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Failed
openmodelica_dataReconciliation.TSP_Splitter7.mos (from (result.xml))
Stacktrace
Output mismatch (see stdout for details)
Standard Output
+ TSP_Splitter7 ... equation mismatch [time: 20] ==== Log C:\WINDOWS\TEMP/omc-rtest-OpenModelica/openmodelica/dataReconciliation/TSP_Splitter7.mos_temp54/log-TSP_Splitter7.mos true "" true "Notification: Automatically loaded package Modelica 3.2.3 due to uses annotation from NewDataReconciliationSimpleTests. Notification: Automatically loaded package Complex 3.2.3 due to uses annotation from Modelica. Notification: Automatically loaded package ModelicaServices 3.2.3 due to uses annotation from Modelica. Notification: Automatically loaded package ThermoSysPro 3.2 due to uses annotation from NewDataReconciliationSimpleTests. " ModelInfo: NewDataReconciliationSimpleTests.TSP_Splitter7 ========================================================================== OrderedVariables (207) ======================================== 1: new_Sink1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 2: new_Sink1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 3: new_Sink1.C.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 4: new_Sink1.C.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real 5: new_Sink1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 6: new_Sink1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 7: new_Sink1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 8: new_Sink1.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real 9: new_Sink1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real 10: new_Sink1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 11: lumpedStraightPipe1.pro.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 12: lumpedStraightPipe1.pro.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 13: lumpedStraightPipe1.pro.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 14: lumpedStraightPipe1.pro.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 15: lumpedStraightPipe1.pro.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 16: lumpedStraightPipe1.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 17: lumpedStraightPipe1.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 18: lumpedStraightPipe1.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 19: lumpedStraightPipe1.pro.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 20: lumpedStraightPipe1.pro.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 21: lumpedStraightPipe1.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 22: lumpedStraightPipe1.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 23: lumpedStraightPipe1.C2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 24: lumpedStraightPipe1.C2.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real 25: lumpedStraightPipe1.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 26: lumpedStraightPipe1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 27: lumpedStraightPipe1.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 28: lumpedStraightPipe1.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 29: lumpedStraightPipe1.C1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 30: lumpedStraightPipe1.C1.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real 31: lumpedStraightPipe1.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 32: lumpedStraightPipe1.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 33: lumpedStraightPipe1.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real 34: lumpedStraightPipe1.Pm:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid average pressure" type: Real 35: lumpedStraightPipe1.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 36: lumpedStraightPipe1.mu:VARIABLE(min = 0.0 unit = "Pa.s" ) "Fluid dynamic viscosity" type: Real 37: lumpedStraightPipe1.rho:VARIABLE(min = 0.0 unit = "kg/m3" ) "Fluid density" type: Real 38: lumpedStraightPipe1.lam:VARIABLE() "Friction pressure loss coefficient" type: Real 39: lumpedStraightPipe1.Relim:VARIABLE(unit = "1" ) "Limit Reynolds number" type: Real 40: lumpedStraightPipe1.Re:VARIABLE(unit = "1" ) "Reynolds number" type: Real 41: lumpedStraightPipe1.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real 42: lumpedStraightPipe1.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Total pressure loss" type: Real 43: lumpedStraightPipe1.deltaPf:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Friction pressure loss" type: Real 44: lumpedStraightPipe1.khi:VARIABLE() "Hydraulic pressure loss coefficient" type: Real 45: lumpedStraightPipe3.pro.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 46: lumpedStraightPipe3.pro.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 47: lumpedStraightPipe3.pro.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 48: lumpedStraightPipe3.pro.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 49: lumpedStraightPipe3.pro.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 50: lumpedStraightPipe3.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 51: lumpedStraightPipe3.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 52: lumpedStraightPipe3.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 53: lumpedStraightPipe3.pro.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 54: lumpedStraightPipe3.pro.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 55: lumpedStraightPipe3.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 56: lumpedStraightPipe3.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 57: lumpedStraightPipe3.C2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 58: lumpedStraightPipe3.C2.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real 59: lumpedStraightPipe3.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 60: lumpedStraightPipe3.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 61: lumpedStraightPipe3.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 62: lumpedStraightPipe3.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 63: lumpedStraightPipe3.C1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 64: lumpedStraightPipe3.C1.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real 65: lumpedStraightPipe3.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 66: lumpedStraightPipe3.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 67: lumpedStraightPipe3.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real 68: lumpedStraightPipe3.Pm:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid average pressure" type: Real 69: lumpedStraightPipe3.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 70: lumpedStraightPipe3.mu:VARIABLE(min = 0.0 unit = "Pa.s" ) "Fluid dynamic viscosity" type: Real 71: lumpedStraightPipe3.rho:VARIABLE(min = 0.0 unit = "kg/m3" ) "Fluid density" type: Real 72: lumpedStraightPipe3.lam:VARIABLE() "Friction pressure loss coefficient" type: Real 73: lumpedStraightPipe3.Relim:VARIABLE(unit = "1" ) "Limit Reynolds number" type: Real 74: lumpedStraightPipe3.Re:VARIABLE(unit = "1" ) "Reynolds number" type: Real 75: lumpedStraightPipe3.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real 76: lumpedStraightPipe3.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Total pressure loss" type: Real 77: lumpedStraightPipe3.deltaPf:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Friction pressure loss" type: Real 78: lumpedStraightPipe3.khi:VARIABLE() "Hydraulic pressure loss coefficient" type: Real 79: sourceQ2.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 80: sourceQ2.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 81: sourceQ2.C.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 82: sourceQ2.C.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real 83: sourceQ2.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 84: sourceQ2.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 85: sourceQ2.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 86: sourceQ2.IMassFlow.signal:VARIABLE(flow=false ) type: Real 87: sourceQ2.h:VARIABLE(unit = "J/kg" protected = true ) "Fluid specific enthalpy" type: Real 88: sourceQ2.Q:VARIABLE(unit = "kg/s" protected = true ) "Mass flow rate" type: Real 89: sourceQ2.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true ) "Fluid pressure" type: Real 90: sourceQ1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 91: sourceQ1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 92: sourceQ1.C.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 93: sourceQ1.C.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real 94: sourceQ1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 95: sourceQ1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 96: sourceQ1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 97: sourceQ1.IMassFlow.signal:VARIABLE(flow=false ) type: Real 98: sourceQ1.h:VARIABLE(unit = "J/kg" protected = true ) "Fluid specific enthalpy" type: Real 99: sourceQ1.Q:VARIABLE(unit = "kg/s" protected = true ) "Mass flow rate" type: Real 100: sourceQ1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true ) "Fluid pressure" type: Real 101: lumpedStraightPipe2.pro.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 102: lumpedStraightPipe2.pro.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 103: lumpedStraightPipe2.pro.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 104: lumpedStraightPipe2.pro.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 105: lumpedStraightPipe2.pro.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 106: lumpedStraightPipe2.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 107: lumpedStraightPipe2.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 108: lumpedStraightPipe2.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 109: lumpedStraightPipe2.pro.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 110: lumpedStraightPipe2.pro.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 111: lumpedStraightPipe2.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 112: lumpedStraightPipe2.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 113: lumpedStraightPipe2.C2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 114: lumpedStraightPipe2.C2.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real 115: lumpedStraightPipe2.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 116: lumpedStraightPipe2.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 117: lumpedStraightPipe2.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 118: lumpedStraightPipe2.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 119: lumpedStraightPipe2.C1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 120: lumpedStraightPipe2.C1.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real 121: lumpedStraightPipe2.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 122: lumpedStraightPipe2.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 123: lumpedStraightPipe2.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real 124: lumpedStraightPipe2.Pm:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid average pressure" type: Real 125: lumpedStraightPipe2.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 126: lumpedStraightPipe2.mu:VARIABLE(min = 0.0 unit = "Pa.s" ) "Fluid dynamic viscosity" type: Real 127: lumpedStraightPipe2.rho:VARIABLE(min = 0.0 unit = "kg/m3" ) "Fluid density" type: Real 128: lumpedStraightPipe2.lam:VARIABLE() "Friction pressure loss coefficient" type: Real 129: lumpedStraightPipe2.Relim:VARIABLE(unit = "1" ) "Limit Reynolds number" type: Real 130: lumpedStraightPipe2.Re:VARIABLE(unit = "1" ) "Reynolds number" type: Real 131: lumpedStraightPipe2.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real 132: lumpedStraightPipe2.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Total pressure loss" type: Real 133: lumpedStraightPipe2.deltaPf:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Friction pressure loss" type: Real 134: lumpedStraightPipe2.khi:VARIABLE() "Hydraulic pressure loss coefficient" type: Real 135: staticDrum1.Cth.W:VARIABLE(flow=true unit = "W" ) "Thermal flow rate. Positive when going into the component" type: Real 136: staticDrum1.Cth.T:VARIABLE(flow=false min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature" type: Real 137: staticDrum1.vsat.cv:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant volume" type: Real 138: staticDrum1.vsat.pt:VARIABLE() "Derivative of pressure wrt. temperature" type: Real 139: staticDrum1.vsat.cp:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant pressure" type: Real 140: staticDrum1.vsat.h:VARIABLE(unit = "J/kg" ) "Specific enthalpy" type: Real 141: staticDrum1.vsat.rho:VARIABLE(min = 0.0 unit = "kg/m3" ) "Density" type: Real 142: staticDrum1.vsat.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature" type: Real 143: staticDrum1.vsat.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Pressure" type: Real 144: staticDrum1.lsat.cv:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant volume" type: Real 145: staticDrum1.lsat.pt:VARIABLE() "Derivative of pressure wrt. temperature" type: Real 146: staticDrum1.lsat.cp:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant pressure" type: Real 147: staticDrum1.lsat.h:VARIABLE(unit = "J/kg" ) "Specific enthalpy" type: Real 148: staticDrum1.lsat.rho:VARIABLE(min = 0.0 unit = "kg/m3" ) "Density" type: Real 149: staticDrum1.lsat.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature" type: Real 150: staticDrum1.lsat.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Pressure" type: Real 151: staticDrum1.Ce_sup.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 152: staticDrum1.Ce_sup.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 153: staticDrum1.Ce_sup.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 154: staticDrum1.Ce_sup.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real 155: staticDrum1.Ce_sup.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 156: staticDrum1.Ce_sup.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 157: staticDrum1.Ce_steam.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 158: staticDrum1.Ce_steam.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 159: staticDrum1.Ce_steam.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 160: staticDrum1.Ce_steam.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real 161: staticDrum1.Ce_steam.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 162: staticDrum1.Ce_steam.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 163: staticDrum1.Cs_purg.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 164: staticDrum1.Cs_purg.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 165: staticDrum1.Cs_purg.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 166: staticDrum1.Cs_purg.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real 167: staticDrum1.Cs_purg.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 168: staticDrum1.Cs_purg.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 169: staticDrum1.Cs_sur.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 170: staticDrum1.Cs_sur.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 171: staticDrum1.Cs_sur.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 172: staticDrum1.Cs_sur.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real 173: staticDrum1.Cs_sur.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 174: staticDrum1.Cs_sur.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 175: staticDrum1.Cs_eva.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 176: staticDrum1.Cs_eva.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 177: staticDrum1.Cs_eva.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 178: staticDrum1.Cs_eva.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real 179: staticDrum1.Cs_eva.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 180: staticDrum1.Cs_eva.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 181: staticDrum1.Cs_sup.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 182: staticDrum1.Cs_sup.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 183: staticDrum1.Cs_sup.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 184: staticDrum1.Cs_sup.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real 185: staticDrum1.Cs_sup.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 186: staticDrum1.Cs_sup.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 187: staticDrum1.Ce_eco.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 188: staticDrum1.Ce_eco.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 189: staticDrum1.Ce_eco.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 190: staticDrum1.Ce_eco.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real 191: staticDrum1.Ce_eco.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 192: staticDrum1.Ce_eco.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 193: staticDrum1.Ce_eva.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 194: staticDrum1.Ce_eva.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 195: staticDrum1.Ce_eva.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 196: staticDrum1.Ce_eva.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real 197: staticDrum1.Ce_eva.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 198: staticDrum1.Ce_eva.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 199: staticDrum1.hv:VARIABLE(start = 2.8e6 unit = "J/kg" ) "Gas phase specific enthalpy" type: Real 200: staticDrum1.hl:VARIABLE(start = 1e5 unit = "J/kg" ) "Liquid phase specific enthalpy" type: Real 201: staticDrum1.P:VARIABLE(min = 0.0 start = 1e6 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 202: staticDrum1.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 203: sourceQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 204: sourceQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real 205: sourceQ2.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 206: sourceQ2.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real 207: new_Sink1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real OrderedEquation (167, 207) ======================================== 1/1 (1): sourceQ1.Q0 = 100.0 [binding |0|0|0|0|] 2/2 (1): sourceQ1.h0 = 1e6 [binding |0|0|0|0|] 3/3 (1): sourceQ2.Q0 = 100.0 [binding |0|0|0|0|] 4/4 (1): sourceQ2.h0 = 1e6 [binding |0|0|0|0|] 5/5 (1): new_Sink1.h0 = 1e5 [binding |0|0|0|0|] 6/6 (1): sourceQ1.C.P = lumpedStraightPipe2.C1.P [dynamic |0|0|0|0|] 7/7 (1): sourceQ1.C.Q = lumpedStraightPipe2.C1.Q [dynamic |0|0|0|0|] 8/8 (1): sourceQ1.C.a = lumpedStraightPipe2.C1.a [dynamic |0|0|0|0|] 9/9 (1): sourceQ1.C.b = lumpedStraightPipe2.C1.b [dynamic |0|0|0|0|] 10/10 (1): sourceQ1.C.h = lumpedStraightPipe2.C1.h [dynamic |0|0|0|0|] 11/11 (1): sourceQ1.C.h_vol = lumpedStraightPipe2.C1.h_vol [dynamic |0|0|0|0|] 12/12 (1): lumpedStraightPipe2.C2.P = staticDrum1.Ce_steam.P [dynamic |0|0|0|0|] 13/13 (1): lumpedStraightPipe2.C2.Q = staticDrum1.Ce_steam.Q [dynamic |0|0|0|0|] 14/14 (1): lumpedStraightPipe2.C2.a = staticDrum1.Ce_steam.a [dynamic |0|0|0|0|] 15/15 (1): lumpedStraightPipe2.C2.b = staticDrum1.Ce_steam.b [dynamic |0|0|0|0|] 16/16 (1): lumpedStraightPipe2.C2.h = staticDrum1.Ce_steam.h [dynamic |0|0|0|0|] 17/17 (1): lumpedStraightPipe2.C2.h_vol = staticDrum1.Ce_steam.h_vol [dynamic |0|0|0|0|] 18/18 (1): sourceQ2.C.P = lumpedStraightPipe3.C1.P [dynamic |0|0|0|0|] 19/19 (1): sourceQ2.C.Q = lumpedStraightPipe3.C1.Q [dynamic |0|0|0|0|] 20/20 (1): sourceQ2.C.a = lumpedStraightPipe3.C1.a [dynamic |0|0|0|0|] 21/21 (1): sourceQ2.C.b = lumpedStraightPipe3.C1.b [dynamic |0|0|0|0|] 22/22 (1): sourceQ2.C.h = lumpedStraightPipe3.C1.h [dynamic |0|0|0|0|] 23/23 (1): sourceQ2.C.h_vol = lumpedStraightPipe3.C1.h_vol [dynamic |0|0|0|0|] 24/24 (1): lumpedStraightPipe3.C2.P = staticDrum1.Ce_eco.P [dynamic |0|0|0|0|] 25/25 (1): lumpedStraightPipe3.C2.Q = staticDrum1.Ce_eco.Q [dynamic |0|0|0|0|] 26/26 (1): lumpedStraightPipe3.C2.a = staticDrum1.Ce_eco.a [dynamic |0|0|0|0|] 27/27 (1): lumpedStraightPipe3.C2.b = staticDrum1.Ce_eco.b [dynamic |0|0|0|0|] 28/28 (1): lumpedStraightPipe3.C2.h = staticDrum1.Ce_eco.h [dynamic |0|0|0|0|] 29/29 (1): lumpedStraightPipe3.C2.h_vol = staticDrum1.Ce_eco.h_vol [dynamic |0|0|0|0|] 30/30 (1): staticDrum1.Cs_sup.P = lumpedStraightPipe1.C1.P [dynamic |0|0|0|0|] 31/31 (1): staticDrum1.Cs_sup.Q = lumpedStraightPipe1.C1.Q [dynamic |0|0|0|0|] 32/32 (1): staticDrum1.Cs_sup.a = lumpedStraightPipe1.C1.a [dynamic |0|0|0|0|] 33/33 (1): staticDrum1.Cs_sup.b = lumpedStraightPipe1.C1.b [dynamic |0|0|0|0|] 34/34 (1): staticDrum1.Cs_sup.h = lumpedStraightPipe1.C1.h [dynamic |0|0|0|0|] 35/35 (1): staticDrum1.Cs_sup.h_vol = lumpedStraightPipe1.C1.h_vol [dynamic |0|0|0|0|] 36/36 (1): lumpedStraightPipe1.C2.P = new_Sink1.C.P [dynamic |0|0|0|0|] 37/37 (1): lumpedStraightPipe1.C2.Q = new_Sink1.C.Q [dynamic |0|0|0|0|] 38/38 (1): lumpedStraightPipe1.C2.a = new_Sink1.C.a [dynamic |0|0|0|0|] 39/39 (1): lumpedStraightPipe1.C2.b = new_Sink1.C.b [dynamic |0|0|0|0|] 40/40 (1): lumpedStraightPipe1.C2.h = new_Sink1.C.h [dynamic |0|0|0|0|] 41/41 (1): lumpedStraightPipe1.C2.h_vol = new_Sink1.C.h_vol [dynamic |0|0|0|0|] 42/42 (1): staticDrum1.Cth.W = 0.0 [dynamic |0|0|0|0|] 43/43 (1): staticDrum1.Ce_sup.Q = 0.0 [dynamic |0|0|0|0|] 44/44 (1): staticDrum1.Ce_sup.h = 1e5 [dynamic |0|0|0|0|] 45/45 (1): staticDrum1.Ce_sup.b = true [dynamic |0|0|0|0|] 46/46 (1): staticDrum1.Ce_eva.Q = 0.0 [dynamic |0|0|0|0|] 47/47 (1): staticDrum1.Ce_eva.h = 1e5 [dynamic |0|0|0|0|] 48/48 (1): staticDrum1.Ce_eva.b = true [dynamic |0|0|0|0|] 49/49 (1): staticDrum1.Cs_eva.Q = 0.0 [dynamic |0|0|0|0|] 50/50 (1): staticDrum1.Cs_eva.h = 1e5 [dynamic |0|0|0|0|] 51/51 (1): staticDrum1.Cs_eva.a = true [dynamic |0|0|0|0|] 52/52 (1): staticDrum1.Cs_purg.Q = 0.0 [dynamic |0|0|0|0|] 53/53 (1): staticDrum1.Cs_purg.h = 1e5 [dynamic |0|0|0|0|] 54/54 (1): staticDrum1.Cs_purg.a = true [dynamic |0|0|0|0|] 55/55 (1): staticDrum1.Cs_sur.Q = 0.0 [dynamic |0|0|0|0|] 56/56 (1): staticDrum1.Cs_sur.h = 1e5 [dynamic |0|0|0|0|] 57/57 (1): staticDrum1.Cs_sur.a = true [dynamic |0|0|0|0|] 58/58 (1): staticDrum1.P = staticDrum1.Ce_steam.P [dynamic |0|0|0|0|] 59/59 (1): staticDrum1.P = staticDrum1.Ce_sup.P [dynamic |0|0|0|0|] 60/60 (1): staticDrum1.P = staticDrum1.Ce_eva.P [dynamic |0|0|0|0|] 61/61 (1): staticDrum1.P = staticDrum1.Ce_eco.P [dynamic |0|0|0|0|] 62/62 (1): staticDrum1.P = staticDrum1.Cs_eva.P [dynamic |0|0|0|0|] 63/63 (1): staticDrum1.P = staticDrum1.Cs_purg.P [dynamic |0|0|0|0|] 64/64 (1): staticDrum1.P = staticDrum1.Cs_sup.P [dynamic |0|0|0|0|] 65/65 (1): staticDrum1.P = staticDrum1.Cs_sur.P [dynamic |0|0|0|0|] 66/66 (1): staticDrum1.Ce_sup.h_vol = staticDrum1.hl [dynamic |0|0|0|0|] 67/67 (1): staticDrum1.Ce_eva.h_vol = staticDrum1.hl [dynamic |0|0|0|0|] 68/68 (1): staticDrum1.Ce_eco.h_vol = staticDrum1.hl [dynamic |0|0|0|0|] 69/69 (1): staticDrum1.Ce_steam.h_vol = staticDrum1.hv [dynamic |0|0|0|0|] 70/70 (1): staticDrum1.Cs_purg.h_vol = staticDrum1.hl [dynamic |0|0|0|0|] 71/71 (1): staticDrum1.Cs_sup.h_vol = staticDrum1.hl [dynamic |0|0|0|0|] 72/72 (1): staticDrum1.Cs_eva.h_vol = staticDrum1.hl [dynamic |0|0|0|0|] 73/73 (1): staticDrum1.Cs_sur.h_vol = (1.0 - staticDrum1.x) * staticDrum1.hl + staticDrum1.x * staticDrum1.hv [dynamic |0|0|0|0|] 74/74 (1): staticDrum1.Ce_eco.Q + staticDrum1.Ce_steam.Q + staticDrum1.Ce_sup.Q + staticDrum1.Ce_eva.Q + (-staticDrum1.Cs_purg.Q) - staticDrum1.Cs_sup.Q - staticDrum1.Cs_sur.Q - staticDrum1.Cs_eva.Q = 0.0 [dynamic |0|0|0|0|] 75/75 (1): staticDrum1.Ce_eco.Q * staticDrum1.Ce_eco.h + staticDrum1.Ce_steam.Q * staticDrum1.Ce_steam.h + staticDrum1.Ce_sup.Q * staticDrum1.Ce_sup.h + staticDrum1.Ce_eva.Q * staticDrum1.Ce_eva.h + staticDrum1.Cth.W - staticDrum1.Cs_sup.Q * staticDrum1.Cs_sup.h - staticDrum1.Cs_purg.Q * staticDrum1.Cs_purg.h - staticDrum1.Cs_sur.Q * staticDrum1.Cs_sur.h - staticDrum1.Cs_eva.Q * staticDrum1.Cs_eva.h = 0.0 [dynamic |0|0|0|0|] 76/76 (14): (staticDrum1.lsat, staticDrum1.vsat) = ThermoSysPro.Properties.WaterSteam.IF97.Water_sat_P(staticDrum1.P) [dynamic |0|0|0|0|] 77/90 (1): staticDrum1.hl = staticDrum1.lsat.h [dynamic |0|0|0|0|] 78/91 (1): staticDrum1.hv = staticDrum1.vsat.h [dynamic |0|0|0|0|] 79/92 (1): staticDrum1.T = staticDrum1.lsat.T [dynamic |0|0|0|0|] 80/93 (1): staticDrum1.Cth.T = staticDrum1.T [dynamic |0|0|0|0|] 81/94 (1): lumpedStraightPipe2.C1.h = lumpedStraightPipe2.C2.h [dynamic |0|0|0|0|] 82/95 (1): lumpedStraightPipe2.C1.Q = lumpedStraightPipe2.C2.Q [dynamic |0|0|0|0|] 83/96 (1): lumpedStraightPipe2.C1.P - lumpedStraightPipe2.C2.P = lumpedStraightPipe2.deltaP [dynamic |0|0|0|0|] 84/97 (1): lumpedStraightPipe2.h = lumpedStraightPipe2.C1.h [dynamic |0|0|0|0|] 85/98 (1): lumpedStraightPipe2.Q = lumpedStraightPipe2.C1.Q [dynamic |0|0|0|0|] 86/99 (1): lumpedStraightPipe2.h = ThermoSysPro.Functions.SmoothCond(lumpedStraightPipe2.Q, lumpedStraightPipe2.C1.h_vol, lumpedStraightPipe2.C2.h_vol, 1.0) [dynamic |0|0|0|0|] 87/100 (1): lumpedStraightPipe2.deltaP = lumpedStraightPipe2.deltaPf + 9.80665 * lumpedStraightPipe2.rho * (lumpedStraightPipe2.z2 - lumpedStraightPipe2.z1) [dynamic |0|0|0|0|] 88/101 (1): lumpedStraightPipe2.deltaPf = 0.5 * lumpedStraightPipe2.khi * ThermoSysPro.Functions.ThermoSquare(lumpedStraightPipe2.Q, lumpedStraightPipe2.eps) / (lumpedStraightPipe2.A ^ 2.0 * lumpedStraightPipe2.rho) [dynamic |0|0|0|0|] 89/102 (1): lumpedStraightPipe2.khi = lumpedStraightPipe2.lam * lumpedStraightPipe2.L / lumpedStraightPipe2.D [dynamic |0|0|0|0|] 90/103 (1): lumpedStraightPipe2.lam = lumpedStraightPipe2.lambda [dynamic |0|0|0|0|] 91/104 (1): lumpedStraightPipe2.Relim = 5.6e6 [dynamic |0|0|0|0|] 92/105 (1): lumpedStraightPipe2.Re = 4.0 * abs(lumpedStraightPipe2.Q) / (lumpedStraightPipe2.mu * lumpedStraightPipe2.Pw) [dynamic |0|0|0|0|] 93/106 (1): lumpedStraightPipe2.Pm = 0.5 * (lumpedStraightPipe2.C1.P + lumpedStraightPipe2.C2.P) [dynamic |0|0|0|0|] 94/107 (10): lumpedStraightPipe2.pro = ThermoSysPro.Properties.Fluid.Ph(lumpedStraightPipe2.Pm, lumpedStraightPipe2.h, lumpedStraightPipe2.mode, lumpedStraightPipe2.fluid) [dynamic |0|0|0|0|] 95/117 (1): lumpedStraightPipe2.T = lumpedStraightPipe2.pro.T [dynamic |0|0|0|0|] 96/118 (1): lumpedStraightPipe2.rho = lumpedStraightPipe2.pro.d [dynamic |0|0|0|0|] 97/119 (1): lumpedStraightPipe2.mu = ThermoSysPro.Properties.Fluid.DynamicViscosity_Ph(lumpedStraightPipe2.Pm, lumpedStraightPipe2.h, lumpedStraightPipe2.fluid, lumpedStraightPipe2.mode, 0.1, 0.1, 0.1, 0.0) [dynamic |0|0|0|0|] 98/120 (1): sourceQ1.C.P = sourceQ1.P [dynamic |0|0|0|0|] 99/121 (1): sourceQ1.C.Q = sourceQ1.Q [dynamic |0|0|0|0|] 100/122 (1): sourceQ1.C.h_vol = sourceQ1.h [dynamic |0|0|0|0|] 101/123 (1): sourceQ1.IMassFlow.signal = sourceQ1.Q0 [dynamic |0|0|0|0|] 102/124 (1): sourceQ1.Q = sourceQ1.IMassFlow.signal [dynamic |0|0|0|0|] 103/125 (1): sourceQ1.ISpecificEnthalpy.signal = sourceQ1.h0 [dynamic |0|0|0|0|] 104/126 (1): sourceQ1.h = sourceQ1.ISpecificEnthalpy.signal [dynamic |0|0|0|0|] 105/127 (1): sourceQ2.C.P = sourceQ2.P [dynamic |0|0|0|0|] 106/128 (1): sourceQ2.C.Q = sourceQ2.Q [dynamic |0|0|0|0|] 107/129 (1): sourceQ2.C.h_vol = sourceQ2.h [dynamic |0|0|0|0|] 108/130 (1): sourceQ2.IMassFlow.signal = sourceQ2.Q0 [dynamic |0|0|0|0|] 109/131 (1): sourceQ2.Q = sourceQ2.IMassFlow.signal [dynamic |0|0|0|0|] 110/132 (1): sourceQ2.ISpecificEnthalpy.signal = sourceQ2.h0 [dynamic |0|0|0|0|] 111/133 (1): sourceQ2.h = sourceQ2.ISpecificEnthalpy.signal [dynamic |0|0|0|0|] 112/134 (1): lumpedStraightPipe3.C1.h = lumpedStraightPipe3.C2.h [dynamic |0|0|0|0|] 113/135 (1): lumpedStraightPipe3.C1.Q = lumpedStraightPipe3.C2.Q [dynamic |0|0|0|0|] 114/136 (1): lumpedStraightPipe3.C1.P - lumpedStraightPipe3.C2.P = lumpedStraightPipe3.deltaP [dynamic |0|0|0|0|] 115/137 (1): lumpedStraightPipe3.h = lumpedStraightPipe3.C1.h [dynamic |0|0|0|0|] 116/138 (1): lumpedStraightPipe3.Q = lumpedStraightPipe3.C1.Q [dynamic |0|0|0|0|] 117/139 (1): lumpedStraightPipe3.h = ThermoSysPro.Functions.SmoothCond(lumpedStraightPipe3.Q, lumpedStraightPipe3.C1.h_vol, lumpedStraightPipe3.C2.h_vol, 1.0) [dynamic |0|0|0|0|] 118/140 (1): lumpedStraightPipe3.deltaP = lumpedStraightPipe3.deltaPf + 9.80665 * lumpedStraightPipe3.rho * (lumpedStraightPipe3.z2 - lumpedStraightPipe3.z1) [dynamic |0|0|0|0|] 119/141 (1): lumpedStraightPipe3.deltaPf = 0.5 * lumpedStraightPipe3.khi * ThermoSysPro.Functions.ThermoSquare(lumpedStraightPipe3.Q, lumpedStraightPipe3.eps) / (lumpedStraightPipe3.A ^ 2.0 * lumpedStraightPipe3.rho) [dynamic |0|0|0|0|] 120/142 (1): lumpedStraightPipe3.khi = lumpedStraightPipe3.lam * lumpedStraightPipe3.L / lumpedStraightPipe3.D [dynamic |0|0|0|0|] 121/143 (1): lumpedStraightPipe3.lam = lumpedStraightPipe3.lambda [dynamic |0|0|0|0|] 122/144 (1): lumpedStraightPipe3.Relim = 5.6e6 [dynamic |0|0|0|0|] 123/145 (1): lumpedStraightPipe3.Re = 4.0 * abs(lumpedStraightPipe3.Q) / (lumpedStraightPipe3.mu * lumpedStraightPipe3.Pw) [dynamic |0|0|0|0|] 124/146 (1): lumpedStraightPipe3.Pm = 0.5 * (lumpedStraightPipe3.C1.P + lumpedStraightPipe3.C2.P) [dynamic |0|0|0|0|] 125/147 (10): lumpedStraightPipe3.pro = ThermoSysPro.Properties.Fluid.Ph(lumpedStraightPipe3.Pm, lumpedStraightPipe3.h, lumpedStraightPipe3.mode, lumpedStraightPipe3.fluid) [dynamic |0|0|0|0|] 126/157 (1): lumpedStraightPipe3.T = lumpedStraightPipe3.pro.T [dynamic |0|0|0|0|] 127/158 (1): lumpedStraightPipe3.rho = lumpedStraightPipe3.pro.d [dynamic |0|0|0|0|] 128/159 (1): lumpedStraightPipe3.mu = ThermoSysPro.Properties.Fluid.DynamicViscosity_Ph(lumpedStraightPipe3.Pm, lumpedStraightPipe3.h, lumpedStraightPipe3.fluid, lumpedStraightPipe3.mode, 0.1, 0.1, 0.1, 0.0) [dynamic |0|0|0|0|] 129/160 (1): lumpedStraightPipe1.C1.h = lumpedStraightPipe1.C2.h [dynamic |0|0|0|0|] 130/161 (1): lumpedStraightPipe1.C1.Q = lumpedStraightPipe1.C2.Q [dynamic |0|0|0|0|] 131/162 (1): lumpedStraightPipe1.C1.P - lumpedStraightPipe1.C2.P = lumpedStraightPipe1.deltaP [dynamic |0|0|0|0|] 132/163 (1): lumpedStraightPipe1.h = lumpedStraightPipe1.C1.h [dynamic |0|0|0|0|] 133/164 (1): lumpedStraightPipe1.Q = lumpedStraightPipe1.C1.Q [dynamic |0|0|0|0|] 134/165 (1): lumpedStraightPipe1.h = ThermoSysPro.Functions.SmoothCond(lumpedStraightPipe1.Q, lumpedStraightPipe1.C1.h_vol, lumpedStraightPipe1.C2.h_vol, 1.0) [dynamic |0|0|0|0|] 135/166 (1): lumpedStraightPipe1.deltaP = lumpedStraightPipe1.deltaPf + 9.80665 * lumpedStraightPipe1.rho * (lumpedStraightPipe1.z2 - lumpedStraightPipe1.z1) [dynamic |0|0|0|0|] 136/167 (1): lumpedStraightPipe1.deltaPf = 0.5 * lumpedStraightPipe1.khi * ThermoSysPro.Functions.ThermoSquare(lumpedStraightPipe1.Q, lumpedStraightPipe1.eps) / (lumpedStraightPipe1.A ^ 2.0 * lumpedStraightPipe1.rho) [dynamic |0|0|0|0|] 137/168 (1): lumpedStraightPipe1.khi = lumpedStraightPipe1.lam * lumpedStraightPipe1.L / lumpedStraightPipe1.D [dynamic |0|0|0|0|] 138/169 (1): lumpedStraightPipe1.lam = lumpedStraightPipe1.lambda [dynamic |0|0|0|0|] 139/170 (1): lumpedStraightPipe1.Relim = 5.6e6 [dynamic |0|0|0|0|] 140/171 (1): lumpedStraightPipe1.Re = 4.0 * abs(lumpedStraightPipe1.Q) / (lumpedStraightPipe1.mu * lumpedStraightPipe1.Pw) [dynamic |0|0|0|0|] 141/172 (1): lumpedStraightPipe1.Pm = 0.5 * (lumpedStraightPipe1.C1.P + lumpedStraightPipe1.C2.P) [dynamic |0|0|0|0|] 142/173 (10): lumpedStraightPipe1.pro = ThermoSysPro.Properties.Fluid.Ph(lumpedStraightPipe1.Pm, lumpedStraightPipe1.h, lumpedStraightPipe1.mode, lumpedStraightPipe1.fluid) [dynamic |0|0|0|0|] 143/183 (1): lumpedStraightPipe1.T = lumpedStraightPipe1.pro.T [dynamic |0|0|0|0|] 144/184 (1): lumpedStraightPipe1.rho = lumpedStraightPipe1.pro.d [dynamic |0|0|0|0|] 145/185 (1): lumpedStraightPipe1.mu = ThermoSysPro.Properties.Fluid.DynamicViscosity_Ph(lumpedStraightPipe1.Pm, lumpedStraightPipe1.h, lumpedStraightPipe1.fluid, lumpedStraightPipe1.mode, 0.1, 0.1, 0.1, 0.0) [dynamic |0|0|0|0|] 146/186 (1): new_Sink1.C.P = new_Sink1.P [dynamic |0|0|0|0|] 147/187 (1): new_Sink1.C.Q = new_Sink1.Q [dynamic |0|0|0|0|] 148/188 (1): new_Sink1.C.h_vol = new_Sink1.h [dynamic |0|0|0|0|] 149/189 (1): new_Sink1.ISpecificEnthalpy.signal = new_Sink1.h0 [dynamic |0|0|0|0|] 150/190 (1): new_Sink1.h = new_Sink1.ISpecificEnthalpy.signal [dynamic |0|0|0|0|] 151/191 (1): staticDrum1.Ce_eva.a = true [binding |0|0|0|0|] 152/192 (1): staticDrum1.Ce_eco.a = true [binding |0|0|0|0|] 153/193 (1): staticDrum1.Cs_sup.b = true [binding |0|0|0|0|] 154/194 (1): staticDrum1.Cs_eva.b = true [binding |0|0|0|0|] 155/195 (1): staticDrum1.Cs_sur.b = true [binding |0|0|0|0|] 156/196 (1): staticDrum1.Cs_purg.b = true [binding |0|0|0|0|] 157/197 (1): staticDrum1.Ce_steam.a = true [binding |0|0|0|0|] 158/198 (1): staticDrum1.Ce_sup.a = true [binding |0|0|0|0|] 159/199 (1): lumpedStraightPipe2.C1.a = true [binding |0|0|0|0|] 160/200 (1): lumpedStraightPipe2.C2.b = true [binding |0|0|0|0|] 161/201 (1): sourceQ1.C.b = true [binding |0|0|0|0|] 162/202 (1): sourceQ2.C.b = true [binding |0|0|0|0|] 163/203 (1): lumpedStraightPipe3.C1.a = true [binding |0|0|0|0|] 164/204 (1): lumpedStraightPipe3.C2.b = true [binding |0|0|0|0|] 165/205 (1): lumpedStraightPipe1.C1.a = true [binding |0|0|0|0|] 166/206 (1): lumpedStraightPipe1.C2.b = true [binding |0|0|0|0|] 167/207 (1): new_Sink1.C.a = true [binding |0|0|0|0|] Matching ======================================== 207 variables and equations var 1 is solved in eqn 39 var 2 is solved in eqn 207 var 3 is solved in eqn 40 var 4 is solved in eqn 37 var 5 is solved in eqn 188 var 6 is solved in eqn 36 var 7 is solved in eqn 189 var 8 is solved in eqn 190 var 9 is solved in eqn 187 var 10 is solved in eqn 186 var 11 is solved in eqn 182 var 12 is solved in eqn 181 var 13 is solved in eqn 180 var 14 is solved in eqn 179 var 15 is solved in eqn 178 var 16 is solved in eqn 177 var 17 is solved in eqn 176 var 18 is solved in eqn 175 var 19 is solved in eqn 184 var 20 is solved in eqn 173 var 21 is solved in eqn 206 var 22 is solved in eqn 38 var 23 is solved in eqn 160 var 24 is solved in eqn 161 var 25 is solved in eqn 41 var 26 is solved in eqn 172 var 27 is solved in eqn 33 var 28 is solved in eqn 205 var 29 is solved in eqn 163 var 30 is solved in eqn 31 var 31 is solved in eqn 35 var 32 is solved in eqn 30 var 33 is solved in eqn 165 var 34 is solved in eqn 174 var 35 is solved in eqn 183 var 36 is solved in eqn 185 var 37 is solved in eqn 167 var 38 is solved in eqn 169 var 39 is solved in eqn 170 var 40 is solved in eqn 171 var 41 is solved in eqn 164 var 42 is solved in eqn 162 var 43 is solved in eqn 166 var 44 is solved in eqn 168 var 45 is solved in eqn 156 var 46 is solved in eqn 155 var 47 is solved in eqn 154 var 48 is solved in eqn 153 var 49 is solved in eqn 152 var 50 is solved in eqn 151 var 51 is solved in eqn 150 var 52 is solved in eqn 149 var 53 is solved in eqn 148 var 54 is solved in eqn 147 var 55 is solved in eqn 204 var 56 is solved in eqn 26 var 57 is solved in eqn 28 var 58 is solved in eqn 135 var 59 is solved in eqn 139 var 60 is solved in eqn 24 var 61 is solved in eqn 21 var 62 is solved in eqn 203 var 63 is solved in eqn 134 var 64 is solved in eqn 19 var 65 is solved in eqn 23 var 66 is solved in eqn 136 var 67 is solved in eqn 137 var 68 is solved in eqn 146 var 69 is solved in eqn 157 var 70 is solved in eqn 159 var 71 is solved in eqn 158 var 72 is solved in eqn 143 var 73 is solved in eqn 144 var 74 is solved in eqn 145 var 75 is solved in eqn 138 var 76 is solved in eqn 140 var 77 is solved in eqn 141 var 78 is solved in eqn 142 var 79 is solved in eqn 202 var 80 is solved in eqn 20 var 81 is solved in eqn 22 var 82 is solved in eqn 128 var 83 is solved in eqn 129 var 84 is solved in eqn 18 var 85 is solved in eqn 132 var 86 is solved in eqn 130 var 87 is solved in eqn 133 var 88 is solved in eqn 131 var 89 is solved in eqn 127 var 90 is solved in eqn 201 var 91 is solved in eqn 8 var 92 is solved in eqn 10 var 93 is solved in eqn 121 var 94 is solved in eqn 122 var 95 is solved in eqn 6 var 96 is solved in eqn 125 var 97 is solved in eqn 123 var 98 is solved in eqn 126 var 99 is solved in eqn 124 var 100 is solved in eqn 120 var 101 is solved in eqn 116 var 102 is solved in eqn 115 var 103 is solved in eqn 114 var 104 is solved in eqn 113 var 105 is solved in eqn 112 var 106 is solved in eqn 111 var 107 is solved in eqn 110 var 108 is solved in eqn 109 var 109 is solved in eqn 108 var 110 is solved in eqn 107 var 111 is solved in eqn 200 var 112 is solved in eqn 14 var 113 is solved in eqn 94 var 114 is solved in eqn 95 var 115 is solved in eqn 17 var 116 is solved in eqn 12 var 117 is solved in eqn 9 var 118 is solved in eqn 199 var 119 is solved in eqn 97 var 120 is solved in eqn 7 var 121 is solved in eqn 11 var 122 is solved in eqn 96 var 123 is solved in eqn 99 var 124 is solved in eqn 106 var 125 is solved in eqn 117 var 126 is solved in eqn 119 var 127 is solved in eqn 118 var 128 is solved in eqn 103 var 129 is solved in eqn 104 var 130 is solved in eqn 105 var 131 is solved in eqn 98 var 132 is solved in eqn 100 var 133 is solved in eqn 101 var 134 is solved in eqn 102 var 135 is solved in eqn 42 var 136 is solved in eqn 93 var 137 is solved in eqn 89 var 138 is solved in eqn 88 var 139 is solved in eqn 87 var 140 is solved in eqn 86 var 141 is solved in eqn 85 var 142 is solved in eqn 84 var 143 is solved in eqn 83 var 144 is solved in eqn 82 var 145 is solved in eqn 81 var 146 is solved in eqn 80 var 147 is solved in eqn 90 var 148 is solved in eqn 77 var 149 is solved in eqn 76 var 150 is solved in eqn 79 var 151 is solved in eqn 45 var 152 is solved in eqn 198 var 153 is solved in eqn 44 var 154 is solved in eqn 43 var 155 is solved in eqn 66 var 156 is solved in eqn 59 var 157 is solved in eqn 15 var 158 is solved in eqn 197 var 159 is solved in eqn 16 var 160 is solved in eqn 13 var 161 is solved in eqn 69 var 162 is solved in eqn 58 var 163 is solved in eqn 196 var 164 is solved in eqn 54 var 165 is solved in eqn 53 var 166 is solved in eqn 52 var 167 is solved in eqn 70 var 168 is solved in eqn 63 var 169 is solved in eqn 195 var 170 is solved in eqn 57 var 171 is solved in eqn 56 var 172 is solved in eqn 55 var 173 is solved in eqn 73 var 174 is solved in eqn 65 var 175 is solved in eqn 194 var 176 is solved in eqn 51 var 177 is solved in eqn 50 var 178 is solved in eqn 49 var 179 is solved in eqn 72 var 180 is solved in eqn 62 var 181 is solved in eqn 193 var 182 is solved in eqn 32 var 183 is solved in eqn 34 var 184 is solved in eqn 74 var 185 is solved in eqn 71 var 186 is solved in eqn 64 var 187 is solved in eqn 27 var 188 is solved in eqn 192 var 189 is solved in eqn 75 var 190 is solved in eqn 25 var 191 is solved in eqn 29 var 192 is solved in eqn 61 var 193 is solved in eqn 48 var 194 is solved in eqn 191 var 195 is solved in eqn 47 var 196 is solved in eqn 46 var 197 is solved in eqn 67 var 198 is solved in eqn 60 var 199 is solved in eqn 91 var 200 is solved in eqn 68 var 201 is solved in eqn 78 var 202 is solved in eqn 92 var 203 is solved in eqn 1 var 204 is solved in eqn 2 var 205 is solved in eqn 3 var 206 is solved in eqn 4 var 207 is solved in eqn 5 Standard BLT of the original model:(207) ============================================================ 207: new_Sink1.h0: (5/5): (1): new_Sink1.h0 = 1e5 206: sourceQ2.h0: (4/4): (1): sourceQ2.h0 = 1e6 205: sourceQ2.Q0: (3/3): (1): sourceQ2.Q0 = 100.0 204: sourceQ1.h0: (2/2): (1): sourceQ1.h0 = 1e6 203: sourceQ1.Q0: (1/1): (1): sourceQ1.Q0 = 100.0 202: staticDrum1.T: (79/92): (1): staticDrum1.T = staticDrum1.lsat.T 201: staticDrum1.P: (76/78): (14): (staticDrum1.lsat, staticDrum1.vsat) = ThermoSysPro.Properties.WaterSteam.IF97.Water_sat_P(staticDrum1.P) 200: staticDrum1.hl: (68/68): (1): staticDrum1.Ce_eco.h_vol = staticDrum1.hl 199: staticDrum1.hv: (78/91): (1): staticDrum1.hv = staticDrum1.vsat.h 198: staticDrum1.Ce_eva.P: (60/60): (1): staticDrum1.P = staticDrum1.Ce_eva.P 197: staticDrum1.Ce_eva.h_vol: (67/67): (1): staticDrum1.Ce_eva.h_vol = staticDrum1.hl 196: staticDrum1.Ce_eva.Q: (46/46): (1): staticDrum1.Ce_eva.Q = 0.0 195: staticDrum1.Ce_eva.h: (47/47): (1): staticDrum1.Ce_eva.h = 1e5 194: staticDrum1.Ce_eva.a: (151/191): (1): staticDrum1.Ce_eva.a = true 193: staticDrum1.Ce_eva.b: (48/48): (1): staticDrum1.Ce_eva.b = true 192: staticDrum1.Ce_eco.P: (61/61): (1): staticDrum1.P = staticDrum1.Ce_eco.P 191: staticDrum1.Ce_eco.h_vol: (29/29): (1): lumpedStraightPipe3.C2.h_vol = staticDrum1.Ce_eco.h_vol 190: staticDrum1.Ce_eco.Q: (2 ...[truncated 190948 chars]... unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real -76: lumpedStraightPipe3.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Total pressure loss" type: Real -77: lumpedStraightPipe3.deltaPf:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Friction pressure loss" type: Real +76: lumpedStraightPipe3.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Total pressure loss" type: Real +77: lumpedStraightPipe3.deltaPf:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Friction pressure loss" type: Real 78: lumpedStraightPipe3.khi:VARIABLE() "Hydraulic pressure loss coefficient" type: Real 79: sourceQ2.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 80: sourceQ2.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -81: sourceQ2.C.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real +81: sourceQ2.C.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 82: sourceQ2.C.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real -83: sourceQ2.C.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -84: sourceQ2.C.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +83: sourceQ2.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +84: sourceQ2.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 85: sourceQ2.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 86: sourceQ2.IMassFlow.signal:VARIABLE(flow=false ) type: Real 87: sourceQ2.h:VARIABLE(unit = "J/kg" protected = true ) "Fluid specific enthalpy" type: Real 88: sourceQ2.Q:VARIABLE(unit = "kg/s" protected = true ) "Mass flow rate" type: Real -89: sourceQ2.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 protected = true ) "Fluid pressure" type: Real +89: sourceQ2.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true ) "Fluid pressure" type: Real 90: sourceQ1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 91: sourceQ1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -92: sourceQ1.C.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real +92: sourceQ1.C.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 93: sourceQ1.C.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real -94: sourceQ1.C.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -95: sourceQ1.C.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +94: sourceQ1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +95: sourceQ1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 96: sourceQ1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 97: sourceQ1.IMassFlow.signal:VARIABLE(flow=false ) type: Real 98: sourceQ1.h:VARIABLE(unit = "J/kg" protected = true ) "Fluid specific enthalpy" type: Real 99: sourceQ1.Q:VARIABLE(unit = "kg/s" protected = true ) "Mass flow rate" type: Real -100: sourceQ1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 protected = true ) "Fluid pressure" type: Real +100: sourceQ1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true ) "Fluid pressure" type: Real 101: lumpedStraightPipe2.pro.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 102: lumpedStraightPipe2.pro.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 103: lumpedStraightPipe2.pro.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 104: lumpedStraightPipe2.pro.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 105: lumpedStraightPipe2.pro.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -106: lumpedStraightPipe2.pro.cp:VARIABLE(min = 1e-09 max = 9.999999999999999e+59 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real -107: lumpedStraightPipe2.pro.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -108: lumpedStraightPipe2.pro.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -109: lumpedStraightPipe2.pro.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +106: lumpedStraightPipe2.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real +107: lumpedStraightPipe2.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +108: lumpedStraightPipe2.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +109: lumpedStraightPipe2.pro.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 110: lumpedStraightPipe2.pro.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 111: lumpedStraightPipe2.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 112: lumpedStraightPipe2.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -113: lumpedStraightPipe2.C2.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real +113: lumpedStraightPipe2.C2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 114: lumpedStraightPipe2.C2.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real -115: lumpedStraightPipe2.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -116: lumpedStraightPipe2.C2.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +115: lumpedStraightPipe2.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +116: lumpedStraightPipe2.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 117: lumpedStraightPipe2.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 118: lumpedStraightPipe2.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -119: lumpedStraightPipe2.C1.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real +119: lumpedStraightPipe2.C1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 120: lumpedStraightPipe2.C1.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real -121: lumpedStraightPipe2.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -122: lumpedStraightPipe2.C1.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +121: lumpedStraightPipe2.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +122: lumpedStraightPipe2.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 123: lumpedStraightPipe2.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real -124: lumpedStraightPipe2.Pm:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid average pressure" type: Real +124: lumpedStraightPipe2.Pm:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid average pressure" type: Real 125: lumpedStraightPipe2.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 126: lumpedStraightPipe2.mu:VARIABLE(min = 0.0 unit = "Pa.s" ) "Fluid dynamic viscosity" type: Real 127: lumpedStraightPipe2.rho:VARIABLE(min = 0.0 unit = "kg/m3" ) "Fluid density" type: Real 128: lumpedStraightPipe2.lam:VARIABLE() "Friction pressure loss coefficient" type: Real 129: lumpedStraightPipe2.Relim:VARIABLE(unit = "1" ) "Limit Reynolds number" type: Real 130: lumpedStraightPipe2.Re:VARIABLE(unit = "1" ) "Reynolds number" type: Real 131: lumpedStraightPipe2.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real -132: lumpedStraightPipe2.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Total pressure loss" type: Real -133: lumpedStraightPipe2.deltaPf:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Friction pressure loss" type: Real +132: lumpedStraightPipe2.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Total pressure loss" type: Real +133: lumpedStraightPipe2.deltaPf:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Friction pressure loss" type: Real 134: lumpedStraightPipe2.khi:VARIABLE() "Hydraulic pressure loss coefficient" type: Real 135: staticDrum1.Cth.W:VARIABLE(flow=true unit = "W" ) "Thermal flow rate. Positive when going into the component" type: Real 136: staticDrum1.Cth.T:VARIABLE(flow=false min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature" type: Real 137: staticDrum1.vsat.cv:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant volume" type: Real 138: staticDrum1.vsat.pt:VARIABLE() "Derivative of pressure wrt. temperature" type: Real 139: staticDrum1.vsat.cp:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant pressure" type: Real 140: staticDrum1.vsat.h:VARIABLE(unit = "J/kg" ) "Specific enthalpy" type: Real 141: staticDrum1.vsat.rho:VARIABLE(min = 0.0 unit = "kg/m3" ) "Density" type: Real 142: staticDrum1.vsat.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature" type: Real -143: staticDrum1.vsat.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Pressure" type: Real +143: staticDrum1.vsat.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Pressure" type: Real 144: staticDrum1.lsat.cv:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant volume" type: Real 145: staticDrum1.lsat.pt:VARIABLE() "Derivative of pressure wrt. temperature" type: Real 146: staticDrum1.lsat.cp:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant pressure" type: Real 147: staticDrum1.lsat.h:VARIABLE(unit = "J/kg" ) "Specific enthalpy" type: Real 148: staticDrum1.lsat.rho:VARIABLE(min = 0.0 unit = "kg/m3" ) "Density" type: Real 149: staticDrum1.lsat.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature" type: Real -150: staticDrum1.lsat.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Pressure" type: Real +150: staticDrum1.lsat.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Pressure" type: Real 151: staticDrum1.Ce_sup.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 152: staticDrum1.Ce_sup.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -153: staticDrum1.Ce_sup.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real +153: staticDrum1.Ce_sup.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 154: staticDrum1.Ce_sup.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real -155: staticDrum1.Ce_sup.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -156: staticDrum1.Ce_sup.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +155: staticDrum1.Ce_sup.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +156: staticDrum1.Ce_sup.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 157: staticDrum1.Ce_steam.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 158: staticDrum1.Ce_steam.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -159: staticDrum1.Ce_steam.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real +159: staticDrum1.Ce_steam.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 160: staticDrum1.Ce_steam.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real -161: staticDrum1.Ce_steam.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -162: staticDrum1.Ce_steam.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +161: staticDrum1.Ce_steam.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +162: staticDrum1.Ce_steam.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 163: staticDrum1.Cs_purg.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 164: staticDrum1.Cs_purg.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -165: staticDrum1.Cs_purg.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real +165: staticDrum1.Cs_purg.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 166: staticDrum1.Cs_purg.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real -167: staticDrum1.Cs_purg.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -168: staticDrum1.Cs_purg.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +167: staticDrum1.Cs_purg.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +168: staticDrum1.Cs_purg.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 169: staticDrum1.Cs_sur.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 170: staticDrum1.Cs_sur.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -171: staticDrum1.Cs_sur.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real +171: staticDrum1.Cs_sur.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 172: staticDrum1.Cs_sur.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real -173: staticDrum1.Cs_sur.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -174: staticDrum1.Cs_sur.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +173: staticDrum1.Cs_sur.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +174: staticDrum1.Cs_sur.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 175: staticDrum1.Cs_eva.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 176: staticDrum1.Cs_eva.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -177: staticDrum1.Cs_eva.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real +177: staticDrum1.Cs_eva.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 178: staticDrum1.Cs_eva.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real -179: staticDrum1.Cs_eva.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -180: staticDrum1.Cs_eva.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +179: staticDrum1.Cs_eva.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +180: staticDrum1.Cs_eva.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 181: staticDrum1.Cs_sup.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 182: staticDrum1.Cs_sup.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -183: staticDrum1.Cs_sup.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real +183: staticDrum1.Cs_sup.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 184: staticDrum1.Cs_sup.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real -185: staticDrum1.Cs_sup.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -186: staticDrum1.Cs_sup.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +185: staticDrum1.Cs_sup.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +186: staticDrum1.Cs_sup.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 187: staticDrum1.Ce_eco.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 188: staticDrum1.Ce_eco.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -189: staticDrum1.Ce_eco.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real +189: staticDrum1.Ce_eco.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 190: staticDrum1.Ce_eco.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real -191: staticDrum1.Ce_eco.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -192: staticDrum1.Ce_eco.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +191: staticDrum1.Ce_eco.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +192: staticDrum1.Ce_eco.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 193: staticDrum1.Ce_eva.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 194: staticDrum1.Ce_eva.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -195: staticDrum1.Ce_eva.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real +195: staticDrum1.Ce_eva.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 196: staticDrum1.Ce_eva.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real -197: staticDrum1.Ce_eva.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -198: staticDrum1.Ce_eva.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real -199: staticDrum1.hv:VARIABLE(start = 2800000.0 unit = "J/kg" ) "Gas phase specific enthalpy" type: Real -200: staticDrum1.hl:VARIABLE(start = 100000.0 unit = "J/kg" ) "Liquid phase specific enthalpy" type: Real -201: staticDrum1.P:VARIABLE(min = 0.0 start = 1000000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure" type: Real +197: staticDrum1.Ce_eva.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +198: staticDrum1.Ce_eva.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real +199: staticDrum1.hv:VARIABLE(start = 2.8e6 unit = "J/kg" ) "Gas phase specific enthalpy" type: Real +200: staticDrum1.hl:VARIABLE(start = 1e5 unit = "J/kg" ) "Liquid phase specific enthalpy" type: Real +201: staticDrum1.P:VARIABLE(min = 0.0 start = 1e6 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 202: staticDrum1.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 203: sourceQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 204: sourceQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real 205: sourceQ2.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 206: sourceQ2.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real @@ -1115,14 +1115,14 @@ OrderedEquation (167, 207) ======================================== 1/1 (1): lumpedStraightPipe1.Q = 0.0 [binding |0|0|0|0|] 2/2 (1): lumpedStraightPipe3.Q = 0.0 [binding |0|0|0|0|] 3/3 (1): sourceQ1.Q0 = 100.0 [binding |0|0|0|0|] -4/4 (1): sourceQ1.h0 = 1000000.0 [binding |0|0|0|0|] +4/4 (1): sourceQ1.h0 = 1e6 [binding |0|0|0|0|] 5/5 (1): sourceQ2.Q0 = 100.0 [binding |0|0|0|0|] -6/6 (1): sourceQ2.h0 = 1000000.0 [binding |0|0|0|0|] -7/7 (1): new_Sink1.h0 = 100000.0 [binding |0|0|0|0|] +6/6 (1): sourceQ2.h0 = 1e6 [binding |0|0|0|0|] +7/7 (1): new_Sink1.h0 = 1e5 [binding |0|0|0|0|] 8/8 (1): sourceQ1.C.P = lumpedStraightPipe2.C1.P [dynamic |0|0|0|0|] 9/9 (1): sourceQ1.C.Q = lumpedStraightPipe2.C1.Q [dynamic |0|0|0|0|] 10/10 (1): sourceQ1.C.a = lumpedStraightPipe2.C1.a [dynamic |0|0|0|0|] 11/11 (1): sourceQ1.C.b = lumpedStraightPipe2.C1.b [dynamic |0|0|0|0|] 12/12 (1): sourceQ1.C.h = lumpedStraightPipe2.C1.h [dynamic |0|0|0|0|] @@ -1157,23 +1157,23 @@ 41/41 (1): lumpedStraightPipe1.C2.b = new_Sink1.C.b [dynamic |0|0|0|0|] 42/42 (1): lumpedStraightPipe1.C2.h = new_Sink1.C.h [dynamic |0|0|0|0|] 43/43 (1): lumpedStraightPipe1.C2.h_vol = new_Sink1.C.h_vol [dynamic |0|0|0|0|] 44/44 (1): staticDrum1.Cth.W = 0.0 [dynamic |0|0|0|0|] 45/45 (1): staticDrum1.Ce_sup.Q = 0.0 [dynamic |0|0|0|0|] -46/46 (1): staticDrum1.Ce_sup.h = 100000.0 [dynamic |0|0|0|0|] +46/46 (1): staticDrum1.Ce_sup.h = 1e5 [dynamic |0|0|0|0|] 47/47 (1): staticDrum1.Ce_sup.b = true [dynamic |0|0|0|0|] 48/48 (1): staticDrum1.Ce_eva.Q = 0.0 [dynamic |0|0|0|0|] -49/49 (1): staticDrum1.Ce_eva.h = 100000.0 [dynamic |0|0|0|0|] +49/49 (1): staticDrum1.Ce_eva.h = 1e5 [dynamic |0|0|0|0|] 50/50 (1): staticDrum1.Ce_eva.b = true [dynamic |0|0|0|0|] 51/51 (1): staticDrum1.Cs_eva.Q = 0.0 [dynamic |0|0|0|0|] -52/52 (1): staticDrum1.Cs_eva.h = 100000.0 [dynamic |0|0|0|0|] +52/52 (1): staticDrum1.Cs_eva.h = 1e5 [dynamic |0|0|0|0|] 53/53 (1): staticDrum1.Cs_eva.a = true [dynamic |0|0|0|0|] 54/54 (1): staticDrum1.Cs_purg.Q = 0.0 [dynamic |0|0|0|0|] -55/55 (1): staticDrum1.Cs_purg.h = 100000.0 [dynamic |0|0|0|0|] +55/55 (1): staticDrum1.Cs_purg.h = 1e5 [dynamic |0|0|0|0|] 56/56 (1): staticDrum1.Cs_purg.a = true [dynamic |0|0|0|0|] 57/57 (1): staticDrum1.Cs_sur.Q = 0.0 [dynamic |0|0|0|0|] -58/58 (1): staticDrum1.Cs_sur.h = 100000.0 [dynamic |0|0|0|0|] +58/58 (1): staticDrum1.Cs_sur.h = 1e5 [dynamic |0|0|0|0|] 59/59 (1): staticDrum1.Cs_sur.a = true [dynamic |0|0|0|0|] 60/60 (1): staticDrum1.P = staticDrum1.Ce_steam.P [dynamic |0|0|0|0|] 61/61 (1): staticDrum1.P = staticDrum1.Ce_sup.P [dynamic |0|0|0|0|] 62/62 (1): staticDrum1.P = staticDrum1.Ce_eva.P [dynamic |0|0|0|0|] 63/63 (1): staticDrum1.P = staticDrum1.Ce_eco.P [dynamic |0|0|0|0|] @@ -1200,15 +1200,15 @@ 84/97 (1): lumpedStraightPipe2.C1.Q = lumpedStraightPipe2.C2.Q [dynamic |0|0|0|0|] 85/98 (1): lumpedStraightPipe2.C1.P - lumpedStraightPipe2.C2.P = lumpedStraightPipe2.deltaP [dynamic |0|0|0|0|] 86/99 (1): lumpedStraightPipe2.h = lumpedStraightPipe2.C1.h [dynamic |0|0|0|0|] 87/100 (1): lumpedStraightPipe2.Q = lumpedStraightPipe2.C1.Q [dynamic |0|0|0|0|] 88/101 (1): lumpedStraightPipe2.h = ThermoSysPro.Functions.SmoothCond(lumpedStraightPipe2.Q, lumpedStraightPipe2.C1.h_vol, lumpedStraightPipe2.C2.h_vol, 1.0) [dynamic |0|0|0|0|] -89/102 (1): lumpedStraightPipe2.deltaP = lumpedStraightPipe2.deltaPf + 9.806649999999999 * lumpedStraightPipe2.rho * (lumpedStraightPipe2.z2 - lumpedStraightPipe2.z1) [dynamic |0|0|0|0|] +89/102 (1): lumpedStraightPipe2.deltaP = lumpedStraightPipe2.deltaPf + 9.80665 * lumpedStraightPipe2.rho * (lumpedStraightPipe2.z2 - lumpedStraightPipe2.z1) [dynamic |0|0|0|0|] 90/103 (1): lumpedStraightPipe2.deltaPf = 0.5 * lumpedStraightPipe2.khi * ThermoSysPro.Functions.ThermoSquare(lumpedStraightPipe2.Q, lumpedStraightPipe2.eps) / (lumpedStraightPipe2.A ^ 2.0 * lumpedStraightPipe2.rho) [dynamic |0|0|0|0|] 91/104 (1): lumpedStraightPipe2.khi = lumpedStraightPipe2.lam * lumpedStraightPipe2.L / lumpedStraightPipe2.D [dynamic |0|0|0|0|] 92/105 (1): lumpedStraightPipe2.lam = lumpedStraightPipe2.lambda [dynamic |0|0|0|0|] -93/106 (1): lumpedStraightPipe2.Relim = 5600000.0 [dynamic |0|0|0|0|] +93/106 (1): lumpedStraightPipe2.Relim = 5.6e6 [dynamic |0|0|0|0|] 94/107 (1): lumpedStraightPipe2.Re = 4.0 * abs(lumpedStraightPipe2.Q) / (lumpedStraightPipe2.mu * lumpedStraightPipe2.Pw) [dynamic |0|0|0|0|] 95/108 (1): lumpedStraightPipe2.Pm = 0.5 * (lumpedStraightPipe2.C1.P + lumpedStraightPipe2.C2.P) [dynamic |0|0|0|0|] 96/109 (10): lumpedStraightPipe2.pro = ThermoSysPro.Properties.Fluid.Ph(lumpedStraightPipe2.Pm, lumpedStraightPipe2.h, lumpedStraightPipe2.mode, lumpedStraightPipe2.fluid) [dynamic |0|0|0|0|] 97/119 (1): lumpedStraightPipe2.T = lumpedStraightPipe2.pro.T [dynamic |0|0|0|0|] 98/120 (1): lumpedStraightPipe2.rho = lumpedStraightPipe2.pro.d [dynamic |0|0|0|0|] @@ -1229,15 +1229,15 @@ 113/135 (1): lumpedStraightPipe3.C1.Q = lumpedStraightPipe3.C2.Q [dynamic |0|0|0|0|] 114/136 (1): lumpedStraightPipe3.C1.P - lumpedStraightPipe3.C2.P = lumpedStraightPipe3.deltaP [dynamic |0|0|0|0|] 115/137 (1): lumpedStraightPipe3.h = lumpedStraightPipe3.C1.h [dynamic |0|0|0|0|] 116/138 (1): lumpedStraightPipe3.Q = lumpedStraightPipe3.C1.Q [dynamic |0|0|0|0|] 117/139 (1): lumpedStraightPipe3.h = ThermoSysPro.Functions.SmoothCond(lumpedStraightPipe3.Q, lumpedStraightPipe3.C1.h_vol, lumpedStraightPipe3.C2.h_vol, 1.0) [dynamic |0|0|0|0|] -118/140 (1): lumpedStraightPipe3.deltaP = lumpedStraightPipe3.deltaPf + 9.806649999999999 * lumpedStraightPipe3.rho * (lumpedStraightPipe3.z2 - lumpedStraightPipe3.z1) [dynamic |0|0|0|0|] +118/140 (1): lumpedStraightPipe3.deltaP = lumpedStraightPipe3.deltaPf + 9.80665 * lumpedStraightPipe3.rho * (lumpedStraightPipe3.z2 - lumpedStraightPipe3.z1) [dynamic |0|0|0|0|] 119/141 (1): lumpedStraightPipe3.deltaPf = 0.5 * lumpedStraightPipe3.khi * ThermoSysPro.Functions.ThermoSquare(lumpedStraightPipe3.Q, lumpedStraightPipe3.eps) / (lumpedStraightPipe3.A ^ 2.0 * lumpedStraightPipe3.rho) [dynamic |0|0|0|0|] 120/142 (1): lumpedStraightPipe3.khi = lumpedStraightPipe3.lam * lumpedStraightPipe3.L / lumpedStraightPipe3.D [dynamic |0|0|0|0|] 121/143 (1): lumpedStraightPipe3.lam = lumpedStraightPipe3.lambda [dynamic |0|0|0|0|] -122/144 (1): lumpedStraightPipe3.Relim = 5600000.0 [dynamic |0|0|0|0|] +122/144 (1): lumpedStraightPipe3.Relim = 5.6e6 [dynamic |0|0|0|0|] 123/145 (1): lumpedStraightPipe3.Re = 4.0 * abs(lumpedStraightPipe3.Q) / (lumpedStraightPipe3.mu * lumpedStraightPipe3.Pw) [dynamic |0|0|0|0|] 124/146 (1): lumpedStraightPipe3.Pm = 0.5 * (lumpedStraightPipe3.C1.P + lumpedStraightPipe3.C2.P) [dynamic |0|0|0|0|] 125/147 (10): lumpedStraightPipe3.pro = ThermoSysPro.Properties.Fluid.Ph(lumpedStraightPipe3.Pm, lumpedStraightPipe3.h, lumpedStraightPipe3.mode, lumpedStraightPipe3.fluid) [dynamic |0|0|0|0|] 126/157 (1): lumpedStraightPipe3.T = lumpedStraightPipe3.pro.T [dynamic |0|0|0|0|] 127/158 (1): lumpedStraightPipe3.rho = lumpedStraightPipe3.pro.d [dynamic |0|0|0|0|] @@ -1246,15 +1246,15 @@ 130/161 (1): lumpedStraightPipe1.C1.Q = lumpedStraightPipe1.C2.Q [dynamic |0|0|0|0|] 131/162 (1): lumpedStraightPipe1.C1.P - lumpedStraightPipe1.C2.P = lumpedStraightPipe1.deltaP [dynamic |0|0|0|0|] 132/163 (1): lumpedStraightPipe1.h = lumpedStraightPipe1.C1.h [dynamic |0|0|0|0|] 133/164 (1): lumpedStraightPipe1.Q = lumpedStraightPipe1.C1.Q [dynamic |0|0|0|0|] 134/165 (1): lumpedStraightPipe1.h = ThermoSysPro.Functions.SmoothCond(lumpedStraightPipe1.Q, lumpedStraightPipe1.C1.h_vol, lumpedStraightPipe1.C2.h_vol, 1.0) [dynamic |0|0|0|0|] -135/166 (1): lumpedStraightPipe1.deltaP = lumpedStraightPipe1.deltaPf + 9.806649999999999 * lumpedStraightPipe1.rho * (lumpedStraightPipe1.z2 - lumpedStraightPipe1.z1) [dynamic |0|0|0|0|] +135/166 (1): lumpedStraightPipe1.deltaP = lumpedStraightPipe1.deltaPf + 9.80665 * lumpedStraightPipe1.rho * (lumpedStraightPipe1.z2 - lumpedStraightPipe1.z1) [dynamic |0|0|0|0|] 136/167 (1): lumpedStraightPipe1.deltaPf = 0.5 * lumpedStraightPipe1.khi * ThermoSysPro.Functions.ThermoSquare(lumpedStraightPipe1.Q, lumpedStraightPipe1.eps) / (lumpedStraightPipe1.A ^ 2.0 * lumpedStraightPipe1.rho) [dynamic |0|0|0|0|] 137/168 (1): lumpedStraightPipe1.khi = lumpedStraightPipe1.lam * lumpedStraightPipe1.L / lumpedStraightPipe1.D [dynamic |0|0|0|0|] 138/169 (1): lumpedStraightPipe1.lam = lumpedStraightPipe1.lambda [dynamic |0|0|0|0|] -139/170 (1): lumpedStraightPipe1.Relim = 5600000.0 [dynamic |0|0|0|0|] +139/170 (1): lumpedStraightPipe1.Relim = 5.6e6 [dynamic |0|0|0|0|] 140/171 (1): lumpedStraightPipe1.Re = 4.0 * abs(lumpedStraightPipe1.Q) / (lumpedStraightPipe1.mu * lumpedStraightPipe1.Pw) [dynamic |0|0|0|0|] 141/172 (1): lumpedStraightPipe1.Pm = 0.5 * (lumpedStraightPipe1.C1.P + lumpedStraightPipe1.C2.P) [dynamic |0|0|0|0|] 142/173 (10): lumpedStraightPipe1.pro = ThermoSysPro.Properties.Fluid.Ph(lumpedStraightPipe1.Pm, lumpedStraightPipe1.h, lumpedStraightPipe1.mode, lumpedStraightPipe1.fluid) [dynamic |0|0|0|0|] 143/183 (1): lumpedStraightPipe1.T = lumpedStraightPipe1.pro.T [dynamic |0|0|0|0|] 144/184 (1): lumpedStraightPipe1.rho = lumpedStraightPipe1.pro.d [dynamic |0|0|0|0|] @@ -1494,23 +1494,23 @@ var 207 is solved in eqn 7 Standard BLT of the original model:(207) ============================================================ -207: new_Sink1.h0: (7/7): (1): new_Sink1.h0 = 100000.0 -206: sourceQ2.h0: (6/6): (1): sourceQ2.h0 = 1000000.0 +207: new_Sink1.h0: (7/7): (1): new_Sink1.h0 = 1e5 +206: sourceQ2.h0: (6/6): (1): sourceQ2.h0 = 1e6 205: sourceQ2.Q0: (5/5): (1): sourceQ2.Q0 = 100.0 -204: sourceQ1.h0: (4/4): (1): sourceQ1.h0 = 1000000.0 +204: sourceQ1.h0: (4/4): (1): sourceQ1.h0 = 1e6 203: sourceQ1.Q0: (3/3): (1): sourceQ1.Q0 = 100.0 202: staticDrum1.T: (81/94): (1): staticDrum1.T = staticDrum1.lsat.T 201: staticDrum1.P: (78/80): (14): (staticDrum1.lsat, staticDrum1.vsat) = ThermoSysPro.Properties.WaterSteam.IF97.Water_sat_P(staticDrum1.P) 200: staticDrum1.hl: (70/70): (1): staticDrum1.Ce_eco.h_vol = staticDrum1.hl 199: staticDrum1.hv: (80/93): (1): staticDrum1.hv = staticDrum1.vsat.h 198: staticDrum1.Ce_eva.P: (62/62): (1): staticDrum1.P = staticDrum1.Ce_eva.P 197: staticDrum1.Ce_eva.h_vol: (69/69): (1): staticDrum1.Ce_eva.h_vol = staticDrum1.hl 196: staticDrum1.Ce_eva.Q: (48/48): (1): staticDrum1.Ce_eva.Q = 0.0 -195: staticDrum1.Ce_eva.h: (49/49): (1): staticDrum1.Ce_eva.h = 100000.0 +195: staticDrum1.Ce_eva.h: (49/49): (1): staticDrum1.Ce_eva.h = 1e5 194: staticDrum1.Ce_eva.a: (151/191): (1): staticDrum1.Ce_eva.a = true 193: staticDrum1.Ce_eva.b: (50/50): (1): staticDrum1.Ce_eva.b = true 192: staticDrum1.Ce_eco.P: (63/63): (1): staticDrum1.P = staticDrum1.Ce_eco.P 191: staticDrum1.Ce_eco.h_vol: (31/31): (1): lumpedStraightPipe3.C2.h_vol = staticDrum1.Ce_eco.h_vol 190: staticDrum1.Ce_eco.Q: (27/27): (1): lumpedStraightPipe3.C2.Q = staticDrum1.Ce_eco.Q @@ -1524,23 +1524,23 @@ 182: staticDrum1.Cs_sup.a: (34/34): (1): staticDrum1.Cs_sup.a = lumpedStraightPipe1.C1.a 181: staticDrum1.Cs_sup.b: (153/193): (1): staticDrum1.Cs_sup.b = true 180: staticDrum1.Cs_eva.P: (64/64): (1): staticDrum1.P = staticDrum1.Cs_eva.P 179: staticDrum1.Cs_eva.h_vol: (74/74): (1): staticDrum1.Cs_eva.h_vol = staticDrum1.hl 178: staticDrum1.Cs_eva.Q: (51/51): (1): staticDrum1.Cs_eva.Q = 0.0 -177: staticDrum1.Cs_eva.h: (52/52): (1): staticDrum1.Cs_eva.h = 100000.0 +177: staticDrum1.Cs_eva.h: (52/52): (1): staticDrum1.Cs_eva.h = 1e5 176: staticDrum1.Cs_eva.a: (53/53): (1): staticDrum1.Cs_eva.a = true 175: staticDrum1.Cs_eva.b: (154/194): (1): staticDrum1.Cs_eva.b = true 174: staticDrum1.Cs_sur.P: (67/67): (1): staticDrum1.P = staticDrum1.Cs_sur.P 173: staticDrum1.Cs_sur.h_vol: (75/75): (1): staticDrum1.Cs_sur.h_vol = (1.0 - staticDrum1.x) * staticDrum1.hl + staticDrum1.x * staticDrum1.hv 172: staticDrum1.Cs_sur.Q: (57/57): (1): staticDrum1.Cs_sur.Q = 0.0 -171: staticDrum1.Cs_sur.h: (58/58): (1): staticDrum1.Cs_sur.h = 100000.0 +171: staticDrum1.Cs_sur.h: (58/58): (1): staticDrum1.Cs_sur.h = 1e5 170: staticDrum1.Cs_sur.a: (59/59): (1): staticDrum1.Cs_sur.a = true 169: staticDrum1.Cs_sur.b: (155/195): (1): staticDrum1.Cs_sur.b = true 168: staticDrum1.Cs_purg.P: (65/65): (1): staticDrum1.P = staticDrum1.Cs_purg.P 167: staticDrum1.Cs_purg.h_vol: (72/72): (1): staticDrum1.Cs_purg.h_vol = staticDrum1.hl 166: staticDrum1.Cs_purg.Q: (54/54): (1): staticDrum1.Cs_purg.Q = 0.0 -165: staticDrum1.Cs_purg.h: (55/55): (1): staticDrum1.Cs_purg.h = 100000.0 +165: staticDrum1.Cs_purg.h: (55/55): (1): staticDrum1.Cs_purg.h = 1e5 164: staticDrum1.Cs_purg.a: (56/56): (1): staticDrum1.Cs_purg.a = true 163: staticDrum1.Cs_purg.b: (156/196): (1): staticDrum1.Cs_purg.b = true 162: staticDrum1.Ce_steam.P: (60/60): (1): staticDrum1.P = staticDrum1.Ce_steam.P 161: staticDrum1.Ce_steam.h_vol: (71/71): (1): staticDrum1.Ce_steam.h_vol = staticDrum1.hv 160: staticDrum1.Ce_steam.Q: (76/76): (1): staticDrum1.Ce_eco.Q + staticDrum1.Ce_steam.Q + staticDrum1.Ce_sup.Q + staticDrum1.Ce_eva.Q + (-staticDrum1.Cs_purg.Q) - staticDrum1.Cs_sup.Q - staticDrum1.Cs_sur.Q - staticDrum1.Cs_eva.Q = 0.0 @@ -1548,11 +1548,11 @@ 158: staticDrum1.Ce_steam.a: (157/197): (1): staticDrum1.Ce_steam.a = true 157: staticDrum1.Ce_steam.b: (17/17): (1): lumpedStraightPipe2.C2.b = staticDrum1.Ce_steam.b 156: staticDrum1.Ce_sup.P: (61/61): (1): staticDrum1.P = staticDrum1.Ce_sup.P 155: staticDrum1.Ce_sup.h_vol: (68/68): (1): staticDrum1.Ce_sup.h_vol = staticDrum1.hl 154: staticDrum1.Ce_sup.Q: (45/45): (1): staticDrum1.Ce_sup.Q = 0.0 -153: staticDrum1.Ce_sup.h: (46/46): (1): staticDrum1.Ce_sup.h = 100000.0 +153: staticDrum1.Ce_sup.h: (46/46): (1): staticDrum1.Ce_sup.h = 1e5 152: staticDrum1.Ce_sup.a: (158/198): (1): staticDrum1.Ce_sup.a = true 151: staticDrum1.Ce_sup.b: (47/47): (1): staticDrum1.Ce_sup.b = true 150: staticDrum1.lsat.P: (78/81): (14): (staticDrum1.lsat, staticDrum1.vsat) = ThermoSysPro.Properties.WaterSteam.IF97.Water_sat_P(staticDrum1.P) 149: staticDrum1.lsat.T: (78/78): (14): (staticDrum1.lsat, staticDrum1.vsat) = ThermoSysPro.Properties.WaterSteam.IF97.Water_sat_P(staticDrum1.P) 148: staticDrum1.lsat.rho: (78/79): (14): (staticDrum1.lsat, staticDrum1.vsat) = ThermoSysPro.Properties.WaterSteam.IF97.Water_sat_P(staticDrum1.P) @@ -1569,14 +1569,14 @@ 137: staticDrum1.vsat.cv: (78/91): (14): (staticDrum1.lsat, staticDrum1.vsat) = ThermoSysPro.Properties.WaterSteam.IF97.Water_sat_P(staticDrum1.P) 136: staticDrum1.Cth.T: (82/95): (1): staticDrum1.Cth.T = staticDrum1.T 135: staticDrum1.Cth.W: (44/44): (1): staticDrum1.Cth.W = 0.0 134: lumpedStraightPipe2.khi: (91/104): (1): lumpedStraightPipe2.khi = lumpedStraightPipe2.lam * lumpedStraightPipe2.L / lumpedStraightPipe2.D 133: lumpedStraightPipe2.deltaPf: (90/103): (1): lumpedStraightPipe2.deltaPf = 0.5 * lumpedStraightPipe2.khi * ThermoSysPro.Functions.ThermoSquare(lumpedStraightPipe2.Q, lumpedStraightPipe2.eps) / (lumpedStraightPipe2.A ^ 2.0 * lumpedStraightPipe2.rho) -132: lumpedStraightPipe2.deltaP: (89/102): (1): lumpedStraightPipe2.deltaP = lumpedStraightPipe2.deltaPf + 9.806649999999999 * lumpedStraightPipe2.rho * (lumpedStraightPipe2.z2 - lumpedStraightPipe2.z1) +132: lumpedStraightPipe2.deltaP: (89/102): (1): lumpedStraightPipe2.deltaP = lumpedStraightPipe2.deltaPf + 9.80665 * lumpedStraightPipe2.rho * (lumpedStraightPipe2.z2 - lumpedStraightPipe2.z1) 131: lumpedStraightPipe2.Q: (87/100): (1): lumpedStraightPipe2.Q = lumpedStraightPipe2.C1.Q 130: lumpedStraightPipe2.Re: (94/107): (1): lumpedStraightPipe2.Re = 4.0 * abs(lumpedStraightPipe2.Q) / (lumpedStraightPipe2.mu * lumpedStraightPipe2.Pw) -129: lumpedStraightPipe2.Relim: (93/106): (1): lumpedStraightPipe2.Relim = 5600000.0 +129: lumpedStraightPipe2.Relim: (93/106): (1): lumpedStraightPipe2.Relim = 5.6e6 128: lumpedStraightPipe2.lam: (92/105): (1): lumpedStraightPipe2.lam = lumpedStraightPipe2.lambda 127: lumpedStraightPipe2.rho: (98/120): (1): lumpedStraightPipe2.rho = lumpedStraightPipe2.pro.d 126: lumpedStraightPipe2.mu: (99/121): (1): lumpedStraightPipe2.mu = ThermoSysPro.Properties.Fluid.DynamicViscosity_Ph(lumpedStraightPipe2.Pm, lumpedStraightPipe2.h, lumpedStraightPipe2.fluid, lumpedStraightPipe2.mode, 0.1, 0.1, 0.1, 0.0) 125: lumpedStraightPipe2.T: (97/119): (1): lumpedStraightPipe2.T = lumpedStraightPipe2.pro.T 124: lumpedStraightPipe2.Pm: (95/108): (1): lumpedStraightPipe2.Pm = 0.5 * (lumpedStraightPipe2.C1.P + lumpedStraightPipe2.C2.P) @@ -1625,14 +1625,14 @@ 81: sourceQ2.C.h: (24/24): (1): sourceQ2.C.h = lumpedStraightPipe3.C1.h 80: sourceQ2.C.a: (22/22): (1): sourceQ2.C.a = lumpedStraightPipe3.C1.a 79: sourceQ2.C.b: (162/202): (1): sourceQ2.C.b = true 78: lumpedStraightPipe3.khi: (120/142): (1): lumpedStraightPipe3.khi = lumpedStraightPipe3.lam * lumpedStraightPipe3.L / lumpedStraightPipe3.D 77: lumpedStraightPipe3.deltaPf: (119/141): (1): lumpedStraightPipe3.deltaPf = 0.5 * lumpedStraightPipe3.khi * ThermoSysPro.Functions.ThermoSquare(lumpedStraightPipe3.Q, lumpedStraightPipe3.eps) / (lumpedStraightPipe3.A ^ 2.0 * lumpedStraightPipe3.rho) -76: lumpedStraightPipe3.deltaP: (118/140): (1): lumpedStraightPipe3.deltaP = lumpedStraightPipe3.deltaPf + 9.806649999999999 * lumpedStraightPipe3.rho * (lumpedStraightPipe3.z2 - lumpedStraightPipe3.z1) +76: lumpedStraightPipe3.deltaP: (118/140): (1): lumpedStraightPipe3.deltaP = lumpedStraightPipe3.deltaPf + 9.80665 * lumpedStraightPipe3.rho * (lumpedStraightPipe3.z2 - lumpedStraightPipe3.z1) 75: lumpedStraightPipe3.Q: (2/2): (1): lumpedStraightPipe3.Q = 0.0 74: lumpedStraightPipe3.Re: (123/145): (1): lumpedStraightPipe3.Re = 4.0 * abs(lumpedStraightPipe3.Q) / (lumpedStraightPipe3.mu * lumpedStraightPipe3.Pw) -73: lumpedStraightPipe3.Relim: (122/144): (1): lumpedStraightPipe3.Relim = 5600000.0 +73: lumpedStraightPipe3.Relim: (122/144): (1): lumpedStraightPipe3.Relim = 5.6e6 72: lumpedStraightPipe3.lam: (121/143): (1): lumpedStraightPipe3.lam = lumpedStraightPipe3.lambda 71: lumpedStraightPipe3.rho: (127/158): (1): lumpedStraightPipe3.rho = lumpedStraightPipe3.pro.d 70: lumpedStraightPipe3.mu: (128/159): (1): lumpedStraightPipe3.mu = ThermoSysPro.Properties.Fluid.DynamicViscosity_Ph(lumpedStraightPipe3.Pm, lumpedStraightPipe3.h, lumpedStraightPipe3.fluid, lumpedStraightPipe3.mode, 0.1, 0.1, 0.1, 0.0) 69: lumpedStraightPipe3.T: (126/157): (1): lumpedStraightPipe3.T = lumpedStraightPipe3.pro.T 68: lumpedStraightPipe3.Pm: (124/146): (1): lumpedStraightPipe3.Pm = 0.5 * (lumpedStraightPipe3.C1.P + lumpedStraightPipe3.C2.P) @@ -1658,15 +1658,15 @@ 48: lumpedStraightPipe3.pro.ddph: (125/153): (10): lumpedStraightPipe3.pro = ThermoSysPro.Properties.Fluid.Ph(lumpedStraightPipe3.Pm, lumpedStraightPipe3.h, lumpedStraightPipe3.mode, lumpedStraightPipe3.fluid) 47: lumpedStraightPipe3.pro.duph: (125/154): (10): lumpedStraightPipe3.pro = ThermoSysPro.Properties.Fluid.Ph(lumpedStraightPipe3.Pm, lumpedStraightPipe3.h, lumpedStraightPipe3.mode, lumpedStraightPipe3.fluid) 46: lumpedStraightPipe3.pro.duhp: (125/155): (10): lumpedStraightPipe3.pro = ThermoSysPro.Properties.Fluid.Ph(lumpedStraightPipe3.Pm, lumpedStraightPipe3.h, lumpedStraightPipe3.mode, lumpedStraightPipe3.fluid) 45: lumpedStraightPipe3.pro.x: (125/156): (10): lumpedStraightPipe3.pro = ThermoSysPro.Properties.Fluid.Ph(lumpedStraightPipe3.Pm, lumpedStraightPipe3.h, lumpedStraightPipe3.mode, lumpedStraightPipe3.fluid) 44: lumpedStraightPipe1.khi: (137/168): (1): lumpedStraightPipe1.khi = lumpedStraightPipe1.lam * lumpedStraightPipe1.L / lumpedStraightPipe1.D -43: lumpedStraightPipe1.deltaPf: (135/166): (1): lumpedStraightPipe1.deltaP = lumpedStraightPipe1.deltaPf + 9.806649999999999 * lumpedStraightPipe1.rho * (lumpedStraightPipe1.z2 - lumpedStraightPipe1.z1) +43: lumpedStraightPipe1.deltaPf: (135/166): (1): lumpedStraightPipe1.deltaP = lumpedStraightPipe1.deltaPf + 9.80665 * lumpedStraightPipe1.rho * (lumpedStraightPipe1.z2 - lumpedStraightPipe1.z1) 42: lumpedStraightPipe1.deltaP: (131/162): (1): lumpedStraightPipe1.C1.P - lumpedStraightPipe1.C2.P = lumpedStraightPipe1.deltaP 41: lumpedStraightPipe1.Q: (1/1): (1): lumpedStraightPipe1.Q = 0.0 40: lumpedStraightPipe1.Re: (140/171): (1): lumpedStraightPipe1.Re = 4.0 * abs(lumpedStraightPipe1.Q) / (lumpedStraightPipe1.mu * lumpedStraightPipe1.Pw) -39: lumpedStraightPipe1.Relim: (139/170): (1): lumpedStraightPipe1.Relim = 5600000.0 +39: lumpedStraightPipe1.Relim: (139/170): (1): lumpedStraightPipe1.Relim = 5.6e6 38: lumpedStraightPipe1.lam: (138/169): (1): lumpedStraightPipe1.lam = lumpedStraightPipe1.lambda 37: lumpedStraightPipe1.rho: (136/167): (1): lumpedStraightPipe1.deltaPf = 0.5 * lumpedStraightPipe1.khi * ThermoSysPro.Functions.ThermoSquare(lumpedStraightPipe1.Q, lumpedStraightPipe1.eps) / (lumpedStraightPipe1.A ^ 2.0 * lumpedStraightPipe1.rho) 36: lumpedStraightPipe1.mu: (145/185): (1): lumpedStraightPipe1.mu = ThermoSysPro.Properties.Fluid.DynamicViscosity_Ph(lumpedStraightPipe1.Pm, lumpedStraightPipe1.h, lumpedStraightPipe1.fluid, lumpedStraightPipe1.mode, 0.1, 0.1, 0.1, 0.0) 35: lumpedStraightPipe1.T: (143/183): (1): lumpedStraightPipe1.T = lumpedStraightPipe1.pro.T 34: lumpedStraightPipe1.Pm: (142/174): (10): lumpedStraightPipe1.pro = ThermoSysPro.Properties.Fluid.Ph(lumpedStraightPipe1.Pm, lumpedStraightPipe1.h, lumpedStraightPipe1.mode, lumpedStraightPipe1.fluid) @@ -1739,14 +1739,14 @@ 169: staticDrum1.Cs_sur.b: (155/195): (1): staticDrum1.Cs_sur.b = true 175: staticDrum1.Cs_eva.b: (154/194): (1): staticDrum1.Cs_eva.b = true 181: staticDrum1.Cs_sup.b: (153/193): (1): staticDrum1.Cs_sup.b = true 188: staticDrum1.Ce_eco.a: (152/192): (1): staticDrum1.Ce_eco.a = true 194: staticDrum1.Ce_eva.a: (151/191): (1): staticDrum1.Ce_eva.a = true -207: new_Sink1.h0: (7/7): (1): new_Sink1.h0 = 100000.0 -206: sourceQ2.h0: (6/6): (1): sourceQ2.h0 = 1000000.0 +207: new_Sink1.h0: (7/7): (1): new_Sink1.h0 = 1e5 +206: sourceQ2.h0: (6/6): (1): sourceQ2.h0 = 1e6 205: sourceQ2.Q0: (5/5): (1): sourceQ2.Q0 = 100.0 -204: sourceQ1.h0: (4/4): (1): sourceQ1.h0 = 1000000.0 +204: sourceQ1.h0: (4/4): (1): sourceQ1.h0 = 1e6 203: sourceQ1.Q0: (3/3): (1): sourceQ1.Q0 = 100.0 75: lumpedStraightPipe3.Q: (2/2): (1): lumpedStraightPipe3.Q = 0.0 41: lumpedStraightPipe1.Q: (1/1): (1): lumpedStraightPipe1.Q = 0.0 @@ -1878,17 +1878,18 @@ ========================================================================== -Passed Set_S has 13 equations and 13 variables record SimulationResult -resultFile = "econcile", -simulationOptions = "startTime = 0.0, stopTime = 1.0, numberOfIntervals = 500, tolerance = 1e-06, method = 'dassl', fileNamePrefix = 'NewDataReconciliationSimpleTests.TSP_Splitter7', options = '', outputFormat = 'mat', variableFilter = '.*', cflags = '', simflags = '-reconcile -sx=./NewDataReconciliationSimpleTests/resources/DataReconciliationSimpleTests.TSP_Splitter7_Inputs.csv -eps=0.0023 -lv=LOG_JAC'", -messages = "LOG_SUCCESS | info | The initialization finished successfully without homotopy method. +resultFile = "", +simulationOptions = "startTime = 0.0, stopTime = 1.0, numberOfIntervals = 500, tolerance = 1e-6, method = 'dassl', fileNamePrefix = 'NewDataReconciliationSimpleTests.TSP_Splitter7', options = '', outputFormat = 'mat', variableFilter = '.*', cflags = '', simflags = '-reconcile -sx=./NewDataReconciliationSimpleTests/resources/DataReconciliationSimpleTests.TSP_Splitter7_Inputs.csv -eps=0.0023 -lv=LOG_JAC'", +messages = "Simulation execution failed for model: NewDataReconciliationSimpleTests.TSP_Splitter7 +LOG_SUCCESS | info | The initialization finished successfully without homotopy method. LOG_SUCCESS | info | The simulation finished successfully. LOG_STDOUT | info | DataReconciliation Starting! LOG_STDOUT | info | NewDataReconciliationSimpleTests.TSP_Splitter7 -LOG_STDOUT | info | DataReconciliation Completed! +LOG_STDOUT | error | Measurement input file path not found ./NewDataReconciliationSimpleTests/resources/DataReconciliationSimpleTests.TSP_Splitter7_Inputs.csv. " end SimulationResult; "[ThermoSysPro 3.2.0/WaterSteam/Junctions/StaticDrum.mo:13:3-15:24:writable] Warning: Connector Ce_eva is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0). [ThermoSysPro 3.2.0/WaterSteam/Junctions/StaticDrum.mo:16:3-18:24:writable] Warning: Connector Ce_eco is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0). [ThermoSysPro 3.2.0/WaterSteam/Junctions/StaticDrum.mo:19:3-20:82:writable] Warning: Connector Cs_sup is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0). '' Equation mismatch: omc-diff says: ------------Failed 'e' '"' Line 1883: Text differs: expected: resultFile = "econcile", got: resultFile = "", == 1 out of 1 tests failed [openmodelica/dataReconciliation/TSP_Splitter7.mos_temp54, time: 20]