Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ModelicaTest_3.2.1_ModelicaTest.Fluid.TestComponents.Vessels.TestInitialization.conf.json
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo", uses=false)
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo", uses=false)
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.2.3+maint.om/package.mo", uses=false)
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaTest 3.2.1+maint.om/package.mo", uses=false)
Using package ModelicaTest with version 3.2.1 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaTest 3.2.1+maint.om/package.mo)
Using package Modelica with version 3.2.3 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.2.3+maint.om/package.mo)
Using package Complex with version 4.0.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo)
Using package ModelicaServices with version 4.0.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo)
Running command: translateModel(ModelicaTest.Fluid.TestComponents.Vessels.TestInitialization,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ModelicaTest_3.2.1_ModelicaTest.Fluid.TestComponents.Vessels.TestInitialization")
translateModel(ModelicaTest.Fluid.TestComponents.Vessels.TestInitialization,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ModelicaTest_3.2.1_ModelicaTest.Fluid.TestComponents.Vessels.TestInitialization")
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo): time 0.001124/0.001124, allocations: 111 kB / 16.42 MB, free: 6.469 MB / 14.72 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo): time 0.001097/0.001097, allocations: 189.5 kB / 17.36 MB, free: 5.707 MB / 14.72 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.2.3+maint.om/package.mo): time 1.201/1.201, allocations: 205.1 MB / 223.2 MB, free: 12.24 MB / 190.1 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaTest 3.2.1+maint.om/package.mo): time 0.1558/0.1558, allocations: 38 MB / 308.6 MB, free: 5.977 MB / 254.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 1.752e-05/1.752e-05, allocations: 2.281 kB / 433.6 MB, free: 14.48 MB / 318.1 MB
Notification: Performance of NFInst.instantiate(ModelicaTest.Fluid.TestComponents.Vessels.TestInitialization): time 0.3323/0.3323, allocations: 152 MB / 0.5719 GB, free: 13.03 MB / 414.1 MB
Notification: Performance of NFInst.instExpressions: time 0.01106/0.3434, allocations: 10.38 MB / 0.582 GB, free: 10.35 MB / 414.1 MB
Notification: Performance of NFInst.updateImplicitVariability: time 0.0009424/0.3444, allocations: 34.09 kB / 0.5821 GB, free: 10.33 MB / 414.1 MB
Notification: Performance of NFTyping.typeComponents: time 0.001284/0.3457, allocations: 413 kB / 0.5825 GB, free: 10.02 MB / 414.1 MB
Notification: Performance of NFTyping.typeBindings: time 0.003422/0.3491, allocations: 1.436 MB / 0.5839 GB, free: 9.137 MB / 414.1 MB
Notification: Performance of NFTyping.typeClassSections: time 0.005734/0.3549, allocations: 2.721 MB / 0.5865 GB, free: 7.543 MB / 414.1 MB
Notification: Performance of NFFlatten.flatten: time 0.002941/0.3578, allocations: 2.85 MB / 0.5893 GB, free: 6.086 MB / 414.1 MB
Notification: Performance of NFFlatten.resolveConnections: time 0.0008902/0.3587, allocations: 0.7328 MB / 0.59 GB, free: 5.414 MB / 414.1 MB
Notification: Performance of NFEvalConstants.evaluate: time 0.00144/0.3602, allocations: 1.143 MB / 0.5911 GB, free: 4.344 MB / 414.1 MB
Notification: Performance of NFSimplifyModel.simplify: time 0.001184/0.3614, allocations: 1.037 MB / 0.5921 GB, free: 3.383 MB / 414.1 MB
Notification: Performance of NFPackage.collectConstants: time 0.0001407/0.3615, allocations: 100 kB / 0.5922 GB, free: 3.285 MB / 414.1 MB
Notification: Performance of NFFlatten.collectFunctions: time 0.003546/0.3651, allocations: 2.038 MB / 0.5942 GB, free: 1.359 MB / 414.1 MB
Notification: Performance of combineBinaries: time 0.001513/0.3666, allocations: 1.956 MB / 0.5961 GB, free: 15.47 MB / 430.1 MB
Notification: Performance of replaceArrayConstructors: time 0.0007746/0.3674, allocations: 1.158 MB / 0.5973 GB, free: 14.35 MB / 430.1 MB
Notification: Performance of NFVerifyModel.verify: time 0.0002254/0.3676, allocations: 163.5 kB / 0.5974 GB, free: 14.19 MB / 430.1 MB
Notification: Performance of FrontEnd: time 0.0001559/0.3678, allocations: 34.08 kB / 0.5975 GB, free: 14.16 MB / 430.1 MB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 179 (143)
 * Number of variables: 187 (141)
Notification: Performance of Bindings: time 0.004525/0.3723, allocations: 5.154 MB / 0.6025 GB, free: 8.895 MB / 430.1 MB
Notification: Performance of FunctionAlias: time 0.0005307/0.3729, allocations: 0.5371 MB / 0.603 GB, free: 8.375 MB / 430.1 MB
Notification: Performance of Early Inline: time 0.002982/0.3759, allocations: 3.222 MB / 0.6062 GB, free: 5.172 MB / 430.1 MB
Notification: Performance of simplify1: time 0.0002335/0.3761, allocations: 210.5 kB / 0.6064 GB, free: 4.977 MB / 430.1 MB
Notification: Performance of Alias: time 0.002545/0.3787, allocations: 2.526 MB / 0.6088 GB, free: 2.277 MB / 430.1 MB
Notification: Performance of simplify2: time 0.0002054/0.3789, allocations: 183 kB / 0.609 GB, free: 2.105 MB / 430.1 MB
Notification: Performance of Events: time 0.0007353/0.3796, allocations: 0.6816 MB / 0.6097 GB, free: 1.438 MB / 430.1 MB
Notification: Performance of Detect States: time 0.0007281/0.3804, allocations: 0.7747 MB / 0.6104 GB, free: 0.6562 MB / 430.1 MB
Notification: Performance of Partitioning: time 0.001092/0.3815, allocations: 1.172 MB / 0.6116 GB, free: 15.3 MB / 446.1 MB
Error: Internal error NBAdjacency.Matrix.create failed to create adjacency matrix for system:
System Variables (120/177)
****************************
(1)       [DER-] (1) Real $DER.vol1.m
(2)       [ALGB] (1) Real vol1.mb_flow
(3)       [ALGB] (1) protected Real[1] pipe2.flowModel.diameters = 0.5 * (pipe2.flowModel.dimensions[2:2] + pipe2.flowModel.dimensions[1:1])
(4)       [ALGB] (2) final Real[2] pipe1.flowModel.roughnesses = {pipe1.roughness, pipe1.roughness} (min = {0.0 for $i1 in 1:2})
(5)       [ALGB] (2) protected Real[2] vol1.portsData_zeta_in
(6)       [ALGB] (1) flow Real pipe1.port_b.m_flow (min = -1e5, max = 1e60)
(7)       [ALGB] (2) Real[2] vol1.ports_E_flow
(8)       [DISC] (2) Boolean[2] $SEV_0[$i1]
(9)       [ALGB] (1) Real[1] pipe2.flowModel.Is
(10)      [ALGB] (2) final Real[2] pipe2.flowModel.roughnesses = {pipe2.roughness, pipe2.roughness} (min = {0.0 for $i1 in 1:2})
(11)      [ALGB] (2) Real[2] vol1.s (start = {vol1.fluidLevel_max for $i1 in 1:2})
(12)      [ALGB] (2) protected Real[2] vol1.portsData_diameter
(13)      [ALGB] (2) final Real[2] pipe1.flowModel.dimensions = {(4.0 * pipe1.crossArea) / pipe1.perimeter, (4.0 * pipe1.crossArea) / pipe1.perimeter}
(14)      [ALGB] (1) final Real[1] pipe1.flowModel.dheights = {pipe1.height_ab}
(15)      [DISC] (2) protected Boolean[2] vol1.inFlow (start = {false for $i1 in 1:2})
(16)      [ALGB] (2) Real[2] vol1.ports_H_flow (min = {-1e8 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1000.0 for $i1 in 1:2})
(17)      [ALGB] (1) Real pipe2.port_b.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(18)      [ALGB] (1) stream Real[1] sin1.ports.h_outflow (min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(19)      [ALGB] (1) Real[1] pipe2.flowModel.Fs_p
(20)      [DISC] (2) Boolean[2] $SEV_3[$i1]
(21)      [ALGB] (1) Real[1] sou1.ports.p (start = {1e5 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e5 for $i1 in 1:1})
(22)      [ALGB] (2) Real[2] vol1.ports_penetration
(23)      [ALGB] (2) Real[2] vol1.m_flow_turbulent
(24)      [ALGB] (1) Real pipe1.port_a.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(25)      [ALGB] (1) Real[1] pipe2.flowModel.Fs_fg
(26)      [ALGB] (2) Real[2] vol1.portInDensities (start = {1.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {1.0 for $i1 in 1:2})
(27)      [ALGB] (2) protected Real[2] vol1.portsData_zeta_in_internal = vol1.portsData.zeta_in
(28)      [ALGB] (1) Real[1] pipe2.flowModel.pathLengths_internal = pipe2.flowModel.pathLengths
(29)      [ALGB] (1) stream Real pipe2.port_b.h_outflow (min = -1e10, max = 1e10, nominal = 1e6)
(30)      [DISC] (2) Boolean[2] $SEV_6[$i1]
(31)      [ALGB] (1) stream Real pipe1.port_a.h_outflow (min = -1e10, max = 1e10, nominal = 1e6)
(32)      [ALGB] (1) final Real[1] pipe2.flowModel.pathLengths = {pipe2.length}
(33)      [ALGB] (1) Real $FUN_8
(34)      [ALGB] (1) flow Real pipe2.port_b.m_flow (min = -1e5, max = 1e60)
(35)      [ALGB] (2) final Real[2] pipe2.flowModel.dimensions = {(4.0 * pipe2.crossArea) / pipe2.perimeter, (4.0 * pipe2.crossArea) / pipe2.perimeter}
(36)      [ALGB] (1) Real vol1.medium.state.T (start = 288.15, min = 273.15, max = 373.15, nominal = 300.0)
(37)      [ALGB] (1) Real $FUN_6
(38)      [DISC] (1) Boolean $SEV_21
(39)      [ALGB] (1) Real $FUN_5
(40)      [ALGB] (4) input Real[2, 2] pipe1.flowModel.states.p (start = {1e5 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e5 for $i1 in 1:2})
(41)      [ALGB] (1) Real vol1.Hb_flow
(42)      [ALGB] (1) Real $FUN_4
(43)      [ALGB] (1) protected Real[1] pipe1.flowModel.diameters = 0.5 * (pipe1.flowModel.dimensions[2:2] + pipe1.flowModel.dimensions[1:1])
(44)      [ALGB] (1) Real $FUN_2
(45)      [ALGB] (1) Real $FUN_1
(46)      [ALGB] (1) Real vol1.medium.T_degC = Modelica.SIunits.Conversions.to_degC(-((-273.15) - vol1.medium.T_degC))
(47)      [ALGB] (2) Real[2] vol1.ports.p (start = {1e5 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e5 for $i1 in 1:2})
(48)      [DISC] (2) Boolean[2] $SEV_9[$i1]
(49)      [ALGB] (1) flow Real[1] sin1.ports.m_flow (min = {-1e60}, max = {1e60})
(50)      [ALGB] (2) Real[2] pipe2.flowModel.vs = {(-pipe2.port_b.m_flow) / (pipe2.flowModel.crossAreas[1] * ModelicaTest.Fluid.TestComponents.Vessels.TestInitialization.pipe2.Medium.density(pipe2.flowModel.states[1])), -pipe2.port_b.m_flow / (ModelicaTest.Fluid.TestComponents.Vessels.TestInitialization.pipe2.Medium.density(pipe2.flowModel.states[2]) * pipe2.flowModel.crossAreas[2])} / pipe2.nParallel
(51)      [ALGB] (1) Real[1] pipe1.flowModel.Fs_p
(52)      [ALGB] (2) stream Real[2] vol1.ports.h_outflow (min = {-1e10 for $i1 in 1:2}, max = {1e10 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2})
(53)      [ALGB] (1) Real[1] vol1.heatTransfer.Ts = {ModelicaTest.Fluid.TestComponents.Vessels.TestInitialization.vol1.heatTransfer.Medium.temperature(vol1.heatTransfer.states[1])} (start = {288.15 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, nominal = {300.0 for $i1 in 1:1})
(54)      [ALGB] (1) Real[1] vol1.heatTransfer.Q_flows
(55)      [DISC] (2) Boolean[2] $SEV_10[$i1]
(56)      [ALGB] (1) Real vol1.Qb_flow
(57)      [DISC] (2) Boolean[2] $SEV_2[$i1]
(58)      [ALGB] (1) final input Real[1, 1] vol1.heatTransfer.states.p = {vol1.medium.state.p} (start = {1e5 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e5 for $i1 in 1:1})
(59)      [ALGB] (2) protected Real[2] vol1.portsData_diameter_internal = vol1.portsData.diameter
(60)      [ALGB] (1) Real[1] pipe2.flowModel.Ib_flows
(61)      [ALGB] (1) Real[1] sin1.ports.p (start = {1e5 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e5 for $i1 in 1:1})
(62)      [ALGB] (1) Real[1] pipe1.flowModel.rhos_act (start = {1.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {1.0 for $i1 in 1:1})
(63)      [DISC] (1) Boolean $SEV_19
(64)      [ALGB] (4) input Real[2, 2] pipe2.flowModel.states.T (start = {288.15 for $i1 in 1:2}, min = {273.15 for $states1 in 1:2}, max = {373.15 for $states1 in 1:2}, nominal = {300.0 for $i1 in 1:2})
(65)      [ALGB] (1) Real vol1.medium.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(66)      [ALGB] (2) final Real[2] pipe1.flowModel.crossAreas = {pipe1.crossArea, pipe1.crossArea}
(67)      [ALGB] (1) Real[1] pipe1.flowModel.Fs_fg
(68)      [ALGB] (1) Real[1] pipe2.flowModel.m_flows (start = {0.0 for $i1 in 1:1}, min = {-1e60 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, StateSelect = default)
(69)      [ALGB] (4) input Real[2, 2] pipe1.flowModel.states.T (start = {288.15 for $i1 in 1:2}, min = {273.15 for $states1 in 1:2}, max = {373.15 for $states1 in 1:2}, nominal = {300.0 for $i1 in 1:2})
(70)      [ALGB] (1) Real[1] pipe1.flowModel.Is
(71)      [DISC] (1) Boolean $SEV_12
(72)      [ALGB] (1) Real[1] pipe2.flowModel.rhos_act (start = {1.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {1.0 for $i1 in 1:1})
(73)      [ALGB] (1) flow Real[1] vol1.heatTransfer.heatPorts.Q_flow
(74)      [DISC] (1) Boolean $SEV_11
(75)      [DISC] (2) Boolean[2] $SEV_5[$i1]
(76)      [ALGB] (1) Real[1] pipe2.flowModel.dps_fg (start = {pipe2.flowModel.p_a_start - pipe2.flowModel.p_b_start for $i1 in 1:1})
(77)      [ALGB] (1) Real[1] pipe1.flowModel.m_flows (start = {0.0 for $i1 in 1:1}, min = {-1e60 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, StateSelect = default)
(78)      [ALGB] (1) Real[1] pipe1.flowModel.Ib_flows
(79)      [ALGB] (1) flow Real[1] sou1.ports.m_flow (min = {-1e60}, max = {1e60})
(80)      [ALGB] (2) protected Real[2] vol1.portsData_height
(81)      [ALGB] (1) Real[1] pipe2.flowModel.mus_act (start = {0.001 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {0.001 for $i1 in 1:1})
(82)      [ALGB] (1) stream Real[1] sou1.ports.h_outflow (min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(83)      [ALGB] (2) Real[2] pipe2.flowModel.rhos = {ModelicaTest.Fluid.TestComponents.Vessels.TestInitialization.pipe2.flowModel.Medium.density(pipe2.flowModel.states[$i1]) for $i1 in 1:2} (start = {1.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {1.0 for $i1 in 1:2})
(84)      [ALGB] (1) Real pipe1.port_b.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(85)      [ALGB] (2) Real[2] pipe2.flowModel.mus = {ModelicaTest.Fluid.TestComponents.Vessels.TestInitialization.pipe2.flowModel.Medium.dynamicViscosity(pipe2.flowModel.states[$i1]) for $i1 in 1:2} (start = {0.001 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {0.001 for $i1 in 1:2})
(86)      [ALGB] (1) Real[1] pipe1.flowModel.mus_act (start = {0.001 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {0.001 for $i1 in 1:1})
(87)      [ALGB] (2) Real[2] vol1.portAreas = {0.7853981633974483 * vol1.portsData_diameter[i] ^ 2.0 for i in 1:2}
(88)      [DISC] (2) Boolean[2] $SEV_8[$i1]
(89)      [ALGB] (1) Real vol1.medium.p_bar = Modelica.SIunits.Conversions.to_bar(99999.99999999999 * vol1.medium.p_bar)
(90)      [ALGB] (2) Real[2] vol1.vessel_ps_static (start = {1e5 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e5 for $i1 in 1:2})
(91)      [ALGB] (2) Real[2] pipe1.flowModel.mus = {ModelicaTest.Fluid.TestComponents.Vessels.TestInitialization.pipe1.flowModel.Medium.dynamicViscosity(pipe1.flowModel.states[$i1]) for $i1 in 1:2} (start = {0.001 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {0.001 for $i1 in 1:2})
(92)      [ALGB] (1) final input Real[1, 1] vol1.heatTransfer.states.T = {vol1.medium.state.T} (start = {288.15 for $i1 in 1:1}, min = {273.15}, max = {373.15}, nominal = {300.0 for $i1 in 1:1})
(93)      [DISC] (2) protected Boolean[2] vol1.regularFlow (start = {true for $i1 in 1:2})
(94)      [ALGB] (1) Real vol1.medium.d (start = 1.0, min = 0.0, max = 1e5, nominal = 1.0)
(95)      [ALGB] (2) protected Real[2] vol1.portsData_zeta_out_internal = vol1.portsData.zeta_out
(96)      [ALGB] (1) Real pipe2.port_a.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(97)      [ALGB] (4) input Real[2, 2] pipe2.flowModel.states.p (start = {1e5 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e5 for $i1 in 1:2})
(98)      [DISC] (2) Boolean[2] $SEV_1[$i1]
(99)      [ALGB] (2) protected Real[2] vol1.portsData_height_internal = vol1.portsData.height
(100)     [DER-] (1) Real $DER.vol1.U
(101)     [ALGB] (1) Real[1] pipe1.flowModel.dps_fg (start = {pipe1.flowModel.p_a_start - pipe1.flowModel.p_b_start for $i1 in 1:1})
(102)     [ALGB] (1) final Real[1] pipe1.flowModel.pathLengths = {pipe1.length}
(103)     [ALGB] (2) Real[2] vol1.portVelocities
(104)     [ALGB] (1) Real vol1.medium.u (min = -1e8, max = 1e8, nominal = 1e6)
(105)     [ALGB] (1) Real[1] pipe1.flowModel.Res_turbulent_internal = pipe1.flowModel.Re_turbulent * {1.0 for $i1 in 1:1}
(106)     [ALGB] (2) Real[2] pipe1.flowModel.vs = {(-pipe1.port_b.m_flow) / (pipe1.flowModel.crossAreas[1] * ModelicaTest.Fluid.TestComponents.Vessels.TestInitialization.pipe1.Medium.density(pipe1.flowModel.states[1])), -pipe1.port_b.m_flow / (ModelicaTest.Fluid.TestComponents.Vessels.TestInitialization.pipe1.Medium.density(pipe1.flowModel.states[2]) * pipe1.flowModel.crossAreas[2])} / pipe1.nParallel
(107)     [ALGB] (2) protected Real[2] vol1.portsData_zeta_out
(108)     [DISC] (2) Boolean[2] $SEV_4[$i1]
(109)     [ALGB] (2) Real[2] pipe1.flowModel.rhos = {ModelicaTest.Fluid.TestComponents.Vessels.TestInitialization.pipe1.flowModel.Medium.density(pipe1.flowModel.states[$i1]) for $i1 in 1:2} (start = {1.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {1.0 for $i1 in 1:2})
(110)     [ALGB] (2) final Real[2] pipe2.flowModel.crossAreas = {pipe2.crossArea, pipe2.crossArea}
(111)     [ALGB] (1) stream Real pipe2.port_a.h_outflow (min = -1e10, max = 1e10, nominal = 1e6)
(112)     [ALGB] (2) flow Real[2] vol1.ports.m_flow (min = {-1e5 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2})
(113)     [ALGB] (1) stream Real pipe1.port_b.h_outflow (min = -1e10, max = 1e10, nominal = 1e6)
(114)     [ALGB] (1) protected Real pipe1.flowModel.dp_fric_nominal = sum({ModelicaTest.Fluid.TestComponents.Vessels.TestInitialization.pipe1.flowModel.WallFriction.pressureLoss_m_flow(pipe1.flowModel.m_flow_nominal / pipe1.flowModel.nParallel, pipe1.flowModel.rho_nominal, pipe1.flowModel.rho_nominal, pipe1.flowModel.mu_nominal, pipe1.flowModel.mu_nominal, pipe1.flowModel.pathLengths_internal[1], pipe1.flowModel.diameters[1], ((pipe1.flowModel.crossAreas[2:2] + pipe1.flowModel.crossAreas[1:1]) / 2.0)[1], ((pipe1.flowModel.roughnesses[2:2] + pipe1.flowModel.roughnesses[1:1]) / 2.0)[1], pipe1.flowModel.m_flow_small / pipe1.flowModel.nParallel, pipe1.flowModel.Res_turbulent_internal[1])}) (min = 0.0, nominal = 1e5)
(115)     [ALGB] (1) final Real[1] pipe2.flowModel.dheights = {pipe2.height_ab}
(116)     [ALGB] (1) Real[1] vol1.heatTransfer.heatPorts.T (start = {288.15 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, nominal = {300.0 for $i1 in 1:1})
(117)     [ALGB] (1) protected Real pipe2.flowModel.dp_fric_nominal = sum({ModelicaTest.Fluid.TestComponents.Vessels.TestInitialization.pipe2.flowModel.WallFriction.pressureLoss_m_flow(pipe2.flowModel.m_flow_nominal / pipe2.flowModel.nParallel, pipe2.flowModel.rho_nominal, pipe2.flowModel.rho_nominal, pipe2.flowModel.mu_nominal, pipe2.flowModel.mu_nominal, pipe2.flowModel.pathLengths_internal[1], pipe2.flowModel.diameters[1], ((pipe2.flowModel.crossAreas[2:2] + pipe2.flowModel.crossAreas[1:1]) / 2.0)[1], ((pipe2.flowModel.roughnesses[2:2] + pipe2.flowModel.roughnesses[1:1]) / 2.0)[1], pipe2.flowModel.m_flow_small / pipe2.flowModel.nParallel, pipe2.flowModel.Res_turbulent_internal[1])}) (min = 0.0, nominal = 1e5)
(118)     [ALGB] (1) Real[1] pipe1.flowModel.pathLengths_internal = pipe1.flowModel.pathLengths
(119)     [ALGB] (1) Real[1] pipe2.flowModel.Res_turbulent_internal = pipe2.flowModel.Re_turbulent * {1.0 for $i1 in 1:1}
(120)     [DISC] (2) Boolean[2] $SEV_7[$i1]


System Equations (122/169)
****************************
(1)       [SCAL] (1) pipe1.port_b.p = vol1.ports[1].p ($RES_SIM_132)
(2)       [ARRY] (2) vol1.portsData_height_internal = vol1.portsData.height ($RES_BND_180)
(3)       [ARRY] (2) pipe1.flowModel.dimensions = {(4.0 * pipe1.crossArea) / pipe1.perimeter, (4.0 * pipe1.crossArea) / pipe1.perimeter} ($RES_BND_145)
(4)       [SCAL] (1) sou1.ports[1].m_flow - pipe1.port_b.m_flow = 0.0 ($RES_SIM_133)
(5)       [FOR-] (2) ($RES_SIM_16)
(5)       [----] for $i1 in 1:2 loop
(5)       [----]   [-IF-] (1)if vol1.regularFlow[$i1] then
(5)       [----]   [----]   [SCAL] (1) vol1.ports[$i1].p = vol1.vessel_ps_static[$i1] + (0.5 / vol1.portAreas[$i1] ^ 2.0) * smooth(2, if $SEV_8[$i1] then (vol1.ports_penetration[$i1] * ((-1.0) + vol1.portAreas[$i1] ^ 2.0 / vol1.vesselArea ^ 2.0 + vol1.portsData_zeta_in[$i1]) * vol1.ports[$i1].m_flow ^ 2.0) / vol1.portInDensities[$i1] else if $SEV_9[$i1] then -(((1.0 + vol1.portsData_zeta_out[$i1]) - vol1.portAreas[$i1] ^ 2.0 / vol1.vesselArea ^ 2.0) * vol1.ports[$i1].m_flow ^ 2.0) / (vol1.ports_penetration[$i1] * vol1.medium.d) else if $SEV_10[$i1] then Modelica.Fluid.Utilities.regSquare2.regSquare2_utility(vol1.ports[$i1].m_flow, vol1.m_flow_turbulent[$i1], (vol1.ports_penetration[$i1] * ((-1.0) + vol1.portAreas[$i1] ^ 2.0 / vol1.vesselArea ^ 2.0 + vol1.portsData_zeta_in[$i1])) / vol1.portInDensities[$i1], ((1.0 + vol1.portsData_zeta_out[$i1]) - vol1.portAreas[$i1] ^ 2.0 / vol1.vesselArea ^ 2.0) / (vol1.ports_penetration[$i1] * vol1.medium.d), false, 1.0) else -Modelica.Fluid.Utilities.regSquare2.regSquare2_utility(-vol1.ports[$i1].m_flow, vol1.m_flow_turbulent[$i1], ((1.0 + vol1.portsData_zeta_out[$i1]) - vol1.portAreas[$i1] ^ 2.0 / vol1.vesselArea ^ 2.0) / (vol1.ports_penetration[$i1] * vol1.medium.d), (vol1.ports_penetration[$i1] * ((-1.0) + vol1.portAreas[$i1] ^ 2.0 / vol1.vesselArea ^ 2.0 + vol1.portsData_zeta_in[$i1])) / vol1.portInDensities[$i1], false, 1.0)) ($RES_SIM_18)
(5)       [----]   [----] elseif vol1.inFlow[$i1] then
(5)       [----]   [----]   [SCAL] (1) vol1.ports[$i1].p = vol1.vessel_ps_static[$i1] ($RES_SIM_19)
(5)       [----]   [----] else
(5)       [----]   [----]   [SCAL] (1) vol1.ports[$i1].m_flow = 0.0 ($RES_SIM_20)
(5)       [----]   [----] end if;
(5)       [----] end for;
(6)       [ARRY] (2) vol1.portsData_zeta_in_internal = vol1.portsData.zeta_in ($RES_BND_181)
(7)       [ARRY] (2) pipe1.flowModel.roughnesses = {pipe1.roughness, pipe1.roughness} ($RES_BND_146)
(8)       [SCAL] (1) sou1.ports[1].p = pipe1.port_a.p ($RES_SIM_134)
(9)       [SCAL] (1) vol1.medium.state.p = 99999.99999999999 * vol1.medium.p_bar ($RES_SIM_52)
(10)      [ARRY] (2) vol1.portsData_zeta_out_internal = vol1.portsData.zeta_out ($RES_BND_182)
(11)      [ARRY] (1) pipe1.flowModel.dheights = {pipe1.height_ab} ($RES_BND_147)
(12)      [ARRY] (2) vol1.portsData_zeta_out = vol1.portsData_zeta_out_internal ($RES_SIM_135)
(13)      [SCAL] (1) vol1.medium.state.T = -((-273.15) - vol1.medium.T_degC) ($RES_SIM_53)
(14)      [ARRY] (1) pipe1.flowModel.pathLengths = {pipe1.length} ($RES_BND_148)
(15)      [ARRY] (4) pipe1.flowModel.states = {ModelicaTest.Fluid.TestComponents.Vessels.TestInitialization.pipe1.Medium.ThermodynamicState(pipe1.port_a.p, 298.15 + 9.945795414988312e-4 * sou1.ports[1].h_outflow), ModelicaTest.Fluid.TestComponents.Vessels.TestInitialization.pipe1.Medium.ThermodynamicState(pipe1.port_b.p, 298.15 + 9.945795414988312e-4 * vol1.ports[1].h_outflow)} ($RES_BND_183)
(16)      [ARRY] (2) vol1.portsData_zeta_in = vol1.portsData_zeta_in_internal ($RES_SIM_136)
(17)      [FOR-] (2) ($RES_BND_149)
(17)      [----] for $i1 in 1:2 loop
(17)      [----]   [SCAL] (1) pipe1.flowModel.rhos[$i1] = (0.003483703884165752 * pipe1.flowModel.states.T) / pipe1.flowModel.states.p ($RES_BND_150)
(17)      [----] end for;
(18)      [ARRY] (4) pipe2.flowModel.states = {ModelicaTest.Fluid.TestComponents.Vessels.TestInitialization.pipe2.Medium.ThermodynamicState(pipe2.port_a.p, 298.15 + 9.945795414988312e-4 * vol1.ports[2].h_outflow), ModelicaTest.Fluid.TestComponents.Vessels.TestInitialization.pipe2.Medium.ThermodynamicState(pipe2.port_b.p, 298.15 + 9.945795414988312e-4 * sin1.ports[1].h_outflow)} ($RES_BND_184)
(19)      [ARRY] (2) vol1.portsData_height = vol1.portsData_height_internal ($RES_SIM_137)
(20)      [SCAL] (1) vol1.medium.d = -(0.003483703884165752 * (99999.99999999999 * vol1.medium.p_bar)) / ((-273.15) - vol1.medium.T_degC) ($RES_SIM_55)
(21)      [ARRY] (2) vol1.heatTransfer.states = {vol1.medium.state} ($RES_BND_185)
(22)      [ARRY] (2) vol1.portsData_diameter = vol1.portsData_diameter_internal ($RES_SIM_138)
(23)      [SCAL] (1) vol1.medium.u = 287.0508037566665 * ((-273.15) - vol1.medium.T_degC) + 1005.45 * ((-298.15) - ((-273.15) - vol1.medium.T_degC)) ($RES_SIM_57)
(24)      [FOR-] (2) ($RES_EVT_210)
(24)      [----] for $i1 in 1:2 loop
(24)      [----]   [SCAL] (1) $SEV_5[$i1] = vol1.portsData_height[$i1] >= vol1.fluidLevel_max ($RES_EVT_211)
(24)      [----] end for;
(25)      [FOR-] (2) ($RES_EVT_212)
(25)      [----] for $i1 in 1:2 loop
(25)      [----]   [SCAL] (1) $SEV_6[$i1] = $SEV_4[$i1] or $SEV_5[$i1] ($RES_EVT_213)
(25)      [----] end for;
(26)      [FOR-] (2) ($RES_EVT_214)
(26)      [----] for $i1 in 1:2 loop
(26)      [----]   [SCAL] (1) $SEV_7[$i1] = not vol1.regularFlow[$i1] and $SEV_6[$i1] ($RES_EVT_215)
(26)      [----] end for;
(27)      [FOR-] (2) ($RES_EVT_216)
(27)      [----] for $i1 in 1:2 loop
(27)      [----]   [SCAL] (1) $SEV_8[$i1] = vol1.ports[$i1].m_flow >= vol1.m_flow_turbulent[$i1] ($RES_EVT_217)
(27)      [----] end for;
(28)      [FOR-] (2) ($RES_EVT_218)
(28)      [----] for $i1 in 1:2 loop
(28)      [----]   [SCAL] (1) $SEV_9[$i1] = vol1.ports[$i1].m_flow <= (-vol1.m_flow_turbulent[$i1]) ($RES_EVT_219)
(28)      [----] end for;
(29)      [FOR-] (2) ($RES_SIM_21)
(29)      [----] for $i1 in 1:2 loop
(29)      [----]   [-IF-] (1)if vol1.regularFlow[$i1] then
(29)      [----]   [----]   [SCAL] (1) vol1.s[$i1] = 0.0 - vol1.portsData_height[$i1] ($RES_SIM_23)
(29)      [----]   [----] elseif vol1.inFlow[$i1] then
(29)      [----]   [----]   [SCAL] (1) vol1.s[$i1] = vol1.ports[$i1].m_flow ($RES_SIM_24)
(29)      [----]   [----] else
(29)      [----]   [----]   [SCAL] (1) vol1.s[$i1] = ((vol1.ports[$i1].p - vol1.vessel_ps_static[$i1]) / 101325.0) * (vol1.portsData_height[$i1] - 0.0) ($RES_SIM_25)
(29)      [----]   [----] end if;
(29)      [----] end for;
(30)      [FOR-] (2) ($RES_BND_151)
(30)      [----] for $i1 in 1:2 loop
(30)      [----]   [SCAL] (1) pipe1.flowModel.mus[$i1] = 1.82e-5 ($RES_BND_152)
(30)      [----] end for;
(31)      [ARRY] (1) pipe1.flowModel.pathLengths_internal = pipe1.flowModel.pathLengths ($RES_BND_153)
(32)      [SCAL] (1) sou1.ports[1].p = sou1.p ($RES_SIM_106)
(33)      [SCAL] (1) pipe1.flowModel.Res_turbulent_internal[1] = pipe1.flowModel.Re_turbulent ($RES_BND_154)
(34)      [SCAL] (1) sou1.ports[1].h_outflow = 1005.45 * ((-298.15) + sou1.T) ($RES_SIM_107)
(35)      [ARRY] (1) pipe1.flowModel.diameters = 0.5 * (pipe1.flowModel.dimensions[2:2] + pipe1.flowModel.dimensions[1:1]) ($RES_BND_155)
(36)      [SCAL] (1) pipe2.port_a.h_outflow = sin1.ports[1].h_outflow + system.g * pipe2.height_ab ($RES_SIM_61)
(37)      [FOR-] (2) ($RES_SIM_26)
(37)      [----] for $i1 in 1:2 loop
(37)      [----]   [SCAL] (1) vol1.ports[$i1].h_outflow = 1005.45 * ((-298.15) - ((-273.15) - vol1.medium.T_degC)) ($RES_SIM_27)
(37)      [----] end for;
(38)      [SCAL] (1) pipe2.port_b.h_outflow = vol1.ports[2].h_outflow - system.g * pipe2.height_ab ($RES_SIM_62)
(39)      [ARRY] (2) pipe2.flowModel.vs = {-pipe2.port_b.m_flow / (pipe2.flowModel.crossAreas[1] * ((0.003483703884165752 * pipe2.flowModel.states.T) / pipe2.flowModel.states.p)), -pipe2.port_b.m_flow / (((0.003483703884165752 * pipe2.flowModel.states.T) / pipe2.flowModel.states.p) * pipe2.flowModel.crossAreas[2])} / pipe2.nParallel ($RES_BND_157)
(40)      [FOR-] (2) ($RES_SIM_28)
(40)      [----] for $i1 in 1:2 loop
(40)      [----]   [SCAL] (1) vol1.ports_E_flow[$i1] = vol1.ports[$i1].m_flow * (vol1.portVelocities[$i1] * 0.5 * vol1.portVelocities[$i1] + system.g * vol1.portsData_height[$i1]) ($RES_SIM_29)
(40)      [----] end for;
(41)      [ARRY] (2) pipe2.flowModel.crossAreas = {pipe2.crossArea, pipe2.crossArea} ($RES_BND_158)
(42)      [SCAL] (1) -pipe2.port_b.m_flow = pipe2.flowModel.m_flows[1] ($RES_SIM_64)
(43)      [ARRY] (2) pipe2.flowModel.dimensions = {(4.0 * pipe2.crossArea) / pipe2.perimeter, (4.0 * pipe2.crossArea) / pipe2.perimeter} ($RES_BND_159)
(44)      [ARRY] (1) {0.0} = pipe2.flowModel.Ib_flows - (pipe2.flowModel.Fs_fg + pipe2.flowModel.Fs_p) ($RES_SIM_65)
(45)      [ARRY] (1) pipe2.flowModel.Is = {pipe2.flowModel.m_flows[1] * pipe2.flowModel.pathLengths[1]} ($RES_SIM_66)
(46)      [ARRY] (1) pipe2.flowModel.dps_fg = {(2.0 * (pipe2.flowModel.Fs_fg[1] / pipe2.flowModel.nParallel)) / (pipe2.flowModel.crossAreas[1] + pipe2.flowModel.crossAreas[2])} ($RES_SIM_67)
(47)      [ARRY] (1) pipe2.flowModel.Fs_p = pipe2.flowModel.nParallel * {0.5 * (pipe2.flowModel.crossAreas[1] + pipe2.flowModel.crossAreas[2]) * (pipe2.flowModel.states.T - pipe2.flowModel.states.T)} ($RES_SIM_68)
(48)      [ARRY] (1) pipe2.flowModel.Ib_flows = {0.0} ($RES_SIM_69)
(49)      [FOR-] (2) ($RES_EVT_220)
(49)      [----] for $i1 in 1:2 loop
(49)      [----]   [SCAL] (1) $SEV_10[$i1] = (vol1.ports_penetration[$i1] * ((-1.0) + vol1.portAreas[$i1] ^ 2.0 / vol1.vesselArea ^ 2.0 + vol1.portsData_zeta_in[$i1])) / vol1.portInDensities[$i1] >= ((1.0 + vol1.portsData_zeta_out[$i1]) - vol1.portAreas[$i1] ^ 2.0 / vol1.vesselArea ^ 2.0) / (vol1.ports_penetration[$i1] * vol1.medium.d) ($RES_EVT_221)
(49)      [----] end for;
(50)      [SCAL] (1) $SEV_11 = vol1.ports[2].m_flow > 0.0 ($RES_EVT_222)
(51)      [SCAL] (1) $SEV_12 = vol1.ports[1].m_flow > 0.0 ($RES_EVT_223)
(52)      [SCAL] (1) vol1.ports_H_flow[2] = smooth(0, vol1.ports[2].m_flow * (if $SEV_11 then pipe2.port_a.h_outflow else vol1.ports[2].h_outflow)) ($RES_SIM_30)
(53)      [ARRY] (2) pipe2.flowModel.roughnesses = {pipe2.roughness, pipe2.roughness} ($RES_BND_160)
(54)      [SCAL] (1) vol1.m_flow_turbulent[2] = max(vol1.m_flow_small, 0.0014294246573833558 * vol1.portsData_diameter[2]) ($RES_SIM_31)
(55)      [ARRY] (1) pipe2.flowModel.dheights = {pipe2.height_ab} ($RES_BND_161)
(56)      [SCAL] (1) vol1.portVelocities[2] = smooth(0, (vol1.ports[2].m_flow / vol1.portAreas[2]) / ((0.003483703884165752 * vol1.vessel_ps_static[2]) / (298.15 + 9.945795414988312e-4 * (if $SEV_11 then pipe2.port_a.h_outflow else vol1.ports[2].h_outflow)))) ($RES_SIM_32)
(57)      [ARRY] (1) pipe2.flowModel.pathLengths = {pipe2.length} ($RES_BND_162)
(58)      [SCAL] (1) vol1.portInDensities[2] = (0.003483703884165752 * vol1.vessel_ps_static[2]) / (298.15 + 9.945795414988312e-4 * pipe2.port_a.h_outflow) ($RES_SIM_33)
(59)      [FOR-] (2) ($RES_BND_163)
(59)      [----] for $i1 in 1:2 loop
(59)      [----]   [SCAL] (1) pipe2.flowModel.rhos[$i1] = (0.003483703884165752 * pipe2.flowModel.states.T) / pipe2.flowModel.states.p ($RES_BND_164)
(59)      [----] end for;
(60)      [SCAL] (1) vol1.ports_H_flow[1] = smooth(0, vol1.ports[1].m_flow * (if $SEV_12 then pipe1.port_b.h_outflow else vol1.ports[1].h_outflow)) ($RES_SIM_34)
(61)      [SCAL] (1) pipe2.flowModel.rhos_act[1] = noEvent(if $SEV_19 then pipe2.flowModel.rhos[1] else pipe2.flowModel.rhos[2]) ($RES_SIM_70)
(62)      [SCAL] (1) vol1.m_flow_turbulent[1] = max(vol1.m_flow_small, 0.0014294246573833558 * vol1.portsData_diameter[1]) ($RES_SIM_35)
(63)      [FOR-] (2) ($RES_BND_165)
(63)      [----] for $i1 in 1:2 loop
(63)      [----]   [SCAL] (1) pipe2.flowModel.mus[$i1] = 1.82e-5 ($RES_BND_166)
(63)      [----] end for;
(64)      [SCAL] (1) pipe2.flowModel.mus_act[1] = noEvent(if $SEV_19 then pipe2.flowModel.mus[1] else pipe2.flowModel.mus[2]) ($RES_SIM_71)
(65)      [SCAL] (1) vol1.portVelocities[1] = smooth(0, (vol1.ports[1].m_flow / vol1.portAreas[1]) / ((0.003483703884165752 * vol1.vessel_ps_static[1]) / (298.15 + 9.945795414988312e-4 * (if $SEV_12 then pipe1.port_b.h_outflow else vol1.ports[1].h_outflow)))) ($RES_SIM_36)
(66)      [ARRY] (1) pipe2.flowModel.m_flows = {homotopy(({$FUN_2} .* pipe2.flowModel.nParallel)[1], (pipe2.flowModel.m_flow_nominal / pipe2.flowModel.dp_nominal * (pipe2.flowModel.dps_fg - (pipe2.flowModel.g * pipe2.flowModel.dheights) .* pipe2.flowModel.rho_nominal))[1])} ($RES_SIM_72)
(67)      [SCAL] (1) vol1.portInDensities[1] = (0.003483703884165752 * vol1.vessel_ps_static[1]) / (298.15 + 9.945795414988312e-4 * pipe1.port_b.h_outflow) ($RES_SIM_37)
(68)      [ARRY] (1) pipe2.flowModel.pathLengths_internal = pipe2.flowModel.pathLengths ($RES_BND_167)
(69)      [SCAL] (1) pipe2.flowModel.Res_turbulent_internal[1] = pipe2.flowModel.Re_turbulent ($RES_BND_168)
(70)      [SCAL] (1) pipe1.port_a.h_outflow = vol1.ports[1].h_outflow + system.g * pipe1.height_ab ($RES_SIM_74)
(71)      [ARRY] (1) pipe2.flowModel.diameters = 0.5 * (pipe2.flowModel.dimensions[2:2] + pipe2.flowModel.dimensions[1:1]) ($RES_BND_169)
(72)      [SCAL] (1) pipe1.port_b.h_outflow = sou1.ports[1].h_outflow - system.g * pipe1.height_ab ($RES_SIM_75)
(73)      [SCAL] (1) -pipe1.port_b.m_flow = pipe1.flowModel.m_flows[1] ($RES_SIM_77)
(74)      [ARRY] (1) {0.0} = pipe1.flowModel.Ib_flows - (pipe1.flowModel.Fs_fg + pipe1.flowModel.Fs_p) ($RES_SIM_78)
(75)      [ARRY] (1) pipe1.flowModel.Is = {pipe1.flowModel.m_flows[1] * pipe1.flowModel.pathLengths[1]} ($RES_SIM_79)
(76)      [SCAL] (1) $SEV_19 = pipe2.flowModel.m_flows[1] > 0.0 ($RES_EVT_230)
(77)      [SCAL] (1) $SEV_21 = pipe1.flowModel.m_flows[1] > 0.0 ($RES_EVT_232)
(78)      [SCAL] (1) $FUN_1 = ModelicaTest.Fluid.TestComponents.Vessels.TestInitialization.pipe1.flowModel.WallFriction.massFlowRate_dp_staticHead(pipe1.flowModel.dps_fg[1], pipe1.flowModel.rhos[1], pipe1.flowModel.rhos[2], pipe1.flowModel.mus[1], pipe1.flowModel.mus[2], pipe1.flowModel.pathLengths_internal[1], pipe1.flowModel.diameters[1], (pipe1.flowModel.g * pipe1.flowModel.dheights)[1], (0.5 .* (pipe1.flowModel.crossAreas[1:1] + pipe1.flowModel.crossAreas[2:2]))[1], (0.5 .* (pipe1.flowModel.roughnesses[1:1] + pipe1.flowModel.roughnesses[2:2]))[1], pipe1.flowModel.dp_small, pipe1.flowModel.Res_turbulent_internal[1]) ($RES_$AUX_194)
(79)      [SCAL] (1) $FUN_2 = ModelicaTest.Fluid.TestComponents.Vessels.TestInitialization.pipe2.flowModel.WallFriction.massFlowRate_dp_staticHead(pipe2.flowModel.dps_fg[1], pipe2.flowModel.rhos[1], pipe2.flowModel.rhos[2], pipe2.flowModel.mus[1], pipe2.flowModel.mus[2], pipe2.flowModel.pathLengths_internal[1], pipe2.flowModel.diameters[1], (pipe2.flowModel.g * pipe2.flowModel.dheights)[1], (0.5 .* (pipe2.flowModel.crossAreas[1:1] + pipe2.flowModel.crossAreas[2:2]))[1], (0.5 .* (pipe2.flowModel.roughnesses[1:1] + pipe2.flowModel.roughnesses[2:2]))[1], pipe2.flowModel.dp_small, pipe2.flowModel.Res_turbulent_internal[1]) ($RES_$AUX_193)
(80)      [SCAL] (1) vol1.mb_flow = sum(vol1.ports.m_flow) ($RES_$AUX_192)
(81)      [SCAL] (1) $FUN_4 = sum(vol1.ports_H_flow) ($RES_$AUX_191)
(82)      [SCAL] (1) $FUN_5 = sum(vol1.ports_E_flow) ($RES_$AUX_190)
(83)      [SCAL] (1) vol1.Qb_flow = vol1.heatTransfer.Q_flows[1] ($RES_SIM_40)
(84)      [SCAL] (1) vol1.Hb_flow = $FUN_4 + $FUN_5 ($RES_SIM_41)
(85)      [FOR-] (2) ($RES_SIM_43)
(85)      [----] for $i1 in 1:2 loop
(85)      [----]   [SCAL] (1) vol1.vessel_ps_static[$i1] = 99999.99999999999 * vol1.medium.p_bar ($RES_SIM_44)
(85)      [----] end for;
(86)      [SCAL] (1) vol1.heatTransfer.heatPorts[1].Q_flow = 0.0 ($RES_SIM_126)
(87)      [ARRY] (1) pipe1.flowModel.dps_fg = {(2.0 * (pipe1.flowModel.Fs_fg[1] / pipe1.flowModel.nParallel)) / (pipe1.flowModel.crossAreas[1] + pipe1.flowModel.crossAreas[2])} ($RES_SIM_80)
(88)      [SCAL] (1) vol1.ports[2].m_flow - pipe2.port_b.m_flow = 0.0 ($RES_SIM_127)
(89)      [ARRY] (1) vol1.heatTransfer.Ts = {vol1.heatTransfer.states.p} ($RES_BND_175)
(90)      [ARRY] (1) pipe1.flowModel.Fs_p = pipe1.flowModel.nParallel * {0.5 * (pipe1.flowModel.crossAreas[1] + pipe1.flowModel.crossAreas[2]) * (pipe1.flowModel.states.T - pipe1.flowModel.states.T)} ($RES_SIM_81)
(91)      [ARRY] (1) vol1.heatTransfer.Q_flows = vol1.heatTransfer.heatPorts.Q_flow ($RES_SIM_46)
(92)      [SCAL] (1) pipe2.port_b.m_flow + sin1.ports[1].m_flow = 0.0 ($RES_SIM_128)
(93)      [FOR-] (2) ($RES_BND_176)
(93)      [----] for $i1 in 1:2 loop
(93)      [----]   [SCAL] (1) vol1.portAreas[$i1] = 0.7853981633974483 * vol1.portsData_diameter[$i1] ^ 2.0 ($RES_BND_177)
(93)      [----] end for;
(94)      [ARRY] (1) pipe1.flowModel.Ib_flows = {0.0} ($RES_SIM_82)
(95)      [ARRY] (1) vol1.heatTransfer.Ts = vol1.heatTransfer.heatPorts.T ($RES_SIM_47)
(96)      [SCAL] (1) vol1.ports[1].m_flow + pipe1.port_b.m_flow = 0.0 ($RES_SIM_129)
(97)      [SCAL] (1) pipe1.flowModel.rhos_act[1] = noEvent(if $SEV_21 then pipe1.flowModel.rhos[1] else pipe1.flowModel.rhos[2]) ($RES_SIM_83)
(98)      [SCAL] (1) pipe1.flowModel.mus_act[1] = noEvent(if $SEV_21 then pipe1.flowModel.mus[1] else pipe1.flowModel.mus[2]) ($RES_SIM_84)
(99)      [ARRY] (2) vol1.portsData_diameter_internal = vol1.portsData.diameter ($RES_BND_179)
(100)     [ARRY] (1) pipe1.flowModel.m_flows = {homotopy(({$FUN_1} .* pipe1.flowModel.nParallel)[1], (pipe1.flowModel.m_flow_nominal / pipe1.flowModel.dp_nominal * (pipe1.flowModel.dps_fg - (pipe1.flowModel.g * pipe1.flowModel.dheights) .* pipe1.flowModel.rho_nominal))[1])} ($RES_SIM_85)
(101)     [SCAL] (1) sin1.ports[1].p = sin1.p ($RES_SIM_86)
(102)     [SCAL] (1) sin1.ports[1].h_outflow = 1005.45 * ((-298.15) + sin1.T) ($RES_SIM_87)
(103)     [FOR-] (2) ($RES_EVT_200)
(103)     [----] for $i1 in 1:2 loop
(103)     [----]   [SCAL] (1) $SEV_0[$i1] = 0.0 - (vol1.portsData_height[$i1] + 0.1 * vol1.portsData_diameter[$i1]) > 0.1 * vol1.portsData_diameter[$i1] ($RES_EVT_201)
(103)     [----] end for;
(104)     [FOR-] (2) ($RES_EVT_202)
(104)     [----] for $i1 in 1:2 loop
(104)     [----]   [SCAL] (1) $SEV_1[$i1] = 0.0 - (vol1.portsData_height[$i1] + 0.1 * vol1.portsData_diameter[$i1]) < (-0.1 * vol1.portsData_diameter[$i1]) ($RES_EVT_203)
(104)     [----] end for;
(105)     [SCAL] (1) vol1.m = vol1.V * vol1.medium.d ($RES_SIM_9)
(106)     [FOR-] (2) ($RES_EVT_204)
(106)     [----] for $i1 in 1:2 loop
(106)     [----]   [SCAL] (1) $SEV_2[$i1] = 0.1 * vol1.portsData_diameter[$i1] > 0.0 ($RES_EVT_205)
(106)     [----] end for;
(107)     [SCAL] (1) vol1.U = vol1.m * vol1.medium.u ($RES_SIM_8)
(108)     [SCAL] (1) $DER.vol1.U = vol1.Qb_flow + vol1.Hb_flow ($RES_SIM_7)
(109)     [FOR-] (2) ($RES_EVT_206)
(109)     [----] for $i1 in 1:2 loop
(109)     [----]   [SCAL] (1) $SEV_3[$i1] = 0.0 >= vol1.portsData_height[$i1] ($RES_EVT_207)
(109)     [----] end for;
(110)     [SCAL] (1) $DER.vol1.m = vol1.mb_flow ($RES_SIM_6)
(111)     [FOR-] (2) ($RES_EVT_208)
(111)     [----] for $i1 in 1:2 loop
(111)     [----]   [SCAL] (1) $SEV_4[$i1] = vol1.s[$i1] > 0.0 ($RES_EVT_209)
(111)     [----] end for;
(112)     [SCAL] (1) $FUN_6 = ModelicaTest.Fluid.TestComponents.Vessels.TestInitialization.pipe2.flowModel.WallFriction.pressureLoss_m_flow(pipe2.flowModel.m_flow_nominal / pipe2.flowModel.nParallel, pipe2.flowModel.rho_nominal, pipe2.flowModel.rho_nominal, pipe2.flowModel.mu_nominal, pipe2.flowModel.mu_nominal, pipe2.flowModel.pathLengths_internal[1], pipe2.flowModel.diameters[1], (0.5 .* (pipe2.flowModel.crossAreas[2:2] + pipe2.flowModel.crossAreas[1:1]))[1], (0.5 .* (pipe2.flowModel.roughnesses[2:2] + pipe2.flowModel.roughnesses[1:1]))[1], pipe2.flowModel.m_flow_small / pipe2.flowModel.nParallel, pipe2.flowModel.Res_turbulent_internal[1]) ($RES_$AUX_189)
(113)     [SCAL] (1) pipe2.flowModel.dp_fric_nominal = sum({$FUN_6}) ($RES_$AUX_188)
(114)     [SCAL] (1) $FUN_8 = ModelicaTest.Fluid.TestComponents.Vessels.TestInitialization.pipe1.flowModel.WallFriction.pressureLoss_m_flow(pipe1.flowModel.m_flow_nominal / pipe1.flowModel.nParallel, pipe1.flowModel.rho_nominal, pipe1.flowModel.rho_nominal, pipe1.flowModel.mu_nominal, pipe1.flowModel.mu_nominal, pipe1.flowModel.pathLengths_internal[1], pipe1.flowModel.diameters[1], (0.5 .* (pipe1.flowModel.crossAreas[2:2] + pipe1.flowModel.crossAreas[1:1]))[1], (0.5 .* (pipe1.flowModel.roughnesses[2:2] + pipe1.flowModel.roughnesses[1:1]))[1], pipe1.flowModel.m_flow_small / pipe1.flowModel.nParallel, pipe1.flowModel.Res_turbulent_internal[1]) ($RES_$AUX_187)
(115)     [SCAL] (1) pipe1.flowModel.dp_fric_nominal = sum({$FUN_8}) ($RES_$AUX_186)
(116)     [FOR-] (2) ($RES_SIM_10)
(116)     [----] for $i1 in 1:2 loop
(116)     [----]   [SCAL] (1) vol1.ports_penetration[$i1] = smooth(1, if $SEV_0[$i1] then 1.0 else if $SEV_1[$i1] then 0.001 else if $SEV_2[$i1] then 0.5005 - 0.24975 * ((-3.0) + ((0.0 - (0.1 * vol1.portsData_diameter[$i1] + vol1.portsData_height[$i1])) / (0.1 * vol1.portsData_diameter[$i1])) ^ 2.0) * ((10.0 * (0.0 - (vol1.portsData_height[$i1] + 0.1 * vol1.portsData_diameter[$i1]))) / vol1.portsData_diameter[$i1]) else 0.5005) ($RES_SIM_11)
(116)     [----] end for;
(117)     [FOR-] (2) ($RES_SIM_12)
(117)     [----] for $i1 in 1:2 loop
(117)     [----]   [SCAL] (1) vol1.regularFlow[$i1] = $SEV_3[$i1] ($RES_SIM_13)
(117)     [----] end for;
(118)     [SCAL] (1) pipe2.port_b.p = sin1.ports[1].p ($RES_SIM_130)
(119)     [ARRY] (2) pipe1.flowModel.vs = {-pipe1.port_b.m_flow / (pipe1.flowModel.crossAreas[1] * ((0.003483703884165752 * pipe1.flowModel.states.T) / pipe1.flowModel.states.p)), -pipe1.port_b.m_flow / (((0.003483703884165752 * pipe1.flowModel.states.T) / pipe1.flowModel.states.p) * pipe1.flowModel.crossAreas[2])} / pipe1.nParallel ($RES_BND_143)
(120)     [SCAL] (1) vol1.ports[2].p = pipe2.port_a.p ($RES_SIM_131)
(121)     [FOR-] (2) ($RES_SIM_14)
(121)     [----] for $i1 in 1:2 loop
(121)     [----]   [SCAL] (1) vol1.inFlow[$i1] = $SEV_7[$i1] ($RES_SIM_15)
(121)     [----] end for;
(122)     [ARRY] (2) pipe1.flowModel.crossAreas = {pipe1.crossArea, pipe1.crossArea} ($RES_BND_144)