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Failed
openmodelica_dataReconciliation.TSP_Splitter4.mos (from (result.xml))
Stacktrace
Output mismatch (see stdout for details)
Standard Output
+ TSP_Splitter4 ... equation mismatch [time: 21] ==== Log C:\Windows\TEMP/omc-rtest-OpenModelica/openmodelica/dataReconciliation/TSP_Splitter4.mos_temp2304/log-TSP_Splitter4.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_Splitter4 ========================================================================== OrderedVariables (187) ======================================== 1: sourceQ1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 2: sourceQ1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 3: 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 4: 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 5: sourceQ1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 6: sourceQ1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 7: sourceQ1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 8: sourceQ1.IMassFlow.signal:VARIABLE(flow=false ) type: Real 9: sourceQ1.h:VARIABLE(unit = "J/kg" protected = true ) "Fluid specific enthalpy" type: Real 10: sourceQ1.Q:VARIABLE(unit = "kg/s" protected = true ) "Mass flow rate" type: Real 11: sourceQ1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true ) "Fluid pressure" type: Real 12: sink1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 13: sink1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 14: 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 15: 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 16: sink1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 17: sink1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 18: sink1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 19: sink1.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real 20: sink1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real 21: sink1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 22: sourcePQ1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 23: sourcePQ1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 24: sourcePQ1.C.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 25: sourcePQ1.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 26: sourcePQ1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 27: sourcePQ1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 28: sourcePQ1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 29: sourcePQ1.IPressure.signal:VARIABLE(flow=false ) type: Real 30: sourcePQ1.IMassFlow.signal:VARIABLE(flow=false ) type: Real 31: sourcePQ1.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real 32: sourcePQ1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real 33: sourcePQ1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 34: mixer21.pro.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 35: mixer21.pro.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 36: mixer21.pro.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 37: mixer21.pro.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 38: mixer21.pro.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 39: mixer21.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 40: mixer21.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 41: mixer21.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 42: mixer21.pro.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 43: mixer21.pro.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 44: mixer21.Oalpha1.signal:VARIABLE(flow=false ) type: Real 45: mixer21.Ialpha1.signal:VARIABLE(flow=false ) type: Real 46: mixer21.Ce1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 47: mixer21.Ce1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 48: 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 49: 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 50: mixer21.Ce1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 51: mixer21.Ce1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 52: mixer21.Cs.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 53: mixer21.Cs.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 54: 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 55: 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 56: mixer21.Cs.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 57: mixer21.Cs.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 58: mixer21.Ce2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 59: mixer21.Ce2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 60: 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 61: 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 62: mixer21.Ce2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 63: mixer21.Ce2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 64: mixer21.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 65: mixer21.h:VARIABLE(start = 1e6 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 66: mixer21.P:VARIABLE(min = 0.0 start = 1e6 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 67: mixer21.alpha1:VARIABLE() "Extraction coefficient for inlet 1 (<=1)" type: Real 68: singularPressureLoss3.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 69: singularPressureLoss3.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 70: singularPressureLoss3.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 71: singularPressureLoss3.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 72: singularPressureLoss3.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real 73: 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 74: singularPressureLoss3.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 75: singularPressureLoss3.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 76: singularPressureLoss3.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real 77: singularPressureLoss3.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 78: singularPressureLoss3.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 79: singularPressureLoss3.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 80: singularPressureLoss3.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 81: singularPressureLoss3.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 82: singularPressureLoss3.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 83: 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 84: singularPressureLoss3.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 85: singularPressureLoss3.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 86: singularPressureLoss3.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 87: singularPressureLoss3.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 88: singularPressureLoss3.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 89: singularPressureLoss3.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 90: 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 91: 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 92: singularPressureLoss3.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 93: singularPressureLoss3.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 94: singularPressureLoss3.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 95: singularPressureLoss3.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 96: 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 97: 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 98: singularPressureLoss3.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 99: singularPressureLoss3.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 100: singularPressureLoss3.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 101: singularPressureLoss3.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 102: singularPressureLoss3.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 103: singularPressureLoss3.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 104: singularPressureLoss3.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real 105: singularPressureLoss3.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 106: singularPressureLoss2.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 107: singularPressureLoss2.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 108: singularPressureLoss2.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 109: singularPressureLoss2.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 110: singularPressureLoss2.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real 111: 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 112: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 113: singularPressureLoss2.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 114: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real 115: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 116: singularPressureLoss2.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 117: singularPressureLoss2.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 118: singularPressureLoss2.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 119: singularPressureLoss2.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 120: singularPressureLoss2.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 121: 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 122: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 123: singularPressureLoss2.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 124: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 125: singularPressureLoss2.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 126: singularPressureLoss2.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 127: singularPressureLoss2.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 128: 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 129: 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 130: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 131: singularPressureLoss2.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 132: singularPressureLoss2.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 133: singularPressureLoss2.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 134: 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 135: 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 136: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 137: singularPressureLoss2.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 138: singularPressureLoss2.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 139: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 140: singularPressureLoss2.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 141: singularPressureLoss2.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 142: singularPressureLoss2.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real 143: singularPressureLoss2.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 144: singularPressureLoss1.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 145: singularPressureLoss1.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 146: singularPressureLoss1.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 147: singularPressureLoss1.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 148: singularPressureLoss1.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real 149: 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 150: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 151: singularPressureLoss1.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 152: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real 153: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 154: singularPressureLoss1.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 155: singularPressureLoss1.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 156: singularPressureLoss1.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 157: singularPressureLoss1.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 158: singularPressureLoss1.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 159: 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 160: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 161: singularPressureLoss1.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 162: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 163: singularPressureLoss1.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 164: singularPressureLoss1.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 165: singularPressureLoss1.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 166: 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 167: 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 168: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 169: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 170: singularPressureLoss1.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 171: singularPressureLoss1.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 172: 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 173: 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 174: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 175: singularPressureLoss1.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 176: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 177: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 178: singularPressureLoss1.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 179: singularPressureLoss1.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 180: singularPressureLoss1.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real 181: singularPressureLoss1.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 182: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real 183: sourcePQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 184: sourcePQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real 185: sink1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real 186: sourceQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 187: sourceQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real OrderedEquation (151, 187) ======================================== 1/1 (1): sourcePQ1.P0 = 3e5 [binding |0|0|0|0|] 2/2 (1): sourcePQ1.Q0 = 100.0 [binding |0|0|0|0|] 3/3 (1): sourcePQ1.h0 = 1e5 [binding |0|0|0|0|] 4/4 (1): sink1.h0 = 1e5 [binding |0|0|0|0|] 5/5 (1): sourceQ1.Q0 = 100.0 [binding |0|0|0|0|] 6/6 (1): sourceQ1.h0 = 1e5 [binding |0|0|0|0|] 7/7 (1): mixer21.Cs.P = singularPressureLoss1.C1.P [dynamic |0|0|0|0|] 8/8 (1): mixer21.Cs.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|] 9/9 (1): mixer21.Cs.a = singularPressureLoss1.C1.a [dynamic |0|0|0|0|] 10/10 (1): mixer21.Cs.b = singularPressureLoss1.C1.b [dynamic |0|0|0|0|] 11/11 (1): mixer21.Cs.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|] 12/12 (1): mixer21.Cs.h_vol = singularPressureLoss1.C1.h_vol [dynamic |0|0|0|0|] 13/13 (1): singularPressureLoss2.C2.P = mixer21.Ce1.P [dynamic |0|0|0|0|] 14/14 (1): singularPressureLoss2.C2.Q = mixer21.Ce1.Q [dynamic |0|0|0|0|] 15/15 (1): singularPressureLoss2.C2.a = mixer21.Ce1.a [dynamic |0|0|0|0|] 16/16 (1): singularPressureLoss2.C2.b = mixer21.Ce1.b [dynamic |0|0|0|0|] 17/17 (1): singularPressureLoss2.C2.h = mixer21.Ce1.h [dynamic |0|0|0|0|] 18/18 (1): singularPressureLoss2.C2.h_vol = mixer21.Ce1.h_vol [dynamic |0|0|0|0|] 19/19 (1): singularPressureLoss3.C2.P = mixer21.Ce2.P [dynamic |0|0|0|0|] 20/20 (1): singularPressureLoss3.C2.Q = mixer21.Ce2.Q [dynamic |0|0|0|0|] 21/21 (1): singularPressureLoss3.C2.a = mixer21.Ce2.a [dynamic |0|0|0|0|] 22/22 (1): singularPressureLoss3.C2.b = mixer21.Ce2.b [dynamic |0|0|0|0|] 23/23 (1): singularPressureLoss3.C2.h = mixer21.Ce2.h [dynamic |0|0|0|0|] 24/24 (1): singularPressureLoss3.C2.h_vol = mixer21.Ce2.h_vol [dynamic |0|0|0|0|] 25/25 (1): sourcePQ1.C.P = singularPressureLoss2.C1.P [dynamic |0|0|0|0|] 26/26 (1): sourcePQ1.C.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|] 27/27 (1): sourcePQ1.C.a = singularPressureLoss2.C1.a [dynamic |0|0|0|0|] 28/28 (1): sourcePQ1.C.b = singularPressureLoss2.C1.b [dynamic |0|0|0|0|] 29/29 (1): sourcePQ1.C.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|] 30/30 (1): sourcePQ1.C.h_vol = singularPressureLoss2.C1.h_vol [dynamic |0|0|0|0|] 31/31 (1): singularPressureLoss1.C2.P = sink1.C.P [dynamic |0|0|0|0|] 32/32 (1): singularPressureLoss1.C2.Q = sink1.C.Q [dynamic |0|0|0|0|] 33/33 (1): singularPressureLoss1.C2.a = sink1.C.a [dynamic |0|0|0|0|] 34/34 (1): singularPressureLoss1.C2.b = sink1.C.b [dynamic |0|0|0|0|] 35/35 (1): singularPressureLoss1.C2.h = sink1.C.h [dynamic |0|0|0|0|] 36/36 (1): singularPressureLoss1.C2.h_vol = sink1.C.h_vol [dynamic |0|0|0|0|] 37/37 (1): sourceQ1.C.P = singularPressureLoss3.C1.P [dynamic |0|0|0|0|] 38/38 (1): sourceQ1.C.Q = singularPressureLoss3.C1.Q [dynamic |0|0|0|0|] 39/39 (1): sourceQ1.C.a = singularPressureLoss3.C1.a [dynamic |0|0|0|0|] 40/40 (1): sourceQ1.C.b = singularPressureLoss3.C1.b [dynamic |0|0|0|0|] 41/41 (1): sourceQ1.C.h = singularPressureLoss3.C1.h [dynamic |0|0|0|0|] 42/42 (1): sourceQ1.C.h_vol = singularPressureLoss3.C1.h_vol [dynamic |0|0|0|0|] 43/43 (1): singularPressureLoss1.C1.P - singularPressureLoss1.C2.P = singularPressureLoss1.deltaP [dynamic |0|0|0|0|] 44/44 (1): singularPressureLoss1.C2.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|] 45/45 (1): singularPressureLoss1.C2.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|] 46/46 (1): singularPressureLoss1.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|] 47/47 (1): singularPressureLoss1.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|] 48/48 (1): 0.0 = singularPressureLoss1.C1.h - singularPressureLoss1.C1.h_vol [dynamic |0|0|0|0|] 49/49 (1): singularPressureLoss1.deltaP = singularPressureLoss1.K * singularPressureLoss1.Q * abs(singularPressureLoss1.Q) / singularPressureLoss1.rho [dynamic |0|0|0|0|] 50/50 (1): singularPressureLoss1.Pm = 0.5 * (singularPressureLoss1.C1.P + singularPressureLoss1.C2.P) [dynamic |0|0|0|0|] 51/51 (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) [dynamic |0|0|0|0|] 52/61 (1): singularPressureLoss1.h = singularPressureLoss1.pro_pT.h [dynamic |0|0|0|0|] 53/62 (1): singularPressureLoss1.rho = singularPressureLoss1.pro_pT.d [dynamic |0|0|0|0|] 54/63 (1): singularPressureLoss1.pro_ph.d = 0.0 [dynamic |0|0|0|0|] 55/64 (1): singularPressureLoss1.pro_ph.T = 0.0 [dynamic |0|0|0|0|] 56/65 (1): singularPressureLoss1.pro_ph.u = 0.0 [dynamic |0|0|0|0|] 57/66 (1): singularPressureLoss1.pro_ph.s = 0.0 [dynamic |0|0|0|0|] 58/67 (1): singularPressureLoss1.pro_ph.cp = 0.0 [dynamic |0|0|0|0|] 59/68 (1): singularPressureLoss1.pro_ph.ddhp = 0.0 [dynamic |0|0|0|0|] 60/69 (1): singularPressureLoss1.pro_ph.ddph = 0.0 [dynamic |0|0|0|0|] 61/70 (1): singularPressureLoss1.pro_ph.duph = 0.0 [dynamic |0|0|0|0|] 62/71 (1): singularPressureLoss1.pro_ph.duhp = 0.0 [dynamic |0|0|0|0|] 63/72 (1): singularPressureLoss1.pro_ph.x = 0.0 [dynamic |0|0|0|0|] 64/73 (1): singularPressureLoss2.C1.P - singularPressureLoss2.C2.P = singularPressureLoss2.deltaP [dynamic |0|0|0|0|] 65/74 (1): singularPressureLoss2.C2.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|] 66/75 (1): singularPressureLoss2.C2.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|] 67/76 (1): singularPressureLoss2.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|] 68/77 (1): singularPressureLoss2.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|] 69/78 (1): 0.0 = singularPressureLoss2.C1.h - singularPressureLoss2.C1.h_vol [dynamic |0|0|0|0|] 70/79 (1): singularPressureLoss2.deltaP = singularPressureLoss2.K * singularPressureLoss2.Q * abs(singularPressureLoss2.Q) / singularPressureLoss2.rho [dynamic |0|0|0|0|] 71/80 (1): singularPressureLoss2.Pm = 0.5 * (singularPressureLoss2.C1.P + singularPressureLoss2.C2.P) [dynamic |0|0|0|0|] 72/81 (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid) [dynamic |0|0|0|0|] 73/91 (1): singularPressureLoss2.h = singularPressureLoss2.pro_pT.h [dynamic |0|0|0|0|] 74/92 (1): singularPressureLoss2.rho = singularPressureLoss2.pro_pT.d [dynamic |0|0|0|0|] 75/93 (1): singularPressureLoss2.pro_ph.d = 0.0 [dynamic |0|0|0|0|] 76/94 (1): singularPressureLoss2.pro_ph.T = 0.0 [dynamic |0|0|0|0|] 77/95 (1): singularPressureLoss2.pro_ph.u = 0.0 [dynamic |0|0|0|0|] 78/96 (1): singularPressureLoss2.pro_ph.s = 0.0 [dynamic |0|0|0|0|] 79/97 (1): singularPressureLoss2.pro_ph.cp = 0.0 [dynamic |0|0|0|0|] 80/98 (1): singularPressureLoss2.pro_ph.ddhp = 0.0 [dynamic |0|0|0|0|] 81/99 (1): singularPressureLoss2.pro_ph.ddph = 0.0 [dynamic |0|0|0|0|] 82/100 (1): singularPressureLoss2.pro_ph.duph = 0.0 [dynamic |0|0|0|0|] 83/101 (1): singularPressureLoss2.pro_ph.duhp = 0.0 [dynamic |0|0|0|0|] 84/102 (1): singularPressureLoss2.pro_ph.x = 0.0 [dynamic |0|0|0|0|] 85/103 (1): singularPressureLoss3.C1.P - singularPressureLoss3.C2.P = singularPressureLoss3.deltaP [dynamic |0|0|0|0|] 86/104 (1): singularPressureLoss3.C2.Q = singularPressureLoss3.C1.Q [dynamic |0|0|0|0|] 87/105 (1): singularPressureLoss3.C2.h = singularPressureLoss3.C1.h [dynamic |0|0|0|0|] 88/106 (1): singularPressureLoss3.h = singularPressureLoss3.C1.h [dynamic |0|0|0|0|] 89/107 (1): singularPressureLoss3.Q = singularPressureLoss3.C1.Q [dynamic |0|0|0|0|] 90/108 (1): 0.0 = singularPressureLoss3.C1.h - singularPressureLoss3.C1.h_vol [dynamic |0|0|0|0|] 91/109 (1): singularPressureLoss3.deltaP = singularPressureLoss3.K * singularPressureLoss3.Q * abs(singularPressureLoss3.Q) / singularPressureLoss3.rho [dynamic |0|0|0|0|] 92/110 (1): singularPressureLoss3.Pm = 0.5 * (singularPressureLoss3.C1.P + singularPressureLoss3.C2.P) [dynamic |0|0|0|0|] 93/111 (10): singularPressureLoss3.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss3.Pm, singularPressureLoss3.T, singularPressureLoss3.mode, singularPressureLoss3.fluid) [dynamic |0|0|0|0|] 94/121 (1): singularPressureLoss3.h = singularPressureLoss3.pro_pT.h [dynamic |0|0|0|0|] 95/122 (1): singularPressureLoss3.rho = singularPressureLoss3.pro_pT.d [dynamic |0|0|0|0|] 96/123 (1): singularPressureLoss3.pro_ph.d = 0.0 [dynamic |0|0|0|0|] 97/124 (1): singularPressureLoss3.pro_ph.T = 0.0 [dynamic |0|0|0|0|] 98/125 (1): singularPressureLoss3.pro_ph.u = 0.0 [dynamic |0|0|0|0|] 99/126 (1): singularPressureLoss3.pro_ph.s = 0.0 [dynamic |0|0|0|0|] 100/127 (1): singularPressureLoss3.pro_ph.cp = 0.0 [dynamic |0|0|0|0|] 101/128 (1): singularPressureLoss3.pro_ph.ddhp = 0.0 [dynamic |0|0|0|0|] 102/129 (1): singularPressureLoss3.pro_ph.ddph = 0.0 [dynamic |0|0|0|0|] 103/130 (1): singularPressureLoss3.pro_ph.duph = 0.0 [dynamic |0|0|0|0|] 104/131 (1): singularPressureLoss3.pro_ph.duhp = 0.0 [dynamic |0|0|0|0|] 105/132 (1): singularPressureLoss3.pro_ph.x = 0.0 [dynamic |0|0|0|0|] 106/133 (1): mixer21.Ialpha1.signal = 0.5 [dynamic |0|0|0|0|] 107/134 (1): mixer21.P = mixer21.Ce1.P [dynamic |0|0|0|0|] 108/135 (1): mixer21.P = mixer21.Ce2.P [dynamic |0|0|0|0|] 109/136 (1): mixer21.P = mixer21.Cs.P [dynamic |0|0|0|0|] 110/137 (1): mixer21.Ce1.h_vol = mixer21.h [dynamic |0|0|0|0|] 111/138 (1): mixer21.Ce2.h_vol = mixer21.h [dynamic |0|0|0|0|] 112/139 (1): mixer21.Cs.h_vol = mixer21.h [dynamic |0|0|0|0|] 113/140 (1): 0.0 = mixer21.Ce1.Q + mixer21.Ce2.Q - mixer21.Cs.Q [dynamic |0|0|0|0|] 114/141 (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|] 115/142 (1): mixer21.alpha1 = mixer21.Ce1.Q / mixer21.Cs.Q [dynamic |0|0|0|0|] 116/143 (1): mixer21.Oalpha1.signal = mixer21.alpha1 [dynamic |0|0|0|0|] 117/144 (10): mixer21.pro = ThermoSysPro.Properties.Fluid.Ph(mixer21.P, mixer21.h, mixer21.mode, mixer21.fluid) [dynamic |0|0|0|0|] 118/154 (1): mixer21.T = mixer21.pro.T [dynamic |0|0|0|0|] 119/155 (1): sourcePQ1.C.P = sourcePQ1.P [dynamic |0|0|0|0|] 120/156 (1): sourcePQ1.C.Q = sourcePQ1.Q [dynamic |0|0|0|0|] 121/157 (1): sourcePQ1.C.h_vol = sourcePQ1.h [dynamic |0|0|0|0|] 122/158 (1): sourcePQ1.IMassFlow.signal = sourcePQ1.Q0 [dynamic |0|0|0|0|] 123/159 (1): sourcePQ1.Q = sourcePQ1.IMassFlow.signal [dynamic |0|0|0|0|] 124/160 (1): sourcePQ1.IPressure.signal = sourcePQ1.P0 [dynamic |0|0|0|0|] 125/161 (1): sourcePQ1.P = sourcePQ1.IPressure.signal [dynamic |0|0|0|0|] 126/162 (1): sourcePQ1.ISpecificEnthalpy.signal = sourcePQ1.h0 [dynamic |0|0|0|0|] 127/163 (1): sourcePQ1.h = sourcePQ1.ISpecificEnthalpy.signal [dynamic |0|0|0|0|] 128/164 (1): sink1.C.P = sink1.P [dynamic |0|0|0|0|] 129/165 (1): sink1.C.Q = sink1.Q [dynamic |0|0|0|0|] 130/166 (1): sink1.C.h_vol = sink1.h [dynamic |0|0|0|0|] 131/167 (1): sink1.ISpecificEnthalpy.signal = sink1.h0 [dynamic |0|0|0|0|] 132/168 (1): sink1.h = sink1.ISpecificEnthalpy.signal [dynamic |0|0|0|0|] 133/169 (1): sourceQ1.C.P = sourceQ1.P [dynamic |0|0|0|0|] 134/170 (1): sourceQ1.C.Q = sourceQ1.Q [dynamic |0|0|0|0|] 135/171 (1): sourceQ1.C.h_vol = sourceQ1.h [dynamic |0|0|0|0|] 136/172 (1): sourceQ1.IMassFlow.signal = sourceQ1.Q0 [dynamic |0|0|0|0|] 137/173 (1): sourceQ1.Q = sourceQ1.IMassFlow.signal [dynamic |0|0|0|0|] 138/174 (1): sourceQ1.ISpecificEnthalpy.signal = sourceQ1.h0 [dynamic |0|0|0|0|] 139/175 (1): sourceQ1.h = sourceQ1.ISpecificEnthalpy.signal [dynamic |0|0|0|0|] 140/176 (1): singularPressureLoss1.C1.a = true [binding |0|0|0|0|] 141/177 (1): singularPressureLoss1.C2.b = true [binding |0|0|0|0|] 142/178 (1): singularPressureLoss2.C1.a = true [binding |0|0|0|0|] 143/179 (1): singularPressureLoss2.C2.b = true [binding |0|0|0|0|] 144/180 (1): singularPressureLoss3.C1.a = true [binding |0|0|0|0|] 145/181 (1): singularPressureLoss3.C2.b = true [binding |0|0|0|0|] 146/182 (1): mixer21.Ce2.a = true [binding |0|0|0|0|] 147/183 (1): mixer21.Cs.b = true [binding |0|0|0|0|] 148/184 (1): mixer21.Ce1.a = true [binding |0|0|0|0|] 149/185 (1): sourcePQ1.C.b = true [binding |0|0|0|0|] 150/186 (1): sink1.C.a = true [binding |0|0|0|0|] 151/187 (1): sourceQ1.C.b = true [binding |0|0|0|0|] Matching ======================================== 187 variables and equations var 1 is solved in eqn 187 var 2 is solved in eqn 39 var 3 is solved in eqn 41 var 4 is solved in eqn 170 var 5 is solved in eqn 171 var 6 is solved in eqn 37 var 7 is solved in eqn 174 var 8 is solved in eqn 172 var 9 is solved in eqn 175 var 10 is solved in eqn 173 var 11 is solved in eqn 169 var 12 is solved in eqn 34 var 13 is solved in eqn 186 var 14 is solved in eqn 35 var 15 is solved in eqn 32 var 16 is solved in eqn 166 var 17 is solved in eqn 31 var 18 is solved in eqn 167 var 19 is solved in eqn 168 var 20 is solved in eqn 165 var 21 is solved in eqn 164 var 22 is solved in eqn 185 var 23 is solved in eqn 27 var 24 is solved in eqn 29 var 25 is solved in eqn 156 var 26 is solved in eqn 157 var 27 is solved in eqn 155 var 28 is solved in eqn 162 var 29 is solved in eqn 160 var 30 is solved in eqn 158 var 31 is solved in eqn 163 var 32 is solved in eqn 159 var 33 is solved in eqn 161 var 34 is solved in eqn 153 var 35 is solved in eqn 152 var 36 is solved in eqn 151 var 37 is solved in eqn 150 var 38 is solved in eqn 149 var 39 is solved in eqn 148 var 40 is solved in eqn 147 var 41 is solved in eqn 146 var 42 is solved in eqn 145 var 43 is solved in eqn 144 var 44 is solved in eqn 143 var 45 is solved in eqn 133 var 46 is solved in eqn 16 var 47 is solved in eqn 184 var 48 is solved in eqn 17 var 49 is solved in eqn 14 var 50 is solved in eqn 137 var 51 is solved in eqn 13 var 52 is solved in eqn 183 var 53 is solved in eqn 9 var 54 is solved in eqn 141 var 55 is solved in eqn 140 var 56 is solved in eqn 12 var 57 is solved in eqn 136 var 58 is solved in eqn 22 var 59 is solved in eqn 182 var 60 is solved in eqn 23 var 61 is solved in eqn 20 var 62 is solved in eqn 138 var 63 is solved in eqn 135 var 64 is solved in eqn 154 var 65 is solved in eqn 139 var 66 is solved in eqn 134 var 67 is solved in eqn 142 var 68 is solved in eqn 113 var 69 is solved in eqn 120 var 70 is solved in eqn 119 var 71 is solved in eqn 118 var 72 is solved in eqn 117 var 73 is solved in eqn 116 var 74 is solved in eqn 115 var 75 is solved in eqn 114 var 76 is solved in eqn 121 var 77 is solved in eqn 112 var 78 is solved in eqn 132 var 79 is solved in eqn 131 var 80 is solved in eqn 130 var 81 is solved in eqn 129 var 82 is solved in eqn 128 var 83 is solved in eqn 127 var 84 is solved in eqn 126 var 85 is solved in eqn 125 var 86 is solved in eqn 123 var 87 is solved in eqn 124 var 88 is solved in eqn 181 var 89 is solved in eqn 21 var 90 is solved in eqn 105 var 91 is solved in eqn 104 var 92 is solved in eqn 24 var 93 is solved in eqn 19 var 94 is solved in eqn 40 var 95 is solved in eqn 180 var 96 is solved in eqn 108 var 97 is solved in eqn 38 var 98 is solved in eqn 42 var 99 is solved in eqn 103 var 100 is solved in eqn 106 var 101 is solved in eqn 110 var 102 is solved in eqn 111 var 103 is solved in eqn 122 var 104 is solved in eqn 107 var 105 is solved in eqn 109 var 106 is solved in eqn 82 var 107 is solved in eqn 90 var 108 is solved in eqn 89 var 109 is solved in eqn 88 var 110 is solved in eqn 87 var 111 is solved in eqn 86 var 112 is solved in eqn 85 var 113 is solved in eqn 84 var 114 is solved in eqn 91 var 115 is solved in eqn 92 var 116 is solved in eqn 102 var 117 is solved in eqn 101 var 118 is solved in eqn 100 var 119 is solved in eqn 99 var 120 is solved in eqn 98 var 121 is solved in eqn 97 var 122 is solved in eqn 96 var 123 is solved in eqn 95 var 124 is solved in eqn 93 var 125 is solved in eqn 94 var 126 is solved in eqn 179 var 127 is solved in eqn 15 var 128 is solved in eqn 75 var 129 is solved in eqn 74 var 130 is solved in eqn 18 var 131 is solved in eqn 80 var 132 is solved in eqn 28 var 133 is solved in eqn 178 var 134 is solved in eqn 78 var 135 is solved in eqn 26 var 136 is solved in eqn 30 var 137 is solved in eqn 25 var 138 is solved in eqn 76 var 139 is solved in eqn 81 var 140 is solved in eqn 83 var 141 is solved in eqn 79 var 142 is solved in eqn 77 var 143 is solved in eqn 73 var 144 is solved in eqn 53 var 145 is solved in eqn 60 var 146 is solved in eqn 59 var 147 is solved in eqn 58 var 148 is solved in eqn 57 var 149 is solved in eqn 56 var 150 is solved in eqn 55 var 151 is solved in eqn 54 var 152 is solved in eqn 61 var 153 is solved in eqn 52 var 154 is solved in eqn 72 var 155 is solved in eqn 71 var 156 is solved in eqn 70 var 157 is solved in eqn 69 var 158 is solved in eqn 68 var 159 is solved in eqn 67 var 160 is solved in eqn 66 var 161 is solved in eqn 65 var 162 is solved in eqn 63 var 163 is solved in eqn 64 var 164 is solved in eqn 177 var 165 is solved in eqn 33 var 166 is solved in eqn 45 var 167 is solved in eqn 44 var 168 is solved in eqn 36 var 169 is solved in eqn 43 var 170 is solved in eqn 10 var 171 is solved in eqn 176 var 172 is solved in eqn 11 var 173 is solved in eqn 8 var 174 is solved in eqn 48 var 175 is solved in eqn 7 var 176 is solved in eqn 46 var 177 is solved in eqn 50 var 178 is solved in eqn 51 var 179 is solved in eqn 62 var 180 is solved in eqn 47 var 181 is solved in eqn 49 var 182 is solved in eqn 1 var 183 is solved in eqn 2 var 184 is solved in eqn 3 var 185 is solved in eqn 4 var 186 is solved in eqn 5 var 187 is solved in eqn 6 Standard BLT of the original model:(187) ============================================================ 187: sourceQ1.h0: (6/6): (1): sourceQ1.h0 = 1e5 186: sourceQ1.Q0: (5/5): (1): sourceQ1.Q0 = 100.0 185: sink1.h0: (4/4): (1): sink1.h0 = 1e5 184: sourcePQ1.h0: (3/3): (1): sourcePQ1.h0 = 1e5 183: sourcePQ1.Q0: (2/2): (1): sourcePQ1.Q0 = 100.0 182: sourcePQ1.P0: (1/1): (1): sourcePQ1.P0 = 3e5 181: singularPressureLoss1.deltaP: (49/49): (1): singularPressureLoss1.deltaP = singularPressureLoss1.K * singularPressureLoss1.Q * abs(singularPressureLoss1.Q) / singularPressureLoss1.rho 180: singularPressureLoss1.Q: (47/47): (1): singularPressureLoss1.Q = singularPressureLoss1.C1.Q 179: singularPressureLoss1.rho: (53/62): (1): singularPressureLoss1.rho = singularPressureLoss1.pro_pT.d 178: singularPressureLoss1.T: (51/51): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 177: singularPressureLoss1.Pm: (50/50): (1): singularPressureLoss1.Pm = 0.5 * (singularPressureLoss1.C1.P + singularPressureLoss1.C2.P) 176: singularPressureLoss1.h: (46/46): (1): singularPressureLoss1.h = singularPressureLoss1.C1.h 175: singularPressureLoss1.C1.P: (7/7): (1): mixer21.Cs.P = singularPressureLoss1.C1.P 174: singularPressureLoss1.C1.h_vol: (48/48): (1): 0.0 = singularPressureLoss1.C1.h - singularPressureLoss1.C1.h_vol 173: singularPressureLoss1.C1.Q: (8/8): (1): mixer21.Cs.Q = singularPressureLoss1.C1.Q 172: singularPressureLoss1.C1.h: (11/11): (1): mixer21.Cs.h = singularPressureLoss1.C1.h 171: singularPressureLoss1.C1.a: (140/176): (1): singularPressureLoss1.C1.a = true 170: singularPressureLoss1.C1.b: (10/10): (1): mixer21.Cs.b = singularPressureLoss1.C1.b 169: singularPressureLoss1.C2.P: (43/43): (1): singularPressureLoss1.C1.P - singularPressureLoss1.C2.P = singularPressureLoss1.deltaP 168: singularPressureLoss1.C2.h_vol: (36/36): (1): singularPressureLoss1.C2.h_vol = sink1.C.h_vol 167: singularPressureLoss1.C2.Q: (44/44): (1): singularPressureLoss1.C2.Q = singularPressureLoss1.C1.Q 166: singularPressureLoss1.C2.h: (45/45): (1): singularPressureLoss1.C2.h = singularPressureLoss1.C1.h 165: singularPressureLoss1.C2.a: (33/33): (1): singularPressureLoss1.C2.a = sink1.C.a 164: singularPressureLoss1.C2.b: (141/177): (1): singularPressureLoss1.C2.b = true 163: singularPressureLoss1.pro_ph.T: (55/64): (1): singularPressureLoss1.pro_ph.T = 0.0 162: singularPressureLoss1.pro_ph.d: (54/63): (1): singularPressureLoss1.pro_ph.d = 0.0 161: singularPressureLoss1.pro_ph.u: (56/65): (1): singularPressureLoss1.pro_ph.u = 0.0 160: singularPressureLoss1.pro_ph.s: (57/66): (1): singularPressureLoss1.pro_ph.s = 0.0 159: singularPressureLoss1.pro_ph.cp: (58/67): (1): singularPressureLoss1.pro_ph.cp = 0.0 158: singularPressureLoss1.pro_ph.ddhp: (59/68): (1): singularPressureLoss1.pro_ph.ddhp = 0.0 157: singularPressureLoss1.pro_ph.ddph: (60/69): (1): singularPressureLoss1.pro_ph.ddph = 0.0 156: singularPressureLoss1.pro_ph.duph: (61/70): (1): singularPressureLoss1.pro_ph.duph = 0.0 155: singularPressureLoss1.pro_ph.duhp: (62/71): (1): singularPressureLoss1.pro_ph.duhp = 0.0 154: singularPressureLoss1.pro_ph.x: (63/72): (1): singularPressureLoss1.pro_ph.x = 0.0 153: singularPressureLoss1.pro_pT.d: (51/52): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 152: singularPressureLoss1.pro_pT.h: (52/61): (1): singularPressureLoss1.h = singularPressureLoss1.pro_pT.h 151: singularPressureLoss1.pro_pT.u: (51/54): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 150: singularPressureLoss1.pro_pT.s: (51/55): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 149: singularPressureLoss1.pro_pT.cp: (51/56): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 148: singularPressureLoss1.pro_pT.ddTp: (51/57): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 147: singularPressureLoss1.pro_pT.ddpT: (51/58): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 146: singularPressureLoss1.pro_pT.dupT: (51/59): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 145: singularPressureLoss1.pro_pT.duTp: (51/60): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 144: singularPressureLoss1.pro_pT.x: (51/53): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 143: singularPressureLoss2.deltaP: (64/73): (1): singularPressureLoss2.C1.P - singularPressureLoss2.C2.P = singularPressureLoss2.deltaP 142: singularPressureLoss2.Q: (68/77): (1): singularPressureLoss2.Q = singularPressureLoss2.C1.Q 141: singularPressureLoss2.rho: (70/79): (1): singularPressureLoss2.deltaP = singularPressureLoss2.K * singularPressureLoss2.Q * abs(singularPressureLoss2.Q) / singularPressureLoss2.rho 140: singularPressureLoss2.T: (72/83): (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid) 139: singularPressureLoss2.Pm: (72/81): (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid) 138: singularPressureLoss2.h: (67/76): (1): singularPressureLoss2.h = singularPressureLoss2.C1.h 137: singularPressureLoss2.C1.P: (25/25): (1): sourcePQ1.C.P = singularPressureLoss2.C1.P 136: singularPressureLoss2.C1.h_vol: (30/30): (1): sourcePQ1.C.h_vol = singularPressureLoss2.C1.h_vol 135: singularPressureLoss2.C1.Q: (26/26): (1): sourcePQ1.C.Q = singularPressureLoss2.C1.Q 134: singularPressureLoss2.C1.h: (69/78): (1): 0.0 = singularPressureLoss2.C1.h - singularPressureLoss2.C1.h_vol 133: singularPressureLoss2.C1.a: (142/178): (1): singularPressureLoss2.C1.a = true 132: singularPressureLoss2.C1.b: (28/28): (1): sourcePQ1.C.b = singularPressureLoss2.C1.b 131: singularPressureLoss2.C2.P: (71/80): (1): singularPressureLoss2.Pm = 0.5 * (singularPressureLoss2.C1.P + ...[truncated 131747 chars]... min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real +182: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real 183: sourcePQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 184: sourcePQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real 185: sink1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real 186: sourceQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 187: sourceQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real OrderedEquation (151, 187) ======================================== -1/1 (1): sourcePQ1.P0 = 300000.0 [binding |0|0|0|0|] +1/1 (1): sourcePQ1.P0 = 3e5 [binding |0|0|0|0|] 2/2 (1): sourcePQ1.Q0 = 100.0 [binding |0|0|0|0|] -3/3 (1): sourcePQ1.h0 = 100000.0 [binding |0|0|0|0|] -4/4 (1): sink1.h0 = 100000.0 [binding |0|0|0|0|] +3/3 (1): sourcePQ1.h0 = 1e5 [binding |0|0|0|0|] +4/4 (1): sink1.h0 = 1e5 [binding |0|0|0|0|] 5/5 (1): sourceQ1.Q0 = 100.0 [binding |0|0|0|0|] -6/6 (1): sourceQ1.h0 = 100000.0 [binding |0|0|0|0|] +6/6 (1): sourceQ1.h0 = 1e5 [binding |0|0|0|0|] 7/7 (1): mixer21.Cs.P = singularPressureLoss1.C1.P [dynamic |0|0|0|0|] 8/8 (1): mixer21.Cs.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|] 9/9 (1): mixer21.Cs.a = singularPressureLoss1.C1.a [dynamic |0|0|0|0|] 10/10 (1): mixer21.Cs.b = singularPressureLoss1.C1.b [dynamic |0|0|0|0|] 11/11 (1): mixer21.Cs.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|] @@ -548,16 +548,16 @@ var 187 is solved in eqn 6 Standard BLT of the original model:(187) ============================================================ -187: sourceQ1.h0: (6/6): (1): sourceQ1.h0 = 100000.0 +187: sourceQ1.h0: (6/6): (1): sourceQ1.h0 = 1e5 186: sourceQ1.Q0: (5/5): (1): sourceQ1.Q0 = 100.0 -185: sink1.h0: (4/4): (1): sink1.h0 = 100000.0 -184: sourcePQ1.h0: (3/3): (1): sourcePQ1.h0 = 100000.0 +185: sink1.h0: (4/4): (1): sink1.h0 = 1e5 +184: sourcePQ1.h0: (3/3): (1): sourcePQ1.h0 = 1e5 183: sourcePQ1.Q0: (2/2): (1): sourcePQ1.Q0 = 100.0 -182: sourcePQ1.P0: (1/1): (1): sourcePQ1.P0 = 300000.0 +182: sourcePQ1.P0: (1/1): (1): sourcePQ1.P0 = 3e5 181: singularPressureLoss1.deltaP: (49/49): (1): singularPressureLoss1.deltaP = singularPressureLoss1.K * singularPressureLoss1.Q * abs(singularPressureLoss1.Q) / singularPressureLoss1.rho 180: singularPressureLoss1.Q: (47/47): (1): singularPressureLoss1.Q = singularPressureLoss1.C1.Q 179: singularPressureLoss1.rho: (53/62): (1): singularPressureLoss1.rho = singularPressureLoss1.pro_pT.d 178: singularPressureLoss1.T: (51/51): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 177: singularPressureLoss1.Pm: (50/50): (1): singularPressureLoss1.Pm = 0.5 * (singularPressureLoss1.C1.P + singularPressureLoss1.C2.P) @@ -746,11 +746,11 @@ 3: singularPressureLoss1.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real Boundary conditions (6) ======================================== -1: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real +1: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real 2: sourcePQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 3: sourcePQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real 4: sink1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real 5: sourceQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 6: sourceQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real @@ -769,16 +769,16 @@ 95: singularPressureLoss3.C1.a: (144/180): (1): singularPressureLoss3.C1.a = true 126: singularPressureLoss2.C2.b: (143/179): (1): singularPressureLoss2.C2.b = true 133: singularPressureLoss2.C1.a: (142/178): (1): singularPressureLoss2.C1.a = true 164: singularPressureLoss1.C2.b: (141/177): (1): singularPressureLoss1.C2.b = true 171: singularPressureLoss1.C1.a: (140/176): (1): singularPressureLoss1.C1.a = true -187: sourceQ1.h0: (6/6): (1): sourceQ1.h0 = 100000.0 +187: sourceQ1.h0: (6/6): (1): sourceQ1.h0 = 1e5 186: sourceQ1.Q0: (5/5): (1): sourceQ1.Q0 = 100.0 -185: sink1.h0: (4/4): (1): sink1.h0 = 100000.0 -184: sourcePQ1.h0: (3/3): (1): sourcePQ1.h0 = 100000.0 +185: sink1.h0: (4/4): (1): sink1.h0 = 1e5 +184: sourcePQ1.h0: (3/3): (1): sourcePQ1.h0 = 1e5 183: sourcePQ1.Q0: (2/2): (1): sourcePQ1.Q0 = 100.0 -182: sourcePQ1.P0: (1/1): (1): sourcePQ1.P0 = 300000.0 +182: sourcePQ1.P0: (1/1): (1): sourcePQ1.P0 = 3e5 E-BLT: equations that compute the variables of interest:(3) ============================================================ @@ -823,190 +823,190 @@ OrderedVariables (187) ======================================== 1: sourceQ1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 2: sourceQ1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -3: sourceQ1.C.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real +3: 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 4: 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 -5: sourceQ1.C.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -6: sourceQ1.C.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +5: sourceQ1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +6: sourceQ1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 7: sourceQ1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 8: sourceQ1.IMassFlow.signal:VARIABLE(flow=false ) type: Real 9: sourceQ1.h:VARIABLE(unit = "J/kg" protected = true ) "Fluid specific enthalpy" type: Real 10: sourceQ1.Q:VARIABLE(unit = "kg/s" protected = true ) "Mass flow rate" type: Real -11: sourceQ1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 protected = true ) "Fluid pressure" type: Real +11: sourceQ1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true ) "Fluid pressure" type: Real 12: sink1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 13: sink1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -14: 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 +14: 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 15: 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 -16: sink1.C.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -17: 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 +16: sink1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +17: sink1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 18: sink1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 19: sink1.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real 20: sink1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real -21: sink1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure" type: Real +21: sink1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 22: sourcePQ1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 23: sourcePQ1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -24: sourcePQ1.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 +24: sourcePQ1.C.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 25: sourcePQ1.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 -26: sourcePQ1.C.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -27: sourcePQ1.C.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +26: sourcePQ1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +27: sourcePQ1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 28: sourcePQ1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 29: sourcePQ1.IPressure.signal:VARIABLE(flow=false ) type: Real 30: sourcePQ1.IMassFlow.signal:VARIABLE(flow=false ) type: Real 31: sourcePQ1.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real 32: sourcePQ1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real -33: sourcePQ1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure" type: Real +33: sourcePQ1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 34: mixer21.pro.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 35: mixer21.pro.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 36: mixer21.pro.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 37: mixer21.pro.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 38: mixer21.pro.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -39: mixer21.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 -40: mixer21.pro.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -41: mixer21.pro.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -42: mixer21.pro.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +39: mixer21.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real +40: mixer21.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +41: mixer21.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +42: mixer21.pro.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 43: mixer21.pro.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 44: mixer21.Oalpha1.signal:VARIABLE(flow=false ) type: Real 45: mixer21.Ialpha1.signal:VARIABLE(flow=false ) type: Real 46: mixer21.Ce1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 47: mixer21.Ce1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -48: mixer21.Ce1.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real +48: 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 49: 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 -50: mixer21.Ce1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -51: 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 +50: mixer21.Ce1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +51: mixer21.Ce1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 52: mixer21.Cs.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 53: mixer21.Cs.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -54: 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 +54: 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 55: 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 -56: mixer21.Cs.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -57: 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 +56: mixer21.Cs.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +57: mixer21.Cs.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 58: mixer21.Ce2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 59: mixer21.Ce2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -60: 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 +60: 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 61: 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 -62: mixer21.Ce2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -63: 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 +62: mixer21.Ce2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +63: mixer21.Ce2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 64: mixer21.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real -65: mixer21.h:VARIABLE(start = 1000000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real -66: mixer21.P:VARIABLE(min = 0.0 start = 1000000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure" type: Real +65: mixer21.h:VARIABLE(start = 1e6 unit = "J/kg" ) "Fluid specific enthalpy" type: Real +66: mixer21.P:VARIABLE(min = 0.0 start = 1e6 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 67: mixer21.alpha1:VARIABLE() "Extraction coefficient for inlet 1 (<=1)" type: Real 68: singularPressureLoss3.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 69: singularPressureLoss3.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 70: singularPressureLoss3.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 71: singularPressureLoss3.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 72: singularPressureLoss3.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real -73: 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 -74: singularPressureLoss3.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -75: singularPressureLoss3.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -76: singularPressureLoss3.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real -77: singularPressureLoss3.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +73: 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 +74: singularPressureLoss3.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +75: singularPressureLoss3.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +76: singularPressureLoss3.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real +77: singularPressureLoss3.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 78: singularPressureLoss3.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 79: singularPressureLoss3.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 80: singularPressureLoss3.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 81: singularPressureLoss3.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 82: singularPressureLoss3.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -83: 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 -84: singularPressureLoss3.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -85: singularPressureLoss3.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -86: singularPressureLoss3.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +83: 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 +84: singularPressureLoss3.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +85: singularPressureLoss3.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +86: singularPressureLoss3.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 87: singularPressureLoss3.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 88: singularPressureLoss3.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 89: singularPressureLoss3.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -90: 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 +90: 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 91: 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 -92: singularPressureLoss3.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -93: 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 +92: singularPressureLoss3.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +93: singularPressureLoss3.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 94: singularPressureLoss3.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 95: singularPressureLoss3.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -96: 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 +96: 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 97: 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 -98: singularPressureLoss3.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -99: 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 -100: singularPressureLoss3.h:VARIABLE(start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real -101: singularPressureLoss3.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real +98: singularPressureLoss3.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +99: singularPressureLoss3.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real +100: singularPressureLoss3.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real +101: singularPressureLoss3.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 102: singularPressureLoss3.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 103: singularPressureLoss3.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 104: singularPressureLoss3.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real -105: singularPressureLoss3.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real +105: singularPressureLoss3.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 106: singularPressureLoss2.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 107: singularPressureLoss2.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 108: singularPressureLoss2.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 109: singularPressureLoss2.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 110: singularPressureLoss2.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real -111: 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 -112: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -113: singularPressureLoss2.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -114: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real -115: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +111: 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 +112: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +113: singularPressureLoss2.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +114: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real +115: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 116: singularPressureLoss2.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 117: singularPressureLoss2.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 118: singularPressureLoss2.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 119: singularPressureLoss2.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 120: singularPressureLoss2.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -121: 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 -122: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -123: singularPressureLoss2.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -124: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +121: 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 +122: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +123: singularPressureLoss2.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +124: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 125: singularPressureLoss2.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 126: singularPressureLoss2.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 127: singularPressureLoss2.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -128: 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 +128: 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 129: 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 -130: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -131: 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 +130: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +131: singularPressureLoss2.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 132: singularPressureLoss2.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 133: singularPressureLoss2.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -134: 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 +134: 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 135: 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 -136: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -137: 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 -138: singularPressureLoss2.h:VARIABLE(start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real -139: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real +136: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +137: singularPressureLoss2.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real +138: singularPressureLoss2.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real +139: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 140: singularPressureLoss2.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 141: singularPressureLoss2.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 142: singularPressureLoss2.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real -143: singularPressureLoss2.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real +143: singularPressureLoss2.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 144: singularPressureLoss1.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 145: singularPressureLoss1.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 146: singularPressureLoss1.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 147: singularPressureLoss1.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 148: singularPressureLoss1.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real -149: 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 -150: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -151: singularPressureLoss1.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -152: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real -153: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +149: 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 +150: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +151: singularPressureLoss1.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +152: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real +153: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 154: singularPressureLoss1.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 155: singularPressureLoss1.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 156: singularPressureLoss1.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 157: singularPressureLoss1.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 158: singularPressureLoss1.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -159: 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 -160: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -161: singularPressureLoss1.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -162: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +159: 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 +160: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +161: singularPressureLoss1.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +162: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 163: singularPressureLoss1.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 164: singularPressureLoss1.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 165: singularPressureLoss1.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -166: 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 +166: 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 167: 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 -168: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -169: 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 +168: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +169: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 170: singularPressureLoss1.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 171: singularPressureLoss1.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -172: 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 +172: 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 173: 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 -174: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -175: 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 -176: singularPressureLoss1.h:VARIABLE(start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real -177: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real +174: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +175: singularPressureLoss1.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real +176: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real +177: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 178: singularPressureLoss1.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 179: singularPressureLoss1.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 180: singularPressureLoss1.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real -181: singularPressureLoss1.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real -182: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real +181: singularPressureLoss1.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real +182: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real 183: sourcePQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 184: sourcePQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real 185: sink1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real 186: sourceQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 187: sourceQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real @@ -1014,16 +1014,16 @@ OrderedEquation (151, 187) ======================================== 1/1 (1): singularPressureLoss3.Q = 0.0 [binding |0|0|0|0|] 2/2 (1): singularPressureLoss2.Q = 0.0 [binding |0|0|0|0|] -3/3 (1): sourcePQ1.P0 = 300000.0 [binding |0|0|0|0|] +3/3 (1): sourcePQ1.P0 = 3e5 [binding |0|0|0|0|] 4/4 (1): sourcePQ1.Q0 = 100.0 [binding |0|0|0|0|] -5/5 (1): sourcePQ1.h0 = 100000.0 [binding |0|0|0|0|] -6/6 (1): sink1.h0 = 100000.0 [binding |0|0|0|0|] +5/5 (1): sourcePQ1.h0 = 1e5 [binding |0|0|0|0|] +6/6 (1): sink1.h0 = 1e5 [binding |0|0|0|0|] 7/7 (1): sourceQ1.Q0 = 100.0 [binding |0|0|0|0|] -8/8 (1): sourceQ1.h0 = 100000.0 [binding |0|0|0|0|] +8/8 (1): sourceQ1.h0 = 1e5 [binding |0|0|0|0|] 9/9 (1): mixer21.Cs.P = singularPressureLoss1.C1.P [dynamic |0|0|0|0|] 10/10 (1): mixer21.Cs.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|] 11/11 (1): mixer21.Cs.a = singularPressureLoss1.C1.a [dynamic |0|0|0|0|] 12/12 (1): mixer21.Cs.b = singularPressureLoss1.C1.b [dynamic |0|0|0|0|] 13/13 (1): mixer21.Cs.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|] @@ -1358,16 +1358,16 @@ var 187 is solved in eqn 8 Standard BLT of the original model:(187) ============================================================ -187: sourceQ1.h0: (8/8): (1): sourceQ1.h0 = 100000.0 +187: sourceQ1.h0: (8/8): (1): sourceQ1.h0 = 1e5 186: sourceQ1.Q0: (7/7): (1): sourceQ1.Q0 = 100.0 -185: sink1.h0: (6/6): (1): sink1.h0 = 100000.0 -184: sourcePQ1.h0: (5/5): (1): sourcePQ1.h0 = 100000.0 +185: sink1.h0: (6/6): (1): sink1.h0 = 1e5 +184: sourcePQ1.h0: (5/5): (1): sourcePQ1.h0 = 1e5 183: sourcePQ1.Q0: (4/4): (1): sourcePQ1.Q0 = 100.0 -182: sourcePQ1.P0: (3/3): (1): sourcePQ1.P0 = 300000.0 +182: sourcePQ1.P0: (3/3): (1): sourcePQ1.P0 = 3e5 181: singularPressureLoss1.deltaP: (45/45): (1): singularPressureLoss1.C1.P - singularPressureLoss1.C2.P = singularPressureLoss1.deltaP 180: singularPressureLoss1.Q: (49/49): (1): singularPressureLoss1.Q = singularPressureLoss1.C1.Q 179: singularPressureLoss1.rho: (51/51): (1): singularPressureLoss1.deltaP = singularPressureLoss1.K * singularPressureLoss1.Q * abs(singularPressureLoss1.Q) / singularPressureLoss1.rho 178: singularPressureLoss1.T: (53/55): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 177: singularPressureLoss1.Pm: (53/53): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) @@ -1556,11 +1556,11 @@ 3: singularPressureLoss1.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real Boundary conditions (6) ======================================== -1: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real +1: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real 2: sourcePQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 3: sourcePQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real 4: sink1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real 5: sourceQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 6: sourceQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real @@ -1579,16 +1579,16 @@ 95: singularPressureLoss3.C1.a: (144/180): (1): singularPressureLoss3.C1.a = true 126: singularPressureLoss2.C2.b: (143/179): (1): singularPressureLoss2.C2.b = true 133: singularPressureLoss2.C1.a: (142/178): (1): singularPressureLoss2.C1.a = true 164: singularPressureLoss1.C2.b: (141/177): (1): singularPressureLoss1.C2.b = true 171: singularPressureLoss1.C1.a: (140/176): (1): singularPressureLoss1.C1.a = true -187: sourceQ1.h0: (8/8): (1): sourceQ1.h0 = 100000.0 +187: sourceQ1.h0: (8/8): (1): sourceQ1.h0 = 1e5 186: sourceQ1.Q0: (7/7): (1): sourceQ1.Q0 = 100.0 -185: sink1.h0: (6/6): (1): sink1.h0 = 100000.0 -184: sourcePQ1.h0: (5/5): (1): sourcePQ1.h0 = 100000.0 +185: sink1.h0: (6/6): (1): sink1.h0 = 1e5 +184: sourcePQ1.h0: (5/5): (1): sourcePQ1.h0 = 1e5 183: sourcePQ1.Q0: (4/4): (1): sourcePQ1.Q0 = 100.0 -182: sourcePQ1.P0: (3/3): (1): sourcePQ1.P0 = 300000.0 +182: sourcePQ1.P0: (3/3): (1): sourcePQ1.P0 = 3e5 142: singularPressureLoss2.Q: (2/2): (1): singularPressureLoss2.Q = 0.0 104: singularPressureLoss3.Q: (1/1): (1): singularPressureLoss3.Q = 0.0 E-BLT: equations that compute the variables of interest:(1) @@ -1704,17 +1704,18 @@ ========================================================================== -Passed Set_S has 8 equations and 8 variables record SimulationResult -resultFile = "econcile", -simulationOptions = "startTime = 0.0, stopTime = 1.0, numberOfIntervals = 500, tolerance = 1e-06, method = 'dassl', fileNamePrefix = 'NewDataReconciliationSimpleTests.TSP_Splitter4', options = '', outputFormat = 'mat', variableFilter = '.*', cflags = '', simflags = '-reconcile -sx=./NewDataReconciliationSimpleTests/resources/DataReconciliationSimpleTests.TSP_Splitter4_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_Splitter4', options = '', outputFormat = 'mat', variableFilter = '.*', cflags = '', simflags = '-reconcile -sx=./NewDataReconciliationSimpleTests/resources/DataReconciliationSimpleTests.TSP_Splitter4_Inputs.csv -eps=0.0023 -lv=LOG_JAC'", +messages = "Simulation execution failed for model: NewDataReconciliationSimpleTests.TSP_Splitter4 +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_Splitter4 -LOG_STDOUT | info | DataReconciliation Completed! +LOG_STDOUT | error | Measurement input file path not found ./NewDataReconciliationSimpleTests/resources/DataReconciliationSimpleTests.TSP_Splitter4_Inputs.csv. " end SimulationResult; "[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). [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). '' Equation mismatch: omc-diff says: ------------Failed 'e' '"' Line 1709: Text differs: expected: resultFile = "econcile", got: resultFile = "", == 1 out of 1 tests failed [openmodelica/dataReconciliation/TSP_Splitter4.mos_temp2304, time: 22]