ThermoPower.Examples.BraytonCycle.ClosedLoopSimulator.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 578 * Number of variables: 578 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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. Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: plant.compressor.tau:VARIABLE(unit = "N.m" ) "net torque acting on the compressor" type: Real plant.generator.tau:VARIABLE(unit = "N.m" ) "Torque at shaft" type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 40 * Number of states: 0 () * Number of discrete variables: 1 (plant.network.closedInternal) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (151): * Single equations (assignments): 141 * Array equations: 0 * Algorithm blocks: 5 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 4 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 4 {1,1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {15 52} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 14 (plant.generator.omega_m,plant.generator.shaft.phi,plant.network.delta,plant.CombustionChamber1.fluegas.p,plant.CombustionChamber1.fluegas.Xi[2],plant.CombustionChamber1.fluegas.Xi[3],plant.CombustionChamber1.fluegas.Xi[4],plant.CombustionChamber1.fluegas.Xi[5],plant.CombustionChamber1.fluegas.T,plant.CombustionChamber1.fluegas.R,plant.CombustionChamber1.Tm,plant.gasFlowActuator.y,plant.powerSensor1.y,pID.I) * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (131): * Single equations (assignments): 123 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 5 * Torn equation systems: 3 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 5 {1,1,1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(1,100.0%) 1} * Non-linear torn systems: 2 {3 8,1 4} ThermoPower.Examples.BraytonCycle.OpenLoopSimulator.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 565 * Number of variables: 565 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 38 * Number of states: 0 () * Number of discrete variables: 1 (plant.network.closedInternal) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (155): * Single equations (assignments): 145 * Array equations: 0 * Algorithm blocks: 5 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 4 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 4 {1,1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {12 39} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 13 (plant.generator.omega_m,plant.generator.shaft.phi,plant.network.delta,plant.CombustionChamber1.fluegas.p,plant.CombustionChamber1.fluegas.Xi[2],plant.CombustionChamber1.fluegas.Xi[3],plant.CombustionChamber1.fluegas.Xi[4],plant.CombustionChamber1.fluegas.Xi[5],plant.CombustionChamber1.fluegas.T,plant.CombustionChamber1.fluegas.R,plant.CombustionChamber1.Tm,plant.gasFlowActuator.y,plant.powerSensor1.y) * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (122): * Single equations (assignments): 114 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 5 * Torn equation systems: 3 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 5 {1,1,1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(1,100.0%) 1} * Non-linear torn systems: 2 {3 8,1 4} ThermoPower.Examples.CISE.Simulators.CISESim120501.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 1218 * Number of variables: 1218 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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. Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: Plant.ValveOpening:VARIABLE() type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 54 * Number of states: 0 () * Number of discrete variables: 28 (Plant.PressDrop.state.phase,Plant.HeaderUpper.fluidState.phase,Plant.HeaderLower.fluidState.phase,Plant.Valve.fluidState.phase,Plant.Pipe2Valve.fluidState[2].phase,Plant.Pipe2Valve.fluidState[1].phase,Plant.SH.fluidState[5].phase,Plant.SH.fluidState[4].phase,Plant.SH.fluidState[3].phase,Plant.SH.fluidState[2].phase,Plant.SH.fluidState[1].phase,Plant.SH.heatTransfer.dew.phase,Plant.SH.heatTransfer.bubble.phase,Plant.Pipe2SH.fluidState[2].phase,Plant.Pipe2SH.fluidState[1].phase,Plant.Pipe2Drum.fluidState[2].phase,Plant.Pipe2Drum.fluidState[1].phase,Plant.Risers.fluidState[7].phase,Plant.Risers.fluidState[6].phase,Plant.Risers.fluidState[5].phase,Plant.Risers.fluidState[4].phase,Plant.Risers.fluidState[3].phase,Plant.Risers.fluidState[2].phase,Plant.Risers.fluidState[1].phase,Plant.Downcomer.fluidState[2].phase,Plant.Downcomer.fluidState[1].phase,Plant.Drum.vapourState.phase,Plant.Drum.liquidState.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (475): * Single equations (assignments): 467 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 3 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 5 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 5 {1 3,1 5,5 69,2 13,16 185} Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 2 * Number of states: 41 (Plant.Drum.p,Plant.Drum.hl,Plant.Drum.hv,Plant.Drum.Tm,Plant.Drum.y,Plant.Downcomer.htilde[1],Plant.Risers.p,Plant.Risers.htilde[1],Plant.Risers.htilde[2],Plant.Risers.htilde[3],Plant.Risers.htilde[4],Plant.Risers.htilde[5],Plant.Risers.htilde[6],Plant.Pipe2Drum.htilde[1],Plant.Pipe2SH.p,Plant.Pipe2SH.htilde[1],Plant.SH.htilde[1],Plant.SH.htilde[2],Plant.SH.htilde[3],Plant.SH.htilde[4],Plant.Pipe2Valve.p,Plant.Pipe2Valve.htilde[1],Plant.HeaderLower.p,Plant.HeaderLower.h,Plant.HeaderLower.Tm,Plant.HeaderUpper.h,Plant.HeaderUpper.Tm,Plant.DowncomerWall.Tvol[1],Plant.RisersWalls.Tvol[1],Plant.RisersWalls.Tvol[2],Plant.RisersWalls.Tvol[3],Plant.RisersWalls.Tvol[4],Plant.RisersWalls.Tvol[5],Plant.RisersWalls.Tvol[6],Plant.Pipe2DrumWall.Tvol[1],Plant.Pipe2SHWall.Tvol[1],Plant.SHWall.Tvol[1],Plant.SHWall.Tvol[2],Plant.SHWall.Tvol[3],Plant.SHWall.Tvol[4],Plant.Pipe2ValveWall.Tvol[1]) * Number of discrete variables: 66 ($cse1.phase,$cse1.region,$cse2.phase,$cse2.region,$cse3.region3boundary,$cse4.region3boundary,$cse6.region3boundary,$cse7.region3boundary,$cse8.phase,$cse8.region,$cse9.phase,$cse9.region,$cse10.phase,$cse10.region,$cse11.phase,$cse11.region,$cse14.region3boundary,$cse15.region3boundary,$cse16.phase,$cse16.region,$cse17.phase,$cse17.region,$cse18.phase,$cse18.region,$cse19.phase,$cse19.region,$cse20.phase,$cse20.region,$cse21.phase,$cse21.region,$cse22.phase,$cse22.region,$cse25.region3boundary,$cse26.region3boundary,$cse27.phase,$cse27.region,$cse28.phase,$cse28.region,$cse31.phase,$cse31.region,$cse32.phase,$cse32.region,$cse35.region3boundary,$cse36.region3boundary,$cse37.phase,$cse37.region,$cse39.region3boundary,$cse40.region3boundary,$cse41.phase,$cse41.region,$cse42.phase,$cse42.region,$cse43.phase,$cse43.region,$cse44.phase,$cse44.region,$cse45.phase,$cse45.region,$cse48.region3boundary,$cse49.region3boundary,$cse50.phase,$cse50.region,$cse55.phase,$cse55.region,$cse56.phase,$cse56.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (593): * Single equations (assignments): 523 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 45 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 2 * Torn equation systems: 23 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 2 {1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 18 {(3,77.8%) 7,(1,100.0%) 1,(9,65.4%) 21,(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,(6,63.9%) 13,(1,100.0%) 1,(1,100.0%) 1,(1,100.0%) 1,(1,100.0%) 1,(1,100.0%) 1} * Non-linear torn systems: 5 {4 4,1 2,1 22,1 12,1 10} ThermoPower.Examples.CISE.Simulators.CISESim180503.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 1218 * Number of variables: 1218 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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. Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: Plant.ValveOpening:VARIABLE() type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 54 * Number of states: 0 () * Number of discrete variables: 28 (Plant.PressDrop.state.phase,Plant.HeaderUpper.fluidState.phase,Plant.HeaderLower.fluidState.phase,Plant.Valve.fluidState.phase,Plant.Pipe2Valve.fluidState[2].phase,Plant.Pipe2Valve.fluidState[1].phase,Plant.SH.fluidState[5].phase,Plant.SH.fluidState[4].phase,Plant.SH.fluidState[3].phase,Plant.SH.fluidState[2].phase,Plant.SH.fluidState[1].phase,Plant.SH.heatTransfer.dew.phase,Plant.SH.heatTransfer.bubble.phase,Plant.Pipe2SH.fluidState[2].phase,Plant.Pipe2SH.fluidState[1].phase,Plant.Pipe2Drum.fluidState[2].phase,Plant.Pipe2Drum.fluidState[1].phase,Plant.Risers.fluidState[7].phase,Plant.Risers.fluidState[6].phase,Plant.Risers.fluidState[5].phase,Plant.Risers.fluidState[4].phase,Plant.Risers.fluidState[3].phase,Plant.Risers.fluidState[2].phase,Plant.Risers.fluidState[1].phase,Plant.Downcomer.fluidState[2].phase,Plant.Downcomer.fluidState[1].phase,Plant.Drum.vapourState.phase,Plant.Drum.liquidState.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (475): * Single equations (assignments): 467 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 3 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 5 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 5 {1 3,1 5,5 69,2 13,16 185} Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 2 * Number of states: 41 (Plant.Drum.p,Plant.Drum.hl,Plant.Drum.hv,Plant.Drum.Tm,Plant.Drum.y,Plant.Downcomer.htilde[1],Plant.Risers.p,Plant.Risers.htilde[1],Plant.Risers.htilde[2],Plant.Risers.htilde[3],Plant.Risers.htilde[4],Plant.Risers.htilde[5],Plant.Risers.htilde[6],Plant.Pipe2Drum.htilde[1],Plant.Pipe2SH.p,Plant.Pipe2SH.htilde[1],Plant.SH.htilde[1],Plant.SH.htilde[2],Plant.SH.htilde[3],Plant.SH.htilde[4],Plant.Pipe2Valve.p,Plant.Pipe2Valve.htilde[1],Plant.HeaderLower.p,Plant.HeaderLower.h,Plant.HeaderLower.Tm,Plant.HeaderUpper.h,Plant.HeaderUpper.Tm,Plant.DowncomerWall.Tvol[1],Plant.RisersWalls.Tvol[1],Plant.RisersWalls.Tvol[2],Plant.RisersWalls.Tvol[3],Plant.RisersWalls.Tvol[4],Plant.RisersWalls.Tvol[5],Plant.RisersWalls.Tvol[6],Plant.Pipe2DrumWall.Tvol[1],Plant.Pipe2SHWall.Tvol[1],Plant.SHWall.Tvol[1],Plant.SHWall.Tvol[2],Plant.SHWall.Tvol[3],Plant.SHWall.Tvol[4],Plant.Pipe2ValveWall.Tvol[1]) * Number of discrete variables: 66 ($cse1.phase,$cse1.region,$cse2.phase,$cse2.region,$cse3.region3boundary,$cse4.region3boundary,$cse6.region3boundary,$cse7.region3boundary,$cse8.phase,$cse8.region,$cse9.phase,$cse9.region,$cse10.phase,$cse10.region,$cse11.phase,$cse11.region,$cse14.region3boundary,$cse15.region3boundary,$cse16.phase,$cse16.region,$cse17.phase,$cse17.region,$cse18.phase,$cse18.region,$cse19.phase,$cse19.region,$cse20.phase,$cse20.region,$cse21.phase,$cse21.region,$cse22.phase,$cse22.region,$cse25.region3boundary,$cse26.region3boundary,$cse27.phase,$cse27.region,$cse28.phase,$cse28.region,$cse31.phase,$cse31.region,$cse32.phase,$cse32.region,$cse35.region3boundary,$cse36.region3boundary,$cse37.phase,$cse37.region,$cse39.region3boundary,$cse40.region3boundary,$cse41.phase,$cse41.region,$cse42.phase,$cse42.region,$cse43.phase,$cse43.region,$cse44.phase,$cse44.region,$cse45.phase,$cse45.region,$cse48.region3boundary,$cse49.region3boundary,$cse50.phase,$cse50.region,$cse55.phase,$cse55.region,$cse56.phase,$cse56.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (593): * Single equations (assignments): 523 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 45 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 2 * Torn equation systems: 23 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 2 {1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 18 {(3,77.8%) 7,(1,100.0%) 1,(9,65.4%) 21,(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,(6,63.9%) 13,(1,100.0%) 1,(1,100.0%) 1,(1,100.0%) 1,(1,100.0%) 1,(1,100.0%) 1} * Non-linear torn systems: 5 {4 4,1 2,1 22,1 12,1 10} ThermoPower.Examples.CISE.Simulators.CISESim180504.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 1218 * Number of variables: 1218 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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. Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: Plant.ValveOpening:VARIABLE() type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 54 * Number of states: 0 () * Number of discrete variables: 28 (Plant.PressDrop.state.phase,Plant.HeaderUpper.fluidState.phase,Plant.HeaderLower.fluidState.phase,Plant.Valve.fluidState.phase,Plant.Pipe2Valve.fluidState[2].phase,Plant.Pipe2Valve.fluidState[1].phase,Plant.SH.fluidState[5].phase,Plant.SH.fluidState[4].phase,Plant.SH.fluidState[3].phase,Plant.SH.fluidState[2].phase,Plant.SH.fluidState[1].phase,Plant.SH.heatTransfer.dew.phase,Plant.SH.heatTransfer.bubble.phase,Plant.Pipe2SH.fluidState[2].phase,Plant.Pipe2SH.fluidState[1].phase,Plant.Pipe2Drum.fluidState[2].phase,Plant.Pipe2Drum.fluidState[1].phase,Plant.Risers.fluidState[7].phase,Plant.Risers.fluidState[6].phase,Plant.Risers.fluidState[5].phase,Plant.Risers.fluidState[4].phase,Plant.Risers.fluidState[3].phase,Plant.Risers.fluidState[2].phase,Plant.Risers.fluidState[1].phase,Plant.Downcomer.fluidState[2].phase,Plant.Downcomer.fluidState[1].phase,Plant.Drum.vapourState.phase,Plant.Drum.liquidState.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (475): * Single equations (assignments): 467 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 3 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 5 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 5 {1 3,1 5,5 69,2 13,16 185} Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 2 * Number of states: 41 (Plant.Drum.p,Plant.Drum.hl,Plant.Drum.hv,Plant.Drum.Tm,Plant.Drum.y,Plant.Downcomer.htilde[1],Plant.Risers.p,Plant.Risers.htilde[1],Plant.Risers.htilde[2],Plant.Risers.htilde[3],Plant.Risers.htilde[4],Plant.Risers.htilde[5],Plant.Risers.htilde[6],Plant.Pipe2Drum.htilde[1],Plant.Pipe2SH.p,Plant.Pipe2SH.htilde[1],Plant.SH.htilde[1],Plant.SH.htilde[2],Plant.SH.htilde[3],Plant.SH.htilde[4],Plant.Pipe2Valve.p,Plant.Pipe2Valve.htilde[1],Plant.HeaderLower.p,Plant.HeaderLower.h,Plant.HeaderLower.Tm,Plant.HeaderUpper.h,Plant.HeaderUpper.Tm,Plant.DowncomerWall.Tvol[1],Plant.RisersWalls.Tvol[1],Plant.RisersWalls.Tvol[2],Plant.RisersWalls.Tvol[3],Plant.RisersWalls.Tvol[4],Plant.RisersWalls.Tvol[5],Plant.RisersWalls.Tvol[6],Plant.Pipe2DrumWall.Tvol[1],Plant.Pipe2SHWall.Tvol[1],Plant.SHWall.Tvol[1],Plant.SHWall.Tvol[2],Plant.SHWall.Tvol[3],Plant.SHWall.Tvol[4],Plant.Pipe2ValveWall.Tvol[1]) * Number of discrete variables: 66 ($cse1.phase,$cse1.region,$cse2.phase,$cse2.region,$cse3.region3boundary,$cse4.region3boundary,$cse6.region3boundary,$cse7.region3boundary,$cse8.phase,$cse8.region,$cse9.phase,$cse9.region,$cse10.phase,$cse10.region,$cse11.phase,$cse11.region,$cse14.region3boundary,$cse15.region3boundary,$cse16.phase,$cse16.region,$cse17.phase,$cse17.region,$cse18.phase,$cse18.region,$cse19.phase,$cse19.region,$cse20.phase,$cse20.region,$cse21.phase,$cse21.region,$cse22.phase,$cse22.region,$cse25.region3boundary,$cse26.region3boundary,$cse27.phase,$cse27.region,$cse28.phase,$cse28.region,$cse31.phase,$cse31.region,$cse32.phase,$cse32.region,$cse35.region3boundary,$cse36.region3boundary,$cse37.phase,$cse37.region,$cse39.region3boundary,$cse40.region3boundary,$cse41.phase,$cse41.region,$cse42.phase,$cse42.region,$cse43.phase,$cse43.region,$cse44.phase,$cse44.region,$cse45.phase,$cse45.region,$cse48.region3boundary,$cse49.region3boundary,$cse50.phase,$cse50.region,$cse55.phase,$cse55.region,$cse56.phase,$cse56.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (593): * Single equations (assignments): 523 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 45 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 2 * Torn equation systems: 23 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 2 {1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 18 {(3,77.8%) 7,(1,100.0%) 1,(9,65.4%) 21,(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,(6,63.9%) 13,(1,100.0%) 1,(1,100.0%) 1,(1,100.0%) 1,(1,100.0%) 1,(1,100.0%) 1} * Non-linear torn systems: 5 {4 4,1 2,1 22,1 12,1 10} ThermoPower.Examples.CISE.Simulators.CISESim2States120501.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 565 * Number of variables: 565 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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. Warning: The initial conditions are over specified. The following 1 initial equations are redundant, so they are removed from the initialization sytem: $DER.Plant.SH.p = 0.0. Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: Plant.ValveOpening:VARIABLE() type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 28 * Number of states: 0 () * Number of discrete variables: 12 (Plant.Valve.fluidState.phase,Plant.Pipe2Valve.fluidState[2].phase,Plant.Pipe2Valve.fluidState[1].phase,Plant.SH.fluidState[5].phase,Plant.SH.fluidState[4].phase,Plant.SH.fluidState[3].phase,Plant.SH.fluidState[2].phase,Plant.SH.fluidState[1].phase,Plant.SH.heatTransfer.dew.phase,Plant.SH.heatTransfer.bubble.phase,Plant.Pipe2SH.fluidState[2].phase,Plant.Pipe2SH.fluidState[1].phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (255): * Single equations (assignments): 249 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 1 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 5 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(1,100.0%) 1} * Non-linear torn systems: 4 {1 3,1 8,5 70,2 13} Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 3 * Number of states: 16 (Plant.Pipe2SH.p,Plant.Pipe2SH.htilde[1],Plant.SH.htilde[1],Plant.SH.htilde[2],Plant.SH.htilde[3],Plant.SH.htilde[4],Plant.Pipe2Valve.p,Plant.Pipe2Valve.htilde[1],Plant.Pipe2SHWall.Tvol[1],Plant.SHWall.Tvol[1],Plant.SHWall.Tvol[2],Plant.SHWall.Tvol[3],Plant.SHWall.Tvol[4],Plant.Pipe2ValveWall.Tvol[1],Plant.DrumBoiler.Vld,Plant.DrumBoiler.p) * Number of discrete variables: 36 ($cse2.phase,$cse2.region,$cse3.phase,$cse3.region,$cse6.region3boundary,$cse7.region3boundary,$cse8.phase,$cse8.region,$cse10.region3boundary,$cse11.region3boundary,$cse12.phase,$cse12.region,$cse13.phase,$cse13.region,$cse14.phase,$cse14.region,$cse15.phase,$cse15.region,$cse16.phase,$cse16.region,$cse17.phase,$cse17.region,$cse18.phase,$cse18.region,$cse19.phase,$cse19.region,$cse20.phase,$cse20.region,$cse21.phase,$cse21.region,$cse24.phase,$cse24.region,$cse29.phase,$cse29.region,$cse36.region3boundary,$cse37.region3boundary) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (275): * Single equations (assignments): 241 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 22 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 1 * Torn equation systems: 11 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 1 {1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 8 {(1,100.0%) 1,(1,100.0%) 1,(6,72.2%) 14,(1,100.0%) 1,(1,100.0%) 1,(1,100.0%) 1,(1,100.0%) 1,(1,100.0%) 1} * Non-linear torn systems: 3 {2 7,1 11,1 12} ThermoPower.Examples.HRB.Simulators.ClosedLoopDigitalSimulator.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 1372 * Number of variables: 1372 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or nominal values. It is recommended to resolve the conflicts, because otherwise the system could be hard to solve. To print the conflicting alias sets and the chosen candidates please use -d=aliasConflicts. Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: DigitalPI1.CSwind:DISCRETE(fixed = false ) "Control signal before anti-windup filtering" type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 40 * Number of states: 0 () * Number of discrete variables: 23 ($PRE.DigitalPI1.firstTrigger,DigitalPI1.firstTrigger,$whenCondition1,DigitalPI1.sampleTrigger,Plant.WaterOut.fluidState.phase,Plant.WaterIn.fluidState.phase,Plant.Boiler.WaterSide.fluidState[11].phase,Plant.Boiler.WaterSide.fluidState[10].phase,Plant.Boiler.WaterSide.fluidState[9].phase,Plant.Boiler.WaterSide.fluidState[8].phase,Plant.Boiler.WaterSide.fluidState[7].phase,Plant.Boiler.WaterSide.fluidState[6].phase,Plant.Boiler.WaterSide.fluidState[5].phase,Plant.Boiler.WaterSide.fluidState[4].phase,Plant.Boiler.WaterSide.fluidState[3].phase,Plant.Boiler.WaterSide.fluidState[2].phase,Plant.Boiler.WaterSide.fluidState[1].phase,DigitalPI1.e,$PRE.DigitalPI1.e_int,DigitalPI1.e_int,DigitalPI1.e_int_wind,DigitalPI1.CSwind,DigitalPI1.CS) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (264): * Single equations (assignments): 260 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 3 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 3 {1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {35 470} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 2 * Number of states: 40 (Plant.Boiler.WaterSide.p,Plant.Boiler.WaterSide.htilde[1],Plant.Boiler.WaterSide.htilde[2],Plant.Boiler.WaterSide.htilde[3],Plant.Boiler.WaterSide.htilde[4],Plant.Boiler.WaterSide.htilde[5],Plant.Boiler.WaterSide.htilde[6],Plant.Boiler.WaterSide.htilde[7],Plant.Boiler.WaterSide.htilde[8],Plant.Boiler.WaterSide.htilde[9],Plant.Boiler.WaterSide.htilde[10],Plant.Boiler.TubeWalls.Tvol[1],Plant.Boiler.TubeWalls.Tvol[2],Plant.Boiler.TubeWalls.Tvol[3],Plant.Boiler.TubeWalls.Tvol[4],Plant.Boiler.TubeWalls.Tvol[5],Plant.Boiler.TubeWalls.Tvol[6],Plant.Boiler.TubeWalls.Tvol[7],Plant.Boiler.TubeWalls.Tvol[8],Plant.Boiler.TubeWalls.Tvol[9],Plant.Boiler.TubeWalls.Tvol[10],Plant.Boiler.GasSide.Ttilde[1],Plant.Boiler.GasSide.Ttilde[2],Plant.Boiler.GasSide.Ttilde[3],Plant.Boiler.GasSide.Ttilde[4],Plant.Boiler.GasSide.Ttilde[5],Plant.Boiler.GasSide.Ttilde[6],Plant.Boiler.GasSide.Ttilde[7],Plant.Boiler.GasSide.Ttilde[8],Plant.Boiler.GasSide.Ttilde[9],Plant.Boiler.GasSide.Ttilde[10],Plant.Boiler.GasSide.Xtilde[1,1],Plant.Boiler.GasSide.Xtilde[1,2],Plant.Boiler.GasSide.p,Plant.GasFlowActuator.y,Plant.WaterOutTSensor.y,Plant.GasInTSensor.y,Plant.GasOutTSensor.y,Plant.ValveOpeningActuator.y,Plant.WaterInTSensor.y) * Number of discrete variables: 30 (DigitalPI1.sampleTrigger,$cse1.phase,$cse1.region,$cse3.phase,$cse3.region,$cse4.phase,$cse4.region,$cse5.phase,$cse5.region,$cse6.phase,$cse6.region,$cse7.phase,$cse7.region,$cse8.phase,$cse8.region,$cse9.phase,$cse9.region,$cse10.phase,$cse10.region,$cse11.phase,$cse11.region,$cse12.phase,$cse12.region,$whenCondition1,DigitalPI1.firstTrigger,DigitalPI1.e,DigitalPI1.e_int,DigitalPI1.e_int_wind,DigitalPI1.CSwind,DigitalPI1.CS) * Number of discrete states: 1 (DigitalPI1.e_int) * Top-level inputs: 0 Notification: Strong component statistics for simulation (593): * Single equations (assignments): 550 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 11 * When equations: 6 * If-equations: 0 * Equation systems (linear and non-linear blocks): 4 * Torn equation systems: 22 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 4 {1,1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 22 {(11,62.8%) 20,(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,(11,62.8%) 40,(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} * Non-linear torn systems: 0 ThermoPower.Examples.HRB.Simulators.ClosedLoopDigitalSimulatorSimplified.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 1246 * Number of variables: 1246 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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. Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: DigitalPI1.CSwind:DISCRETE(fixed = false ) "Control signal before anti-windup filtering" type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 232 * Number of states: 0 () * Number of discrete variables: 10 ($PRE.DigitalPI1.firstTrigger,DigitalPI1.firstTrigger,$whenCondition1,DigitalPI1.sampleTrigger,DigitalPI1.e,$PRE.DigitalPI1.e_int,DigitalPI1.e_int,DigitalPI1.e_int_wind,DigitalPI1.CSwind,DigitalPI1.CS) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (477): * Single equations (assignments): 473 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 3 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 3 {1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {33 312} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 2 * Number of states: 38 (Plant.Boiler.WaterSide.p,Plant.Boiler.WaterSide.htilde[1],Plant.Boiler.WaterSide.htilde[2],Plant.Boiler.WaterSide.htilde[3],Plant.Boiler.WaterSide.htilde[4],Plant.Boiler.WaterSide.htilde[5],Plant.Boiler.WaterSide.htilde[6],Plant.Boiler.WaterSide.htilde[7],Plant.Boiler.WaterSide.htilde[8],Plant.Boiler.WaterSide.htilde[9],Plant.Boiler.WaterSide.htilde[10],Plant.Boiler.TubeWalls.Tvol[1],Plant.Boiler.TubeWalls.Tvol[2],Plant.Boiler.TubeWalls.Tvol[3],Plant.Boiler.TubeWalls.Tvol[4],Plant.Boiler.TubeWalls.Tvol[5],Plant.Boiler.TubeWalls.Tvol[6],Plant.Boiler.TubeWalls.Tvol[7],Plant.Boiler.TubeWalls.Tvol[8],Plant.Boiler.TubeWalls.Tvol[9],Plant.Boiler.TubeWalls.Tvol[10],Plant.Boiler.GasSide.Ttilde[1],Plant.Boiler.GasSide.Ttilde[2],Plant.Boiler.GasSide.Ttilde[3],Plant.Boiler.GasSide.Ttilde[4],Plant.Boiler.GasSide.Ttilde[5],Plant.Boiler.GasSide.Ttilde[6],Plant.Boiler.GasSide.Ttilde[7],Plant.Boiler.GasSide.Ttilde[8],Plant.Boiler.GasSide.Ttilde[9],Plant.Boiler.GasSide.Ttilde[10],Plant.Boiler.GasSide.p,Plant.GasFlowActuator.y,Plant.WaterOutTSensor.y,Plant.GasInTSensor.y,Plant.GasOutTSensor.y,Plant.ValveOpeningActuator.y,Plant.WaterInTSensor.y) * Number of discrete variables: 8 (DigitalPI1.sampleTrigger,$whenCondition1,DigitalPI1.firstTrigger,DigitalPI1.e,DigitalPI1.e_int,DigitalPI1.e_int_wind,DigitalPI1.CSwind,DigitalPI1.CS) * Number of discrete states: 1 (DigitalPI1.e_int) * Top-level inputs: 0 Notification: Strong component statistics for simulation (449): * Single equations (assignments): 417 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 6 * If-equations: 0 * Equation systems (linear and non-linear blocks): 4 * Torn equation systems: 22 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 4 {1,1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 22 {(11,62.8%) 40,(1,100.0%) 1,(10,92.0%) 21,(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} * Non-linear torn systems: 0 ThermoPower.Examples.HRB.Simulators.ClosedLoopSimulator.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 1369 * Number of variables: 1369 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 38 * Number of states: 0 () * Number of discrete variables: 13 (Plant.WaterOut.fluidState.phase,Plant.WaterIn.fluidState.phase,Plant.Boiler.WaterSide.fluidState[11].phase,Plant.Boiler.WaterSide.fluidState[10].phase,Plant.Boiler.WaterSide.fluidState[9].phase,Plant.Boiler.WaterSide.fluidState[8].phase,Plant.Boiler.WaterSide.fluidState[7].phase,Plant.Boiler.WaterSide.fluidState[6].phase,Plant.Boiler.WaterSide.fluidState[5].phase,Plant.Boiler.WaterSide.fluidState[4].phase,Plant.Boiler.WaterSide.fluidState[3].phase,Plant.Boiler.WaterSide.fluidState[2].phase,Plant.Boiler.WaterSide.fluidState[1].phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (268): * Single equations (assignments): 264 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 3 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 3 {1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {34 462} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 41 (Plant.Boiler.WaterSide.p,Plant.Boiler.WaterSide.htilde[1],Plant.Boiler.WaterSide.htilde[2],Plant.Boiler.WaterSide.htilde[3],Plant.Boiler.WaterSide.htilde[4],Plant.Boiler.WaterSide.htilde[5],Plant.Boiler.WaterSide.htilde[6],Plant.Boiler.WaterSide.htilde[7],Plant.Boiler.WaterSide.htilde[8],Plant.Boiler.WaterSide.htilde[9],Plant.Boiler.WaterSide.htilde[10],Plant.Boiler.TubeWalls.Tvol[1],Plant.Boiler.TubeWalls.Tvol[2],Plant.Boiler.TubeWalls.Tvol[3],Plant.Boiler.TubeWalls.Tvol[4],Plant.Boiler.TubeWalls.Tvol[5],Plant.Boiler.TubeWalls.Tvol[6],Plant.Boiler.TubeWalls.Tvol[7],Plant.Boiler.TubeWalls.Tvol[8],Plant.Boiler.TubeWalls.Tvol[9],Plant.Boiler.TubeWalls.Tvol[10],Plant.Boiler.GasSide.Ttilde[1],Plant.Boiler.GasSide.Ttilde[2],Plant.Boiler.GasSide.Ttilde[3],Plant.Boiler.GasSide.Ttilde[4],Plant.Boiler.GasSide.Ttilde[5],Plant.Boiler.GasSide.Ttilde[6],Plant.Boiler.GasSide.Ttilde[7],Plant.Boiler.GasSide.Ttilde[8],Plant.Boiler.GasSide.Ttilde[9],Plant.Boiler.GasSide.Ttilde[10],Plant.Boiler.GasSide.Xtilde[1,1],Plant.Boiler.GasSide.Xtilde[1,2],Plant.Boiler.GasSide.p,Plant.GasFlowActuator.y,Plant.WaterInTSensor.y,Plant.WaterOutTSensor.y,Plant.GasInTSensor.y,Plant.GasOutTSensor.y,Plant.ValveOpeningActuator.y,TempController.x) * Number of discrete variables: 22 ($cse1.phase,$cse1.region,$cse3.phase,$cse3.region,$cse4.phase,$cse4.region,$cse5.phase,$cse5.region,$cse6.phase,$cse6.region,$cse7.phase,$cse7.region,$cse8.phase,$cse8.region,$cse9.phase,$cse9.region,$cse10.phase,$cse10.region,$cse11.phase,$cse11.region,$cse12.phase,$cse12.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (589): * Single equations (assignments): 552 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 11 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 4 * Torn equation systems: 22 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 4 {1,1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 22 {(11,62.8%) 20,(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,(11,62.8%) 40,(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} * Non-linear torn systems: 0 ThermoPower.Examples.HRB.Simulators.OpenLoopSimulator.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 1371 * Number of variables: 1371 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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. Warning: Assuming fixed start value for the following 34 variables: Plant.GasOutTSensor.y:VARIABLE(start = Plant.GasOutTSensor.y_start ) "Connector of Real output signal" type: Real Plant.WaterOutTSensor.y:VARIABLE(start = Plant.WaterOutTSensor.y_start ) "Connector of Real output signal" type: Real Plant.Boiler.GasSide.p:VARIABLE(min = max(max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, 0.0)))))))), max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, 0.0))))))))))))))))))))))))))))))))))))))))) max = min(min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, 100000000.0)))))), min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, 100000000.0))))))))))))))))))))))))))))) start = Plant.Boiler.GasSide.pstart unit = "Pa" nominal = 1000000.0 stateSelect=StateSelect.prefer ) type: Real Plant.Boiler.GasSide.Xtilde[1,2]:VARIABLE(min = max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, 0.0))))))))))))))))))))))))))))))))))))))))))))))))) max = min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, 1.0))))))))))))))))))))))))))))))))))))))))))))))))) start = 0.232 unit = "kg/kg" nominal = 0.1 stateSelect=StateSelect.prefer ) "Composition state variables" type: Real [1,2] Plant.Boiler.GasSide.Xtilde[1,1]:VARIABLE(min = max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, 0.0))))))))))))))))))))))))))))))))))))))))))))))))) max = min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, min(1.0, 1.0))))))))))))))))))))))))))))))))))))))))))))))))) start = 0.768 unit = "kg/kg" nominal = 0.1 stateSelect=StateSelect.prefer ) "Composition state variables" type: Real [1,2] -- Plant.Boiler.WaterSide.htilde[5]:VARIABLE(min = max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, -10000000000.0))) max = min(10000000000.0, min(10000000000.0, min(10000000000.0, 10000000000.0))) start = Plant.Boiler.WaterSide.hstart[6] unit = "J/kg" nominal = 500000.0 stateSelect=StateSelect.prefer ) "Enthalpy state variables" type: Real [10] Plant.Boiler.WaterSide.htilde[4]:VARIABLE(min = max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, -10000000000.0))) max = min(10000000000.0, min(10000000000.0, min(10000000000.0, 10000000000.0))) start = Plant.Boiler.WaterSide.hstart[5] unit = "J/kg" nominal = 500000.0 stateSelect=StateSelect.prefer ) "Enthalpy state variables" type: Real [10] Plant.Boiler.WaterSide.htilde[3]:VARIABLE(min = max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, -10000000000.0))) max = min(10000000000.0, min(10000000000.0, min(10000000000.0, 10000000000.0))) start = Plant.Boiler.WaterSide.hstart[4] unit = "J/kg" nominal = 500000.0 stateSelect=StateSelect.prefer ) "Enthalpy state variables" type: Real [10] Plant.Boiler.WaterSide.htilde[2]:VARIABLE(min = max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, -10000000000.0))) max = min(10000000000.0, min(10000000000.0, min(10000000000.0, 10000000000.0))) start = Plant.Boiler.WaterSide.hstart[3] unit = "J/kg" nominal = 500000.0 stateSelect=StateSelect.prefer ) "Enthalpy state variables" type: Real [10] Plant.Boiler.WaterSide.htilde[1]:VARIABLE(min = max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, -10000000000.0)))))) max = min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, 10000000000.0)))))) start = Plant.Boiler.WaterSide.hstart[2] unit = "J/kg" nominal = 500000.0 stateSelect=StateSelect.prefer ) "Enthalpy state variables" type: Real [10] Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: $DERAliasPlant.Boiler.WaterSide.p:VARIABLE(nominal = 1000000.0 ) type: Real $DERAliasPlant.Boiler.WaterSide.htilde[9]:VARIABLE(nominal = 500000.0 ) type: Real $DERAliasPlant.Boiler.WaterSide.htilde[8]:VARIABLE(nominal = 500000.0 ) type: Real $DERAliasPlant.Boiler.WaterSide.htilde[7]:VARIABLE(nominal = 500000.0 ) type: Real $DERAliasPlant.Boiler.WaterSide.htilde[6]:VARIABLE(nominal = 500000.0 ) type: Real -- $DERAliasPlant.Boiler.WaterSide.htilde[4]:VARIABLE(nominal = 500000.0 ) type: Real $DERAliasPlant.Boiler.WaterSide.htilde[3]:VARIABLE(nominal = 500000.0 ) type: Real $DERAliasPlant.Boiler.WaterSide.htilde[2]:VARIABLE(nominal = 500000.0 ) type: Real $DERAliasPlant.Boiler.WaterSide.htilde[1]:VARIABLE(nominal = 500000.0 ) type: Real $DERAliasPlant.Boiler.WaterSide.htilde[10]:VARIABLE(nominal = 500000.0 ) type: Real Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: $DERAliasPlant.Boiler.GasSide.Ttilde[10]:VARIABLE(nominal = 500.0 ) type: Real $DERAliasPlant.Boiler.GasSide.gas[10].T:VARIABLE(nominal = 500.0 ) type: Real $DERAliasPlant.Boiler.GasSide.gas[9].T:VARIABLE(nominal = 500.0 ) type: Real $DERAliasPlant.Boiler.GasSide.gas[8].T:VARIABLE(nominal = 500.0 ) type: Real $DERAliasPlant.Boiler.GasSide.gas[7].T:VARIABLE(nominal = 500.0 ) type: Real -- $DERAliasPlant.Boiler.GasSide.gas[5].T:VARIABLE(nominal = 500.0 ) type: Real $DERAliasPlant.Boiler.GasSide.gas[4].T:VARIABLE(nominal = 500.0 ) type: Real $DERAliasPlant.Boiler.GasSide.gas[3].T:VARIABLE(nominal = 500.0 ) type: Real $DERAliasPlant.Boiler.GasSide.gas[2].T:VARIABLE(nominal = 500.0 ) type: Real $DERAliasPlant.Boiler.GasSide.p:VARIABLE(nominal = 1000000.0 ) type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 38 * Number of states: 0 () * Number of discrete variables: 13 (Plant.WaterOut.fluidState.phase,Plant.WaterIn.fluidState.phase,Plant.Boiler.WaterSide.fluidState[11].phase,Plant.Boiler.WaterSide.fluidState[10].phase,Plant.Boiler.WaterSide.fluidState[9].phase,Plant.Boiler.WaterSide.fluidState[8].phase,Plant.Boiler.WaterSide.fluidState[7].phase,Plant.Boiler.WaterSide.fluidState[6].phase,Plant.Boiler.WaterSide.fluidState[5].phase,Plant.Boiler.WaterSide.fluidState[4].phase,Plant.Boiler.WaterSide.fluidState[3].phase,Plant.Boiler.WaterSide.fluidState[2].phase,Plant.Boiler.WaterSide.fluidState[1].phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (662): * Single equations (assignments): 635 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 5 * Torn equation systems: 22 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 5 {1,1,1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 20 {(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} * Non-linear torn systems: 2 {11 40,11 20} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 40 (Plant.Boiler.WaterSide.p,Plant.Boiler.WaterSide.htilde[1],Plant.Boiler.WaterSide.htilde[2],Plant.Boiler.WaterSide.htilde[3],Plant.Boiler.WaterSide.htilde[4],Plant.Boiler.WaterSide.htilde[5],Plant.Boiler.WaterSide.htilde[6],Plant.Boiler.WaterSide.htilde[7],Plant.Boiler.WaterSide.htilde[8],Plant.Boiler.WaterSide.htilde[9],Plant.Boiler.WaterSide.htilde[10],Plant.Boiler.TubeWalls.Tvol[1],Plant.Boiler.TubeWalls.Tvol[2],Plant.Boiler.TubeWalls.Tvol[3],Plant.Boiler.TubeWalls.Tvol[4],Plant.Boiler.TubeWalls.Tvol[5],Plant.Boiler.TubeWalls.Tvol[6],Plant.Boiler.TubeWalls.Tvol[7],Plant.Boiler.TubeWalls.Tvol[8],Plant.Boiler.TubeWalls.Tvol[9],Plant.Boiler.TubeWalls.Tvol[10],Plant.Boiler.GasSide.Ttilde[1],Plant.Boiler.GasSide.Ttilde[2],Plant.Boiler.GasSide.Ttilde[3],Plant.Boiler.GasSide.Ttilde[4],Plant.Boiler.GasSide.Ttilde[5],Plant.Boiler.GasSide.Ttilde[6],Plant.Boiler.GasSide.Ttilde[7],Plant.Boiler.GasSide.Ttilde[8],Plant.Boiler.GasSide.Ttilde[9],Plant.Boiler.GasSide.Ttilde[10],Plant.Boiler.GasSide.Xtilde[1,1],Plant.Boiler.GasSide.Xtilde[1,2],Plant.Boiler.GasSide.p,Plant.GasFlowActuator.y,Plant.WaterInTSensor.y,Plant.WaterOutTSensor.y,Plant.GasInTSensor.y,Plant.GasOutTSensor.y,Plant.ValveOpeningActuator.y) * Number of discrete variables: 22 ($cse41.phase,$cse41.region,$cse43.phase,$cse43.region,$cse44.phase,$cse44.region,$cse45.phase,$cse45.region,$cse46.phase,$cse46.region,$cse47.phase,$cse47.region,$cse48.phase,$cse48.region,$cse49.phase,$cse49.region,$cse50.phase,$cse50.region,$cse51.phase,$cse51.region,$cse52.phase,$cse52.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (589): * Single equations (assignments): 552 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 11 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 4 * Torn equation systems: 22 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 4 {1,1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 22 {(11,62.8%) 20,(1,100.0%) 1,(1,100.0%) 1,(1,100.0%) 1,(1,100.0%) 1,(1,100.0%) 1,(1,100.0%) 1,(1,100.0%) 1,(1,100.0%) 1,(1,100.0%) 1,(1,100.0%) 1,(11,62.8%) 40,(1,100.0%) 1,(1,100.0%) 1,(1,100.0%) 1,(1,100.0%) 1,(1,100.0%) 1,(1,100.0%) 1,(1,100.0%) 1,(1,100.0%) 1,(1,100.0%) 1,(1,100.0%) 1} * Non-linear torn systems: 0 ThermoPower.Examples.HRB.Simulators.OpenLoopSimulatorHtc.err [ThermoPower 3.1/Examples.mo:1429:85-1429:104:writable] Error: Variable gamma_nom not found in scope ThermoPower.Gas.Flow1DFV$Plant$Boiler$GasSide. Error: Error occurred while flattening model ThermoPower.Examples.HRB.Simulators.OpenLoopSimulatorHtc ThermoPower.Examples.HRB.Simulators.OpenLoopSimulatorSS.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 1371 * Number of variables: 1371 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 38 * Number of states: 0 () * Number of discrete variables: 13 (Plant.WaterOut.fluidState.phase,Plant.WaterIn.fluidState.phase,Plant.Boiler.WaterSide.fluidState[11].phase,Plant.Boiler.WaterSide.fluidState[10].phase,Plant.Boiler.WaterSide.fluidState[9].phase,Plant.Boiler.WaterSide.fluidState[8].phase,Plant.Boiler.WaterSide.fluidState[7].phase,Plant.Boiler.WaterSide.fluidState[6].phase,Plant.Boiler.WaterSide.fluidState[5].phase,Plant.Boiler.WaterSide.fluidState[4].phase,Plant.Boiler.WaterSide.fluidState[3].phase,Plant.Boiler.WaterSide.fluidState[2].phase,Plant.Boiler.WaterSide.fluidState[1].phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (270): * Single equations (assignments): 266 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 3 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 3 {1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {34 459} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 40 (Plant.Boiler.WaterSide.p,Plant.Boiler.WaterSide.htilde[1],Plant.Boiler.WaterSide.htilde[2],Plant.Boiler.WaterSide.htilde[3],Plant.Boiler.WaterSide.htilde[4],Plant.Boiler.WaterSide.htilde[5],Plant.Boiler.WaterSide.htilde[6],Plant.Boiler.WaterSide.htilde[7],Plant.Boiler.WaterSide.htilde[8],Plant.Boiler.WaterSide.htilde[9],Plant.Boiler.WaterSide.htilde[10],Plant.Boiler.TubeWalls.Tvol[1],Plant.Boiler.TubeWalls.Tvol[2],Plant.Boiler.TubeWalls.Tvol[3],Plant.Boiler.TubeWalls.Tvol[4],Plant.Boiler.TubeWalls.Tvol[5],Plant.Boiler.TubeWalls.Tvol[6],Plant.Boiler.TubeWalls.Tvol[7],Plant.Boiler.TubeWalls.Tvol[8],Plant.Boiler.TubeWalls.Tvol[9],Plant.Boiler.TubeWalls.Tvol[10],Plant.Boiler.GasSide.Ttilde[1],Plant.Boiler.GasSide.Ttilde[2],Plant.Boiler.GasSide.Ttilde[3],Plant.Boiler.GasSide.Ttilde[4],Plant.Boiler.GasSide.Ttilde[5],Plant.Boiler.GasSide.Ttilde[6],Plant.Boiler.GasSide.Ttilde[7],Plant.Boiler.GasSide.Ttilde[8],Plant.Boiler.GasSide.Ttilde[9],Plant.Boiler.GasSide.Ttilde[10],Plant.Boiler.GasSide.Xtilde[1,1],Plant.Boiler.GasSide.Xtilde[1,2],Plant.Boiler.GasSide.p,Plant.GasFlowActuator.y,Plant.WaterInTSensor.y,Plant.WaterOutTSensor.y,Plant.GasInTSensor.y,Plant.GasOutTSensor.y,Plant.ValveOpeningActuator.y) * Number of discrete variables: 22 ($cse2.phase,$cse2.region,$cse3.phase,$cse3.region,$cse4.phase,$cse4.region,$cse5.phase,$cse5.region,$cse6.phase,$cse6.region,$cse7.phase,$cse7.region,$cse8.phase,$cse8.region,$cse9.phase,$cse9.region,$cse10.phase,$cse10.region,$cse11.phase,$cse11.region,$cse12.phase,$cse12.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (589): * Single equations (assignments): 552 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 11 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 4 * Torn equation systems: 22 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 4 {1,1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 22 {(11,62.8%) 20,(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,(11,62.8%) 40,(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} * Non-linear torn systems: 0 ThermoPower.Examples.HRB.Simulators.OpenLoopSimulatorSimplified.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 1245 * Number of variables: 1245 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 230 * Number of states: 0 () * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (484): * Single equations (assignments): 480 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 3 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 3 {1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {32 300} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 38 (Plant.Boiler.WaterSide.p,Plant.Boiler.WaterSide.htilde[1],Plant.Boiler.WaterSide.htilde[2],Plant.Boiler.WaterSide.htilde[3],Plant.Boiler.WaterSide.htilde[4],Plant.Boiler.WaterSide.htilde[5],Plant.Boiler.WaterSide.htilde[6],Plant.Boiler.WaterSide.htilde[7],Plant.Boiler.WaterSide.htilde[8],Plant.Boiler.WaterSide.htilde[9],Plant.Boiler.WaterSide.htilde[10],Plant.Boiler.TubeWalls.Tvol[1],Plant.Boiler.TubeWalls.Tvol[2],Plant.Boiler.TubeWalls.Tvol[3],Plant.Boiler.TubeWalls.Tvol[4],Plant.Boiler.TubeWalls.Tvol[5],Plant.Boiler.TubeWalls.Tvol[6],Plant.Boiler.TubeWalls.Tvol[7],Plant.Boiler.TubeWalls.Tvol[8],Plant.Boiler.TubeWalls.Tvol[9],Plant.Boiler.TubeWalls.Tvol[10],Plant.Boiler.GasSide.Ttilde[1],Plant.Boiler.GasSide.Ttilde[2],Plant.Boiler.GasSide.Ttilde[3],Plant.Boiler.GasSide.Ttilde[4],Plant.Boiler.GasSide.Ttilde[5],Plant.Boiler.GasSide.Ttilde[6],Plant.Boiler.GasSide.Ttilde[7],Plant.Boiler.GasSide.Ttilde[8],Plant.Boiler.GasSide.Ttilde[9],Plant.Boiler.GasSide.Ttilde[10],Plant.Boiler.GasSide.p,Plant.GasFlowActuator.y,Plant.WaterInTSensor.y,Plant.WaterOutTSensor.y,Plant.GasInTSensor.y,Plant.GasOutTSensor.y,Plant.ValveOpeningActuator.y) * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (445): * Single equations (assignments): 419 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 4 * Torn equation systems: 22 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 4 {1,1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 22 {(11,62.8%) 40,(1,100.0%) 1,(10,92.0%) 21,(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} * Non-linear torn systems: 0 ThermoPower.Examples.HRB.Simulators.TestPI.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 18 * Number of variables: 18 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: Assuming fixed start value for the following 1 variables: digitalPI.e_int:DISCRETE(start = digitalPI.CSstart * digitalPI.Ti / digitalPI.Kp fixed = false ) "Integrated error" type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 3 * Number of states: 0 () * Number of discrete variables: 17 ($PRE.digitalPI.firstTrigger,digitalPI.firstTrigger,$whenCondition1,digitalPI.sampleTrigger,$whenCondition2,digitalPI.e,$PRE.digitalPI.e_int,digitalPI.e_int,digitalPI.e_int_wind,digitalPI.CSwind,digitalPI.CS,timeTable.a,timeTable.b,timeTable.last,$PRE.timeTable.nextEvent,timeTable.nextEvent,timeTable.nextEventScaled) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (16): * Single equations (assignments): 15 * Array equations: 0 * Algorithm blocks: 1 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 0 * Mixed (continuous/discrete) equation systems: 0 Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 1 (integrator.y) * Number of discrete variables: 14 (digitalPI.sampleTrigger,$whenCondition1,$whenCondition2,digitalPI.firstTrigger,digitalPI.e,digitalPI.e_int,digitalPI.e_int_wind,digitalPI.CSwind,digitalPI.CS,timeTable.a,timeTable.b,timeTable.last,timeTable.nextEvent,timeTable.nextEventScaled) * Number of discrete states: 7 (timeTable.nextEvent,timeTable.last,timeTable.nextEventScaled,timeTable.b,timeTable.a,$whenCondition2,digitalPI.e_int) * Top-level inputs: 0 Notification: Strong component statistics for simulation (12): * Single equations (assignments): 5 * Array equations: 0 * Algorithm blocks: 1 * Record equations: 0 * When equations: 6 ThermoPower.Examples.RankineCycle.Simulators.ClosedLoop.err [ThermoPower 3.1/Examples.mo:2534:70-2534:81:writable] Error: Variable q_nom not found in scope ThermoPower.Examples.RankineCycle.Models. [ThermoPower 3.1/Examples.mo:2542:21-2542:69:writable] Error: Cyclically dependent constants or parameters found in scope : {q_nom}, {head_nom} (ignore with -d=ignoreCycles). Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 2388 * Number of variables: 2388 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: The given system is mixed-determined. [index = 1] Warning: Assuming fixed start value for the following 2 variables: plant.generator.shaft.phi:VARIABLE(flow=false unit = "rad" ) "Absolute rotation angle of flange" type: Real plant.condenser.Vl:VARIABLE(start = plant.condenser.Vlstart unit = "m3" ) "Liquid volume" type: Real Warning: The initial conditions are over specified. The following 3 initial equations are redundant, so they are removed from the initialization sytem: $DER.plant.evaporator.gasFlow.p = 0.0 $DER.plant.economizer.fluidFlow.p = 0.0 $DER.plant.economizer.gasFlow.p = 0.0. Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: plant.evaporator.water.Vv:DUMMY_STATE(unit = "m3" ) "Steam volume" type: Real plant.economizer.fluidFlow.heatTransfer.w_wnom:VARIABLE(unit = "1" ) "Ratio between actual and nominal flow rate" type: Real plant.economizer.gasFlow.heatTransfer.w_wnom:VARIABLE(unit = "1" ) "Ratio between actual and nominal flow rate" type: Real plant.superheater.gasFlow.heatTransfer.w_wnom:VARIABLE(unit = "1" ) "Ratio between actual and nominal flow rate" type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 91 * Number of states: 0 () * Number of discrete variables: 22 (plant.stateWaterEconomizer_in.fluidState.phase,plant.stateWaterEvaporator_in.fluidState.phase,plant.stateWaterSuperheater_out.fluidState.phase,plant.stateWaterSuperheater_in.fluidState.phase,plant.superheater.fluidFlow.fluidState[7].phase,plant.superheater.fluidFlow.fluidState[6].phase,plant.superheater.fluidFlow.fluidState[5].phase,plant.superheater.fluidFlow.fluidState[4].phase,plant.superheater.fluidFlow.fluidState[3].phase,plant.superheater.fluidFlow.fluidState[2].phase,plant.superheater.fluidFlow.fluidState[1].phase,plant.economizer.fluidFlow.fluidState[6].phase,plant.economizer.fluidFlow.fluidState[5].phase,plant.economizer.fluidFlow.fluidState[4].phase,plant.economizer.fluidFlow.fluidState[3].phase,plant.economizer.fluidFlow.fluidState[2].phase,plant.economizer.fluidFlow.fluidState[1].phase,plant.steamTurbine.steamState_in.phase,plant.steamTurbine.steamState_iso.phase,plant.network.closedInternal,plant.prescribedSpeedPump.feedWaterPump.int_Np,plant.prescribedSpeedPump.feedWaterPump.inletFluidState.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (614): * Single equations (assignments): 601 * Array equations: 4 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 6 * Torn equation systems: 3 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 6 {1,1,1,1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(1,100.0%) 3} * Non-linear torn systems: 2 {1 1,53 588} Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 6 * Number of states: 66 ($STATESET3.x,$STATESET2.x[6],$STATESET2.x[5],$STATESET2.x[4],$STATESET2.x[3],$STATESET2.x[2],$STATESET2.x[1],$STATESET1.x[6],$STATESET1.x[5],$STATESET1.x[4],$STATESET1.x[3],$STATESET1.x[2],$STATESET1.x[1],plant.condenser.Vl,plant.powerSensor.y,plant.gasFlowActuator.y,plant.nPumpActuator.y,plant.voidFractionSensor.y,plant.generator.omega_m,plant.generator.shaft.phi,plant.network.delta,plant.economizer.fluidFlow.htilde[1],plant.economizer.fluidFlow.htilde[2],plant.economizer.fluidFlow.htilde[3],plant.economizer.fluidFlow.htilde[4],plant.economizer.fluidFlow.htilde[5],plant.economizer.metalTube.Tvol[1],plant.economizer.metalTube.Tvol[2],plant.economizer.metalTube.Tvol[3],plant.economizer.metalTube.Tvol[4],plant.economizer.metalTube.Tvol[5],plant.economizer.gasFlow.Ttilde[1],plant.economizer.gasFlow.Ttilde[2],plant.economizer.gasFlow.Ttilde[3],plant.economizer.gasFlow.Ttilde[4],plant.economizer.gasFlow.Ttilde[5],plant.economizer.gasFlow.Xtilde[1,1],plant.economizer.gasFlow.Xtilde[1,2],plant.economizer.gasFlow.Xtilde[1,3],plant.economizer.gasFlow.Xtilde[1,4],plant.economizer.gasFlow.Xtilde[1,5],plant.evaporator.water.Vld,plant.evaporator.water.p,plant.evaporator.gasFlow.Ttilde[1],plant.evaporator.gasFlow.Ttilde[2],plant.superheater.fluidFlow.p,plant.superheater.fluidFlow.htilde[1],plant.superheater.fluidFlow.htilde[2],plant.superheater.fluidFlow.htilde[3],plant.superheater.fluidFlow.htilde[4],plant.superheater.fluidFlow.htilde[5],plant.superheater.fluidFlow.htilde[6],plant.superheater.metalTube.Tvol[1],plant.superheater.metalTube.Tvol[2],plant.superheater.metalTube.Tvol[3],plant.superheater.metalTube.Tvol[4],plant.superheater.metalTube.Tvol[5],plant.superheater.metalTube.Tvol[6],plant.superheater.gasFlow.Ttilde[1],plant.superheater.gasFlow.Ttilde[2],plant.superheater.gasFlow.Ttilde[3],plant.superheater.gasFlow.Ttilde[4],plant.superheater.gasFlow.Ttilde[5],plant.superheater.gasFlow.p,voidFractionController.I,powerController.I) * Number of discrete variables: 52 ($cse2.phase,$cse2.region,$cse3.phase,$cse3.region,$cse4.phase,$cse4.region,$cse5.phase,$cse5.region,$cse9.phase,$cse9.region,$cse10.phase,$cse10.region,$cse11.phase,$cse11.region,$cse12.phase,$cse12.region,$cse13.phase,$cse13.region,$cse14.phase,$cse14.region,$cse15.phase,$cse15.region,$cse24.region3boundary,$cse25.region3boundary,$cse34.phase,$cse34.region,$cse35.phase,$cse35.region,$cse36.phase,$cse36.region,$cse37.phase,$cse37.region,$cse38.phase,$cse38.region,$cse39.phase,$cse39.region,$cse40.phase,$cse40.region,$cse41.phase,$cse41.region,$cse42.phase,$cse42.region,$cse43.phase,$cse43.region,$cse44.phase,$cse44.region,$cse45.phase,$cse45.region,$cse48.phase,$cse48.region,$cse52.phase,$cse52.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (975): * Single equations (assignments): 931 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 25 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 6 * Torn equation systems: 13 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 6 {1,1,1,1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 8 {(7,69.4%) 12,(1,100.0%) 3,(1,100.0%) 4,(2,100.0%) 3,(2,100.0%) 3,(2,100.0%) 3,(1,100.0%) 4,(15,33.8%) 40} * Non-linear torn systems: 5 {7 22,2 1,7 1,7 1,3 15} ThermoPower.PowerPlants.ElectricGeneratorGroup.Tests.Test_Generator_SE.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 91 * Number of variables: 91 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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. Warning: Assuming fixed start value for the following 3 variables: generator_SE.shaft.phi:VARIABLE(flow=false unit = "rad" ) "Absolute rotation angle of flange" type: Real generator_SE.d_delta:VARIABLE(unit = "rad/s" ) "Variation of loaded angle" type: Real generator_SE.delta:VARIABLE(start = generator_SE.delta_start unit = "rad" ) "Loaded angle" type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 17 * Number of states: 0 () * Number of discrete variables: 3 (valveHP.fluidState.phase,steamTurbineStodola.steamState_in.phase,steamTurbineStodola.steamState_iso.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (42): * Single equations (assignments): 41 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {1 8} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 3 (generator_SE.delta,generator_SE.d_delta,generator_SE.shaft.phi) * Number of discrete variables: 4 ($cse3.phase,$cse3.region,$cse4.phase,$cse4.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (25): * Single equations (assignments): 23 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 1 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {1 10} ThermoPower.PowerPlants.ElectricGeneratorGroup.Tests.Test_Generator_SE_breaker.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 94 * Number of variables: 94 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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. Warning: Assuming fixed start value for the following 3 variables: generator_SE.shaft.phi:VARIABLE(flow=false unit = "rad" ) "Absolute rotation angle of flange" type: Real generator_SE.d_delta:VARIABLE(unit = "rad/s" ) "Variation of loaded angle" type: Real generator_SE.delta:VARIABLE(start = generator_SE.delta_start unit = "rad" ) "Loaded angle" type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 17 * Number of states: 0 () * Number of discrete variables: 3 (valveHP.fluidState.phase,steamTurbineStodola.steamState_in.phase,steamTurbineStodola.steamState_iso.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (43): * Single equations (assignments): 42 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {1 8} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 3 (generator_SE.delta,generator_SE.d_delta,generator_SE.shaft.phi) * Number of discrete variables: 4 ($cse3.phase,$cse3.region,$cse4.phase,$cse4.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (25): * Single equations (assignments): 23 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 1 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {1 10} ThermoPower.PowerPlants.ElectricGeneratorGroup.Tests.Test_Generator_SE_com.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 91 * Number of variables: 91 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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. Warning: Assuming fixed start value for the following 3 variables: generator_SE.shaft.phi:VARIABLE(flow=false unit = "rad" ) "Absolute rotation angle of flange" type: Real generator_SE.d_delta:VARIABLE(unit = "rad/s" ) "Variation of loaded angle" type: Real generator_SE.delta:VARIABLE(start = generator_SE.delta_start unit = "rad" ) "Loaded angle" type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 17 * Number of states: 0 () * Number of discrete variables: 3 (valveHP.fluidState.phase,steamTurbineStodola.steamState_in.phase,steamTurbineStodola.steamState_iso.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (42): * Single equations (assignments): 41 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {1 8} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 3 (generator_SE.delta,generator_SE.d_delta,generator_SE.shaft.phi) * Number of discrete variables: 4 ($cse3.phase,$cse3.region,$cse4.phase,$cse4.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (27): * Single equations (assignments): 25 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 1 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {1 10} ThermoPower.PowerPlants.Simulators.CCPP_Sim3.err [ThermoPower 3.1/PowerPlants.mo:3950:70-3951:22:writable] Error: Variable q_nom not found in scope ThermoPower.PowerPlants.HRSG.Components. [ThermoPower 3.1/PowerPlants.mo:3960:21-3960:69:writable] Error: Cyclically dependent constants or parameters found in scope : {q_nom}, {head_nom} (ignore with -d=ignoreCycles). Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 7835 * Number of variables: 7835 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: The given system is mixed-determined. [index = 1] Warning: Assuming fixed start value for the following 1 variables: sTG_3LRh.controlledCondeser.condenserIdeal_tap.Vl:VARIABLE(start = sTG_3LRh.controlledCondeser.condenserIdeal_tap.Vlstart unit = "m3" stateSelect=StateSelect.prefer ) "Liquid volume" type: Real Warning: The initial conditions are over specified. The following 23 initial equations are redundant, so they are removed from the initialization sytem: $DER.hRSG.drums.IPd.p = 0.0 $DER.hRSG.HeatExchangersGroup.Ev_IP.fluidFlow.p = 0.0 $DER.hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.p = 0.0 $DER.hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.p = 0.0 $DER.hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.p = 0.0 -- $DER.hRSG.HeatExchangersGroup.Sh_IP.gasFlow.p = 0.0 $DER.hRSG.HeatExchangersGroup.Ev_HP.gasFlow.p = 0.0 $DER.hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.gasFlow.p = 0.0 $DER.hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.gasFlow.p = 0.0 $DER.hRSG.HeatExchangersGroup.Ec_LP.gasFlow.p = 0.0. Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.heatTransfer.w_wnom:VARIABLE(unit = "1" ) "Ratio between actual and nominal flow rate" type: Real hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.heatTransfer.w_wnom:VARIABLE(unit = "1" ) "Ratio between actual and nominal flow rate" type: Real hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.heatTransfer.w_wnom:VARIABLE(unit = "1" ) "Ratio between actual and nominal flow rate" type: Real hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.heatTransfer.w_wnom:VARIABLE(unit = "1" ) "Ratio between actual and nominal flow rate" type: Real hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.heatTransfer.w_wnom:VARIABLE(unit = "1" ) "Ratio between actual and nominal flow rate" type: Real hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.heatTransfer.w_wnom:VARIABLE(unit = "1" ) "Ratio between actual and nominal flow rate" type: Real hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.heatTransfer.w_wnom:VARIABLE(unit = "1" ) "Ratio between actual and nominal flow rate" type: Real Warning: Iteration variables with default zero start attribute in equation system w/o analytic Jacobian: $DER.hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.gasFlow.gas[1].T:DUMMY_DER(fixed = false ) "Temperature of medium" type: Real [3] Warning: Iteration variables with default zero start attribute in equation system w/o analytic Jacobian: $DER.hRSG.HeatExchangersGroup.Ev_HP.gasFlow.gas[1].T:DUMMY_DER(fixed = false ) "Temperature of medium" type: Real [4] Warning: Iteration variables with default zero start attribute in equation system w/o analytic Jacobian: $DER.hRSG.HeatExchangersGroup.Ev_IP.gasFlow.gas[1].T:DUMMY_DER(fixed = false ) "Temperature of medium" type: Real [4] Warning: Iteration variables with default zero start attribute in equation system w/o analytic Jacobian: $DER.hRSG.HeatExchangersGroup.Sh_LP.gasFlow.gas[1].T:DUMMY_DER(fixed = false ) "Temperature of medium" type: Real [3] Warning: Iteration variables with default zero start attribute in equation system w/o analytic Jacobian: $DER.hRSG.HeatExchangersGroup.Ec2_HP.gasFlow.gas[1].T:DUMMY_DER(fixed = false ) "Temperature of medium" type: Real [3] Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 408 * Number of states: 0 () * Number of discrete variables: 101 (sTG_3LRh.totalFeedPump.feedWaterPump.int_Np,sTG_3LRh.totalFeedPump.feedWaterPump.inletFluidState.phase,sTG_3LRh.steamTurbines.valveLP.fluidState.phase,sTG_3LRh.steamTurbines.valveIP.fluidState.phase,sTG_3LRh.steamTurbines.valveHP.fluidState.phase,sTG_3LRh.steamTurbines.mixLP.fluidState.phase,sTG_3LRh.steamTurbines.ST_LP.steamState_in.phase,sTG_3LRh.steamTurbines.ST_LP.steamState_iso.phase,sTG_3LRh.steamTurbines.ST_IP.steamState_in.phase,sTG_3LRh.steamTurbines.ST_IP.steamState_iso.phase,sTG_3LRh.steamTurbines.ST_HP.steamState_in.phase,sTG_3LRh.steamTurbines.ST_HP.steamState_iso.phase,hRSG.HeatExchangersGroup.mixIP.fluidState.phase,hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Ev_HP.fluidFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Ev_HP.fluidFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Ev_HP.fluidFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Ev_HP.fluidFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Ev_IP.fluidFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Ev_IP.fluidFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Ev_IP.fluidFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Ev_IP.fluidFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Ev_LP.fluidFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Ev_LP.fluidFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Ev_LP.fluidFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Ev_LP.fluidFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.fluidState[1].phase,hRSG.drums.LPd.vapourState.phase,hRSG.drums.LPd.liquidState.phase,hRSG.drums.IPd.vapourState.phase,hRSG.drums.IPd.liquidState.phase,hRSG.drums.HPd.vapourState.phase,hRSG.drums.HPd.liquidState.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (1865): * Single equations (assignments): 1832 * Array equations: 18 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 8 * Torn equation systems: 7 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 8 {1,1,1,1,1,1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(1,100.0%) 3} * Non-linear torn systems: 6 {7 56,1 1,1 1,1 1,171 1810,1 1} Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 76 * Number of states: 235 ($STATESET9.x[6],$STATESET9.x[5],$STATESET9.x[4],$STATESET9.x[3],$STATESET9.x[2],$STATESET9.x[1],$STATESET8.x[6],$STATESET8.x[5],$STATESET8.x[4],$STATESET8.x[3],$STATESET8.x[2],$STATESET8.x[1],$STATESET7.x[6],$STATESET7.x[5],$STATESET7.x[4],$STATESET7.x[3],$STATESET7.x[2],$STATESET7.x[1],$STATESET6.x[6],$STATESET6.x[5],$STATESET6.x[4],$STATESET6.x[3],$STATESET6.x[2],$STATESET6.x[1],$STATESET5.x[6],$STATESET5.x[5],$STATESET5.x[4],$STATESET5.x[3],$STATESET5.x[2],$STATESET5.x[1],$STATESET4.x[6],$STATESET4.x[5],$STATESET4.x[4],$STATESET4.x[3],$STATESET4.x[2],$STATESET4.x[1],$STATESET3.x[6],$STATESET3.x[5],$STATESET3.x[4],$STATESET3.x[3],$STATESET3.x[2],$STATESET3.x[1],$STATESET2.x[6],$STATESET2.x[5],$STATESET2.x[4],$STATESET2.x[3],$STATESET2.x[2],$STATESET2.x[1],$STATESET1.x[6],$STATESET1.x[5],$STATESET1.x[4],$STATESET1.x[3],$STATESET1.x[2],$STATESET1.x[1],hRSG.drums.HPd.p,hRSG.drums.HPd.hl,hRSG.drums.HPd.hv,hRSG.drums.HPd.y,hRSG.drums.IPd.hl,hRSG.drums.IPd.hv,hRSG.drums.IPd.y,hRSG.drums.LPd.hl,hRSG.drums.LPd.hv,hRSG.drums.LPd.y,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.htilde[1],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.htilde[2],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.htilde[3],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.htilde[4],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.htilde[5],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.htilde[6],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_A.Tvol[1],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_A.Tvol[2],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_A.Tvol[3],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_A.Tvol[4],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_A.Tvol[5],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_A.Tvol[6],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.p,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.htilde[1],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.htilde[2],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.htilde[3],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.htilde[4],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.htilde[5],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.htilde[6],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_B.Tvol[1],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_B.Tvol[2],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_B.Tvol[3],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_B.Tvol[4],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_B.Tvol[5],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_B.Tvol[6],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.htilde[1],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.htilde[2],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.htilde[3],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.htilde[4],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.htilde[5],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.htilde[6],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_A.Tvol[1],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_A.Tvol[2],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_A.Tvol[3],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_A.Tvol[4],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_A.Tvol[5],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_A.Tvol[6],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.p,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.htilde[1],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.htilde[2],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.htilde[3],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.htilde[4],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.htilde[5],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.htilde[6],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_B.Tvol[1],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_B.Tvol[2],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_B.Tvol[3],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_B.Tvol[4],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_B.Tvol[5],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_B.Tvol[6],hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.htilde[1],hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.htilde[2],hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.htilde[3],hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.htilde[4],hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.htilde[5],hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.htilde[6],hRSG.HeatExchangersGroup.Ec2_HP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Ec2_HP.metalTube.Tvol[1],hRSG.HeatExchangersGroup.Ec2_HP.metalTube.Tvol[2],hRSG.HeatExchangersGroup.Ec2_HP.metalTube.Tvol[3],hRSG.HeatExchangersGroup.Ec2_HP.metalTube.Tvol[4],hRSG.HeatExchangersGroup.Ec2_HP.metalTube.Tvol[5],hRSG.HeatExchangersGroup.Ec2_HP.metalTube.Tvol[6],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.htilde[1],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.htilde[2],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.htilde[3],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.htilde[4],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.htilde[5],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.htilde[6],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_A.Tvol[1],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_A.Tvol[2],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_A.Tvol[3],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_A.Tvol[4],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_A.Tvol[5],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_A.Tvol[6],hRSG.HeatExchangersGroup.Ec1HP_EcIP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.htilde[1],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.htilde[2],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.htilde[3],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.htilde[4],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.htilde[5],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.htilde[6],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_B.Tvol[1],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_B.Tvol[2],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_B.Tvol[3],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_B.Tvol[4],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_B.Tvol[5],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_B.Tvol[6],hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.htilde[1],hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.htilde[2],hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.htilde[3],hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.htilde[4],hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.htilde[5],hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.htilde[6],hRSG.HeatExchangersGroup.Ec_LP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Ec_LP.gasFlow.Ttilde[2],hRSG.HeatExchangersGroup.Ec_LP.gasFlow.Xtilde[1,1],hRSG.HeatExchangersGroup.Ec_LP.gasFlow.Xtilde[1,2],hRSG.HeatExchangersGroup.Ec_LP.gasFlow.Xtilde[1,3],hRSG.HeatExchangersGroup.Ec_LP.gasFlow.Xtilde[1,4],hRSG.HeatExchangersGroup.Ec_LP.gasFlow.Xtilde[1,5],hRSG.HeatExchangersGroup.Ec_LP.metalTube.Tvol[1],hRSG.HeatExchangersGroup.Ec_LP.metalTube.Tvol[2],hRSG.HeatExchangersGroup.Ec_LP.metalTube.Tvol[3],hRSG.HeatExchangersGroup.Ec_LP.metalTube.Tvol[4],hRSG.HeatExchangersGroup.Ec_LP.metalTube.Tvol[5],hRSG.HeatExchangersGroup.Ec_LP.metalTube.Tvol[6],hRSG.HeatExchangersGroup.Ev_LP.fluidFlow.htilde[1],hRSG.HeatExchangersGroup.Ev_LP.fluidFlow.htilde[2],hRSG.HeatExchangersGroup.Ev_LP.fluidFlow.htilde[3],hRSG.HeatExchangersGroup.Ev_LP.metalTube.Tvol[1],hRSG.HeatExchangersGroup.Ev_LP.metalTube.Tvol[2],hRSG.HeatExchangersGroup.Ev_LP.metalTube.Tvol[3],hRSG.HeatExchangersGroup.Ev_LP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Ev_LP.gasFlow.Ttilde[2],hRSG.HeatExchangersGroup.Ev_IP.fluidFlow.htilde[1],hRSG.HeatExchangersGroup.Ev_IP.fluidFlow.htilde[2],hRSG.HeatExchangersGroup.Ev_IP.fluidFlow.htilde[3],hRSG.HeatExchangersGroup.Ev_IP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Ev_IP.gasFlow.Ttilde[2],hRSG.HeatExchangersGroup.Ev_IP.metalTube.Tvol[1],hRSG.HeatExchangersGroup.Ev_IP.metalTube.Tvol[2],hRSG.HeatExchangersGroup.Ev_IP.metalTube.Tvol[3],hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.p,hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.htilde[1],hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.htilde[2],hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.htilde[3],hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.htilde[4],hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.htilde[5],hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.htilde[6],hRSG.HeatExchangersGroup.Sh_LP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Sh_LP.metalTube.Tvol[1],hRSG.HeatExchangersGroup.Sh_LP.metalTube.Tvol[2],hRSG.HeatExchangersGroup.Sh_LP.metalTube.Tvol[3],hRSG.HeatExchangersGroup.Sh_LP.metalTube.Tvol[4],hRSG.HeatExchangersGroup.Sh_LP.metalTube.Tvol[5],hRSG.HeatExchangersGroup.Sh_LP.metalTube.Tvol[6],hRSG.HeatExchangersGroup.Ev_HP.fluidFlow.htilde[1],hRSG.HeatExchangersGroup.Ev_HP.fluidFlow.htilde[2],hRSG.HeatExchangersGroup.Ev_HP.fluidFlow.htilde[3],hRSG.HeatExchangersGroup.Ev_HP.metalTube.Tvol[1],hRSG.HeatExchangersGroup.Ev_HP.metalTube.Tvol[2],hRSG.HeatExchangersGroup.Ev_HP.metalTube.Tvol[3],hRSG.HeatExchangersGroup.Ev_HP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Ev_HP.gasFlow.Ttilde[2],hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.htilde[1],hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.htilde[2],hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.htilde[3],hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.htilde[4],hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.htilde[5],hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.htilde[6],hRSG.HeatExchangersGroup.Sh_IP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Sh_IP.metalTube.Tvol[1],hRSG.HeatExchangersGroup.Sh_IP.metalTube.Tvol[2],hRSG.HeatExchangersGroup.Sh_IP.metalTube.Tvol[3],hRSG.HeatExchangersGroup.Sh_IP.metalTube.Tvol[4],hRSG.HeatExchangersGroup.Sh_IP.metalTube.Tvol[5],hRSG.HeatExchangersGroup.Sh_IP.metalTube.Tvol[6],hRSG.HeatExchangersGroup.mixIP.p,hRSG.HeatExchangersGroup.mixIP.h,singleShaft.network.delta,singleShaft.damper.phi_rel,singleShaft.damper.w_rel,sTG_3LRh.steamTurbines.mixLP.h,sTG_3LRh.controlledCondeser.pID.I,sTG_3LRh.controlledCondeser.condenserIdeal_tap.Vl,levelsControl.Level_HP.I,levelsControl.Level_IP.I,levelsControl.Level_LP.I) * Number of discrete variables: 284 ($cse1.phase,$cse1.region,$cse5.phase,$cse5.region,$cse9.phase,$cse9.region,$cse14.phase,$cse14.region,$cse15.phase,$cse15.region,$cse17.phase,$cse17.region,$cse19.phase,$cse19.region,$cse21.phase,$cse21.region,$cse23.phase,$cse23.region,$cse25.phase,$cse25.region,$cse28.phase,$cse28.region,$cse37.phase,$cse37.region,$cse38.phase,$cse38.region,$cse39.phase,$cse39.region,$cse40.phase,$cse40.region,$cse41.phase,$cse41.region,$cse42.phase,$cse42.region,$cse43.phase,$cse43.region,$cse44.phase,$cse44.region,$cse45.phase,$cse45.region,$cse46.phase,$cse46.region,$cse47.phase,$cse47.region,$cse48.phase,$cse48.region,$cse49.phase,$cse49.region,$cse50.phase,$cse50.region,$cse59.phase,$cse59.region,$cse60.phase,$cse60.region,$cse61.phase,$cse61.region,$cse62.phase,$cse62.region,$cse63.phase,$cse63.region,$cse64.phase,$cse64.region,$cse65.phase,$cse65.region,$cse66.phase,$cse66.region,$cse67.region3boundary,$cse68.region3boundary,$cse78.phase,$cse78.region,$cse79.phase,$cse79.region,$cse80.phase,$cse80.region,$cse81.phase,$cse81.region,$cse82.phase,$cse82.region,$cse83.phase,$cse83.region,$cse84.phase,$cse84.region,$cse93.phase,$cse93.region,$cse94.phase,$cse94.region,$cse95.phase,$cse95.region,$cse96.phase,$cse96.region,$cse97.phase,$cse97.region,$cse98.phase,$cse98.region,$cse99.phase,$cse99.region,$cse100.phase,$cse100.region,$cse109.phase,$cse109.region,$cse110.phase,$cse110.region,$cse111.phase,$cse111.region,$cse112.phase,$cse112.region,$cse113.phase,$cse113.region,$cse114.phase,$cse114.region,$cse115.phase,$cse115.region,$cse116.phase,$cse116.region,$cse117.region3boundary,$cse118.region3boundary,$cse128.phase,$cse128.region,$cse129.phase,$cse129.region,$cse130.phase,$cse130.region,$cse131.phase,$cse131.region,$cse132.phase,$cse132.region,$cse133.phase,$cse133.region,$cse134.phase,$cse134.region,$cse135.phase,$cse135.region,$cse136.phase,$cse136.region,$cse137.phase,$cse137.region,$cse138.phase,$cse138.region,$cse139.phase,$cse139.region,$cse140.phase,$cse140.region,$cse141.phase,$cse141.region,$cse143.phase,$cse143.region,$cse144.phase,$cse144.region,$cse145.phase,$cse145.region,$cse146.phase,$cse146.region,$cse147.phase,$cse147.region,$cse148.phase,$cse148.region,$cse149.phase,$cse149.region,$cse150.phase,$cse150.region,$cse151.phase,$cse151.region,$cse152.phase,$cse152.region,$cse153.phase,$cse153.region,$cse154.phase,$cse154.region,$cse155.phase,$cse155.region,$cse156.phase,$cse156.region,$cse165.phase,$cse165.region,$cse166.phase,$cse166.region,$cse167.phase,$cse167.region,$cse168.phase,$cse168.region,$cse169.phase,$cse169.region,$cse170.phase,$cse170.region,$cse171.phase,$cse171.region,$cse180.phase,$cse180.region,$cse181.phase,$cse181.region,$cse182.phase,$cse182.region,$cse183.phase,$cse183.region,$cse184.phase,$cse184.region,$cse185.phase,$cse185.region,$cse186.phase,$cse186.region,$cse187.phase,$cse187.region,$cse188.phase,$cse188.region,$cse189.phase,$cse189.region,$cse190.phase,$cse190.region,$cse191.phase,$cse191.region,$cse192.phase,$cse192.region,$cse193.phase,$cse193.region,$cse195.phase,$cse195.region,$cse196.phase,$cse196.region,$cse197.phase,$cse197.region,$cse198.phase,$cse198.region,$cse199.phase,$cse199.region,$cse200.phase,$cse200.region,$cse205.phase,$cse205.region,$cse206.phase,$cse206.region,$cse207.phase,$cse207.region,$cse208.phase,$cse208.region,$cse209.phase,$cse209.region,$cse210.phase,$cse210.region,$cse212.phase,$cse212.region,$cse213.phase,$cse213.region,$cse214.phase,$cse214.region,$cse215.phase,$cse215.region,$cse216.phase,$cse216.region,$cse217.phase,$cse217.region,$cse218.phase,$cse218.region,$cse228.phase,$cse228.region,$cse229.phase,$cse229.region,$cse230.phase,$cse230.region,$cse231.phase,$cse231.region,$cse232.phase,$cse232.region,$cse233.phase,$cse233.region,$cse234.phase,$cse234.region,$cse235.region3boundary,$cse236.region3boundary,$cse237.phase,$cse237.region,$cse238.phase,$cse238.region,$cse240.region3boundary,$cse241.region3boundary,$cse242.phase,$cse242.region,$cse243.phase,$cse243.region,$cse245.region3boundary,$cse246.region3boundary,$cse247.phase,$cse247.region,$cse248.phase,$cse248.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (2959): * Single equations (assignments): 2760 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 146 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 8 * Torn equation systems: 45 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 8 {1,1,1,1,1,1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 29 {(1,100.0%) 3,(7,69.4%) 12,(7,69.4%) 12,(2,100.0%) 3,(1,100.0%) 4,(1,100.0%) 3,(1,100.0%) 3,(1,100.0%) 3,(1,100.0%) 2,(1,100.0%) 4,(1,100.0%) 4,(1,100.0%) 2,(1,100.0%) 4,(1,100.0%) 2,(2,100.0%) 3,(1,100.0%) 2,(1,100.0%) 4,(1,100.0%) 4,(1,100.0%) 2,(1,100.0%) 4,(1,100.0%) 2,(2,100.0%) 3,(1,100.0%) 2,(1,100.0%) 4,(1,100.0%) 4,(1,100.0%) 2,(1,100.0%) 4,(1,100.0%) 2,(1,100.0%) 4} * Non-linear torn systems: 16 {21 69,1 10,1 10,21 68,34 129,7 1,7 1,7 1,7 1,7 1,7 1,7 1,7 1,7 1,1 10,1 1} ThermoPower.PowerPlants.Simulators.SteamPlant_Sim1.err [ThermoPower 3.1/PowerPlants.mo:3950:70-3951:22:writable] Error: Variable q_nom not found in scope ThermoPower.PowerPlants.HRSG.Components. [ThermoPower 3.1/PowerPlants.mo:3960:21-3960:69:writable] Error: Cyclically dependent constants or parameters found in scope : {q_nom}, {head_nom} (ignore with -d=ignoreCycles). Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 7839 * Number of variables: 7839 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: The given system is mixed-determined. [index = 2] Warning: Assuming fixed start value for the following 2 variables: sTG_3LRh.controlledCondeser.condenserIdeal_tap.Vl:VARIABLE(start = sTG_3LRh.controlledCondeser.condenserIdeal_tap.Vlstart unit = "m3" stateSelect=StateSelect.prefer ) "Liquid volume" type: Real sTG_3LRh.controlledCondeser.pID.I:VARIABLE(start = sTG_3LRh.controlledCondeser.pID.CSstart / sTG_3LRh.controlledCondeser.pID.Kp ) "Integral action / Kp" type: Real Warning: The initial conditions are over specified. The following 23 initial equations are redundant, so they are removed from the initialization sytem: $DER.hRSG.drums.IPd.p = 0.0 $DER.hRSG.HeatExchangersGroup.Ev_IP.fluidFlow.p = 0.0 $DER.hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.p = 0.0 $DER.hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.p = 0.0 $DER.hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.p = 0.0 -- $DER.hRSG.HeatExchangersGroup.Sh_IP.gasFlow.p = 0.0 $DER.hRSG.HeatExchangersGroup.Ev_HP.gasFlow.p = 0.0 $DER.hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.gasFlow.p = 0.0 $DER.hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.gasFlow.p = 0.0 $DER.hRSG.HeatExchangersGroup.Ec_LP.gasFlow.p = 0.0. Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.heatTransfer.w_wnom:VARIABLE(unit = "1" ) "Ratio between actual and nominal flow rate" type: Real hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.heatTransfer.w_wnom:VARIABLE(unit = "1" ) "Ratio between actual and nominal flow rate" type: Real hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.heatTransfer.w_wnom:VARIABLE(unit = "1" ) "Ratio between actual and nominal flow rate" type: Real hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.heatTransfer.w_wnom:VARIABLE(unit = "1" ) "Ratio between actual and nominal flow rate" type: Real hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.heatTransfer.w_wnom:VARIABLE(unit = "1" ) "Ratio between actual and nominal flow rate" type: Real hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.heatTransfer.w_wnom:VARIABLE(unit = "1" ) "Ratio between actual and nominal flow rate" type: Real hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.heatTransfer.w_wnom:VARIABLE(unit = "1" ) "Ratio between actual and nominal flow rate" type: Real Warning: Iteration variables with default zero start attribute in equation system w/o analytic Jacobian: $DER.hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.gasFlow.gas[1].T:DUMMY_DER(fixed = false ) "Temperature of medium" type: Real [3] Warning: Iteration variables with default zero start attribute in equation system w/o analytic Jacobian: $DER.hRSG.HeatExchangersGroup.Ev_HP.gasFlow.gas[1].T:DUMMY_DER(fixed = false ) "Temperature of medium" type: Real [4] Warning: Iteration variables with default zero start attribute in equation system w/o analytic Jacobian: $DER.hRSG.HeatExchangersGroup.Ev_IP.gasFlow.gas[1].T:DUMMY_DER(fixed = false ) "Temperature of medium" type: Real [4] Warning: Iteration variables with default zero start attribute in equation system w/o analytic Jacobian: $DER.hRSG.HeatExchangersGroup.Ev_LP.gasFlow.gas[1].T:DUMMY_DER(fixed = false ) "Temperature of medium" type: Real [4] Warning: Iteration variables with default zero start attribute in equation system w/o analytic Jacobian: $DER.hRSG.HeatExchangersGroup.Sh_LP.gasFlow.gas[1].T:DUMMY_DER(fixed = false ) "Temperature of medium" type: Real [3] Warning: Iteration variables with default zero start attribute in equation system w/o analytic Jacobian: $DER.hRSG.HeatExchangersGroup.Ec2_HP.gasFlow.gas[1].T:DUMMY_DER(fixed = false ) "Temperature of medium" type: Real [3] Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 403 * Number of states: 0 () * Number of discrete variables: 101 (sTG_3LRh.totalFeedPump.feedWaterPump.int_Np,sTG_3LRh.totalFeedPump.feedWaterPump.inletFluidState.phase,sTG_3LRh.steamTurbines.valveLP.fluidState.phase,sTG_3LRh.steamTurbines.valveIP.fluidState.phase,sTG_3LRh.steamTurbines.valveHP.fluidState.phase,sTG_3LRh.steamTurbines.mixLP.fluidState.phase,sTG_3LRh.steamTurbines.ST_LP.steamState_in.phase,sTG_3LRh.steamTurbines.ST_LP.steamState_iso.phase,sTG_3LRh.steamTurbines.ST_IP.steamState_in.phase,sTG_3LRh.steamTurbines.ST_IP.steamState_iso.phase,sTG_3LRh.steamTurbines.ST_HP.steamState_in.phase,sTG_3LRh.steamTurbines.ST_HP.steamState_iso.phase,hRSG.HeatExchangersGroup.mixIP.fluidState.phase,hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Ev_HP.fluidFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Ev_HP.fluidFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Ev_HP.fluidFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Ev_HP.fluidFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Ev_IP.fluidFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Ev_IP.fluidFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Ev_IP.fluidFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Ev_IP.fluidFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Ev_LP.fluidFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Ev_LP.fluidFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Ev_LP.fluidFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Ev_LP.fluidFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.fluidState[1].phase,hRSG.drums.LPd.vapourState.phase,hRSG.drums.LPd.liquidState.phase,hRSG.drums.IPd.vapourState.phase,hRSG.drums.IPd.liquidState.phase,hRSG.drums.HPd.vapourState.phase,hRSG.drums.HPd.liquidState.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (1854): * Single equations (assignments): 1821 * Array equations: 18 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 9 * Torn equation systems: 6 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 9 {1,1,1,1,1,1,1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(1,100.0%) 3} * Non-linear torn systems: 5 {7 56,1 1,1 1,1 1,171 1810} Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 76 * Number of states: 235 ($STATESET9.x[6],$STATESET9.x[5],$STATESET9.x[4],$STATESET9.x[3],$STATESET9.x[2],$STATESET9.x[1],$STATESET8.x[6],$STATESET8.x[5],$STATESET8.x[4],$STATESET8.x[3],$STATESET8.x[2],$STATESET8.x[1],$STATESET7.x[6],$STATESET7.x[5],$STATESET7.x[4],$STATESET7.x[3],$STATESET7.x[2],$STATESET7.x[1],$STATESET6.x[6],$STATESET6.x[5],$STATESET6.x[4],$STATESET6.x[3],$STATESET6.x[2],$STATESET6.x[1],$STATESET5.x[6],$STATESET5.x[5],$STATESET5.x[4],$STATESET5.x[3],$STATESET5.x[2],$STATESET5.x[1],$STATESET4.x[6],$STATESET4.x[5],$STATESET4.x[4],$STATESET4.x[3],$STATESET4.x[2],$STATESET4.x[1],$STATESET3.x[6],$STATESET3.x[5],$STATESET3.x[4],$STATESET3.x[3],$STATESET3.x[2],$STATESET3.x[1],$STATESET2.x[6],$STATESET2.x[5],$STATESET2.x[4],$STATESET2.x[3],$STATESET2.x[2],$STATESET2.x[1],$STATESET1.x[6],$STATESET1.x[5],$STATESET1.x[4],$STATESET1.x[3],$STATESET1.x[2],$STATESET1.x[1],hRSG.drums.HPd.p,hRSG.drums.HPd.hl,hRSG.drums.HPd.hv,hRSG.drums.HPd.y,hRSG.drums.IPd.hl,hRSG.drums.IPd.hv,hRSG.drums.IPd.y,hRSG.drums.LPd.hl,hRSG.drums.LPd.hv,hRSG.drums.LPd.y,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.htilde[1],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.htilde[2],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.htilde[3],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.htilde[4],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.htilde[5],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.htilde[6],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_A.Tvol[1],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_A.Tvol[2],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_A.Tvol[3],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_A.Tvol[4],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_A.Tvol[5],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_A.Tvol[6],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.p,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.htilde[1],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.htilde[2],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.htilde[3],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.htilde[4],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.htilde[5],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.htilde[6],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_B.Tvol[1],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_B.Tvol[2],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_B.Tvol[3],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_B.Tvol[4],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_B.Tvol[5],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_B.Tvol[6],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.htilde[1],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.htilde[2],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.htilde[3],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.htilde[4],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.htilde[5],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.htilde[6],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_A.Tvol[1],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_A.Tvol[2],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_A.Tvol[3],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_A.Tvol[4],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_A.Tvol[5],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_A.Tvol[6],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.p,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.htilde[1],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.htilde[2],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.htilde[3],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.htilde[4],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.htilde[5],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.htilde[6],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_B.Tvol[1],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_B.Tvol[2],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_B.Tvol[3],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_B.Tvol[4],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_B.Tvol[5],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_B.Tvol[6],hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.htilde[1],hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.htilde[2],hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.htilde[3],hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.htilde[4],hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.htilde[5],hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.htilde[6],hRSG.HeatExchangersGroup.Ec2_HP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Ec2_HP.metalTube.Tvol[1],hRSG.HeatExchangersGroup.Ec2_HP.metalTube.Tvol[2],hRSG.HeatExchangersGroup.Ec2_HP.metalTube.Tvol[3],hRSG.HeatExchangersGroup.Ec2_HP.metalTube.Tvol[4],hRSG.HeatExchangersGroup.Ec2_HP.metalTube.Tvol[5],hRSG.HeatExchangersGroup.Ec2_HP.metalTube.Tvol[6],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.htilde[1],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.htilde[2],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.htilde[3],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.htilde[4],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.htilde[5],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.htilde[6],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_A.Tvol[1],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_A.Tvol[2],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_A.Tvol[3],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_A.Tvol[4],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_A.Tvol[5],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_A.Tvol[6],hRSG.HeatExchangersGroup.Ec1HP_EcIP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.htilde[1],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.htilde[2],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.htilde[3],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.htilde[4],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.htilde[5],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.htilde[6],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_B.Tvol[1],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_B.Tvol[2],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_B.Tvol[3],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_B.Tvol[4],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_B.Tvol[5],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_B.Tvol[6],hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.htilde[1],hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.htilde[2],hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.htilde[3],hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.htilde[4],hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.htilde[5],hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.htilde[6],hRSG.HeatExchangersGroup.Ec_LP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Ec_LP.gasFlow.Ttilde[2],hRSG.HeatExchangersGroup.Ec_LP.gasFlow.Xtilde[1,1],hRSG.HeatExchangersGroup.Ec_LP.gasFlow.Xtilde[1,2],hRSG.HeatExchangersGroup.Ec_LP.gasFlow.Xtilde[1,3],hRSG.HeatExchangersGroup.Ec_LP.gasFlow.Xtilde[1,4],hRSG.HeatExchangersGroup.Ec_LP.gasFlow.Xtilde[1,5],hRSG.HeatExchangersGroup.Ec_LP.metalTube.Tvol[1],hRSG.HeatExchangersGroup.Ec_LP.metalTube.Tvol[2],hRSG.HeatExchangersGroup.Ec_LP.metalTube.Tvol[3],hRSG.HeatExchangersGroup.Ec_LP.metalTube.Tvol[4],hRSG.HeatExchangersGroup.Ec_LP.metalTube.Tvol[5],hRSG.HeatExchangersGroup.Ec_LP.metalTube.Tvol[6],hRSG.HeatExchangersGroup.Ev_LP.fluidFlow.htilde[1],hRSG.HeatExchangersGroup.Ev_LP.fluidFlow.htilde[2],hRSG.HeatExchangersGroup.Ev_LP.fluidFlow.htilde[3],hRSG.HeatExchangersGroup.Ev_LP.metalTube.Tvol[1],hRSG.HeatExchangersGroup.Ev_LP.metalTube.Tvol[2],hRSG.HeatExchangersGroup.Ev_LP.metalTube.Tvol[3],hRSG.HeatExchangersGroup.Ev_LP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Ev_LP.gasFlow.Ttilde[2],hRSG.HeatExchangersGroup.Ev_IP.fluidFlow.htilde[1],hRSG.HeatExchangersGroup.Ev_IP.fluidFlow.htilde[2],hRSG.HeatExchangersGroup.Ev_IP.fluidFlow.htilde[3],hRSG.HeatExchangersGroup.Ev_IP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Ev_IP.gasFlow.Ttilde[2],hRSG.HeatExchangersGroup.Ev_IP.metalTube.Tvol[1],hRSG.HeatExchangersGroup.Ev_IP.metalTube.Tvol[2],hRSG.HeatExchangersGroup.Ev_IP.metalTube.Tvol[3],hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.p,hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.htilde[1],hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.htilde[2],hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.htilde[3],hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.htilde[4],hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.htilde[5],hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.htilde[6],hRSG.HeatExchangersGroup.Sh_LP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Sh_LP.metalTube.Tvol[1],hRSG.HeatExchangersGroup.Sh_LP.metalTube.Tvol[2],hRSG.HeatExchangersGroup.Sh_LP.metalTube.Tvol[3],hRSG.HeatExchangersGroup.Sh_LP.metalTube.Tvol[4],hRSG.HeatExchangersGroup.Sh_LP.metalTube.Tvol[5],hRSG.HeatExchangersGroup.Sh_LP.metalTube.Tvol[6],hRSG.HeatExchangersGroup.Ev_HP.fluidFlow.htilde[1],hRSG.HeatExchangersGroup.Ev_HP.fluidFlow.htilde[2],hRSG.HeatExchangersGroup.Ev_HP.fluidFlow.htilde[3],hRSG.HeatExchangersGroup.Ev_HP.metalTube.Tvol[1],hRSG.HeatExchangersGroup.Ev_HP.metalTube.Tvol[2],hRSG.HeatExchangersGroup.Ev_HP.metalTube.Tvol[3],hRSG.HeatExchangersGroup.Ev_HP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Ev_HP.gasFlow.Ttilde[2],hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.htilde[1],hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.htilde[2],hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.htilde[3],hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.htilde[4],hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.htilde[5],hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.htilde[6],hRSG.HeatExchangersGroup.Sh_IP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Sh_IP.metalTube.Tvol[1],hRSG.HeatExchangersGroup.Sh_IP.metalTube.Tvol[2],hRSG.HeatExchangersGroup.Sh_IP.metalTube.Tvol[3],hRSG.HeatExchangersGroup.Sh_IP.metalTube.Tvol[4],hRSG.HeatExchangersGroup.Sh_IP.metalTube.Tvol[5],hRSG.HeatExchangersGroup.Sh_IP.metalTube.Tvol[6],hRSG.HeatExchangersGroup.mixIP.p,hRSG.HeatExchangersGroup.mixIP.h,sTG_3LRh.steamTurbines.mixLP.h,sTG_3LRh.controlledCondeser.pID.I,sTG_3LRh.controlledCondeser.condenserIdeal_tap.Vl,levelsControl.Level_HP.I,levelsControl.Level_IP.I,levelsControl.Level_LP.I,singleShaft.network.delta,singleShaft.damper.phi_rel,singleShaft.damper.w_rel) * Number of discrete variables: 284 ($cse1.phase,$cse1.region,$cse5.phase,$cse5.region,$cse9.phase,$cse9.region,$cse14.phase,$cse14.region,$cse15.phase,$cse15.region,$cse17.phase,$cse17.region,$cse19.phase,$cse19.region,$cse21.phase,$cse21.region,$cse23.phase,$cse23.region,$cse25.phase,$cse25.region,$cse28.phase,$cse28.region,$cse37.phase,$cse37.region,$cse38.phase,$cse38.region,$cse39.phase,$cse39.region,$cse40.phase,$cse40.region,$cse41.phase,$cse41.region,$cse42.phase,$cse42.region,$cse43.phase,$cse43.region,$cse44.phase,$cse44.region,$cse45.phase,$cse45.region,$cse46.phase,$cse46.region,$cse47.phase,$cse47.region,$cse48.phase,$cse48.region,$cse49.phase,$cse49.region,$cse50.phase,$cse50.region,$cse59.phase,$cse59.region,$cse60.phase,$cse60.region,$cse61.phase,$cse61.region,$cse62.phase,$cse62.region,$cse63.phase,$cse63.region,$cse64.phase,$cse64.region,$cse65.phase,$cse65.region,$cse66.phase,$cse66.region,$cse67.region3boundary,$cse68.region3boundary,$cse78.phase,$cse78.region,$cse79.phase,$cse79.region,$cse80.phase,$cse80.region,$cse81.phase,$cse81.region,$cse82.phase,$cse82.region,$cse83.phase,$cse83.region,$cse84.phase,$cse84.region,$cse93.phase,$cse93.region,$cse94.phase,$cse94.region,$cse95.phase,$cse95.region,$cse96.phase,$cse96.region,$cse97.phase,$cse97.region,$cse98.phase,$cse98.region,$cse99.phase,$cse99.region,$cse100.phase,$cse100.region,$cse109.phase,$cse109.region,$cse110.phase,$cse110.region,$cse111.phase,$cse111.region,$cse112.phase,$cse112.region,$cse113.phase,$cse113.region,$cse114.phase,$cse114.region,$cse115.phase,$cse115.region,$cse116.phase,$cse116.region,$cse117.region3boundary,$cse118.region3boundary,$cse128.phase,$cse128.region,$cse129.phase,$cse129.region,$cse130.phase,$cse130.region,$cse131.phase,$cse131.region,$cse132.phase,$cse132.region,$cse133.phase,$cse133.region,$cse134.phase,$cse134.region,$cse135.phase,$cse135.region,$cse136.phase,$cse136.region,$cse137.phase,$cse137.region,$cse138.phase,$cse138.region,$cse139.phase,$cse139.region,$cse140.phase,$cse140.region,$cse141.phase,$cse141.region,$cse143.phase,$cse143.region,$cse144.phase,$cse144.region,$cse145.phase,$cse145.region,$cse146.phase,$cse146.region,$cse147.phase,$cse147.region,$cse148.phase,$cse148.region,$cse149.phase,$cse149.region,$cse150.phase,$cse150.region,$cse151.phase,$cse151.region,$cse152.phase,$cse152.region,$cse153.phase,$cse153.region,$cse154.phase,$cse154.region,$cse155.phase,$cse155.region,$cse156.phase,$cse156.region,$cse165.phase,$cse165.region,$cse166.phase,$cse166.region,$cse167.phase,$cse167.region,$cse168.phase,$cse168.region,$cse169.phase,$cse169.region,$cse170.phase,$cse170.region,$cse171.phase,$cse171.region,$cse180.phase,$cse180.region,$cse181.phase,$cse181.region,$cse182.phase,$cse182.region,$cse183.phase,$cse183.region,$cse184.phase,$cse184.region,$cse185.phase,$cse185.region,$cse186.phase,$cse186.region,$cse187.phase,$cse187.region,$cse188.phase,$cse188.region,$cse189.phase,$cse189.region,$cse190.phase,$cse190.region,$cse191.phase,$cse191.region,$cse192.phase,$cse192.region,$cse193.phase,$cse193.region,$cse195.phase,$cse195.region,$cse196.phase,$cse196.region,$cse197.phase,$cse197.region,$cse198.phase,$cse198.region,$cse199.phase,$cse199.region,$cse200.phase,$cse200.region,$cse205.phase,$cse205.region,$cse206.phase,$cse206.region,$cse207.phase,$cse207.region,$cse208.phase,$cse208.region,$cse209.phase,$cse209.region,$cse210.phase,$cse210.region,$cse212.phase,$cse212.region,$cse213.phase,$cse213.region,$cse214.phase,$cse214.region,$cse215.phase,$cse215.region,$cse216.phase,$cse216.region,$cse217.phase,$cse217.region,$cse218.phase,$cse218.region,$cse228.phase,$cse228.region,$cse229.phase,$cse229.region,$cse230.phase,$cse230.region,$cse231.phase,$cse231.region,$cse232.phase,$cse232.region,$cse233.phase,$cse233.region,$cse234.phase,$cse234.region,$cse235.region3boundary,$cse236.region3boundary,$cse237.phase,$cse237.region,$cse238.phase,$cse238.region,$cse240.region3boundary,$cse241.region3boundary,$cse242.phase,$cse242.region,$cse243.phase,$cse243.region,$cse245.region3boundary,$cse246.region3boundary,$cse247.phase,$cse247.region,$cse248.phase,$cse248.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (2945): * Single equations (assignments): 2745 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 146 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 9 * Torn equation systems: 45 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 9 {1,1,1,1,1,1,1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 29 {(1,100.0%) 3,(7,69.4%) 12,(7,69.4%) 12,(1,100.0%) 4,(2,100.0%) 3,(1,100.0%) 3,(1,100.0%) 3,(1,100.0%) 3,(1,100.0%) 2,(1,100.0%) 4,(2,100.0%) 3,(1,100.0%) 2,(1,100.0%) 4,(1,100.0%) 2,(1,100.0%) 4,(1,100.0%) 2,(1,100.0%) 4,(1,100.0%) 4,(1,100.0%) 2,(1,100.0%) 4,(1,100.0%) 2,(1,100.0%) 4,(1,100.0%) 2,(1,100.0%) 4,(2,100.0%) 3,(1,100.0%) 2,(1,100.0%) 4,(1,100.0%) 2,(2,100.0%) 3} * Non-linear torn systems: 16 {21 69,1 10,1 10,21 68,34 129,7 1,7 1,7 1,7 1,7 1,7 1,7 1,7 1,7 1,1 10,1 1} ThermoPower.PowerPlants.Simulators.SteamPlant_Sim1_dp.err [ThermoPower 3.1/PowerPlants.mo:3950:70-3951:22:writable] Error: Variable q_nom not found in scope ThermoPower.PowerPlants.HRSG.Components. [ThermoPower 3.1/PowerPlants.mo:3960:21-3960:69:writable] Error: Cyclically dependent constants or parameters found in scope : {q_nom}, {head_nom} (ignore with -d=ignoreCycles). Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 7839 * Number of variables: 7839 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: The given system is mixed-determined. [index = 1] Warning: Assuming fixed start value for the following 1 variables: sTG_3LRh.controlledCondeser.condenserIdeal_tap.Vl:VARIABLE(start = sTG_3LRh.controlledCondeser.condenserIdeal_tap.Vlstart unit = "m3" stateSelect=StateSelect.prefer ) "Liquid volume" type: Real Warning: The initial conditions are over specified. The following 25 initial equations are redundant, so they are removed from the initialization sytem: $DER.hRSG.drums.IPd.p = 0.0 $DER.hRSG.HeatExchangersGroup.Ev_IP.fluidFlow.p = 0.0 $DER.hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.p = 0.0 $DER.hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.p = 0.0 $DER.hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.p = 0.0 -- $DER.hRSG.HeatExchangersGroup.Sh_IP.gasFlow.p = 0.0 $DER.hRSG.HeatExchangersGroup.Ev_HP.gasFlow.p = 0.0 $DER.hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.gasFlow.p = 0.0 $DER.hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.gasFlow.p = 0.0 $DER.hRSG.HeatExchangersGroup.Ec_LP.gasFlow.p = 0.0. Warning: Iteration variables with default zero start attribute in equation system w/o analytic Jacobian: $DER.hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.gasFlow.gas[1].T:DUMMY_DER(fixed = false ) "Temperature of medium" type: Real [3] Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.heatTransfer.w_wnom:VARIABLE(unit = "1" ) "Ratio between actual and nominal flow rate" type: Real hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.heatTransfer.w_wnom:VARIABLE(unit = "1" ) "Ratio between actual and nominal flow rate" type: Real hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.heatTransfer.w_wnom:VARIABLE(unit = "1" ) "Ratio between actual and nominal flow rate" type: Real hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.heatTransfer.w_wnom:VARIABLE(unit = "1" ) "Ratio between actual and nominal flow rate" type: Real hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.heatTransfer.w_wnom:VARIABLE(unit = "1" ) "Ratio between actual and nominal flow rate" type: Real hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.heatTransfer.w_wnom:VARIABLE(unit = "1" ) "Ratio between actual and nominal flow rate" type: Real hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.heatTransfer.w_wnom:VARIABLE(unit = "1" ) "Ratio between actual and nominal flow rate" type: Real Warning: Iteration variables with default zero start attribute in equation system w/o analytic Jacobian: $DER.hRSG.HeatExchangersGroup.Ev_HP.gasFlow.gas[1].T:DUMMY_DER(fixed = false ) "Temperature of medium" type: Real [4] Warning: Iteration variables with default zero start attribute in equation system w/o analytic Jacobian: $DER.hRSG.HeatExchangersGroup.Ev_IP.gasFlow.gas[1].T:DUMMY_DER(fixed = false ) "Temperature of medium" type: Real [4] Warning: Iteration variables with default zero start attribute in equation system w/o analytic Jacobian: $DER.hRSG.HeatExchangersGroup.Sh_LP.gasFlow.gas[1].T:DUMMY_DER(fixed = false ) "Temperature of medium" type: Real [3] Warning: Iteration variables with default zero start attribute in equation system w/o analytic Jacobian: $DER.hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.gasFlow.gas[1].T:DUMMY_DER(fixed = false ) "Temperature of medium" type: Real [3] Warning: Iteration variables with default zero start attribute in equation system w/o analytic Jacobian: $DER.hRSG.HeatExchangersGroup.Ec2_HP.gasFlow.gas[1].T:DUMMY_DER(fixed = false ) "Temperature of medium" type: Real [3] Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 411 * Number of states: 0 () * Number of discrete variables: 101 (sTG_3LRh.totalFeedPump.feedWaterPump.int_Np,sTG_3LRh.totalFeedPump.feedWaterPump.inletFluidState.phase,sTG_3LRh.steamTurbines.valveLP.fluidState.phase,sTG_3LRh.steamTurbines.valveIP.fluidState.phase,sTG_3LRh.steamTurbines.valveHP.fluidState.phase,sTG_3LRh.steamTurbines.mixLP.fluidState.phase,sTG_3LRh.steamTurbines.ST_LP.steamState_in.phase,sTG_3LRh.steamTurbines.ST_LP.steamState_iso.phase,sTG_3LRh.steamTurbines.ST_IP.steamState_in.phase,sTG_3LRh.steamTurbines.ST_IP.steamState_iso.phase,sTG_3LRh.steamTurbines.ST_HP.steamState_in.phase,sTG_3LRh.steamTurbines.ST_HP.steamState_iso.phase,hRSG.HeatExchangersGroup.mixIP.fluidState.phase,hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Ev_HP.fluidFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Ev_HP.fluidFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Ev_HP.fluidFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Ev_HP.fluidFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Ev_IP.fluidFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Ev_IP.fluidFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Ev_IP.fluidFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Ev_IP.fluidFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Ev_LP.fluidFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Ev_LP.fluidFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Ev_LP.fluidFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Ev_LP.fluidFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.fluidState[1].phase,hRSG.drums.LPd.vapourState.phase,hRSG.drums.LPd.liquidState.phase,hRSG.drums.IPd.vapourState.phase,hRSG.drums.IPd.liquidState.phase,hRSG.drums.HPd.vapourState.phase,hRSG.drums.HPd.liquidState.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (1869): * Single equations (assignments): 1835 * Array equations: 18 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 9 * Torn equation systems: 7 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 9 {1,1,1,1,1,1,1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(1,100.0%) 3} * Non-linear torn systems: 6 {7 56,1 1,1 1,1 1,169 1798,1 1} Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 78 * Number of states: 233 ($STATESET9.x[6],$STATESET9.x[5],$STATESET9.x[4],$STATESET9.x[3],$STATESET9.x[2],$STATESET9.x[1],$STATESET8.x[6],$STATESET8.x[5],$STATESET8.x[4],$STATESET8.x[3],$STATESET8.x[2],$STATESET8.x[1],$STATESET7.x[6],$STATESET7.x[5],$STATESET7.x[4],$STATESET7.x[3],$STATESET7.x[2],$STATESET7.x[1],$STATESET6.x[6],$STATESET6.x[5],$STATESET6.x[4],$STATESET6.x[3],$STATESET6.x[2],$STATESET6.x[1],$STATESET5.x[6],$STATESET5.x[5],$STATESET5.x[4],$STATESET5.x[3],$STATESET5.x[2],$STATESET5.x[1],$STATESET4.x[6],$STATESET4.x[5],$STATESET4.x[4],$STATESET4.x[3],$STATESET4.x[2],$STATESET4.x[1],$STATESET3.x[6],$STATESET3.x[5],$STATESET3.x[4],$STATESET3.x[3],$STATESET3.x[2],$STATESET3.x[1],$STATESET2.x[6],$STATESET2.x[5],$STATESET2.x[4],$STATESET2.x[3],$STATESET2.x[2],$STATESET2.x[1],$STATESET1.x[6],$STATESET1.x[5],$STATESET1.x[4],$STATESET1.x[3],$STATESET1.x[2],$STATESET1.x[1],hRSG.drums.HPd.p,hRSG.drums.HPd.hl,hRSG.drums.HPd.hv,hRSG.drums.HPd.y,hRSG.drums.IPd.hl,hRSG.drums.IPd.hv,hRSG.drums.IPd.y,hRSG.drums.LPd.hl,hRSG.drums.LPd.hv,hRSG.drums.LPd.y,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.htilde[1],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.htilde[2],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.htilde[3],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.htilde[4],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.htilde[5],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.htilde[6],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_A.Tvol[1],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_A.Tvol[2],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_A.Tvol[3],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_A.Tvol[4],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_A.Tvol[5],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_A.Tvol[6],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.htilde[1],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.htilde[2],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.htilde[3],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.htilde[4],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.htilde[5],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.htilde[6],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_B.Tvol[1],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_B.Tvol[2],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_B.Tvol[3],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_B.Tvol[4],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_B.Tvol[5],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_B.Tvol[6],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.htilde[1],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.htilde[2],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.htilde[3],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.htilde[4],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.htilde[5],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.htilde[6],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_A.Tvol[1],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_A.Tvol[2],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_A.Tvol[3],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_A.Tvol[4],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_A.Tvol[5],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_A.Tvol[6],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.htilde[1],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.htilde[2],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.htilde[3],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.htilde[4],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.htilde[5],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.htilde[6],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_B.Tvol[1],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_B.Tvol[2],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_B.Tvol[3],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_B.Tvol[4],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_B.Tvol[5],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_B.Tvol[6],hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.htilde[1],hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.htilde[2],hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.htilde[3],hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.htilde[4],hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.htilde[5],hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.htilde[6],hRSG.HeatExchangersGroup.Ec2_HP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Ec2_HP.metalTube.Tvol[1],hRSG.HeatExchangersGroup.Ec2_HP.metalTube.Tvol[2],hRSG.HeatExchangersGroup.Ec2_HP.metalTube.Tvol[3],hRSG.HeatExchangersGroup.Ec2_HP.metalTube.Tvol[4],hRSG.HeatExchangersGroup.Ec2_HP.metalTube.Tvol[5],hRSG.HeatExchangersGroup.Ec2_HP.metalTube.Tvol[6],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.htilde[1],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.htilde[2],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.htilde[3],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.htilde[4],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.htilde[5],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.htilde[6],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_A.Tvol[1],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_A.Tvol[2],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_A.Tvol[3],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_A.Tvol[4],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_A.Tvol[5],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_A.Tvol[6],hRSG.HeatExchangersGroup.Ec1HP_EcIP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.htilde[1],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.htilde[2],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.htilde[3],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.htilde[4],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.htilde[5],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.htilde[6],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_B.Tvol[1],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_B.Tvol[2],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_B.Tvol[3],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_B.Tvol[4],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_B.Tvol[5],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_B.Tvol[6],hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.htilde[1],hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.htilde[2],hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.htilde[3],hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.htilde[4],hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.htilde[5],hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.htilde[6],hRSG.HeatExchangersGroup.Ec_LP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Ec_LP.gasFlow.Ttilde[2],hRSG.HeatExchangersGroup.Ec_LP.gasFlow.Xtilde[1,1],hRSG.HeatExchangersGroup.Ec_LP.gasFlow.Xtilde[1,2],hRSG.HeatExchangersGroup.Ec_LP.gasFlow.Xtilde[1,3],hRSG.HeatExchangersGroup.Ec_LP.gasFlow.Xtilde[1,4],hRSG.HeatExchangersGroup.Ec_LP.gasFlow.Xtilde[1,5],hRSG.HeatExchangersGroup.Ec_LP.metalTube.Tvol[1],hRSG.HeatExchangersGroup.Ec_LP.metalTube.Tvol[2],hRSG.HeatExchangersGroup.Ec_LP.metalTube.Tvol[3],hRSG.HeatExchangersGroup.Ec_LP.metalTube.Tvol[4],hRSG.HeatExchangersGroup.Ec_LP.metalTube.Tvol[5],hRSG.HeatExchangersGroup.Ec_LP.metalTube.Tvol[6],hRSG.HeatExchangersGroup.Ev_LP.fluidFlow.htilde[1],hRSG.HeatExchangersGroup.Ev_LP.fluidFlow.htilde[2],hRSG.HeatExchangersGroup.Ev_LP.fluidFlow.htilde[3],hRSG.HeatExchangersGroup.Ev_LP.metalTube.Tvol[1],hRSG.HeatExchangersGroup.Ev_LP.metalTube.Tvol[2],hRSG.HeatExchangersGroup.Ev_LP.metalTube.Tvol[3],hRSG.HeatExchangersGroup.Ev_LP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Ev_LP.gasFlow.Ttilde[2],hRSG.HeatExchangersGroup.Ev_IP.fluidFlow.htilde[1],hRSG.HeatExchangersGroup.Ev_IP.fluidFlow.htilde[2],hRSG.HeatExchangersGroup.Ev_IP.fluidFlow.htilde[3],hRSG.HeatExchangersGroup.Ev_IP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Ev_IP.gasFlow.Ttilde[2],hRSG.HeatExchangersGroup.Ev_IP.metalTube.Tvol[1],hRSG.HeatExchangersGroup.Ev_IP.metalTube.Tvol[2],hRSG.HeatExchangersGroup.Ev_IP.metalTube.Tvol[3],hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.p,hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.htilde[1],hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.htilde[2],hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.htilde[3],hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.htilde[4],hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.htilde[5],hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.htilde[6],hRSG.HeatExchangersGroup.Sh_LP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Sh_LP.metalTube.Tvol[1],hRSG.HeatExchangersGroup.Sh_LP.metalTube.Tvol[2],hRSG.HeatExchangersGroup.Sh_LP.metalTube.Tvol[3],hRSG.HeatExchangersGroup.Sh_LP.metalTube.Tvol[4],hRSG.HeatExchangersGroup.Sh_LP.metalTube.Tvol[5],hRSG.HeatExchangersGroup.Sh_LP.metalTube.Tvol[6],hRSG.HeatExchangersGroup.Ev_HP.fluidFlow.htilde[1],hRSG.HeatExchangersGroup.Ev_HP.fluidFlow.htilde[2],hRSG.HeatExchangersGroup.Ev_HP.fluidFlow.htilde[3],hRSG.HeatExchangersGroup.Ev_HP.metalTube.Tvol[1],hRSG.HeatExchangersGroup.Ev_HP.metalTube.Tvol[2],hRSG.HeatExchangersGroup.Ev_HP.metalTube.Tvol[3],hRSG.HeatExchangersGroup.Ev_HP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Ev_HP.gasFlow.Ttilde[2],hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.htilde[1],hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.htilde[2],hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.htilde[3],hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.htilde[4],hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.htilde[5],hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.htilde[6],hRSG.HeatExchangersGroup.Sh_IP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Sh_IP.metalTube.Tvol[1],hRSG.HeatExchangersGroup.Sh_IP.metalTube.Tvol[2],hRSG.HeatExchangersGroup.Sh_IP.metalTube.Tvol[3],hRSG.HeatExchangersGroup.Sh_IP.metalTube.Tvol[4],hRSG.HeatExchangersGroup.Sh_IP.metalTube.Tvol[5],hRSG.HeatExchangersGroup.Sh_IP.metalTube.Tvol[6],hRSG.HeatExchangersGroup.mixIP.p,hRSG.HeatExchangersGroup.mixIP.h,levelsControl.Level_HP.I,levelsControl.Level_IP.I,levelsControl.Level_LP.I,singleShaft.network.delta,singleShaft.damper.phi_rel,singleShaft.damper.w_rel,sTG_3LRh.steamTurbines.mixLP.h,sTG_3LRh.controlledCondeser.pID.I,sTG_3LRh.controlledCondeser.condenserIdeal_tap.Vl) * Number of discrete variables: 284 ($cse1.phase,$cse1.region,$cse5.phase,$cse5.region,$cse9.phase,$cse9.region,$cse14.phase,$cse14.region,$cse15.phase,$cse15.region,$cse17.phase,$cse17.region,$cse19.phase,$cse19.region,$cse21.phase,$cse21.region,$cse23.phase,$cse23.region,$cse25.phase,$cse25.region,$cse28.phase,$cse28.region,$cse37.phase,$cse37.region,$cse38.phase,$cse38.region,$cse39.phase,$cse39.region,$cse40.phase,$cse40.region,$cse41.phase,$cse41.region,$cse42.phase,$cse42.region,$cse43.phase,$cse43.region,$cse44.phase,$cse44.region,$cse45.phase,$cse45.region,$cse46.phase,$cse46.region,$cse47.phase,$cse47.region,$cse48.phase,$cse48.region,$cse49.phase,$cse49.region,$cse50.phase,$cse50.region,$cse59.phase,$cse59.region,$cse60.phase,$cse60.region,$cse61.phase,$cse61.region,$cse62.phase,$cse62.region,$cse63.phase,$cse63.region,$cse64.phase,$cse64.region,$cse65.phase,$cse65.region,$cse66.phase,$cse66.region,$cse67.region3boundary,$cse68.region3boundary,$cse78.phase,$cse78.region,$cse79.phase,$cse79.region,$cse80.phase,$cse80.region,$cse81.phase,$cse81.region,$cse82.phase,$cse82.region,$cse83.phase,$cse83.region,$cse84.phase,$cse84.region,$cse93.phase,$cse93.region,$cse94.phase,$cse94.region,$cse95.phase,$cse95.region,$cse96.phase,$cse96.region,$cse97.phase,$cse97.region,$cse98.phase,$cse98.region,$cse99.phase,$cse99.region,$cse100.phase,$cse100.region,$cse109.phase,$cse109.region,$cse110.phase,$cse110.region,$cse111.phase,$cse111.region,$cse112.phase,$cse112.region,$cse113.phase,$cse113.region,$cse114.phase,$cse114.region,$cse115.phase,$cse115.region,$cse116.phase,$cse116.region,$cse117.region3boundary,$cse118.region3boundary,$cse128.phase,$cse128.region,$cse129.phase,$cse129.region,$cse130.phase,$cse130.region,$cse131.phase,$cse131.region,$cse132.phase,$cse132.region,$cse133.phase,$cse133.region,$cse134.phase,$cse134.region,$cse135.phase,$cse135.region,$cse136.phase,$cse136.region,$cse137.phase,$cse137.region,$cse138.phase,$cse138.region,$cse139.phase,$cse139.region,$cse140.phase,$cse140.region,$cse141.phase,$cse141.region,$cse143.phase,$cse143.region,$cse144.phase,$cse144.region,$cse145.phase,$cse145.region,$cse146.phase,$cse146.region,$cse147.phase,$cse147.region,$cse148.phase,$cse148.region,$cse149.phase,$cse149.region,$cse150.phase,$cse150.region,$cse151.phase,$cse151.region,$cse152.phase,$cse152.region,$cse153.phase,$cse153.region,$cse154.phase,$cse154.region,$cse155.phase,$cse155.region,$cse156.phase,$cse156.region,$cse165.phase,$cse165.region,$cse166.phase,$cse166.region,$cse167.phase,$cse167.region,$cse168.phase,$cse168.region,$cse169.phase,$cse169.region,$cse170.phase,$cse170.region,$cse171.phase,$cse171.region,$cse180.phase,$cse180.region,$cse181.phase,$cse181.region,$cse182.phase,$cse182.region,$cse183.phase,$cse183.region,$cse184.phase,$cse184.region,$cse185.phase,$cse185.region,$cse186.phase,$cse186.region,$cse187.phase,$cse187.region,$cse188.phase,$cse188.region,$cse189.phase,$cse189.region,$cse190.phase,$cse190.region,$cse191.phase,$cse191.region,$cse192.phase,$cse192.region,$cse193.phase,$cse193.region,$cse195.phase,$cse195.region,$cse196.phase,$cse196.region,$cse197.phase,$cse197.region,$cse198.phase,$cse198.region,$cse199.phase,$cse199.region,$cse200.phase,$cse200.region,$cse209.phase,$cse209.region,$cse210.phase,$cse210.region,$cse211.phase,$cse211.region,$cse212.phase,$cse212.region,$cse213.phase,$cse213.region,$cse214.phase,$cse214.region,$cse216.phase,$cse216.region,$cse217.phase,$cse217.region,$cse218.phase,$cse218.region,$cse219.phase,$cse219.region,$cse220.phase,$cse220.region,$cse221.phase,$cse221.region,$cse222.phase,$cse222.region,$cse231.phase,$cse231.region,$cse232.phase,$cse232.region,$cse233.phase,$cse233.region,$cse234.phase,$cse234.region,$cse235.phase,$cse235.region,$cse236.phase,$cse236.region,$cse237.phase,$cse237.region,$cse238.region3boundary,$cse239.region3boundary,$cse240.phase,$cse240.region,$cse241.phase,$cse241.region,$cse243.region3boundary,$cse244.region3boundary,$cse245.phase,$cse245.region,$cse246.phase,$cse246.region,$cse248.region3boundary,$cse249.region3boundary,$cse250.phase,$cse250.region,$cse251.phase,$cse251.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (2904): * Single equations (assignments): 2708 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 146 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 7 * Torn equation systems: 43 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 7 {1,1,1,1,1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 27 {(1,100.0%) 3,(2,100.0%) 3,(2,100.0%) 3,(1,100.0%) 3,(1,100.0%) 3,(1,100.0%) 3,(1,100.0%) 2,(1,100.0%) 4,(2,100.0%) 3,(1,100.0%) 2,(2,100.0%) 3,(1,100.0%) 2,(2,100.0%) 3,(1,100.0%) 2,(1,100.0%) 4,(2,100.0%) 3,(1,100.0%) 2,(1,100.0%) 4,(1,100.0%) 2,(1,100.0%) 4,(1,100.0%) 2,(2,100.0%) 3,(2,100.0%) 3,(1,100.0%) 2,(1,100.0%) 4,(1,100.0%) 2,(2,100.0%) 3} * Non-linear torn systems: 16 {21 69,1 10,35 134,34 129,7 1,7 1,7 1,7 1,7 1,7 1,7 1,7 1,7 1,1 10,1 10,1 1} ThermoPower.PowerPlants.Simulators.SteamPlant_Sim2.err [ThermoPower 3.1/PowerPlants.mo:3950:70-3951:22:writable] Error: Variable q_nom not found in scope ThermoPower.PowerPlants.HRSG.Components. [ThermoPower 3.1/PowerPlants.mo:3960:21-3960:69:writable] Error: Cyclically dependent constants or parameters found in scope : {q_nom}, {head_nom} (ignore with -d=ignoreCycles). Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 7839 * Number of variables: 7839 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: The given system is mixed-determined. [index = 1] Warning: Assuming fixed start value for the following 1 variables: sTG_3LRh.controlledCondeser.condenserIdeal_tap.Vl:VARIABLE(start = sTG_3LRh.controlledCondeser.condenserIdeal_tap.Vlstart unit = "m3" stateSelect=StateSelect.prefer ) "Liquid volume" type: Real Warning: The initial conditions are over specified. The following 23 initial equations are redundant, so they are removed from the initialization sytem: $DER.hRSG.drums.IPd.p = 0.0 $DER.hRSG.HeatExchangersGroup.Ev_IP.fluidFlow.p = 0.0 $DER.hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.p = 0.0 $DER.hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.p = 0.0 $DER.hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.p = 0.0 -- $DER.hRSG.HeatExchangersGroup.Sh_IP.gasFlow.p = 0.0 $DER.hRSG.HeatExchangersGroup.Ev_HP.gasFlow.p = 0.0 $DER.hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.gasFlow.p = 0.0 $DER.hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.gasFlow.p = 0.0 $DER.hRSG.HeatExchangersGroup.Ec_LP.gasFlow.p = 0.0. Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.heatTransfer.w_wnom:VARIABLE(unit = "1" ) "Ratio between actual and nominal flow rate" type: Real hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.heatTransfer.w_wnom:VARIABLE(unit = "1" ) "Ratio between actual and nominal flow rate" type: Real hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.heatTransfer.w_wnom:VARIABLE(unit = "1" ) "Ratio between actual and nominal flow rate" type: Real hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.heatTransfer.w_wnom:VARIABLE(unit = "1" ) "Ratio between actual and nominal flow rate" type: Real hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.heatTransfer.w_wnom:VARIABLE(unit = "1" ) "Ratio between actual and nominal flow rate" type: Real hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.heatTransfer.w_wnom:VARIABLE(unit = "1" ) "Ratio between actual and nominal flow rate" type: Real hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.heatTransfer.w_wnom:VARIABLE(unit = "1" ) "Ratio between actual and nominal flow rate" type: Real Warning: Iteration variables with default zero start attribute in equation system w/o analytic Jacobian: $DER.hRSG.HeatExchangersGroup.Ec1HP_EcIP.gasFlow.gas[1].T:DUMMY_DER(fixed = false ) "Temperature of medium" type: Real [3] Warning: Iteration variables with default zero start attribute in equation system w/o analytic Jacobian: $DER.hRSG.HeatExchangersGroup.Ev_IP.gasFlow.gas[1].T:DUMMY_DER(fixed = false ) "Temperature of medium" type: Real [4] Warning: Iteration variables with default zero start attribute in equation system w/o analytic Jacobian: $DER.hRSG.HeatExchangersGroup.Ec2_HP.gasFlow.gas[1].T:DUMMY_DER(fixed = false ) "Temperature of medium" type: Real [3] Warning: Iteration variables with default zero start attribute in equation system w/o analytic Jacobian: $DER.hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.gasFlow.gas[1].T:DUMMY_DER(fixed = false ) "Temperature of medium" type: Real [3] Warning: Iteration variables with default zero start attribute in equation system w/o analytic Jacobian: $DER.hRSG.HeatExchangersGroup.Ev_HP.gasFlow.gas[1].T:DUMMY_DER(fixed = false ) "Temperature of medium" type: Real [4] Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 403 * Number of states: 0 () * Number of discrete variables: 101 (sTG_3LRh.totalFeedPump.feedWaterPump.int_Np,sTG_3LRh.totalFeedPump.feedWaterPump.inletFluidState.phase,sTG_3LRh.steamTurbines.valveLP.fluidState.phase,sTG_3LRh.steamTurbines.valveIP.fluidState.phase,sTG_3LRh.steamTurbines.valveHP.fluidState.phase,sTG_3LRh.steamTurbines.mixLP.fluidState.phase,sTG_3LRh.steamTurbines.ST_LP.steamState_in.phase,sTG_3LRh.steamTurbines.ST_LP.steamState_iso.phase,sTG_3LRh.steamTurbines.ST_IP.steamState_in.phase,sTG_3LRh.steamTurbines.ST_IP.steamState_iso.phase,sTG_3LRh.steamTurbines.ST_HP.steamState_in.phase,sTG_3LRh.steamTurbines.ST_HP.steamState_iso.phase,hRSG.HeatExchangersGroup.mixIP.fluidState.phase,hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Ev_HP.fluidFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Ev_HP.fluidFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Ev_HP.fluidFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Ev_HP.fluidFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Ev_IP.fluidFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Ev_IP.fluidFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Ev_IP.fluidFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Ev_IP.fluidFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Ev_LP.fluidFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Ev_LP.fluidFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Ev_LP.fluidFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Ev_LP.fluidFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.fluidState[1].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.fluidState[7].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.fluidState[6].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.fluidState[5].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.fluidState[4].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.fluidState[3].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.fluidState[2].phase,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.fluidState[1].phase,hRSG.drums.LPd.vapourState.phase,hRSG.drums.LPd.liquidState.phase,hRSG.drums.IPd.vapourState.phase,hRSG.drums.IPd.liquidState.phase,hRSG.drums.HPd.vapourState.phase,hRSG.drums.HPd.liquidState.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (1853): * Single equations (assignments): 1820 * Array equations: 18 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 8 * Torn equation systems: 7 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 8 {1,1,1,1,1,1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(1,100.0%) 3} * Non-linear torn systems: 6 {7 56,1 1,1 1,1 1,171 1810,1 1} Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 76 * Number of states: 235 ($STATESET9.x[6],$STATESET9.x[5],$STATESET9.x[4],$STATESET9.x[3],$STATESET9.x[2],$STATESET9.x[1],$STATESET8.x[6],$STATESET8.x[5],$STATESET8.x[4],$STATESET8.x[3],$STATESET8.x[2],$STATESET8.x[1],$STATESET7.x[6],$STATESET7.x[5],$STATESET7.x[4],$STATESET7.x[3],$STATESET7.x[2],$STATESET7.x[1],$STATESET6.x[6],$STATESET6.x[5],$STATESET6.x[4],$STATESET6.x[3],$STATESET6.x[2],$STATESET6.x[1],$STATESET5.x[6],$STATESET5.x[5],$STATESET5.x[4],$STATESET5.x[3],$STATESET5.x[2],$STATESET5.x[1],$STATESET4.x[6],$STATESET4.x[5],$STATESET4.x[4],$STATESET4.x[3],$STATESET4.x[2],$STATESET4.x[1],$STATESET3.x[6],$STATESET3.x[5],$STATESET3.x[4],$STATESET3.x[3],$STATESET3.x[2],$STATESET3.x[1],$STATESET2.x[6],$STATESET2.x[5],$STATESET2.x[4],$STATESET2.x[3],$STATESET2.x[2],$STATESET2.x[1],$STATESET1.x[6],$STATESET1.x[5],$STATESET1.x[4],$STATESET1.x[3],$STATESET1.x[2],$STATESET1.x[1],hRSG.drums.HPd.p,hRSG.drums.HPd.hl,hRSG.drums.HPd.hv,hRSG.drums.HPd.y,hRSG.drums.IPd.hl,hRSG.drums.IPd.hv,hRSG.drums.IPd.y,hRSG.drums.LPd.hl,hRSG.drums.LPd.hv,hRSG.drums.LPd.y,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.htilde[1],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.htilde[2],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.htilde[3],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.htilde[4],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.htilde[5],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidAFlow.htilde[6],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_A.Tvol[1],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_A.Tvol[2],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_A.Tvol[3],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_A.Tvol[4],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_A.Tvol[5],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_A.Tvol[6],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.p,hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.htilde[1],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.htilde[2],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.htilde[3],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.htilde[4],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.htilde[5],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.fluidBFlow.htilde[6],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_B.Tvol[1],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_B.Tvol[2],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_B.Tvol[3],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_B.Tvol[4],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_B.Tvol[5],hRSG.HeatExchangersGroup.Sh1HP_Rh1IP.metalTube_B.Tvol[6],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.htilde[1],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.htilde[2],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.htilde[3],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.htilde[4],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.htilde[5],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.htilde[6],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_A.Tvol[1],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_A.Tvol[2],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_A.Tvol[3],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_A.Tvol[4],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_A.Tvol[5],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_A.Tvol[6],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.p,hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.htilde[1],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.htilde[2],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.htilde[3],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.htilde[4],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.htilde[5],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidBFlow.htilde[6],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_B.Tvol[1],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_B.Tvol[2],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_B.Tvol[3],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_B.Tvol[4],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_B.Tvol[5],hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.metalTube_B.Tvol[6],hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.htilde[1],hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.htilde[2],hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.htilde[3],hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.htilde[4],hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.htilde[5],hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.htilde[6],hRSG.HeatExchangersGroup.Ec2_HP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Ec2_HP.metalTube.Tvol[1],hRSG.HeatExchangersGroup.Ec2_HP.metalTube.Tvol[2],hRSG.HeatExchangersGroup.Ec2_HP.metalTube.Tvol[3],hRSG.HeatExchangersGroup.Ec2_HP.metalTube.Tvol[4],hRSG.HeatExchangersGroup.Ec2_HP.metalTube.Tvol[5],hRSG.HeatExchangersGroup.Ec2_HP.metalTube.Tvol[6],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.htilde[1],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.htilde[2],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.htilde[3],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.htilde[4],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.htilde[5],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidAFlow.htilde[6],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_A.Tvol[1],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_A.Tvol[2],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_A.Tvol[3],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_A.Tvol[4],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_A.Tvol[5],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_A.Tvol[6],hRSG.HeatExchangersGroup.Ec1HP_EcIP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.htilde[1],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.htilde[2],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.htilde[3],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.htilde[4],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.htilde[5],hRSG.HeatExchangersGroup.Ec1HP_EcIP.fluidBFlow.htilde[6],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_B.Tvol[1],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_B.Tvol[2],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_B.Tvol[3],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_B.Tvol[4],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_B.Tvol[5],hRSG.HeatExchangersGroup.Ec1HP_EcIP.metalTube_B.Tvol[6],hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.htilde[1],hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.htilde[2],hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.htilde[3],hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.htilde[4],hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.htilde[5],hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.htilde[6],hRSG.HeatExchangersGroup.Ec_LP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Ec_LP.gasFlow.Ttilde[2],hRSG.HeatExchangersGroup.Ec_LP.gasFlow.Xtilde[1,1],hRSG.HeatExchangersGroup.Ec_LP.gasFlow.Xtilde[1,2],hRSG.HeatExchangersGroup.Ec_LP.gasFlow.Xtilde[1,3],hRSG.HeatExchangersGroup.Ec_LP.gasFlow.Xtilde[1,4],hRSG.HeatExchangersGroup.Ec_LP.gasFlow.Xtilde[1,5],hRSG.HeatExchangersGroup.Ec_LP.metalTube.Tvol[1],hRSG.HeatExchangersGroup.Ec_LP.metalTube.Tvol[2],hRSG.HeatExchangersGroup.Ec_LP.metalTube.Tvol[3],hRSG.HeatExchangersGroup.Ec_LP.metalTube.Tvol[4],hRSG.HeatExchangersGroup.Ec_LP.metalTube.Tvol[5],hRSG.HeatExchangersGroup.Ec_LP.metalTube.Tvol[6],hRSG.HeatExchangersGroup.Ev_LP.fluidFlow.htilde[1],hRSG.HeatExchangersGroup.Ev_LP.fluidFlow.htilde[2],hRSG.HeatExchangersGroup.Ev_LP.fluidFlow.htilde[3],hRSG.HeatExchangersGroup.Ev_LP.metalTube.Tvol[1],hRSG.HeatExchangersGroup.Ev_LP.metalTube.Tvol[2],hRSG.HeatExchangersGroup.Ev_LP.metalTube.Tvol[3],hRSG.HeatExchangersGroup.Ev_LP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Ev_LP.gasFlow.Ttilde[2],hRSG.HeatExchangersGroup.Ev_IP.fluidFlow.htilde[1],hRSG.HeatExchangersGroup.Ev_IP.fluidFlow.htilde[2],hRSG.HeatExchangersGroup.Ev_IP.fluidFlow.htilde[3],hRSG.HeatExchangersGroup.Ev_IP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Ev_IP.gasFlow.Ttilde[2],hRSG.HeatExchangersGroup.Ev_IP.metalTube.Tvol[1],hRSG.HeatExchangersGroup.Ev_IP.metalTube.Tvol[2],hRSG.HeatExchangersGroup.Ev_IP.metalTube.Tvol[3],hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.p,hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.htilde[1],hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.htilde[2],hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.htilde[3],hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.htilde[4],hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.htilde[5],hRSG.HeatExchangersGroup.Sh_LP.fluidFlow.htilde[6],hRSG.HeatExchangersGroup.Sh_LP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Sh_LP.metalTube.Tvol[1],hRSG.HeatExchangersGroup.Sh_LP.metalTube.Tvol[2],hRSG.HeatExchangersGroup.Sh_LP.metalTube.Tvol[3],hRSG.HeatExchangersGroup.Sh_LP.metalTube.Tvol[4],hRSG.HeatExchangersGroup.Sh_LP.metalTube.Tvol[5],hRSG.HeatExchangersGroup.Sh_LP.metalTube.Tvol[6],hRSG.HeatExchangersGroup.Ev_HP.fluidFlow.htilde[1],hRSG.HeatExchangersGroup.Ev_HP.fluidFlow.htilde[2],hRSG.HeatExchangersGroup.Ev_HP.fluidFlow.htilde[3],hRSG.HeatExchangersGroup.Ev_HP.metalTube.Tvol[1],hRSG.HeatExchangersGroup.Ev_HP.metalTube.Tvol[2],hRSG.HeatExchangersGroup.Ev_HP.metalTube.Tvol[3],hRSG.HeatExchangersGroup.Ev_HP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Ev_HP.gasFlow.Ttilde[2],hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.htilde[1],hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.htilde[2],hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.htilde[3],hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.htilde[4],hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.htilde[5],hRSG.HeatExchangersGroup.Sh_IP.fluidFlow.htilde[6],hRSG.HeatExchangersGroup.Sh_IP.gasFlow.Ttilde[1],hRSG.HeatExchangersGroup.Sh_IP.metalTube.Tvol[1],hRSG.HeatExchangersGroup.Sh_IP.metalTube.Tvol[2],hRSG.HeatExchangersGroup.Sh_IP.metalTube.Tvol[3],hRSG.HeatExchangersGroup.Sh_IP.metalTube.Tvol[4],hRSG.HeatExchangersGroup.Sh_IP.metalTube.Tvol[5],hRSG.HeatExchangersGroup.Sh_IP.metalTube.Tvol[6],hRSG.HeatExchangersGroup.mixIP.p,hRSG.HeatExchangersGroup.mixIP.h,sTG_3LRh.steamTurbines.mixLP.h,sTG_3LRh.controlledCondeser.pID.I,sTG_3LRh.controlledCondeser.condenserIdeal_tap.Vl,levelsControl.Level_HP.I,levelsControl.Level_IP.I,levelsControl.Level_LP.I,singleShaft.network.delta,singleShaft.damper.phi_rel,singleShaft.damper.w_rel) * Number of discrete variables: 284 ($cse1.phase,$cse1.region,$cse5.phase,$cse5.region,$cse9.phase,$cse9.region,$cse14.phase,$cse14.region,$cse15.phase,$cse15.region,$cse17.phase,$cse17.region,$cse19.phase,$cse19.region,$cse21.phase,$cse21.region,$cse23.phase,$cse23.region,$cse25.phase,$cse25.region,$cse28.phase,$cse28.region,$cse37.phase,$cse37.region,$cse38.phase,$cse38.region,$cse39.phase,$cse39.region,$cse40.phase,$cse40.region,$cse41.phase,$cse41.region,$cse42.phase,$cse42.region,$cse43.phase,$cse43.region,$cse44.phase,$cse44.region,$cse45.phase,$cse45.region,$cse46.phase,$cse46.region,$cse47.phase,$cse47.region,$cse48.phase,$cse48.region,$cse49.phase,$cse49.region,$cse50.phase,$cse50.region,$cse59.phase,$cse59.region,$cse60.phase,$cse60.region,$cse61.phase,$cse61.region,$cse62.phase,$cse62.region,$cse63.phase,$cse63.region,$cse64.phase,$cse64.region,$cse65.phase,$cse65.region,$cse66.phase,$cse66.region,$cse67.region3boundary,$cse68.region3boundary,$cse78.phase,$cse78.region,$cse79.phase,$cse79.region,$cse80.phase,$cse80.region,$cse81.phase,$cse81.region,$cse82.phase,$cse82.region,$cse83.phase,$cse83.region,$cse84.phase,$cse84.region,$cse93.phase,$cse93.region,$cse94.phase,$cse94.region,$cse95.phase,$cse95.region,$cse96.phase,$cse96.region,$cse97.phase,$cse97.region,$cse98.phase,$cse98.region,$cse99.phase,$cse99.region,$cse100.phase,$cse100.region,$cse109.phase,$cse109.region,$cse110.phase,$cse110.region,$cse111.phase,$cse111.region,$cse112.phase,$cse112.region,$cse113.phase,$cse113.region,$cse114.phase,$cse114.region,$cse115.phase,$cse115.region,$cse116.phase,$cse116.region,$cse117.region3boundary,$cse118.region3boundary,$cse128.phase,$cse128.region,$cse129.phase,$cse129.region,$cse130.phase,$cse130.region,$cse131.phase,$cse131.region,$cse132.phase,$cse132.region,$cse133.phase,$cse133.region,$cse134.phase,$cse134.region,$cse135.phase,$cse135.region,$cse136.phase,$cse136.region,$cse137.phase,$cse137.region,$cse138.phase,$cse138.region,$cse139.phase,$cse139.region,$cse140.phase,$cse140.region,$cse141.phase,$cse141.region,$cse143.phase,$cse143.region,$cse144.phase,$cse144.region,$cse145.phase,$cse145.region,$cse146.phase,$cse146.region,$cse147.phase,$cse147.region,$cse148.phase,$cse148.region,$cse149.phase,$cse149.region,$cse150.phase,$cse150.region,$cse151.phase,$cse151.region,$cse152.phase,$cse152.region,$cse153.phase,$cse153.region,$cse154.phase,$cse154.region,$cse155.phase,$cse155.region,$cse156.phase,$cse156.region,$cse165.phase,$cse165.region,$cse166.phase,$cse166.region,$cse167.phase,$cse167.region,$cse168.phase,$cse168.region,$cse169.phase,$cse169.region,$cse170.phase,$cse170.region,$cse171.phase,$cse171.region,$cse180.phase,$cse180.region,$cse181.phase,$cse181.region,$cse182.phase,$cse182.region,$cse183.phase,$cse183.region,$cse184.phase,$cse184.region,$cse185.phase,$cse185.region,$cse186.phase,$cse186.region,$cse187.phase,$cse187.region,$cse188.phase,$cse188.region,$cse189.phase,$cse189.region,$cse190.phase,$cse190.region,$cse191.phase,$cse191.region,$cse192.phase,$cse192.region,$cse193.phase,$cse193.region,$cse195.phase,$cse195.region,$cse196.phase,$cse196.region,$cse197.phase,$cse197.region,$cse198.phase,$cse198.region,$cse199.phase,$cse199.region,$cse200.phase,$cse200.region,$cse205.phase,$cse205.region,$cse206.phase,$cse206.region,$cse207.phase,$cse207.region,$cse208.phase,$cse208.region,$cse209.phase,$cse209.region,$cse210.phase,$cse210.region,$cse212.phase,$cse212.region,$cse213.phase,$cse213.region,$cse214.phase,$cse214.region,$cse215.phase,$cse215.region,$cse216.phase,$cse216.region,$cse217.phase,$cse217.region,$cse218.phase,$cse218.region,$cse228.phase,$cse228.region,$cse229.phase,$cse229.region,$cse230.phase,$cse230.region,$cse231.phase,$cse231.region,$cse232.phase,$cse232.region,$cse233.phase,$cse233.region,$cse234.phase,$cse234.region,$cse235.region3boundary,$cse236.region3boundary,$cse237.phase,$cse237.region,$cse238.phase,$cse238.region,$cse240.region3boundary,$cse241.region3boundary,$cse242.phase,$cse242.region,$cse243.phase,$cse243.region,$cse245.region3boundary,$cse246.region3boundary,$cse247.phase,$cse247.region,$cse248.phase,$cse248.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (2945): * Single equations (assignments): 2746 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 146 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 8 * Torn equation systems: 45 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 8 {1,1,1,1,1,1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 29 {(1,100.0%) 3,(7,69.4%) 12,(7,69.4%) 12,(2,100.0%) 3,(2,100.0%) 3,(1,100.0%) 3,(1,100.0%) 3,(1,100.0%) 3,(1,100.0%) 2,(2,100.0%) 3,(1,100.0%) 4,(1,100.0%) 2,(1,100.0%) 4,(1,100.0%) 2,(1,100.0%) 4,(1,100.0%) 2,(1,100.0%) 4,(2,100.0%) 3,(1,100.0%) 2,(1,100.0%) 4,(1,100.0%) 2,(1,100.0%) 4,(1,100.0%) 2,(1,100.0%) 4,(1,100.0%) 4,(1,100.0%) 2,(1,100.0%) 4,(1,100.0%) 2,(2,100.0%) 3} * Non-linear torn systems: 16 {21 69,1 10,1 10,21 68,34 129,7 1,7 1,7 1,7 1,7 1,7 1,7 1,7 1,7 1,1 10,1 1} ThermoPower.PowerPlants.SteamTurbineGroup.Tests.TestST3LRh_base.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 224 * Number of variables: 224 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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. Warning: Assuming fixed start value for the following 2 variables: constantSpeed.phi:VARIABLE(unit = "rad" ) "Angle of flange with respect to support (= flange.phi - support.phi)" type: Real steamTurbines.mixLP.h:VARIABLE(min = max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, -10000000000.0)))))))))) max = min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, 10000000000.0)))))))))) start = steamTurbines.mixLP.hstart unit = "J/kg" nominal = 500000.0 stateSelect=StateSelect.prefer ) "Fluid specific enthalpy" type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 33 * Number of states: 0 () * Number of discrete variables: 7 (steamTurbines.mixLP.fluidState.phase,steamTurbines.ST_LP.steamState_in.phase,steamTurbines.ST_LP.steamState_iso.phase,steamTurbines.ST_IP.steamState_in.phase,steamTurbines.ST_IP.steamState_iso.phase,steamTurbines.ST_HP.steamState_in.phase,steamTurbines.ST_HP.steamState_iso.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (63): * Single equations (assignments): 62 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {1 6} Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 6 * Number of states: 2 (steamTurbines.mixLP.h,constantSpeed.phi) * Number of discrete variables: 4 ($cse3.phase,$cse3.region,$cse4.phase,$cse4.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (26): * Single equations (assignments): 23 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 2 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {1 4} ThermoPower.PowerPlants.SteamTurbineGroup.Tests.TestST3LRh_bypass.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 385 * Number of variables: 385 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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. Warning: Assuming fixed start value for the following 2 variables: constantSpeed.phi:VARIABLE(unit = "rad" ) "Angle of flange with respect to support (= flange.phi - support.phi)" type: Real steamTurbines.mixLP.h:VARIABLE(min = max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, -10000000000.0))))))))))))))) max = min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, 10000000000.0))))))))))))))) start = steamTurbines.mixLP.hstart unit = "J/kg" nominal = 500000.0 stateSelect=StateSelect.prefer ) "Fluid specific enthalpy" type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 67 * Number of states: 0 () * Number of discrete variables: 13 (steamTurbines.ST_LP.steamState_in.phase,steamTurbines.ST_LP.steamState_iso.phase,steamTurbines.ST_IP.steamState_in.phase,steamTurbines.ST_IP.steamState_iso.phase,steamTurbines.ST_HP.steamState_in.phase,steamTurbines.ST_HP.steamState_iso.phase,steamTurbines.byPassLP.fluidState.phase,steamTurbines.byPassIP.fluidState.phase,steamTurbines.byPassHP.fluidState.phase,steamTurbines.valveLP.fluidState.phase,steamTurbines.valveIP.fluidState.phase,steamTurbines.valveHP.fluidState.phase,steamTurbines.mixLP.fluidState.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (137): * Single equations (assignments): 133 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 4 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 4 {1 7,1 6,1 7,1 7} Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 10 * Number of states: 2 (steamTurbines.mixLP.h,constantSpeed.phi) * Number of discrete variables: 14 ($cse1.phase,$cse1.region,$cse23.phase,$cse23.region,$cse24.phase,$cse24.region,$cse27.phase,$cse27.region,$cse28.phase,$cse28.region,$cse31.phase,$cse31.region,$cse32.phase,$cse32.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (68): * Single equations (assignments): 60 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 4 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 4 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 4 {1 4,1 10,1 10,1 10} ThermoPower.PowerPlants.SteamTurbineGroup.Tests.TestST3LRh_valve.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 266 * Number of variables: 266 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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. Warning: Assuming fixed start value for the following 2 variables: constantSpeed.phi:VARIABLE(unit = "rad" ) "Angle of flange with respect to support (= flange.phi - support.phi)" type: Real steamTurbines.mixLP.h:VARIABLE(min = max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, -10000000000.0))))))))) max = min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, 10000000000.0))))))))) start = steamTurbines.mixLP.hstart unit = "J/kg" nominal = 500000.0 stateSelect=StateSelect.prefer ) "Fluid specific enthalpy" type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 48 * Number of states: 0 () * Number of discrete variables: 10 (steamTurbines.valveLP.fluidState.phase,steamTurbines.valveIP.fluidState.phase,steamTurbines.valveHP.fluidState.phase,steamTurbines.mixLP.fluidState.phase,steamTurbines.ST_LP.steamState_in.phase,steamTurbines.ST_LP.steamState_iso.phase,steamTurbines.ST_IP.steamState_in.phase,steamTurbines.ST_IP.steamState_iso.phase,steamTurbines.ST_HP.steamState_in.phase,steamTurbines.ST_HP.steamState_iso.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (87): * Single equations (assignments): 83 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 4 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 4 {1 8,1 7,1 8,1 8} Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 2 (steamTurbines.mixLP.h,constantSpeed.phi) * Number of discrete variables: 14 ($cse3.phase,$cse3.region,$cse4.phase,$cse4.region,$cse7.phase,$cse7.region,$cse8.phase,$cse8.region,$cse11.phase,$cse11.region,$cse12.phase,$cse12.region,$cse13.phase,$cse13.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (45): * Single equations (assignments): 37 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 4 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 4 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 4 {1 5,1 11,1 11,1 11} ThermoPower.PowerPlants.SteamTurbineGroup.Tests.TestSTG_cc.err [ThermoPower 3.1/PowerPlants.mo:3950:70-3951:22:writable] Error: Variable q_nom not found in scope ThermoPower.PowerPlants.HRSG.Components. [ThermoPower 3.1/PowerPlants.mo:3960:21-3960:69:writable] Error: Cyclically dependent constants or parameters found in scope : {q_nom}, {head_nom} (ignore with -d=ignoreCycles). Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 395 * Number of variables: 395 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: The given system is mixed-determined. [index = 1] Warning: Assuming fixed start value for the following 3 variables: constantSpeed.phi:VARIABLE(unit = "rad" ) "Angle of flange with respect to support (= flange.phi - support.phi)" type: Real sTG_3LRh.controlledCondeser.condenserIdeal_tap.Vl:VARIABLE(start = sTG_3LRh.controlledCondeser.condenserIdeal_tap.Vlstart unit = "m3" stateSelect=StateSelect.prefer ) "Liquid volume" type: Real sTG_3LRh.controlledCondeser.pID.I:VARIABLE(start = sTG_3LRh.controlledCondeser.pID.CSstart / sTG_3LRh.controlledCondeser.pID.Kp ) "Integral action / Kp" type: Real Warning: The initial conditions are over specified. The following 1 initial equations are redundant, so they are removed from the initialization sytem: $DER.sTG_3LRh.steamTurbines.mixLP.p = 0.0. Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 58 * Number of states: 0 () * Number of discrete variables: 12 (sTG_3LRh.totalFeedPump.feedWaterPump.int_Np,sTG_3LRh.totalFeedPump.feedWaterPump.inletFluidState.phase,sTG_3LRh.steamTurbines.valveLP.fluidState.phase,sTG_3LRh.steamTurbines.valveIP.fluidState.phase,sTG_3LRh.steamTurbines.valveHP.fluidState.phase,sTG_3LRh.steamTurbines.mixLP.fluidState.phase,sTG_3LRh.steamTurbines.ST_LP.steamState_in.phase,sTG_3LRh.steamTurbines.ST_LP.steamState_iso.phase,sTG_3LRh.steamTurbines.ST_IP.steamState_in.phase,sTG_3LRh.steamTurbines.ST_IP.steamState_iso.phase,sTG_3LRh.steamTurbines.ST_HP.steamState_in.phase,sTG_3LRh.steamTurbines.ST_HP.steamState_iso.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (127): * Single equations (assignments): 122 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 5 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(1,100.0%) 3} * Non-linear torn systems: 4 {2 16,1 7,1 7,1 1} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 3 * Number of states: 4 (constantSpeed.phi,sTG_3LRh.steamTurbines.mixLP.h,sTG_3LRh.controlledCondeser.pID.I,sTG_3LRh.controlledCondeser.condenserIdeal_tap.Vl) * Number of discrete variables: 16 ($cse1.phase,$cse1.region,$cse9.phase,$cse9.region,$cse10.phase,$cse10.region,$cse12.phase,$cse12.region,$cse14.phase,$cse14.region,$cse16.phase,$cse16.region,$cse18.phase,$cse18.region,$cse20.phase,$cse20.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (66): * Single equations (assignments): 55 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 5 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 6 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(1,100.0%) 3} * Non-linear torn systems: 5 {1 4,1 10,1 10,1 10,1 1} ThermoPower.PowerPlants.SteamTurbineGroup.Tests.TestTurbineHPefficiency.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 90 * Number of variables: 90 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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. Warning: Assuming fixed start value for the following 1 variables: constantSpeed.phi:VARIABLE(unit = "rad" ) "Angle of flange with respect to support (= flange.phi - support.phi)" type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 18 * Number of states: 0 () * Number of discrete variables: 3 (valveHP.fluidState.phase,steamTurbineVarEta.steamState_in.phase,steamTurbineVarEta.steamState_iso.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (37): * Single equations (assignments): 36 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {1 8} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 1 (constantSpeed.phi) * Number of discrete variables: 4 ($cse3.phase,$cse3.region,$cse4.phase,$cse4.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (22): * Single equations (assignments): 20 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 1 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {1 10} ThermoPower.Test.DistributedParameterComponents.CheckFlow1DFV2phMassBalance.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 79 * Number of variables: 79 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or nominal values. It is recommended to resolve the conflicts, because otherwise the system could be hard to solve. To print the conflicting alias sets and the chosen candidates please use -d=aliasConflicts. Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 11 * Number of states: 0 () * Number of discrete variables: 4 (dew.phase,bubble.phase,fluid[2].phase,fluid[1].phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (57): * Single equations (assignments): 56 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 1 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 0 * Mixed (continuous/discrete) equation systems: 0 Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 1 (rhobar_check[1]) * Number of discrete variables: 6 ($cse1.phase,$cse1.region,$cse2.phase,$cse2.region,$cse3.region3boundary,$cse4.region3boundary) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (92): * Single equations (assignments): 87 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 5 * When equations: 0 ThermoPower.Test.DistributedParameterComponents.TestConstantHeatTransferTwoGrid_Fcoarse.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 104 * Number of variables: 104 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or nominal values. It is recommended to resolve the conflicts, because otherwise the system could be hard to solve. To print the conflicting alias sets and the chosen candidates please use -d=aliasConflicts. Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 5 * Number of states: 0 () * Number of discrete variables: 4 (fluidState[4].phase,fluidState[3].phase,fluidState[2].phase,fluidState[1].phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (27): * Single equations (assignments): 25 * Array equations: 2 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 0 * Mixed (continuous/discrete) equation systems: 0 Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 0 () * Number of discrete variables: 8 ($cse1.phase,$cse1.region,$cse2.phase,$cse2.region,$cse3.phase,$cse3.region,$cse4.phase,$cse4.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (27): * Single equations (assignments): 21 * Array equations: 2 * Algorithm blocks: 0 * Record equations: 4 * When equations: 0 ThermoPower.Test.DistributedParameterComponents.TestConstantHeatTransferTwoGrid_Wcoarse.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 137 * Number of variables: 137 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or nominal values. It is recommended to resolve the conflicts, because otherwise the system could be hard to solve. To print the conflicting alias sets and the chosen candidates please use -d=aliasConflicts. Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 8 * Number of states: 0 () * Number of discrete variables: 7 (fluidState[7].phase,fluidState[6].phase,fluidState[5].phase,fluidState[4].phase,fluidState[3].phase,fluidState[2].phase,fluidState[1].phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (39): * Single equations (assignments): 37 * Array equations: 2 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 0 * Mixed (continuous/discrete) equation systems: 0 Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 0 () * Number of discrete variables: 14 ($cse1.phase,$cse1.region,$cse2.phase,$cse2.region,$cse3.phase,$cse3.region,$cse4.phase,$cse4.region,$cse5.phase,$cse5.region,$cse6.phase,$cse6.region,$cse7.phase,$cse7.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (39): * Single equations (assignments): 30 * Array equations: 2 * Algorithm blocks: 0 * Record equations: 7 * When equations: 0 ThermoPower.Test.DistributedParameterComponents.TestFlow1D2phChen.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 455 * Number of variables: 455 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 47 * Number of states: 0 () * Number of discrete variables: 10 (hex.fluidState[8].phase,hex.fluidState[7].phase,hex.fluidState[6].phase,hex.fluidState[5].phase,hex.fluidState[4].phase,hex.fluidState[3].phase,hex.fluidState[2].phase,hex.fluidState[1].phase,hex.dew.phase,hex.bubble.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (120): * Single equations (assignments): 119 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {9 183} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 3 * Number of states: 16 (hex.p,hex.htilde[1],hex.htilde[2],hex.htilde[3],hex.htilde[4],hex.htilde[5],hex.htilde[6],hex.htilde[7],Tube.T[1],Tube.T[2],Tube.T[3],Tube.T[4],Tube.T[5],Tube.T[6],Tube.T[7],Tube.T[8]) * Number of discrete variables: 20 ($cse1.region3boundary,$cse2.region3boundary,$cse3.phase,$cse3.region,$cse5.phase,$cse5.region,$cse6.phase,$cse6.region,$cse7.phase,$cse7.region,$cse8.phase,$cse8.region,$cse9.phase,$cse9.region,$cse10.phase,$cse10.region,$cse11.phase,$cse11.region,$cse12.phase,$cse12.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (226): * Single equations (assignments): 197 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 12 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 17 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 17 {(8,67.2%) 14,(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} * Non-linear torn systems: 0 ThermoPower.Test.DistributedParameterComponents.TestFlow1D2phChen_hf.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 423 * Number of variables: 423 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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. Warning: The initial conditions are over specified. The following 10 initial equations are redundant, so they are removed from the initialization sytem: $DER.hex.p = 0.0 $DER.hex.htilde[1] = 0.0 $DER.hex.htilde[2] = 0.0 $DER.hex.htilde[3] = 0.0 $DER.hex.htilde[4] = 0.0 $DER.hex.htilde[5] = 0.0 $DER.hex.htilde[6] = 0.0 $DER.hex.htilde[7] = 0.0 $DER.hex.htilde[8] = 0.0 $DER.hex.htilde[9] = 0.0. Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 57 * Number of states: 0 () * Number of discrete variables: 12 (hex.fluidState[10].phase,hex.fluidState[9].phase,hex.fluidState[8].phase,hex.fluidState[7].phase,hex.fluidState[6].phase,hex.fluidState[5].phase,hex.fluidState[4].phase,hex.fluidState[3].phase,hex.fluidState[2].phase,hex.fluidState[1].phase,hex.dew.phase,hex.bubble.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (200): * Single equations (assignments): 199 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {10 89} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 10 (hex.p,hex.htilde[1],hex.htilde[2],hex.htilde[3],hex.htilde[4],hex.htilde[5],hex.htilde[6],hex.htilde[7],hex.htilde[8],hex.htilde[9]) * Number of discrete variables: 24 ($cse1.region3boundary,$cse2.region3boundary,$cse3.phase,$cse3.region,$cse5.phase,$cse5.region,$cse6.phase,$cse6.region,$cse7.phase,$cse7.region,$cse8.phase,$cse8.region,$cse9.phase,$cse9.region,$cse10.phase,$cse10.region,$cse11.phase,$cse11.region,$cse12.phase,$cse12.region,$cse13.phase,$cse13.region,$cse14.phase,$cse14.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (220): * Single equations (assignments): 205 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 14 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(10,64.0%) 18} * Non-linear torn systems: 0 ThermoPower.Test.DistributedParameterComponents.TestFlow1D2phDB.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 454 * Number of variables: 454 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 17 * Number of states: 0 () * Number of discrete variables: 10 (hex.fluidState[8].phase,hex.fluidState[7].phase,hex.fluidState[6].phase,hex.fluidState[5].phase,hex.fluidState[4].phase,hex.fluidState[3].phase,hex.fluidState[2].phase,hex.fluidState[1].phase,hex.dew.phase,hex.bubble.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (99): * Single equations (assignments): 98 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {9 198} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 17 * Number of states: 16 (hex.p,hex.htilde[1],hex.htilde[2],hex.htilde[3],hex.htilde[4],hex.htilde[5],hex.htilde[6],hex.htilde[7],Tube.T[1],Tube.T[2],Tube.T[3],Tube.T[4],Tube.T[5],Tube.T[6],Tube.T[7],Tube.T[8]) * Number of discrete variables: 20 ($cse4.phase,$cse4.region,$cse5.phase,$cse5.region,$cse6.phase,$cse6.region,$cse7.phase,$cse7.region,$cse8.phase,$cse8.region,$cse9.phase,$cse9.region,$cse10.phase,$cse10.region,$cse11.phase,$cse11.region,$cse12.region3boundary,$cse13.region3boundary,$cse15.phase,$cse15.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (238): * Single equations (assignments): 208 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 12 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 18 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 17 {(8,67.2%) 14,(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} * Non-linear torn systems: 1 {1 10} ThermoPower.Test.DistributedParameterComponents.TestFlow1D2phDB_hf.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 422 * Number of variables: 422 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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. Warning: The initial conditions are over specified. The following 10 initial equations are redundant, so they are removed from the initialization sytem: $DER.hex.p = 0.0 $DER.hex.htilde[1] = 0.0 $DER.hex.htilde[2] = 0.0 $DER.hex.htilde[3] = 0.0 $DER.hex.htilde[4] = 0.0 $DER.hex.htilde[5] = 0.0 $DER.hex.htilde[6] = 0.0 $DER.hex.htilde[7] = 0.0 $DER.hex.htilde[8] = 0.0 $DER.hex.htilde[9] = 0.0. Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 19 * Number of states: 0 () * Number of discrete variables: 12 (hex.fluidState[10].phase,hex.fluidState[9].phase,hex.fluidState[8].phase,hex.fluidState[7].phase,hex.fluidState[6].phase,hex.fluidState[5].phase,hex.fluidState[4].phase,hex.fluidState[3].phase,hex.fluidState[2].phase,hex.fluidState[1].phase,hex.dew.phase,hex.bubble.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (192): * Single equations (assignments): 191 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {10 89} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 10 (hex.p,hex.htilde[1],hex.htilde[2],hex.htilde[3],hex.htilde[4],hex.htilde[5],hex.htilde[6],hex.htilde[7],hex.htilde[8],hex.htilde[9]) * Number of discrete variables: 24 ($cse1.region3boundary,$cse2.region3boundary,$cse3.phase,$cse3.region,$cse5.phase,$cse5.region,$cse6.phase,$cse6.region,$cse7.phase,$cse7.region,$cse8.phase,$cse8.region,$cse9.phase,$cse9.region,$cse10.phase,$cse10.region,$cse11.phase,$cse11.region,$cse12.phase,$cse12.region,$cse13.phase,$cse13.region,$cse14.phase,$cse14.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (230): * Single equations (assignments): 215 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 14 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(10,64.0%) 18} * Non-linear torn systems: 0 ThermoPower.Test.DistributedParameterComponents.TestFlow1Dfem2ph.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 1653 * Number of variables: 1653 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 870 * Number of states: 0 () * Number of discrete variables: 13 (hex.fluidState[11].phase,hex.fluidState[10].phase,hex.fluidState[9].phase,hex.fluidState[8].phase,hex.fluidState[7].phase,hex.fluidState[6].phase,hex.fluidState[5].phase,hex.fluidState[4].phase,hex.fluidState[3].phase,hex.fluidState[2].phase,hex.fluidState[1].phase,hex.dew.phase,hex.bubble.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (1264): * Single equations (assignments): 1263 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {12 195} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 2 * Number of states: 23 (hex.p,hex.h[1],hex.h[2],hex.h[3],hex.h[4],hex.h[5],hex.h[6],hex.h[7],hex.h[8],hex.h[9],hex.h[10],hex.h[11],MetalWall.T[1],MetalWall.T[2],MetalWall.T[3],MetalWall.T[4],MetalWall.T[5],MetalWall.T[6],MetalWall.T[7],MetalWall.T[8],MetalWall.T[9],MetalWall.T[10],MetalWall.T[11]) * Number of discrete variables: 28 ($cse5.phase,$cse5.region,$cse7.phase,$cse7.region,$cse9.phase,$cse9.region,$cse11.phase,$cse11.region,$cse13.phase,$cse13.region,$cse15.phase,$cse15.region,$cse17.phase,$cse17.region,$cse19.phase,$cse19.region,$cse21.phase,$cse21.region,$cse23.phase,$cse23.region,$cse25.phase,$cse25.region,$cse26.phase,$cse26.region,$cse27.phase,$cse27.region,$cse28.region3boundary,$cse29.region3boundary) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (498): * Single equations (assignments): 482 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 15 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(12,54.9%) 80} * Non-linear torn systems: 0 ThermoPower.Test.DistributedParameterComponents.TestFlowDependentHeatTransferCoefficient2ph.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 165 * Number of variables: 165 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 13 * Number of states: 0 () * Number of discrete variables: 6 (fluidState[6].phase,fluidState[5].phase,fluidState[4].phase,fluidState[3].phase,fluidState[2].phase,fluidState[1].phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (65): * Single equations (assignments): 64 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 1 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 0 * Mixed (continuous/discrete) equation systems: 0 Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 3 * Number of states: 0 () * Number of discrete variables: 14 ($cse1.phase,$cse1.region,$cse2.phase,$cse2.region,$cse3.phase,$cse3.region,$cse4.phase,$cse4.region,$cse5.phase,$cse5.region,$cse6.phase,$cse6.region,$cse7.region3boundary,$cse8.region3boundary) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (67): * Single equations (assignments): 59 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 8 * When equations: 0 ThermoPower.Test.DistributedParameterComponents.TestGasFlow1DFV_A.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 535 * Number of variables: 535 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 82 * Number of states: 0 () * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (214): * Single equations (assignments): 210 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 3 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 3 {1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {10 98} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 2 * Number of states: 11 (Mbal,hex.Ttilde[1],hex.Ttilde[2],hex.Ttilde[3],hex.Ttilde[4],hex.Ttilde[5],hex.Ttilde[6],hex.Ttilde[7],hex.Ttilde[8],hex.Ttilde[9],hex.p) * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (181): * Single equations (assignments): 177 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 3 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 3 {1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(10,64.0%) 36} * Non-linear torn systems: 0 ThermoPower.Test.DistributedParameterComponents.TestGasFlow1DFV_B.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 680 * Number of variables: 680 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 11 * Number of states: 0 () * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (180): * Single equations (assignments): 176 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 3 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 3 {1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {12 155} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 10 * Number of states: 13 (Mbal,hex.Ttilde[1],hex.Ttilde[2],hex.Ttilde[3],hex.Ttilde[4],hex.Ttilde[5],hex.Ttilde[6],hex.Ttilde[7],hex.Ttilde[8],hex.Ttilde[9],hex.Xtilde[1,1],hex.Xtilde[1,2],hex.p) * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (280): * Single equations (assignments): 276 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 3 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 3 {1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(10,64.0%) 36} * Non-linear torn systems: 0 ThermoPower.Test.DistributedParameterComponents.TestGasFlow1DFV_C.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 696 * Number of variables: 696 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 11 * Number of states: 0 () * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (211): * Single equations (assignments): 207 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 3 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 3 {1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {28 156} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 10 * Number of states: 29 (Mbal,hex.Ttilde[1],hex.Ttilde[2],hex.Ttilde[3],hex.Ttilde[4],hex.Ttilde[5],hex.Ttilde[6],hex.Ttilde[7],hex.Ttilde[8],hex.Ttilde[9],hex.Xtilde[1,1],hex.Xtilde[1,2],hex.Xtilde[2,1],hex.Xtilde[2,2],hex.Xtilde[3,1],hex.Xtilde[3,2],hex.Xtilde[4,1],hex.Xtilde[4,2],hex.Xtilde[5,1],hex.Xtilde[5,2],hex.Xtilde[6,1],hex.Xtilde[6,2],hex.Xtilde[7,1],hex.Xtilde[7,2],hex.Xtilde[8,1],hex.Xtilde[8,2],hex.Xtilde[9,1],hex.Xtilde[9,2],hex.p) * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (312): * Single equations (assignments): 308 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 3 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 3 {1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(10,64.0%) 36} * Non-linear torn systems: 0 ThermoPower.Test.DistributedParameterComponents.TestHeatTransfer2phDB.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 203 * Number of variables: 203 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 10 * Number of states: 0 () * Number of discrete variables: 8 (fluidState[6].phase,fluidState[5].phase,fluidState[4].phase,fluidState[3].phase,fluidState[2].phase,fluidState[1].phase,heatTransfer.dew.phase,heatTransfer.bubble.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (96): * Single equations (assignments): 95 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 1 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 0 * Mixed (continuous/discrete) equation systems: 0 Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 3 * Number of states: 0 () * Number of discrete variables: 16 ($cse1.phase,$cse1.region,$cse2.phase,$cse2.region,$cse3.phase,$cse3.region,$cse4.phase,$cse4.region,$cse5.phase,$cse5.region,$cse6.phase,$cse6.region,$cse7.phase,$cse7.region,$cse8.region3boundary,$cse9.region3boundary) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (97): * Single equations (assignments): 88 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 9 * When equations: 0 ThermoPower.Test.DistributedParameterComponents.TestRefrigerantEvaporator.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 1456 * Number of variables: 1456 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 43 * Number of states: 0 () * Number of discrete variables: 12 (fluid_T_in.fluidState.phase,fluid_T_out.fluidState.phase,fluidFlow.fluidState[1].phase,fluidFlow.fluidState[2].phase,fluidFlow.fluidState[3].phase,fluidFlow.fluidState[4].phase,fluidFlow.fluidState[5].phase,fluidFlow.fluidState[6].phase,fluidFlow.fluidState[7].phase,fluidFlow.fluidState[8].phase,fluidFlow.fluidState[9].phase,fluidFlow.fluidState[10].phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (369): * Single equations (assignments): 360 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 5 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 3 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 3 {1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {22 311} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 21 * Number of states: 31 (gasFlow.Ttilde[1],gasFlow.Ttilde[2],gasFlow.Ttilde[3],gasFlow.Ttilde[4],gasFlow.Ttilde[5],gasFlow.Ttilde[6],gasFlow.Ttilde[7],gasFlow.Ttilde[8],gasFlow.Ttilde[9],gasFlow.Xtilde[1,1],gasFlow.Xtilde[1,2],gasFlow.Xtilde[1,3],gasFlow.Xtilde[1,4],fluidFlow.htilde[1],fluidFlow.htilde[2],fluidFlow.htilde[3],fluidFlow.htilde[4],fluidFlow.htilde[5],fluidFlow.htilde[6],fluidFlow.htilde[7],fluidFlow.htilde[8],fluidFlow.htilde[9],tubeWall.Tvol[1],tubeWall.Tvol[2],tubeWall.Tvol[3],tubeWall.Tvol[4],tubeWall.Tvol[5],tubeWall.Tvol[6],tubeWall.Tvol[7],tubeWall.Tvol[8],tubeWall.Tvol[9]) * Number of discrete variables: 23 (fluid_T_in.fluidState.phase,fluid_T_out.fluidState.phase,fluidFlow.fluidState[2].phase,fluidFlow.fluidState[3].phase,fluidFlow.fluidState[4].phase,fluidFlow.fluidState[5].phase,fluidFlow.fluidState[6].phase,fluidFlow.fluidState[7].phase,fluidFlow.fluidState[8].phase,fluidFlow.fluidState[9].phase,fluidFlow.fluidState[10].phase,$cse1.phase,$cse2.phase,$cse8.phase,$cse9.phase,$cse10.phase,$cse11.phase,$cse12.phase,$cse13.phase,$cse14.phase,$cse15.phase,$cse16.phase,fluidFlow.fluidState[1].phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (610): * Single equations (assignments): 577 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 12 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 3 * Torn equation systems: 18 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 3 {1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 18 {(1,100.0%) 4,(2,100.0%) 3,(2,100.0%) 3,(2,100.0%) 3,(2,100.0%) 3,(2,100.0%) 3,(2,100.0%) 3,(1,100.0%) 4,(1,100.0%) 4,(1,100.0%) 2,(1,100.0%) 2,(1,100.0%) 2,(1,100.0%) 2,(1,100.0%) 2,(1,100.0%) 2,(1,100.0%) 2,(1,100.0%) 2,(1,100.0%) 2} * Non-linear torn systems: 0 ThermoPower.Test.DistributedParameterComponents.TestWalls.err [ThermoPower 3.1/Thermal.mo:581:5-581:61:writable] Warning: No corresponding 'inner' declaration found for component .ThermoPower.System wall1.system declared as 'outer '. The existing 'inner' components are: There are no 'inner' components defined in the model in any of the parent scopes of 'outer' component's scope: ThermoPower.Thermal.MetalWallFV$wall1. Check if you have not misspelled the 'outer' component name. Please declare an 'inner' component with the same name in the top scope. Continuing flattening by only considering the 'outer' component declaration. [ThermoPower 3.1/Thermal.mo:581:5-581:61:writable] Warning: No corresponding 'inner' declaration found for component .ThermoPower.System wall2.system declared as 'outer '. The existing 'inner' components are: There are no 'inner' components defined in the model in any of the parent scopes of 'outer' component's scope: ThermoPower.Thermal.MetalWallFV$wall2. Check if you have not misspelled the 'outer' component name. Please declare an 'inner' component with the same name in the top scope. Continuing flattening by only considering the 'outer' component declaration. Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 44 * Number of variables: 44 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 4 * Number of states: 0 () * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (21): * Single equations (assignments): 21 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 0 * Mixed (continuous/discrete) equation systems: 0 Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 4 (wall1.Tvol[1],wall1.Tvol[2],wall2.Tvol[1],wall2.Tvol[2]) * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (17): * Single equations (assignments): 17 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 ThermoPower.Test.DistributedParameterComponents.TestWaterFlow1DFEM_A.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 1391 * Number of variables: 1391 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 807 * Number of states: 0 () * Number of discrete variables: 14 (T_out.fluidState.phase,T_in.fluidState.phase,hex.fluidState[12].phase,hex.fluidState[11].phase,hex.fluidState[10].phase,hex.fluidState[9].phase,hex.fluidState[8].phase,hex.fluidState[7].phase,hex.fluidState[6].phase,hex.fluidState[5].phase,hex.fluidState[4].phase,hex.fluidState[3].phase,hex.fluidState[2].phase,hex.fluidState[1].phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (931): * Single equations (assignments): 930 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {13 163} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 2 * Number of states: 13 (hex.p,hex.h[1],hex.h[2],hex.h[3],hex.h[4],hex.h[5],hex.h[6],hex.h[7],hex.h[8],hex.h[9],hex.h[10],hex.h[11],hex.h[12]) * Number of discrete variables: 28 ($cse1.phase,$cse1.region,$cse2.phase,$cse2.region,$cse16.phase,$cse16.region,$cse17.phase,$cse17.region,$cse18.phase,$cse18.region,$cse19.phase,$cse19.region,$cse20.phase,$cse20.region,$cse21.phase,$cse21.region,$cse22.phase,$cse22.region,$cse23.phase,$cse23.region,$cse24.phase,$cse24.region,$cse25.phase,$cse25.region,$cse26.phase,$cse26.region,$cse27.phase,$cse27.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (163): * Single equations (assignments): 148 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 14 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {13 126} ThermoPower.Test.DistributedParameterComponents.TestWaterFlow1DFEM_B.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 1387 * Number of variables: 1387 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 807 * Number of states: 0 () * Number of discrete variables: 14 (T_out.fluidState.phase,T_in.fluidState.phase,hex.fluidState[12].phase,hex.fluidState[11].phase,hex.fluidState[10].phase,hex.fluidState[9].phase,hex.fluidState[8].phase,hex.fluidState[7].phase,hex.fluidState[6].phase,hex.fluidState[5].phase,hex.fluidState[4].phase,hex.fluidState[3].phase,hex.fluidState[2].phase,hex.fluidState[1].phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (916): * Single equations (assignments): 915 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {13 187} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 9 * Number of states: 13 (hex.p,hex.h[1],hex.h[2],hex.h[3],hex.h[4],hex.h[5],hex.h[6],hex.h[7],hex.h[8],hex.h[9],hex.h[10],hex.h[11],hex.h[12]) * Number of discrete variables: 28 ($cse1.phase,$cse1.region,$cse2.phase,$cse2.region,$cse16.phase,$cse16.region,$cse17.phase,$cse17.region,$cse18.phase,$cse18.region,$cse19.phase,$cse19.region,$cse20.phase,$cse20.region,$cse21.phase,$cse21.region,$cse22.phase,$cse22.region,$cse23.phase,$cse23.region,$cse24.phase,$cse24.region,$cse25.phase,$cse25.region,$cse26.phase,$cse26.region,$cse27.phase,$cse27.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (168): * Single equations (assignments): 153 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 14 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {13 126} ThermoPower.Test.DistributedParameterComponents.TestWaterFlow1DFEM_C.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 1363 * Number of variables: 1363 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 820 * Number of states: 0 () * Number of discrete variables: 14 (T_out.fluidState.phase,T_in.fluidState.phase,hex.fluidState[12].phase,hex.fluidState[11].phase,hex.fluidState[10].phase,hex.fluidState[9].phase,hex.fluidState[8].phase,hex.fluidState[7].phase,hex.fluidState[6].phase,hex.fluidState[5].phase,hex.fluidState[4].phase,hex.fluidState[3].phase,hex.fluidState[2].phase,hex.fluidState[1].phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (962): * Single equations (assignments): 961 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {13 141} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 2 * Number of states: 13 (hex.p,hex.h[1],hex.h[2],hex.h[3],hex.h[4],hex.h[5],hex.h[6],hex.h[7],hex.h[8],hex.h[9],hex.h[10],hex.h[11],hex.h[12]) * Number of discrete variables: 28 ($cse1.phase,$cse1.region,$cse2.phase,$cse2.region,$cse16.phase,$cse16.region,$cse17.phase,$cse17.region,$cse18.phase,$cse18.region,$cse19.phase,$cse19.region,$cse20.phase,$cse20.region,$cse21.phase,$cse21.region,$cse22.phase,$cse22.region,$cse23.phase,$cse23.region,$cse24.phase,$cse24.region,$cse25.phase,$cse25.region,$cse26.phase,$cse26.region,$cse27.phase,$cse27.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (179): * Single equations (assignments): 164 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 14 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {13 106} ThermoPower.Test.DistributedParameterComponents.TestWaterFlow1DFEM_D.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 1341 * Number of variables: 1341 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 820 * Number of states: 0 () * Number of discrete variables: 12 (hex.fluidState[12].phase,hex.fluidState[11].phase,hex.fluidState[10].phase,hex.fluidState[9].phase,hex.fluidState[8].phase,hex.fluidState[7].phase,hex.fluidState[6].phase,hex.fluidState[5].phase,hex.fluidState[4].phase,hex.fluidState[3].phase,hex.fluidState[2].phase,hex.fluidState[1].phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (956): * Single equations (assignments): 955 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {13 142} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 2 * Number of states: 13 (hex.p,hex.h[1],hex.h[2],hex.h[3],hex.h[4],hex.h[5],hex.h[6],hex.h[7],hex.h[8],hex.h[9],hex.h[10],hex.h[11],hex.h[12]) * Number of discrete variables: 24 ($cse13.phase,$cse13.region,$cse14.phase,$cse14.region,$cse15.phase,$cse15.region,$cse16.phase,$cse16.region,$cse17.phase,$cse17.region,$cse18.phase,$cse18.region,$cse19.phase,$cse19.region,$cse20.phase,$cse20.region,$cse21.phase,$cse21.region,$cse22.phase,$cse22.region,$cse23.phase,$cse23.region,$cse24.phase,$cse24.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (171): * Single equations (assignments): 157 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 12 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 2 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(1,100.0%) 1} * Non-linear torn systems: 1 {13 106} ThermoPower.Test.DistributedParameterComponents.TestWaterFlow1DFEM_E.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 2772 * Number of variables: 2772 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 1613 * Number of states: 0 () * Number of discrete variables: 28 (SensT_B_out.fluidState.phase,SensT_A_out.fluidState.phase,SensT_B_in.fluidState.phase,SensT_A_in.fluidState.phase,hexB.fluidState[12].phase,hexB.fluidState[11].phase,hexB.fluidState[10].phase,hexB.fluidState[9].phase,hexB.fluidState[8].phase,hexB.fluidState[7].phase,hexB.fluidState[6].phase,hexB.fluidState[5].phase,hexB.fluidState[4].phase,hexB.fluidState[3].phase,hexB.fluidState[2].phase,hexB.fluidState[1].phase,hexA.fluidState[12].phase,hexA.fluidState[11].phase,hexA.fluidState[10].phase,hexA.fluidState[9].phase,hexA.fluidState[8].phase,hexA.fluidState[7].phase,hexA.fluidState[6].phase,hexA.fluidState[5].phase,hexA.fluidState[4].phase,hexA.fluidState[3].phase,hexA.fluidState[2].phase,hexA.fluidState[1].phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (1830): * Single equations (assignments): 1829 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {26 362} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 16 * Number of states: 26 (hexA.p,hexA.h[1],hexA.h[2],hexA.h[3],hexA.h[4],hexA.h[5],hexA.h[6],hexA.h[7],hexA.h[8],hexA.h[9],hexA.h[10],hexA.h[11],hexA.h[12],hexB.p,hexB.h[1],hexB.h[2],hexB.h[3],hexB.h[4],hexB.h[5],hexB.h[6],hexB.h[7],hexB.h[8],hexB.h[9],hexB.h[10],hexB.h[11],hexB.h[12]) * Number of discrete variables: 56 ($cse1.phase,$cse1.region,$cse2.phase,$cse2.region,$cse3.phase,$cse3.region,$cse4.phase,$cse4.region,$cse18.phase,$cse18.region,$cse19.phase,$cse19.region,$cse20.phase,$cse20.region,$cse21.phase,$cse21.region,$cse22.phase,$cse22.region,$cse23.phase,$cse23.region,$cse24.phase,$cse24.region,$cse25.phase,$cse25.region,$cse26.phase,$cse26.region,$cse27.phase,$cse27.region,$cse28.phase,$cse28.region,$cse29.phase,$cse29.region,$cse55.phase,$cse55.region,$cse56.phase,$cse56.region,$cse57.phase,$cse57.region,$cse58.phase,$cse58.region,$cse59.phase,$cse59.region,$cse60.phase,$cse60.region,$cse61.phase,$cse61.region,$cse62.phase,$cse62.region,$cse63.phase,$cse63.region,$cse64.phase,$cse64.region,$cse65.phase,$cse65.region,$cse66.phase,$cse66.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (323): * Single equations (assignments): 293 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 28 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 2 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 2 {13 126,13 126} ThermoPower.Test.DistributedParameterComponents.TestWaterFlow1DFEM_F.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 4501 * Number of variables: 4501 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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. Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: hexB.phi[1]:VARIABLE(unit = "W/m2" ) "Heat flux entering the fluid" type: Real [16] hexB.phi[16]:VARIABLE(unit = "W/m2" ) "Heat flux entering the fluid" type: Real [16] hexB.phi[5]:VARIABLE(unit = "W/m2" ) "Heat flux entering the fluid" type: Real [16] hexB.phi[3]:VARIABLE(unit = "W/m2" ) "Heat flux entering the fluid" type: Real [16] hexB.phi[2]:VARIABLE(unit = "W/m2" ) "Heat flux entering the fluid" type: Real [16] -- hexA.phi[8]:VARIABLE(unit = "W/m2" ) "Heat flux entering the fluid" type: Real [16] hexB.phi[11]:VARIABLE(unit = "W/m2" ) "Heat flux entering the fluid" type: Real [16] hexA.phi[4]:VARIABLE(unit = "W/m2" ) "Heat flux entering the fluid" type: Real [16] hexB.phi[14]:VARIABLE(unit = "W/m2" ) "Heat flux entering the fluid" type: Real [16] hexA.phi[2]:VARIABLE(unit = "W/m2" ) "Heat flux entering the fluid" type: Real [16] Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 2917 * Number of states: 0 () * Number of discrete variables: 36 (SensT_B_out.fluidState.phase,SensT_A_out.fluidState.phase,SensT_B_in.fluidState.phase,SensT_A_in.fluidState.phase,hexB.fluidState[16].phase,hexB.fluidState[15].phase,hexB.fluidState[14].phase,hexB.fluidState[13].phase,hexB.fluidState[12].phase,hexB.fluidState[11].phase,hexB.fluidState[10].phase,hexB.fluidState[9].phase,hexB.fluidState[8].phase,hexB.fluidState[7].phase,hexB.fluidState[6].phase,hexB.fluidState[5].phase,hexB.fluidState[4].phase,hexB.fluidState[3].phase,hexB.fluidState[2].phase,hexB.fluidState[1].phase,hexA.fluidState[16].phase,hexA.fluidState[15].phase,hexA.fluidState[14].phase,hexA.fluidState[13].phase,hexA.fluidState[12].phase,hexA.fluidState[11].phase,hexA.fluidState[10].phase,hexA.fluidState[9].phase,hexA.fluidState[8].phase,hexA.fluidState[7].phase,hexA.fluidState[6].phase,hexA.fluidState[5].phase,hexA.fluidState[4].phase,hexA.fluidState[3].phase,hexA.fluidState[2].phase,hexA.fluidState[1].phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (3223): * Single equations (assignments): 3222 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {45 539} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 16 * Number of states: 50 (hexA.p,hexA.h[1],hexA.h[2],hexA.h[3],hexA.h[4],hexA.h[5],hexA.h[6],hexA.h[7],hexA.h[8],hexA.h[9],hexA.h[10],hexA.h[11],hexA.h[12],hexA.h[13],hexA.h[14],hexA.h[15],hexA.h[16],hexB.p,hexB.h[1],hexB.h[2],hexB.h[3],hexB.h[4],hexB.h[5],hexB.h[6],hexB.h[7],hexB.h[8],hexB.h[9],hexB.h[10],hexB.h[11],hexB.h[12],hexB.h[13],hexB.h[14],hexB.h[15],hexB.h[16],MetalWall.T[1],MetalWall.T[2],MetalWall.T[3],MetalWall.T[4],MetalWall.T[5],MetalWall.T[6],MetalWall.T[7],MetalWall.T[8],MetalWall.T[9],MetalWall.T[10],MetalWall.T[11],MetalWall.T[12],MetalWall.T[13],MetalWall.T[14],MetalWall.T[15],MetalWall.T[16]) * Number of discrete variables: 72 ($cse1.phase,$cse1.region,$cse2.phase,$cse2.region,$cse3.phase,$cse3.region,$cse4.phase,$cse4.region,$cse24.phase,$cse24.region,$cse25.phase,$cse25.region,$cse26.phase,$cse26.region,$cse27.phase,$cse27.region,$cse28.phase,$cse28.region,$cse29.phase,$cse29.region,$cse30.phase,$cse30.region,$cse31.phase,$cse31.region,$cse32.phase,$cse32.region,$cse33.phase,$cse33.region,$cse34.phase,$cse34.region,$cse35.phase,$cse35.region,$cse36.phase,$cse36.region,$cse37.phase,$cse37.region,$cse38.phase,$cse38.region,$cse39.phase,$cse39.region,$cse73.phase,$cse73.region,$cse74.phase,$cse74.region,$cse75.phase,$cse75.region,$cse76.phase,$cse76.region,$cse77.phase,$cse77.region,$cse78.phase,$cse78.region,$cse79.phase,$cse79.region,$cse80.phase,$cse80.region,$cse81.phase,$cse81.region,$cse82.phase,$cse82.region,$cse83.phase,$cse83.region,$cse84.phase,$cse84.region,$cse85.phase,$cse85.region,$cse86.phase,$cse86.region,$cse87.phase,$cse87.region,$cse88.phase,$cse88.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (455): * Single equations (assignments): 385 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 36 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 34 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 32 {(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} * Non-linear torn systems: 2 {17 174,17 174} ThermoPower.Test.DistributedParameterComponents.TestWaterFlow1DFEM_G.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 496 * Number of variables: 496 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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. Warning: Assuming fixed start value for the following 6 variables: hex.h[6]:VARIABLE(min = max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, -10000000000.0)))) max = min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, 10000000000.0)))) start = hex.hstart[6] unit = "J/kg" nominal = 500000.0 ) "Fluid specific enthalpy" type: Real [6] hex.h[5]:VARIABLE(min = max(-10000000000.0, max(-10000000000.0, -10000000000.0)) max = min(10000000000.0, min(10000000000.0, 10000000000.0)) start = hex.hstart[5] unit = "J/kg" nominal = 500000.0 ) "Fluid specific enthalpy" type: Real [6] hex.h[4]:VARIABLE(min = max(-10000000000.0, max(-10000000000.0, -10000000000.0)) max = min(10000000000.0, min(10000000000.0, 10000000000.0)) start = hex.hstart[4] unit = "J/kg" nominal = 500000.0 ) "Fluid specific enthalpy" type: Real [6] hex.h[3]:VARIABLE(min = max(-10000000000.0, max(-10000000000.0, -10000000000.0)) max = min(10000000000.0, min(10000000000.0, 10000000000.0)) start = hex.hstart[3] unit = "J/kg" nominal = 500000.0 ) "Fluid specific enthalpy" type: Real [6] hex.h[2]:VARIABLE(min = max(-10000000000.0, max(-10000000000.0, -10000000000.0)) max = min(10000000000.0, min(10000000000.0, 10000000000.0)) start = hex.hstart[2] unit = "J/kg" nominal = 500000.0 ) "Fluid specific enthalpy" type: Real [6] hex.h[1]:VARIABLE(min = max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, -10000000000.0)))) max = min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, 10000000000.0)))) start = 100000.0 unit = "J/kg" nominal = 500000.0 ) "Fluid specific enthalpy" type: Real [6] Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: $DERAliashex.h[4]:VARIABLE(nominal = 500000.0 ) type: Real $DERAliashex.h[6]:VARIABLE(nominal = 500000.0 ) type: Real $DERAliashex.h[5]:VARIABLE(nominal = 500000.0 ) type: Real $DERAliashex.h[3]:VARIABLE(nominal = 500000.0 ) type: Real $DERAliashex.h[1]:VARIABLE(nominal = 500000.0 ) type: Real $DERAliashex.h[2]:VARIABLE(nominal = 500000.0 ) type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 197 * Number of states: 0 () * Number of discrete variables: 15 (T_out.fluidState.phase,T_in.fluidState.phase,hex.fluidState[6].phase,hex.fluidState[5].phase,hex.fluidState[4].phase,hex.fluidState[3].phase,hex.fluidState[2].phase,hex.fluidState[1].phase,$whenCondition1,MassFlowRate.a,MassFlowRate.b,MassFlowRate.last,$PRE.MassFlowRate.nextEvent,MassFlowRate.nextEvent,MassFlowRate.nextEventScaled) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (299): * Single equations (assignments): 297 * Array equations: 0 * Algorithm blocks: 1 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {6 49} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 2 * Number of states: 6 (hex.h[1],hex.h[2],hex.h[3],hex.h[4],hex.h[5],hex.h[6]) * Number of discrete variables: 22 ($cse17.phase,$cse17.region,$cse18.phase,$cse18.region,$cse19.phase,$cse19.region,$cse20.phase,$cse20.region,$cse21.phase,$cse21.region,$cse22.phase,$cse22.region,$cse30.phase,$cse30.region,$cse31.phase,$cse31.region,$whenCondition1,MassFlowRate.a,MassFlowRate.b,MassFlowRate.last,MassFlowRate.nextEvent,MassFlowRate.nextEventScaled) * Number of discrete states: 6 (MassFlowRate.nextEvent,MassFlowRate.last,MassFlowRate.nextEventScaled,MassFlowRate.b,MassFlowRate.a,$whenCondition1) * Top-level inputs: 0 Notification: Strong component statistics for simulation (99): * Single equations (assignments): 89 * Array equations: 0 * Algorithm blocks: 1 * Record equations: 8 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {6 54} ThermoPower.Test.DistributedParameterComponents.TestWaterFlow1DFEM_J.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 1155 * Number of variables: 1155 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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. Warning: Assuming fixed start value for the following 12 variables: pipe1.h[11]:VARIABLE(min = max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, -10000000000.0))) max = min(10000000000.0, min(10000000000.0, min(10000000000.0, 10000000000.0))) start = pipe1.hstart[11] unit = "J/kg" nominal = 500000.0 ) "Fluid specific enthalpy" type: Real [11] pipe1.h[10]:VARIABLE(min = max(-10000000000.0, max(-10000000000.0, -10000000000.0)) max = min(10000000000.0, min(10000000000.0, 10000000000.0)) start = pipe1.hstart[10] unit = "J/kg" nominal = 500000.0 ) "Fluid specific enthalpy" type: Real [11] pipe1.h[9]:VARIABLE(min = max(-10000000000.0, max(-10000000000.0, -10000000000.0)) max = min(10000000000.0, min(10000000000.0, 10000000000.0)) start = pipe1.hstart[9] unit = "J/kg" nominal = 500000.0 ) "Fluid specific enthalpy" type: Real [11] pipe1.h[8]:VARIABLE(min = max(-10000000000.0, max(-10000000000.0, -10000000000.0)) max = min(10000000000.0, min(10000000000.0, 10000000000.0)) start = pipe1.hstart[8] unit = "J/kg" nominal = 500000.0 ) "Fluid specific enthalpy" type: Real [11] pipe1.h[7]:VARIABLE(min = max(-10000000000.0, max(-10000000000.0, -10000000000.0)) max = min(10000000000.0, min(10000000000.0, 10000000000.0)) start = pipe1.hstart[7] unit = "J/kg" nominal = 500000.0 ) "Fluid specific enthalpy" type: Real [11] -- pipe1.h[4]:VARIABLE(min = max(-10000000000.0, max(-10000000000.0, -10000000000.0)) max = min(10000000000.0, min(10000000000.0, 10000000000.0)) start = pipe1.hstart[4] unit = "J/kg" nominal = 500000.0 ) "Fluid specific enthalpy" type: Real [11] pipe1.h[3]:VARIABLE(min = max(-10000000000.0, max(-10000000000.0, -10000000000.0)) max = min(10000000000.0, min(10000000000.0, 10000000000.0)) start = pipe1.hstart[3] unit = "J/kg" nominal = 500000.0 ) "Fluid specific enthalpy" type: Real [11] pipe1.h[2]:VARIABLE(min = max(-10000000000.0, max(-10000000000.0, -10000000000.0)) max = min(10000000000.0, min(10000000000.0, 10000000000.0)) start = pipe1.hstart[2] unit = "J/kg" nominal = 500000.0 ) "Fluid specific enthalpy" type: Real [11] pipe1.h[1]:VARIABLE(min = max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, -10000000000.0))) max = min(10000000000.0, min(10000000000.0, min(10000000000.0, 10000000000.0))) start = pipe1.hstart[1] unit = "J/kg" nominal = 500000.0 ) "Fluid specific enthalpy" type: Real [11] pipe1.p:VARIABLE(min = max(611.657, max(611.657, max(611.657, max(611.657, max(611.657, max(611.657, max(611.657, max(611.657, max(611.657, max(611.657, max(611.657, max(611.657, max(611.657, max(611.657, max(611.657, max(611.657, max(611.657, max(611.657, max(611.657, max(611.657, max(611.657, max(611.657, 611.657)))))))))))))))))))))) max = min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, 100000000.0)))))))))))))))))))))) start = pipe1.pstart unit = "Pa" nominal = 1000000.0 ) "Fluid pressure" type: Real Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: $DERAliaspipe1.h[5]:VARIABLE(nominal = 500000.0 ) type: Real $DERAliaspipe1.h[9]:VARIABLE(nominal = 500000.0 ) type: Real $DERAliaspipe1.h[7]:VARIABLE(nominal = 500000.0 ) type: Real $DERAliaspipe1.h[8]:VARIABLE(nominal = 500000.0 ) type: Real $DERAliaspipe1.h[10]:VARIABLE(nominal = 500000.0 ) type: Real -- $DERAliaspipe1.h[4]:VARIABLE(nominal = 500000.0 ) type: Real $DERAliaspipe1.h[3]:VARIABLE(nominal = 500000.0 ) type: Real $DERAliaspipe1.h[2]:VARIABLE(nominal = 500000.0 ) type: Real $DERAliaspipe1.h[1]:VARIABLE(nominal = 500000.0 ) type: Real $DERAliaspipe1.h[6]:VARIABLE(nominal = 500000.0 ) type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 696 * Number of states: 0 () * Number of discrete variables: 11 (pipe1.fluidState[11].phase,pipe1.fluidState[10].phase,pipe1.fluidState[9].phase,pipe1.fluidState[8].phase,pipe1.fluidState[7].phase,pipe1.fluidState[6].phase,pipe1.fluidState[5].phase,pipe1.fluidState[4].phase,pipe1.fluidState[3].phase,pipe1.fluidState[2].phase,pipe1.fluidState[1].phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (846): * Single equations (assignments): 845 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {17 98} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 12 (pipe1.p,pipe1.h[1],pipe1.h[2],pipe1.h[3],pipe1.h[4],pipe1.h[5],pipe1.h[6],pipe1.h[7],pipe1.h[8],pipe1.h[9],pipe1.h[10],pipe1.h[11]) * Number of discrete variables: 22 ($cse21.phase,$cse21.region,$cse22.phase,$cse22.region,$cse23.phase,$cse23.region,$cse24.phase,$cse24.region,$cse25.phase,$cse25.region,$cse26.phase,$cse26.region,$cse27.phase,$cse27.region,$cse28.phase,$cse28.region,$cse29.phase,$cse29.region,$cse30.phase,$cse30.region,$cse31.phase,$cse31.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (128): * Single equations (assignments): 116 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 11 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {15 122} ThermoPower.Test.DistributedParameterComponents.TestWaterFlow1DFEM_K.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 1176 * Number of variables: 1176 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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. Warning: Assuming fixed start value for the following 12 variables: pipe1.h[11]:VARIABLE(min = max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, -10000000000.0))) max = min(10000000000.0, min(10000000000.0, min(10000000000.0, 10000000000.0))) start = pipe1.hstart[11] unit = "J/kg" nominal = 500000.0 ) "Fluid specific enthalpy" type: Real [11] pipe1.h[10]:VARIABLE(min = max(-10000000000.0, max(-10000000000.0, -10000000000.0)) max = min(10000000000.0, min(10000000000.0, 10000000000.0)) start = pipe1.hstart[10] unit = "J/kg" nominal = 500000.0 ) "Fluid specific enthalpy" type: Real [11] pipe1.h[9]:VARIABLE(min = max(-10000000000.0, max(-10000000000.0, -10000000000.0)) max = min(10000000000.0, min(10000000000.0, 10000000000.0)) start = pipe1.hstart[9] unit = "J/kg" nominal = 500000.0 ) "Fluid specific enthalpy" type: Real [11] pipe1.h[8]:VARIABLE(min = max(-10000000000.0, max(-10000000000.0, -10000000000.0)) max = min(10000000000.0, min(10000000000.0, 10000000000.0)) start = pipe1.hstart[8] unit = "J/kg" nominal = 500000.0 ) "Fluid specific enthalpy" type: Real [11] pipe1.h[7]:VARIABLE(min = max(-10000000000.0, max(-10000000000.0, -10000000000.0)) max = min(10000000000.0, min(10000000000.0, 10000000000.0)) start = pipe1.hstart[7] unit = "J/kg" nominal = 500000.0 ) "Fluid specific enthalpy" type: Real [11] -- pipe1.h[4]:VARIABLE(min = max(-10000000000.0, max(-10000000000.0, -10000000000.0)) max = min(10000000000.0, min(10000000000.0, 10000000000.0)) start = pipe1.hstart[4] unit = "J/kg" nominal = 500000.0 ) "Fluid specific enthalpy" type: Real [11] pipe1.h[3]:VARIABLE(min = max(-10000000000.0, max(-10000000000.0, -10000000000.0)) max = min(10000000000.0, min(10000000000.0, 10000000000.0)) start = pipe1.hstart[3] unit = "J/kg" nominal = 500000.0 ) "Fluid specific enthalpy" type: Real [11] pipe1.h[2]:VARIABLE(min = max(-10000000000.0, max(-10000000000.0, -10000000000.0)) max = min(10000000000.0, min(10000000000.0, 10000000000.0)) start = pipe1.hstart[2] unit = "J/kg" nominal = 500000.0 ) "Fluid specific enthalpy" type: Real [11] pipe1.h[1]:VARIABLE(min = max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, -10000000000.0))) max = min(10000000000.0, min(10000000000.0, min(10000000000.0, 10000000000.0))) start = pipe1.hstart[1] unit = "J/kg" nominal = 500000.0 ) "Fluid specific enthalpy" type: Real [11] pipe1.p:VARIABLE(min = max(611.657, max(611.657, max(611.657, max(611.657, max(611.657, max(611.657, max(611.657, max(611.657, max(611.657, max(611.657, max(611.657, max(611.657, max(611.657, max(611.657, max(611.657, max(611.657, max(611.657, max(611.657, max(611.657, max(611.657, max(611.657, max(611.657, 611.657)))))))))))))))))))))) max = min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, 100000000.0)))))))))))))))))))))) start = pipe1.pstart unit = "Pa" nominal = 1000000.0 ) "Fluid pressure" type: Real Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: $DERAliaspipe1.p:VARIABLE(nominal = 1000000.0 ) type: Real $DERAliaspipe1.h[11]:VARIABLE(nominal = 500000.0 ) type: Real $DERAliaspipe1.h[1]:VARIABLE(nominal = 500000.0 ) type: Real $DERAliaspipe1.h[2]:VARIABLE(nominal = 500000.0 ) type: Real $DERAliaspipe1.h[3]:VARIABLE(nominal = 500000.0 ) type: Real -- $DERAliaspipe1.h[9]:VARIABLE(nominal = 500000.0 ) type: Real $DERAliaspipe1.h[8]:VARIABLE(nominal = 500000.0 ) type: Real $DERAliaspipe1.h[7]:VARIABLE(nominal = 500000.0 ) type: Real $DERAliaspipe1.h[6]:VARIABLE(nominal = 500000.0 ) type: Real $DERAliaspipe1.h[5]:VARIABLE(nominal = 500000.0 ) type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 683 * Number of states: 0 () * Number of discrete variables: 11 (pipe1.fluidState[11].phase,pipe1.fluidState[10].phase,pipe1.fluidState[9].phase,pipe1.fluidState[8].phase,pipe1.fluidState[7].phase,pipe1.fluidState[6].phase,pipe1.fluidState[5].phase,pipe1.fluidState[4].phase,pipe1.fluidState[3].phase,pipe1.fluidState[2].phase,pipe1.fluidState[1].phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (815): * Single equations (assignments): 814 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {15 122} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 12 (pipe1.p,pipe1.h[1],pipe1.h[2],pipe1.h[3],pipe1.h[4],pipe1.h[5],pipe1.h[6],pipe1.h[7],pipe1.h[8],pipe1.h[9],pipe1.h[10],pipe1.h[11]) * Number of discrete variables: 22 ($cse22.phase,$cse22.region,$cse23.phase,$cse23.region,$cse24.phase,$cse24.region,$cse25.phase,$cse25.region,$cse26.phase,$cse26.region,$cse27.phase,$cse27.region,$cse28.phase,$cse28.region,$cse29.phase,$cse29.region,$cse30.phase,$cse30.region,$cse31.phase,$cse31.region,$cse32.phase,$cse32.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (109): * Single equations (assignments): 97 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 11 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {15 144} ThermoPower.Test.DistributedParameterComponents.TestWaterFlow1DFV2ph.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 884 * Number of variables: 884 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 22 * Number of states: 0 () * Number of discrete variables: 17 (hexFV.fluidState[15].phase,hexFV.fluidState[14].phase,hexFV.fluidState[13].phase,hexFV.fluidState[12].phase,hexFV.fluidState[11].phase,hexFV.fluidState[10].phase,hexFV.fluidState[9].phase,hexFV.fluidState[8].phase,hexFV.fluidState[7].phase,hexFV.fluidState[6].phase,hexFV.fluidState[5].phase,hexFV.fluidState[4].phase,hexFV.fluidState[3].phase,hexFV.fluidState[2].phase,hexFV.fluidState[1].phase,hexFV.heatTransfer.dew.phase,hexFV.heatTransfer.bubble.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (181): * Single equations (assignments): 179 * Array equations: 1 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {15 367} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 31 * Number of states: 29 (hexFV.p,hexFV.htilde[1],hexFV.htilde[2],hexFV.htilde[3],hexFV.htilde[4],hexFV.htilde[5],hexFV.htilde[6],hexFV.htilde[7],hexFV.htilde[8],hexFV.htilde[9],hexFV.htilde[10],hexFV.htilde[11],hexFV.htilde[12],hexFV.htilde[13],hexFV.htilde[14],metalTubeFV.Tvol[1],metalTubeFV.Tvol[2],metalTubeFV.Tvol[3],metalTubeFV.Tvol[4],metalTubeFV.Tvol[5],metalTubeFV.Tvol[6],metalTubeFV.Tvol[7],metalTubeFV.Tvol[8],metalTubeFV.Tvol[9],metalTubeFV.Tvol[10],metalTubeFV.Tvol[11],metalTubeFV.Tvol[12],metalTubeFV.Tvol[13],metalTubeFV.Tvol[14]) * Number of discrete variables: 36 ($cse4.phase,$cse4.region,$cse5.phase,$cse5.region,$cse6.phase,$cse6.region,$cse7.phase,$cse7.region,$cse8.phase,$cse8.region,$cse9.phase,$cse9.region,$cse10.phase,$cse10.region,$cse11.phase,$cse11.region,$cse12.phase,$cse12.region,$cse13.phase,$cse13.region,$cse14.phase,$cse14.region,$cse15.phase,$cse15.region,$cse16.phase,$cse16.region,$cse17.phase,$cse17.region,$cse18.phase,$cse18.region,$cse19.region3boundary,$cse20.region3boundary,$cse22.phase,$cse22.region,$cse23.region3boundary,$cse24.region3boundary) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (463): * Single equations (assignments): 424 * Array equations: 1 * Algorithm blocks: 0 * Record equations: 22 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 16 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 15 {(15,59.6%) 28,(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} * Non-linear torn systems: 1 {1 17} ThermoPower.Test.DistributedParameterComponents.TestWaterFlow1DFV2ph_A.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 451 * Number of variables: 451 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 15 * Number of states: 0 () * Number of discrete variables: 10 (hex.fluidState[10].phase,hex.fluidState[9].phase,hex.fluidState[8].phase,hex.fluidState[7].phase,hex.fluidState[6].phase,hex.fluidState[5].phase,hex.fluidState[4].phase,hex.fluidState[3].phase,hex.fluidState[2].phase,hex.fluidState[1].phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (141): * Single equations (assignments): 140 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {10 89} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 19 * Number of states: 11 (Mbal,hex.p,hex.htilde[1],hex.htilde[2],hex.htilde[3],hex.htilde[4],hex.htilde[5],hex.htilde[6],hex.htilde[7],hex.htilde[8],hex.htilde[9]) * Number of discrete variables: 22 ($cse2.phase,$cse2.region,$cse3.phase,$cse3.region,$cse4.phase,$cse4.region,$cse5.phase,$cse5.region,$cse6.phase,$cse6.region,$cse7.phase,$cse7.region,$cse8.phase,$cse8.region,$cse9.phase,$cse9.region,$cse10.phase,$cse10.region,$cse11.phase,$cse11.region,$cse12.region3boundary,$cse13.region3boundary) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (199): * Single equations (assignments): 185 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 13 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(10,64.0%) 18} * Non-linear torn systems: 0 ThermoPower.Test.DistributedParameterComponents.TestWaterFlow1DFV2ph_B.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 451 * Number of variables: 451 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 15 * Number of states: 0 () * Number of discrete variables: 10 (hex.fluidState[10].phase,hex.fluidState[9].phase,hex.fluidState[8].phase,hex.fluidState[7].phase,hex.fluidState[6].phase,hex.fluidState[5].phase,hex.fluidState[4].phase,hex.fluidState[3].phase,hex.fluidState[2].phase,hex.fluidState[1].phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (141): * Single equations (assignments): 140 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {10 89} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 21 * Number of states: 11 (Mbal,hex.p,hex.htilde[1],hex.htilde[2],hex.htilde[3],hex.htilde[4],hex.htilde[5],hex.htilde[6],hex.htilde[7],hex.htilde[8],hex.htilde[9]) * Number of discrete variables: 22 ($cse2.phase,$cse2.region,$cse3.phase,$cse3.region,$cse4.phase,$cse4.region,$cse5.phase,$cse5.region,$cse6.phase,$cse6.region,$cse7.phase,$cse7.region,$cse8.phase,$cse8.region,$cse9.phase,$cse9.region,$cse10.phase,$cse10.region,$cse11.phase,$cse11.region,$cse12.region3boundary,$cse13.region3boundary) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (199): * Single equations (assignments): 185 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 13 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(10,64.0%) 18} * Non-linear torn systems: 0 ThermoPower.Test.DistributedParameterComponents.TestWaterFlow1DFV2ph_C.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 852 * Number of variables: 852 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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. Warning: The initial conditions are over specified. The following 1 initial equations are redundant, so they are removed from the initialization sytem: $DER.hex.p = 0.0. Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 25 * Number of states: 0 () * Number of discrete variables: 20 (hex.fluidState[20].phase,hex.fluidState[19].phase,hex.fluidState[18].phase,hex.fluidState[17].phase,hex.fluidState[16].phase,hex.fluidState[15].phase,hex.fluidState[14].phase,hex.fluidState[13].phase,hex.fluidState[12].phase,hex.fluidState[11].phase,hex.fluidState[10].phase,hex.fluidState[9].phase,hex.fluidState[8].phase,hex.fluidState[7].phase,hex.fluidState[6].phase,hex.fluidState[5].phase,hex.fluidState[4].phase,hex.fluidState[3].phase,hex.fluidState[2].phase,hex.fluidState[1].phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (291): * Single equations (assignments): 271 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 1 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 19 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 19 {1 9,1 9,1 9,1 9,1 9,1 9,1 9,1 9,1 9,1 9,1 9,1 9,1 9,1 9,1 9,1 9,1 9,1 9,1 5} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 42 * Number of states: 20 (Mbal,hex.htilde[1],hex.htilde[2],hex.htilde[3],hex.htilde[4],hex.htilde[5],hex.htilde[6],hex.htilde[7],hex.htilde[8],hex.htilde[9],hex.htilde[10],hex.htilde[11],hex.htilde[12],hex.htilde[13],hex.htilde[14],hex.htilde[15],hex.htilde[16],hex.htilde[17],hex.htilde[18],hex.htilde[19]) * Number of discrete variables: 82 ($cse2.phase,$cse2.region,$cse3.phase,$cse3.region,$cse4.phase,$cse4.region,$cse5.phase,$cse5.region,$cse6.phase,$cse6.region,$cse7.phase,$cse7.region,$cse8.phase,$cse8.region,$cse9.phase,$cse9.region,$cse10.phase,$cse10.region,$cse11.phase,$cse11.region,$cse12.phase,$cse12.region,$cse13.phase,$cse13.region,$cse14.phase,$cse14.region,$cse15.phase,$cse15.region,$cse16.phase,$cse16.region,$cse17.phase,$cse17.region,$cse18.phase,$cse18.region,$cse19.phase,$cse19.region,$cse20.phase,$cse20.region,$cse21.phase,$cse21.region,$cse22.phase,$cse22.region,$cse23.phase,$cse23.region,$cse24.phase,$cse24.region,$cse25.phase,$cse25.region,$cse26.phase,$cse26.region,$cse27.phase,$cse27.region,$cse28.phase,$cse28.region,$cse29.phase,$cse29.region,$cse30.phase,$cse30.region,$cse31.phase,$cse31.region,$cse32.phase,$cse32.region,$cse33.phase,$cse33.region,$cse34.phase,$cse34.region,$cse35.phase,$cse35.region,$cse36.phase,$cse36.region,$cse37.phase,$cse37.region,$cse38.phase,$cse38.region,$cse39.phase,$cse39.region,$cse40.phase,$cse40.region,$cse41.phase,$cse41.region,$cse42.region3boundary,$cse43.region3boundary) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (380): * Single equations (assignments): 318 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 43 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 19 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 19 {(2,100.0%) 3,(2,100.0%) 3,(1,100.0%) 4,(2,100.0%) 3,(2,100.0%) 3,(2,100.0%) 3,(1,100.0%) 4,(2,100.0%) 3,(2,100.0%) 3,(2,100.0%) 3,(2,100.0%) 3,(2,100.0%) 3,(2,100.0%) 3,(1,100.0%) 4,(2,100.0%) 3,(1,100.0%) 4,(2,100.0%) 3,(1,100.0%) 4,(2,100.0%) 3} * Non-linear torn systems: 0 ThermoPower.Test.DistributedParameterComponents.TestWaterFlow1DFV2ph_D.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 451 * Number of variables: 451 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 15 * Number of states: 0 () * Number of discrete variables: 10 (hex.fluidState[10].phase,hex.fluidState[9].phase,hex.fluidState[8].phase,hex.fluidState[7].phase,hex.fluidState[6].phase,hex.fluidState[5].phase,hex.fluidState[4].phase,hex.fluidState[3].phase,hex.fluidState[2].phase,hex.fluidState[1].phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (141): * Single equations (assignments): 140 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {10 89} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 19 * Number of states: 11 (Mbal,hex.p,hex.htilde[1],hex.htilde[2],hex.htilde[3],hex.htilde[4],hex.htilde[5],hex.htilde[6],hex.htilde[7],hex.htilde[8],hex.htilde[9]) * Number of discrete variables: 22 ($cse2.phase,$cse2.region,$cse3.phase,$cse3.region,$cse4.phase,$cse4.region,$cse5.phase,$cse5.region,$cse6.phase,$cse6.region,$cse7.phase,$cse7.region,$cse8.phase,$cse8.region,$cse9.phase,$cse9.region,$cse10.phase,$cse10.region,$cse11.phase,$cse11.region,$cse12.region3boundary,$cse13.region3boundary) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (199): * Single equations (assignments): 185 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 13 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(10,64.0%) 18} * Non-linear torn systems: 0 ThermoPower.Test.DistributedParameterComponents.TestWaterFlow1DFV_A.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 762 * Number of variables: 762 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 26 * Number of states: 0 () * Number of discrete variables: 22 (T_out.fluidState.phase,T_in.fluidState.phase,hex.fluidState[20].phase,hex.fluidState[19].phase,hex.fluidState[18].phase,hex.fluidState[17].phase,hex.fluidState[16].phase,hex.fluidState[15].phase,hex.fluidState[14].phase,hex.fluidState[13].phase,hex.fluidState[12].phase,hex.fluidState[11].phase,hex.fluidState[10].phase,hex.fluidState[9].phase,hex.fluidState[8].phase,hex.fluidState[7].phase,hex.fluidState[6].phase,hex.fluidState[5].phase,hex.fluidState[4].phase,hex.fluidState[3].phase,hex.fluidState[2].phase,hex.fluidState[1].phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (166): * Single equations (assignments): 165 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {20 156} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 20 (hex.p,hex.htilde[1],hex.htilde[2],hex.htilde[3],hex.htilde[4],hex.htilde[5],hex.htilde[6],hex.htilde[7],hex.htilde[8],hex.htilde[9],hex.htilde[10],hex.htilde[11],hex.htilde[12],hex.htilde[13],hex.htilde[14],hex.htilde[15],hex.htilde[16],hex.htilde[17],hex.htilde[18],hex.htilde[19]) * Number of discrete variables: 44 ($cse2.phase,$cse2.region,$cse3.phase,$cse3.region,$cse4.phase,$cse4.region,$cse5.phase,$cse5.region,$cse6.phase,$cse6.region,$cse7.phase,$cse7.region,$cse8.phase,$cse8.region,$cse9.phase,$cse9.region,$cse10.phase,$cse10.region,$cse11.phase,$cse11.region,$cse12.phase,$cse12.region,$cse13.phase,$cse13.region,$cse14.phase,$cse14.region,$cse15.phase,$cse15.region,$cse16.phase,$cse16.region,$cse17.phase,$cse17.region,$cse18.phase,$cse18.region,$cse19.phase,$cse19.region,$cse20.phase,$cse20.region,$cse21.phase,$cse21.region,$cse23.phase,$cse23.region,$cse24.phase,$cse24.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (260): * Single equations (assignments): 237 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 22 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(20,57.2%) 38} * Non-linear torn systems: 0 ThermoPower.Test.DistributedParameterComponents.TestWaterFlow1DFV_A_Fast.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 636 * Number of variables: 636 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 82 * Number of states: 0 () * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (302): * Single equations (assignments): 283 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 19 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 19 {1 3,1 3,1 3,1 3,1 3,1 3,1 3,1 3,1 3,1 3,1 3,1 3,1 3,1 3,1 3,1 3,1 3,1 3,1 3} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 20 (hex.p,hex.htilde[1],hex.htilde[2],hex.htilde[3],hex.htilde[4],hex.htilde[5],hex.htilde[6],hex.htilde[7],hex.htilde[8],hex.htilde[9],hex.htilde[10],hex.htilde[11],hex.htilde[12],hex.htilde[13],hex.htilde[14],hex.htilde[15],hex.htilde[16],hex.htilde[17],hex.htilde[18],hex.htilde[19]) * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (200): * Single equations (assignments): 199 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(19,57.6%) 39} * Non-linear torn systems: 0 ThermoPower.Test.DistributedParameterComponents.TestWaterFlow1DFV_AdaptiveAverageTemp.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 208 * Number of variables: 208 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 10 * Number of states: 0 () * Number of discrete variables: 6 (hex.fluidState[4].phase,hex.fluidState[3].phase,hex.fluidState[2].phase,hex.fluidState[1].phase,T_out.fluidState.phase,T_in.fluidState.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (49): * Single equations (assignments): 48 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {4 41} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 4 (hex.p,hex.htilde[1],hex.htilde[2],hex.htilde[3]) * Number of discrete variables: 12 ($cse1.phase,$cse1.region,$cse3.phase,$cse3.region,$cse4.phase,$cse4.region,$cse6.phase,$cse6.region,$cse7.phase,$cse7.region,$cse8.phase,$cse8.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (77): * Single equations (assignments): 70 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 6 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(4,81.2%) 6} * Non-linear torn systems: 0 ThermoPower.Test.DistributedParameterComponents.TestWaterFlow1DFV_B.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 420 * Number of variables: 420 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 16 * Number of states: 0 () * Number of discrete variables: 12 (hex.fluidState[10].phase,hex.fluidState[9].phase,hex.fluidState[8].phase,hex.fluidState[7].phase,hex.fluidState[6].phase,hex.fluidState[5].phase,hex.fluidState[4].phase,hex.fluidState[3].phase,hex.fluidState[2].phase,hex.fluidState[1].phase,T_out.fluidState.phase,T_in.fluidState.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (77): * Single equations (assignments): 76 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {10 113} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 10 (hex.p,hex.htilde[1],hex.htilde[2],hex.htilde[3],hex.htilde[4],hex.htilde[5],hex.htilde[6],hex.htilde[7],hex.htilde[8],hex.htilde[9]) * Number of discrete variables: 24 ($cse1.phase,$cse1.region,$cse3.phase,$cse3.region,$cse4.phase,$cse4.region,$cse6.phase,$cse6.region,$cse7.phase,$cse7.region,$cse8.phase,$cse8.region,$cse9.phase,$cse9.region,$cse10.phase,$cse10.region,$cse11.phase,$cse11.region,$cse12.phase,$cse12.region,$cse13.phase,$cse13.region,$cse14.phase,$cse14.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (155): * Single equations (assignments): 142 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 12 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(10,64.0%) 18} * Non-linear torn systems: 0 ThermoPower.Test.DistributedParameterComponents.TestWaterFlow1DFV_D.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 216 * Number of variables: 216 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 11 * Number of states: 0 () * Number of discrete variables: 5 (hex.fluidState[5].phase,hex.fluidState[4].phase,hex.fluidState[3].phase,hex.fluidState[2].phase,hex.fluidState[1].phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (55): * Single equations (assignments): 54 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {5 37} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 5 (hex.p,hex.htilde[1],hex.htilde[2],hex.htilde[3],hex.htilde[4]) * Number of discrete variables: 10 ($cse2.phase,$cse2.region,$cse5.phase,$cse5.region,$cse6.phase,$cse6.region,$cse7.phase,$cse7.region,$cse8.phase,$cse8.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (68): * Single equations (assignments): 61 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 5 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 2 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 2 {(5,76.0%) 8,(1,100.0%) 1} * Non-linear torn systems: 0 ThermoPower.Test.DistributedParameterComponents.TestWaterFlow1DFV_DB.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 505 * Number of variables: 505 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 16 * Number of states: 0 () * Number of discrete variables: 12 (T_out.fluidState.phase,T_in.fluidState.phase,hexFV.fluidState[10].phase,hexFV.fluidState[9].phase,hexFV.fluidState[8].phase,hexFV.fluidState[7].phase,hexFV.fluidState[6].phase,hexFV.fluidState[5].phase,hexFV.fluidState[4].phase,hexFV.fluidState[3].phase,hexFV.fluidState[2].phase,hexFV.fluidState[1].phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (73): * Single equations (assignments): 72 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {10 202} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 10 (hexFV.p,hexFV.htilde[1],hexFV.htilde[2],hexFV.htilde[3],hexFV.htilde[4],hexFV.htilde[5],hexFV.htilde[6],hexFV.htilde[7],hexFV.htilde[8],hexFV.htilde[9]) * Number of discrete variables: 24 ($cse1.phase,$cse1.region,$cse3.phase,$cse3.region,$cse4.phase,$cse4.region,$cse5.phase,$cse5.region,$cse6.phase,$cse6.region,$cse7.phase,$cse7.region,$cse8.phase,$cse8.region,$cse9.phase,$cse9.region,$cse10.phase,$cse10.region,$cse11.phase,$cse11.region,$cse13.phase,$cse13.region,$cse14.phase,$cse14.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (240): * Single equations (assignments): 227 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 12 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(10,64.0%) 18} * Non-linear torn systems: 0 ThermoPower.Test.DistributedParameterComponents.TestWaterFlow1DFV_E.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 1552 * Number of variables: 1552 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 56 * Number of states: 0 () * Number of discrete variables: 44 (hexFVa.fluidState[20].phase,hexFVa.fluidState[19].phase,hexFVa.fluidState[18].phase,hexFVa.fluidState[17].phase,hexFVa.fluidState[16].phase,hexFVa.fluidState[15].phase,hexFVa.fluidState[14].phase,hexFVa.fluidState[13].phase,hexFVa.fluidState[12].phase,hexFVa.fluidState[11].phase,hexFVa.fluidState[10].phase,hexFVa.fluidState[9].phase,hexFVa.fluidState[8].phase,hexFVa.fluidState[7].phase,hexFVa.fluidState[6].phase,hexFVa.fluidState[5].phase,hexFVa.fluidState[4].phase,hexFVa.fluidState[3].phase,hexFVa.fluidState[2].phase,hexFVa.fluidState[1].phase,hexFVb.fluidState[20].phase,hexFVb.fluidState[19].phase,hexFVb.fluidState[18].phase,hexFVb.fluidState[17].phase,hexFVb.fluidState[16].phase,hexFVb.fluidState[15].phase,hexFVb.fluidState[14].phase,hexFVb.fluidState[13].phase,hexFVb.fluidState[12].phase,hexFVb.fluidState[11].phase,hexFVb.fluidState[10].phase,hexFVb.fluidState[9].phase,hexFVb.fluidState[8].phase,hexFVb.fluidState[7].phase,hexFVb.fluidState[6].phase,hexFVb.fluidState[5].phase,hexFVb.fluidState[4].phase,hexFVb.fluidState[3].phase,hexFVb.fluidState[2].phase,hexFVb.fluidState[1].phase,SensT_B_out.fluidState.phase,SensT_A_out.fluidState.phase,SensT_B_in.fluidState.phase,SensT_A_in.fluidState.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (246): * Single equations (assignments): 245 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {40 466} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 40 (hexFVb.p,hexFVb.htilde[1],hexFVb.htilde[2],hexFVb.htilde[3],hexFVb.htilde[4],hexFVb.htilde[5],hexFVb.htilde[6],hexFVb.htilde[7],hexFVb.htilde[8],hexFVb.htilde[9],hexFVb.htilde[10],hexFVb.htilde[11],hexFVb.htilde[12],hexFVb.htilde[13],hexFVb.htilde[14],hexFVb.htilde[15],hexFVb.htilde[16],hexFVb.htilde[17],hexFVb.htilde[18],hexFVb.htilde[19],hexFVa.p,hexFVa.htilde[1],hexFVa.htilde[2],hexFVa.htilde[3],hexFVa.htilde[4],hexFVa.htilde[5],hexFVa.htilde[6],hexFVa.htilde[7],hexFVa.htilde[8],hexFVa.htilde[9],hexFVa.htilde[10],hexFVa.htilde[11],hexFVa.htilde[12],hexFVa.htilde[13],hexFVa.htilde[14],hexFVa.htilde[15],hexFVa.htilde[16],hexFVa.htilde[17],hexFVa.htilde[18],hexFVa.htilde[19]) * Number of discrete variables: 88 ($cse1.phase,$cse1.region,$cse2.phase,$cse2.region,$cse3.phase,$cse3.region,$cse4.phase,$cse4.region,$cse5.phase,$cse5.region,$cse6.phase,$cse6.region,$cse7.phase,$cse7.region,$cse8.phase,$cse8.region,$cse9.phase,$cse9.region,$cse10.phase,$cse10.region,$cse11.phase,$cse11.region,$cse12.phase,$cse12.region,$cse13.phase,$cse13.region,$cse14.phase,$cse14.region,$cse15.phase,$cse15.region,$cse16.phase,$cse16.region,$cse17.phase,$cse17.region,$cse18.phase,$cse18.region,$cse19.phase,$cse19.region,$cse20.phase,$cse20.region,$cse21.phase,$cse21.region,$cse22.phase,$cse22.region,$cse23.phase,$cse23.region,$cse24.phase,$cse24.region,$cse27.phase,$cse27.region,$cse28.phase,$cse28.region,$cse29.phase,$cse29.region,$cse30.phase,$cse30.region,$cse31.phase,$cse31.region,$cse32.phase,$cse32.region,$cse33.phase,$cse33.region,$cse34.phase,$cse34.region,$cse35.phase,$cse35.region,$cse36.phase,$cse36.region,$cse37.phase,$cse37.region,$cse38.phase,$cse38.region,$cse39.phase,$cse39.region,$cse40.phase,$cse40.region,$cse41.phase,$cse41.region,$cse42.phase,$cse42.region,$cse43.phase,$cse43.region,$cse44.phase,$cse44.region,$cse45.phase,$cse45.region,$cse46.phase,$cse46.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (560): * Single equations (assignments): 495 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 44 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 21 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 21 {(20,57.2%) 38,(20,57.2%) 38,(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} * Non-linear torn systems: 0 ThermoPower.Test.DistributedParameterComponents.TestWaterFlow1DFV_F.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 1647 * Number of variables: 1647 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 56 * Number of states: 0 () * Number of discrete variables: 44 (hexFVa.fluidState[20].phase,hexFVa.fluidState[19].phase,hexFVa.fluidState[18].phase,hexFVa.fluidState[17].phase,hexFVa.fluidState[16].phase,hexFVa.fluidState[15].phase,hexFVa.fluidState[14].phase,hexFVa.fluidState[13].phase,hexFVa.fluidState[12].phase,hexFVa.fluidState[11].phase,hexFVa.fluidState[10].phase,hexFVa.fluidState[9].phase,hexFVa.fluidState[8].phase,hexFVa.fluidState[7].phase,hexFVa.fluidState[6].phase,hexFVa.fluidState[5].phase,hexFVa.fluidState[4].phase,hexFVa.fluidState[3].phase,hexFVa.fluidState[2].phase,hexFVa.fluidState[1].phase,hexFVb.fluidState[20].phase,hexFVb.fluidState[19].phase,hexFVb.fluidState[18].phase,hexFVb.fluidState[17].phase,hexFVb.fluidState[16].phase,hexFVb.fluidState[15].phase,hexFVb.fluidState[14].phase,hexFVb.fluidState[13].phase,hexFVb.fluidState[12].phase,hexFVb.fluidState[11].phase,hexFVb.fluidState[10].phase,hexFVb.fluidState[9].phase,hexFVb.fluidState[8].phase,hexFVb.fluidState[7].phase,hexFVb.fluidState[6].phase,hexFVb.fluidState[5].phase,hexFVb.fluidState[4].phase,hexFVb.fluidState[3].phase,hexFVb.fluidState[2].phase,hexFVb.fluidState[1].phase,SensT_B_out.fluidState.phase,SensT_A_out.fluidState.phase,SensT_B_in.fluidState.phase,SensT_A_in.fluidState.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (284): * Single equations (assignments): 283 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {40 523} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 59 (hexFVb.p,hexFVb.htilde[1],hexFVb.htilde[2],hexFVb.htilde[3],hexFVb.htilde[4],hexFVb.htilde[5],hexFVb.htilde[6],hexFVb.htilde[7],hexFVb.htilde[8],hexFVb.htilde[9],hexFVb.htilde[10],hexFVb.htilde[11],hexFVb.htilde[12],hexFVb.htilde[13],hexFVb.htilde[14],hexFVb.htilde[15],hexFVb.htilde[16],hexFVb.htilde[17],hexFVb.htilde[18],hexFVb.htilde[19],hexFVa.p,hexFVa.htilde[1],hexFVa.htilde[2],hexFVa.htilde[3],hexFVa.htilde[4],hexFVa.htilde[5],hexFVa.htilde[6],hexFVa.htilde[7],hexFVa.htilde[8],hexFVa.htilde[9],hexFVa.htilde[10],hexFVa.htilde[11],hexFVa.htilde[12],hexFVa.htilde[13],hexFVa.htilde[14],hexFVa.htilde[15],hexFVa.htilde[16],hexFVa.htilde[17],hexFVa.htilde[18],hexFVa.htilde[19],metalTubeFV.Tvol[1],metalTubeFV.Tvol[2],metalTubeFV.Tvol[3],metalTubeFV.Tvol[4],metalTubeFV.Tvol[5],metalTubeFV.Tvol[6],metalTubeFV.Tvol[7],metalTubeFV.Tvol[8],metalTubeFV.Tvol[9],metalTubeFV.Tvol[10],metalTubeFV.Tvol[11],metalTubeFV.Tvol[12],metalTubeFV.Tvol[13],metalTubeFV.Tvol[14],metalTubeFV.Tvol[15],metalTubeFV.Tvol[16],metalTubeFV.Tvol[17],metalTubeFV.Tvol[18],metalTubeFV.Tvol[19]) * Number of discrete variables: 88 ($cse1.phase,$cse1.region,$cse2.phase,$cse2.region,$cse3.phase,$cse3.region,$cse4.phase,$cse4.region,$cse5.phase,$cse5.region,$cse6.phase,$cse6.region,$cse7.phase,$cse7.region,$cse8.phase,$cse8.region,$cse9.phase,$cse9.region,$cse10.phase,$cse10.region,$cse11.phase,$cse11.region,$cse12.phase,$cse12.region,$cse13.phase,$cse13.region,$cse14.phase,$cse14.region,$cse15.phase,$cse15.region,$cse16.phase,$cse16.region,$cse17.phase,$cse17.region,$cse18.phase,$cse18.region,$cse19.phase,$cse19.region,$cse20.phase,$cse20.region,$cse21.phase,$cse21.region,$cse22.phase,$cse22.region,$cse23.phase,$cse23.region,$cse24.phase,$cse24.region,$cse27.phase,$cse27.region,$cse28.phase,$cse28.region,$cse29.phase,$cse29.region,$cse30.phase,$cse30.region,$cse31.phase,$cse31.region,$cse32.phase,$cse32.region,$cse33.phase,$cse33.region,$cse34.phase,$cse34.region,$cse35.phase,$cse35.region,$cse36.phase,$cse36.region,$cse37.phase,$cse37.region,$cse38.phase,$cse38.region,$cse39.phase,$cse39.region,$cse40.phase,$cse40.region,$cse41.phase,$cse41.region,$cse42.phase,$cse42.region,$cse43.phase,$cse43.region,$cse44.phase,$cse44.region,$cse45.phase,$cse45.region,$cse46.phase,$cse46.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (617): * Single equations (assignments): 533 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 44 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 40 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 40 {(20,57.2%) 38,(20,57.2%) 38,(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} * Non-linear torn systems: 0 ThermoPower.Test.ElectricalComponents.TestElectrical1.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 29 * Number of variables: 29 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: Assuming fixed start value for the following 1 variables: turboGenInertia.phi:VARIABLE(unit = "rad" ) "Absolute rotation angle of component" type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 4 * Number of states: 0 () * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (14): * Single equations (assignments): 14 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 0 * Mixed (continuous/discrete) equation systems: 0 Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 2 (turboGenInertia.phi,turboGenInertia.w) * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (11): * Single equations (assignments): 11 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 ThermoPower.Test.ElectricalComponents.TestElectrical2.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 38 * Number of variables: 38 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: Assuming fixed start value for the following 1 variables: turboGenInertia.phi:VARIABLE(unit = "rad" ) "Absolute rotation angle of component" type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 4 * Number of states: 0 () * Number of discrete variables: 1 (Breaker1.closed) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (18): * Single equations (assignments): 17 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(1,100.0%) 1} * Non-linear torn systems: 0 Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 2 (turboGenInertia.phi,turboGenInertia.w) * Number of discrete variables: 1 (Breaker1.closed) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (15): * Single equations (assignments): 14 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(1,100.0%) 1} * Non-linear torn systems: 0 ThermoPower.Test.ElectricalComponents.TestN2GControl.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 82 * Number of variables: 82 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: Assuming fixed start value for the following 3 variables: generator_b.shaft.phi:VARIABLE(flow=false unit = "rad" ) "Absolute rotation angle of flange" type: Real generator_a.shaft.phi:VARIABLE(flow=false unit = "rad" ) "Absolute rotation angle of flange" type: Real network.delta_b:VARIABLE(unit = "rad" ) "Phase B" type: Real Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: load_a.f:VARIABLE(unit = "Hz" ) "Frequency" type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 9 * Number of states: 0 () * Number of discrete variables: 2 (network.closedInternal_gen_b,network.closedInternal_gen_a) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (33): * Single equations (assignments): 31 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 1 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 1 {1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {1 26} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 8 (network.delta_b,network.delta_ab,generator_a.omega_m,generator_a.shaft.phi,generator_b.omega_m,generator_b.shaft.phi,filter_a.y,filter_b.y) * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (46): * Single equations (assignments): 46 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 ThermoPower.Test.ElectricalComponents.TestNetworkGridGenerator_Pmax.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 47 * Number of variables: 47 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: Assuming fixed start value for the following 1 variables: damper.phi_rel:VARIABLE(start = 0.0 unit = "rad" nominal = if damper.phi_nominal >= 1e-15 then damper.phi_nominal else 1.0 stateSelect=StateSelect.prefer ) "Relative rotation angle (= flange_b.phi - flange_a.phi)" type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 3 * Number of states: 0 () * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (33): * Single equations (assignments): 32 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 1 * Torn equation systems: 0 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 1 {1} * Without analytic Jacobian: 0 Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 4 * Number of states: 3 (network.delta,damper.phi_rel,damper.w_rel) * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (23): * Single equations (assignments): 22 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(1,100.0%) 4} * Non-linear torn systems: 0 ThermoPower.Test.ElectricalComponents.TestNetworkGridTwoGenerators.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 60 * Number of variables: 60 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: Assuming fixed start value for the following 3 variables: gen_b.shaft.phi:VARIABLE(flow=false unit = "rad" ) "Absolute rotation angle of flange" type: Real gen_a.shaft.phi:VARIABLE(flow=false unit = "rad" ) "Absolute rotation angle of flange" type: Real network.delta_a:VARIABLE(unit = "rad" ) "Phase A" type: Real Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: network.delta_bg:DUMMY_STATE(unit = "rad" ) "Load angle between generator side B and the grid" type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 8 * Number of states: 0 () * Number of discrete variables: 3 (network.closedInternal_grid,network.closedInternal_gen_b,network.closedInternal_gen_a) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (51): * Single equations (assignments): 50 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {2 4} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 2 * Number of states: 7 (network.delta_a,network.delta_ab,network.delta_ag,gen_a.omega_m,gen_a.shaft.phi,gen_b.omega_m,gen_b.shaft.phi) * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (44): * Single equations (assignments): 44 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 ThermoPower.Test.GasComponents.TestCC.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 289 * Number of variables: 289 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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. Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: CombustionChamber1.M:DUMMY_STATE(min = 0.0 unit = "kg" ) "Gas total mass" type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 17 * Number of states: 0 () * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (65): * Single equations (assignments): 63 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 1 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 1 {1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {10 32} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 5 * Number of states: 7 (CombustionChamber1.fluegas.p,CombustionChamber1.fluegas.Xi[2],CombustionChamber1.fluegas.Xi[3],CombustionChamber1.fluegas.Xi[4],CombustionChamber1.fluegas.Xi[5],CombustionChamber1.fluegas.T,CombustionChamber1.fluegas.R) * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (70): * Single equations (assignments): 67 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 1 * Torn equation systems: 2 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 1 {1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(1,100.0%) 1} * Non-linear torn systems: 1 {2 11} ThermoPower.Test.GasComponents.TestCompressorConstSpeed.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 128 * Number of variables: 128 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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. Warning: Assuming fixed start value for the following 1 variables: ConstantSpeed1.phi:VARIABLE(unit = "rad" ) "Angle of flange with respect to support (= flange.phi - support.phi)" type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 21 * Number of states: 0 () * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (48): * Single equations (assignments): 43 * Array equations: 0 * Algorithm blocks: 3 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 2 * Torn equation systems: 0 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 2 {1,1} * Without analytic Jacobian: 0 Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 1 (ConstantSpeed1.phi) * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (13): * Single equations (assignments): 11 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 2 * Torn equation systems: 0 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 2 {1,1} * Without analytic Jacobian: 0 ThermoPower.Test.GasComponents.TestCompressorInertia.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 130 * Number of variables: 130 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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. Warning: Assuming fixed start value for the following 1 variables: Compressor.phi:VARIABLE(unit = "rad" ) "shaft rotation angle" type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 16 * Number of states: 0 () * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (50): * Single equations (assignments): 44 * Array equations: 0 * Algorithm blocks: 3 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 3 * Torn equation systems: 0 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 3 {1,1,1} * Without analytic Jacobian: 0 Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 2 (Inertia1.w,Compressor.phi) * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (20): * Single equations (assignments): 17 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 3 * Torn equation systems: 0 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 3 {1,1,1} * Without analytic Jacobian: 0 ThermoPower.Test.GasComponents.TestFanMech.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 136 * Number of variables: 136 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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. Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: FanMech1.s:VARIABLE() "Auxiliary Variable" type: Real Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: Clutch1.sa:VARIABLE(unit = "1" ) "Path parameter of friction characteristic tau = f(a_relfric)" type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 24 * Number of states: 0 () * Number of discrete variables: 8 (Clutch1.free,$PRE.Clutch1.startForward,Clutch1.startForward,$PRE.Clutch1.startBackward,Clutch1.startBackward,Clutch1.locked,$PRE.Clutch1.mode,Clutch1.mode) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (65): * Single equations (assignments): 62 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 1 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 2 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 2 {1 6,4 10} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 3 (ConstantSpeed1.phi,Clutch1.phi_rel,Clutch1.w_rel) * Number of discrete variables: 5 (Clutch1.free,Clutch1.startForward,Clutch1.startBackward,Clutch1.locked,Clutch1.mode) * Number of discrete states: 3 (Clutch1.mode,Clutch1.startBackward,Clutch1.startForward) * Top-level inputs: 0 Notification: Strong component statistics for simulation (33): * Single equations (assignments): 31 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 2 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 2 {1 5,2 12} ThermoPower.Test.GasComponents.TestGT.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 226 * Number of variables: 226 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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. Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: GTunit.tau:VARIABLE(unit = "N.m" ) "net torque acting on the turbine" type: Real GTunit.ZLPout:VARIABLE(unit = "W" ) "zero_loss power output" type: Real Inertia.w:VARIABLE(unit = "rad/s" ) "Absolute angular velocity of component (= der(phi))" type: Real GTunit.ZLPout_ISO:VARIABLE(unit = "W" ) "zero_loss power output, referred to ISO conditions " type: Real Generator.Pe:VARIABLE(unit = "W" ) "Electrical Power" type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 29 * Number of states: 0 () * Number of discrete variables: 1 (BooleanStep1.y) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (66): * Single equations (assignments): 61 * Array equations: 0 * Algorithm blocks: 3 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 1 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 1 {1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {5 9} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 2 (Inertia.phi,Inertia.w) * Number of discrete variables: 1 (BooleanStep1.y) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (33): * Single equations (assignments): 30 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 2 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 2 {1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(1,100.0%) 1} * Non-linear torn systems: 0 ThermoPower.Test.GasComponents.TestGT_ISO.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 234 * Number of variables: 234 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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. Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: GT.ZLPout_ISO:VARIABLE(unit = "W" ) "zero_loss power output, referred to ISO conditions " type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 28 * Number of states: 0 () * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (63): * Single equations (assignments): 60 * Array equations: 0 * Algorithm blocks: 1 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 1 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 1 {1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {4 11} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 1 (ConstantSpeed1.phi) * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (24): * Single equations (assignments): 22 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 1 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 1 {1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {4 11} ThermoPower.Test.GasComponents.TestGasMixer.err [ThermoPower 3.1/Gas.mo:766:38-766:68:writable] Warning: Non-array modification 'StateSelect.prefer' for array component, possibly due to missing 'each'. Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 200 * Number of variables: 200 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 9 * Number of states: 0 () * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (53): * Single equations (assignments): 52 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {8 35} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 5 * Number of states: 4 (Mixer1.gas.p,Mixer1.gas.Xi[1],Mixer1.gas.Xi[2],Mixer1.gas.T) * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (61): * Single equations (assignments): 58 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 1 * Torn equation systems: 2 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 1 {1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(1,100.0%) 1} * Non-linear torn systems: 1 {3 14} ThermoPower.Test.GasComponents.TestGasTurbine.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 126 * Number of variables: 126 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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. Warning: Assuming fixed start value for the following 1 variables: Inertia1.phi:VARIABLE(unit = "rad" ) "Absolute rotation angle of component" type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 20 * Number of states: 0 () * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (49): * Single equations (assignments): 46 * Array equations: 0 * Algorithm blocks: 2 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 1 * Torn equation systems: 0 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 1 {1} * Without analytic Jacobian: 0 Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 2 (Inertia1.phi,Inertia1.w) * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (14): * Single equations (assignments): 13 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 1 * Torn equation systems: 0 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 1 {1} * Without analytic Jacobian: 0 ThermoPower.Test.GasComponents.TestGasTurbineStodola.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 128 * Number of variables: 128 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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. Warning: Assuming fixed start value for the following 1 variables: ConstantSpeed1.phi:VARIABLE(unit = "rad" ) "Angle of flange with respect to support (= flange.phi - support.phi)" type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 21 * Number of states: 0 () * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (49): * Single equations (assignments): 47 * Array equations: 0 * Algorithm blocks: 1 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 1 * Torn equation systems: 0 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 1 {1} * Without analytic Jacobian: 0 Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 4 * Number of states: 1 (ConstantSpeed1.phi) * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (16): * Single equations (assignments): 15 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 1 * Torn equation systems: 0 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 1 {1} * Without analytic Jacobian: 0 ThermoPower.Test.GasComponents.TestGasValve.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 424 * Number of variables: 424 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 58 * Number of states: 0 () * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (142): * Single equations (assignments): 133 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 7 * Torn equation systems: 2 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 7 {1,1,1,1,1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 2 {2 18,2 18} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 15 * Number of states: 0 () * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (75): * Single equations (assignments): 66 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 7 * Torn equation systems: 2 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 7 {1,1,1,1,1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 2 {2 20,2 21} ThermoPower.Test.GasComponents.TestGasValveOpPoint.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 340 * Number of variables: 340 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 18 * Number of states: 0 () * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (86): * Single equations (assignments): 80 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 4 * Torn equation systems: 2 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 4 {1,1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 2 {1 12,1 12} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 7 * Number of states: 0 () * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (46): * Single equations (assignments): 40 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 4 * Torn equation systems: 2 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 4 {1,1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 2 {1 13,1 14} ThermoPower.Test.GasComponents.TestTurboJetConstSpeed.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 455 * Number of variables: 455 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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. Warning: Assuming fixed start value for the following 1 variables: ConstantSpeed1.phi:VARIABLE(unit = "rad" ) "Angle of flange with respect to support (= flange.phi - support.phi)" type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 36 * Number of states: 0 () * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (117): * Single equations (assignments): 110 * Array equations: 0 * Algorithm blocks: 5 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 1 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 1 {1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {14 51} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 2 * Number of states: 9 (CombustionChamber1.fluegas.p,CombustionChamber1.fluegas.Xi[2],CombustionChamber1.fluegas.Xi[3],CombustionChamber1.fluegas.Xi[4],CombustionChamber1.fluegas.Xi[5],CombustionChamber1.fluegas.T,CombustionChamber1.fluegas.R,CombustionChamber1.Tm,ConstantSpeed1.phi) * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (88): * Single equations (assignments): 83 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 2 * Torn equation systems: 3 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 2 {1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(1,100.0%) 1} * Non-linear torn systems: 2 {3 15,3 12} ThermoPower.Test.GasComponents.TestTurboJetInertia.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 489 * Number of variables: 489 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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. Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: Turbine1.tau:VARIABLE(unit = "N.m" ) "net torque acting on the turbine" type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 35 * Number of states: 0 () * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (126): * Single equations (assignments): 120 * Array equations: 0 * Algorithm blocks: 4 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 1 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 1 {1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {17 58} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 10 (CombustionChamber1.fluegas.p,CombustionChamber1.fluegas.Xi[2],CombustionChamber1.fluegas.Xi[3],CombustionChamber1.fluegas.Xi[4],CombustionChamber1.fluegas.Xi[5],CombustionChamber1.fluegas.T,CombustionChamber1.fluegas.R,CombustionChamber1.Tm,Inertia1.phi,Inertia1.w) * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (93): * Single equations (assignments): 88 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 2 * Torn equation systems: 3 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 2 {1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(1,100.0%) 1} * Non-linear torn systems: 2 {5 24,3 12} ThermoPower.Test.WaterComponents.TestAccumulator.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 62 * Number of variables: 62 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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. Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: $DER.Accumulator1.Vg:DUMMY_DER(fixed = false ) "Volume occupied by gas" type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 2 * Number of states: 0 () * Number of discrete variables: 1 (Accumulator1.liquidState.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (19): * Single equations (assignments): 18 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {6 14} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 4 (Accumulator1.zl,Accumulator1.hl,Accumulator1.rhog,Accumulator1.Tg) * Number of discrete variables: 2 ($cse1.phase,$cse1.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (32): * Single equations (assignments): 30 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 1 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(2,100.0%) 1} * Non-linear torn systems: 0 ThermoPower.Test.WaterComponents.TestBarometricCondenser.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 89 * Number of variables: 89 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or nominal values. It is recommended to resolve the conflicts, because otherwise the system could be hard to solve. To print the conflicting alias sets and the chosen candidates please use -d=aliasConflicts. Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 9 * Number of states: 0 () * Number of discrete variables: 15 ($whenCondition1,$whenCondition2,steamFlowRate.a,steamFlowRate.b,steamFlowRate.last,$PRE.steamFlowRate.nextEvent,steamFlowRate.nextEvent,steamFlowRate.nextEventScaled,coolingFlowRate.a,coolingFlowRate.b,coolingFlowRate.last,$PRE.coolingFlowRate.nextEvent,coolingFlowRate.nextEvent,coolingFlowRate.nextEventScaled,tank.liquidState.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (36): * Single equations (assignments): 32 * Array equations: 0 * Algorithm blocks: 2 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 2 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 2 {1 1,2 2} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 3 (barometricCondenser.hl,tank.y,tank.h) * Number of discrete variables: 21 ($cse1.phase,$cse1.region,$cse2.phase,$cse3.phase,$cse4.phase,$cse5.phase,$cse5.region,$cse6.phase,$cse6.region,$whenCondition1,$whenCondition2,steamFlowRate.a,steamFlowRate.b,steamFlowRate.last,steamFlowRate.nextEvent,steamFlowRate.nextEventScaled,coolingFlowRate.a,coolingFlowRate.b,coolingFlowRate.last,coolingFlowRate.nextEvent,coolingFlowRate.nextEventScaled) * Number of discrete states: 12 (coolingFlowRate.nextEvent,coolingFlowRate.last,coolingFlowRate.nextEventScaled,coolingFlowRate.b,coolingFlowRate.a,$whenCondition2,steamFlowRate.nextEvent,steamFlowRate.last,steamFlowRate.nextEventScaled,steamFlowRate.b,steamFlowRate.a,$whenCondition1) * Top-level inputs: 0 Notification: Strong component statistics for simulation (30): * Single equations (assignments): 21 * Array equations: 0 * Algorithm blocks: 2 * Record equations: 5 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 2 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 2 {1 2,1 1} ThermoPower.Test.WaterComponents.TestCoeffValve.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 124 * Number of variables: 124 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 12 * Number of states: 0 () * Number of discrete variables: 4 (ValveLiq4.fluidState.phase,ValveLiq3.fluidState.phase,ValveLiq2.fluidState.phase,ValveLiq1.fluidState.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (23): * Single equations (assignments): 23 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 0 * Mixed (continuous/discrete) equation systems: 0 Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 2 * Number of states: 0 () * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (4): * Single equations (assignments): 4 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 ThermoPower.Test.WaterComponents.TestCoolingTower.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 234 * Number of variables: 234 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 1 * Number of states: 0 () * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (102): * Single equations (assignments): 101 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {36 117} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 6 * Number of states: 27 (coolingTower.M[1],coolingTower.M[2],coolingTower.M[3],coolingTower.M[4],coolingTower.M[5],coolingTower.M[6],coolingTower.M[7],coolingTower.M[8],coolingTower.M[9],coolingTower.hltilde[1],coolingTower.hltilde[2],coolingTower.hltilde[3],coolingTower.hltilde[4],coolingTower.hltilde[5],coolingTower.hltilde[6],coolingTower.hltilde[7],coolingTower.hltilde[8],coolingTower.hltilde[9],coolingTower.Tp[1],coolingTower.Tp[2],coolingTower.Tp[3],coolingTower.Tp[4],coolingTower.Tp[5],coolingTower.Tp[6],coolingTower.Tp[7],coolingTower.Tp[8],coolingTower.Tp[9]) * Number of discrete variables: 18 ($cse6.phase,$cse6.region,$cse12.phase,$cse12.region,$cse18.phase,$cse18.region,$cse24.phase,$cse24.region,$cse30.phase,$cse30.region,$cse36.phase,$cse36.region,$cse42.phase,$cse42.region,$cse48.phase,$cse48.region,$cse54.phase,$cse54.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (211): * Single equations (assignments): 166 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 27 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 18 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 9 {(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} * Non-linear torn systems: 9 {2 5,2 5,2 5,2 5,2 5,2 5,2 5,2 5,2 5} ThermoPower.Test.WaterComponents.TestCoolingTowerStatic.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 234 * Number of variables: 234 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 10 * Number of states: 0 () * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (57): * Single equations (assignments): 56 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {36 108} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 6 * Number of states: 0 () * Number of discrete variables: 18 ($cse6.phase,$cse6.region,$cse12.phase,$cse12.region,$cse18.phase,$cse18.region,$cse24.phase,$cse24.region,$cse30.phase,$cse30.region,$cse36.phase,$cse36.region,$cse42.phase,$cse42.region,$cse48.phase,$cse48.region,$cse54.phase,$cse54.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (50): * Single equations (assignments): 49 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {36 153} ThermoPower.Test.WaterComponents.TestJoin.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 162 * Number of variables: 162 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 10 * Number of states: 0 () * Number of discrete variables: 6 (T6.fluidState.phase,T5.fluidState.phase,T4.fluidState.phase,T3.fluidState.phase,T2.fluidState.phase,T1.fluidState.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (40): * Single equations (assignments): 40 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 0 * Mixed (continuous/discrete) equation systems: 0 Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 0 () * Number of discrete variables: 12 ($cse1.phase,$cse1.region,$cse2.phase,$cse2.region,$cse3.phase,$cse3.region,$cse4.phase,$cse4.region,$cse5.phase,$cse5.region,$cse6.phase,$cse6.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (38): * Single equations (assignments): 32 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 6 * When equations: 0 ThermoPower.Test.WaterComponents.TestJoinRev.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 166 * Number of variables: 166 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 8 * Number of states: 0 () * Number of discrete variables: 26 ($whenCondition2,$whenCondition1,$PRE.Sine1.T_start,Sine1.T_start,$PRE.Sine1.count,Sine1.count,$PRE.Sine2.T_start,Sine2.T_start,$PRE.Sine2.count,Sine2.count,T6.fluidState.phase,T5.fluidState.phase,T4.fluidState.phase,T3.fluidState.phase,T2.fluidState.phase,T1.fluidState.phase,$whenCondition4,$whenCondition3,$PRE.Sine3.T_start,Sine3.T_start,$PRE.Sine3.count,Sine3.count,$PRE.Sine4.T_start,Sine4.T_start,$PRE.Sine4.count,Sine4.count) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (54): * Single equations (assignments): 50 * Array equations: 0 * Algorithm blocks: 4 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 0 * Mixed (continuous/discrete) equation systems: 0 Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 2 * Number of states: 0 () * Number of discrete variables: 24 ($cse1.phase,$cse1.region,$cse2.phase,$cse2.region,$cse3.phase,$cse3.region,$whenCondition2,$whenCondition1,Sine1.T_start,Sine1.count,Sine2.T_start,Sine2.count,$cse4.phase,$cse4.region,$cse5.phase,$cse5.region,$cse6.phase,$cse6.region,$whenCondition4,$whenCondition3,Sine3.T_start,Sine3.count,Sine4.T_start,Sine4.count) * Number of discrete states: 4 (Sine3.count,Sine4.count,Sine1.count,Sine2.count) * Top-level inputs: 0 Notification: Strong component statistics for simulation (48): * Single equations (assignments): 34 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 6 * When equations: 8 ThermoPower.Test.WaterComponents.TestMixer.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 119 * Number of variables: 119 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 6 * Number of states: 0 () * Number of discrete variables: 3 (header.fluidState.phase,pressDrop.state.phase,mixer.fluidState.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (22): * Single equations (assignments): 20 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 2 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 2 {3 13,2 7} Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 4 (mixer.p,mixer.h,header.p,header.h) * Number of discrete variables: 4 ($cse3.phase,$cse3.region,$cse6.phase,$cse6.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (36): * Single equations (assignments): 31 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 2 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 1 * Torn equation systems: 2 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 1 {2} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(1,100.0%) 1} * Non-linear torn systems: 1 {1 2} ThermoPower.Test.WaterComponents.TestMixerSlowFast.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 99 * Number of variables: 99 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 6 * Number of states: 0 () * Number of discrete variables: 3 (Header1.fluidState.phase,PressDrop1.state.phase,Mixer1.fluidState.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (22): * Single equations (assignments): 21 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {5 19} Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 4 (Mixer1.p,Mixer1.h,Header1.p,Header1.h) * Number of discrete variables: 4 ($cse3.phase,$cse3.region,$cse5.phase,$cse5.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (38): * Single equations (assignments): 33 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 2 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 2 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 2 {2,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(1,100.0%) 1} * Non-linear torn systems: 0 ThermoPower.Test.WaterComponents.TestMixerSlowFastSteam.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 99 * Number of variables: 99 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 6 * Number of states: 0 () * Number of discrete variables: 3 (Header1.fluidState.phase,PressDrop1.state.phase,Mixer1.fluidState.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (22): * Single equations (assignments): 21 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {5 19} Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 4 (Mixer1.p,Mixer1.h,Header1.p,Header1.h) * Number of discrete variables: 4 ($cse3.phase,$cse3.region,$cse5.phase,$cse5.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (38): * Single equations (assignments): 33 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 2 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 2 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 2 {2,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(1,100.0%) 1} * Non-linear torn systems: 0 ThermoPower.Test.WaterComponents.TestST1.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 75 * Number of variables: 75 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 7 * Number of states: 0 () * Number of discrete variables: 2 (SensT1.fluidState.phase,ST.fluidState_in.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (26): * Single equations (assignments): 24 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 2 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(1,100.0%) 2} * Non-linear torn systems: 1 {1 3} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 4 (ST.P_HP,ST.P_LP,Inertia1.phi,Inertia1.w) * Number of discrete variables: 6 ($cse2.phase,$cse2.region,$cse3.phase,$cse3.region,$cse4.phase,$cse4.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (22): * Single equations (assignments): 18 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 3 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(1,100.0%) 1} * Non-linear torn systems: 0 ThermoPower.Test.WaterComponents.TestST2.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 65 * Number of variables: 65 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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. Warning: It was not possible to determine if the initialization problem is consistent, because of not evaluable parameters/start values during compile time: Inertia1.a = $START.Inertia1.a (0.0 = $START.Inertia1.a) Warning: The initial conditions are over specified. The following 1 initial equations are redundant, so they are removed from the initialization sytem: Inertia1.a = $START.Inertia1.a. Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 8 * Number of states: 0 () * Number of discrete variables: 1 (ST.fluidState_in.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (24): * Single equations (assignments): 23 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(1,100.0%) 1} * Non-linear torn systems: 0 Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 2 * Number of states: 3 (ST.P_HP,ST.P_LP,Speed1.phi) * Number of discrete variables: 4 ($cse2.phase,$cse2.region,$cse3.phase,$cse3.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (18): * Single equations (assignments): 15 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 2 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(1,100.0%) 1} * Non-linear torn systems: 0 ThermoPower.Test.WaterComponents.TestSources.err [ThermoPower 3.1/Water.mo:296:5-296:61:writable] Warning: No corresponding 'inner' declaration found for component .ThermoPower.System source_w_h.system declared as 'outer '. The existing 'inner' components are: There are no 'inner' components defined in the model in any of the parent scopes of 'outer' component's scope: ThermoPower.Water.SourceMassFlow$source_w_h. Check if you have not misspelled the 'outer' component name. Please declare an 'inner' component with the same name in the top scope. Continuing flattening by only considering the 'outer' component declaration. [ThermoPower 3.1/Water.mo:405:5-405:61:writable] Warning: No corresponding 'inner' declaration found for component .ThermoPower.System sink_w_h.system declared as 'outer '. The existing 'inner' components are: There are no 'inner' components defined in the model in any of the parent scopes of 'outer' component's scope: ThermoPower.Water.SinkMassFlow. Check if you have not misspelled the 'outer' component name. Please declare an 'inner' component with the same name in the top scope. Continuing flattening by only considering the 'outer' component declaration. [ThermoPower 3.1/Water.mo:296:5-296:61:writable] Warning: No corresponding 'inner' declaration found for component .ThermoPower.System source_w_T.system declared as 'outer '. The existing 'inner' components are: There are no 'inner' components defined in the model in any of the parent scopes of 'outer' component's scope: ThermoPower.Water.SourceMassFlow$source_w_T. Check if you have not misspelled the 'outer' component name. Please declare an 'inner' component with the same name in the top scope. Continuing flattening by only considering the 'outer' component declaration. [ThermoPower 3.1/Water.mo:296:5-296:61:writable] Warning: No corresponding 'inner' declaration found for component .ThermoPower.System source_w_h_in.system declared as 'outer '. The existing 'inner' components are: There are no 'inner' components defined in the model in any of the parent scopes of 'outer' component's scope: ThermoPower.Water.SourceMassFlow$source_w_h_in. Check if you have not misspelled the 'outer' component name. Please declare an 'inner' component with the same name in the top scope. Continuing flattening by only considering the 'outer' component declaration. [ThermoPower 3.1/Water.mo:296:5-296:61:writable] Warning: No corresponding 'inner' declaration found for component .ThermoPower.System source_w_T_in.system declared as 'outer '. The existing 'inner' components are: There are no 'inner' components defined in the model in any of the parent scopes of 'outer' component's scope: ThermoPower.Water.SourceMassFlow$source_w_T_in. Check if you have not misspelled the 'outer' component name. Please declare an 'inner' component with the same name in the top scope. Continuing flattening by only considering the 'outer' component declaration. [ThermoPower 3.1/Water.mo:405:5-405:61:writable] Warning: No corresponding 'inner' declaration found for component .ThermoPower.System sink_w_T.system declared as 'outer '. The existing 'inner' components are: There are no 'inner' components defined in the model in any of the parent scopes of 'outer' component's scope: ThermoPower.Water.SinkMassFlow$sink_w_T. Check if you have not misspelled the 'outer' component name. Please declare an 'inner' component with the same name in the top scope. Continuing flattening by only considering the 'outer' component declaration. [ThermoPower 3.1/Water.mo:405:5-405:61:writable] Warning: No corresponding 'inner' declaration found for component .ThermoPower.System sink_w_h_in.system declared as 'outer '. The existing 'inner' components are: There are no 'inner' components defined in the model in any of the parent scopes of 'outer' component's scope: ThermoPower.Water.SinkMassFlow$sink_w_h_in. Check if you have not misspelled the 'outer' component name. Please declare an 'inner' component with the same name in the top scope. Continuing flattening by only considering the 'outer' component declaration. [ThermoPower 3.1/Water.mo:405:5-405:61:writable] Warning: No corresponding 'inner' declaration found for component .ThermoPower.System sink_w_T_in.system declared as 'outer '. The existing 'inner' components are: There are no 'inner' components defined in the model in any of the parent scopes of 'outer' component's scope: ThermoPower.Water.SinkMassFlow$sink_w_T_in. Check if you have not misspelled the 'outer' component name. Please declare an 'inner' component with the same name in the top scope. Continuing flattening by only considering the 'outer' component declaration. [ThermoPower 3.1/Water.mo:186:5-186:61:writable] Warning: No corresponding 'inner' declaration found for component .ThermoPower.System sink_P_h.system declared as 'outer '. The existing 'inner' components are: There are no 'inner' components defined in the model in any of the parent scopes of 'outer' component's scope: ThermoPower.Water.SinkPressure. Check if you have not misspelled the 'outer' component name. Please declare an 'inner' component with the same name in the top scope. Continuing flattening by only considering the 'outer' component declaration. [ThermoPower 3.1/Water.mo:78:5-78:61:writable] Warning: No corresponding 'inner' declaration found for component .ThermoPower.System source_P_h.system declared as 'outer '. The existing 'inner' components are: There are no 'inner' components defined in the model in any of the parent scopes of 'outer' component's scope: ThermoPower.Water.SourcePressure. Check if you have not misspelled the 'outer' component name. Please declare an 'inner' component with the same name in the top scope. Continuing flattening by only considering the 'outer' component declaration. [ThermoPower 3.1/Water.mo:186:5-186:61:writable] Warning: No corresponding 'inner' declaration found for component .ThermoPower.System sink_P_T.system declared as 'outer '. The existing 'inner' components are: There are no 'inner' components defined in the model in any of the parent scopes of 'outer' component's scope: ThermoPower.Water.SinkPressure$sink_P_T. Check if you have not misspelled the 'outer' component name. Please declare an 'inner' component with the same name in the top scope. Continuing flattening by only considering the 'outer' component declaration. [ThermoPower 3.1/Water.mo:78:5-78:61:writable] Warning: No corresponding 'inner' declaration found for component .ThermoPower.System source_P_T.system declared as 'outer '. The existing 'inner' components are: There are no 'inner' components defined in the model in any of the parent scopes of 'outer' component's scope: ThermoPower.Water.SourcePressure$source_P_T. Check if you have not misspelled the 'outer' component name. Please declare an 'inner' component with the same name in the top scope. Continuing flattening by only considering the 'outer' component declaration. [ThermoPower 3.1/Water.mo:78:5-78:61:writable] Warning: No corresponding 'inner' declaration found for component .ThermoPower.System source_P_h_in.system declared as 'outer '. The existing 'inner' components are: There are no 'inner' components defined in the model in any of the parent scopes of 'outer' component's scope: ThermoPower.Water.SourcePressure$source_P_h_in. Check if you have not misspelled the 'outer' component name. Please declare an 'inner' component with the same name in the top scope. Continuing flattening by only considering the 'outer' component declaration. [ThermoPower 3.1/Water.mo:78:5-78:61:writable] Warning: No corresponding 'inner' declaration found for component .ThermoPower.System source_P_T_in.system declared as 'outer '. The existing 'inner' components are: There are no 'inner' components defined in the model in any of the parent scopes of 'outer' component's scope: ThermoPower.Water.SourcePressure$source_P_T_in. Check if you have not misspelled the 'outer' component name. Please declare an 'inner' component with the same name in the top scope. Continuing flattening by only considering the 'outer' component declaration. [ThermoPower 3.1/Water.mo:186:5-186:61:writable] Warning: No corresponding 'inner' declaration found for component .ThermoPower.System sink_P_h_in.system declared as 'outer '. The existing 'inner' components are: There are no 'inner' components defined in the model in any of the parent scopes of 'outer' component's scope: ThermoPower.Water.SinkPressure$sink_P_h_in. Check if you have not misspelled the 'outer' component name. Please declare an 'inner' component with the same name in the top scope. Continuing flattening by only considering the 'outer' component declaration. [ThermoPower 3.1/Water.mo:186:5-186:61:writable] Warning: No corresponding 'inner' declaration found for component .ThermoPower.System sink_P_T_in.system declared as 'outer '. The existing 'inner' components are: There are no 'inner' components defined in the model in any of the parent scopes of 'outer' component's scope: ThermoPower.Water.SinkPressure$sink_P_T_in. Check if you have not misspelled the 'outer' component name. Please declare an 'inner' component with the same name in the top scope. Continuing flattening by only considering the 'outer' component declaration. Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 124 * Number of variables: 124 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 12 * Number of states: 0 () * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (12): * Single equations (assignments): 12 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 0 * Mixed (continuous/discrete) equation systems: 0 Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 0 () * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (0): * Single equations (assignments): 0 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 ThermoPower.Test.WaterComponents.TestSplitRev.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 174 * Number of variables: 174 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 12 * Number of states: 0 () * Number of discrete variables: 26 ($whenCondition2,$whenCondition1,$PRE.Sine1.T_start,Sine1.T_start,$PRE.Sine1.count,Sine1.count,$PRE.Sine2.T_start,Sine2.T_start,$PRE.Sine2.count,Sine2.count,T3.fluidState.phase,T2.fluidState.phase,T1.fluidState.phase,T6.fluidState.phase,T5.fluidState.phase,T4.fluidState.phase,$whenCondition4,$whenCondition3,$PRE.Sine3.T_start,Sine3.T_start,$PRE.Sine3.count,Sine3.count,$PRE.Sine4.T_start,Sine4.T_start,$PRE.Sine4.count,Sine4.count) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (56): * Single equations (assignments): 52 * Array equations: 0 * Algorithm blocks: 4 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 0 * Mixed (continuous/discrete) equation systems: 0 Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 2 * Number of states: 0 () * Number of discrete variables: 24 ($cse1.phase,$cse1.region,$cse2.phase,$cse2.region,$cse3.phase,$cse3.region,$whenCondition2,$whenCondition1,Sine1.T_start,Sine1.count,Sine2.T_start,Sine2.count,$cse4.phase,$cse4.region,$cse5.phase,$cse5.region,$cse6.phase,$cse6.region,$whenCondition4,$whenCondition3,Sine3.T_start,Sine3.count,Sine4.T_start,Sine4.count) * Number of discrete states: 4 (Sine4.count,Sine3.count,Sine2.count,Sine1.count) * Top-level inputs: 0 Notification: Strong component statistics for simulation (47): * Single equations (assignments): 33 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 6 * When equations: 8 ThermoPower.Test.WaterComponents.TestValveChoked.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 75 * Number of variables: 75 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 9 * Number of states: 0 () * Number of discrete variables: 2 (ValveVap.fluidState.phase,ValveLiqChocked.fluidState.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (25): * Single equations (assignments): 25 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 0 * Mixed (continuous/discrete) equation systems: 0 Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 2 * Number of states: 0 () * Number of discrete variables: 0 () * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (14): * Single equations (assignments): 14 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 ThermoPower.Test.WaterComponents.TestValves.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 128 * Number of variables: 128 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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. Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: SourceP1.flange.m_flow:VARIABLE(flow=true min = -100000.0 max = 100000.0 unit = "kg/s" ) "Mass flow rate from the connection point into the component" type: Real SourceP2.flange.m_flow:VARIABLE(flow=true min = -100000.0 max = 100000.0 unit = "kg/s" ) "Mass flow rate from the connection point into the component" type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 6 * Number of states: 0 () * Number of discrete variables: 5 (V5.fluidState.phase,V4.fluidState.phase,V3.fluidState.phase,V2.fluidState.phase,V1.fluidState.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (18): * Single equations (assignments): 17 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {7 16} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 0 () * Number of discrete variables: 10 ($cse3.phase,$cse3.region,$cse8.phase,$cse8.region,$cse13.phase,$cse13.region,$cse18.phase,$cse18.region,$cse22.phase,$cse22.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (14): * Single equations (assignments): 13 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {5 35} ThermoPower.Test.WaterComponents.ValveZeroFlow.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 71 * Number of variables: 71 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 5 * Number of states: 0 () * Number of discrete variables: 3 (V3.fluidState.phase,V2.fluidState.phase,V1.fluidState.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (14): * Single equations (assignments): 13 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {2 6} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 0 () * Number of discrete variables: 4 ($cse1.phase,$cse1.region,$cse4.phase,$cse4.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (9): * Single equations (assignments): 8 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {2 11} ThermoPower.Test.WaterComponents.ValveZeroFlow2.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 79 * Number of variables: 79 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 6 * Number of states: 0 () * Number of discrete variables: 3 (Valve.fluidState.phase,Tank2.liquidState.phase,Tank1.liquidState.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (44): * Single equations (assignments): 42 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 2 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 2 {1 1,1 1} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 4 (Tank1.y,Tank1.h,Tank2.y,Tank2.h) * Number of discrete variables: 6 ($cse1.phase,$cse1.region,$cse4.phase,$cse4.region,$cse5.phase,$cse5.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (40): * Single equations (assignments): 35 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 3 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 2 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 2 {1 1,1 1} ThermoPower.Test.WaterComponents.WaterPump.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 60 * Number of variables: 60 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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. Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: Pump.w:VARIABLE(min = -100000.0 max = 100000.0 unit = "kg/s" ) "Mass flow rate (total)" type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 4 * Number of states: 0 () * Number of discrete variables: 2 (Pump.int_Np,Pump.inletFluidState.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (17): * Single equations (assignments): 16 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {4 5} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 1 (Pump.h) * Number of discrete variables: 2 ($cse1.phase,$cse1.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (14): * Single equations (assignments): 13 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {2 8} ThermoPower.Test.WaterComponents.WaterPumpMech.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 121 * Number of variables: 121 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 7 * Number of states: 0 () * Number of discrete variables: 2 (Pump.int_Np,Pump.inletFluidState.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (43): * Single equations (assignments): 42 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {4 4} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 5 * Number of states: 4 (Pump.h,SimpleMotor1.L.i,SimpleMotor1.Damper.phi_rel,SimpleMotor1.Damper.w_rel) * Number of discrete variables: 2 ($cse2.phase,$cse2.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (34): * Single equations (assignments): 33 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 1 {2 7} ThermoPower.Test.WaterComponents.WaterPumps.err Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 170 * Number of variables: 170 Warning: Deprecated debug flag -d=disablePartitioning detected. Use --preOptModules-=clockPartitioning instead. Warning: The model contains alias variables with conflicting start and/or 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. Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: Pump2.w:VARIABLE(min = -100000.0 max = 100000.0 unit = "kg/s" ) "Mass flow rate (total)" type: Real Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: Pump3.w:VARIABLE(min = -100000.0 max = 100000.0 unit = "kg/s" ) "Mass flow rate (total)" type: Real Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: Pump1.w:VARIABLE(min = -100000.0 max = 100000.0 unit = "kg/s" ) "Mass flow rate (total)" type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 13 * Number of states: 0 () * Number of discrete variables: 6 (Pump3.int_Np,Pump3.inletFluidState.phase,Pump2.int_Np,Pump2.inletFluidState.phase,Pump1.int_Np,Pump1.inletFluidState.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (47): * Single equations (assignments): 44 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 3 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 3 {4 5,4 5,4 5} Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 3 (Pump1.h,Pump2.h,Pump3.h) * Number of discrete variables: 6 ($cse1.phase,$cse1.region,$cse3.phase,$cse3.region,$cse5.phase,$cse5.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (35): * Single equations (assignments): 32 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 0 * Torn equation systems: 3 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 0 * Non-linear torn systems: 3 {2 8,2 8,2 8}