[:1:1-1:32:writable] Error: Class GC_set_max_heap_size not found in scope (looking for a function or record). Notification: Performance of loadModel(Modelica): time 1.098/1.098, allocations: 111.2 MB / 118.2 MB, free: 15.64 MB / 106.7 MB Notification: Performance of FrontEnd - loaded program: time 0.1059/1.204, allocations: 27.5 MB / 145.7 MB, free: 4.172 MB / 122.7 MB Notification: Performance of FrontEnd - Absyn->SCode: time 0.1502/1.354, allocations: 25.16 MB / 170.9 MB, free: 1.816 MB / 138.7 MB Notification: Performance of FrontEnd - scodeFlatten: time 3.804/5.158, allocations: 1.613 GB / 1.78 GB, free: 36.39 MB / 234.7 MB Notification: Performance of FrontEnd - mkProgramGraph: time 0.0002625/5.158, allocations: 67.03 kB / 1.78 GB, free: 36.36 MB / 234.7 MB [/var/lib/hudson/slave/workspace/OpenModelica_TEST_LIBS/OpenModelica/OMCompiler/build/lib/omlibrary/Modelica 3.1/StateGraph.mo:1989:5-1989:55:writable] Warning: No corresponding 'inner' declaration found for component .Modelica.StateGraph.Interfaces.CompositeStepState controller.InitialStep1.stateGraphRoot declared as 'outer '. The existing 'inner' components are: .Modelica.Fluid.System system; defined in scope: Modelica.Fluid.Examples.AST_BatchPlant.BatchPlant_StandardWater. Referenced by 'outer' components: {V15.system, V12.system, B5.heatTransfer.system} Check if you have not misspelled the 'outer' component name. Please declare an 'inner' component with the same name in the top scope. Continuing flattening by only considering the 'outer' component declaration. [/var/lib/hudson/slave/workspace/OpenModelica_TEST_LIBS/OpenModelica/OMCompiler/build/lib/omlibrary/Modelica 3.1/StateGraph.mo:1989:5-1989:55:writable] Warning: No corresponding 'inner' declaration found for component .Modelica.StateGraph.Interfaces.CompositeStepState controller.Step1.stateGraphRoot declared as 'outer '. The existing 'inner' components are: .Modelica.Fluid.System system; defined in scope: Modelica.Fluid.Examples.AST_BatchPlant.BatchPlant_StandardWater. Referenced by 'outer' components: {V15.system, V12.system, B5.heatTransfer.system} Check if you have not misspelled the 'outer' component name. Please declare an 'inner' component with the same name in the top scope. Continuing flattening by only considering the 'outer' component declaration. [/var/lib/hudson/slave/workspace/OpenModelica_TEST_LIBS/OpenModelica/OMCompiler/build/lib/omlibrary/Modelica 3.1/StateGraph.mo:1989:5-1989:55:writable] Warning: No corresponding 'inner' declaration found for component .Modelica.StateGraph.Interfaces.CompositeStepState controller.Step2.stateGraphRoot declared as 'outer '. The existing 'inner' components are: .Modelica.Fluid.System system; defined in scope: Modelica.Fluid.Examples.AST_BatchPlant.BatchPlant_StandardWater. Referenced by 'outer' components: {V15.system, V12.system, B5.heatTransfer.system} Check if you have not misspelled the 'outer' component name. Please declare an 'inner' component with the same name in the top scope. Continuing flattening by only considering the 'outer' component declaration. [/var/lib/hudson/slave/workspace/OpenModelica_TEST_LIBS/OpenModelica/OMCompiler/build/lib/omlibrary/Modelica 3.1/StateGraph.mo:1989:5-1989:55:writable] Warning: No corresponding 'inner' declaration found for component .Modelica.StateGraph.Interfaces.CompositeStepState controller.Step3.stateGraphRoot declared as 'outer '. The existing 'inner' components are: .Modelica.Fluid.System system; defined in scope: Modelica.Fluid.Examples.AST_BatchPlant.BatchPlant_StandardWater. Referenced by 'outer' components: {V15.system, V12.system, B5.heatTransfer.system} Check if you have not misspelled the 'outer' component name. Please declare an 'inner' component with the same name in the top scope. Continuing flattening by only considering the 'outer' component declaration. [/var/lib/hudson/slave/workspace/OpenModelica_TEST_LIBS/OpenModelica/OMCompiler/build/lib/omlibrary/Modelica 3.1/StateGraph.mo:1989:5-1989:55:writable] Warning: No corresponding 'inner' declaration found for component .Modelica.StateGraph.Interfaces.CompositeStepState controller.Step4.stateGraphRoot declared as 'outer '. The existing 'inner' components are: .Modelica.Fluid.System system; defined in scope: Modelica.Fluid.Examples.AST_BatchPlant.BatchPlant_StandardWater. Referenced by 'outer' components: {V15.system, V12.system, B5.heatTransfer.system} Check if you have not misspelled the 'outer' component name. Please declare an 'inner' component with the same name in the top scope. Continuing flattening by only considering the 'outer' component declaration. [/var/lib/hudson/slave/workspace/OpenModelica_TEST_LIBS/OpenModelica/OMCompiler/build/lib/omlibrary/Modelica 3.1/StateGraph.mo:1989:5-1989:55:writable] Warning: No corresponding 'inner' declaration found for component .Modelica.StateGraph.Interfaces.CompositeStepState controller.Step5.stateGraphRoot declared as 'outer '. The existing 'inner' components are: .Modelica.Fluid.System system; defined in scope: Modelica.Fluid.Examples.AST_BatchPlant.BatchPlant_StandardWater. Referenced by 'outer' components: {V15.system, V12.system, B5.heatTransfer.system} Check if you have not misspelled the 'outer' component name. Please declare an 'inner' component with the same name in the top scope. Continuing flattening by only considering the 'outer' component declaration. [/var/lib/hudson/slave/workspace/OpenModelica_TEST_LIBS/OpenModelica/OMCompiler/build/lib/omlibrary/Modelica 3.1/StateGraph.mo:1989:5-1989:55:writable] Warning: No corresponding 'inner' declaration found for component .Modelica.StateGraph.Interfaces.CompositeStepState controller.Step6.stateGraphRoot declared as 'outer '. The existing 'inner' components are: .Modelica.Fluid.System system; defined in scope: Modelica.Fluid.Examples.AST_BatchPlant.BatchPlant_StandardWater. Referenced by 'outer' components: {V15.system, V12.system, B5.heatTransfer.system} Check if you have not misspelled the 'outer' component name. Please declare an 'inner' component with the same name in the top scope. Continuing flattening by only considering the 'outer' component declaration. [/var/lib/hudson/slave/workspace/OpenModelica_TEST_LIBS/OpenModelica/OMCompiler/build/lib/omlibrary/Modelica 3.1/StateGraph.mo:1989:5-1989:55:writable] Warning: No corresponding 'inner' declaration found for component .Modelica.StateGraph.Interfaces.CompositeStepState controller.Step7.stateGraphRoot declared as 'outer '. The existing 'inner' components are: .Modelica.Fluid.System system; defined in scope: Modelica.Fluid.Examples.AST_BatchPlant.BatchPlant_StandardWater. Referenced by 'outer' components: {V15.system, V12.system, B5.heatTransfer.system} Check if you have not misspelled the 'outer' component name. Please declare an 'inner' component with the same name in the top scope. Continuing flattening by only considering the 'outer' component declaration. [/var/lib/hudson/slave/workspace/OpenModelica_TEST_LIBS/OpenModelica/OMCompiler/build/lib/omlibrary/Modelica 3.1/StateGraph.mo:1989:5-1989:55:writable] Warning: No corresponding 'inner' declaration found for component .Modelica.StateGraph.Interfaces.CompositeStepState controller.Step8.stateGraphRoot declared as 'outer '. The existing 'inner' components are: .Modelica.Fluid.System system; defined in scope: Modelica.Fluid.Examples.AST_BatchPlant.BatchPlant_StandardWater. Referenced by 'outer' components: {V15.system, V12.system, B5.heatTransfer.system} Check if you have not misspelled the 'outer' component name. Please declare an 'inner' component with the same name in the top scope. Continuing flattening by only considering the 'outer' component declaration. [/var/lib/hudson/slave/workspace/OpenModelica_TEST_LIBS/OpenModelica/OMCompiler/build/lib/omlibrary/Modelica 3.1/StateGraph.mo:1989:5-1989:55:writable] Warning: No corresponding 'inner' declaration found for component .Modelica.StateGraph.Interfaces.CompositeStepState controller.Step9.stateGraphRoot declared as 'outer '. The existing 'inner' components are: .Modelica.Fluid.System system; defined in scope: Modelica.Fluid.Examples.AST_BatchPlant.BatchPlant_StandardWater. Referenced by 'outer' components: {V15.system, V12.system, B5.heatTransfer.system} Check if you have not misspelled the 'outer' component name. Please declare an 'inner' component with the same name in the top scope. Continuing flattening by only considering the 'outer' component declaration. [/var/lib/hudson/slave/workspace/OpenModelica_TEST_LIBS/OpenModelica/OMCompiler/build/lib/omlibrary/Modelica 3.1/StateGraph.mo:1989:5-1989:55:writable] Warning: No corresponding 'inner' declaration found for component .Modelica.StateGraph.Interfaces.CompositeStepState controller.Step10.stateGraphRoot declared as 'outer '. The existing 'inner' components are: .Modelica.Fluid.System system; defined in scope: Modelica.Fluid.Examples.AST_BatchPlant.BatchPlant_StandardWater. Referenced by 'outer' components: {V15.system, V12.system, B5.heatTransfer.system} Check if you have not misspelled the 'outer' component name. Please declare an 'inner' component with the same name in the top scope. Continuing flattening by only considering the 'outer' component declaration. [/var/lib/hudson/slave/workspace/OpenModelica_TEST_LIBS/OpenModelica/OMCompiler/build/lib/omlibrary/Modelica 3.1/StateGraph.mo:1989:5-1989:55:writable] Warning: No corresponding 'inner' declaration found for component .Modelica.StateGraph.Interfaces.CompositeStepState controller.Step11.stateGraphRoot declared as 'outer '. The existing 'inner' components are: .Modelica.Fluid.System system; defined in scope: Modelica.Fluid.Examples.AST_BatchPlant.BatchPlant_StandardWater. Referenced by 'outer' components: {V15.system, V12.system, B5.heatTransfer.system} Check if you have not misspelled the 'outer' component name. Please declare an 'inner' component with the same name in the top scope. Continuing flattening by only considering the 'outer' component declaration. [/var/lib/hudson/slave/workspace/OpenModelica_TEST_LIBS/OpenModelica/OMCompiler/build/lib/omlibrary/Modelica 3.1/StateGraph.mo:1989:5-1989:55:writable] Warning: No corresponding 'inner' declaration found for component .Modelica.StateGraph.Interfaces.CompositeStepState controller.Step12.stateGraphRoot declared as 'outer '. The existing 'inner' components are: .Modelica.Fluid.System system; defined in scope: Modelica.Fluid.Examples.AST_BatchPlant.BatchPlant_StandardWater. Referenced by 'outer' components: {V15.system, V12.system, B5.heatTransfer.system} Check if you have not misspelled the 'outer' component name. Please declare an 'inner' component with the same name in the top scope. Continuing flattening by only considering the 'outer' component declaration. [/var/lib/hudson/slave/workspace/OpenModelica_TEST_LIBS/OpenModelica/OMCompiler/build/lib/omlibrary/Modelica 3.1/StateGraph.mo:1989:5-1989:55:writable] Warning: No corresponding 'inner' declaration found for component .Modelica.StateGraph.Interfaces.CompositeStepState controller.Step13.stateGraphRoot declared as 'outer '. The existing 'inner' components are: .Modelica.Fluid.System system; defined in scope: Modelica.Fluid.Examples.AST_BatchPlant.BatchPlant_StandardWater. Referenced by 'outer' components: {V15.system, V12.system, B5.heatTransfer.system} Check if you have not misspelled the 'outer' component name. Please declare an 'inner' component with the same name in the top scope. Continuing flattening by only considering the 'outer' component declaration. [/var/lib/hudson/slave/workspace/OpenModelica_TEST_LIBS/OpenModelica/OMCompiler/build/lib/omlibrary/Modelica 3.1/StateGraph.mo:1989:5-1989:55:writable] Warning: No corresponding 'inner' declaration found for component .Modelica.StateGraph.Interfaces.CompositeStepState controller.Step14.stateGraphRoot declared as 'outer '. The existing 'inner' components are: .Modelica.Fluid.System system; defined in scope: Modelica.Fluid.Examples.AST_BatchPlant.BatchPlant_StandardWater. Referenced by 'outer' components: {V15.system, V12.system, B5.heatTransfer.system} Check if you have not misspelled the 'outer' component name. Please declare an 'inner' component with the same name in the top scope. Continuing flattening by only considering the 'outer' component declaration. Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 2283 * Number of variables: 2283 Notification: Performance of Generate backend data structure: time 20.86/26.02, allocations: 3.625 GB / 5.405 GB, free: 20.46 MB / 0.5105 GB Notification: Performance of prepare preOptimizeDAE: time 5.096e-05/26.02, allocations: 18.09 kB / 5.405 GB, free: 20.45 MB / 0.5105 GB Notification: Performance of preOpt normalInlineFunction (simulation): time 0.008055/26.03, allocations: 1.112 MB / 5.406 GB, free: 19.92 MB / 0.5105 GB Notification: Performance of preOpt evaluateParameters (simulation): time 0.02969/26.06, allocations: 6.096 MB / 5.412 GB, free: 18.88 MB / 0.5105 GB Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.002021/26.06, allocations: 1.118 MB / 5.413 GB, free: 18.11 MB / 0.5105 GB Notification: Performance of preOpt expandDerOperator (simulation): time 0.004882/26.07, allocations: 0.5155 MB / 5.414 GB, free: 18.1 MB / 0.5105 GB Notification: Performance of preOpt removeEqualFunctionCalls (simulation): time 0.04245/26.11, allocations: 11.97 MB / 5.425 GB, free: 18.06 MB / 0.5105 GB Notification: Performance of preOpt clockPartitioning (simulation): time 0.04981/26.16, allocations: 12.02 MB / 5.437 GB, free: 16.24 MB / 0.5105 GB Notification: Performance of preOpt findStateOrder (simulation): time 0.0007203/26.16, allocations: 26.88 kB / 5.437 GB, free: 16.24 MB / 0.5105 GB Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.004509/26.16, allocations: 27.08 kB / 5.437 GB, free: 16.24 MB / 0.5105 GB Notification: Performance of preOpt inlineArrayEqn (simulation): time 0.001056/26.17, allocations: 0.5434 MB / 5.438 GB, free: 16.22 MB / 0.5105 GB Notification: Performance of preOpt removeSimpleEquations (simulation): time 1.276/27.44, allocations: 85.18 MB / 5.521 GB, free: 67.62 MB / 0.5418 GB Notification: Performance of preOpt comSubExp (simulation): time 0.0234/27.47, allocations: 5.297 MB / 5.526 GB, free: 67.59 MB / 0.5418 GB Notification: Performance of preOpt resolveLoops (simulation): time 0.01711/27.48, allocations: 4.912 MB / 5.531 GB, free: 67.55 MB / 0.5418 GB Notification: Performance of preOpt evalFunc (simulation): time 0.7493/28.23, allocations: 160.5 MB / 5.688 GB, free: 20.34 MB / 0.5887 GB Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 0.02166/28.25, allocations: 5.186 MB / 5.693 GB, free: 20.18 MB / 0.5887 GB Notification: Performance of pre-optimization done (n=823): time 3.65e-05/28.25, allocations: 0 / 5.693 GB, free: 20.18 MB / 0.5887 GB Notification: Performance of matching and sorting (n=897): time 0.3741/28.63, allocations: 44.4 MB / 5.736 GB, free: 8.938 MB / 0.5887 GB Notification: Performance of inlineWhenForInitialization (initialization): time 0.0003927/28.63, allocations: 290.9 kB / 5.736 GB, free: 8.621 MB / 0.5887 GB Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.01452/28.64, allocations: 3.62 MB / 5.74 GB, free: 6.457 MB / 0.5887 GB Notification: Performance of collectPreVariables (initialization): time 0.003331/28.65, allocations: 97.28 kB / 5.74 GB, free: 6.391 MB / 0.5887 GB Notification: Performance of collectInitialEqns (initialization): time 0.005291/28.65, allocations: 2.714 MB / 5.743 GB, free: 4.562 MB / 0.5887 GB Notification: Performance of collectInitialBindings (initialization): time 0.007876/28.66, allocations: 2.817 MB / 5.745 GB, free: 2.344 MB / 0.5887 GB Notification: Performance of simplifyInitialFunctions (initialization): time 0.003597/28.66, allocations: 0 / 5.745 GB, free: 2.344 MB / 0.5887 GB Notification: Performance of setup shared object (initialization): time 0.001543/28.66, allocations: 0.7045 MB / 5.746 GB, free: 1.922 MB / 0.5887 GB Notification: Performance of preBalanceInitialSystem (initialization): time 0.0249/28.69, allocations: 5.054 MB / 5.751 GB, free: 0 / 0.5887 GB Notification: Performance of partitionIndependentBlocks (initialization): time 0.5691/29.26, allocations: 6.983 MB / 5.758 GB, free: 121.5 MB / 0.5887 GB Notification: The given system is mixed-determined. [index = 2] Notification: Performance of analyzeInitialSystem (initialization): time 0.3516/29.61, allocations: 40.49 MB / 5.797 GB, free: 120.3 MB / 0.5887 GB Notification: Performance of solveInitialSystemEqSystem (initialization): time 0.0001812/29.61, allocations: 26.41 kB / 5.797 GB, free: 120.3 MB / 0.5887 GB Notification: Performance of matching and sorting (n=1336) (initialization): time 0.15/29.76, allocations: 21.6 MB / 5.818 GB, free: 119.8 MB / 0.5887 GB Notification: Performance of prepare postOptimizeDAE: time 2.503e-05/29.76, allocations: 6.062 kB / 5.818 GB, free: 119.8 MB / 0.5887 GB Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.0001557/29.76, allocations: 61.22 kB / 5.818 GB, free: 119.8 MB / 0.5887 GB Notification: Performance of postOpt tearingSystem (initialization): time 0.01683/29.78, allocations: 2.949 MB / 5.821 GB, free: 119.5 MB / 0.5887 GB Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.02041/29.8, allocations: 2.254 MB / 5.824 GB, free: 119.5 MB / 0.5887 GB Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.04612/29.84, allocations: 27.26 MB / 5.85 GB, free: 99.18 MB / 0.5887 GB Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.02406/29.87, allocations: 0.8243 MB / 5.851 GB, free: 99.18 MB / 0.5887 GB Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.00483/29.87, allocations: 0.5396 MB / 5.852 GB, free: 99.18 MB / 0.5887 GB Warning: Assuming fixed start value for the following 38 variables: volume4.medium.h:VARIABLE(min = max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, -100000000.0))))))))))))))))))))) max = min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, 100000000.0))))))))))))))))))))) start = volume4.h_start unit = "J/kg" nominal = 1000000.0 stateSelect=StateSelect.prefer ) "Specific enthalpy of medium" type: Real volume4.medium.p:VARIABLE(min = max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, 2000.0))))))))))))))))))) max = min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, 1000000000.0))))))))))))))))))) start = 101325.0 unit = "Pa" nominal = 100000.0 stateSelect=StateSelect.prefer ) "Absolute pressure of medium" type: Real B6.level:VARIABLE(min = 0.0 start = B6.level_start unit = "m" stateSelect=StateSelect.prefer ) "Fluid level in the tank" type: Real B6.medium.h:VARIABLE(min = max(-100000000.0, max(-100000000.0, max(-100000000.0, -100000000.0))) max = min(100000000.0, min(100000000.0, min(100000000.0, 100000000.0))) start = B6.h_start unit = "J/kg" nominal = 1000000.0 stateSelect=StateSelect.prefer ) "Specific enthalpy of medium" type: Real pipePump2B2.mediums[2].h:VARIABLE(min = max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, -100000000.0)))))) max = min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, 100000000.0)))))) start = pipePump2B2.h_start unit = "J/kg" nominal = 1000000.0 stateSelect=StateSelect.prefer ) "Specific enthalpy of medium" type: Real [2] pipePump2B2.mediums[2].p:VARIABLE(min = max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, 2000.0))))))))) max = min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, 1000000000.0))))))))) start = 101325.0 unit = "Pa" nominal = 100000.0 stateSelect=StateSelect.prefer ) "Absolute pressure of medium" type: Real [2] pipePump2B2.mediums[1].h:VARIABLE(min = max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, -100000000.0)))))) max = min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, 100000000.0)))))) start = pipePump2B2.h_start unit = "J/kg" nominal = 1000000.0 stateSelect=StateSelect.prefer ) "Specific enthalpy of medium" type: Real [2] pipePump2B2.mediums[1].p:VARIABLE(min = max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, 2000.0))))))))) max = min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, 1000000000.0))))))))) start = 101325.0 unit = "Pa" nominal = 100000.0 stateSelect=StateSelect.prefer ) "Absolute pressure of medium" type: Real [2] pipePump1B1.mediums[2].h:VARIABLE(min = max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, -100000000.0)))))) max = min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, 100000000.0)))))) start = pipePump1B1.h_start unit = "J/kg" nominal = 1000000.0 stateSelect=StateSelect.prefer ) "Specific enthalpy of medium" type: Real [2] pipePump1B1.mediums[2].p:VARIABLE(min = max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, 2000.0))))))))) max = min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, 1000000000.0))))))))) start = 101325.0 unit = "Pa" nominal = 100000.0 stateSelect=StateSelect.prefer ) "Absolute pressure of medium" type: Real [2] pipePump1B1.mediums[1].h:VARIABLE(min = max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, -100000000.0)))))) max = min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, 100000000.0)))))) start = pipePump1B1.h_start unit = "J/kg" nominal = 1000000.0 stateSelect=StateSelect.prefer ) "Specific enthalpy of medium" type: Real [2] pipePump1B1.mediums[1].p:VARIABLE(min = max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, 2000.0))))))))) max = min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, 1000000000.0))))))))) start = 101325.0 unit = "Pa" nominal = 100000.0 stateSelect=StateSelect.prefer ) "Absolute pressure of medium" type: Real [2] pipeB1B2.mediums[2].h:VARIABLE(min = max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, -100000000.0)))))) max = min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, 100000000.0)))))) start = pipeB1B2.h_start unit = "J/kg" nominal = 1000000.0 stateSelect=StateSelect.prefer ) "Specific enthalpy of medium" type: Real [2] pipeB1B2.mediums[2].p:VARIABLE(min = max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, 2000.0))))))))) max = min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, 1000000000.0))))))))) start = 101325.0 unit = "Pa" nominal = 100000.0 stateSelect=StateSelect.prefer ) "Absolute pressure of medium" type: Real [2] pipeB1B2.mediums[1].h:VARIABLE(min = max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, -100000000.0)))))) max = min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, 100000000.0)))))) start = pipeB1B2.h_start unit = "J/kg" nominal = 1000000.0 stateSelect=StateSelect.prefer ) "Specific enthalpy of medium" type: Real [2] pipeB1B2.mediums[1].p:VARIABLE(min = max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, 2000.0))))))))) max = min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, 1000000000.0))))))))) start = 101325.0 unit = "Pa" nominal = 100000.0 stateSelect=StateSelect.prefer ) "Absolute pressure of medium" type: Real [2] B7.level:VARIABLE(min = 0.0 start = B7.level_start unit = "m" stateSelect=StateSelect.prefer ) "Fluid level in the tank" type: Real B7.medium.h:VARIABLE(min = max(-100000000.0, max(-100000000.0, max(-100000000.0, -100000000.0))) max = min(100000000.0, min(100000000.0, min(100000000.0, 100000000.0))) start = B7.h_start unit = "J/kg" nominal = 1000000.0 stateSelect=StateSelect.prefer ) "Specific enthalpy of medium" type: Real B4.level:VARIABLE(min = 0.0 start = B4.level_start unit = "m" stateSelect=StateSelect.prefer ) "Fluid level in the tank" type: Real B4.medium.h:VARIABLE(min = max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, -100000000.0)))) max = min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, 100000000.0)))) start = B4.h_start unit = "J/kg" nominal = 1000000.0 stateSelect=StateSelect.prefer ) "Specific enthalpy of medium" type: Real B3.level:VARIABLE(min = 0.0 start = B3.level_start unit = "m" stateSelect=StateSelect.prefer ) "Fluid level in the tank" type: Real B3.medium.h:VARIABLE(min = max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, -100000000.0)))))))) max = min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, 100000000.0)))))))) start = B3.h_start unit = "J/kg" nominal = 1000000.0 stateSelect=StateSelect.prefer ) "Specific enthalpy of medium" type: Real B2.level:VARIABLE(min = 0.0 start = B2.level_start unit = "m" stateSelect=StateSelect.prefer ) "Fluid level in the tank" type: Real B2.medium.h:VARIABLE(min = max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, -100000000.0))))) max = min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, 100000000.0))))) start = B2.h_start unit = "J/kg" nominal = 1000000.0 stateSelect=StateSelect.prefer ) "Specific enthalpy of medium" type: Real B1.level:VARIABLE(min = 0.0 start = B1.level_start unit = "m" stateSelect=StateSelect.prefer ) "Fluid level in the tank" type: Real B1.medium.h:VARIABLE(min = max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, -100000000.0))))) max = min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, 100000000.0))))) start = B1.h_start unit = "J/kg" nominal = 1000000.0 stateSelect=StateSelect.prefer ) "Specific enthalpy of medium" type: Real P2.medium.h:VARIABLE(min = max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, -100000000.0)))))) max = min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, 100000000.0)))))) start = P2.h_start unit = "J/kg" nominal = 1000000.0 stateSelect=StateSelect.prefer ) "Specific enthalpy of medium" type: Real P2.medium.p:VARIABLE(min = max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, 2000.0)))))) max = min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, 1000000000.0)))))) start = P2.p_start unit = "Pa" nominal = 100000.0 stateSelect=StateSelect.prefer ) "Absolute pressure of medium" type: Real P1.medium.h:VARIABLE(min = max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, -100000000.0)))))) max = min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, 100000000.0)))))) start = P1.h_start unit = "J/kg" nominal = 1000000.0 stateSelect=StateSelect.prefer ) "Specific enthalpy of medium" type: Real P1.medium.p:VARIABLE(min = max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, 2000.0)))))) max = min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, 1000000000.0)))))) start = P1.p_start unit = "Pa" nominal = 100000.0 stateSelect=StateSelect.prefer ) "Absolute pressure of medium" type: Real volume5.medium.h:VARIABLE(min = max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, max(-100000000.0, -100000000.0)))))))))))) max = min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, 100000000.0)))))))))))) start = volume5.h_start unit = "J/kg" nominal = 1000000.0 stateSelect=StateSelect.prefer ) "Specific enthalpy of medium" type: Real volume5.medium.p:VARIABLE(min = max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, 2000.0))))))))))) max = min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, 1000000000.0))))))))))) start = 101325.0 unit = "Pa" nominal = 100000.0 stateSelect=StateSelect.prefer ) "Absolute pressure of medium" type: Real controller.Transition7.t_start:DISCRETE(unit = "s" fixed = false protected = true ) "Time instant at which the transition would fire, if waitTime would be zero" type: Real controller.Transition3.t_start:DISCRETE(unit = "s" fixed = false protected = true ) "Time instant at which the transition would fire, if waitTime would be zero" type: Real controller.Transition1.t_start:DISCRETE(unit = "s" fixed = false protected = true ) "Time instant at which the transition would fire, if waitTime would be zero" type: Real B5.InnerTankTop[1].m_flow_negative:DISCRETE(start = true fixed = false ) "true= massflow out of tank" type: Boolean [1] B5.InnerTankSide[1].m_flow_negative:DISCRETE(start = true fixed = false ) "true= massflow out of tank" type: Boolean [1] B5.InnerTankBottom[1].m_flow_negative:DISCRETE(start = true fixed = false ) "true= massflow out of tank" type: Boolean [1] Warning: Assuming redundant initial conditions for the following 2 initial equations: $PRE.P1_on.y = 0.0 $PRE.P2_on.y = P2_on.y Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: B2.Wb_flow:VARIABLE(unit = "W" ) "Work flow across boundaries or source term" type: Real Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: $DER.B1.heatTransfer.states[1].d:DUMMY_DER(fixed = false ) "density" type: Real [1] $DER.B1.medium.u:DUMMY_DER(fixed = false ) "Specific internal energy of medium" type: Real Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: $DER.B3.heatTransfer.states[1].d:DUMMY_DER(fixed = false ) "density" type: Real [1] $DER.B3.medium.u:DUMMY_DER(fixed = false ) "Specific internal energy of medium" type: Real Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: $DER.B4.heatTransfer.states[1].d:DUMMY_DER(fixed = false ) "density" type: Real [1] $DER.B4.medium.u:DUMMY_DER(fixed = false ) "Specific internal energy of medium" type: Real Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: $DER.B7.heatTransfer.states[1].d:DUMMY_DER(fixed = false ) "density" type: Real [1] $DER.B7.medium.u:DUMMY_DER(fixed = false ) "Specific internal energy of medium" type: Real Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: $DER.B6.heatTransfer.states[1].d:DUMMY_DER(fixed = false ) "density" type: Real [1] $DER.B6.medium.u:DUMMY_DER(fixed = false ) "Specific internal energy of medium" type: Real Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: $DER.B5.V:DUMMY_DER(fixed = false ) "Actual tank volume" type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 290 * Number of states: 0 () * Number of discrete variables: 315 ($PRE.controller.Transition1.enableFire,$PRE.controller.Transition2.enableFire,$PRE.controller.Transition3.enableFire,$PRE.controller.Transition4.enableFire,$PRE.controller.Transition5.enableFire,$PRE.controller.Transition6.enableFire,$PRE.controller.Transition7.enableFire,$PRE.controller.Transition8.enableFire,$PRE.controller.Transition9.enableFire,$PRE.controller.Transition10.enableFire,$PRE.controller.Transition11.enableFire,$PRE.controller.Transition12.enableFire,$PRE.controller.Transition13.enableFire,$PRE.controller.TransitionWithSignal1.enableFire,controller.InitialStep1.stateGraphRoot.resume,controller.InitialStep1.stateGraphRoot.suspend,controller.Step1.stateGraphRoot.resume,controller.Step1.stateGraphRoot.suspend,controller.Step2.stateGraphRoot.resume,controller.Step2.stateGraphRoot.suspend,controller.Step3.stateGraphRoot.resume,controller.Step3.stateGraphRoot.suspend,controller.Step4.stateGraphRoot.resume,controller.Step4.stateGraphRoot.suspend,controller.Step5.stateGraphRoot.resume,controller.Step5.stateGraphRoot.suspend,controller.Step6.stateGraphRoot.resume,controller.Step6.stateGraphRoot.suspend,controller.Step7.stateGraphRoot.resume,controller.Step7.stateGraphRoot.suspend,controller.Step8.stateGraphRoot.resume,controller.Step8.stateGraphRoot.suspend,controller.Step9.stateGraphRoot.resume,controller.Step9.stateGraphRoot.suspend,controller.Step10.stateGraphRoot.resume,controller.Step10.stateGraphRoot.suspend,controller.Step11.stateGraphRoot.resume,controller.Step11.stateGraphRoot.suspend,controller.Step12.stateGraphRoot.resume,controller.Step12.stateGraphRoot.suspend,controller.Step13.stateGraphRoot.resume,controller.Step13.stateGraphRoot.suspend,controller.Step14.stateGraphRoot.resume,controller.Step14.stateGraphRoot.suspend,controller.actuators.V21,controller.actuators.V19,controller.actuators.V10,controller.actuators.V4,controller.actuators.V2,pipeB7Pump.flowModel.states[2].phase,pipeB7Pump.flowModel.states[1].phase,pipeB6Pump.flowModel.states[2].phase,pipeB6Pump.flowModel.states[1].phase,pipeB1B1.flowModel.states[2].phase,pipeB1B1.flowModel.states[1].phase,pipeB2B3.flowModel.states[2].phase,pipeB2B3.flowModel.states[1].phase,pipeB1B3.flowModel.states[2].phase,pipeB1B3.flowModel.states[1].phase,P2.state_a.phase,P1.state_a.phase,V18.state_b.phase,V18.state_a.phase,V21.state_b.phase,V21.state_a.phase,V10.state_b.phase,V10.state_a.phase,V19.state_b.phase,V19.state_a.phase,V20.state_b.phase,V20.state_a.phase,V25.state_b.phase,V25.state_a.phase,V24.state_b.phase,V24.state_a.phase,V5.state_b.phase,V5.state_a.phase,V22.state_b.phase,V22.state_a.phase,V1.state_b.phase,V1.state_a.phase,V23.state_b.phase,V23.state_a.phase,V6.state_b.phase,V6.state_a.phase,V3.state_b.phase,V3.state_a.phase,V4.state_b.phase,V4.state_a.phase,V2.state_b.phase,V2.state_a.phase,V9.state_b.phase,V9.state_a.phase,V8.state_b.phase,V8.state_a.phase,V11.state_b.phase,V11.state_a.phase,controller.Transition7.condition,controller.Transition3.condition,controller.Transition1.condition,V15.state_b.phase,V15.state_a.phase,V12.state_b.phase,V12.state_a.phase,$whenCondition7,$whenCondition6,$whenCondition5,$whenCondition4,$whenCondition3,$whenCondition2,$whenCondition1,$PRE.B5.InnerTankTop[1].m_flow_negative,B5.InnerTankTop[1].m_flow_negative,$PRE.B5.InnerTankSide[1].m_flow_negative,B5.InnerTankSide[1].m_flow_negative,$PRE.B5.InnerTankBottom[1].m_flow_negative,B5.InnerTankBottom[1].m_flow_negative,B5.heatTransfer.states[1].phase,$PRE.controller.InitialStep1.localActive,controller.InitialStep1.localActive,$PRE.controller.InitialStep1.newActive,controller.InitialStep1.newActive,$PRE.controller.InitialStep1.oldActive,controller.InitialStep1.oldActive,controller.InitialStep1.active,controller.Transition1.enableFire,controller.Transition1.fire,$PRE.controller.Transition1.t_start,controller.Transition1.t_start,$PRE.controller.Step1.localActive,controller.Step1.localActive,$PRE.controller.Step1.newActive,controller.Step1.newActive,$PRE.controller.Step1.oldActive,controller.Step1.oldActive,controller.Step1.active,controller.Transition2.enableFire,controller.Transition2.condition,$PRE.controller.Step2.localActive,controller.Step2.localActive,$PRE.controller.Step2.newActive,controller.Step2.newActive,$PRE.controller.Step2.oldActive,controller.Step2.oldActive,controller.Step2.active,controller.Transition3.enableFire,controller.Transition3.fire,$PRE.controller.Transition3.t_start,controller.Transition3.t_start,$PRE.controller.Step3.localActive,controller.Step3.localActive,$PRE.controller.Step3.newActive,controller.Step3.newActive,$PRE.controller.Step3.oldActive,controller.Step3.oldActive,controller.Step3.active,controller.Transition4.enableFire,controller.Transition4.condition,$PRE.controller.Step4.localActive,controller.Step4.localActive,$PRE.controller.Step4.newActive,controller.Step4.newActive,$PRE.controller.Step4.oldActive,controller.Step4.oldActive,controller.Step4.active,controller.Transition5.enableFire,$PRE.controller.Step5.localActive,controller.Step5.localActive,$PRE.controller.Step5.newActive,controller.Step5.newActive,$PRE.controller.Step5.oldActive,controller.Step5.oldActive,controller.Step5.active,controller.Transition6.enableFire,controller.Transition6.condition,$PRE.controller.Step6.localActive,controller.Step6.localActive,$PRE.controller.Step6.newActive,controller.Step6.newActive,$PRE.controller.Step6.oldActive,controller.Step6.oldActive,controller.Step6.active,controller.Transition7.enableFire,controller.Transition7.fire,$PRE.controller.Transition7.t_start,controller.Transition7.t_start,controller.Parallel1.inPort.occupied,controller.Parallel1.outPort.available,$PRE.controller.Step7.localActive,controller.Step7.localActive,$PRE.controller.Step7.newActive,controller.Step7.newActive,$PRE.controller.Step7.oldActive,controller.Step7.oldActive,controller.Step7.active,$PRE.controller.Step8.localActive,controller.Step8.localActive,$PRE.controller.Step8.newActive,controller.Step8.newActive,$PRE.controller.Step8.oldActive,controller.Step8.oldActive,controller.Step8.active,$PRE.controller.Step9.localActive,controller.Step9.localActive,$PRE.controller.Step9.newActive,controller.Step9.newActive,$PRE.controller.Step9.oldActive,controller.Step9.oldActive,controller.Step9.active,$PRE.controller.Step10.localActive,controller.Step10.localActive,$PRE.controller.Step10.newActive,controller.Step10.newActive,$PRE.controller.Step10.oldActive,controller.Step10.oldActive,controller.Step10.active,$PRE.controller.Step11.localActive,controller.Step11.localActive,$PRE.controller.Step11.newActive,controller.Step11.newActive,$PRE.controller.Step11.oldActive,controller.Step11.oldActive,controller.Step11.active,$PRE.controller.Step12.localActive,controller.Step12.localActive,$PRE.controller.Step12.newActive,controller.Step12.newActive,$PRE.controller.Step12.oldActive,controller.Step12.oldActive,controller.Step12.active,$PRE.controller.Step13.localActive,controller.Step13.localActive,$PRE.controller.Step13.newActive,controller.Step13.newActive,$PRE.controller.Step13.oldActive,controller.Step13.oldActive,controller.Step13.active,$PRE.controller.Step14.localActive,controller.Step14.localActive,$PRE.controller.Step14.newActive,controller.Step14.newActive,$PRE.controller.Step14.oldActive,controller.Step14.oldActive,controller.Step14.active,controller.Transition8.enableFire,controller.Transition9.enableFire,controller.Transition9.condition,controller.Transition10.enableFire,controller.Transition10.condition,controller.Transition11.enableFire,controller.Transition11.condition,controller.Transition12.enableFire,controller.Transition12.condition,controller.Transition13.enableFire,controller.Transition13.condition,controller.T5_idle,controller.T7_idle,controller.TransitionWithSignal1.enableFire,controller.BooleanExpression1.y,volume5.medium.phase,P1.heatTransfer.states[1].phase,P2.heatTransfer.states[1].phase,B1.heatTransfer.states[1].phase,$PRE.B1.ports_m_flow_out[1],B1.ports_m_flow_out[1],$PRE.B1.aboveLevel[1],B1.aboveLevel[1],P1_on.endValue,P1_on.rate,P1_on.T,P2_on.endValue,P2_on.rate,P2_on.T,B2.heatTransfer.states[1].phase,$PRE.B2.ports_m_flow_out[1],B2.ports_m_flow_out[1],$PRE.B2.aboveLevel[1],B2.aboveLevel[1],B3.heatTransfer.states[1].phase,$PRE.B3.ports_m_flow_out[1],B3.ports_m_flow_out[1],$PRE.B3.ports_m_flow_out[2],B3.ports_m_flow_out[2],$PRE.B3.aboveLevel[1],B3.aboveLevel[1],$PRE.B3.aboveLevel[2],B3.aboveLevel[2],B4.heatTransfer.states[1].phase,$PRE.B4.ports_m_flow_out[1],B4.ports_m_flow_out[1],$PRE.B4.aboveLevel[1],B4.aboveLevel[1],B7.heatTransfer.states[1].phase,$PRE.B7.ports_m_flow_out[1],B7.ports_m_flow_out[1],$PRE.B7.aboveLevel[1],B7.aboveLevel[1],pipeB1B2.statesFM[1].phase,pipeB1B2.statesFM[2].phase,pipePump1B1.statesFM[1].phase,pipePump1B1.statesFM[2].phase,pipePump2B2.statesFM[1].phase,pipePump2B2.statesFM[2].phase,B6.heatTransfer.states[1].phase,$PRE.B6.ports_m_flow_out[1],B6.ports_m_flow_out[1],$PRE.B6.aboveLevel[1],B6.aboveLevel[1],volume4.medium.phase,pipePump2B2.state_b.phase,pipePump2B2.state_a.phase,pipePump1B1.state_b.phase,pipePump1B1.state_a.phase,pipeB1B2.state_b.phase,pipeB1B2.state_a.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (1196): * Single equations (assignments): 1165 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 31 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 2 {(1,100.0%) 6,(1,100.0%) 6} * Non-linear torn systems: 29 {2 2,2 4,2 4,1 2,2 4,2 2,1 1,2 4,2 4,2 8,2 4,2 8,1 2,1 1,1 1,2 6,1 2,2 12,1 1,1 1,1 1,1 1,1 1,2 6,2 16,1 1,1 1,1 1,2 12} Notification: Performance of prepare postOptimizeDAE: time 0.009692/29.88, allocations: 1.503 MB / 5.853 GB, free: 98.91 MB / 0.5887 GB Notification: Performance of postOpt lateInlineFunction (simulation): time 0.01093/29.89, allocations: 1.874 MB / 5.855 GB, free: 98.91 MB / 0.5887 GB Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.1783/30.07, allocations: 37.05 MB / 5.891 GB, free: 96.71 MB / 0.5887 GB Notification: Performance of postOpt inlineArrayEqn (simulation): time 0.001107/30.07, allocations: 349.5 kB / 5.891 GB, free: 96.71 MB / 0.5887 GB Notification: Performance of postOpt constantLinearSystem (simulation): time 0.0002005/30.07, allocations: 5.062 kB / 5.891 GB, free: 96.71 MB / 0.5887 GB Notification: Performance of postOpt simplifysemiLinear (simulation): time 0.1197/30.19, allocations: 29.27 MB / 5.92 GB, free: 87.89 MB / 0.5887 GB Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.7048/30.9, allocations: 49.11 MB / 5.968 GB, free: 117.8 MB / 0.5887 GB Notification: Performance of postOpt simplifyComplexFunction (simulation): time 0.000245/30.9, allocations: 3.844 kB / 5.968 GB, free: 117.8 MB / 0.5887 GB Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.01729/30.92, allocations: 1.832 MB / 5.97 GB, free: 117.8 MB / 0.5887 GB Notification: Performance of postOpt tearingSystem (simulation): time 0.02128/30.94, allocations: 5.307 MB / 5.975 GB, free: 117.4 MB / 0.5887 GB Notification: Performance of postOpt inputDerivativesUsed (simulation): time 0.003188/30.94, allocations: 266 kB / 5.975 GB, free: 117.4 MB / 0.5887 GB Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 0.04755/30.99, allocations: 27.87 MB / 6.002 GB, free: 98.82 MB / 0.5887 GB Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 1.62e-05/30.99, allocations: 7.094 kB / 6.002 GB, free: 98.82 MB / 0.5887 GB Notification: Performance of postOpt detectJacobianSparsePattern (simulation): time 0.1428/31.13, allocations: 38.97 MB / 6.04 GB, free: 97.23 MB / 0.5887 GB Notification: Performance of postOpt generateSymbolicLinearization (simulation): time 0.1735/31.31, allocations: 51.4 MB / 6.091 GB, free: 83.4 MB / 0.5887 GB Notification: Performance of postOpt removeConstants (simulation): time 0.01158/31.32, allocations: 2.633 MB / 6.093 GB, free: 81.99 MB / 0.5887 GB Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.005363/31.32, allocations: 85.06 kB / 6.093 GB, free: 81.96 MB / 0.5887 GB Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.01676/31.34, allocations: 0.6613 MB / 6.094 GB, free: 81.93 MB / 0.5887 GB Notification: Performance of postOpt findZeroCrossings (simulation): time 0.005167/31.34, allocations: 0.9368 MB / 6.095 GB, free: 81.79 MB / 0.5887 GB Notification: Performance of postOpt collapseArrayExpressions (simulation): time 0.003718/31.35, allocations: 441.1 kB / 6.095 GB, free: 81.71 MB / 0.5887 GB Notification: Performance of sort global known variables: time 0.007222/31.36, allocations: 2.375 MB / 6.098 GB, free: 80.81 MB / 0.5887 GB Notification: Performance of remove unused functions: time 0.04763/31.4, allocations: 7.508 MB / 6.105 GB, free: 76.86 MB / 0.5887 GB Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 8 * Number of states: 34 (B5.medium.h,B5.level,volume5.medium.p,volume5.medium.h,P1.medium.p,P1.medium.h,P2.medium.p,P2.medium.h,B1.medium.h,B1.level,B2.medium.h,B2.level,B3.medium.h,B3.level,B4.medium.h,B4.level,B7.medium.h,B7.level,pipeB1B2.mediums[1].p,pipeB1B2.mediums[1].h,pipeB1B2.mediums[2].p,pipeB1B2.mediums[2].h,pipePump1B1.mediums[1].p,pipePump1B1.mediums[1].h,pipePump1B1.mediums[2].p,pipePump1B1.mediums[2].h,pipePump2B2.mediums[1].p,pipePump2B2.mediums[1].h,pipePump2B2.mediums[2].p,pipePump2B2.mediums[2].h,B6.medium.h,B6.level,volume4.medium.p,volume4.medium.h) * Number of discrete variables: 328 (controller.Step14.localActive,controller.Step13.active,controller.Step13.localActive,controller.Transition7.enableFire,controller.Step12.localActive,controller.Step11.localActive,controller.Step10.active,controller.Step10.localActive,controller.Step9.localActive,controller.Step8.localActive,controller.Step7.localActive,controller.Step6.localActive,controller.Step5.localActive,controller.Step4.localActive,controller.Step3.localActive,controller.Transition3.enableFire,controller.Step2.localActive,controller.Step1.localActive,controller.Transition1.enableFire,controller.InitialStep1.localActive,$cse7.phase,$cse7.region,$cse11.phase,$cse11.region,$cse12.phase,$cse12.region,$cse13.phase,$cse13.region,$cse17.phase,$cse17.region,$cse18.phase,$cse18.region,$cse19.phase,$cse19.region,$cse20.phase,$cse20.region,$cse24.phase,$cse24.region,$cse25.phase,$cse25.region,$cse31.phase,$cse31.region,$cse32.phase,$cse32.region,$cse40.phase,$cse40.region,$cse41.phase,$cse41.region,$cse47.phase,$cse47.region,$cse48.phase,$cse48.region,$cse54.phase,$cse54.region,$cse55.phase,$cse55.region,$cse61.phase,$cse61.region,$cse62.phase,$cse62.region,$cse63.phase,$cse63.region,$cse64.phase,$cse64.region,$cse68.phase,$cse68.region,$cse69.phase,$cse69.region,$cse70.phase,$cse70.region,$cse71.phase,$cse71.region,$cse72.phase,$cse72.region,$cse73.phase,$cse73.region,$cse74.phase,$cse74.region,$cse78.phase,$cse78.region,$cse79.phase,$cse79.region,$cse83.phase,$cse83.region,$cse84.phase,$cse84.region,$cse85.phase,$cse85.region,$cse86.phase,$cse86.region,$cse89.phase,$cse92.phase,$cse96.phase,$cse96.region,$cse97.phase,$cse97.region,$cse100.phase,$cse103.phase,$cse107.phase,$cse107.region,$cse110.phase,$cse113.phase,$cse117.phase,$cse117.region,$cse121.phase,$cse124.phase,$cse128.phase,$cse128.region,$cse131.phase,$cse134.phase,$cse138.phase,$cse138.region,$cse139.phase,$cse139.region,$cse142.phase,$cse145.phase,$cse151.phase,$cse154.phase,$cse158.phase,$cse158.region,$cse159.phase,$cse159.region,$cse162.phase,$cse165.phase,$cse169.phase,$cse169.region,$cse170.phase,$cse170.region,$cse173.phase,$cse176.phase,$cse180.phase,$cse180.region,$cse181.phase,$cse181.region,$cse184.phase,$cse187.phase,$cse193.phase,$cse196.phase,$cse200.phase,$cse200.region,$cse201.phase,$cse201.region,$cse204.phase,$cse207.phase,$cse211.phase,$cse211.region,$cse212.phase,$cse212.region,$cse215.phase,$cse218.phase,$cse222.phase,$cse222.region,$cse223.phase,$cse223.region,$cse226.phase,$cse229.phase,$cse233.phase,$cse233.region,$cse234.phase,$cse234.region,$cse237.phase,$cse240.phase,$cse244.phase,$cse244.region,$cse245.phase,$cse245.region,$cse248.phase,$cse251.phase,$cse255.phase,$cse255.region,$cse256.phase,$cse256.region,$cse259.phase,$cse262.phase,$cse266.phase,$cse266.region,$cse267.phase,$cse267.region,$cse270.phase,$cse273.phase,$cse277,$cse278,$cse279,$cse280,$cse281,$cse282,$cse283,$cse284,$cse285,$cse286,$cse287,$cse288,$cse289,$cse290,$cse291.phase,$cse291.region,$cse292.phase,$cse292.region,$cse295.phase,$cse298.phase,$cse302.phase,$cse302.region,$cse303.phase,$cse303.region,$cse306.phase,$cse309.phase,$cse313.phase,$cse313.region,$whenCondition7,$whenCondition6,$whenCondition5,$whenCondition4,$whenCondition3,$whenCondition2,$whenCondition1,B5.InnerTankTop[1].m_flow_negative,B5.InnerTankSide[1].m_flow_negative,B5.InnerTankBottom[1].m_flow_negative,B5.heatTransfer.states[1].phase,controller.InitialStep1.newActive,controller.InitialStep1.oldActive,controller.InitialStep1.active,controller.Transition1.fire,controller.Transition1.t_start,controller.Step1.newActive,controller.Step1.oldActive,controller.Step1.active,controller.Transition2.enableFire,controller.Transition2.condition,controller.Step2.newActive,controller.Step2.oldActive,controller.Step2.active,controller.Transition3.fire,controller.Transition3.t_start,controller.Step3.newActive,controller.Step3.oldActive,controller.Step3.active,controller.Transition4.enableFire,controller.Transition4.condition,controller.Step4.newActive,controller.Step4.oldActive,controller.Step4.active,controller.Transition5.enableFire,controller.Step5.newActive,controller.Step5.oldActive,controller.Step5.active,controller.Transition6.enableFire,controller.Transition6.condition,controller.Step6.newActive,controller.Step6.oldActive,controller.Step6.active,controller.Transition7.fire,controller.Transition7.t_start,controller.Parallel1.inPort.occupied,controller.Parallel1.outPort.available,controller.Step7.newActive,controller.Step7.oldActive,controller.Step7.active,controller.Step8.newActive,controller.Step8.oldActive,controller.Step8.active,controller.Step9.newActive,controller.Step9.oldActive,controller.Step9.active,controller.Step10.newActive,controller.Step10.oldActive,controller.Step11.newActive,controller.Step11.oldActive,controller.Step11.active,controller.Step12.newActive,controller.Step12.oldActive,controller.Step12.active,controller.Step13.newActive,controller.Step13.oldActive,controller.Step14.newActive,controller.Step14.oldActive,controller.Step14.active,controller.Transition8.enableFire,controller.Transition9.enableFire,controller.Transition9.condition,controller.Transition10.enableFire,controller.Transition10.condition,controller.Transition11.enableFire,controller.Transition11.condition,controller.Transition12.enableFire,controller.Transition12.condition,controller.Transition13.enableFire,controller.Transition13.condition,controller.T5_idle,controller.T7_idle,controller.TransitionWithSignal1.enableFire,controller.BooleanExpression1.y,volume5.medium.phase,P1.heatTransfer.states[1].phase,P2.heatTransfer.states[1].phase,B1.heatTransfer.states[1].phase,B1.ports_m_flow_out[1],B1.aboveLevel[1],P1_on.endValue,P1_on.rate,P1_on.T,P2_on.endValue,P2_on.rate,P2_on.T,B2.heatTransfer.states[1].phase,B2.ports_m_flow_out[1],B2.aboveLevel[1],B3.heatTransfer.states[1].phase,B3.ports_m_flow_out[1],B3.ports_m_flow_out[2],B3.aboveLevel[1],B3.aboveLevel[2],B4.heatTransfer.states[1].phase,B4.ports_m_flow_out[1],B4.aboveLevel[1],B7.heatTransfer.states[1].phase,B7.ports_m_flow_out[1],B7.aboveLevel[1],pipeB1B2.statesFM[1].phase,pipeB1B2.statesFM[2].phase,pipePump1B1.statesFM[1].phase,pipePump1B1.statesFM[2].phase,pipePump2B2.statesFM[1].phase,pipePump2B2.statesFM[2].phase,B6.heatTransfer.states[1].phase,B6.ports_m_flow_out[1],B6.aboveLevel[1],volume4.medium.phase) * Number of discrete states: 34 (B5.InnerTankSide[1].m_flow_negative,controller.InitialStep1.newActive,controller.Step1.newActive,controller.Step2.newActive,controller.Step3.newActive,controller.Step4.newActive,controller.Step5.newActive,controller.Step6.newActive,controller.Step7.newActive,controller.Step8.newActive,B5.InnerTankBottom[1].m_flow_negative,controller.Step9.newActive,controller.Step10.newActive,controller.Step11.newActive,controller.Step12.newActive,controller.Step13.newActive,controller.Step14.newActive,B1.aboveLevel[1],B2.aboveLevel[1],B3.aboveLevel[1],B3.ports_m_flow_out[1],B3.aboveLevel[2],B4.aboveLevel[1],B4.ports_m_flow_out[1],B5.InnerTankTop[1].m_flow_negative,B7.aboveLevel[1],B1.ports_m_flow_out[1],B2.ports_m_flow_out[1],B3.ports_m_flow_out[2],B7.ports_m_flow_out[1],B6.aboveLevel[1],B6.ports_m_flow_out[1],P2_on.y,P1_on.y) * Top-level inputs: 0 Notification: Strong component statistics for simulation (1050): * Single equations (assignments): 898 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 99 * When equations: 24 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 29 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 2 {(1,100.0%) 6,(1,100.0%) 6} * Non-linear torn systems: 27 {1 1,1 1,1 1,1 1,1 1,1 1,1 1,1 1,1 1,2 6,1 1,2 6,2 4,2 4,1 5,1 5,2 4,2 4,2 2,2 2,1 2,2 11,2 11,1 2,2 17,2 23,2 17} Notification: Performance of Backend phase and start with SimCode phase: time 0.04123/31.44, allocations: 11.06 MB / 6.116 GB, free: 69.06 MB / 0.5887 GB Notification: Performance of simCode: created initialization part: time 0.5889/32.03, allocations: 19.87 MB / 6.135 GB, free: 113.9 MB / 0.5887 GB Notification: Performance of simCode: created event and clocks part: time 2.154e-05/32.03, allocations: 7.938 kB / 6.135 GB, free: 113.9 MB / 0.5887 GB Notification: Performance of simCode: created simulation system equations: time 0.05604/32.09, allocations: 15.44 MB / 6.15 GB, free: 113.3 MB / 0.5887 GB Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.0555/32.14, allocations: 3.531 MB / 6.154 GB, free: 113.2 MB / 0.5887 GB Notification: Performance of simCode: created linear, non-linear and system jacobian parts: time 0.1272/32.27, allocations: 26.39 MB / 6.179 GB, free: 109.4 MB / 0.5887 GB Notification: Performance of simCode: all other stuff during SimCode phase: time 0.03325/32.31, allocations: 7.693 MB / 6.187 GB, free: 108.4 MB / 0.5887 GB Notification: Performance of SimCode: time 1.703e-06/32.31, allocations: 0 / 6.187 GB, free: 108.4 MB / 0.5887 GB