[/var/lib/hudson/slave/workspace/LibraryExperimental/OpenModelica/build/lib/omlibrary/ThermoPower 3.1/Examples.mo:2534:70-2534:81:writable] Error: Variable q_nom not found in scope ThermoPower.Examples.RankineCycle.Models. [/var/lib/hudson/slave/workspace/LibraryExperimental/OpenModelica/build/lib/omlibrary/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}