Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr Modelica_3.1_Modelica.Fluid.Examples.AST_BatchPlant.Test.TwoTanks.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)
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(Modelica.Fluid.Examples.AST_BatchPlant.Test.TwoTanks,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="Modelica_3.1_Modelica.Fluid.Examples.AST_BatchPlant.Test.TwoTanks")
translateModel(Modelica.Fluid.Examples.AST_BatchPlant.Test.TwoTanks,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="Modelica_3.1_Modelica.Fluid.Examples.AST_BatchPlant.Test.TwoTanks")
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo): time 0.001066/0.001066, allocations: 105.8 kB / 16.42 MB, free: 6.461 MB / 14.72 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo): time 0.001105/0.001105, allocations: 189.9 kB / 17.36 MB, free: 5.73 MB / 14.72 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.2.3+maint.om/package.mo): time 1.365/1.365, allocations: 205.1 MB / 223.2 MB, free: 12.25 MB / 190.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 2.517e-05/2.518e-05, allocations: 2.281 kB / 327.2 MB, free: 3.344 MB / 270.1 MB
Notification: Performance of NFInst.instantiate(Modelica.Fluid.Examples.AST_BatchPlant.Test.TwoTanks): time 0.01741/0.01744, allocations: 17.53 MB / 344.7 MB, free: 1.734 MB / 286.1 MB
Notification: Performance of NFInst.instExpressions: time 0.009115/0.02661, allocations: 5.98 MB / 350.7 MB, free: 11.74 MB / 302.1 MB
Notification: Performance of NFInst.updateImplicitVariability: time 0.001143/0.02781, allocations: 19.88 kB / 350.7 MB, free: 11.72 MB / 302.1 MB
Notification: Performance of NFTyping.typeComponents: time 0.001032/0.02885, allocations: 325.9 kB / 351 MB, free: 11.4 MB / 302.1 MB
Notification: Performance of NFTyping.typeBindings: time 0.002958/0.03194, allocations: 1.026 MB / 352.1 MB, free: 10.37 MB / 302.1 MB
Notification: Performance of NFTyping.typeClassSections: time 0.004335/0.03629, allocations: 1.66 MB / 353.7 MB, free: 8.707 MB / 302.1 MB
Notification: Performance of NFFlatten.flatten: time 0.003215/0.03952, allocations: 2.225 MB / 355.9 MB, free: 6.473 MB / 302.1 MB
Notification: Performance of NFFlatten.resolveConnections: time 0.0007741/0.04031, allocations: 0.5171 MB / 356.5 MB, free: 5.941 MB / 302.1 MB
Notification: Performance of NFEvalConstants.evaluate: time 0.001428/0.04174, allocations: 0.9074 MB / 357.4 MB, free: 5.031 MB / 302.1 MB
Notification: Performance of NFSimplifyModel.simplify: time 0.0009153/0.04267, allocations: 0.7514 MB / 358.1 MB, free: 4.277 MB / 302.1 MB
Notification: Performance of NFPackage.collectConstants: time 0.0001084/0.04279, allocations: 68 kB / 358.2 MB, free: 4.211 MB / 302.1 MB
Notification: Performance of NFFlatten.collectFunctions: time 0.002274/0.04508, allocations: 1.116 MB / 359.3 MB, free: 3.094 MB / 302.1 MB
Notification: Performance of combineBinaries: time 0.001323/0.04641, allocations: 1.552 MB / 360.9 MB, free: 1.527 MB / 302.1 MB
Notification: Performance of replaceArrayConstructors: time 0.0006537/0.04707, allocations: 0.9303 MB / 361.8 MB, free: 0.5859 MB / 302.1 MB
Notification: Performance of NFVerifyModel.verify: time 0.0002082/0.04729, allocations: 127.6 kB / 361.9 MB, free: 472 kB / 302.1 MB
Notification: Performance of FrontEnd: time 0.0001878/0.04748, allocations: 23.88 kB / 361.9 MB, free: 448 kB / 302.1 MB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 120 (109)
 * Number of variables: 124 (112)
Notification: Performance of Bindings: time 0.004024/0.05152, allocations: 4.022 MB / 365.9 MB, free: 12.29 MB / 318.1 MB
Notification: Performance of FunctionAlias: time 0.0003792/0.0519, allocations: 292.6 kB / 366.2 MB, free: 11.99 MB / 318.1 MB
Notification: Performance of Early Inline: time 0.002186/0.0541, allocations: 2.174 MB / 368.4 MB, free: 9.781 MB / 318.1 MB
Notification: Performance of simplify1: time 0.0002604/0.05437, allocations: 187.7 kB / 368.6 MB, free: 9.598 MB / 318.1 MB
Notification: Performance of Alias: time 0.002158/0.05654, allocations: 1.92 MB / 370.5 MB, free: 7.5 MB / 318.1 MB
Notification: Performance of simplify2: time 0.0001976/0.05675, allocations: 171.8 kB / 370.7 MB, free: 7.332 MB / 318.1 MB
Notification: Performance of Events: time 0.0006041/0.05736, allocations: 0.4991 MB / 371.2 MB, free: 6.816 MB / 318.1 MB
Notification: Performance of Detect States: time 0.0008634/0.05824, allocations: 0.5851 MB / 371.8 MB, free: 6.207 MB / 318.1 MB
Notification: Performance of Partitioning: time 0.0008485/0.0591, allocations: 0.797 MB / 372.6 MB, free: 5.332 MB / 318.1 MB
Error: Internal error NBAdjacency.Matrix.create failed to create adjacency matrix for system:
System Variables (114/126)
****************************
(1)       [ALGB] (1) stream Real pipe.port_a.h_outflow (min = -1e10, max = 1e10, nominal = 1e6)
(2)       [ALGB] (1) Real[1] tank1.heatTransfer.surfaceAreas = {sqrt(3.141592653589793 * tank1.crossArea) * 2.0 * tank1.level + tank1.crossArea}
(3)       [ALGB] (1) Real[1] pipe.flowModel.Ib_flows
(4)       [ALGB] (1) Real[1] tank2.heatTransfer.surfaceAreas = {sqrt(3.141592653589793 * tank2.crossArea) * 2.0 * tank2.level + tank2.crossArea}
(5)       [ALGB] (1) protected Real pipe.flowModel.dp_fric_nominal = sum({Modelica.Fluid.Examples.AST_BatchPlant.Test.TwoTanks.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)
(6)       [ALGB] (2) Real[2] pipe.flowModel.vs = {(-pipe.port_b.m_flow) / (pipe.flowModel.crossAreas[1] * Modelica.Fluid.Examples.AST_BatchPlant.Test.TwoTanks.pipe.Medium.density(pipe.flowModel.states[1])), -pipe.port_b.m_flow / (Modelica.Fluid.Examples.AST_BatchPlant.Test.TwoTanks.pipe.Medium.density(pipe.flowModel.states[2]) * pipe.flowModel.crossAreas[2])} / pipe.nParallel
(7)       [ALGB] (1) protected Real[1] pipe.flowModel.diameters = 0.5 * (pipe.flowModel.dimensions[2:2] + pipe.flowModel.dimensions[1:1])
(8)       [ALGB] (1) Real tank2.medium.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(9)       [ALGB] (1) protected Real[1] tank1.portsData_height = tank1.portsData.height
(10)      [ALGB] (1) final Real tank2.fluidVolume = tank2.fluidVolume
(11)      [ALGB] (1) Real tank1.medium.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(12)      [ALGB] (1) Real $FUN_10
(13)      [ALGB] (1) Real[1] tank1.heatTransfer.Q_flows
(14)      [ALGB] (2) Real[2] pipe.flowModel.mus = {Modelica.Fluid.Examples.AST_BatchPlant.Test.TwoTanks.pipe.flowModel.Medium.dynamicViscosity(pipe.flowModel.states[$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})
(15)      [ALGB] (1) Real tank1.mb_flow
(16)      [ALGB] (1) protected Real[1] tank2.portsData_height = tank2.portsData.height
(17)      [ALGB] (1) protected Real[1] tank1.zetas_out
(18)      [ALGB] (1) flow Real[1] tank1.ports.m_flow (start = {0.0 for $i1 in 1:1}, min = {-1e5 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1})
(19)      [DER-] (1) Real $DER.tank1.U
(20)      [ALGB] (1) Real[1] tank2.port_b_H_flow_bottom (min = {-1e8 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1000.0 for $i1 in 1:1})
(21)      [ALGB] (1) Real tank1.level (start = tank1.level_start, StateSelect = prefer)
(22)      [ALGB] (1) final input Real[1, 1] tank2.heatTransfer.states.T = {tank2.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})
(23)      [ALGB] (1) Real pipe.port_b.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(24)      [ALGB] (1) flow Real[1] tank1.heatTransfer.heatPorts.Q_flow
(25)      [ALGB] (1) Real[1] tank1.port_b_H_flow_bottom (min = {-1e8 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1000.0 for $i1 in 1:1})
(26)      [ALGB] (1) Real[1] pipe.flowModel.pathLengths_internal = pipe.flowModel.pathLengths
(27)      [ALGB] (1) Real tank1.medium.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(28)      [ALGB] (2) final Real[2] pipe.flowModel.dimensions = {(4.0 * pipe.crossArea) / pipe.perimeter, (4.0 * pipe.crossArea) / pipe.perimeter}
(29)      [ALGB] (1) Real $FUN_9
(30)      [DISC] (1) protected Boolean[1] tank1.aboveLevel
(31)      [ALGB] (1) Real tank2.level (start = tank2.level_start, StateSelect = prefer)
(32)      [ALGB] (1) Real $FUN_7
(33)      [ALGB] (1) Real $FUN_6
(34)      [ALGB] (1) Real $FUN_5
(35)      [DISC] (1) Boolean $SEV_20
(36)      [ALGB] (1) Real $FUN_4
(37)      [ALGB] (1) Real $FUN_3
(38)      [ALGB] (1) protected Real[1] tank1.portsData_diameter2
(39)      [ALGB] (1) Real[1] pipe.flowModel.Fs_p
(40)      [ALGB] (1) Real $FUN_2
(41)      [ALGB] (1) protected Real[1] tank1.bottomArea
(42)      [DER-] (1) Real $DER.tank1.m
(43)      [ALGB] (1) final input Real[1, 1] tank1.heatTransfer.states.p = {tank1.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})
(44)      [ALGB] (1) Real[1] tank2.heatTransfer.Ts = {Modelica.Fluid.Examples.AST_BatchPlant.Test.TwoTanks.tank2.heatTransfer.Medium.temperature(tank2.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})
(45)      [ALGB] (1) stream Real[1] tank2.ports.h_outflow (min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(46)      [ALGB] (1) Real[1] tank2.heatTransfer.Q_flows
(47)      [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)
(48)      [ALGB] (1) final input Real[1, 1] tank2.heatTransfer.states.p = {tank2.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})
(49)      [ALGB] (2) final Real[2] pipe.flowModel.roughnesses = {pipe.roughness, pipe.roughness} (min = {0.0 for $i1 in 1:2})
(50)      [ALGB] (1) Real[1] tank2.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})
(51)      [ALGB] (1) Real[1] pipe.flowModel.dps_fg (start = {pipe.flowModel.p_a_start - pipe.flowModel.p_b_start for $i1 in 1:1})
(52)      [ALGB] (1) Real tank2.Qb_flow
(53)      [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})
(54)      [DISC] (1) Boolean $SEV_19
(55)      [DISC] (1) protected Boolean[1] tank2.aboveLevel
(56)      [DISC] (1) Boolean $SEV_18
(57)      [ALGB] (1) protected Real[1] tank1.portsData_diameter = tank1.portsData.diameter
(58)      [DISC] (1) Boolean $SEV_17
(59)      [DISC] (1) Boolean $SEV_16
(60)      [ALGB] (1) protected Real[1] tank1.levelAbovePort
(61)      [ALGB] (1) Real[1] pipe.flowModel.Res_turbulent_internal = pipe.flowModel.Re_turbulent * {1.0 for $i1 in 1:1}
(62)      [DISC] (1) Boolean $SEV_15
(63)      [ALGB] (1) Real[1] tank2.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})
(64)      [DISC] (1) Boolean $SEV_14
(65)      [ALGB] (1) final Real[1] pipe.flowModel.dheights = {pipe.height_ab}
(66)      [ALGB] (1) protected Real[1] tank2.bottomArea
(67)      [ALGB] (1) final input Real[1, 1] tank1.heatTransfer.states.T = {tank1.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})
(68)      [DISC] (1) Boolean $SEV_10
(69)      [ALGB] (1) Real tank2.Hb_flow
(70)      [ALGB] (1) final Real[1] pipe.flowModel.pathLengths = {pipe.length}
(71)      [ALGB] (1) flow Real[1] tank2.ports.m_flow (start = {0.0 for $i1 in 1:1}, min = {-1e5 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1})
(72)      [ALGB] (1) stream Real pipe.port_b.h_outflow (min = -1e10, max = 1e10, nominal = 1e6)
(73)      [ALGB] (1) Real pipe.port_a.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(74)      [ALGB] (1) protected Real[1] tank2.levelAbovePort
(75)      [ALGB] (1) protected Real[1] tank1.portsData_height2
(76)      [ALGB] (1) Real tank1.Qb_flow
(77)      [ALGB] (1) protected Real[1] tank2.portsData_diameter = tank2.portsData.diameter
(78)      [ALGB] (1) protected Real[1] tank2.portsData_height2
(79)      [ALGB] (1) flow Real[1] tank2.heatTransfer.heatPorts.Q_flow
(80)      [ALGB] (1) Real tank1.medium.T_degC = Modelica.SIunits.Conversions.to_degC(-((-273.15) - tank1.medium.T_degC))
(81)      [ALGB] (1) Real[1] tank1.heatTransfer.Ts = {Modelica.Fluid.Examples.AST_BatchPlant.Test.TwoTanks.tank1.heatTransfer.Medium.temperature(tank1.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})
(82)      [ALGB] (1) stream Real[1] tank1.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)      [DISC] (1) Boolean $SEV_9
(84)      [DISC] (1) Boolean $SEV_8
(85)      [DISC] (1) Boolean $SEV_7
(86)      [DISC] (1) Boolean $SEV_6
(87)      [DISC] (1) Boolean $SEV_5
(88)      [ALGB] (1) Real[1] pipe.flowModel.Is
(89)      [DISC] (1) Boolean $SEV_4
(90)      [DER-] (1) Real $DER.tank2.U
(91)      [ALGB] (1) Real[1] tank1.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})
(92)      [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})
(93)      [DISC] (1) Boolean $SEV_3
(94)      [ALGB] (1) flow Real pipe.port_b.m_flow (min = -1e5, max = 1e60)
(95)      [ALGB] (1) protected Real[1] tank2.zetas_out
(96)      [DISC] (1) Boolean $SEV_1
(97)      [ALGB] (1) protected Real[1] tank1.ports_emptyPipeHysteresis (min = {0.0 for $i1 in 1:1})
(98)      [DISC] (1) Boolean $SEV_0
(99)      [ALGB] (1) Real tank1.Hb_flow
(100)     [DISC] (1) Boolean $TEV_1
(101)     [DISC] (1) Boolean $TEV_0
(102)     [ALGB] (1) Real tank2.medium.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(103)     [ALGB] (1) protected Real[1] tank2.ports_emptyPipeHysteresis (min = {0.0 for $i1 in 1:1})
(104)     [ALGB] (1) final Real tank1.fluidVolume = tank1.fluidVolume
(105)     [ALGB] (1) Real[1] pipe.flowModel.Fs_fg
(106)     [ALGB] (1) Real tank2.medium.T_degC = Modelica.SIunits.Conversions.to_degC(-((-273.15) - tank2.medium.T_degC))
(107)     [ALGB] (2) final Real[2] pipe.flowModel.crossAreas = {pipe.crossArea, pipe.crossArea}
(108)     [ALGB] (2) Real[2] pipe.flowModel.rhos = {Modelica.Fluid.Examples.AST_BatchPlant.Test.TwoTanks.pipe.flowModel.Medium.density(pipe.flowModel.states[$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})
(109)     [ALGB] (1) Real[1] tank1.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})
(110)     [ALGB] (1) protected Real[1] tank2.portsData_diameter2
(111)     [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})
(112)     [ALGB] (1) Real tank2.mb_flow
(113)     [DER-] (1) Real $DER.tank2.m
(114)     [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 (111/122)
****************************
(1)       [ARRY] (1) pipe.flowModel.dps_fg = {(2.0 * (pipe.flowModel.Fs_fg[1] / pipe.flowModel.nParallel)) / (pipe.flowModel.crossAreas[1] + pipe.flowModel.crossAreas[2])} ($RES_SIM_15)
(2)       [ARRY] (1) pipe.flowModel.Fs_p = pipe.flowModel.nParallel * {0.5 * (pipe.flowModel.crossAreas[1] + pipe.flowModel.crossAreas[2]) * (pipe.flowModel.states.T - pipe.flowModel.states.T)} ($RES_SIM_16)
(3)       [ARRY] (1) pipe.flowModel.Ib_flows = {0.0} ($RES_SIM_17)
(4)       [SCAL] (1) pipe.flowModel.rhos_act[1] = noEvent(if $SEV_3 then pipe.flowModel.rhos[1] else pipe.flowModel.rhos[2]) ($RES_SIM_18)
(5)       [SCAL] (1) pipe.flowModel.mus_act[1] = noEvent(if $SEV_3 then pipe.flowModel.mus[1] else pipe.flowModel.mus[2]) ($RES_SIM_19)
(6)       [SCAL] (1) $FUN_2 = sum(tank1.ports.m_flow) ($RES_$AUX_140)
(7)       [SCAL] (1) pipe.port_b.m_flow + tank2.ports[1].m_flow = 0.0 ($RES_SIM_91)
(8)       [SCAL] (1) $DER.tank1.m = tank1.mb_flow ($RES_SIM_56)
(9)       [SCAL] (1) tank2.heatTransfer.heatPorts[1].Q_flow = 0.0 ($RES_SIM_92)
(10)      [SCAL] (1) $DER.tank1.U = tank1.Qb_flow + tank1.Hb_flow ($RES_SIM_57)
(11)      [SCAL] (1) tank1.heatTransfer.heatPorts[1].Q_flow = 0.0 ($RES_SIM_93)
(12)      [SCAL] (1) tank1.U = tank1.m * (4184.0 * ((-273.15) - ((-273.15) - tank1.medium.T_degC))) ($RES_SIM_58)
(13)      [SCAL] (1) pipe.port_b.p = tank2.ports[1].p ($RES_SIM_94)
(14)      [SCAL] (1) tank1.m = 995.586 * tank1.fluidVolume ($RES_SIM_59)
(15)      [SCAL] (1) tank1.ports[1].m_flow - pipe.port_b.m_flow = 0.0 ($RES_SIM_95)
(16)      [SCAL] (1) tank1.ports[1].p = pipe.port_a.p ($RES_SIM_96)
(17)      [ARRY] (1) tank2.portsData_height = tank2.portsData_height2 ($RES_SIM_97)
(18)      [SCAL] (1) $SEV_20 = tank1.level <= tank1.height ($RES_EVT_170)
(19)      [ARRY] (1) tank2.portsData_diameter = tank2.portsData_diameter2 ($RES_SIM_98)
(20)      [ARRY] (1) tank1.portsData_height = tank1.portsData_height2 ($RES_SIM_99)
(21)      [ARRY] (1) tank2.heatTransfer.surfaceAreas = {2.0 * $FUN_9 * tank2.level + tank2.crossArea} ($RES_BND_111)
(22)      [ARRY] (1) tank2.heatTransfer.Ts = {tank2.heatTransfer.states.p} ($RES_BND_112)
(23)      [ARRY] (1) tank1.portsData_diameter = tank1.portsData_diameter2 ($RES_SIM_100)
(24)      [ARRY] (1) tank2.portsData_diameter = tank2.portsData.diameter ($RES_BND_113)
(25)      [ARRY] (1) tank2.portsData_height = tank2.portsData.height ($RES_BND_114)
(26)      [ARRY] (1) pipe.flowModel.m_flows = {homotopy(({$FUN_6} .* pipe.flowModel.nParallel)[1], (pipe.flowModel.m_flow_nominal / pipe.flowModel.dp_nominal * (pipe.flowModel.dps_fg - (pipe.flowModel.g * pipe.flowModel.dheights) .* pipe.flowModel.rho_nominal))[1])} ($RES_SIM_20)
(27)      [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_115)
(28)      [SCAL] (1) $FUN_3 = sum(tank1.port_b_H_flow_bottom) ($RES_$AUX_139)
(29)      [SCAL] (1) $DER.tank2.m = tank2.mb_flow ($RES_SIM_21)
(30)      [ARRY] (2) pipe.flowModel.crossAreas = {pipe.crossArea, pipe.crossArea} ($RES_BND_116)
(31)      [SCAL] (1) $FUN_4 = sum(tank2.ports.m_flow) ($RES_$AUX_138)
(32)      [SCAL] (1) $DER.tank2.U = tank2.Qb_flow + tank2.Hb_flow ($RES_SIM_22)
(33)      [ARRY] (2) pipe.flowModel.dimensions = {(4.0 * pipe.crossArea) / pipe.perimeter, (4.0 * pipe.crossArea) / pipe.perimeter} ($RES_BND_117)
(34)      [SCAL] (1) $FUN_5 = sum(tank2.port_b_H_flow_bottom) ($RES_$AUX_137)
(35)      [SCAL] (1) tank2.U = tank2.m * (4184.0 * ((-273.15) - ((-273.15) - tank2.medium.T_degC))) ($RES_SIM_23)
(36)      [ARRY] (2) pipe.flowModel.roughnesses = {pipe.roughness, pipe.roughness} ($RES_BND_118)
(37)      [SCAL] (1) $FUN_6 = Modelica.Fluid.Examples.AST_BatchPlant.Test.TwoTanks.pipe.flowModel.WallFriction.massFlowRate_dp_staticHead(pipe.flowModel.dps_fg[1], pipe.flowModel.rhos[1], pipe.flowModel.rhos[2], pipe.flowModel.mus[1], pipe.flowModel.mus[2], pipe.flowModel.pathLengths_internal[1], pipe.flowModel.diameters[1], (pipe.flowModel.g * pipe.flowModel.dheights)[1], (0.5 .* (pipe.flowModel.crossAreas[1:1] + pipe.flowModel.crossAreas[2:2]))[1], (0.5 .* (pipe.flowModel.roughnesses[1:1] + pipe.flowModel.roughnesses[2:2]))[1], pipe.flowModel.dp_small, pipe.flowModel.Res_turbulent_internal[1]) ($RES_$AUX_136)
(38)      [SCAL] (1) tank2.m = 995.586 * tank2.fluidVolume ($RES_SIM_24)
(39)      [ARRY] (1) pipe.flowModel.dheights = {pipe.height_ab} ($RES_BND_119)
(40)      [SCAL] (1) $FUN_7 = Modelica.Fluid.Examples.AST_BatchPlant.Test.TwoTanks.pipe.flowModel.WallFriction.pressureLoss_m_flow(pipe.flowModel.m_flow_nominal / pipe.flowModel.nParallel, pipe.flowModel.rho_nominal, pipe.flowModel.rho_nominal, pipe.flowModel.mu_nominal, pipe.flowModel.mu_nominal, pipe.flowModel.pathLengths_internal[1], pipe.flowModel.diameters[1], (0.5 .* (pipe.flowModel.crossAreas[2:2] + pipe.flowModel.crossAreas[1:1]))[1], (0.5 .* (pipe.flowModel.roughnesses[2:2] + pipe.flowModel.roughnesses[1:1]))[1], pipe.flowModel.m_flow_small / pipe.flowModel.nParallel, pipe.flowModel.Res_turbulent_internal[1]) ($RES_$AUX_135)
(41)      [SCAL] (1) tank1.aboveLevel[1] = $SEV_14 ($RES_SIM_60)
(42)      [SCAL] (1) tank2.aboveLevel[1] = $SEV_4 ($RES_SIM_25)
(43)      [SCAL] (1) pipe.flowModel.dp_fric_nominal = sum({$FUN_7}) ($RES_$AUX_134)
(44)      [SCAL] (1) tank1.levelAbovePort[1] = if tank1.aboveLevel[1] then tank1.level - tank1.portsData_height2[1] else 0.0 ($RES_SIM_61)
(45)      [SCAL] (1) tank2.levelAbovePort[1] = if tank2.aboveLevel[1] then tank2.level - tank2.portsData_height2[1] else 0.0 ($RES_SIM_26)
(46)      [SCAL] (1) $FUN_9 = sqrt(3.141592653589793 * tank2.crossArea) ($RES_$AUX_133)
(47)      [SCAL] (1) tank1.ports[1].h_outflow = 4184.0 * ((-273.15) - ((-273.15) - tank1.medium.T_degC)) ($RES_SIM_62)
(48)      [SCAL] (1) tank2.ports[1].h_outflow = 4184.0 * ((-273.15) - ((-273.15) - tank2.medium.T_degC)) ($RES_SIM_27)
(49)      [SCAL] (1) $FUN_10 = sqrt(3.141592653589793 * tank1.crossArea) ($RES_$AUX_132)
(50)      [SCAL] (1) tank1.zetas_out[1] = 1.0 + (if tank1.aboveLevel[1] then 0.0 else tank1.zetaLarge) ($RES_SIM_63)
(51)      [SCAL] (1) tank2.zetas_out[1] = 1.0 + (if tank2.aboveLevel[1] then 0.0 else tank2.zetaLarge) ($RES_SIM_28)
(52)      [SCAL] (1) tank1.ports[1].p = 995.586 * system.g * tank1.levelAbovePort[1] + tank1.p_ambient + smooth(2, if $SEV_15 then (8.14163185439231e-6 * tank1.ports[1].m_flow ^ 2.0) / (tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1]) else if $SEV_16 then -(8.141631854392309e-4 * tank1.zetas_out[1] * tank1.ports[1].m_flow ^ 2.0) / (tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1]) else if $SEV_17 then Modelica.Fluid.Utilities.regSquare2.regSquare2_utility(tank1.ports[1].m_flow, tank1.m_flow_small, 8.14163185439231e-6 / (tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1]), (8.141631854392309e-4 * tank1.zetas_out[1]) / (tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1]), false, 1.0) else -Modelica.Fluid.Utilities.regSquare2.regSquare2_utility(-tank1.ports[1].m_flow, tank1.m_flow_small, (8.141631854392309e-4 * tank1.zetas_out[1]) / (tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1]), 8.14163185439231e-6 / (tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1]), false, 1.0)) ($RES_SIM_64)
(53)      [SCAL] (1) tank2.ports[1].p = 995.586 * system.g * tank2.levelAbovePort[1] + tank2.p_ambient + smooth(2, if $SEV_5 then (8.14163185439231e-6 * tank2.ports[1].m_flow ^ 2.0) / (tank2.portsData_diameter2[1] * tank2.portsData_diameter2[1] * tank2.portsData_diameter2[1] * tank2.portsData_diameter2[1]) else if $SEV_6 then -(8.141631854392309e-4 * tank2.zetas_out[1] * tank2.ports[1].m_flow ^ 2.0) / (tank2.portsData_diameter2[1] * tank2.portsData_diameter2[1] * tank2.portsData_diameter2[1] * tank2.portsData_diameter2[1]) else if $SEV_7 then Modelica.Fluid.Utilities.regSquare2.regSquare2_utility(tank2.ports[1].m_flow, tank2.m_flow_small, 8.14163185439231e-6 / (tank2.portsData_diameter2[1] * tank2.portsData_diameter2[1] * tank2.portsData_diameter2[1] * tank2.portsData_diameter2[1]), (8.141631854392309e-4 * tank2.zetas_out[1]) / (tank2.portsData_diameter2[1] * tank2.portsData_diameter2[1] * tank2.portsData_diameter2[1] * tank2.portsData_diameter2[1]), false, 1.0) else -Modelica.Fluid.Utilities.regSquare2.regSquare2_utility(-tank2.ports[1].m_flow, tank2.m_flow_small, (8.141631854392309e-4 * tank2.zetas_out[1]) / (tank2.portsData_diameter2[1] * tank2.portsData_diameter2[1] * tank2.portsData_diameter2[1] * tank2.portsData_diameter2[1]), 8.14163185439231e-6 / (tank2.portsData_diameter2[1] * tank2.portsData_diameter2[1] * tank2.portsData_diameter2[1] * tank2.portsData_diameter2[1]), false, 1.0)) ($RES_SIM_29)
(54)      [SCAL] (1) tank1.port_b_H_flow_bottom[1] = smooth(0, tank1.ports[1].m_flow * (if $SEV_18 then pipe.port_a.h_outflow else tank1.ports[1].h_outflow)) ($RES_SIM_66)
(55)      [SCAL] (1) tank1.Qb_flow = tank1.heatTransfer.Q_flows[1] ($RES_SIM_68)
(56)      [SCAL] (1) tank1.Hb_flow = $FUN_3 ($RES_SIM_69)
(57)      [SCAL] (1) $TEV_0 = $PRE.tank2.aboveLevel ($RES_EVT_148)
(58)      [SCAL] (1) $TEV_1 = $PRE.tank1.aboveLevel ($RES_EVT_149)
(59)      [ARRY] (1) pipe.flowModel.pathLengths = {pipe.length} ($RES_BND_120)
(60)      [FOR-] (2) ($RES_BND_121)
(60)      [----] for $i1 in 1:2 loop
(60)      [----]   [SCAL] (1) pipe.flowModel.rhos[$i1] = 995.586 ($RES_BND_122)
(60)      [----] end for;
(61)      [FOR-] (2) ($RES_BND_123)
(61)      [----] for $i1 in 1:2 loop
(61)      [----]   [SCAL] (1) pipe.flowModel.mus[$i1] = 0.001 ($RES_BND_124)
(61)      [----] end for;
(62)      [ARRY] (1) pipe.flowModel.pathLengths_internal = pipe.flowModel.pathLengths ($RES_BND_125)
(63)      [SCAL] (1) tank2.port_b_H_flow_bottom[1] = smooth(0, tank2.ports[1].m_flow * (if $SEV_8 then pipe.port_b.h_outflow else tank2.ports[1].h_outflow)) ($RES_SIM_31)
(64)      [SCAL] (1) pipe.flowModel.Res_turbulent_internal[1] = pipe.flowModel.Re_turbulent ($RES_BND_126)
(65)      [ARRY] (1) pipe.flowModel.diameters = 0.5 * (pipe.flowModel.dimensions[2:2] + pipe.flowModel.dimensions[1:1]) ($RES_BND_127)
(66)      [SCAL] (1) tank2.Qb_flow = tank2.heatTransfer.Q_flows[1] ($RES_SIM_33)
(67)      [SCAL] (1) tank2.Hb_flow = $FUN_5 ($RES_SIM_34)
(68)      [ARRY] (2) tank1.heatTransfer.states = {tank1.medium.state} ($RES_BND_129)
(69)      [SCAL] (1) tank1.mb_flow = $FUN_2 ($RES_SIM_70)
(70)      [SCAL] (1) tank2.mb_flow = $FUN_4 ($RES_SIM_35)
(71)      [SCAL] (1) tank1.fluidVolume = tank1.crossArea * tank1.level + tank1.V0 ($RES_SIM_71)
(72)      [SCAL] (1) tank2.fluidVolume = tank2.crossArea * tank2.level + tank2.V0 ($RES_SIM_36)
(73)      [SCAL] (1) tank1.bottomArea[1] = 3.141592653589793 * (tank1.portsData_diameter2[1] / 2.0) ^ 2.0 ($RES_SIM_73)
(74)      [SCAL] (1) tank2.bottomArea[1] = 3.141592653589793 * (tank2.portsData_diameter2[1] / 2.0) ^ 2.0 ($RES_SIM_38)
(75)      [SCAL] (1) tank1.ports_emptyPipeHysteresis[1] = tank1.portsData_diameter2[1] * tank1.hysteresisFactor ($RES_SIM_74)
(76)      [SCAL] (1) tank2.ports_emptyPipeHysteresis[1] = tank2.portsData_diameter2[1] * tank2.hysteresisFactor ($RES_SIM_39)
(77)      [ARRY] (1) tank1.heatTransfer.Q_flows = tank1.heatTransfer.heatPorts.Q_flow ($RES_SIM_77)
(78)      [SCAL] (1) $SEV_0 = tank2.level_start >= tank2.portsData_height2[1] ($RES_EVT_150)
(79)      [ARRY] (1) tank1.heatTransfer.Ts = tank1.heatTransfer.heatPorts.T ($RES_SIM_78)
(80)      [SCAL] (1) $SEV_1 = tank1.level_start >= tank1.portsData_height2[1] ($RES_EVT_151)
(81)      [SCAL] (1) $SEV_3 = pipe.flowModel.m_flows[1] > 0.0 ($RES_EVT_153)
(82)      [SCAL] (1) $SEV_4 = tank2.level >= (tank2.portsData_height2[1] + tank2.ports_emptyPipeHysteresis[1]) or $PRE.tank2.aboveLevel[1] and tank2.level >= (tank2.portsData_height2[1] - tank2.ports_emptyPipeHysteresis[1]) ($RES_EVT_154)
(83)      [SCAL] (1) $SEV_5 = tank2.ports[1].m_flow >= tank2.m_flow_small ($RES_EVT_155)
(84)      [SCAL] (1) $SEV_6 = tank2.ports[1].m_flow <= (-tank2.m_flow_small) ($RES_EVT_156)
(85)      [SCAL] (1) $SEV_7 = 8.14163185439231e-6 / (tank2.portsData_diameter2[1] * tank2.portsData_diameter2[1] * tank2.portsData_diameter2[1] * tank2.portsData_diameter2[1]) >= (8.141631854392309e-4 * tank2.zetas_out[1]) / (tank2.portsData_diameter2[1] * tank2.portsData_diameter2[1] * tank2.portsData_diameter2[1] * tank2.portsData_diameter2[1]) ($RES_EVT_157)
(86)      [SCAL] (1) $SEV_8 = tank2.ports[1].m_flow > 0.0 ($RES_EVT_158)
(87)      [SCAL] (1) $SEV_9 = tank2.m >= 0.0 ($RES_EVT_159)
(88)      [ARRY] (2) tank2.heatTransfer.states = {tank2.medium.state} ($RES_BND_130)
(89)      [ARRY] (4) pipe.flowModel.states = {Modelica.Fluid.Examples.AST_BatchPlant.Test.TwoTanks.pipe.Medium.ThermodynamicState(pipe.port_a.p, 273.15 + 2.390057361376673e-4 * tank1.ports[1].h_outflow), Modelica.Fluid.Examples.AST_BatchPlant.Test.TwoTanks.pipe.Medium.ThermodynamicState(pipe.port_b.p, 273.15 + 2.390057361376673e-4 * tank2.ports[1].h_outflow)} ($RES_BND_131)
(90)      [ARRY] (1) tank2.heatTransfer.Q_flows = tank2.heatTransfer.heatPorts.Q_flow ($RES_SIM_42)
(91)      [ARRY] (1) tank2.heatTransfer.Ts = tank2.heatTransfer.heatPorts.T ($RES_SIM_43)
(92)      [SCAL] (1) tank1.medium.state.p = tank1.p_ambient ($RES_SIM_83)
(93)      [SCAL] (1) tank2.medium.state.p = tank2.p_ambient ($RES_SIM_48)
(94)      [SCAL] (1) tank1.medium.state.T = -((-273.15) - tank1.medium.T_degC) ($RES_SIM_84)
(95)      [SCAL] (1) tank2.medium.state.T = -((-273.15) - tank2.medium.T_degC) ($RES_SIM_49)
(96)      [SCAL] (1) $SEV_10 = tank2.level <= tank2.height ($RES_EVT_160)
(97)      [SCAL] (1) $SEV_14 = tank1.level >= (tank1.portsData_height2[1] + tank1.ports_emptyPipeHysteresis[1]) or $PRE.tank1.aboveLevel[1] and tank1.level >= (tank1.portsData_height2[1] - tank1.ports_emptyPipeHysteresis[1]) ($RES_EVT_164)
(98)      [SCAL] (1) $SEV_15 = tank1.ports[1].m_flow >= tank1.m_flow_small ($RES_EVT_165)
(99)      [SCAL] (1) pipe.port_a.h_outflow = tank2.ports[1].h_outflow + system.g * pipe.height_ab ($RES_SIM_9)
(100)     [SCAL] (1) $SEV_16 = tank1.ports[1].m_flow <= (-tank1.m_flow_small) ($RES_EVT_166)
(101)     [SCAL] (1) $SEV_17 = 8.14163185439231e-6 / (tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1]) >= (8.141631854392309e-4 * tank1.zetas_out[1]) / (tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1] * tank1.portsData_diameter2[1]) ($RES_EVT_167)
(102)     [SCAL] (1) $SEV_18 = tank1.ports[1].m_flow > 0.0 ($RES_EVT_168)
(103)     [SCAL] (1) $SEV_19 = tank1.m >= 0.0 ($RES_EVT_169)
(104)     [ARRY] (1) tank1.heatTransfer.surfaceAreas = {2.0 * $FUN_10 * tank1.level + tank1.crossArea} ($RES_BND_104)
(105)     [SCAL] (1) pipe.port_b.h_outflow = tank1.ports[1].h_outflow - system.g * pipe.height_ab ($RES_SIM_10)
(106)     [ARRY] (1) tank1.heatTransfer.Ts = {tank1.heatTransfer.states.p} ($RES_BND_105)
(107)     [ARRY] (1) tank1.portsData_diameter = tank1.portsData.diameter ($RES_BND_106)
(108)     [SCAL] (1) -pipe.port_b.m_flow = pipe.flowModel.m_flows[1] ($RES_SIM_12)
(109)     [ARRY] (1) tank1.portsData_height = tank1.portsData.height ($RES_BND_107)
(110)     [ARRY] (1) {0.0} = pipe.flowModel.Ib_flows - (pipe.flowModel.Fs_fg + pipe.flowModel.Fs_p) ($RES_SIM_13)
(111)     [ARRY] (1) pipe.flowModel.Is = {pipe.flowModel.m_flows[1] * pipe.flowModel.pathLengths[1]} ($RES_SIM_14)