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Failed
openmodelica_dataReconciliation.TSP_Pipe1.mos (from (result.xml))
Stacktrace
Output mismatch (see stdout for details)
Standard Output
+ TSP_Pipe1 ... equation mismatch [time: 6]
==== Log C:\Windows\TEMP/omc-rtest-OpenModelica/openmodelica/dataReconciliation/TSP_Pipe1.mos_temp9024/log-TSP_Pipe1.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.
"
"[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).
[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/SourceP.mo:30:3-31:45:writable] Warning: Connector C is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[openmodelica/dataReconciliation/NewDataReconciliationSimpleTests/SinkP.mo:33:3-34:47:writable] Warning: Connector C is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[ThermoSysPro 3.2.0/Properties/WaterSteam/IF97_packages.mo:784:9-784:27:writable] Warning: cv was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[ThermoSysPro 3.2.0/Properties/WaterSteam/IF97_packages.mo:851:9-851:27:writable] Warning: cv was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[ThermoSysPro 3.2.0/Properties/WaterSteam/IF97_packages.mo:1089:9-1089:27:writable] Warning: cv was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[ThermoSysPro 3.2.0/Properties/WaterSteamSimple/prop4_Ph.mo:76:3-76:60:writable] Warning: dh1satp was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[ThermoSysPro 3.2.0/Properties/WaterSteamSimple/prop4_Ph.mo:76:3-76:60:writable] Warning: dh2satp was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[ThermoSysPro 3.2.0/Properties/WaterSteamSimple/prop4_Ph_der.mo:179:3-182:49:writable] Warning: du1satp_der was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[ThermoSysPro 3.2.0/Properties/WaterSteamSimple/prop4_Ph_der.mo:179:3-182:49:writable] Warning: du2satp_der was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
Warning: Out of memory! Faking a stack overflow.
Error: Stack overflow occurred while evaluating simulate(NewDataReconciliationSimpleTests.TSP_Pipe1, simflags = \"-reconcile -sx=./NewDataReconciliationSimpleTests/resources/DataReconciliationSimpleTests.TSP_Pipe1_Inputs.csv -eps=0.0023 -lv=LOG_JAC\"):
[bt] [Symbols are not generated when running the test suite]
"
''
Equation mismatch: diff says:
--- "C:\\Windows\\TEMP/omc-rtest-OpenModelica/openmodelica/dataReconciliation/TSP_Pipe1.mos_temp9024/equations-expected"2024-06-13 13:00:29.583850600 +0200
+++ "C:\\Windows\\TEMP/omc-rtest-OpenModelica/openmodelica/dataReconciliation/TSP_Pipe1.mos_temp9024/equations-got"2024-06-13 13:00:35.573852500 +0200
@@ -5,1202 +5,10 @@
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_Pipe1
-==========================================================================
-
-
-OrderedVariables (128)
-========================================
-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 = 100000.0 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 = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-7: sinkP1.C.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real
-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-09 max = 9.999999999999999e+59 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real
-16: sinkP1.pro.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
-17: sinkP1.pro.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real
-18: sinkP1.pro.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
-19: sinkP1.pro.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real
-20: sinkP1.h:VARIABLE(unit = "J/kg" ) "Fluid enthalpy" type: Real
-21: sinkP1.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real
-22: sinkP1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real
-23: sinkP1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure" type: Real
-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 = 100000.0 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 = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-30: sourceP1.C.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real
-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-09 max = 9.999999999999999e+59 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real
-39: sourceP1.pro.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
-40: sourceP1.pro.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real
-41: sourceP1.pro.d:VARIABLE(min = 1e-09 max = 100000.0 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 = 100000.0 ) "Fluid pressure" type: Real
-47: singularPressureLoss2.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
-48: singularPressureLoss2.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real
-49: singularPressureLoss2.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real
-50: singularPressureLoss2.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real
-51: singularPressureLoss2.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real
-52: 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
-53: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
-54: singularPressureLoss2.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real
-55: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real
-56: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
-57: singularPressureLoss2.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
-58: singularPressureLoss2.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
-59: singularPressureLoss2.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
-60: singularPressureLoss2.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
-61: singularPressureLoss2.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
-62: 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
-63: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
-64: singularPressureLoss2.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real
-65: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
-66: singularPressureLoss2.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real
-67: singularPressureLoss2.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-68: singularPressureLoss2.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-69: 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
-70: 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
-71: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-72: 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
-73: singularPressureLoss2.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-74: singularPressureLoss2.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-75: 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
-76: 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
-77: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-78: 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
-79: singularPressureLoss2.h:VARIABLE(start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real
-80: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real
-81: singularPressureLoss2.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real
-82: singularPressureLoss2.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real
-83: singularPressureLoss2.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
-84: singularPressureLoss2.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real
-85: singularPressureLoss1.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
-86: singularPressureLoss1.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real
-87: singularPressureLoss1.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real
-88: singularPressureLoss1.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real
-89: singularPressureLoss1.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real
-90: 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
-91: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
-92: singularPressureLoss1.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real
-93: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real
-94: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
-95: singularPressureLoss1.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
-96: singularPressureLoss1.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
-97: singularPressureLoss1.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
-98: singularPressureLoss1.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
-99: singularPressureLoss1.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
-100: 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
-101: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
-102: singularPressureLoss1.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real
-103: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
-104: singularPressureLoss1.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real
-105: singularPressureLoss1.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-106: singularPressureLoss1.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-107: 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
-108: 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
-109: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-110: 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
-111: singularPressureLoss1.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-112: singularPressureLoss1.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-113: 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
-114: 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
-115: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-116: 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
-117: singularPressureLoss1.h:VARIABLE(start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real
-118: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real
-119: singularPressureLoss1.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real
-120: singularPressureLoss1.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real
-121: singularPressureLoss1.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
-122: singularPressureLoss1.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real
-123: sourceP1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Source pressure" type: Real
-124: sourceP1.T0:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Source temperature (active if option_temperature=1)" type: Real
-125: sourceP1.h0:VARIABLE(unit = "J/kg" ) "Source specific enthalpy (active if option_temperature=2)" type: Real
-126: sinkP1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Sink pressure" type: Real
-127: sinkP1.T0:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Sink temperature (active if option_temperature=1)" type: Real
-128: sinkP1.h0:VARIABLE(unit = "J/kg" ) "Sink specific enthalpy (active if option_temperature=2)" type: Real
-
-
-OrderedEquation (92, 128)
-========================================
-1/1 (1): sourceP1.P0 = 300000.0 [binding |0|0|0|0|]
-2/2 (1): sourceP1.T0 = 290.0 [binding |0|0|0|0|]
-3/3 (1): sourceP1.h0 = 100000.0 [binding |0|0|0|0|]
-4/4 (1): sinkP1.P0 = 100000.0 [binding |0|0|0|0|]
-5/5 (1): sinkP1.T0 = 290.0 [binding |0|0|0|0|]
-6/6 (1): sinkP1.h0 = 100000.0 [binding |0|0|0|0|]
-7/7 (1): singularPressureLoss1.C2.P = singularPressureLoss2.C1.P [dynamic |0|0|0|0|]
-8/8 (1): singularPressureLoss1.C2.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|]
-9/9 (1): singularPressureLoss1.C2.a = singularPressureLoss2.C1.a [dynamic |0|0|0|0|]
-10/10 (1): singularPressureLoss1.C2.b = singularPressureLoss2.C1.b [dynamic |0|0|0|0|]
-11/11 (1): singularPressureLoss1.C2.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|]
-12/12 (1): singularPressureLoss1.C2.h_vol = singularPressureLoss2.C1.h_vol [dynamic |0|0|0|0|]
-13/13 (1): sourceP1.C.P = singularPressureLoss1.C1.P [dynamic |0|0|0|0|]
-14/14 (1): sourceP1.C.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|]
-15/15 (1): sourceP1.C.a = singularPressureLoss1.C1.a [dynamic |0|0|0|0|]
-16/16 (1): sourceP1.C.b = singularPressureLoss1.C1.b [dynamic |0|0|0|0|]
-17/17 (1): sourceP1.C.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|]
-18/18 (1): sourceP1.C.h_vol = singularPressureLoss1.C1.h_vol [dynamic |0|0|0|0|]
-19/19 (1): singularPressureLoss2.C2.P = sinkP1.C.P [dynamic |0|0|0|0|]
-20/20 (1): singularPressureLoss2.C2.Q = sinkP1.C.Q [dynamic |0|0|0|0|]
-21/21 (1): singularPressureLoss2.C2.a = sinkP1.C.a [dynamic |0|0|0|0|]
-22/22 (1): singularPressureLoss2.C2.b = sinkP1.C.b [dynamic |0|0|0|0|]
-23/23 (1): singularPressureLoss2.C2.h = sinkP1.C.h [dynamic |0|0|0|0|]
-24/24 (1): singularPressureLoss2.C2.h_vol = sinkP1.C.h_vol [dynamic |0|0|0|0|]
-25/25 (1): singularPressureLoss1.C1.P - singularPressureLoss1.C2.P = singularPressureLoss1.deltaP [dynamic |0|0|0|0|]
-26/26 (1): singularPressureLoss1.C2.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|]
-27/27 (1): singularPressureLoss1.C2.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|]
-28/28 (1): singularPressureLoss1.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|]
-29/29 (1): singularPressureLoss1.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|]
-30/30 (1): singularPressureLoss1.h = ThermoSysPro.Functions.SmoothCond(singularPressureLoss1.Q, singularPressureLoss1.C1.h_vol, singularPressureLoss1.C2.h_vol, 1.0) [dynamic |0|0|0|0|]
-31/31 (1): singularPressureLoss1.deltaP = singularPressureLoss1.K * singularPressureLoss1.Q * abs(singularPressureLoss1.Q) / singularPressureLoss1.rho [dynamic |0|0|0|0|]
-32/32 (1): singularPressureLoss1.Pm = 0.5 * (singularPressureLoss1.C1.P + singularPressureLoss1.C2.P) [dynamic |0|0|0|0|]
-33/33 (10): singularPressureLoss1.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss1.Pm, singularPressureLoss1.h, singularPressureLoss1.mode, singularPressureLoss1.fluid) [dynamic |0|0|0|0|]
-34/43 (1): singularPressureLoss1.T = singularPressureLoss1.pro_ph.T [dynamic |0|0|0|0|]
-35/44 (1): singularPressureLoss1.rho = singularPressureLoss1.pro_ph.d [dynamic |0|0|0|0|]
-36/45 (1): singularPressureLoss1.pro_pT.d = 0.0 [dynamic |0|0|0|0|]
-37/46 (1): singularPressureLoss1.pro_pT.h = 0.0 [dynamic |0|0|0|0|]
-38/47 (1): singularPressureLoss1.pro_pT.u = 0.0 [dynamic |0|0|0|0|]
-39/48 (1): singularPressureLoss1.pro_pT.s = 0.0 [dynamic |0|0|0|0|]
-40/49 (1): singularPressureLoss1.pro_pT.cp = 0.0 [dynamic |0|0|0|0|]
-41/50 (1): singularPressureLoss1.pro_pT.ddTp = 0.0 [dynamic |0|0|0|0|]
-42/51 (1): singularPressureLoss1.pro_pT.ddpT = 0.0 [dynamic |0|0|0|0|]
-43/52 (1): singularPressureLoss1.pro_pT.dupT = 0.0 [dynamic |0|0|0|0|]
-44/53 (1): singularPressureLoss1.pro_pT.duTp = 0.0 [dynamic |0|0|0|0|]
-45/54 (1): singularPressureLoss1.pro_pT.x = 0.0 [dynamic |0|0|0|0|]
-46/55 (1): singularPressureLoss2.C1.P - singularPressureLoss2.C2.P = singularPressureLoss2.deltaP [dynamic |0|0|0|0|]
-47/56 (1): singularPressureLoss2.C2.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|]
-48/57 (1): singularPressureLoss2.C2.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|]
-49/58 (1): singularPressureLoss2.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|]
-50/59 (1): singularPressureLoss2.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|]
-51/60 (1): singularPressureLoss2.h = ThermoSysPro.Functions.SmoothCond(singularPressureLoss2.Q, singularPressureLoss2.C1.h_vol, singularPressureLoss2.C2.h_vol, 1.0) [dynamic |0|0|0|0|]
-52/61 (1): singularPressureLoss2.deltaP = singularPressureLoss2.K * singularPressureLoss2.Q * abs(singularPressureLoss2.Q) / singularPressureLoss2.rho [dynamic |0|0|0|0|]
-53/62 (1): singularPressureLoss2.Pm = 0.5 * (singularPressureLoss2.C1.P + singularPressureLoss2.C2.P) [dynamic |0|0|0|0|]
-54/63 (10): singularPressureLoss2.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.Pm, singularPressureLoss2.h, singularPressureLoss2.mode, singularPressureLoss2.fluid) [dynamic |0|0|0|0|]
-55/73 (1): singularPressureLoss2.T = singularPressureLoss2.pro_ph.T [dynamic |0|0|0|0|]
-56/74 (1): singularPressureLoss2.rho = singularPressureLoss2.pro_ph.d [dynamic |0|0|0|0|]
-57/75 (1): singularPressureLoss2.pro_pT.d = 0.0 [dynamic |0|0|0|0|]
-58/76 (1): singularPressureLoss2.pro_pT.h = 0.0 [dynamic |0|0|0|0|]
-59/77 (1): singularPressureLoss2.pro_pT.u = 0.0 [dynamic |0|0|0|0|]
-60/78 (1): singularPressureLoss2.pro_pT.s = 0.0 [dynamic |0|0|0|0|]
-61/79 (1): singularPressureLoss2.pro_pT.cp = 0.0 [dynamic |0|0|0|0|]
-62/80 (1): singularPressureLoss2.pro_pT.ddTp = 0.0 [dynamic |0|0|0|0|]
-63/81 (1): singularPressureLoss2.pro_pT.ddpT = 0.0 [dynamic |0|0|0|0|]
-64/82 (1): singularPressureLoss2.pro_pT.dupT = 0.0 [dynamic |0|0|0|0|]
-65/83 (1): singularPressureLoss2.pro_pT.duTp = 0.0 [dynamic |0|0|0|0|]
-66/84 (1): singularPressureLoss2.pro_pT.x = 0.0 [dynamic |0|0|0|0|]
-67/85 (1): sourceP1.C.P = sourceP1.P [dynamic |0|0|0|0|]
-68/86 (1): sourceP1.C.Q = sourceP1.Q [dynamic |0|0|0|0|]
-69/87 (1): sourceP1.C.h_vol = sourceP1.h [dynamic |0|0|0|0|]
-70/88 (1): sourceP1.IPressure.signal = sourceP1.P0 [dynamic |0|0|0|0|]
-71/89 (1): sourceP1.P = sourceP1.IPressure.signal [dynamic |0|0|0|0|]
-72/90 (1): sourceP1.ITemperature.signal = sourceP1.T0 [dynamic |0|0|0|0|]
-73/91 (1): sourceP1.ISpecificEnthalpy.signal = sourceP1.h0 [dynamic |0|0|0|0|]
-74/92 (1): sourceP1.T = sourceP1.ITemperature.signal [dynamic |0|0|0|0|]
-75/93 (1): sourceP1.h = ThermoSysPro.Properties.WaterSteam.IF97.SpecificEnthalpy_PT(sourceP1.P, sourceP1.T, 0) [dynamic |0|0|0|0|]
-76/94 (10): sourceP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sourceP1.P, sourceP1.h, sourceP1.mode) [dynamic |0|0|0|0|]
-77/104 (1): sinkP1.C.P = sinkP1.P [dynamic |0|0|0|0|]
-78/105 (1): sinkP1.C.Q = sinkP1.Q [dynamic |0|0|0|0|]
-79/106 (1): sinkP1.C.h_vol = sinkP1.h [dynamic |0|0|0|0|]
-80/107 (1): sinkP1.IPressure.signal = sinkP1.P0 [dynamic |0|0|0|0|]
-81/108 (1): sinkP1.P = sinkP1.IPressure.signal [dynamic |0|0|0|0|]
-82/109 (1): sinkP1.ITemperature.signal = sinkP1.T0 [dynamic |0|0|0|0|]
-83/110 (1): sinkP1.ISpecificEnthalpy.signal = sinkP1.h0 [dynamic |0|0|0|0|]
-84/111 (1): sinkP1.T = sinkP1.ITemperature.signal [dynamic |0|0|0|0|]
-85/112 (1): sinkP1.h = ThermoSysPro.Properties.WaterSteam.IF97.SpecificEnthalpy_PT(sinkP1.P, sinkP1.T, 0) [dynamic |0|0|0|0|]
-86/113 (10): sinkP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sinkP1.P, sinkP1.h, sinkP1.mode) [dynamic |0|0|0|0|]
-87/123 (1): singularPressureLoss1.C1.a = true [binding |0|0|0|0|]
-88/124 (1): singularPressureLoss1.C2.b = true [binding |0|0|0|0|]
-89/125 (1): singularPressureLoss2.C1.a = true [binding |0|0|0|0|]
-90/126 (1): singularPressureLoss2.C2.b = true [binding |0|0|0|0|]
-91/127 (1): sourceP1.C.b = true [binding |0|0|0|0|]
-92/128 (1): sinkP1.C.a = true [binding |0|0|0|0|]
-
-Matching
-========================================
-128 variables and equations
-var 1 is solved in eqn 109
-var 2 is solved in eqn 22
-var 3 is solved in eqn 128
-var 4 is solved in eqn 23
-var 5 is solved in eqn 20
-var 6 is solved in eqn 106
-var 7 is solved in eqn 104
-var 8 is solved in eqn 110
-var 9 is solved in eqn 107
-var 10 is solved in eqn 122
-var 11 is solved in eqn 121
-var 12 is solved in eqn 120
-var 13 is solved in eqn 119
-var 14 is solved in eqn 118
-var 15 is solved in eqn 117
-var 16 is solved in eqn 116
-var 17 is solved in eqn 115
-var 18 is solved in eqn 114
-var 19 is solved in eqn 113
-var 20 is solved in eqn 112
-var 21 is solved in eqn 111
-var 22 is solved in eqn 105
-var 23 is solved in eqn 108
-var 24 is solved in eqn 90
-var 25 is solved in eqn 127
-var 26 is solved in eqn 15
-var 27 is solved in eqn 17
-var 28 is solved in eqn 14
-var 29 is solved in eqn 87
-var 30 is solved in eqn 85
-var 31 is solved in eqn 91
-var 32 is solved in eqn 88
-var 33 is solved in eqn 103
-var 34 is solved in eqn 102
-var 35 is solved in eqn 101
-var 36 is solved in eqn 100
-var 37 is solved in eqn 99
-var 38 is solved in eqn 98
-var 39 is solved in eqn 97
-var 40 is solved in eqn 96
-var 41 is solved in eqn 95
-var 42 is solved in eqn 94
-var 43 is solved in eqn 93
-var 44 is solved in eqn 92
-var 45 is solved in eqn 86
-var 46 is solved in eqn 89
-var 47 is solved in eqn 84
-var 48 is solved in eqn 83
-var 49 is solved in eqn 82
-var 50 is solved in eqn 81
-var 51 is solved in eqn 80
-var 52 is solved in eqn 79
-var 53 is solved in eqn 78
-var 54 is solved in eqn 77
-var 55 is solved in eqn 76
-var 56 is solved in eqn 75
-var 57 is solved in eqn 72
-var 58 is solved in eqn 71
-var 59 is solved in eqn 70
-var 60 is solved in eqn 69
-var 61 is solved in eqn 68
-var 62 is solved in eqn 67
-var 63 is solved in eqn 66
-var 64 is solved in eqn 65
-var 65 is solved in eqn 64
-var 66 is solved in eqn 63
-var 67 is solved in eqn 126
-var 68 is solved in eqn 21
-var 69 is solved in eqn 57
-var 70 is solved in eqn 56
-var 71 is solved in eqn 24
-var 72 is solved in eqn 19
-var 73 is solved in eqn 10
-var 74 is solved in eqn 125
-var 75 is solved in eqn 11
-var 76 is solved in eqn 8
-var 77 is solved in eqn 60
-var 78 is solved in eqn 55
-var 79 is solved in eqn 58
-var 80 is solved in eqn 62
-var 81 is solved in eqn 73
-var 82 is solved in eqn 74
-var 83 is solved in eqn 59
-var 84 is solved in eqn 61
-var 85 is solved in eqn 54
-var 86 is solved in eqn 53
-var 87 is solved in eqn 52
-var 88 is solved in eqn 51
-var 89 is solved in eqn 50
-var 90 is solved in eqn 49
-var 91 is solved in eqn 48
-var 92 is solved in eqn 47
-var 93 is solved in eqn 46
-var 94 is solved in eqn 45
-var 95 is solved in eqn 42
-var 96 is solved in eqn 41
-var 97 is solved in eqn 40
-var 98 is solved in eqn 39
-var 99 is solved in eqn 38
-var 100 is solved in eqn 37
-var 101 is solved in eqn 36
-var 102 is solved in eqn 35
-var 103 is solved in eqn 34
-var 104 is solved in eqn 33
-var 105 is solved in eqn 124
-var 106 is solved in eqn 9
-var 107 is solved in eqn 27
-var 108 is solved in eqn 26
-var 109 is solved in eqn 12
-var 110 is solved in eqn 7
-var 111 is solved in eqn 16
-var 112 is solved in eqn 123
-var 113 is solved in eqn 28
-var 114 is solved in eqn 29
-var 115 is solved in eqn 18
-var 116 is solved in eqn 13
-var 117 is solved in eqn 30
-var 118 is solved in eqn 32
-var 119 is solved in eqn 43
-var 120 is solved in eqn 44
-var 121 is solved in eqn 31
-var 122 is solved in eqn 25
-var 123 is solved in eqn 1
-var 124 is solved in eqn 2
-var 125 is solved in eqn 3
-var 126 is solved in eqn 4
-var 127 is solved in eqn 5
-var 128 is solved in eqn 6
-
-Standard BLT of the original model:(128)
-============================================================
-
-128: sinkP1.h0: (6/6): (1): sinkP1.h0 = 100000.0
-127: sinkP1.T0: (5/5): (1): sinkP1.T0 = 290.0
-126: sinkP1.P0: (4/4): (1): sinkP1.P0 = 100000.0
-125: sourceP1.h0: (3/3): (1): sourceP1.h0 = 100000.0
-124: sourceP1.T0: (2/2): (1): sourceP1.T0 = 290.0
-123: sourceP1.P0: (1/1): (1): sourceP1.P0 = 300000.0
-122: singularPressureLoss1.deltaP: (25/25): (1): singularPressureLoss1.C1.P - singularPressureLoss1.C2.P = singularPressureLoss1.deltaP
-121: singularPressureLoss1.Q: (31/31): (1): singularPressureLoss1.deltaP = singularPressureLoss1.K * singularPressureLoss1.Q * abs(singularPressureLoss1.Q) / singularPressureLoss1.rho
-120: singularPressureLoss1.rho: (35/44): (1): singularPressureLoss1.rho = singularPressureLoss1.pro_ph.d
-119: singularPressureLoss1.T: (34/43): (1): singularPressureLoss1.T = singularPressureLoss1.pro_ph.T
-118: singularPressureLoss1.Pm: (32/32): (1): singularPressureLoss1.Pm = 0.5 * (singularPressureLoss1.C1.P + singularPressureLoss1.C2.P)
-117: singularPressureLoss1.h: (30/30): (1): singularPressureLoss1.h = ThermoSysPro.Functions.SmoothCond(singularPressureLoss1.Q, singularPressureLoss1.C1.h_vol, singularPressureLoss1.C2.h_vol, 1.0)
-116: singularPressureLoss1.C1.P: (13/13): (1): sourceP1.C.P = singularPressureLoss1.C1.P
-115: singularPressureLoss1.C1.h_vol: (18/18): (1): sourceP1.C.h_vol = singularPressureLoss1.C1.h_vol
-114: singularPressureLoss1.C1.Q: (29/29): (1): singularPressureLoss1.Q = singularPressureLoss1.C1.Q
-113: singularPressureLoss1.C1.h: (28/28): (1): singularPressureLoss1.h = singularPressureLoss1.C1.h
-112: singularPressureLoss1.C1.a: (87/123): (1): singularPressureLoss1.C1.a = true
-111: singularPressureLoss1.C1.b: (16/16): (1): sourceP1.C.b = singularPressureLoss1.C1.b
-110: singularPressureLoss1.C2.P: (7/7): (1): singularPressureLoss1.C2.P = singularPressureLoss2.C1.P
-109: singularPressureLoss1.C2.h_vol: (12/12): (1): singularPressureLoss1.C2.h_vol = singularPressureLoss2.C1.h_vol
-108: singularPressureLoss1.C2.Q: (26/26): (1): singularPressureLoss1.C2.Q = singularPressureLoss1.C1.Q
-107: singularPressureLoss1.C2.h: (27/27): (1): singularPressureLoss1.C2.h = singularPressureLoss1.C1.h
-106: singularPressureLoss1.C2.a: (9/9): (1): singularPressureLoss1.C2.a = singularPressureLoss2.C1.a
-105: singularPressureLoss1.C2.b: (88/124): (1): singularPressureLoss1.C2.b = true
-104: singularPressureLoss1.pro_ph.T: (33/33): (10): singularPressureLoss1.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss1.Pm, singularPressureLoss1.h, singularPressureLoss1.mode, singularPressureLoss1.fluid)
-103: singularPressureLoss1.pro_ph.d: (33/34): (10): singularPressureLoss1.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss1.Pm, singularPressureLoss1.h, singularPressureLoss1.mode, singularPressureLoss1.fluid)
-102: singularPressureLoss1.pro_ph.u: (33/35): (10): singularPressureLoss1.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss1.Pm, singularPressureLoss1.h, singularPressureLoss1.mode, singularPressureLoss1.fluid)
-101: singularPressureLoss1.pro_ph.s: (33/36): (10): singularPressureLoss1.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss1.Pm, singularPressureLoss1.h, singularPressureLoss1.mode, singularPressureLoss1.fluid)
-100: singularPressureLoss1.pro_ph.cp: (33/37): (10): singularPressureLoss1.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss1.Pm, singularPressureLoss1.h, singularPressureLoss1.mode, singularPressureLoss1.fluid)
-99: singularPressureLoss1.pro_ph.ddhp: (33/38): (10): singularPressureLoss1.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss1.Pm, singularPressureLoss1.h, singularPressureLoss1.mode, singularPressureLoss1.fluid)
-98: singularPressureLoss1.pro_ph.ddph: (33/39): (10): singularPressureLoss1.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss1.Pm, singularPressureLoss1.h, singularPressureLoss1.mode, singularPressureLoss1.fluid)
-97: singularPressureLoss1.pro_ph.duph: (33/40): (10): singularPressureLoss1.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss1.Pm, singularPressureLoss1.h, singularPressureLoss1.mode, singularPressureLoss1.fluid)
-96: singularPressureLoss1.pro_ph.duhp: (33/41): (10): singularPressureLoss1.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss1.Pm, singularPressureLoss1.h, singularPressureLoss1.mode, singularPressureLoss1.fluid)
-95: singularPressureLoss1.pro_ph.x: (33/42): (10): singularPressureLoss1.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss1.Pm, singularPressureLoss1.h, singularPressureLoss1.mode, singularPressureLoss1.fluid)
-94: singularPressureLoss1.pro_pT.d: (36/45): (1): singularPressureLoss1.pro_pT.d = 0.0
-93: singularPressureLoss1.pro_pT.h: (37/46): (1): singularPressureLoss1.pro_pT.h = 0.0
-92: singularPressureLoss1.pro_pT.u: (38/47): (1): singularPressureLoss1.pro_pT.u = 0.0
-91: singularPressureLoss1.pro_pT.s: (39/48): (1): singularPressureLoss1.pro_pT.s = 0.0
-90: singularPressureLoss1.pro_pT.cp: (40/49): (1): singularPressureLoss1.pro_pT.cp = 0.0
-89: singularPressureLoss1.pro_pT.ddTp: (41/50): (1): singularPressureLoss1.pro_pT.ddTp = 0.0
-88: singularPressureLoss1.pro_pT.ddpT: (42/51): (1): singularPressureLoss1.pro_pT.ddpT = 0.0
-87: singularPressureLoss1.pro_pT.dupT: (43/52): (1): singularPressureLoss1.pro_pT.dupT = 0.0
-86: singularPressureLoss1.pro_pT.duTp: (44/53): (1): singularPressureLoss1.pro_pT.duTp = 0.0
-85: singularPressureLoss1.pro_pT.x: (45/54): (1): singularPressureLoss1.pro_pT.x = 0.0
-84: singularPressureLoss2.deltaP: (52/61): (1): singularPressureLoss2.deltaP = singularPressureLoss2.K * singularPressureLoss2.Q * abs(singularPressureLoss2.Q) / singularPressureLoss2.rho
-83: singularPressureLoss2.Q: (50/59): (1): singularPressureLoss2.Q = singularPressureLoss2.C1.Q
-82: singularPressureLoss2.rho: (56/74): (1): singularPressureLoss2.rho = singularPressureLoss2.pro_ph.d
-81: singularPressureLoss2.T: (55/73): (1): singularPressureLoss2.T = singularPressureLoss2.pro_ph.T
-80: singularPressureLoss2.Pm: (53/62): (1): singularPressureLoss2.Pm = 0.5 * (singularPressureLoss2.C1.P + singularPressureLoss2.C2.P)
-79: singularPressureLoss2.h: (49/58): (1): singularPressureLoss2.h = singularPressureLoss2.C1.h
-78: singularPressureLoss2.C1.P: (46/55): (1): singularPressureLoss2.C1.P - singularPressureLoss2.C2.P = singularPressureLoss2.deltaP
-77: singularPressureLoss2.C1.h_vol: (51/60): (1): singularPressureLoss2.h = ThermoSysPro.Functions.SmoothCond(singularPressureLoss2.Q, singularPressureLoss2.C1.h_vol, singularPressureLoss2.C2.h_vol, 1.0)
-76: singularPressureLoss2.C1.Q: (8/8): (1): singularPressureLoss1.C2.Q = singularPressureLoss2.C1.Q
-75: singularPressureLoss2.C1.h: (11/11): (1): singularPressureLoss1.C2.h = singularPressureLoss2.C1.h
-74: singularPressureLoss2.C1.a: (89/125): (1): singularPressureLoss2.C1.a = true
-73: singularPressureLoss2.C1.b: (10/10): (1): singularPressureLoss1.C2.b = singularPressureLoss2.C1.b
-72: singularPressureLoss2.C2.P: (19/19): (1): singularPressureLoss2.C2.P = sinkP1.C.P
-71: singularPressureLoss2.C2.h_vol: (24/24): (1): singularPressureLoss2.C2.h_vol = sinkP1.C.h_vol
-70: singularPressureLoss2.C2.Q: (47/56): (1): singularPressureLoss2.C2.Q = singularPressureLoss2.C1.Q
-69: singularPressureLoss2.C2.h: (48/57): (1): singularPressureLoss2.C2.h = singularPressureLoss2.C1.h
-68: singularPressureLoss2.C2.a: (21/21): (1): singularPressureLoss2.C2.a = sinkP1.C.a
-67: singularPressureLoss2.C2.b: (90/126): (1): singularPressureLoss2.C2.b = true
-66: singularPressureLoss2.pro_ph.T: (54/63): (10): singularPressureLoss2.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.Pm, singularPressureLoss2.h, singularPressureLoss2.mode, singularPressureLoss2.fluid)
-65: singularPressureLoss2.pro_ph.d: (54/64): (10): singularPressureLoss2.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.Pm, singularPressureLoss2.h, singularPressureLoss2.mode, singularPressureLoss2.fluid)
-64: singularPressureLoss2.pro_ph.u: (54/65): (10): singularPressureLoss2.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.Pm, singularPressureLoss2.h, singularPressureLoss2.mode, singularPressureLoss2.fluid)
-63: singularPressureLoss2.pro_ph.s: (54/66): (10): singularPressureLoss2.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.Pm, singularPressureLoss2.h, singularPressureLoss2.mode, singularPressureLoss2.fluid)
-62: singularPressureLoss2.pro_ph.cp: (54/67): (10): singularPressureLoss2.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.Pm, singularPressureLoss2.h, singularPressureLoss2.mode, singularPressureLoss2.fluid)
-61: singularPressureLoss2.pro_ph.ddhp: (54/68): (10): singularPressureLoss2.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.Pm, singularPressureLoss2.h, singularPressureLoss2.mode, singularPressureLoss2.fluid)
-60: singularPressureLoss2.pro_ph.ddph: (54/69): (10): singularPressureLoss2.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.Pm, singularPressureLoss2.h, singularPressureLoss2.mode, singularPressureLoss2.fluid)
-59: singularPressureLoss2.pro_ph.duph: (54/70): (10): singularPressureLoss2.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.Pm, singularPressureLoss2.h, singularPressureLoss2.mode, singularPressureLoss2.fluid)
-58: singularPressureLoss2.pro_ph.duhp: (54/71): (10): singularPressureLoss2.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.Pm, singularPressureLoss2.h, singularPressureLoss2.mode, singularPressureLoss2.fluid)
-57: singularPressureLoss2.pro_ph.x: (54/72): (10): singularPressureLoss2.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.Pm, singularPressureLoss2.h, singularPressureLoss2.mode, singularPressureLoss2.fluid)
-56: singularPressureLoss2.pro_pT.d: (57/75): (1): singularPressureLoss2.pro_pT.d = 0.0
-55: singularPressureLoss2.pro_pT.h: (58/76): (1): singularPressureLoss2.pro_pT.h = 0.0
-54: singularPressureLoss2.pro_pT.u: (59/77): (1): singularPressureLoss2.pro_pT.u = 0.0
-53: singularPressureLoss2.pro_pT.s: (60/78): (1): singularPressureLoss2.pro_pT.s = 0.0
-52: singularPressureLoss2.pro_pT.cp: (61/79): (1): singularPressureLoss2.pro_pT.cp = 0.0
-51: singularPressureLoss2.pro_pT.ddTp: (62/80): (1): singularPressureLoss2.pro_pT.ddTp = 0.0
-50: singularPressureLoss2.pro_pT.ddpT: (63/81): (1): singularPressureLoss2.pro_pT.ddpT = 0.0
-49: singularPressureLoss2.pro_pT.dupT: (64/82): (1): singularPressureLoss2.pro_pT.dupT = 0.0
-48: singularPressureLoss2.pro_pT.duTp: (65/83): (1): singularPressureLoss2.pro_pT.duTp = 0.0
-47: singularPressureLoss2.pro_pT.x: (66/84): (1): singularPressureLoss2.pro_pT.x = 0.0
-46: sourceP1.P: (71/89): (1): sourceP1.P = sourceP1.IPressure.signal
-45: sourceP1.Q: (68/86): (1): sourceP1.C.Q = sourceP1.Q
-44: sourceP1.T: (74/92): (1): sourceP1.T = sourceP1.ITemperature.signal
-43: sourceP1.h: (75/93): (1): sourceP1.h = ThermoSysPro.Properties.WaterSteam.IF97.SpecificEnthalpy_PT(sourceP1.P, sourceP1.T, 0)
-42: sourceP1.pro.T: (76/94): (10): sourceP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sourceP1.P, sourceP1.h, sourceP1.mode)
-41: sourceP1.pro.d: (76/95): (10): sourceP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sourceP1.P, sourceP1.h, sourceP1.mode)
-40: sourceP1.pro.u: (76/96): (10): sourceP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sourceP1.P, sourceP1.h, sourceP1.mode)
-39: sourceP1.pro.s: (76/97): (10): sourceP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sourceP1.P, sourceP1.h, sourceP1.mode)
-38: sourceP1.pro.cp: (76/98): (10): sourceP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sourceP1.P, sourceP1.h, sourceP1.mode)
-37: sourceP1.pro.ddhp: (76/99): (10): sourceP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sourceP1.P, sourceP1.h, sourceP1.mode)
-36: sourceP1.pro.ddph: (76/100): (10): sourceP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sourceP1.P, sourceP1.h, sourceP1.mode)
-35: sourceP1.pro.duph: (76/101): (10): sourceP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sourceP1.P, sourceP1.h, sourceP1.mode)
-34: sourceP1.pro.duhp: (76/102): (10): sourceP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sourceP1.P, sourceP1.h, sourceP1.mode)
-33: sourceP1.pro.x: (76/103): (10): sourceP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sourceP1.P, sourceP1.h, sourceP1.mode)
-32: sourceP1.IPressure.signal: (70/88): (1): sourceP1.IPressure.signal = sourceP1.P0
-31: sourceP1.ISpecificEnthalpy.signal: (73/91): (1): sourceP1.ISpecificEnthalpy.signal = sourceP1.h0
-30: sourceP1.C.P: (67/85): (1): sourceP1.C.P = sourceP1.P
-29: sourceP1.C.h_vol: (69/87): (1): sourceP1.C.h_vol = sourceP1.h
-28: sourceP1.C.Q: (14/14): (1): sourceP1.C.Q = singularPressureLoss1.C1.Q
-27: sourceP1.C.h: (17/17): (1): sourceP1.C.h = singularPressureLoss1.C1.h
-26: sourceP1.C.a: (15/15): (1): sourceP1.C.a = singularPressureLoss1.C1.a
-25: sourceP1.C.b: (91/127): (1): sourceP1.C.b = true
-24: sourceP1.ITemperature.signal: (72/90): (1): sourceP1.ITemperature.signal = sourceP1.T0
-23: sinkP1.P: (81/108): (1): sinkP1.P = sinkP1.IPressure.signal
-22: sinkP1.Q: (78/105): (1): sinkP1.C.Q = sinkP1.Q
-21: sinkP1.T: (84/111): (1): sinkP1.T = sinkP1.ITemperature.signal
-20: sinkP1.h: (85/112): (1): sinkP1.h = ThermoSysPro.Properties.WaterSteam.IF97.SpecificEnthalpy_PT(sinkP1.P, sinkP1.T, 0)
-19: sinkP1.pro.T: (86/113): (10): sinkP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sinkP1.P, sinkP1.h, sinkP1.mode)
-18: sinkP1.pro.d: (86/114): (10): sinkP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sinkP1.P, sinkP1.h, sinkP1.mode)
-17: sinkP1.pro.u: (86/115): (10): sinkP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sinkP1.P, sinkP1.h, sinkP1.mode)
-16: sinkP1.pro.s: (86/116): (10): sinkP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sinkP1.P, sinkP1.h, sinkP1.mode)
-15: sinkP1.pro.cp: (86/117): (10): sinkP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sinkP1.P, sinkP1.h, sinkP1.mode)
-14: sinkP1.pro.ddhp: (86/118): (10): sinkP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sinkP1.P, sinkP1.h, sinkP1.mode)
-13: sinkP1.pro.ddph: (86/119): (10): sinkP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sinkP1.P, sinkP1.h, sinkP1.mode)
-12: sinkP1.pro.duph: (86/120): (10): sinkP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sinkP1.P, sinkP1.h, sinkP1.mode)
-11: sinkP1.pro.duhp: (86/121): (10): sinkP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sinkP1.P, sinkP1.h, sinkP1.mode)
-10: sinkP1.pro.x: (86/122): (10): sinkP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sinkP1.P, sinkP1.h, sinkP1.mode)
-9: sinkP1.IPressure.signal: (80/107): (1): sinkP1.IPressure.signal = sinkP1.P0
-8: sinkP1.ISpecificEnthalpy.signal: (83/110): (1): sinkP1.ISpecificEnthalpy.signal = sinkP1.h0
-7: sinkP1.C.P: (77/104): (1): sinkP1.C.P = sinkP1.P
-6: sinkP1.C.h_vol: (79/106): (1): sinkP1.C.h_vol = sinkP1.h
-5: sinkP1.C.Q: (20/20): (1): singularPressureLoss2.C2.Q = sinkP1.C.Q
-4: sinkP1.C.h: (23/23): (1): singularPressureLoss2.C2.h = sinkP1.C.h
-3: sinkP1.C.a: (92/128): (1): sinkP1.C.a = true
-2: sinkP1.C.b: (22/22): (1): singularPressureLoss2.C2.b = sinkP1.C.b
-1: sinkP1.ITemperature.signal: (82/109): (1): sinkP1.ITemperature.signal = sinkP1.T0
-
-
-Variables of interest (2)
-========================================
-1: singularPressureLoss2.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
-2: singularPressureLoss1.Q:VARIABLE(start = 100.0 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
-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)"
...[truncated 7669 chars]...
ARIABLE(min = 1e-09 max = 9.999999999999999e+59 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real
-39: sourceP1.pro.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
-40: sourceP1.pro.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real
-41: sourceP1.pro.d:VARIABLE(min = 1e-09 max = 100000.0 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 = 100000.0 ) "Fluid pressure" type: Real
-47: singularPressureLoss2.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
-48: singularPressureLoss2.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real
-49: singularPressureLoss2.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real
-50: singularPressureLoss2.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real
-51: singularPressureLoss2.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real
-52: 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
-53: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
-54: singularPressureLoss2.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real
-55: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real
-56: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
-57: singularPressureLoss2.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
-58: singularPressureLoss2.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
-59: singularPressureLoss2.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
-60: singularPressureLoss2.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
-61: singularPressureLoss2.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
-62: 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
-63: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
-64: singularPressureLoss2.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real
-65: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
-66: singularPressureLoss2.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real
-67: singularPressureLoss2.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-68: singularPressureLoss2.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-69: 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
-70: 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
-71: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-72: 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
-73: singularPressureLoss2.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-74: singularPressureLoss2.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-75: 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
-76: 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
-77: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-78: 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
-79: singularPressureLoss2.h:VARIABLE(start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real
-80: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real
-81: singularPressureLoss2.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real
-82: singularPressureLoss2.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real
-83: singularPressureLoss2.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
-84: singularPressureLoss2.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real
-85: singularPressureLoss1.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
-86: singularPressureLoss1.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real
-87: singularPressureLoss1.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real
-88: singularPressureLoss1.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real
-89: singularPressureLoss1.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real
-90: 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
-91: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
-92: singularPressureLoss1.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real
-93: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real
-94: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
-95: singularPressureLoss1.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
-96: singularPressureLoss1.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
-97: singularPressureLoss1.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
-98: singularPressureLoss1.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
-99: singularPressureLoss1.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
-100: 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
-101: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
-102: singularPressureLoss1.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real
-103: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
-104: singularPressureLoss1.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real
-105: singularPressureLoss1.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-106: singularPressureLoss1.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-107: 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
-108: 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
-109: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-110: 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
-111: singularPressureLoss1.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-112: singularPressureLoss1.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-113: 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
-114: 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
-115: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-116: 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
-117: singularPressureLoss1.h:VARIABLE(start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real
-118: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real
-119: singularPressureLoss1.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real
-120: singularPressureLoss1.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real
-121: singularPressureLoss1.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
-122: singularPressureLoss1.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real
-123: sourceP1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Source pressure" type: Real
-124: sourceP1.T0:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Source temperature (active if option_temperature=1)" type: Real
-125: sourceP1.h0:VARIABLE(unit = "J/kg" ) "Source specific enthalpy (active if option_temperature=2)" type: Real
-126: sinkP1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Sink pressure" type: Real
-127: sinkP1.T0:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Sink temperature (active if option_temperature=1)" type: Real
-128: sinkP1.h0:VARIABLE(unit = "J/kg" ) "Sink specific enthalpy (active if option_temperature=2)" type: Real
-
-
-OrderedEquation (92, 128)
-========================================
-1/1 (1): singularPressureLoss1.Q = 0.0 [binding |0|0|0|0|]
-2/2 (1): sourceP1.P0 = 300000.0 [binding |0|0|0|0|]
-3/3 (1): sourceP1.T0 = 290.0 [binding |0|0|0|0|]
-4/4 (1): sourceP1.h0 = 100000.0 [binding |0|0|0|0|]
-5/5 (1): sinkP1.P0 = 100000.0 [binding |0|0|0|0|]
-6/6 (1): sinkP1.T0 = 290.0 [binding |0|0|0|0|]
-7/7 (1): sinkP1.h0 = 100000.0 [binding |0|0|0|0|]
-8/8 (1): singularPressureLoss1.C2.P = singularPressureLoss2.C1.P [dynamic |0|0|0|0|]
-9/9 (1): singularPressureLoss1.C2.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|]
-10/10 (1): singularPressureLoss1.C2.a = singularPressureLoss2.C1.a [dynamic |0|0|0|0|]
-11/11 (1): singularPressureLoss1.C2.b = singularPressureLoss2.C1.b [dynamic |0|0|0|0|]
-12/12 (1): singularPressureLoss1.C2.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|]
-13/13 (1): singularPressureLoss1.C2.h_vol = singularPressureLoss2.C1.h_vol [dynamic |0|0|0|0|]
-14/14 (1): sourceP1.C.P = singularPressureLoss1.C1.P [dynamic |0|0|0|0|]
-15/15 (1): sourceP1.C.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|]
-16/16 (1): sourceP1.C.a = singularPressureLoss1.C1.a [dynamic |0|0|0|0|]
-17/17 (1): sourceP1.C.b = singularPressureLoss1.C1.b [dynamic |0|0|0|0|]
-18/18 (1): sourceP1.C.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|]
-19/19 (1): sourceP1.C.h_vol = singularPressureLoss1.C1.h_vol [dynamic |0|0|0|0|]
-20/20 (1): singularPressureLoss2.C2.P = sinkP1.C.P [dynamic |0|0|0|0|]
-21/21 (1): singularPressureLoss2.C2.Q = sinkP1.C.Q [dynamic |0|0|0|0|]
-22/22 (1): singularPressureLoss2.C2.a = sinkP1.C.a [dynamic |0|0|0|0|]
-23/23 (1): singularPressureLoss2.C2.b = sinkP1.C.b [dynamic |0|0|0|0|]
-24/24 (1): singularPressureLoss2.C2.h = sinkP1.C.h [dynamic |0|0|0|0|]
-25/25 (1): singularPressureLoss2.C2.h_vol = sinkP1.C.h_vol [dynamic |0|0|0|0|]
-26/26 (1): singularPressureLoss1.C1.P - singularPressureLoss1.C2.P = singularPressureLoss1.deltaP [dynamic |0|0|0|0|]
-27/27 (1): singularPressureLoss1.C2.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|]
-28/28 (1): singularPressureLoss1.C2.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|]
-29/29 (1): singularPressureLoss1.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|]
-30/30 (1): singularPressureLoss1.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|]
-31/31 (1): singularPressureLoss1.h = ThermoSysPro.Functions.SmoothCond(singularPressureLoss1.Q, singularPressureLoss1.C1.h_vol, singularPressureLoss1.C2.h_vol, 1.0) [dynamic |0|0|0|0|]
-32/32 (1): singularPressureLoss1.deltaP = singularPressureLoss1.K * singularPressureLoss1.Q * abs(singularPressureLoss1.Q) / singularPressureLoss1.rho [dynamic |0|0|0|0|]
-33/33 (1): singularPressureLoss1.Pm = 0.5 * (singularPressureLoss1.C1.P + singularPressureLoss1.C2.P) [dynamic |0|0|0|0|]
-34/34 (10): singularPressureLoss1.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss1.Pm, singularPressureLoss1.h, singularPressureLoss1.mode, singularPressureLoss1.fluid) [dynamic |0|0|0|0|]
-35/44 (1): singularPressureLoss1.T = singularPressureLoss1.pro_ph.T [dynamic |0|0|0|0|]
-36/45 (1): singularPressureLoss1.rho = singularPressureLoss1.pro_ph.d [dynamic |0|0|0|0|]
-37/46 (1): singularPressureLoss1.pro_pT.d = 0.0 [dynamic |0|0|0|0|]
-38/47 (1): singularPressureLoss1.pro_pT.h = 0.0 [dynamic |0|0|0|0|]
-39/48 (1): singularPressureLoss1.pro_pT.u = 0.0 [dynamic |0|0|0|0|]
-40/49 (1): singularPressureLoss1.pro_pT.s = 0.0 [dynamic |0|0|0|0|]
-41/50 (1): singularPressureLoss1.pro_pT.cp = 0.0 [dynamic |0|0|0|0|]
-42/51 (1): singularPressureLoss1.pro_pT.ddTp = 0.0 [dynamic |0|0|0|0|]
-43/52 (1): singularPressureLoss1.pro_pT.ddpT = 0.0 [dynamic |0|0|0|0|]
-44/53 (1): singularPressureLoss1.pro_pT.dupT = 0.0 [dynamic |0|0|0|0|]
-45/54 (1): singularPressureLoss1.pro_pT.duTp = 0.0 [dynamic |0|0|0|0|]
-46/55 (1): singularPressureLoss1.pro_pT.x = 0.0 [dynamic |0|0|0|0|]
-47/56 (1): singularPressureLoss2.C1.P - singularPressureLoss2.C2.P = singularPressureLoss2.deltaP [dynamic |0|0|0|0|]
-48/57 (1): singularPressureLoss2.C2.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|]
-49/58 (1): singularPressureLoss2.C2.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|]
-50/59 (1): singularPressureLoss2.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|]
-51/60 (1): singularPressureLoss2.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|]
-52/61 (1): singularPressureLoss2.h = ThermoSysPro.Functions.SmoothCond(singularPressureLoss2.Q, singularPressureLoss2.C1.h_vol, singularPressureLoss2.C2.h_vol, 1.0) [dynamic |0|0|0|0|]
-53/62 (1): singularPressureLoss2.deltaP = singularPressureLoss2.K * singularPressureLoss2.Q * abs(singularPressureLoss2.Q) / singularPressureLoss2.rho [dynamic |0|0|0|0|]
-54/63 (1): singularPressureLoss2.Pm = 0.5 * (singularPressureLoss2.C1.P + singularPressureLoss2.C2.P) [dynamic |0|0|0|0|]
-55/64 (10): singularPressureLoss2.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.Pm, singularPressureLoss2.h, singularPressureLoss2.mode, singularPressureLoss2.fluid) [dynamic |0|0|0|0|]
-56/74 (1): singularPressureLoss2.T = singularPressureLoss2.pro_ph.T [dynamic |0|0|0|0|]
-57/75 (1): singularPressureLoss2.rho = singularPressureLoss2.pro_ph.d [dynamic |0|0|0|0|]
-58/76 (1): singularPressureLoss2.pro_pT.d = 0.0 [dynamic |0|0|0|0|]
-59/77 (1): singularPressureLoss2.pro_pT.h = 0.0 [dynamic |0|0|0|0|]
-60/78 (1): singularPressureLoss2.pro_pT.u = 0.0 [dynamic |0|0|0|0|]
-61/79 (1): singularPressureLoss2.pro_pT.s = 0.0 [dynamic |0|0|0|0|]
-62/80 (1): singularPressureLoss2.pro_pT.cp = 0.0 [dynamic |0|0|0|0|]
-63/81 (1): singularPressureLoss2.pro_pT.ddTp = 0.0 [dynamic |0|0|0|0|]
-64/82 (1): singularPressureLoss2.pro_pT.ddpT = 0.0 [dynamic |0|0|0|0|]
-65/83 (1): singularPressureLoss2.pro_pT.dupT = 0.0 [dynamic |0|0|0|0|]
-66/84 (1): singularPressureLoss2.pro_pT.duTp = 0.0 [dynamic |0|0|0|0|]
-67/85 (1): singularPressureLoss2.pro_pT.x = 0.0 [dynamic |0|0|0|0|]
-68/86 (1): sourceP1.C.P = sourceP1.P [dynamic |0|0|0|0|]
-69/87 (1): sourceP1.C.Q = sourceP1.Q [dynamic |0|0|0|0|]
-70/88 (1): sourceP1.C.h_vol = sourceP1.h [dynamic |0|0|0|0|]
-71/89 (1): sourceP1.IPressure.signal = sourceP1.P0 [dynamic |0|0|0|0|]
-72/90 (1): sourceP1.P = sourceP1.IPressure.signal [dynamic |0|0|0|0|]
-73/91 (1): sourceP1.ITemperature.signal = sourceP1.T0 [dynamic |0|0|0|0|]
-74/92 (1): sourceP1.ISpecificEnthalpy.signal = sourceP1.h0 [dynamic |0|0|0|0|]
-75/93 (1): sourceP1.T = sourceP1.ITemperature.signal [dynamic |0|0|0|0|]
-76/94 (1): sourceP1.h = ThermoSysPro.Properties.WaterSteam.IF97.SpecificEnthalpy_PT(sourceP1.P, sourceP1.T, 0) [dynamic |0|0|0|0|]
-77/95 (10): sourceP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sourceP1.P, sourceP1.h, sourceP1.mode) [dynamic |0|0|0|0|]
-78/105 (1): sinkP1.C.P = sinkP1.P [dynamic |0|0|0|0|]
-79/106 (1): sinkP1.C.Q = sinkP1.Q [dynamic |0|0|0|0|]
-80/107 (1): sinkP1.C.h_vol = sinkP1.h [dynamic |0|0|0|0|]
-81/108 (1): sinkP1.P = sinkP1.IPressure.signal [dynamic |0|0|0|0|]
-82/109 (1): sinkP1.ITemperature.signal = sinkP1.T0 [dynamic |0|0|0|0|]
-83/110 (1): sinkP1.ISpecificEnthalpy.signal = sinkP1.h0 [dynamic |0|0|0|0|]
-84/111 (1): sinkP1.T = sinkP1.ITemperature.signal [dynamic |0|0|0|0|]
-85/112 (1): sinkP1.h = ThermoSysPro.Properties.WaterSteam.IF97.SpecificEnthalpy_PT(sinkP1.P, sinkP1.T, 0) [dynamic |0|0|0|0|]
-86/113 (10): sinkP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sinkP1.P, sinkP1.h, sinkP1.mode) [dynamic |0|0|0|0|]
-87/123 (1): singularPressureLoss1.C1.a = true [binding |0|0|0|0|]
-88/124 (1): singularPressureLoss1.C2.b = true [binding |0|0|0|0|]
-89/125 (1): singularPressureLoss2.C1.a = true [binding |0|0|0|0|]
-90/126 (1): singularPressureLoss2.C2.b = true [binding |0|0|0|0|]
-91/127 (1): sourceP1.C.b = true [binding |0|0|0|0|]
-92/128 (1): sinkP1.C.a = true [binding |0|0|0|0|]
-
-Matching
-========================================
-128 variables and equations
-var 1 is solved in eqn 109
-var 2 is solved in eqn 23
-var 3 is solved in eqn 128
-var 4 is solved in eqn 24
-var 5 is solved in eqn 21
-var 6 is solved in eqn 25
-var 7 is solved in eqn 105
-var 8 is solved in eqn 110
-var 9 is solved in eqn 108
-var 10 is solved in eqn 122
-var 11 is solved in eqn 121
-var 12 is solved in eqn 120
-var 13 is solved in eqn 119
-var 14 is solved in eqn 118
-var 15 is solved in eqn 117
-var 16 is solved in eqn 116
-var 17 is solved in eqn 115
-var 18 is solved in eqn 114
-var 19 is solved in eqn 113
-var 20 is solved in eqn 107
-var 21 is solved in eqn 111
-var 22 is solved in eqn 106
-var 23 is solved in eqn 112
-var 24 is solved in eqn 91
-var 25 is solved in eqn 127
-var 26 is solved in eqn 16
-var 27 is solved in eqn 18
-var 28 is solved in eqn 15
-var 29 is solved in eqn 88
-var 30 is solved in eqn 86
-var 31 is solved in eqn 92
-var 32 is solved in eqn 89
-var 33 is solved in eqn 104
-var 34 is solved in eqn 103
-var 35 is solved in eqn 102
-var 36 is solved in eqn 101
-var 37 is solved in eqn 100
-var 38 is solved in eqn 99
-var 39 is solved in eqn 98
-var 40 is solved in eqn 97
-var 41 is solved in eqn 96
-var 42 is solved in eqn 95
-var 43 is solved in eqn 94
-var 44 is solved in eqn 93
-var 45 is solved in eqn 87
-var 46 is solved in eqn 90
-var 47 is solved in eqn 85
-var 48 is solved in eqn 84
-var 49 is solved in eqn 83
-var 50 is solved in eqn 82
-var 51 is solved in eqn 81
-var 52 is solved in eqn 80
-var 53 is solved in eqn 79
-var 54 is solved in eqn 78
-var 55 is solved in eqn 77
-var 56 is solved in eqn 76
-var 57 is solved in eqn 73
-var 58 is solved in eqn 72
-var 59 is solved in eqn 71
-var 60 is solved in eqn 70
-var 61 is solved in eqn 69
-var 62 is solved in eqn 68
-var 63 is solved in eqn 67
-var 64 is solved in eqn 66
-var 65 is solved in eqn 75
-var 66 is solved in eqn 64
-var 67 is solved in eqn 126
-var 68 is solved in eqn 22
-var 69 is solved in eqn 58
-var 70 is solved in eqn 57
-var 71 is solved in eqn 61
-var 72 is solved in eqn 20
-var 73 is solved in eqn 11
-var 74 is solved in eqn 125
-var 75 is solved in eqn 59
-var 76 is solved in eqn 9
-var 77 is solved in eqn 13
-var 78 is solved in eqn 8
-var 79 is solved in eqn 65
-var 80 is solved in eqn 63
-var 81 is solved in eqn 74
-var 82 is solved in eqn 62
-var 83 is solved in eqn 60
-var 84 is solved in eqn 56
-var 85 is solved in eqn 55
-var 86 is solved in eqn 54
-var 87 is solved in eqn 53
-var 88 is solved in eqn 52
-var 89 is solved in eqn 51
-var 90 is solved in eqn 50
-var 91 is solved in eqn 49
-var 92 is solved in eqn 48
-var 93 is solved in eqn 47
-var 94 is solved in eqn 46
-var 95 is solved in eqn 43
-var 96 is solved in eqn 42
-var 97 is solved in eqn 41
-var 98 is solved in eqn 40
-var 99 is solved in eqn 39
-var 100 is solved in eqn 38
-var 101 is solved in eqn 37
-var 102 is solved in eqn 36
-var 103 is solved in eqn 45
-var 104 is solved in eqn 34
-var 105 is solved in eqn 124
-var 106 is solved in eqn 10
-var 107 is solved in eqn 12
-var 108 is solved in eqn 27
-var 109 is solved in eqn 31
-var 110 is solved in eqn 33
-var 111 is solved in eqn 17
-var 112 is solved in eqn 123
-var 113 is solved in eqn 28
-var 114 is solved in eqn 30
-var 115 is solved in eqn 19
-var 116 is solved in eqn 14
-var 117 is solved in eqn 29
-var 118 is solved in eqn 35
-var 119 is solved in eqn 44
-var 120 is solved in eqn 32
-var 121 is solved in eqn 1
-var 122 is solved in eqn 26
-var 123 is solved in eqn 2
-var 124 is solved in eqn 3
-var 125 is solved in eqn 4
-var 126 is solved in eqn 5
-var 127 is solved in eqn 6
-var 128 is solved in eqn 7
-
-Standard BLT of the original model:(128)
-============================================================
-
-128: sinkP1.h0: (7/7): (1): sinkP1.h0 = 100000.0
-127: sinkP1.T0: (6/6): (1): sinkP1.T0 = 290.0
-126: sinkP1.P0: (5/5): (1): sinkP1.P0 = 100000.0
-125: sourceP1.h0: (4/4): (1): sourceP1.h0 = 100000.0
-124: sourceP1.T0: (3/3): (1): sourceP1.T0 = 290.0
-123: sourceP1.P0: (2/2): (1): sourceP1.P0 = 300000.0
-122: singularPressureLoss1.deltaP: (26/26): (1): singularPressureLoss1.C1.P - singularPressureLoss1.C2.P = singularPressureLoss1.deltaP
-121: singularPressureLoss1.Q: (1/1): (1): singularPressureLoss1.Q = 0.0
-120: singularPressureLoss1.rho: (32/32): (1): singularPressureLoss1.deltaP = singularPressureLoss1.K * singularPressureLoss1.Q * abs(singularPressureLoss1.Q) / singularPressureLoss1.rho
-119: singularPressureLoss1.T: (35/44): (1): singularPressureLoss1.T = singularPressureLoss1.pro_ph.T
-118: singularPressureLoss1.Pm: (34/35): (10): singularPressureLoss1.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss1.Pm, singularPressureLoss1.h, singularPressureLoss1.mode, singularPressureLoss1.fluid)
-117: singularPressureLoss1.h: (29/29): (1): singularPressureLoss1.h = singularPressureLoss1.C1.h
-116: singularPressureLoss1.C1.P: (14/14): (1): sourceP1.C.P = singularPressureLoss1.C1.P
-115: singularPressureLoss1.C1.h_vol: (19/19): (1): sourceP1.C.h_vol = singularPressureLoss1.C1.h_vol
-114: singularPressureLoss1.C1.Q: (30/30): (1): singularPressureLoss1.Q = singularPressureLoss1.C1.Q
-113: singularPressureLoss1.C1.h: (28/28): (1): singularPressureLoss1.C2.h = singularPressureLoss1.C1.h
-112: singularPressureLoss1.C1.a: (87/123): (1): singularPressureLoss1.C1.a = true
-111: singularPressureLoss1.C1.b: (17/17): (1): sourceP1.C.b = singularPressureLoss1.C1.b
-110: singularPressureLoss1.C2.P: (33/33): (1): singularPressureLoss1.Pm = 0.5 * (singularPressureLoss1.C1.P + singularPressureLoss1.C2.P)
-109: singularPressureLoss1.C2.h_vol: (31/31): (1): singularPressureLoss1.h = ThermoSysPro.Functions.SmoothCond(singularPressureLoss1.Q, singularPressureLoss1.C1.h_vol, singularPressureLoss1.C2.h_vol, 1.0)
-108: singularPressureLoss1.C2.Q: (27/27): (1): singularPressureLoss1.C2.Q = singularPressureLoss1.C1.Q
-107: singularPressureLoss1.C2.h: (12/12): (1): singularPressureLoss1.C2.h = singularPressureLoss2.C1.h
-106: singularPressureLoss1.C2.a: (10/10): (1): singularPressureLoss1.C2.a = singularPressureLoss2.C1.a
-105: singularPressureLoss1.C2.b: (88/124): (1): singularPressureLoss1.C2.b = true
-104: singularPressureLoss1.pro_ph.T: (34/34): (10): singularPressureLoss1.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss1.Pm, singularPressureLoss1.h, singularPressureLoss1.mode, singularPressureLoss1.fluid)
-103: singularPressureLoss1.pro_ph.d: (36/45): (1): singularPressureLoss1.rho = singularPressureLoss1.pro_ph.d
-102: singularPressureLoss1.pro_ph.u: (34/36): (10): singularPressureLoss1.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss1.Pm, singularPressureLoss1.h, singularPressureLoss1.mode, singularPressureLoss1.fluid)
-101: singularPressureLoss1.pro_ph.s: (34/37): (10): singularPressureLoss1.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss1.Pm, singularPressureLoss1.h, singularPressureLoss1.mode, singularPressureLoss1.fluid)
-100: singularPressureLoss1.pro_ph.cp: (34/38): (10): singularPressureLoss1.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss1.Pm, singularPressureLoss1.h, singularPressureLoss1.mode, singularPressureLoss1.fluid)
-99: singularPressureLoss1.pro_ph.ddhp: (34/39): (10): singularPressureLoss1.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss1.Pm, singularPressureLoss1.h, singularPressureLoss1.mode, singularPressureLoss1.fluid)
-98: singularPressureLoss1.pro_ph.ddph: (34/40): (10): singularPressureLoss1.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss1.Pm, singularPressureLoss1.h, singularPressureLoss1.mode, singularPressureLoss1.fluid)
-97: singularPressureLoss1.pro_ph.duph: (34/41): (10): singularPressureLoss1.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss1.Pm, singularPressureLoss1.h, singularPressureLoss1.mode, singularPressureLoss1.fluid)
-96: singularPressureLoss1.pro_ph.duhp: (34/42): (10): singularPressureLoss1.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss1.Pm, singularPressureLoss1.h, singularPressureLoss1.mode, singularPressureLoss1.fluid)
-95: singularPressureLoss1.pro_ph.x: (34/43): (10): singularPressureLoss1.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss1.Pm, singularPressureLoss1.h, singularPressureLoss1.mode, singularPressureLoss1.fluid)
-94: singularPressureLoss1.pro_pT.d: (37/46): (1): singularPressureLoss1.pro_pT.d = 0.0
-93: singularPressureLoss1.pro_pT.h: (38/47): (1): singularPressureLoss1.pro_pT.h = 0.0
-92: singularPressureLoss1.pro_pT.u: (39/48): (1): singularPressureLoss1.pro_pT.u = 0.0
-91: singularPressureLoss1.pro_pT.s: (40/49): (1): singularPressureLoss1.pro_pT.s = 0.0
-90: singularPressureLoss1.pro_pT.cp: (41/50): (1): singularPressureLoss1.pro_pT.cp = 0.0
-89: singularPressureLoss1.pro_pT.ddTp: (42/51): (1): singularPressureLoss1.pro_pT.ddTp = 0.0
-88: singularPressureLoss1.pro_pT.ddpT: (43/52): (1): singularPressureLoss1.pro_pT.ddpT = 0.0
-87: singularPressureLoss1.pro_pT.dupT: (44/53): (1): singularPressureLoss1.pro_pT.dupT = 0.0
-86: singularPressureLoss1.pro_pT.duTp: (45/54): (1): singularPressureLoss1.pro_pT.duTp = 0.0
-85: singularPressureLoss1.pro_pT.x: (46/55): (1): singularPressureLoss1.pro_pT.x = 0.0
-84: singularPressureLoss2.deltaP: (47/56): (1): singularPressureLoss2.C1.P - singularPressureLoss2.C2.P = singularPressureLoss2.deltaP
-83: singularPressureLoss2.Q: (51/60): (1): singularPressureLoss2.Q = singularPressureLoss2.C1.Q
-82: singularPressureLoss2.rho: (53/62): (1): singularPressureLoss2.deltaP = singularPressureLoss2.K * singularPressureLoss2.Q * abs(singularPressureLoss2.Q) / singularPressureLoss2.rho
-81: singularPressureLoss2.T: (56/74): (1): singularPressureLoss2.T = singularPressureLoss2.pro_ph.T
-80: singularPressureLoss2.Pm: (54/63): (1): singularPressureLoss2.Pm = 0.5 * (singularPressureLoss2.C1.P + singularPressureLoss2.C2.P)
-79: singularPressureLoss2.h: (55/65): (10): singularPressureLoss2.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.Pm, singularPressureLoss2.h, singularPressureLoss2.mode, singularPressureLoss2.fluid)
-78: singularPressureLoss2.C1.P: (8/8): (1): singularPressureLoss1.C2.P = singularPressureLoss2.C1.P
-77: singularPressureLoss2.C1.h_vol: (13/13): (1): singularPressureLoss1.C2.h_vol = singularPressureLoss2.C1.h_vol
-76: singularPressureLoss2.C1.Q: (9/9): (1): singularPressureLoss1.C2.Q = singularPressureLoss2.C1.Q
-75: singularPressureLoss2.C1.h: (50/59): (1): singularPressureLoss2.h = singularPressureLoss2.C1.h
-74: singularPressureLoss2.C1.a: (89/125): (1): singularPressureLoss2.C1.a = true
-73: singularPressureLoss2.C1.b: (11/11): (1): singularPressureLoss1.C2.b = singularPressureLoss2.C1.b
-72: singularPressureLoss2.C2.P: (20/20): (1): singularPressureLoss2.C2.P = sinkP1.C.P
-71: singularPressureLoss2.C2.h_vol: (52/61): (1): singularPressureLoss2.h = ThermoSysPro.Functions.SmoothCond(singularPressureLoss2.Q, singularPressureLoss2.C1.h_vol, singularPressureLoss2.C2.h_vol, 1.0)
-70: singularPressureLoss2.C2.Q: (48/57): (1): singularPressureLoss2.C2.Q = singularPressureLoss2.C1.Q
-69: singularPressureLoss2.C2.h: (49/58): (1): singularPressureLoss2.C2.h = singularPressureLoss2.C1.h
-68: singularPressureLoss2.C2.a: (22/22): (1): singularPressureLoss2.C2.a = sinkP1.C.a
-67: singularPressureLoss2.C2.b: (90/126): (1): singularPressureLoss2.C2.b = true
-66: singularPressureLoss2.pro_ph.T: (55/64): (10): singularPressureLoss2.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.Pm, singularPressureLoss2.h, singularPressureLoss2.mode, singularPressureLoss2.fluid)
-65: singularPressureLoss2.pro_ph.d: (57/75): (1): singularPressureLoss2.rho = singularPressureLoss2.pro_ph.d
-64: singularPressureLoss2.pro_ph.u: (55/66): (10): singularPressureLoss2.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.Pm, singularPressureLoss2.h, singularPressureLoss2.mode, singularPressureLoss2.fluid)
-63: singularPressureLoss2.pro_ph.s: (55/67): (10): singularPressureLoss2.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.Pm, singularPressureLoss2.h, singularPressureLoss2.mode, singularPressureLoss2.fluid)
-62: singularPressureLoss2.pro_ph.cp: (55/68): (10): singularPressureLoss2.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.Pm, singularPressureLoss2.h, singularPressureLoss2.mode, singularPressureLoss2.fluid)
-61: singularPressureLoss2.pro_ph.ddhp: (55/69): (10): singularPressureLoss2.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.Pm, singularPressureLoss2.h, singularPressureLoss2.mode, singularPressureLoss2.fluid)
-60: singularPressureLoss2.pro_ph.ddph: (55/70): (10): singularPressureLoss2.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.Pm, singularPressureLoss2.h, singularPressureLoss2.mode, singularPressureLoss2.fluid)
-59: singularPressureLoss2.pro_ph.duph: (55/71): (10): singularPressureLoss2.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.Pm, singularPressureLoss2.h, singularPressureLoss2.mode, singularPressureLoss2.fluid)
-58: singularPressureLoss2.pro_ph.duhp: (55/72): (10): singularPressureLoss2.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.Pm, singularPressureLoss2.h, singularPressureLoss2.mode, singularPressureLoss2.fluid)
-57: singularPressureLoss2.pro_ph.x: (55/73): (10): singularPressureLoss2.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.Pm, singularPressureLoss2.h, singularPressureLoss2.mode, singularPressureLoss2.fluid)
-56: singularPressureLoss2.pro_pT.d: (58/76): (1): singularPressureLoss2.pro_pT.d = 0.0
-55: singularPressureLoss2.pro_pT.h: (59/77): (1): singularPressureLoss2.pro_pT.h = 0.0
-54: singularPressureLoss2.pro_pT.u: (60/78): (1): singularPressureLoss2.pro_pT.u = 0.0
-53: singularPressureLoss2.pro_pT.s: (61/79): (1): singularPressureLoss2.pro_pT.s = 0.0
-52: singularPressureLoss2.pro_pT.cp: (62/80): (1): singularPressureLoss2.pro_pT.cp = 0.0
-51: singularPressureLoss2.pro_pT.ddTp: (63/81): (1): singularPressureLoss2.pro_pT.ddTp = 0.0
-50: singularPressureLoss2.pro_pT.ddpT: (64/82): (1): singularPressureLoss2.pro_pT.ddpT = 0.0
-49: singularPressureLoss2.pro_pT.dupT: (65/83): (1): singularPressureLoss2.pro_pT.dupT = 0.0
-48: singularPressureLoss2.pro_pT.duTp: (66/84): (1): singularPressureLoss2.pro_pT.duTp = 0.0
-47: singularPressureLoss2.pro_pT.x: (67/85): (1): singularPressureLoss2.pro_pT.x = 0.0
-46: sourceP1.P: (72/90): (1): sourceP1.P = sourceP1.IPressure.signal
-45: sourceP1.Q: (69/87): (1): sourceP1.C.Q = sourceP1.Q
-44: sourceP1.T: (75/93): (1): sourceP1.T = sourceP1.ITemperature.signal
-43: sourceP1.h: (76/94): (1): sourceP1.h = ThermoSysPro.Properties.WaterSteam.IF97.SpecificEnthalpy_PT(sourceP1.P, sourceP1.T, 0)
-42: sourceP1.pro.T: (77/95): (10): sourceP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sourceP1.P, sourceP1.h, sourceP1.mode)
-41: sourceP1.pro.d: (77/96): (10): sourceP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sourceP1.P, sourceP1.h, sourceP1.mode)
-40: sourceP1.pro.u: (77/97): (10): sourceP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sourceP1.P, sourceP1.h, sourceP1.mode)
-39: sourceP1.pro.s: (77/98): (10): sourceP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sourceP1.P, sourceP1.h, sourceP1.mode)
-38: sourceP1.pro.cp: (77/99): (10): sourceP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sourceP1.P, sourceP1.h, sourceP1.mode)
-37: sourceP1.pro.ddhp: (77/100): (10): sourceP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sourceP1.P, sourceP1.h, sourceP1.mode)
-36: sourceP1.pro.ddph: (77/101): (10): sourceP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sourceP1.P, sourceP1.h, sourceP1.mode)
-35: sourceP1.pro.duph: (77/102): (10): sourceP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sourceP1.P, sourceP1.h, sourceP1.mode)
-34: sourceP1.pro.duhp: (77/103): (10): sourceP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sourceP1.P, sourceP1.h, sourceP1.mode)
-33: sourceP1.pro.x: (77/104): (10): sourceP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sourceP1.P, sourceP1.h, sourceP1.mode)
-32: sourceP1.IPressure.signal: (71/89): (1): sourceP1.IPressure.signal = sourceP1.P0
-31: sourceP1.ISpecificEnthalpy.signal: (74/92): (1): sourceP1.ISpecificEnthalpy.signal = sourceP1.h0
-30: sourceP1.C.P: (68/86): (1): sourceP1.C.P = sourceP1.P
-29: sourceP1.C.h_vol: (70/88): (1): sourceP1.C.h_vol = sourceP1.h
-28: sourceP1.C.Q: (15/15): (1): sourceP1.C.Q = singularPressureLoss1.C1.Q
-27: sourceP1.C.h: (18/18): (1): sourceP1.C.h = singularPressureLoss1.C1.h
-26: sourceP1.C.a: (16/16): (1): sourceP1.C.a = singularPressureLoss1.C1.a
-25: sourceP1.C.b: (91/127): (1): sourceP1.C.b = true
-24: sourceP1.ITemperature.signal: (73/91): (1): sourceP1.ITemperature.signal = sourceP1.T0
-23: sinkP1.P: (85/112): (1): sinkP1.h = ThermoSysPro.Properties.WaterSteam.IF97.SpecificEnthalpy_PT(sinkP1.P, sinkP1.T, 0)
-22: sinkP1.Q: (79/106): (1): sinkP1.C.Q = sinkP1.Q
-21: sinkP1.T: (84/111): (1): sinkP1.T = sinkP1.ITemperature.signal
-20: sinkP1.h: (80/107): (1): sinkP1.C.h_vol = sinkP1.h
-19: sinkP1.pro.T: (86/113): (10): sinkP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sinkP1.P, sinkP1.h, sinkP1.mode)
-18: sinkP1.pro.d: (86/114): (10): sinkP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sinkP1.P, sinkP1.h, sinkP1.mode)
-17: sinkP1.pro.u: (86/115): (10): sinkP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sinkP1.P, sinkP1.h, sinkP1.mode)
-16: sinkP1.pro.s: (86/116): (10): sinkP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sinkP1.P, sinkP1.h, sinkP1.mode)
-15: sinkP1.pro.cp: (86/117): (10): sinkP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sinkP1.P, sinkP1.h, sinkP1.mode)
-14: sinkP1.pro.ddhp: (86/118): (10): sinkP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sinkP1.P, sinkP1.h, sinkP1.mode)
-13: sinkP1.pro.ddph: (86/119): (10): sinkP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sinkP1.P, sinkP1.h, sinkP1.mode)
-12: sinkP1.pro.duph: (86/120): (10): sinkP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sinkP1.P, sinkP1.h, sinkP1.mode)
-11: sinkP1.pro.duhp: (86/121): (10): sinkP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sinkP1.P, sinkP1.h, sinkP1.mode)
-10: sinkP1.pro.x: (86/122): (10): sinkP1.pro = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sinkP1.P, sinkP1.h, sinkP1.mode)
-9: sinkP1.IPressure.signal: (81/108): (1): sinkP1.P = sinkP1.IPressure.signal
-8: sinkP1.ISpecificEnthalpy.signal: (83/110): (1): sinkP1.ISpecificEnthalpy.signal = sinkP1.h0
-7: sinkP1.C.P: (78/105): (1): sinkP1.C.P = sinkP1.P
-6: sinkP1.C.h_vol: (25/25): (1): singularPressureLoss2.C2.h_vol = sinkP1.C.h_vol
-5: sinkP1.C.Q: (21/21): (1): singularPressureLoss2.C2.Q = sinkP1.C.Q
-4: sinkP1.C.h: (24/24): (1): singularPressureLoss2.C2.h = sinkP1.C.h
-3: sinkP1.C.a: (92/128): (1): sinkP1.C.a = true
-2: sinkP1.C.b: (23/23): (1): singularPressureLoss2.C2.b = sinkP1.C.b
-1: sinkP1.ITemperature.signal: (82/109): (1): sinkP1.ITemperature.signal = sinkP1.T0
-
-
-Variables of interest (2)
-========================================
-1: singularPressureLoss2.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
-2: singularPressureLoss1.Q:VARIABLE(start = 100.0 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
-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
-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:(13)
-============================================================
-
-3: sinkP1.C.a: (92/128): (1): sinkP1.C.a = true
-25: sourceP1.C.b: (91/127): (1): sourceP1.C.b = true
-67: singularPressureLoss2.C2.b: (90/126): (1): singularPressureLoss2.C2.b = true
-74: singularPressureLoss2.C1.a: (89/125): (1): singularPressureLoss2.C1.a = true
-105: singularPressureLoss1.C2.b: (88/124): (1): singularPressureLoss1.C2.b = true
-112: singularPressureLoss1.C1.a: (87/123): (1): singularPressureLoss1.C1.a = true
-128: sinkP1.h0: (7/7): (1): sinkP1.h0 = 100000.0
-127: sinkP1.T0: (6/6): (1): sinkP1.T0 = 290.0
-126: sinkP1.P0: (5/5): (1): sinkP1.P0 = 100000.0
-125: sourceP1.h0: (4/4): (1): sourceP1.h0 = 100000.0
-124: sourceP1.T0: (3/3): (1): sourceP1.T0 = 290.0
-123: sourceP1.P0: (2/2): (1): sourceP1.P0 = 300000.0
-121: singularPressureLoss1.Q: (1/1): (1): singularPressureLoss1.Q = 0.0
-
-
-E-BLT: equations that compute the variables of interest:(1)
-============================================================
-
-83: singularPressureLoss2.Q: (51/60): (1): singularPressureLoss2.Q = singularPressureLoss2.C1.Q
-
-
-Extracting SET-C and SET-S from E-BLT
-Procedure is applied on each equation in the E-BLT
-==========================================================================
->>>83: singularPressureLoss2.Q: (51/60): (1): singularPressureLoss2.Q = singularPressureLoss2.C1.Q
-76: singularPressureLoss2.C1.Q: (9/9): (1): singularPressureLoss1.C2.Q = singularPressureLoss2.C1.Q
-108: singularPressureLoss1.C2.Q: (27/27): (1): singularPressureLoss1.C2.Q = singularPressureLoss1.C1.Q
-114: singularPressureLoss1.C1.Q: (30/30): (1): singularPressureLoss1.Q = singularPressureLoss1.C1.Q
-Procedure success
-
-Extraction procedure is successfully completed in iteration count: 2
-==========================================================================
-
-Final set of equations after extraction algorithm
-==========================================================================
-SET_C: {51}
-SET_S: {30, 27, 9}
-
-
-SET_C (1, 1)
-========================================
-1/1 (1): singularPressureLoss2.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|]
-
-
-SET_S (3, 3)
-========================================
-1/1 (1): singularPressureLoss1.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|]
-2/2 (1): singularPressureLoss1.C2.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|]
-3/3 (1): singularPressureLoss1.C2.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|]
-
-
-Unknown variables in SET_S (3)
-========================================
-
-1: singularPressureLoss1.C1.Q type: Real
-2: singularPressureLoss1.C2.Q type: Real
-3: singularPressureLoss2.C1.Q type: Real
-
-
-
-Automatic Verification Steps of DataReconciliation Algorithm
-==========================================================================
-
-knownVariables:{83, 121} (2)
-========================================
-1: singularPressureLoss2.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
-2: singularPressureLoss1.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
-
--SET_C:{51}
--SET_S:{30, 27, 9}
-
-Condition-1 "SET_C and SET_S must not have no equations in common"
-==========================================================================
--Passed
-
-Condition-2 "All variables of interest must be involved in SET_C or SET_S"
-==========================================================================
--Passed
-
--SET_C has known variables:{83} (1)
-========================================
-1: singularPressureLoss2.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
-
-
--SET_S has known variables:{121} (1)
-========================================
-1: singularPressureLoss1.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
-
-Condition-3 "SET_C equations must be strictly less than Variable of Interest"
-==========================================================================
--Passed
--SET_C contains:1 equations < 2 known variables
-
-Condition-4 "SET_S should contain all intermediate variables involved in SET_C"
-==========================================================================
-
--SET_C has intermediate variables:{76} (1)
-========================================
-1: 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
-
-
--SET_S has intermediate variables involved in SET_C:{76} (1)
-========================================
-1: 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
-
--Passed
-
-Condition-5 "SET_S should be square"
-==========================================================================
--Passed
-Set_S has 3 equations and 3 variables
-
-record SimulationResult
-resultFile = "econcile",
-simulationOptions = "startTime = 0.0, stopTime = 1.0, numberOfIntervals = 500, tolerance = 1e-06, method = 'dassl', fileNamePrefix = 'NewDataReconciliationSimpleTests.TSP_Pipe1', options = '', outputFormat = 'mat', variableFilter = '.*', cflags = '', simflags = '-reconcile -sx=./NewDataReconciliationSimpleTests/resources/DataReconciliationSimpleTests.TSP_Pipe1_Inputs.csv -eps=0.0023 -lv=LOG_JAC'",
-messages = "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_Pipe1
-LOG_STDOUT | info | DataReconciliation Completed!
-"
-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).
[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/SourceP.mo:30:3-31:45:writable] Warning: Connector C is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
@@ -1210,6 +18,9 @@
[ThermoSysPro 3.2.0/Properties/WaterSteam/IF97_packages.mo:1089:9-1089:27:writable] Warning: cv was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[ThermoSysPro 3.2.0/Properties/WaterSteamSimple/prop4_Ph.mo:76:3-76:60:writable] Warning: dh1satp was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[ThermoSysPro 3.2.0/Properties/WaterSteamSimple/prop4_Ph.mo:76:3-76:60:writable] Warning: dh2satp was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[ThermoSysPro 3.2.0/Properties/WaterSteamSimple/prop4_Ph_der.mo:179:3-182:49:writable] Warning: du1satp_der was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[ThermoSysPro 3.2.0/Properties/WaterSteamSimple/prop4_Ph_der.mo:179:3-182:49:writable] Warning: du2satp_der was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
+Warning: Out of memory! Faking a stack overflow.
+Error: Stack overflow occurred while evaluating simulate(NewDataReconciliationSimpleTests.TSP_Pipe1, simflags = \"-reconcile -sx=./NewDataReconciliationSimpleTests/resources/DataReconciliationSimpleTests.TSP_Pipe1_Inputs.csv -eps=0.0023 -lv=LOG_JAC\"):
+[bt] [Symbols are not generated when running the test suite]
"
''
Equation mismatch: omc-diff says:
Failed 'M' '"'
Line 10: Text differs:
expected: ModelInfo: NewDataReconciliationSimpleTests.TSP_Pipe
got: "[openmodelica/dataReconciliation/NewDataReconciliationSimpleTests/SingularPressureLoss.mo:
== 1 out of 1 tests failed [openmodelica/dataReconciliation/TSP_Pipe1.mos_temp9024, time: 23]