Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ModelicaTest_3.2.2_ModelicaTest.Fluid.TestPipesAndValves.DynamicPipeClosingValve.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.TestPipesAndValves.DynamicPipeClosingValve,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ModelicaTest_3.2.2_ModelicaTest.Fluid.TestPipesAndValves.DynamicPipeClosingValve")
translateModel(ModelicaTest.Fluid.TestPipesAndValves.DynamicPipeClosingValve,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ModelicaTest_3.2.2_ModelicaTest.Fluid.TestPipesAndValves.DynamicPipeClosingValve")
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo): time 0.001192/0.001192, allocations: 107.9 kB / 16.42 MB, free: 6.504 MB / 14.72 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo): time 0.001227/0.001227, allocations: 187.8 kB / 17.35 MB, free: 5.754 MB / 14.72 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.2.3+maint.om/package.mo): time 1.297/1.297, allocations: 205.1 MB / 223.2 MB, free: 12.25 MB / 190.1 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaTest 3.2.2+maint.om/package.mo): time 0.1694/0.1694, allocations: 39.96 MB / 310.5 MB, free: 4.027 MB / 254.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 1.566e-05/1.567e-05, allocations: 6.219 kB / 436.4 MB, free: 11.8 MB / 318.1 MB
Notification: Performance of NFInst.instantiate(ModelicaTest.Fluid.TestPipesAndValves.DynamicPipeClosingValve): time 0.03717/0.03719, allocations: 47.41 MB / 483.8 MB, free: 12.21 MB / 366.1 MB
Notification: Performance of NFInst.instExpressions: time 0.02855/0.06578, allocations: 25.91 MB / 0.4978 GB, free: 2.227 MB / 382.1 MB
Notification: Performance of NFInst.updateImplicitVariability: time 0.0008856/0.0667, allocations: 35.81 kB / 0.4978 GB, free: 2.191 MB / 382.1 MB
Notification: Performance of NFTyping.typeComponents: time 0.001099/0.0678, allocations: 0.497 MB / 0.4983 GB, free: 1.691 MB / 382.1 MB
Notification: Performance of NFTyping.typeBindings: time 0.01378/0.08159, allocations: 6.043 MB / 0.5042 GB, free: 11.64 MB / 398.1 MB
Notification: Performance of NFTyping.typeClassSections: time 0.008311/0.08992, allocations: 3.91 MB / 0.508 GB, free: 7.723 MB / 398.1 MB
Notification: Performance of NFFlatten.flatten: time 0.003139/0.09307, allocations: 3.177 MB / 0.5111 GB, free: 4.535 MB / 398.1 MB
Notification: Performance of NFFlatten.resolveConnections: time 0.0006814/0.09376, allocations: 0.6298 MB / 0.5117 GB, free: 3.891 MB / 398.1 MB
Notification: Performance of NFEvalConstants.evaluate: time 0.2208/0.3146, allocations: 6.057 MB / 0.5176 GB, free: 13.56 MB / 398.1 MB
Notification: Performance of NFSimplifyModel.simplify: time 0.01654/0.3312, allocations: 8.867 MB / 0.5263 GB, free: 11.21 MB / 398.1 MB
Notification: Performance of NFPackage.collectConstants: time 0.0002905/0.3315, allocations: 83.66 kB / 0.5264 GB, free: 11.21 MB / 398.1 MB
Notification: Performance of NFFlatten.collectFunctions: time 0.01428/0.3458, allocations: 8.034 MB / 0.5342 GB, free: 11.19 MB / 398.1 MB
Notification: Performance of combineBinaries: time 0.002412/0.3482, allocations: 2.056 MB / 0.5362 GB, free: 10.68 MB / 398.1 MB
Notification: Performance of replaceArrayConstructors: time 0.0008365/0.3491, allocations: 1.344 MB / 0.5375 GB, free: 9.988 MB / 398.1 MB
Notification: Performance of NFVerifyModel.verify: time 0.0003138/0.3494, allocations: 181.8 kB / 0.5377 GB, free: 9.953 MB / 398.1 MB
Notification: Performance of FrontEnd: time 0.0002624/0.3497, allocations: 22.56 kB / 0.5377 GB, free: 9.953 MB / 398.1 MB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 196 (142)
 * Number of variables: 216 (174)
Notification: Performance of Bindings: time 0.005208/0.3549, allocations: 5.888 MB / 0.5435 GB, free: 7.73 MB / 398.1 MB
Notification: Performance of FunctionAlias: time 0.000553/0.3554, allocations: 486 kB / 0.544 GB, free: 7.641 MB / 398.1 MB
Notification: Performance of Early Inline: time 0.002808/0.3583, allocations: 3.307 MB / 0.5472 GB, free: 7.422 MB / 398.1 MB
Notification: Performance of simplify1: time 0.000213/0.3585, allocations: 225.1 kB / 0.5474 GB, free: 7.418 MB / 398.1 MB
Notification: Performance of Alias: time 0.001921/0.3604, allocations: 2.313 MB / 0.5497 GB, free: 6.805 MB / 398.1 MB
Notification: Performance of simplify2: time 0.0001744/0.3606, allocations: 227.7 kB / 0.5499 GB, free: 6.801 MB / 398.1 MB
Notification: Performance of Events: time 0.0005567/0.3612, allocations: 0.6217 MB / 0.5505 GB, free: 6.656 MB / 398.1 MB
Notification: Performance of Detect States: time 0.0005857/0.3618, allocations: 0.8318 MB / 0.5513 GB, free: 6.543 MB / 398.1 MB
Notification: Performance of Partitioning: time 0.0009355/0.3627, allocations: 1.293 MB / 0.5526 GB, free: 6.129 MB / 398.1 MB
Error: Internal error NBAdjacency.Matrix.create failed to create adjacency matrix for system:
System Variables (164/206)
****************************
(1)       [ALGB] (1) protected Real sink.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(2)       [ALGB] (1) Real[1] source.ports.p (start = {5e6 for $i1 in 1:1}, min = {611.657 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(3)       [ALGB] (1) Real[1] pipe.heatTransfer.Ts = {ModelicaTest.Fluid.TestPipesAndValves.DynamicPipeClosingValve.pipe.heatTransfer.Medium.temperature(pipe.heatTransfer.states[1])} (start = {288.15 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, nominal = {300.0 for $i1 in 1:1})
(4)       [ALGB] (2) Real[2] pipe.flowModel.rhos = {ModelicaTest.Fluid.TestPipesAndValves.DynamicPipeClosingValve.pipe.flowModel.Medium.density(pipe.flowModel.states[$i1]) for $i1 in 1:2} (start = {150.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2})
(5)       [ALGB] (2) protected Real[2] pipe.vsFM
(6)       [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 $i1 in 1:1})
(7)       [ALGB] (1) protected Real sink.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(8)       [ALGB] (2) Real[2] pipe.flowModel.mus = {ModelicaTest.Fluid.TestPipesAndValves.DynamicPipeClosingValve.pipe.flowModel.Medium.dynamicViscosity(pipe.flowModel.states[$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})
(9)       [DISC] (1) Boolean $SEV_20
(10)      [ALGB] (1) protected Real valve.minLimiter.y
(11)      [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)
(12)      [ALGB] (1) Real valve.port_b_T = Modelica.Fluid.Utilities.regStep(valve.port_b.m_flow, ModelicaTest.Fluid.TestPipesAndValves.DynamicPipeClosingValve.valve.Medium.temperature(valve.state_b), ModelicaTest.Fluid.TestPipesAndValves.DynamicPipeClosingValve.valve.Medium.temperature(ModelicaTest.Fluid.TestPipesAndValves.DynamicPipeClosingValve.valve.Medium.setState_phX(valve.port_b.p, valve.port_b.h_outflow, {}, 0, 0)), valve.m_flow_small) (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(13)      [ALGB] (1) protected Real source.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(14)      [DISC] (1) Boolean $TEV_1
(15)      [DISC] (1) Boolean $TEV_0
(16)      [ALGB] (1) Real[1] pipe.Wb_flows
(17)      [ALGB] (1) protected Real source.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(18)      [ALGB] (1) Real source.medium.sat.Tsat (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(19)      [DISC] (1) protected Integer valve.state_a.phase (min = 0, max = 2)
(20)      [ALGB] (1) Real[1] pipe.flowModel.Fs_p
(21)      [ALGB] (2) final Real[2] pipe.flowModel.dimensions = pipe.dimensionsFM
(22)      [ALGB] (1) final input Real[1, 1] pipe.heatTransfer.states.T = {pipe.mediums[1].state.T} (start = {500.0 for $i1 in 1:1}, min = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(23)      [DISC] (4) Integer[2, 2] pipe.statesFM.phase (min = {0 for $i1 in 1:2}, max = {2 for $i1 in 1:2})
(24)      [ALGB] (1) Real sink.medium.sat.psat (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(25)      [ALGB] (1) Real pipe.state_b.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(26)      [DISC] (1) Boolean $SEV_19
(27)      [DISC] (1) Boolean $SEV_18
(28)      [DISC] (1) Boolean $SEV_17
(29)      [DISC] (1) Boolean $SEV_16
(30)      [ALGB] (1) Real[1] pipe.mediums.T_degC = {Modelica.SIunits.Conversions.to_degC(pipe.mediums[1].T)}
(31)      [DISC] (1) Boolean $SEV_15
(32)      [ALGB] (1) Real pipe.state_b.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(33)      [ALGB] (1) stream Real[1] sink.ports.h_outflow (start = {1e5 for $i1 in 1:1}, min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {5e5 for $i1 in 1:1})
(34)      [DISC] (1) Boolean $SEV_12
(35)      [ALGB] (1) Real pipe.state_b.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0)
(36)      [ALGB] (1) final input Real[1, 1] pipe.heatTransfer.states.d = {pipe.mediums[1].state.d} (start = {150.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(37)      [ALGB] (1) final input Real[1, 1] pipe.heatTransfer.states.h = {pipe.mediums[1].state.h} (start = {1e5 for $i1 in 1:1}, min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {5e5 for $i1 in 1:1})
(38)      [ALGB] (1) stream Real pipe.port_a.h_outflow (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(39)      [DISC] (1) Integer[1] pipe.mediums.phase (fixed = {false for $i1 in 1:1}, start = {1 for $i1 in 1:1}, min = {0 for $i1 in 1:1}, max = {2 for $i1 in 1:1})
(40)      [ALGB] (1) final input Real[1, 1] pipe.heatTransfer.states.p = {pipe.mediums[1].state.p} (start = {5e6 for $i1 in 1:1}, min = {611.657 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(41)      [ALGB] (1) Real valve.V_flow = (-valve.port_b.m_flow) / Modelica.Fluid.Utilities.regStep(-valve.port_b.m_flow, ModelicaTest.Fluid.TestPipesAndValves.DynamicPipeClosingValve.valve.Medium.density(valve.state_a), ModelicaTest.Fluid.TestPipesAndValves.DynamicPipeClosingValve.valve.Medium.density(valve.state_b), valve.m_flow_small)
(42)      [ALGB] (1) Real[1] pipe.flowModel.Fs_fg
(43)      [ALGB] (1) stream Real valve.port_a.h_outflow (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(44)      [ALGB] (1) Real pipe.state_b.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(45)      [ALGB] (1) Real valve.port_b.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(46)      [ALGB] (1) flow Real valve.port_b.m_flow (min = -1e5, max = 1e60)
(47)      [DISC] (1) protected Integer valve.state_b.phase (min = 0, max = 2)
(48)      [ALGB] (1) Real valve.port_a_T = Modelica.Fluid.Utilities.regStep(-valve.port_b.m_flow, ModelicaTest.Fluid.TestPipesAndValves.DynamicPipeClosingValve.valve.Medium.temperature(valve.state_a), ModelicaTest.Fluid.TestPipesAndValves.DynamicPipeClosingValve.valve.Medium.temperature(ModelicaTest.Fluid.TestPipesAndValves.DynamicPipeClosingValve.valve.Medium.setState_phX(pipe.port_b.p, valve.port_a.h_outflow, {}, 0, 0)), valve.m_flow_small) (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(49)      [ALGB] (1) stream Real valve.port_b.h_outflow (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(50)      [DISC] (1) Integer source.medium.state.phase (min = 0, max = 2)
(51)      [ALGB] (1) Real[1] pipe.flowModel.Is
(52)      [ALGB] (1) Real[1] pipe.mb_flows (min = {-1e5 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1})
(53)      [ALGB] (1) Real $FUN_5
(54)      [ALGB] (1) Real sink.medium.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(55)      [ALGB] (1) Real $FUN_4
(56)      [ALGB] (1) Real $FUN_3
(57)      [ALGB] (1) Real $FUN_2
(58)      [ALGB] (1) protected Real valve.relativeFlowCoefficient
(59)      [ALGB] (1) Real $FUN_1
(60)      [DISC] (1) Integer[1] pipe.mediums.state.phase (min = {0 for $i1 in 1:1}, max = {2 for $i1 in 1:1})
(61)      [DER-] (1) Real[1] $DER.pipe.Us
(62)      [ALGB] (1) Real[1] pipe.vs = {(0.5 * (pipe.m_flows[2] + pipe.m_flows[1])) / (pipe.crossAreas[1] * pipe.mediums[1].d)} / pipe.nParallel
(63)      [ALGB] (1) Real pipe.state_a.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(64)      [ALGB] (1) final Real[1] pipe.heatTransfer.vs = pipe.vs
(65)      [ALGB] (1) Real sink.medium.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(66)      [ALGB] (1) Real pipe.port_a.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(67)      [ALGB] (1) Real[1] pipe.flowModel.rhos_act (start = {150.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(68)      [ALGB] (1) Real source.medium.p_bar = Modelica.SIunits.Conversions.to_bar(99999.99999999999 * source.medium.p_bar)
(69)      [ALGB] (1) Real sink.medium.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0)
(70)      [ALGB] (1) Real pipe.state_a.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(71)      [ALGB] (1) protected Real pipe.flowModel.dp_fric_nominal = sum({ModelicaTest.Fluid.TestPipesAndValves.DynamicPipeClosingValve.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)
(72)      [ALGB] (1) Real sink.medium.p_bar = Modelica.SIunits.Conversions.to_bar(99999.99999999999 * sink.medium.p_bar)
(73)      [ALGB] (1) Real pipe.state_a.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0)
(74)      [ALGB] (1) Real[1] pipe.mediums.u (min = {-1e8 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(75)      [ALGB] (1) stream Real[1] source.ports.h_outflow (start = {1e5 for $i1 in 1:1}, min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {5e5 for $i1 in 1:1})
(76)      [ALGB] (1) Real valve.dp_turbulent = max(valve.dp_small, ((ModelicaTest.Fluid.TestPipesAndValves.DynamicPipeClosingValve.valve.Medium.dynamicViscosity(valve.state_a) + ModelicaTest.Fluid.TestPipesAndValves.DynamicPipeClosingValve.valve.Medium.dynamicViscosity(valve.state_b)) ^ 2.0 * 3.141592653589793 * 1.6e7) / (8.0 * valve.Av * max(valve.relativeFlowCoefficient, 0.001) * (ModelicaTest.Fluid.TestPipesAndValves.DynamicPipeClosingValve.valve.Medium.density(valve.state_b) + ModelicaTest.Fluid.TestPipesAndValves.DynamicPipeClosingValve.valve.Medium.density(valve.state_a)))) (min = 0.0, nominal = 1e5)
(77)      [DER-] (1) Real[1] $DER.pipe.ms
(78)      [ALGB] (1) Real sink.medium.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(79)      [ALGB] (1) Real[1] pipe.flowModel.pathLengths_internal = pipe.flowModel.pathLengths
(80)      [ALGB] (2) protected Real[2] pipe.crossAreasFM
(81)      [ALGB] (1) final Real[1] pipe.flowModel.pathLengths = pipe.pathLengths
(82)      [ALGB] (2) protected Real[2] pipe.dimensionsFM
(83)      [ALGB] (1) Real pipe.state_a.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(84)      [ALGB] (1) Real[1] pipe.mediums.d (start = {150.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}, StateSelect = default)
(85)      [ALGB] (1) final Real[1] pipe.flowModel.dheights = pipe.dheightsFM
(86)      [ALGB] (1) Real[1] pipe.flowModel.dps_fg (start = {pipe.flowModel.p_a_start - pipe.flowModel.p_b_start for $i1 in 1:1})
(87)      [ALGB] (2) Real[2] pipe.H_flows (min = {-1e8 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1000.0 for $i1 in 1:2})
(88)      [ALGB] (1) Real[1] pipe.heatTransfer.Q_flows
(89)      [DISC] (1) Boolean $SEV_9
(90)      [DISC] (1) Boolean $SEV_8
(91)      [DISC] (1) Boolean $SEV_7
(92)      [DISC] (1) Boolean $SEV_6
(93)      [DISC] (1) Boolean $SEV_5
(94)      [DISC] (1) Boolean $SEV_4
(95)      [DISC] (4) final input Integer[2, 2] pipe.flowModel.states.phase = {pipe.statesFM[1].phase, pipe.statesFM[2].phase} (min = {0 for $i1 in 1:2}, max = {2 for $i1 in 1:2})
(96)      [ALGB] (1) Real[1] pipe.mediums.T (start = {pipe.T_start}, min = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}, StateSelect = default)
(97)      [ALGB] (2) final Real[2] pipe.flowModel.vs = pipe.vsFM
(98)      [DISC] (1) Boolean $SEV_3
(99)      [DISC] (1) Boolean $SEV_2
(100)     [ALGB] (1) protected Real[1] pipe.dheightsFM
(101)     [ALGB] (1) Real[1] pipe.mediums.sat.Tsat (start = {500.0 for $i1 in 1:1}, min = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(102)     [ALGB] (1) Real[1] pipe.Qb_flows
(103)     [ALGB] (1) Real[1] pipe.flowModel.Res_turbulent_internal = pipe.flowModel.Re_turbulent * {1.0 for $i1 in 1:1}
(104)     [ALGB] (1) Real[1] pipe.mediums.state.p (start = {5e6 for $i1 in 1:1}, min = {611.657 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(105)     [ALGB] (1) Real pipe.port_b.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(106)     [ALGB] (2) final Real[2] pipe.flowModel.roughnesses = pipe.roughnessesFM (min = {0.0 for $i1 in 1:2})
(107)     [ALGB] (1) protected Real valve.state_b.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(108)     [ALGB] (1) Real[1] pipe.mediums.state.h (start = {1e5 for $i1 in 1:1}, min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {5e5 for $i1 in 1:1})
(109)     [ALGB] (1) Real[1] pipe.mediums.state.d (start = {150.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(110)     [ALGB] (1) Real source.medium.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(111)     [ALGB] (1) protected Real valve.state_b.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(112)     [ALGB] (1) flow Real[1] pipe.heatTransfer.heatPorts.Q_flow
(113)     [ALGB] (1) protected Real valve.state_b.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0)
(114)     [ALGB] (2) Real[2] pipe.m_flows (start = {0.0 for $i1 in 1:2}, min = {-1e60 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2})
(115)     [ALGB] (1) protected Real[1] pipe.pathLengths
(116)     [ALGB] (1) Real source.medium.u (min = -1e8, max = 1e8, nominal = 1e6)
(117)     [ALGB] (1) Real[1] pipe.mediums.state.T (start = {500.0 for $i1 in 1:1}, min = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(118)     [ALGB] (1) Real source.medium.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0)
(119)     [ALGB] (1) Real[1] pipe.mediums.p_bar = {Modelica.SIunits.Conversions.to_bar(pipe.mediums[1].p)}
(120)     [ALGB] (1) Real[1] pipe.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})
(121)     [ALGB] (1) Real source.medium.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(122)     [ALGB] (1) final Real[1] pipe.fluidVolumes = {pipe.crossAreas[1]} .* pipe.nParallel
(123)     [ALGB] (1) protected Real valve.state_b.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(124)     [ALGB] (1) Real source.medium.h (StateSelect = default)
(125)     [ALGB] (1) Real sink.medium.T_degC = Modelica.SIunits.Conversions.to_degC(-((-273.15) - sink.medium.T_degC))
(126)     [ALGB] (4) Real[2, 2] pipe.statesFM.p (start = {5e6 for $i1 in 1:2}, min = {611.657 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2})
(127)     [ALGB] (1) Real source.medium.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(128)     [ALGB] (1) Real source.medium.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0, StateSelect = default)
(129)     [ALGB] (1) Real source.medium.sat.psat (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(130)     [ALGB] (1) Real[1] pipe.Hb_flows
(131)     [ALGB] (4) Real[2, 2] pipe.statesFM.h (start = {1e5 for $i1 in 1:2}, min = {-1e10 for $i1 in 1:2}, max = {1e10 for $i1 in 1:2}, nominal = {5e5 for $i1 in 1:2})
(132)     [ALGB] (1) flow Real[1] source.ports.m_flow (min = {-1e60}, max = {1e60})
(133)     [ALGB] (4) Real[2, 2] pipe.statesFM.d (start = {150.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2})
(134)     [ALGB] (4) final input Real[2, 2] pipe.flowModel.states.p = {pipe.statesFM[1].p, pipe.statesFM[2].p} (start = {5e6 for $i1 in 1:2}, min = {611.657 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2})
(135)     [ALGB] (1) Real sink.medium.sat.Tsat (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(136)     [ALGB] (1) flow Real pipe.port_a.m_flow (min = -1e60, max = 1e5)
(137)     [ALGB] (1) flow Real[1] sink.ports.m_flow (min = {-1e60}, max = {1e60})
(138)     [ALGB] (1) Real source.medium.T_degC = Modelica.SIunits.Conversions.to_degC(-((-273.15) - source.medium.T_degC))
(139)     [ALGB] (4) final input Real[2, 2] pipe.flowModel.states.h = {pipe.statesFM[1].h, pipe.statesFM[2].h} (start = {1e5 for $i1 in 1:2}, min = {-1e10 for $i1 in 1:2}, max = {1e10 for $i1 in 1:2}, nominal = {5e5 for $i1 in 1:2})
(140)     [DISC] (1) Integer sink.medium.state.phase (min = 0, max = 2)
(141)     [DER-] (1) Real[1] $DER.pipe.mediums.p
(142)     [ALGB] (4) final input Real[2, 2] pipe.flowModel.states.d = {pipe.statesFM[1].d, pipe.statesFM[2].d} (start = {150.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2})
(143)     [DISC] (1) Integer source.medium.phase (fixed = false, start = 1, min = 0, max = 2)
(144)     [ALGB] (4) Real[2, 2] pipe.statesFM.T (start = {500.0 for $i1 in 1:2}, min = {273.15 for $i1 in 1:2}, max = {2273.15 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2})
(145)     [ALGB] (1) protected Real valve.state_a.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(146)     [ALGB] (2) protected Real[2] pipe.roughnessesFM (min = {0.0 for $i1 in 1:2})
(147)     [ALGB] (1) Real[1] pipe.mediums.sat.psat (start = {5e6 for $i1 in 1:1}, min = {611.657 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(148)     [DER-] (1) Real[1] $DER.pipe.mediums.h
(149)     [ALGB] (2) final Real[2] pipe.flowModel.crossAreas = pipe.crossAreasFM
(150)     [ALGB] (1) Real sink.medium.u (min = -1e8, max = 1e8, nominal = 1e6)
(151)     [DISC] (1) Integer sink.medium.phase (fixed = false, start = 1, min = 0, max = 2)
(152)     [DISC] (1) Integer pipe.state_a.phase (min = 0, max = 2)
(153)     [ALGB] (1) protected Real valve.state_a.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(154)     [ALGB] (4) final input Real[2, 2] pipe.flowModel.states.T = {pipe.statesFM[1].T, pipe.statesFM[2].T} (start = {500.0 for $i1 in 1:2}, min = {273.15 for $i1 in 1:2}, max = {2273.15 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2})
(155)     [ALGB] (1) protected Real valve.state_a.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0)
(156)     [ALGB] (1) Real valve.dp (start = valve.dp_start)
(157)     [DISC] (1) final input Integer[1, 1] pipe.heatTransfer.states.phase = {pipe.mediums[1].state.phase} (min = {0 for $i1 in 1:1}, max = {2 for $i1 in 1:1})
(158)     [ALGB] (1) Real sink.medium.h (StateSelect = default)
(159)     [ALGB] (1) Real[1] sink.ports.p (start = {5e6 for $i1 in 1:1}, min = {611.657 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(160)     [ALGB] (1) protected Real[1] pipe.flowModel.diameters = 0.5 * (pipe.flowModel.dimensions[2:2] + pipe.flowModel.dimensions[1:1])
(161)     [ALGB] (1) Real sink.medium.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0, StateSelect = default)
(162)     [ALGB] (1) protected Real valve.state_a.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0)
(163)     [ALGB] (1) Real[1] pipe.flowModel.Ib_flows
(164)     [DISC] (1) Boolean[1] $SEV_10[$i1]


System Equations (156/186)
****************************
(1)       [ARRY] (1) pipe.mediums.phase = pipe.mediums.state.phase ($RES_SIM_81)
(2)       [SCAL] (1) valve.port_b.p = sink.ports[1].p ($RES_SIM_121)
(3)       [ARRY] (1) pipe.mediums.d = pipe.mediums.state.d ($RES_SIM_82)
(4)       [ARRY] (1) pipe.mediums.T = pipe.mediums.state.T ($RES_SIM_83)
(5)       [SCAL] (1) pipe.port_a.m_flow + source.ports[1].m_flow = 0.0 ($RES_SIM_123)
(6)       [ARRY] (1) pipe.mediums.p = pipe.mediums.state.p ($RES_SIM_84)
(7)       [SCAL] (1) source.ports[1].p = pipe.port_a.p ($RES_SIM_124)
(8)       [ARRY] (1) pipe.mediums.h = pipe.mediums.state.h ($RES_SIM_85)
(9)       [SCAL] (1) pipe.mediums[1].u = pipe.mediums[1].h - pipe.mediums[1].p / pipe.mediums[1].d ($RES_SIM_87)
(10)      [ARRY] (1) pipe.mediums.sat.psat = pipe.mediums.p ($RES_SIM_88)
(11)      [SCAL] (1) pipe.mediums[1].sat.Tsat = Modelica.Media.Water.IF97_Utilities.BaseIF97.Basic.tsat(pipe.mediums[1].p) ($RES_SIM_89)
(12)      [SCAL] (1) $SEV_5 = valve.dp <= (-valve.dp_turbulent) ($RES_EVT_210)
(13)      [SCAL] (1) $SEV_6 = valve.state_b.d > 0.0 ($RES_EVT_211)
(14)      [SCAL] (1) $SEV_7 = valve.state_a.d >= valve.state_b.d ($RES_EVT_212)
(15)      [SCAL] (1) $SEV_8 = valve.relativeFlowCoefficient < valve.minLimiter.uMin ($RES_EVT_213)
(16)      [SCAL] (1) $SEV_9 = pipe.flowModel.m_flows[1] > 0.0 ($RES_EVT_214)
(17)      [SCAL] (1) $SEV_10[1] = pipe.mediums[1].p >= 0.0 ($RES_EVT_215)
(18)      [SCAL] (1) $SEV_12 = (pipe.mediums[1].h < Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(pipe.mediums.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.boilingcurve_p(pipe.mediums.sat.psat)) or pipe.mediums[1].h > Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(pipe.mediums.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.dewcurve_p(pipe.mediums.sat.psat))) or pipe.mediums[1].p > 2.2064e7 ($RES_EVT_217)
(19)      [SCAL] (1) sink.medium.phase = sink.medium.state.phase ($RES_SIM_16)
(20)      [SCAL] (1) pipe.mediums[1].T = Modelica.Media.Water.IF97_Utilities.T_props_ph(pipe.mediums[1].p, pipe.mediums[1].h, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(pipe.mediums[1].p, pipe.mediums[1].h, pipe.mediums[1].phase, 0)) ($RES_SIM_90)
(21)      [SCAL] (1) sink.medium.d = sink.medium.state.d ($RES_SIM_17)
(22)      [SCAL] (1) pipe.mediums[1].d = Modelica.Media.Water.IF97_Utilities.rho_props_ph(pipe.mediums[1].p, pipe.mediums[1].h, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(pipe.mediums[1].p, pipe.mediums[1].h, pipe.mediums[1].phase, 0)) ($RES_SIM_91)
(23)      [SCAL] (1) -((-273.15) - sink.medium.T_degC) = sink.medium.state.T ($RES_SIM_18)
(24)      [SCAL] (1) pipe.mediums[1].phase = if $SEV_12 then 1 else 2 ($RES_SIM_92)
(25)      [SCAL] (1) 99999.99999999999 * sink.medium.p_bar = sink.medium.state.p ($RES_SIM_19)
(26)      [SCAL] (1) source.ports[1].p = 99999.99999999999 * source.medium.p_bar ($RES_SIM_94)
(27)      [SCAL] (1) source.ports[1].h_outflow = source.medium.h ($RES_SIM_95)
(28)      [SCAL] (1) source.medium.h = source.state.h ($RES_SIM_96)
(29)      [SCAL] (1) 99999.99999999999 * source.medium.p_bar = source.state.p ($RES_SIM_97)
(30)      [SCAL] (1) $SEV_15 = (source.medium.h < Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(source.medium.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.boilingcurve_p(source.medium.sat.psat)) or source.medium.h > Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(source.medium.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.dewcurve_p(source.medium.sat.psat))) or 99999.99999999999 * source.medium.p_bar > 2.2064e7 ($RES_EVT_220)
(31)      [SCAL] (1) $SEV_16 = valve.port_b.m_flow > valve.m_flow_small ($RES_EVT_221)
(32)      [SCAL] (1) $SEV_17 = valve.port_b.m_flow < (-valve.m_flow_small) ($RES_EVT_222)
(33)      [SCAL] (1) $SEV_18 = valve.m_flow_small > 0.0 ($RES_EVT_223)
(34)      [SCAL] (1) $SEV_19 = (-valve.port_b.m_flow) > valve.m_flow_small ($RES_EVT_224)
(35)      [SCAL] (1) $SEV_20 = (-valve.port_b.m_flow) < (-valve.m_flow_small) ($RES_EVT_225)
(36)      [SCAL] (1) sink.medium.h = sink.medium.state.h ($RES_SIM_20)
(37)      [SCAL] (1) sink.medium.u = sink.medium.h - (99999.99999999999 * sink.medium.p_bar) / sink.medium.d ($RES_SIM_22)
(38)      [SCAL] (1) sink.medium.sat.psat = 99999.99999999999 * sink.medium.p_bar ($RES_SIM_23)
(39)      [SCAL] (1) sink.medium.sat.Tsat = Modelica.Media.Water.IF97_Utilities.BaseIF97.Basic.tsat(99999.99999999999 * sink.medium.p_bar) ($RES_SIM_24)
(40)      [SCAL] (1) -((-273.15) - sink.medium.T_degC) = Modelica.Media.Water.IF97_Utilities.T_props_ph(99999.99999999999 * sink.medium.p_bar, sink.medium.h, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(99999.99999999999 * sink.medium.p_bar, sink.medium.h, sink.medium.phase, 0)) ($RES_SIM_25)
(41)      [SCAL] (1) sink.medium.d = Modelica.Media.Water.IF97_Utilities.rho_props_ph(99999.99999999999 * sink.medium.p_bar, sink.medium.h, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(99999.99999999999 * sink.medium.p_bar, sink.medium.h, sink.medium.phase, 0)) ($RES_SIM_26)
(42)      [SCAL] (1) sink.medium.phase = if $SEV_2 then 1 else 2 ($RES_SIM_27)
(43)      [SCAL] (1) valve.dp = pipe.port_b.p - valve.port_b.p ($RES_SIM_31)
(44)      [SCAL] (1) valve.port_a.h_outflow = sink.ports[1].h_outflow ($RES_SIM_35)
(45)      [SCAL] (1) -valve.port_b.m_flow = homotopy(valve.Av * valve.relativeFlowCoefficient * smooth(2, if $SEV_3 then (if $SEV_4 then sqrt(valve.state_a.d) else 0.0) * sqrt(valve.dp) else if $SEV_5 then -(if $SEV_6 then sqrt(valve.state_b.d) else 0.0) * sqrt(abs(valve.dp)) else if $SEV_7 then Modelica.Fluid.Utilities.regRoot2.regRoot2_utility(valve.dp, valve.dp_turbulent, valve.state_a.d, valve.state_b.d, false, 1.0) else -Modelica.Fluid.Utilities.regRoot2.regRoot2_utility(-valve.dp, valve.dp_turbulent, valve.state_b.d, valve.state_a.d, false, 1.0)), (valve.dp * valve.m_flow_nominal * valve.relativeFlowCoefficient) / valve.dp_nominal) ($RES_SIM_36)
(46)      [SCAL] (1) valve.minLimiter.y = smooth(0, noEvent(if $SEV_8 then valve.minLimiter.uMin else valve.relativeFlowCoefficient)) ($RES_SIM_38)
(47)      [ARRY] (1) pipe.fluidVolumes = {pipe.crossAreas[1]} .* pipe.nParallel ($RES_BND_129)
(48)      [SCAL] (1) $DER.pipe.ms[1] = pipe.mb_flows[1] ($RES_SIM_39)
(49)      [ARRY] (1) pipe.mediums.p_bar = {1e-5 * pipe.mediums[1].p} ($RES_BND_130)
(50)      [SCAL] (1) $DER.pipe.Us[1] = pipe.Wb_flows[1] + pipe.Hb_flows[1] + pipe.Qb_flows[1] ($RES_SIM_40)
(51)      [ARRY] (1) pipe.mediums.T_degC = {(-273.15) + pipe.mediums[1].T} ($RES_BND_131)
(52)      [SCAL] (1) pipe.ms[1] = pipe.fluidVolumes[1] * pipe.mediums[1].d ($RES_SIM_41)
(53)      [ARRY] (2) pipe.flowModel.vs = pipe.vsFM ($RES_BND_132)
(54)      [SCAL] (1) pipe.Us[1] = pipe.ms[1] * pipe.mediums[1].u ($RES_SIM_42)
(55)      [ARRY] (2) pipe.flowModel.crossAreas = pipe.crossAreasFM ($RES_BND_133)
(56)      [SCAL] (1) pipe.port_b.p = pipe.mediums[1].p ($RES_SIM_43)
(57)      [ARRY] (2) pipe.flowModel.dimensions = pipe.dimensionsFM ($RES_BND_134)
(58)      [ARRY] (1) pipe.vsFM[2:2] = pipe.vs ($RES_SIM_44)
(59)      [ARRY] (2) pipe.flowModel.roughnesses = pipe.roughnessesFM ($RES_BND_135)
(60)      [SCAL] (1) pipe.vsFM[1] = ((pipe.m_flows[1] / pipe.state_a.d) / pipe.crossAreas[1]) / pipe.nParallel ($RES_SIM_45)
(61)      [ARRY] (1) pipe.flowModel.dheights = pipe.dheightsFM ($RES_BND_136)
(62)      [ARRY] (1) pipe.m_flows[1:1] = pipe.flowModel.m_flows[:] ($RES_SIM_46)
(63)      [ARRY] (1) pipe.flowModel.pathLengths = pipe.pathLengths ($RES_BND_137)
(64)      [ARRY] (5) pipe.statesFM[2:2] = pipe.mediums[:].state ($RES_SIM_47)
(65)      [FOR-] (2) ($RES_BND_138)
(65)      [----] for $i1 in 1:2 loop
(65)      [----]   [SCAL] (1) pipe.flowModel.rhos[$i1] = pipe.flowModel.states.d ($RES_BND_139)
(65)      [----] end for;
(66)      [SCAL] (1) $FUN_1 = ModelicaTest.Fluid.TestPipesAndValves.DynamicPipeClosingValve.pipe.flowModel.WallFriction.massFlowRate_dp_staticHead(pipe.flowModel.dps_fg[1], pipe.flowModel.rhos[1], pipe.flowModel.rhos[2], pipe.flowModel.mus[1], pipe.flowModel.mus[2], pipe.flowModel.pathLengths_internal[1], pipe.flowModel.diameters[1], (pipe.flowModel.g * pipe.flowModel.dheights)[1], (0.5 .* (pipe.flowModel.crossAreas[1:1] + pipe.flowModel.crossAreas[2:2]))[1], (0.5 .* (pipe.flowModel.roughnesses[1:1] + pipe.flowModel.roughnesses[2:2]))[1], pipe.flowModel.dp_small, pipe.flowModel.Res_turbulent_internal[1]) ($RES_$AUX_166)
(67)      [RECD] (5) pipe.statesFM[1] = pipe.state_a ($RES_SIM_48)
(68)      [SCAL] (1) $FUN_2 = sum(pipe.flowModel.dps_fg) ($RES_$AUX_165)
(69)      [SCAL] (1) $FUN_3 = semiLinear(pipe.port_a.m_flow, source.ports[1].h_outflow, pipe.mediums[1].h) ($RES_$AUX_164)
(70)      [SCAL] (1) $FUN_4 = semiLinear(valve.port_b.m_flow, valve.port_a.h_outflow, pipe.mediums[1].h) ($RES_$AUX_163)
(71)      [SCAL] (1) $FUN_5 = ModelicaTest.Fluid.TestPipesAndValves.DynamicPipeClosingValve.pipe.flowModel.WallFriction.pressureLoss_m_flow(pipe.flowModel.m_flow_nominal / pipe.flowModel.nParallel, pipe.flowModel.rho_nominal, pipe.flowModel.rho_nominal, pipe.flowModel.mu_nominal, pipe.flowModel.mu_nominal, pipe.flowModel.pathLengths_internal[1], pipe.flowModel.diameters[1], (0.5 .* (pipe.flowModel.crossAreas[2:2] + pipe.flowModel.crossAreas[1:1]))[1], (0.5 .* (pipe.flowModel.roughnesses[2:2] + pipe.flowModel.roughnesses[1:1]))[1], pipe.flowModel.m_flow_small / pipe.flowModel.nParallel, pipe.flowModel.Res_turbulent_internal[1]) ($RES_$AUX_162)
(72)      [SCAL] (1) pipe.flowModel.dp_fric_nominal = sum({$FUN_5}) ($RES_$AUX_161)
(73)      [FOR-] (2) ($RES_BND_140)
(73)      [----] for $i1 in 1:2 loop
(73)      [----]   [SCAL] (1) pipe.flowModel.mus[$i1] = Modelica.Media.Water.IF97_Utilities.dynamicViscosity(pipe.flowModel.states.d, pipe.flowModel.states.h, pipe.flowModel.states.phase, pipe.flowModel.states.p) ($RES_BND_141)
(73)      [----] end for;
(74)      [ARRY] (1) pipe.flowModel.pathLengths_internal = pipe.flowModel.pathLengths ($RES_BND_142)
(75)      [SCAL] (1) valve.port_b.h_outflow = pipe.mediums[1].h ($RES_SIM_51)
(76)      [SCAL] (1) pipe.flowModel.Res_turbulent_internal[1] = pipe.flowModel.Re_turbulent ($RES_BND_143)
(77)      [SCAL] (1) pipe.port_a.h_outflow = pipe.mediums[1].h ($RES_SIM_52)
(78)      [ARRY] (1) pipe.flowModel.diameters = 0.5 * (pipe.flowModel.dimensions[2:2] + pipe.flowModel.dimensions[1:1]) ($RES_BND_144)
(79)      [SCAL] (1) valve.port_b.m_flow = -pipe.m_flows[2] ($RES_SIM_53)
(80)      [SCAL] (1) 99999.99999999999 * sink.medium.p_bar = sink.state.p ($RES_SIM_9)
(81)      [SCAL] (1) pipe.port_a.m_flow = pipe.m_flows[1] ($RES_SIM_54)
(82)      [SCAL] (1) sink.medium.h = sink.state.h ($RES_SIM_8)
(83)      [SCAL] (1) pipe.H_flows[2] = -$FUN_4 ($RES_SIM_55)
(84)      [ARRY] (1) pipe.vs = {(0.5 * (pipe.m_flows[2] + pipe.m_flows[1])) / (pipe.crossAreas[1] * pipe.mediums[1].d)} / pipe.nParallel ($RES_BND_146)
(85)      [SCAL] (1) sink.ports[1].h_outflow = sink.medium.h ($RES_SIM_7)
(86)      [SCAL] (1) pipe.H_flows[1] = $FUN_3 ($RES_SIM_56)
(87)      [SCAL] (1) sink.ports[1].p = 99999.99999999999 * sink.medium.p_bar ($RES_SIM_6)
(88)      [SCAL] (1) pipe.mb_flows[1] = pipe.m_flows[1] - pipe.m_flows[2] ($RES_SIM_57)
(89)      [SCAL] (1) source.state.h = Modelica.Media.Water.IF97_Utilities.h_pT(source.p, source.T, 0) ($RES_SIM_170)
(90)      [ARRY] (1) pipe.heatTransfer.Ts = {pipe.heatTransfer.states.h} ($RES_BND_148)
(91)      [SCAL] (1) valve.relativeFlowCoefficient = ramp.offset + (if $TEV_0 then 0.0 else if $TEV_1 then (ramp.height * (time - ramp.startTime)) / ramp.duration else ramp.height) ($RES_SIM_5)
(92)      [SCAL] (1) pipe.Hb_flows[1] = pipe.H_flows[1] - pipe.H_flows[2] ($RES_SIM_58)
(93)      [ARRY] (1) pipe.heatTransfer.vs = pipe.vs ($RES_BND_149)
(94)      [ARRY] (2) pipe.roughnessesFM[:] = {pipe.roughnesses[1], pipe.roughnesses[1]} ($RES_SIM_59)
(95)      [SCAL] (1) source.state.p = source.p ($RES_SIM_173)
(96)      [SCAL] (1) pipe.state_a.phase = 0 ($RES_SIM_174)
(97)      [SCAL] (1) pipe.state_a.h = source.ports[1].h_outflow ($RES_SIM_175)
(98)      [SCAL] (1) pipe.state_a.d = Modelica.Media.Water.IF97_Utilities.rho_ph(pipe.port_a.p, source.ports[1].h_outflow, 0, 0) ($RES_SIM_176)
(99)      [SCAL] (1) pipe.state_a.T = Modelica.Media.Water.IF97_Utilities.T_ph(pipe.port_a.p, source.ports[1].h_outflow, 0, 0) ($RES_SIM_177)
(100)     [SCAL] (1) pipe.state_a.p = pipe.port_a.p ($RES_SIM_178)
(101)     [ARRY] (2) pipe.dimensionsFM[:] = {pipe.dimensions[1], pipe.dimensions[1]} ($RES_SIM_60)
(102)     [ARRY] (2) pipe.crossAreasFM[:] = {pipe.crossAreas[1], pipe.crossAreas[1]} ($RES_SIM_61)
(103)     [ARRY] (1) pipe.dheightsFM[:] = {0.0} ($RES_SIM_62)
(104)     [SCAL] (1) valve.V_flow = -valve.port_b.m_flow / smooth(1, if $SEV_19 then valve.state_a.d else if $SEV_20 then valve.state_b.d else if $SEV_18 then 0.5 * (valve.state_a.d + valve.state_b.d) - 0.25 * (valve.state_b.d - valve.state_a.d) * ((-3.0) + (valve.port_b.m_flow / (-valve.m_flow_small)) ^ 2.0) * (valve.port_b.m_flow / valve.m_flow_small) else 0.5 * (valve.state_a.d + valve.state_b.d)) ($RES_BND_153)
(105)     [ARRY] (1) pipe.pathLengths[:] = {1.0} ($RES_SIM_63)
(106)     [SCAL] (1) valve.port_a_T = smooth(1, if $SEV_19 then valve.state_a.T else if $SEV_20 then Modelica.Media.Water.IF97_Utilities.T_ph(pipe.port_b.p, valve.port_a.h_outflow, 0, 0) else if $SEV_18 then 0.5 * (valve.state_a.T + Modelica.Media.Water.IF97_Utilities.T_ph(pipe.port_b.p, valve.port_a.h_outflow, 0, 0)) - 0.25 * (Modelica.Media.Water.IF97_Utilities.T_ph(pipe.port_b.p, valve.port_a.h_outflow, 0, 0) - valve.state_a.T) * ((-3.0) + (valve.port_b.m_flow / (-valve.m_flow_small)) ^ 2.0) * (valve.port_b.m_flow / valve.m_flow_small) else 0.5 * (valve.state_a.T + Modelica.Media.Water.IF97_Utilities.T_ph(pipe.port_b.p, valve.port_a.h_outflow, 0, 0))) ($RES_BND_154)
(107)     [ARRY] (1) pipe.Wb_flows = (pipe.crossAreas * pipe.vs * (($FUN_2 + pipe.port_b.p) - ((system.g * {0.0}) / pipe.mediums.d + pipe.port_a.p))) / ({1.0} * {1.0}) .* {1.0} .* pipe.nParallel ($RES_SIM_64)
(108)     [SCAL] (1) valve.port_b_T = smooth(1, if $SEV_16 then valve.state_b.T else if $SEV_17 then Modelica.Media.Water.IF97_Utilities.T_ph(valve.port_b.p, valve.port_b.h_outflow, 0, 0) else if $SEV_18 then 0.25 * (Modelica.Media.Water.IF97_Utilities.T_ph(valve.port_b.p, valve.port_b.h_outflow, 0, 0) - valve.state_b.T) * ((-3.0) + (valve.port_b.m_flow / valve.m_flow_small) ^ 2.0) * (valve.port_b.m_flow / valve.m_flow_small) + 0.5 * (valve.state_b.T + Modelica.Media.Water.IF97_Utilities.T_ph(valve.port_b.p, valve.port_b.h_outflow, 0, 0)) else 0.5 * (valve.state_b.T + Modelica.Media.Water.IF97_Utilities.T_ph(valve.port_b.p, valve.port_b.h_outflow, 0, 0))) ($RES_BND_155)
(109)     [SCAL] (1) source.medium.phase = source.medium.state.phase ($RES_SIM_104)
(110)     [ARRY] (1) pipe.Qb_flows = pipe.heatTransfer.Q_flows ($RES_SIM_65)
(111)     [SCAL] (1) valve.dp_turbulent = max(valve.dp_small, (6.283185307179586e6 * (Modelica.Media.Water.IF97_Utilities.dynamicViscosity(valve.state_a.d, valve.state_a.T, valve.state_a.p, valve.state_a.phase) + Modelica.Media.Water.IF97_Utilities.dynamicViscosity(valve.state_b.d, valve.state_b.T, valve.state_b.p, valve.state_b.phase)) ^ 2.0) / (valve.Av * max(valve.relativeFlowCoefficient, 0.001) * (valve.state_b.d + valve.state_a.d))) ($RES_BND_156)
(112)     [SCAL] (1) source.medium.d = source.medium.state.d ($RES_SIM_105)
(113)     [ARRY] (1) pipe.heatTransfer.Q_flows = pipe.heatTransfer.heatPorts.Q_flow ($RES_SIM_66)
(114)     [SCAL] (1) -((-273.15) - source.medium.T_degC) = source.medium.state.T ($RES_SIM_106)
(115)     [ARRY] (1) pipe.heatTransfer.Ts = pipe.heatTransfer.heatPorts.T ($RES_SIM_67)
(116)     [SCAL] (1) pipe.state_b.h = valve.port_a.h_outflow ($RES_SIM_180)
(117)     [SCAL] (1) 99999.99999999999 * source.medium.p_bar = source.medium.state.p ($RES_SIM_107)
(118)     [ARRY] (1) {0.0} = pipe.flowModel.Ib_flows - (pipe.flowModel.Fs_fg + pipe.flowModel.Fs_p) ($RES_SIM_68)
(119)     [SCAL] (1) pipe.state_b.d = Modelica.Media.Water.IF97_Utilities.rho_ph(pipe.port_b.p, valve.port_a.h_outflow, 0, 0) ($RES_SIM_181)
(120)     [ARRY] (10) pipe.flowModel.states = pipe.statesFM ($RES_BND_159)
(121)     [SCAL] (1) source.medium.h = source.medium.state.h ($RES_SIM_108)
(122)     [ARRY] (1) pipe.flowModel.Is = {pipe.flowModel.m_flows[1] * pipe.flowModel.pathLengths[1]} ($RES_SIM_69)
(123)     [SCAL] (1) pipe.state_b.T = Modelica.Media.Water.IF97_Utilities.T_ph(pipe.port_b.p, valve.port_a.h_outflow, 0, 0) ($RES_SIM_182)
(124)     [SCAL] (1) pipe.state_b.p = pipe.port_b.p ($RES_SIM_183)
(125)     [SCAL] (1) valve.state_a.phase = 0 ($RES_SIM_184)
(126)     [SCAL] (1) valve.state_a.h = valve.port_b.h_outflow ($RES_SIM_185)
(127)     [SCAL] (1) valve.state_a.d = Modelica.Media.Water.IF97_Utilities.rho_ph(pipe.port_b.p, valve.port_b.h_outflow, 0, 0) ($RES_SIM_186)
(128)     [SCAL] (1) valve.state_a.T = Modelica.Media.Water.IF97_Utilities.T_ph(pipe.port_b.p, valve.port_b.h_outflow, 0, 0) ($RES_SIM_187)
(129)     [SCAL] (1) valve.state_a.p = pipe.port_b.p ($RES_SIM_188)
(130)     [SCAL] (1) valve.state_b.phase = 0 ($RES_SIM_189)
(131)     [ARRY] (5) pipe.heatTransfer.states = pipe.mediums.state ($RES_BND_160)
(132)     [ARRY] (1) pipe.flowModel.dps_fg = {(2.0 * (pipe.flowModel.Fs_fg[1] / pipe.flowModel.nParallel)) / (pipe.flowModel.crossAreas[1] + pipe.flowModel.crossAreas[2])} ($RES_SIM_70)
(133)     [SCAL] (1) source.medium.u = source.medium.h - (99999.99999999999 * source.medium.p_bar) / source.medium.d ($RES_SIM_110)
(134)     [ARRY] (1) pipe.flowModel.Fs_p = pipe.flowModel.nParallel * {0.5 * (pipe.flowModel.crossAreas[1] + pipe.flowModel.crossAreas[2]) * (pipe.flowModel.states.phase - pipe.flowModel.states.phase)} ($RES_SIM_71)
(135)     [SCAL] (1) source.medium.sat.psat = 99999.99999999999 * source.medium.p_bar ($RES_SIM_111)
(136)     [ARRY] (1) pipe.flowModel.Ib_flows = {0.0} ($RES_SIM_72)
(137)     [SCAL] (1) source.medium.sat.Tsat = Modelica.Media.Water.IF97_Utilities.BaseIF97.Basic.tsat(99999.99999999999 * source.medium.p_bar) ($RES_SIM_112)
(138)     [SCAL] (1) pipe.flowModel.rhos_act[1] = noEvent(if $SEV_9 then pipe.flowModel.rhos[1] else pipe.flowModel.rhos[2]) ($RES_SIM_73)
(139)     [SCAL] (1) -((-273.15) - source.medium.T_degC) = Modelica.Media.Water.IF97_Utilities.T_props_ph(99999.99999999999 * source.medium.p_bar, source.medium.h, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(99999.99999999999 * source.medium.p_bar, source.medium.h, source.medium.phase, 0)) ($RES_SIM_113)
(140)     [SCAL] (1) pipe.flowModel.mus_act[1] = noEvent(if $SEV_9 then pipe.flowModel.mus[1] else pipe.flowModel.mus[2]) ($RES_SIM_74)
(141)     [SCAL] (1) source.medium.d = Modelica.Media.Water.IF97_Utilities.rho_props_ph(99999.99999999999 * source.medium.p_bar, source.medium.h, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(99999.99999999999 * source.medium.p_bar, source.medium.h, source.medium.phase, 0)) ($RES_SIM_114)
(142)     [ARRY] (1) pipe.flowModel.m_flows = {homotopy(({$FUN_1} .* 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_75)
(143)     [SCAL] (1) source.medium.phase = if $SEV_15 then 1 else 2 ($RES_SIM_115)
(144)     [SCAL] (1) valve.port_b.m_flow + sink.ports[1].m_flow = 0.0 ($RES_SIM_117)
(145)     [SCAL] (1) valve.state_b.h = sink.ports[1].h_outflow ($RES_SIM_190)
(146)     [SCAL] (1) pipe.heatTransfer.heatPorts[1].Q_flow = 0.0 ($RES_SIM_118)
(147)     [SCAL] (1) valve.state_b.d = Modelica.Media.Water.IF97_Utilities.rho_ph(valve.port_b.p, sink.ports[1].h_outflow, 0, 0) ($RES_SIM_191)
(148)     [SCAL] (1) valve.state_b.T = Modelica.Media.Water.IF97_Utilities.T_ph(valve.port_b.p, sink.ports[1].h_outflow, 0, 0) ($RES_SIM_192)
(149)     [SCAL] (1) valve.state_b.p = valve.port_b.p ($RES_SIM_193)
(150)     [SCAL] (1) sink.state.h = Modelica.Media.Water.IF97_Utilities.h_pT(sink.p, sink.T, 0) ($RES_SIM_195)
(151)     [SCAL] (1) sink.state.p = sink.p ($RES_SIM_198)
(152)     [SCAL] (1) $TEV_0 = time < ramp.startTime ($RES_EVT_203)
(153)     [SCAL] (1) $TEV_1 = time < (ramp.startTime + ramp.duration) ($RES_EVT_204)
(154)     [SCAL] (1) $SEV_2 = (sink.medium.h < Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(sink.medium.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.boilingcurve_p(sink.medium.sat.psat)) or sink.medium.h > Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(sink.medium.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.dewcurve_p(sink.medium.sat.psat))) or 99999.99999999999 * sink.medium.p_bar > 2.2064e7 ($RES_EVT_207)
(155)     [SCAL] (1) $SEV_3 = valve.dp >= valve.dp_turbulent ($RES_EVT_208)
(156)     [SCAL] (1) $SEV_4 = valve.state_a.d > 0.0 ($RES_EVT_209)