![[Jenkins]](/jenkins/static/7b8bca15/images/svgs/logo.svg){kind=logo}
Failed
openmodelica_dataReconciliation.TSP_FourFlows.mos (from (result.xml))
Stacktrace
Output mismatch (see stdout for details)
Standard Output
+ TSP_FourFlows ... equation mismatch [time: 20] ==== Log C:\WINDOWS\TEMP/omc-rtest-OpenModelica/openmodelica/dataReconciliation/TSP_FourFlows.mos_temp1067/log-TSP_FourFlows.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_FourFlows ========================================================================== OrderedVariables (245) ======================================== 1: constante1.y.signal:VARIABLE(flow=false ) type: Real 2: sourceQ1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 3: sourceQ1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 4: sourceQ1.C.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 5: sourceQ1.C.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real 6: sourceQ1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 7: sourceQ1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 8: sourceQ1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 9: sourceQ1.IMassFlow.signal:VARIABLE(flow=false ) type: Real 10: sourceQ1.h:VARIABLE(unit = "J/kg" protected = true ) "Fluid specific enthalpy" type: Real 11: sourceQ1.Q:VARIABLE(unit = "kg/s" protected = true ) "Mass flow rate" type: Real 12: sourceQ1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true ) "Fluid pressure" type: Real 13: mixer21.pro.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 14: mixer21.pro.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 15: mixer21.pro.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 16: mixer21.pro.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 17: mixer21.pro.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 18: mixer21.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 19: mixer21.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 20: mixer21.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 21: mixer21.pro.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 22: mixer21.pro.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 23: mixer21.Oalpha1.signal:VARIABLE(flow=false ) type: Real 24: mixer21.Ialpha1.signal:VARIABLE(flow=false ) type: Real 25: mixer21.Ce1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 26: mixer21.Ce1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 27: mixer21.Ce1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 28: mixer21.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 29: mixer21.Ce1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 30: mixer21.Ce1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 31: mixer21.Cs.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 32: mixer21.Cs.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 33: mixer21.Cs.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 34: mixer21.Cs.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 35: mixer21.Cs.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 36: mixer21.Cs.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 37: mixer21.Ce2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 38: mixer21.Ce2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 39: mixer21.Ce2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 40: mixer21.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 41: mixer21.Ce2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 42: mixer21.Ce2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 43: mixer21.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 44: mixer21.h:VARIABLE(start = 1e6 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 45: mixer21.P:VARIABLE(min = 0.0 start = 1e6 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 46: mixer21.alpha1:VARIABLE() "Extraction coefficient for inlet 1 (<=1)" type: Real 47: splitter21.pro.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 48: splitter21.pro.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 49: splitter21.pro.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 50: splitter21.pro.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 51: splitter21.pro.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 52: splitter21.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 53: splitter21.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 54: splitter21.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 55: splitter21.pro.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 56: splitter21.pro.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 57: splitter21.Oalpha1.signal:VARIABLE(flow=false ) type: Real 58: splitter21.Ialpha1.signal:VARIABLE(flow=false ) type: Real 59: splitter21.Cs2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 60: splitter21.Cs2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 61: splitter21.Cs2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 62: splitter21.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 63: splitter21.Cs2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 64: splitter21.Cs2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 65: splitter21.Cs1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 66: splitter21.Cs1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 67: splitter21.Cs1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 68: splitter21.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 69: splitter21.Cs1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 70: splitter21.Cs1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 71: splitter21.Ce.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 72: splitter21.Ce.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 73: splitter21.Ce.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 74: splitter21.Ce.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 75: splitter21.Ce.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 76: splitter21.Ce.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 77: splitter21.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 78: splitter21.h:VARIABLE(start = 1e6 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 79: splitter21.P:VARIABLE(min = 0.0 start = 1e6 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 80: splitter21.alpha1:VARIABLE() "Extraction coefficient for outlet 1 (<=1)" type: Real 81: singularPressureLoss4.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 82: singularPressureLoss4.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 83: singularPressureLoss4.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 84: singularPressureLoss4.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 85: singularPressureLoss4.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real 86: 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 87: singularPressureLoss4.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 88: singularPressureLoss4.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 89: singularPressureLoss4.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real 90: singularPressureLoss4.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 91: singularPressureLoss4.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 92: singularPressureLoss4.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 93: singularPressureLoss4.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 94: singularPressureLoss4.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 95: singularPressureLoss4.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 96: 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 97: singularPressureLoss4.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 98: singularPressureLoss4.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 99: singularPressureLoss4.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 100: singularPressureLoss4.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 101: singularPressureLoss4.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 102: singularPressureLoss4.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 103: 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 104: 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 105: singularPressureLoss4.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 106: singularPressureLoss4.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 107: singularPressureLoss4.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 108: singularPressureLoss4.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 109: 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 110: 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 111: singularPressureLoss4.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 112: singularPressureLoss4.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 113: singularPressureLoss4.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 114: singularPressureLoss4.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 115: singularPressureLoss4.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 116: singularPressureLoss4.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 117: singularPressureLoss4.Q:VARIABLE(start = 99.5 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real 118: singularPressureLoss4.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 119: singularPressureLoss3.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 120: singularPressureLoss3.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 121: singularPressureLoss3.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 122: singularPressureLoss3.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 123: singularPressureLoss3.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real 124: 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 125: singularPressureLoss3.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 126: singularPressureLoss3.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 127: singularPressureLoss3.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real 128: singularPressureLoss3.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 129: singularPressureLoss3.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 130: singularPressureLoss3.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 131: singularPressureLoss3.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 132: singularPressureLoss3.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 133: singularPressureLoss3.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 134: 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 135: singularPressureLoss3.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 136: singularPressureLoss3.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 137: singularPressureLoss3.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 138: singularPressureLoss3.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 139: singularPressureLoss3.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 140: singularPressureLoss3.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 141: 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 142: 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 143: singularPressureLoss3.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 144: singularPressureLoss3.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 145: singularPressureLoss3.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 146: singularPressureLoss3.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 147: 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 148: 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 149: singularPressureLoss3.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 150: singularPressureLoss3.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 151: singularPressureLoss3.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 152: singularPressureLoss3.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 153: singularPressureLoss3.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 154: singularPressureLoss3.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 155: singularPressureLoss3.Q:VARIABLE(start = 49.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real 156: singularPressureLoss3.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 157: singularPressureLoss2.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 158: singularPressureLoss2.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 159: singularPressureLoss2.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 160: singularPressureLoss2.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 161: singularPressureLoss2.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real 162: 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 163: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 164: singularPressureLoss2.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 165: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real 166: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 167: singularPressureLoss2.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 168: singularPressureLoss2.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 169: singularPressureLoss2.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 170: singularPressureLoss2.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 171: singularPressureLoss2.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 172: 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 173: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 174: singularPressureLoss2.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 175: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 176: singularPressureLoss2.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 177: singularPressureLoss2.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 178: singularPressureLoss2.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 179: 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 180: 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 181: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 182: singularPressureLoss2.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 183: singularPressureLoss2.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 184: singularPressureLoss2.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 185: 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 186: 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 187: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 188: singularPressureLoss2.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 189: singularPressureLoss2.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 190: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 191: singularPressureLoss2.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 192: singularPressureLoss2.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 193: singularPressureLoss2.Q:VARIABLE(start = 50.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real 194: singularPressureLoss2.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 195: singularPressureLoss1.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 196: singularPressureLoss1.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 197: singularPressureLoss1.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 198: singularPressureLoss1.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 199: singularPressureLoss1.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real 200: 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 201: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 202: singularPressureLoss1.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 203: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real 204: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 205: singularPressureLoss1.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 206: singularPressureLoss1.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 207: singularPressureLoss1.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 208: singularPressureLoss1.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 209: singularPressureLoss1.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 210: 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 211: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 212: singularPressureLoss1.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 213: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 214: singularPressureLoss1.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 215: singularPressureLoss1.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 216: singularPressureLoss1.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 217: 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 218: 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 219: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 220: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 221: singularPressureLoss1.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 222: singularPressureLoss1.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 223: 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 224: 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 225: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 226: singularPressureLoss1.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 227: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 228: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 229: singularPressureLoss1.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 230: singularPressureLoss1.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 231: singularPressureLoss1.Q:VARIABLE(start = 100.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real 232: singularPressureLoss1.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 233: sink1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 234: sink1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 235: 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 236: 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 237: sink1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 238: sink1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 239: sink1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 240: sink1.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real 241: sink1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real 242: sink1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 243: sink1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real 244: sourceQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 245: sourceQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real OrderedEquation (191, 245) ======================================== 1/1 (1): sink1.h0 = 1e5 [binding |0|0|0|0|] 2/2 (1): sourceQ1.Q0 = 100.0 [binding |0|0|0|0|] 3/3 (1): sourceQ1.h0 = 1e5 [binding |0|0|0|0|] 4/4 (1): singularPressureLoss3.C2.P = mixer21.Ce2.P [dynamic |0|0|0|0|] 5/5 (1): singularPressureLoss3.C2.Q = mixer21.Ce2.Q [dynamic |0|0|0|0|] 6/6 (1): singularPressureLoss3.C2.a = mixer21.Ce2.a [dynamic |0|0|0|0|] 7/7 (1): singularPressureLoss3.C2.b = mixer21.Ce2.b [dynamic |0|0|0|0|] 8/8 (1): singularPressureLoss3.C2.h = mixer21.Ce2.h [dynamic |0|0|0|0|] 9/9 (1): singularPressureLoss3.C2.h_vol = mixer21.Ce2.h_vol [dynamic |0|0|0|0|] 10/10 (1): singularPressureLoss2.C2.P = mixer21.Ce1.P [dynamic |0|0|0|0|] 11/11 (1): singularPressureLoss2.C2.Q = mixer21.Ce1.Q [dynamic |0|0|0|0|] 12/12 (1): singularPressureLoss2.C2.a = mixer21.Ce1.a [dynamic |0|0|0|0|] 13/13 (1): singularPressureLoss2.C2.b = mixer21.Ce1.b [dynamic |0|0|0|0|] 14/14 (1): singularPressureLoss2.C2.h = mixer21.Ce1.h [dynamic |0|0|0|0|] 15/15 (1): singularPressureLoss2.C2.h_vol = mixer21.Ce1.h_vol [dynamic |0|0|0|0|] 16/16 (1): splitter21.Cs1.P = singularPressureLoss2.C1.P [dynamic |0|0|0|0|] 17/17 (1): splitter21.Cs1.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|] 18/18 (1): splitter21.Cs1.a = singularPressureLoss2.C1.a [dynamic |0|0|0|0|] 19/19 (1): splitter21.Cs1.b = singularPressureLoss2.C1.b [dynamic |0|0|0|0|] 20/20 (1): splitter21.Cs1.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|] 21/21 (1): splitter21.Cs1.h_vol = singularPressureLoss2.C1.h_vol [dynamic |0|0|0|0|] 22/22 (1): splitter21.Cs2.P = singularPressureLoss3.C1.P [dynamic |0|0|0|0|] 23/23 (1): splitter21.Cs2.Q = singularPressureLoss3.C1.Q [dynamic |0|0|0|0|] 24/24 (1): splitter21.Cs2.a = singularPressureLoss3.C1.a [dynamic |0|0|0|0|] 25/25 (1): splitter21.Cs2.b = singularPressureLoss3.C1.b [dynamic |0|0|0|0|] 26/26 (1): splitter21.Cs2.h = singularPressureLoss3.C1.h [dynamic |0|0|0|0|] 27/27 (1): splitter21.Cs2.h_vol = singularPressureLoss3.C1.h_vol [dynamic |0|0|0|0|] 28/28 (1): mixer21.Cs.P = singularPressureLoss4.C1.P [dynamic |0|0|0|0|] 29/29 (1): mixer21.Cs.Q = singularPressureLoss4.C1.Q [dynamic |0|0|0|0|] 30/30 (1): mixer21.Cs.a = singularPressureLoss4.C1.a [dynamic |0|0|0|0|] 31/31 (1): mixer21.Cs.b = singularPressureLoss4.C1.b [dynamic |0|0|0|0|] 32/32 (1): mixer21.Cs.h = singularPressureLoss4.C1.h [dynamic |0|0|0|0|] 33/33 (1): mixer21.Cs.h_vol = singularPressureLoss4.C1.h_vol [dynamic |0|0|0|0|] 34/34 (1): singularPressureLoss1.C2.P = splitter21.Ce.P [dynamic |0|0|0|0|] 35/35 (1): singularPressureLoss1.C2.Q = splitter21.Ce.Q [dynamic |0|0|0|0|] 36/36 (1): singularPressureLoss1.C2.a = splitter21.Ce.a [dynamic |0|0|0|0|] 37/37 (1): singularPressureLoss1.C2.b = splitter21.Ce.b [dynamic |0|0|0|0|] 38/38 (1): singularPressureLoss1.C2.h = splitter21.Ce.h [dynamic |0|0|0|0|] 39/39 (1): singularPressureLoss1.C2.h_vol = splitter21.Ce.h_vol [dynamic |0|0|0|0|] 40/40 (1): singularPressureLoss4.C2.P = sink1.C.P [dynamic |0|0|0|0|] 41/41 (1): singularPressureLoss4.C2.Q = sink1.C.Q [dynamic |0|0|0|0|] 42/42 (1): singularPressureLoss4.C2.a = sink1.C.a [dynamic |0|0|0|0|] 43/43 (1): singularPressureLoss4.C2.b = sink1.C.b [dynamic |0|0|0|0|] 44/44 (1): singularPressureLoss4.C2.h = sink1.C.h [dynamic |0|0|0|0|] 45/45 (1): singularPressureLoss4.C2.h_vol = sink1.C.h_vol [dynamic |0|0|0|0|] 46/46 (1): sourceQ1.C.P = singularPressureLoss1.C1.P [dynamic |0|0|0|0|] 47/47 (1): sourceQ1.C.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|] 48/48 (1): sourceQ1.C.a = singularPressureLoss1.C1.a [dynamic |0|0|0|0|] 49/49 (1): sourceQ1.C.b = singularPressureLoss1.C1.b [dynamic |0|0|0|0|] 50/50 (1): sourceQ1.C.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|] 51/51 (1): sourceQ1.C.h_vol = singularPressureLoss1.C1.h_vol [dynamic |0|0|0|0|] 52/52 (1): constante1.y.signal = splitter21.Ialpha1.signal [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 = singularPressureLoss4.C1.h - singularPressureLoss4.C1.h_vol [dynamic |0|0|0|0|] 127/154 (1): singularPressureLoss4.deltaP = singularPressureLoss4.K * singularPressureLoss4.Q * abs(singularPressureLoss4.Q) / singularPressureLoss4.rho [dynamic |0|0|0|0|] 128/155 (1): singularPressureLoss4.Pm = 0.5 * (singularPressureLoss4.C1.P + singularPressureLoss4.C2.P) [dynamic |0|0|0|0|] 129/156 (10): singularPressureLoss4.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss4.Pm, singularPressureLoss4.T, singularPressureLoss4.mode, singularPressureLoss4.fluid) [dynamic |0|0|0|0|] 130/166 (1): singularPressureLoss4.h = singularPressureLoss4.pro_pT.h [dynamic |0|0|0|0|] 131/167 (1): singularPressureLoss4.rho = singularPressureLoss4.pro_pT.d [dynamic |0|0|0|0|] 132/168 (1): singularPressureLoss4.pro_ph.d = 0.0 [dynamic |0|0|0|0|] 133/169 (1): singularPressureLoss4.pro_ph.T = 0.0 [dynamic |0|0|0|0|] 134/170 (1): singularPressureLoss4.pro_ph.u = 0.0 [dynamic |0|0|0|0|] 135/171 (1): singularPressureLoss4.pro_ph.s = 0.0 [dynamic |0|0|0|0|] 136/172 (1): singularPressureLoss4.pro_ph.cp = 0.0 [dynamic |0|0|0|0|] 137/173 (1): singularPressureLoss4.pro_ph.ddhp = 0.0 [dynamic |0|0|0|0|] 138/174 (1): singularPressureLoss4.pro_ph.ddph = 0.0 [dynamic |0|0|0|0|] 139/175 (1): singularPressureLoss4.pro_ph.duph = 0.0 [dynamic |0|0|0|0|] 140/176 (1): singularPressureLoss4.pro_ph.duhp = 0.0 [dynamic |0|0|0|0|] 141/177 (1): singularPressureLoss4.pro_ph.x = 0.0 [dynamic |0|0|0|0|] 142/178 (1): splitter21.P = splitter21.Ce.P [dynamic |0|0|0|0|] 143/179 (1): splitter21.P = splitter21.Cs1.P [dynamic |0|0|0|0|] 144/180 (1): splitter21.P = splitter21.Cs2.P [dynamic |0|0|0|0|] 145/181 (1): splitter21.Ce.h_vol = splitter21.h [dynamic |0|0|0|0|] 146/182 (1): splitter21.Cs1.h_vol = splitter21.h [dynamic |0|0|0|0|] 147/183 (1): splitter21.Cs2.h_vol = splitter21.h [dynamic |0|0|0|0|] 148/184 (1): 0.0 = splitter21.Ce.Q + (-splitter21.Cs1.Q) - splitter21.Cs2.Q [dynamic |0|0|0|0|] 149/185 (1): 0.0 = splitter21.Ce.Q * splitter21.Ce.h + (-splitter21.Cs1.Q) * splitter21.Cs1.h - splitter21.Cs2.Q * splitter21.Cs2.h [dynamic |0|0|0|0|] 150/186 (1): splitter21.Cs1.Q = splitter21.Ialpha1.signal * splitter21.Ce.Q [dynamic |0|0|0|0|] 151/187 (1): splitter21.alpha1 = splitter21.Cs1.Q / splitter21.Ce.Q [dynamic |0|0|0|0|] 152/188 (1): splitter21.Oalpha1.signal = splitter21.alpha1 [dynamic |0|0|0|0|] 153/189 (10): splitter21.pro = ThermoSysPro.Properties.Fluid.Ph(splitter21.P, splitter21.h, splitter21.mode, splitter21.fluid) [dynamic |0|0|0|0|] 154/199 (1): splitter21.T = splitter21.pro.T [dynamic |0|0|0|0|] 155/200 (1): mixer21.Ialpha1.signal = 0.5 [dynamic |0|0|0|0|] 156/201 (1): mixer21.P = mixer21.Ce1.P [dynamic |0|0|0|0|] 157/202 (1): mixer21.P = mixer21.Ce2.P [dynamic |0|0|0|0|] 158/203 (1): mixer21.P = mixer21.Cs.P [dynamic |0|0|0|0|] 159/204 (1): mixer21.Ce1.h_vol = mixer21.h [dynamic |0|0|0|0|] 160/205 (1): mixer21.Ce2.h_vol = mixer21.h [dynamic |0|0|0|0|] 161/206 (1): mixer21.Cs.h_vol = mixer21.h [dynamic |0|0|0|0|] 162/207 (1): 0.0 = mixer21.Ce1.Q + mixer21.Ce2.Q - mixer21.Cs.Q [dynamic |0|0|0|0|] 163/208 (1): 0.0 = mixer21.Ce1.Q * mixer21.Ce1.h + mixer21.Ce2.Q * mixer21.Ce2.h - mixer21.Cs.Q * mixer21.Cs.h [dynamic |0|0|0|0|] 164/209 (1): mixer21.alpha1 = mixer21.Ce1.Q / mixer21.Cs.Q [dynamic |0|0|0|0|] 165/210 (1): mixer21.Oalpha1.signal = mixer21.alpha1 [dynamic |0|0|0|0|] 166/211 (10): mixer21.pro = ThermoSysPro.Properties.Fluid.Ph(mixer21.P, mixer21.h, mixer21.mode, mixer21.fluid) [dynamic |0|0|0|0|] 167/221 (1): mixer21.T = mixer21.pro.T [dynamic |0|0|0|0|] 168/222 (1): sourceQ1.C.P = sourceQ1.P [dynamic |0|0|0|0|] 169/223 (1): sourceQ1.C.Q = sourceQ1.Q [dynamic |0|0|0|0|] 170/224 (1): sourceQ1.C.h_vol = sourceQ1.h [dynamic |0|0|0|0|] 171/225 (1): sourceQ1.IMassFlow.signal = sourceQ1.Q0 [dynamic |0|0|0|0|] 172/226 (1): sourceQ1.Q = sourceQ1.IMassFlow.signal [dynamic |0|0|0|0|] 173/227 (1): sourceQ1.ISpecificEnthalpy.signal = sourceQ1.h0 [dynamic |0|0|0|0|] 174/228 (1): sourceQ1.h = sourceQ1.ISpecificEnthalpy.signal [dynamic |0|0|0|0|] 175/229 (1): constante1.y.signal = constante1.k [dynamic |0|0|0|0|] 176/230 (1): sink1.C.a = true [binding |0|0|0|0|] 177/231 (1): singularPressureLoss1.C1.a = true [binding |0|0|0|0|] 178/232 (1): singularPressureLoss1.C2.b = true [binding |0|0|0|0|] 179/233 (1): singularPressureLoss2.C1.a = true [binding |0|0|0|0|] 180/234 (1): singularPressureLoss2.C2.b = true [binding |0|0|0|0|] 181/235 (1): singularPressureLoss3.C1.a = true [binding |0|0|0|0|] 182/236 (1): singularPressureLoss3.C2.b = true [binding |0|0|0|0|] 183/237 (1): singularPressureLoss4.C1.a = true [binding |0|0|0|0|] 184/238 (1): singularPressureLoss4.C2.b = true [binding |0|0|0|0|] 185/239 (1): splitter21.Ce.a = true [binding |0|0|0|0|] 186/240 (1): splitter21.Cs1.b = true [binding |0|0|0|0|] 187/241 (1): splitter21.Cs2.b = true [binding |0|0|0|0|] 188/242 (1): mixer21.Ce2.a = true [binding |0|0|0|0|] 189/243 (1): mixer21.Cs.b = true [binding |0|0|0|0|] 190/244 (1): mixer21.Ce1.a = true [binding |0|0|0|0|] 191/245 (1): sourceQ1.C.b = true [binding |0|0|0|0|] Matching ======================================== 245 variables and equations var 1 is solved in eqn 229 var 2 is solved in eqn 245 var 3 is solved in eqn 48 var 4 is solved in eqn 50 var 5 is solved in eqn 223 var 6 is solved in eqn 224 var 7 is solved in eqn 46 var 8 is solved in eqn 227 var 9 is solved in eqn 225 var 10 is solved in eqn 228 var 11 is solved in eqn 226 var 12 is solved in eqn 222 var 13 is solved in eqn 220 var 14 is solved in eqn 219 var 15 is solved in eqn 218 var 16 is solved in eqn 217 var 17 is solved in eqn 216 var 18 is solved in eqn 215 var 19 is solved in eqn 214 var 20 is solved in eqn 213 var 21 is solved in eq ...[truncated 202109 chars]... lume" type: Real +27: mixer21.Ce1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 28: mixer21.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 -29: mixer21.Ce1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -30: mixer21.Ce1.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +29: mixer21.Ce1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +30: mixer21.Ce1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 31: mixer21.Cs.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 32: mixer21.Cs.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -33: mixer21.Cs.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real +33: mixer21.Cs.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 34: mixer21.Cs.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 -35: mixer21.Cs.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -36: mixer21.Cs.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +35: mixer21.Cs.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +36: mixer21.Cs.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 37: mixer21.Ce2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 38: mixer21.Ce2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -39: mixer21.Ce2.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real +39: mixer21.Ce2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 40: mixer21.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 -41: mixer21.Ce2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -42: mixer21.Ce2.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +41: mixer21.Ce2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +42: mixer21.Ce2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 43: mixer21.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real -44: mixer21.h:VARIABLE(start = 1000000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real -45: mixer21.P:VARIABLE(min = 0.0 start = 1000000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure" type: Real +44: mixer21.h:VARIABLE(start = 1e6 unit = "J/kg" ) "Fluid specific enthalpy" type: Real +45: mixer21.P:VARIABLE(min = 0.0 start = 1e6 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 46: mixer21.alpha1:VARIABLE() "Extraction coefficient for inlet 1 (<=1)" type: Real 47: splitter21.pro.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 48: splitter21.pro.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 49: splitter21.pro.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 50: splitter21.pro.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 51: splitter21.pro.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -52: splitter21.pro.cp:VARIABLE(min = 1e-09 max = 9.999999999999999e+59 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real -53: splitter21.pro.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -54: splitter21.pro.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -55: splitter21.pro.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +52: splitter21.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real +53: splitter21.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +54: splitter21.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +55: splitter21.pro.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 56: splitter21.pro.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 57: splitter21.Oalpha1.signal:VARIABLE(flow=false ) type: Real 58: splitter21.Ialpha1.signal:VARIABLE(flow=false ) type: Real 59: splitter21.Cs2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 60: splitter21.Cs2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -61: splitter21.Cs2.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real +61: splitter21.Cs2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 62: splitter21.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 -63: splitter21.Cs2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -64: splitter21.Cs2.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +63: splitter21.Cs2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +64: splitter21.Cs2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 65: splitter21.Cs1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 66: splitter21.Cs1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -67: splitter21.Cs1.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real +67: splitter21.Cs1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 68: splitter21.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 -69: splitter21.Cs1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -70: splitter21.Cs1.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +69: splitter21.Cs1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +70: splitter21.Cs1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 71: splitter21.Ce.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 72: splitter21.Ce.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -73: splitter21.Ce.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real +73: splitter21.Ce.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 74: splitter21.Ce.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 -75: splitter21.Ce.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -76: splitter21.Ce.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +75: splitter21.Ce.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +76: splitter21.Ce.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 77: splitter21.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real -78: splitter21.h:VARIABLE(start = 1000000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real -79: splitter21.P:VARIABLE(min = 0.0 start = 1000000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure" type: Real +78: splitter21.h:VARIABLE(start = 1e6 unit = "J/kg" ) "Fluid specific enthalpy" type: Real +79: splitter21.P:VARIABLE(min = 0.0 start = 1e6 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 80: splitter21.alpha1:VARIABLE() "Extraction coefficient for outlet 1 (<=1)" type: Real 81: singularPressureLoss4.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 82: singularPressureLoss4.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 83: singularPressureLoss4.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 84: singularPressureLoss4.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 85: singularPressureLoss4.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real -86: 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 -87: singularPressureLoss4.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -88: singularPressureLoss4.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -89: singularPressureLoss4.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real -90: singularPressureLoss4.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +86: 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 +87: singularPressureLoss4.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +88: singularPressureLoss4.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +89: singularPressureLoss4.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real +90: singularPressureLoss4.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 91: singularPressureLoss4.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 92: singularPressureLoss4.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 93: singularPressureLoss4.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 94: singularPressureLoss4.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 95: singularPressureLoss4.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -96: 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 -97: singularPressureLoss4.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -98: singularPressureLoss4.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -99: singularPressureLoss4.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +96: 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 +97: singularPressureLoss4.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +98: singularPressureLoss4.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +99: singularPressureLoss4.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 100: singularPressureLoss4.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 101: singularPressureLoss4.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 102: singularPressureLoss4.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -103: 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 +103: 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 104: 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 -105: singularPressureLoss4.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -106: 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 +105: singularPressureLoss4.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +106: singularPressureLoss4.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 107: singularPressureLoss4.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 108: singularPressureLoss4.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -109: 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 +109: 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 110: 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 -111: singularPressureLoss4.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -112: 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 -113: singularPressureLoss4.h:VARIABLE(start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real -114: singularPressureLoss4.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real +111: singularPressureLoss4.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +112: singularPressureLoss4.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real +113: singularPressureLoss4.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real +114: singularPressureLoss4.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 115: singularPressureLoss4.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 116: singularPressureLoss4.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 117: singularPressureLoss4.Q:VARIABLE(start = 99.5 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real -118: singularPressureLoss4.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real +118: singularPressureLoss4.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 119: singularPressureLoss3.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 120: singularPressureLoss3.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 121: singularPressureLoss3.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 122: singularPressureLoss3.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 123: singularPressureLoss3.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real -124: 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 -125: singularPressureLoss3.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -126: singularPressureLoss3.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -127: singularPressureLoss3.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real -128: singularPressureLoss3.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +124: 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 +125: singularPressureLoss3.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +126: singularPressureLoss3.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +127: singularPressureLoss3.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real +128: singularPressureLoss3.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 129: singularPressureLoss3.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 130: singularPressureLoss3.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 131: singularPressureLoss3.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 132: singularPressureLoss3.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 133: singularPressureLoss3.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -134: 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 -135: singularPressureLoss3.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -136: singularPressureLoss3.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -137: singularPressureLoss3.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +134: 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 +135: singularPressureLoss3.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +136: singularPressureLoss3.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +137: singularPressureLoss3.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 138: singularPressureLoss3.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 139: singularPressureLoss3.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 140: singularPressureLoss3.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -141: 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 +141: 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 142: 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 -143: singularPressureLoss3.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -144: 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 +143: singularPressureLoss3.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +144: singularPressureLoss3.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 145: singularPressureLoss3.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 146: singularPressureLoss3.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -147: 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 +147: 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 148: 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 -149: singularPressureLoss3.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -150: 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 -151: singularPressureLoss3.h:VARIABLE(start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real -152: singularPressureLoss3.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real +149: singularPressureLoss3.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +150: singularPressureLoss3.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real +151: singularPressureLoss3.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real +152: singularPressureLoss3.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 153: singularPressureLoss3.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 154: singularPressureLoss3.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 155: singularPressureLoss3.Q:VARIABLE(start = 49.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real -156: singularPressureLoss3.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real +156: singularPressureLoss3.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 157: singularPressureLoss2.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 158: singularPressureLoss2.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 159: singularPressureLoss2.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 160: singularPressureLoss2.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 161: singularPressureLoss2.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real -162: 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 -163: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -164: singularPressureLoss2.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -165: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real -166: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +162: 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 +163: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +164: singularPressureLoss2.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +165: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real +166: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 167: singularPressureLoss2.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 168: singularPressureLoss2.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 169: singularPressureLoss2.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 170: singularPressureLoss2.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 171: singularPressureLoss2.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -172: 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 -173: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -174: singularPressureLoss2.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -175: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +172: 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 +173: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +174: singularPressureLoss2.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +175: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 176: singularPressureLoss2.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 177: singularPressureLoss2.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 178: singularPressureLoss2.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -179: 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 +179: 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 180: 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 -181: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -182: 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 +181: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +182: singularPressureLoss2.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 183: singularPressureLoss2.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 184: singularPressureLoss2.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -185: 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 +185: 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 186: 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 -187: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -188: 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 -189: singularPressureLoss2.h:VARIABLE(start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real -190: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real +187: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +188: singularPressureLoss2.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real +189: singularPressureLoss2.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real +190: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 191: singularPressureLoss2.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 192: singularPressureLoss2.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 193: singularPressureLoss2.Q:VARIABLE(start = 50.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real -194: singularPressureLoss2.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real +194: singularPressureLoss2.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 195: singularPressureLoss1.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 196: singularPressureLoss1.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 197: singularPressureLoss1.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 198: singularPressureLoss1.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 199: singularPressureLoss1.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real -200: 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 -201: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -202: singularPressureLoss1.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -203: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real -204: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +200: 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 +201: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +202: singularPressureLoss1.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +203: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real +204: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 205: singularPressureLoss1.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 206: singularPressureLoss1.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 207: singularPressureLoss1.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 208: singularPressureLoss1.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 209: singularPressureLoss1.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -210: 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 -211: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -212: singularPressureLoss1.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -213: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +210: 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 +211: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +212: singularPressureLoss1.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +213: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 214: singularPressureLoss1.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 215: singularPressureLoss1.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 216: singularPressureLoss1.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -217: 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 +217: 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 218: 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 -219: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -220: 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 +219: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +220: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 221: singularPressureLoss1.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 222: singularPressureLoss1.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -223: 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 +223: 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 224: 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 -225: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -226: 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 -227: singularPressureLoss1.h:VARIABLE(start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real -228: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real +225: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +226: singularPressureLoss1.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real +227: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real +228: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 229: singularPressureLoss1.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 230: singularPressureLoss1.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 231: singularPressureLoss1.Q:VARIABLE(start = 100.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real -232: singularPressureLoss1.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real +232: singularPressureLoss1.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 233: sink1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 234: sink1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -235: 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 +235: 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 236: 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 -237: sink1.C.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -238: 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 +237: sink1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +238: sink1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 239: sink1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 240: sink1.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real 241: sink1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real -242: sink1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure" type: Real +242: sink1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 243: sink1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real 244: sourceQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 245: sourceQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real OrderedEquation (191, 245) ======================================== 1/1 (1): singularPressureLoss4.Q = 0.0 [binding |0|0|0|0|] -2/2 (1): sink1.h0 = 100000.0 [binding |0|0|0|0|] +2/2 (1): sink1.h0 = 1e5 [binding |0|0|0|0|] 3/3 (1): sourceQ1.Q0 = 100.0 [binding |0|0|0|0|] -4/4 (1): sourceQ1.h0 = 100000.0 [binding |0|0|0|0|] +4/4 (1): sourceQ1.h0 = 1e5 [binding |0|0|0|0|] 5/5 (1): singularPressureLoss3.C2.P = mixer21.Ce2.P [dynamic |0|0|0|0|] 6/6 (1): singularPressureLoss3.C2.Q = mixer21.Ce2.Q [dynamic |0|0|0|0|] 7/7 (1): singularPressureLoss3.C2.a = mixer21.Ce2.a [dynamic |0|0|0|0|] 8/8 (1): singularPressureLoss3.C2.b = mixer21.Ce2.b [dynamic |0|0|0|0|] 9/9 (1): singularPressureLoss3.C2.h = mixer21.Ce2.h [dynamic |0|0|0|0|] @@ -1755,13 +1755,13 @@ var 245 is solved in eqn 4 Standard BLT of the original model:(245) ============================================================ -245: sourceQ1.h0: (4/4): (1): sourceQ1.h0 = 100000.0 +245: sourceQ1.h0: (4/4): (1): sourceQ1.h0 = 1e5 244: sourceQ1.Q0: (3/3): (1): sourceQ1.Q0 = 100.0 -243: sink1.h0: (2/2): (1): sink1.h0 = 100000.0 +243: sink1.h0: (2/2): (1): sink1.h0 = 1e5 242: sink1.P: (54/54): (1): sink1.C.P = sink1.P 241: sink1.Q: (55/55): (1): sink1.C.Q = sink1.Q 240: sink1.h: (58/58): (1): sink1.h = sink1.ISpecificEnthalpy.signal 239: sink1.ISpecificEnthalpy.signal: (57/57): (1): sink1.ISpecificEnthalpy.signal = sink1.h0 238: sink1.C.P: (41/41): (1): singularPressureLoss4.C2.P = sink1.C.P @@ -2036,13 +2036,13 @@ 177: singularPressureLoss2.C2.b: (180/234): (1): singularPressureLoss2.C2.b = true 184: singularPressureLoss2.C1.a: (179/233): (1): singularPressureLoss2.C1.a = true 215: singularPressureLoss1.C2.b: (178/232): (1): singularPressureLoss1.C2.b = true 222: singularPressureLoss1.C1.a: (177/231): (1): singularPressureLoss1.C1.a = true 234: sink1.C.a: (176/230): (1): sink1.C.a = true -245: sourceQ1.h0: (4/4): (1): sourceQ1.h0 = 100000.0 +245: sourceQ1.h0: (4/4): (1): sourceQ1.h0 = 1e5 244: sourceQ1.Q0: (3/3): (1): sourceQ1.Q0 = 100.0 -243: sink1.h0: (2/2): (1): sink1.h0 = 100000.0 +243: sink1.h0: (2/2): (1): sink1.h0 = 1e5 117: singularPressureLoss4.Q: (1/1): (1): singularPressureLoss4.Q = 0.0 E-BLT: equations that compute the variables of interest:(3) ============================================================ @@ -2225,17 +2225,18 @@ ========================================================================== -Passed Set_S has 15 equations and 15 variables record SimulationResult -resultFile = "econcile", -simulationOptions = "startTime = 0.0, stopTime = 1.0, numberOfIntervals = 500, tolerance = 1e-06, method = 'dassl', fileNamePrefix = 'NewDataReconciliationSimpleTests.TSP_FourFlows', options = '', outputFormat = 'mat', variableFilter = '.*', cflags = '', simflags = '-reconcile -sx=./NewDataReconciliationSimpleTests/resources/DataReconciliationSimpleTests.TSP_FourFlows_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_FourFlows', options = '', outputFormat = 'mat', variableFilter = '.*', cflags = '', simflags = '-reconcile -sx=./NewDataReconciliationSimpleTests/resources/DataReconciliationSimpleTests.TSP_FourFlows_Inputs.csv -eps=0.0023 -lv=LOG_JAC'", +messages = "Simulation execution failed for model: NewDataReconciliationSimpleTests.TSP_FourFlows +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_FourFlows -LOG_STDOUT | info | DataReconciliation Completed! +LOG_STDOUT | error | Measurement input file path not found ./NewDataReconciliationSimpleTests/resources/DataReconciliationSimpleTests.TSP_FourFlows_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 2230: Text differs: expected: resultFile = "econcile", got: resultFile = "", == 1 out of 1 tests failed [openmodelica/dataReconciliation/TSP_FourFlows.mos_temp1067, time: 20]