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Failed
openmodelica_dataReconciliation.TSP_FourFlows8.mos (from (result.xml))
Stacktrace
Output mismatch (see stdout for details)
Standard Output
+ TSP_FourFlows8 ... equation mismatch [time: 21] ==== Log C:\Windows\TEMP/omc-rtest-OpenModelica/openmodelica/dataReconciliation/TSP_FourFlows8.mos_temp1482/log-TSP_FourFlows8.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_FourFlows8 ========================================================================== OrderedVariables (284) ======================================== 1: source1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 2: source1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 3: source1.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: source1.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: source1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 6: source1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 7: source1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 8: source1.IMassFlow.signal:VARIABLE(flow=false ) type: Real 9: source1.h:VARIABLE(unit = "J/kg" protected = true ) "Fluid specific enthalpy" type: Real 10: source1.Q:VARIABLE(unit = "kg/s" protected = true ) "Mass flow rate" type: Real 11: source1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true ) "Fluid pressure" type: Real 12: staticDrum2.Cs2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 13: staticDrum2.Cs2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 14: staticDrum2.Cs2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 15: staticDrum2.Cs2.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 16: staticDrum2.Cs2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 17: staticDrum2.Cs2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 18: staticDrum2.Cs1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 19: staticDrum2.Cs1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 20: staticDrum2.Cs1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 21: staticDrum2.Cs1.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 22: staticDrum2.Cs1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 23: staticDrum2.Cs1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 24: staticDrum2.Ce2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 25: staticDrum2.Ce2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 26: staticDrum2.Ce2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 27: staticDrum2.Ce2.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 28: staticDrum2.Ce2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 29: staticDrum2.Ce2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 30: staticDrum2.Ce1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 31: staticDrum2.Ce1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 32: staticDrum2.Ce1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 33: staticDrum2.Ce1.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 34: staticDrum2.Ce1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 35: staticDrum2.Ce1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 36: staticDrum2.pro.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 37: staticDrum2.pro.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 38: staticDrum2.pro.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 39: staticDrum2.pro.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 40: staticDrum2.pro.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 41: staticDrum2.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 42: staticDrum2.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 43: staticDrum2.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 44: staticDrum2.pro.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 45: staticDrum2.pro.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 46: staticDrum2.BH:VARIABLE(unit = "W" ) "Right hand side of the energybalance equation" type: Real 47: staticDrum2.BQ:VARIABLE(unit = "kg/s" ) "Right hand side of the mass balance equation" type: Real 48: staticDrum2.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 49: staticDrum2.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 50: staticDrum2.P:VARIABLE(min = 0.0 start = 2.5e6 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 51: staticDrum2.T:VARIABLE(min = 0.0 start = 471.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 52: staticDrum1.Cth.W:VARIABLE(flow=true unit = "W" ) "Thermal flow rate. Positive when going into the component" type: Real 53: staticDrum1.Cth.T:VARIABLE(flow=false min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature" type: Real 54: staticDrum1.vsat.cv:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant volume" type: Real 55: staticDrum1.vsat.pt:VARIABLE() "Derivative of pressure wrt. temperature" type: Real 56: staticDrum1.vsat.cp:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant pressure" type: Real 57: staticDrum1.vsat.h:VARIABLE(unit = "J/kg" ) "Specific enthalpy" type: Real 58: staticDrum1.vsat.rho:VARIABLE(min = 0.0 unit = "kg/m3" ) "Density" type: Real 59: staticDrum1.vsat.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature" type: Real 60: staticDrum1.vsat.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Pressure" type: Real 61: staticDrum1.lsat.cv:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant volume" type: Real 62: staticDrum1.lsat.pt:VARIABLE() "Derivative of pressure wrt. temperature" type: Real 63: staticDrum1.lsat.cp:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant pressure" type: Real 64: staticDrum1.lsat.h:VARIABLE(unit = "J/kg" ) "Specific enthalpy" type: Real 65: staticDrum1.lsat.rho:VARIABLE(min = 0.0 unit = "kg/m3" ) "Density" type: Real 66: staticDrum1.lsat.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature" type: Real 67: staticDrum1.lsat.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Pressure" type: Real 68: staticDrum1.Ce_sup.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 69: staticDrum1.Ce_sup.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 70: 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 71: 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 72: staticDrum1.Ce_sup.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 73: staticDrum1.Ce_sup.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 74: staticDrum1.Ce_steam.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 75: staticDrum1.Ce_steam.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 76: 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 77: 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 78: staticDrum1.Ce_steam.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 79: staticDrum1.Ce_steam.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 80: staticDrum1.Cs_purg.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 81: staticDrum1.Cs_purg.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 82: 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 83: 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 84: staticDrum1.Cs_purg.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 85: staticDrum1.Cs_purg.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 86: staticDrum1.Cs_sur.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 87: staticDrum1.Cs_sur.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 88: 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 89: 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 90: staticDrum1.Cs_sur.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 91: staticDrum1.Cs_sur.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 92: staticDrum1.Cs_eva.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 93: staticDrum1.Cs_eva.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 94: 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 95: 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 96: staticDrum1.Cs_eva.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 97: staticDrum1.Cs_eva.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 98: staticDrum1.Cs_sup.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 99: staticDrum1.Cs_sup.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 100: 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 101: 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 102: staticDrum1.Cs_sup.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 103: staticDrum1.Cs_sup.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 104: staticDrum1.Ce_eco.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 105: staticDrum1.Ce_eco.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 106: 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 107: 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 108: staticDrum1.Ce_eco.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 109: staticDrum1.Ce_eco.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 110: staticDrum1.Ce_eva.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 111: staticDrum1.Ce_eva.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 112: 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 113: 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 114: staticDrum1.Ce_eva.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 115: staticDrum1.Ce_eva.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 116: staticDrum1.hv:VARIABLE(start = 2.8e6 unit = "J/kg" ) "Gas phase specific enthalpy" type: Real 117: staticDrum1.hl:VARIABLE(start = 1e5 unit = "J/kg" ) "Liquid phase specific enthalpy" type: Real 118: staticDrum1.P:VARIABLE(min = 0.0 start = 2.9e6 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 119: staticDrum1.T:VARIABLE(min = 0.0 start = 473.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 120: singularPressureLoss4.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 121: singularPressureLoss4.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 122: singularPressureLoss4.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 123: singularPressureLoss4.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 124: singularPressureLoss4.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real 125: singularPressureLoss4.pro_pT.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 126: singularPressureLoss4.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 127: singularPressureLoss4.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 128: singularPressureLoss4.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real 129: singularPressureLoss4.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 130: singularPressureLoss4.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 131: singularPressureLoss4.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 132: singularPressureLoss4.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 133: singularPressureLoss4.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 134: singularPressureLoss4.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 135: singularPressureLoss4.pro_ph.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 136: singularPressureLoss4.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 137: singularPressureLoss4.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 138: singularPressureLoss4.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 139: singularPressureLoss4.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 140: singularPressureLoss4.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 141: singularPressureLoss4.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 142: singularPressureLoss4.C2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 143: singularPressureLoss4.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 144: singularPressureLoss4.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 145: singularPressureLoss4.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 146: singularPressureLoss4.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 147: singularPressureLoss4.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 148: singularPressureLoss4.C1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 149: singularPressureLoss4.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 150: singularPressureLoss4.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 151: singularPressureLoss4.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 152: singularPressureLoss4.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 153: singularPressureLoss4.Pm:VARIABLE(min = 0.0 start = 1.5e6 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 154: singularPressureLoss4.T:VARIABLE(min = 0.0 start = 472.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 155: singularPressureLoss4.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 156: singularPressureLoss4.Q:VARIABLE(start = 98.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real 157: singularPressureLoss4.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 158: singularPressureLoss3.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 159: singularPressureLoss3.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 160: singularPressureLoss3.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 161: singularPressureLoss3.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 162: singularPressureLoss3.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real 163: singularPressureLoss3.pro_pT.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 164: singularPressureLoss3.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 165: singularPressureLoss3.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 166: singularPressureLoss3.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real 167: singularPressureLoss3.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 168: singularPressureLoss3.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 169: singularPressureLoss3.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 170: singularPressureLoss3.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 171: singularPressureLoss3.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 172: singularPressureLoss3.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 173: singularPressureLoss3.pro_ph.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 174: singularPressureLoss3.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 175: singularPressureLoss3.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 176: singularPressureLoss3.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 177: singularPressureLoss3.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 178: singularPressureLoss3.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 179: singularPressureLoss3.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 180: singularPressureLoss3.C2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 181: singularPressureLoss3.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 182: singularPressureLoss3.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 183: singularPressureLoss3.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 184: singularPressureLoss3.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 185: singularPressureLoss3.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 186: singularPressureLoss3.C1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 187: singularPressureLoss3.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 188: singularPressureLoss3.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 189: singularPressureLoss3.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 190: singularPressureLoss3.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 191: singularPressureLoss3.Pm:VARIABLE(min = 0.0 start = 1.5e6 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 192: singularPressureLoss3.T:VARIABLE(min = 0.0 start = 465.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 193: singularPressureLoss3.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 194: singularPressureLoss3.Q:VARIABLE(start = 99.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real 195: singularPressureLoss3.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 196: singularPressureLoss2.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 197: singularPressureLoss2.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 198: singularPressureLoss2.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 199: singularPressureLoss2.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 200: singularPressureLoss2.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real 201: singularPressureLoss2.pro_pT.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 202: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 203: singularPressureLoss2.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 204: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real 205: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 206: singularPressureLoss2.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 207: singularPressureLoss2.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 208: singularPressureLoss2.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 209: singularPressureLoss2.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 210: singularPressureLoss2.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 211: singularPressureLoss2.pro_ph.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 212: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 213: singularPressureLoss2.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 214: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 215: singularPressureLoss2.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 216: singularPressureLoss2.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 217: singularPressureLoss2.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 218: singularPressureLoss2.C2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 219: singularPressureLoss2.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 220: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 221: singularPressureLoss2.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 222: singularPressureLoss2.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 223: singularPressureLoss2.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 224: singularPressureLoss2.C1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 225: singularPressureLoss2.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 226: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 227: singularPressureLoss2.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 228: singularPressureLoss2.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 229: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1.5e6 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 230: singularPressureLoss2.T:VARIABLE(min = 0.0 start = 470.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 231: singularPressureLoss2.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 232: singularPressureLoss2.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real 233: singularPressureLoss2.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 234: singularPressureLoss1.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 235: singularPressureLoss1.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 236: singularPressureLoss1.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 237: singularPressureLoss1.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 238: singularPressureLoss1.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real 239: singularPressureLoss1.pro_pT.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 240: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 241: singularPressureLoss1.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 242: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real 243: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 244: singularPressureLoss1.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 245: singularPressureLoss1.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 246: singularPressureLoss1.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 247: singularPressureLoss1.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 248: singularPressureLoss1.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 249: singularPressureLoss1.pro_ph.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 250: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 251: singularPressureLoss1.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 252: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 253: singularPressureLoss1.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 254: singularPressureLoss1.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 255: singularPressureLoss1.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 256: singularPressureLoss1.C2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 257: singularPressureLoss1.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 258: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 259: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 260: singularPressureLoss1.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 261: singularPressureLoss1.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 262: singularPressureLoss1.C1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 263: singularPressureLoss1.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 264: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 265: singularPressureLoss1.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 266: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 267: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1.5e6 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 268: singularPressureLoss1.T:VARIABLE(min = 0.0 start = 473.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 269: singularPressureLoss1.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 270: singularPressureLoss1.Q:VARIABLE(start = 100.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real 271: singularPressureLoss1.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 272: sink1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 273: sink1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 274: 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 275: 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 276: sink1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 277: sink1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 278: sink1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 279: sink1.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real 280: sink1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real 281: sink1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 282: sink1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real 283: source1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 284: source1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real OrderedEquation (226, 284) ======================================== 1/1 (1): sink1.h0 = 1e6 [binding |0|0|0|0|] 2/2 (1): source1.Q0 = 100.0 [binding |0|0|0|0|] 3/3 (1): source1.h0 = 1e6 [binding |0|0|0|0|] 4/4 (1): singularPressureLoss4.C2.P = sink1.C.P [dynamic |0|0|0|0|] 5/5 (1): singularPressureLoss4.C2.Q = sink1.C.Q [dynamic |0|0|0|0|] 6/6 (1): singularPressureLoss4.C2.a = sink1.C.a [dynamic |0|0|0|0|] 7/7 (1): singularPressureLoss4.C2.b = sink1.C.b [dynamic |0|0|0|0|] 8/8 (1): singularPressureLoss4.C2.h = sink1.C.h [dynamic |0|0|0|0|] 9/9 (1): singularPressureLoss4.C2.h_vol = sink1.C.h_vol [dynamic |0|0|0|0|] 10/10 (1): singularPressureLoss1.C2.P = staticDrum1.Ce_sup.P [dynamic |0|0|0|0|] 11/11 (1): singularPressureLoss1.C2.Q = staticDrum1.Ce_sup.Q [dynamic |0|0|0|0|] 12/12 (1): singularPressureLoss1.C2.a = staticDrum1.Ce_sup.a [dynamic |0|0|0|0|] 13/13 (1): singularPressureLoss1.C2.b = staticDrum1.Ce_sup.b [dynamic |0|0|0|0|] 14/14 (1): singularPressureLoss1.C2.h = staticDrum1.Ce_sup.h [dynamic |0|0|0|0|] 15/15 (1): singularPressureLoss1.C2.h_vol = staticDrum1.Ce_sup.h_vol [dynamic |0|0|0|0|] 16/16 (1): staticDrum1.Cs_sur.P = singularPressureLoss2.C1.P [dynamic |0|0|0|0|] 17/17 (1): staticDrum1.Cs_sur.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|] 18/18 (1): staticDrum1.Cs_sur.a = singularPressureLoss2.C1.a [dynamic |0|0|0|0|] 19/19 (1): staticDrum1.Cs_sur.b = singularPressureLoss2.C1.b [dynamic |0|0|0|0|] 20/20 (1): staticDrum1.Cs_sur.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|] 21/21 (1): staticDrum1.Cs_sur.h_vol = singularPressureLoss2.C1.h_vol [dynamic |0|0|0|0|] 22/22 (1): staticDrum1.Cs_eva.P = singularPressureLoss3.C1.P [dynamic |0|0|0|0|] 23/23 (1): staticDrum1.Cs_eva.Q = singularPressureLoss3.C1.Q [dynamic |0|0|0|0|] 24/24 (1): staticDrum1.Cs_eva.a = singularPressureLoss3.C1.a [dynamic |0|0|0|0|] 25/25 (1): staticDrum1.Cs_eva.b = singularPressureLoss3.C1.b [dynamic |0|0|0|0|] 26/26 (1): staticDrum1.Cs_eva.h = singularPressureLoss3.C1.h [dynamic |0|0|0|0|] 27/27 (1): staticDrum1.Cs_eva.h_vol = singularPressureLoss3.C1.h_vol [dynamic |0|0|0|0|] 28/28 (1): source1.C.P = singularPressureLoss1.C1.P [dynamic |0|0|0|0|] 29/29 (1): source1.C.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|] 30/30 (1): source1.C.a = singularPressureLoss1.C1.a [dynamic |0|0|0|0|] 31/31 (1): source1.C.b = singularPressureLoss1.C1.b [dynamic |0|0|0|0|] 32/32 (1): source1.C.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|] 33/33 (1): source1.C.h_vol = singularPressureLoss1.C1.h_vol [dynamic |0|0|0|0|] 34/34 (1): singularPressureLoss2.C2.P = staticDrum2.Ce2.P [dynamic |0|0|0|0|] 35/35 (1): singularPressureLoss2.C2.Q = staticDrum2.Ce2.Q [dynamic |0|0|0|0|] 36/36 (1): singularPressureLoss2.C2.a = staticDrum2.Ce2.a [dynamic |0|0|0|0|] 37/37 (1): singularPressureLoss2.C2.b = staticDrum2.Ce2.b [dynamic |0|0|0|0|] 38/38 (1): singularPressureLoss2.C2.h = staticDrum2.Ce2.h [dynamic |0|0|0|0|] 39/39 (1): singularPressureLoss2.C2.h_vol = staticDrum2.Ce2.h_vol [dynamic |0|0|0|0|] 40/40 (1): singularPressureLoss3.C2.P = staticDrum2.Ce1.P [dynamic |0|0|0|0|] 41/41 (1): singularPressureLoss3.C2.Q = staticDrum2.Ce1.Q [dynamic |0|0|0|0|] 42/42 (1): singularPressureLoss3.C2.a = staticDrum2.Ce1.a [dynamic |0|0|0|0|] 43/43 (1): singularPressureLoss3.C2.b = staticDrum2.Ce1.b [dynamic |0|0|0|0|] 44/44 (1): singularPressureLoss3.C2.h = staticDrum2.Ce1.h [dynamic |0|0|0|0|] 45/45 (1): singularPressureLoss3.C2.h_vol = staticDrum2.Ce1.h_vol [dynamic |0|0|0|0|] 46/46 (1): staticDrum2.Cs2.P = singularPressureLoss4.C1.P [dynamic |0|0|0|0|] 47/47 (1): staticDrum2.Cs2.Q = singularPressureLoss4.C1.Q [dynamic |0|0|0|0|] 48/48 (1): staticDrum2.Cs2.a = singularPressureLoss4.C1.a [dynamic |0|0|0|0|] 49/49 (1): staticDrum2.Cs2.b = singularPressureLoss4.C1.b [dynamic |0|0|0|0|] 50/50 (1): staticDrum2.Cs2.h = singularPressureLoss4.C1.h [dynamic |0|0|0|0|] 51/51 (1): staticDrum2.Cs2.h_vol = singularPressureLoss4.C1.h_vol [dynamic |0|0|0|0|] 52/52 (1): staticDrum1.Cth.W = 0.0 [dynamic |0|0|0|0|] 53/53 (1): sink1.C.P = sink1.P [dynamic |0|0|0|0|] 54/54 (1): sink1.C.Q = sink1.Q [dynamic |0|0|0|0|] 55/55 (1): sink1.C.h_vol = sink1.h [dynamic |0|0|0|0|] 56/56 (1): sink1.ISpecificEnthalpy.signal = sink1.h0 [dynamic |0|0|0|0|] 57/57 (1): sink1.h = sink1.ISpecificEnthalpy.signal [dynamic |0|0|0|0|] 58/58 (1): singularPressureLoss1.C1.P - singularPressureLoss1.C2.P = singularPressureLoss1.deltaP [dynamic |0|0|0|0|] 59/59 (1): singularPressureLoss1.C2.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|] 60/60 (1): singularPressureLoss1.C2.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|] 61/61 (1): singularPressureLoss1.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|] 62/62 (1): singularPressureLoss1.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|] 63/63 (1): 0.0 = singularPressureLoss1.C1.h - singularPressureLoss1.C1.h_vol [dynamic |0|0|0|0|] 64/64 (1): singularPressureLoss1.deltaP = singularPressureLoss1.K * singularPressureLoss1.Q * abs(singularPressureLoss1.Q) / singularPressureLoss1.rho [dynamic |0|0|0|0|] 65/65 (1): singularPressureLoss1.Pm = 0.5 * (singularPressureLoss1.C1.P + singularPressureLoss1.C2.P) [dynamic |0|0|0|0|] 66/66 (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) [dynamic |0|0|0|0|] 67/76 (1): singularPressureLoss1.h = singularPressureLoss1.pro_pT.h [dynamic |0|0|0|0|] 68/77 (1): singularPressureLoss1.rho = singularPressureLoss1.pro_pT.d [dynamic |0|0|0|0|] 69/78 (1): singularPressureLoss1.pro_ph.d = 0.0 [dynamic |0|0|0|0|] 70/79 (1): singularPressureLoss1.pro_ph.T = 0.0 [dynamic |0|0|0|0|] 71/80 (1): singularPressureLoss1.pro_ph.u = 0.0 [dynamic |0|0|0|0|] 72/81 (1): singularPressureLoss1.pro_ph.s = 0.0 [dynamic |0|0|0|0|] 73/82 (1): singularPressureLoss1.pro_ph.cp = 0.0 [dynamic |0|0|0|0|] 74/83 (1): singularPressureLoss1.pro_ph.ddhp = 0.0 [dynamic |0|0|0|0|] 75/84 (1): singularPressureLoss1.pro_ph.ddph = 0.0 [dynamic |0|0|0|0|] 76/85 (1): singularPressureLoss1.pro_ph.duph = 0.0 [dynamic |0|0|0|0|] 77/86 (1): singularPressureLoss1.pro_ph.duhp = 0.0 [dynamic |0|0|0|0|] 78/87 (1): singularPressureLoss1.pro_ph.x = 0.0 [dynamic |0|0|0|0|] 79/88 (1): singularPressureLoss2.C1.P - singularPressureLoss2.C2.P = singularPressureLoss2.deltaP [dynamic |0|0|0|0|] 80/89 (1): singularPressureLoss2.C2.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|] 81/90 (1): singularPressureLoss2.C2.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|] 82/91 (1): singularPressureLoss2.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|] 83/92 (1): singularPressureLoss2.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|] 84/93 (1): 0.0 = singularPressureLoss2.C1.h - singularPressureLoss2.C1.h_vol [dynamic |0|0|0|0|] 85/94 (1): singularPressureLoss2.deltaP = singularPressureLoss2.K * singularPressureLoss2.Q * abs(singularPressureLoss2.Q) / singularPressureLoss2.rho [dynamic |0|0|0|0|] 86/95 (1): singularPressureLoss2.Pm = 0.5 * (singularPressureLoss2.C1.P + singularPressureLoss2.C2.P) [dynamic |0|0|0|0|] 87/96 (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid) [dynamic |0|0|0|0|] 88/106 (1): singularPressureLoss2.h = singularPressureLoss2.pro_pT.h [dynamic |0|0|0|0|] 89/107 (1): singularPressureLoss2.rho = singularPressureLoss2.pro_pT.d [dynamic |0|0|0|0|] 90/108 (1): singularPressureLoss2.pro_ph.d = 0.0 [dynamic |0|0|0|0|] 91/109 (1): singularPressureLoss2.pro_ph.T = 0.0 [dynamic |0|0|0|0|] 92/110 (1): singularPressureLoss2.pro_ph.u = 0.0 [dynamic |0|0|0|0|] 93/111 (1): singularPressureLoss2.pro_ph.s = 0.0 [dynamic |0|0|0|0|] 94/112 (1): singularPressureLoss2.pro_ph.cp = 0.0 [dynamic |0|0|0|0|] 95/113 (1): singularPressureLoss2.pro_ph.ddhp = 0.0 [dynamic |0|0|0|0|] 96/114 (1): singularPressureLoss2.pro_ph.ddph = 0.0 [dynamic |0|0|0|0|] 97/115 (1): singularPressureLoss2.pro_ph.duph = 0.0 [dynamic |0|0|0|0|] 98/116 (1): singularPressureLoss2.pro_ph.duhp = 0.0 [dynamic |0|0|0|0|] 99/117 (1): singularPressureLoss2.pro_ph.x = 0.0 [dynamic |0|0|0|0|] 100/118 (1): singularPressureLoss3.C1.P - singularPressureLoss3.C2.P = singularPressureLoss3.deltaP [dynamic |0|0|0|0|] 101/119 (1): singularPressureLoss3.C2.Q = singularPressureLoss3.C1.Q [dynamic |0|0|0|0|] 102/120 (1): singularPressureLoss3.C2.h = singularPressureLoss3.C1.h [dynamic |0|0|0|0|] 103/121 (1): singularPressureLoss3.h = singularPressureLoss3.C1.h [dynamic |0|0|0|0|] 104/122 (1): singularPressureLoss3.Q = singularPressureLoss3.C1.Q [dynamic |0|0|0|0|] 105/123 (1): 0.0 = singularPressureLoss3.C1.h - singularPressureLoss3.C1.h_vol [dynamic |0|0|0|0|] 106/124 (1): singularPressureLoss3.deltaP = singularPressureLoss3.K * singularPressureLoss3.Q * abs(singularPressureLoss3.Q) / singularPressureLoss3.rho [dynamic |0|0|0|0|] 107/125 (1): singularPressureLoss3.Pm = 0.5 * (singularPressureLoss3.C1.P + singularPressureLoss3.C2.P) [dynamic |0|0|0|0|] 108/126 (10): singularPressureLoss3.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss3.Pm, singularPressureLoss3.T, singularPressureLoss3.mode, singularPressureLoss3.fluid) [dynamic |0|0|0|0|] 109/136 (1): singularPressureLoss3.h = singularPressureLoss3.pro_pT.h [dynamic |0|0|0|0|] 110/137 (1): singularPressureLoss3.rho = singularPressureLoss3.pro_pT.d [dynamic |0|0|0|0|] 111/138 (1): singularPressureLoss3.pro_ph.d = 0.0 [dynamic |0|0|0|0|] 112/139 (1): singularPressureLoss3.pro_ph.T = 0.0 [dynamic |0|0|0|0|] 113/140 (1): singularPressureLoss3.pro_ph.u = 0.0 [dynamic |0|0|0|0|] 114/141 (1): singularPressureLoss3.pro_ph.s = 0.0 [dynamic |0|0|0|0|] 115/142 (1): singularPressureLoss3.pro_ph.cp = 0.0 [dynamic |0|0|0|0|] 116/143 (1): singularPressureLoss3.pro_ph.ddhp = 0.0 [dynamic |0|0|0|0|] 117/144 (1): singularPressureLoss3.pro_ph.ddph = 0.0 [dynamic |0|0|0|0|] 118/145 (1): singularPressureLoss3.pro_ph.duph = 0.0 [dynamic |0|0|0|0|] 119/146 (1): singularPressureLoss3.pro_ph.duhp = 0.0 [dynamic |0|0|0|0|] 120/147 (1): singularPressureLoss3.pro_ph.x = 0.0 [dynamic |0|0|0|0|] 121/148 (1): singularPressureLoss4.C1.P - singularPressureLoss4.C2.P = singularPressureLoss4.deltaP [dynamic |0|0|0|0|] 122/149 (1): singularPressureLoss4.C2.Q = singularPressureLoss4.C1.Q [dynamic |0|0|0|0|] 123/150 (1): singularPressureLoss4.C2.h = singularPressureLoss4.C1.h [dynamic |0|0|0|0|] 124/151 (1): singularPressureLoss4.h = singularPressureLoss4.C1.h [dynamic |0|0|0|0|] 125/152 (1): singularPressureLoss4.Q = singularPressureLoss4.C1.Q [dynamic |0|0|0|0|] 126/153 (1): 0.0 = singularPressureLos ...[truncated 264644 chars]... nit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 107: 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 -108: staticDrum1.Ce_eco.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -109: 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 +108: staticDrum1.Ce_eco.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +109: staticDrum1.Ce_eco.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 110: staticDrum1.Ce_eva.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 111: staticDrum1.Ce_eva.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -112: 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 +112: 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 113: 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 -114: staticDrum1.Ce_eva.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -115: 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 -116: staticDrum1.hv:VARIABLE(start = 2800000.0 unit = "J/kg" ) "Gas phase specific enthalpy" type: Real -117: staticDrum1.hl:VARIABLE(start = 100000.0 unit = "J/kg" ) "Liquid phase specific enthalpy" type: Real -118: staticDrum1.P:VARIABLE(min = 0.0 start = 2900000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure" type: Real +114: staticDrum1.Ce_eva.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +115: staticDrum1.Ce_eva.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real +116: staticDrum1.hv:VARIABLE(start = 2.8e6 unit = "J/kg" ) "Gas phase specific enthalpy" type: Real +117: staticDrum1.hl:VARIABLE(start = 1e5 unit = "J/kg" ) "Liquid phase specific enthalpy" type: Real +118: staticDrum1.P:VARIABLE(min = 0.0 start = 2.9e6 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 119: staticDrum1.T:VARIABLE(min = 0.0 start = 473.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 120: singularPressureLoss4.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 121: singularPressureLoss4.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 122: singularPressureLoss4.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 123: singularPressureLoss4.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 124: singularPressureLoss4.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real -125: singularPressureLoss4.pro_pT.cp:VARIABLE(min = 1e-09 max = 9.999999999999999e+59 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real -126: singularPressureLoss4.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -127: singularPressureLoss4.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -128: singularPressureLoss4.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real -129: singularPressureLoss4.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +125: singularPressureLoss4.pro_pT.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real +126: singularPressureLoss4.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +127: singularPressureLoss4.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +128: singularPressureLoss4.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real +129: singularPressureLoss4.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 130: singularPressureLoss4.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 131: singularPressureLoss4.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 132: singularPressureLoss4.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 133: singularPressureLoss4.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 134: singularPressureLoss4.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -135: singularPressureLoss4.pro_ph.cp:VARIABLE(min = 1e-09 max = 9.999999999999999e+59 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real -136: singularPressureLoss4.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -137: singularPressureLoss4.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -138: singularPressureLoss4.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +135: singularPressureLoss4.pro_ph.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real +136: singularPressureLoss4.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +137: singularPressureLoss4.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +138: singularPressureLoss4.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 139: singularPressureLoss4.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 140: singularPressureLoss4.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 141: singularPressureLoss4.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -142: singularPressureLoss4.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 +142: singularPressureLoss4.C2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 143: singularPressureLoss4.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 -144: singularPressureLoss4.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -145: singularPressureLoss4.C2.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +144: singularPressureLoss4.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +145: singularPressureLoss4.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 146: singularPressureLoss4.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 147: singularPressureLoss4.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -148: singularPressureLoss4.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 +148: singularPressureLoss4.C1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 149: singularPressureLoss4.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 -150: singularPressureLoss4.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -151: singularPressureLoss4.C1.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real -152: singularPressureLoss4.h:VARIABLE(start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real -153: singularPressureLoss4.Pm:VARIABLE(min = 0.0 start = 1500000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real +150: singularPressureLoss4.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +151: singularPressureLoss4.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real +152: singularPressureLoss4.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real +153: singularPressureLoss4.Pm:VARIABLE(min = 0.0 start = 1.5e6 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 154: singularPressureLoss4.T:VARIABLE(min = 0.0 start = 472.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 155: singularPressureLoss4.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 156: singularPressureLoss4.Q:VARIABLE(start = 98.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real -157: singularPressureLoss4.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real +157: singularPressureLoss4.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 158: singularPressureLoss3.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 159: singularPressureLoss3.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 160: singularPressureLoss3.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 161: singularPressureLoss3.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 162: singularPressureLoss3.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real -163: singularPressureLoss3.pro_pT.cp:VARIABLE(min = 1e-09 max = 9.999999999999999e+59 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real -164: singularPressureLoss3.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -165: singularPressureLoss3.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -166: singularPressureLoss3.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real -167: singularPressureLoss3.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +163: singularPressureLoss3.pro_pT.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real +164: singularPressureLoss3.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +165: singularPressureLoss3.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +166: singularPressureLoss3.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real +167: singularPressureLoss3.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 168: singularPressureLoss3.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 169: singularPressureLoss3.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 170: singularPressureLoss3.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 171: singularPressureLoss3.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 172: singularPressureLoss3.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -173: singularPressureLoss3.pro_ph.cp:VARIABLE(min = 1e-09 max = 9.999999999999999e+59 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real -174: singularPressureLoss3.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -175: singularPressureLoss3.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -176: singularPressureLoss3.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +173: singularPressureLoss3.pro_ph.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real +174: singularPressureLoss3.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +175: singularPressureLoss3.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +176: singularPressureLoss3.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 177: singularPressureLoss3.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 178: singularPressureLoss3.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 179: singularPressureLoss3.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -180: singularPressureLoss3.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 +180: singularPressureLoss3.C2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 181: singularPressureLoss3.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 -182: singularPressureLoss3.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -183: singularPressureLoss3.C2.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +182: singularPressureLoss3.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +183: singularPressureLoss3.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 184: singularPressureLoss3.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 185: singularPressureLoss3.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -186: singularPressureLoss3.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 +186: singularPressureLoss3.C1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 187: singularPressureLoss3.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 -188: singularPressureLoss3.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -189: singularPressureLoss3.C1.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real -190: singularPressureLoss3.h:VARIABLE(start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real -191: singularPressureLoss3.Pm:VARIABLE(min = 0.0 start = 1500000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real +188: singularPressureLoss3.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +189: singularPressureLoss3.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real +190: singularPressureLoss3.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real +191: singularPressureLoss3.Pm:VARIABLE(min = 0.0 start = 1.5e6 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 192: singularPressureLoss3.T:VARIABLE(min = 0.0 start = 465.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 193: singularPressureLoss3.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 194: singularPressureLoss3.Q:VARIABLE(start = 99.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real -195: singularPressureLoss3.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real +195: singularPressureLoss3.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 196: singularPressureLoss2.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 197: singularPressureLoss2.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 198: singularPressureLoss2.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 199: singularPressureLoss2.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 200: singularPressureLoss2.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real -201: singularPressureLoss2.pro_pT.cp:VARIABLE(min = 1e-09 max = 9.999999999999999e+59 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real -202: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -203: singularPressureLoss2.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -204: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real -205: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +201: singularPressureLoss2.pro_pT.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real +202: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +203: singularPressureLoss2.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +204: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real +205: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 206: singularPressureLoss2.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 207: singularPressureLoss2.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 208: singularPressureLoss2.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 209: singularPressureLoss2.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 210: singularPressureLoss2.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -211: singularPressureLoss2.pro_ph.cp:VARIABLE(min = 1e-09 max = 9.999999999999999e+59 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real -212: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -213: singularPressureLoss2.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -214: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +211: singularPressureLoss2.pro_ph.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real +212: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +213: singularPressureLoss2.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +214: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 215: singularPressureLoss2.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 216: singularPressureLoss2.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 217: singularPressureLoss2.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -218: singularPressureLoss2.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 +218: singularPressureLoss2.C2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 219: singularPressureLoss2.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 -220: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -221: singularPressureLoss2.C2.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +220: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +221: singularPressureLoss2.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 222: singularPressureLoss2.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 223: singularPressureLoss2.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -224: singularPressureLoss2.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 +224: singularPressureLoss2.C1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 225: singularPressureLoss2.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 -226: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -227: singularPressureLoss2.C1.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real -228: singularPressureLoss2.h:VARIABLE(start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real -229: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1500000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real +226: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +227: singularPressureLoss2.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real +228: singularPressureLoss2.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real +229: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1.5e6 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 230: singularPressureLoss2.T:VARIABLE(min = 0.0 start = 470.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 231: singularPressureLoss2.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 232: singularPressureLoss2.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real -233: singularPressureLoss2.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real +233: singularPressureLoss2.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 234: singularPressureLoss1.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 235: singularPressureLoss1.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 236: singularPressureLoss1.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 237: singularPressureLoss1.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 238: singularPressureLoss1.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real -239: singularPressureLoss1.pro_pT.cp:VARIABLE(min = 1e-09 max = 9.999999999999999e+59 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real -240: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -241: singularPressureLoss1.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -242: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real -243: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +239: singularPressureLoss1.pro_pT.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real +240: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +241: singularPressureLoss1.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +242: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real +243: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 244: singularPressureLoss1.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 245: singularPressureLoss1.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 246: singularPressureLoss1.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 247: singularPressureLoss1.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 248: singularPressureLoss1.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -249: singularPressureLoss1.pro_ph.cp:VARIABLE(min = 1e-09 max = 9.999999999999999e+59 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real -250: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -251: singularPressureLoss1.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -252: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +249: singularPressureLoss1.pro_ph.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real +250: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +251: singularPressureLoss1.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +252: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 253: singularPressureLoss1.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 254: singularPressureLoss1.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 255: singularPressureLoss1.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -256: singularPressureLoss1.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 +256: singularPressureLoss1.C2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 257: singularPressureLoss1.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 -258: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -259: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +258: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +259: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 260: singularPressureLoss1.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 261: singularPressureLoss1.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -262: singularPressureLoss1.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 +262: singularPressureLoss1.C1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 263: singularPressureLoss1.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 -264: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -265: singularPressureLoss1.C1.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real -266: singularPressureLoss1.h:VARIABLE(start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real -267: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1500000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real +264: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +265: singularPressureLoss1.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real +266: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real +267: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1.5e6 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 268: singularPressureLoss1.T:VARIABLE(min = 0.0 start = 473.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 269: singularPressureLoss1.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 270: singularPressureLoss1.Q:VARIABLE(start = 100.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real -271: singularPressureLoss1.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real +271: singularPressureLoss1.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 272: sink1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 273: sink1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -274: sink1.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 +274: 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 275: 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 -276: sink1.C.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -277: sink1.C.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +276: sink1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +277: sink1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 278: sink1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 279: sink1.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real 280: sink1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real -281: sink1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure" type: Real +281: sink1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 282: sink1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real 283: source1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 284: source1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real OrderedEquation (226, 284) ======================================== 1/1 (1): singularPressureLoss4.Q = 0.0 [binding |0|0|0|0|] 2/2 (1): singularPressureLoss3.Q = 0.0 [binding |0|0|0|0|] -3/3 (1): sink1.h0 = 1000000.0 [binding |0|0|0|0|] +3/3 (1): sink1.h0 = 1e6 [binding |0|0|0|0|] 4/4 (1): source1.Q0 = 100.0 [binding |0|0|0|0|] -5/5 (1): source1.h0 = 1000000.0 [binding |0|0|0|0|] +5/5 (1): source1.h0 = 1e6 [binding |0|0|0|0|] 6/6 (1): singularPressureLoss4.C2.P = sink1.C.P [dynamic |0|0|0|0|] 7/7 (1): singularPressureLoss4.C2.Q = sink1.C.Q [dynamic |0|0|0|0|] 8/8 (1): singularPressureLoss4.C2.a = sink1.C.a [dynamic |0|0|0|0|] 9/9 (1): singularPressureLoss4.C2.b = sink1.C.b [dynamic |0|0|0|0|] 10/10 (1): singularPressureLoss4.C2.h = sink1.C.h [dynamic |0|0|0|0|] @@ -1650,23 +1650,23 @@ 140/176 (1): singularPressureLoss4.pro_ph.ddph = 0.0 [dynamic |0|0|0|0|] 141/177 (1): singularPressureLoss4.pro_ph.duph = 0.0 [dynamic |0|0|0|0|] 142/178 (1): singularPressureLoss4.pro_ph.duhp = 0.0 [dynamic |0|0|0|0|] 143/179 (1): singularPressureLoss4.pro_ph.x = 0.0 [dynamic |0|0|0|0|] 144/180 (1): staticDrum1.Ce_steam.Q = 0.0 [dynamic |0|0|0|0|] -145/181 (1): staticDrum1.Ce_steam.h = 100000.0 [dynamic |0|0|0|0|] +145/181 (1): staticDrum1.Ce_steam.h = 1e5 [dynamic |0|0|0|0|] 146/182 (1): staticDrum1.Ce_steam.b = true [dynamic |0|0|0|0|] 147/183 (1): staticDrum1.Ce_eva.Q = 0.0 [dynamic |0|0|0|0|] -148/184 (1): staticDrum1.Ce_eva.h = 100000.0 [dynamic |0|0|0|0|] +148/184 (1): staticDrum1.Ce_eva.h = 1e5 [dynamic |0|0|0|0|] 149/185 (1): staticDrum1.Ce_eva.b = true [dynamic |0|0|0|0|] 150/186 (1): staticDrum1.Ce_eco.Q = 0.0 [dynamic |0|0|0|0|] -151/187 (1): staticDrum1.Ce_eco.h = 100000.0 [dynamic |0|0|0|0|] +151/187 (1): staticDrum1.Ce_eco.h = 1e5 [dynamic |0|0|0|0|] 152/188 (1): staticDrum1.Ce_eco.b = true [dynamic |0|0|0|0|] 153/189 (1): staticDrum1.Cs_purg.Q = 0.0 [dynamic |0|0|0|0|] -154/190 (1): staticDrum1.Cs_purg.h = 100000.0 [dynamic |0|0|0|0|] +154/190 (1): staticDrum1.Cs_purg.h = 1e5 [dynamic |0|0|0|0|] 155/191 (1): staticDrum1.Cs_purg.a = true [dynamic |0|0|0|0|] 156/192 (1): staticDrum1.Cs_sup.Q = 0.0 [dynamic |0|0|0|0|] -157/193 (1): staticDrum1.Cs_sup.h = 100000.0 [dynamic |0|0|0|0|] +157/193 (1): staticDrum1.Cs_sup.h = 1e5 [dynamic |0|0|0|0|] 158/194 (1): staticDrum1.Cs_sup.a = true [dynamic |0|0|0|0|] 159/195 (1): staticDrum1.P = staticDrum1.Ce_steam.P [dynamic |0|0|0|0|] 160/196 (1): staticDrum1.P = staticDrum1.Ce_sup.P [dynamic |0|0|0|0|] 161/197 (1): staticDrum1.P = staticDrum1.Ce_eva.P [dynamic |0|0|0|0|] 162/198 (1): staticDrum1.P = staticDrum1.Ce_eco.P [dynamic |0|0|0|0|] @@ -1688,11 +1688,11 @@ 178/227 (1): staticDrum1.hl = staticDrum1.lsat.h [dynamic |0|0|0|0|] 179/228 (1): staticDrum1.hv = staticDrum1.vsat.h [dynamic |0|0|0|0|] 180/229 (1): staticDrum1.T = staticDrum1.lsat.T [dynamic |0|0|0|0|] 181/230 (1): staticDrum1.Cth.T = staticDrum1.T [dynamic |0|0|0|0|] 182/231 (1): staticDrum2.Cs1.Q = 0.0 [dynamic |0|0|0|0|] -183/232 (1): staticDrum2.Cs1.h = 100000.0 [dynamic |0|0|0|0|] +183/232 (1): staticDrum2.Cs1.h = 1e5 [dynamic |0|0|0|0|] 184/233 (1): staticDrum2.Cs1.a = true [dynamic |0|0|0|0|] 185/234 (1): staticDrum2.BQ = staticDrum2.Ce1.Q + staticDrum2.Ce2.Q + (-staticDrum2.Cs1.Q) - staticDrum2.Cs2.Q [dynamic |0|0|0|0|] 186/235 (1): 0.0 = staticDrum2.BQ [dynamic |0|0|0|0|] 187/236 (1): staticDrum2.P = staticDrum2.Ce1.P [dynamic |0|0|0|0|] 188/237 (1): staticDrum2.P = staticDrum2.Ce2.P [dynamic |0|0|0|0|] @@ -2024,13 +2024,13 @@ var 284 is solved in eqn 5 Standard BLT of the original model:(284) ============================================================ -284: source1.h0: (5/5): (1): source1.h0 = 1000000.0 +284: source1.h0: (5/5): (1): source1.h0 = 1e6 283: source1.Q0: (4/4): (1): source1.Q0 = 100.0 -282: sink1.h0: (3/3): (1): sink1.h0 = 1000000.0 +282: sink1.h0: (3/3): (1): sink1.h0 = 1e6 281: sink1.P: (55/55): (1): sink1.C.P = sink1.P 280: sink1.Q: (56/56): (1): sink1.C.Q = sink1.Q 279: sink1.h: (59/59): (1): sink1.h = sink1.ISpecificEnthalpy.signal 278: sink1.ISpecificEnthalpy.signal: (58/58): (1): sink1.ISpecificEnthalpy.signal = sink1.h0 277: sink1.C.P: (6/6): (1): singularPressureLoss4.C2.P = sink1.C.P @@ -2196,23 +2196,23 @@ 117: staticDrum1.hl: (178/227): (1): staticDrum1.hl = staticDrum1.lsat.h 116: staticDrum1.hv: (179/228): (1): staticDrum1.hv = staticDrum1.vsat.h 115: staticDrum1.Ce_eva.P: (161/197): (1): staticDrum1.P = staticDrum1.Ce_eva.P 114: staticDrum1.Ce_eva.h_vol: (168/204): (1): staticDrum1.Ce_eva.h_vol = staticDrum1.hl 113: staticDrum1.Ce_eva.Q: (147/183): (1): staticDrum1.Ce_eva.Q = 0.0 -112: staticDrum1.Ce_eva.h: (148/184): (1): staticDrum1.Ce_eva.h = 100000.0 +112: staticDrum1.Ce_eva.h: (148/184): (1): staticDrum1.Ce_eva.h = 1e5 111: staticDrum1.Ce_eva.a: (214/272): (1): staticDrum1.Ce_eva.a = true 110: staticDrum1.Ce_eva.b: (149/185): (1): staticDrum1.Ce_eva.b = true 109: staticDrum1.Ce_eco.P: (162/198): (1): staticDrum1.P = staticDrum1.Ce_eco.P 108: staticDrum1.Ce_eco.h_vol: (169/205): (1): staticDrum1.Ce_eco.h_vol = staticDrum1.hl 107: staticDrum1.Ce_eco.Q: (150/186): (1): staticDrum1.Ce_eco.Q = 0.0 -106: staticDrum1.Ce_eco.h: (151/187): (1): staticDrum1.Ce_eco.h = 100000.0 +106: staticDrum1.Ce_eco.h: (151/187): (1): staticDrum1.Ce_eco.h = 1e5 105: staticDrum1.Ce_eco.a: (215/273): (1): staticDrum1.Ce_eco.a = true 104: staticDrum1.Ce_eco.b: (152/188): (1): staticDrum1.Ce_eco.b = true 103: staticDrum1.Cs_sup.P: (165/201): (1): staticDrum1.P = staticDrum1.Cs_sup.P 102: staticDrum1.Cs_sup.h_vol: (172/208): (1): staticDrum1.Cs_sup.h_vol = staticDrum1.hl 101: staticDrum1.Cs_sup.Q: (156/192): (1): staticDrum1.Cs_sup.Q = 0.0 -100: staticDrum1.Cs_sup.h: (157/193): (1): staticDrum1.Cs_sup.h = 100000.0 +100: staticDrum1.Cs_sup.h: (157/193): (1): staticDrum1.Cs_sup.h = 1e5 99: staticDrum1.Cs_sup.a: (158/194): (1): staticDrum1.Cs_sup.a = true 98: staticDrum1.Cs_sup.b: (216/274): (1): staticDrum1.Cs_sup.b = true 97: staticDrum1.Cs_eva.P: (163/199): (1): staticDrum1.P = staticDrum1.Cs_eva.P 96: staticDrum1.Cs_eva.h_vol: (173/209): (1): staticDrum1.Cs_eva.h_vol = staticDrum1.hl 95: staticDrum1.Cs_eva.Q: (25/25): (1): staticDrum1.Cs_eva.Q = singularPressureLoss3.C1.Q @@ -2226,17 +2226,17 @@ 87: staticDrum1.Cs_sur.a: (20/20): (1): staticDrum1.Cs_sur.a = singularPressureLoss2.C1.a 86: staticDrum1.Cs_sur.b: (218/276): (1): staticDrum1.Cs_sur.b = true 85: staticDrum1.Cs_purg.P: (164/200): (1): staticDrum1.P = staticDrum1.Cs_purg.P 84: staticDrum1.Cs_purg.h_vol: (171/207): (1): staticDrum1.Cs_purg.h_vol = staticDrum1.hl 83: staticDrum1.Cs_purg.Q: (153/189): (1): staticDrum1.Cs_purg.Q = 0.0 -82: staticDrum1.Cs_purg.h: (154/190): (1): staticDrum1.Cs_purg.h = 100000.0 +82: staticDrum1.Cs_purg.h: (154/190): (1): staticDrum1.Cs_purg.h = 1e5 81: staticDrum1.Cs_purg.a: (155/191): (1): staticDrum1.Cs_purg.a = true 80: staticDrum1.Cs_purg.b: (219/277): (1): staticDrum1.Cs_purg.b = true 79: staticDrum1.Ce_steam.P: (159/195): (1): staticDrum1.P = staticDrum1.Ce_steam.P 78: staticDrum1.Ce_steam.h_vol: (170/206): (1): staticDrum1.Ce_steam.h_vol = staticDrum1.hv 77: staticDrum1.Ce_steam.Q: (144/180): (1): staticDrum1.Ce_steam.Q = 0.0 -76: staticDrum1.Ce_steam.h: (145/181): (1): staticDrum1.Ce_steam.h = 100000.0 +76: staticDrum1.Ce_steam.h: (145/181): (1): staticDrum1.Ce_steam.h = 1e5 75: staticDrum1.Ce_steam.a: (220/278): (1): staticDrum1.Ce_steam.a = true 74: staticDrum1.Ce_steam.b: (146/182): (1): staticDrum1.Ce_steam.b = true 73: staticDrum1.Ce_sup.P: (160/196): (1): staticDrum1.P = staticDrum1.Ce_sup.P 72: staticDrum1.Ce_sup.h_vol: (167/203): (1): staticDrum1.Ce_sup.h_vol = staticDrum1.hl 71: staticDrum1.Ce_sup.Q: (175/211): (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 @@ -2288,11 +2288,11 @@ 25: staticDrum2.Ce2.a: (223/281): (1): staticDrum2.Ce2.a = true 24: staticDrum2.Ce2.b: (39/39): (1): singularPressureLoss2.C2.b = staticDrum2.Ce2.b 23: staticDrum2.Cs1.P: (189/238): (1): staticDrum2.P = staticDrum2.Cs1.P 22: staticDrum2.Cs1.h_vol: (195/244): (1): staticDrum2.Cs1.h_vol = staticDrum2.h 21: staticDrum2.Cs1.Q: (182/231): (1): staticDrum2.Cs1.Q = 0.0 -20: staticDrum2.Cs1.h: (183/232): (1): staticDrum2.Cs1.h = 100000.0 +20: staticDrum2.Cs1.h: (183/232): (1): staticDrum2.Cs1.h = 1e5 19: staticDrum2.Cs1.a: (184/233): (1): staticDrum2.Cs1.a = true 18: staticDrum2.Cs1.b: (224/282): (1): staticDrum2.Cs1.b = true 17: staticDrum2.Cs2.P: (190/239): (1): staticDrum2.P = staticDrum2.Cs2.P 16: staticDrum2.Cs2.h_vol: (196/245): (1): staticDrum2.Cs2.h_vol = staticDrum2.h 15: staticDrum2.Cs2.Q: (49/49): (1): staticDrum2.Cs2.Q = singularPressureLoss4.C1.Q @@ -2350,13 +2350,13 @@ 216: singularPressureLoss2.C2.b: (209/267): (1): singularPressureLoss2.C2.b = true 223: singularPressureLoss2.C1.a: (208/266): (1): singularPressureLoss2.C1.a = true 254: singularPressureLoss1.C2.b: (207/265): (1): singularPressureLoss1.C2.b = true 261: singularPressureLoss1.C1.a: (206/264): (1): singularPressureLoss1.C1.a = true 273: sink1.C.a: (205/263): (1): sink1.C.a = true -284: source1.h0: (5/5): (1): source1.h0 = 1000000.0 +284: source1.h0: (5/5): (1): source1.h0 = 1e6 283: source1.Q0: (4/4): (1): source1.Q0 = 100.0 -282: sink1.h0: (3/3): (1): sink1.h0 = 1000000.0 +282: sink1.h0: (3/3): (1): sink1.h0 = 1e6 194: singularPressureLoss3.Q: (2/2): (1): singularPressureLoss3.Q = 0.0 156: singularPressureLoss4.Q: (1/1): (1): singularPressureLoss4.Q = 0.0 E-BLT: equations that compute the variables of interest:(2) @@ -2527,17 +2527,18 @@ ========================================================================== -Passed Set_S has 20 equations and 20 variables record SimulationResult -resultFile = "econcile", -simulationOptions = "startTime = 0.0, stopTime = 1.0, numberOfIntervals = 500, tolerance = 1e-06, method = 'dassl', fileNamePrefix = 'NewDataReconciliationSimpleTests.TSP_FourFlows8', options = '', outputFormat = 'mat', variableFilter = '.*', cflags = '', simflags = '-reconcile -sx=./NewDataReconciliationSimpleTests/resources/NewDataReconciliationSimpleTests.TSP_FourFlows8_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_FourFlows8', options = '', outputFormat = 'mat', variableFilter = '.*', cflags = '', simflags = '-reconcile -sx=./NewDataReconciliationSimpleTests/resources/NewDataReconciliationSimpleTests.TSP_FourFlows8_Inputs.csv -eps=0.0023 -lv=LOG_JAC'", +messages = "Simulation execution failed for model: NewDataReconciliationSimpleTests.TSP_FourFlows8 +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_FourFlows8 -LOG_STDOUT | info | DataReconciliation Completed! +LOG_STDOUT | error | Measurement input file path not found ./NewDataReconciliationSimpleTests/resources/NewDataReconciliationSimpleTests.TSP_FourFlows8_Inputs.csv. " end SimulationResult; "[openmodelica/dataReconciliation/NewDataReconciliationSimpleTests/Sink.mo:17:3-19:16:writable] Warning: Connector C is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0). [openmodelica/dataReconciliation/NewDataReconciliationSimpleTests/SingularPressureLoss.mo:20:3-22:16:writable] Warning: Connector C1 is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0). [openmodelica/dataReconciliation/NewDataReconciliationSimpleTests/SingularPressureLoss.mo:23:3-24:52:writable] Warning: Connector C2 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 2532: Text differs: expected: resultFile = "econcile", got: resultFile = "", == 1 out of 1 tests failed [openmodelica/dataReconciliation/TSP_FourFlows8.mos_temp1482, time: 22]