800] "" [Timeout remaining time 800] "" Variables in the reference:PID_NDVW3.I.y,PID_NDVW3.resetValueI,PID_NDVW3.resetValueID,PID_NDVW3.resetValueP,PID_NDVW3.smoothPIDInput.y_aux,PID_NDVW3.smoothPIDOutput.y_aux,PID_NDVW3.smoothPIDOutput1.y_aux,PID_preheaterLP3.I.y,PID_preheaterLP3.resetValueI,PID_preheaterLP3.resetValueID,PID_preheaterLP3.resetValueP,PID_preheaterLP3.smoothPIDInput.y_aux,PID_preheaterLP3.smoothPIDOutput.y_aux,PID_preheaterLP3.smoothPIDOutput1.y_aux,PID_preheaterLP4.I.y,PID_preheaterLP4.resetValueI,PID_preheaterLP4.resetValueID,PID_preheaterLP4.resetValueP,PID_preheaterLP4.smoothPIDInput.y_aux,PID_preheaterLP4.smoothPIDOutput.y_aux,PID_preheaterLP4.smoothPIDOutput1.y_aux,PI_Pump_cond.I.y,PI_Pump_cond.resetValueI,PI_Pump_cond.resetValueID,PI_Pump_cond.resetValueP,PI_Pump_cond.smoothPIDInput.y_aux,PI_Pump_cond.smoothPIDOutput.y_aux,PI_Pump_cond.smoothPIDOutput1.y_aux,PI_preheater1.I.y,PI_preheater1.resetValueI,PI_preheater1.resetValueID,PI_preheater1.resetValueP,PI_preheater1.smoothPIDInput.y_aux,PI_preheater1.smoothPIDOutput.y_aux,PI_preheater1.smoothPIDOutput1.y_aux,PI_valveControl_preheater_HP.I.y,PI_valveControl_preheater_HP.resetValueI,PI_valveControl_preheater_HP.resetValueID,PI_valveControl_preheater_HP.resetValueP,PI_valveControl_preheater_HP.smoothPIDInput.y_aux,PI_valveControl_preheater_HP.smoothPIDOutput.y_aux,PI_valveControl_preheater_HP.smoothPIDOutput1.y_aux,Time,condenser.shell.h_liq,condenser.shell.h_vap,condenser.shell.p_vap,condenser.shell.volume_vap,condenser.tubes.h,condenser.tubes.p,condenser.wall.U[1],condenser.wall.U[2],condenser.wall.U[3],downComer_feedWaterTank.h[1],downComer_feedWaterTank.h[2],downComer_feedWaterTank.h[3],downComer_feedWaterTank.p[1],downComer_feedWaterTank.p[2],downComer_feedWaterTank.p[3],feedWaterTank.volume.h_liq,feedWaterTank.volume.h_vap,feedWaterTank.volume.p_vap,feedWaterTank.volume.volume_vap,feedWaterTank.wall.U[1],feedWaterTank.wall.U[2],feedWaterTank.wall.U[3],inertia.phi,join_HP.h,join_HP.p,join_IP3.h,join_IP3.p,join_LP1.h,join_LP1.p,join_LP2.h,join_LP2.p,join_LP_main.h,join_LP_main.p,join_preheater_LP3.h,join_preheater_LP3.p,measurement.y,preheater_HP.shell.h_liq,preheater_HP.shell.h_vap,preheater_HP.shell.p_vap,preheater_HP.shell.volume_vap,preheater_HP.tubes.h,preheater_HP.tubes.p,preheater_HP.wall.U[1],preheater_HP.wall.U[2],preheater_HP.wall.U[3],preheater_LP1.shell.h_liq,preheater_LP1.shell.h_vap,preheater_LP1.shell.p_vap,preheater_LP1.shell.volume_vap,preheater_LP1.tubes.h,preheater_LP1.tubes.p,preheater_LP1.wall.U[1],preheater_LP1.wall.U[2],preheater_LP1.wall.U[3],preheater_LP2.shell.h_liq,preheater_LP2.shell.h_vap,preheater_LP2.shell.p_vap,preheater_LP2.shell.volume_vap,preheater_LP2.tubes.h,preheater_LP2.tubes.p,preheater_LP2.wall.U[1],preheater_LP2.wall.U[2],preheater_LP2.wall.U[3],preheater_LP3.shell.h_liq,preheater_LP3.shell.h_vap,preheater_LP3.shell.p_vap,preheater_LP3.shell.volume_vap,preheater_LP3.tubes.h,preheater_LP3.tubes.p,preheater_LP3.wall.U[1],preheater_LP3.wall.U[2],preheater_LP3.wall.U[3],preheater_LP4.shell.h_liq,preheater_LP4.shell.h_vap,preheater_LP4.shell.p_vap,preheater_LP4.shell.volume_vap,preheater_LP4.tubes.h,preheater_LP4.tubes.p,preheater_LP4.wall.U[1],preheater_LP4.wall.U[2],preheater_LP4.wall.U[3],split_IP2.h,split_IP2.p,split_LP3.h,split_LP3.p,steamGenerator.h_HP,steamGenerator.h_IP,steamGenerator.heatRelease.x_scaled[1],steamGenerator.heatRelease.x_scaled[2],steamGenerator.p_HP,steamGenerator.p_IP Variables in the result:$cse132,$cse134,$cse136,$cse137,$cse140,$cse177,$cse179,$cse181,$cse182,$cse185,$cse222,$cse224,$cse226,$cse227,$cse230,$cse264,$cse266,$cse268,$cse269,$cse272,$cse304,$cse306,$cse308,$cse309,$cse312,$cse47,$cse49,$cse51,$cse52,$cse55,$cse87,$cse89,$cse91,$cse92,$cse95,INIT.CharLine_Delta_p_HP_mLS_[1,1],INIT.CharLine_Delta_p_HP_mLS_[1,2],INIT.CharLine_Delta_p_HP_mLS_[10,1],INIT.CharLine_Delta_p_HP_mLS_[10,2],INIT.CharLine_Delta_p_HP_mLS_[11,1],INIT.CharLine_Delta_p_HP_mLS_[11,2],INIT.CharLine_Delta_p_HP_mLS_[2,1],INIT.CharLine_Delta_p_HP_mLS_[2,2],INIT.CharLine_Delta_p_HP_mLS_[3,1],INIT.CharLine_Delta_p_HP_mLS_[3,2],INIT.CharLine_Delta_p_HP_mLS_[4,1],INIT.CharLine_Delta_p_HP_mLS_[4,2],INIT.CharLine_Delta_p_HP_mLS_[5,1],INIT.CharLine_Delta_p_HP_mLS_[5,2],INIT.CharLine_Delta_p_HP_mLS_[6,1],INIT.CharLine_Delta_p_HP_mLS_[6,2],INIT.CharLine_Delta_p_HP_mLS_[7,1],INIT.CharLine_Delta_p_HP_mLS_[7,2],INIT.CharLine_Delta_p_HP_mLS_[8,1],INIT.CharLine_Delta_p_HP_mLS_[8,2],INIT.CharLine_Delta_p_HP_mLS_[9,1],INIT.CharLine_Delta_p_HP_mLS_[9,2],INIT.CharLine_Delta_p_IP_mRS_[1,1],INIT.CharLine_Delta_p_IP_mRS_[1,2],INIT.CharLine_Delta_p_IP_mRS_[10,1],INIT.CharLine_Delta_p_IP_mRS_[10,2],INIT.CharLine_Delta_p_IP_mRS_[11,1],INIT.CharLine_Delta_p_IP_mRS_[11,2],INIT.CharLine_Delta_p_IP_mRS_[2,1],INIT.CharLine_Delta_p_IP_mRS_[2,2],INIT.CharLine_Delta_p_IP_mRS_[3,1],INIT.CharLine_Delta_p_IP_mRS_[3,2],INIT.CharLine_Delta_p_IP_mRS_[4,1],INIT.CharLine_Delta_p_IP_mRS_[4,2],INIT.CharLine_Delta_p_IP_mRS_[5,1],INIT.CharLine_Delta_p_IP_mRS_[5,2],INIT.CharLine_Delta_p_IP_mRS_[6,1],INIT.CharLine_Delta_p_IP_mRS_[6,2],INIT.CharLine_Delta_p_IP_mRS_[7,1],INIT.CharLine_Delta_p_IP_mRS_[7,2],INIT.CharLine_Delta_p_IP_mRS_[8,1],INIT.CharLine_Delta_p_IP_mRS_[8,2],INIT.CharLine_Delta_p_IP_mRS_[9,1],INIT.CharLine_Delta_p_IP_mRS_[9,2],INIT.Delta_p_LS_nom,INIT.Delta_p_RS_nom,INIT.IP1_pressure,INIT.IP2_pressure,INIT.IP3_pressure,INIT.P_target_,INIT.Pump_FW.Delta_p,INIT.Pump_FW.P_pump,INIT.Pump_FW.efficiency,INIT.Pump_FW.h_in,INIT.Pump_FW.h_out,INIT.Pump_FW.m_flow,INIT.Pump_FW.p_in,INIT.Pump_FW.p_out,INIT.Pump_FW.rho_in,INIT.Pump_FW.summary.inlet.h,INIT.Pump_FW.summary.inlet.m_flow,INIT.Pump_FW.summary.inlet.p,INIT.Pump_FW.summary.outlet.h,INIT.Pump_FW.summary.outlet.m_flow,INIT.Pump_FW.summary.outlet.p,INIT.Pump_FW.summary.outline.Delta_p,INIT.Pump_FW.summary.outline.P_pump,INIT.Pump_cond.Delta_p,INIT.Pump_cond.P_pump,INIT.Pump_cond.efficiency,INIT.Pump_cond.h_in,INIT.Pump_cond.h_out,INIT.Pump_cond.m_flow,INIT.Pump_cond.p_in,INIT.Pump_cond.p_out,INIT.Pump_cond.rho_in,INIT.Pump_cond.summary.inlet.h,INIT.Pump_cond.summary.inlet.m_flow,INIT.Pump_cond.summary.inlet.p,INIT.Pump_cond.summary.outlet.h,INIT.Pump_cond.summary.outlet.m_flow,INIT.Pump_cond.summary.outlet.p,INIT.Pump_cond.summary.outline.Delta_p,INIT.Pump_cond.summary.outline.P_pump,INIT.T_LS_nom,INIT.T_RS_nom,INIT.Turbine_HP.Delta_p,INIT.Turbine_HP.P_turbine,INIT.Turbine_HP.efficiency,INIT.Turbine_HP.h_in,INIT.Turbine_HP.h_out,INIT.Turbine_HP.m_flow,INIT.Turbine_HP.p_in,INIT.Turbine_HP.p_out,INIT.Turbine_HP.rho_in,INIT.Turbine_HP.summary.inlet.h,INIT.Turbine_HP.summary.inlet.m_flow,INIT.Turbine_HP.summary.inlet.p,INIT.Turbine_HP.summary.outlet.h,INIT.Turbine_HP.summary.outlet.m_flow,INIT.Turbine_HP.summary.outlet.p,INIT.Turbine_HP.summary.outline.Delta_p,INIT.Turbine_HP.summary.outline.P_turbine,INIT.Turbine_IP1.Delta_p,INIT.Turbine_IP1.P_turbine,INIT.Turbine_IP1.efficiency,INIT.Turbine_IP1.h_in,INIT.Turbine_IP1.h_out,INIT.Turbine_IP1.m_flow,INIT.Turbine_IP1.p_in,INIT.Turbine_IP1.p_out,INIT.Turbine_IP1.rho_in,INIT.Turbine_IP1.summary.inlet.h,INIT.Turbine_IP1.summary.inlet.m_flow,INIT.Turbine_IP1.summary.inlet.p,INIT.Turbine_IP1.summary.outlet.h,INIT.Turbine_IP1.summary.outlet.m_flow,INIT.Turbine_IP1.summary.outlet.p,INIT.Turbine_IP1.summary.outline.Delta_p,INIT.Turbine_IP1.summary.outline.P_turbine,INIT.Turbine_IP2.Delta_p,INIT.Turbine_IP2.P_turbine,INIT.Turbine_IP2.efficiency,INIT.Turbine_IP2.h_in,INIT.Turbine_IP2.h_out,INIT.Turbine_IP2.m_flow,INIT.Turbine_IP2.p_in,INIT.Turbine_IP2.p_out,INIT.Turbine_IP2.rho_in,INIT.Turbine_IP2.summary.inlet.h,INIT.Turbine_IP2.summary.inlet.m_flow,INIT.Turbine_IP2.summary.inlet.p,INIT.Turbine_IP2.summary.outlet.h,INIT.Turbine_IP2.summary.outlet.m_flow,INIT.Turbine_IP2.summary.outlet.p,INIT.Turbine_IP2.summary.outline.Delta_p,INIT.Turbine_IP2.summary.outline.P_turbine,INIT.Turbine_IP3.Delta_p,INIT.Turbine_IP3.P_turbine,INIT.Turbine_IP3.efficiency,INIT.Turbine_IP3.h_in,INIT.Turbine_IP3.h_out,INIT.Turbine_IP3.m_flow,INIT.Turbine_IP3.p_in,INIT.Turbine_IP3.p_out,INIT.Turbine_IP3.rho_in,INIT.Turbine_IP3.summary.inlet.h,INIT.Turbine_IP3.summary.inlet.m_flow,INIT.Turbine_IP3.summary.inlet.p,INIT.Turbine_IP3.summary.outlet.h,INIT.Turbine_IP3.summary.outlet.m_flow,INIT.Turbine_IP3.summary.outlet.p,INIT.Turbine_IP3.summary.outline.Delta_p,INIT.Turbine_IP3.summary.outline.P_turbine,INIT.Turbine_LP1.Delta_p,INIT.Turbine_LP1.P_turbine,INIT.Turbine_LP1.efficiency,INIT.Turbine_LP1.h_in,INIT.Turbine_LP1.h_out,INIT.Turbine_LP1.m_flow,INIT.Turbine_LP1.p_in,INIT.Turbine_LP1.p_out,INIT.Turbine_LP1.rho_in,INIT.Turbine_LP1.summary.inlet.h,INIT.Turbine_LP1.summary.inlet.m_flow,INIT.Turbine_LP1.summary.inlet.p,INIT.Turbine_LP1.summary.outlet.h,INIT.Turbine_LP1.summary.outlet.m_flow,INIT.Turbine_LP1.summary.outlet.p,INIT.Turbine_LP1.summary.outline.Delta_p,INIT.Turbine_LP1.summary.outline.P_turbine,INIT.Turbine_LP2.Delta_p,INIT.Turbine_LP2.P_turbine,INIT.Turbine_LP2.efficiency,INIT.Turbine_LP2.h_in,INIT.Turbine_LP2.h_out,INIT.Turbine_LP2.m_flow,INIT.Turbine_LP2.p_in,INIT.Turbine_LP2.p_out,INIT.Turbine_LP2.rho_in,INIT.Turbine_LP2.summary.inlet.h,INIT.Turbine_LP2.summary.inlet.m_flow,INIT.Turbine_LP2.summary.inlet.p,INIT.Turbine_LP2.summary.outlet.h,INIT.Turbine_LP2.summary.outlet.m_flow,INIT.Turbine_LP2.summary.outlet.p,INIT.Turbine_LP2.summary.outline.Delta_p,INIT.Turbine_LP2.summary.outline.P_turbine,INIT.Turbine_LP3.Delta_p,INIT.Turbine_LP3.P_turbine,INIT.Turbine_LP3.efficiency,INIT.Turbine_LP3.h_in,INIT.Turbine_LP3.h_out,INIT.Turbine_LP3.m_flow,INIT.Turbine_LP3.p_in,INIT.Turbine_LP3.p_out,INIT.Turbine_LP3.rho_in,INIT.Turbine_LP3.summary.inlet.h,INIT.Turbine_LP3.summary.inlet.m_flow,INIT.Turbine_LP3.summary.inlet.p,INIT.Turbine_LP3.summary.outlet.h,INIT.Turbine_LP3.summary.outlet.m_flow,INIT.Turbine_LP3.summary.outlet.p,INIT.Turbine_LP3.summary.outline.Delta_p,INIT.Turbine_LP3.summary.outline.P_turbine,INIT.Turbine_LP4.Delta_p,INIT.Turbine_LP4.P_turbine,INIT.Turbine_LP4.efficiency,INIT.Turbine_LP4.h_in,INIT.Turbine_LP4.h_out,INIT.Turbine_LP4.m_flow,INIT.Turbine_LP4.p_in,INIT.Turbine_LP4.p_out,INIT.Turbine_LP4.rho_in,INIT.Turbine_LP4.summary.inlet.h,INIT.Turbine_LP4.summary.inlet.m_flow,INIT.Turbine_LP4.summary.inlet.p,INIT.Turbine_LP4.summary.outlet.h,INIT.Turbine_LP4.summary.outlet.m_flow,INIT.Turbine_LP4.summary.outlet.p,INIT.Turbine_LP4.summary.outline.Delta_p,INIT.Turbine_LP4.summary.outline.P_turbine,INIT.boiler.CharLine_Delta_p_HP_mLS_[1,1],INIT.boiler.CharLine_Delta_p_HP_mLS_[1,2],INIT.boiler.CharLine_Delta_p_HP_mLS_[10,1],INIT.boiler.CharLine_Delta_p_HP_mLS_[10,2],INIT.boiler.CharLine_Delta_p_HP_mLS_[11,1],INIT.boiler.CharLine_Delta_p_HP_mLS_[11,2],INIT.boiler.CharLine_Delta_p_HP_mLS_[2,1],INIT.boiler.CharLine_Delta_p_HP_mLS_[2,2],INIT.boiler.CharLine_Delta_p_HP_mLS_[3,1],INIT.boiler.CharLine_Delta_p_HP_mLS_[3,2],INIT.boiler.CharLine_Delta_p_HP_mLS_[4,1],INIT.boiler.CharLine_Delta_p_HP_mLS_[4,2],INIT.boiler.CharLine_Delta_p_HP_mLS_[5,1],INIT.boiler.CharLine_Delta_p_HP_mLS_[5,2],INIT.boiler.CharLine_Delta_p_HP_mLS_[6,1],INIT.boiler.CharLine_Delta_p_HP_mLS_[6,2],INIT.boiler.CharLine_Delta_p_HP_mLS_[7,1],INIT.boiler.CharLine_Delta_p_HP_mLS_[7,2],INIT.boiler.CharLine_Delta_p_HP_mLS_[8,1],INIT.boiler.CharLine_Delta_p_HP_mLS_[8,2],INIT.boiler.CharLine_Delta_p_HP_mLS_[9,1],INIT.boiler.CharLine_Delta_p_HP_mLS_[9,2],INIT.boiler.CharLine_Delta_p_IP_mRS_[1,1],INIT.boiler.CharLine_Delta_p_IP_mRS_[1,2],INIT.boiler.CharLine_Delta_p_IP_mRS_[10,1],INIT.boiler.CharLine_Delta_p_IP_mRS_[10,2],INIT.boiler.CharLine_Delta_p_IP_mRS_[11,1],INIT.boiler.CharLine_Delta_p_IP_mRS_[11,2],INIT.boiler.CharLine_Delta_p_IP_mRS_[2,1],INIT.boiler.CharLine_Delta_p_IP_mRS_[2,2],INIT.boiler.CharLine_Delta_p_IP_mRS_[3,1],INIT.boiler.CharLine_Delta_p_IP_mRS_[3,2],INIT.boiler.CharLine_Delta_p_IP_mRS_[4,1],INIT.boiler.CharLine_Delta_p_IP_mRS_[4,2],INIT.boiler.CharLine_Delta_p_IP_mRS_[5,1],INIT.boiler.CharLine_Delta_p_IP_mRS_[5,2],INIT.boiler.CharLine_Delta_p_IP_mRS_[6,1],INIT.boiler.CharLine_Delta_p_IP_mRS_[6,2],INIT.boiler.CharLine_Delta_p_IP_mRS_[7,1],INIT.boiler.CharLine_Delta_p_IP_mRS_[7,2],INIT.boiler.CharLine_Delta_p_IP_mRS_[8,1],INIT.boiler.CharLine_Delta_p_IP_mRS_[8,2],INIT.boiler.CharLine_Delta_p_IP_mRS_[9,1],INIT.boiler.CharLine_Delta_p_IP_mRS_[9,2],INIT.boiler.Delta_p_LS_,INIT.boiler.Delta_p_LS_nom,INIT.boiler.Delta_p_RS_,INIT.boiler.Delta_p_RS_nom,INIT.boiler.Q_flow,INIT.boiler.Q_flow_LS_,INIT.boiler.Q_flow_RS_,INIT.boiler.T_LS_nom,INIT.boiler.T_RS_nom,INIT.boiler.h_LS_in,INIT.boiler.h_LS_out,INIT.boiler.h_RS_in,INIT.boiler.h_RS_out,INIT.boiler.m_flow_LS_nom,INIT.boiler.m_flow_RS_nom,INIT.boiler.m_flow_cRH,INIT.boiler.m_flow_feed,INIT.boiler.p_LS_in,INIT.boiler.p_LS_out,INIT.boiler.p_LS_out_nom,INIT.boiler.p_RS_in,INIT.boiler.p_RS_out,INIT.boiler.p_RS_out_nom,INIT.boiler.table1.columns[1],INIT.boiler.table1.extrapolation,INIT.boiler.table1.isCsvExt,INIT.boiler.table1.n,INIT.boiler.table1.nHeaderLines,INIT.boiler.table1.smoothness,INIT.boiler.table1.tableOnFile,INIT.boiler.table1.table[1,1],INIT.boiler.table1.table[1,2],INIT.boiler.table1.table[10,1],INIT.boiler.table1.table[10,2],INIT.boiler.table1.table[11,1],INIT.boiler.table1.table[11,2],INIT.boiler.table1.table[2,1],INIT.boiler.table1.table[2,2],INIT.boiler.table1.table[3,1],INIT.boiler.table1.table[3,2],INIT.boiler.table1.table[4,1],INIT.boiler.table1.table[4,2],INIT.boiler.table1.table[5,1],INIT.boiler.table1.table[5,2],INIT.boiler.table1.table[6,1],INIT.boiler.table1.table[6,2],INIT.boiler.table1.table[7,1],INIT.boiler.table1.table[7,2],INIT.boiler.table1.table[8,1],INIT.boiler.table1.table[8,2],INIT.boiler.table1.table[9,1],INIT.boiler.table1.table[9,2],INIT.boiler.table1.u_max,INIT.boiler.table1.u_min,INIT.boiler.table1.verboseExtrapolation,INIT.boiler.table1.verboseRead,INIT.boiler.table2.columns[1],INIT.boiler.table2.extrapolation,INIT.boiler.table2.isCsvExt,INIT.boiler.table2.n,INIT.boiler.table2.nHeaderLines,INIT.boiler.table2.smoothness,INIT.boiler.table2.tableOnFile,INIT.boiler.table2.table[1,1],INIT.boiler.table2.table[1,2],INIT.boiler.table2.table[10,1],INIT.boiler.table2.table[10,2],INIT.boiler.table2.table[11,1],INIT.boiler.table2.table[11,2],INIT.boiler.table2.table[2,1],INIT.boiler.table2.table[2,2],INIT.boiler.table2.table[3,1],INIT.boiler.table2.table[3,2],INIT.boiler.table2.table[4,1],INIT.boiler.table2.table[4,2],INIT.boiler.table2.table[5,1],INIT.boiler.table2.table[5,2],INIT.boiler.table2.table[6,1],INIT.boiler.table2.table[6,2],INIT.boiler.table2.table[7,1],INIT.boiler.table2.table[7,2],INIT.boiler.table2.table[8,1],INIT.boiler.table2.table[8,2],INIT.boiler.table2.table[9,1],INIT.boiler.table2.table[9,2],INIT.boiler.table2.u_max,INIT.boiler.table2.u_min,INIT.boiler.table2.verboseExtrapolation,INIT.boiler.table2.verboseRead,INIT.condenser.h_in,INIT.condenser.h_out,INIT.condenser.isFilled,INIT.condenser.level_abs,INIT.condenser.m_flow_in,INIT.condenser.p_condenser,INIT.condenser.p_in,INIT.condenser.p_out,INIT.condenser.summary.inlet.h,INIT.condenser.summary.inlet.m_flow,INIT.condenser.summary.inlet.p,INIT.condenser.summary.outlet.h,INIT.condenser.summary.outlet.m_flow,INIT.condenser.summary.outlet.p,INIT.downComer_Delta_p_nom,INIT.downComer_feedWaterTank.CharLine_Delta_p_fric_P_target_[1,1],INIT.downComer_feedWaterTank.CharLine_Delta_p_fric_P_target_[1,2],INIT.downComer_feedWaterTank.CharLine_Delta_p_fric_P_target_[2,1],INIT.downComer_feedWaterTank.CharLine_Delta_p_fric_P_target_[2,2],INIT.downComer_feedWaterTank.Delta_p_fric,INIT.downComer_feedWaterTank.Delta_p_geo,INIT.downComer_feedWaterTank.Delta_p_nom,INIT.downComer_feedWaterTank.Delta_x[1],INIT.downComer_feedWaterTank.Delta_x[2],INIT.downComer_feedWaterTank.Delta_x[3],INIT.downComer_feedWaterTank.N_cv,INIT.downComer_feedWaterTank.frictionAtInlet,INIT.downComer_feedWaterTank.frictionAtOutlet,INIT.downComer_feedWaterTank.h_in,INIT.downComer_feedWaterTank.m_flow,INIT.downComer_feedWaterTank.p[1],INIT.downComer_feedWaterTank.p[2],INIT.downComer_feedWaterTank.p[3],INIT.downComer_feedWaterTank.p_in,INIT.downComer_feedWaterTank.p_out,INIT.downComer_feedWaterTank.summary.inlet.h,INIT.downComer_feedWaterTank.summary.inlet.m_flow,INIT.downComer_feedWaterTank.summary.inlet.p,INIT.downComer_feedWaterTank.summary.outlet.h,INIT.downComer_feedWaterTank.summary.outlet.m_flow,INIT.downComer_feedWaterTank.summary.outlet.p,INIT.downComer_feedWaterTank.table.columns[1],INIT.downComer_feedWaterTank.table.extrapolation,INIT.downComer_feedWaterTank.table.isCsvExt,INIT.downComer_feedWaterTank.table.n,INIT.downComer_feedWaterTank.table.nHeaderLines,INIT.downComer_feedWaterTank.table.smoothness,INIT.downComer_feedWaterTank.table.tableOnFile,INIT.downComer_feedWaterTank.table.table[1,1],INIT.downComer_feedWaterTank.table.table[1,2],INIT.downComer_feedWaterTank.table.table[2,1],INIT.downComer_feedWaterTank.table.table[2,2],INIT.downComer_feedWaterTank.table.u_max,INIT.downComer_feedWaterTank.table.u_min,INIT.downComer_feedWaterTank.table.verboseExtrapolation,INIT.downComer_feedWaterTank.table.verboseRead,INIT.downComer_feedWaterTank.z_in,INIT.downComer_feedWaterTank.z_out,INIT.downComer_z_in,INIT.downComer_z_out,INIT.efficiency_Pump_FW,INIT.efficiency_Pump_cond,INIT.efficiency_Pump_preheater_LP1,INIT.efficiency_Pump_preheater_LP3,INIT.efficiency_Turb_HP,INIT.efficiency_Turb_IP1,INIT.efficiency_Turb_IP2,INIT.efficiency_Turb_IP3,INIT.efficiency_Turb_LP1,INIT.efficiency_Turb_LP2,INIT.efficiency_Turb_LP3,INIT.efficiency_Turb_LP4,INIT.feedwatertank.h_cond_in,INIT.feedwatertank.h_cond_out,INIT.feedwatertank.h_tap_in1,INIT.feedwatertank.h_tap_in2,INIT.feedwatertank.isFilled,INIT.feedwatertank.level_abs,INIT.feedwatertank.m_flow_FW,INIT.feedwatertank.m_flow_cond,INIT.feedwatertank.m_flow_nom,INIT.feedwatertank.m_flow_tap1,INIT.feedwatertank.m_flow_tap2,INIT.feedwatertank.p_FWT,INIT.feedwatertank.p_FWT_nom,INIT.feedwatertank.p_FWT_out,INIT.feedwatertank.summary.inlet_cond.h,INIT.feedwatertank.summary.inlet_cond.m_flow,INIT.feedwatertank.summary.inlet_cond.p,INIT.feedwatertank.summary.inlet_tap1.h,INIT.feedwatertank.summary.inlet_tap1.m_flow,INIT.feedwatertank.summary.inlet_tap1.p,INIT.feedwatertank.summary.inlet_tap2.h,INIT.feedwatertank.summary.inlet_tap2.m_flow,INIT.feedwatertank.summary.inlet_tap2.p,INIT.feedwatertank.summary.outlet_cond.h,INIT.feedwatertank.summary.outlet_cond.m_flow,INIT.feedwatertank.summary.outlet_cond.p,INIT.join_HP.h1,INIT.join_HP.m_flow_1,INIT.join_HP.m_flow_2,INIT.join_HP.m_flow_3,INIT.join_HP.p,INIT.join_HP.summary.inlet.h,INIT.join_HP.summary.inlet.m_flow,INIT.join_HP.summary.inlet.p,INIT.join_HP.summary.outlet1.h,INIT.join_HP.summary.outlet1.m_flow,INIT.join_HP.summary.outlet1.p,INIT.join_HP.summary.outlet2.h,INIT.join_HP.summary.outlet2.m_flow,INIT.join_HP.summary.outlet2.p,INIT.join_LP_main.h1,INIT.join_LP_main.h2,INIT.join_LP_main.h3,INIT.join_LP_main.m_flow_1,INIT.join_LP_main.m_flow_2,INIT.join_LP_main.m_flow_3,INIT.join_LP_main.p,INIT.join_LP_main.summary.inlet1.h,INIT.join_LP_main.summary.inlet1.m_flow,INIT.join_LP_main.summary.inlet1.p,INIT.join_LP_main.summary.inlet2.h,INIT.join_LP_main.summary.inlet2.m_flow,INIT.join_LP_main.summary.inlet2.p,INIT.join_LP_main.summary.outlet.h,INIT.join_LP_main.summary.outlet.m_flow,INIT.join_LP_main.summary.outlet.p,INIT.join_preheater_LP3.h1,INIT.join_preheater_LP3.h2,INIT.join_preheater_LP3.h3,INIT.join_preheater_LP3.m_flow_1,INIT.join_preheater_LP3.m_flow_2,INIT.join_preheater_LP3.m_flow_3,INIT.join_preheater_LP3.p,INIT.join_preheater_LP3.summary.inlet1.h,INIT.join_preheater_LP3.summary.inlet1.m_flow,INIT.join_preheater_LP3.summary.inlet1.p,INIT.join_preheater_LP3.summary.inlet2.h,INIT.join_preheater_LP3.summary.inlet2.m_flow,INIT.join_preheater_LP3.summary.inlet2.p,INIT.join_preheater_LP3.summary.outlet.h,INIT.join_preheater_LP3.summary.outlet.m_flow,INIT.join_preheater_LP3.summary.outlet.p,INIT.m_flow_nom,INIT.mixerIP2.h1,INIT.mixerIP2.h2,INIT.mixerIP2.h3,INIT.mixerIP2.m_flow_1,INIT.mixerIP2.m_flow_2,INIT.mixerIP2.m_flow_3,INIT.mixerIP2.p,INIT.mixerIP2.summary.inlet1.h,INIT.mixerIP2.summary.inlet1.m_flow,INIT.mixerIP2.summary.inlet1.p,INIT.mixerIP2.summary.inlet2.h,INIT.mixerIP2.summary.inlet2.m_flow,INIT.mixerIP2.summary.inlet2.p,INIT.mixerIP2.summary.outlet.h,INIT.mixerIP2.summary.outlet.m_flow,INIT.mixerIP2.summary.outlet.p,INIT.mixer_condenser.h1,INIT.mixer_condenser.h2,INIT.mixer_condenser.h3,INIT.mixer_condenser.m_flow_1,INIT.mixer_condenser.m_flow_2,INIT.mixer_condenser.m_flow_3,INIT.mixer_condenser.p,INIT.mixer_condenser.summary.inlet1.h,INIT.mixer_condenser.summary.inlet1.m_flow,INIT.mixer_condenser.summary.inlet1.p,INIT.mixer_condenser.summary.inlet2.h,INIT.mixer_condenser.summary.inlet2.m_flow,INIT.mixer_condenser.summary.inlet2.p,INIT.mixer_condenser.summary.outlet.h,INIT.mixer_condenser.summary.outlet.m_flow,INIT.mixer_condenser.summary.outlet.p,INIT.p_FWT,INIT.p_LS_out_nom,INIT.p_RS_out_nom,INIT.p_condenser,INIT.preheater_HP.CharLine_m_flow_tap_P_target_[1,1],INIT.preheater_HP.CharLine_m_flow_tap_P_target_[1,2],INIT.preheater_HP.CharLine_m_flow_tap_P_target_[2,1],INIT.preheater_HP.CharLine_m_flow_tap_P_target_[2,2],INIT.preheater_HP.CharLine_p_tap_P_target_[1,1],INIT.preheater_HP.CharLine_p_tap_P_target_[1,2],INIT.preheater_HP.CharLine_p_tap_P_target_[2,1],INIT.preheater_HP.CharLine_p_tap_P_target_[2,2],INIT.preheater_HP.Delta_h_tap_out_sc,INIT.preheater_HP.h_cond_in,INIT.preheater_HP.h_cond_out,INIT.preheater_HP.h_tap_in,INIT.preheater_HP.h_tap_out,INIT.preheater_HP.isFilled,INIT.preheater_HP.level_abs,INIT.preheater_HP.m_flow_cond,INIT.preheater_HP.m_flow_tap,INIT.preheater_HP.m_flow_tap_nom,INIT.preheater_HP.p_cond,INIT.preheater_HP.p_tap,INIT.preheater_HP.p_tap_nom,INIT.preheater_HP.p_tap_out,INIT.preheater_HP.summary.inlet_cond.h,INIT.preheater_HP.summary.inlet_cond.m_flow,INIT.preheater_HP.summary.inlet_cond.p,INIT.preheater_HP.summary.inlet_tap.h,INIT.preheater_HP.summary.inlet_tap.m_flow,INIT.preheater_HP.summary.inlet_tap.p,INIT.preheater_HP.summary.outlet_cond.h,INIT.preheater_HP.summary.outlet_cond.m_flow,INIT.preheater_HP.summary.outlet_cond.p,INIT.preheater_HP.summary.outlet_tap.h,INIT.preheater_HP.summary.outlet_tap.m_flow,INIT.preheater_HP.summary.outlet_tap.p,INIT.preheater_HP.table1.columns[1],INIT.preheater_HP.table1.extrapolation,INIT.preheater_HP.table1.isCsvExt,INIT.preheater_HP.table1.n,INIT.preheater_HP.table1.nHeaderLines,INIT.preheater_HP.table1.smoothness,INIT.preheater_HP.table1.tableOnFile,INIT.preheater_HP.table1.table[1,1],INIT.preheater_HP.table1.table[1,2],INIT.preheater_HP.table1.table[2,1],INIT.preheater_HP.table1.table[2,2],INIT.preheater_HP.table1.u_max,INIT.preheater_HP.table1.u_min,INIT.preheater_HP.table1.verboseExtrapolation,INIT.preheater_HP.table1.verboseRead,INIT.preheater_HP.table2.columns[1],INIT.preheater_HP.table2.extrapolation,INIT.preheater_HP.table2.isCsvExt,INIT.preheater_HP.table2.n,INIT.preheater_HP.table2.nHeaderLines,INIT.preheater_HP.table2.smoothness,INIT.preheater_HP.table2.tableOnFile,INIT.preheater_HP.table2.table[1,1],INIT.preheater_HP.table2.table[1,2],INIT.preheater_HP.table2.table[2,1],INIT.preheater_HP.table2.table[2,2],INIT.preheater_HP.table2.u_max,INIT.preheater_HP.table2.u_min,INIT.preheater_HP.table2.verboseExtrapolation,INIT.preheater_HP.table2.verboseRead,INIT.preheater_HP_m_flow_tap,INIT.preheater_HP_p_tap,INIT.preheater_LP1.CharLine_m_flow_tap_P_target_[1,1],INIT.preheater_LP1.CharLine_m_flow_tap_P_target_[1,2],INIT.preheater_LP1.CharLine_m_flow_tap_P_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filterSimulationResults("ClaRa_dev_ClaRa.Examples.SteamCycle_01_res.mat", "/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ClaRa_dev_ClaRa.Examples.SteamCycle_01.diff.mat", vars={"split_LP3.p", "split_IP2.p", "preheater_LP4.tubes.p", "preheater_LP4.tubes.h", "preheater_LP4.shell.p_vap", "preheater_LP4.shell.h_vap", "preheater_LP4.shell.h_liq", "preheater_LP3.tubes.p", "preheater_LP3.shell.p_vap", "preheater_LP3.shell.h_liq", "preheater_LP2.tubes.p", "preheater_LP2.shell.p_vap", "preheater_LP2.shell.h_liq", "preheater_LP1.wall.U[3]", "preheater_LP1.wall.U[2]", "preheater_LP1.wall.U[1]", "preheater_LP1.tubes.p", "preheater_LP1.tubes.h", "preheater_LP1.shell.p_vap", "preheater_LP1.shell.h_vap", "preheater_LP1.shell.h_liq", "preheater_HP.tubes.p", "measurement.y", "join_preheater_LP3.p", "join_LP_main.p", "join_LP_main.h", "join_LP2.p", "join_LP1.p", "join_IP3.p", "feedWaterTank.volume.volume_vap", "feedWaterTank.volume.p_vap", "feedWaterTank.volume.h_vap", "downComer_feedWaterTank.p[3]", "downComer_feedWaterTank.p[2]", "downComer_feedWaterTank.p[1]", "condenser.tubes.h", "condenser.shell.volume_vap", "condenser.shell.p_vap", "condenser.shell.h_liq", "PI_preheater1.I.y", "PID_preheaterLP4.smoothPIDOutput.y_aux", "PID_preheaterLP4.smoothPIDInput.y_aux", "PID_preheaterLP4.resetValueP", "PID_preheaterLP4.I.y", "PID_preheaterLP3.smoothPIDOutput.y_aux", "PID_preheaterLP3.I.y", "PID_NDVW3.smoothPIDInput.y_aux", "PID_NDVW3.I.y"}, removeDescription=false) [Timeout 800] "" [Timeout remaining time 800] filterSimulationResults("/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/ReferenceFiles/ClaRa/ReferenceResults/ClaRa.Examples.SteamCycle_01.mat", "/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ClaRa_dev_ClaRa.Examples.SteamCycle_01.diff.ref.mat", vars={"split_LP3.p", "split_IP2.p", "preheater_LP4.tubes.p", "preheater_LP4.tubes.h", "preheater_LP4.shell.p_vap", "preheater_LP4.shell.h_vap", "preheater_LP4.shell.h_liq", "preheater_LP3.tubes.p", "preheater_LP3.shell.p_vap", "preheater_LP3.shell.h_liq", "preheater_LP2.tubes.p", "preheater_LP2.shell.p_vap", "preheater_LP2.shell.h_liq", "preheater_LP1.wall.U[3]", "preheater_LP1.wall.U[2]", "preheater_LP1.wall.U[1]", "preheater_LP1.tubes.p", "preheater_LP1.tubes.h", "preheater_LP1.shell.p_vap", "preheater_LP1.shell.h_vap", "preheater_LP1.shell.h_liq", "preheater_HP.tubes.p", "measurement.y", "join_preheater_LP3.p", "join_LP_main.p", "join_LP_main.h", "join_LP2.p", "join_LP1.p", "join_IP3.p", "feedWaterTank.volume.volume_vap", "feedWaterTank.volume.p_vap", "feedWaterTank.volume.h_vap", "downComer_feedWaterTank.p[3]", "downComer_feedWaterTank.p[2]", "downComer_feedWaterTank.p[1]", "condenser.tubes.h", "condenser.shell.volume_vap", "condenser.shell.p_vap", "condenser.shell.h_liq", "PI_preheater1.I.y", "PID_preheaterLP4.smoothPIDOutput.y_aux", "PID_preheaterLP4.smoothPIDInput.y_aux", "PID_preheaterLP4.resetValueP", "PID_preheaterLP4.I.y", "PID_preheaterLP3.smoothPIDOutput.y_aux", "PID_preheaterLP3.I.y", "PID_NDVW3.smoothPIDInput.y_aux", "PID_NDVW3.I.y"}, removeDescription=false) [Timeout 800] "" [Timeout remaining time 800] [Calling sys.exit(0), Time elapsed: 48.646937157958746]