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Failed
openmodelica_dataReconciliation.TSP_Pipe11.mos (from (result.xml))
Stacktrace
Output mismatch (see stdout for details)
Standard Output
+ TSP_Pipe11 ... equation mismatch [time: 22]
==== Log C:\WINDOWS\TEMP/omc-rtest-OpenModelica/openmodelica/dataReconciliation/TSP_Pipe11.mos_temp5031/log-TSP_Pipe11.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_Pipe11
==========================================================================
OrderedVariables (102)
========================================
1: sourcePQ1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
2: sourcePQ1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
3: 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
4: 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
5: sourcePQ1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
6: sourcePQ1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
7: sourcePQ1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real
8: sourcePQ1.IPressure.signal:VARIABLE(flow=false ) type: Real
9: sourcePQ1.IMassFlow.signal:VARIABLE(flow=false ) type: Real
10: sourcePQ1.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real
11: sourcePQ1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real
12: sourcePQ1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real
13: singularPressureLoss2.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
14: singularPressureLoss2.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real
15: singularPressureLoss2.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real
16: singularPressureLoss2.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real
17: singularPressureLoss2.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real
18: 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
19: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
20: singularPressureLoss2.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real
21: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real
22: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
23: singularPressureLoss2.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
24: singularPressureLoss2.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
25: singularPressureLoss2.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
26: singularPressureLoss2.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
27: singularPressureLoss2.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
28: 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
29: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
30: singularPressureLoss2.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real
31: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
32: singularPressureLoss2.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real
33: singularPressureLoss2.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
34: singularPressureLoss2.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
35: 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
36: 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
37: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
38: singularPressureLoss2.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
39: singularPressureLoss2.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
40: singularPressureLoss2.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
41: 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
42: 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
43: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
44: singularPressureLoss2.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
45: singularPressureLoss2.h:VARIABLE(start = 1.1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
46: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real
47: singularPressureLoss2.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real
48: singularPressureLoss2.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real
49: singularPressureLoss2.Q:VARIABLE(start = 99.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
50: singularPressureLoss2.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real
51: singularPressureLoss1.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
52: singularPressureLoss1.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real
53: singularPressureLoss1.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real
54: singularPressureLoss1.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real
55: singularPressureLoss1.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real
56: 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
57: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
58: singularPressureLoss1.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real
59: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real
60: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
61: singularPressureLoss1.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
62: singularPressureLoss1.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
63: singularPressureLoss1.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
64: singularPressureLoss1.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
65: singularPressureLoss1.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
66: 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
67: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
68: singularPressureLoss1.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real
69: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
70: singularPressureLoss1.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real
71: singularPressureLoss1.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
72: singularPressureLoss1.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
73: 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
74: 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
75: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
76: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
77: singularPressureLoss1.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
78: singularPressureLoss1.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
79: 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
80: 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
81: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
82: singularPressureLoss1.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
83: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
84: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real
85: singularPressureLoss1.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real
86: singularPressureLoss1.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real
87: singularPressureLoss1.Q:VARIABLE(start = 100.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
88: singularPressureLoss1.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real
89: sink1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
90: sink1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
91: 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
92: 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
93: sink1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
94: sink1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
95: sink1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real
96: sink1.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real
97: sink1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real
98: sink1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real
99: sink1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real
100: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real
101: sourcePQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real
102: sourcePQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real
OrderedEquation (84, 102)
========================================
1/1 (1): sink1.h0 = 1e5 [binding |0|0|0|0|]
2/2 (1): sourcePQ1.P0 = 3e5 [binding |0|0|0|0|]
3/3 (1): sourcePQ1.Q0 = 100.0 [binding |0|0|0|0|]
4/4 (1): sourcePQ1.h0 = 105000.0 [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): singularPressureLoss2.C2.P = sink1.C.P [dynamic |0|0|0|0|]
12/12 (1): singularPressureLoss2.C2.Q = sink1.C.Q [dynamic |0|0|0|0|]
13/13 (1): singularPressureLoss2.C2.a = sink1.C.a [dynamic |0|0|0|0|]
14/14 (1): singularPressureLoss2.C2.b = sink1.C.b [dynamic |0|0|0|0|]
15/15 (1): singularPressureLoss2.C2.h = sink1.C.h [dynamic |0|0|0|0|]
16/16 (1): singularPressureLoss2.C2.h_vol = sink1.C.h_vol [dynamic |0|0|0|0|]
17/17 (1): singularPressureLoss1.C2.P = singularPressureLoss2.C1.P [dynamic |0|0|0|0|]
18/18 (1): singularPressureLoss1.C2.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|]
19/19 (1): singularPressureLoss1.C2.a = singularPressureLoss2.C1.a [dynamic |0|0|0|0|]
20/20 (1): singularPressureLoss1.C2.b = singularPressureLoss2.C1.b [dynamic |0|0|0|0|]
21/21 (1): singularPressureLoss1.C2.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|]
22/22 (1): singularPressureLoss1.C2.h_vol = singularPressureLoss2.C1.h_vol [dynamic |0|0|0|0|]
23/23 (1): sink1.C.P = sink1.P [dynamic |0|0|0|0|]
24/24 (1): sink1.C.Q = sink1.Q [dynamic |0|0|0|0|]
25/25 (1): sink1.C.h_vol = sink1.h [dynamic |0|0|0|0|]
26/26 (1): sink1.ISpecificEnthalpy.signal = sink1.h0 [dynamic |0|0|0|0|]
27/27 (1): sink1.h = sink1.ISpecificEnthalpy.signal [dynamic |0|0|0|0|]
28/28 (1): singularPressureLoss1.C1.P - singularPressureLoss1.C2.P = singularPressureLoss1.deltaP [dynamic |0|0|0|0|]
29/29 (1): singularPressureLoss1.C2.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|]
30/30 (1): singularPressureLoss1.C2.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|]
31/31 (1): singularPressureLoss1.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|]
32/32 (1): singularPressureLoss1.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|]
33/33 (1): 0.0 = singularPressureLoss1.C1.h - singularPressureLoss1.C1.h_vol [dynamic |0|0|0|0|]
34/34 (1): singularPressureLoss1.deltaP = singularPressureLoss1.K * singularPressureLoss1.Q * abs(singularPressureLoss1.Q) / singularPressureLoss1.rho [dynamic |0|0|0|0|]
35/35 (1): singularPressureLoss1.Pm = 0.5 * (singularPressureLoss1.C1.P + singularPressureLoss1.C2.P) [dynamic |0|0|0|0|]
36/36 (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) [dynamic |0|0|0|0|]
37/46 (1): singularPressureLoss1.h = singularPressureLoss1.pro_pT.h [dynamic |0|0|0|0|]
38/47 (1): singularPressureLoss1.rho = singularPressureLoss1.pro_pT.d [dynamic |0|0|0|0|]
39/48 (1): singularPressureLoss1.pro_ph.d = 0.0 [dynamic |0|0|0|0|]
40/49 (1): singularPressureLoss1.pro_ph.T = 0.0 [dynamic |0|0|0|0|]
41/50 (1): singularPressureLoss1.pro_ph.u = 0.0 [dynamic |0|0|0|0|]
42/51 (1): singularPressureLoss1.pro_ph.s = 0.0 [dynamic |0|0|0|0|]
43/52 (1): singularPressureLoss1.pro_ph.cp = 0.0 [dynamic |0|0|0|0|]
44/53 (1): singularPressureLoss1.pro_ph.ddhp = 0.0 [dynamic |0|0|0|0|]
45/54 (1): singularPressureLoss1.pro_ph.ddph = 0.0 [dynamic |0|0|0|0|]
46/55 (1): singularPressureLoss1.pro_ph.duph = 0.0 [dynamic |0|0|0|0|]
47/56 (1): singularPressureLoss1.pro_ph.duhp = 0.0 [dynamic |0|0|0|0|]
48/57 (1): singularPressureLoss1.pro_ph.x = 0.0 [dynamic |0|0|0|0|]
49/58 (1): singularPressureLoss2.C1.P - singularPressureLoss2.C2.P = singularPressureLoss2.deltaP [dynamic |0|0|0|0|]
50/59 (1): singularPressureLoss2.C2.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|]
51/60 (1): singularPressureLoss2.C2.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|]
52/61 (1): singularPressureLoss2.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|]
53/62 (1): singularPressureLoss2.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|]
54/63 (1): 0.0 = singularPressureLoss2.C1.h - singularPressureLoss2.C1.h_vol [dynamic |0|0|0|0|]
55/64 (1): singularPressureLoss2.deltaP = singularPressureLoss2.K * singularPressureLoss2.Q * abs(singularPressureLoss2.Q) / singularPressureLoss2.rho [dynamic |0|0|0|0|]
56/65 (1): singularPressureLoss2.Pm = 0.5 * (singularPressureLoss2.C1.P + singularPressureLoss2.C2.P) [dynamic |0|0|0|0|]
57/66 (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid) [dynamic |0|0|0|0|]
58/76 (1): singularPressureLoss2.h = singularPressureLoss2.pro_pT.h [dynamic |0|0|0|0|]
59/77 (1): singularPressureLoss2.rho = singularPressureLoss2.pro_pT.d [dynamic |0|0|0|0|]
60/78 (1): singularPressureLoss2.pro_ph.d = 0.0 [dynamic |0|0|0|0|]
61/79 (1): singularPressureLoss2.pro_ph.T = 0.0 [dynamic |0|0|0|0|]
62/80 (1): singularPressureLoss2.pro_ph.u = 0.0 [dynamic |0|0|0|0|]
63/81 (1): singularPressureLoss2.pro_ph.s = 0.0 [dynamic |0|0|0|0|]
64/82 (1): singularPressureLoss2.pro_ph.cp = 0.0 [dynamic |0|0|0|0|]
65/83 (1): singularPressureLoss2.pro_ph.ddhp = 0.0 [dynamic |0|0|0|0|]
66/84 (1): singularPressureLoss2.pro_ph.ddph = 0.0 [dynamic |0|0|0|0|]
67/85 (1): singularPressureLoss2.pro_ph.duph = 0.0 [dynamic |0|0|0|0|]
68/86 (1): singularPressureLoss2.pro_ph.duhp = 0.0 [dynamic |0|0|0|0|]
69/87 (1): singularPressureLoss2.pro_ph.x = 0.0 [dynamic |0|0|0|0|]
70/88 (1): sourcePQ1.C.P = sourcePQ1.P [dynamic |0|0|0|0|]
71/89 (1): sourcePQ1.C.Q = sourcePQ1.Q [dynamic |0|0|0|0|]
72/90 (1): sourcePQ1.C.h_vol = sourcePQ1.h [dynamic |0|0|0|0|]
73/91 (1): sourcePQ1.IMassFlow.signal = sourcePQ1.Q0 [dynamic |0|0|0|0|]
74/92 (1): sourcePQ1.Q = sourcePQ1.IMassFlow.signal [dynamic |0|0|0|0|]
75/93 (1): sourcePQ1.IPressure.signal = sourcePQ1.P0 [dynamic |0|0|0|0|]
76/94 (1): sourcePQ1.P = sourcePQ1.IPressure.signal [dynamic |0|0|0|0|]
77/95 (1): sourcePQ1.ISpecificEnthalpy.signal = sourcePQ1.h0 [dynamic |0|0|0|0|]
78/96 (1): sourcePQ1.h = sourcePQ1.ISpecificEnthalpy.signal [dynamic |0|0|0|0|]
79/97 (1): sink1.C.a = true [binding |0|0|0|0|]
80/98 (1): singularPressureLoss1.C1.a = true [binding |0|0|0|0|]
81/99 (1): singularPressureLoss1.C2.b = true [binding |0|0|0|0|]
82/100 (1): singularPressureLoss2.C1.a = true [binding |0|0|0|0|]
83/101 (1): singularPressureLoss2.C2.b = true [binding |0|0|0|0|]
84/102 (1): sourcePQ1.C.b = true [binding |0|0|0|0|]
Matching
========================================
102 variables and equations
var 1 is solved in eqn 102
var 2 is solved in eqn 7
var 3 is solved in eqn 9
var 4 is solved in eqn 89
var 5 is solved in eqn 90
var 6 is solved in eqn 88
var 7 is solved in eqn 95
var 8 is solved in eqn 93
var 9 is solved in eqn 91
var 10 is solved in eqn 96
var 11 is solved in eqn 92
var 12 is solved in eqn 94
var 13 is solved in eqn 68
var 14 is solved in eqn 75
var 15 is solved in eqn 74
var 16 is solved in eqn 73
var 17 is solved in eqn 72
var 18 is solved in eqn 71
var 19 is solved in eqn 70
var 20 is solved in eqn 69
var 21 is solved in eqn 76
var 22 is solved in eqn 67
var 23 is solved in eqn 87
var 24 is solved in eqn 86
var 25 is solved in eqn 85
var 26 is solved in eqn 84
var 27 is solved in eqn 83
var 28 is solved in eqn 82
var 29 is solved in eqn 81
var 30 is solved in eqn 80
var 31 is solved in eqn 78
var 32 is solved in eqn 79
var 33 is solved in eqn 101
var 34 is solved in eqn 13
var 35 is solved in eqn 60
var 36 is solved in eqn 59
var 37 is solved in eqn 16
var 38 is solved in eqn 58
var 39 is solved in eqn 20
var 40 is solved in eqn 100
var 41 is solved in eqn 21
var 42 is solved in eqn 18
var 43 is solved in eqn 63
var 44 is solved in eqn 17
var 45 is solved in eqn 61
var 46 is solved in eqn 65
var 47 is solved in eqn 66
var 48 is solved in eqn 77
var 49 is solved in eqn 62
var 50 is solved in eqn 64
var 51 is solved in eqn 38
var 52 is solved in eqn 45
var 53 is solved in eqn 44
var 54 is solved in eqn 43
var 55 is solved in eqn 42
var 56 is solved in eqn 41
var 57 is solved in eqn 40
var 58 is solved in eqn 39
var 59 is solved in eqn 46
var 60 is solved in eqn 47
var 61 is solved in eqn 57
var 62 is solved in eqn 56
var 63 is solved in eqn 55
var 64 is solved in eqn 54
var 65 is solved in eqn 53
var 66 is solved in eqn 52
var 67 is solved in eqn 51
var 68 is solved in eqn 50
var 69 is solved in eqn 48
var 70 is solved in eqn 49
var 71 is solved in eqn 99
var 72 is solved in eqn 19
var 73 is solved in eqn 30
var 74 is solved in eqn 29
var 75 is solved in eqn 22
var 76 is solved in eqn 35
var 77 is solved in eqn 8
var 78 is solved in eqn 98
var 79 is solved in eqn 33
var 80 is solved in eqn 6
var 81 is solved in eqn 10
var 82 is solved in eqn 5
var 83 is solved in eqn 31
var 84 is solved in eqn 36
var 85 is solved in eqn 37
var 86 is solved in eqn 34
var 87 is solved in eqn 32
var 88 is solved in eqn 28
var 89 is solved in eqn 14
var 90 is solved in eqn 97
var 91 is solved in eqn 15
var 92 is solved in eqn 12
var 93 is solved in eqn 25
var 94 is solved in eqn 11
var 95 is solved in eqn 26
var 96 is solved in eqn 27
var 97 is solved in eqn 24
var 98 is solved in eqn 23
var 99 is solved in eqn 1
var 100 is solved in eqn 2
var 101 is solved in eqn 3
var 102 is solved in eqn 4
Standard BLT of the original model:(102)
============================================================
102: sourcePQ1.h0: (4/4): (1): sourcePQ1.h0 = 105000.0
101: sourcePQ1.Q0: (3/3): (1): sourcePQ1.Q0 = 100.0
100: sourcePQ1.P0: (2/2): (1): sourcePQ1.P0 = 3e5
99: sink1.h0: (1/1): (1): sink1.h0 = 1e5
98: sink1.P: (23/23): (1): sink1.C.P = sink1.P
97: sink1.Q: (24/24): (1): sink1.C.Q = sink1.Q
96: sink1.h: (27/27): (1): sink1.h = sink1.ISpecificEnthalpy.signal
95: sink1.ISpecificEnthalpy.signal: (26/26): (1): sink1.ISpecificEnthalpy.signal = sink1.h0
94: sink1.C.P: (11/11): (1): singularPressureLoss2.C2.P = sink1.C.P
93: sink1.C.h_vol: (25/25): (1): sink1.C.h_vol = sink1.h
92: sink1.C.Q: (12/12): (1): singularPressureLoss2.C2.Q = sink1.C.Q
91: sink1.C.h: (15/15): (1): singularPressureLoss2.C2.h = sink1.C.h
90: sink1.C.a: (79/97): (1): sink1.C.a = true
89: sink1.C.b: (14/14): (1): singularPressureLoss2.C2.b = sink1.C.b
88: singularPressureLoss1.deltaP: (28/28): (1): singularPressureLoss1.C1.P - singularPressureLoss1.C2.P = singularPressureLoss1.deltaP
87: singularPressureLoss1.Q: (32/32): (1): singularPressureLoss1.Q = singularPressureLoss1.C1.Q
86: singularPressureLoss1.rho: (34/34): (1): singularPressureLoss1.deltaP = singularPressureLoss1.K * singularPressureLoss1.Q * abs(singularPressureLoss1.Q) / singularPressureLoss1.rho
85: singularPressureLoss1.T: (36/37): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid)
84: singularPressureLoss1.Pm: (36/36): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid)
83: singularPressureLoss1.h: (31/31): (1): singularPressureLoss1.h = singularPressureLoss1.C1.h
82: singularPressureLoss1.C1.P: (5/5): (1): sourcePQ1.C.P = singularPressureLoss1.C1.P
81: singularPressureLoss1.C1.h_vol: (10/10): (1): sourcePQ1.C.h_vol = singularPressureLoss1.C1.h_vol
80: singularPressureLoss1.C1.Q: (6/6): (1): sourcePQ1.C.Q = singularPressureLoss1.C1.Q
79: singularPressureLoss1.C1.h: (33/33): (1): 0.0 = singularPressureLoss1.C1.h - singularPressureLoss1.C1.h_vol
78: singularPressureLoss1.C1.a: (80/98): (1): singularPressureLoss1.C1.a = true
77: singularPressureLoss1.C1.b: (8/8): (1): sourcePQ1.C.b = singularPressureLoss1.C1.b
76: singularPressureLoss1.C2.P: (35/35): (1): singularPressureLoss1.Pm = 0.5 * (singularPressureLoss1.C1.P + singularPressureLoss1.C2.P)
75: singularPressureLoss1.C2.h_vol: (22/22): (1): singularPressureLoss1.C2.h_vol = singularPressureLoss2.C1.h_vol
74: singularPressureLoss1.C2.Q: (29/29): (1): singularPressureLoss1.C2.Q = singularPressureLoss1.C1.Q
73: singularPressureLoss1.C2.h: (30/30): (1): singularPressureLoss1.C2.h = singularPressureLoss1.C1.h
72: singularPressureLoss1.C2.a: (19/19): (1): singularPressureLoss1.C2.a = singularPressureLoss2.C1.a
71: singularPressureLoss1.C2.b: (81/99): (1): singularPressureLoss1.C2.b = true
70: singularPressureLoss1.pro_ph.T: (40/49): (1): singularPressureLoss1.pro_ph.T = 0.0
69: singularPressureLoss1.pro_ph.d: (39/48): (1): singularPressureLoss1.pro_ph.d = 0.0
68: singularPressureLoss1.pro_ph.u: (41/50): (1): singularPressureLoss1.pro_ph.u = 0.0
67: singularPressureLoss1.pro_ph.s: (42/51): (1): singularPressureLoss1.pro_ph.s = 0.0
66: singularPressureLoss1.pro_ph.cp: (43/52): (1): singularPressureLoss1.pro_ph.cp = 0.0
65: singularPressureLoss1.pro_ph.ddhp: (44/53): (1): singularPressureLoss1.pro_ph.ddhp = 0.0
64: singularPressureLoss1.pro_ph.ddph: (45/54): (1): singularPressureLoss1.pro_ph.ddph = 0.0
63: singularPressureLoss1.pro_ph.duph: (46/55): (1): singularPressureLoss1.pro_ph.duph = 0.0
62: singularPressureLoss1.pro_ph.duhp: (47/56): (1): singularPressureLoss1.pro_ph.duhp = 0.0
61: singularPressureLoss1.pro_ph.x: (48/57): (1): singularPressureLoss1.pro_ph.x = 0.0
60: singularPressureLoss1.pro_pT.d: (38/47): (1): singularPressureLoss1.rho = singularPressureLoss1.pro_pT.d
59: singularPressureLoss1.pro_pT.h: (37/46): (1): singularPressureLoss1.h = singularPressureLoss1.pro_pT.h
58: singularPressureLoss1.pro_pT.u: (36/39): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid)
57: singularPressureLoss1.pro_pT.s: (36/40): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid)
56: singularPressureLoss1.pro_pT.cp: (36/41): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid)
55: singularPressureLoss1.pro_pT.ddTp: (36/42): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid)
54: singularPressureLoss1.pro_pT.ddpT: (36/43): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid)
53: singularPressureLoss1.pro_pT.dupT: (36/44): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid)
52: singularPressureLoss1.pro_pT.duTp: (36/45): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid)
51: singularPressureLoss1.pro_pT.x: (36/38): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid)
50: singularPressureLoss2.deltaP: (55/64): (1): singularPressureLoss2.deltaP = singularPressureLoss2.K * singularPressureLoss2.Q * abs(singularPressureLoss2.Q) / singularPressureLoss2.rho
49: singularPressureLoss2.Q: (53/62): (1): singularPressureLoss2.Q = singularPressureLoss2.C1.Q
48: singularPressureLoss2.rho: (59/77): (1): singularPressureLoss2.rho = singularPressureLoss2.pro_pT.d
47: singularPressureLoss2.T: (57/66): (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid)
46: singularPressureLoss2.Pm: (56/65): (1): singularPressureLoss2.Pm = 0.5 * (singularPressureLoss2.C1.P + singularPressureLoss2.C2.P)
45: singularPressureLoss2.h: (52/61): (1): singularPressureLoss2.h = singularPressureLoss2.C1.h
44: singularPressureLoss2.C1.P: (17/17): (1): singularPressureLoss1.C2.P = singularPressureLoss2.C1.P
43: singularPressureLoss2.C1.h_vol: (54/63): (1): 0.0 = singularPressureLoss2.C1.h - singularPressureLoss2.C1.h_vol
42: singularPressureLoss2.C1.Q: (18/18): (1): singularPressureLoss1.C2.Q = singularPressureLoss2.C1.Q
41: singularPressureLoss2.C1.h: (21/21): (1): singularPressureLoss1.C2.h = singularPressureLoss2.C1.h
40: singularPressureLoss2.C1.a: (82/100): (1): singularPressureLoss2.C1.a = true
39: singularPressureLoss2.C1.b: (20/20): (1): singularPressureLoss1.C2.b = singularPressureLoss2.C1.b
38: singularPressureLoss2.C2.P: (49/58): (1): singularPressureLoss2.C1.P - singularPressureLoss2.C2.P = singularPressureLoss2.deltaP
37: singularPressureLoss2.C2.h_vol: (16/16): (1): singularPressureLoss2.C2.h_vol = sink1.C.h_vol
36: singularPressureLoss2.C2.Q: (50/59): (1): singularPressureLoss2.C2.Q = singularPressureLoss2.C1.Q
35: singularPressureLoss2.C2.h: (51/60): (1): singularPressureLoss2.C2.h = singularPressureLoss2.C1.h
34: singularPressureLoss2.C2.a: (13/13): (1): singularPressureLoss2.C2.a = sink1.C.a
33: singularPressureLoss2.C2.b: (83/101): (1): singularPressureLoss2.C2.b = true
32: singularPressureLoss2.pro_ph.T: (61/79): (1): singularPressureLoss2.pro_ph.T = 0.0
31: singularPressureLoss2.pro_ph.d: (60/78): (1): singularPressureLoss2.pro_ph.d = 0.0
30: singularPressureLoss2.pro_ph.u: (62/80): (1): singularPressureLoss2.pro_ph.u = 0.0
29: singularPressureLoss2.pro_ph.s: (63/81): (1): singularPressureLoss2.pro_ph.s = 0.0
28: singularPressureLoss2.pro_ph.cp: (64/82): (1): singularPressureLoss2.pro_ph.cp = 0.0
27: singularPressureLoss2.pro_ph.ddhp: (65/83): (1): singularPressureLoss2.pro_ph.ddhp = 0.0
26: singularPressureLoss2.pro_ph.ddph: (66/84): (1): singularPressureLoss2.pro_ph.ddph = 0.0
25: singularPressureLoss2.pro_ph.duph: (67/85): (1): singularPressureLoss2.pro_ph.duph = 0.0
24: singularPressureLoss2.pro_ph.duhp: (68/86): (1): singularPressureLoss2.pro_ph.duhp = 0.0
23: singularPressureLoss2.pro_ph.x: (69/87): (1): singularPressureLoss2.pro_ph.x = 0.0
22: singularPressureLoss2.pro_pT.d: (57/67): (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid)
21: singularPressureLoss2.pro_pT.h: (58/76): (1): singularPressureLoss2.h = singularPressureLoss2.pro_pT.h
20: singularPressureLoss2.pro_pT.u: (57/69): (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid)
19: singularPressureLoss2.pro_pT.s: (57/70): (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid)
18: singularPressureLoss2.pro_pT.cp: (57/71): (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid)
17: singularPressureLoss2.pro_pT.ddTp: (57/72): (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid)
16: singularPressureLoss2.pro_pT.ddpT: (57/73): (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid)
15: singularPressureLoss2.pro_pT.dupT: (57/74): (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid)
14: singularPressureLoss2.pro_pT.duTp: (57/75): (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid)
13: singularPressureLoss2.pro_pT.x: (57/68): (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid)
12: sourcePQ1.P: (76/94): (1): sourcePQ1.P = sourcePQ1.IPressure.signal
11: sourcePQ1.Q: (74/92): (1): sourcePQ1.Q = sourcePQ1.IMassFlow.signal
10: sourcePQ1.h: (78/96): (1): sourcePQ1.h = sourcePQ1.ISpecificEnthalpy.signal
9: sourcePQ1.IMassFlow.signal: (73/91): (1): sourcePQ1.IMassFlow.signal = sourcePQ1.Q0
8: sourcePQ1.IPressure.signal: (75/93): (1): sourcePQ1.IPressure.signal = sourcePQ1.P0
7: sourcePQ1.ISpecificEnthalpy.signal: (77/95): (1): sourcePQ1.ISpecificEnthalpy.signal = sourcePQ1.h0
6: sourcePQ1.C.P: (70/88): (1): sourcePQ1.C.P = sourcePQ1.P
5: sourcePQ1.C.h_vol: (72/90): (1): sourcePQ1.C.h_vol = sourcePQ1.h
4: sourcePQ1.C.Q: (71/89): (1): sourcePQ1.C.Q = sourcePQ1.Q
3: sourcePQ1.C.h: (9/9): (1): sourcePQ1.C.h = singularPressureLoss1.C1.h
2: sourcePQ1.C.a: (7/7): (1): sourcePQ1.C.a = singularPressureLoss1.C1.a
1: sourcePQ1.C.b: (84/102): (1): sourcePQ1.C.b = true
Variables of interest (6)
========================================
1: singularPressureLoss2.h:VARIABLE(start = 1.1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
2: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real
3: singularPressureLoss2.Q:VARIABLE(start = 99.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
4: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
5: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real
6: singularPressureLoss1.Q:VARIABLE(start = 100.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
Boundary conditions (4)
========================================
1: sink1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real
2: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real
3: sourcePQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real
4: sourcePQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real
Binding equations:(10)
============================================================
1: sourcePQ1.C.b: (84/102): (1): sourcePQ1.C.b = true
33: singularPressureLoss2.C2.b: (83/101): (1): singularPressureLoss2.C2.b = true
40: singularPressureLoss2.C1.a: (82/100): (1): singularPressureLoss2.C1.a = true
71: singularPressureLoss1.C2.b: (81/99): (1): singularPressureLoss1.C2.b = true
78: singularPressureLoss1.C1.a: (80/98): (1): singularPressureLoss1.C1.a = true
90: sink1.C.a: (79/97): (1): sink1.C.a = true
102: sourcePQ1.h0: (4/4): (1): sourcePQ1.h0 = 105000.0
101: sourcePQ1.Q0: (3/3): (1): sourcePQ1.Q0 = 100.0
100: sourcePQ1.P0: (2/2): (1): sourcePQ1.P0 = 3e5
99: sink1.h0: (1/1): (1): sink1.h0 = 1e5
E-BLT: equations that compute the variables of interest:(6)
============================================================
45: singularPressureLoss2.h: (52/61): (1): singularPressureLoss2.h = singularPressureLoss2.C1.h
46: singularPressureLoss2.Pm: (56/65): (1): singularPressureLoss2.Pm = 0.5 * (singularPressureLoss2.C1.P + singularPressureLoss2.C2.P)
49: singularPressureLoss2.Q: (53/62): (1): singularPressureLoss2.Q = singularPressureLoss2.C1.Q
83: singularPressureLoss1.h: (31/31): (1): singularPressureLoss1.h = singularPressureLoss1.C1.h
84: singularPressureLoss1.Pm: (36/36): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid)
87: singularPressureLoss1.Q: (32/32): (1): singularPressureLoss1.Q = singularPressureLoss1.C1.Q
Extracting SET-C and SET-S from E-BLT
Procedure is applied on each equation in the E-BLT
==========================================================================
>>>45: singularPressureLoss2.h: (52/61): (1): singularPressureLoss2.h = singularPressureLoss2.C1.h
41: singularPressureLoss2.C1.h: (21/21): (1): singularPressureLoss1.C2.h = singularPressureLoss2.C1.h
73: singularPressureLoss1.C2.h: (30/30): (1): singularPressureLoss1.C2.h = singularPressureLoss1.C1.h
79: singularPressureLoss1.C1.h: (33/33): (1): 0.0 = singularPressureLoss1.C1.h - singularPressureLoss1.C1.h_vol
81: singularPressureLoss1.C1.h_vol: (10/10): (1): sourcePQ1.C.h_vol = singularPressureLoss1.C1.h_vol
5: sourcePQ1.C.h_vol: (72/90): (1): sourcePQ1.C.h_vol = sourcePQ1.h
10: sourcePQ1.h: (78/96): (1): sourcePQ1.h = sourcePQ1.ISpecificEnthalpy.signal
7: sourcePQ1.ISpecificEnthalpy.signal: (77/95): (1): sourcePQ1.ISpecificEnthalpy.signal = sourcePQ1.h0
sourcePQ1.h0 is a boundary condition ---> exit procedure
Procedure failed
>>>46: singularPressureLoss2.Pm: (56/65): (1): singularPressureLoss2.Pm = 0.5 * (singularPressureLoss2.C1.P + singularPressureLoss2.C2.P)
44: singularPressureLoss2.C1.P: (17/17): (1): singularPressureLoss1.C2.P = singularPressureLoss2.C1.P
76: singularPressureLoss1.C2.P: (35/35): (1): singularPressureLoss1.Pm = 0.5 * (singularPressureLoss1.C1.P + singularPressureLoss1.C2.P)
82: singularPressureLoss1.C1.P: (5/5): (1): sourcePQ1.C.P = singularPressureLoss1.C1.P
6: sourcePQ1.C.P: (70/88): (1): sourcePQ1.C.P = sourcePQ1.P
12: sourcePQ1.P: (76/94): (1): sourcePQ1.P = sourcePQ1.IPressure.signal
8: sourcePQ1.IPressure.signal: (75/93): (1): sourcePQ1.IPressure.signal = sourcePQ1.P0
sourcePQ1.P0 is a boundary condition ---> exit procedure
Procedure failed
>>>49: singularPressureLoss2.Q: (53/62): (1): singularPressureLoss2.Q = singularPressureLoss2.C1.Q
42: singularPressureLoss2.C1.Q: (18/18): (1): singularPressureLoss1.C2.Q = singularPressureLoss2.C1.Q
74: singularPressureLoss1.C2.Q: (29/29): (1): singularPressureLoss1.C2.Q = singularPressureLoss1.C1.Q
80: singularPressureLoss1.C1.Q: (6/6): (1): sourcePQ1.C.Q = singularPressureLoss1.C1.Q
4: sourcePQ1.C.Q: (71/89): (1): sourcePQ1.C.Q = sourcePQ1.Q
11: sourcePQ1.Q: (74/92): (1): sourcePQ1.Q = sourcePQ1.IMassFlow.signal
9: sourcePQ1.IMassFlow.signal: (73/91): (1): sourcePQ1.IMassFlow.signal = sourcePQ1.Q0
sourcePQ1.Q0 is a boundary condition ---> exit procedure
Procedure failed
>>>83: singularPressureLoss1.h: (31/31): (1): singularPressureLoss1.h = singularPressureLoss1.C1.h
79: singularPressureLoss1.C1.h: (33/33): (1): 0.0 = singularPressureLoss1.C1.h - singularPressureLoss1.C1.h_vol
81: singularPressureLoss1.C1.h_vol: (10/10): (1): sourcePQ1.C.h_vol = singularPressureLoss1.C1.h_vol
5: sourcePQ1.C.h_vol: (72/90): (1): sourcePQ1.C.h_vol = sourcePQ1.h
10: sourcePQ1.h: (78/96): (1): sourcePQ1.h = sourcePQ1.ISpecificEnthalpy.signal
7: sourcePQ1.ISpecificEnthalpy.signal: (77/95): (1): sourcePQ1.ISpecificEnthalpy.signal = sourcePQ1.h0
sourcePQ1.h0 is a boundary condition ---> exit procedure
Procedure failed
>>>84: singularPressureLoss1.Pm: (36/36): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid)
85: singularPressureLoss1.T: (36/37): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid)
51: singularPressureLoss1.pro_pT.x: (36/38): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid)
52: singularPressureLoss1.pro_pT.duTp: (36/45): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid)
53: singularPressureLoss1.pro_pT.dupT: (36/44): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid)
54: singularPressureLoss1.pro_pT.ddpT: (36/43): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid)
55: singularPressureLoss1.pro_pT.ddTp: (36/42): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid)
56: singularPressureLoss1.pro_pT.cp: (36/41): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid)
57: singularPressureLoss1.pro_pT.s: (36/40): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid)
58: singularPressureLoss1.pro_pT.u: (36/39): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid)
59: singularPressureLoss1.pro_pT.h: (37/46): (1): singularPressureLoss1.h = singularPressureLoss1.pro_pT.h
60: singularPressureLoss1.pro_pT.d: (38/47): (1): singularPressureLoss1.rho = singularPressureLoss1.pro_pT.d
86: singularPressureLoss1.rho: (34/34): (1): singularPressureLoss1.deltaP = singularPressureLoss1.K * singularPressureLoss1.Q * abs(singularPressureLoss1.Q) / singularPressureLoss1.rho
88: singularPressureLoss1.deltaP: (28/28): (1): singularPressureLoss1.C1.P - singularPressureLoss1.C2.P = singularPressureLoss1.deltaP
76: singularPressureLoss1.C2.P: (35/35): (1): singularPressureLoss1.Pm = 0.5 * (singularPressureLoss1.C1.P + singularPressureLoss1.C2.P)
82: singularPressureLoss1.C1.P: (5/5): (1): sourcePQ1.C.P = singularPressureLoss1.C1.P
6: sourcePQ1.C.P: (70/88): (1): sourcePQ1.C.P = sourcePQ1.P
12: sourcePQ1.P: (76/94): (1): sourcePQ1.P = sourcePQ1.IPressure.signal
8: sourcePQ1.IPressure.signal: (75/93): (1): sourcePQ1.IPressure.signal = sourcePQ1.P0
sourcePQ1.P0 is a boundary condition ---> exit procedure
Procedure failed
>>>87: singularPressureLoss1.Q: (32/32): (1): singularPressureLoss1.Q = singularPressureLoss1.C1.Q
80: singularPressureLoss1.C1.Q: (6/6): (1): sourcePQ1.C.Q = singularPressureLoss1.C1.Q
4: sourcePQ1.C.Q: (71/89): (1): sourcePQ1.C.Q = sourcePQ1.Q
11: sourcePQ1.Q: (74/92): (1): sourcePQ1.Q = sourcePQ1.IMassFlow.signal
9: sourcePQ1.IMassFlow.signal: (73/91): (1): sourcePQ1.IMassFlow.signal = sourcePQ1.Q0
sourcePQ1.Q0 is a boundary condition ---> exit procedure
Procedure failed
Extraction procedure failed for iteration count: 1, re-running with modified model
==========================================================================
OrderedVariables (102)
========================================
1: sourcePQ1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
2: sourcePQ1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
3: 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
4: 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
5: sourcePQ1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
6: sourcePQ1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
7: sourcePQ1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real
8: sourcePQ1.IPressure.signal:VARIABLE(flow=false ) type: Real
9: sourcePQ1.IMassFlow.signal:VARIABLE(flow=false ) type: Real
10: sourcePQ1.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real
11: sourcePQ1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real
12: sourcePQ1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real
13: singularPressureLoss2.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
14: singularPressureLoss2.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real
15: singularPressureLoss2.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real
16: singularPressureLoss2.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real
17: singularPressureLoss2.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real
18: 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
19: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
20: singularPressureLoss2.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real
21: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real
22: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
23: singularPressureLoss2.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
24: singularPressureLoss2.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
25: singularPressureLoss2.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
26: singularPressureLoss2.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
27: singularPressureLoss2.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
28: 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
29: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
30: singularPressureLoss2.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit =
...[truncated 65324 chars]...
) "Singular pressure loss" type: Real
+50: singularPressureLoss2.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real
51: singularPressureLoss1.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
52: singularPressureLoss1.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real
53: singularPressureLoss1.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real
54: singularPressureLoss1.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real
55: singularPressureLoss1.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real
-56: 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
-57: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
-58: singularPressureLoss1.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real
-59: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real
-60: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
+56: 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
+57: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
+58: singularPressureLoss1.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real
+59: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real
+60: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
61: singularPressureLoss1.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
62: singularPressureLoss1.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
63: singularPressureLoss1.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
64: singularPressureLoss1.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
65: singularPressureLoss1.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
-66: 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
-67: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
-68: singularPressureLoss1.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real
-69: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
+66: 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
+67: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
+68: singularPressureLoss1.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real
+69: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
70: singularPressureLoss1.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real
71: singularPressureLoss1.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
72: singularPressureLoss1.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-73: 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
+73: 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
74: 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
-75: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-76: 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
+75: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
+76: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
77: singularPressureLoss1.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
78: singularPressureLoss1.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-79: 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
+79: 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
80: 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
-81: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-82: 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
-83: singularPressureLoss1.h:VARIABLE(start = 100000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
-84: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real
+81: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
+82: singularPressureLoss1.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
+83: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
+84: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real
85: singularPressureLoss1.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real
86: singularPressureLoss1.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real
87: singularPressureLoss1.Q:VARIABLE(start = 100.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
-88: singularPressureLoss1.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real
+88: singularPressureLoss1.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real
89: sink1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
90: sink1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-91: 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
+91: 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
92: 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
-93: sink1.C.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-94: 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
+93: sink1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
+94: sink1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
95: sink1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real
96: sink1.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real
97: sink1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real
-98: sink1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure" type: Real
+98: sink1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real
99: sink1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real
-100: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real
+100: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real
101: sourcePQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real
102: sourcePQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real
OrderedEquation (84, 102)
========================================
-1/1 (1): sink1.h0 = 100000.0 [binding |0|0|0|0|]
-2/2 (1): sourcePQ1.P0 = 300000.0 [binding |0|0|0|0|]
+1/1 (1): sink1.h0 = 1e5 [binding |0|0|0|0|]
+2/2 (1): sourcePQ1.P0 = 3e5 [binding |0|0|0|0|]
3/3 (1): sourcePQ1.Q0 = 100.0 [binding |0|0|0|0|]
4/4 (1): sourcePQ1.h0 = 105000.0 [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|]
@@ -313,12 +313,12 @@
Standard BLT of the original model:(102)
============================================================
102: sourcePQ1.h0: (4/4): (1): sourcePQ1.h0 = 105000.0
101: sourcePQ1.Q0: (3/3): (1): sourcePQ1.Q0 = 100.0
-100: sourcePQ1.P0: (2/2): (1): sourcePQ1.P0 = 300000.0
-99: sink1.h0: (1/1): (1): sink1.h0 = 100000.0
+100: sourcePQ1.P0: (2/2): (1): sourcePQ1.P0 = 3e5
+99: sink1.h0: (1/1): (1): sink1.h0 = 1e5
98: sink1.P: (23/23): (1): sink1.C.P = sink1.P
97: sink1.Q: (24/24): (1): sink1.C.Q = sink1.Q
96: sink1.h: (27/27): (1): sink1.h = sink1.ISpecificEnthalpy.signal
95: sink1.ISpecificEnthalpy.signal: (26/26): (1): sink1.ISpecificEnthalpy.signal = sink1.h0
94: sink1.C.P: (11/11): (1): singularPressureLoss2.C2.P = sink1.C.P
@@ -417,22 +417,22 @@
1: sourcePQ1.C.b: (84/102): (1): sourcePQ1.C.b = true
Variables of interest (6)
========================================
-1: singularPressureLoss2.h:VARIABLE(start = 110000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
-2: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real
+1: singularPressureLoss2.h:VARIABLE(start = 1.1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
+2: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real
3: singularPressureLoss2.Q:VARIABLE(start = 99.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
-4: singularPressureLoss1.h:VARIABLE(start = 100000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
-5: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real
+4: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
+5: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real
6: singularPressureLoss1.Q:VARIABLE(start = 100.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
Boundary conditions (4)
========================================
1: sink1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real
-2: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real
+2: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real
3: sourcePQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real
4: sourcePQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real
Binding equations:(10)
@@ -444,12 +444,12 @@
71: singularPressureLoss1.C2.b: (81/99): (1): singularPressureLoss1.C2.b = true
78: singularPressureLoss1.C1.a: (80/98): (1): singularPressureLoss1.C1.a = true
90: sink1.C.a: (79/97): (1): sink1.C.a = true
102: sourcePQ1.h0: (4/4): (1): sourcePQ1.h0 = 105000.0
101: sourcePQ1.Q0: (3/3): (1): sourcePQ1.Q0 = 100.0
-100: sourcePQ1.P0: (2/2): (1): sourcePQ1.P0 = 300000.0
-99: sink1.h0: (1/1): (1): sink1.h0 = 100000.0
+100: sourcePQ1.P0: (2/2): (1): sourcePQ1.P0 = 3e5
+99: sink1.h0: (1/1): (1): sink1.h0 = 1e5
E-BLT: equations that compute the variables of interest:(6)
============================================================
@@ -539,119 +539,119 @@
OrderedVariables (102)
========================================
1: sourcePQ1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
2: sourcePQ1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-3: 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
+3: 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
4: 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
-5: sourcePQ1.C.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-6: 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
+5: sourcePQ1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
+6: sourcePQ1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
7: sourcePQ1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real
8: sourcePQ1.IPressure.signal:VARIABLE(flow=false ) type: Real
9: sourcePQ1.IMassFlow.signal:VARIABLE(flow=false ) type: Real
10: sourcePQ1.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real
11: sourcePQ1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real
-12: sourcePQ1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure" type: Real
+12: sourcePQ1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real
13: singularPressureLoss2.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
14: singularPressureLoss2.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real
15: singularPressureLoss2.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real
16: singularPressureLoss2.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real
17: singularPressureLoss2.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real
-18: 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
-19: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
-20: singularPressureLoss2.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real
-21: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real
-22: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
+18: 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
+19: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
+20: singularPressureLoss2.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real
+21: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real
+22: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
23: singularPressureLoss2.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
24: singularPressureLoss2.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
25: singularPressureLoss2.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
26: singularPressureLoss2.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
27: singularPressureLoss2.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
-28: 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
-29: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
-30: singularPressureLoss2.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real
-31: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
+28: 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
+29: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
+30: singularPressureLoss2.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real
+31: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
32: singularPressureLoss2.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real
33: singularPressureLoss2.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
34: singularPressureLoss2.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-35: 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
+35: 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
36: 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
-37: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-38: 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
+37: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
+38: singularPressureLoss2.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
39: singularPressureLoss2.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
40: singularPressureLoss2.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-41: 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
+41: 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
42: 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
-43: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-44: 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
-45: singularPressureLoss2.h:VARIABLE(start = 110000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
-46: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real
+43: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
+44: singularPressureLoss2.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
+45: singularPressureLoss2.h:VARIABLE(start = 1.1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
+46: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real
47: singularPressureLoss2.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real
48: singularPressureLoss2.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real
49: singularPressureLoss2.Q:VARIABLE(start = 99.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
-50: singularPressureLoss2.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real
+50: singularPressureLoss2.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real
51: singularPressureLoss1.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
52: singularPressureLoss1.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real
53: singularPressureLoss1.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real
54: singularPressureLoss1.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real
55: singularPressureLoss1.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real
-56: 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
-57: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
-58: singularPressureLoss1.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real
-59: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real
-60: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
+56: 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
+57: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
+58: singularPressureLoss1.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real
+59: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real
+60: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
61: singularPressureLoss1.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real
62: singularPressureLoss1.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
63: singularPressureLoss1.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
64: singularPressureLoss1.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
65: singularPressureLoss1.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
-66: 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
-67: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
-68: singularPressureLoss1.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real
-69: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
+66: 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
+67: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real
+68: singularPressureLoss1.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real
+69: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real
70: singularPressureLoss1.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real
71: singularPressureLoss1.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
72: singularPressureLoss1.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-73: 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
+73: 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
74: 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
-75: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-76: 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
+75: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
+76: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
77: singularPressureLoss1.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
78: singularPressureLoss1.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-79: 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
+79: 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
80: 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
-81: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-82: 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
-83: singularPressureLoss1.h:VARIABLE(start = 100000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
-84: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real
+81: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
+82: singularPressureLoss1.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
+83: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
+84: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real
85: singularPressureLoss1.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real
86: singularPressureLoss1.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real
87: singularPressureLoss1.Q:VARIABLE(start = 100.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
-88: singularPressureLoss1.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real
+88: singularPressureLoss1.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real
89: sink1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
90: sink1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean
-91: 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
+91: 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
92: 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
-93: sink1.C.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
-94: 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
+93: sink1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real
+94: sink1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
95: sink1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real
96: sink1.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real
97: sink1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real
-98: sink1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure" type: Real
+98: sink1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real
99: sink1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real
-100: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real
+100: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real
101: sourcePQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real
102: sourcePQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real
OrderedEquation (84, 102)
========================================
1/1 (1): singularPressureLoss2.h = 0.0 [binding |0|0|0|0|]
2/2 (1): singularPressureLoss2.Pm = 0.0 [binding |0|0|0|0|]
3/3 (1): singularPressureLoss2.Q = 0.0 [binding |0|0|0|0|]
-4/4 (1): sink1.h0 = 100000.0 [binding |0|0|0|0|]
-5/5 (1): sourcePQ1.P0 = 300000.0 [binding |0|0|0|0|]
+4/4 (1): sink1.h0 = 1e5 [binding |0|0|0|0|]
+5/5 (1): sourcePQ1.P0 = 3e5 [binding |0|0|0|0|]
6/6 (1): sourcePQ1.Q0 = 100.0 [binding |0|0|0|0|]
7/7 (1): sourcePQ1.h0 = 105000.0 [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|]
@@ -839,12 +839,12 @@
Standard BLT of the original model:(102)
============================================================
102: sourcePQ1.h0: (7/7): (1): sourcePQ1.h0 = 105000.0
101: sourcePQ1.Q0: (6/6): (1): sourcePQ1.Q0 = 100.0
-100: sourcePQ1.P0: (5/5): (1): sourcePQ1.P0 = 300000.0
-99: sink1.h0: (4/4): (1): sink1.h0 = 100000.0
+100: sourcePQ1.P0: (5/5): (1): sourcePQ1.P0 = 3e5
+99: sink1.h0: (4/4): (1): sink1.h0 = 1e5
98: sink1.P: (26/26): (1): sink1.C.P = sink1.P
97: sink1.Q: (27/27): (1): sink1.C.Q = sink1.Q
96: sink1.h: (30/30): (1): sink1.h = sink1.ISpecificEnthalpy.signal
95: sink1.ISpecificEnthalpy.signal: (29/29): (1): sink1.ISpecificEnthalpy.signal = sink1.h0
94: sink1.C.P: (14/14): (1): singularPressureLoss2.C2.P = sink1.C.P
@@ -943,22 +943,22 @@
1: sourcePQ1.C.b: (84/102): (1): sourcePQ1.C.b = true
Variables of interest (6)
========================================
-1: singularPressureLoss2.h:VARIABLE(start = 110000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
-2: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real
+1: singularPressureLoss2.h:VARIABLE(start = 1.1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
+2: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real
3: singularPressureLoss2.Q:VARIABLE(start = 99.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
-4: singularPressureLoss1.h:VARIABLE(start = 100000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
-5: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real
+4: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
+5: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real
6: singularPressureLoss1.Q:VARIABLE(start = 100.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
Boundary conditions (4)
========================================
1: sink1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real
-2: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real
+2: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real
3: sourcePQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real
4: sourcePQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real
Binding equations:(13)
@@ -970,12 +970,12 @@
71: singularPressureLoss1.C2.b: (81/99): (1): singularPressureLoss1.C2.b = true
78: singularPressureLoss1.C1.a: (80/98): (1): singularPressureLoss1.C1.a = true
90: sink1.C.a: (79/97): (1): sink1.C.a = true
102: sourcePQ1.h0: (7/7): (1): sourcePQ1.h0 = 105000.0
101: sourcePQ1.Q0: (6/6): (1): sourcePQ1.Q0 = 100.0
-100: sourcePQ1.P0: (5/5): (1): sourcePQ1.P0 = 300000.0
-99: sink1.h0: (4/4): (1): sink1.h0 = 100000.0
+100: sourcePQ1.P0: (5/5): (1): sourcePQ1.P0 = 3e5
+99: sink1.h0: (4/4): (1): sink1.h0 = 1e5
49: singularPressureLoss2.Q: (3/3): (1): singularPressureLoss2.Q = 0.0
46: singularPressureLoss2.Pm: (2/2): (1): singularPressureLoss2.Pm = 0.0
45: singularPressureLoss2.h: (1/1): (1): singularPressureLoss2.h = 0.0
@@ -1116,27 +1116,27 @@
Parameters in SET_S (6)
========================================
1: singularPressureLoss2.mode:PARAM() = 0 "IF97 region. 1:liquid - 2:steam - 4:saturation line - 0:automatic" type: Integer
2: singularPressureLoss2.fluid:PARAM() = 1 "1: water/steam - 2: C3H3F5" type: Integer
-3: singularPressureLoss2.K:PARAM() = 0.0001 "Pressure loss coefficient" type: Real
+3: singularPressureLoss2.K:PARAM() = 1e-4 "Pressure loss coefficient" type: Real
4: singularPressureLoss1.mode:PARAM() = 0 "IF97 region. 1:liquid - 2:steam - 4:saturation line - 0:automatic" type: Integer
5: singularPressureLoss1.fluid:PARAM() = 1 "1: water/steam - 2: C3H3F5" type: Integer
-6: singularPressureLoss1.K:PARAM() = 0.0001 "Pressure loss coefficient" type: Real
+6: singularPressureLoss1.K:PARAM() = 1e-4 "Pressure loss coefficient" type: Real
Automatic Verification Steps of DataReconciliation Algorithm
==========================================================================
knownVariables:{45, 46, 49, 83, 84, 87} (6)
========================================
-1: singularPressureLoss2.h:VARIABLE(start = 110000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
-2: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real
+1: singularPressureLoss2.h:VARIABLE(start = 1.1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
+2: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real
3: singularPressureLoss2.Q:VARIABLE(start = 99.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
-4: singularPressureLoss1.h:VARIABLE(start = 100000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
-5: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real
+4: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
+5: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real
6: singularPressureLoss1.Q:VARIABLE(start = 100.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
-SET_C:{34, 38, 35}
-SET_S:{55, 24, 33, 39, 40, 41, 37, 60, 61, 62, 58, 52, 59, 20, 31, 56, 21, 32}
@@ -1149,19 +1149,19 @@
-Passed
-SET_C has known variables:{87, 84, 83} (3)
========================================
1: singularPressureLoss1.Q:VARIABLE(start = 100.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
-2: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real
-3: singularPressureLoss1.h:VARIABLE(start = 100000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
+2: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real
+3: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
-SET_S has known variables:{49, 46, 45} (3)
========================================
1: singularPressureLoss2.Q:VARIABLE(start = 99.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real
-2: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real
-3: singularPressureLoss2.h:VARIABLE(start = 110000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
+2: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real
+3: singularPressureLoss2.h:VARIABLE(start = 1.1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real
Condition-3 "SET_C equations must be strictly less than Variable of Interest"
==========================================================================
-Passed
-SET_C contains:3 equations < 6 known variables
@@ -1170,37 +1170,38 @@
==========================================================================
-SET_C has intermediate variables:{80, 76, 82, 79} (4)
========================================
1: singularPressureLoss1.C1.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real
-2: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real
-3: 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
-4: 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
+2: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
+3: singularPressureLoss1.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
+4: 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
-SET_S has intermediate variables involved in SET_C:{80, 76, 82, 79} (4)
========================================
1: singularPressureLoss1.C1.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real
-2: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real
-3: 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
-4: 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
+2: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
+3: singularPressureLoss1.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real
+4: 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
-Passed
Condition-5 "SET_S should be square"
==========================================================================
-Passed
Set_S has 36 equations and 36 variables
record SimulationResult
-resultFile = "econcile",
-simulationOptions = "startTime = 0.0, stopTime = 1.0, numberOfIntervals = 500, tolerance = 1e-06, method = 'dassl', fileNamePrefix = 'NewDataReconciliationSimpleTests.TSP_Pipe11', options = '', outputFormat = 'mat', variableFilter = '.*', cflags = '', simflags = '-reconcile -sx=./NewDataReconciliationSimpleTests/resources/NewDataReconciliationSimpleTests.TSP_Pipe11_Inputs.csv -eps=0.0023 -lv=LOG_JAC'",
-messages = "LOG_SUCCESS | info | The initialization finished successfully without homotopy method.
+resultFile = "",
+simulationOptions = "startTime = 0.0, stopTime = 1.0, numberOfIntervals = 500, tolerance = 1e-6, method = 'dassl', fileNamePrefix = 'NewDataReconciliationSimpleTests.TSP_Pipe11', options = '', outputFormat = 'mat', variableFilter = '.*', cflags = '', simflags = '-reconcile -sx=./NewDataReconciliationSimpleTests/resources/NewDataReconciliationSimpleTests.TSP_Pipe11_Inputs.csv -eps=0.0023 -lv=LOG_JAC'",
+messages = "Simulation execution failed for model: NewDataReconciliationSimpleTests.TSP_Pipe11
+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_Pipe11
-LOG_STDOUT | info | DataReconciliation Completed!
+LOG_STDOUT | error | Measurement input file path not found ./NewDataReconciliationSimpleTests/resources/NewDataReconciliationSimpleTests.TSP_Pipe11_Inputs.csv.
"
end SimulationResult;
"[openmodelica/dataReconciliation/NewDataReconciliationSimpleTests/Sink.mo:17:3-19:16:writable] Warning: Connector C is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[openmodelica/dataReconciliation/NewDataReconciliationSimpleTests/SingularPressureLoss.mo:20:3-22:16:writable] Warning: Connector C1 is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[openmodelica/dataReconciliation/NewDataReconciliationSimpleTests/SingularPressureLoss.mo:23:3-24:52:writable] Warning: Connector C2 is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
''
Equation mismatch: omc-diff says:
------------------------Failed 'e' '"'
Line 1195: Text differs:
expected: resultFile = "econcile",
got: resultFile = "",
== 1 out of 1 tests failed [openmodelica/dataReconciliation/TSP_Pipe11.mos_temp5031, time: 23]