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Failed
openmodelica_dataReconciliation.TSP_Splitter2.mos (from (result.xml))
Stacktrace
Output mismatch (see stdout for details)
Standard Output
+ TSP_Splitter2 ... equation mismatch [time: 18] ==== Log C:\WINDOWS\TEMP/omc-rtest-OpenModelica/openmodelica/dataReconciliation/TSP_Splitter2.mos_temp7188/log-TSP_Splitter2.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_Splitter2 ========================================================================== OrderedVariables (200) ======================================== 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: sinkP1.ITemperature.signal:VARIABLE(flow=false ) type: Real 13: sinkP1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 14: sinkP1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 15: sinkP1.C.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 16: sinkP1.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 17: sinkP1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 18: sinkP1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 19: sinkP1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 20: sinkP1.IPressure.signal:VARIABLE(flow=false ) type: Real 21: sinkP1.pro.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 22: sinkP1.pro.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 23: sinkP1.pro.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 24: sinkP1.pro.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 25: sinkP1.pro.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 26: sinkP1.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 27: sinkP1.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 28: sinkP1.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 29: sinkP1.pro.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 30: sinkP1.pro.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 31: sinkP1.h:VARIABLE(unit = "J/kg" ) "Fluid enthalpy" type: Real 32: sinkP1.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 33: sinkP1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real 34: sinkP1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 35: sourceQ2.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 36: sourceQ2.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 37: sourceQ2.C.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 38: sourceQ2.C.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real 39: sourceQ2.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 40: sourceQ2.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 41: sourceQ2.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 42: sourceQ2.IMassFlow.signal:VARIABLE(flow=false ) type: Real 43: sourceQ2.h:VARIABLE(unit = "J/kg" protected = true ) "Fluid specific enthalpy" type: Real 44: sourceQ2.Q:VARIABLE(unit = "kg/s" protected = true ) "Mass flow rate" type: Real 45: sourceQ2.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true ) "Fluid pressure" type: Real 46: mixer21.pro.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 47: mixer21.pro.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 48: mixer21.pro.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 49: mixer21.pro.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 50: mixer21.pro.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 51: mixer21.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 52: mixer21.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 53: mixer21.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 54: mixer21.pro.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 55: mixer21.pro.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 56: mixer21.Oalpha1.signal:VARIABLE(flow=false ) type: Real 57: mixer21.Ialpha1.signal:VARIABLE(flow=false ) type: Real 58: mixer21.Ce1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 59: mixer21.Ce1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 60: 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 61: 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 62: mixer21.Ce1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 63: mixer21.Ce1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 64: mixer21.Cs.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 65: mixer21.Cs.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 66: 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 67: 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 68: mixer21.Cs.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 69: mixer21.Cs.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 70: mixer21.Ce2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 71: mixer21.Ce2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 72: 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 73: 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 74: mixer21.Ce2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 75: mixer21.Ce2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 76: mixer21.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 77: mixer21.h:VARIABLE(start = 1e6 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 78: mixer21.P:VARIABLE(min = 0.0 start = 1e6 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 79: mixer21.alpha1:VARIABLE() "Extraction coefficient for inlet 1 (<=1)" type: Real 80: singularPressureLoss3.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 81: singularPressureLoss3.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 82: singularPressureLoss3.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 83: singularPressureLoss3.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 84: singularPressureLoss3.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real 85: 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 86: singularPressureLoss3.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 87: singularPressureLoss3.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 88: singularPressureLoss3.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real 89: singularPressureLoss3.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 90: singularPressureLoss3.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 91: singularPressureLoss3.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 92: singularPressureLoss3.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 93: singularPressureLoss3.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 94: singularPressureLoss3.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 95: 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 96: singularPressureLoss3.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 97: singularPressureLoss3.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 98: singularPressureLoss3.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 99: singularPressureLoss3.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 100: singularPressureLoss3.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 101: singularPressureLoss3.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 102: 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 103: 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 104: singularPressureLoss3.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 105: singularPressureLoss3.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 106: singularPressureLoss3.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 107: singularPressureLoss3.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 108: 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 109: 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 110: singularPressureLoss3.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 111: singularPressureLoss3.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 112: singularPressureLoss3.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 113: singularPressureLoss3.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 114: singularPressureLoss3.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 115: singularPressureLoss3.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 116: singularPressureLoss3.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real 117: singularPressureLoss3.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 118: singularPressureLoss2.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 119: singularPressureLoss2.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 120: singularPressureLoss2.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 121: singularPressureLoss2.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 122: singularPressureLoss2.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real 123: 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 124: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 125: singularPressureLoss2.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 126: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real 127: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 128: singularPressureLoss2.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 129: singularPressureLoss2.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 130: singularPressureLoss2.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 131: singularPressureLoss2.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 132: singularPressureLoss2.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 133: 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 134: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 135: singularPressureLoss2.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 136: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 137: singularPressureLoss2.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 138: singularPressureLoss2.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 139: singularPressureLoss2.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 140: 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 141: 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 142: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 143: singularPressureLoss2.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 144: singularPressureLoss2.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 145: singularPressureLoss2.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 146: 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 147: 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 148: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 149: singularPressureLoss2.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 150: singularPressureLoss2.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 151: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 152: singularPressureLoss2.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 153: singularPressureLoss2.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 154: singularPressureLoss2.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real 155: singularPressureLoss2.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 156: singularPressureLoss1.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 157: singularPressureLoss1.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 158: singularPressureLoss1.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 159: singularPressureLoss1.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 160: singularPressureLoss1.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real 161: 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 162: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 163: singularPressureLoss1.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 164: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real 165: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 166: singularPressureLoss1.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 167: singularPressureLoss1.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 168: singularPressureLoss1.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 169: singularPressureLoss1.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 170: singularPressureLoss1.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 171: 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 172: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 173: singularPressureLoss1.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 174: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 175: singularPressureLoss1.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 176: singularPressureLoss1.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 177: singularPressureLoss1.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 178: 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 179: 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 180: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 181: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 182: singularPressureLoss1.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 183: singularPressureLoss1.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 184: 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 185: 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 186: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 187: singularPressureLoss1.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 188: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 189: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 190: singularPressureLoss1.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 191: singularPressureLoss1.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 192: singularPressureLoss1.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real 193: singularPressureLoss1.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 194: sourceQ2.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 195: sourceQ2.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real 196: sinkP1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Sink pressure" type: Real 197: sinkP1.T0:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Sink temperature (active if option_temperature=1)" type: Real 198: sinkP1.h0:VARIABLE(unit = "J/kg" ) "Sink specific enthalpy (active if option_temperature=2)" type: Real 199: sourceQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 200: sourceQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real OrderedEquation (155, 200) ======================================== 1/1 (1): sourceQ2.Q0 = 100.0 [binding |0|0|0|0|] 2/2 (1): sourceQ2.h0 = 1e5 [binding |0|0|0|0|] 3/3 (1): sinkP1.P0 = 1e5 [binding |0|0|0|0|] 4/4 (1): sinkP1.T0 = 290.0 [binding |0|0|0|0|] 5/5 (1): sinkP1.h0 = 1e5 [binding |0|0|0|0|] 6/6 (1): sourceQ1.Q0 = 100.0 [binding |0|0|0|0|] 7/7 (1): sourceQ1.h0 = 1e5 [binding |0|0|0|0|] 8/8 (1): mixer21.Cs.P = singularPressureLoss1.C1.P [dynamic |0|0|0|0|] 9/9 (1): mixer21.Cs.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|] 10/10 (1): mixer21.Cs.a = singularPressureLoss1.C1.a [dynamic |0|0|0|0|] 11/11 (1): mixer21.Cs.b = singularPressureLoss1.C1.b [dynamic |0|0|0|0|] 12/12 (1): mixer21.Cs.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|] 13/13 (1): mixer21.Cs.h_vol = singularPressureLoss1.C1.h_vol [dynamic |0|0|0|0|] 14/14 (1): sourceQ2.C.P = singularPressureLoss2.C1.P [dynamic |0|0|0|0|] 15/15 (1): sourceQ2.C.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|] 16/16 (1): sourceQ2.C.a = singularPressureLoss2.C1.a [dynamic |0|0|0|0|] 17/17 (1): sourceQ2.C.b = singularPressureLoss2.C1.b [dynamic |0|0|0|0|] 18/18 (1): sourceQ2.C.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|] 19/19 (1): sourceQ2.C.h_vol = singularPressureLoss2.C1.h_vol [dynamic |0|0|0|0|] 20/20 (1): singularPressureLoss2.C2.P = mixer21.Ce1.P [dynamic |0|0|0|0|] 21/21 (1): singularPressureLoss2.C2.Q = mixer21.Ce1.Q [dynamic |0|0|0|0|] 22/22 (1): singularPressureLoss2.C2.a = mixer21.Ce1.a [dynamic |0|0|0|0|] 23/23 (1): singularPressureLoss2.C2.b = mixer21.Ce1.b [dynamic |0|0|0|0|] 24/24 (1): singularPressureLoss2.C2.h = mixer21.Ce1.h [dynamic |0|0|0|0|] 25/25 (1): singularPressureLoss2.C2.h_vol = mixer21.Ce1.h_vol [dynamic |0|0|0|0|] 26/26 (1): singularPressureLoss3.C2.P = mixer21.Ce2.P [dynamic |0|0|0|0|] 27/27 (1): singularPressureLoss3.C2.Q = mixer21.Ce2.Q [dynamic |0|0|0|0|] 28/28 (1): singularPressureLoss3.C2.a = mixer21.Ce2.a [dynamic |0|0|0|0|] 29/29 (1): singularPressureLoss3.C2.b = mixer21.Ce2.b [dynamic |0|0|0|0|] 30/30 (1): singularPressureLoss3.C2.h = mixer21.Ce2.h [dynamic |0|0|0|0|] 31/31 (1): singularPressureLoss3.C2.h_vol = mixer21.Ce2.h_vol [dynamic |0|0|0|0|] 32/32 (1): singularPressureLoss1.C2.P = sinkP1.C.P [dynamic |0|0|0|0|] 33/33 (1): singularPressureLoss1.C2.Q = sinkP1.C.Q [dynamic |0|0|0|0|] 34/34 (1): singularPressureLoss1.C2.a = sinkP1.C.a [dynamic |0|0|0|0|] 35/35 (1): singularPressureLoss1.C2.b = sinkP1.C.b [dynamic |0|0|0|0|] 36/36 (1): singularPressureLoss1.C2.h = sinkP1.C.h [dynamic |0|0|0|0|] 37/37 (1): singularPressureLoss1.C2.h_vol = sinkP1.C.h_vol [dynamic |0|0|0|0|] 38/38 (1): sourceQ1.C.P = singularPressureLoss3.C1.P [dynamic |0|0|0|0|] 39/39 (1): sourceQ1.C.Q = singularPressureLoss3.C1.Q [dynamic |0|0|0|0|] 40/40 (1): sourceQ1.C.a = singularPressureLoss3.C1.a [dynamic |0|0|0|0|] 41/41 (1): sourceQ1.C.b = singularPressureLoss3.C1.b [dynamic |0|0|0|0|] 42/42 (1): sourceQ1.C.h = singularPressureLoss3.C1.h [dynamic |0|0|0|0|] 43/43 (1): sourceQ1.C.h_vol = singularPressureLoss3.C1.h_vol [dynamic |0|0|0|0|] 44/44 (1): singularPressureLoss1.C1.P - singularPressureLoss1.C2.P = singularPressureLoss1.deltaP [dynamic |0|0|0|0|] 45/45 (1): singularPressureLoss1.C2.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|] 46/46 (1): singularPressureLoss1.C2.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|] 47/47 (1): singularPressureLoss1.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|] 48/48 (1): singularPressureLoss1.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|] 49/49 (1): 0.0 = singularPressureLoss1.C1.h - singularPressureLoss1.C1.h_vol [dynamic |0|0|0|0|] 50/50 (1): singularPressureLoss1.deltaP = singularPressureLoss1.K * singularPressureLoss1.Q * abs(singularPressureLoss1.Q) / singularPressureLoss1.rho [dynamic |0|0|0|0|] 51/51 (1): singularPressureLoss1.Pm = 0.5 * (singularPressureLoss1.C1.P + singularPressureLoss1.C2.P) [dynamic |0|0|0|0|] 52/52 (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) [dynamic |0|0|0|0|] 53/62 (1): singularPressureLoss1.h = singularPressureLoss1.pro_pT.h [dynamic |0|0|0|0|] 54/63 (1): singularPressureLoss1.rho = singularPressureLoss1.pro_pT.d [dynamic |0|0|0|0|] 55/64 (1): singularPressureLoss1.pro_ph.d = 0.0 [dynamic |0|0|0|0|] 56/65 (1): singularPressureLoss1.pro_ph.T = 0.0 [dynamic |0|0|0|0|] 57/66 (1): singularPressureLoss1.pro_ph.u = 0.0 [dynamic |0|0|0|0|] 58/67 (1): singularPressureLoss1.pro_ph.s = 0.0 [dynamic |0|0|0|0|] 59/68 (1): singularPressureLoss1.pro_ph.cp = 0.0 [dynamic |0|0|0|0|] 60/69 (1): singularPressureLoss1.pro_ph.ddhp = 0.0 [dynamic |0|0|0|0|] 61/70 (1): singularPressureLoss1.pro_ph.ddph = 0.0 [dynamic |0|0|0|0|] 62/71 (1): singularPressureLoss1.pro_ph.duph = 0.0 [dynamic |0|0|0|0|] 63/72 (1): singularPressureLoss1.pro_ph.duhp = 0.0 [dynamic |0|0|0|0|] 64/73 (1): singularPressureLoss1.pro_ph.x = 0.0 [dynamic |0|0|0|0|] 65/74 (1): singularPressureLoss2.C1.P - singularPressureLoss2.C2.P = singularPressureLoss2.deltaP [dynamic |0|0|0|0|] 66/75 (1): singularPressureLoss2.C2.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|] 67/76 (1): singularPressureLoss2.C2.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|] 68/77 (1): singularPressureLoss2.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|] 69/78 (1): singularPressureLoss2.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|] 70/79 (1): 0.0 = singularPressureLoss2.C1.h - singularPressureLoss2.C1.h_vol [dynamic |0|0|0|0|] 71/80 (1): singularPressureLoss2.deltaP = singularPressureLoss2.K * singularPressureLoss2.Q * abs(singularPressureLoss2.Q) / singularPressureLoss2.rho [dynamic |0|0|0|0|] 72/81 (1): singularPressureLoss2.Pm = 0.5 * (singularPressureLoss2.C1.P + singularPressureLoss2.C2.P) [dynamic |0|0|0|0|] 73/82 (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid) [dynamic |0|0|0|0|] 74/92 (1): singularPressureLoss2.h = singularPressureLoss2.pro_pT.h [dynamic |0|0|0|0|] 75/93 (1): singularPressureLoss2.rho = singularPressureLoss2.pro_pT.d [dynamic |0|0|0|0|] 76/94 (1): singularPressureLoss2.pro_ph.d = 0.0 [dynamic |0|0|0|0|] 77/95 (1): singularPressureLoss2.pro_ph.T = 0.0 [dynamic |0|0|0|0|] 78/96 (1): singularPressureLoss2.pro_ph.u = 0.0 [dynamic |0|0|0|0|] 79/97 (1): singularPressureLoss2.pro_ph.s = 0.0 [dynamic |0|0|0|0|] 80/98 (1): singularPressureLoss2.pro_ph.cp = 0.0 [dynamic |0|0|0|0|] 81/99 (1): singularPressureLoss2.pro_ph.ddhp = 0.0 [dynamic |0|0|0|0|] 82/100 (1): singularPressureLoss2.pro_ph.ddph = 0.0 [dynamic |0|0|0|0|] 83/101 (1): singularPressureLoss2.pro_ph.duph = 0.0 [dynamic |0|0|0|0|] 84/102 (1): singularPressureLoss2.pro_ph.duhp = 0.0 [dynamic |0|0|0|0|] 85/103 (1): singularPressureLoss2.pro_ph.x = 0.0 [dynamic |0|0|0|0|] 86/104 (1): singularPressureLoss3.C1.P - singularPressureLoss3.C2.P = singularPressureLoss3.deltaP [dynamic |0|0|0|0|] 87/105 (1): singularPressureLoss3.C2.Q = singularPressureLoss3.C1.Q [dynamic |0|0|0|0|] 88/106 (1): singularPressureLoss3.C2.h = singularPressureLoss3.C1.h [dynamic |0|0|0|0|] 89/107 (1): singularPressureLoss3.h = singularPressureLoss3.C1.h [dynamic |0|0|0|0|] 90/108 (1): singularPressureLoss3.Q = singularPressureLoss3.C1.Q [dynamic |0|0|0|0|] 91/109 (1): 0.0 = singularPressureLoss3.C1.h - singularPressureLoss3.C1.h_vol [dynamic |0|0|0|0|] 92/110 (1): singularPressureLoss3.deltaP = singularPressureLoss3.K * singularPressureLoss3.Q * abs(singularPressureLoss3.Q) / singularPressureLoss3.rho [dynamic |0|0|0|0|] 93/111 (1): singularPressureLoss3.Pm = 0.5 * (singularPressureLoss3.C1.P + singularPressureLoss3.C2.P) [dynamic |0|0|0|0|] 94/112 (10): singularPressureLoss3.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss3.Pm, singularPressureLoss3.T, singularPressureLoss3.mode, singularPressureLoss3.fluid) [dynamic |0|0|0|0|] 95/122 (1): singularPressureLoss3.h = singularPressureLoss3.pro_pT.h [dynamic |0|0|0|0|] 96/123 (1): singularPressureLoss3.rho = singularPressureLoss3.pro_pT.d [dynamic |0|0|0|0|] 97/124 (1): singularPressureLoss3.pro_ph.d = 0.0 [dynamic |0|0|0|0|] 98/125 (1): singularPressureLoss3.pro_ph.T = 0.0 [dynamic |0|0|0|0|] 99/126 (1): singularPressureLoss3.pro_ph.u = 0.0 [dynamic |0|0|0|0|] 100/127 (1): singularPressureLoss3.pro_ph.s = 0.0 [dynamic |0|0|0|0|] 101/128 (1): singularPressureLoss3.pro_ph.cp = 0.0 [dynamic |0|0|0|0|] 102/129 (1): singularPressureLoss3.pro_ph.ddhp = 0.0 [dynamic |0|0|0|0|] 103/130 (1): singularPressureLoss3.pro_ph.ddph = 0.0 [dynamic |0|0|0|0|] 104/131 (1): singularPressureLoss3.pro_ph.duph = 0.0 [dynamic |0|0|0|0|] 105/132 (1): singularPressureLoss3.pro_ph.duhp = 0.0 [dynamic |0|0|0|0|] 106/133 (1): singularPressureLoss3.pro_ph.x = 0.0 [dynamic |0|0|0|0|] 107/134 (1): mixer21.Ialpha1.signal = 0.5 [dynamic |0|0|0|0|] 108/135 (1): mixer21.P = mixer21.Ce1.P [dynamic |0|0|0|0|] 109/136 (1): mixer21.P = mixer21.Ce2.P [dynamic |0|0|0|0|] 110/137 (1): mixer21.P = mixer21.Cs.P [dynamic |0|0|0|0|] 111/138 (1): mixer21.Ce1.h_vol = mixer21.h [dynamic |0|0|0|0|] 112/139 (1): mixer21.Ce2.h_vol = mixer21.h [dynamic |0|0|0|0|] 113/140 (1): mixer21.Cs.h_vol = mixer21.h [dynamic |0|0|0|0|] 114/141 (1): 0.0 = mixer21.Ce1.Q + mixer21.Ce2.Q - mixer21.Cs.Q [dynamic |0|0|0|0|] 115/142 (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|] 116/143 (1): mixer21.alpha1 = mixer21.Ce1.Q / mixer21.Cs.Q [dynamic |0|0|0|0|] 117/144 (1): mixer21.Oalpha1.signal = mixer21.alpha1 [dynamic |0|0|0|0|] 118/145 (10): mixer21.pro = ThermoSysPro.Properties.Fluid.Ph(mixer21.P, mixer21.h, mixer21.mode, mixer21.fluid) [dynamic |0|0|0|0|] 119/155 (1): mixer21.T = mixer21.pro.T [dynamic |0|0|0|0|] 120/156 (1): sourceQ2.C.P = sourceQ2.P [dynamic |0|0|0|0|] 121/157 (1): sourceQ2.C.Q = sourceQ2.Q [dynamic |0|0|0|0|] 122/158 (1): sourceQ2.C.h_vol = sourceQ2.h [dynamic |0|0|0|0|] 123/159 (1): sourceQ2.IMassFlow.signal = sourceQ2.Q0 [dynamic |0|0|0|0|] 124/160 (1): sourceQ2.Q = sourceQ2.IMassFlow.signal [dynamic |0|0|0|0|] 125/161 (1): sourceQ2.ISpecificEnthalpy.signal = sourceQ2.h0 [dynamic |0|0|0|0|] 126/162 (1): sourceQ2.h = sourceQ2.ISpecificEnthalpy.signal [dynamic |0|0|0|0|] 127/163 (1): sinkP1.C.P = sinkP1.P [dynamic |0|0|0|0|] 128/164 (1): sinkP1.C.Q = sinkP1.Q [dynamic |0|0|0|0|] 129/165 (1): sinkP1.C.h_vol = sinkP1.h [dynamic |0|0|0|0|] 130/166 (1): sinkP1.IPressure.signal = sinkP1.P0 [dynamic |0|0|0|0|] 131/167 (1): sinkP1.P = sinkP1.IPressure.signal [dynamic |0|0|0|0|] 132/168 (1): sinkP1.ITemperature.signal = sinkP1.T0 [dynamic |0|0|0|0|] 133/169 (1): sinkP1.ISpecificEnthalpy.signal = sinkP1.h0 [dynamic |0|0|0|0|] 134/170 (1): sinkP1.T = sinkP1.ITemperature.signal [dynamic |0|0|0|0|] 135/171 (1): sinkP1.h = ThermoSysPro.Properties.WaterSteam.IF97.SpecificEnthalpy_PT(sinkP1.P, sinkP1.T, 0) [dynamic |0|0|0|0|] 136/172 (10): sinkP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sinkP1.P, sinkP1.h, sinkP1.mode) [dynamic |0|0|0|0|] 137/182 (1): sourceQ1.C.P = sourceQ1.P [dynamic |0|0|0|0|] 138/183 (1): sourceQ1.C.Q = sourceQ1.Q [dynamic |0|0|0|0|] 139/184 (1): sourceQ1.C.h_vol = sourceQ1.h [dynamic |0|0|0|0|] 140/185 (1): sourceQ1.IMassFlow.signal = sourceQ1.Q0 [dynamic |0|0|0|0|] 141/186 (1): sourceQ1.Q = sourceQ1.IMassFlow.signal [dynamic |0|0|0|0|] 142/187 (1): sourceQ1.ISpecificEnthalpy.signal = sourceQ1.h0 [dynamic |0|0|0|0|] 143/188 (1): sourceQ1.h = sourceQ1.ISpecificEnthalpy.signal [dynamic |0|0|0|0|] 144/189 (1): singularPressureLoss1.C1.a = true [binding |0|0|0|0|] 145/190 (1): singularPressureLoss1.C2.b = true [binding |0|0|0|0|] 146/191 (1): singularPressureLoss2.C1.a = true [binding |0|0|0|0|] 147/192 (1): singularPressureLoss2.C2.b = true [binding |0|0|0|0|] 148/193 (1): singularPressureLoss3.C1.a = true [binding |0|0|0|0|] 149/194 (1): singularPressureLoss3.C2.b = true [binding |0|0|0|0|] 150/195 (1): mixer21.Ce2.a = true [binding |0|0|0|0|] 151/196 (1): mixer21.Cs.b = true [binding |0|0|0|0|] 152/197 (1): mixer21.Ce1.a = true [binding |0|0|0|0|] 153/198 (1): sourceQ2.C.b = true [binding |0|0|0|0|] 154/199 (1): sinkP1.C.a = true [binding |0|0|0|0|] 155/200 (1): sourceQ1.C.b = true [binding |0|0|0|0|] Matching ======================================== 200 variables and equations var 1 is solved in eqn 200 var 2 is solved in eqn 40 var 3 is solved in eqn 42 var 4 is solved in eqn 183 var 5 is solved in eqn 184 var 6 is solved in eqn 38 var 7 is solved in eqn 187 var 8 is solved in eqn 185 var 9 is solved in eqn 188 var 10 is solved in eqn 186 var 11 is solved in eqn 182 var 12 is solved in eqn 168 var 13 is solved in eqn 35 var 14 is solved in eqn 199 var 15 is solved in eqn 36 var 16 is solved in eqn 33 var 17 is solved in eqn 165 var 18 is solved in eqn 163 var 19 is solved in eqn 169 var 20 is solved in eqn 166 var 21 is solved in eqn 181 var 22 is solved in eqn 180 var 23 is solved in eqn 179 var 24 is solved in eqn 178 var 25 is solved in eqn 177 var 26 is solved in eqn 176 var 27 is solved in eqn 175 var 28 is solved in eqn 174 var 29 is solved in eqn 173 var 30 is solved in eqn 172 var 31 is solved in eqn 171 var 32 is solved in eqn 170 var 33 is solved in eqn 164 var 34 is solved in eqn 167 var 35 is solved in eqn 198 var 36 is solved in eqn 16 var 37 is solved in eqn 18 var 38 is solved in eqn 157 var 39 is solved in eqn 158 var 40 is solved in eqn 14 var 41 is solved in eqn 161 var 42 is solved in eqn 159 var 43 is solved in eqn 162 var 44 is solved in eqn 160 var 45 is solved in eqn 156 var 46 is solved in eqn 154 var 47 is solved in eqn 153 var 48 is solved in eqn 152 var 49 is solved in eqn 151 var 50 is solved in eqn 150 var 51 is solved in eqn 149 var 52 is solved in eqn 148 var 53 is solved in eqn 147 var 54 is solved in eqn 146 var 55 is solved in eqn 145 var 56 is solved in eqn 144 var 57 is solved in eqn 134 var 58 is solved in eqn 23 var 59 is solved in eqn 197 var 60 is solved in eqn 24 var 61 is solved in eqn 21 var 62 is solved in eqn 138 var 63 is solved in eqn 135 var 64 is solved in eqn 196 var 65 is solved in eqn 10 var 66 is solved in eqn 142 var 67 is solved in eqn 141 var 68 is solved in eqn 13 var 69 is solved in eqn 8 var 70 is solved in eqn 29 var 71 is solved in eqn 195 var 72 is solved in eqn 30 var 73 is solved in eqn 27 var 74 is solved in eqn 139 var 75 is solved in eqn 136 var 76 is solved in eqn 155 var 77 is solved in eqn 140 var 78 is solved in eqn 137 var 79 is solved in eqn 143 var 80 is solved in eqn 114 var 81 is solved in eqn 121 var 82 is solved in eqn 120 var 83 is solved in eqn 119 var 84 is solved in eqn 118 var 85 is solved in eqn 117 var 86 is solved in eqn 116 var 87 is solved in eqn 115 var 88 is solved in eqn 122 var 89 is solved in eqn 113 var 90 is solved in eqn 133 var 91 is solved in eqn 132 var 92 is solved in eqn 131 var 93 is solved in eqn 130 var 94 is solved in eqn 129 var 95 is solved in eqn 128 var 96 is solved in eqn 127 var 97 is solved in eqn 126 var 98 is solved in eqn 124 var 99 is solved in eqn 125 var 100 is solved in eqn 194 var 101 is solved in eqn 28 var 102 is solved in eqn 106 var 103 is solved in eqn 105 var 104 is solved in eqn 31 var 105 is solved in eqn 26 var 106 is solved in eqn 41 var 107 is solved in eqn 193 var 108 is solved in eqn 109 var 109 is solved in eqn 39 var 110 is solved in eqn 43 var 111 is solved in eqn 104 var 112 is solved in eqn 107 var 113 is solved in eqn 111 var 114 is solved in eqn 112 var 115 is solved in eqn 123 var 116 is solved in eqn 108 var 117 is solved in eqn 110 var 118 is solved in eqn 84 var 119 is solved in eqn 91 var 120 is solved in eqn 90 var 121 is solved in eqn 89 var 122 is solved in eqn 88 var 123 is solved in eqn 87 var 124 is solved in eqn 86 var 125 is solved in eqn 85 var 126 is solved in eqn 92 var 127 is solved in eqn 83 var 128 is solved in eqn 103 var 129 is solved in eqn 102 var 130 is solved in eqn 101 var 131 is solved in eqn 100 var 132 is solved in eqn 99 var 133 is solved in eqn 98 var 134 is solved in eqn 97 var 135 is solved in eqn 96 var 136 is solved in eqn 94 var 137 is solved in eqn 95 var 138 is solved in eqn 192 var 139 is solved in eqn 22 var 140 is solved in eqn 76 var 141 is solved in eqn 75 var 142 is solved in eqn 25 var 143 is solved in eqn 20 var 144 is solved in eqn 17 var 145 is solved in eqn 191 var 146 is solved in eqn 79 var 147 is solved in eqn 15 var 148 is solved in eqn 19 var 149 is solved in eqn 74 var 150 is solved in eqn 77 var 151 is solved in eqn 81 var 152 is solved in eqn 82 var 153 is solved in eqn 93 var 154 is solved in eqn 78 var 155 is solved in eqn 80 var 156 is solved in eqn 54 var 157 is solved in eqn 61 var 158 is solved in eqn 60 var 159 is solved in eqn 59 var 160 is solved in eqn 58 var 161 is solved in eqn 57 var 162 is solved in eqn 56 var 163 is solved in eqn 55 var 164 is solved in eqn 62 var 165 is solved in eqn 53 var 166 is solved in eqn 73 var 167 is solved in eqn 72 var 168 is solved in eqn 71 var 169 is solved in eqn 70 var 170 is solved in eqn 69 var 171 is solved in eqn 68 var 172 is solved in eqn 67 var 173 is solved in eqn 66 var 174 is solved in eqn 64 var 175 is solved in eqn 65 var 176 is solved in eqn 190 var 177 is solved in eqn 34 var 178 is solved in eqn 46 var 179 is solved in eqn 45 var 180 is solved in eqn 37 var 181 is solved in eqn 32 var 182 is solved in eqn 11 var 183 is solved in eqn 189 var 184 is solved in eqn 12 var 185 is solved in eqn 9 var 186 is solved in eqn 49 var 187 is solved in eqn 44 var 188 is solved in eqn 47 var 189 is solved in eqn 51 var 190 is solved in eqn 52 var 191 is solved in eqn 63 var 192 is solved in eqn 48 var 193 is solved in eqn 50 var 194 is solved in eqn 1 var 195 is solved in eqn 2 var 196 is solved in eqn 3 var 197 is solved in eqn 4 var 198 is solved in eqn 5 var 199 is solved in eqn 6 var 200 is solved in eqn 7 Standard BLT of the original model:(200) ============================================================ 200: sourceQ1.h0: (7/7): (1): sourceQ1.h0 = 1e5 199: sourceQ1.Q0: (6/6): (1): sourceQ1.Q0 = 100.0 198: sinkP1.h0: (5/5): (1): sinkP1.h0 = 1e5 197: sinkP1.T0: (4/4): (1): sinkP1.T0 = 290.0 196: sinkP1.P0: (3/3): (1): sinkP1.P0 = 1e5 195: sourceQ2.h0: (2/2): (1): sourceQ2.h0 = 1e5 194: sourceQ2.Q0: (1/1): (1): sourceQ2.Q0 = 100.0 193: singularPressureLoss1.deltaP: (50/50): (1): singularPressureLoss1.deltaP = singularPressureLoss1.K * singularPressureLoss1.Q * abs(singularPressureLoss1.Q) / singularPressureLoss1.rho 192: singularPressureLoss1.Q: (48/48): (1): singularPressureLoss1.Q = singularPressureLoss1.C1.Q 191: singularPressureLoss1.rho: (54/63): (1): singularPressureLoss1.rho = singularPressureLoss1.pro_pT.d 190: singularPressureLoss1.T: (52/52): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 189: singularPressureLoss1.Pm: (51/51): (1): singularPressureLoss1.Pm = 0.5 * (singularPressureLoss1.C1.P + singularPressureLoss1.C2.P) 188: singularPressureLoss1.h: (47/47): (1): singularPressureLoss1.h = singularPressureLoss1.C1.h 187: singularPressureLoss1.C1.P: (44/44): (1): singularPressureLoss1.C1.P - singularPressureLoss1.C2.P = singularPressureLoss1.deltaP 186: singularPressureLoss1.C1.h_vol: (49/49): (1): 0.0 = singularPressureLoss1.C1.h - singularPressureLoss1.C1.h_vol 185: singularPressureLoss1.C1.Q: (9/9): (1): mixer21.Cs.Q = singularPressureLoss1.C1.Q 184: singularPressureLoss1.C1.h: (12/12): (1): mixer21.Cs.h = singularPressureLoss1.C1.h 183: singularPressureLoss1.C1.a: (144/189): (1): singularPressureLoss1.C1.a = true 182: singularPressureLoss1.C1.b: (11/11): (1): mixer21.Cs.b = singularPressureLoss1.C1.b 181: singularPressureLoss1.C2.P: (32/32): (1): singularPressureLoss1.C2.P = sinkP1.C.P 180: singularPressureLoss1.C2.h_vol: (37/37): (1): singularPressureLoss1.C2.h_vol = sinkP1.C.h_vol 179: singularPressureLoss1.C2.Q: (45/45): (1): singularPressureLoss1.C2.Q = singularPressureLoss1.C1.Q 178: singularPressureLoss1.C2.h: (46/46): (1): singularPressureLoss1.C2.h = singularPressureLoss1.C1.h 177: singularPressureLoss1.C2.a: (34/34): (1): singularPressureLoss1.C2.a = sinkP1.C.a 176: singularPressureLoss1.C2.b: (145/190): (1): singularPressureLoss1.C2.b = true 175: singularPressureLoss1.pro_ph.T: (56/65): (1): singularPressureLoss1.pro_ph.T = 0.0 174: singularPressureLoss1.pro_ph.d: (55/64): (1): singularPressureLoss1.pro_ph.d = 0.0 173: singularPressureLoss1.pro_ph.u: (57/66): (1): singularPressureLoss1.pro_ph.u = 0.0 172: singularPressureLoss1.pro_ph.s: (58/67): (1): singularPressureLoss1.pro_ph.s = 0.0 171: singularPressureLoss1.pro_ph.cp: (59/68): (1): singularPressureLoss1.pro_ph.cp = 0.0 170: singularPressureLoss1.pro_ph.ddhp: (60/69): (1): singularPressureLoss1.pro_ph.ddhp = 0.0 169: singularPressureLoss1.pro_ph.ddph: (61/70): (1): singularPressureLoss1.pro_ph.ddph = 0.0 168: singularPressureLoss1.pro_ph.duph: (62/71): (1): singularPressureLoss1.pro_ph.duph = 0.0 167: singularPressureLoss1.pro_ph.duhp: (63/72): (1): singularPressureLoss1.pro_ph.duhp = 0.0 166: singularPressureLoss1.pro_ph.x: (64/73): (1): singularPressureLoss1.pro_ph.x = 0.0 165: singularPressureLoss1.pro_pT.d: (52/53): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 164: singularPressureLoss1.pro_pT.h: (53/62): (1): singularPressureLoss1.h = singularPressureLoss1.pro_pT.h 163: singularPressureLoss1.pro_pT.u: (52/55): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 162: singularPressureLoss1.pro_pT.s: (52/56): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 161: singularPressureLoss1.pro_pT.cp: (52/57): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 160: singularPressureLoss1.pro_pT.ddTp: (52/58): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 159: singularPressureLoss1.pro_pT.ddpT: (52/59): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 158: singularPressureLoss1.pro_pT.dupT: (52/60): ( ...[truncated 143098 chars]... |0|0|] 9/9 (1): mixer21.Cs.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|] 10/10 (1): mixer21.Cs.a = singularPressureLoss1.C1.a [dynamic |0|0|0|0|] 11/11 (1): mixer21.Cs.b = singularPressureLoss1.C1.b [dynamic |0|0|0|0|] 12/12 (1): mixer21.Cs.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|] @@ -578,16 +578,16 @@ var 200 is solved in eqn 7 Standard BLT of the original model:(200) ============================================================ -200: sourceQ1.h0: (7/7): (1): sourceQ1.h0 = 100000.0 +200: sourceQ1.h0: (7/7): (1): sourceQ1.h0 = 1e5 199: sourceQ1.Q0: (6/6): (1): sourceQ1.Q0 = 100.0 -198: sinkP1.h0: (5/5): (1): sinkP1.h0 = 100000.0 +198: sinkP1.h0: (5/5): (1): sinkP1.h0 = 1e5 197: sinkP1.T0: (4/4): (1): sinkP1.T0 = 290.0 -196: sinkP1.P0: (3/3): (1): sinkP1.P0 = 100000.0 -195: sourceQ2.h0: (2/2): (1): sourceQ2.h0 = 100000.0 +196: sinkP1.P0: (3/3): (1): sinkP1.P0 = 1e5 +195: sourceQ2.h0: (2/2): (1): sourceQ2.h0 = 1e5 194: sourceQ2.Q0: (1/1): (1): sourceQ2.Q0 = 100.0 193: singularPressureLoss1.deltaP: (50/50): (1): singularPressureLoss1.deltaP = singularPressureLoss1.K * singularPressureLoss1.Q * abs(singularPressureLoss1.Q) / singularPressureLoss1.rho 192: singularPressureLoss1.Q: (48/48): (1): singularPressureLoss1.Q = singularPressureLoss1.C1.Q 191: singularPressureLoss1.rho: (54/63): (1): singularPressureLoss1.rho = singularPressureLoss1.pro_pT.d 190: singularPressureLoss1.T: (52/52): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) @@ -791,11 +791,11 @@ Boundary conditions (7) ======================================== 1: sourceQ2.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 2: sourceQ2.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real -3: sinkP1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Sink pressure" type: Real +3: sinkP1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Sink pressure" type: Real 4: sinkP1.T0:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Sink temperature (active if option_temperature=1)" type: Real 5: sinkP1.h0:VARIABLE(unit = "J/kg" ) "Sink specific enthalpy (active if option_temperature=2)" type: Real 6: sourceQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 7: sourceQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real @@ -813,16 +813,16 @@ 107: singularPressureLoss3.C1.a: (148/193): (1): singularPressureLoss3.C1.a = true 138: singularPressureLoss2.C2.b: (147/192): (1): singularPressureLoss2.C2.b = true 145: singularPressureLoss2.C1.a: (146/191): (1): singularPressureLoss2.C1.a = true 176: singularPressureLoss1.C2.b: (145/190): (1): singularPressureLoss1.C2.b = true 183: singularPressureLoss1.C1.a: (144/189): (1): singularPressureLoss1.C1.a = true -200: sourceQ1.h0: (7/7): (1): sourceQ1.h0 = 100000.0 +200: sourceQ1.h0: (7/7): (1): sourceQ1.h0 = 1e5 199: sourceQ1.Q0: (6/6): (1): sourceQ1.Q0 = 100.0 -198: sinkP1.h0: (5/5): (1): sinkP1.h0 = 100000.0 +198: sinkP1.h0: (5/5): (1): sinkP1.h0 = 1e5 197: sinkP1.T0: (4/4): (1): sinkP1.T0 = 290.0 -196: sinkP1.P0: (3/3): (1): sinkP1.P0 = 100000.0 -195: sourceQ2.h0: (2/2): (1): sourceQ2.h0 = 100000.0 +196: sinkP1.P0: (3/3): (1): sinkP1.P0 = 1e5 +195: sourceQ2.h0: (2/2): (1): sourceQ2.h0 = 1e5 194: sourceQ2.Q0: (1/1): (1): sourceQ2.Q0 = 100.0 E-BLT: equations that compute the variables of interest:(3) ============================================================ @@ -868,204 +868,204 @@ OrderedVariables (200) ======================================== 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: sinkP1.ITemperature.signal:VARIABLE(flow=false ) type: Real 13: sinkP1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 14: sinkP1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -15: sinkP1.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 +15: sinkP1.C.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 16: sinkP1.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 -17: sinkP1.C.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -18: sinkP1.C.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +17: sinkP1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +18: sinkP1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 19: sinkP1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 20: sinkP1.IPressure.signal:VARIABLE(flow=false ) type: Real 21: sinkP1.pro.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 22: sinkP1.pro.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 23: sinkP1.pro.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 24: sinkP1.pro.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 25: sinkP1.pro.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -26: sinkP1.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 -27: sinkP1.pro.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -28: sinkP1.pro.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -29: sinkP1.pro.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +26: sinkP1.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real +27: sinkP1.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +28: sinkP1.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +29: sinkP1.pro.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 30: sinkP1.pro.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 31: sinkP1.h:VARIABLE(unit = "J/kg" ) "Fluid enthalpy" type: Real 32: sinkP1.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 33: sinkP1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real -34: sinkP1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure" type: Real +34: sinkP1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 35: sourceQ2.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 36: sourceQ2.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -37: sourceQ2.C.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real +37: sourceQ2.C.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 38: sourceQ2.C.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real -39: sourceQ2.C.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -40: sourceQ2.C.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +39: sourceQ2.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +40: sourceQ2.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 41: sourceQ2.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 42: sourceQ2.IMassFlow.signal:VARIABLE(flow=false ) type: Real 43: sourceQ2.h:VARIABLE(unit = "J/kg" protected = true ) "Fluid specific enthalpy" type: Real 44: sourceQ2.Q:VARIABLE(unit = "kg/s" protected = true ) "Mass flow rate" type: Real -45: sourceQ2.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 protected = true ) "Fluid pressure" type: Real +45: sourceQ2.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true ) "Fluid pressure" type: Real 46: mixer21.pro.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 47: mixer21.pro.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 48: mixer21.pro.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 49: mixer21.pro.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 50: mixer21.pro.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -51: 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 -52: mixer21.pro.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -53: mixer21.pro.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -54: mixer21.pro.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +51: mixer21.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real +52: mixer21.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +53: mixer21.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +54: mixer21.pro.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 55: mixer21.pro.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 56: mixer21.Oalpha1.signal:VARIABLE(flow=false ) type: Real 57: mixer21.Ialpha1.signal:VARIABLE(flow=false ) type: Real 58: mixer21.Ce1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 59: mixer21.Ce1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -60: 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 +60: 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 61: 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 -62: mixer21.Ce1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -63: 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 +62: mixer21.Ce1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +63: mixer21.Ce1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 64: mixer21.Cs.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 65: mixer21.Cs.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -66: 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 +66: 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 67: 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 -68: mixer21.Cs.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -69: 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 +68: mixer21.Cs.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +69: mixer21.Cs.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 70: mixer21.Ce2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 71: mixer21.Ce2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -72: 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 +72: 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 73: 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 -74: mixer21.Ce2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -75: 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 +74: mixer21.Ce2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +75: mixer21.Ce2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 76: mixer21.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real -77: mixer21.h:VARIABLE(start = 1000000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real -78: mixer21.P:VARIABLE(min = 0.0 start = 1000000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure" type: Real +77: mixer21.h:VARIABLE(start = 1e6 unit = "J/kg" ) "Fluid specific enthalpy" type: Real +78: mixer21.P:VARIABLE(min = 0.0 start = 1e6 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 79: mixer21.alpha1:VARIABLE() "Extraction coefficient for inlet 1 (<=1)" type: Real 80: singularPressureLoss3.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 81: singularPressureLoss3.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 82: singularPressureLoss3.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 83: singularPressureLoss3.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 84: singularPressureLoss3.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real -85: 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 -86: singularPressureLoss3.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -87: singularPressureLoss3.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -88: singularPressureLoss3.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real -89: singularPressureLoss3.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +85: 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 +86: singularPressureLoss3.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +87: singularPressureLoss3.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +88: singularPressureLoss3.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real +89: singularPressureLoss3.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 90: singularPressureLoss3.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 91: singularPressureLoss3.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 92: singularPressureLoss3.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 93: singularPressureLoss3.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 94: singularPressureLoss3.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -95: 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 -96: singularPressureLoss3.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -97: singularPressureLoss3.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -98: singularPressureLoss3.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +95: 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 +96: singularPressureLoss3.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +97: singularPressureLoss3.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +98: singularPressureLoss3.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 99: singularPressureLoss3.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 100: singularPressureLoss3.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 101: singularPressureLoss3.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -102: 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 +102: 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 103: 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 -104: singularPressureLoss3.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -105: 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 +104: singularPressureLoss3.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +105: singularPressureLoss3.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 106: singularPressureLoss3.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 107: singularPressureLoss3.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -108: 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 +108: 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 109: 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 -110: singularPressureLoss3.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -111: 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 -112: singularPressureLoss3.h:VARIABLE(start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real -113: singularPressureLoss3.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real +110: singularPressureLoss3.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +111: singularPressureLoss3.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real +112: singularPressureLoss3.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real +113: singularPressureLoss3.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 114: singularPressureLoss3.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 115: singularPressureLoss3.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 116: singularPressureLoss3.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real -117: singularPressureLoss3.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real +117: singularPressureLoss3.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 118: singularPressureLoss2.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 119: singularPressureLoss2.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 120: singularPressureLoss2.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 121: singularPressureLoss2.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 122: singularPressureLoss2.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real -123: 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 -124: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -125: singularPressureLoss2.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -126: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real -127: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +123: 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 +124: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +125: singularPressureLoss2.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +126: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real +127: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 128: singularPressureLoss2.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 129: singularPressureLoss2.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 130: singularPressureLoss2.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 131: singularPressureLoss2.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 132: singularPressureLoss2.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -133: 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 -134: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -135: singularPressureLoss2.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -136: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +133: 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 +134: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +135: singularPressureLoss2.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +136: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 137: singularPressureLoss2.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 138: singularPressureLoss2.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 139: singularPressureLoss2.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -140: 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 +140: 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 141: 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 -142: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -143: 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 +142: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +143: singularPressureLoss2.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 144: singularPressureLoss2.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 145: singularPressureLoss2.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -146: 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 +146: 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 147: 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 -148: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -149: 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 -150: singularPressureLoss2.h:VARIABLE(start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real -151: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real +148: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +149: singularPressureLoss2.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real +150: singularPressureLoss2.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real +151: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 152: singularPressureLoss2.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 153: singularPressureLoss2.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 154: singularPressureLoss2.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real -155: singularPressureLoss2.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real +155: singularPressureLoss2.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 156: singularPressureLoss1.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 157: singularPressureLoss1.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 158: singularPressureLoss1.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 159: singularPressureLoss1.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 160: singularPressureLoss1.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real -161: 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 -162: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -163: singularPressureLoss1.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -164: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real -165: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +161: 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 +162: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +163: singularPressureLoss1.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +164: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real +165: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 166: singularPressureLoss1.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 167: singularPressureLoss1.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 168: singularPressureLoss1.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 169: singularPressureLoss1.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 170: singularPressureLoss1.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -171: 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 -172: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -173: singularPressureLoss1.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -174: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +171: 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 +172: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +173: singularPressureLoss1.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +174: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 175: singularPressureLoss1.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 176: singularPressureLoss1.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 177: singularPressureLoss1.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -178: 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 +178: 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 179: 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 -180: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -181: 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 +180: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +181: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 182: singularPressureLoss1.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 183: singularPressureLoss1.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -184: 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 +184: 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 185: 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 -186: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -187: 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 -188: singularPressureLoss1.h:VARIABLE(start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real -189: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real +186: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +187: singularPressureLoss1.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real +188: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real +189: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 190: singularPressureLoss1.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 191: singularPressureLoss1.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 192: singularPressureLoss1.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real -193: singularPressureLoss1.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real +193: singularPressureLoss1.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 194: sourceQ2.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 195: sourceQ2.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real -196: sinkP1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Sink pressure" type: Real +196: sinkP1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Sink pressure" type: Real 197: sinkP1.T0:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Sink temperature (active if option_temperature=1)" type: Real 198: sinkP1.h0:VARIABLE(unit = "J/kg" ) "Sink specific enthalpy (active if option_temperature=2)" type: Real 199: sourceQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 200: sourceQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real @@ -1073,16 +1073,16 @@ OrderedEquation (155, 200) ======================================== 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): sourceQ2.Q0 = 100.0 [binding |0|0|0|0|] -4/4 (1): sourceQ2.h0 = 100000.0 [binding |0|0|0|0|] -5/5 (1): sinkP1.P0 = 100000.0 [binding |0|0|0|0|] +4/4 (1): sourceQ2.h0 = 1e5 [binding |0|0|0|0|] +5/5 (1): sinkP1.P0 = 1e5 [binding |0|0|0|0|] 6/6 (1): sinkP1.T0 = 290.0 [binding |0|0|0|0|] -7/7 (1): sinkP1.h0 = 100000.0 [binding |0|0|0|0|] +7/7 (1): sinkP1.h0 = 1e5 [binding |0|0|0|0|] 8/8 (1): sourceQ1.Q0 = 100.0 [binding |0|0|0|0|] -9/9 (1): sourceQ1.h0 = 100000.0 [binding |0|0|0|0|] +9/9 (1): sourceQ1.h0 = 1e5 [binding |0|0|0|0|] 10/10 (1): mixer21.Cs.P = singularPressureLoss1.C1.P [dynamic |0|0|0|0|] 11/11 (1): mixer21.Cs.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|] 12/12 (1): mixer21.Cs.a = singularPressureLoss1.C1.a [dynamic |0|0|0|0|] 13/13 (1): mixer21.Cs.b = singularPressureLoss1.C1.b [dynamic |0|0|0|0|] 14/14 (1): mixer21.Cs.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|] @@ -1433,16 +1433,16 @@ var 200 is solved in eqn 9 Standard BLT of the original model:(200) ============================================================ -200: sourceQ1.h0: (9/9): (1): sourceQ1.h0 = 100000.0 +200: sourceQ1.h0: (9/9): (1): sourceQ1.h0 = 1e5 199: sourceQ1.Q0: (8/8): (1): sourceQ1.Q0 = 100.0 -198: sinkP1.h0: (7/7): (1): sinkP1.h0 = 100000.0 +198: sinkP1.h0: (7/7): (1): sinkP1.h0 = 1e5 197: sinkP1.T0: (6/6): (1): sinkP1.T0 = 290.0 -196: sinkP1.P0: (5/5): (1): sinkP1.P0 = 100000.0 -195: sourceQ2.h0: (4/4): (1): sourceQ2.h0 = 100000.0 +196: sinkP1.P0: (5/5): (1): sinkP1.P0 = 1e5 +195: sourceQ2.h0: (4/4): (1): sourceQ2.h0 = 1e5 194: sourceQ2.Q0: (3/3): (1): sourceQ2.Q0 = 100.0 193: singularPressureLoss1.deltaP: (52/52): (1): singularPressureLoss1.deltaP = singularPressureLoss1.K * singularPressureLoss1.Q * abs(singularPressureLoss1.Q) / singularPressureLoss1.rho 192: singularPressureLoss1.Q: (50/50): (1): singularPressureLoss1.Q = singularPressureLoss1.C1.Q 191: singularPressureLoss1.rho: (56/65): (1): singularPressureLoss1.rho = singularPressureLoss1.pro_pT.d 190: singularPressureLoss1.T: (54/54): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) @@ -1646,11 +1646,11 @@ Boundary conditions (7) ======================================== 1: sourceQ2.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 2: sourceQ2.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real -3: sinkP1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Sink pressure" type: Real +3: sinkP1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Sink pressure" type: Real 4: sinkP1.T0:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Sink temperature (active if option_temperature=1)" type: Real 5: sinkP1.h0:VARIABLE(unit = "J/kg" ) "Sink specific enthalpy (active if option_temperature=2)" type: Real 6: sourceQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 7: sourceQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real @@ -1668,16 +1668,16 @@ 107: singularPressureLoss3.C1.a: (148/193): (1): singularPressureLoss3.C1.a = true 138: singularPressureLoss2.C2.b: (147/192): (1): singularPressureLoss2.C2.b = true 145: singularPressureLoss2.C1.a: (146/191): (1): singularPressureLoss2.C1.a = true 176: singularPressureLoss1.C2.b: (145/190): (1): singularPressureLoss1.C2.b = true 183: singularPressureLoss1.C1.a: (144/189): (1): singularPressureLoss1.C1.a = true -200: sourceQ1.h0: (9/9): (1): sourceQ1.h0 = 100000.0 +200: sourceQ1.h0: (9/9): (1): sourceQ1.h0 = 1e5 199: sourceQ1.Q0: (8/8): (1): sourceQ1.Q0 = 100.0 -198: sinkP1.h0: (7/7): (1): sinkP1.h0 = 100000.0 +198: sinkP1.h0: (7/7): (1): sinkP1.h0 = 1e5 197: sinkP1.T0: (6/6): (1): sinkP1.T0 = 290.0 -196: sinkP1.P0: (5/5): (1): sinkP1.P0 = 100000.0 -195: sourceQ2.h0: (4/4): (1): sourceQ2.h0 = 100000.0 +196: sinkP1.P0: (5/5): (1): sinkP1.P0 = 1e5 +195: sourceQ2.h0: (4/4): (1): sourceQ2.h0 = 1e5 194: sourceQ2.Q0: (3/3): (1): sourceQ2.Q0 = 100.0 154: singularPressureLoss2.Q: (2/2): (1): singularPressureLoss2.Q = 0.0 116: singularPressureLoss3.Q: (1/1): (1): singularPressureLoss3.Q = 0.0 @@ -1794,17 +1794,18 @@ ========================================================================== -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_Splitter2', options = '', outputFormat = 'mat', variableFilter = '.*', cflags = '', simflags = '-reconcile -sx=./NewDataReconciliationSimpleTests/resources/DataReconciliationSimpleTests.TSP_Splitter2_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_Splitter2', options = '', outputFormat = 'mat', variableFilter = '.*', cflags = '', simflags = '-reconcile -sx=./NewDataReconciliationSimpleTests/resources/DataReconciliationSimpleTests.TSP_Splitter2_Inputs.csv -eps=0.0023 -lv=LOG_JAC'", +messages = "Simulation execution failed for model: NewDataReconciliationSimpleTests.TSP_Splitter2 +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_Splitter2 -LOG_STDOUT | info | DataReconciliation Completed! +LOG_STDOUT | error | Measurement input file path not found ./NewDataReconciliationSimpleTests/resources/DataReconciliationSimpleTests.TSP_Splitter2_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 1799: Text differs: expected: resultFile = "econcile", got: resultFile = "", == 1 out of 1 tests failed [openmodelica/dataReconciliation/TSP_Splitter2.mos_temp7188, time: 18]