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Failed
openmodelica_dataReconciliation.TSP_FourFlows3.mos (from (result.xml))
Stacktrace
Output mismatch (see stdout for details)
Standard Output
+ TSP_FourFlows3 ... equation mismatch [time: 24] ==== Log C:\Windows\TEMP/omc-rtest-OpenModelica/openmodelica/dataReconciliation/TSP_FourFlows3.mos_temp8704/log-TSP_FourFlows3.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_FourFlows3 ========================================================================== OrderedVariables (284) ======================================== 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: sourceP1.ITemperature.signal:VARIABLE(flow=false ) type: Real 25: sourceP1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 26: sourceP1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 27: 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 28: 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 29: sourceP1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 30: sourceP1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 31: sourceP1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 32: sourceP1.IPressure.signal:VARIABLE(flow=false ) type: Real 33: sourceP1.pro.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 34: sourceP1.pro.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 35: sourceP1.pro.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 36: sourceP1.pro.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 37: sourceP1.pro.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 38: sourceP1.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 39: sourceP1.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 40: sourceP1.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 41: sourceP1.pro.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 42: sourceP1.pro.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 43: sourceP1.h:VARIABLE(unit = "J/kg" ) "Fluid enthalpy" type: Real 44: sourceP1.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 45: sourceP1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real 46: sourceP1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 47: volumeB2.Cs2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 48: volumeB2.Cs2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 49: volumeB2.Cs2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 50: volumeB2.Cs2.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real 51: volumeB2.Cs2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 52: volumeB2.Cs2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 53: volumeB2.Cs1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 54: volumeB2.Cs1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 55: volumeB2.Cs1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 56: volumeB2.Cs1.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real 57: volumeB2.Cs1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 58: volumeB2.Cs1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 59: volumeB2.Ce2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 60: volumeB2.Ce2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 61: volumeB2.Ce2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 62: volumeB2.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 63: volumeB2.Ce2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 64: volumeB2.Ce2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 65: volumeB2.Ce1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 66: volumeB2.Ce1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 67: volumeB2.Ce1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 68: volumeB2.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 69: volumeB2.Ce1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 70: volumeB2.Ce1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 71: volumeB2.pro.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 72: volumeB2.pro.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 73: volumeB2.pro.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 74: volumeB2.pro.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 75: volumeB2.pro.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 76: volumeB2.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 77: volumeB2.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 78: volumeB2.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 79: volumeB2.pro.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 80: volumeB2.pro.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 81: volumeB2.BH:VARIABLE(unit = "W" ) "Right hand side of the energybalance equation" type: Real 82: volumeB2.BQ:VARIABLE(unit = "kg/s" ) "Right hand side of the mass balance equation" type: Real 83: volumeB2.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 84: volumeB2.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 85: volumeB2.P:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 86: volumeB2.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 87: volumeB1.Cs2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 88: volumeB1.Cs2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 89: volumeB1.Cs2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 90: volumeB1.Cs2.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real 91: volumeB1.Cs2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 92: volumeB1.Cs2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 93: volumeB1.Cs1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 94: volumeB1.Cs1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 95: volumeB1.Cs1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 96: volumeB1.Cs1.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real 97: volumeB1.Cs1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 98: volumeB1.Cs1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 99: volumeB1.Ce2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 100: volumeB1.Ce2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 101: volumeB1.Ce2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 102: volumeB1.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 103: volumeB1.Ce2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 104: volumeB1.Ce2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 105: volumeB1.Ce1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 106: volumeB1.Ce1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 107: volumeB1.Ce1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 108: volumeB1.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 109: volumeB1.Ce1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 110: volumeB1.Ce1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 111: volumeB1.pro.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 112: volumeB1.pro.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 113: volumeB1.pro.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 114: volumeB1.pro.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 115: volumeB1.pro.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 116: volumeB1.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 117: volumeB1.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 118: volumeB1.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 119: volumeB1.pro.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 120: volumeB1.pro.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 121: volumeB1.BH:VARIABLE(unit = "W" ) "Right hand side of the energybalance equation" type: Real 122: volumeB1.BQ:VARIABLE(unit = "kg/s" ) "Right hand side of the mass balance equation" type: Real 123: volumeB1.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 124: volumeB1.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 125: volumeB1.P:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 126: volumeB1.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 127: singularPressureLoss4.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 128: singularPressureLoss4.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 129: singularPressureLoss4.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 130: singularPressureLoss4.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 131: singularPressureLoss4.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real 132: singularPressureLoss4.pro_pT.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 133: singularPressureLoss4.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 134: singularPressureLoss4.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 135: singularPressureLoss4.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real 136: singularPressureLoss4.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 137: singularPressureLoss4.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 138: singularPressureLoss4.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 139: singularPressureLoss4.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 140: singularPressureLoss4.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 141: singularPressureLoss4.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 142: singularPressureLoss4.pro_ph.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 143: singularPressureLoss4.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 144: singularPressureLoss4.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 145: singularPressureLoss4.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 146: singularPressureLoss4.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 147: singularPressureLoss4.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 148: singularPressureLoss4.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 149: singularPressureLoss4.C2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 150: singularPressureLoss4.C2.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real 151: singularPressureLoss4.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 152: singularPressureLoss4.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 153: singularPressureLoss4.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 154: singularPressureLoss4.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 155: singularPressureLoss4.C1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 156: singularPressureLoss4.C1.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real 157: singularPressureLoss4.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 158: singularPressureLoss4.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 159: singularPressureLoss4.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 160: singularPressureLoss4.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 161: singularPressureLoss4.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 162: singularPressureLoss4.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 163: singularPressureLoss4.Q:VARIABLE(start = 99.5 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real 164: singularPressureLoss4.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 165: singularPressureLoss3.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 166: singularPressureLoss3.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 167: singularPressureLoss3.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 168: singularPressureLoss3.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 169: singularPressureLoss3.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real 170: 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 171: singularPressureLoss3.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 172: singularPressureLoss3.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 173: singularPressureLoss3.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real 174: singularPressureLoss3.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 175: singularPressureLoss3.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 176: singularPressureLoss3.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 177: singularPressureLoss3.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 178: singularPressureLoss3.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 179: singularPressureLoss3.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 180: 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 181: singularPressureLoss3.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 182: singularPressureLoss3.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 183: singularPressureLoss3.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 184: singularPressureLoss3.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 185: singularPressureLoss3.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 186: singularPressureLoss3.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 187: 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 188: 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 189: singularPressureLoss3.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 190: singularPressureLoss3.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 191: singularPressureLoss3.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 192: singularPressureLoss3.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 193: 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 194: 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 195: singularPressureLoss3.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 196: singularPressureLoss3.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 197: singularPressureLoss3.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 198: singularPressureLoss3.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 199: singularPressureLoss3.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 200: singularPressureLoss3.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 201: singularPressureLoss3.Q:VARIABLE(start = 49.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real 202: singularPressureLoss3.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 203: singularPressureLoss2.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 204: singularPressureLoss2.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 205: singularPressureLoss2.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 206: singularPressureLoss2.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 207: singularPressureLoss2.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real 208: 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 209: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 210: singularPressureLoss2.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 211: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real 212: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 213: singularPressureLoss2.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 214: singularPressureLoss2.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 215: singularPressureLoss2.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 216: singularPressureLoss2.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 217: singularPressureLoss2.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 218: 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 219: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 220: singularPressureLoss2.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 221: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 222: singularPressureLoss2.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 223: singularPressureLoss2.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 224: singularPressureLoss2.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 225: 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 226: 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 227: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 228: singularPressureLoss2.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 229: singularPressureLoss2.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 230: singularPressureLoss2.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 231: 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 232: 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 233: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 234: singularPressureLoss2.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 235: singularPressureLoss2.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 236: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 237: singularPressureLoss2.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 238: singularPressureLoss2.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 239: singularPressureLoss2.Q:VARIABLE(start = 50.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real 240: singularPressureLoss2.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 241: singularPressureLoss1.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 242: singularPressureLoss1.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 243: singularPressureLoss1.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 244: singularPressureLoss1.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 245: singularPressureLoss1.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real 246: 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 247: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 248: singularPressureLoss1.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 249: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real 250: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 251: singularPressureLoss1.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 252: singularPressureLoss1.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 253: singularPressureLoss1.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 254: singularPressureLoss1.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 255: singularPressureLoss1.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 256: 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 257: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 258: singularPressureLoss1.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 259: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 260: singularPressureLoss1.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 261: singularPressureLoss1.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 262: singularPressureLoss1.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 263: 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 264: 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 265: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 266: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 267: singularPressureLoss1.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 268: singularPressureLoss1.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 269: 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 270: 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 271: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 272: singularPressureLoss1.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 273: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 274: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 275: singularPressureLoss1.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 276: singularPressureLoss1.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 277: singularPressureLoss1.Q:VARIABLE(start = 100.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real 278: singularPressureLoss1.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 279: sourceP1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Source pressure" type: Real 280: sourceP1.T0:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Source temperature (active if option_temperature=1)" type: Real 281: sourceP1.h0:VARIABLE(unit = "J/kg" ) "Source specific enthalpy (active if option_temperature=2)" type: Real 282: sinkP1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Sink pressure" type: Real 283: sinkP1.T0:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Sink temperature (active if option_temperature=1)" type: Real 284: sinkP1.h0:VARIABLE(unit = "J/kg" ) "Sink specific enthalpy (active if option_temperature=2)" type: Real OrderedEquation (212, 284) ======================================== 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): sinkP1.P0 = 1e5 [binding |0|0|0|0|] 5/5 (1): sinkP1.T0 = 290.0 [binding |0|0|0|0|] 6/6 (1): sinkP1.h0 = 1e5 [binding |0|0|0|0|] 7/7 (1): volumeB1.Cs1.P = singularPressureLoss2.C1.P [dynamic |0|0|0|0|] 8/8 (1): volumeB1.Cs1.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|] 9/9 (1): volumeB1.Cs1.a = singularPressureLoss2.C1.a [dynamic |0|0|0|0|] 10/10 (1): volumeB1.Cs1.b = singularPressureLoss2.C1.b [dynamic |0|0|0|0|] 11/11 (1): volumeB1.Cs1.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|] 12/12 (1): volumeB1.Cs1.h_vol = singularPressureLoss2.C1.h_vol [dynamic |0|0|0|0|] 13/13 (1): singularPressureLoss2.C2.P = volumeB2.Ce1.P [dynamic |0|0|0|0|] 14/14 (1): singularPressureLoss2.C2.Q = volumeB2.Ce1.Q [dynamic |0|0|0|0|] 15/15 (1): singularPressureLoss2.C2.a = volumeB2.Ce1.a [dynamic |0|0|0|0|] 16/16 (1): singularPressureLoss2.C2.b = volumeB2.Ce1.b [dynamic |0|0|0|0|] 17/17 (1): singularPressureLoss2.C2.h = volumeB2.Ce1.h [dynamic |0|0|0|0|] 18/18 (1): singularPressureLoss2.C2.h_vol = volumeB2.Ce1.h_vol [dynamic |0|0|0|0|] 19/19 (1): volumeB1.Cs2.P = singularPressureLoss3.C1.P [dynamic |0|0|0|0|] 20/20 (1): volumeB1.Cs2.Q = singularPressureLoss3.C1.Q [dynamic |0|0|0|0|] 21/21 (1): volumeB1.Cs2.a = singularPressureLoss3.C1.a [dynamic |0|0|0|0|] 22/22 (1): volumeB1.Cs2.b = singularPressureLoss3.C1.b [dynamic |0|0|0|0|] 23/23 (1): volumeB1.Cs2.h = singularPressureLoss3.C1.h [dynamic |0|0|0|0|] 24/24 (1): volumeB1.Cs2.h_vol = singularPressureLoss3.C1.h_vol [dynamic |0|0|0|0|] 25/25 (1): singularPressureLoss3.C2.P = volumeB2.Ce2.P [dynamic |0|0|0|0|] 26/26 (1): singularPressureLoss3.C2.Q = volumeB2.Ce2.Q [dynamic |0|0|0|0|] 27/27 (1): singularPressureLoss3.C2.a = volumeB2.Ce2.a [dynamic |0|0|0|0|] 28/28 (1): singularPressureLoss3.C2.b = volumeB2.Ce2.b [dynamic |0|0|0|0|] 29/29 (1): singularPressureLoss3.C2.h = volumeB2.Ce2.h [dynamic |0|0|0|0|] 30/30 (1): singularPressureLoss3.C2.h_vol = volumeB2.Ce2.h_vol [dynamic |0|0|0|0|] 31/31 (1): volumeB2.Cs1.P = singularPressureLoss4.C1.P [dynamic |0|0|0|0|] 32/32 (1): volumeB2.Cs1.Q = singularPressureLoss4.C1.Q [dynamic |0|0|0|0|] 33/33 (1): volumeB2.Cs1.a = singularPressureLoss4.C1.a [dynamic |0|0|0|0|] 34/34 (1): volumeB2.Cs1.b = singularPressureLoss4.C1.b [dynamic |0|0|0|0|] 35/35 (1): volumeB2.Cs1.h = singularPressureLoss4.C1.h [dynamic |0|0|0|0|] 36/36 (1): volumeB2.Cs1.h_vol = singularPressureLoss4.C1.h_vol [dynamic |0|0|0|0|] 37/37 (1): singularPressureLoss1.C2.P = volumeB1.Ce1.P [dynamic |0|0|0|0|] 38/38 (1): singularPressureLoss1.C2.Q = volumeB1.Ce1.Q [dynamic |0|0|0|0|] 39/39 (1): singularPressureLoss1.C2.a = volumeB1.Ce1.a [dynamic |0|0|0|0|] 40/40 (1): singularPressureLoss1.C2.b = volumeB1.Ce1.b [dynamic |0|0|0|0|] 41/41 (1): singularPressureLoss1.C2.h = volumeB1.Ce1.h [dynamic |0|0|0|0|] 42/42 (1): singularPressureLoss1.C2.h_vol = volumeB1.Ce1.h_vol [dynamic |0|0|0|0|] 43/43 (1): sourceP1.C.P = singularPressureLoss1.C1.P [dynamic |0|0|0|0|] 44/44 (1): sourceP1.C.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|] 45/45 (1): sourceP1.C.a = singularPressureLoss1.C1.a [dynamic |0|0|0|0|] 46/46 (1): sourceP1.C.b = singularPressureLoss1.C1.b [dynamic |0|0|0|0|] 47/47 (1): sourceP1.C.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|] 48/48 (1): sourceP1.C.h_vol = singularPressureLoss1.C1.h_vol [dynamic |0|0|0|0|] 49/49 (1): singularPressureLoss4.C2.P = sinkP1.C.P [dynamic |0|0|0|0|] 50/50 (1): singularPressureLoss4.C2.Q = sinkP1.C.Q [dynamic |0|0|0|0|] 51/51 (1): singularPressureLoss4.C2.a = sinkP1.C.a [dynamic |0|0|0|0|] 52/52 (1): singularPressureLoss4.C2.b = sinkP1.C.b [dynamic |0|0|0|0|] 53/53 (1): singularPressureLoss4.C2.h = sinkP1.C.h [dynamic |0|0|0|0|] 54/54 (1): singularPressureLoss4.C2.h_vol = sinkP1.C.h_vol [dynamic |0|0|0|0|] 55/55 (1): singularPressureLoss1.C1.P - singularPressureLoss1.C2.P = singularPressureLoss1.deltaP [dynamic |0|0|0|0|] 56/56 (1): singularPressureLoss1.C2.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|] 57/57 (1): singularPressureLoss1.C2.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|] 58/58 (1): singularPressureLoss1.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|] 59/59 (1): singularPressureLoss1.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|] 60/60 (1): 0.0 = singularPressureLoss1.C1.h - singularPressureLoss1.C1.h_vol [dynamic |0|0|0|0|] 61/61 (1): singularPressureLoss1.deltaP = singularPressureLoss1.K * singularPressureLoss1.Q * abs(singularPressureLoss1.Q) / singularPressureLoss1.rho [dynamic |0|0|0|0|] 62/62 (1): singularPressureLoss1.Pm = 0.5 * (singularPressureLoss1.C1.P + singularPressureLoss1.C2.P) [dynamic |0|0|0|0|] 63/63 (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) [dynamic |0|0|0|0|] 64/73 (1): singularPressureLoss1.h = singularPressureLoss1.pro_pT.h [dynamic |0|0|0|0|] 65/74 (1): singularPressureLoss1.rho = singularPressureLoss1.pro_pT.d [dynamic |0|0|0|0|] 66/75 (1): singularPressureLoss1.pro_ph.d = 0.0 [dynamic |0|0|0|0|] 67/76 (1): singularPressureLoss1.pro_ph.T = 0.0 [dynamic |0|0|0|0|] 68/77 (1): singularPressureLoss1.pro_ph.u = 0.0 [dynamic |0|0|0|0|] 69/78 (1): singularPressureLoss1.pro_ph.s = 0.0 [dynamic |0|0|0|0|] 70/79 (1): singularPressureLoss1.pro_ph.cp = 0.0 [dynamic |0|0|0|0|] 71/80 (1): singularPressureLoss1.pro_ph.ddhp = 0.0 [dynamic |0|0|0|0|] 72/81 (1): singularPressureLoss1.pro_ph.ddph = 0.0 [dynamic |0|0|0|0|] 73/82 (1): singularPressureLoss1.pro_ph.duph = 0.0 [dynamic |0|0|0|0|] 74/83 (1): singularPressureLoss1.pro_ph.duhp = 0.0 [dynamic |0|0|0|0|] 75/84 (1): singularPressureLoss1.pro_ph.x = 0.0 [dynamic |0|0|0|0|] 76/85 (1): singularPressureLoss2.C1.P - singularPressureLoss2.C2.P = singularPressureLoss2.deltaP [dynamic |0|0|0|0|] 77/86 (1): singularPressureLoss2.C2.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|] 78/87 (1): singularPressureLoss2.C2.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|] 79/88 (1): singularPressureLoss2.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|] 80/89 (1): singularPressureLoss2.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|] 81/90 (1): 0.0 = singularPressureLoss2.C1.h - singularPressureLoss2.C1.h_vol [dynamic |0|0|0|0|] 82/91 (1): singularPressureLoss2.deltaP = singularPressureLoss2.K * singularPressureLoss2.Q * abs(singularPressureLoss2.Q) / singularPressureLoss2.rho [dynamic |0|0|0|0|] 83/92 (1): singularPressureLoss2.Pm = 0.5 * (singularPressureLoss2.C1.P + singularPressureLoss2.C2.P) [dynamic |0|0|0|0|] 84/93 (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid) [dynamic |0|0|0|0|] 85/103 (1): singularPressureLoss2.h = singularPressureLoss2.pro_pT.h [dynamic |0|0|0|0|] 86/104 (1): singularPressureLoss2.rho = singularPressureLoss2.pro_pT.d [dynamic |0|0|0|0|] 87/105 (1): singularPressureLoss2.pro_ph.d = 0.0 [dynamic |0|0|0|0|] 88/106 (1): singularPressureLoss2.pro_ph.T = 0.0 [dynamic |0|0|0|0|] 89/107 (1): singularPressureLoss2.pro_ph.u = 0.0 [dynamic |0|0|0|0|] 90/108 (1): singularPressureLoss2.pro_ph.s = 0.0 [dynamic |0|0|0|0|] 91/109 (1): singularPressureLoss2.pro_ph.cp = 0.0 [dynamic |0|0|0|0|] 92/110 (1): singularPressureLoss2.pro_ph.ddhp = 0.0 [dynamic |0|0|0|0|] 93/111 (1): singularPressureLoss2.pro_ph.ddph = 0.0 [dynamic |0|0|0|0|] 94/112 (1): singularPressureLoss2.pro_ph.duph = 0.0 [dynamic |0|0|0|0|] 95/113 (1): singularPressureLoss2.pro_ph.duhp = 0.0 [dynamic |0|0|0|0|] 96/114 (1): singularPressureLoss2.pro_ph.x = 0.0 [dynamic |0|0|0|0|] 97/115 (1): singularPressureLoss3.C1.P - singularPressureLoss3.C2.P = singularPressureLoss3.deltaP [dynamic |0|0|0|0|] 98/116 (1): singularPressureLoss3.C2.Q = singularPressureLoss3.C1.Q [dynamic |0|0|0|0|] 99/117 (1): singularPressureLoss3.C2.h = singularPressureLoss3.C1.h [dynamic |0|0|0|0|] 100/118 (1): singularPressureLoss3.h = singularPressureLoss3.C1.h [dynamic |0|0|0|0|] 101/119 (1): singularPressureLoss3.Q = singularPressureLoss3.C1.Q [dynamic |0|0|0|0|] 102/120 (1): 0.0 = singularPressureLoss3.C1.h - singularPressureLoss3.C1.h_vol [dynamic |0|0|0|0|] 103/121 (1): singularPressureLoss3.deltaP = singularPressureLoss3.K * singularPressureLoss3.Q * abs(singularPressureLoss3.Q) / singularPressureLoss3.rho [dynamic |0|0|0|0|] 104/122 (1): singularPressureLoss3.Pm = 0.5 * (singularPressureLoss3.C1.P + singularPressureLoss3.C2.P) [dynamic |0|0|0|0|] 105/123 (10): singularPressureLoss3.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss3.Pm, singularPressureLoss3.T, singularPressureLoss3.mode, singularPressureLoss3.fluid) [dynamic |0|0|0|0|] 106/133 (1): singularPressureLoss3.h = singularPressureLoss3.pro_pT.h [dynamic |0|0|0|0|] 107/134 (1): singularPressureLoss3.rho = singularPressureLoss3.pro_pT.d [dynamic |0|0|0|0|] 108/135 (1): singularPressureLoss3.pro_ph.d = 0.0 [dynamic |0|0|0|0|] 109/136 (1): singularPressureLoss3.pro_ph.T = 0.0 [dynamic |0|0|0|0|] 110/137 (1): singularPressureLoss3.pro_ph.u = 0.0 [dynamic |0|0|0|0|] 111/138 (1): singularPressureLoss3.pro_ph.s = 0.0 [dynamic |0|0|0|0|] 112/139 (1): singularPressureLoss3.pro_ph.cp = 0.0 [dynamic |0|0|0|0|] 113/140 (1): singularPressureLoss3.pro_ph.ddhp = 0.0 [dynamic |0|0|0|0|] 114/141 (1): singularPressureLoss3.pro_ph.ddph = 0.0 [dynamic |0|0|0|0|] 115/142 (1): singularPressureLoss3.pro_ph.duph = 0.0 [dynamic |0|0|0|0|] 116/143 (1): singularPressureLoss3.pro_ph.duhp = 0.0 [dynamic |0|0|0|0|] 117/144 (1): singularPressureLoss3.pro_ph.x = 0.0 [dynamic |0|0|0|0|] 118/145 (1): singularPressureLoss4.C1.P - singularPressureLoss4.C2.P = singularPressureLoss4.deltaP [dynamic |0|0|0|0|] 119/146 (1): singularPressureLoss4.C2.Q = singularPressureLoss4.C1.Q [dynamic |0|0|0|0|] 120/147 (1): singularPressureLoss4.C2.h = singularPressureLoss4.C1.h [dynamic |0|0|0|0|] 121/148 (1): singularPressureLoss4.h = singularPressureLoss4.C1.h [dynamic |0|0|0|0|] 122/149 (1): singularPressureLoss4.Q = singularPressureLoss4.C1.Q [dynamic |0|0|0|0|] 123/150 (1): 0.0 = singularPressureLoss4.C1.h - singularPressureLoss4.C1.h_vol [dynamic |0|0|0|0|] 124/151 (1): singularPressureLoss4.deltaP = singularPressureLoss4.K * singularPressureLoss4.Q * abs(singularPressureLoss4.Q) / singularPressureLoss4.rho [dynamic |0|0|0|0|] 125/152 (1): singularPressureLoss4.Pm = 0.5 * (singularPressureLoss4.C1.P + singularPressureLoss4.C2.P) [dynamic |0|0|0|0|] 126/153 (10): singularPressureLoss4.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss4.Pm, singularPressureLoss4.T, singularPressureLoss4.mode, singularPressureLoss4.fluid) [dynamic |0|0|0|0|] 127/163 (1): singularPressureLoss4.h = singularPressureLoss4.pro_pT.h [dynamic |0|0|0|0|] 128/164 (1): singularPressureLoss4.rho = singularPressureLoss4.pro_pT.d [dynamic |0|0|0|0|] 129/165 (1): singularPressureLoss4.pro_ph.d = 0.0 [dynamic |0|0|0|0|] 130/166 (1): singularPressureLoss4.pro_ph.T = 0.0 [dynamic |0|0|0|0|] 131/167 (1): singularPressureLoss4.pro_ph.u = 0.0 [dynamic |0|0|0|0|] 132/168 (1): singularPressureLoss4.pro_ph.s = 0.0 [dynamic |0|0|0|0|] 133/169 (1): singularPressureLoss4.pro_ph.cp = 0.0 [dynamic |0|0|0|0|] 134/170 (1): singularPressureLoss4.pro_ph.ddhp = 0.0 [dynamic |0|0|0|0|] 135/171 (1): singularPressureLoss4.pro_ ...[truncated 426005 chars]... 0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +97: volumeB1.Cs1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +98: volumeB1.Cs1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 99: volumeB1.Ce2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 100: volumeB1.Ce2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -101: volumeB1.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 +101: volumeB1.Ce2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 102: volumeB1.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 -103: volumeB1.Ce2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -104: volumeB1.Ce2.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +103: volumeB1.Ce2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +104: volumeB1.Ce2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 105: volumeB1.Ce1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 106: volumeB1.Ce1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -107: volumeB1.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 +107: volumeB1.Ce1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 108: volumeB1.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 -109: volumeB1.Ce1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -110: volumeB1.Ce1.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +109: volumeB1.Ce1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +110: volumeB1.Ce1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 111: volumeB1.pro.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 112: volumeB1.pro.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 113: volumeB1.pro.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 114: volumeB1.pro.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 115: volumeB1.pro.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -116: volumeB1.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 -117: volumeB1.pro.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -118: volumeB1.pro.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -119: volumeB1.pro.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +116: volumeB1.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real +117: volumeB1.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +118: volumeB1.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +119: volumeB1.pro.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 120: volumeB1.pro.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 121: volumeB1.BH:VARIABLE(unit = "W" ) "Right hand side of the energybalance equation" type: Real 122: volumeB1.BQ:VARIABLE(unit = "kg/s" ) "Right hand side of the mass balance equation" type: Real 123: volumeB1.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real -124: volumeB1.h:VARIABLE(start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real -125: volumeB1.P:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure" type: Real +124: volumeB1.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real +125: volumeB1.P:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 126: volumeB1.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 127: singularPressureLoss4.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 128: singularPressureLoss4.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 129: singularPressureLoss4.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 130: singularPressureLoss4.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 131: singularPressureLoss4.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real -132: singularPressureLoss4.pro_pT.cp:VARIABLE(min = 1e-09 max = 9.999999999999999e+59 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real -133: singularPressureLoss4.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -134: singularPressureLoss4.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -135: singularPressureLoss4.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real -136: singularPressureLoss4.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +132: singularPressureLoss4.pro_pT.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real +133: singularPressureLoss4.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +134: singularPressureLoss4.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +135: singularPressureLoss4.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real +136: singularPressureLoss4.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 137: singularPressureLoss4.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 138: singularPressureLoss4.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 139: singularPressureLoss4.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 140: singularPressureLoss4.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 141: singularPressureLoss4.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -142: singularPressureLoss4.pro_ph.cp:VARIABLE(min = 1e-09 max = 9.999999999999999e+59 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real -143: singularPressureLoss4.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -144: singularPressureLoss4.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -145: singularPressureLoss4.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +142: singularPressureLoss4.pro_ph.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real +143: singularPressureLoss4.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +144: singularPressureLoss4.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +145: singularPressureLoss4.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 146: singularPressureLoss4.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 147: singularPressureLoss4.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 148: singularPressureLoss4.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -149: singularPressureLoss4.C2.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real +149: singularPressureLoss4.C2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 150: singularPressureLoss4.C2.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real -151: singularPressureLoss4.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -152: singularPressureLoss4.C2.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +151: singularPressureLoss4.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +152: singularPressureLoss4.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 153: singularPressureLoss4.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 154: singularPressureLoss4.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -155: singularPressureLoss4.C1.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real +155: singularPressureLoss4.C1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 156: singularPressureLoss4.C1.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real -157: singularPressureLoss4.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -158: singularPressureLoss4.C1.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real -159: singularPressureLoss4.h:VARIABLE(start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real -160: singularPressureLoss4.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real +157: singularPressureLoss4.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +158: singularPressureLoss4.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real +159: singularPressureLoss4.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real +160: singularPressureLoss4.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 161: singularPressureLoss4.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 162: singularPressureLoss4.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 163: singularPressureLoss4.Q:VARIABLE(start = 99.5 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real -164: singularPressureLoss4.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real +164: singularPressureLoss4.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 165: singularPressureLoss3.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 166: singularPressureLoss3.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 167: singularPressureLoss3.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 168: singularPressureLoss3.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 169: singularPressureLoss3.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real -170: 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 -171: singularPressureLoss3.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -172: singularPressureLoss3.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -173: singularPressureLoss3.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real -174: singularPressureLoss3.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +170: 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 +171: singularPressureLoss3.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +172: singularPressureLoss3.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +173: singularPressureLoss3.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real +174: singularPressureLoss3.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 175: singularPressureLoss3.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 176: singularPressureLoss3.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 177: singularPressureLoss3.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 178: singularPressureLoss3.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 179: singularPressureLoss3.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -180: 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 -181: singularPressureLoss3.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -182: singularPressureLoss3.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -183: singularPressureLoss3.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +180: 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 +181: singularPressureLoss3.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +182: singularPressureLoss3.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +183: singularPressureLoss3.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 184: singularPressureLoss3.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 185: singularPressureLoss3.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 186: singularPressureLoss3.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -187: 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 +187: 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 188: 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 -189: singularPressureLoss3.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -190: 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 +189: singularPressureLoss3.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +190: singularPressureLoss3.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 191: singularPressureLoss3.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 192: singularPressureLoss3.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -193: 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 +193: 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 194: 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 -195: singularPressureLoss3.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -196: 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 -197: singularPressureLoss3.h:VARIABLE(start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real -198: singularPressureLoss3.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real +195: singularPressureLoss3.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +196: singularPressureLoss3.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real +197: singularPressureLoss3.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real +198: singularPressureLoss3.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 199: singularPressureLoss3.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 200: singularPressureLoss3.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 201: singularPressureLoss3.Q:VARIABLE(start = 49.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real -202: singularPressureLoss3.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real +202: singularPressureLoss3.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 203: singularPressureLoss2.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 204: singularPressureLoss2.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 205: singularPressureLoss2.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 206: singularPressureLoss2.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 207: singularPressureLoss2.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real -208: 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 -209: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -210: singularPressureLoss2.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -211: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real -212: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +208: 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 +209: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +210: singularPressureLoss2.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +211: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real +212: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 213: singularPressureLoss2.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 214: singularPressureLoss2.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 215: singularPressureLoss2.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 216: singularPressureLoss2.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 217: singularPressureLoss2.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -218: 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 -219: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -220: singularPressureLoss2.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -221: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +218: 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 +219: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +220: singularPressureLoss2.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +221: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 222: singularPressureLoss2.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 223: singularPressureLoss2.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 224: singularPressureLoss2.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -225: 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 +225: 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 226: 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 -227: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -228: 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 +227: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +228: singularPressureLoss2.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 229: singularPressureLoss2.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 230: singularPressureLoss2.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -231: 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 +231: 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 232: 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 -233: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -234: 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 -235: singularPressureLoss2.h:VARIABLE(start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real -236: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real +233: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +234: singularPressureLoss2.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real +235: singularPressureLoss2.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real +236: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 237: singularPressureLoss2.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 238: singularPressureLoss2.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 239: singularPressureLoss2.Q:VARIABLE(start = 50.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real -240: singularPressureLoss2.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real +240: singularPressureLoss2.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 241: singularPressureLoss1.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 242: singularPressureLoss1.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 243: singularPressureLoss1.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 244: singularPressureLoss1.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 245: singularPressureLoss1.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real -246: 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 -247: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -248: singularPressureLoss1.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -249: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real -250: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +246: 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 +247: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +248: singularPressureLoss1.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +249: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real +250: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 251: singularPressureLoss1.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 252: singularPressureLoss1.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 253: singularPressureLoss1.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 254: singularPressureLoss1.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 255: singularPressureLoss1.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -256: 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 -257: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -258: singularPressureLoss1.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -259: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +256: 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 +257: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +258: singularPressureLoss1.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +259: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 260: singularPressureLoss1.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 261: singularPressureLoss1.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 262: singularPressureLoss1.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -263: 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 +263: 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 264: 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 -265: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -266: 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 +265: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +266: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 267: singularPressureLoss1.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 268: singularPressureLoss1.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -269: 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 +269: 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 270: 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 -271: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -272: 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 -273: singularPressureLoss1.h:VARIABLE(start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real -274: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real +271: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +272: singularPressureLoss1.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real +273: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real +274: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 275: singularPressureLoss1.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 276: singularPressureLoss1.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 277: singularPressureLoss1.Q:VARIABLE(start = 100.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real -278: singularPressureLoss1.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real -279: sourceP1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Source pressure" type: Real +278: singularPressureLoss1.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real +279: sourceP1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Source pressure" type: Real 280: sourceP1.T0:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Source temperature (active if option_temperature=1)" type: Real 281: sourceP1.h0:VARIABLE(unit = "J/kg" ) "Source specific enthalpy (active if option_temperature=2)" type: Real -282: sinkP1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Sink pressure" type: Real +282: sinkP1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Sink pressure" type: Real 283: sinkP1.T0:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Sink temperature (active if option_temperature=1)" type: Real 284: sinkP1.h0:VARIABLE(unit = "J/kg" ) "Sink specific enthalpy (active if option_temperature=2)" type: Real OrderedEquation (212, 284) ======================================== 1/1 (1): singularPressureLoss1.Q = 0.0 [binding |0|0|0|0|] 2/2 (1): singularPressureLoss3.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): sinkP1.P0 = 100000.0 [binding |0|0|0|0|] +5/5 (1): sourceP1.h0 = 1e5 [binding |0|0|0|0|] +6/6 (1): sinkP1.P0 = 1e5 [binding |0|0|0|0|] 7/7 (1): sinkP1.T0 = 290.0 [binding |0|0|0|0|] -8/8 (1): sinkP1.h0 = 100000.0 [binding |0|0|0|0|] +8/8 (1): sinkP1.h0 = 1e5 [binding |0|0|0|0|] 9/9 (1): volumeB1.Cs1.P = singularPressureLoss2.C1.P [dynamic |0|0|0|0|] 10/10 (1): volumeB1.Cs1.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|] 11/11 (1): volumeB1.Cs1.a = singularPressureLoss2.C1.a [dynamic |0|0|0|0|] 12/12 (1): volumeB1.Cs1.b = singularPressureLoss2.C1.b [dynamic |0|0|0|0|] 13/13 (1): volumeB1.Cs1.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|] @@ -2876,11 +2876,11 @@ 137/173 (1): singularPressureLoss4.pro_ph.ddph = 0.0 [dynamic |0|0|0|0|] 138/174 (1): singularPressureLoss4.pro_ph.duph = 0.0 [dynamic |0|0|0|0|] 139/175 (1): singularPressureLoss4.pro_ph.duhp = 0.0 [dynamic |0|0|0|0|] 140/176 (1): singularPressureLoss4.pro_ph.x = 0.0 [dynamic |0|0|0|0|] 141/177 (1): volumeB1.Ce2.Q = 0.0 [dynamic |0|0|0|0|] -142/178 (1): volumeB1.Ce2.h = 100000.0 [dynamic |0|0|0|0|] +142/178 (1): volumeB1.Ce2.h = 1e5 [dynamic |0|0|0|0|] 143/179 (1): volumeB1.Ce2.b = true [dynamic |0|0|0|0|] 144/180 (1): volumeB1.BQ = volumeB1.Ce1.Q + volumeB1.Ce2.Q + (-volumeB1.Cs1.Q) - volumeB1.Cs2.Q [dynamic |0|0|0|0|] 145/181 (1): 0.0 = volumeB1.BQ [dynamic |0|0|0|0|] 146/182 (1): volumeB1.P = volumeB1.Ce1.P [dynamic |0|0|0|0|] 147/183 (1): volumeB1.P = volumeB1.Ce2.P [dynamic |0|0|0|0|] @@ -2894,11 +2894,11 @@ 155/191 (1): volumeB1.Cs2.h_vol = volumeB1.h [dynamic |0|0|0|0|] 156/192 (10): volumeB1.pro = ThermoSysPro.Properties.Fluid.Ph(volumeB1.P, volumeB1.h, volumeB1.mode, volumeB1.fluid) [dynamic |0|0|0|0|] 157/202 (1): volumeB1.T = volumeB1.pro.T [dynamic |0|0|0|0|] 158/203 (1): volumeB1.rho = volumeB1.pro.d [dynamic |0|0|0|0|] 159/204 (1): volumeB2.Cs2.Q = 0.0 [dynamic |0|0|0|0|] -160/205 (1): volumeB2.Cs2.h = 100000.0 [dynamic |0|0|0|0|] +160/205 (1): volumeB2.Cs2.h = 1e5 [dynamic |0|0|0|0|] 161/206 (1): volumeB2.Cs2.a = true [dynamic |0|0|0|0|] 162/207 (1): volumeB2.BQ = volumeB2.Ce1.Q + volumeB2.Ce2.Q + (-volumeB2.Cs1.Q) - volumeB2.Cs2.Q [dynamic |0|0|0|0|] 163/208 (1): 0.0 = volumeB2.BQ [dynamic |0|0|0|0|] 164/209 (1): volumeB2.P = volumeB2.Ce1.P [dynamic |0|0|0|0|] 165/210 (1): volumeB2.P = volumeB2.Ce2.P [dynamic |0|0|0|0|] @@ -3239,16 +3239,16 @@ var 284 is solved in eqn 8 Standard BLT of the original model:(284) ============================================================ -284: sinkP1.h0: (8/8): (1): sinkP1.h0 = 100000.0 +284: sinkP1.h0: (8/8): (1): sinkP1.h0 = 1e5 283: sinkP1.T0: (7/7): (1): sinkP1.T0 = 290.0 -282: sinkP1.P0: (6/6): (1): sinkP1.P0 = 100000.0 -281: sourceP1.h0: (5/5): (1): sourceP1.h0 = 100000.0 +282: sinkP1.P0: (6/6): (1): sinkP1.P0 = 1e5 +281: sourceP1.h0: (5/5): (1): sourceP1.h0 = 1e5 280: sourceP1.T0: (4/4): (1): sourceP1.T0 = 290.0 -279: sourceP1.P0: (3/3): (1): sourceP1.P0 = 300000.0 +279: sourceP1.P0: (3/3): (1): sourceP1.P0 = 3e5 278: singularPressureLoss1.deltaP: (57/57): (1): singularPressureLoss1.C1.P - singularPressureLoss1.C2.P = singularPressureLoss1.deltaP 277: singularPressureLoss1.Q: (1/1): (1): singularPressureLoss1.Q = 0.0 276: singularPressureLoss1.rho: (63/63): (1): singularPressureLoss1.deltaP = singularPressureLoss1.K * singularPressureLoss1.Q * abs(singularPressureLoss1.Q) / singularPressureLoss1.rho 275: singularPressureLoss1.T: (65/66): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 274: singularPressureLoss1.Pm: (65/65): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) @@ -3422,11 +3422,11 @@ 106: volumeB1.Ce1.a: (203/275): (1): volumeB1.Ce1.a = true 105: volumeB1.Ce1.b: (42/42): (1): singularPressureLoss1.C2.b = volumeB1.Ce1.b 104: volumeB1.Ce2.P: (147/183): (1): volumeB1.P = volumeB1.Ce2.P 103: volumeB1.Ce2.h_vol: (153/189): (1): volumeB1.Ce2.h_vol = volumeB1.h 102: volumeB1.Ce2.Q: (141/177): (1): volumeB1.Ce2.Q = 0.0 -101: volumeB1.Ce2.h: (142/178): (1): volumeB1.Ce2.h = 100000.0 +101: volumeB1.Ce2.h: (142/178): (1): volumeB1.Ce2.h = 1e5 100: volumeB1.Ce2.a: (204/276): (1): volumeB1.Ce2.a = true 99: volumeB1.Ce2.b: (143/179): (1): volumeB1.Ce2.b = true 98: volumeB1.Cs1.P: (148/184): (1): volumeB1.P = volumeB1.Cs1.P 97: volumeB1.Cs1.h_vol: (154/190): (1): volumeB1.Cs1.h_vol = volumeB1.h 96: volumeB1.Cs1.Q: (144/180): (1): volumeB1.BQ = volumeB1.Ce1.Q + volumeB1.Ce2.Q + (-volumeB1.Cs1.Q) - volumeB1.Cs2.Q @@ -3474,11 +3474,11 @@ 54: volumeB2.Cs1.a: (35/35): (1): volumeB2.Cs1.a = singularPressureLoss4.C1.a 53: volumeB2.Cs1.b: (209/281): (1): volumeB2.Cs1.b = true 52: volumeB2.Cs2.P: (167/212): (1): volumeB2.P = volumeB2.Cs2.P 51: volumeB2.Cs2.h_vol: (173/218): (1): volumeB2.Cs2.h_vol = volumeB2.h 50: volumeB2.Cs2.Q: (159/204): (1): volumeB2.Cs2.Q = 0.0 -49: volumeB2.Cs2.h: (160/205): (1): volumeB2.Cs2.h = 100000.0 +49: volumeB2.Cs2.h: (160/205): (1): volumeB2.Cs2.h = 1e5 48: volumeB2.Cs2.a: (161/206): (1): volumeB2.Cs2.a = true 47: volumeB2.Cs2.b: (210/282): (1): volumeB2.Cs2.b = true 46: sourceP1.P: (181/235): (1): sourceP1.P = sourceP1.IPressure.signal 45: sourceP1.Q: (178/232): (1): sourceP1.C.Q = sourceP1.Q 44: sourceP1.T: (184/238): (1): sourceP1.h = ThermoSysPro.Properties.WaterSteam.IF97.SpecificEnthalpy_PT(sourceP1.P, sourceP1.T, 0) @@ -3535,14 +3535,14 @@ 4: singularPressureLoss1.Q:VARIABLE(start = 100.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real Boundary conditions (6) ======================================== -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: sinkP1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Sink pressure" type: Real +4: sinkP1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Sink pressure" type: Real 5: sinkP1.T0:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Sink temperature (active if option_temperature=1)" type: Real 6: sinkP1.h0:VARIABLE(unit = "J/kg" ) "Sink specific enthalpy (active if option_temperature=2)" type: Real Binding equations:(26) @@ -3564,16 +3564,16 @@ 192: singularPressureLoss3.C1.a: (199/271): (1): singularPressureLoss3.C1.a = true 223: singularPressureLoss2.C2.b: (198/270): (1): singularPressureLoss2.C2.b = true 230: singularPressureLoss2.C1.a: (197/269): (1): singularPressureLoss2.C1.a = true 261: singularPressureLoss1.C2.b: (196/268): (1): singularPressureLoss1.C2.b = true 268: singularPressureLoss1.C1.a: (195/267): (1): singularPressureLoss1.C1.a = true -284: sinkP1.h0: (8/8): (1): sinkP1.h0 = 100000.0 +284: sinkP1.h0: (8/8): (1): sinkP1.h0 = 1e5 283: sinkP1.T0: (7/7): (1): sinkP1.T0 = 290.0 -282: sinkP1.P0: (6/6): (1): sinkP1.P0 = 100000.0 -281: sourceP1.h0: (5/5): (1): sourceP1.h0 = 100000.0 +282: sinkP1.P0: (6/6): (1): sinkP1.P0 = 1e5 +281: sourceP1.h0: (5/5): (1): sourceP1.h0 = 1e5 280: sourceP1.T0: (4/4): (1): sourceP1.T0 = 290.0 -279: sourceP1.P0: (3/3): (1): sourceP1.P0 = 300000.0 +279: sourceP1.P0: (3/3): (1): sourceP1.P0 = 3e5 201: singularPressureLoss3.Q: (2/2): (1): singularPressureLoss3.Q = 0.0 277: singularPressureLoss1.Q: (1/1): (1): singularPressureLoss1.Q = 0.0 E-BLT: equations that compute the variables of interest:(2) @@ -3734,17 +3734,18 @@ ========================================================================== -Passed Set_S has 17 equations and 17 variables record SimulationResult -resultFile = "econcile", -simulationOptions = "startTime = 0.0, stopTime = 1.0, numberOfIntervals = 500, tolerance = 1e-06, method = 'dassl', fileNamePrefix = 'NewDataReconciliationSimpleTests.TSP_FourFlows3', options = '', outputFormat = 'mat', variableFilter = '.*', cflags = '', simflags = '-reconcile -sx=./NewDataReconciliationSimpleTests/resources/DataReconciliationSimpleTests.TSP_FourFlows3_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_FourFlows3', options = '', outputFormat = 'mat', variableFilter = '.*', cflags = '', simflags = '-reconcile -sx=./NewDataReconciliationSimpleTests/resources/DataReconciliationSimpleTests.TSP_FourFlows3_Inputs.csv -eps=0.0023 -lv=LOG_JAC'", +messages = "Simulation execution failed for model: NewDataReconciliationSimpleTests.TSP_FourFlows3 +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_FourFlows3 -LOG_STDOUT | info | DataReconciliation Completed! +LOG_STDOUT | error | Measurement input file path not found ./NewDataReconciliationSimpleTests/resources/DataReconciliationSimpleTests.TSP_FourFlows3_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 3739: Text differs: expected: resultFile = "econcile", got: resultFile = "", == 1 out of 1 tests failed [openmodelica/dataReconciliation/TSP_FourFlows3.mos_temp8704, time: 25]