Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries/ --ompython_omhome=/usr Modelica_3.1_Modelica.Fluid.Examples.AST_BatchPlant.BatchPlant_StandardWater.conf.json
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.1.0+maint.om/package.mo", uses=false)
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 1.0.0/package.mo", uses=false)
Using package ModelicaServices with version 1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 1.0.0/package.mo)
Using package Modelica with version 3.1 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.1.0+maint.om/package.mo)
Running command: translateModel(Modelica.Fluid.Examples.AST_BatchPlant.BatchPlant_StandardWater,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="Modelica_3.1_Modelica.Fluid.Examples.AST_BatchPlant.BatchPlant_StandardWater")
translateModel(Modelica.Fluid.Examples.AST_BatchPlant.BatchPlant_StandardWater,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="Modelica_3.1_Modelica.Fluid.Examples.AST_BatchPlant.BatchPlant_StandardWater")
[<interactive>:1:1-1:32:writable] Error: Class GC_set_max_heap_size not found in scope <global scope> (looking for a function or record).
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.1.0+maint.om/package.mo): time 0.8242/0.8242, allocations: 110.7 MB / 118 MB, free: 14.56 MB / 106.7 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 1.0.0/package.mo): time 0.001774/0.001774, allocations: 152 kB / 143.7 MB, free: 4.879 MB / 122.7 MB
Notification: Performance of FrontEnd - loaded program: time 7.714e-06/7.745e-06, allocations: 0 / 173.5 MB, free: 23.04 MB / 138.7 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 0.0575/0.05753, allocations: 25.16 MB / 198.6 MB, free: 13.95 MB / 154.7 MB
Notification: Performance of FrontEnd - scodeFlatten: time 3.305/3.363, allocations: 1.613 GB / 1.807 GB, free: 49.08 MB / 234.7 MB
Notification: Performance of FrontEnd - mkProgramGraph: time 0.0001947/3.363, allocations: 66.52 kB / 1.807 GB, free: 49.08 MB / 234.7 MB
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.1.0+maint.om/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.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.1.0+maint.om/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.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.1.0+maint.om/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.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.1.0+maint.om/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.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.1.0+maint.om/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.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.1.0+maint.om/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.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.1.0+maint.om/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.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.1.0+maint.om/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.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.1.0+maint.om/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.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.1.0+maint.om/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.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.1.0+maint.om/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.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.1.0+maint.om/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.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.1.0+maint.om/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.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.1.0+maint.om/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.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.1.0+maint.om/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: Performance of FrontEnd: time 14.62/17.98, allocations: 3.611 GB / 5.418 GB, free: 23.13 MB / 0.5105 GB
Notification: Performance of Transformations before backend: time 0.0009156/17.98, allocations: 241.1 kB / 5.418 GB, free: 23.09 MB / 0.5105 GB
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 0.04651/18.03, allocations: 14.12 MB / 5.432 GB, free: 16.89 MB / 0.5105 GB
Notification: Performance of prepare preOptimizeDAE: time 4.003e-05/18.03, allocations: 13.06 kB / 5.432 GB, free: 16.89 MB / 0.5105 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.005905/18.03, allocations: 1.121 MB / 5.433 GB, free: 16.34 MB / 0.5105 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.01869/18.05, allocations: 6.086 MB / 5.439 GB, free: 15.31 MB / 0.5105 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.001451/18.05, allocations: 1.122 MB / 5.44 GB, free: 14.54 MB / 0.5105 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.004217/18.06, allocations: 0.5163 MB / 5.441 GB, free: 14.53 MB / 0.5105 GB
Notification: Performance of preOpt removeEqualFunctionCalls (simulation): time 0.03135/18.09, allocations: 11.97 MB / 5.452 GB, free: 14.49 MB / 0.5105 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.04243/18.13, allocations: 12.02 MB / 5.464 GB, free: 12.68 MB / 0.5105 GB
Notification: Performance of preOpt findStateOrder (simulation): time 0.0007789/18.13, allocations: 31.86 kB / 5.464 GB, free: 12.68 MB / 0.5105 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.0053/18.14, allocations: 28.5 kB / 5.464 GB, free: 12.67 MB / 0.5105 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 0.0008526/18.14, allocations: 0.5427 MB / 5.465 GB, free: 12.65 MB / 0.5105 GB
Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.192/18.33, allocations: 85.18 MB / 5.548 GB, free: 0.4922 MB / 0.5417 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.01661/18.35, allocations: 5.287 MB / 5.553 GB, free: 464 kB / 0.5417 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.01693/18.36, allocations: 4.914 MB / 5.558 GB, free: 412 kB / 0.5417 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.8208/19.18, allocations: 160.5 MB / 5.715 GB, free: 21.3 MB / 0.5886 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 0.01017/19.19, allocations: 5.178 MB / 5.72 GB, free: 21.14 MB / 0.5886 GB
Notification: Performance of pre-optimization done (n=823): time 1.436e-05/19.19, allocations: 7.625 kB / 5.72 GB, free: 21.14 MB / 0.5886 GB
Notification: Performance of matching and sorting (n=897): time 0.2266/19.42, allocations: 44.41 MB / 5.763 GB, free: 19.27 MB / 0.5886 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 0.0002686/19.42, allocations: 290 kB / 5.763 GB, free: 19.05 MB / 0.5886 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.01023/19.43, allocations: 3.617 MB / 5.767 GB, free: 18.63 MB / 0.5886 GB
Notification: Performance of collectPreVariables (initialization): time 0.002439/19.43, allocations: 97.59 kB / 5.767 GB, free: 18.6 MB / 0.5886 GB
Notification: Performance of collectInitialEqns (initialization): time 0.002883/19.44, allocations: 2.708 MB / 5.77 GB, free: 17.25 MB / 0.5886 GB
Notification: Performance of collectInitialBindings (initialization): time 0.004847/19.44, allocations: 2.817 MB / 5.772 GB, free: 15.42 MB / 0.5886 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.002234/19.44, allocations: 0 / 5.772 GB, free: 15.42 MB / 0.5886 GB
Notification: Performance of setup shared object (initialization): time 0.001237/19.44, allocations: 0.7089 MB / 5.773 GB, free: 15.09 MB / 0.5886 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.01099/19.46, allocations: 4.767 MB / 5.778 GB, free: 13.65 MB / 0.5886 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.01285/19.47, allocations: 6.98 MB / 5.785 GB, free: 8.418 MB / 0.5886 GB
Notification: The given system is mixed-determined.   [index = 2]
Notification: Performance of analyzeInitialSystem (initialization): time 0.6728/20.14, allocations: 41.89 MB / 5.825 GB, free: 107.6 MB / 0.5886 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 0.0001307/20.14, allocations: 20.5 kB / 5.825 GB, free: 107.6 MB / 0.5886 GB
Notification: Performance of matching and sorting (n=1336) (initialization): time 0.09365/20.24, allocations: 21.61 MB / 5.847 GB, free: 107.1 MB / 0.5886 GB
Notification: Performance of prepare postOptimizeDAE: time 2.023e-05/20.24, allocations: 2.562 kB / 5.847 GB, free: 107.1 MB / 0.5886 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.0001864/20.24, allocations: 64.72 kB / 5.847 GB, free: 107.1 MB / 0.5886 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.008608/20.24, allocations: 2.946 MB / 5.85 GB, free: 106.9 MB / 0.5886 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.01063/20.25, allocations: 2.248 MB / 5.852 GB, free: 106.9 MB / 0.5886 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.02523/20.28, allocations: 27.28 MB / 5.878 GB, free: 86.54 MB / 0.5886 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.01348/20.29, allocations: 0.8206 MB / 5.879 GB, free: 86.54 MB / 0.5886 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.003853/20.3, allocations: 0.5428 MB / 5.88 GB, free: 86.54 MB / 0.5886 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 0.007139/20.3, allocations: 1.489 MB / 5.881 GB, free: 86.27 MB / 0.5886 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.007778/20.31, allocations: 1.873 MB / 5.883 GB, free: 86.27 MB / 0.5886 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.09198/20.4, allocations: 37.06 MB / 5.919 GB, free: 84.01 MB / 0.5886 GB
Notification: Performance of postOpt inlineArrayEqn (simulation): time 0.0004158/20.4, allocations: 351.8 kB / 5.919 GB, free: 84.01 MB / 0.5886 GB
Notification: Performance of postOpt constantLinearSystem (simulation): time 0.0001085/20.4, allocations: 3.906 kB / 5.919 GB, free: 84.01 MB / 0.5886 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 0.07849/20.48, allocations: 29.27 MB / 5.948 GB, free: 82.42 MB / 0.5886 GB
Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.6075/21.09, allocations: 49 MB / 5.996 GB, free: 107.2 MB / 0.5886 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 0.000142/21.09, allocations: 0 / 5.996 GB, free: 107.2 MB / 0.5886 GB
Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.009515/21.1, allocations: 1.837 MB / 5.998 GB, free: 107.2 MB / 0.5886 GB
Notification: Performance of postOpt tearingSystem (simulation): time 0.01136/21.11, allocations: 5.303 MB / 6.003 GB, free: 106.9 MB / 0.5886 GB
Notification: Performance of postOpt inputDerivativesUsed (simulation): time 0.003138/21.12, allocations: 254.4 kB / 6.003 GB, free: 106.9 MB / 0.5886 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 0.02421/21.14, allocations: 27.89 MB / 6.03 GB, free: 88.28 MB / 0.5886 GB
Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 7.594e-06/21.14, allocations: 3.188 kB / 6.03 GB, free: 88.28 MB / 0.5886 GB
Notification: Performance of postOpt detectJacobianSparsePattern (simulation): time 0.1002/21.24, allocations: 38.96 MB / 6.068 GB, free: 86.69 MB / 0.5886 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.01137/21.25, allocations: 2.642 MB / 6.071 GB, free: 86.25 MB / 0.5886 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.005567/21.26, allocations: 85.56 kB / 6.071 GB, free: 86.25 MB / 0.5886 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0121/21.27, allocations: 0.6612 MB / 6.072 GB, free: 86.22 MB / 0.5886 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 0.004562/21.27, allocations: 0.9356 MB / 6.073 GB, free: 86.21 MB / 0.5886 GB
Notification: Performance of postOpt collapseArrayExpressions (simulation): time 0.003545/21.28, allocations: 447.2 kB / 6.073 GB, free: 86.21 MB / 0.5886 GB
Notification: Performance of sort global known variables: time 0.007314/21.28, allocations: 2.375 MB / 6.075 GB, free: 86.03 MB / 0.5886 GB
Notification: Performance of remove unused functions: time 0.03848/21.32, allocations: 6.071 MB / 6.081 GB, free: 86.03 MB / 0.5886 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 0.03559/21.36, allocations: 11.05 MB / 6.092 GB, free: 83.65 MB / 0.5886 GB
Notification: Performance of simCode: created initialization part: time 0.03914/21.4, allocations: 19.16 MB / 6.111 GB, free: 82.79 MB / 0.5886 GB
Notification: Performance of simCode: created event and clocks part: time 1.157e-05/21.4, allocations: 1.906 kB / 6.111 GB, free: 82.78 MB / 0.5886 GB
Notification: Performance of simCode: created simulation system equations: time 0.02895/21.43, allocations: 15.44 MB / 6.126 GB, free: 82.2 MB / 0.5886 GB
Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.02437/21.45, allocations: 3.534 MB / 6.129 GB, free: 82.14 MB / 0.5886 GB
Notification: Performance of simCode: created linear, non-linear and system jacobian parts: time 0.07066/21.52, allocations: 26.34 MB / 6.155 GB, free: 75.34 MB / 0.5886 GB
Notification: Performance of simCode: all other stuff during SimCode phase: time 0.014/21.54, allocations: 7.585 MB / 6.162 GB, free: 73.94 MB / 0.5886 GB
Notification: Performance of SimCode: time 1.422e-06/21.54, allocations: 0 / 6.162 GB, free: 73.94 MB / 0.5886 GB
Notification: Performance of Templates: time 1.654/23.19, allocations: 293.7 MB / 6.449 GB, free: 80.79 MB / 0.5886 GB
make -j1 -f Modelica_3.1_Modelica.Fluid.Examples.AST_BatchPlant.BatchPlant_StandardWater.makefile
(rm -f Modelica_3.1_Modelica.Fluid.Examples.AST_BatchPlant.BatchPlant_StandardWater.pipe ; mkfifo Modelica_3.1_Modelica.Fluid.Examples.AST_BatchPlant.BatchPlant_StandardWater.pipe ; head -c 1048576 < Modelica_3.1_Modelica.Fluid.Examples.AST_BatchPlant.BatchPlant_StandardWater.pipe >> ../files/Modelica_3.1_Modelica.Fluid.Examples.AST_BatchPlant.BatchPlant_StandardWater.sim & ./Modelica_3.1_Modelica.Fluid.Examples.AST_BatchPlant.BatchPlant_StandardWater  -abortSlowSimulation -alarm=480 -lv LOG_STATS > Modelica_3.1_Modelica.Fluid.Examples.AST_BatchPlant.BatchPlant_StandardWater.pipe 2>&1)