[/var/lib/hudson/slave/workspace/LibraryExperimental/OpenModelica/build/lib/omlibrary/ThermoPower 3.1/PowerPlants.mo:3950:70-3951:22:writable] Error: Variable q_nom not found in scope ThermoPower.PowerPlants.HRSG.Components. [/var/lib/hudson/slave/workspace/LibraryExperimental/OpenModelica/build/lib/omlibrary/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.Sh1HP_Rh1IP.fluidAFlow.p = 0.0 $DER.hRSG.HeatExchangersGroup.Sh2HP_Rh2IP.fluidAFlow.p = 0.0 $DER.hRSG.HeatExchangersGroup.Ev_HP.fluidFlow.p = 0.0 $DER.hRSG.HeatExchangersGroup.Ec2_HP.fluidFlow.p = 0.0 $DER.hRSG.drums.LPd.p = 0.0 $DER.hRSG.HeatExchangersGroup.Ev_LP.fluidFlow.p = 0.0 $DER.hRSG.HeatExchangersGroup.Ec_LP.fluidFlow.p = 0.0 $DER.sTG_3LRh.steamTurbines.mixLP.p = 0.0 $DER.hRSG.HeatExchangersGroup.Ev_LP.gasFlow.p = 0.0 $DER.hRSG.HeatExchangersGroup.Ec1HP_EcIP.gasFlow.p = 0.0 $DER.hRSG.HeatExchangersGroup.Sh_LP.gasFlow.p = 0.0 $DER.hRSG.HeatExchangersGroup.Ev_IP.gasFlow.p = 0.0 $DER.hRSG.HeatExchangersGroup.Ec2_HP.gasFlow.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}