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Failed
openmodelica_dataReconciliation.TSP_Splitter1.mos (from (result.xml))
Stacktrace
Output mismatch (see stdout for details)
Standard Output
+ TSP_Splitter1.mos ... equation mismatch [time: 26] ==== Log C:\WINDOWS\TEMP/omc-rtest-OpenModelica/openmodelica/dataReconciliation/TSP_Splitter1.mos_temp2479/log-TSP_Splitter1.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_Splitter1 ========================================================================== OrderedVariables (226) ======================================== 1: sinkP1.ITemperature.signal:VARIABLE(flow=false ) type: Real 2: sinkP1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 3: sinkP1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 4: 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 5: 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 6: sinkP1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 7: sinkP1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 8: sinkP1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 9: sinkP1.IPressure.signal:VARIABLE(flow=false ) type: Real 10: sinkP1.pro.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 11: sinkP1.pro.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 12: sinkP1.pro.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 13: sinkP1.pro.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 14: sinkP1.pro.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 15: sinkP1.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 16: sinkP1.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 17: sinkP1.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 18: sinkP1.pro.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 19: sinkP1.pro.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 20: sinkP1.h:VARIABLE(unit = "J/kg" ) "Fluid enthalpy" type: Real 21: sinkP1.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 22: sinkP1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real 23: sinkP1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 24: sourceP2.ITemperature.signal:VARIABLE(flow=false ) type: Real 25: sourceP2.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 26: sourceP2.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 27: sourceP2.C.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 28: sourceP2.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 29: sourceP2.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 30: sourceP2.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 31: sourceP2.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 32: sourceP2.IPressure.signal:VARIABLE(flow=false ) type: Real 33: sourceP2.pro.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 34: sourceP2.pro.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 35: sourceP2.pro.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 36: sourceP2.pro.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 37: sourceP2.pro.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 38: sourceP2.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 39: sourceP2.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 40: sourceP2.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 41: sourceP2.pro.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 42: sourceP2.pro.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 43: sourceP2.h:VARIABLE(unit = "J/kg" ) "Fluid enthalpy" type: Real 44: sourceP2.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 45: sourceP2.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real 46: sourceP2.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 47: sourceP1.ITemperature.signal:VARIABLE(flow=false ) type: Real 48: sourceP1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 49: sourceP1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 50: sourceP1.C.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 51: sourceP1.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 52: sourceP1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 53: sourceP1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 54: sourceP1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 55: sourceP1.IPressure.signal:VARIABLE(flow=false ) type: Real 56: sourceP1.pro.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 57: sourceP1.pro.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 58: sourceP1.pro.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 59: sourceP1.pro.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 60: sourceP1.pro.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 61: sourceP1.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 62: sourceP1.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 63: sourceP1.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 64: sourceP1.pro.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 65: sourceP1.pro.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 66: sourceP1.h:VARIABLE(unit = "J/kg" ) "Fluid enthalpy" type: Real 67: sourceP1.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 68: sourceP1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real 69: sourceP1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 70: mixer21.pro.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 71: mixer21.pro.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 72: mixer21.pro.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 73: mixer21.pro.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 74: mixer21.pro.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 75: mixer21.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 76: mixer21.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 77: mixer21.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 78: mixer21.pro.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 79: mixer21.pro.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 80: mixer21.Oalpha1.signal:VARIABLE(flow=false ) type: Real 81: mixer21.Ialpha1.signal:VARIABLE(flow=false ) type: Real 82: mixer21.Ce1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 83: mixer21.Ce1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 84: 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 85: 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 86: mixer21.Ce1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 87: mixer21.Ce1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 88: mixer21.Cs.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 89: mixer21.Cs.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 90: 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 91: 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 92: mixer21.Cs.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 93: mixer21.Cs.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 94: mixer21.Ce2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 95: mixer21.Ce2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 96: 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 97: 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 98: mixer21.Ce2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 99: mixer21.Ce2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 100: mixer21.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 101: mixer21.h:VARIABLE(start = 1e6 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 102: mixer21.P:VARIABLE(min = 0.0 start = 1e6 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 103: mixer21.alpha1:VARIABLE() "Extraction coefficient for inlet 1 (<=1)" type: Real 104: singularPressureLoss3.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 105: singularPressureLoss3.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 106: singularPressureLoss3.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 107: singularPressureLoss3.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 108: singularPressureLoss3.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real 109: 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 110: singularPressureLoss3.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 111: singularPressureLoss3.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 112: singularPressureLoss3.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real 113: singularPressureLoss3.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 114: singularPressureLoss3.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 115: singularPressureLoss3.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 116: singularPressureLoss3.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 117: singularPressureLoss3.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 118: singularPressureLoss3.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 119: 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 120: singularPressureLoss3.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 121: singularPressureLoss3.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 122: singularPressureLoss3.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 123: singularPressureLoss3.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 124: singularPressureLoss3.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 125: singularPressureLoss3.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 126: 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 127: 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 128: singularPressureLoss3.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 129: singularPressureLoss3.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 130: singularPressureLoss3.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 131: singularPressureLoss3.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 132: 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 133: 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 134: singularPressureLoss3.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 135: singularPressureLoss3.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 136: singularPressureLoss3.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 137: singularPressureLoss3.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 138: singularPressureLoss3.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 139: singularPressureLoss3.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 140: singularPressureLoss3.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real 141: singularPressureLoss3.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 142: singularPressureLoss2.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 143: singularPressureLoss2.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 144: singularPressureLoss2.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 145: singularPressureLoss2.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 146: singularPressureLoss2.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real 147: 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 148: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 149: singularPressureLoss2.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 150: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real 151: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 152: singularPressureLoss2.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 153: singularPressureLoss2.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 154: singularPressureLoss2.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 155: singularPressureLoss2.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 156: singularPressureLoss2.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 157: 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 158: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 159: singularPressureLoss2.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 160: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 161: singularPressureLoss2.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 162: singularPressureLoss2.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 163: singularPressureLoss2.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 164: 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 165: 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 166: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 167: singularPressureLoss2.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 168: singularPressureLoss2.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 169: singularPressureLoss2.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 170: 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 171: 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 172: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 173: singularPressureLoss2.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 174: singularPressureLoss2.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 175: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 176: singularPressureLoss2.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 177: singularPressureLoss2.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 178: singularPressureLoss2.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real 179: singularPressureLoss2.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 180: singularPressureLoss1.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 181: singularPressureLoss1.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 182: singularPressureLoss1.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 183: singularPressureLoss1.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 184: singularPressureLoss1.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real 185: 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 186: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 187: singularPressureLoss1.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 188: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real 189: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 190: singularPressureLoss1.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 191: singularPressureLoss1.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 192: singularPressureLoss1.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 193: singularPressureLoss1.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 194: singularPressureLoss1.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 195: 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 196: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 197: singularPressureLoss1.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 198: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 199: singularPressureLoss1.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 200: singularPressureLoss1.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 201: singularPressureLoss1.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 202: 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 203: 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 204: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 205: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 206: singularPressureLoss1.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 207: singularPressureLoss1.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 208: 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 209: 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 210: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 211: singularPressureLoss1.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 212: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 213: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 214: singularPressureLoss1.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 215: singularPressureLoss1.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 216: singularPressureLoss1.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real 217: singularPressureLoss1.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 218: sourceP1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Source pressure" type: Real 219: sourceP1.T0:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Source temperature (active if option_temperature=1)" type: Real 220: sourceP1.h0:VARIABLE(unit = "J/kg" ) "Source specific enthalpy (active if option_temperature=2)" type: Real 221: sourceP2.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Source pressure" type: Real 222: sourceP2.T0:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Source temperature (active if option_temperature=1)" type: Real 223: sourceP2.h0:VARIABLE(unit = "J/kg" ) "Source specific enthalpy (active if option_temperature=2)" type: Real 224: sinkP1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Sink pressure" type: Real 225: sinkP1.T0:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Sink temperature (active if option_temperature=1)" type: Real 226: sinkP1.h0:VARIABLE(unit = "J/kg" ) "Sink specific enthalpy (active if option_temperature=2)" type: Real OrderedEquation (163, 226) ======================================== 1/1 (1): sourceP1.P0 = 3e5 [binding |0|0|0|0|] 2/2 (1): sourceP1.T0 = 290.0 [binding |0|0|0|0|] 3/3 (1): sourceP1.h0 = 1e5 [binding |0|0|0|0|] 4/4 (1): sourceP2.P0 = 3e5 [binding |0|0|0|0|] 5/5 (1): sourceP2.T0 = 290.0 [binding |0|0|0|0|] 6/6 (1): sourceP2.h0 = 1e5 [binding |0|0|0|0|] 7/7 (1): sinkP1.P0 = 1e5 [binding |0|0|0|0|] 8/8 (1): sinkP1.T0 = 290.0 [binding |0|0|0|0|] 9/9 (1): sinkP1.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|] 15/15 (1): mixer21.Cs.h_vol = singularPressureLoss1.C1.h_vol [dynamic |0|0|0|0|] 16/16 (1): sourceP1.C.P = singularPressureLoss2.C1.P [dynamic |0|0|0|0|] 17/17 (1): sourceP1.C.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|] 18/18 (1): sourceP1.C.a = singularPressureLoss2.C1.a [dynamic |0|0|0|0|] 19/19 (1): sourceP1.C.b = singularPressureLoss2.C1.b [dynamic |0|0|0|0|] 20/20 (1): sourceP1.C.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|] 21/21 (1): sourceP1.C.h_vol = singularPressureLoss2.C1.h_vol [dynamic |0|0|0|0|] 22/22 (1): singularPressureLoss2.C2.P = mixer21.Ce1.P [dynamic |0|0|0|0|] 23/23 (1): singularPressureLoss2.C2.Q = mixer21.Ce1.Q [dynamic |0|0|0|0|] 24/24 (1): singularPressureLoss2.C2.a = mixer21.Ce1.a [dynamic |0|0|0|0|] 25/25 (1): singularPressureLoss2.C2.b = mixer21.Ce1.b [dynamic |0|0|0|0|] 26/26 (1): singularPressureLoss2.C2.h = mixer21.Ce1.h [dynamic |0|0|0|0|] 27/27 (1): singularPressureLoss2.C2.h_vol = mixer21.Ce1.h_vol [dynamic |0|0|0|0|] 28/28 (1): sourceP2.C.P = singularPressureLoss3.C1.P [dynamic |0|0|0|0|] 29/29 (1): sourceP2.C.Q = singularPressureLoss3.C1.Q [dynamic |0|0|0|0|] 30/30 (1): sourceP2.C.a = singularPressureLoss3.C1.a [dynamic |0|0|0|0|] 31/31 (1): sourceP2.C.b = singularPressureLoss3.C1.b [dynamic |0|0|0|0|] 32/32 (1): sourceP2.C.h = singularPressureLoss3.C1.h [dynamic |0|0|0|0|] 33/33 (1): sourceP2.C.h_vol = singularPressureLoss3.C1.h_vol [dynamic |0|0|0|0|] 34/34 (1): singularPressureLoss3.C2.P = mixer21.Ce2.P [dynamic |0|0|0|0|] 35/35 (1): singularPressureLoss3.C2.Q = mixer21.Ce2.Q [dynamic |0|0|0|0|] 36/36 (1): singularPressureLoss3.C2.a = mixer21.Ce2.a [dynamic |0|0|0|0|] 37/37 (1): singularPressureLoss3.C2.b = mixer21.Ce2.b [dynamic |0|0|0|0|] 38/38 (1): singularPressureLoss3.C2.h = mixer21.Ce2.h [dynamic |0|0|0|0|] 39/39 (1): singularPressureLoss3.C2.h_vol = mixer21.Ce2.h_vol [dynamic |0|0|0|0|] 40/40 (1): singularPressureLoss1.C2.P = sinkP1.C.P [dynamic |0|0|0|0|] 41/41 (1): singularPressureLoss1.C2.Q = sinkP1.C.Q [dynamic |0|0|0|0|] 42/42 (1): singularPressureLoss1.C2.a = sinkP1.C.a [dynamic |0|0|0|0|] 43/43 (1): singularPressureLoss1.C2.b = sinkP1.C.b [dynamic |0|0|0|0|] 44/44 (1): singularPressureLoss1.C2.h = sinkP1.C.h [dynamic |0|0|0|0|] 45/45 (1): singularPressureLoss1.C2.h_vol = sinkP1.C.h_vol [dynamic |0|0|0|0|] 46/46 (1): singularPressureLoss1.C1.P - singularPressureLoss1.C2.P = singularPressureLoss1.deltaP [dynamic |0|0|0|0|] 47/47 (1): singularPressureLoss1.C2.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|] 48/48 (1): singularPressureLoss1.C2.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|] 49/49 (1): singularPressureLoss1.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|] 50/50 (1): singularPressureLoss1.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|] 51/51 (1): 0.0 = singularPressureLoss1.C1.h - singularPressureLoss1.C1.h_vol [dynamic |0|0|0|0|] 52/52 (1): singularPressureLoss1.deltaP = singularPressureLoss1.K * singularPressureLoss1.Q * abs(singularPressureLoss1.Q) / singularPressureLoss1.rho [dynamic |0|0|0|0|] 53/53 (1): singularPressureLoss1.Pm = 0.5 * (singularPressureLoss1.C1.P + singularPressureLoss1.C2.P) [dynamic |0|0|0|0|] 54/54 (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) [dynamic |0|0|0|0|] 55/64 (1): singularPressureLoss1.h = singularPressureLoss1.pro_pT.h [dynamic |0|0|0|0|] 56/65 (1): singularPressureLoss1.rho = singularPressureLoss1.pro_pT.d [dynamic |0|0|0|0|] 57/66 (1): singularPressureLoss1.pro_ph.d = 0.0 [dynamic |0|0|0|0|] 58/67 (1): singularPressureLoss1.pro_ph.T = 0.0 [dynamic |0|0|0|0|] 59/68 (1): singularPressureLoss1.pro_ph.u = 0.0 [dynamic |0|0|0|0|] 60/69 (1): singularPressureLoss1.pro_ph.s = 0.0 [dynamic |0|0|0|0|] 61/70 (1): singularPressureLoss1.pro_ph.cp = 0.0 [dynamic |0|0|0|0|] 62/71 (1): singularPressureLoss1.pro_ph.ddhp = 0.0 [dynamic |0|0|0|0|] 63/72 (1): singularPressureLoss1.pro_ph.ddph = 0.0 [dynamic |0|0|0|0|] 64/73 (1): singularPressureLoss1.pro_ph.duph = 0.0 [dynamic |0|0|0|0|] 65/74 (1): singularPressureLoss1.pro_ph.duhp = 0.0 [dynamic |0|0|0|0|] 66/75 (1): singularPressureLoss1.pro_ph.x = 0.0 [dynamic |0|0|0|0|] 67/76 (1): singularPressureLoss2.C1.P - singularPressureLoss2.C2.P = singularPressureLoss2.deltaP [dynamic |0|0|0|0|] 68/77 (1): singularPressureLoss2.C2.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|] 69/78 (1): singularPressureLoss2.C2.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|] 70/79 (1): singularPressureLoss2.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|] 71/80 (1): singularPressureLoss2.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|] 72/81 (1): 0.0 = singularPressureLoss2.C1.h - singularPressureLoss2.C1.h_vol [dynamic |0|0|0|0|] 73/82 (1): singularPressureLoss2.deltaP = singularPressureLoss2.K * singularPressureLoss2.Q * abs(singularPressureLoss2.Q) / singularPressureLoss2.rho [dynamic |0|0|0|0|] 74/83 (1): singularPressureLoss2.Pm = 0.5 * (singularPressureLoss2.C1.P + singularPressureLoss2.C2.P) [dynamic |0|0|0|0|] 75/84 (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid) [dynamic |0|0|0|0|] 76/94 (1): singularPressureLoss2.h = singularPressureLoss2.pro_pT.h [dynamic |0|0|0|0|] 77/95 (1): singularPressureLoss2.rho = singularPressureLoss2.pro_pT.d [dynamic |0|0|0|0|] 78/96 (1): singularPressureLoss2.pro_ph.d = 0.0 [dynamic |0|0|0|0|] 79/97 (1): singularPressureLoss2.pro_ph.T = 0.0 [dynamic |0|0|0|0|] 80/98 (1): singularPressureLoss2.pro_ph.u = 0.0 [dynamic |0|0|0|0|] 81/99 (1): singularPressureLoss2.pro_ph.s = 0.0 [dynamic |0|0|0|0|] 82/100 (1): singularPressureLoss2.pro_ph.cp = 0.0 [dynamic |0|0|0|0|] 83/101 (1): singularPressureLoss2.pro_ph.ddhp = 0.0 [dynamic |0|0|0|0|] 84/102 (1): singularPressureLoss2.pro_ph.ddph = 0.0 [dynamic |0|0|0|0|] 85/103 (1): singularPressureLoss2.pro_ph.duph = 0.0 [dynamic |0|0|0|0|] 86/104 (1): singularPressureLoss2.pro_ph.duhp = 0.0 [dynamic |0|0|0|0|] 87/105 (1): singularPressureLoss2.pro_ph.x = 0.0 [dynamic |0|0|0|0|] 88/106 (1): singularPressureLoss3.C1.P - singularPressureLoss3.C2.P = singularPressureLoss3.deltaP [dynamic |0|0|0|0|] 89/107 (1): singularPressureLoss3.C2.Q = singularPressureLoss3.C1.Q [dynamic |0|0|0|0|] 90/108 (1): singularPressureLoss3.C2.h = singularPressureLoss3.C1.h [dynamic |0|0|0|0|] 91/109 (1): singularPressureLoss3.h = singularPressureLoss3.C1.h [dynamic |0|0|0|0|] 92/110 (1): singularPressureLoss3.Q = singularPressureLoss3.C1.Q [dynamic |0|0|0|0|] 93/111 (1): 0.0 = singularPressureLoss3.C1.h - singularPressureLoss3.C1.h_vol [dynamic |0|0|0|0|] 94/112 (1): singularPressureLoss3.deltaP = singularPressureLoss3.K * singularPressureLoss3.Q * abs(singularPressureLoss3.Q) / singularPressureLoss3.rho [dynamic |0|0|0|0|] 95/113 (1): singularPressureLoss3.Pm = 0.5 * (singularPressureLoss3.C1.P + singularPressureLoss3.C2.P) [dynamic |0|0|0|0|] 96/114 (10): singularPressureLoss3.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss3.Pm, singularPressureLoss3.T, singularPressureLoss3.mode, singularPressureLoss3.fluid) [dynamic |0|0|0|0|] 97/124 (1): singularPressureLoss3.h = singularPressureLoss3.pro_pT.h [dynamic |0|0|0|0|] 98/125 (1): singularPressureLoss3.rho = singularPressureLoss3.pro_pT.d [dynamic |0|0|0|0|] 99/126 (1): singularPressureLoss3.pro_ph.d = 0.0 [dynamic |0|0|0|0|] 100/127 (1): singularPressureLoss3.pro_ph.T = 0.0 [dynamic |0|0|0|0|] 101/128 (1): singularPressureLoss3.pro_ph.u = 0.0 [dynamic |0|0|0|0|] 102/129 (1): singularPressureLoss3.pro_ph.s = 0.0 [dynamic |0|0|0|0|] 103/130 (1): singularPressureLoss3.pro_ph.cp = 0.0 [dynamic |0|0|0|0|] 104/131 (1): singularPressureLoss3.pro_ph.ddhp = 0.0 [dynamic |0|0|0|0|] 105/132 (1): singularPressureLoss3.pro_ph.ddph = 0.0 [dynamic |0|0|0|0|] 106/133 (1): singularPressureLoss3.pro_ph.duph = 0.0 [dynamic |0|0|0|0|] 107/134 (1): singularPressureLoss3.pro_ph.duhp = 0.0 [dynamic |0|0|0|0|] 108/135 (1): singularPressureLoss3.pro_ph.x = 0.0 [dynamic |0|0|0|0|] 109/136 (1): mixer21.Ialpha1.signal = 0.5 [dynamic |0|0|0|0|] 110/137 (1): mixer21.P = mixer21.Ce1.P [dynamic |0|0|0|0|] 111/138 (1): mixer21.P = mixer21.Ce2.P [dynamic |0|0|0|0|] 112/139 (1): mixer21.P = mixer21.Cs.P [dynamic |0|0|0|0|] 113/140 (1): mixer21.Ce1.h_vol = mixer21.h [dynamic |0|0|0|0|] 114/141 (1): mixer21.Ce2.h_vol = mixer21.h [dynamic |0|0|0|0|] 115/142 (1): mixer21.Cs.h_vol = mixer21.h [dynamic |0|0|0|0|] 116/143 (1): 0.0 = mixer21.Ce1.Q + mixer21.Ce2.Q - mixer21.Cs.Q [dynamic |0|0|0|0|] 117/144 (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|] 118/145 (1): mixer21.alpha1 = mixer21.Ce1.Q / mixer21.Cs.Q [dynamic |0|0|0|0|] 119/146 (1): mixer21.Oalpha1.signal = mixer21.alpha1 [dynamic |0|0|0|0|] 120/147 (10): mixer21.pro = ThermoSysPro.Properties.Fluid.Ph(mixer21.P, mixer21.h, mixer21.mode, mixer21.fluid) [dynamic |0|0|0|0|] 121/157 (1): mixer21.T = mixer21.pro.T [dynamic |0|0|0|0|] 122/158 (1): sourceP1.C.P = sourceP1.P [dynamic |0|0|0|0|] 123/159 (1): sourceP1.C.Q = sourceP1.Q [dynamic |0|0|0|0|] 124/160 (1): sourceP1.C.h_vol = sourceP1.h [dynamic |0|0|0|0|] 125/161 (1): sourceP1.IPressure.signal = sourceP1.P0 [dynamic |0|0|0|0|] 126/162 (1): sourceP1.P = sourceP1.IPressure.signal [dynamic |0|0|0|0|] 127/163 (1): sourceP1.ITemperature.signal = sourceP1.T0 [dynamic |0|0|0|0|] 128/164 (1): sourceP1.ISpecificEnthalpy.signal = sourceP1.h0 [dynamic |0|0|0|0|] 129/165 (1): sourceP1.T = sourceP1.ITemperature.signal [dynamic |0|0|0|0|] 130/166 (1): sourceP1.h = ThermoSysPro.Properties.WaterSteam.IF97.SpecificEnthalpy_PT(sourceP1.P, sourceP1.T, 0) [dynamic |0|0|0|0|] 131/167 (10): sourceP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sourceP1.P, sourceP1.h, sourceP1.mode) [dynamic |0|0|0|0|] 132/177 (1): sourceP2.C.P = sourceP2.P [dynamic |0|0|0|0|] 133/178 (1): sourceP2.C.Q = sourceP2.Q [dynamic |0|0|0|0|] 134/179 (1): sourceP2.C.h_vol = sourceP2.h [dynamic |0|0|0|0|] 135/180 (1): sourceP2.IPressure.signal = sourceP2.P0 [dynamic |0|0|0|0|] 136/181 (1): sourceP2.P = sourceP2.IPressure.signal [dynamic |0|0|0|0|] 137/182 (1): sourceP2.ITemperature.signal = sourceP2.T0 [dynamic |0|0|0|0|] 138/183 (1): sourceP2.ISpecificEnthalpy.signal = sourceP2.h0 [dynamic |0|0|0|0|] 139/184 (1): sourceP2.T = sourceP2.ITemperature.signal [dynamic |0|0|0|0|] 140/185 (1): sourceP2.h = ThermoSysPro.Properties.WaterSteam.IF97.SpecificEnthalpy_PT(sourceP2.P, sourceP2.T, 0) [dynamic |0|0|0|0|] 141/186 (10): sourceP2.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sourceP2.P, sourceP2.h, sourceP2.mode) [dynamic |0|0|0|0|] 142/196 (1): sinkP1.C.P = sinkP1.P [dynamic |0|0|0|0|] 143/197 (1): sinkP1.C.Q = sinkP1.Q [dynamic |0|0|0|0|] 144/198 (1): sinkP1.C.h_vol = sinkP1.h [dynamic |0|0|0|0|] 145/199 (1): sinkP1.IPressure.signal = sinkP1.P0 [dynamic |0|0|0|0|] 146/200 (1): sinkP1.P = sinkP1.IPressure.signal [dynamic |0|0|0|0|] 147/201 (1): sinkP1.ITemperature.signal = sinkP1.T0 [dynamic |0|0|0|0|] 148/202 (1): sinkP1.ISpecificEnthalpy.signal = sinkP1.h0 [dynamic |0|0|0|0|] 149/203 (1): sinkP1.T = sinkP1.ITemperature.signal [dynamic |0|0|0|0|] 150/204 (1): sinkP1.h = ThermoSysPro.Properties.WaterSteam.IF97.SpecificEnthalpy_PT(sinkP1.P, sinkP1.T, 0) [dynamic |0|0|0|0|] 151/205 (10): sinkP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sinkP1.P, sinkP1.h, sinkP1.mode) [dynamic |0|0|0|0|] 152/215 (1): singularPressureLoss1.C1.a = true [binding |0|0|0|0|] 153/216 (1): singularPressureLoss1.C2.b = true [binding |0|0|0|0|] 154/217 (1): singularPressureLoss2.C1.a = true [binding |0|0|0|0|] 155/218 (1): singularPressureLoss2.C2.b = true [binding |0|0|0|0|] 156/219 (1): singularPressureLoss3.C1.a = true [binding |0|0|0|0|] 157/220 (1): singularPressureLoss3.C2.b = true [binding |0|0|0|0|] 158/221 (1): mixer21.Ce2.a = true [binding |0|0|0|0|] 159/222 (1): mixer21.Cs.b = true [binding |0|0|0|0|] 160/223 (1): mixer21.Ce1.a = true [binding |0|0|0|0|] 161/224 (1): sourceP1.C.b = true [binding |0|0|0|0|] 162/225 (1): sourceP2.C.b = true [binding |0|0|0|0|] 163/226 (1): sinkP1.C.a = true [binding |0|0|0|0|] Matching ======================================== 226 variables and equations var 1 is solved in eqn 201 var 2 is solved in eqn 43 var 3 is solved in eqn 226 var 4 is solved in eqn 44 var 5 is solved in eqn 41 var 6 is solved in eqn 198 var 7 is solved in eqn 196 var 8 is solved in eqn 202 var 9 is solved in eqn 199 var 10 is solved in eqn 214 var 11 is solved in eqn 213 var 12 is solved in eqn 212 var 13 is solved in eqn 211 var 14 is solved in eqn 210 var 15 is solved in eqn 209 var 16 is solved in eqn 208 var 17 is solved in eqn 207 var 18 is solved in eqn 206 var 19 is solved in eqn 205 var 20 is solved in eqn 204 var 21 is solved in eqn 203 var 22 is solved in eqn 197 var 23 is solved in eqn 200 var 24 is solved in eqn 182 var 25 is solved in eqn 225 var 26 is solved in eqn 30 var 27 is solved in eqn 32 var 28 is solved in eqn 29 var 29 is solved in eqn 179 var 30 is solved in eqn 177 var 31 is solved in eqn 183 var 32 is solved in eqn 180 var 33 is solved in eqn 195 var 34 is solved in eqn 194 var 35 is solved in eqn 193 var 36 is solved in eqn 192 var 37 is solved in eqn 191 var 38 is solved in eqn 190 var 39 is solved in eqn 189 var 40 is solved in eqn 188 var 41 is solved in eqn 187 var 42 is solved in eqn 186 var 43 is solved in eqn 185 var 44 is solved in eqn 184 var 45 is solved in eqn 178 var 46 is solved in eqn 181 var 47 is solved in eqn 163 var 48 is solved in eqn 224 var 49 is solved in eqn 18 var 50 is solved in eqn 20 var 51 is solved in eqn 17 var 52 is solved in eqn 160 var 53 is solved in eqn 158 var 54 is solved in eqn 164 var 55 is solved in eqn 161 var 56 is solved in eqn 176 var 57 is solved in eqn 175 var 58 is solved in eqn 174 var 59 is solved in eqn 173 var 60 is solved in eqn 172 var 61 is solved in eqn 171 var 62 is solved in eqn 170 var 63 is solved in eqn 169 var 64 is solved in eqn 168 var 65 is solved in eqn 167 var 66 is solved in eqn 166 var 67 is solved in eqn 165 var 68 is solved in eqn 159 var 69 is solved in eqn 162 var 70 is solved in eqn 156 var 71 is solved in eqn 155 var 72 is solved in eqn 154 var 73 is solved in eqn 153 var 74 is solved in eqn 152 var 75 is solved in eqn 151 var 76 is solved in eqn 150 var 77 is solved in eqn 149 var 78 is solved in eqn 148 var 79 is solved in eqn 147 var 80 is solved in eqn 146 var 81 is solved in eqn 136 var 82 is solved in eqn 25 var 83 is solved in eqn 223 var 84 is solved in eqn 26 var 85 is solved in eqn 23 var 86 is solved in eqn 140 var 87 is solved in eqn 137 var 88 is solved in eqn 222 var 89 is solved in eqn 12 var 90 is solved in eqn 14 var 91 is solved in eqn 143 var 92 is solved in eqn 15 var 93 is solved in eqn 139 var 94 is solved in eqn 37 var 95 is solved in eqn 221 var 96 is solved in eqn 38 var 97 is solved in eqn 144 var 98 is solved in eqn 141 var 99 is solved in eqn 34 var 100 is solved in eqn 157 var 101 is solved in eqn 142 var 102 is solved in eqn 138 var 103 is solved in eqn 145 var 104 is solved in eqn 116 var 105 is solved in eqn 123 var 106 is solved in eqn 122 var 107 is solved in eqn 121 var 108 is solved in eqn 120 var 109 is solved in eqn 119 var 110 is solved in eqn 118 var 111 is solved in eqn 117 var 112 is solved in eqn 124 var 113 is solved in eqn 115 var 114 is solved in eqn 135 var 115 is solved in eqn 134 var 116 is solved in eqn 133 var 117 is solved in eqn 132 var 118 is solved in eqn 131 var 119 is solved in eqn 130 var 120 is solved in eqn 129 var 121 is solved in eqn 128 var 122 is solved in eqn 126 var 123 is solved in eqn 127 var 124 is solved in eqn 220 var 125 is solved in eqn 36 var 126 is solved in eqn 108 var 127 is solved in eqn 35 var 128 is solved in eqn 39 var 129 is solved in eqn 106 var 130 is solved in eqn 31 var 131 is solved in eqn 219 var 132 is solved in eqn 111 var 133 is solved in eqn 107 var 134 is solved in eqn 33 var 135 is solved in eqn 28 var 136 is solved in eqn 109 var 137 is solved in eqn 113 var 138 is solved in eqn 114 var 139 is solved in eqn 125 var 140 is solved in eqn 110 var 141 is solved in eqn 112 var 142 is solved in eqn 86 var 143 is solved in eqn 93 var 144 is solved in eqn 92 var 145 is solved in eqn 91 var 146 is solved in eqn 90 var 147 is solved in eqn 89 var 148 is solved in eqn 88 var 149 is solved in eqn 87 var 150 is solved in eqn 94 var 151 is solved in eqn 85 var 152 is solved in eqn 105 var 153 is solved in eqn 104 var 154 is solved in eqn 103 var 155 is solved in eqn 102 var 156 is solved in eqn 101 var 157 is solved in eqn 100 var 158 is solved in eqn 99 var 159 is solved in eqn 98 var 160 is solved in eqn 96 var 161 is solved in eqn 97 var 162 is solved in eqn 218 var 163 is solved in eqn 24 var 164 is solved in eqn 78 var 165 is solved in eqn 77 var 166 is solved in eqn 27 var 167 is solved in eqn 22 var 168 is solved in eqn 19 var 169 is solved in eqn 217 var 170 is solved in eqn 81 var 171 is solved in eqn 80 var 172 is solved in eqn 21 var 173 is solved in eqn 16 var 174 is solved in eqn 79 var 175 is solved in eqn 83 var 176 is solved in eqn 84 var 177 is solved in eqn 95 var 178 is solved in eqn 82 var 179 is solved in eqn 76 var 180 is solved in eqn 55 var 181 is solved in eqn 63 var 182 is solved in eqn 62 var 183 is solved in eqn 61 var 184 is solved in eqn 60 var 185 is solved in eqn 59 var 186 is solved in eqn 58 var 187 is solved in eqn 57 var 188 is solved in eqn 56 var 189 is solved in eqn 65 var 190 is solved in eqn 75 var 191 is solved in eqn 74 var 192 is solved in eqn 73 var 193 is solved in eqn 72 var 194 is solved in eqn 71 var 195 is solved in eqn 70 var 196 is solved in eqn 69 var 197 is solved in eqn 68 var 198 is solved in eqn 66 var 199 is solved in eqn 67 var 200 is solved in eqn 216 var 201 is solved in eqn 42 var 202 is solved in eqn 48 var 203 is solved in eqn 47 var 204 is solved in eqn 45 var 205 is solved in eqn 40 var 206 is solved in eqn 13 var 207 is solved in eqn 215 var 208 is solved in eqn 49 var 209 is solved in eqn 11 var 210 is solved in eqn 51 var 211 is solved in eqn 10 var 212 is solved in eqn 64 var 213 is solved in eqn 53 var 214 is solved in eqn 54 var 215 is solved in eqn 52 var 216 is solved in eqn 50 var 217 is solved in eqn 46 var 218 is solved in eqn 1 var 219 is solved in eqn 2 var 220 is solved in eqn 3 var 221 is solved in eqn 4 var 222 is solved in eqn 5 var 223 is solved in eqn 6 var 224 is solved in eqn 7 var 225 is solved in eqn 8 var 226 is solved in eqn 9 Standard BLT of the original model:(226) ============================================================ 226: sinkP1.h0: (9/9): (1): sinkP1.h0 = 1e5 225: sinkP1.T0: (8/8): (1): sinkP1.T0 = 290.0 224: sinkP1.P0: (7/7): (1): sinkP1.P0 = 1e5 223: sourceP2.h0: (6/6): (1): sourceP2.h0 = 1e5 222: sourceP2.T0: (5/5): (1): sourceP2.T0 = 290.0 221: sourceP2.P0: (4/4): (1): sourceP2.P0 = 3e5 220: sourceP1.h0: (3 ...[truncated 172592 chars]... enthalpy" type: Real 13: sinkP1.pro.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 14: sinkP1.pro.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -15: 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 -16: sinkP1.pro.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -17: sinkP1.pro.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -18: sinkP1.pro.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +15: sinkP1.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real +16: sinkP1.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +17: sinkP1.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +18: sinkP1.pro.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 19: sinkP1.pro.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 20: sinkP1.h:VARIABLE(unit = "J/kg" ) "Fluid enthalpy" type: Real 21: sinkP1.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 22: sinkP1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real -23: sinkP1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure" type: Real +23: sinkP1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 24: sourceP2.ITemperature.signal:VARIABLE(flow=false ) type: Real 25: sourceP2.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 26: sourceP2.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -27: sourceP2.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 +27: sourceP2.C.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 28: sourceP2.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 -29: sourceP2.C.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -30: sourceP2.C.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +29: sourceP2.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +30: sourceP2.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 31: sourceP2.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 32: sourceP2.IPressure.signal:VARIABLE(flow=false ) type: Real 33: sourceP2.pro.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 34: sourceP2.pro.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 35: sourceP2.pro.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 36: sourceP2.pro.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 37: sourceP2.pro.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -38: sourceP2.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 -39: sourceP2.pro.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -40: sourceP2.pro.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -41: sourceP2.pro.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +38: sourceP2.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real +39: sourceP2.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +40: sourceP2.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +41: sourceP2.pro.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 42: sourceP2.pro.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 43: sourceP2.h:VARIABLE(unit = "J/kg" ) "Fluid enthalpy" type: Real 44: sourceP2.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 45: sourceP2.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real -46: sourceP2.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure" type: Real +46: sourceP2.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 47: sourceP1.ITemperature.signal:VARIABLE(flow=false ) type: Real 48: sourceP1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 49: sourceP1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -50: sourceP1.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 +50: sourceP1.C.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 51: sourceP1.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 -52: sourceP1.C.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -53: sourceP1.C.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +52: sourceP1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +53: sourceP1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 54: sourceP1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 55: sourceP1.IPressure.signal:VARIABLE(flow=false ) type: Real 56: sourceP1.pro.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 57: sourceP1.pro.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 58: sourceP1.pro.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 59: sourceP1.pro.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 60: sourceP1.pro.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -61: sourceP1.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 -62: sourceP1.pro.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -63: sourceP1.pro.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -64: sourceP1.pro.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +61: sourceP1.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real +62: sourceP1.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +63: sourceP1.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +64: sourceP1.pro.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 65: sourceP1.pro.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 66: sourceP1.h:VARIABLE(unit = "J/kg" ) "Fluid enthalpy" type: Real 67: sourceP1.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 68: sourceP1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real -69: sourceP1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure" type: Real +69: sourceP1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 70: mixer21.pro.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 71: mixer21.pro.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 72: mixer21.pro.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 73: mixer21.pro.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 74: mixer21.pro.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -75: 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 -76: mixer21.pro.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -77: mixer21.pro.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -78: mixer21.pro.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +75: mixer21.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real +76: mixer21.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +77: mixer21.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +78: mixer21.pro.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 79: mixer21.pro.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 80: mixer21.Oalpha1.signal:VARIABLE(flow=false ) type: Real 81: mixer21.Ialpha1.signal:VARIABLE(flow=false ) type: Real 82: mixer21.Ce1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 83: mixer21.Ce1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -84: 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 +84: 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 85: 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 -86: mixer21.Ce1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -87: 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 +86: mixer21.Ce1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +87: mixer21.Ce1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 88: mixer21.Cs.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 89: mixer21.Cs.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -90: 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 +90: 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 91: 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 -92: mixer21.Cs.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -93: 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 +92: mixer21.Cs.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +93: mixer21.Cs.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 94: mixer21.Ce2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 95: mixer21.Ce2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -96: 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 +96: 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 97: 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 -98: mixer21.Ce2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -99: 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 +98: mixer21.Ce2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +99: mixer21.Ce2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 100: mixer21.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real -101: mixer21.h:VARIABLE(start = 1000000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real -102: mixer21.P:VARIABLE(min = 0.0 start = 1000000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure" type: Real +101: mixer21.h:VARIABLE(start = 1e6 unit = "J/kg" ) "Fluid specific enthalpy" type: Real +102: mixer21.P:VARIABLE(min = 0.0 start = 1e6 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 103: mixer21.alpha1:VARIABLE() "Extraction coefficient for inlet 1 (<=1)" type: Real 104: singularPressureLoss3.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 105: singularPressureLoss3.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 106: singularPressureLoss3.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 107: singularPressureLoss3.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 108: singularPressureLoss3.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real -109: 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 -110: singularPressureLoss3.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -111: singularPressureLoss3.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -112: singularPressureLoss3.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real -113: singularPressureLoss3.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +109: 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 +110: singularPressureLoss3.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +111: singularPressureLoss3.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +112: singularPressureLoss3.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real +113: singularPressureLoss3.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 114: singularPressureLoss3.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 115: singularPressureLoss3.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 116: singularPressureLoss3.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 117: singularPressureLoss3.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 118: singularPressureLoss3.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -119: 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 -120: singularPressureLoss3.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -121: singularPressureLoss3.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -122: singularPressureLoss3.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +119: 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 +120: singularPressureLoss3.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +121: singularPressureLoss3.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +122: singularPressureLoss3.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 123: singularPressureLoss3.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 124: singularPressureLoss3.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 125: singularPressureLoss3.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -126: 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 +126: 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 127: 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 -128: singularPressureLoss3.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -129: 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 +128: singularPressureLoss3.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +129: singularPressureLoss3.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 130: singularPressureLoss3.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 131: singularPressureLoss3.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -132: 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 +132: 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 133: 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 -134: singularPressureLoss3.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -135: 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 -136: singularPressureLoss3.h:VARIABLE(start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real -137: singularPressureLoss3.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real +134: singularPressureLoss3.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +135: singularPressureLoss3.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real +136: singularPressureLoss3.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real +137: singularPressureLoss3.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 138: singularPressureLoss3.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 139: singularPressureLoss3.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 140: singularPressureLoss3.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real -141: singularPressureLoss3.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real +141: singularPressureLoss3.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 142: singularPressureLoss2.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 143: singularPressureLoss2.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 144: singularPressureLoss2.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 145: singularPressureLoss2.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 146: singularPressureLoss2.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real -147: 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 -148: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -149: singularPressureLoss2.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -150: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real -151: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +147: 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 +148: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +149: singularPressureLoss2.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +150: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real +151: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 152: singularPressureLoss2.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 153: singularPressureLoss2.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 154: singularPressureLoss2.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 155: singularPressureLoss2.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 156: singularPressureLoss2.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -157: 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 -158: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -159: singularPressureLoss2.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -160: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +157: 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 +158: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +159: singularPressureLoss2.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +160: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 161: singularPressureLoss2.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 162: singularPressureLoss2.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 163: singularPressureLoss2.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -164: 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 +164: 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 165: 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 -166: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -167: 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 +166: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +167: singularPressureLoss2.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 168: singularPressureLoss2.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 169: singularPressureLoss2.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -170: 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 +170: 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 171: 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 -172: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -173: 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 -174: singularPressureLoss2.h:VARIABLE(start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real -175: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real +172: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +173: singularPressureLoss2.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real +174: singularPressureLoss2.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real +175: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 176: singularPressureLoss2.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 177: singularPressureLoss2.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 178: singularPressureLoss2.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real -179: singularPressureLoss2.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real +179: singularPressureLoss2.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 180: singularPressureLoss1.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 181: singularPressureLoss1.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 182: singularPressureLoss1.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 183: singularPressureLoss1.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 184: singularPressureLoss1.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real -185: 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 -186: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -187: singularPressureLoss1.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -188: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real -189: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +185: 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 +186: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +187: singularPressureLoss1.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +188: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real +189: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 190: singularPressureLoss1.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 191: singularPressureLoss1.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 192: singularPressureLoss1.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 193: singularPressureLoss1.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 194: singularPressureLoss1.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -195: 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 -196: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -197: singularPressureLoss1.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -198: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +195: 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 +196: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +197: singularPressureLoss1.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +198: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 199: singularPressureLoss1.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 200: singularPressureLoss1.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 201: singularPressureLoss1.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -202: 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 +202: 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 203: 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 -204: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -205: 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 +204: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +205: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 206: singularPressureLoss1.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 207: singularPressureLoss1.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -208: 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 +208: 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 209: 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 -210: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -211: 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 -212: singularPressureLoss1.h:VARIABLE(start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real -213: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real +210: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +211: singularPressureLoss1.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real +212: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real +213: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 214: singularPressureLoss1.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 215: singularPressureLoss1.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 216: singularPressureLoss1.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real -217: singularPressureLoss1.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real -218: sourceP1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Source pressure" type: Real +217: singularPressureLoss1.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real +218: sourceP1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Source pressure" type: Real 219: sourceP1.T0:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Source temperature (active if option_temperature=1)" type: Real 220: sourceP1.h0:VARIABLE(unit = "J/kg" ) "Source specific enthalpy (active if option_temperature=2)" type: Real -221: sourceP2.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Source pressure" type: Real +221: sourceP2.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Source pressure" type: Real 222: sourceP2.T0:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Source temperature (active if option_temperature=1)" type: Real 223: sourceP2.h0:VARIABLE(unit = "J/kg" ) "Source specific enthalpy (active if option_temperature=2)" type: Real -224: sinkP1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Sink pressure" type: Real +224: sinkP1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Sink pressure" type: Real 225: sinkP1.T0:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Sink temperature (active if option_temperature=1)" type: Real 226: sinkP1.h0:VARIABLE(unit = "J/kg" ) "Sink specific enthalpy (active if option_temperature=2)" type: Real OrderedEquation (163, 226) ======================================== 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): sourceP1.P0 = 300000.0 [binding |0|0|0|0|] +3/3 (1): sourceP1.P0 = 3e5 [binding |0|0|0|0|] 4/4 (1): sourceP1.T0 = 290.0 [binding |0|0|0|0|] -5/5 (1): sourceP1.h0 = 100000.0 [binding |0|0|0|0|] -6/6 (1): sourceP2.P0 = 300000.0 [binding |0|0|0|0|] +5/5 (1): sourceP1.h0 = 1e5 [binding |0|0|0|0|] +6/6 (1): sourceP2.P0 = 3e5 [binding |0|0|0|0|] 7/7 (1): sourceP2.T0 = 290.0 [binding |0|0|0|0|] -8/8 (1): sourceP2.h0 = 100000.0 [binding |0|0|0|0|] -9/9 (1): sinkP1.P0 = 100000.0 [binding |0|0|0|0|] +8/8 (1): sourceP2.h0 = 1e5 [binding |0|0|0|0|] +9/9 (1): sinkP1.P0 = 1e5 [binding |0|0|0|0|] 10/10 (1): sinkP1.T0 = 290.0 [binding |0|0|0|0|] -11/11 (1): sinkP1.h0 = 100000.0 [binding |0|0|0|0|] +11/11 (1): sinkP1.h0 = 1e5 [binding |0|0|0|0|] 12/12 (1): mixer21.Cs.P = singularPressureLoss1.C1.P [dynamic |0|0|0|0|] 13/13 (1): mixer21.Cs.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|] 14/14 (1): mixer21.Cs.a = singularPressureLoss1.C1.a [dynamic |0|0|0|0|] 15/15 (1): mixer21.Cs.b = singularPressureLoss1.C1.b [dynamic |0|0|0|0|] 16/16 (1): mixer21.Cs.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|] @@ -1602,19 +1602,19 @@ var 226 is solved in eqn 11 Standard BLT of the original model:(226) ============================================================ -226: sinkP1.h0: (11/11): (1): sinkP1.h0 = 100000.0 +226: sinkP1.h0: (11/11): (1): sinkP1.h0 = 1e5 225: sinkP1.T0: (10/10): (1): sinkP1.T0 = 290.0 -224: sinkP1.P0: (9/9): (1): sinkP1.P0 = 100000.0 -223: sourceP2.h0: (8/8): (1): sourceP2.h0 = 100000.0 +224: sinkP1.P0: (9/9): (1): sinkP1.P0 = 1e5 +223: sourceP2.h0: (8/8): (1): sourceP2.h0 = 1e5 222: sourceP2.T0: (7/7): (1): sourceP2.T0 = 290.0 -221: sourceP2.P0: (6/6): (1): sourceP2.P0 = 300000.0 -220: sourceP1.h0: (5/5): (1): sourceP1.h0 = 100000.0 +221: sourceP2.P0: (6/6): (1): sourceP2.P0 = 3e5 +220: sourceP1.h0: (5/5): (1): sourceP1.h0 = 1e5 219: sourceP1.T0: (4/4): (1): sourceP1.T0 = 290.0 -218: sourceP1.P0: (3/3): (1): sourceP1.P0 = 300000.0 +218: sourceP1.P0: (3/3): (1): sourceP1.P0 = 3e5 217: singularPressureLoss1.deltaP: (48/48): (1): singularPressureLoss1.C1.P - singularPressureLoss1.C2.P = singularPressureLoss1.deltaP 216: singularPressureLoss1.Q: (52/52): (1): singularPressureLoss1.Q = singularPressureLoss1.C1.Q 215: singularPressureLoss1.rho: (54/54): (1): singularPressureLoss1.deltaP = singularPressureLoss1.K * singularPressureLoss1.Q * abs(singularPressureLoss1.Q) / singularPressureLoss1.rho 214: singularPressureLoss1.T: (56/56): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 213: singularPressureLoss1.Pm: (55/55): (1): singularPressureLoss1.Pm = 0.5 * (singularPressureLoss1.C1.P + singularPressureLoss1.C2.P) @@ -1839,17 +1839,17 @@ 3: singularPressureLoss1.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real Boundary conditions (9) ======================================== -1: sourceP1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Source pressure" type: Real +1: sourceP1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Source pressure" type: Real 2: sourceP1.T0:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Source temperature (active if option_temperature=1)" type: Real 3: sourceP1.h0:VARIABLE(unit = "J/kg" ) "Source specific enthalpy (active if option_temperature=2)" type: Real -4: sourceP2.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Source pressure" type: Real +4: sourceP2.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Source pressure" type: Real 5: sourceP2.T0:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Source temperature (active if option_temperature=1)" type: Real 6: sourceP2.h0:VARIABLE(unit = "J/kg" ) "Source specific enthalpy (active if option_temperature=2)" type: Real -7: sinkP1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Sink pressure" type: Real +7: sinkP1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Sink pressure" type: Real 8: sinkP1.T0:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Sink temperature (active if option_temperature=1)" type: Real 9: sinkP1.h0:VARIABLE(unit = "J/kg" ) "Sink specific enthalpy (active if option_temperature=2)" type: Real Binding equations:(23) @@ -1865,19 +1865,19 @@ 131: singularPressureLoss3.C1.a: (156/219): (1): singularPressureLoss3.C1.a = true 162: singularPressureLoss2.C2.b: (155/218): (1): singularPressureLoss2.C2.b = true 169: singularPressureLoss2.C1.a: (154/217): (1): singularPressureLoss2.C1.a = true 200: singularPressureLoss1.C2.b: (153/216): (1): singularPressureLoss1.C2.b = true 207: singularPressureLoss1.C1.a: (152/215): (1): singularPressureLoss1.C1.a = true -226: sinkP1.h0: (11/11): (1): sinkP1.h0 = 100000.0 +226: sinkP1.h0: (11/11): (1): sinkP1.h0 = 1e5 225: sinkP1.T0: (10/10): (1): sinkP1.T0 = 290.0 -224: sinkP1.P0: (9/9): (1): sinkP1.P0 = 100000.0 -223: sourceP2.h0: (8/8): (1): sourceP2.h0 = 100000.0 +224: sinkP1.P0: (9/9): (1): sinkP1.P0 = 1e5 +223: sourceP2.h0: (8/8): (1): sourceP2.h0 = 1e5 222: sourceP2.T0: (7/7): (1): sourceP2.T0 = 290.0 -221: sourceP2.P0: (6/6): (1): sourceP2.P0 = 300000.0 -220: sourceP1.h0: (5/5): (1): sourceP1.h0 = 100000.0 +221: sourceP2.P0: (6/6): (1): sourceP2.P0 = 3e5 +220: sourceP1.h0: (5/5): (1): sourceP1.h0 = 1e5 219: sourceP1.T0: (4/4): (1): sourceP1.T0 = 290.0 -218: sourceP1.P0: (3/3): (1): sourceP1.P0 = 300000.0 +218: sourceP1.P0: (3/3): (1): sourceP1.P0 = 3e5 178: singularPressureLoss2.Q: (2/2): (1): singularPressureLoss2.Q = 0.0 140: singularPressureLoss3.Q: (1/1): (1): singularPressureLoss3.Q = 0.0 E-BLT: equations that compute the variables of interest:(1) @@ -1993,17 +1993,18 @@ ========================================================================== -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_Splitter1', options = '', outputFormat = 'mat', variableFilter = '.*', cflags = '', simflags = '-reconcile -sx=./NewDataReconciliationSimpleTests/resources/DataReconciliationSimpleTests.TSP_Splitter1_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_Splitter1', options = '', outputFormat = 'mat', variableFilter = '.*', cflags = '', simflags = '-reconcile -sx=./NewDataReconciliationSimpleTests/resources/DataReconciliationSimpleTests.TSP_Splitter1_Inputs.csv -eps=0.0023 -lv=LOG_JAC'", +messages = "Simulation execution failed for model: NewDataReconciliationSimpleTests.TSP_Splitter1 +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_Splitter1 -LOG_STDOUT | info | DataReconciliation Completed! +LOG_STDOUT | error | Measurement input file path not found ./NewDataReconciliationSimpleTests/resources/DataReconciliationSimpleTests.TSP_Splitter1_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 1998: Text differs: expected: resultFile = "econcile", got: resultFile = "", == 1 out of 1 tests failed [openmodelica/dataReconciliation/TSP_Splitter1.mos_temp2479, time: 27]