Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ModelicaTest_3.2.2_ModelicaTest.Fluid.TestComponents.Vessels.TestSimpleTank.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 3.2.2+maint.om/package.mo", uses=false)
Using package ModelicaTest with version 3.2.2 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaTest 3.2.2+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.TestSimpleTank,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ModelicaTest_3.2.2_ModelicaTest.Fluid.TestComponents.Vessels.TestSimpleTank")
translateModel(ModelicaTest.Fluid.TestComponents.Vessels.TestSimpleTank,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ModelicaTest_3.2.2_ModelicaTest.Fluid.TestComponents.Vessels.TestSimpleTank")
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo): time 0.001051/0.001051, allocations: 107.3 kB / 16.42 MB, free: 5.973 MB / 14.72 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo): time 0.001068/0.001068, allocations: 191.3 kB / 17.36 MB, free: 5.566 MB / 14.72 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.2.3+maint.om/package.mo): time 1.264/1.264, 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 3.2.2+maint.om/package.mo): time 0.1796/0.1796, allocations: 39.96 MB / 310.5 MB, free: 4.027 MB / 254.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 2.384e-05/2.384e-05, allocations: 6.438 kB / 436.4 MB, free: 11.8 MB / 318.1 MB
Notification: Performance of NFInst.instantiate(ModelicaTest.Fluid.TestComponents.Vessels.TestSimpleTank): time 0.01335/0.01339, allocations: 16.68 MB / 453.1 MB, free: 11.05 MB / 334.1 MB
Notification: Performance of NFInst.instExpressions: time 0.009242/0.02267, allocations: 6.899 MB / 460 MB, free: 4.129 MB / 334.1 MB
Notification: Performance of NFInst.updateImplicitVariability: time 0.0008088/0.02352, allocations: 23.81 kB / 460 MB, free: 4.105 MB / 334.1 MB
Notification: Performance of NFTyping.typeComponents: time 0.0009611/0.02449, allocations: 389.8 kB / 460.4 MB, free: 3.723 MB / 334.1 MB
Notification: Performance of NFTyping.typeBindings: time 0.002207/0.02678, allocations: 1.007 MB / 461.4 MB, free: 2.711 MB / 334.1 MB
Notification: Performance of NFTyping.typeClassSections: time 0.00459/0.03138, allocations: 1.981 MB / 463.4 MB, free: 0.7422 MB / 334.1 MB
Notification: Performance of NFFlatten.flatten: time 0.002538/0.03393, allocations: 2.284 MB / 465.7 MB, free: 14.45 MB / 350.1 MB
Notification: Performance of NFFlatten.resolveConnections: time 0.0008235/0.03476, allocations: 0.6358 MB / 466.3 MB, free: 13.8 MB / 350.1 MB
Notification: Performance of NFEvalConstants.evaluate: time 0.001243/0.03601, allocations: 0.9385 MB / 467.2 MB, free: 12.86 MB / 350.1 MB
Notification: Performance of NFSimplifyModel.simplify: time 0.000887/0.03691, allocations: 0.7553 MB / 468 MB, free: 12.1 MB / 350.1 MB
Notification: Performance of NFPackage.collectConstants: time 0.0001244/0.03705, allocations: 80 kB / 468.1 MB, free: 12.02 MB / 350.1 MB
Notification: Performance of NFFlatten.collectFunctions: time 0.002331/0.03939, allocations: 1.303 MB / 469.4 MB, free: 10.71 MB / 350.1 MB
Notification: Performance of combineBinaries: time 0.001238/0.04064, allocations: 1.572 MB / 470.9 MB, free: 9.129 MB / 350.1 MB
Notification: Performance of replaceArrayConstructors: time 0.0006221/0.04127, allocations: 0.934 MB / 471.9 MB, free: 8.184 MB / 350.1 MB
Notification: Performance of NFVerifyModel.verify: time 0.000192/0.04147, allocations: 143.6 kB / 472 MB, free: 8.043 MB / 350.1 MB
Notification: Performance of FrontEnd: time 0.0001576/0.04164, allocations: 27.86 kB / 472 MB, free: 8.016 MB / 350.1 MB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 153 (122)
 * Number of variables: 157 (123)
Notification: Performance of Bindings: time 0.003964/0.04561, allocations: 4.201 MB / 476.2 MB, free: 3.68 MB / 350.1 MB
Notification: Performance of FunctionAlias: time 0.0004538/0.04608, allocations: 421.2 kB / 476.6 MB, free: 3.246 MB / 350.1 MB
Notification: Performance of Early Inline: time 0.00245/0.04854, allocations: 2.501 MB / 479.1 MB, free: 0.707 MB / 350.1 MB
Notification: Performance of simplify1: time 0.0001728/0.04873, allocations: 135.8 kB / 479.3 MB, free: 0.5742 MB / 350.1 MB
Notification: Performance of Alias: time 0.002531/0.05126, allocations: 2.301 MB / 481.6 MB, free: 14.05 MB / 366.1 MB
Notification: Performance of simplify2: time 0.0001365/0.05141, allocations: 111.8 kB / 481.7 MB, free: 13.95 MB / 366.1 MB
Notification: Performance of Events: time 0.0006703/0.05209, allocations: 0.5423 MB / 482.2 MB, free: 13.41 MB / 366.1 MB
Notification: Performance of Detect States: time 0.0007381/0.05284, allocations: 0.7501 MB / 483 MB, free: 12.62 MB / 366.1 MB
Notification: Performance of Partitioning: time 0.0008927/0.05374, allocations: 0.8953 MB / 483.9 MB, free: 11.61 MB / 366.1 MB
Error: Internal error NBAdjacency.Matrix.create failed to create adjacency matrix for system:
System Variables (107/152)
****************************
(1)       [DISC] (2) protected Boolean[2] tank.inFlow (start = {false for $i1 in 1:2})
(2)       [DISC] (2) Boolean[2] $SEV_22[$i1]
(3)       [ALGB] (1) stream Real pipe.port_a.h_outflow (min = -1e10, max = 1e10, nominal = 1e6)
(4)       [ALGB] (1) Real[1] tank.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})
(5)       [ALGB] (1) Real[1] pipe.flowModel.Ib_flows
(6)       [ALGB] (1) protected Real pipe.flowModel.dp_fric_nominal = sum({ModelicaTest.Fluid.TestComponents.Vessels.TestSimpleTank.pipe.flowModel.WallFriction.pressureLoss_m_flow(pipe.flowModel.m_flow_nominal / pipe.flowModel.nParallel, pipe.flowModel.rho_nominal, pipe.flowModel.rho_nominal, pipe.flowModel.mu_nominal, pipe.flowModel.mu_nominal, pipe.flowModel.pathLengths_internal[1], pipe.flowModel.diameters[1], ((pipe.flowModel.crossAreas[2:2] + pipe.flowModel.crossAreas[1:1]) / 2.0)[1], ((pipe.flowModel.roughnesses[2:2] + pipe.flowModel.roughnesses[1:1]) / 2.0)[1], pipe.flowModel.m_flow_small / pipe.flowModel.nParallel, pipe.flowModel.Res_turbulent_internal[1])}) (min = 0.0, nominal = 1e5)
(7)       [ALGB] (1) Real tank.medium.T_degC = Modelica.SIunits.Conversions.to_degC(-((-273.15) - tank.medium.T_degC))
(8)       [ALGB] (2) Real[2] pipe.flowModel.vs = {(-pipe.port_b.m_flow) / (pipe.flowModel.crossAreas[1] * ModelicaTest.Fluid.TestComponents.Vessels.TestSimpleTank.pipe.Medium.density(pipe.flowModel.states[1])), -pipe.port_b.m_flow / (ModelicaTest.Fluid.TestComponents.Vessels.TestSimpleTank.pipe.Medium.density(pipe.flowModel.states[2]) * pipe.flowModel.crossAreas[2])} / pipe.nParallel
(9)       [ALGB] (1) protected Real[1] pipe.flowModel.diameters = 0.5 * (pipe.flowModel.dimensions[2:2] + pipe.flowModel.dimensions[1:1])
(10)      [ALGB] (1) Real $FUN_12
(11)      [DISC] (2) Boolean[2] $SEV_18[$i1]
(12)      [ALGB] (1) Real $FUN_10
(13)      [ALGB] (2) Real[2] pipe.flowModel.mus = {ModelicaTest.Fluid.TestComponents.Vessels.TestSimpleTank.pipe.flowModel.Medium.dynamicViscosity(pipe.flowModel.states[$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})
(14)      [DISC] (2) protected Boolean[2] tank.regularFlow (start = {true for $i1 in 1:2})
(15)      [ALGB] (2) protected Real[2] tank.portsData_height
(16)      [ALGB] (2) stream Real[2] tank.ports.h_outflow (min = {-1e10 for $i1 in 1:2}, max = {1e10 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2})
(17)      [ALGB] (1) Real tank.Hb_flow
(18)      [DISC] (1) protected discrete Real timeTable.nextEventScaled (fixed = true, start = 0.0)
(19)      [ALGB] (2) protected Real[2] tank.portsData_zeta_in_internal = tank.portsData.zeta_in
(20)      [ALGB] (2) flow Real[2] tank.ports.m_flow (min = {-1e5 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2})
(21)      [ALGB] (2) Real[2] tank.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})
(22)      [DISC] (1) protected Real timeTable.a
(23)      [ALGB] (2) Real[2] tank.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})
(24)      [DISC] (1) protected Real timeTable.b
(25)      [ALGB] (1) Real pipe.port_b.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(26)      [ALGB] (2) protected Real[2] tank.portsData_height_internal = tank.portsData.height
(27)      [DER-] (1) Real $DER.tank.U
(28)      [DISC] (2) Boolean[2] $SEV_14[$i1]
(29)      [ALGB] (1) Real tank.Qb_flow
(30)      [DISC] (1) Boolean $SEV_27
(31)      [ALGB] (1) Real[1] pipe.flowModel.pathLengths_internal = pipe.flowModel.pathLengths
(32)      [DISC] (1) Boolean $SEV_26
(33)      [DISC] (1) Boolean $SEV_25
(34)      [DISC] (2) Boolean[2] $SEV_21[$i1]
(35)      [ALGB] (2) final Real[2] pipe.flowModel.dimensions = {(4.0 * pipe.crossArea) / pipe.perimeter, (4.0 * pipe.crossArea) / pipe.perimeter}
(36)      [DISC] (1) Integer $FUN_9
(37)      [DISC] (1) Boolean $SEV_24
(38)      [ALGB] (2) Real[2] tank.ports_E_flow
(39)      [ALGB] (2) Real[2] tank.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})
(40)      [ALGB] (1) Real $FUN_8
(41)      [ALGB] (1) Real $FUN_7
(42)      [ALGB] (1) Real $FUN_6
(43)      [ALGB] (1) Real $FUN_4
(44)      [ALGB] (1) Real flowSource.medium.p_bar = Modelica.SIunits.Conversions.to_bar(99999.99999999999 * flowSource.medium.p_bar)
(45)      [ALGB] (1) Real $FUN_3
(46)      [ALGB] (1) Real[1] pipe.flowModel.Fs_p
(47)      [ALGB] (1) Real $FUN_2
(48)      [ALGB] (2) protected Real[2] tank.portsData_diameter_internal = tank.portsData.diameter
(49)      [DISC] (2) Boolean[2] $SEV_17[$i1]
(50)      [ALGB] (1) Real timeTable.y
(51)      [ALGB] (1) Real[1] pipe.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)
(52)      [DISC] (1) protected discrete Real timeTable.nextEvent (fixed = true, start = 0.0)
(53)      [ALGB] (2) Real[2] tank.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})
(54)      [ALGB] (1) Real[1] tank.heatTransfer.Q_flows
(55)      [DER-] (1) Real $DER.tank.m
(56)      [ALGB] (2) final Real[2] pipe.flowModel.roughnesses = {pipe.roughness, pipe.roughness} (min = {0.0 for $i1 in 1:2})
(57)      [ALGB] (1) Real[1] pipe.flowModel.dps_fg (start = {pipe.flowModel.p_a_start - pipe.flowModel.p_b_start for $i1 in 1:1})
(58)      [ALGB] (2) protected Real[2] tank.portsData_zeta_out
(59)      [ALGB] (1) Real[1] ambient_fixed.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})
(60)      [ALGB] (1) Real[1] pipe.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})
(61)      [ALGB] (1) Real[1] tank.heatTransfer.surfaceAreas = {sqrt(3.141592653589793 * tank.crossArea) * 2.0 * tank.fluidLevel + tank.crossArea}
(62)      [ALGB] (1) flow Real[1] ambient_fixed.ports.m_flow (min = {-1e60}, max = {1e60})
(63)      [ALGB] (2) Real[2] tank.ports_penetration
(64)      [ALGB] (2) Real[2] tank.portAreas = {0.7853981633974483 * tank.portsData_diameter[i] ^ 2.0 for i in 1:2}
(65)      [ALGB] (1) Real[1] pipe.flowModel.Res_turbulent_internal = pipe.flowModel.Re_turbulent * {1.0 for $i1 in 1:1}
(66)      [ALGB] (1) flow Real[1] tank.heatTransfer.heatPorts.Q_flow
(67)      [ALGB] (1) final Real[1] pipe.flowModel.dheights = {pipe.height_ab}
(68)      [ALGB] (1) flow Real[1] flowSource.ports.m_flow (min = {-1e60}, max = {1e60})
(69)      [DISC] (2) Boolean[2] $SEV_13[$i1]
(70)      [DISC] (2) Boolean[2] $SEV_20[$i1]
(71)      [ALGB] (1) final input Real[1, 1] tank.heatTransfer.states.T = {tank.medium.state.T} (start = {288.15 for $i1 in 1:1}, min = {1.0 for $i1 in 1:1}, max = {1e4 for $i1 in 1:1}, nominal = {300.0 for $i1 in 1:1})
(72)      [ALGB] (1) final Real[1] pipe.flowModel.pathLengths = {pipe.length}
(73)      [ALGB] (1) stream Real[1] ambient_fixed.ports.h_outflow (min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(74)      [ALGB] (2) Real[2] tank.portVelocities
(75)      [ALGB] (1) stream Real pipe.port_b.h_outflow (min = -1e10, max = 1e10, nominal = 1e6)
(76)      [ALGB] (1) Real pipe.port_a.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(77)      [ALGB] (1) Real tank.medium.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(78)      [ALGB] (1) Real[1] flowSource.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})
(79)      [ALGB] (2) protected Real[2] tank.portsData_zeta_in
(80)      [DISC] (2) Boolean[2] $SEV_16[$i1]
(81)      [ALGB] (2) protected Real[2] tank.portsData_diameter
(82)      [ALGB] (2) Real[2] tank.s (start = {tank.fluidLevel_max for $i1 in 1:2})
(83)      [DISC] (2) Boolean[2] $SEV_23[$i1]
(84)      [DISC] (1) Boolean $SEV_9
(85)      [ALGB] (1) final Real tank.fluidVolume = tank.fluidVolume
(86)      [ALGB] (2) Real[2] tank.m_flow_turbulent
(87)      [ALGB] (1) Real[1] pipe.flowModel.Is
(88)      [DISC] (1) Boolean $SEV_4
(89)      [ALGB] (4) input Real[2, 2] pipe.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})
(90)      [ALGB] (1) flow Real pipe.port_b.m_flow (min = -1e5, max = 1e60)
(91)      [DISC] (2) Boolean[2] $SEV_19[$i1]
(92)      [ALGB] (1) stream Real[1] flowSource.ports.h_outflow (min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(93)      [ALGB] (1) Real tank.mb_flow
(94)      [ALGB] (1) final input Real[1, 1] tank.heatTransfer.states.p = {tank.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})
(95)      [DISC] (1) Boolean $TEV_0
(96)      [ALGB] (1) Real[1] tank.heatTransfer.Ts = {ModelicaTest.Fluid.TestComponents.Vessels.TestSimpleTank.tank.heatTransfer.Medium.temperature(tank.heatTransfer.states[1])} (start = {288.15 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, nominal = {300.0 for $i1 in 1:1})
(97)      [ALGB] (2) protected Real[2] tank.portsData_zeta_out_internal = tank.portsData.zeta_out
(98)      [ALGB] (1) protected final Real tank.fluidLevel = tank.fluidLevel (min = 0.0)
(99)      [ALGB] (1) Real tank.medium.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(100)     [ALGB] (1) Real[1] pipe.flowModel.Fs_fg
(101)     [ALGB] (2) final Real[2] pipe.flowModel.crossAreas = {pipe.crossArea, pipe.crossArea}
(102)     [ALGB] (2) Real[2] pipe.flowModel.rhos = {ModelicaTest.Fluid.TestComponents.Vessels.TestSimpleTank.pipe.flowModel.Medium.density(pipe.flowModel.states[$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})
(103)     [ALGB] (1) Real[1] pipe.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})
(104)     [ALGB] (1) Real flowSource.medium.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(105)     [DISC] (1) protected Integer timeTable.last (start = 1)
(106)     [DISC] (2) Boolean[2] $SEV_15[$i1]
(107)     [ALGB] (4) input Real[2, 2] pipe.flowModel.states.T (start = {288.15 for $i1 in 1:2}, min = {1.0 for $i1 in 1:2}, max = {1e4 for $i1 in 1:2}, nominal = {300.0 for $i1 in 1:2})


System Equations (103/148)
****************************
(1)       [ARRY] (2) pipe.flowModel.dimensions = {(4.0 * pipe.crossArea) / pipe.perimeter, (4.0 * pipe.crossArea) / pipe.perimeter} ($RES_BND_145)
(2)       [ARRY] (2) pipe.flowModel.roughnesses = {pipe.roughness, pipe.roughness} ($RES_BND_146)
(3)       [ARRY] (1) pipe.flowModel.dheights = {pipe.height_ab} ($RES_BND_147)
(4)       [ARRY] (1) pipe.flowModel.pathLengths = {pipe.length} ($RES_BND_148)
(5)       [FOR-] (2) ($RES_BND_149)
(5)       [----] for $i1 in 1:2 loop
(5)       [----]   [SCAL] (1) pipe.flowModel.rhos[$i1] = 995.586 ($RES_BND_150)
(5)       [----] end for;
(6)       [SCAL] (1) flowSource.medium.state.p = 99999.99999999999 * flowSource.medium.p_bar ($RES_SIM_19)
(7)       [SCAL] (1) tank.portVelocities[1] = smooth(0, 0.0010044335697769957 * (tank.ports[1].m_flow / tank.portAreas[1])) ($RES_SIM_90)
(8)       [SCAL] (1) tank.portInDensities[1] = 995.586 ($RES_SIM_91)
(9)       [SCAL] (1) tank.Qb_flow = tank.heatTransfer.Q_flows[1] ($RES_SIM_94)
(10)      [SCAL] (1) tank.Hb_flow = $FUN_2 + $FUN_3 ($RES_SIM_95)
(11)      [FOR-] (2) ($RES_SIM_97)
(11)      [----] for $i1 in 1:2 loop
(11)      [----]   [SCAL] (1) tank.vessel_ps_static[$i1] = system.g * max(0.0, tank.fluidLevel - tank.portsData_height[$i1]) * 995.586 + tank.p_ambient ($RES_SIM_98)
(11)      [----] end for;
(12)      [SCAL] (1) $TEV_0 = $PRE.timeTable.nextEvent ($RES_EVT_174)
(13)      [SCAL] (1) $SEV_4 = abs(sum({abs(flowSource.ports[1].m_flow)}) - abs(flowSource.ports[1].m_flow)) <= 1e-60 ($RES_EVT_175)
(14)      [SCAL] (1) tank.fluidVolume = tank.crossArea * tank.fluidLevel ($RES_SIM_101)
(15)      [ARRY] (1) tank.heatTransfer.Q_flows = tank.heatTransfer.heatPorts.Q_flow ($RES_SIM_102)
(16)      [ARRY] (1) tank.heatTransfer.Ts = tank.heatTransfer.heatPorts.T ($RES_SIM_103)
(17)      [FOR-] (2) ($RES_BND_151)
(17)      [----] for $i1 in 1:2 loop
(17)      [----]   [SCAL] (1) pipe.flowModel.mus[$i1] = 0.001 ($RES_BND_152)
(17)      [----] end for;
(18)      [ARRY] (1) pipe.flowModel.pathLengths_internal = pipe.flowModel.pathLengths ($RES_BND_153)
(19)      [SCAL] (1) pipe.flowModel.Res_turbulent_internal[1] = pipe.flowModel.Re_turbulent ($RES_BND_154)
(20)      [SCAL] (1) $DER.tank.m = tank.mb_flow ($RES_SIM_60)
(21)      [ARRY] (1) pipe.flowModel.diameters = 0.5 * (pipe.flowModel.dimensions[2:2] + pipe.flowModel.dimensions[1:1]) ($RES_BND_155)
(22)      [SCAL] (1) $DER.tank.U = tank.Qb_flow + tank.Hb_flow ($RES_SIM_61)
(23)      [SCAL] (1) tank.medium.state.p = tank.p_ambient ($RES_SIM_108)
(24)      [SCAL] (1) tank.U = tank.m * (4184.0 * ((-273.15) - ((-273.15) - tank.medium.T_degC))) ($RES_SIM_62)
(25)      [SCAL] (1) tank.medium.state.T = -((-273.15) - tank.medium.T_degC) ($RES_SIM_109)
(26)      [SCAL] (1) tank.m = 995.586 * tank.fluidVolume ($RES_SIM_63)
(27)      [SCAL] (1) pipe.port_a.h_outflow = ambient_fixed.ports[1].h_outflow + system.g * pipe.height_ab ($RES_SIM_28)
(28)      [FOR-] (2) ($RES_SIM_64)
(28)      [----] for $i1 in 1:2 loop
(28)      [----]   [SCAL] (1) tank.ports_penetration[$i1] = smooth(1, if $SEV_13[$i1] then 1.0 else if $SEV_14[$i1] then 0.001 else if $SEV_15[$i1] then 0.5005 - 0.24975 * ((-3.0) + ((tank.fluidLevel - (0.1 * tank.portsData_diameter[$i1] + tank.portsData_height[$i1])) / (0.1 * tank.portsData_diameter[$i1])) ^ 2.0) * ((10.0 * (tank.fluidLevel - (tank.portsData_height[$i1] + 0.1 * tank.portsData_diameter[$i1]))) / tank.portsData_diameter[$i1]) else 0.5005) ($RES_SIM_65)
(28)      [----] end for;
(29)      [SCAL] (1) pipe.port_b.h_outflow = tank.ports[1].h_outflow - system.g * pipe.height_ab ($RES_SIM_29)
(30)      [ARRY] (2) tank.heatTransfer.states = {tank.medium.state} ($RES_BND_159)
(31)      [FOR-] (2) ($RES_SIM_66)
(31)      [----] for $i1 in 1:2 loop
(31)      [----]   [SCAL] (1) tank.regularFlow[$i1] = $SEV_16[$i1] ($RES_SIM_67)
(31)      [----] end for;
(32)      [FOR-] (2) ($RES_SIM_68)
(32)      [----] for $i1 in 1:2 loop
(32)      [----]   [SCAL] (1) tank.inFlow[$i1] = $SEV_20[$i1] ($RES_SIM_69)
(32)      [----] end for;
(33)      [SCAL] (1) $SEV_9 = pipe.flowModel.m_flows[1] > 0.0 ($RES_EVT_180)
(34)      [FOR-] (2) ($RES_EVT_184)
(34)      [----] for $i1 in 1:2 loop
(34)      [----]   [SCAL] (1) $SEV_13[$i1] = tank.fluidLevel - (tank.portsData_height[$i1] + 0.1 * tank.portsData_diameter[$i1]) > 0.1 * tank.portsData_diameter[$i1] ($RES_EVT_185)
(34)      [----] end for;
(35)      [FOR-] (2) ($RES_EVT_186)
(35)      [----] for $i1 in 1:2 loop
(35)      [----]   [SCAL] (1) $SEV_14[$i1] = tank.fluidLevel - (tank.portsData_height[$i1] + 0.1 * tank.portsData_diameter[$i1]) < (-0.1 * tank.portsData_diameter[$i1]) ($RES_EVT_187)
(35)      [----] end for;
(36)      [FOR-] (2) ($RES_EVT_188)
(36)      [----] for $i1 in 1:2 loop
(36)      [----]   [SCAL] (1) $SEV_15[$i1] = 0.1 * tank.portsData_diameter[$i1] > 0.0 ($RES_EVT_189)
(36)      [----] end for;
(37)      [SCAL] (1) tank.mb_flow = sum(tank.ports.m_flow) ($RES_$AUX_169)
(38)      [SCAL] (1) $FUN_2 = sum(tank.ports_H_flow) ($RES_$AUX_168)
(39)      [SCAL] (1) $FUN_3 = sum(tank.ports_E_flow) ($RES_$AUX_167)
(40)      [SCAL] (1) $FUN_4 = ModelicaTest.Fluid.TestComponents.Vessels.TestSimpleTank.pipe.flowModel.WallFriction.massFlowRate_dp_staticHead(pipe.flowModel.dps_fg[1], pipe.flowModel.rhos[1], pipe.flowModel.rhos[2], pipe.flowModel.mus[1], pipe.flowModel.mus[2], pipe.flowModel.pathLengths_internal[1], pipe.flowModel.diameters[1], (pipe.flowModel.g * pipe.flowModel.dheights)[1], (0.5 .* (pipe.flowModel.crossAreas[1:1] + pipe.flowModel.crossAreas[2:2]))[1], (0.5 .* (pipe.flowModel.roughnesses[1:1] + pipe.flowModel.roughnesses[2:2]))[1], pipe.flowModel.dp_small, pipe.flowModel.Res_turbulent_internal[1]) ($RES_$AUX_166)
(41)      [SCAL] (1) -timeTable.y = sum(flowSource.ports.m_flow) ($RES_$AUX_165)
(42)      [ARRY] (4) pipe.flowModel.states = {ModelicaTest.Fluid.TestComponents.Vessels.TestSimpleTank.pipe.Medium.ThermodynamicState(pipe.port_a.p, 273.15 + 2.390057361376673e-4 * tank.ports[1].h_outflow), ModelicaTest.Fluid.TestComponents.Vessels.TestSimpleTank.pipe.Medium.ThermodynamicState(pipe.port_b.p, 273.15 + 2.390057361376673e-4 * ambient_fixed.ports[1].h_outflow)} ($RES_BND_160)
(43)      [TUPL] (4) ($FUN_6, $FUN_7, $FUN_8, $FUN_9) = ModelicaTest.Fluid.TestComponents.Vessels.TestSimpleTank.timeTable.getInterpolationCoefficients(timeTable.table, timeTable.offset, timeTable.startTime, time, timeTable.last, 1e-13, timeTable.shiftTime) ($RES_$AUX_164)
(44)      [SCAL] (1) -pipe.port_b.m_flow = pipe.flowModel.m_flows[1] ($RES_SIM_31)
(45)      [SCAL] (1) $FUN_10 = ModelicaTest.Fluid.TestComponents.Vessels.TestSimpleTank.pipe.flowModel.WallFriction.pressureLoss_m_flow(pipe.flowModel.m_flow_nominal / pipe.flowModel.nParallel, pipe.flowModel.rho_nominal, pipe.flowModel.rho_nominal, pipe.flowModel.mu_nominal, pipe.flowModel.mu_nominal, pipe.flowModel.pathLengths_internal[1], pipe.flowModel.diameters[1], (0.5 .* (pipe.flowModel.crossAreas[2:2] + pipe.flowModel.crossAreas[1:1]))[1], (0.5 .* (pipe.flowModel.roughnesses[2:2] + pipe.flowModel.roughnesses[1:1]))[1], pipe.flowModel.m_flow_small / pipe.flowModel.nParallel, pipe.flowModel.Res_turbulent_internal[1]) ($RES_$AUX_163)
(46)      [ARRY] (1) {0.0} = pipe.flowModel.Ib_flows - (pipe.flowModel.Fs_fg + pipe.flowModel.Fs_p) ($RES_SIM_32)
(47)      [SCAL] (1) pipe.flowModel.dp_fric_nominal = sum({$FUN_10}) ($RES_$AUX_162)
(48)      [ARRY] (1) pipe.flowModel.Is = {pipe.flowModel.m_flows[1] * pipe.flowModel.pathLengths[1]} ($RES_SIM_33)
(49)      [SCAL] (1) $FUN_12 = sqrt(3.141592653589793 * tank.crossArea) ($RES_$AUX_161)
(50)      [SCAL] (1) tank.ports[1].m_flow - pipe.port_b.m_flow = 0.0 ($RES_SIM_116)
(51)      [ARRY] (1) pipe.flowModel.dps_fg = {(2.0 * (pipe.flowModel.Fs_fg[1] / pipe.flowModel.nParallel)) / (pipe.flowModel.crossAreas[1] + pipe.flowModel.crossAreas[2])} ($RES_SIM_34)
(52)      [SCAL] (1) tank.heatTransfer.heatPorts[1].Q_flow = 0.0 ($RES_SIM_117)
(53)      [FOR-] (2) ($RES_SIM_70)
(53)      [----] for $i1 in 1:2 loop
(53)      [----]   [-IF-] (1)if tank.regularFlow[$i1] then
(53)      [----]   [----]   [SCAL] (1) tank.ports[$i1].p = tank.vessel_ps_static[$i1] + (0.5 / tank.portAreas[$i1] ^ 2.0) * smooth(2, if $SEV_21[$i1] then (tank.ports_penetration[$i1] * ((-1.0) + tank.portAreas[$i1] ^ 2.0 / tank.vesselArea ^ 2.0 + tank.portsData_zeta_in[$i1]) * tank.ports[$i1].m_flow ^ 2.0) / tank.portInDensities[$i1] else if $SEV_22[$i1] then -(((1.0 + tank.portsData_zeta_out[$i1]) - tank.portAreas[$i1] ^ 2.0 / tank.vesselArea ^ 2.0) * tank.ports[$i1].m_flow ^ 2.0) / (tank.ports_penetration[$i1] * 995.586) else if $SEV_23[$i1] then Modelica.Fluid.Utilities.regSquare2.regSquare2_utility(tank.ports[$i1].m_flow, tank.m_flow_turbulent[$i1], (tank.ports_penetration[$i1] * ((-1.0) + tank.portAreas[$i1] ^ 2.0 / tank.vesselArea ^ 2.0 + tank.portsData_zeta_in[$i1])) / tank.portInDensities[$i1], ((1.0 + tank.portsData_zeta_out[$i1]) - tank.portAreas[$i1] ^ 2.0 / tank.vesselArea ^ 2.0) / (tank.ports_penetration[$i1] * 995.586), false, 1.0) else -Modelica.Fluid.Utilities.regSquare2.regSquare2_utility(-tank.ports[$i1].m_flow, tank.m_flow_turbulent[$i1], ((1.0 + tank.portsData_zeta_out[$i1]) - tank.portAreas[$i1] ^ 2.0 / tank.vesselArea ^ 2.0) / (tank.ports_penetration[$i1] * 995.586), (tank.ports_penetration[$i1] * ((-1.0) + tank.portAreas[$i1] ^ 2.0 / tank.vesselArea ^ 2.0 + tank.portsData_zeta_in[$i1])) / tank.portInDensities[$i1], false, 1.0)) ($RES_SIM_72)
(53)      [----]   [----] elseif tank.inFlow[$i1] then
(53)      [----]   [----]   [SCAL] (1) tank.ports[$i1].p = tank.vessel_ps_static[$i1] ($RES_SIM_73)
(53)      [----]   [----] else
(53)      [----]   [----]   [SCAL] (1) tank.ports[$i1].m_flow = 0.0 ($RES_SIM_74)
(53)      [----]   [----] end if;
(53)      [----] end for;
(54)      [ARRY] (1) pipe.flowModel.Fs_p = pipe.flowModel.nParallel * {0.5 * (pipe.flowModel.crossAreas[1] + pipe.flowModel.crossAreas[2]) * (pipe.flowModel.states.T - pipe.flowModel.states.T)} ($RES_SIM_35)
(55)      [ARRY] (1) pipe.flowModel.Ib_flows = {0.0} ($RES_SIM_36)
(56)      [SCAL] (1) pipe.port_b.m_flow + ambient_fixed.ports[1].m_flow = 0.0 ($RES_SIM_119)
(57)      [SCAL] (1) pipe.flowModel.rhos_act[1] = noEvent(if $SEV_9 then pipe.flowModel.rhos[1] else pipe.flowModel.rhos[2]) ($RES_SIM_37)
(58)      [SCAL] (1) pipe.flowModel.mus_act[1] = noEvent(if $SEV_9 then pipe.flowModel.mus[1] else pipe.flowModel.mus[2]) ($RES_SIM_38)
(59)      [ARRY] (1) pipe.flowModel.m_flows = {homotopy(({$FUN_4} .* pipe.flowModel.nParallel)[1], (pipe.flowModel.m_flow_nominal / pipe.flowModel.dp_nominal * (pipe.flowModel.dps_fg - (pipe.flowModel.g * pipe.flowModel.dheights) .* pipe.flowModel.rho_nominal))[1])} ($RES_SIM_39)
(60)      [FOR-] (2) ($RES_SIM_75)
(60)      [----] for $i1 in 1:2 loop
(60)      [----]   [-IF-] (1)if tank.regularFlow[$i1] then
(60)      [----]   [----]   [SCAL] (1) tank.s[$i1] = tank.fluidLevel - tank.portsData_height[$i1] ($RES_SIM_77)
(60)      [----]   [----] elseif tank.inFlow[$i1] then
(60)      [----]   [----]   [SCAL] (1) tank.s[$i1] = tank.ports[$i1].m_flow ($RES_SIM_78)
(60)      [----]   [----] else
(60)      [----]   [----]   [SCAL] (1) tank.s[$i1] = ((tank.ports[$i1].p - tank.vessel_ps_static[$i1]) / 101325.0) * (tank.portsData_height[$i1] - tank.fluidLevel) ($RES_SIM_79)
(60)      [----]   [----] end if;
(60)      [----] end for;
(61)      [FOR-] (2) ($RES_EVT_190)
(61)      [----] for $i1 in 1:2 loop
(61)      [----]   [SCAL] (1) $SEV_16[$i1] = tank.fluidLevel >= tank.portsData_height[$i1] ($RES_EVT_191)
(61)      [----] end for;
(62)      [FOR-] (2) ($RES_EVT_192)
(62)      [----] for $i1 in 1:2 loop
(62)      [----]   [SCAL] (1) $SEV_17[$i1] = tank.s[$i1] > 0.0 ($RES_EVT_193)
(62)      [----] end for;
(63)      [FOR-] (2) ($RES_EVT_194)
(63)      [----] for $i1 in 1:2 loop
(63)      [----]   [SCAL] (1) $SEV_18[$i1] = tank.portsData_height[$i1] >= tank.fluidLevel_max ($RES_EVT_195)
(63)      [----] end for;
(64)      [FOR-] (2) ($RES_EVT_196)
(64)      [----] for $i1 in 1:2 loop
(64)      [----]   [SCAL] (1) $SEV_19[$i1] = $SEV_17[$i1] or $SEV_18[$i1] ($RES_EVT_197)
(64)      [----] end for;
(65)      [FOR-] (2) ($RES_EVT_198)
(65)      [----] for $i1 in 1:2 loop
(65)      [----]   [SCAL] (1) $SEV_20[$i1] = not tank.regularFlow[$i1] and $SEV_19[$i1] ($RES_EVT_199)
(65)      [----] end for;
(66)      [ARRY] (1) tank.heatTransfer.surfaceAreas = {2.0 * $FUN_12 * tank.fluidLevel + tank.crossArea} ($RES_BND_132)
(67)      [SCAL] (1) ambient_fixed.ports[1].p = pipe.port_b.p ($RES_SIM_120)
(68)      [ARRY] (1) tank.heatTransfer.Ts = {tank.heatTransfer.states.p} ($RES_BND_133)
(69)      [SCAL] (1) tank.ports[2].m_flow + flowSource.ports[1].m_flow = 0.0 ($RES_SIM_121)
(70)      [FOR-] (2) ($RES_BND_134)
(70)      [----] for $i1 in 1:2 loop
(70)      [----]   [SCAL] (1) tank.portAreas[$i1] = 0.7853981633974483 * tank.portsData_diameter[$i1] ^ 2.0 ($RES_BND_135)
(70)      [----] end for;
(71)      [SCAL] (1) ambient_fixed.ports[1].p = ambient_fixed.p ($RES_SIM_40)
(72)      [SCAL] (1) flowSource.ports[1].p = tank.ports[2].p ($RES_SIM_122)
(73)      [SCAL] (1) ambient_fixed.ports[1].h_outflow = 4184.0 * ((-273.15) + ambient_fixed.T) ($RES_SIM_41)
(74)      [SCAL] (1) pipe.port_a.p = tank.ports[1].p ($RES_SIM_123)
(75)      [ARRY] (2) tank.portsData_diameter_internal = tank.portsData.diameter ($RES_BND_137)
(76)      [ARRY] (2) tank.portsData_zeta_out = tank.portsData_zeta_out_internal ($RES_SIM_125)
(77)      [ARRY] (2) tank.portsData_height_internal = tank.portsData.height ($RES_BND_138)
(78)      [ARRY] (2) tank.portsData_zeta_in = tank.portsData_zeta_in_internal ($RES_SIM_126)
(79)      [ARRY] (2) tank.portsData_zeta_in_internal = tank.portsData.zeta_in ($RES_BND_139)
(80)      [FOR-] (2) ($RES_SIM_80)
(80)      [----] for $i1 in 1:2 loop
(80)      [----]   [SCAL] (1) tank.ports[$i1].h_outflow = 4184.0 * ((-273.15) - ((-273.15) - tank.medium.T_degC)) ($RES_SIM_81)
(80)      [----] end for;
(81)      [ARRY] (2) tank.portsData_height = tank.portsData_height_internal ($RES_SIM_127)
(82)      [ARRY] (2) tank.portsData_diameter = tank.portsData_diameter_internal ($RES_SIM_128)
(83)      [FOR-] (2) ($RES_SIM_82)
(83)      [----] for $i1 in 1:2 loop
(83)      [----]   [SCAL] (1) tank.ports_E_flow[$i1] = tank.ports[$i1].m_flow * (tank.portVelocities[$i1] * 0.5 * tank.portVelocities[$i1] + system.g * tank.portsData_height[$i1]) ($RES_SIM_83)
(83)      [----] end for;
(84)      [SCAL] (1) tank.ports_H_flow[2] = smooth(0, tank.ports[2].m_flow * (if $SEV_24 then flowSource.ports[1].h_outflow else tank.ports[2].h_outflow)) ($RES_SIM_84)
(85)      [SCAL] (1) tank.m_flow_turbulent[2] = tank.m_flow_small ($RES_SIM_85)
(86)      [SCAL] (1) tank.portVelocities[2] = smooth(0, 0.0010044335697769957 * (tank.ports[2].m_flow / tank.portAreas[2])) ($RES_SIM_86)
(87)      [SCAL] (1) tank.portInDensities[2] = 995.586 ($RES_SIM_87)
(88)      [SCAL] (1) tank.ports_H_flow[1] = smooth(0, tank.ports[1].m_flow * (if $SEV_25 then pipe.port_a.h_outflow else tank.ports[1].h_outflow)) ($RES_SIM_88)
(89)      [SCAL] (1) tank.m_flow_turbulent[1] = tank.m_flow_small ($RES_SIM_89)
(90)      [FOR-] (2) ($RES_EVT_200)
(90)      [----] for $i1 in 1:2 loop
(90)      [----]   [SCAL] (1) $SEV_21[$i1] = tank.ports[$i1].m_flow >= tank.m_flow_turbulent[$i1] ($RES_EVT_201)
(90)      [----] end for;
(91)      [FOR-] (2) ($RES_EVT_202)
(91)      [----] for $i1 in 1:2 loop
(91)      [----]   [SCAL] (1) $SEV_22[$i1] = tank.ports[$i1].m_flow <= (-tank.m_flow_turbulent[$i1]) ($RES_EVT_203)
(91)      [----] end for;
(92)      [FOR-] (2) ($RES_EVT_204)
(92)      [----] for $i1 in 1:2 loop
(92)      [----]   [SCAL] (1) $SEV_23[$i1] = (tank.ports_penetration[$i1] * ((-1.0) + tank.portAreas[$i1] ^ 2.0 / tank.vesselArea ^ 2.0 + tank.portsData_zeta_in[$i1])) / tank.portInDensities[$i1] >= ((1.0 + tank.portsData_zeta_out[$i1]) - tank.portAreas[$i1] ^ 2.0 / tank.vesselArea ^ 2.0) / (tank.ports_penetration[$i1] * 995.586) ($RES_EVT_205)
(92)      [----] end for;
(93)      [SCAL] (1) flowSource.ports[1].h_outflow = 4184.0 * ((-273.15) + flowSource.T) ($RES_SIM_8)
(94)      [SCAL] (1) flowSource.ports[1].p = 99999.99999999999 * flowSource.medium.p_bar ($RES_SIM_7)
(95)      [SCAL] (1) $SEV_24 = tank.ports[2].m_flow > 0.0 ($RES_EVT_206)
(96)      [SCAL] (1) $SEV_25 = tank.ports[1].m_flow > 0.0 ($RES_EVT_207)
(97)      [SCAL] (1) timeTable.y = timeTable.a * time + timeTable.b ($RES_SIM_5)
(98)      [SCAL] (1) $SEV_26 = tank.fluidLevel > (-1e-6 * tank.fluidLevel_max) ($RES_EVT_208)
(99)      [ALGO] (5) ($RES_SIM_4)
(99)      [----] assert(not (timeTable.table[1, 1] > 0.0 or timeTable.table[1, 1] < 0.0), "The first point in time has to be set to 0, but is table[1,1] = " + String(timeTable.table[1, 1], 6, 0, true), AssertionLevel.error);

(99)      [----] when {time >= $PRE.timeTable.nextEvent, initial()} then
(99)      [----]   (timeTable.a, timeTable.b, timeTable.nextEventScaled, timeTable.last) := ($FUN_6, $FUN_7, $FUN_8, $FUN_9);
(99)      [----]   timeTable.nextEvent := timeTable.nextEventScaled;
(99)      [----] end when;

(100)     [SCAL] (1) $SEV_27 = tank.fluidLevel <= tank.fluidLevel_max ($RES_EVT_209)
(101)     [ARRY] (2) tank.portsData_zeta_out_internal = tank.portsData.zeta_out ($RES_BND_140)
(102)     [ARRY] (2) pipe.flowModel.vs = {-(0.0010044335697769957 * pipe.port_b.m_flow) / pipe.flowModel.crossAreas[1], -(0.0010044335697769957 * pipe.port_b.m_flow) / pipe.flowModel.crossAreas[2]} / pipe.nParallel ($RES_BND_143)
(103)     [ARRY] (2) pipe.flowModel.crossAreas = {pipe.crossArea, pipe.crossArea} ($RES_BND_144)