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Failed
openmodelica_dataReconciliation.TSP_Splitter5.mos (from (result.xml))
Stacktrace
Output mismatch (see stdout for details)
Standard Output
+ TSP_Splitter5 ... equation mismatch [time: 19]
==== Log C:\Windows\TEMP/omc-rtest-OpenModelica/openmodelica/dataReconciliation/TSP_Splitter5.mos_temp9448/log-TSP_Splitter5.mos
true
""
true
"Notification: Automatically loaded package Modelica 3.2.3 due to uses annotation from NewDataReconciliationSimpleTests.
Notification: Automatically loaded package Complex 3.2.3 due to uses annotation from Modelica.
Notification: Automatically loaded package ModelicaServices 3.2.3 due to uses annotation from Modelica.
Notification: Automatically loaded package ThermoSysPro 3.2 due to uses annotation from NewDataReconciliationSimpleTests.
"
ModelInfo: NewDataReconciliationSimpleTests.TSP_Splitter5
==========================================================================
OrderedVariables (219)
========================================
1: sink1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
2: sink1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
3: sink1.C.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
4: sink1.C.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real
5: sink1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
6: sink1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
7: sink1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real
8: sink1.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real
9: sink1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real
10: sink1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real
11: staticDrum1.Cth.W:VARIABLE(flow=true unit = "W" ) "Thermal flow rate. Positive when going into the component" type: Real
12: staticDrum1.Cth.T:VARIABLE(flow=false min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature" type: Real
13: staticDrum1.vsat.cv:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant volume" type: Real
14: staticDrum1.vsat.pt:VARIABLE() "Derivative of pressure wrt. temperature" type: Real
15: staticDrum1.vsat.cp:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant pressure" type: Real
16: staticDrum1.vsat.h:VARIABLE(unit = "J/kg" ) "Specific enthalpy" type: Real
17: staticDrum1.vsat.rho:VARIABLE(min = 0.0 unit = "kg/m3" ) "Density" type: Real
18: staticDrum1.vsat.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature" type: Real
19: staticDrum1.vsat.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Pressure" type: Real
20: staticDrum1.lsat.cv:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant volume" type: Real
21: staticDrum1.lsat.pt:VARIABLE() "Derivative of pressure wrt. temperature" type: Real
22: staticDrum1.lsat.cp:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant pressure" type: Real
23: staticDrum1.lsat.h:VARIABLE(unit = "J/kg" ) "Specific enthalpy" type: Real
24: staticDrum1.lsat.rho:VARIABLE(min = 0.0 unit = "kg/m3" ) "Density" type: Real
25: staticDrum1.lsat.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature" type: Real
26: staticDrum1.lsat.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Pressure" type: Real
27: staticDrum1.Ce_sup.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
28: staticDrum1.Ce_sup.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
29: staticDrum1.Ce_sup.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
30: staticDrum1.Ce_sup.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
31: staticDrum1.Ce_sup.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
32: staticDrum1.Ce_sup.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
33: staticDrum1.Ce_steam.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
34: staticDrum1.Ce_steam.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
35: staticDrum1.Ce_steam.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
36: staticDrum1.Ce_steam.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
37: staticDrum1.Ce_steam.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
38: staticDrum1.Ce_steam.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
39: staticDrum1.Cs_purg.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
40: staticDrum1.Cs_purg.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
41: staticDrum1.Cs_purg.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
42: staticDrum1.Cs_purg.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
43: staticDrum1.Cs_purg.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
44: staticDrum1.Cs_purg.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
45: staticDrum1.Cs_sur.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
46: staticDrum1.Cs_sur.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
47: staticDrum1.Cs_sur.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
48: staticDrum1.Cs_sur.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
49: staticDrum1.Cs_sur.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
50: staticDrum1.Cs_sur.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
51: staticDrum1.Cs_eva.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
52: staticDrum1.Cs_eva.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
53: staticDrum1.Cs_eva.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
54: staticDrum1.Cs_eva.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
55: staticDrum1.Cs_eva.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
56: staticDrum1.Cs_eva.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
57: staticDrum1.Cs_sup.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
58: staticDrum1.Cs_sup.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
59: staticDrum1.Cs_sup.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
60: staticDrum1.Cs_sup.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
61: staticDrum1.Cs_sup.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
62: staticDrum1.Cs_sup.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
63: staticDrum1.Ce_eco.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
64: staticDrum1.Ce_eco.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
65: staticDrum1.Ce_eco.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
66: staticDrum1.Ce_eco.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
67: staticDrum1.Ce_eco.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
68: staticDrum1.Ce_eco.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
69: staticDrum1.Ce_eva.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
70: staticDrum1.Ce_eva.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
71: staticDrum1.Ce_eva.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
72: staticDrum1.Ce_eva.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
73: staticDrum1.Ce_eva.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
74: staticDrum1.Ce_eva.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
75: staticDrum1.hv:VARIABLE(start = 2.8e6 unit = "J/kg" ) "Gas phase specific enthalpy" type: Real
76: staticDrum1.hl:VARIABLE(start = 1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Liquid phase specific enthalpy" type: Real
77: staticDrum1.P:VARIABLE(min = 0.0 start = 1e6 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real
78: staticDrum1.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real
79: sourceQ2.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
80: sourceQ2.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
81: sourceQ2.C.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
82: sourceQ2.C.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real
83: sourceQ2.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
84: sourceQ2.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
85: sourceQ2.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real
86: sourceQ2.IMassFlow.signal:VARIABLE(flow=false ) type: Real
87: sourceQ2.h:VARIABLE(unit = "J/kg" protected = true ) "Fluid specific enthalpy" type: Real
88: sourceQ2.Q:VARIABLE(unit = "kg/s" protected = true ) "Mass flow rate" type: Real
89: sourceQ2.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true ) "Fluid pressure" type: Real
90: sourceQ3.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
91: sourceQ3.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
92: sourceQ3.C.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
93: sourceQ3.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
94: sourceQ3.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
95: sourceQ3.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
96: sourceQ3.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real
97: sourceQ3.IMassFlow.signal:VARIABLE(flow=false ) type: Real
98: sourceQ3.h:VARIABLE(unit = "J/kg" protected = true ) "Fluid specific enthalpy" type: Real
99: sourceQ3.Q:VARIABLE(unit = "kg/s" protected = true ) "Mass flow rate" type: Real
100: sourceQ3.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true ) "Fluid pressure" type: Real
101: singularPressureLoss3.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
102: singularPressureLoss3.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real
103: singularPressureLoss3.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real
104: singularPressureLoss3.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real
105: singularPressureLoss3.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real
106: singularPressureLoss3.pro_pT.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real
107: singularPressureLoss3.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
108: singularPressureLoss3.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real
109: singularPressureLoss3.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real
110: singularPressureLoss3.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
111: singularPressureLoss3.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
112: singularPressureLoss3.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
113: singularPressureLoss3.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
114: singularPressureLoss3.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
115: singularPressureLoss3.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
116: singularPressureLoss3.pro_ph.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real
117: singularPressureLoss3.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
118: singularPressureLoss3.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real
119: singularPressureLoss3.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
120: singularPressureLoss3.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real
121: singularPressureLoss3.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
122: singularPressureLoss3.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
123: singularPressureLoss3.C2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
124: singularPressureLoss3.C2.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real
125: singularPressureLoss3.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
126: singularPressureLoss3.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
127: singularPressureLoss3.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
128: singularPressureLoss3.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
129: singularPressureLoss3.C1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
130: singularPressureLoss3.C1.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real
131: singularPressureLoss3.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
132: singularPressureLoss3.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
133: singularPressureLoss3.h:VARIABLE(start = 1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
134: singularPressureLoss3.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real
135: singularPressureLoss3.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real
136: singularPressureLoss3.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real
137: singularPressureLoss3.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
138: singularPressureLoss3.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real
139: singularPressureLoss2.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
140: singularPressureLoss2.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real
141: singularPressureLoss2.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real
142: singularPressureLoss2.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real
143: singularPressureLoss2.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real
144: singularPressureLoss2.pro_pT.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real
145: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
146: singularPressureLoss2.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real
147: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real
148: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
149: singularPressureLoss2.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
150: singularPressureLoss2.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
151: singularPressureLoss2.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
152: singularPressureLoss2.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
153: singularPressureLoss2.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
154: singularPressureLoss2.pro_ph.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real
155: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
156: singularPressureLoss2.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real
157: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
158: singularPressureLoss2.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real
159: singularPressureLoss2.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
160: singularPressureLoss2.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
161: singularPressureLoss2.C2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
162: 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
163: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
164: singularPressureLoss2.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
165: singularPressureLoss2.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
166: singularPressureLoss2.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
167: singularPressureLoss2.C1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
168: 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
169: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
170: singularPressureLoss2.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
171: singularPressureLoss2.h:VARIABLE(start = 1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
172: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real
173: singularPressureLoss2.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real
174: singularPressureLoss2.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real
175: singularPressureLoss2.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
176: singularPressureLoss2.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real
177: singularPressureLoss1.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
178: singularPressureLoss1.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real
179: singularPressureLoss1.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real
180: singularPressureLoss1.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real
181: singularPressureLoss1.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real
182: singularPressureLoss1.pro_pT.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real
183: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
184: singularPressureLoss1.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real
185: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real
186: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
187: singularPressureLoss1.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
188: singularPressureLoss1.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
189: singularPressureLoss1.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
190: singularPressureLoss1.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
191: singularPressureLoss1.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
192: singularPressureLoss1.pro_ph.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real
193: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
194: singularPressureLoss1.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real
195: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
196: singularPressureLoss1.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real
197: singularPressureLoss1.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
198: singularPressureLoss1.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
199: singularPressureLoss1.C2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
200: 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
201: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
202: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
203: singularPressureLoss1.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
204: singularPressureLoss1.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
205: singularPressureLoss1.C1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
206: 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
207: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
208: singularPressureLoss1.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
209: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
210: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real
211: singularPressureLoss1.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real
212: singularPressureLoss1.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real
213: singularPressureLoss1.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
214: singularPressureLoss1.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real
215: sourceQ3.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real
216: sourceQ3.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real
217: sourceQ2.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real
218: sourceQ2.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real
219: sink1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real
OrderedEquation (179, 219)
========================================
1/1 (1): sourceQ3.Q0 = 100.0 [binding |0|0|0|0|]
2/2 (1): sourceQ3.h0 = 1e6 [binding |0|0|0|0|]
3/3 (1): sourceQ2.Q0 = 100.0 [binding |0|0|0|0|]
4/4 (1): sourceQ2.h0 = 1e6 [binding |0|0|0|0|]
5/5 (1): sink1.h0 = 1e5 [binding |0|0|0|0|]
6/6 (1): sourceQ3.C.P = singularPressureLoss3.C1.P [dynamic |0|0|0|0|]
7/7 (1): sourceQ3.C.Q = singularPressureLoss3.C1.Q [dynamic |0|0|0|0|]
8/8 (1): sourceQ3.C.a = singularPressureLoss3.C1.a [dynamic |0|0|0|0|]
9/9 (1): sourceQ3.C.b = singularPressureLoss3.C1.b [dynamic |0|0|0|0|]
10/10 (1): sourceQ3.C.h = singularPressureLoss3.C1.h [dynamic |0|0|0|0|]
11/11 (1): sourceQ3.C.h_vol = singularPressureLoss3.C1.h_vol [dynamic |0|0|0|0|]
12/12 (1): sourceQ2.C.P = singularPressureLoss2.C1.P [dynamic |0|0|0|0|]
13/13 (1): sourceQ2.C.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|]
14/14 (1): sourceQ2.C.a = singularPressureLoss2.C1.a [dynamic |0|0|0|0|]
15/15 (1): sourceQ2.C.b = singularPressureLoss2.C1.b [dynamic |0|0|0|0|]
16/16 (1): sourceQ2.C.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|]
17/17 (1): sourceQ2.C.h_vol = singularPressureLoss2.C1.h_vol [dynamic |0|0|0|0|]
18/18 (1): singularPressureLoss2.C2.P = staticDrum1.Ce_steam.P [dynamic |0|0|0|0|]
19/19 (1): singularPressureLoss2.C2.Q = staticDrum1.Ce_steam.Q [dynamic |0|0|0|0|]
20/20 (1): singularPressureLoss2.C2.a = staticDrum1.Ce_steam.a [dynamic |0|0|0|0|]
21/21 (1): singularPressureLoss2.C2.b = staticDrum1.Ce_steam.b [dynamic |0|0|0|0|]
22/22 (1): singularPressureLoss2.C2.h = staticDrum1.Ce_steam.h [dynamic |0|0|0|0|]
23/23 (1): singularPressureLoss2.C2.h_vol = staticDrum1.Ce_steam.h_vol [dynamic |0|0|0|0|]
24/24 (1): singularPressureLoss3.C2.P = staticDrum1.Ce_eco.P [dynamic |0|0|0|0|]
25/25 (1): singularPressureLoss3.C2.Q = staticDrum1.Ce_eco.Q [dynamic |0|0|0|0|]
26/26 (1): singularPressureLoss3.C2.a = staticDrum1.Ce_eco.a [dynamic |0|0|0|0|]
27/27 (1): singularPressureLoss3.C2.b = staticDrum1.Ce_eco.b [dynamic |0|0|0|0|]
28/28 (1): singularPressureLoss3.C2.h = staticDrum1.Ce_eco.h [dynamic |0|0|0|0|]
29/29 (1): singularPressureLoss3.C2.h_vol = staticDrum1.Ce_eco.h_vol [dynamic |0|0|0|0|]
30/30 (1): staticDrum1.Cs_sup.P = singularPressureLoss1.C1.P [dynamic |0|0|0|0|]
31/31 (1): staticDrum1.Cs_sup.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|]
32/32 (1): staticDrum1.Cs_sup.a = singularPressureLoss1.C1.a [dynamic |0|0|0|0|]
33/33 (1): staticDrum1.Cs_sup.b = singularPressureLoss1.C1.b [dynamic |0|0|0|0|]
34/34 (1): staticDrum1.Cs_sup.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|]
35/35 (1): staticDrum1.Cs_sup.h_vol = singularPressureLoss1.C1.h_vol [dynamic |0|0|0|0|]
36/36 (1): singularPressureLoss1.C2.P = sink1.C.P [dynamic |0|0|0|0|]
37/37 (1): singularPressureLoss1.C2.Q = sink1.C.Q [dynamic |0|0|0|0|]
38/38 (1): singularPressureLoss1.C2.a = sink1.C.a [dynamic |0|0|0|0|]
39/39 (1): singularPressureLoss1.C2.b = sink1.C.b [dynamic |0|0|0|0|]
40/40 (1): singularPressureLoss1.C2.h = sink1.C.h [dynamic |0|0|0|0|]
41/41 (1): singularPressureLoss1.C2.h_vol = sink1.C.h_vol [dynamic |0|0|0|0|]
42/42 (1): staticDrum1.Cth.W = 0.0 [dynamic |0|0|0|0|]
43/43 (1): singularPressureLoss1.C1.P - singularPressureLoss1.C2.P = singularPressureLoss1.deltaP [dynamic |0|0|0|0|]
44/44 (1): singularPressureLoss1.C2.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|]
45/45 (1): singularPressureLoss1.C2.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|]
46/46 (1): singularPressureLoss1.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|]
47/47 (1): singularPressureLoss1.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|]
48/48 (1): 0.0 = singularPressureLoss1.C1.h - singularPressureLoss1.C1.h_vol [dynamic |0|0|0|0|]
49/49 (1): singularPressureLoss1.deltaP = singularPressureLoss1.K * singularPressureLoss1.Q * abs(singularPressureLoss1.Q) / singularPressureLoss1.rho [dynamic |0|0|0|0|]
50/50 (1): singularPressureLoss1.Pm = 0.5 * (singularPressureLoss1.C1.P + singularPressureLoss1.C2.P) [dynamic |0|0|0|0|]
51/51 (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) [dynamic |0|0|0|0|]
52/61 (1): singularPressureLoss1.h = singularPressureLoss1.pro_pT.h [dynamic |0|0|0|0|]
53/62 (1): singularPressureLoss1.rho = singularPressureLoss1.pro_pT.d [dynamic |0|0|0|0|]
54/63 (1): singularPressureLoss1.pro_ph.d = 0.0 [dynamic |0|0|0|0|]
55/64 (1): singularPressureLoss1.pro_ph.T = 0.0 [dynamic |0|0|0|0|]
56/65 (1): singularPressureLoss1.pro_ph.u = 0.0 [dynamic |0|0|0|0|]
57/66 (1): singularPressureLoss1.pro_ph.s = 0.0 [dynamic |0|0|0|0|]
58/67 (1): singularPressureLoss1.pro_ph.cp = 0.0 [dynamic |0|0|0|0|]
59/68 (1): singularPressureLoss1.pro_ph.ddhp = 0.0 [dynamic |0|0|0|0|]
60/69 (1): singularPressureLoss1.pro_ph.ddph = 0.0 [dynamic |0|0|0|0|]
61/70 (1): singularPressureLoss1.pro_ph.duph = 0.0 [dynamic |0|0|0|0|]
62/71 (1): singularPressureLoss1.pro_ph.duhp = 0.0 [dynamic |0|0|0|0|]
63/72 (1): singularPressureLoss1.pro_ph.x = 0.0 [dynamic |0|0|0|0|]
64/73 (1): singularPressureLoss2.C1.P - singularPressureLoss2.C2.P = singularPressureLoss2.deltaP [dynamic |0|0|0|0|]
65/74 (1): singularPressureLoss2.C2.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|]
66/75 (1): singularPressureLoss2.C2.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|]
67/76 (1): singularPressureLoss2.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|]
68/77 (1): singularPressureLoss2.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|]
69/78 (1): 0.0 = singularPressureLoss2.C1.h - singularPressureLoss2.C1.h_vol [dynamic |0|0|0|0|]
70/79 (1): singularPressureLoss2.deltaP = singularPressureLoss2.K * singularPressureLoss2.Q * abs(singularPressureLoss2.Q) / singularPressureLoss2.rho [dynamic |0|0|0|0|]
71/80 (1): singularPressureLoss2.Pm = 0.5 * (singularPressureLoss2.C1.P + singularPressureLoss2.C2.P) [dynamic |0|0|0|0|]
72/81 (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid) [dynamic |0|0|0|0|]
73/91 (1): singularPressureLoss2.h = singularPressureLoss2.pro_pT.h [dynamic |0|0|0|0|]
74/92 (1): singularPressureLoss2.rho = singularPressureLoss2.pro_pT.d [dynamic |0|0|0|0|]
75/93 (1): singularPressureLoss2.pro_ph.d = 0.0 [dynamic |0|0|0|0|]
76/94 (1): singularPressureLoss2.pro_ph.T = 0.0 [dynamic |0|0|0|0|]
77/95 (1): singularPressureLoss2.pro_ph.u = 0.0 [dynamic |0|0|0|0|]
78/96 (1): singularPressureLoss2.pro_ph.s = 0.0 [dynamic |0|0|0|0|]
79/97 (1): singularPressureLoss2.pro_ph.cp = 0.0 [dynamic |0|0|0|0|]
80/98 (1): singularPressureLoss2.pro_ph.ddhp = 0.0 [dynamic |0|0|0|0|]
81/99 (1): singularPressureLoss2.pro_ph.ddph = 0.0 [dynamic |0|0|0|0|]
82/100 (1): singularPressureLoss2.pro_ph.duph = 0.0 [dynamic |0|0|0|0|]
83/101 (1): singularPressureLoss2.pro_ph.duhp = 0.0 [dynamic |0|0|0|0|]
84/102 (1): singularPressureLoss2.pro_ph.x = 0.0 [dynamic |0|0|0|0|]
85/103 (1): singularPressureLoss3.C1.P - singularPressureLoss3.C2.P = singularPressureLoss3.deltaP [dynamic |0|0|0|0|]
86/104 (1): singularPressureLoss3.C2.Q = singularPressureLoss3.C1.Q [dynamic |0|0|0|0|]
87/105 (1): singularPressureLoss3.C2.h = singularPressureLoss3.C1.h [dynamic |0|0|0|0|]
88/106 (1): singularPressureLoss3.h = singularPressureLoss3.C1.h [dynamic |0|0|0|0|]
89/107 (1): singularPressureLoss3.Q = singularPressureLoss3.C1.Q [dynamic |0|0|0|0|]
90/108 (1): 0.0 = singularPressureLoss3.C1.h - singularPressureLoss3.C1.h_vol [dynamic |0|0|0|0|]
91/109 (1): singularPressureLoss3.deltaP = singularPressureLoss3.K * singularPressureLoss3.Q * abs(singularPressureLoss3.Q) / singularPressureLoss3.rho [dynamic |0|0|0|0|]
92/110 (1): singularPressureLoss3.Pm = 0.5 * (singularPressureLoss3.C1.P + singularPressureLoss3.C2.P) [dynamic |0|0|0|0|]
93/111 (10): singularPressureLoss3.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss3.Pm, singularPressureLoss3.T, singularPressureLoss3.mode, singularPressureLoss3.fluid) [dynamic |0|0|0|0|]
94/121 (1): singularPressureLoss3.h = singularPressureLoss3.pro_pT.h [dynamic |0|0|0|0|]
95/122 (1): singularPressureLoss3.rho = singularPressureLoss3.pro_pT.d [dynamic |0|0|0|0|]
96/123 (1): singularPressureLoss3.pro_ph.d = 0.0 [dynamic |0|0|0|0|]
97/124 (1): singularPressureLoss3.pro_ph.T = 0.0 [dynamic |0|0|0|0|]
98/125 (1): singularPressureLoss3.pro_ph.u = 0.0 [dynamic |0|0|0|0|]
99/126 (1): singularPressureLoss3.pro_ph.s = 0.0 [dynamic |0|0|0|0|]
100/127 (1): singularPressureLoss3.pro_ph.cp = 0.0 [dynamic |0|0|0|0|]
101/128 (1): singularPressureLoss3.pro_ph.ddhp = 0.0 [dynamic |0|0|0|0|]
102/129 (1): singularPressureLoss3.pro_ph.ddph = 0.0 [dynamic |0|0|0|0|]
103/130 (1): singularPressureLoss3.pro_ph.duph = 0.0 [dynamic |0|0|0|0|]
104/131 (1): singularPressureLoss3.pro_ph.duhp = 0.0 [dynamic |0|0|0|0|]
105/132 (1): singularPressureLoss3.pro_ph.x = 0.0 [dynamic |0|0|0|0|]
106/133 (1): sourceQ3.C.P = sourceQ3.P [dynamic |0|0|0|0|]
107/134 (1): sourceQ3.C.Q = sourceQ3.Q [dynamic |0|0|0|0|]
108/135 (1): sourceQ3.C.h_vol = sourceQ3.h [dynamic |0|0|0|0|]
109/136 (1): sourceQ3.IMassFlow.signal = sourceQ3.Q0 [dynamic |0|0|0|0|]
110/137 (1): sourceQ3.Q = sourceQ3.IMassFlow.signal [dynamic |0|0|0|0|]
111/138 (1): sourceQ3.ISpecificEnthalpy.signal = sourceQ3.h0 [dynamic |0|0|0|0|]
112/139 (1): sourceQ3.h = sourceQ3.ISpecificEnthalpy.signal [dynamic |0|0|0|0|]
113/140 (1): sourceQ2.C.P = sourceQ2.P [dynamic |0|0|0|0|]
114/141 (1): sourceQ2.C.Q = sourceQ2.Q [dynamic |0|0|0|0|]
115/142 (1): sourceQ2.C.h_vol = sourceQ2.h [dynamic |0|0|0|0|]
116/143 (1): sourceQ2.IMassFlow.signal = sourceQ2.Q0 [dynamic |0|0|0|0|]
117/144 (1): sourceQ2.Q = sourceQ2.IMassFlow.signal [dynamic |0|0|0|0|]
118/145 (1): sourceQ2.ISpecificEnthalpy.signal = sourceQ2.h0 [dynamic |0|0|0|0|]
119/146 (1): sourceQ2.h = sourceQ2.ISpecificEnthalpy.signal [dynamic |0|0|0|0|]
120/147 (1): staticDrum1.Ce_sup.Q = 0.0 [dynamic |0|0|0|0|]
121/148 (1): staticDrum1.Ce_sup.h = 1e5 [dynamic |0|0|0|0|]
122/149 (1): staticDrum1.Ce_sup.b = true [dynamic |0|0|0|0|]
123/150 (1): staticDrum1.Ce_eva.Q = 0.0 [dynamic |0|0|0|0|]
124/151 (1): staticDrum1.Ce_eva.h = 1e5 [dynamic |0|0|0|0|]
125/152 (1): staticDrum1.Ce_eva.b = true [dynamic |0|0|0|0|]
126/153 (1): staticDrum1.Cs_eva.Q = 0.0 [dynamic |0|0|0|0|]
127/154 (1): staticDrum1.Cs_eva.h = 1e5 [dynamic |0|0|0|0|]
128/155 (1): staticDrum1.Cs_eva.a = true [dynamic |0|0|0|0|]
129/156 (1): staticDrum1.Cs_purg.Q = 0.0 [dynamic |0|0|0|0|]
130/157 (1): staticDrum1.Cs_purg.h = 1e5 [dynamic |0|0|0|0|]
131/158 (1): staticDrum1.Cs_purg.a = true [dynamic |0|0|0|0|]
132/159 (1): staticDrum1.Cs_sur.Q = 0.0 [dynamic |0|0|0|0|]
133/160 (1): staticDrum1.Cs_sur.h = 1e5 [dynamic |0|0|0|0|]
134/161 (1): staticDrum1.Cs_sur.a = true [dynamic |0|0|0|0|]
135/162 (1): staticDrum1.P = staticDrum1.Ce_steam.P [dynamic |0|0|0|0|]
136/163 (1): staticDrum1.P = staticDrum1.Ce_sup.P [dynamic |0|0|0|0|]
137/164 (1): staticDrum1.P = staticDrum1.Ce_eva.P [dynamic |0|0|0|0|]
138/165 (1): staticDrum1.P = staticDrum1.Ce_eco.P [dynamic |0|0|0|0|]
139/166 (1): staticDrum1.P = staticDrum1.Cs_eva.P [dynamic |0|0|0|0|]
140/167 (1): staticDrum1.P = staticDrum1.Cs_purg.P [dynamic |0|0|0|0|]
141/168 (1): staticDrum1.P = staticDrum1.Cs_sup.P [dynamic |0|0|0|0|]
142/169 (1): staticDrum1.P = staticDrum1.Cs_sur.P [dynamic |0|0|0|0|]
143/170 (1): staticDrum1.Ce_sup.h_vol = staticDrum1.hl [dynamic |0|0|0|0|]
144/171 (1): staticDrum1.Ce_eva.h_vol = staticDrum1.hl [dynamic |0|0|0|0|]
145/172 (1): staticDrum1.Ce_eco.h_vol = staticDrum1.hl [dynamic |0|0|0|0|]
146/173 (1): staticDrum1.Ce_steam.h_vol = staticDrum1.hv [dynamic |0|0|0|0|]
147/174 (1): staticDrum1.Cs_purg.h_vol = staticDrum1.hl [dynamic |0|0|0|0|]
148/175 (1): staticDrum1.Cs_sup.h_vol = staticDrum1.hl [dynamic |0|0|0|0|]
149/176 (1): staticDrum1.Cs_eva.h_vol = staticDrum1.hl [dynamic |0|0|0|0|]
150/177 (1): staticDrum1.Cs_sur.h_vol = (1.0 - staticDrum1.x) * staticDrum1.hl + staticDrum1.x * staticDrum1.hv [dynamic |0|0|0|0|]
151/178 (1): staticDrum1.Ce_eco.Q + staticDrum1.Ce_steam.Q + staticDrum1.Ce_sup.Q + staticDrum1.Ce_eva.Q + (-staticDrum1.Cs_purg.Q) - staticDrum1.Cs_sup.Q - staticDrum1.Cs_sur.Q - staticDrum1.Cs_eva.Q = 0.0 [dynamic |0|0|0|0|]
152/179 (1): staticDrum1.Ce_eco.Q * staticDrum1.Ce_eco.h + staticDrum1.Ce_steam.Q * staticDrum1.Ce_steam.h + staticDrum1.Ce_sup.Q * staticDrum1.Ce_sup.h + staticDrum1.Ce_eva.Q * staticDrum1.Ce_eva.h + staticDrum1.Cth.W - staticDrum1.Cs_sup.Q * staticDrum1.Cs_sup.h - staticDrum1.Cs_purg.Q * staticDrum1.Cs_purg.h - staticDrum1.Cs_sur.Q * staticDrum1.Cs_sur.h - staticDrum1.Cs_eva.Q * staticDrum1.Cs_eva.h = 0.0 [dynamic |0|0|0|0|]
153/180 (14): (staticDrum1.lsat, staticDrum1.vsat) = ThermoSysPro.Properties.WaterSteam.IF97.Water_sat_P(staticDrum1.P) [dynamic |0|0|0|0|]
154/194 (1): staticDrum1.hl = staticDrum1.lsat.h [dynamic |0|0|0|0|]
155/195 (1): staticDrum1.hv = staticDrum1.vsat.h [dynamic |0|0|0|0|]
156/196 (1): staticDrum1.T = staticDrum1.lsat.T [dynamic |0|0|0|0|]
157/197 (1): staticDrum1.Cth.T = staticDrum1.T [dynamic |0|0|0|0|]
158/198 (1): sink1.C.P = sink1.P [dynamic |0|0|0|0|]
159/199 (1): sink1.C.Q = sink1.Q [dynamic |0|0|0|0|]
160/200 (1): sink1.C.h_vol = sink1.h [dynamic |0|0|0|0|]
161/201 (1): sink1.ISpecificEnthalpy.signal = sink1.h0 [dynamic |0|0|0|0|]
162/202 (1): sink1.h = sink1.ISpecificEnthalpy.signal [dynamic |0|0|0|0|]
163/203 (1): singularPressureLoss1.C1.a = true [binding |0|0|0|0|]
164/204 (1): singularPressureLoss1.C2.b = true [binding |0|0|0|0|]
165/205 (1): singularPressureLoss2.C1.a = true [binding |0|0|0|0|]
166/206 (1): singularPressureLoss2.C2.b = true [binding |0|0|0|0|]
167/207 (1): singularPressureLoss3.C1.a = true [binding |0|0|0|0|]
168/208 (1): singularPressureLoss3.C2.b = true [binding |0|0|0|0|]
169/209 (1): sourceQ3.C.b = true [binding |0|0|0|0|]
170/210 (1): sourceQ2.C.b = true [binding |0|0|0|0|]
171/211 (1): staticDrum1.Ce_eva.a = true [binding |0|0|0|0|]
172/212 (1): staticDrum1.Ce_eco.a = true [binding |0|0|0|0|]
173/213 (1): staticDrum1.Cs_sup.b = true [binding |0|0|0|0|]
174/214 (1): staticDrum1.Cs_eva.b = true [binding |0|0|0|0|]
175/215 (1): staticDrum1.Cs_sur.b = true [binding |0|0|0|0|]
176/216 (1): staticDrum1.Cs_purg.b = true [binding |0|0|0|0|]
177/217 (1): staticDrum1.Ce_steam.a = true [binding |0|0|0|0|]
178/218 (1): staticDrum1.Ce_sup.a = true [binding |0|0|0|0|]
179/219 (1): sink1.C.a = true [binding |0|0|0|0|]
Matching
========================================
219 variables and equations
var 1 is solved in eqn 39
var 2 is solved in eqn 219
var 3 is solved in eqn 40
var 4 is solved in eqn 37
var 5 is solved in eqn 200
var 6 is solved in eqn 36
var 7 is solved in eqn 201
var 8 is solved in eqn 202
var 9 is solved in eqn 199
var 10 is solved in eqn 198
var 11 is solved in eqn 42
var 12 is solved in eqn 197
var 13 is solved in eqn 193
var 14 is solved in eqn 192
var 15 is solved in eqn 191
var 16 is solved in eqn 190
var 17 is solved in eqn 189
var 18 is solved in eqn 188
var 19 is solved in eqn 187
var 20 is solved in eqn 186
var 21 is solved in eqn 185
var 22 is solved in eqn 184
var 23 is solved in eqn 194
var 24 is solved in eqn 182
var 25 is solved in eqn 181
var 26 is solved in eqn 180
var 27 is solved in eqn 149
var 28 is solved in eqn 218
var 29 is solved in eqn 148
var 30 is solved in eqn 147
var 31 is solved in eqn 170
var 32 is solved in eqn 163
var 33 is solved in eqn 21
var 34 is solved in eqn 217
var 35 is solved in eqn 22
var 36 is solved in eqn 19
var 37 is solved in eqn 173
var 38 is solved in eqn 162
var 39 is solved in eqn 216
var 40 is solved in eqn 158
var 41 is solved in eqn 157
var 42 is solved in eqn 156
var 43 is solved in eqn 174
var 44 is solved in eqn 167
var 45 is solved in eqn 215
var 46 is solved in eqn 161
var 47 is solved in eqn 160
var 48 is solved in eqn 159
var 49 is solved in eqn 177
var 50 is solved in eqn 169
var 51 is solved in eqn 214
var 52 is solved in eqn 155
var 53 is solved in eqn 154
var 54 is solved in eqn 153
var 55 is solved in eqn 176
var 56 is solved in eqn 166
var 57 is solved in eqn 213
var 58 is solved in eqn 32
var 59 is solved in eqn 179
var 60 is solved in eqn 178
var 61 is solved in eqn 35
var 62 is solved in eqn 168
var 63 is solved in eqn 27
var 64 is solved in eqn 212
var 65 is solved in eqn 28
var 66 is solved in eqn 25
var 67 is solved in eqn 172
var 68 is solved in eqn 165
var 69 is solved in eqn 152
var 70 is solved in eqn 211
var 71 is solved in eqn 151
var 72 is solved in eqn 150
var 73 is solved in eqn 171
var 74 is solved in eqn 164
var 75 is solved in eqn 195
var 76 is solved in eqn 175
var 77 is solved in eqn 183
var 78 is solved in eqn 196
var 79 is solved in eqn 210
var 80 is solved in eqn 14
var 81 is solved in eqn 16
var 82 is solved in eqn 141
var 83 is solved in eqn 142
var 84 is solved in eqn 12
var 85 is solved in eqn 145
var 86 is solved in eqn 143
var 87 is solved in eqn 146
var 88 is solved in eqn 144
var 89 is solved in eqn 140
var 90 is solved in eqn 209
var 91 is solved in eqn 8
var 92 is solved in eqn 10
var 93 is solved in eqn 134
var 94 is solved in eqn 135
var 95 is solved in eqn 6
var 96 is solved in eqn 138
var 97 is solved in eqn 136
var 98 is solved in eqn 139
var 99 is solved in eqn 137
var 100 is solved in eqn 133
var 101 is solved in eqn 113
var 102 is solved in eqn 120
var 103 is solved in eqn 119
var 104 is solved in eqn 118
var 105 is solved in eqn 117
var 106 is solved in eqn 116
var 107 is solved in eqn 115
var 108 is solved in eqn 114
var 109 is solved in eqn 121
var 110 is solved in eqn 112
var 111 is solved in eqn 132
var 112 is solved in eqn 131
var 113 is solved in eqn 130
var 114 is solved in eqn 129
var 115 is solved in eqn 128
var 116 is solved in eqn 127
var 117 is solved in eqn 126
var 118 is solved in eqn 125
var 119 is solved in eqn 123
var 120 is solved in eqn 124
var 121 is solved in eqn 208
var 122 is solved in eqn 26
var 123 is solved in eqn 105
var 124 is solved in eqn 104
var 125 is solved in eqn 29
var 126 is solved in eqn 24
var 127 is solved in eqn 9
var 128 is solved in eqn 207
var 129 is solved in eqn 108
var 130 is solved in eqn 7
var 131 is solved in eqn 11
var 132 is solved in eqn 103
var 133 is solved in eqn 106
var 134 is solved in eqn 110
var 135 is solved in eqn 111
var 136 is solved in eqn 122
var 137 is solved in eqn 107
var 138 is solved in eqn 109
var 139 is solved in eqn 83
var 140 is solved in eqn 90
var 141 is solved in eqn 89
var 142 is solved in eqn 88
var 143 is solved in eqn 87
var 144 is solved in eqn 86
var 145 is solved in eqn 85
var 146 is solved in eqn 84
var 147 is solved in eqn 91
var 148 is solved in eqn 82
var 149 is solved in eqn 102
var 150 is solved in eqn 101
var 151 is solved in eqn 100
var 152 is solved in eqn 99
var 153 is solved in eqn 98
var 154 is solved in eqn 97
var 155 is solved in eqn 96
var 156 is solved in eqn 95
var 157 is solved in eqn 93
var 158 is solved in eqn 94
var 159 is solved in eqn 206
var 160 is solved in eqn 20
var 161 is solved in eqn 75
var 162 is solved in eqn 74
var 163 is solved in eqn 23
var 164 is solved in eqn 18
var 165 is solved in eqn 15
var 166 is solved in eqn 205
var 167 is solved in eqn 78
var 168 is solved in eqn 13
var 169 is solved in eqn 17
var 170 is solved in eqn 73
var 171 is solved in eqn 76
var 172 is solved in eqn 80
var 173 is solved in eqn 81
var 174 is solved in eqn 92
var 175 is solved in eqn 77
var 176 is solved in eqn 79
var 177 is solved in eq
...[truncated 213737 chars]...
.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real
-109: singularPressureLoss3.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real
-110: singularPressureLoss3.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
+106: singularPressureLoss3.pro_pT.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real
+107: singularPressureLoss3.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
+108: singularPressureLoss3.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real
+109: singularPressureLoss3.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real
+110: singularPressureLoss3.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
111: singularPressureLoss3.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
112: singularPressureLoss3.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
113: singularPressureLoss3.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
114: singularPressureLoss3.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
115: singularPressureLoss3.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
-116: singularPressureLoss3.pro_ph.cp:VARIABLE(min = 1e-09 max = 9.999999999999999e+59 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real
-117: singularPressureLoss3.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
-118: singularPressureLoss3.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real
-119: singularPressureLoss3.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
+116: singularPressureLoss3.pro_ph.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real
+117: singularPressureLoss3.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
+118: singularPressureLoss3.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real
+119: singularPressureLoss3.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
120: singularPressureLoss3.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real
121: singularPressureLoss3.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
122: singularPressureLoss3.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-123: singularPressureLoss3.C2.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
+123: singularPressureLoss3.C2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
124: singularPressureLoss3.C2.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real
-125: singularPressureLoss3.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-126: singularPressureLoss3.C2.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real
+125: singularPressureLoss3.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
+126: singularPressureLoss3.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
127: singularPressureLoss3.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
128: singularPressureLoss3.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-129: singularPressureLoss3.C1.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
+129: singularPressureLoss3.C1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
130: singularPressureLoss3.C1.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real
-131: singularPressureLoss3.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-132: singularPressureLoss3.C1.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real
-133: singularPressureLoss3.h:VARIABLE(start = 100000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
-134: singularPressureLoss3.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real
+131: singularPressureLoss3.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
+132: singularPressureLoss3.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
+133: singularPressureLoss3.h:VARIABLE(start = 1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
+134: singularPressureLoss3.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real
135: singularPressureLoss3.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real
136: singularPressureLoss3.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real
137: singularPressureLoss3.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
-138: singularPressureLoss3.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real
+138: singularPressureLoss3.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real
139: singularPressureLoss2.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
140: singularPressureLoss2.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real
141: singularPressureLoss2.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real
142: singularPressureLoss2.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real
143: singularPressureLoss2.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real
-144: 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
-145: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
-146: singularPressureLoss2.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real
-147: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real
-148: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
+144: singularPressureLoss2.pro_pT.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real
+145: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
+146: singularPressureLoss2.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real
+147: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real
+148: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
149: singularPressureLoss2.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
150: singularPressureLoss2.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
151: singularPressureLoss2.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
152: singularPressureLoss2.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
153: singularPressureLoss2.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
-154: 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
-155: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
-156: singularPressureLoss2.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real
-157: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
+154: singularPressureLoss2.pro_ph.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real
+155: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
+156: singularPressureLoss2.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real
+157: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
158: singularPressureLoss2.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real
159: singularPressureLoss2.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
160: singularPressureLoss2.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-161: 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
+161: singularPressureLoss2.C2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
162: 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
-163: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-164: 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
+163: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
+164: singularPressureLoss2.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
165: singularPressureLoss2.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
166: singularPressureLoss2.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-167: 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
+167: singularPressureLoss2.C1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
168: 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
-169: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-170: 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
-171: singularPressureLoss2.h:VARIABLE(start = 100000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
-172: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real
+169: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
+170: singularPressureLoss2.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
+171: singularPressureLoss2.h:VARIABLE(start = 1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
+172: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real
173: singularPressureLoss2.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real
174: singularPressureLoss2.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real
175: singularPressureLoss2.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
-176: singularPressureLoss2.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real
+176: singularPressureLoss2.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real
177: singularPressureLoss1.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
178: singularPressureLoss1.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real
179: singularPressureLoss1.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real
180: singularPressureLoss1.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real
181: singularPressureLoss1.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real
-182: 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
-183: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
-184: singularPressureLoss1.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real
-185: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real
-186: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
+182: singularPressureLoss1.pro_pT.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real
+183: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
+184: singularPressureLoss1.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real
+185: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real
+186: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
187: singularPressureLoss1.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
188: singularPressureLoss1.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
189: singularPressureLoss1.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
190: singularPressureLoss1.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
191: singularPressureLoss1.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
-192: 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
-193: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
-194: singularPressureLoss1.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real
-195: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
+192: singularPressureLoss1.pro_ph.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real
+193: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
+194: singularPressureLoss1.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real
+195: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
196: singularPressureLoss1.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real
197: singularPressureLoss1.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
198: singularPressureLoss1.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-199: 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
+199: singularPressureLoss1.C2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
200: 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
-201: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-202: 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
+201: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
+202: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
203: singularPressureLoss1.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
204: singularPressureLoss1.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-205: 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
+205: singularPressureLoss1.C1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
206: 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
-207: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-208: 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
-209: singularPressureLoss1.h:VARIABLE(start = 100000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
-210: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real
+207: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
+208: singularPressureLoss1.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
+209: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
+210: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real
211: singularPressureLoss1.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real
212: singularPressureLoss1.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real
213: singularPressureLoss1.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
-214: singularPressureLoss1.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real
+214: singularPressureLoss1.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real
215: sourceQ3.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real
216: sourceQ3.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real
217: sourceQ2.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real
218: sourceQ2.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real
219: sink1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real
@@ -1237,14 +1237,14 @@
1/1 (1): staticDrum1.hl = 0.0 [binding |0|0|0|0|]
2/2 (1): singularPressureLoss3.h = 0.0 [binding |0|0|0|0|]
3/3 (1): singularPressureLoss3.Q = 0.0 [binding |0|0|0|0|]
4/4 (1): singularPressureLoss2.Q = 0.0 [binding |0|0|0|0|]
5/5 (1): sourceQ3.Q0 = 100.0 [binding |0|0|0|0|]
-6/6 (1): sourceQ3.h0 = 1000000.0 [binding |0|0|0|0|]
+6/6 (1): sourceQ3.h0 = 1e6 [binding |0|0|0|0|]
7/7 (1): sourceQ2.Q0 = 100.0 [binding |0|0|0|0|]
-8/8 (1): sourceQ2.h0 = 1000000.0 [binding |0|0|0|0|]
-9/9 (1): sink1.h0 = 100000.0 [binding |0|0|0|0|]
+8/8 (1): sourceQ2.h0 = 1e6 [binding |0|0|0|0|]
+9/9 (1): sink1.h0 = 1e5 [binding |0|0|0|0|]
10/10 (1): sourceQ3.C.P = singularPressureLoss3.C1.P [dynamic |0|0|0|0|]
11/11 (1): sourceQ3.C.Q = singularPressureLoss3.C1.Q [dynamic |0|0|0|0|]
12/12 (1): sourceQ3.C.a = singularPressureLoss3.C1.a [dynamic |0|0|0|0|]
13/13 (1): sourceQ3.C.b = singularPressureLoss3.C1.b [dynamic |0|0|0|0|]
14/14 (1): sourceQ3.C.h = singularPressureLoss3.C1.h [dynamic |0|0|0|0|]
@@ -1352,23 +1352,23 @@
116/143 (1): sourceQ2.C.Q = sourceQ2.Q [dynamic |0|0|0|0|]
117/144 (1): sourceQ2.C.h_vol = sourceQ2.h [dynamic |0|0|0|0|]
118/145 (1): sourceQ2.Q = sourceQ2.IMassFlow.signal [dynamic |0|0|0|0|]
119/146 (1): sourceQ2.h = sourceQ2.ISpecificEnthalpy.signal [dynamic |0|0|0|0|]
120/147 (1): staticDrum1.Ce_sup.Q = 0.0 [dynamic |0|0|0|0|]
-121/148 (1): staticDrum1.Ce_sup.h = 100000.0 [dynamic |0|0|0|0|]
+121/148 (1): staticDrum1.Ce_sup.h = 1e5 [dynamic |0|0|0|0|]
122/149 (1): staticDrum1.Ce_sup.b = true [dynamic |0|0|0|0|]
123/150 (1): staticDrum1.Ce_eva.Q = 0.0 [dynamic |0|0|0|0|]
-124/151 (1): staticDrum1.Ce_eva.h = 100000.0 [dynamic |0|0|0|0|]
+124/151 (1): staticDrum1.Ce_eva.h = 1e5 [dynamic |0|0|0|0|]
125/152 (1): staticDrum1.Ce_eva.b = true [dynamic |0|0|0|0|]
126/153 (1): staticDrum1.Cs_eva.Q = 0.0 [dynamic |0|0|0|0|]
-127/154 (1): staticDrum1.Cs_eva.h = 100000.0 [dynamic |0|0|0|0|]
+127/154 (1): staticDrum1.Cs_eva.h = 1e5 [dynamic |0|0|0|0|]
128/155 (1): staticDrum1.Cs_eva.a = true [dynamic |0|0|0|0|]
129/156 (1): staticDrum1.Cs_purg.Q = 0.0 [dynamic |0|0|0|0|]
-130/157 (1): staticDrum1.Cs_purg.h = 100000.0 [dynamic |0|0|0|0|]
+130/157 (1): staticDrum1.Cs_purg.h = 1e5 [dynamic |0|0|0|0|]
131/158 (1): staticDrum1.Cs_purg.a = true [dynamic |0|0|0|0|]
132/159 (1): staticDrum1.Cs_sur.Q = 0.0 [dynamic |0|0|0|0|]
-133/160 (1): staticDrum1.Cs_sur.h = 100000.0 [dynamic |0|0|0|0|]
+133/160 (1): staticDrum1.Cs_sur.h = 1e5 [dynamic |0|0|0|0|]
134/161 (1): staticDrum1.Cs_sur.a = true [dynamic |0|0|0|0|]
135/162 (1): staticDrum1.P = staticDrum1.Ce_steam.P [dynamic |0|0|0|0|]
136/163 (1): staticDrum1.P = staticDrum1.Ce_sup.P [dynamic |0|0|0|0|]
137/164 (1): staticDrum1.P = staticDrum1.Ce_eva.P [dynamic |0|0|0|0|]
138/165 (1): staticDrum1.P = staticDrum1.Ce_eco.P [dynamic |0|0|0|0|]
@@ -1638,14 +1638,14 @@
var 219 is solved in eqn 9
Standard BLT of the original model:(219)
============================================================
-219: sink1.h0: (9/9): (1): sink1.h0 = 100000.0
-218: sourceQ2.h0: (8/8): (1): sourceQ2.h0 = 1000000.0
+219: sink1.h0: (9/9): (1): sink1.h0 = 1e5
+218: sourceQ2.h0: (8/8): (1): sourceQ2.h0 = 1e6
217: sourceQ2.Q0: (7/7): (1): sourceQ2.Q0 = 100.0
-216: sourceQ3.h0: (6/6): (1): sourceQ3.h0 = 1000000.0
+216: sourceQ3.h0: (6/6): (1): sourceQ3.h0 = 1e6
215: sourceQ3.Q0: (5/5): (1): sourceQ3.Q0 = 100.0
214: singularPressureLoss1.deltaP: (47/47): (1): singularPressureLoss1.C1.P - singularPressureLoss1.C2.P = singularPressureLoss1.deltaP
213: singularPressureLoss1.Q: (51/51): (1): singularPressureLoss1.Q = singularPressureLoss1.C1.Q
212: singularPressureLoss1.rho: (53/53): (1): singularPressureLoss1.deltaP = singularPressureLoss1.K * singularPressureLoss1.Q * abs(singularPressureLoss1.Q) / singularPressureLoss1.rho
211: singularPressureLoss1.T: (55/56): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid)
@@ -1786,11 +1786,11 @@
76: staticDrum1.hl: (1/1): (1): staticDrum1.hl = 0.0
75: staticDrum1.hv: (155/195): (1): staticDrum1.hv = staticDrum1.vsat.h
74: staticDrum1.Ce_eva.P: (137/164): (1): staticDrum1.P = staticDrum1.Ce_eva.P
73: staticDrum1.Ce_eva.h_vol: (144/171): (1): staticDrum1.Ce_eva.h_vol = staticDrum1.hl
72: staticDrum1.Ce_eva.Q: (123/150): (1): staticDrum1.Ce_eva.Q = 0.0
-71: staticDrum1.Ce_eva.h: (124/151): (1): staticDrum1.Ce_eva.h = 100000.0
+71: staticDrum1.Ce_eva.h: (124/151): (1): staticDrum1.Ce_eva.h = 1e5
70: staticDrum1.Ce_eva.a: (171/211): (1): staticDrum1.Ce_eva.a = true
69: staticDrum1.Ce_eva.b: (125/152): (1): staticDrum1.Ce_eva.b = true
68: staticDrum1.Ce_eco.P: (138/165): (1): staticDrum1.P = staticDrum1.Ce_eco.P
67: staticDrum1.Ce_eco.h_vol: (145/172): (1): staticDrum1.Ce_eco.h_vol = staticDrum1.hl
66: staticDrum1.Ce_eco.Q: (29/29): (1): singularPressureLoss3.C2.Q = staticDrum1.Ce_eco.Q
@@ -1804,23 +1804,23 @@
58: staticDrum1.Cs_sup.a: (36/36): (1): staticDrum1.Cs_sup.a = singularPressureLoss1.C1.a
57: staticDrum1.Cs_sup.b: (173/213): (1): staticDrum1.Cs_sup.b = true
56: staticDrum1.Cs_eva.P: (139/166): (1): staticDrum1.P = staticDrum1.Cs_eva.P
55: staticDrum1.Cs_eva.h_vol: (149/176): (1): staticDrum1.Cs_eva.h_vol = staticDrum1.hl
54: staticDrum1.Cs_eva.Q: (126/153): (1): staticDrum1.Cs_eva.Q = 0.0
-53: staticDrum1.Cs_eva.h: (127/154): (1): staticDrum1.Cs_eva.h = 100000.0
+53: staticDrum1.Cs_eva.h: (127/154): (1): staticDrum1.Cs_eva.h = 1e5
52: staticDrum1.Cs_eva.a: (128/155): (1): staticDrum1.Cs_eva.a = true
51: staticDrum1.Cs_eva.b: (174/214): (1): staticDrum1.Cs_eva.b = true
50: staticDrum1.Cs_sur.P: (142/169): (1): staticDrum1.P = staticDrum1.Cs_sur.P
49: staticDrum1.Cs_sur.h_vol: (150/177): (1): staticDrum1.Cs_sur.h_vol = (1.0 - staticDrum1.x) * staticDrum1.hl + staticDrum1.x * staticDrum1.hv
48: staticDrum1.Cs_sur.Q: (132/159): (1): staticDrum1.Cs_sur.Q = 0.0
-47: staticDrum1.Cs_sur.h: (133/160): (1): staticDrum1.Cs_sur.h = 100000.0
+47: staticDrum1.Cs_sur.h: (133/160): (1): staticDrum1.Cs_sur.h = 1e5
46: staticDrum1.Cs_sur.a: (134/161): (1): staticDrum1.Cs_sur.a = true
45: staticDrum1.Cs_sur.b: (175/215): (1): staticDrum1.Cs_sur.b = true
44: staticDrum1.Cs_purg.P: (140/167): (1): staticDrum1.P = staticDrum1.Cs_purg.P
43: staticDrum1.Cs_purg.h_vol: (147/174): (1): staticDrum1.Cs_purg.h_vol = staticDrum1.hl
42: staticDrum1.Cs_purg.Q: (129/156): (1): staticDrum1.Cs_purg.Q = 0.0
-41: staticDrum1.Cs_purg.h: (130/157): (1): staticDrum1.Cs_purg.h = 100000.0
+41: staticDrum1.Cs_purg.h: (130/157): (1): staticDrum1.Cs_purg.h = 1e5
40: staticDrum1.Cs_purg.a: (131/158): (1): staticDrum1.Cs_purg.a = true
39: staticDrum1.Cs_purg.b: (176/216): (1): staticDrum1.Cs_purg.b = true
38: staticDrum1.Ce_steam.P: (135/162): (1): staticDrum1.P = staticDrum1.Ce_steam.P
37: staticDrum1.Ce_steam.h_vol: (146/173): (1): staticDrum1.Ce_steam.h_vol = staticDrum1.hv
36: staticDrum1.Ce_steam.Q: (23/23): (1): singularPressureLoss2.C2.Q = staticDrum1.Ce_steam.Q
@@ -1828,11 +1828,11 @@
34: staticDrum1.Ce_steam.a: (177/217): (1): staticDrum1.Ce_steam.a = true
33: staticDrum1.Ce_steam.b: (25/25): (1): singularPressureLoss2.C2.b = staticDrum1.Ce_steam.b
32: staticDrum1.Ce_sup.P: (136/163): (1): staticDrum1.P = staticDrum1.Ce_sup.P
31: staticDrum1.Ce_sup.h_vol: (143/170): (1): staticDrum1.Ce_sup.h_vol = staticDrum1.hl
30: staticDrum1.Ce_sup.Q: (120/147): (1): staticDrum1.Ce_sup.Q = 0.0
-29: staticDrum1.Ce_sup.h: (121/148): (1): staticDrum1.Ce_sup.h = 100000.0
+29: staticDrum1.Ce_sup.h: (121/148): (1): staticDrum1.Ce_sup.h = 1e5
28: staticDrum1.Ce_sup.a: (178/218): (1): staticDrum1.Ce_sup.a = true
27: staticDrum1.Ce_sup.b: (122/149): (1): staticDrum1.Ce_sup.b = true
26: staticDrum1.lsat.P: (153/180): (14): (staticDrum1.lsat, staticDrum1.vsat) = ThermoSysPro.Properties.WaterSteam.IF97.Water_sat_P(staticDrum1.P)
25: staticDrum1.lsat.T: (153/181): (14): (staticDrum1.lsat, staticDrum1.vsat) = ThermoSysPro.Properties.WaterSteam.IF97.Water_sat_P(staticDrum1.P)
24: staticDrum1.lsat.rho: (153/182): (14): (staticDrum1.lsat, staticDrum1.vsat) = ThermoSysPro.Properties.WaterSteam.IF97.Water_sat_P(staticDrum1.P)
@@ -1861,16 +1861,16 @@
1: sink1.C.b: (43/43): (1): singularPressureLoss1.C2.b = sink1.C.b
Variables of interest (7)
========================================
-1: staticDrum1.hl:VARIABLE(start = 100000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Liquid phase specific enthalpy" type: Real
-2: singularPressureLoss3.h:VARIABLE(start = 100000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
+1: staticDrum1.hl:VARIABLE(start = 1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Liquid phase specific enthalpy" type: Real
+2: singularPressureLoss3.h:VARIABLE(start = 1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
3: singularPressureLoss3.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
-4: singularPressureLoss2.h:VARIABLE(start = 100000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
+4: singularPressureLoss2.h:VARIABLE(start = 1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
5: singularPressureLoss2.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
-6: singularPressureLoss1.h:VARIABLE(start = 100000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
+6: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
7: singularPressureLoss1.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
Boundary conditions (5)
========================================
@@ -1899,14 +1899,14 @@
128: singularPressureLoss3.C1.a: (167/207): (1): singularPressureLoss3.C1.a = true
159: singularPressureLoss2.C2.b: (166/206): (1): singularPressureLoss2.C2.b = true
166: singularPressureLoss2.C1.a: (165/205): (1): singularPressureLoss2.C1.a = true
197: singularPressureLoss1.C2.b: (164/204): (1): singularPressureLoss1.C2.b = true
204: singularPressureLoss1.C1.a: (163/203): (1): singularPressureLoss1.C1.a = true
-219: sink1.h0: (9/9): (1): sink1.h0 = 100000.0
-218: sourceQ2.h0: (8/8): (1): sourceQ2.h0 = 1000000.0
+219: sink1.h0: (9/9): (1): sink1.h0 = 1e5
+218: sourceQ2.h0: (8/8): (1): sourceQ2.h0 = 1e6
217: sourceQ2.Q0: (7/7): (1): sourceQ2.Q0 = 100.0
-216: sourceQ3.h0: (6/6): (1): sourceQ3.h0 = 1000000.0
+216: sourceQ3.h0: (6/6): (1): sourceQ3.h0 = 1e6
215: sourceQ3.Q0: (5/5): (1): sourceQ3.Q0 = 100.0
175: singularPressureLoss2.Q: (4/4): (1): singularPressureLoss2.Q = 0.0
137: singularPressureLoss3.Q: (3/3): (1): singularPressureLoss3.Q = 0.0
133: singularPressureLoss3.h: (2/2): (1): singularPressureLoss3.h = 0.0
76: staticDrum1.hl: (1/1): (1): staticDrum1.hl = 0.0
@@ -1926,20 +1926,20 @@
>>>171: singularPressureLoss2.h: (71/80): (1): singularPressureLoss2.h = singularPressureLoss2.C1.h
167: singularPressureLoss2.C1.h: (70/79): (1): singularPressureLoss2.C2.h = singularPressureLoss2.C1.h
161: singularPressureLoss2.C2.h: (26/26): (1): singularPressureLoss2.C2.h = staticDrum1.Ce_steam.h
35: staticDrum1.Ce_steam.h: (152/179): (1): staticDrum1.Ce_eco.Q * staticDrum1.Ce_eco.h + staticDrum1.Ce_steam.Q * staticDrum1.Ce_steam.h + staticDrum1.Ce_sup.Q * staticDrum1.Ce_sup.h + staticDrum1.Ce_eva.Q * staticDrum1.Ce_eva.h + staticDrum1.Cth.W - staticDrum1.Cs_sup.Q * staticDrum1.Cs_sup.h - staticDrum1.Cs_purg.Q * staticDrum1.Cs_purg.h - staticDrum1.Cs_sur.Q * staticDrum1.Cs_sur.h - staticDrum1.Cs_eva.Q * staticDrum1.Cs_eva.h = 0.0
11: staticDrum1.Cth.W: (46/46): (1): staticDrum1.Cth.W = 0.0
-29: staticDrum1.Ce_sup.h: (121/148): (1): staticDrum1.Ce_sup.h = 100000.0
+29: staticDrum1.Ce_sup.h: (121/148): (1): staticDrum1.Ce_sup.h = 1e5
30: staticDrum1.Ce_sup.Q: (120/147): (1): staticDrum1.Ce_sup.Q = 0.0
36: staticDrum1.Ce_steam.Q: (23/23): (1): singularPressureLoss2.C2.Q = staticDrum1.Ce_steam.Q
162: singularPressureLoss2.C2.Q: (69/78): (1): singularPressureLoss2.C2.Q = singularPressureLoss2.C1.Q
168: singularPressureLoss2.C1.Q: (72/81): (1): singularPressureLoss2.Q = singularPressureLoss2.C1.Q
-41: staticDrum1.Cs_purg.h: (130/157): (1): staticDrum1.Cs_purg.h = 100000.0
+41: staticDrum1.Cs_purg.h: (130/157): (1): staticDrum1.Cs_purg.h = 1e5
42: staticDrum1.Cs_purg.Q: (129/156): (1): staticDrum1.Cs_purg.Q = 0.0
-47: staticDrum1.Cs_sur.h: (133/160): (1): staticDrum1.Cs_sur.h = 100000.0
+47: staticDrum1.Cs_sur.h: (133/160): (1): staticDrum1.Cs_sur.h = 1e5
48: staticDrum1.Cs_sur.Q: (132/159): (1): staticDrum1.Cs_sur.Q = 0.0
-53: staticDrum1.Cs_eva.h: (127/154): (1): staticDrum1.Cs_eva.h = 100000.0
+53: staticDrum1.Cs_eva.h: (127/154): (1): staticDrum1.Cs_eva.h = 1e5
54: staticDrum1.Cs_eva.Q: (126/153): (1): staticDrum1.Cs_eva.Q = 0.0
59: staticDrum1.Cs_sup.h: (38/38): (1): staticDrum1.Cs_sup.h = singularPressureLoss1.C1.h
205: singularPressureLoss1.C1.h: (52/52): (1): 0.0 = singularPressureLoss1.C1.h - singularPressureLoss1.C1.h_vol
207: singularPressureLoss1.C1.h_vol: (39/39): (1): staticDrum1.Cs_sup.h_vol = singularPressureLoss1.C1.h_vol
61: staticDrum1.Cs_sup.h_vol: (148/175): (1): staticDrum1.Cs_sup.h_vol = staticDrum1.hl
@@ -1949,11 +1949,11 @@
130: singularPressureLoss3.C1.Q: (93/111): (1): singularPressureLoss3.Q = singularPressureLoss3.C1.Q
72: staticDrum1.Ce_eva.Q: (123/150): (1): staticDrum1.Ce_eva.Q = 0.0
65: staticDrum1.Ce_eco.h: (32/32): (1): singularPressureLoss3.C2.h = staticDrum1.Ce_eco.h
123: singularPressureLoss3.C2.h: (91/109): (1): singularPressureLoss3.C2.h = singularPressureLoss3.C1.h
129: singularPressureLoss3.C1.h: (92/110): (1): singularPressureLoss3.h = singularPressureLoss3.C1.h
-71: staticDrum1.Ce_eva.h: (124/151): (1): staticDrum1.Ce_eva.h = 100000.0
+71: staticDrum1.Ce_eva.h: (124/151): (1): staticDrum1.Ce_eva.h = 1e5
Procedure success
>>>209: singularPressureLoss1.h: (50/50): (1): singularPressureLoss1.h = singularPressureLoss1.C1.h
205: singularPressureLoss1.C1.h: (52/52): (1): 0.0 = singularPressureLoss1.C1.h - singularPressureLoss1.C1.h_vol
207: singularPressureLoss1.C1.h_vol: (39/39): (1): staticDrum1.Cs_sup.h_vol = singularPressureLoss1.C1.h_vol
@@ -1992,11 +1992,11 @@
3/3 (1): singularPressureLoss1.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|]
SET_S (29, 29)
========================================
-1/1 (1): staticDrum1.Ce_eva.h = 100000.0 [dynamic |0|0|0|0|]
+1/1 (1): staticDrum1.Ce_eva.h = 1e5 [dynamic |0|0|0|0|]
2/2 (1): singularPressureLoss3.h = singularPressureLoss3.C1.h [dynamic |0|0|0|0|]
3/3 (1): singularPressureLoss3.C2.h = singularPressureLoss3.C1.h [dynamic |0|0|0|0|]
4/4 (1): singularPressureLoss3.C2.h = staticDrum1.Ce_eco.h [dynamic |0|0|0|0|]
5/5 (1): staticDrum1.Ce_eva.Q = 0.0 [dynamic |0|0|0|0|]
6/6 (1): singularPressureLoss3.Q = singularPressureLoss3.C1.Q [dynamic |0|0|0|0|]
@@ -2006,20 +2006,20 @@
10/10 (1): staticDrum1.Cs_sup.h_vol = staticDrum1.hl [dynamic |0|0|0|0|]
11/11 (1): staticDrum1.Cs_sup.h_vol = singularPressureLoss1.C1.h_vol [dynamic |0|0|0|0|]
12/12 (1): 0.0 = singularPressureLoss1.C1.h - singularPressureLoss1.C1.h_vol [dynamic |0|0|0|0|]
13/13 (1): staticDrum1.Cs_sup.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|]
14/14 (1): staticDrum1.Cs_eva.Q = 0.0 [dynamic |0|0|0|0|]
-15/15 (1): staticDrum1.Cs_eva.h = 100000.0 [dynamic |0|0|0|0|]
+15/15 (1): staticDrum1.Cs_eva.h = 1e5 [dynamic |0|0|0|0|]
16/16 (1): staticDrum1.Cs_sur.Q = 0.0 [dynamic |0|0|0|0|]
-17/17 (1): staticDrum1.Cs_sur.h = 100000.0 [dynamic |0|0|0|0|]
+17/17 (1): staticDrum1.Cs_sur.h = 1e5 [dynamic |0|0|0|0|]
18/18 (1): staticDrum1.Cs_purg.Q = 0.0 [dynamic |0|0|0|0|]
-19/19 (1): staticDrum1.Cs_purg.h = 100000.0 [dynamic |0|0|0|0|]
+19/19 (1): staticDrum1.Cs_purg.h = 1e5 [dynamic |0|0|0|0|]
20/20 (1): singularPressureLoss2.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|]
21/21 (1): singularPressureLoss2.C2.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|]
22/22 (1): singularPressureLoss2.C2.Q = staticDrum1.Ce_steam.Q [dynamic |0|0|0|0|]
23/23 (1): staticDrum1.Ce_sup.Q = 0.0 [dynamic |0|0|0|0|]
-24/24 (1): staticDrum1.Ce_sup.h = 100000.0 [dynamic |0|0|0|0|]
+24/24 (1): staticDrum1.Ce_sup.h = 1e5 [dynamic |0|0|0|0|]
25/25 (1): staticDrum1.Cth.W = 0.0 [dynamic |0|0|0|0|]
26/26 (1): staticDrum1.Ce_eco.Q * staticDrum1.Ce_eco.h + staticDrum1.Ce_steam.Q * staticDrum1.Ce_steam.h + staticDrum1.Ce_sup.Q * staticDrum1.Ce_sup.h + staticDrum1.Ce_eva.Q * staticDrum1.Ce_eva.h + staticDrum1.Cth.W - staticDrum1.Cs_sup.Q * staticDrum1.Cs_sup.h - staticDrum1.Cs_purg.Q * staticDrum1.Cs_purg.h - staticDrum1.Cs_sur.Q * staticDrum1.Cs_sur.h - staticDrum1.Cs_eva.Q * staticDrum1.Cs_eva.h = 0.0 [dynamic |0|0|0|0|]
27/27 (1): singularPressureLoss2.C2.h = staticDrum1.Ce_steam.h [dynamic |0|0|0|0|]
28/28 (1): singularPressureLoss2.C2.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|]
29/29 (1): staticDrum1.Cs_sup.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|]
@@ -2063,16 +2063,16 @@
Automatic Verification Steps of DataReconciliation Algorithm
==========================================================================
knownVariables:{76, 133, 137, 171, 175, 209, 213} (7)
========================================
-1: staticDrum1.hl:VARIABLE(start = 100000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Liquid phase specific enthalpy" type: Real
-2: singularPressureLoss3.h:VARIABLE(start = 100000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
+1: staticDrum1.hl:VARIABLE(start = 1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Liquid phase specific enthalpy" type: Real
+2: singularPressureLoss3.h:VARIABLE(start = 1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
3: singularPressureLoss3.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
-4: singularPressureLoss2.h:VARIABLE(start = 100000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
+4: singularPressureLoss2.h:VARIABLE(start = 1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
5: singularPressureLoss2.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
-6: singularPressureLoss1.h:VARIABLE(start = 100000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
+6: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
7: singularPressureLoss1.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
-SET_C:{71, 50, 51}
-SET_S:{124, 92, 91, 32, 123, 93, 90, 29, 151, 148, 39, 52, 38, 126, 127, 132, 133, 129, 130, 72, 69, 23, 120, 121, 46, 152, 26, 70, 35}
@@ -2085,20 +2085,20 @@
-Passed
-SET_C has known variables:{213, 209, 171} (3)
========================================
1: singularPressureLoss1.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
-2: singularPressureLoss1.h:VARIABLE(start = 100000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
-3: singularPressureLoss2.h:VARIABLE(start = 100000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
+2: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
+3: singularPressureLoss2.h:VARIABLE(start = 1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
-SET_S has known variables:{175, 137, 133, 76} (4)
========================================
1: singularPressureLoss2.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
2: singularPressureLoss3.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
-3: singularPressureLoss3.h:VARIABLE(start = 100000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
-4: staticDrum1.hl:VARIABLE(start = 100000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Liquid phase specific enthalpy" type: Real
+3: singularPressureLoss3.h:VARIABLE(start = 1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
+4: staticDrum1.hl:VARIABLE(start = 1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Liquid phase specific enthalpy" type: Real
Condition-3 "SET_C equations must be strictly less than Variable of Interest"
==========================================================================
-Passed
-SET_C contains:3 equations < 7 known variables
@@ -2107,35 +2107,36 @@
==========================================================================
-SET_C has intermediate variables:{206, 205, 167} (3)
========================================
1: 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
-2: 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
-3: 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
+2: singularPressureLoss1.C1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
+3: singularPressureLoss2.C1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
-SET_S has intermediate variables involved in SET_C:{206, 205, 167} (3)
========================================
1: 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
-2: 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
-3: 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
+2: singularPressureLoss1.C1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
+3: singularPressureLoss2.C1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
-Passed
Condition-5 "SET_S should be square"
==========================================================================
-Passed
Set_S has 29 equations and 29 variables
record SimulationResult
-resultFile = "econcile",
-simulationOptions = "startTime = 0.0, stopTime = 1.0, numberOfIntervals = 500, tolerance = 1e-06, method = 'dassl', fileNamePrefix = 'NewDataReconciliationSimpleTests.TSP_Splitter5', options = '', outputFormat = 'mat', variableFilter = '.*', cflags = '', simflags = '-reconcile -sx=./NewDataReconciliationSimpleTests/resources/NewDataReconciliationSimpleTests.TSP_Splitter5_Inputs.csv -eps=0.0023 -lv=LOG_JAC'",
-messages = "LOG_SUCCESS | info | The initialization finished successfully without homotopy method.
+resultFile = "",
+simulationOptions = "startTime = 0.0, stopTime = 1.0, numberOfIntervals = 500, tolerance = 1e-6, method = 'dassl', fileNamePrefix = 'NewDataReconciliationSimpleTests.TSP_Splitter5', options = '', outputFormat = 'mat', variableFilter = '.*', cflags = '', simflags = '-reconcile -sx=./NewDataReconciliationSimpleTests/resources/NewDataReconciliationSimpleTests.TSP_Splitter5_Inputs.csv -eps=0.0023 -lv=LOG_JAC'",
+messages = "Simulation execution failed for model: NewDataReconciliationSimpleTests.TSP_Splitter5
+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_Splitter5
-LOG_STDOUT | info | DataReconciliation Completed!
+LOG_STDOUT | error | Measurement input file path not found ./NewDataReconciliationSimpleTests/resources/NewDataReconciliationSimpleTests.TSP_Splitter5_Inputs.csv.
"
end SimulationResult;
"[openmodelica/dataReconciliation/NewDataReconciliationSimpleTests/SingularPressureLoss.mo:20:3-22:16:writable] Warning: Connector C1 is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[openmodelica/dataReconciliation/NewDataReconciliationSimpleTests/SingularPressureLoss.mo:23:3-24:52:writable] Warning: Connector C2 is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[openmodelica/dataReconciliation/NewDataReconciliationSimpleTests/SingularPressureLoss.mo:20:3-22:16:writable] Warning: Connector C1 is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
''
Equation mismatch: omc-diff says:
----------------------------Failed 'e' '"'
Line 2130: Text differs:
expected: resultFile = "econcile",
got: resultFile = "",
== 1 out of 1 tests failed [openmodelica/dataReconciliation/TSP_Splitter5.mos_temp9448, time: 19]