Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr Modelica_3.1_Modelica.Fluid.Examples.AST_BatchPlant.Test.TankWithEmptyingPipe1.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.TankWithEmptyingPipe1,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="Modelica_3.1_Modelica.Fluid.Examples.AST_BatchPlant.Test.TankWithEmptyingPipe1")
translateModel(Modelica.Fluid.Examples.AST_BatchPlant.Test.TankWithEmptyingPipe1,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="Modelica_3.1_Modelica.Fluid.Examples.AST_BatchPlant.Test.TankWithEmptyingPipe1")
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo): time 0.001262/0.001262, allocations: 109.9 kB / 16.42 MB, free: 6.031 MB / 14.72 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo): time 0.001204/0.001204, allocations: 193.1 kB / 17.35 MB, free: 5.625 MB / 14.72 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.2.3+maint.om/package.mo): time 1.377/1.377, allocations: 205.1 MB / 223.2 MB, free: 12.25 MB / 190.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 1.482e-05/1.483e-05, allocations: 3.547 kB / 327.2 MB, free: 3.352 MB / 270.1 MB
Notification: Performance of NFInst.instantiate(Modelica.Fluid.Examples.AST_BatchPlant.Test.TankWithEmptyingPipe1): time 0.01909/0.01912, allocations: 20.6 MB / 347.8 MB, free: 14.66 MB / 302.1 MB
Notification: Performance of NFInst.instExpressions: time 0.008628/0.02778, allocations: 6.984 MB / 354.8 MB, free: 7.656 MB / 302.1 MB
Notification: Performance of NFInst.updateImplicitVariability: time 0.0004686/0.02827, allocations: 23.81 kB / 354.8 MB, free: 7.633 MB / 302.1 MB
Notification: Performance of NFTyping.typeComponents: time 0.0008595/0.02914, allocations: 373.6 kB / 355.2 MB, free: 7.266 MB / 302.1 MB
Notification: Performance of NFTyping.typeBindings: time 0.002009/0.03115, allocations: 1.084 MB / 356.2 MB, free: 6.176 MB / 302.1 MB
Notification: Performance of NFTyping.typeClassSections: time 0.003506/0.03467, allocations: 1.862 MB / 358.1 MB, free: 4.309 MB / 302.1 MB
Notification: Performance of NFFlatten.flatten: time 0.002119/0.0368, allocations: 2.26 MB / 360.4 MB, free: 2.043 MB / 302.1 MB
Notification: Performance of NFFlatten.resolveConnections: time 0.0007065/0.03752, allocations: 0.6007 MB / 361 MB, free: 1.434 MB / 302.1 MB
Notification: Performance of NFEvalConstants.evaluate: time 0.001082/0.03861, allocations: 0.9346 MB / 361.9 MB, free: 0.4961 MB / 302.1 MB
Notification: Performance of NFSimplifyModel.simplify: time 0.0007926/0.03942, allocations: 0.7241 MB / 362.6 MB, free: 15.77 MB / 318.1 MB
Notification: Performance of NFPackage.collectConstants: time 0.0001078/0.03954, allocations: 72 kB / 362.7 MB, free: 15.7 MB / 318.1 MB
Notification: Performance of NFFlatten.collectFunctions: time 0.001836/0.04138, allocations: 1.256 MB / 363.9 MB, free: 14.44 MB / 318.1 MB
Notification: Performance of combineBinaries: time 0.001212/0.0426, allocations: 1.571 MB / 365.5 MB, free: 12.86 MB / 318.1 MB
Notification: Performance of replaceArrayConstructors: time 0.0006244/0.04324, allocations: 0.9577 MB / 366.5 MB, free: 11.89 MB / 318.1 MB
Notification: Performance of NFVerifyModel.verify: time 0.0001497/0.04339, allocations: 143.6 kB / 366.6 MB, free: 11.75 MB / 318.1 MB
Notification: Performance of FrontEnd: time 0.0001306/0.04353, allocations: 27.88 kB / 366.6 MB, free: 11.72 MB / 318.1 MB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 145 (121)
 * Number of variables: 149 (123)
Notification: Performance of Bindings: time 0.003813/0.04735, allocations: 4.135 MB / 370.8 MB, free: 7.434 MB / 318.1 MB
Notification: Performance of FunctionAlias: time 0.0004283/0.04779, allocations: 392.7 kB / 371.2 MB, free: 7.039 MB / 318.1 MB
Notification: Performance of Early Inline: time 0.002405/0.0502, allocations: 2.455 MB / 373.6 MB, free: 4.543 MB / 318.1 MB
Notification: Performance of simplify1: time 0.0001983/0.05041, allocations: 151.8 kB / 373.8 MB, free: 4.395 MB / 318.1 MB
Notification: Performance of Alias: time 0.00256/0.05298, allocations: 2.34 MB / 376.1 MB, free: 1.836 MB / 318.1 MB
Notification: Performance of simplify2: time 0.0001491/0.05314, allocations: 139.8 kB / 376.2 MB, free: 1.699 MB / 318.1 MB
Notification: Performance of Events: time 0.0006732/0.05382, allocations: 0.5644 MB / 376.8 MB, free: 1.113 MB / 318.1 MB
Notification: Performance of Detect States: time 0.0006401/0.05447, allocations: 0.6007 MB / 377.4 MB, free: 0.5 MB / 318.1 MB
Notification: Performance of Partitioning: time 0.1658/0.2203, allocations: 0.869 MB / 378.3 MB, free: 22.75 MB / 318.1 MB
Error: Internal error NBAdjacency.Matrix.create failed to create adjacency matrix for system:
System Variables (102/135)
****************************
(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) protected Real pipe.flowModel.dp_fric_nominal = sum({Modelica.Fluid.Examples.AST_BatchPlant.Test.TankWithEmptyingPipe1.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)
(5)       [ALGB] (2) Real[2] pipe.flowModel.vs = {(-pipe.port_b.m_flow) / (pipe.flowModel.crossAreas[1] * Modelica.Fluid.Examples.AST_BatchPlant.Test.TankWithEmptyingPipe1.pipe.Medium.density(pipe.flowModel.states[1])), -pipe.port_b.m_flow / (Modelica.Fluid.Examples.AST_BatchPlant.Test.TankWithEmptyingPipe1.pipe.Medium.density(pipe.flowModel.states[2]) * pipe.flowModel.crossAreas[2])} / pipe.nParallel
(6)       [ALGB] (1) protected Real[1] pipe.flowModel.diameters = 0.5 * (pipe.flowModel.dimensions[2:2] + pipe.flowModel.dimensions[1:1])
(7)       [ALGB] (1) stream Real valveDiscrete.port_b.h_outflow (min = -1e10, max = 1e10, nominal = 1e6)
(8)       [ALGB] (2) protected Real[2] tank1.portsData_height = tank1.portsData.height
(9)       [ALGB] (1) Real tank1.medium.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(10)      [DISC] (2) Boolean[2] $SEV_0[$i1]
(11)      [ALGB] (1) Real[1] tank1.heatTransfer.Q_flows
(12)      [ALGB] (2) Real[2] pipe.flowModel.mus = {Modelica.Fluid.Examples.AST_BatchPlant.Test.TankWithEmptyingPipe1.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})
(13)      [ALGB] (1) Real valveDiscrete.V_flow = (995.586 * valveDiscrete.V_flow) / Modelica.Fluid.Utilities.regStep(995.586 * valveDiscrete.V_flow, Modelica.Fluid.Examples.AST_BatchPlant.Test.TankWithEmptyingPipe1.valveDiscrete.Medium.density(valveDiscrete.state_a), Modelica.Fluid.Examples.AST_BatchPlant.Test.TankWithEmptyingPipe1.valveDiscrete.Medium.density(valveDiscrete.state_b), valveDiscrete.m_flow_small)
(14)      [ALGB] (1) Real tank1.mb_flow
(15)      [ALGB] (2) protected Real[2] tank1.zetas_out
(16)      [ALGB] (2) flow Real[2] tank1.ports.m_flow (start = {0.0 for $i1 in 1:2}, min = {-1e5 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2})
(17)      [DER-] (1) Real $DER.tank1.U
(18)      [DISC] (2) Boolean[2] $SEV_3[$i1]
(19)      [ALGB] (1) protected Real valveDiscrete.state_b.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(20)      [ALGB] (1) Real tank1.level (start = tank1.level_start, StateSelect = prefer)
(21)      [ALGB] (1) Real pipe.port_b.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(22)      [ALGB] (1) Real valveDiscrete.port_a.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(23)      [ALGB] (1) flow Real[1] tank1.heatTransfer.heatPorts.Q_flow
(24)      [ALGB] (2) Real[2] tank1.port_b_H_flow_bottom (min = {-1e8 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1000.0 for $i1 in 1:2})
(25)      [DISC] (1) Boolean $SEV_28
(26)      [DISC] (1) Boolean $SEV_27
(27)      [ALGB] (1) Real[1] pipe.flowModel.pathLengths_internal = pipe.flowModel.pathLengths
(28)      [DISC] (1) Boolean $SEV_26
(29)      [DISC] (2) Boolean[2] $SEV_6[$i1]
(30)      [DISC] (1) Boolean $SEV_25
(31)      [ALGB] (2) final Real[2] pipe.flowModel.dimensions = {(4.0 * pipe.crossArea) / pipe.perimeter, (4.0 * pipe.crossArea) / pipe.perimeter}
(32)      [ALGB] (1) Real tank1.medium.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(33)      [ALGB] (1) Real valveDiscrete.port_b_T = Modelica.Fluid.Utilities.regStep(-995.586 * valveDiscrete.V_flow, Modelica.Fluid.Examples.AST_BatchPlant.Test.TankWithEmptyingPipe1.valveDiscrete.Medium.temperature(valveDiscrete.state_b), Modelica.Fluid.Examples.AST_BatchPlant.Test.TankWithEmptyingPipe1.valveDiscrete.Medium.temperature(Modelica.Fluid.Examples.AST_BatchPlant.Test.TankWithEmptyingPipe1.valveDiscrete.Medium.setState_phX(valveDiscrete.port_b.p, valveDiscrete.port_b.h_outflow, {})), valveDiscrete.m_flow_small) (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(34)      [DISC] (1) Boolean $SEV_24
(35)      [ALGB] (1) Real $FUN_8
(36)      [DISC] (2) protected Boolean[2] tank1.aboveLevel
(37)      [ALGB] (1) Real $FUN_6
(38)      [ALGB] (1) Real $FUN_5
(39)      [DISC] (1) Boolean $SEV_20
(40)      [ALGB] (1) Real $FUN_4
(41)      [ALGB] (1) Real flowSource.medium.p_bar = Modelica.SIunits.Conversions.to_bar(99999.99999999999 * flowSource.medium.p_bar)
(42)      [ALGB] (1) Real $FUN_3
(43)      [ALGB] (2) protected Real[2] tank1.portsData_diameter2
(44)      [ALGB] (1) Real[1] pipe.flowModel.Fs_p
(45)      [ALGB] (2) protected Real[2] tank1.bottomArea
(46)      [DER-] (1) Real $DER.tank1.m
(47)      [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})
(48)      [DISC] (2) Boolean[2] $SEV_9[$i1]
(49)      [ALGB] (1) protected Real valveDiscrete.state_a.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(50)      [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)
(51)      [ALGB] (2) final Real[2] pipe.flowModel.roughnesses = {pipe.roughness, pipe.roughness} (min = {0.0 for $i1 in 1:2})
(52)      [ALGB] (1) Real[1] pipe.flowModel.dps_fg (start = {pipe.flowModel.p_a_start - pipe.flowModel.p_b_start for $i1 in 1:1})
(53)      [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})
(54)      [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})
(55)      [ALGB] (1) flow Real[1] ambient_fixed.ports.m_flow (min = {-1e60}, max = {1e60})
(56)      [ALGB] (2) protected Real[2] tank1.portsData_diameter = tank1.portsData.diameter
(57)      [ALGB] (2) protected Real[2] tank1.levelAbovePort
(58)      [ALGB] (1) Real[1] pipe.flowModel.Res_turbulent_internal = pipe.flowModel.Re_turbulent * {1.0 for $i1 in 1:1}
(59)      [ALGB] (1) flow Real[1] flowSource.ports.m_flow (min = {-1e60}, max = {1e60})
(60)      [ALGB] (1) final Real[1] pipe.flowModel.dheights = {pipe.height_ab}
(61)      [DISC] (1) Boolean $SEV_13
(62)      [DISC] (1) Boolean $SEV_12
(63)      [DISC] (1) Boolean $SEV_11
(64)      [DISC] (2) Boolean[2] $SEV_5[$i1]
(65)      [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})
(66)      [DISC] (1) Boolean $SEV_10
(67)      [ALGB] (1) final Real[1] pipe.flowModel.pathLengths = {pipe.length}
(68)      [ALGB] (1) protected Real valveDiscrete.state_a.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(69)      [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})
(70)      [ALGB] (1) stream Real pipe.port_b.h_outflow (min = -1e10, max = 1e10, nominal = 1e6)
(71)      [ALGB] (1) Real pipe.port_a.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(72)      [ALGB] (2) protected Real[2] tank1.portsData_height2
(73)      [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})
(74)      [ALGB] (1) Real tank1.Qb_flow
(75)      [ALGB] (1) Real tank1.medium.T_degC = Modelica.SIunits.Conversions.to_degC(-((-273.15) - tank1.medium.T_degC))
(76)      [ALGB] (1) Real[1] tank1.heatTransfer.Ts = {Modelica.Fluid.Examples.AST_BatchPlant.Test.TankWithEmptyingPipe1.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})
(77)      [ALGB] (2) stream Real[2] tank1.ports.h_outflow (min = {-1e10 for $i1 in 1:2}, max = {1e10 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2})
(78)      [DISC] (2) Boolean[2] $SEV_8[$i1]
(79)      [ALGB] (1) stream Real valveDiscrete.port_a.h_outflow (min = -1e10, max = 1e10, nominal = 1e6)
(80)      [ALGB] (1) Real valveDiscrete.port_a_T = Modelica.Fluid.Utilities.regStep(995.586 * valveDiscrete.V_flow, Modelica.Fluid.Examples.AST_BatchPlant.Test.TankWithEmptyingPipe1.valveDiscrete.Medium.temperature(valveDiscrete.state_a), Modelica.Fluid.Examples.AST_BatchPlant.Test.TankWithEmptyingPipe1.valveDiscrete.Medium.temperature(Modelica.Fluid.Examples.AST_BatchPlant.Test.TankWithEmptyingPipe1.valveDiscrete.Medium.setState_phX(valveDiscrete.port_a.p, valveDiscrete.port_a.h_outflow, {})), valveDiscrete.m_flow_small) (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(81)      [ALGB] (1) Real[1] pipe.flowModel.Is
(82)      [ALGB] (2) Real[2] tank1.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})
(83)      [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})
(84)      [ALGB] (1) flow Real pipe.port_b.m_flow (min = -1e5, max = 1e60)
(85)      [DISC] (1) Boolean $SEV_2
(86)      [ALGB] (2) protected Real[2] tank1.ports_emptyPipeHysteresis (min = {0.0 for $i1 in 1:2})
(87)      [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})
(88)      [ALGB] (1) Real valveDiscrete.port_b.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(89)      [ALGB] (1) Real tank1.Hb_flow
(90)      [DISC] (1) Boolean $TEV_0
(91)      [ALGB] (1) final Real tank1.fluidVolume = tank1.fluidVolume
(92)      [ALGB] (1) Real[1] pipe.flowModel.Fs_fg
(93)      [ALGB] (2) final Real[2] pipe.flowModel.crossAreas = {pipe.crossArea, pipe.crossArea}
(94)      [ALGB] (2) Real[2] pipe.flowModel.rhos = {Modelica.Fluid.Examples.AST_BatchPlant.Test.TankWithEmptyingPipe1.pipe.flowModel.Medium.density(pipe.flowModel.states[$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})
(95)      [DISC] (2) Boolean[2] $SEV_4[$i1]
(96)      [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})
(97)      [ALGB] (1) Real flowSource.medium.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(98)      [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})
(99)      [ALGB] (1) protected Real valveDiscrete.state_b.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(100)     [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})
(101)     [ALGB] (1) Real valveDiscrete.dp (start = valveDiscrete.dp_start)
(102)     [DISC] (2) Boolean[2] $SEV_7[$i1]


System Equations (102/131)
****************************
(1)       [FOR-] (2) ($RES_BND_145)
(1)       [----] for $i1 in 1:2 loop
(1)       [----]   [SCAL] (1) pipe.flowModel.rhos[$i1] = 995.586 ($RES_BND_146)
(1)       [----] end for;
(2)       [ARRY] (1) tank1.heatTransfer.Ts = tank1.heatTransfer.heatPorts.T ($RES_SIM_50)
(3)       [ARRY] (1) pipe.flowModel.Ib_flows = {0.0} ($RES_SIM_15)
(4)       [SCAL] (1) pipe.flowModel.rhos_act[1] = noEvent(if $SEV_2 then pipe.flowModel.rhos[1] else pipe.flowModel.rhos[2]) ($RES_SIM_16)
(5)       [FOR-] (2) ($RES_BND_147)
(5)       [----] for $i1 in 1:2 loop
(5)       [----]   [SCAL] (1) pipe.flowModel.mus[$i1] = 0.001 ($RES_BND_148)
(5)       [----] end for;
(6)       [SCAL] (1) pipe.flowModel.mus_act[1] = noEvent(if $SEV_2 then pipe.flowModel.mus[1] else pipe.flowModel.mus[2]) ($RES_SIM_17)
(7)       [ARRY] (1) pipe.flowModel.m_flows = {homotopy(({$FUN_5} .* pipe.flowModel.nParallel)[1], (pipe.flowModel.m_flow_nominal / pipe.flowModel.dp_nominal * (pipe.flowModel.dps_fg - (pipe.flowModel.g * pipe.flowModel.dheights) .* pipe.flowModel.rho_nominal))[1])} ($RES_SIM_18)
(8)       [ARRY] (1) pipe.flowModel.pathLengths_internal = pipe.flowModel.pathLengths ($RES_BND_149)
(9)       [SCAL] (1) $DER.tank1.m = tank1.mb_flow ($RES_SIM_19)
(10)      [SCAL] (1) tank1.medium.state.p = tank1.p_ambient ($RES_SIM_55)
(11)      [SCAL] (1) tank1.medium.state.T = -((-273.15) - tank1.medium.T_degC) ($RES_SIM_56)
(12)      [SCAL] (1) flowSource.ports[1].p = 99999.99999999999 * flowSource.medium.p_bar ($RES_SIM_92)
(13)      [SCAL] (1) flowSource.ports[1].h_outflow = 4184.0 * ((-273.15) + flowSource.T) ($RES_SIM_93)
(14)      [SCAL] (1) $SEV_27 = 995.586 * valveDiscrete.V_flow > valveDiscrete.m_flow_small ($RES_EVT_210)
(15)      [SCAL] (1) $SEV_28 = 995.586 * valveDiscrete.V_flow < (-valveDiscrete.m_flow_small) ($RES_EVT_211)
(16)      [SCAL] (1) $TEV_0 = $PRE.tank1.aboveLevel[$i1] ($RES_EVT_174)
(17)      [FOR-] (2) ($RES_EVT_175)
(17)      [----] for $i1 in 1:2 loop
(17)      [----]   [SCAL] (1) $SEV_0[$i1] = tank1.level_start >= tank1.portsData_height2[$i1] ($RES_EVT_176)
(17)      [----] end for;
(18)      [SCAL] (1) $SEV_2 = pipe.flowModel.m_flows[1] > 0.0 ($RES_EVT_178)
(19)      [FOR-] (2) ($RES_EVT_179)
(19)      [----] for $i1 in 1:2 loop
(19)      [----]   [SCAL] (1) $SEV_3[$i1] = tank1.level >= (tank1.portsData_height2[$i1] + tank1.ports_emptyPipeHysteresis[$i1]) ($RES_EVT_180)
(19)      [----] end for;
(20)      [SCAL] (1) $DER.tank1.U = tank1.Qb_flow + tank1.Hb_flow ($RES_SIM_20)
(21)      [SCAL] (1) pipe.flowModel.Res_turbulent_internal[1] = pipe.flowModel.Re_turbulent ($RES_BND_150)
(22)      [SCAL] (1) tank1.U = tank1.m * (4184.0 * ((-273.15) - ((-273.15) - tank1.medium.T_degC))) ($RES_SIM_21)
(23)      [ARRY] (1) pipe.flowModel.diameters = 0.5 * (pipe.flowModel.dimensions[2:2] + pipe.flowModel.dimensions[1:1]) ($RES_BND_151)
(24)      [SCAL] (1) tank1.m = 995.586 * tank1.fluidVolume ($RES_SIM_22)
(25)      [FOR-] (2) ($RES_SIM_23)
(25)      [----] for $i1 in 1:2 loop
(25)      [----]   [SCAL] (1) tank1.aboveLevel[$i1] = $SEV_6[$i1] ($RES_SIM_24)
(25)      [----] end for;
(26)      [SCAL] (1) flowSource.medium.state.p = 99999.99999999999 * flowSource.medium.p_bar ($RES_SIM_105)
(27)      [ARRY] (2) tank1.heatTransfer.states = {tank1.medium.state} ($RES_BND_153)
(28)      [ARRY] (4) pipe.flowModel.states = {Modelica.Fluid.Examples.AST_BatchPlant.Test.TankWithEmptyingPipe1.pipe.Medium.ThermodynamicState(pipe.port_a.p, 273.15 + 2.390057361376673e-4 * tank1.ports[2].h_outflow), Modelica.Fluid.Examples.AST_BatchPlant.Test.TankWithEmptyingPipe1.pipe.Medium.ThermodynamicState(pipe.port_b.p, 273.15 + 2.390057361376673e-4 * flowSource.ports[1].h_outflow)} ($RES_BND_154)
(29)      [FOR-] (2) ($RES_SIM_25)
(29)      [----] for $i1 in 1:2 loop
(29)      [----]   [SCAL] (1) tank1.levelAbovePort[$i1] = if tank1.aboveLevel[$i1] then tank1.level - tank1.portsData_height2[$i1] else 0.0 ($RES_SIM_26)
(29)      [----] end for;
(30)      [FOR-] (2) ($RES_SIM_27)
(30)      [----] for $i1 in 1:2 loop
(30)      [----]   [SCAL] (1) tank1.ports[$i1].h_outflow = 4184.0 * ((-273.15) - ((-273.15) - tank1.medium.T_degC)) ($RES_SIM_28)
(30)      [----] end for;
(31)      [FOR-] (2) ($RES_SIM_29)
(31)      [----] for $i1 in 1:2 loop
(31)      [----]   [SCAL] (1) tank1.zetas_out[$i1] = 1.0 + (if tank1.aboveLevel[$i1] then 0.0 else tank1.zetaLarge) ($RES_SIM_30)
(31)      [----] end for;
(32)      [SCAL] (1) valveDiscrete.dp = valveDiscrete.port_a.p - valveDiscrete.port_b.p ($RES_SIM_66)
(33)      [SCAL] (1) valveDiscrete.port_b.h_outflow = ambient_fixed.ports[1].h_outflow ($RES_SIM_69)
(34)      [FOR-] (2) ($RES_EVT_181)
(34)      [----] for $i1 in 1:2 loop
(34)      [----]   [SCAL] (1) $SEV_4[$i1] = tank1.level >= (tank1.portsData_height2[$i1] - tank1.ports_emptyPipeHysteresis[$i1]) ($RES_EVT_182)
(34)      [----] end for;
(35)      [FOR-] (2) ($RES_EVT_183)
(35)      [----] for $i1 in 1:2 loop
(35)      [----]   [SCAL] (1) $SEV_5[$i1] = $TEV_0 and $SEV_4[$i1] ($RES_EVT_184)
(35)      [----] end for;
(36)      [FOR-] (2) ($RES_EVT_185)
(36)      [----] for $i1 in 1:2 loop
(36)      [----]   [SCAL] (1) $SEV_6[$i1] = $SEV_3[$i1] or $SEV_5[$i1] ($RES_EVT_186)
(36)      [----] end for;
(37)      [FOR-] (2) ($RES_EVT_187)
(37)      [----] for $i1 in 1:2 loop
(37)      [----]   [SCAL] (1) $SEV_7[$i1] = tank1.ports[$i1].m_flow >= tank1.m_flow_small ($RES_EVT_188)
(37)      [----] end for;
(38)      [FOR-] (2) ($RES_EVT_189)
(38)      [----] for $i1 in 1:2 loop
(38)      [----]   [SCAL] (1) $SEV_8[$i1] = tank1.ports[$i1].m_flow <= (-tank1.m_flow_small) ($RES_EVT_190)
(38)      [----] end for;
(39)      [SCAL] (1) tank1.ports[2].m_flow - pipe.port_b.m_flow = 0.0 ($RES_SIM_113)
(40)      [FOR-] (2) ($RES_SIM_31)
(40)      [----] for $i1 in 1:2 loop
(40)      [----]   [SCAL] (1) tank1.ports[$i1].p = system.g * tank1.levelAbovePort[$i1] * 995.586 + tank1.p_ambient + smooth(2, if $SEV_7[$i1] then (0.008105694691387022 * tank1.ports[$i1].m_flow ^ 2.0) / (995.586 * tank1.portsData_diameter2[$i1] * tank1.portsData_diameter2[$i1] * tank1.portsData_diameter2[$i1] * tank1.portsData_diameter2[$i1]) else if $SEV_8[$i1] then -(0.8105694691387022 * tank1.zetas_out[$i1] * tank1.ports[$i1].m_flow ^ 2.0) / (995.586 * tank1.portsData_diameter2[$i1] * tank1.portsData_diameter2[$i1] * tank1.portsData_diameter2[$i1] * tank1.portsData_diameter2[$i1]) else if $SEV_9[$i1] then Modelica.Fluid.Utilities.regSquare2.regSquare2_utility(tank1.ports[$i1].m_flow, tank1.m_flow_small, 0.008105694691387022 / (995.586 * tank1.portsData_diameter2[$i1] * tank1.portsData_diameter2[$i1] * tank1.portsData_diameter2[$i1] * tank1.portsData_diameter2[$i1]), (0.8105694691387022 * tank1.zetas_out[$i1]) / (995.586 * tank1.portsData_diameter2[$i1] * tank1.portsData_diameter2[$i1] * tank1.portsData_diameter2[$i1] * tank1.portsData_diameter2[$i1]), false, 1.0) else -Modelica.Fluid.Utilities.regSquare2.regSquare2_utility(-tank1.ports[$i1].m_flow, tank1.m_flow_small, (0.8105694691387022 * tank1.zetas_out[$i1]) / (995.586 * tank1.portsData_diameter2[$i1] * tank1.portsData_diameter2[$i1] * tank1.portsData_diameter2[$i1] * tank1.portsData_diameter2[$i1]), 0.008105694691387022 / (995.586 * tank1.portsData_diameter2[$i1] * tank1.portsData_diameter2[$i1] * tank1.portsData_diameter2[$i1] * tank1.portsData_diameter2[$i1]), false, 1.0)) ($RES_SIM_32)
(40)      [----] end for;
(41)      [SCAL] (1) tank1.heatTransfer.heatPorts[1].Q_flow = 0.0 ($RES_SIM_114)
(42)      [SCAL] (1) -flowSource.m_flow = sum(flowSource.ports.m_flow) ($RES_$AUX_162)
(43)      [SCAL] (1) tank1.ports[1].m_flow - 995.586 * valveDiscrete.V_flow = 0.0 ($RES_SIM_115)
(44)      [SCAL] (1) pipe.port_a.p = tank1.ports[2].p ($RES_SIM_116)
(45)      [SCAL] (1) $FUN_3 = sum(tank1.ports.m_flow) ($RES_$AUX_160)
(46)      [SCAL] (1) valveDiscrete.port_b.p = tank1.ports[1].p ($RES_SIM_117)
(47)      [SCAL] (1) valveDiscrete.port_a.h_outflow = tank1.ports[1].h_outflow ($RES_SIM_70)
(48)      [SCAL] (1) tank1.port_b_H_flow_bottom[2] = smooth(0, tank1.ports[2].m_flow * (if $SEV_10 then pipe.port_a.h_outflow else tank1.ports[2].h_outflow)) ($RES_SIM_35)
(49)      [SCAL] (1) pipe.port_b.m_flow + flowSource.ports[1].m_flow = 0.0 ($RES_SIM_118)
(50)      [SCAL] (1) 995.586 * valveDiscrete.V_flow = if open.k then valveDiscrete.k * valveDiscrete.dp else valveDiscrete.k * valveDiscrete.opening_min * valveDiscrete.dp ($RES_SIM_71)
(51)      [SCAL] (1) tank1.port_b_H_flow_bottom[1] = smooth(0, tank1.ports[1].m_flow * (if $SEV_11 then valveDiscrete.port_b.h_outflow else tank1.ports[1].h_outflow)) ($RES_SIM_36)
(52)      [SCAL] (1) flowSource.ports[1].p = pipe.port_b.p ($RES_SIM_119)
(53)      [SCAL] (1) ambient_fixed.ports[1].p = ambient_fixed.p ($RES_SIM_72)
(54)      [SCAL] (1) ambient_fixed.ports[1].h_outflow = 4184.0 * ((-273.15) + ambient_fixed.T) ($RES_SIM_73)
(55)      [SCAL] (1) tank1.Qb_flow = tank1.heatTransfer.Q_flows[1] ($RES_SIM_38)
(56)      [SCAL] (1) tank1.Hb_flow = $FUN_4 ($RES_SIM_39)
(57)      [FOR-] (2) ($RES_EVT_191)
(57)      [----] for $i1 in 1:2 loop
(57)      [----]   [SCAL] (1) $SEV_9[$i1] = 0.008105694691387022 / (995.586 * tank1.portsData_diameter2[$i1] * tank1.portsData_diameter2[$i1] * tank1.portsData_diameter2[$i1] * tank1.portsData_diameter2[$i1]) >= (0.8105694691387022 * tank1.zetas_out[$i1]) / (995.586 * tank1.portsData_diameter2[$i1] * tank1.portsData_diameter2[$i1] * tank1.portsData_diameter2[$i1] * tank1.portsData_diameter2[$i1]) ($RES_EVT_192)
(57)      [----] end for;
(58)      [SCAL] (1) $SEV_10 = tank1.ports[2].m_flow > 0.0 ($RES_EVT_193)
(59)      [SCAL] (1) $SEV_11 = tank1.ports[1].m_flow > 0.0 ($RES_EVT_194)
(60)      [SCAL] (1) $SEV_12 = tank1.m >= 0.0 ($RES_EVT_195)
(61)      [SCAL] (1) $SEV_13 = tank1.level <= tank1.height ($RES_EVT_196)
(62)      [SCAL] (1) valveDiscrete.port_a_T = smooth(1, if $SEV_27 then valveDiscrete.state_a.T else if $SEV_28 then 273.15 + 2.390057361376673e-4 * valveDiscrete.port_a.h_outflow else if $SEV_26 then 0.25 * ((273.15 + 2.390057361376673e-4 * valveDiscrete.port_a.h_outflow) - valveDiscrete.state_a.T) * ((-3.0) + (995.586 * valveDiscrete.V_flow / valveDiscrete.m_flow_small) ^ 2.0) * ((995.586 * valveDiscrete.V_flow) / valveDiscrete.m_flow_small) + 0.5 * (273.15 + valveDiscrete.state_a.T + 2.390057361376673e-4 * valveDiscrete.port_a.h_outflow) else 0.5 * (273.15 + valveDiscrete.state_a.T + 2.390057361376673e-4 * valveDiscrete.port_a.h_outflow)) ($RES_BND_130)
(63)      [SCAL] (1) $FUN_4 = sum(tank1.port_b_H_flow_bottom) ($RES_$AUX_159)
(64)      [SCAL] (1) valveDiscrete.port_b_T = smooth(1, if $SEV_24 then valveDiscrete.state_b.T else if $SEV_25 then 273.15 + 2.390057361376673e-4 * valveDiscrete.port_b.h_outflow else if $SEV_26 then 0.5 * (273.15 + valveDiscrete.state_b.T + 2.390057361376673e-4 * valveDiscrete.port_b.h_outflow) - 0.25 * ((273.15 + 2.390057361376673e-4 * valveDiscrete.port_b.h_outflow) - valveDiscrete.state_b.T) * ((-3.0) + (995.586 * valveDiscrete.V_flow / (-valveDiscrete.m_flow_small)) ^ 2.0) * ((995.586 * valveDiscrete.V_flow) / valveDiscrete.m_flow_small) else 0.5 * (273.15 + valveDiscrete.state_b.T + 2.390057361376673e-4 * valveDiscrete.port_b.h_outflow)) ($RES_BND_131)
(65)      [SCAL] (1) $FUN_5 = Modelica.Fluid.Examples.AST_BatchPlant.Test.TankWithEmptyingPipe1.pipe.flowModel.WallFriction.massFlowRate_dp_staticHead(pipe.flowModel.dps_fg[1], pipe.flowModel.rhos[1], pipe.flowModel.rhos[2], pipe.flowModel.mus[1], pipe.flowModel.mus[2], pipe.flowModel.pathLengths_internal[1], pipe.flowModel.diameters[1], (pipe.flowModel.g * pipe.flowModel.dheights)[1], (0.5 .* (pipe.flowModel.crossAreas[1:1] + pipe.flowModel.crossAreas[2:2]))[1], (0.5 .* (pipe.flowModel.roughnesses[1:1] + pipe.flowModel.roughnesses[2:2]))[1], pipe.flowModel.dp_small, pipe.flowModel.Res_turbulent_internal[1]) ($RES_$AUX_158)
(66)      [SCAL] (1) $FUN_6 = Modelica.Fluid.Examples.AST_BatchPlant.Test.TankWithEmptyingPipe1.pipe.flowModel.WallFriction.pressureLoss_m_flow(pipe.flowModel.m_flow_nominal / pipe.flowModel.nParallel, pipe.flowModel.rho_nominal, pipe.flowModel.rho_nominal, pipe.flowModel.mu_nominal, pipe.flowModel.mu_nominal, pipe.flowModel.pathLengths_internal[1], pipe.flowModel.diameters[1], (0.5 .* (pipe.flowModel.crossAreas[2:2] + pipe.flowModel.crossAreas[1:1]))[1], (0.5 .* (pipe.flowModel.roughnesses[2:2] + pipe.flowModel.roughnesses[1:1]))[1], pipe.flowModel.m_flow_small / pipe.flowModel.nParallel, pipe.flowModel.Res_turbulent_internal[1]) ($RES_$AUX_157)
(67)      [SCAL] (1) pipe.flowModel.dp_fric_nominal = sum({$FUN_6}) ($RES_$AUX_156)
(68)      [SCAL] (1) 995.586 * valveDiscrete.V_flow + ambient_fixed.ports[1].m_flow = 0.0 ($RES_SIM_121)
(69)      [SCAL] (1) $FUN_8 = sqrt(3.141592653589793 * tank1.crossArea) ($RES_$AUX_155)
(70)      [SCAL] (1) tank1.mb_flow = $FUN_3 ($RES_SIM_40)
(71)      [SCAL] (1) ambient_fixed.ports[1].p = valveDiscrete.port_a.p ($RES_SIM_122)
(72)      [ARRY] (1) tank1.heatTransfer.surfaceAreas = {2.0 * $FUN_8 * tank1.level + tank1.crossArea} ($RES_BND_135)
(73)      [SCAL] (1) tank1.fluidVolume = tank1.crossArea * tank1.level + tank1.V0 ($RES_SIM_41)
(74)      [ARRY] (2) tank1.portsData_height = tank1.portsData_height2 ($RES_SIM_123)
(75)      [ARRY] (1) tank1.heatTransfer.Ts = {tank1.heatTransfer.states.p} ($RES_BND_136)
(76)      [ARRY] (2) tank1.portsData_diameter = tank1.portsData_diameter2 ($RES_SIM_124)
(77)      [ARRY] (2) tank1.portsData_diameter = tank1.portsData.diameter ($RES_BND_137)
(78)      [FOR-] (2) ($RES_SIM_43)
(78)      [----] for $i1 in 1:2 loop
(78)      [----]   [SCAL] (1) tank1.bottomArea[$i1] = 3.141592653589793 * (tank1.portsData_diameter2[$i1] / 2.0) ^ 2.0 ($RES_SIM_44)
(78)      [----] end for;
(79)      [ARRY] (2) tank1.portsData_height = tank1.portsData.height ($RES_BND_138)
(80)      [ARRY] (2) pipe.flowModel.vs = {-(0.0010044335697769957 * pipe.port_b.m_flow) / pipe.flowModel.crossAreas[1], -(0.0010044335697769957 * pipe.port_b.m_flow) / pipe.flowModel.crossAreas[2]} / pipe.nParallel ($RES_BND_139)
(81)      [FOR-] (2) ($RES_SIM_45)
(81)      [----] for $i1 in 1:2 loop
(81)      [----]   [SCAL] (1) tank1.ports_emptyPipeHysteresis[$i1] = tank1.portsData_diameter2[$i1] * tank1.hysteresisFactor ($RES_SIM_46)
(81)      [----] end for;
(82)      [SCAL] (1) valveDiscrete.state_a.p = valveDiscrete.port_a.p ($RES_SIM_163)
(83)      [SCAL] (1) valveDiscrete.state_a.T = 273.15 + 2.390057361376673e-4 * ambient_fixed.ports[1].h_outflow ($RES_SIM_164)
(84)      [SCAL] (1) valveDiscrete.state_b.p = valveDiscrete.port_b.p ($RES_SIM_165)
(85)      [ARRY] (1) tank1.heatTransfer.Q_flows = tank1.heatTransfer.heatPorts.Q_flow ($RES_SIM_49)
(86)      [SCAL] (1) valveDiscrete.state_b.T = 273.15 + 2.390057361376673e-4 * tank1.ports[1].h_outflow ($RES_SIM_166)
(87)      [SCAL] (1) $SEV_20 = abs(sum({abs(flowSource.ports[1].m_flow)}) - abs(flowSource.ports[1].m_flow)) <= 1e-60 ($RES_EVT_203)
(88)      [SCAL] (1) pipe.port_b.h_outflow = tank1.ports[2].h_outflow - system.g * pipe.height_ab ($RES_SIM_8)
(89)      [SCAL] (1) pipe.port_a.h_outflow = flowSource.ports[1].h_outflow + system.g * pipe.height_ab ($RES_SIM_7)
(90)      [SCAL] (1) $SEV_24 = (-995.586 * valveDiscrete.V_flow) > valveDiscrete.m_flow_small ($RES_EVT_207)
(91)      [SCAL] (1) $SEV_25 = (-995.586 * valveDiscrete.V_flow) < (-valveDiscrete.m_flow_small) ($RES_EVT_208)
(92)      [SCAL] (1) $SEV_26 = valveDiscrete.m_flow_small > 0.0 ($RES_EVT_209)
(93)      [ARRY] (2) pipe.flowModel.crossAreas = {pipe.crossArea, pipe.crossArea} ($RES_BND_140)
(94)      [SCAL] (1) -pipe.port_b.m_flow = pipe.flowModel.m_flows[1] ($RES_SIM_10)
(95)      [ARRY] (2) pipe.flowModel.dimensions = {(4.0 * pipe.crossArea) / pipe.perimeter, (4.0 * pipe.crossArea) / pipe.perimeter} ($RES_BND_141)
(96)      [ARRY] (1) {0.0} = pipe.flowModel.Ib_flows - (pipe.flowModel.Fs_fg + pipe.flowModel.Fs_p) ($RES_SIM_11)
(97)      [ARRY] (2) pipe.flowModel.roughnesses = {pipe.roughness, pipe.roughness} ($RES_BND_142)
(98)      [ARRY] (1) pipe.flowModel.Is = {pipe.flowModel.m_flows[1] * pipe.flowModel.pathLengths[1]} ($RES_SIM_12)
(99)      [ARRY] (1) pipe.flowModel.dheights = {pipe.height_ab} ($RES_BND_143)
(100)     [ARRY] (1) pipe.flowModel.dps_fg = {(2.0 * (pipe.flowModel.Fs_fg[1] / pipe.flowModel.nParallel)) / (pipe.flowModel.crossAreas[1] + pipe.flowModel.crossAreas[2])} ($RES_SIM_13)
(101)     [ARRY] (1) pipe.flowModel.pathLengths = {pipe.length} ($RES_BND_144)
(102)     [ARRY] (1) pipe.flowModel.Fs_p = pipe.flowModel.nParallel * {0.5 * (pipe.flowModel.crossAreas[1] + pipe.flowModel.crossAreas[2]) * (pipe.flowModel.states.T - pipe.flowModel.states.T)} ($RES_SIM_14)