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Failed
tests / 06 testsuite-clang 3/3 / openmodelica_dataReconciliation.TSP_Pipe3.mos (from (result.xml))
Stacktrace
Output mismatch (see stdout for details)
Standard Output
+ TSP_Pipe3 ... equation mismatch [time: 291]
==== Log /tmp/omc-rtest-unknown/openmodelica/dataReconciliation/TSP_Pipe3.mos_temp1659/log-TSP_Pipe3.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_Pipe3
==========================================================================
OrderedVariables (140)
========================================
1: singularPressureLoss3.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
2: singularPressureLoss3.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real
3: singularPressureLoss3.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real
4: singularPressureLoss3.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real
5: singularPressureLoss3.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real
6: 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
7: singularPressureLoss3.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
8: singularPressureLoss3.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real
9: singularPressureLoss3.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real
10: singularPressureLoss3.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
11: singularPressureLoss3.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
12: singularPressureLoss3.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
13: singularPressureLoss3.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
14: singularPressureLoss3.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
15: singularPressureLoss3.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
16: 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
17: singularPressureLoss3.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
18: singularPressureLoss3.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real
19: singularPressureLoss3.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
20: singularPressureLoss3.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real
21: singularPressureLoss3.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
22: singularPressureLoss3.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
23: 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
24: 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
25: singularPressureLoss3.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
26: singularPressureLoss3.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
27: singularPressureLoss3.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
28: singularPressureLoss3.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
29: 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
30: 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
31: singularPressureLoss3.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
32: singularPressureLoss3.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
33: singularPressureLoss3.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real
34: singularPressureLoss3.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real
35: singularPressureLoss3.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 uncertain=Uncertainty.refine) "Fluid temperature" type: Real
36: singularPressureLoss3.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real
37: singularPressureLoss3.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
38: singularPressureLoss3.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real
39: singularPressureLoss2.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
40: singularPressureLoss2.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real
41: singularPressureLoss2.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real
42: singularPressureLoss2.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real
43: singularPressureLoss2.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real
44: 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
45: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
46: singularPressureLoss2.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real
47: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real
48: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
49: singularPressureLoss2.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
50: singularPressureLoss2.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
51: singularPressureLoss2.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
52: singularPressureLoss2.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
53: singularPressureLoss2.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
54: 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
55: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
56: singularPressureLoss2.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real
57: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
58: singularPressureLoss2.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real
59: singularPressureLoss2.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
60: singularPressureLoss2.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
61: 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
62: 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
63: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
64: singularPressureLoss2.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
65: singularPressureLoss2.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
66: singularPressureLoss2.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
67: 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
68: 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
69: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
70: singularPressureLoss2.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
71: singularPressureLoss2.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real
72: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real
73: singularPressureLoss2.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 uncertain=Uncertainty.refine) "Fluid temperature" type: Real
74: singularPressureLoss2.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real
75: singularPressureLoss2.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
76: singularPressureLoss2.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real
77: singularPressureLoss1.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
78: singularPressureLoss1.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real
79: singularPressureLoss1.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real
80: singularPressureLoss1.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real
81: singularPressureLoss1.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real
82: 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
83: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
84: singularPressureLoss1.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real
85: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real
86: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
87: singularPressureLoss1.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
88: singularPressureLoss1.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
89: singularPressureLoss1.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
90: singularPressureLoss1.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
91: singularPressureLoss1.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
92: 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
93: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
94: singularPressureLoss1.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real
95: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
96: singularPressureLoss1.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real
97: singularPressureLoss1.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
98: singularPressureLoss1.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
99: 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
100: 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
101: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
102: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
103: singularPressureLoss1.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
104: singularPressureLoss1.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
105: 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
106: 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
107: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
108: singularPressureLoss1.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
109: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real
110: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real
111: singularPressureLoss1.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 uncertain=Uncertainty.refine) "Fluid temperature" type: Real
112: singularPressureLoss1.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real
113: singularPressureLoss1.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
114: singularPressureLoss1.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real
115: sink1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
116: sink1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
117: 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
118: 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
119: sink1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
120: sink1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
121: sink1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real
122: sink1.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real
123: sink1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real
124: sink1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real
125: sourcePQ1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
126: sourcePQ1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
127: sourcePQ1.C.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
128: sourcePQ1.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
129: sourcePQ1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
130: sourcePQ1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
131: sourcePQ1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real
132: sourcePQ1.IPressure.signal:VARIABLE(flow=false ) type: Real
133: sourcePQ1.IMassFlow.signal:VARIABLE(flow=false ) type: Real
134: sourcePQ1.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real
135: sourcePQ1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real
136: sourcePQ1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real
137: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real
138: sourcePQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real
139: sourcePQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real
140: sink1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real
OrderedEquation (113, 140)
========================================
1/1 (1): sourcePQ1.P0 = 3e5 [binding |0|0|0|0|]
2/2 (1): sourcePQ1.Q0 = 100.0 [binding |0|0|0|0|]
3/3 (1): sourcePQ1.h0 = 1e5 [binding |0|0|0|0|]
4/4 (1): sink1.h0 = 1e5 [binding |0|0|0|0|]
5/5 (1): sourcePQ1.C.P = singularPressureLoss1.C1.P [dynamic |0|0|0|0|]
6/6 (1): sourcePQ1.C.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|]
7/7 (1): sourcePQ1.C.a = singularPressureLoss1.C1.a [dynamic |0|0|0|0|]
8/8 (1): sourcePQ1.C.b = singularPressureLoss1.C1.b [dynamic |0|0|0|0|]
9/9 (1): sourcePQ1.C.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|]
10/10 (1): sourcePQ1.C.h_vol = singularPressureLoss1.C1.h_vol [dynamic |0|0|0|0|]
11/11 (1): singularPressureLoss1.C2.P = singularPressureLoss2.C1.P [dynamic |0|0|0|0|]
12/12 (1): singularPressureLoss1.C2.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|]
13/13 (1): singularPressureLoss1.C2.a = singularPressureLoss2.C1.a [dynamic |0|0|0|0|]
14/14 (1): singularPressureLoss1.C2.b = singularPressureLoss2.C1.b [dynamic |0|0|0|0|]
15/15 (1): singularPressureLoss1.C2.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|]
16/16 (1): singularPressureLoss1.C2.h_vol = singularPressureLoss2.C1.h_vol [dynamic |0|0|0|0|]
17/17 (1): singularPressureLoss2.C2.P = singularPressureLoss3.C1.P [dynamic |0|0|0|0|]
18/18 (1): singularPressureLoss2.C2.Q = singularPressureLoss3.C1.Q [dynamic |0|0|0|0|]
19/19 (1): singularPressureLoss2.C2.a = singularPressureLoss3.C1.a [dynamic |0|0|0|0|]
20/20 (1): singularPressureLoss2.C2.b = singularPressureLoss3.C1.b [dynamic |0|0|0|0|]
21/21 (1): singularPressureLoss2.C2.h = singularPressureLoss3.C1.h [dynamic |0|0|0|0|]
22/22 (1): singularPressureLoss2.C2.h_vol = singularPressureLoss3.C1.h_vol [dynamic |0|0|0|0|]
23/23 (1): singularPressureLoss3.C2.P = sink1.C.P [dynamic |0|0|0|0|]
24/24 (1): singularPressureLoss3.C2.Q = sink1.C.Q [dynamic |0|0|0|0|]
25/25 (1): singularPressureLoss3.C2.a = sink1.C.a [dynamic |0|0|0|0|]
26/26 (1): singularPressureLoss3.C2.b = sink1.C.b [dynamic |0|0|0|0|]
27/27 (1): singularPressureLoss3.C2.h = sink1.C.h [dynamic |0|0|0|0|]
28/28 (1): singularPressureLoss3.C2.h_vol = sink1.C.h_vol [dynamic |0|0|0|0|]
29/29 (1): sourcePQ1.C.P = sourcePQ1.P [dynamic |0|0|0|0|]
30/30 (1): sourcePQ1.C.Q = sourcePQ1.Q [dynamic |0|0|0|0|]
31/31 (1): sourcePQ1.C.h_vol = sourcePQ1.h [dynamic |0|0|0|0|]
32/32 (1): sourcePQ1.IMassFlow.signal = sourcePQ1.Q0 [dynamic |0|0|0|0|]
33/33 (1): sourcePQ1.Q = sourcePQ1.IMassFlow.signal [dynamic |0|0|0|0|]
34/34 (1): sourcePQ1.IPressure.signal = sourcePQ1.P0 [dynamic |0|0|0|0|]
35/35 (1): sourcePQ1.P = sourcePQ1.IPressure.signal [dynamic |0|0|0|0|]
36/36 (1): sourcePQ1.ISpecificEnthalpy.signal = sourcePQ1.h0 [dynamic |0|0|0|0|]
37/37 (1): sourcePQ1.h = sourcePQ1.ISpecificEnthalpy.signal [dynamic |0|0|0|0|]
38/38 (1): sink1.C.P = sink1.P [dynamic |0|0|0|0|]
39/39 (1): sink1.C.Q = sink1.Q [dynamic |0|0|0|0|]
40/40 (1): sink1.C.h_vol = sink1.h [dynamic |0|0|0|0|]
41/41 (1): sink1.ISpecificEnthalpy.signal = sink1.h0 [dynamic |0|0|0|0|]
42/42 (1): sink1.h = sink1.ISpecificEnthalpy.signal [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): sourcePQ1.C.b = true [binding |0|0|0|0|]
107/134 (1): sink1.C.a = true [binding |0|0|0|0|]
108/135 (1): singularPressureLoss1.C1.a = true [binding |0|0|0|0|]
109/136 (1): singularPressureLoss1.C2.b = true [binding |0|0|0|0|]
110/137 (1): singularPressureLoss2.C1.a = true [binding |0|0|0|0|]
111/138 (1): singularPressureLoss2.C2.b = true [binding |0|0|0|0|]
112/139 (1): singularPressureLoss3.C1.a = true [binding |0|0|0|0|]
113/140 (1): singularPressureLoss3.C2.b = true [binding |0|0|0|0|]
Matching
========================================
140 variables and equations
var 1 is solved in eqn 113
var 2 is solved in eqn 120
var 3 is solved in eqn 119
var 4 is solved in eqn 118
var 5 is solved in eqn 117
var 6 is solved in eqn 116
var 7 is solved in eqn 115
var 8 is solved in eqn 114
var 9 is solved in eqn 121
var 10 is solved in eqn 112
var 11 is solved in eqn 132
var 12 is solved in eqn 131
var 13 is solved in eqn 130
var 14 is solved in eqn 129
var 15 is solved in eqn 128
var 16 is solved in eqn 127
var 17 is solved in eqn 126
var 18 is solved in eqn 125
var 19 is solved in eqn 123
var 20 is solved in eqn 124
var 21 is solved in eqn 140
var 22 is solved in eqn 25
var 23 is solved in eqn 105
var 24 is solved in eqn 104
var 25 is solved in eqn 28
var 26 is solved in eqn 103
var 27 is solved in eqn 20
var 28 is solved in eqn 139
var 29 is solved in eqn 21
var 30 is solved in eqn 18
var 31 is solved in eqn 108
var 32 is solved in eqn 17
var 33 is solved in eqn 106
var 34 is solved in eqn 110
var 35 is solved in eqn 111
var 36 is solved in eqn 122
var 37 is solved in eqn 107
var 38 is solved in eqn 109
var 39 is solved in eqn 83
var 40 is solved in eqn 90
var 41 is solved in eqn 89
var 42 is solved in eqn 88
var 43 is solved in eqn 87
var 44 is solved in eqn 86
var 45 is solved in eqn 85
var 46 is solved in eqn 84
var 47 is solved in eqn 91
var 48 is solved in eqn 82
var 49 is solved in eqn 102
var 50 is solved in eqn 101
var 51 is solved in eqn 100
var 52 is solved in eqn 99
var 53 is solved in eqn 98
var 54 is solved in eqn 97
var 55 is solved in eqn 96
var 56 is solved in eqn 95
var 57 is solved in eqn 93
var 58 is solved in eqn 94
var 59 is solved in eqn 138
var 60 is solved in eqn 19
var 61 is solved in eqn 75
var 62 is solved in eqn 74
var 63 is solved in eqn 22
var 64 is solved in eqn 73
var 65 is solved in eqn 14
var 66 is solved in eqn 137
var 67 is solved in eqn 15
var 68 is solved in eqn 12
var 69 is solved in eqn 78
var 70 is solved in eqn 11
var 71 is solved in eqn 76
var 72 is solved in eqn 80
var 73 is solved in eqn 81
var 74 is solved in eqn 92
var 75 is solved in eqn 77
var 76 is solved in eqn 79
var 77 is solved in eqn 53
var 78 is solved in eqn 60
var 79 is solved in eqn 59
var 80 is solved in eqn 58
var 81 is solved in eqn 57
var 82 is solved in eqn 56
var 83 is solved in eqn 55
var 84 is solved in eqn 54
var 85 is solved in eqn 61
var 86 is solved in eqn 52
var 87 is solved in eqn 72
var 88 is solved in eqn 71
var 89 is solved in eqn 70
var 90 is solved in eqn 69
var 91 is solved in eqn 68
var 92 is solved in eqn 67
var 93 is solved in eqn 66
var 94 is solved in eqn 65
var 95 is solved in eqn 63
var 96 is solved in eqn 64
var 97 is solved in eqn 136
var 98 is solved in eqn 13
var 99 is solved in eqn 45
var 100 is solved in eqn 44
var 101 is solved in eqn 16
var 102 is solved in eqn 43
var 103 is solved in eqn 8
var 104 is solved in eqn 135
var 105 is solved in eqn 48
var 106 is solved in eqn 6
var 107 is solved in eqn 10
var 108 is solved in eqn 5
var 109 is solved in eqn 46
var 110 is solved in eqn 50
var 111 is solved in eqn 51
var 112 is solved in eqn 62
var 113 is solved in eqn 47
var 114 is solved in eqn 49
var 115 is solved in eqn 26
var 116 is solved in eqn 134
var 117 is solved in eqn 27
var 118 is solved in eqn 24
var 119 is solved in eqn 40
var 120 is solved in eqn 23
var 121 is solved in eqn 41
var 122 is solved in eqn 42
var 123 is solved in eqn 39
var 124 is solved in eqn 38
var 125 is solved in eqn 133
var 126 is solved in eqn 7
var 127 is solved in eqn 9
var 128 is solved in eqn 30
var 129 is solved in eqn 31
var 130 is solved in eqn 29
var 131 is solved in eqn 36
var 132 is solved in eqn 34
var 133 is solved in eqn 32
var 134 is solved in eqn 37
var 135 is solved in eqn 33
var 136 is solved in eqn 35
var 137 is solved in eqn 1
var 138 is solved in eqn 2
var 139 is solved in eqn 3
var 140 is solved in eqn 4
Standard BLT of the original model:(140)
============================================================
140: sink1.h0: (4/4): (1): sink1.h0 = 1e5
139: sourcePQ1.h0: (3/3): (1): sourcePQ1.h0 = 1e5
138: sourcePQ1.Q0: (2/2): (1): sourcePQ1.Q0 = 100.0
137: sourcePQ1.P0: (1/1): (1): sourcePQ1.P0 = 3e5
136: sourcePQ1.P: (35/35): (1): sourcePQ1.P = sourcePQ1.IPressure.signal
135: sourcePQ1.Q: (33/33): (1): sourcePQ1.Q = sourcePQ1.IMassFlow.signal
134: sourcePQ1.h: (37/37): (1): sourcePQ1.h = sourcePQ1.ISpecificEnthalpy.signal
133: sourcePQ1.IMassFlow.signal: (32/32): (1): sourcePQ1.IMassFlow.signal = sourcePQ1.Q0
132: sourcePQ1.IPressure.signal: (34/34): (1): sourcePQ1.IPressure.signal = sourcePQ1.P0
131: sourcePQ1.ISpecificEnthalpy.signal: (36/36): (1): sourcePQ1.ISpecificEnthalpy.signal = sourcePQ1.h0
130: sourcePQ1.C.P: (29/29): (1): sourcePQ1.C.P = sourcePQ1.P
129: sourcePQ1.C.h_vol: (31/31): (1): sourcePQ1.C.h_vol = sourcePQ1.h
128: sourcePQ1.C.Q: (30/30): (1): sourcePQ1.C.Q = sourcePQ1.Q
127: sourcePQ1.C.h: (9/9): (1): sourcePQ1.C.h = singularPressureLoss1.C1.h
126: sourcePQ1.C.a: (7/7): (1): sourcePQ1.C.a = singularPressureLoss1.C1.a
125: sourcePQ1.C.b: (106/133): (1): sourcePQ1.C.b = true
124: sink1.P: (38/38): (1): sink1.C.P = sink1.P
123: sink1.Q: (39/39): (1): sink1.C.Q = sink1.Q
122: sink1.h: (42/42): (1): sink1.h = sink1.ISpecificEnthalpy.signal
121: sink1.ISpecificEnthalpy.signal: (41/41): (1): sink1.ISpecificEnthalpy.signal = sink1.h0
120: sink1.C.P: (23/23): (1): singularPressureLoss3.C2.P = sink1.C.P
119: sink1.C.h_vol: (40/40): (1): sink1.C.h_vol = sink1.h
118: sink1.C.Q: (24/24): (1): singularPressureLoss3.C2.Q = sink1.C.Q
117: sink1.C.h: (27/27): (1): singularPressureLoss3.C2.h = sink1.C.h
116: sink1.C.a: (107/134): (1): sink1.C.a = true
115: sink1.C.b: (26/26): (1): singularPressureLoss3.C2.b = sink1.C.b
114: singularPressureLoss1.deltaP: (49/49): (1): singularPressureLoss1.deltaP = singularPressureLoss1.K * singularPressureLoss1.Q * abs(singularPressureLoss1.Q) / singularPressureLoss1.rho
113: singularPressureLoss1.Q: (47/47): (1): singularPressureLoss1.Q = singularPressureLoss1.C1.Q
112: singularPressureLoss1.rho: (53/62): (1): singularPressureLoss1.rho = singularPressureLoss1.pro_pT.d
111: singularPressureLoss1.T: (51/51): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid)
110: singularPressureLoss1.Pm: (50/50): (1): singularPressureLoss1.Pm = 0.5 * (singularPressureLoss1.C1.P + singularPressureLoss1.C2.P)
109: singularPressureLoss1.h: (46/46): (1): singularPressureLoss1.h = singularPressureLoss1.C1.h
108: singularPressureLoss1.C1.P: (5/5): (1): sourcePQ1.C.P = singularPressureLoss1.C1.P
107: singularPressureLoss1.C1.h_vol: (10/10): (1): sourcePQ1.C.h_vol = singularPressureLoss1.C1.h_vol
106: singularPressureLoss1.C1.Q: (6/6): (1): sourcePQ1.C.Q = singularPressureLoss1.C1.Q
105: singularPressureLoss1.C1.h: (48/48): (1): 0.0 = singularPressureLoss1.C1.h - singularPressureLoss1.C1.h_vol
104: singularPressureLoss1.C1.a: (108/135): (1): singularPressureLoss1.C1.a = true
103: singularPressureLoss1.C1.b: (8/8): (1): sourcePQ1.C.b = singularPressureLoss1.C1.b
102: singularPressureLoss1.C2.P: (43/43): (1): singularPressureLoss1.C1.P - singularPressureLoss1.C2.P = singularPressureLoss1.deltaP
101: singularPressureLoss1.C2.h_vol: (16/16): (1): singularPressureLoss1.C2.h_vol = singularPressureLoss2.C1.h_vol
100: singularPressureLoss1.C2.Q: (44/44): (1): singularPressureLoss1.C2.Q = singularPressureLoss1.C1.Q
99: singularPressureLoss1.C2.h: (45/45): (1): singularPressureLoss1.C2.h = singularPressureLoss1.C1.h
98: singularPressureLoss1.C2.a: (13/13): (1): singularPressureLoss1.C2.a = singularPressureLoss2.C1.a
97: singularPressureLoss1.C2.b: (109/136): (1): singularPressureLoss1.C2.b = true
96: singularPressureLoss1.pro_ph.T: (55/64): (1): singularPressureLoss1.pro_ph.T = 0.0
95: singularPressureLoss1.pro_ph.d: (54/63): (1): singularPressureLoss1.pro_ph.d = 0.0
94: singularPressureLoss1.pro_ph.u: (56/65): (1): singularPressureLoss1.pro_ph.u = 0.0
93: singularPressureLoss1.pro_ph.s: (57/66): (1): singularPressureLoss1.pro_ph.s = 0.0
92: singularPressureLoss1.pro_ph.cp: (58/67): (1): singularPressureLoss1.pro_ph.cp = 0.0
91: singularPressureLoss1.pro_ph.ddhp: (59/68): (1): singularPressureLoss1.pro_ph.ddhp = 0.0
90: singularPressureLoss1.pro_ph.ddph: (60/69): (1): singularPressureLoss1.pro_ph.ddph = 0.0
89: singularPressureLoss1.pro_ph.duph: (61/70): (1): singularPressureLoss1.pro_ph.duph = 0.0
88: singularPressureLoss1.pro_ph.duhp: (62/71): (1): singularPressureLoss1.pro_ph.duhp = 0.0
87: singularPressureLoss1.pro_ph.x: (63/72): (1): singularPressureLoss1.pro_ph.x = 0.0
86: singularPressureLoss1.pro_pT.d: (51/52): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid)
85: singularPressureLoss1.pro_pT.h: (52/61): (1): singularPressureLoss1.h = singularPressureLoss1.pro_pT.h
84: singularPressureLoss1.pro_pT.u: (51/54): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid)
83: singularPressureLoss1.pro_pT.s: (51/55): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid)
82: singularPressureLoss1.pro_pT.cp: (51/56): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid)
81: singularPressureLoss1.pro_pT.ddTp: (51/57): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid)
80: singularPressureLoss1.pro_pT.ddpT: (51/58): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid)
79: singularPressureLoss1.pro_pT.dupT: (51/59): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid)
78: singularPressureLoss1.pro_pT.duTp: (51/60): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid)
77: singularPressureLoss1.pro_pT.x: (51/53): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid)
76: singularPressureLoss2.deltaP: (70/79): (1): singularPressureLoss2.deltaP = singularPressureLoss2.K * singularPressureLoss2.Q * abs(singularPressureLoss2.Q) / singularPressureLoss2.rho
75: singularPressureLoss2.Q: (68/77): (1): singularPressureLoss2.Q = singularPressureLoss2.C1.Q
74: singularPressureLoss2.rho: (74/92): (1): singularPressureLoss2.rho = singularPressureLoss2.pro_pT.d
73: singularPressureLoss2.T: (72/81): (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid)
72: singularPressureLoss2.Pm: (71/80): (1): singularPressureLoss2.Pm = 0.5 * (singularPressureLoss2.C1.P + singularPressureLoss2.C2.P)
71: singularPressureLoss2.h: (67/76): (1): singularPressureLoss2.h = singularPressureLoss2.C1.h
70: singularPressureLoss2.C1.P: (11/11): (1): singularPressureLoss1.C2.P = singularPressureLoss2.C1.P
69: singularPressureLoss2.C1.h_vol: (69/78): (1): 0.0 = singularPressureLoss2.C1.h - singularPressureLoss2.C1.h_vol
68: singularPressureLoss2.C1.Q: (12/12): (1): singularPressureLoss1.C2.Q = singularPressureLoss2.C1.Q
67: singularPressureLoss2.C1.h: (15/15): (1): singularPressureLoss1.C2.h = singularPressureLoss2.C1.h
66: singularPressureLoss2.C1.a: (110/137): (1): singularPressureLoss2.C1.a = true
65: singularPressureLoss2.C1.b: (14/14): (1): singularPressureLoss1.C2.b = singularPressureLoss2.C1.b
64: singularPressureLoss2.C2.P: (64/73): (1): singularPressureLoss2.C1.P - singularPressureLoss2.C2.P = singularPressureLoss2.deltaP
63: singularPressureLoss2.C2.h_vol: (22/22): (1): singularPressureLoss2.C2.h_vol = singularPressureLoss3.C1.h_vol
62: singularPressureLoss2.C2.Q: (65/74): (1): singularPressureLoss2.C2.Q = singularPressureLoss2.C1.Q
61: singularPressureLoss2.C2.h: (66/75): (1): singularPressureLoss2.C2.h = singularPressureLoss2.C1.h
60: singularPressureLoss2.C2.a: (19/19): (1): singularPressureLoss2.C2.a = singularPressureLoss3.C1.a
59: singularPressureLoss2.C2.b: (111/138): (1): singularPressureLoss2.C2.b = true
58: singularPressureLoss2.pro_ph.T: (76/94): (1): singularPressureLoss2.pro_ph.T = 0.0
57: singularPressureLoss2.pro_ph.d: (75/93): (1): singularPressureLoss2.pro_ph.d = 0.0
56: singularPressureLoss2.pro_ph.u: (77/95): (1): singularPressureLoss2.pro_ph.u = 0.0
55: singularPressureLoss2.pro_ph.s: (78/96): (1): singularPressureLoss2.pro_ph.s = 0.0
54: singularPressureLoss2.pro_ph.cp: (79/97): (1): singularPressureLoss2.pro_ph.cp = 0.0
53: singularPressureLoss2.pro_ph.ddhp: (80/98): (1): singularPressureLoss2.pro_ph.ddhp = 0.0
52: singularPressureLoss2.pro_ph.ddph: (81/99): (1): singularPressureLoss2.pro_ph.ddph = 0.0
51: singularPressureLoss2.pro_ph.duph: (82/100): (1): singularPressureLoss2.pro_ph.duph = 0.0
50: singularPressureLoss2.pro_ph.duhp: (83/101): (1): singularPressureLoss2.pro_ph.duhp = 0.0
49: singularPressureLoss2.pro_ph.x: (84/102): (1): singularPressureLoss2.pro_ph.x = 0.0
48: singularPressureLoss2.pro_pT.d: (72/82): (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid)
47: singularPressureLoss2.pro_pT.h: (73/91): (1): singularPressureLoss2.h = singularPressureLoss2.pro_pT.h
46: singularPressureLoss2.pro_pT.u: (72/84): (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid)
45: singularPressureLoss2.pro_pT.s: (72/85): (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid)
44: singularPressureLoss2.pro_pT.cp: (72/86): (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid)
43: singularPressureLoss2.pro_pT.ddTp: (72/87): (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid)
42: singularPressureLoss2.pro_pT.ddpT: (72/88): (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid)
41: singularPressureLoss2.pro_pT.dupT: (72/89): (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid)
40: singularPressureLoss2.pro_pT.duTp: (72/90): (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid)
39: singularPressureLoss2.pro_pT.x: (72/83): (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid)
38: singularPressureLoss3.deltaP: (91/109): (1): singularPressureLoss3.deltaP = singularPressureLoss3.K * singularPressureLoss3.Q * abs(singularPressureLoss3.Q) / singularPressureLoss3.rho
37: singularPressureLoss3.Q: (89/107): (1): singularPressureLoss3.Q = singularPressureLoss3.C1.Q
36: singularPressureLoss3.rho: (95/122): (1): singularPressureLoss3.rho = singularPressureLoss3.pro_pT.d
35: singularPressureLoss3.T: (93/111): (10): singularPressureLoss3.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss3.Pm, singularPressureLoss3.T, singularPressureLoss3.mode, singularPressureLoss3.fluid)
34: singularPressureLoss3.Pm: (92/110): (1): singularPressureLoss3.Pm = 0.5 * (singularPressureLoss3.C1.P + singularPressureLoss3.C2.P)
33: singularPressureLoss3.h: (88/106): (1): singularPressureLoss3.h = singularPressureLoss3.C1.h
32: singularPressureLoss3.C1.P: (17/17): (1): singularPressureLoss2.C2.P = singularPressureLoss3.C1.P
31: singularPressureLoss3.C1.h_vol: (90/108): (1): 0.0 = singularPressureLoss3.C1.h - singularPressureLoss3.C1.h_vol
30: singularPressureLoss3.C1.Q: (18/18): (1): singularPressureLoss2.C2.Q = singularPressureLoss3.C1.Q
29: singularPressureLoss3.C1.h: (21/21): (1): singularPressureLoss2.C2.h = singularPressureLoss3.C1.h
28: singularPressureLoss3.C1.a: (112/139): (1): singularPressureLoss3.C1.a = true
27: singularPressureLoss3.C1.b: (20/20): (1): singularPressureLoss2.C2.b = singularPressureLoss3.C1.b
26: singularPressureLoss3.C2.P: (85/103): (1): singularPressureLoss3.C1.P - singularPressureLoss3.C2.P = singularPressureLoss3.deltaP
25: singularPressureLoss3.C2.h_vol: (28/28): (1): singularPressureLoss3.C2.h_vol = sink1.C.h_vol
24: singularPressureLoss3.C2.Q: (86/104): (1): singularPressureLoss3.C2.Q = singularPressureLoss3.C1.Q
23: singularPressureLoss3.C2.h: (87/105): (1): singularPressureLoss3.C2.h = singularPressureLoss3.C1.h
22: singularPressureLoss3.C2.a: (25/25): (1): singularPressureLoss3.C2.a = sink1.C.a
21: singularPressureLoss3.C2.b: (113/140): (1): singularPressureLoss3.C2.b = true
20: singularPressureLoss3.pro_ph.T: (97/124): (1): singularPressureLoss3.pro_ph.T = 0.0
19: singularPressureLoss3.pro_ph.d: (96/123): (1): singularPressureLoss3.pro_ph.d = 0.0
18: singularPressureLoss3.pro_ph.u: (98/125): (1): singularPressureLoss3.pro_ph.u = 0.0
17: singularPressureLoss3.pro_ph.s: (99/126): (1): singularPressureLoss3.pro_ph.s = 0.0
16: singularPressureLoss3.pro_ph.cp: (100/127): (1): singularPressureLoss3.pro_ph.cp = 0.0
15: singularPressureLoss3.pro_ph.ddhp: (101/128): (1): singularPressureLoss3.pro_ph.ddhp = 0.0
14: singularPressureLoss3.pro_ph.ddph: (102/129): (1): singularPressureLoss3.pro_ph.ddph = 0.0
13: singularPressureLoss3.pro_ph.duph: (103/130): (1): singularPressureLoss3.pro_ph.duph = 0.0
12: singularPressureLoss3.pro_ph.duhp: (104/131): (1): singularPressureLoss3.pro_ph.duhp = 0.0
11: singularPressureLoss3.pro_ph.x: (105/132): (1): singularPressureLoss3.pro_ph.x = 0.0
10: singularPressureLoss3.pro_pT.d: (93/112): (10): singularPressureLoss3.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss3.Pm, singularPressureLoss3.T, singularPressureLoss3.mode, singularPressureLoss3.fluid)
9: singularPressureLoss3.pro_pT.h: (94/121): (1): singularPressureLoss3.h = singularPressureLoss3.pro_pT.h
8: singularPressureLoss3.pro_pT.u: (93/114): (10): singularPressureLoss3.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss3.Pm, singularPressureLoss3.T, singularPressureLoss3.mode, singularPressureLoss3.fluid)
7: singularPressureLoss3.pro_pT.s: (93/115): (10): singularPressureLoss3.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss3.Pm, singularPressureLoss3.T, singularPressureLoss3.mode, singularPressureLoss3.fluid)
6: singularPressureLoss3.pro_pT.cp: (93/116): (10): singularPressureLoss3.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss3.Pm, singularPressureLoss3.T, singularPressureLoss3.mode, singularPressureLoss3.fluid)
5: singularPressureLoss3.pro_pT.ddTp: (93/117): (10): singularPressureLoss3.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss3.Pm, singularPressureLoss3.T, singularPressureLoss3.mode, singularPressureLoss3.fluid)
4: singularPressureLoss3.pro_pT.ddpT: (93/118): (10): singularPressureLoss3.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss3.Pm, singularPressureLoss3.T, singularPressureLoss3.mode, singularPressureLoss3.fluid)
3: singularPressureLoss3.pro_pT.dupT: (93/119): (10): singularPressureLoss3.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss3.Pm, singularPressureLoss3.T, singularPressureLoss3.mode, singularPressureLoss3.fluid)
2: singularP
...[truncated 207399 chars]...
2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
100: 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
-101: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-102: 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
+101: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
+102: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
103: singularPressureLoss1.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
104: singularPressureLoss1.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-105: 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
+105: 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
106: 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
-107: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-108: 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
-109: singularPressureLoss1.h:VARIABLE(start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real
-110: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real
+107: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
+108: singularPressureLoss1.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
+109: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real
+110: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real
111: singularPressureLoss1.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 uncertain=Uncertainty.refine) "Fluid temperature" type: Real
112: singularPressureLoss1.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real
113: singularPressureLoss1.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
-114: singularPressureLoss1.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real
+114: singularPressureLoss1.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real
115: sink1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
116: sink1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-117: sink1.C.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
+117: 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
118: 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
-119: sink1.C.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-120: sink1.C.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real
+119: sink1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
+120: sink1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
121: sink1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real
122: sink1.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real
123: sink1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real
-124: sink1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure" type: Real
+124: sink1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real
125: sourcePQ1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
126: sourcePQ1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-127: sourcePQ1.C.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
+127: sourcePQ1.C.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
128: sourcePQ1.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
-129: sourcePQ1.C.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-130: sourcePQ1.C.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real
+129: sourcePQ1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
+130: sourcePQ1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
131: sourcePQ1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real
132: sourcePQ1.IPressure.signal:VARIABLE(flow=false ) type: Real
133: sourcePQ1.IMassFlow.signal:VARIABLE(flow=false ) type: Real
134: sourcePQ1.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real
135: sourcePQ1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real
-136: sourcePQ1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure" type: Real
-137: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real
+136: sourcePQ1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real
+137: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real
138: sourcePQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real
139: sourcePQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real
140: sink1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real
OrderedEquation (113, 140)
========================================
1/1 (1): singularPressureLoss3.T = 0.0 [binding |0|0|0|0|]
2/2 (1): singularPressureLoss3.Q = 0.0 [binding |0|0|0|0|]
-3/3 (1): sourcePQ1.P0 = 300000.0 [binding |0|0|0|0|]
+3/3 (1): sourcePQ1.P0 = 3e5 [binding |0|0|0|0|]
4/4 (1): sourcePQ1.Q0 = 100.0 [binding |0|0|0|0|]
-5/5 (1): sourcePQ1.h0 = 100000.0 [binding |0|0|0|0|]
-6/6 (1): sink1.h0 = 100000.0 [binding |0|0|0|0|]
+5/5 (1): sourcePQ1.h0 = 1e5 [binding |0|0|0|0|]
+6/6 (1): sink1.h0 = 1e5 [binding |0|0|0|0|]
7/7 (1): sourcePQ1.C.P = singularPressureLoss1.C1.P [dynamic |0|0|0|0|]
8/8 (1): sourcePQ1.C.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|]
9/9 (1): sourcePQ1.C.a = singularPressureLoss1.C1.a [dynamic |0|0|0|0|]
10/10 (1): sourcePQ1.C.b = singularPressureLoss1.C1.b [dynamic |0|0|0|0|]
11/11 (1): sourcePQ1.C.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|]
@@ -1083,14 +1083,14 @@
var 140 is solved in eqn 6
Standard BLT of the original model:(140)
============================================================
-140: sink1.h0: (6/6): (1): sink1.h0 = 100000.0
-139: sourcePQ1.h0: (5/5): (1): sourcePQ1.h0 = 100000.0
+140: sink1.h0: (6/6): (1): sink1.h0 = 1e5
+139: sourcePQ1.h0: (5/5): (1): sourcePQ1.h0 = 1e5
138: sourcePQ1.Q0: (4/4): (1): sourcePQ1.Q0 = 100.0
-137: sourcePQ1.P0: (3/3): (1): sourcePQ1.P0 = 300000.0
+137: sourcePQ1.P0: (3/3): (1): sourcePQ1.P0 = 3e5
136: sourcePQ1.P: (31/31): (1): sourcePQ1.C.P = sourcePQ1.P
135: sourcePQ1.Q: (32/32): (1): sourcePQ1.C.Q = sourcePQ1.Q
134: sourcePQ1.h: (37/37): (1): sourcePQ1.h = sourcePQ1.ISpecificEnthalpy.signal
133: sourcePQ1.IMassFlow.signal: (34/34): (1): sourcePQ1.Q = sourcePQ1.IMassFlow.signal
132: sourcePQ1.IPressure.signal: (35/35): (1): sourcePQ1.P = sourcePQ1.IPressure.signal
@@ -1237,11 +1237,11 @@
6: singularPressureLoss1.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
Boundary conditions (4)
========================================
-1: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real
+1: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real
2: sourcePQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real
3: sourcePQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real
4: sink1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real
@@ -1254,14 +1254,14 @@
66: singularPressureLoss2.C1.a: (110/137): (1): singularPressureLoss2.C1.a = true
97: singularPressureLoss1.C2.b: (109/136): (1): singularPressureLoss1.C2.b = true
104: singularPressureLoss1.C1.a: (108/135): (1): singularPressureLoss1.C1.a = true
116: sink1.C.a: (107/134): (1): sink1.C.a = true
125: sourcePQ1.C.b: (106/133): (1): sourcePQ1.C.b = true
-140: sink1.h0: (6/6): (1): sink1.h0 = 100000.0
-139: sourcePQ1.h0: (5/5): (1): sourcePQ1.h0 = 100000.0
+140: sink1.h0: (6/6): (1): sink1.h0 = 1e5
+139: sourcePQ1.h0: (5/5): (1): sourcePQ1.h0 = 1e5
138: sourcePQ1.Q0: (4/4): (1): sourcePQ1.Q0 = 100.0
-137: sourcePQ1.P0: (3/3): (1): sourcePQ1.P0 = 300000.0
+137: sourcePQ1.P0: (3/3): (1): sourcePQ1.P0 = 3e5
37: singularPressureLoss3.Q: (2/2): (1): singularPressureLoss3.Q = 0.0
35: singularPressureLoss3.T: (1/1): (1): singularPressureLoss3.T = 0.0
E-BLT: equations that compute the variables of interest:(4)
@@ -1360,156 +1360,156 @@
1: singularPressureLoss3.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
2: singularPressureLoss3.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real
3: singularPressureLoss3.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real
4: singularPressureLoss3.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real
5: singularPressureLoss3.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real
-6: singularPressureLoss3.pro_pT.cp:VARIABLE(min = 1e-09 max = 9.999999999999999e+59 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real
-7: singularPressureLoss3.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
-8: singularPressureLoss3.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real
-9: singularPressureLoss3.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real
-10: singularPressureLoss3.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
+6: 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
+7: singularPressureLoss3.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
+8: singularPressureLoss3.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real
+9: singularPressureLoss3.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real
+10: singularPressureLoss3.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
11: singularPressureLoss3.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
12: singularPressureLoss3.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
13: singularPressureLoss3.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
14: singularPressureLoss3.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
15: singularPressureLoss3.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
-16: 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
-17: singularPressureLoss3.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
-18: singularPressureLoss3.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real
-19: singularPressureLoss3.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
+16: 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
+17: singularPressureLoss3.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
+18: singularPressureLoss3.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real
+19: singularPressureLoss3.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
20: singularPressureLoss3.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real
21: singularPressureLoss3.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
22: singularPressureLoss3.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-23: 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
+23: 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
24: 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
-25: singularPressureLoss3.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-26: 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
+25: singularPressureLoss3.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
+26: singularPressureLoss3.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
27: singularPressureLoss3.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
28: singularPressureLoss3.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-29: 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
+29: 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
30: 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
-31: singularPressureLoss3.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-32: 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
-33: singularPressureLoss3.h:VARIABLE(start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real
-34: singularPressureLoss3.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real
+31: singularPressureLoss3.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
+32: singularPressureLoss3.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
+33: singularPressureLoss3.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real
+34: singularPressureLoss3.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real
35: singularPressureLoss3.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 uncertain=Uncertainty.refine) "Fluid temperature" type: Real
36: singularPressureLoss3.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real
37: singularPressureLoss3.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
-38: singularPressureLoss3.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real
+38: singularPressureLoss3.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real
39: singularPressureLoss2.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
40: singularPressureLoss2.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real
41: singularPressureLoss2.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real
42: singularPressureLoss2.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real
43: singularPressureLoss2.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real
-44: 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
-45: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
-46: singularPressureLoss2.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real
-47: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real
-48: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
+44: 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
+45: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
+46: singularPressureLoss2.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real
+47: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real
+48: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
49: singularPressureLoss2.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
50: singularPressureLoss2.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
51: singularPressureLoss2.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
52: singularPressureLoss2.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
53: singularPressureLoss2.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
-54: 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
-55: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
-56: singularPressureLoss2.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real
-57: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
+54: 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
+55: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
+56: singularPressureLoss2.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real
+57: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
58: singularPressureLoss2.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real
59: singularPressureLoss2.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
60: singularPressureLoss2.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-61: 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
+61: 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
62: 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
-63: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-64: 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
+63: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
+64: singularPressureLoss2.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
65: singularPressureLoss2.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
66: singularPressureLoss2.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-67: 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
+67: 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
68: 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
-69: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-70: 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
-71: singularPressureLoss2.h:VARIABLE(start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real
-72: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real
+69: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
+70: singularPressureLoss2.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
+71: singularPressureLoss2.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real
+72: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real
73: singularPressureLoss2.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 uncertain=Uncertainty.refine) "Fluid temperature" type: Real
74: singularPressureLoss2.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real
75: singularPressureLoss2.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
-76: singularPressureLoss2.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real
+76: singularPressureLoss2.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real
77: singularPressureLoss1.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
78: singularPressureLoss1.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real
79: singularPressureLoss1.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real
80: singularPressureLoss1.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real
81: singularPressureLoss1.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real
-82: 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
-83: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
-84: singularPressureLoss1.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real
-85: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real
-86: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
+82: 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
+83: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
+84: singularPressureLoss1.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real
+85: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real
+86: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
87: singularPressureLoss1.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
88: singularPressureLoss1.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
89: singularPressureLoss1.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
90: singularPressureLoss1.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
91: singularPressureLoss1.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
-92: 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
-93: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
-94: singularPressureLoss1.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real
-95: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
+92: 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
+93: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
+94: singularPressureLoss1.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real
+95: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
96: singularPressureLoss1.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real
97: singularPressureLoss1.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
98: singularPressureLoss1.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-99: 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
+99: 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
100: 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
-101: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-102: 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
+101: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
+102: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
103: singularPressureLoss1.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
104: singularPressureLoss1.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-105: 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
+105: 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
106: 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
-107: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-108: 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
-109: singularPressureLoss1.h:VARIABLE(start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real
-110: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real
+107: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
+108: singularPressureLoss1.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
+109: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real
+110: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real
111: singularPressureLoss1.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 uncertain=Uncertainty.refine) "Fluid temperature" type: Real
112: singularPressureLoss1.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real
113: singularPressureLoss1.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
-114: singularPressureLoss1.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real
+114: singularPressureLoss1.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real
115: sink1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
116: sink1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-117: sink1.C.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
+117: 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
118: 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
-119: sink1.C.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-120: sink1.C.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real
+119: sink1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
+120: sink1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
121: sink1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real
122: sink1.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real
123: sink1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real
-124: sink1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure" type: Real
+124: sink1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real
125: sourcePQ1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
126: sourcePQ1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-127: sourcePQ1.C.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
+127: sourcePQ1.C.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
128: sourcePQ1.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
-129: sourcePQ1.C.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-130: sourcePQ1.C.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real
+129: sourcePQ1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
+130: sourcePQ1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
131: sourcePQ1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real
132: sourcePQ1.IPressure.signal:VARIABLE(flow=false ) type: Real
133: sourcePQ1.IMassFlow.signal:VARIABLE(flow=false ) type: Real
134: sourcePQ1.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real
135: sourcePQ1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real
-136: sourcePQ1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure" type: Real
-137: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real
+136: sourcePQ1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real
+137: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real
138: sourcePQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real
139: sourcePQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real
140: sink1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real
OrderedEquation (113, 140)
========================================
1/1 (1): singularPressureLoss2.T = 0.0 [binding |0|0|0|0|]
2/2 (1): singularPressureLoss3.T = 0.0 [binding |0|0|0|0|]
3/3 (1): singularPressureLoss3.Q = 0.0 [binding |0|0|0|0|]
-4/4 (1): sourcePQ1.P0 = 300000.0 [binding |0|0|0|0|]
+4/4 (1): sourcePQ1.P0 = 3e5 [binding |0|0|0|0|]
5/5 (1): sourcePQ1.Q0 = 100.0 [binding |0|0|0|0|]
-6/6 (1): sourcePQ1.h0 = 100000.0 [binding |0|0|0|0|]
-7/7 (1): sink1.h0 = 100000.0 [binding |0|0|0|0|]
+6/6 (1): sourcePQ1.h0 = 1e5 [binding |0|0|0|0|]
+7/7 (1): sink1.h0 = 1e5 [binding |0|0|0|0|]
8/8 (1): sourcePQ1.C.P = singularPressureLoss1.C1.P [dynamic |0|0|0|0|]
9/9 (1): sourcePQ1.C.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|]
10/10 (1): sourcePQ1.C.a = singularPressureLoss1.C1.a [dynamic |0|0|0|0|]
11/11 (1): sourcePQ1.C.b = singularPressureLoss1.C1.b [dynamic |0|0|0|0|]
12/12 (1): sourcePQ1.C.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|]
@@ -1760,14 +1760,14 @@
var 140 is solved in eqn 7
Standard BLT of the original model:(140)
============================================================
-140: sink1.h0: (7/7): (1): sink1.h0 = 100000.0
-139: sourcePQ1.h0: (6/6): (1): sourcePQ1.h0 = 100000.0
+140: sink1.h0: (7/7): (1): sink1.h0 = 1e5
+139: sourcePQ1.h0: (6/6): (1): sourcePQ1.h0 = 1e5
138: sourcePQ1.Q0: (5/5): (1): sourcePQ1.Q0 = 100.0
-137: sourcePQ1.P0: (4/4): (1): sourcePQ1.P0 = 300000.0
+137: sourcePQ1.P0: (4/4): (1): sourcePQ1.P0 = 3e5
136: sourcePQ1.P: (32/32): (1): sourcePQ1.C.P = sourcePQ1.P
135: sourcePQ1.Q: (33/33): (1): sourcePQ1.C.Q = sourcePQ1.Q
134: sourcePQ1.h: (34/34): (1): sourcePQ1.C.h_vol = sourcePQ1.h
133: sourcePQ1.IMassFlow.signal: (35/35): (1): sourcePQ1.Q = sourcePQ1.IMassFlow.signal
132: sourcePQ1.IPressure.signal: (36/36): (1): sourcePQ1.P = sourcePQ1.IPressure.signal
@@ -1914,11 +1914,11 @@
6: singularPressureLoss1.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
Boundary conditions (4)
========================================
-1: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real
+1: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real
2: sourcePQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real
3: sourcePQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real
4: sink1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real
@@ -1931,14 +1931,14 @@
66: singularPressureLoss2.C1.a: (110/137): (1): singularPressureLoss2.C1.a = true
97: singularPressureLoss1.C2.b: (109/136): (1): singularPressureLoss1.C2.b = true
104: singularPressureLoss1.C1.a: (108/135): (1): singularPressureLoss1.C1.a = true
116: sink1.C.a: (107/134): (1): sink1.C.a = true
125: sourcePQ1.C.b: (106/133): (1): sourcePQ1.C.b = true
-140: sink1.h0: (7/7): (1): sink1.h0 = 100000.0
-139: sourcePQ1.h0: (6/6): (1): sourcePQ1.h0 = 100000.0
+140: sink1.h0: (7/7): (1): sink1.h0 = 1e5
+139: sourcePQ1.h0: (6/6): (1): sourcePQ1.h0 = 1e5
138: sourcePQ1.Q0: (5/5): (1): sourcePQ1.Q0 = 100.0
-137: sourcePQ1.P0: (4/4): (1): sourcePQ1.P0 = 300000.0
+137: sourcePQ1.P0: (4/4): (1): sourcePQ1.P0 = 3e5
37: singularPressureLoss3.Q: (3/3): (1): singularPressureLoss3.Q = 0.0
35: singularPressureLoss3.T: (2/2): (1): singularPressureLoss3.T = 0.0
73: singularPressureLoss2.T: (1/1): (1): singularPressureLoss2.T = 0.0
@@ -2149,17 +2149,17 @@
Parameters in SET_S (9)
========================================
1: singularPressureLoss3.mode:PARAM() = 0 "IF97 region. 1:liquid - 2:steam - 4:saturation line - 0:automatic" type: Integer
2: singularPressureLoss3.fluid:PARAM() = 1 "1: water/steam - 2: C3H3F5" type: Integer
-3: singularPressureLoss3.K:PARAM() = 0.0001 "Pressure loss coefficient" type: Real
+3: singularPressureLoss3.K:PARAM() = 1e-4 "Pressure loss coefficient" type: Real
4: singularPressureLoss2.mode:PARAM() = 0 "IF97 region. 1:liquid - 2:steam - 4:saturation line - 0:automatic" type: Integer
5: singularPressureLoss2.fluid:PARAM() = 1 "1: water/steam - 2: C3H3F5" type: Integer
-6: singularPressureLoss2.K:PARAM() = 0.0001 "Pressure loss coefficient" type: Real
+6: singularPressureLoss2.K:PARAM() = 1e-4 "Pressure loss coefficient" type: Real
7: singularPressureLoss1.mode:PARAM() = 0 "IF97 region. 1:liquid - 2:steam - 4:saturation line - 0:automatic" type: Integer
8: singularPressureLoss1.fluid:PARAM() = 1 "1: water/steam - 2: C3H3F5" type: Integer
-9: singularPressureLoss1.K:PARAM() = 0.0001 "Pressure loss coefficient" type: Real
+9: singularPressureLoss1.K:PARAM() = 1e-4 "Pressure loss coefficient" type: Real
Automatic Verification Steps of DataReconciliation Algorithm
==========================================================================
@@ -2207,22 +2207,22 @@
-SET_C has intermediate variables:{106, 68, 102, 108, 110} (5)
========================================
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: 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
-3: 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
-4: 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
-5: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real
+3: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
+4: singularPressureLoss1.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
+5: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real
-SET_S has intermediate variables involved in SET_C:{106, 68, 102, 108, 110} (5)
========================================
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: 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
-3: 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
-4: 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
-5: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real
+3: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
+4: singularPressureLoss1.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
+5: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real
-Passed
Condition-5 "SET_S should be square"
==========================================================================
@@ -2231,17 +2231,16 @@
The selection of a new tearing variable failed.
record SimulationResult
resultFile = "",
-simulationOptions = "startTime = 0.0, stopTime = 1.0, numberOfIntervals = 500, tolerance = 1e-06, method = 'dassl', fileNamePrefix = 'NewDataReconciliationSimpleTests.TSP_Pipe3', options = '', outputFormat = 'mat', variableFilter = '.*', cflags = '', simflags = '-reconcile -sx=./NewDataReconciliationSimpleTests/resources/DataReconciliationSimpleTests.TSP_Pipe3_Inputs.csv -eps=0.0023 -lv=LOG_JAC'",
+simulationOptions = "startTime = 0.0, stopTime = 1.0, numberOfIntervals = 500, tolerance = 1e-6, method = 'dassl', fileNamePrefix = 'NewDataReconciliationSimpleTests.TSP_Pipe3', options = '', outputFormat = 'mat', variableFilter = '.*', cflags = '', simflags = '-reconcile -sx=./NewDataReconciliationSimpleTests/resources/DataReconciliationSimpleTests.TSP_Pipe3_Inputs.csv -eps=0.0023 -lv=LOG_JAC'",
messages = "Simulation execution failed for model: NewDataReconciliationSimpleTests.TSP_Pipe3
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_Pipe3
-LOG_STDOUT | warning | The default linear solver fails, the fallback solver with total pivoting is started at time 1.000000. That might raise performance issues, for more information use -lv LOG_LS.
LOG_NLS | error | residualFunc76: Iteration variable xloc[0] is nan.
LOG_ASSERT | debug | residualFunc76 failed at time=1.
| | | | For more information please use -lv LOG_NLS.
LOG_ASSERT | debug | Solving non-linear system 76 failed at time=1.
| | | | For more information please use -lv LOG_NLS.
Equation mismatch: omc-diff says:
--------------------------------Failed 'S' 'N'
Line 2242: Text differs:
expected: LOG_STDOUT | warning | The default linear solver fails, the fallback solver with total pivoting is started at time
got: LOG_NLS | error | residualFunc
== 1 out of 1 tests failed [openmodelica/dataReconciliation/TSP_Pipe3.mos_temp1659, time: 291]