Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ClaRa_dev_ClaRa.Examples.SteamPowerPlant_01.conf.json loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.2-main/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.2-main/package.mo): time 0.1315/0.1315, allocations: 23.17 MB / 41.77 MB, free: 7.547 MB / 34.91 MB " [Timeout remaining time 180] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/SMArtIInt 0.1.1-Release_Dymola_2023x_Refresh_1/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/SMArtIInt 0.1.1-Release_Dymola_2023x_Refresh_1/package.mo): time 0.009422/0.009422, allocations: 1.428 MB / 52.85 MB, free: 1.547 MB / 34.91 MB " [Timeout remaining time 180] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo): time 0.001312/0.001312, allocations: 96.03 kB / 62.95 MB, free: 3.258 MB / 46.55 MB " [Timeout remaining time 180] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo): time 0.001438/0.001438, allocations: 191.6 kB / 73.16 MB, free: 8.543 MB / 62.07 MB " [Timeout remaining time 180] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.0.0+maint.om/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.0.0+maint.om/package.mo): time 1.457/1.457, allocations: 225.6 MB / 308.8 MB, free: 1.254 MB / 206.1 MB " [Timeout remaining time 178] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/package.mo): time 0.9125/0.9125, allocations: 129 MB / 500 MB, free: 3.363 MB / 366.1 MB " [Timeout remaining time 179] Using package ClaRa with version 1.8.2 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/package.mo) Using package Modelica with version 4.0.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.0.0+maint.om/package.mo) Using package Complex with version 4.0.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo) Using package ModelicaServices with version 4.0.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo) Using package SMArtIInt with version 0.1.1 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/SMArtIInt 0.1.1-Release_Dymola_2023x_Refresh_1/package.mo) Using package TILMedia with version 1.8.2 ClaRa (/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.2-main/package.mo) Running command: 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[Timeout 660] "Warning: Requested package SMArtIInt of version 0.2.2, but this package was already loaded with version 0.1.1. There are no conversion annotations for this version but 0.2.2 is newer than 0.1.1. There is a possibility that 0.1.1 remains backwards compatible, but it is not loaded so OpenModelica cannot verify this. Notification: Performance of FrontEnd - loaded program: time 0.003797/0.003797, allocations: 136.1 kB / 0.6764 GB, free: 6.141 MB / 478.1 MB Notification: Performance of FrontEnd - Absyn->SCode: time 0.162/0.1658, allocations: 86.82 MB / 0.7611 GB, free: 15.16 MB / 0.5607 GB Notification: Performance of NFInst.instantiate(ClaRa.Examples.SteamPowerPlant_01): time 1.29/1.456, allocations: 0.5619 GB / 1.323 GB, free: 14.99 MB / 0.8732 GB Notification: Performance of NFInst.instExpressions: time 1.088/2.544, allocations: 238 MB / 1.555 GB, free: 15.25 MB / 1.014 GB Notification: Performance of NFInst.updateImplicitVariability: time 0.1608/2.705, allocations: 2.579 MB / 1.558 GB, free: 15.25 MB / 1.014 GB [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/Basics/Interfaces/CycleSumModel.mo:3:3-3:52:writable] Warning: Connector cycleSumPort is not balanced: The number of potential variables (0) is not equal to the number of flow variables (4). [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/StaticCycles/Triple.mo:32:3-32:182:writable] Warning: Connector steamSignal is not balanced: The number of potential variables (3) is not equal to the number of flow variables (0). [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/StaticCycles/Furnace/TripleFlueGas.mo:27:3-27:200:writable] Warning: Connector gasSignal is not balanced: The number of potential variables (12) is not equal to the number of flow variables (0). [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/StaticCycles/Triple.mo:32:3-32:182:writable] Warning: Connector steamSignal is not balanced: The number of potential variables (3) is not equal to the number of flow variables (0). [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/StaticCycles/Furnace/TripleFlueGas.mo:27:3-27:200:writable] Warning: Connector gasSignal is not balanced: The number of potential variables (12) is not equal to the number of flow variables (0). [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/StaticCycles/Triple.mo:32:3-32:182:writable] Warning: Connector steamSignal is not balanced: The number of potential variables (3) is not equal to the number of flow variables (0). [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/StaticCycles/Furnace/TripleFlueGas.mo:27:3-27:200:writable] Warning: Connector gasSignal is not balanced: The number of potential variables (12) is not equal to the number of flow variables (0). [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/StaticCycles/Triple.mo:32:3-32:182:writable] Warning: Connector steamSignal is not balanced: The number of potential variables (3) is not equal to the number of flow variables (0). [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/StaticCycles/Furnace/TripleFlueGas.mo:27:3-27:200:writable] Warning: Connector gasSignal is not balanced: The number of potential variables (12) is not equal to the number of flow variables (0). [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/StaticCycles/Triple.mo:32:3-32:182:writable] Warning: Connector steamSignal is not balanced: The number of potential variables (3) is not equal to the number of flow variables (0). [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/StaticCycles/Furnace/TripleFlueGas.mo:27:3-27:200:writable] Warning: Connector gasSignal is not balanced: The number of potential variables (12) is not equal to the number of flow variables (0). [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/StaticCycles/Triple.mo:32:3-32:182:writable] Warning: Connector steamSignal is not balanced: The number of potential variables (3) is not equal to the number of flow variables (0). [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/StaticCycles/Furnace/TripleFlueGas.mo:27:3-27:200:writable] Warning: Connector gasSignal is not balanced: The number of potential variables (12) is not equal to the number of flow variables (0). [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/StaticCycles/Triple.mo:32:3-32:182:writable] Warning: Connector steamSignal is not balanced: The number of potential variables (3) is not equal to the number of flow variables (0). [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/Basics/Interfaces/CycleSumModel.mo:3:3-3:52:writable] Warning: Connector cycleSumPort is not balanced: The number of potential variables (0) is not equal to the number of flow variables (4). Notification: Performance of NFTyping.typeComponents: time 0.1576/2.862, allocations: 62.45 MB / 1.619 GB, free: 0.6172 MB / 1.014 GB [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.2-main/GasFunctions.mo:240:23-244:26:writable] Warning: Pure function 'TILMedia.GasFunctions.specificEnthalpy_pTxi' contains a call to impure function 'TILMedia.Internals.GasFunctions.specificEnthalpy_pTxi'. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.2-main/VLEFluidFunctions.mo:175:13-179:19:writable] Warning: Pure function 'TILMedia.Internals.VLEFluidConfigurations.FullyMixtureCompatible.VLEFluidFunctions.density_phxi' contains a call to impure function 'TILMedia.Internals.VLEFluidFunctions.density_phxi'. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.2-main/VLEFluidFunctions.mo:200:13-204:40:writable] Warning: Pure function 'TILMedia.Internals.VLEFluidConfigurations.FullyMixtureCompatible.VLEFluidFunctions.specificIsobaricHeatCapacity_phxi' contains a call to impure function 'TILMedia.Internals.VLEFluidFunctions.specificIsobaricHeatCapacity_phxi'. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.2-main/VLEFluidFunctions.mo:255:13-259:28:writable] Warning: Pure function 'TILMedia.Internals.VLEFluidConfigurations.FullyMixtureCompatible.VLEFluidFunctions.dynamicViscosity_phxi' contains a call to impure function 'TILMedia.Internals.VLEFluidFunctions.dynamicViscosity_phxi'. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.2-main/VLEFluidFunctions.mo:250:13-254:31:writable] Warning: Pure function 'TILMedia.Internals.VLEFluidConfigurations.FullyMixtureCompatible.VLEFluidFunctions.thermalConductivity_phxi' contains a call to impure function 'TILMedia.Internals.VLEFluidFunctions.thermalConductivity_phxi'. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.2-main/VLEFluidFunctions.mo:770:13-774:24:writable] Warning: Pure function 'TILMedia.Internals.VLEFluidConfigurations.FullyMixtureCompatible.VLEFluidFunctions.bubbleDensity_pxi' contains a call to impure function 'TILMedia.Internals.VLEFluidFunctions.bubbleDensity_pxi'. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.2-main/VLEFluidFunctions.mo:780:13-784:33:writable] Warning: Pure function 'TILMedia.Internals.VLEFluidConfigurations.FullyMixtureCompatible.VLEFluidFunctions.bubbleSpecificEnthalpy_pxi' contains a call to impure function 'TILMedia.Internals.VLEFluidFunctions.bubbleSpecificEnthalpy_pxi'. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.2-main/VLEFluidFunctions.mo:350:13-354:28:writable] Warning: Pure function 'TILMedia.Internals.VLEFluidConfigurations.FullyMixtureCompatible.VLEFluidFunctions.specificEnthalpy_psxi' contains a call to impure function 'TILMedia.Internals.VLEFluidFunctions.specificEnthalpy_psxi'. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.2-main/VLEFluidFunctions.mo:180:13-184:27:writable] Warning: Pure function 'TILMedia.Internals.VLEFluidConfigurations.FullyMixtureCompatible.VLEFluidFunctions.specificEntropy_phxi' contains a call to impure function 'TILMedia.Internals.VLEFluidFunctions.specificEntropy_phxi'. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.2-main/VLEFluidFunctions.mo:185:13-189:23:writable] Warning: Pure function 'TILMedia.Internals.VLEFluidConfigurations.FullyMixtureCompatible.VLEFluidFunctions.temperature_phxi' contains a call to impure function 'TILMedia.Internals.VLEFluidFunctions.temperature_phxi'. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.2-main/VLEFluidFunctions.mo:775:13-779:30:writable] Warning: Pure function 'TILMedia.Internals.VLEFluidConfigurations.FullyMixtureCompatible.VLEFluidFunctions.dewSpecificEnthalpy_pxi' contains a call to impure function 'TILMedia.Internals.VLEFluidFunctions.dewSpecificEnthalpy_pxi'. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.2-main/GasFunctions.mo:15:23-19:21:writable] Warning: Pure function 'TILMedia.GasFunctions.temperature_phxi' contains a call to impure function 'TILMedia.Internals.GasFunctions.temperature_phxi'. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.2-main/VLEFluidFunctions.mo:520:13-524:28:writable] Warning: Pure function 'TILMedia.Internals.VLEFluidConfigurations.FullyMixtureCompatible.VLEFluidFunctions.specificEnthalpy_pTxi' contains a call to impure function 'TILMedia.Internals.VLEFluidFunctions.specificEnthalpy_pTxi'. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.2-main/VLEFluidFunctions.mo:765:13-769:21:writable] Warning: Pure function 'TILMedia.Internals.VLEFluidConfigurations.FullyMixtureCompatible.VLEFluidFunctions.dewDensity_pxi' contains a call to impure function 'TILMedia.Internals.VLEFluidFunctions.dewDensity_pxi'. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.2-main/VLEFluidFunctions.mo:515:13-519:19:writable] Warning: Pure function 'TILMedia.Internals.VLEFluidConfigurations.FullyMixtureCompatible.VLEFluidFunctions.density_pTxi' contains a call to impure function 'TILMedia.Internals.VLEFluidFunctions.density_pTxi'. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.2-main/GasFunctions.mo:235:23-239:17:writable] Warning: Pure function 'TILMedia.GasFunctions.density_pTxi' contains a call to impure function 'TILMedia.Internals.GasFunctions.density_pTxi'. Notification: Performance of NFTyping.typeBindings: time 0.3268/3.189, allocations: 113.1 MB / 1.729 GB, free: 15.61 MB / 1.108 GB Notification: Performance of NFTyping.typeClassSections: time 0.2263/3.415, allocations: 90.04 MB / 1.817 GB, free: 11.9 MB / 1.186 GB Notification: Performance of NFFlatten.flatten: time 1.829/5.245, allocations: 389.5 MB / 2.198 GB, free: 19.5 MB / 1.28 GB Notification: Performance of NFFlatten.resolveConnections: time 0.3665/5.611, allocations: 152.9 MB / 2.347 GB, free: 5.141 MB / 1.342 GB Notification: Performance of NFEvalConstants.evaluate: time 2.1/7.711, allocations: 171.5 MB / 2.515 GB, free: 27.21 MB / 1.42 GB Notification: Performance of NFSimplifyModel.simplify: time 0.3464/8.058, allocations: 212.9 MB / 2.723 GB, free: 15.46 MB / 1.42 GB Notification: Performance of NFPackage.collectConstants: time 0.1589/8.217, allocations: 40.8 MB / 2.762 GB, free: 11.89 MB / 1.42 GB Notification: Performance of NFFlatten.collectFunctions: time 0.2786/8.495, allocations: 53.31 MB / 2.814 GB, free: 15.7 MB / 1.467 GB Notification: Performance of NFScalarize.scalarize: time 0.2876/8.783, allocations: 163.5 MB / 2.974 GB, free: 6.98 MB / 1.608 GB Notification: Performance of NFVerifyModel.verify: time 2.501/11.28, allocations: 205.1 MB / 3.174 GB, free: 132.8 MB / 1.671 GB Notification: Performance of NFConvertDAE.convert: time 2.911/14.19, allocations: 0.5855 GB / 3.76 GB, free: 126.9 MB / 1.875 GB Notification: Performance of FrontEnd - DAE generated: time 4.247e-06/14.19, allocations: 0 / 3.76 GB, free: 126.9 MB / 1.875 GB Notification: Performance of FrontEnd: time 1.022e-06/14.19, allocations: 2.688 kB / 3.76 GB, free: 126.9 MB / 1.875 GB Notification: Performance of Transformations before backend: time 0.01701/14.21, allocations: 0.5625 kB / 3.76 GB, free: 126.9 MB / 1.875 GB Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 50243 * Number of variables: 50243 Notification: Performance of Generate backend data structure: time 1.96/16.17, allocations: 0.6996 GB / 4.459 GB, free: 4.508 MB / 2.281 GB Notification: Performance of prepare preOptimizeDAE: time 5.848e-05/16.17, allocations: 8.031 kB / 4.459 GB, free: 4.5 MB / 2.281 GB Notification: Performance of preOpt normalInlineFunction (simulation): time 0.2054/16.38, allocations: 39.69 MB / 4.498 GB, free: 12.57 MB / 2.328 GB Notification: Performance of preOpt evaluateParameters (simulation): time 1.855/18.23, allocations: 405.4 MB / 4.894 GB, free: 0.8398 GB / 2.391 GB Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.01479/18.25, allocations: 14.22 MB / 4.908 GB, free: 0.8311 GB / 2.391 GB Notification: Performance of preOpt expandDerOperator (simulation): time 0.08071/18.33, allocations: 13.55 MB / 4.921 GB, free: 0.8268 GB / 2.391 GB Notification: Performance of preOpt clockPartitioning (simulation): time 0.7548/19.08, allocations: 414.6 MB / 5.326 GB, free: 0.5314 GB / 2.391 GB Notification: Performance of preOpt findStateOrder (simulation): time 0.007224/19.09, allocations: 1.01 MB / 5.327 GB, free: 0.5304 GB / 2.391 GB Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.07718/19.17, allocations: 7.329 MB / 5.334 GB, free: 0.5235 GB / 2.391 GB Notification: Performance of preOpt inlineArrayEqn (simulation): time 0.01606/19.18, allocations: 14.54 MB / 5.348 GB, free: 0.5093 GB / 2.391 GB Notification: Performance of preOpt removeEqualRHS (simulation): time 0.6727/19.86, allocations: 414.5 MB / 5.753 GB, free: 107.4 MB / 2.391 GB Warning: The model contains alias variables with redundant start and/or conflicting nominal values. It is recommended to resolve the conflicts, because otherwise the system could be hard to solve. To print the conflicting alias sets and the chosen candidates please use -d=aliasConflicts. Notification: Performance of preOpt removeSimpleEquations (simulation): time 4.785/24.64, allocations: 1.543 GB / 7.296 GB, free: 483.4 MB / 2.625 GB Notification: Performance of preOpt comSubExp (simulation): time 0.5792/25.22, allocations: 381 MB / 7.668 GB, free: 325.1 MB / 2.625 GB Notification: Performance of preOpt resolveLoops (simulation): time 0.3424/25.56, allocations: 190.4 MB / 7.854 GB, free: 187.4 MB / 2.625 GB Notification: Performance of preOpt evalFunc (simulation): time 0.04465/25.61, allocations: 7.084 MB / 7.861 GB, free: 182 MB / 2.625 GB Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 1.633/27.24, allocations: 332.4 MB / 8.186 GB, free: 0.9166 GB / 2.625 GB Notification: Performance of preOpt simplifyInStream (simulation): time 0.2123/27.45, allocations: 43.03 MB / 8.228 GB, free: 0.904 GB / 2.625 GB Notification: Performance of pre-optimization done (n=26535): time 0.0008209/27.45, allocations: 0 / 8.228 GB, free: 0.904 GB / 2.625 GB Notification: Performance of matching and sorting (n=26544): time 254.4/281.8, allocations: 71.16 GB / 79.39 GB, free: 1.017 GB / 2.625 GB Notification: Performance of inlineWhenForInitialization (initialization): time 0.01793/281.9, allocations: 86.27 MB / 79.47 GB, free: 0.9149 GB / 2.625 GB Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.7116/282.6, allocations: 327.1 MB / 79.79 GB, free: 0.8051 GB / 2.625 GB Notification: Performance of collectPreVariables (initialization): time 0.04792/282.6, allocations: 3.055 MB / 79.8 GB, free: 0.8029 GB / 2.625 GB Notification: Performance of collectInitialEqns (initialization): time 0.1497/282.8, allocations: 130.7 MB / 79.92 GB, free: 0.7127 GB / 2.625 GB Notification: Performance of collectInitialBindings (initialization): time 0.1138/282.9, allocations: 93.78 MB / 80.02 GB, free: 0.635 GB / 2.625 GB Notification: Performance of simplifyInitialFunctions (initialization): time 0.2696/283.2, allocations: 64.01 MB / 80.08 GB, free: 0.5783 GB / 2.625 GB Notification: Performance of setup shared object (initialization): time 7.912e-05/283.2, allocations: 308.8 kB / 80.08 GB, free: 0.578 GB / 2.625 GB Notification: Performance of preBalanceInitialSystem (initialization): time 1.432/284.6, allocations: 221.3 MB / 80.29 GB, free: 0.9395 GB / 2.625 GB Notification: Performance of partitionIndependentBlocks (initialization): time 0.4298/285, allocations: 273.6 MB / 80.56 GB, free: 0.8751 GB / 2.625 GB Notification: Performance of analyzeInitialSystem (initialization): time 14.93/299.9, allocations: 2.332 GB / 82.89 GB, free: 0.7129 GB / 2.625 GB Notification: Performance of solveInitialSystemEqSystem (initialization): time 0.0022/299.9, allocations: 389.2 kB / 82.89 GB, free: 0.7129 GB / 2.625 GB Notification: Performance of matching and sorting (n=41915) (initialization): time 2.424/302.4, allocations: 0.532 GB / 83.43 GB, free: 0.8282 GB / 2.625 GB Notification: Performance of prepare postOptimizeDAE: time 0.002334/302.4, allocations: 0.6115 MB / 83.43 GB, free: 0.8282 GB / 2.625 GB Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.01639/302.4, allocations: 5.03 MB / 83.43 GB, free: 0.8282 GB / 2.625 GB Notification: Performance of postOpt tearingSystem (initialization): time 1.173/303.6, allocations: 117.3 MB / 83.55 GB, free: 0.8217 GB / 2.625 GB Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.3771/303.9, allocations: 57.14 MB / 83.6 GB, free: 0.8213 GB / 2.625 GB Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.4109/304.3, allocations: 486.7 MB / 84.08 GB, free: 463.4 MB / 2.625 GB Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.3329/304.7, allocations: 9.877 MB / 84.09 GB, free: 463.3 MB / 2.625 GB Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.08448/304.8, allocations: 11.8 MB / 84.1 GB, free: 463.3 MB / 2.625 GB Warning: Assuming fixed start value for the following 308 variables: inertia.phi:VARIABLE(start = 0.0 unit = \"rad\" fixed = true ) \"Absolute rotation angle of component\" type: Real burner1.p:VARIABLE(min = 0.0 start = burner1.p_start_flueGas_out unit = \"Pa\" fixed = true nominal = 1e5 ) \"Pressure inside volume\" type: Real burner2.p:VARIABLE(min = 0.0 start = burner2.p_start_flueGas_out unit = \"Pa\" fixed = true nominal = 1e5 ) \"Pressure inside volume\" type: Real burner3.p:VARIABLE(min = 0.0 start = burner3.p_start_flueGas_out unit = \"Pa\" fixed = true nominal = 1e5 ) \"Pressure inside volume\" type: Real flameRoom_evap_1.p:VARIABLE(min = 0.0 start = flameRoom_evap_1.p_start_flueGas_out unit = \"Pa\" fixed = true nominal = 1e5 ) \"Pressure inside volume\" type: Real flameRoom_rh_2.p:VARIABLE(min = 0.0 start = flameRoom_rh_2.p_start_flueGas_out unit = \"Pa\" fixed = true nominal = 1e5 ) \"Pressure inside volume\" type: Real burner4.p:VARIABLE(min = 0.0 start = burner4.p_start_flueGas_out unit = \"Pa\" fixed = true nominal = 1e5 ) \"Pressure inside volume\" type: Real flameRoom_evap_2.p:VARIABLE(min = 0.0 start = flameRoom_evap_2.p_start_flueGas_out unit = \"Pa\" fixed = true nominal = 1e5 ) \"Pressure inside volume\" type: Real flameRoom_sh_1.p:VARIABLE(min = 0.0 start = flameRoom_sh_1.p_start_flueGas_out unit = \"Pa\" fixed = true nominal = 1e5 ) \"Pressure inside volume\" type: Real flameRoom_sh_2.p:VARIABLE(min = 0.0 start = flameRoom_sh_2.p_start_flueGas_out unit = \"Pa\" fixed = true nominal = 1e5 ) \"Pressure inside volume\" type: Real flameRoom_sh_4.p:VARIABLE(min = 0.0 start = flameRoom_sh_4.p_start_flueGas_out unit = \"Pa\" fixed = true nominal = 1e5 ) \"Pressure inside volume\" type: Real flameRoom_sh_3.p:VARIABLE(min = 0.0 start = flameRoom_sh_3.p_start_flueGas_out unit = \"Pa\" fixed = true nominal = 1e5 ) \"Pressure inside volume\" type: Real flameRoom_rh_1.p:VARIABLE(min = 0.0 start = flameRoom_rh_1.p_start_flueGas_out unit = \"Pa\" fixed = true nominal = 1e5 ) \"Pressure inside volume\" type: Real flameRoom_eco.p:VARIABLE(min = 0.0 start = flameRoom_eco.p_start_flueGas_out unit = \"Pa\" fixed = true nominal = 1e5 ) \"Pressure inside volume\" type: Real evap_1.h[1]:VARIABLE(start = evap_1.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] evap_1.h[2]:VARIABLE(start = evap_1.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] evap_1.h[3]:VARIABLE(start = evap_1.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] evap_1.h[4]:VARIABLE(start = evap_1.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] evap_1.h[5]:VARIABLE(start = evap_1.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] evap_1.p[1]:VARIABLE(min = 0.0 start = evap_1.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] evap_1.p[2]:VARIABLE(min = 0.0 start = evap_1.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] evap_1.p[3]:VARIABLE(min = 0.0 start = evap_1.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] evap_1.p[4]:VARIABLE(min = 0.0 start = evap_1.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] evap_1.p[5]:VARIABLE(min = 0.0 start = evap_1.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] evap_2.h[1]:VARIABLE(start = evap_2.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [4] evap_2.h[2]:VARIABLE(start = evap_2.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [4] evap_2.h[3]:VARIABLE(start = evap_2.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [4] evap_2.h[4]:VARIABLE(start = evap_2.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [4] evap_2.p[1]:VARIABLE(min = 0.0 start = evap_2.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [4] evap_2.p[2]:VARIABLE(min = 0.0 start = evap_2.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [4] evap_2.p[3]:VARIABLE(min = 0.0 start = evap_2.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [4] evap_2.p[4]:VARIABLE(min = 0.0 start = evap_2.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [4] evap_3.h[1]:VARIABLE(start = evap_3.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [4] evap_3.h[2]:VARIABLE(start = evap_3.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [4] evap_3.h[3]:VARIABLE(start = evap_3.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [4] evap_3.h[4]:VARIABLE(start = evap_3.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [4] evap_3.p[1]:VARIABLE(min = 0.0 start = evap_3.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [4] evap_3.p[2]:VARIABLE(min = 0.0 start = evap_3.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [4] evap_3.p[3]:VARIABLE(min = 0.0 start = evap_3.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [4] evap_3.p[4]:VARIABLE(min = 0.0 start = evap_3.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [4] evap_4.h[1]:VARIABLE(start = evap_4.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [3] evap_4.h[2]:VARIABLE(start = evap_4.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [3] evap_4.h[3]:VARIABLE(start = evap_4.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [3] evap_4.p[1]:VARIABLE(min = 0.0 start = evap_4.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [3] evap_4.p[2]:VARIABLE(min = 0.0 start = evap_4.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [3] evap_4.p[3]:VARIABLE(min = 0.0 start = evap_4.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [3] sh_1.h[1]:VARIABLE(start = sh_1.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_1.h[2]:VARIABLE(start = sh_1.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_1.h[3]:VARIABLE(start = sh_1.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_1.h[4]:VARIABLE(start = sh_1.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_1.h[5]:VARIABLE(start = sh_1.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_1.p[1]:VARIABLE(min = 0.0 start = sh_1.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_1.p[2]:VARIABLE(min = 0.0 start = sh_1.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_1.p[3]:VARIABLE(min = 0.0 start = sh_1.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_1.p[4]:VARIABLE(min = 0.0 start = sh_1.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_1.p[5]:VARIABLE(min = 0.0 start = sh_1.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_2.h[1]:VARIABLE(start = sh_2.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_2.h[2]:VARIABLE(start = sh_2.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_2.h[3]:VARIABLE(start = sh_2.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_2.h[4]:VARIABLE(start = sh_2.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_2.h[5]:VARIABLE(start = sh_2.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_2.p[1]:VARIABLE(min = 0.0 start = sh_2.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_2.p[2]:VARIABLE(min = 0.0 start = sh_2.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_2.p[3]:VARIABLE(min = 0.0 start = sh_2.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_2.p[4]:VARIABLE(min = 0.0 start = sh_2.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_2.p[5]:VARIABLE(min = 0.0 start = sh_2.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_3.h[1]:VARIABLE(start = sh_3.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_3.h[2]:VARIABLE(start = sh_3.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_3.h[3]:VARIABLE(start = sh_3.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_3.h[4]:VARIABLE(start = sh_3.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_3.h[5]:VARIABLE(start = sh_3.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_3.p[1]:VARIABLE(min = 0.0 start = sh_3.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_3.p[2]:VARIABLE(min = 0.0 start = sh_3.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_3.p[3]:VARIABLE(min = 0.0 start = sh_3.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_3.p[4]:VARIABLE(min = 0.0 start = sh_3.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_3.p[5]:VARIABLE(min = 0.0 start = sh_3.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_4.h[1]:VARIABLE(start = sh_4.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_4.h[2]:VARIABLE(start = sh_4.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_4.h[3]:VARIABLE(start = sh_4.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_4.h[4]:VARIABLE(start = sh_4.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_4.h[5]:VARIABLE(start = sh_4.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_4.p[1]:VARIABLE(min = 0.0 start = sh_4.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_4.p[2]:VARIABLE(min = 0.0 start = sh_4.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_4.p[3]:VARIABLE(min = 0.0 start = sh_4.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_4.p[4]:VARIABLE(min = 0.0 start = sh_4.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_4.p[5]:VARIABLE(min = 0.0 start = sh_4.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] eco.h[1]:VARIABLE(start = eco.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] eco.h[2]:VARIABLE(start = eco.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] eco.h[3]:VARIABLE(start = eco.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] eco.h[4]:VARIABLE(start = eco.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] eco.h[5]:VARIABLE(start = eco.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] eco.p[1]:VARIABLE(min = 0.0 start = eco.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] eco.p[2]:VARIABLE(min = 0.0 start = eco.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] eco.p[3]:VARIABLE(min = 0.0 start = eco.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] eco.p[4]:VARIABLE(min = 0.0 start = eco.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] eco.p[5]:VARIABLE(min = 0.0 start = eco.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] rh_1.h[1]:VARIABLE(start = rh_1.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] rh_1.h[2]:VARIABLE(start = rh_1.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] rh_1.h[3]:VARIABLE(start = rh_1.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] rh_1.h[4]:VARIABLE(start = rh_1.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] rh_1.h[5]:VARIABLE(start = rh_1.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] rh_1.p[1]:VARIABLE(min = 0.0 start = rh_1.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] rh_1.p[2]:VARIABLE(min = 0.0 start = rh_1.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] rh_1.p[3]:VARIABLE(min = 0.0 start = rh_1.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] rh_1.p[4]:VARIABLE(min = 0.0 start = rh_1.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] rh_1.p[5]:VARIABLE(min = 0.0 start = rh_1.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] rh_2.h[1]:VARIABLE(start = rh_2.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] rh_2.h[2]:VARIABLE(start = rh_2.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] rh_2.h[3]:VARIABLE(start = rh_2.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] rh_2.h[4]:VARIABLE(start = rh_2.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] rh_2.h[5]:VARIABLE(start = rh_2.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] rh_2.p[1]:VARIABLE(min = 0.0 start = rh_2.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] rh_2.p[2]:VARIABLE(min = 0.0 start = rh_2.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] rh_2.p[3]:VARIABLE(min = 0.0 start = rh_2.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] rh_2.p[4]:VARIABLE(min = 0.0 start = rh_2.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] rh_2.p[5]:VARIABLE(min = 0.0 start = rh_2.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] evap_0.h[1]:VARIABLE(start = evap_0.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [4] evap_0.h[2]:VARIABLE(start = evap_0.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [4] evap_0.h[3]:VARIABLE(start = evap_0.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [4] evap_0.h[4]:VARIABLE(start = evap_0.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [4] evap_0.p[1]:VARIABLE(min = 0.0 start = evap_0.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [4] evap_0.p[2]:VARIABLE(min = 0.0 start = evap_0.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [4] evap_0.p[3]:VARIABLE(min = 0.0 start = evap_0.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [4] evap_0.p[4]:VARIABLE(min = 0.0 start = evap_0.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [4] ct_1.h[1]:VARIABLE(start = ct_1.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [7] ct_1.h[2]:VARIABLE(start = ct_1.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [7] ct_1.h[3]:VARIABLE(start = ct_1.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [7] ct_1.h[4]:VARIABLE(start = ct_1.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [7] ct_1.h[5]:VARIABLE(start = ct_1.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [7] ct_1.h[6]:VARIABLE(start = ct_1.mechanicalEquilibrium.h_start[6] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [7] ct_1.h[7]:VARIABLE(start = ct_1.mechanicalEquilibrium.h_start[7] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [7] ct_1.p[1]:VARIABLE(min = 0.0 start = ct_1.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [7] ct_1.p[2]:VARIABLE(min = 0.0 start = ct_1.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [7] ct_1.p[3]:VARIABLE(min = 0.0 start = ct_1.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [7] ct_1.p[4]:VARIABLE(min = 0.0 start = ct_1.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [7] ct_1.p[5]:VARIABLE(min = 0.0 start = ct_1.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [7] ct_1.p[6]:VARIABLE(min = 0.0 start = ct_1.p_start_internal[6] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [7] ct_1.p[7]:VARIABLE(min = 0.0 start = ct_1.p_start_internal[7] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [7] mill4.mass_rct:VARIABLE(min = 0.0 start = mill4.mass_rct_start unit = \"kg\" fixed = true nominal = 1.0 protected = true ) \"Mass of raw coal on the table\" type: Real mill4.mass_pct:VARIABLE(min = 0.0 start = mill4.mass_pct_start unit = \"kg\" fixed = true nominal = 1.0 protected = true ) \"Mass of pulverized coal on the table\" type: Real mill4.mass_pca:VARIABLE(min = 0.0 start = mill4.mass_pca_start unit = \"kg\" fixed = true nominal = 1.0 protected = true ) \"Mass of pulverized coal carried by primary air\" type: Real mill4.T_out:VARIABLE(min = 0.0 start = mill4.T_out_start unit = \"K\" fixed = true nominal = 300.0 protected = true ) \"Classifier Temperature (outlet temperature)\" type: Real mill1.mass_rct:VARIABLE(min = 0.0 start = mill1.mass_rct_start unit = \"kg\" fixed = true nominal = 1.0 protected = true ) \"Mass of raw coal on the table\" type: Real mill1.mass_pct:VARIABLE(min = 0.0 start = mill1.mass_pct_start unit = \"kg\" fixed = true nominal = 1.0 protected = true ) \"Mass of pulverized coal on the table\" type: Real mill1.mass_pca:VARIABLE(min = 0.0 start = mill1.mass_pca_start unit = \"kg\" fixed = true nominal = 1.0 protected = true ) \"Mass of pulverized coal carried by primary air\" type: Real mill1.T_out:VARIABLE(min = 0.0 start = mill1.T_out_start unit = \"K\" fixed = true nominal = 300.0 protected = true ) \"Classifier Temperature (outlet temperature)\" type: Real mill2.mass_rct:VARIABLE(min = 0.0 start = mill2.mass_rct_start unit = \"kg\" fixed = true nominal = 1.0 protected = true ) \"Mass of raw coal on the table\" type: Real mill2.mass_pct:VARIABLE(min = 0.0 start = mill2.mass_pct_start unit = \"kg\" fixed = true nominal = 1.0 protected = true ) \"Mass of pulverized coal on the table\" type: Real mill2.mass_pca:VARIABLE(min = 0.0 start = mill2.mass_pca_start unit = \"kg\" fixed = true nominal = 1.0 protected = true ) \"Mass of pulverized coal carried by primary air\" type: Real mill2.T_out:VARIABLE(min = 0.0 start = mill2.T_out_start unit = \"K\" fixed = true nominal = 300.0 protected = true ) \"Classifier Temperature (outlet temperature)\" type: Real mill3.mass_rct:VARIABLE(min = 0.0 start = mill3.mass_rct_start unit = \"kg\" fixed = true nominal = 1.0 protected = true ) \"Mass of raw coal on the table\" type: Real mill3.mass_pct:VARIABLE(min = 0.0 start = mill3.mass_pct_start unit = \"kg\" fixed = true nominal = 1.0 protected = true ) \"Mass of pulverized coal on the table\" type: Real mill3.mass_pca:VARIABLE(min = 0.0 start = mill3.mass_pca_start unit = \"kg\" fixed = true nominal = 1.0 protected = true ) \"Mass of pulverized coal carried by primary air\" type: Real mill3.T_out:VARIABLE(min = 0.0 start = mill3.T_out_start unit = \"K\" fixed = true nominal = 300.0 protected = true ) \"Classifier Temperature (outlet temperature)\" type: Real eco_down.h[1]:VARIABLE(start = eco_down.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] eco_down.h[2]:VARIABLE(start = eco_down.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] eco_down.h[3]:VARIABLE(start = eco_down.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] eco_down.h[4]:VARIABLE(start = eco_down.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] eco_down.h[5]:VARIABLE(start = eco_down.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] eco_down.p[1]:VARIABLE(min = 0.0 start = eco_down.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] eco_down.p[2]:VARIABLE(min = 0.0 start = eco_down.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] eco_down.p[3]:VARIABLE(min = 0.0 start = eco_down.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] eco_down.p[4]:VARIABLE(min = 0.0 start = eco_down.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] eco_down.p[5]:VARIABLE(min = 0.0 start = eco_down.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] separator.h:VARIABLE(start = separator.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 protected = true ) \"spec. enthalpy state\" type: Real separator.p:VARIABLE(min = 0.0 start = separator.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real rh_pipe.h[1]:VARIABLE(start = rh_pipe.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] rh_pipe.h[2]:VARIABLE(start = rh_pipe.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] rh_pipe.h[3]:VARIABLE(start = rh_pipe.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] rh_pipe.h[4]:VARIABLE(start = rh_pipe.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] rh_pipe.h[5]:VARIABLE(start = rh_pipe.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] rh_pipe.p[1]:VARIABLE(min = 0.0 start = rh_pipe.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] rh_pipe.p[2]:VARIABLE(min = 0.0 start = rh_pipe.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] rh_pipe.p[3]:VARIABLE(min = 0.0 start = rh_pipe.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] rh_pipe.p[4]:VARIABLE(min = 0.0 start = rh_pipe.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] rh_pipe.p[5]:VARIABLE(min = 0.0 start = rh_pipe.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_pipe.h[1]:VARIABLE(start = sh_pipe.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_pipe.h[2]:VARIABLE(start = sh_pipe.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_pipe.h[3]:VARIABLE(start = sh_pipe.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_pipe.h[4]:VARIABLE(start = sh_pipe.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_pipe.h[5]:VARIABLE(start = sh_pipe.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_pipe.p[1]:VARIABLE(min = 0.0 start = sh_pipe.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_pipe.p[2]:VARIABLE(min = 0.0 start = sh_pipe.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_pipe.p[3]:VARIABLE(min = 0.0 start = sh_pipe.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_pipe.p[4]:VARIABLE(min = 0.0 start = sh_pipe.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_pipe.p[5]:VARIABLE(min = 0.0 start = sh_pipe.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] feedWaterTank.volume.h_liq:VARIABLE(start = feedWaterTank.volume.h_liq_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of liquid phase\" type: Real feedWaterTank.volume.h_vap:VARIABLE(start = feedWaterTank.volume.h_vap_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of vapour phase\" type: Real feedWaterTank.volume.p_vap:VARIABLE(min = 0.0 start = feedWaterTank.volume.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"Vapour pressure\" type: Real join_LP1.h:VARIABLE(start = join_LP1.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real join_LP1.p:VARIABLE(min = 0.0 start = join_LP1.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real join_HP.h:VARIABLE(start = join_HP.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real join_HP.p:VARIABLE(min = 0.0 start = Turbine_HP1.p_out_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real join_LP_main.h:VARIABLE(start = join_LP_main.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real join_LP_main.p:VARIABLE(min = 0.0 start = join_LP_main.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real split_IP2.h:VARIABLE(start = split_IP2.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real split_IP2.p:VARIABLE(min = 0.0 start = split_IP2.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real join_IP3.h:VARIABLE(start = join_IP3.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real join_IP3.p:VARIABLE(min = 0.0 start = join_IP3.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real join_LP2.h:VARIABLE(start = join_LP2.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real join_LP2.p:VARIABLE(min = 0.0 start = join_LP2.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real join_LP3.h:VARIABLE(start = join_LP3.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real join_LP3.p:VARIABLE(min = 0.0 start = join_LP3.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real preheater_LP2.tubes.h:VARIABLE(start = preheater_LP2.tubes.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 protected = true ) \"spec. enthalpy state\" type: Real preheater_LP2.tubes.p:VARIABLE(min = 0.0 start = preheater_LP2.tubes.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real preheater_LP2.shell.h_liq:VARIABLE(start = preheater_LP2.shell.h_liq_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of liquid phase\" type: Real preheater_LP2.shell.h_vap:VARIABLE(start = preheater_LP2.shell.h_vap_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of vapour phase\" type: Real preheater_LP2.shell.p_vap:VARIABLE(min = 0.0 start = preheater_LP2.shell.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"Vapour pressure\" type: Real preheater_LP3.tubes.h:VARIABLE(start = preheater_LP3.tubes.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 protected = true ) \"spec. enthalpy state\" type: Real preheater_LP3.tubes.p:VARIABLE(min = 0.0 start = preheater_LP3.tubes.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real preheater_LP3.shell.h_liq:VARIABLE(start = preheater_LP3.shell.h_liq_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of liquid phase\" type: Real preheater_LP3.shell.h_vap:VARIABLE(start = preheater_LP3.shell.h_vap_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of vapour phase\" type: Real preheater_LP3.shell.p_vap:VARIABLE(min = 0.0 start = preheater_LP3.shell.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"Vapour pressure\" type: Real join_preheater_LP3.h:VARIABLE(start = join_preheater_LP3.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real join_preheater_LP3.p:VARIABLE(min = 0.0 start = join_preheater_LP3.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real downComer_feedWaterTank.h[1]:VARIABLE(start = downComer_feedWaterTank.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [3] downComer_feedWaterTank.h[2]:VARIABLE(start = downComer_feedWaterTank.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [3] downComer_feedWaterTank.h[3]:VARIABLE(start = downComer_feedWaterTank.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [3] downComer_feedWaterTank.p[1]:VARIABLE(min = 0.0 start = downComer_feedWaterTank.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [3] downComer_feedWaterTank.p[2]:VARIABLE(min = 0.0 start = downComer_feedWaterTank.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [3] downComer_feedWaterTank.p[3]:VARIABLE(min = 0.0 start = downComer_feedWaterTank.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [3] eco_riser.h[1]:VARIABLE(start = eco_riser.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] eco_riser.h[2]:VARIABLE(start = eco_riser.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] eco_riser.h[3]:VARIABLE(start = eco_riser.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] eco_riser.h[4]:VARIABLE(start = eco_riser.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] eco_riser.h[5]:VARIABLE(start = eco_riser.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] eco_riser.p[1]:VARIABLE(min = 0.0 start = eco_riser.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] eco_riser.p[2]:VARIABLE(min = 0.0 start = eco_riser.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] eco_riser.p[3]:VARIABLE(min = 0.0 start = eco_riser.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] eco_riser.p[4]:VARIABLE(min = 0.0 start = eco_riser.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] eco_riser.p[5]:VARIABLE(min = 0.0 start = eco_riser.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] splitVLE_L2_flex.h:VARIABLE(start = splitVLE_L2_flex.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real splitVLE_L2_flex.p:VARIABLE(min = 0.0 start = splitVLE_L2_flex.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real regenerativeAirPreheater.flueGasCell.h[1]:VARIABLE(start = regenerativeAirPreheater.flueGasCell.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [5] regenerativeAirPreheater.flueGasCell.h[2]:VARIABLE(start = regenerativeAirPreheater.flueGasCell.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [5] regenerativeAirPreheater.flueGasCell.h[3]:VARIABLE(start = regenerativeAirPreheater.flueGasCell.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [5] regenerativeAirPreheater.flueGasCell.h[4]:VARIABLE(start = regenerativeAirPreheater.flueGasCell.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [5] regenerativeAirPreheater.flueGasCell.h[5]:VARIABLE(start = regenerativeAirPreheater.flueGasCell.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [5] regenerativeAirPreheater.flueGasCell.p[1]:VARIABLE(min = 0.0 start = regenerativeAirPreheater.flueGasCell.p_start[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] regenerativeAirPreheater.flueGasCell.p[2]:VARIABLE(min = 0.0 start = regenerativeAirPreheater.flueGasCell.p_start[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] regenerativeAirPreheater.flueGasCell.p[3]:VARIABLE(min = 0.0 start = regenerativeAirPreheater.flueGasCell.p_start[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] regenerativeAirPreheater.flueGasCell.p[4]:VARIABLE(min = 0.0 start = regenerativeAirPreheater.flueGasCell.p_start[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] regenerativeAirPreheater.freshAirCell.h[1]:VARIABLE(start = regenerativeAirPreheater.freshAirCell.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [5] regenerativeAirPreheater.freshAirCell.h[2]:VARIABLE(start = regenerativeAirPreheater.freshAirCell.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [5] regenerativeAirPreheater.freshAirCell.h[3]:VARIABLE(start = regenerativeAirPreheater.freshAirCell.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [5] regenerativeAirPreheater.freshAirCell.h[4]:VARIABLE(start = regenerativeAirPreheater.freshAirCell.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [5] regenerativeAirPreheater.freshAirCell.h[5]:VARIABLE(start = regenerativeAirPreheater.freshAirCell.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [5] regenerativeAirPreheater.freshAirCell.p[1]:VARIABLE(min = 0.0 start = regenerativeAirPreheater.freshAirCell.p_start[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] regenerativeAirPreheater.freshAirCell.p[2]:VARIABLE(min = 0.0 start = regenerativeAirPreheater.freshAirCell.p_start[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] regenerativeAirPreheater.freshAirCell.p[3]:VARIABLE(min = 0.0 start = regenerativeAirPreheater.freshAirCell.p_start[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] regenerativeAirPreheater.freshAirCell.p[4]:VARIABLE(min = 0.0 start = regenerativeAirPreheater.freshAirCell.p_start[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] regenerativeAirPreheater.freshAirCell.p[5]:VARIABLE(min = 0.0 start = regenerativeAirPreheater.freshAirCell.p_start[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] regenerativeAirPreheater.freshAirLeakage_join.bulk.h:VARIABLE(start = regenerativeAirPreheater.freshAirLeakage_join.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Specific enthalpy\" type: Real regenerativeAirPreheater.freshAirLeakage_join.bulk.xi[1]:VARIABLE(min = 0.0 max = 1.0 start = regenerativeAirPreheater.freshAirLeakage_join.xi_start[1] unit = \"1\" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer ) \"Mass fraction\" type: Real [9] regenerativeAirPreheater.freshAirLeakage_join.bulk.xi[2]:VARIABLE(min = 0.0 max = 1.0 start = regenerativeAirPreheater.freshAirLeakage_join.xi_start[2] unit = \"1\" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer ) \"Mass fraction\" type: Real [9] regenerativeAirPreheater.freshAirLeakage_join.bulk.xi[3]:VARIABLE(min = 0.0 max = 1.0 start = regenerativeAirPreheater.freshAirLeakage_join.xi_start[3] unit = \"1\" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer ) \"Mass fraction\" type: Real [9] regenerativeAirPreheater.freshAirLeakage_join.bulk.xi[4]:VARIABLE(min = 0.0 max = 1.0 start = regenerativeAirPreheater.freshAirLeakage_join.xi_start[4] unit = \"1\" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer ) \"Mass fraction\" type: Real [9] regenerativeAirPreheater.freshAirLeakage_join.bulk.xi[5]:VARIABLE(min = 0.0 max = 1.0 start = regenerativeAirPreheater.freshAirLeakage_join.xi_start[5] unit = \"1\" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer ) \"Mass fraction\" type: Real [9] regenerativeAirPreheater.freshAirLeakage_join.bulk.xi[6]:VARIABLE(min = 0.0 max = 1.0 start = regenerativeAirPreheater.freshAirLeakage_join.xi_start[6] unit = \"1\" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer ) \"Mass fraction\" type: Real [9] regenerativeAirPreheater.freshAirLeakage_join.bulk.xi[7]:VARIABLE(min = 0.0 max = 1.0 start = regenerativeAirPreheater.freshAirLeakage_join.xi_start[7] unit = \"1\" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer ) \"Mass fraction\" type: Real [9] regenerativeAirPreheater.freshAirLeakage_join.bulk.xi[8]:VARIABLE(min = 0.0 max = 1.0 start = regenerativeAirPreheater.freshAirLeakage_join.xi_start[8] unit = \"1\" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer ) \"Mass fraction\" type: Real [9] regenerativeAirPreheater.freshAirLeakage_join.bulk.xi[9]:VARIABLE(min = 0.0 max = 1.0 start = regenerativeAirPreheater.freshAirLeakage_join.xi_start[9] unit = \"1\" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer ) \"Mass fraction\" type: Real [9] splitGas_L2_flex.bulk.p:VARIABLE(min = 0.0 start = splitGas_L2_flex.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer protected = true ) \"Pressure\" type: Real splitGas_L2_flex.bulk.h:VARIABLE(start = splitGas_L2_flex.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Specific enthalpy\" type: Real splitGas_L2_flex.bulk.xi[1]:VARIABLE(min = 0.0 max = 1.0 start = splitGas_L2_flex.xi_start[1] unit = \"1\" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer protected = true ) \"Mass fraction\" type: Real [9] splitGas_L2_flex.bulk.xi[2]:VARIABLE(min = 0.0 max = 1.0 start = splitGas_L2_flex.xi_start[2] unit = \"1\" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer protected = true ) \"Mass fraction\" type: Real [9] splitGas_L2_flex.bulk.xi[3]:VARIABLE(min = 0.0 max = 1.0 start = splitGas_L2_flex.xi_start[3] unit = \"1\" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer protected = true ) \"Mass fraction\" type: Real [9] splitGas_L2_flex.bulk.xi[4]:VARIABLE(min = 0.0 max = 1.0 start = splitGas_L2_flex.xi_start[4] unit = \"1\" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer protected = true ) \"Mass fraction\" type: Real [9] splitGas_L2_flex.bulk.xi[5]:VARIABLE(min = 0.0 max = 1.0 start = splitGas_L2_flex.xi_start[5] unit = \"1\" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer protected = true ) \"Mass fraction\" type: Real [9] splitGas_L2_flex.bulk.xi[6]:VARIABLE(min = 0.0 max = 1.0 start = splitGas_L2_flex.xi_start[6] unit = \"1\" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer protected = true ) \"Mass fraction\" type: Real [9] splitGas_L2_flex.bulk.xi[7]:VARIABLE(min = 0.0 max = 1.0 start = splitGas_L2_flex.xi_start[7] unit = \"1\" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer protected = true ) \"Mass fraction\" type: Real [9] splitGas_L2_flex.bulk.xi[8]:VARIABLE(min = 0.0 max = 1.0 start = splitGas_L2_flex.xi_start[8] unit = \"1\" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer protected = true ) \"Mass fraction\" type: Real [9] splitGas_L2_flex.bulk.xi[9]:VARIABLE(min = 0.0 max = 1.0 start = splitGas_L2_flex.xi_start[9] unit = \"1\" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer protected = true ) \"Mass fraction\" type: Real [9] PID_lambda.I.y:VARIABLE(flow=false start = PID_lambda.I.y_start_const fixed = true ) \"Connector of Real output signal\" type: Real preheater_HP.tubes.h:VARIABLE(start = preheater_HP.tubes.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 protected = true ) \"spec. enthalpy state\" type: Real preheater_HP.tubes.p:VARIABLE(min = 0.0 start = preheater_HP.tubes.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real preheater_HP.shell.h_liq:VARIABLE(start = preheater_HP.shell.h_liq_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of liquid phase\" type: Real preheater_HP.shell.h_vap:VARIABLE(start = preheater_HP.shell.h_vap_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of vapour phase\" type: Real preheater_HP.shell.p_vap:VARIABLE(min = 0.0 start = preheater_HP.shell.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"Vapour pressure\" type: Real preheater_LP4.tubes.h:VARIABLE(start = preheater_LP4.tubes.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 protected = true ) \"spec. enthalpy state\" type: Real preheater_LP4.tubes.p:VARIABLE(min = 0.0 start = preheater_LP4.tubes.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real preheater_LP4.shell.h_liq:VARIABLE(start = preheater_LP4.shell.h_liq_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of liquid phase\" type: Real preheater_LP4.shell.h_vap:VARIABLE(start = preheater_LP4.shell.h_vap_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of vapour phase\" type: Real preheater_LP4.shell.p_vap:VARIABLE(min = 0.0 start = preheater_LP4.shell.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"Vapour pressure\" type: Real preheater_LP1.tubes.h:VARIABLE(start = preheater_LP1.tubes.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 protected = true ) \"spec. enthalpy state\" type: Real preheater_LP1.tubes.p:VARIABLE(min = 0.0 start = preheater_LP1.tubes.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real preheater_LP1.shell.h_liq:VARIABLE(start = preheater_LP1.shell.h_liq_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of liquid phase\" type: Real preheater_LP1.shell.h_vap:VARIABLE(start = preheater_LP1.shell.h_vap_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of vapour phase\" type: Real preheater_LP1.shell.p_vap:VARIABLE(min = 0.0 start = preheater_LP1.shell.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"Vapour pressure\" type: Real condenser.tubes.h:VARIABLE(start = condenser.tubes.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 protected = true ) \"spec. enthalpy state\" type: Real condenser.tubes.p:VARIABLE(min = 0.0 start = condenser.tubes.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real condenser.shell.h_liq:VARIABLE(start = condenser.shell.h_liq_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of liquid phase\" type: Real condenser.shell.h_vap:VARIABLE(start = condenser.shell.h_vap_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of vapour phase\" type: Real condenser.shell.p_vap:VARIABLE(min = 0.0 start = condenser.shell.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"Vapour pressure\" type: Real sprayInjector_sh2.h:VARIABLE(start = sprayInjector_sh2.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real sprayInjector_sh2.p:VARIABLE(min = 0.0 start = sprayInjector_sh2.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real sprayInjector_sh4.h:VARIABLE(start = sprayInjector_sh4.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real sprayInjector_sh4.p:VARIABLE(min = 0.0 start = sprayInjector_sh4.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real sprayInjector_sh1.h:VARIABLE(start = sprayInjector_sh1.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real sprayInjector_sh1.p:VARIABLE(min = 0.0 start = sprayInjector_sh1.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real PI_feedwaterPump.switch_OnOff.u2:DISCRETE(flow=false fixed = true ) \"Connector of Boolean input signal\" type: Boolean PID_lambda.switch_OnOff.u2:DISCRETE(flow=false fixed = true ) \"Connector of Boolean input signal\" type: Boolean PI_Pump_cond.switch_OnOff.u2:DISCRETE(flow=false fixed = true ) \"Connector of Boolean input signal\" type: Boolean PID_preheaterLP2.switch_OnOff.u2:DISCRETE(flow=false fixed = true ) \"Connector of Boolean input signal\" type: Boolean PID_preheaterLP3.switch_OnOff.u2:DISCRETE(flow=false fixed = true ) \"Connector of Boolean input signal\" type: Boolean PID_preheaterLP4.switch_OnOff.u2:DISCRETE(flow=false fixed = true ) \"Connector of Boolean input signal\" type: Boolean PID_preheaterLP1.switch_OnOff.u2:DISCRETE(flow=false fixed = true ) \"Connector of Boolean input signal\" type: Boolean PI_valveControl_preheater_HP.switch_OnOff.u2:DISCRETE(flow=false fixed = true ) \"Connector of Boolean input signal\" type: Boolean Notification: Performance of preBalanceInitialSystem (initialization_lambda0): time 0.6175/305.4, allocations: 302 MB / 84.39 GB, free: 314.3 MB / 2.625 GB Notification: Performance of partitionIndependentBlocks (initialization_lambda0): time 1.823/307.2, allocations: 271.5 MB / 84.66 GB, free: 0.7686 GB / 2.625 GB Notification: Performance of analyzeInitialSystem (initialization_lambda0): time 13.77/321, allocations: 2.288 GB / 86.95 GB, free: 433.1 MB / 2.625 GB Notification: Performance of solveInitialSystemEqSystem (initialization_lambda0): time 0.002491/321, allocations: 392 kB / 86.95 GB, free: 432.7 MB / 2.625 GB Notification: Performance of matching and sorting (n=41915) (initialization_lambda0): time 2.479/323.5, allocations: 0.526 GB / 87.47 GB, free: 0.6565 GB / 2.625 GB Notification: Performance of prepare postOptimizeDAE: time 0.004287/323.5, allocations: 0.612 MB / 87.47 GB, free: 0.6565 GB / 2.625 GB Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.01718/323.5, allocations: 5.032 MB / 87.48 GB, free: 0.6564 GB / 2.625 GB Notification: Performance of postOpt tearingSystem (initialization): time 0.9337/324.4, allocations: 89.38 MB / 87.57 GB, free: 0.6449 GB / 2.625 GB Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.3812/324.8, allocations: 57.13 MB / 87.62 GB, free: 0.6309 GB / 2.625 GB Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 1.653/326.5, allocations: 0.4994 GB / 88.12 GB, free: 0.5028 GB / 2.625 GB Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.315/326.8, allocations: 10.14 MB / 88.13 GB, free: 0.5027 GB / 2.625 GB Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.07488/326.8, allocations: 11.66 MB / 88.14 GB, free: 0.5027 GB / 2.625 GB Warning: Assuming fixed start value for the following 308 variables: inertia.phi:VARIABLE(start = 0.0 unit = \"rad\" fixed = true ) \"Absolute rotation angle of component\" type: Real burner1.p:VARIABLE(min = 0.0 start = burner1.p_start_flueGas_out unit = \"Pa\" fixed = true nominal = 1e5 ) \"Pressure inside volume\" type: Real burner2.p:VARIABLE(min = 0.0 start = burner2.p_start_flueGas_out unit = \"Pa\" fixed = true nominal = 1e5 ) \"Pressure inside volume\" type: Real burner3.p:VARIABLE(min = 0.0 start = burner3.p_start_flueGas_out unit = \"Pa\" fixed = true nominal = 1e5 ) \"Pressure inside volume\" type: Real flameRoom_evap_1.p:VARIABLE(min = 0.0 start = flameRoom_evap_1.p_start_flueGas_out unit = \"Pa\" fixed = true nominal = 1e5 ) \"Pressure inside volume\" type: Real flameRoom_rh_2.p:VARIABLE(min = 0.0 start = flameRoom_rh_2.p_start_flueGas_out unit = \"Pa\" fixed = true nominal = 1e5 ) \"Pressure inside volume\" type: Real burner4.p:VARIABLE(min = 0.0 start = burner4.p_start_flueGas_out unit = \"Pa\" fixed = true nominal = 1e5 ) \"Pressure inside volume\" type: Real flameRoom_evap_2.p:VARIABLE(min = 0.0 start = flameRoom_evap_2.p_start_flueGas_out unit = \"Pa\" fixed = true nominal = 1e5 ) \"Pressure inside volume\" type: Real flameRoom_sh_1.p:VARIABLE(min = 0.0 start = flameRoom_sh_1.p_start_flueGas_out unit = \"Pa\" fixed = true nominal = 1e5 ) \"Pressure inside volume\" type: Real flameRoom_sh_2.p:VARIABLE(min = 0.0 start = flameRoom_sh_2.p_start_flueGas_out unit = \"Pa\" fixed = true nominal = 1e5 ) \"Pressure inside volume\" type: Real flameRoom_sh_4.p:VARIABLE(min = 0.0 start = flameRoom_sh_4.p_start_flueGas_out unit = \"Pa\" fixed = true nominal = 1e5 ) \"Pressure inside volume\" type: Real flameRoom_sh_3.p:VARIABLE(min = 0.0 start = flameRoom_sh_3.p_start_flueGas_out unit = \"Pa\" fixed = true nominal = 1e5 ) \"Pressure inside volume\" type: Real flameRoom_rh_1.p:VARIABLE(min = 0.0 start = flameRoom_rh_1.p_start_flueGas_out unit = \"Pa\" fixed = true nominal = 1e5 ) \"Pressure inside volume\" type: Real flameRoom_eco.p:VARIABLE(min = 0.0 start = flameRoom_eco.p_start_flueGas_out unit = \"Pa\" fixed = true nominal = 1e5 ) \"Pressure inside volume\" type: Real evap_1.h[1]:VARIABLE(start = evap_1.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] evap_1.h[2]:VARIABLE(start = evap_1.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] evap_1.h[3]:VARIABLE(start = evap_1.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] evap_1.h[4]:VARIABLE(start = evap_1.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] evap_1.h[5]:VARIABLE(start = evap_1.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] evap_1.p[1]:VARIABLE(min = 0.0 start = evap_1.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] evap_1.p[2]:VARIABLE(min = 0.0 start = evap_1.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] evap_1.p[3]:VARIABLE(min = 0.0 start = evap_1.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] evap_1.p[4]:VARIABLE(min = 0.0 start = evap_1.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] evap_1.p[5]:VARIABLE(min = 0.0 start = evap_1.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] evap_2.h[1]:VARIABLE(start = evap_2.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [4] evap_2.h[2]:VARIABLE(start = evap_2.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [4] evap_2.h[3]:VARIABLE(start = evap_2.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [4] evap_2.h[4]:VARIABLE(start = evap_2.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [4] evap_2.p[1]:VARIABLE(min = 0.0 start = evap_2.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [4] evap_2.p[2]:VARIABLE(min = 0.0 start = evap_2.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [4] evap_2.p[3]:VARIABLE(min = 0.0 start = evap_2.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [4] evap_2.p[4]:VARIABLE(min = 0.0 start = evap_2.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [4] evap_3.h[1]:VARIABLE(start = evap_3.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [4] evap_3.h[2]:VARIABLE(start = evap_3.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [4] evap_3.h[3]:VARIABLE(start = evap_3.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [4] evap_3.h[4]:VARIABLE(start = evap_3.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [4] evap_3.p[1]:VARIABLE(min = 0.0 start = evap_3.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [4] evap_3.p[2]:VARIABLE(min = 0.0 start = evap_3.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [4] evap_3.p[3]:VARIABLE(min = 0.0 start = evap_3.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [4] evap_3.p[4]:VARIABLE(min = 0.0 start = evap_3.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [4] evap_4.h[1]:VARIABLE(start = evap_4.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [3] evap_4.h[2]:VARIABLE(start = evap_4.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [3] evap_4.h[3]:VARIABLE(start = evap_4.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [3] evap_4.p[1]:VARIABLE(min = 0.0 start = evap_4.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [3] evap_4.p[2]:VARIABLE(min = 0.0 start = evap_4.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [3] evap_4.p[3]:VARIABLE(min = 0.0 start = evap_4.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [3] sh_1.h[1]:VARIABLE(start = sh_1.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_1.h[2]:VARIABLE(start = sh_1.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_1.h[3]:VARIABLE(start = sh_1.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_1.h[4]:VARIABLE(start = sh_1.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_1.h[5]:VARIABLE(start = sh_1.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_1.p[1]:VARIABLE(min = 0.0 start = sh_1.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_1.p[2]:VARIABLE(min = 0.0 start = sh_1.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_1.p[3]:VARIABLE(min = 0.0 start = sh_1.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_1.p[4]:VARIABLE(min = 0.0 start = sh_1.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_1.p[5]:VARIABLE(min = 0.0 start = sh_1.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_2.h[1]:VARIABLE(start = sh_2.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_2.h[2]:VARIABLE(start = sh_2.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_2.h[3]:VARIABLE(start = sh_2.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_2.h[4]:VARIABLE(start = sh_2.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_2.h[5]:VARIABLE(start = sh_2.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_2.p[1]:VARIABLE(min = 0.0 start = sh_2.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_2.p[2]:VARIABLE(min = 0.0 start = sh_2.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_2.p[3]:VARIABLE(min = 0.0 start = sh_2.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_2.p[4]:VARIABLE(min = 0.0 start = sh_2.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_2.p[5]:VARIABLE(min = 0.0 start = sh_2.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_3.h[1]:VARIABLE(start = sh_3.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_3.h[2]:VARIABLE(start = sh_3.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_3.h[3]:VARIABLE(start = sh_3.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_3.h[4]:VARIABLE(start = sh_3.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_3.h[5]:VARIABLE(start = sh_3.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_3.p[1]:VARIABLE(min = 0.0 start = sh_3.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_3.p[2]:VARIABLE(min = 0.0 start = sh_3.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_3.p[3]:VARIABLE(min = 0.0 start = sh_3.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_3.p[4]:VARIABLE(min = 0.0 start = sh_3.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_3.p[5]:VARIABLE(min = 0.0 start = sh_3.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_4.h[1]:VARIABLE(start = sh_4.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_4.h[2]:VARIABLE(start = sh_4.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_4.h[3]:VARIABLE(start = sh_4.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_4.h[4]:VARIABLE(start = sh_4.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_4.h[5]:VARIABLE(start = sh_4.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_4.p[1]:VARIABLE(min = 0.0 start = sh_4.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_4.p[2]:VARIABLE(min = 0.0 start = sh_4.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_4.p[3]:VARIABLE(min = 0.0 start = sh_4.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_4.p[4]:VARIABLE(min = 0.0 start = sh_4.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_4.p[5]:VARIABLE(min = 0.0 start = sh_4.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] eco.h[1]:VARIABLE(start = eco.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] eco.h[2]:VARIABLE(start = eco.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] eco.h[3]:VARIABLE(start = eco.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] eco.h[4]:VARIABLE(start = eco.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] eco.h[5]:VARIABLE(start = eco.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] eco.p[1]:VARIABLE(min = 0.0 start = eco.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] eco.p[2]:VARIABLE(min = 0.0 start = eco.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] eco.p[3]:VARIABLE(min = 0.0 start = eco.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] eco.p[4]:VARIABLE(min = 0.0 start = eco.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] eco.p[5]:VARIABLE(min = 0.0 start = eco.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] rh_1.h[1]:VARIABLE(start = rh_1.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] rh_1.h[2]:VARIABLE(start = rh_1.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] rh_1.h[3]:VARIABLE(start = rh_1.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] rh_1.h[4]:VARIABLE(start = rh_1.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] rh_1.h[5]:VARIABLE(start = rh_1.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] rh_1.p[1]:VARIABLE(min = 0.0 start = rh_1.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] rh_1.p[2]:VARIABLE(min = 0.0 start = rh_1.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] rh_1.p[3]:VARIABLE(min = 0.0 start = rh_1.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] rh_1.p[4]:VARIABLE(min = 0.0 start = rh_1.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] rh_1.p[5]:VARIABLE(min = 0.0 start = rh_1.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] rh_2.h[1]:VARIABLE(start = rh_2.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] rh_2.h[2]:VARIABLE(start = rh_2.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] rh_2.h[3]:VARIABLE(start = rh_2.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] rh_2.h[4]:VARIABLE(start = rh_2.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] rh_2.h[5]:VARIABLE(start = rh_2.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] rh_2.p[1]:VARIABLE(min = 0.0 start = rh_2.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] rh_2.p[2]:VARIABLE(min = 0.0 start = rh_2.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] rh_2.p[3]:VARIABLE(min = 0.0 start = rh_2.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] rh_2.p[4]:VARIABLE(min = 0.0 start = rh_2.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] rh_2.p[5]:VARIABLE(min = 0.0 start = rh_2.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] evap_0.h[1]:VARIABLE(start = evap_0.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [4] evap_0.h[2]:VARIABLE(start = evap_0.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [4] evap_0.h[3]:VARIABLE(start = evap_0.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [4] evap_0.h[4]:VARIABLE(start = evap_0.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [4] evap_0.p[1]:VARIABLE(min = 0.0 start = evap_0.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [4] evap_0.p[2]:VARIABLE(min = 0.0 start = evap_0.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [4] evap_0.p[3]:VARIABLE(min = 0.0 start = evap_0.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [4] evap_0.p[4]:VARIABLE(min = 0.0 start = evap_0.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [4] ct_1.h[1]:VARIABLE(start = ct_1.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [7] ct_1.h[2]:VARIABLE(start = ct_1.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [7] ct_1.h[3]:VARIABLE(start = ct_1.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [7] ct_1.h[4]:VARIABLE(start = ct_1.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [7] ct_1.h[5]:VARIABLE(start = ct_1.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [7] ct_1.h[6]:VARIABLE(start = ct_1.mechanicalEquilibrium.h_start[6] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [7] ct_1.h[7]:VARIABLE(start = ct_1.mechanicalEquilibrium.h_start[7] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [7] ct_1.p[1]:VARIABLE(min = 0.0 start = ct_1.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [7] ct_1.p[2]:VARIABLE(min = 0.0 start = ct_1.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [7] ct_1.p[3]:VARIABLE(min = 0.0 start = ct_1.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [7] ct_1.p[4]:VARIABLE(min = 0.0 start = ct_1.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [7] ct_1.p[5]:VARIABLE(min = 0.0 start = ct_1.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [7] ct_1.p[6]:VARIABLE(min = 0.0 start = ct_1.p_start_internal[6] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [7] ct_1.p[7]:VARIABLE(min = 0.0 start = ct_1.p_start_internal[7] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [7] mill4.mass_rct:VARIABLE(min = 0.0 start = mill4.mass_rct_start unit = \"kg\" fixed = true nominal = 1.0 protected = true ) \"Mass of raw coal on the table\" type: Real mill4.mass_pct:VARIABLE(min = 0.0 start = mill4.mass_pct_start unit = \"kg\" fixed = true nominal = 1.0 protected = true ) \"Mass of pulverized coal on the table\" type: Real mill4.mass_pca:VARIABLE(min = 0.0 start = mill4.mass_pca_start unit = \"kg\" fixed = true nominal = 1.0 protected = true ) \"Mass of pulverized coal carried by primary air\" type: Real mill4.T_out:VARIABLE(min = 0.0 start = mill4.T_out_start unit = \"K\" fixed = true nominal = 300.0 protected = true ) \"Classifier Temperature (outlet temperature)\" type: Real mill1.mass_rct:VARIABLE(min = 0.0 start = mill1.mass_rct_start unit = \"kg\" fixed = true nominal = 1.0 protected = true ) \"Mass of raw coal on the table\" type: Real mill1.mass_pct:VARIABLE(min = 0.0 start = mill1.mass_pct_start unit = \"kg\" fixed = true nominal = 1.0 protected = true ) \"Mass of pulverized coal on the table\" type: Real mill1.mass_pca:VARIABLE(min = 0.0 start = mill1.mass_pca_start unit = \"kg\" fixed = true nominal = 1.0 protected = true ) \"Mass of pulverized coal carried by primary air\" type: Real mill1.T_out:VARIABLE(min = 0.0 start = mill1.T_out_start unit = \"K\" fixed = true nominal = 300.0 protected = true ) \"Classifier Temperature (outlet temperature)\" type: Real mill2.mass_rct:VARIABLE(min = 0.0 start = mill2.mass_rct_start unit = \"kg\" fixed = true nominal = 1.0 protected = true ) \"Mass of raw coal on the table\" type: Real mill2.mass_pct:VARIABLE(min = 0.0 start = mill2.mass_pct_start unit = \"kg\" fixed = true nominal = 1.0 protected = true ) \"Mass of pulverized coal on the table\" type: Real mill2.mass_pca:VARIABLE(min = 0.0 start = mill2.mass_pca_start unit = \"kg\" fixed = true nominal = 1.0 protected = true ) \"Mass of pulverized coal carried by primary air\" type: Real mill2.T_out:VARIABLE(min = 0.0 start = mill2.T_out_start unit = \"K\" fixed = true nominal = 300.0 protected = true ) \"Classifier Temperature (outlet temperature)\" type: Real mill3.mass_rct:VARIABLE(min = 0.0 start = mill3.mass_rct_start unit = \"kg\" fixed = true nominal = 1.0 protected = true ) \"Mass of raw coal on the table\" type: Real mill3.mass_pct:VARIABLE(min = 0.0 start = mill3.mass_pct_start unit = \"kg\" fixed = true nominal = 1.0 protected = true ) \"Mass of pulverized coal on the table\" type: Real mill3.mass_pca:VARIABLE(min = 0.0 start = mill3.mass_pca_start unit = \"kg\" fixed = true nominal = 1.0 protected = true ) \"Mass of pulverized coal carried by primary air\" type: Real mill3.T_out:VARIABLE(min = 0.0 start = mill3.T_out_start unit = \"K\" fixed = true nominal = 300.0 protected = true ) \"Classifier Temperature (outlet temperature)\" type: Real eco_down.h[1]:VARIABLE(start = eco_down.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] eco_down.h[2]:VARIABLE(start = eco_down.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] eco_down.h[3]:VARIABLE(start = eco_down.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] eco_down.h[4]:VARIABLE(start = eco_down.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] eco_down.h[5]:VARIABLE(start = eco_down.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] eco_down.p[1]:VARIABLE(min = 0.0 start = eco_down.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] eco_down.p[2]:VARIABLE(min = 0.0 start = eco_down.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] eco_down.p[3]:VARIABLE(min = 0.0 start = eco_down.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] eco_down.p[4]:VARIABLE(min = 0.0 start = eco_down.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] eco_down.p[5]:VARIABLE(min = 0.0 start = eco_down.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] separator.h:VARIABLE(start = separator.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 protected = true ) \"spec. enthalpy state\" type: Real separator.p:VARIABLE(min = 0.0 start = separator.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real rh_pipe.h[1]:VARIABLE(start = rh_pipe.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] rh_pipe.h[2]:VARIABLE(start = rh_pipe.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] rh_pipe.h[3]:VARIABLE(start = rh_pipe.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] rh_pipe.h[4]:VARIABLE(start = rh_pipe.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] rh_pipe.h[5]:VARIABLE(start = rh_pipe.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] rh_pipe.p[1]:VARIABLE(min = 0.0 start = rh_pipe.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] rh_pipe.p[2]:VARIABLE(min = 0.0 start = rh_pipe.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] rh_pipe.p[3]:VARIABLE(min = 0.0 start = rh_pipe.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] rh_pipe.p[4]:VARIABLE(min = 0.0 start = rh_pipe.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] rh_pipe.p[5]:VARIABLE(min = 0.0 start = rh_pipe.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_pipe.h[1]:VARIABLE(start = sh_pipe.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_pipe.h[2]:VARIABLE(start = sh_pipe.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_pipe.h[3]:VARIABLE(start = sh_pipe.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_pipe.h[4]:VARIABLE(start = sh_pipe.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_pipe.h[5]:VARIABLE(start = sh_pipe.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] sh_pipe.p[1]:VARIABLE(min = 0.0 start = sh_pipe.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_pipe.p[2]:VARIABLE(min = 0.0 start = sh_pipe.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_pipe.p[3]:VARIABLE(min = 0.0 start = sh_pipe.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_pipe.p[4]:VARIABLE(min = 0.0 start = sh_pipe.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] sh_pipe.p[5]:VARIABLE(min = 0.0 start = sh_pipe.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] feedWaterTank.volume.h_liq:VARIABLE(start = feedWaterTank.volume.h_liq_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of liquid phase\" type: Real feedWaterTank.volume.h_vap:VARIABLE(start = feedWaterTank.volume.h_vap_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of vapour phase\" type: Real feedWaterTank.volume.p_vap:VARIABLE(min = 0.0 start = feedWaterTank.volume.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"Vapour pressure\" type: Real join_LP1.h:VARIABLE(start = join_LP1.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real join_LP1.p:VARIABLE(min = 0.0 start = join_LP1.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real join_HP.h:VARIABLE(start = join_HP.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real join_HP.p:VARIABLE(min = 0.0 start = Turbine_HP1.p_out_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real join_LP_main.h:VARIABLE(start = join_LP_main.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real join_LP_main.p:VARIABLE(min = 0.0 start = join_LP_main.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real split_IP2.h:VARIABLE(start = split_IP2.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real split_IP2.p:VARIABLE(min = 0.0 start = split_IP2.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real join_IP3.h:VARIABLE(start = join_IP3.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real join_IP3.p:VARIABLE(min = 0.0 start = join_IP3.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real join_LP2.h:VARIABLE(start = join_LP2.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real join_LP2.p:VARIABLE(min = 0.0 start = join_LP2.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real join_LP3.h:VARIABLE(start = join_LP3.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real join_LP3.p:VARIABLE(min = 0.0 start = join_LP3.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real preheater_LP2.tubes.h:VARIABLE(start = preheater_LP2.tubes.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 protected = true ) \"spec. enthalpy state\" type: Real preheater_LP2.tubes.p:VARIABLE(min = 0.0 start = preheater_LP2.tubes.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real preheater_LP2.shell.h_liq:VARIABLE(start = preheater_LP2.shell.h_liq_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of liquid phase\" type: Real preheater_LP2.shell.h_vap:VARIABLE(start = preheater_LP2.shell.h_vap_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of vapour phase\" type: Real preheater_LP2.shell.p_vap:VARIABLE(min = 0.0 start = preheater_LP2.shell.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"Vapour pressure\" type: Real preheater_LP3.tubes.h:VARIABLE(start = preheater_LP3.tubes.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 protected = true ) \"spec. enthalpy state\" type: Real preheater_LP3.tubes.p:VARIABLE(min = 0.0 start = preheater_LP3.tubes.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real preheater_LP3.shell.h_liq:VARIABLE(start = preheater_LP3.shell.h_liq_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of liquid phase\" type: Real preheater_LP3.shell.h_vap:VARIABLE(start = preheater_LP3.shell.h_vap_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of vapour phase\" type: Real preheater_LP3.shell.p_vap:VARIABLE(min = 0.0 start = preheater_LP3.shell.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"Vapour pressure\" type: Real join_preheater_LP3.h:VARIABLE(start = join_preheater_LP3.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real join_preheater_LP3.p:VARIABLE(min = 0.0 start = join_preheater_LP3.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real downComer_feedWaterTank.h[1]:VARIABLE(start = downComer_feedWaterTank.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [3] downComer_feedWaterTank.h[2]:VARIABLE(start = downComer_feedWaterTank.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [3] downComer_feedWaterTank.h[3]:VARIABLE(start = downComer_feedWaterTank.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [3] downComer_feedWaterTank.p[1]:VARIABLE(min = 0.0 start = downComer_feedWaterTank.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [3] downComer_feedWaterTank.p[2]:VARIABLE(min = 0.0 start = downComer_feedWaterTank.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [3] downComer_feedWaterTank.p[3]:VARIABLE(min = 0.0 start = downComer_feedWaterTank.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [3] eco_riser.h[1]:VARIABLE(start = eco_riser.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] eco_riser.h[2]:VARIABLE(start = eco_riser.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] eco_riser.h[3]:VARIABLE(start = eco_riser.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] eco_riser.h[4]:VARIABLE(start = eco_riser.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] eco_riser.h[5]:VARIABLE(start = eco_riser.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] eco_riser.p[1]:VARIABLE(min = 0.0 start = eco_riser.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] eco_riser.p[2]:VARIABLE(min = 0.0 start = eco_riser.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] eco_riser.p[3]:VARIABLE(min = 0.0 start = eco_riser.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] eco_riser.p[4]:VARIABLE(min = 0.0 start = eco_riser.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] eco_riser.p[5]:VARIABLE(min = 0.0 start = eco_riser.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] splitVLE_L2_flex.h:VARIABLE(start = splitVLE_L2_flex.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real splitVLE_L2_flex.p:VARIABLE(min = 0.0 start = splitVLE_L2_flex.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real regenerativeAirPreheater.flueGasCell.h[1]:VARIABLE(start = regenerativeAirPreheater.flueGasCell.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [5] regenerativeAirPreheater.flueGasCell.h[2]:VARIABLE(start = regenerativeAirPreheater.flueGasCell.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [5] regenerativeAirPreheater.flueGasCell.h[3]:VARIABLE(start = regenerativeAirPreheater.flueGasCell.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [5] regenerativeAirPreheater.flueGasCell.h[4]:VARIABLE(start = regenerativeAirPreheater.flueGasCell.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [5] regenerativeAirPreheater.flueGasCell.h[5]:VARIABLE(start = regenerativeAirPreheater.flueGasCell.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [5] regenerativeAirPreheater.flueGasCell.p[1]:VARIABLE(min = 0.0 start = regenerativeAirPreheater.flueGasCell.p_start[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] regenerativeAirPreheater.flueGasCell.p[2]:VARIABLE(min = 0.0 start = regenerativeAirPreheater.flueGasCell.p_start[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] regenerativeAirPreheater.flueGasCell.p[3]:VARIABLE(min = 0.0 start = regenerativeAirPreheater.flueGasCell.p_start[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] regenerativeAirPreheater.flueGasCell.p[4]:VARIABLE(min = 0.0 start = regenerativeAirPreheater.flueGasCell.p_start[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] regenerativeAirPreheater.freshAirCell.h[1]:VARIABLE(start = regenerativeAirPreheater.freshAirCell.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [5] regenerativeAirPreheater.freshAirCell.h[2]:VARIABLE(start = regenerativeAirPreheater.freshAirCell.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [5] regenerativeAirPreheater.freshAirCell.h[3]:VARIABLE(start = regenerativeAirPreheater.freshAirCell.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [5] regenerativeAirPreheater.freshAirCell.h[4]:VARIABLE(start = regenerativeAirPreheater.freshAirCell.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [5] regenerativeAirPreheater.freshAirCell.h[5]:VARIABLE(start = regenerativeAirPreheater.freshAirCell.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [5] regenerativeAirPreheater.freshAirCell.p[1]:VARIABLE(min = 0.0 start = regenerativeAirPreheater.freshAirCell.p_start[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] regenerativeAirPreheater.freshAirCell.p[2]:VARIABLE(min = 0.0 start = regenerativeAirPreheater.freshAirCell.p_start[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] regenerativeAirPreheater.freshAirCell.p[3]:VARIABLE(min = 0.0 start = regenerativeAirPreheater.freshAirCell.p_start[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] regenerativeAirPreheater.freshAirCell.p[4]:VARIABLE(min = 0.0 start = regenerativeAirPreheater.freshAirCell.p_start[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] regenerativeAirPreheater.freshAirCell.p[5]:VARIABLE(min = 0.0 start = regenerativeAirPreheater.freshAirCell.p_start[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] regenerativeAirPreheater.freshAirLeakage_join.bulk.h:VARIABLE(start = regenerativeAirPreheater.freshAirLeakage_join.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Specific enthalpy\" type: Real regenerativeAirPreheater.freshAirLeakage_join.bulk.xi[1]:VARIABLE(min = 0.0 max = 1.0 start = regenerativeAirPreheater.freshAirLeakage_join.xi_start[1] unit = \"1\" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer ) \"Mass fraction\" type: Real [9] regenerativeAirPreheater.freshAirLeakage_join.bulk.xi[2]:VARIABLE(min = 0.0 max = 1.0 start = regenerativeAirPreheater.freshAirLeakage_join.xi_start[2] unit = \"1\" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer ) \"Mass fraction\" type: Real [9] regenerativeAirPreheater.freshAirLeakage_join.bulk.xi[3]:VARIABLE(min = 0.0 max = 1.0 start = regenerativeAirPreheater.freshAirLeakage_join.xi_start[3] unit = \"1\" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer ) \"Mass fraction\" type: Real [9] regenerativeAirPreheater.freshAirLeakage_join.bulk.xi[4]:VARIABLE(min = 0.0 max = 1.0 start = regenerativeAirPreheater.freshAirLeakage_join.xi_start[4] unit = \"1\" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer ) \"Mass fraction\" type: Real [9] regenerativeAirPreheater.freshAirLeakage_join.bulk.xi[5]:VARIABLE(min = 0.0 max = 1.0 start = regenerativeAirPreheater.freshAirLeakage_join.xi_start[5] unit = \"1\" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer ) \"Mass fraction\" type: Real [9] regenerativeAirPreheater.freshAirLeakage_join.bulk.xi[6]:VARIABLE(min = 0.0 max = 1.0 start = regenerativeAirPreheater.freshAirLeakage_join.xi_start[6] unit = \"1\" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer ) \"Mass fraction\" type: Real [9] regenerativeAirPreheater.freshAirLeakage_join.bulk.xi[7]:VARIABLE(min = 0.0 max = 1.0 start = regenerativeAirPreheater.freshAirLeakage_join.xi_start[7] unit = \"1\" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer ) \"Mass fraction\" type: Real [9] regenerativeAirPreheater.freshAirLeakage_join.bulk.xi[8]:VARIABLE(min = 0.0 max = 1.0 start = regenerativeAirPreheater.freshAirLeakage_join.xi_start[8] unit = \"1\" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer ) \"Mass fraction\" type: Real [9] regenerativeAirPreheater.freshAirLeakage_join.bulk.xi[9]:VARIABLE(min = 0.0 max = 1.0 start = regenerativeAirPreheater.freshAirLeakage_join.xi_start[9] unit = \"1\" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer ) \"Mass fraction\" type: Real [9] splitGas_L2_flex.bulk.p:VARIABLE(min = 0.0 start = splitGas_L2_flex.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer protected = true ) \"Pressure\" type: Real splitGas_L2_flex.bulk.h:VARIABLE(start = splitGas_L2_flex.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Specific enthalpy\" type: Real splitGas_L2_flex.bulk.xi[1]:VARIABLE(min = 0.0 max = 1.0 start = splitGas_L2_flex.xi_start[1] unit = \"1\" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer protected = true ) \"Mass fraction\" type: Real [9] splitGas_L2_flex.bulk.xi[2]:VARIABLE(min = 0.0 max = 1.0 start = splitGas_L2_flex.xi_start[2] unit = \"1\" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer protected = true ) \"Mass fraction\" type: Real [9] splitGas_L2_flex.bulk.xi[3]:VARIABLE(min = 0.0 max = 1.0 start = splitGas_L2_flex.xi_start[3] unit = \"1\" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer protected = true ) \"Mass fraction\" type: Real [9] splitGas_L2_flex.bulk.xi[4]:VARIABLE(min = 0.0 max = 1.0 start = splitGas_L2_flex.xi_start[4] unit = \"1\" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer protected = true ) \"Mass fraction\" type: Real [9] splitGas_L2_flex.bulk.xi[5]:VARIABLE(min = 0.0 max = 1.0 start = splitGas_L2_flex.xi_start[5] unit = \"1\" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer protected = true ) \"Mass fraction\" type: Real [9] splitGas_L2_flex.bulk.xi[6]:VARIABLE(min = 0.0 max = 1.0 start = splitGas_L2_flex.xi_start[6] unit = \"1\" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer protected = true ) \"Mass fraction\" type: Real [9] splitGas_L2_flex.bulk.xi[7]:VARIABLE(min = 0.0 max = 1.0 start = splitGas_L2_flex.xi_start[7] unit = \"1\" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer protected = true ) \"Mass fraction\" type: Real [9] splitGas_L2_flex.bulk.xi[8]:VARIABLE(min = 0.0 max = 1.0 start = splitGas_L2_flex.xi_start[8] unit = \"1\" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer protected = true ) \"Mass fraction\" type: Real [9] splitGas_L2_flex.bulk.xi[9]:VARIABLE(min = 0.0 max = 1.0 start = splitGas_L2_flex.xi_start[9] unit = \"1\" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer protected = true ) \"Mass fraction\" type: Real [9] PID_lambda.I.y:VARIABLE(flow=false start = PID_lambda.I.y_start_const fixed = true ) \"Connector of Real output signal\" type: Real preheater_HP.tubes.h:VARIABLE(start = preheater_HP.tubes.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 protected = true ) \"spec. enthalpy state\" type: Real preheater_HP.tubes.p:VARIABLE(min = 0.0 start = preheater_HP.tubes.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real preheater_HP.shell.h_liq:VARIABLE(start = preheater_HP.shell.h_liq_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of liquid phase\" type: Real preheater_HP.shell.h_vap:VARIABLE(start = preheater_HP.shell.h_vap_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of vapour phase\" type: Real preheater_HP.shell.p_vap:VARIABLE(min = 0.0 start = preheater_HP.shell.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"Vapour pressure\" type: Real preheater_LP4.tubes.h:VARIABLE(start = preheater_LP4.tubes.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 protected = true ) \"spec. enthalpy state\" type: Real preheater_LP4.tubes.p:VARIABLE(min = 0.0 start = preheater_LP4.tubes.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real preheater_LP4.shell.h_liq:VARIABLE(start = preheater_LP4.shell.h_liq_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of liquid phase\" type: Real preheater_LP4.shell.h_vap:VARIABLE(start = preheater_LP4.shell.h_vap_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of vapour phase\" type: Real preheater_LP4.shell.p_vap:VARIABLE(min = 0.0 start = preheater_LP4.shell.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"Vapour pressure\" type: Real preheater_LP1.tubes.h:VARIABLE(start = preheater_LP1.tubes.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 protected = true ) \"spec. enthalpy state\" type: Real preheater_LP1.tubes.p:VARIABLE(min = 0.0 start = preheater_LP1.tubes.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real preheater_LP1.shell.h_liq:VARIABLE(start = preheater_LP1.shell.h_liq_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of liquid phase\" type: Real preheater_LP1.shell.h_vap:VARIABLE(start = preheater_LP1.shell.h_vap_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of vapour phase\" type: Real preheater_LP1.shell.p_vap:VARIABLE(min = 0.0 start = preheater_LP1.shell.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"Vapour pressure\" type: Real condenser.tubes.h:VARIABLE(start = condenser.tubes.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 protected = true ) \"spec. enthalpy state\" type: Real condenser.tubes.p:VARIABLE(min = 0.0 start = condenser.tubes.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real condenser.shell.h_liq:VARIABLE(start = condenser.shell.h_liq_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of liquid phase\" type: Real condenser.shell.h_vap:VARIABLE(start = condenser.shell.h_vap_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of vapour phase\" type: Real condenser.shell.p_vap:VARIABLE(min = 0.0 start = condenser.shell.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"Vapour pressure\" type: Real sprayInjector_sh2.h:VARIABLE(start = sprayInjector_sh2.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real sprayInjector_sh2.p:VARIABLE(min = 0.0 start = sprayInjector_sh2.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real sprayInjector_sh4.h:VARIABLE(start = sprayInjector_sh4.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real sprayInjector_sh4.p:VARIABLE(min = 0.0 start = sprayInjector_sh4.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real sprayInjector_sh1.h:VARIABLE(start = sprayInjector_sh1.h_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) type: Real sprayInjector_sh1.p:VARIABLE(min = 0.0 start = sprayInjector_sh1.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"System pressure\" type: Real PI_feedwaterPump.switch_OnOff.u2:DISCRETE(flow=false fixed = true ) \"Connector of Boolean input signal\" type: Boolean PID_lambda.switch_OnOff.u2:DISCRETE(flow=false fixed = true ) \"Connector of Boolean input signal\" type: Boolean PI_Pump_cond.switch_OnOff.u2:DISCRETE(flow=false fixed = true ) \"Connector of Boolean input signal\" type: Boolean PID_preheaterLP2.switch_OnOff.u2:DISCRETE(flow=false fixed = true ) \"Connector of Boolean input signal\" type: Boolean PID_preheaterLP3.switch_OnOff.u2:DISCRETE(flow=false fixed = true ) \"Connector of Boolean input signal\" type: Boolean PID_preheaterLP4.switch_OnOff.u2:DISCRETE(flow=false fixed = true ) \"Connector of Boolean input signal\" type: Boolean PID_preheaterLP1.switch_OnOff.u2:DISCRETE(flow=false fixed = true ) \"Connector of Boolean input signal\" type: Boolean PI_valveControl_preheater_HP.switch_OnOff.u2:DISCRETE(flow=false fixed = true ) \"Connector of Boolean input signal\" type: Boolean Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 6261 * Number of states: 0 () * Number of discrete variables: 66 ($PRE.PI_feedwaterPump.time_lag_I_activation.entryTime,$PRE.PI_feedwaterPump.switch_OnOff.u2,$PRE.PID_lambda.time_lag_I_activation.entryTime,$PRE.PID_lambda.switch_OnOff.u2,$PRE.PI_Pump_cond.time_lag_I_activation.entryTime,$PRE.PI_Pump_cond.switch_OnOff.u2,$PRE.PID_preheaterLP2.time_lag_I_activation.entryTime,$PRE.PID_preheaterLP2.switch_OnOff.u2,$PRE.PID_preheaterLP3.time_lag_I_activation.entryTime,$PRE.PID_preheaterLP3.switch_OnOff.u2,$PRE.PID_preheaterLP4.time_lag_I_activation.entryTime,$PRE.PID_preheaterLP4.switch_OnOff.u2,$PRE.PID_preheaterLP1.time_lag_I_activation.entryTime,$PRE.PID_preheaterLP1.switch_OnOff.u2,$PRE.PI_valveControl_preheater_HP.time_lag_I_activation.entryTime,$PRE.PI_valveControl_preheater_HP.switch_OnOff.u2,valveControl_preheater_HP.pressureLoss.normIsValid,valve_HP.pressureLoss.normIsValid,valve_IP3.pressureLoss.normIsValid,PI_feedwaterPump.I_activation.y,PI_feedwaterPump.time_lag_I_activation.entryTime,PI_feedwaterPump.switch_OnOff.u2,PID_lambda.I_activation.y,PID_lambda.time_lag_I_activation.entryTime,PID_lambda.switch_OnOff.u2,PI_Pump_cond.I_activation.y,PI_Pump_cond.time_lag_I_activation.entryTime,PI_Pump_cond.switch_OnOff.u2,PTarget.nextEventScaled,PTarget.nextEvent,$PRE.PTarget.nextEvent,PTarget.last,PTarget.b,PTarget.a,PID_preheaterLP2.I_activation.y,PID_preheaterLP2.time_lag_I_activation.entryTime,PID_preheaterLP2.switch_OnOff.u2,PID_preheaterLP3.I_activation.y,PID_preheaterLP3.time_lag_I_activation.entryTime,PID_preheaterLP3.switch_OnOff.u2,PID_preheaterLP4.I_activation.y,PID_preheaterLP4.time_lag_I_activation.entryTime,PID_preheaterLP4.switch_OnOff.u2,PID_preheaterLP1.I_activation.y,PID_preheaterLP1.time_lag_I_activation.entryTime,PID_preheaterLP1.switch_OnOff.u2,PI_valveControl_preheater_HP.I_activation.y,PI_valveControl_preheater_HP.time_lag_I_activation.entryTime,PI_valveControl_preheater_HP.switch_OnOff.u2,$whenCondition1,$whenCondition2,$whenCondition3,$whenCondition4,$whenCondition5,$whenCondition6,$whenCondition7,$whenCondition8,$whenCondition9,$whenCondition10,$whenCondition11,$whenCondition12,$whenCondition13,$whenCondition14,$whenCondition15,$whenCondition16,$whenCondition17) * Number of discrete states: 0 () * Number of clocked states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (29512): * Single equations (assignments): 27756 * Array equations: 0 * Algorithm blocks: 1 * Record equations: 1456 * When equations: 0 * If-equations: 0 * Equation systems (not torn): 20 * Torn equation systems: 279 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details (not torn): * Constant Jacobian (size): 0 systems * Linear Jacobian (size,density): 0 systems * Non-linear Jacobian (size): 20 systems {1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1} * Without analytic Jacobian (size): 0 systems Notification: Torn system details for strict tearing set: * Linear torn systems (#iteration vars, #inner vars, density): 221 systems {(1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,2,100.0%), (1,2,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (4,3,87.5%), (1,1,100.0%), (4,3,87.5%), (4,3,87.5%), (1,1,100.0%), (1,1,100.0%), (1,3,100.0%), (4,3,87.5%), (1,1,100.0%), (1,1,100.0%), (4,3,87.5%), (1,4,100.0%), (1,2,100.0%), (4,3,87.5%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (4,3,87.5%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,3,100.0%), (1,4,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,7,100.0%), (1,1,100.0%)} * Non-linear torn systems (#iteration vars, #inner vars): 58 systems {(1,17), (1,17), (1,17), (1,17), (1,17), (1,8), (1,4), (1,4), (1,4), (1,4), (1,4), (1,8), (1,1), (4,49), (1,6), (1,6), (1,6), (1,6), (1,6), (1,6), (1,6), (1,6), (1,6), (1,6), (1,11), (1,6), (1,6), (1,11), (1,1), (1,22), (2,34), (5,14), (1,2), (5,13), (5,13), (2,5), (5,14), (1,5), (1,80), (1,7), (1,3), (5,15), (1,19), (1,13), (1,7), (1,6), (1,2), (1,3), (1,3), (1,3), (1,3), (1,3), (1,3), (1,80), (1,6), (2,20), (2,20), (2,20)} Notification: Performance of prepare postOptimizeDAE: time 0.1603/327, allocations: 15.73 MB / 88.16 GB, free: 0.5015 GB / 2.625 GB Notification: Performance of postOpt lateInlineFunction (simulation): time 0.1526/327.2, allocations: 31.62 MB / 88.19 GB, free: 0.5015 GB / 2.625 GB Notification: Performance of postOpt wrapFunctionCalls (simulation): time 1.178/328.3, allocations: 0.5082 GB / 88.7 GB, free: 336.5 MB / 2.625 GB Notification: Performance of postOpt simplifysemiLinear (simulation): time 2.031/330.4, allocations: 371.9 MB / 89.06 GB, free: 0.747 GB / 2.625 GB Notification: Performance of postOpt simplifyComplexFunction (simulation): time 0.01376/330.4, allocations: 4.069 MB / 89.06 GB, free: 0.7469 GB / 2.625 GB Notification: Performance of postOpt removeConstants (simulation): time 1.101/331.5, allocations: 460.1 MB / 89.51 GB, free: 0.5391 GB / 2.625 GB Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.1318/331.6, allocations: 3.993 MB / 89.52 GB, free: 0.5354 GB / 2.625 GB Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.232/331.8, allocations: 6.234 MB / 89.52 GB, free: 0.5307 GB / 2.625 GB Notification: Performance of postOpt findZeroCrossings (simulation): time 0.06662/331.9, allocations: 12.9 MB / 89.54 GB, free: 0.5199 GB / 2.625 GB [/var/lib/jenkins1/ws/OpenModelicaLibraryTestingWork_2/OpenModelica/OMCompiler/Compiler/BackEnd/DAEMode.mo:528:7-530:90:writable] Error: Internal error DAEMode.traverserStrongComponents failed on equation: 1/1 (24): (hopper.rho_bulk_del, hopper.bulk.kappa, hopper.bulk.drhodp_hxi, hopper.bulk.drhodh_pxi, hopper.bulk.drhodxi_ph, hopper.bulk.p_i, hopper.bulk.xi_gas) = TILMedia.Internals.GasObjectFunctions.additionalProperties_pTxi(hopper.bulk.p, hopper.T_bulk_del, {hopper.xi_flueGas[1], hopper.xi_flueGas[2], hopper.xi_flueGas[3], hopper.xi_flueGas[4], hopper.xi_flueGas[5], hopper.xi_flueGas[6], hopper.xi_flueGas[7], hopper.xi_flueGas[8], hopper.xi_flueGas[9]}, hopper.bulk.gasPointer) Variables: 1: hopper.bulk.p_i[6]:VARIABLE(min = 0.0 unit = \"Pa\" nominal = 1e5 ) \"Partial pressure\" type: Real [10] 2: hopper.bulk.p_i[5]:VARIABLE(min = 0.0 unit = \"Pa\" nominal = 1e5 ) \"Partial pressure\" type: Real [10] 3: hopper.bulk.p_i[4]:VARIABLE(min = 0.0 unit = \"Pa\" nominal = 1e5 ) \"Partial pressure\" type: Real [10] 4: hopper.bulk.p_i[8]:VARIABLE(min = 0.0 unit = \"Pa\" nominal = 1e5 ) \"Partial pressure\" type: Real [10] 5: hopper.bulk.drhodxi_ph[4]:VARIABLE(unit = \"kg/(m3)\" ) \"Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy\" type: Real [9] 6: hopper.bulk.kappa:VARIABLE(unit = \"1/Pa\" ) \"Isothermal compressibility\" type: Real 7: hopper.bulk.drhodh_pxi:VARIABLE(unit = \"kg.s2/m5\" ) \"Derivative of density wrt specific enthalpy at constant pressure and mass fraction\" type: Real 8: hopper.bulk.drhodxi_ph[8]:VARIABLE(unit = \"kg/(m3)\" ) \"Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy\" type: Real [9] 9: hopper.bulk.drhodp_hxi:VARIABLE(unit = \"s2/m2\" ) \"Derivative of density wrt pressure at specific enthalpy and mass fraction\" type: Real 10: hopper.bulk.drhodxi_ph[9]:VARIABLE(unit = \"kg/(m3)\" ) \"Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy\" type: Real [9] 11: hopper.bulk.p_i[10]:VARIABLE(min = 0.0 unit = \"Pa\" nominal = 1e5 ) \"Partial pressure\" type: Real [10] 12: hopper.bulk.xi_gas:VARIABLE(min = 0.0 max = 1.0 unit = \"1\" ) \"Mass fraction of gasoues condensing component\" type: Real 13: hopper.bulk.drhodxi_ph[7]:VARIABLE(unit = \"kg/(m3)\" ) \"Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy\" type: Real [9] 14: hopper.bulk.drhodxi_ph[5]:VARIABLE(unit = \"kg/(m3)\" ) \"Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy\" type: Real [9] 15: hopper.bulk.drhodxi_ph[1]:VARIABLE(unit = \"kg/(m3)\" ) \"Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy\" type: Real [9] 16: hopper.bulk.p_i[9]:VARIABLE(min = 0.0 unit = \"Pa\" nominal = 1e5 ) \"Partial pressure\" type: Real [10] 17: hopper.bulk.drhodxi_ph[6]:VARIABLE(unit = \"kg/(m3)\" ) \"Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy\" type: Real [9] 18: hopper.bulk.p_i[2]:VARIABLE(min = 0.0 unit = \"Pa\" nominal = 1e5 ) \"Partial pressure\" type: Real [10] 19: hopper.mass:VARIABLE(min = 0.0 unit = \"kg\" nominal = 1.0 ) \"Gas mass\" type: Real 20: hopper.rho_bulk_del:VARIABLE(min = 0.0 unit = \"kg/m3\" nominal = 1000.0 ) \"Pseudo state for bulk density\" type: Real 21: hopper.bulk.p_i[3]:VARIABLE(min = 0.0 unit = \"Pa\" nominal = 1e5 ) \"Partial pressure\" type: Real [10] 22: hopper.bulk.p_i[1]:VARIABLE(min = 0.0 unit = \"Pa\" nominal = 1e5 ) \"Partial pressure\" type: Real [10] 23: hopper.bulk.p_i[7]:VARIABLE(min = 0.0 unit = \"Pa\" nominal = 1e5 ) \"Partial pressure\" type: Real [10] 24: hopper.bulk.drhodxi_ph[2]:VARIABLE(unit = \"kg/(m3)\" ) \"Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy\" type: Real [9] [/var/lib/jenkins1/ws/OpenModelicaLibraryTestingWork_2/OpenModelica/OMCompiler/Compiler/BackEnd/DAEMode.mo:528:7-530:90:writable] Error: Internal error DAEMode.traverserStrongComponents failed on equation: 1/1 (1): burner1.pressureLoss.Delta_p = burner1.pressureLoss.Delta_p_nom * burner1.iCom.m_flow_in / burner1.iCom.m_flow_nom 2/2 (1): burner1.iCom.m_flow_in = mill1.summary.m_flow_coal_out - hopper.m_flow_out_del 3/3 (1): -mill1.summary.m_flow_coal_out = (-mill1.m_flow_dc_out) * /*Real*/(mill1.N_mills) 4/4 (1): mill1.m_flow_dc_out = mill1.m_flow_wc_out - mill1.m_flow_evap 5/5 (1): mill1.gasOut.xi[8] = (mill1.m_flow_air_in * splitGas_L2_flex.bulk.xi[8] + mill1.m_flow_evap) / mill1.m_flow_air_out 6/6 (1): mill1.gasOut.humRatio = mill1.gasOut.xi[8] * (1.0 + mill1.gasOut.humRatio) 7/7 (1): mill1.gasOut.xi_dryGas[8] = mill1.gasOut.xi[9] * (1.0 + mill1.gasOut.humRatio) 8/8 (1): mill1.summary.xi_air_h2o_sat = TILMedia.Internals.GasObjectFunctions.saturationMassFraction_pTxidg(mill1.coalOut.p, mill1.T_out, mill1.gasOut.xi_dryGas, mill1.gasOut.gasPointer) 9/9 (1): mill1.gasOut.xi_dryGas[7] = mill1.gasOut.xi[7] * (1.0 + mill1.gasOut.humRatio) 10/10 (1): mill1.gasOut.xi[7] = mill1.m_flow_air_in * splitGas_L2_flex.bulk.xi[7] / mill1.m_flow_air_out 11/11 (1): mill1.Delta_p_pa = mill1.millKoeff.K_12 * abs(mill1.m_flow_air_in) * mill1.m_flow_air_in / $cse557 12/12 (1): splitGas_L2_flex.bulk.p = mill1.coalOut.p + mill1.Delta_p_pa 13/13 (1): hopper.bulk.p = mill1.coalOut.p 14/14 (1): hopper.drhodt = hopper.bulk.drhodh_pxi * der(hopper.h_flueGas_out_del) + hopper.bulk.drhodxi_ph[1] * der(hopper.xi_flueGas[1]) + hopper.bulk.drhodxi_ph[2] * der(hopper.xi_flueGas[2]) + hopper.bulk.drhodxi_ph[3] * der(hopper.xi_flueGas[3]) + hopper.bulk.drhodxi_ph[4] * der(hopper.xi_flueGas[4]) + hopper.bulk.drhodxi_ph[5] * der(hopper.xi_flueGas[5]) + hopper.bulk.drhodxi_ph[6] * der(hopper.xi_flueGas[6]) + hopper.bulk.drhodxi_ph[7] * der(hopper.xi_flueGas[7]) + hopper.bulk.drhodxi_ph[8] * der(hopper.xi_flueGas[8]) + hopper.bulk.drhodxi_ph[9] * der(hopper.xi_flueGas[9]) 15/15 (1): der(hopper.xi_flueGas[1]) = (fluelGasFlowSource_bottom.m_flow_const * (hopper.xi_flueGas_in_del[1] - hopper.xi_flueGas[1]) + hopper.m_flow_out_del * (hopper.eyeOut.xi[1] - hopper.xi_flueGas[1])) / hopper.mass 16/16 (1): der(hopper.xi_flueGas[9]) = (fluelGasFlowSource_bottom.m_flow_const * (hopper.xi_flueGas_in_del[9] - hopper.xi_flueGas[9]) + hopper.m_flow_out_del * (hopper.eyeOut.xi[9] - hopper.xi_flueGas[9])) / hopper.mass 17/17 (1): der(hopper.xi_flueGas[8]) = (fluelGasFlowSource_bottom.m_flow_const * (hopper.xi_flueGas_in_del[8] - hopper.xi_flueGas[8]) + hopper.m_flow_out_del * (hopper.eyeOut.xi[8] - hopper.xi_flueGas[8])) / hopper.mass 18/18 (1): der(hopper.xi_flueGas[7]) = (fluelGasFlowSource_bottom.m_flow_const * (hopper.xi_flueGas_in_del[7] - hopper.xi_flueGas[7]) + hopper.m_flow_out_del * (hopper.eyeOut.xi[7] - hopper.xi_flueGas[7])) / hopper.mass 19/19 (1): der(hopper.xi_flueGas[6]) = (fluelGasFlowSource_bottom.m_flow_const * (hopper.xi_flueGas_in_del[6] - hopper.xi_flueGas[6]) + hopper.m_flow_out_del * (hopper.eyeOut.xi[6] - hopper.xi_flueGas[6])) / hopper.mass 20/20 (1): der(hopper.xi_flueGas[5]) = (fluelGasFlowSource_bottom.m_flow_const * (hopper.xi_flueGas_in_del[5] - hopper.xi_flueGas[5]) + hopper.m_flow_out_del * (hopper.eyeOut.xi[5] - hopper.xi_flueGas[5])) / hopper.mass 21/21 (1): der(hopper.xi_flueGas[4]) = (fluelGasFlowSource_bottom.m_flow_const * (hopper.xi_flueGas_in_del[4] - hopper.xi_flueGas[4]) + hopper.m_flow_out_del * (hopper.eyeOut.xi[4] - hopper.xi_flueGas[4])) / hopper.mass 22/22 (1): der(hopper.xi_flueGas[3]) = (fluelGasFlowSource_bottom.m_flow_const * (hopper.xi_flueGas_in_del[3] - hopper.xi_flueGas[3]) + hopper.m_flow_out_del * (hopper.eyeOut.xi[3] - hopper.xi_flueGas[3])) / hopper.mass 23/23 (1): der(hopper.xi_flueGas[2]) = (fluelGasFlowSource_bottom.m_flow_const * (hopper.xi_flueGas_in_del[2] - hopper.xi_flueGas[2]) + hopper.m_flow_out_del * (hopper.eyeOut.xi[2] - hopper.xi_flueGas[2])) / hopper.mass 24/24 (1): fluelGasFlowSource_bottom.m_flow_const + hopper.m_flow_out_del = hopper.drhodt * hopper.geo.volume 25/25 (1): hopper.eyeOut.xi[9] = if noEvent(hopper.m_flow_out_del > 0.0) then burner1.xi_flueGas[9] else hopper.xi_flueGas[9] 26/26 (1): hopper.eyeOut.xi[8] = if noEvent(hopper.m_flow_out_del > 0.0) then burner1.xi_flueGas[8] else hopper.xi_flueGas[8] 27/27 (1): hopper.eyeOut.xi[7] = if noEvent(hopper.m_flow_out_del > 0.0) then burner1.xi_flueGas[7] else hopper.xi_flueGas[7] 28/28 (1): hopper.eyeOut.xi[6] = if noEvent(hopper.m_flow_out_del > 0.0) then burner1.xi_flueGas[6] else hopper.xi_flueGas[6] 29/29 (1): hopper.eyeOut.xi[5] = if noEvent(hopper.m_flow_out_del > 0.0) then burner1.xi_flueGas[5] else hopper.xi_flueGas[5] 30/30 (1): hopper.eyeOut.xi[4] = if noEvent(hopper.m_flow_out_del > 0.0) then burner1.xi_flueGas[4] else hopper.xi_flueGas[4] 31/31 (1): hopper.eyeOut.xi[3] = if noEvent(hopper.m_flow_out_del > 0.0) then burner1.xi_flueGas[3] else hopper.xi_flueGas[3] 32/32 (1): hopper.eyeOut.xi[2] = if noEvent(hopper.m_flow_out_del > 0.0) then burner1.xi_flueGas[2] else hopper.xi_flueGas[2] 33/33 (1): hopper.eyeOut.xi[1] = if noEvent(hopper.m_flow_out_del > 0.0) then burner1.xi_flueGas[1] else hopper.xi_flueGas[1] 34/34 (1): hopper.mass = hopper.geo.volume * hopper.rho_bulk_del 35/35 (24): (hopper.rho_bulk_del, hopper.bulk.kappa, hopper.bulk.drhodp_hxi, hopper.bulk.drhodh_pxi, hopper.bulk.drhodxi_ph, hopper.bulk.p_i, hopper.bulk.xi_gas) = TILMedia.Internals.GasObjectFunctions.additionalProperties_pTxi(hopper.bulk.p, hopper.T_bulk_del, {hopper.xi_flueGas[1], hopper.xi_flueGas[2], hopper.xi_flueGas[3], hopper.xi_flueGas[4], hopper.xi_flueGas[5], hopper.xi_flueGas[6], hopper.xi_flueGas[7], hopper.xi_flueGas[8], hopper.xi_flueGas[9]}, hopper.bulk.gasPointer) 36/59 (1): hopper.T_bulk_del = TILMedia.Internals.GasObjectFunctions.temperature_phxi(hopper.bulk.p, hopper.h_flueGas_out_del, {hopper.xi_flueGas[1], hopper.xi_flueGas[2], hopper.xi_flueGas[3], hopper.xi_flueGas[4], hopper.xi_flueGas[5], hopper.xi_flueGas[6], hopper.xi_flueGas[7], hopper.xi_flueGas[8], hopper.xi_flueGas[9]}, hopper.bulk.gasPointer) 37/60 (1): hopper.bulk.p = burner1.p + burner1.pressureLoss.Delta_p 38/61 (1): mill1.gasOut.xi[9] = mill1.m_flow_air_in * splitGas_L2_flex.bulk.xi[9] / mill1.m_flow_air_out 39/62 (1): mill1.gasOut.xi[6] = mill1.m_flow_air_in * splitGas_L2_flex.bulk.xi[6] / mill1.m_flow_air_out 40/63 (1): mill1.gasOut.xi_dryGas[6] = mill1.gasOut.xi[6] * (1.0 + mill1.gasOut.humRatio) 41/64 (1): mill1.gasOut.xi[5] = mill1.m_flow_air_in * splitGas_L2_flex.bulk.xi[5] / mill1.m_flow_air_out 42/65 (1): mill1.gasOut.xi_dryGas[5] = mill1.gasOut.xi[5] * (1.0 + mill1.gasOut.humRatio) 43/66 (1): mill1.gasOut.xi[4] = mill1.m_flow_air_in * splitGas_L2_flex.bulk.xi[4] / mill1.m_flow_air_out 44/67 (1): mill1.gasOut.xi_dryGas[4] = mill1.gasOut.xi[4] * (1.0 + mill1.gasOut.humRatio) 45/68 (1): mill1.gasOut.xi[3] = mill1.m_flow_air_in * splitGas_L2_flex.bulk.xi[3] / mill1.m_flow_air_out 46/69 (1): mill1.gasOut.xi_dryGas[3] = mill1.gasOut.xi[3] * (1.0 + mill1.gasOut.humRatio) 47/70 (1): mill1.gasOut.xi[2] = mill1.m_flow_air_in * splitGas_L2_flex.bulk.xi[2] / mill1.m_flow_air_out 48/71 (1): mill1.gasOut.xi_dryGas[2] = mill1.gasOut.xi[2] * (1.0 + mill1.gasOut.humRatio) 49/72 (1): mill1.gasOut.xi[1] = mill1.m_flow_air_in * splitGas_L2_flex.bulk.xi[1] / mill1.m_flow_air_out 50/73 (1): mill1.gasOut.xi_dryGas[1] = mill1.gasOut.xi[1] * (1.0 + mill1.gasOut.humRatio) 51/74 (1): mill1.m_flow_air_out = mill1.m_flow_air_in + mill1.m_flow_evap 52/75 (1): mill1.m_flow_air_evap_max = mill1.m_flow_air_in * (mill1.summary.xi_air_h2o_sat - splitGas_L2_flex.bulk.xi[8]) 53/76 (1): mill1.m_flow_evap = if noEvent(mill1.m_flow_coal_evap_max <= mill1.m_flow_air_evap_max) then mill1.m_flow_wc_out * (mill1.summary.xi_coal_h2o_in - mill1.xi_coal_h2o_res) else mill1.m_flow_air_evap_max Variables: 1: mill1.m_flow_air_evap_max:VARIABLE(unit = \"kg/s\" nominal = 1.0 protected = true ) \"Maximum evaporation flow until air saturation\" type: Real 2: mill1.summary.xi_air_h2o_sat:VARIABLE(min = 0.0 max = 1.0 unit = \"kg/kg\" nominal = 1.0 ) \"Max. water mass fraction at air path\" type: Real 3: mill1.m_flow_air_out:VARIABLE(start = mill1.m_flow_air_out_start unit = \"kg/s\" nominal = 1.0 protected = true ) \"Primary air outlet mass flow rate\" type: Real 4: mill1.gasOut.xi_dryGas[1]:VARIABLE(min = 0.0 max = 1.0 unit = \"1\" ) \"Mass fraction\" type: Real [8] 5: mill1.gasOut.xi[1]:VARIABLE(min = 0.0 max = 1.0 unit = \"1\" nominal = 1.0 ) \"Mass fraction\" type: Real [9] 6: mill1.gasOut.xi_dryGas[2]:VARIABLE(min = 0.0 max = 1.0 unit = \"1\" ) \"Mass fraction\" type: Real [8] 7: mill1.gasOut.xi[2]:VARIABLE(min = 0.0 max = 1.0 unit = \"1\" nominal = 1.0 ) \"Mass fraction\" type: Real [9] 8: mill1.gasOut.xi_dryGas[3]:VARIABLE(min = 0.0 max = 1.0 unit = \"1\" ) \"Mass fraction\" type: Real [8] 9: mill1.gasOut.xi[3]:VARIABLE(min = 0.0 max = 1.0 unit = \"1\" nominal = 1.0 ) \"Mass fraction\" type: Real [9] 10: mill1.gasOut.xi_dryGas[4]:VARIABLE(min = 0.0 max = 1.0 unit = \"1\" ) \"Mass fraction\" type: Real [8] 11: mill1.gasOut.xi[4]:VARIABLE(min = 0.0 max = 1.0 unit = \"1\" nominal = 1.0 ) \"Mass fraction\" type: Real [9] 12: mill1.gasOut.xi_dryGas[5]:VARIABLE(min = 0.0 max = 1.0 unit = \"1\" ) \"Mass fraction\" type: Real [8] 13: mill1.gasOut.xi[5]:VARIABLE(min = 0.0 max = 1.0 unit = \"1\" nominal = 1.0 ) \"Mass fraction\" type: Real [9] 14: mill1.gasOut.xi_dryGas[6]:VARIABLE(min = 0.0 max = 1.0 unit = \"1\" ) \"Mass fraction\" type: Real [8] 15: mill1.gasOut.xi[6]:VARIABLE(min = 0.0 max = 1.0 unit = \"1\" nominal = 1.0 ) \"Mass fraction\" type: Real [9] 16: mill1.gasOut.xi[9]:VARIABLE(min = 0.0 max = 1.0 unit = \"1\" nominal = 1.0 ) \"Mass fraction\" type: Real [9] 17: burner1.pressureLoss.Delta_p:VARIABLE(min = 0.0 start = 0.0 unit = \"Pa\" nominal = 1e5 ) type: Real 18: hopper.T_bulk_del:VARIABLE(min = 0.0 start = 288.15 unit = \"K\" nominal = 300.0 ) \"Pseudo state for bulk temperature\" type: Real 19: hopper.bulk.p_i[6]:VARIABLE(min = 0.0 unit = \"Pa\" nominal = 1e5 ) \"Partial pressure\" type: Real [10] 20: hopper.bulk.p_i[5]:VARIABLE(min = 0.0 unit = \"Pa\" nominal = 1e5 ) \"Partial pressure\" type: Real [10] 21: hopper.bulk.p_i[4]:VARIABLE(min = 0.0 unit = \"Pa\" nominal = 1e5 ) \"Partial pressure\" type: Real [10] 22: hopper.bulk.p_i[8]:VARIABLE(min = 0.0 unit = \"Pa\" nominal = 1e5 ) \"Partial pressure\" type: Real [10] 23: hopper.bulk.drhodxi_ph[4]:VARIABLE(unit = \"kg/(m3)\" ) \"Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy\" type: Real [9] 24: hopper.bulk.kappa:VARIABLE(unit = \"1/Pa\" ) \"Isothermal compressibility\" type: Real 25: hopper.bulk.drhodh_pxi:VARIABLE(unit = \"kg.s2/m5\" ) \"Derivative of density wrt specific enthalpy at constant pressure and mass fraction\" type: Real 26: hopper.bulk.drhodxi_ph[8]:VARIABLE(unit = \"kg/(m3)\" ) \"Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy\" type: Real [9] 27: hopper.bulk.drhodp_hxi:VARIABLE(unit = \"s2/m2\" ) \"Derivative of density wrt pressure at specific enthalpy and mass fraction\" type: Real 28: hopper.bulk.drhodxi_ph[9]:VARIABLE(unit = \"kg/(m3)\" ) \"Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy\" type: Real [9] 29: hopper.bulk.p_i[10]:VARIABLE(min = 0.0 unit = \"Pa\" nominal = 1e5 ) \"Partial pressure\" type: Real [10] 30: hopper.bulk.xi_gas:VARIABLE(min = 0.0 max = 1.0 unit = \"1\" ) \"Mass fraction of gasoues condensing component\" type: Real 31: hopper.bulk.drhodxi_ph[7]:VARIABLE(unit = \"kg/(m3)\" ) \"Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy\" type: Real [9] 32: hopper.bulk.drhodxi_ph[5]:VARIABLE(unit = \"kg/(m3)\" ) \"Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy\" type: Real [9] 33: hopper.bulk.drhodxi_ph[1]:VARIABLE(unit = \"kg/(m3)\" ) \"Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy\" type: Real [9] 34: hopper.bulk.p_i[9]:VARIABLE(min = 0.0 unit = \"Pa\" nominal = 1e5 ) \"Partial pressure\" type: Real [10] 35: hopper.bulk.drhodxi_ph[6]:VARIABLE(unit = \"kg/(m3)\" ) \"Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy\" type: Real [9] 36: hopper.bulk.p_i[2]:VARIABLE(min = 0.0 unit = \"Pa\" nominal = 1e5 ) \"Partial pressure\" type: Real [10] 37: hopper.mass:VARIABLE(min = 0.0 unit = \"kg\" nominal = 1.0 ) \"Gas mass\" type: Real 38: hopper.rho_bulk_del:VARIABLE(min = 0.0 unit = \"kg/m3\" nominal = 1000.0 ) \"Pseudo state for bulk density\" type: Real 39: hopper.bulk.p_i[3]:VARIABLE(min = 0.0 unit = \"Pa\" nominal = 1e5 ) \"Partial pressure\" type: Real [10] 40: hopper.bulk.p_i[1]:VARIABLE(min = 0.0 unit = \"Pa\" nominal = 1e5 ) \"Partial pressure\" type: Real [10] 41: hopper.bulk.p_i[7]:VARIABLE(min = 0.0 unit = \"Pa\" nominal = 1e5 ) \"Partial pressure\" type: Real [10] 42: hopper.bulk.drhodxi_ph[2]:VARIABLE(unit = \"kg/(m3)\" ) \"Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy\" type: Real [9] 43: hopper.eyeOut.xi[1]:VARIABLE(flow=false min = 0.0 max = 1.0 nominal = 1.0 ) \"Mass concentrations\" type: Real [9] 44: hopper.eyeOut.xi[2]:VARIABLE(flow=false min = 0.0 max = 1.0 nominal = 1.0 ) \"Mass concentrations\" type: Real [9] 45: hopper.eyeOut.xi[3]:VARIABLE(flow=false min = 0.0 max = 1.0 nominal = 1.0 ) \"Mass concentrations\" type: Real [9] 46: hopper.eyeOut.xi[4]:VARIABLE(flow=false min = 0.0 max = 1.0 nominal = 1.0 ) \"Mass concentrations\" type: Real [9] 47: hopper.eyeOut.xi[5]:VARIABLE(flow=false min = 0.0 max = 1.0 nominal = 1.0 ) \"Mass concentrations\" type: Real [9] 48: hopper.eyeOut.xi[6]:VARIABLE(flow=false min = 0.0 max = 1.0 nominal = 1.0 ) \"Mass concentrations\" type: Real [9] 49: hopper.eyeOut.xi[7]:VARIABLE(flow=false min = 0.0 max = 1.0 nominal = 1.0 ) \"Mass concentrations\" type: Real [9] 50: hopper.eyeOut.xi[8]:VARIABLE(flow=false min = 0.0 max = 1.0 nominal = 1.0 ) \"Mass concentrations\" type: Real [9] 51: hopper.eyeOut.xi[9]:VARIABLE(flow=false min = 0.0 max = 1.0 nominal = 1.0 ) \"Mass concentrations\" type: Real [9] 52: hopper.drhodt:VARIABLE() \"Density derivative\" type: Real 53: hopper.xi_flueGas[2]:STATE(1)(min = 0.0 max = 1.0 unit = \"kg/kg\" nominal = 1.0 ) \"Flue gas composition \" type: Real [9] 54: hopper.xi_flueGas[3]:STATE(1)(min = 0.0 max = 1.0 unit = \"kg/kg\" nominal = 1.0 ) \"Flue gas composition \" type: Real [9] 55: hopper.xi_flueGas[4]:STATE(1)(min = 0.0 max = 1.0 unit = \"kg/kg\" nominal = 1.0 ) \"Flue gas composition \" type: Real [9] 56: hopper.xi_flueGas[5]:STATE(1)(min = 0.0 max = 1.0 unit = \"kg/kg\" nominal = 1.0 ) \"Flue gas composition \" type: Real [9] 57: hopper.xi_flueGas[6]:STATE(1)(min = 0.0 max = 1.0 unit = \"kg/kg\" nominal = 1.0 ) \"Flue gas composition \" type: Real [9] 58: hopper.xi_flueGas[7]:STATE(1)(min = 0.0 max = 1.0 unit = \"kg/kg\" nominal = 1.0 ) \"Flue gas composition \" type: Real [9] 59: hopper.xi_flueGas[8]:STATE(1)(min = 0.0 max = 1.0 unit = \"kg/kg\" nominal = 1.0 ) \"Flue gas composition \" type: Real [9] 60: hopper.xi_flueGas[9]:STATE(1)(min = 0.0 max = 1.0 unit = \"kg/kg\" nominal = 1.0 ) \"Flue gas composition \" type: Real [9] 61: hopper.m_flow_out_del:VARIABLE(start = -1.0 unit = \"kg/s\" nominal = 1.0 ) \"Pseudo state for outlet mass flow\" type: Real 62: hopper.xi_flueGas[1]:STATE(1)(min = 0.0 max = 1.0 unit = \"kg/kg\" nominal = 1.0 ) \"Flue gas composition \" type: Real [9] 63: hopper.bulk.drhodxi_ph[3]:VARIABLE(unit = \"kg/(m3)\" ) \"Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy\" type: Real [9] 64: hopper.bulk.p:VARIABLE(min = 0.0 start = hopper.p_start_flueGas_out unit = \"Pa\" nominal = 1e5 ) \"Pressure\" type: Real 65: mill1.coalOut.p:VARIABLE(min = 0.0 unit = \"Pa\" nominal = 1e5 ) \"Pressure\" type: Real 66: mill1.Delta_p_pa:VARIABLE(min = 0.0 unit = \"Pa\" nominal = 1e5 protected = true ) \"Primary air difference pressure\" type: Real 67: mill1.m_flow_air_in:VARIABLE(unit = \"kg/s\" nominal = 1.0 protected = true ) \"Primary air inlet mass flow rate\" type: Real 68: mill1.gasOut.xi[7]:VARIABLE(min = 0.0 max = 1.0 unit = \"1\" nominal = 1.0 ) \"Mass fraction\" type: Real [9] 69: mill1.gasOut.xi_dryGas[7]:VARIABLE(min = 0.0 max = 1.0 unit = \"1\" ) \"Mass fraction\" type: Real [8] 70: mill1.gasOut.xi_dryGas[8]:VARIABLE(min = 0.0 max = 1.0 unit = \"1\" ) \"Mass fraction\" type: Real [8] 71: mill1.gasOut.humRatio:VARIABLE() \"Content of condensing component aka humidity ratio\" type: Real 72: mill1.gasOut.xi[8]:VARIABLE(min = 0.0 max = 1.0 unit = \"1\" nominal = 1.0 ) \"Mass fraction\" type: Real [9] 73: mill1.m_flow_evap:VARIABLE(unit = \"kg/s\" nominal = 1.0 protected = true ) \"Mass flow rate of evaporated coal H2O //m_flow_evap\" type: Real 74: mill1.m_flow_dc_out:VARIABLE(unit = \"kg/s\" nominal = 1.0 protected = true ) \"Mass flow of dried coal leaving the mill\" type: Real 75: mill1.summary.m_flow_coal_out:VARIABLE(unit = \"kg/s\" nominal = 1.0 ) \"Coal mass flow leaving the mill\" type: Real 76: burner1.iCom.m_flow_in:VARIABLE(unit = \"kg/s\" nominal = 1.0 protected = true ) \"Inlet mass flow\" type: Real [/var/lib/jenkins1/ws/OpenModelicaLibraryTestingWork_2/OpenModelica/OMCompiler/Compiler/BackEnd/BackendDAEUtil.mo:9806:5-9807:77:writable] Error: Internal error BackendDAEUtil.traverseEqSystemStrongComponents failed with function: omc_DAEMode_traverserStrongComponents Notification: Performance of postOpt createDAEmodeBDAE (simulation): time 1.698/333.6, allocations: 370.9 MB / 89.9 GB, free: 0.6196 GB / 2.625 GB Error: post-optimization module createDAEmodeBDAE (simulation) failed. Error: Internal error SimCode DAEmode: The model ClaRa.Examples.SteamPowerPlant_01 could not be translated " [Timeout remaining time 326] [Calling sys.exit(0), Time elapsed: 337.38157878804486] Failed to read output from testmodel.py, exit status != 0: 333.6238163909875 333.628658632 319.431086306 Calling exit ...