Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ModelicaTest_3.2.1_ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.conf.json
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo", uses=false)
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo", uses=false)
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.2.3+maint.om/package.mo", uses=false)
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaTest 3.2.1+maint.om/package.mo", uses=false)
Using package ModelicaTest with version 3.2.1 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaTest 3.2.1+maint.om/package.mo)
Using package Modelica with version 3.2.3 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.2.3+maint.om/package.mo)
Using package Complex with version 4.0.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo)
Using package ModelicaServices with version 4.0.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo)
Running command: translateModel(ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17,tolerance=1e-07,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ModelicaTest_3.2.1_ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17")
translateModel(ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17,tolerance=1e-07,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ModelicaTest_3.2.1_ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17")
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo): time 0.001235/0.001235, allocations: 107.2 kB / 16.42 MB, free: 5.504 MB / 14.72 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo): time 0.001288/0.001288, allocations: 190.4 kB / 17.35 MB, free: 5.176 MB / 14.72 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.2.3+maint.om/package.mo): time 1.228/1.228, allocations: 205.1 MB / 223.2 MB, free: 12.23 MB / 190.1 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaTest 3.2.1+maint.om/package.mo): time 0.1648/0.1648, allocations: 37.99 MB / 308.6 MB, free: 5.984 MB / 254.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 1.966e-05/1.966e-05, allocations: 9.734 kB / 433.6 MB, free: 14.46 MB / 318.1 MB
Notification: Performance of NFInst.instantiate(ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17): time 0.427/0.427, allocations: 260.3 MB / 0.6777 GB, free: 15.12 MB / 0.4981 GB
Notification: Performance of NFInst.instExpressions: time 0.02668/0.4537, allocations: 19.33 MB / 0.6965 GB, free: 11.75 MB / 0.5137 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.002256/0.456, allocations: 99.44 kB / 0.6966 GB, free: 11.66 MB / 0.5137 GB
Notification: Performance of NFTyping.typeComponents: time 0.002231/0.4583, allocations: 0.9861 MB / 0.6976 GB, free: 10.66 MB / 0.5137 GB
Notification: Performance of NFTyping.typeBindings: time 0.01191/0.4702, allocations: 5.475 MB / 0.7029 GB, free: 5.188 MB / 0.5137 GB
Notification: Performance of NFTyping.typeClassSections: time 0.01119/0.4814, allocations: 5.332 MB / 0.7081 GB, free: 15.84 MB / 0.5294 GB
Notification: Performance of NFFlatten.flatten: time 0.009033/0.4905, allocations: 8.156 MB / 0.7161 GB, free: 7.668 MB / 0.5294 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.002401/0.4929, allocations: 1.681 MB / 0.7177 GB, free: 5.957 MB / 0.5294 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.005027/0.4979, allocations: 3.135 MB / 0.7208 GB, free: 2.812 MB / 0.5294 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.003858/0.5018, allocations: 2.484 MB / 0.7232 GB, free: 328 kB / 0.5294 GB
Notification: Performance of NFPackage.collectConstants: time 0.0005103/0.5023, allocations: 224 kB / 0.7234 GB, free: 104 kB / 0.5294 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.2879/0.7903, allocations: 4.737 MB / 0.7281 GB, free: 11.25 MB / 0.5294 GB
Notification: Performance of combineBinaries: time 0.006401/0.7967, allocations: 4.901 MB / 0.7329 GB, free: 10.04 MB / 0.5294 GB
Notification: Performance of replaceArrayConstructors: time 0.003368/0.8001, allocations: 3.082 MB / 0.7359 GB, free: 8.562 MB / 0.5294 GB
Notification: Performance of NFVerifyModel.verify: time 0.001232/0.8013, allocations: 418.4 kB / 0.7363 GB, free: 8.484 MB / 0.5294 GB
Notification: Performance of FrontEnd: time 0.000484/0.8018, allocations: 70.2 kB / 0.7363 GB, free: 8.473 MB / 0.5294 GB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 452 (361)
 * Number of variables: 492 (375)
Notification: Performance of Bindings: time 0.01208/0.8139, allocations: 12.9 MB / 0.7489 GB, free: 4.129 MB / 0.5294 GB
Notification: Performance of FunctionAlias: time 0.00165/0.8156, allocations: 1.853 MB / 0.7507 GB, free: 3.793 MB / 0.5294 GB
Notification: Performance of Early Inline: time 0.006508/0.8221, allocations: 7.284 MB / 0.7579 GB, free: 3.465 MB / 0.5294 GB
Notification: Performance of simplify1: time 0.000764/0.8229, allocations: 0.5721 MB / 0.7584 GB, free: 3.465 MB / 0.5294 GB
Notification: Performance of Alias: time 0.006314/0.8292, allocations: 5.947 MB / 0.7642 GB, free: 1.859 MB / 0.5294 GB
Notification: Performance of simplify2: time 0.0009462/0.8302, allocations: 0.523 MB / 0.7647 GB, free: 1.848 MB / 0.5294 GB
Notification: Performance of Events: time 0.001789/0.832, allocations: 1.817 MB / 0.7665 GB, free: 1.434 MB / 0.5294 GB
Notification: Performance of Detect States: time 0.001627/0.8336, allocations: 1.852 MB / 0.7683 GB, free: 1.262 MB / 0.5294 GB
Notification: Performance of Partitioning: time 0.002758/0.8364, allocations: 2.714 MB / 0.771 GB, free: 356 kB / 0.5294 GB
Error: Internal error NBAdjacency.Matrix.create failed to create adjacency matrix for system:
System Variables (338/460)
****************************
(1)       [ALGB] (1) Real[1] pipe2.mb_flows (min = {-1e5 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1})
(2)       [ALGB] (1) protected Real valve1.state_b.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(3)       [ALGB] (1) Real[1] pipe2.mediums.T (start = {pipe2.T_start}, min = {200.0 for $i1 in 1:1}, max = {6000.0 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}, StateSelect = prefer)
(4)       [ALGB] (1) Real[1] pipe2.mediums.R (start = {1000.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e7 for $i1 in 1:1}, nominal = {1000.0 for $i1 in 1:1})
(5)       [ALGB] (2) Real[2] pipe3.H_flows (min = {-1e8 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1000.0 for $i1 in 1:2})
(6)       [ALGB] (1) protected Real[1] pipe3.dheightsFM
(7)       [DISC] (1) protected Real valveOpening1.b
(8)       [DISC] (1) protected Real valveOpening1.a
(9)       [ALGB] (2) Real[2] pipe2.H_flows (min = {-1e8 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1000.0 for $i1 in 1:2})
(10)      [ALGB] (1) final Real[1] pipe3.flowModel.dheights = pipe3.dheightsFM
(11)      [ALGB] (2) Real[2] pipe1.H_flows (min = {-1e8 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1000.0 for $i1 in 1:2})
(12)      [DISC] (1) protected discrete Real valveOpening1.nextEvent (fixed = true, start = 0.0)
(13)      [ALGB] (2) final Real[2] pipe1.flowModel.dheights = pipe1.dheightsFM
(14)      [ALGB] (1) Real pipe2.state_b.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(15)      [ALGB] (1) protected Real valve1.state_b.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(16)      [ALGB] (1) stream Real pipe1.port_b.h_outflow (start = 298609.6803431054, min = -1e10, max = 1e10, nominal = 1e5)
(17)      [DER-] (1) Real[1] $DER.pipe3.Us
(18)      [ALGB] (1) Real[1] pipe2.mediums.T_degC = {Modelica.SIunits.Conversions.to_degC(pipe2.mediums[1].T)}
(19)      [ALGB] (1) Real[1] pipe3.mediums.T_degC = {Modelica.SIunits.Conversions.to_degC(pipe3.mediums[1].T)}
(20)      [ALGB] (1) Real junctionVolume.medium.p_bar = Modelica.SIunits.Conversions.to_bar(99999.99999999999 * junctionVolume.medium.p_bar)
(21)      [ALGB] (3) final Real[3] pipe1.flowModel.crossAreas = pipe1.crossAreasFM
(22)      [ALGB] (3) final Real[3] pipe1.flowModel.dimensions = pipe1.dimensionsFM
(23)      [ALGB] (1) Real valve2.V_flow = valve2.m_flow / Modelica.Fluid.Utilities.regStep(valve2.m_flow, ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve2.Medium.density(valve2.state_a), ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve2.Medium.density(valve2.state_b), valve2.m_flow_small)
(24)      [ALGB] (1) Real[1] pipe1.Qb_flows
(25)      [ALGB] (1) stream Real junctionIdeal.port_3.h_outflow (start = 298609.6803431054, min = -1e10, max = 1e10, nominal = 1e5)
(26)      [ALGB] (1) Real pipe3.port_b.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(27)      [ALGB] (1) Real pipe2.state_a.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(28)      [DISC] (1) Boolean[1] $SEV_32[$i1]
(29)      [ALGB] (1) final input Real[1, 1] pipe2.heatTransfer.states.T = {pipe2.mediums[1].state.T} (start = {500.0 for $i1 in 1:1}, min = {200.0 for $i1 in 1:1}, max = {6000.0 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(30)      [DER-] (1) Real[1] $DER.pipe2.Us
(31)      [ALGB] (1) Real valve1.m_flow (start = valve1.m_flow_start, min = -1e60, max = 1e5)
(32)      [ALGB] (1) protected Real valve1.state_a.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(33)      [ALGB] (1) Real[1] pipe1.mediums.state.T (start = {500.0 for $i1 in 1:1}, min = {200.0 for $i1 in 1:1}, max = {6000.0 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(34)      [DER-] (1) Real[1] $DER.pipe1.Us
(35)      [ALGB] (2) Real[2] pipe2.flowModel.mus = {pipe2.flowModel.mu_nominal 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})
(36)      [ALGB] (2) final Real[2] pipe2.flowModel.roughnesses = pipe2.roughnessesFM (min = {0.0 for $i1 in 1:2})
(37)      [ALGB] (1) final Real[1] pipe2.fluidVolumes = {pipe2.crossAreas[1] * 10.0} .* pipe2.nParallel
(38)      [ALGB] (1) protected Real[1] pipe2.pathLengths
(39)      [ALGB] (1) Real pipe2.state_a.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(40)      [ALGB] (1) protected Real[1] pipe2.dheightsFM
(41)      [ALGB] (1) final input Real[1, 1] pipe2.heatTransfer.states.p = {pipe2.mediums[1].state.p} (start = {1e6 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(42)      [ALGB] (1) final input Real[1, 1] pipe3.heatTransfer.states.p = {pipe3.mediums[1].state.p} (start = {1e6 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(43)      [ALGB] (1) flow Real pipe1.port_a.m_flow (min = -1e60, max = 1e5)
(44)      [ALGB] (1) protected Real valve1.state_a.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(45)      [DISC] (3) Boolean[3] $SEV_4[$i1]
(46)      [ALGB] (1) Real[1] pipe1.mediums.state.p (start = {1e6 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(47)      [ALGB] (1) Real[1] pipe1.Hb_flows
(48)      [ALGB] (1) Real[1] pipe2.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})
(49)      [ALGB] (2) final Real[2] pipe3.flowModel.crossAreas = pipe3.crossAreasFM
(50)      [ALGB] (2) final Real[2] pipe3.flowModel.dimensions = pipe3.dimensionsFM
(51)      [ALGB] (1) Real valve1.V_flow = valve1.m_flow / Modelica.Fluid.Utilities.regStep(valve1.m_flow, ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve1.Medium.density(valve1.state_a), ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve1.Medium.density(valve1.state_b), valve1.m_flow_small)
(52)      [ALGB] (1) final input Real[1, 1] pipe3.heatTransfer.states.T = {pipe3.mediums[1].state.T} (start = {500.0 for $i1 in 1:1}, min = {200.0 for $i1 in 1:1}, max = {6000.0 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(53)      [ALGB] (1) Real[1] pipe3.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)      [ALGB] (1) stream Real valve2.port_b.h_outflow (start = 298609.6803431054, min = -1e10, max = 1e10, nominal = 1e5)
(55)      [DER-] (1) Real $DER.junctionIdeal.U
(56)      [ALGB] (2) Real[2] pipe1.flowModel.Fs_fg
(57)      [ALGB] (1) Real valve2.port_b_T = Modelica.Fluid.Utilities.regStep(-valve2.m_flow, ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve2.Medium.temperature(valve2.state_b), ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve2.Medium.temperature(ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve2.Medium.setState_phX(99999.99999999999 * junctionVolume.medium.p_bar, valve2.port_b.h_outflow, {})), valve2.m_flow_small) (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(58)      [ALGB] (1) Real[1] pipe2.flowModel.Ib_flows
(59)      [ALGB] (2) Real[2] pipe3.m_flows (start = {0.0 for $i1 in 1:2}, min = {-1e60 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2})
(60)      [ALGB] (1) Real[1] pipe2.heatTransfer.Q_flows
(61)      [DISC] (1) Boolean[1] $SEV_30[$i1]
(62)      [ALGB] (2) protected Real[2] pipe1.dheightsFM
(63)      [ALGB] (2) Real[2] pipe2.m_flows (start = {0.0 for $i1 in 1:2}, min = {-1e60 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2})
(64)      [ALGB] (1) Real[1] pipe2.flowModel.Is
(65)      [DER-] (1) Real $DER.junctionIdeal.m
(66)      [ALGB] (2) Real[2] pipe1.m_flows (start = {0.0 for $i1 in 1:2}, min = {-1e60 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2})
(67)      [ALGB] (1) flow Real pipe1.port_b.m_flow (min = -1e5, max = 1e60)
(68)      [ALGB] (1) Real[1] pipe3.flowModel.m_flows (start = {0.0 for $i1 in 1:1}, min = {-1e60 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, StateSelect = default)
(69)      [DISC] (1) Boolean $TEV_1
(70)      [ALGB] (1) Real[1] pipe1.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})
(71)      [DISC] (1) Boolean $TEV_0
(72)      [ALGB] (2) protected Real[2] pipe1.pathLengths
(73)      [ALGB] (2) Real[2] pipe1.flowModel.rhos_act (start = {10.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {10.0 for $i1 in 1:2})
(74)      [ALGB] (1) Real[1] pipe1.mediums.T_degC = {Modelica.SIunits.Conversions.to_degC(pipe1.mediums[1].T)}
(75)      [DISC] (1) Boolean[1] $SEV_28[$i1]
(76)      [ALGB] (1) Real valve2.port_a_T = Modelica.Fluid.Utilities.regStep(valve2.m_flow, ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve2.Medium.temperature(valve2.state_a), ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve2.Medium.temperature(ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve2.Medium.setState_phX(pipe3.port_b.p, junctionVolume.port_3.h_outflow, {})), valve2.m_flow_small) (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(77)      [ALGB] (1) flow Real pipe3.port_a.m_flow (min = -1e60, max = 1e5)
(78)      [ALGB] (1) Real[1] pipe3.mb_flows (min = {-1e5 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1})
(79)      [ALGB] (4) final input Real[2, 2] pipe2.flowModel.states.T = {pipe2.statesFM[1].T, pipe2.statesFM[2].T} (start = {500.0 for $i1 in 1:2}, min = {200.0 for $i1 in 1:2}, max = {6000.0 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2})
(80)      [ALGB] (1) Real[1] pipe2.flowModel.m_flows (start = {0.0 for $i1 in 1:1}, min = {-1e60 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, StateSelect = default)
(81)      [ALGB] (2) protected Real[2] pipe2.dimensionsFM
(82)      [ALGB] (2) protected Real[2] pipe2.crossAreasFM
(83)      [ALGB] (1) protected Real[1] pipe3.pathLengths
(84)      [ALGB] (1) stream Real junctionVolume.port_3.h_outflow (start = 298609.6803431054, min = -1e10, max = 1e10, nominal = 1e5)
(85)      [ALGB] (1) Real junctionIdeal.Hb_flow
(86)      [ALGB] (9) final input Real[3, 3] pipe1.flowModel.states.p = {pipe1.statesFM[1].p, pipe1.statesFM[2].p, pipe1.statesFM[3].p} (start = {1e6 for $i1 in 1:3}, min = {0.0 for $i1 in 1:3}, max = {1e8 for $i1 in 1:3}, nominal = {1e6 for $i1 in 1:3})
(87)      [ALGB] (4) Real[2, 2] pipe3.statesFM.p (start = {1e6 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2})
(88)      [ALGB] (1) Real[1] pipe1.Wb_flows
(89)      [ALGB] (1) Real junctionVolume.medium.d (start = 10.0, min = 0.0, max = 1e5, nominal = 10.0)
(90)      [ALGB] (1) Real[1] pipe2.flowModel.Fs_fg
(91)      [ALGB] (1) Real[1] pipe1.vs = {(0.5 * (pipe1.m_flows[2] + pipe1.m_flows[1])) / (pipe1.crossAreas[1] * pipe1.mediums[1].d)} / pipe1.nParallel
(92)      [ALGB] (1) Real valve1.xs
(93)      [ALGB] (4) final input Real[2, 2] pipe2.flowModel.states.p = {pipe2.statesFM[1].p, pipe2.statesFM[2].p} (start = {1e6 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2})
(94)      [ALGB] (1) flow Real[1] pipe3.heatTransfer.heatPorts.Q_flow
(95)      [ALGB] (1) Real junctionVolume.medium.u (min = -1e8, max = 1e8, nominal = 1e6)
(96)      [ALGB] (1) protected Real valve1.minLimiter.y
(97)      [ALGB] (1) Real[1] pipe2.Qb_flows
(98)      [ALGB] (9) final input Real[3, 3] pipe1.flowModel.states.T = {pipe1.statesFM[1].T, pipe1.statesFM[2].T, pipe1.statesFM[3].T} (start = {500.0 for $i1 in 1:3}, min = {200.0 for $i1 in 1:3}, max = {6000.0 for $i1 in 1:3}, nominal = {500.0 for $i1 in 1:3})
(99)      [ALGB] (1) Real[1] pipe2.vs = {(0.5 * (pipe2.m_flows[2] + pipe2.m_flows[1])) / (pipe2.crossAreas[1] * pipe2.mediums[1].d)} / pipe2.nParallel
(100)     [ALGB] (1) Real valve2.xs
(101)     [ALGB] (1) Real[1] pipe3.mediums.u (min = {-1e8 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(102)     [ALGB] (4) Real[2, 2] pipe3.statesFM.T (start = {500.0 for $i1 in 1:2}, min = {200.0 for $i1 in 1:2}, max = {6000.0 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2})
(103)     [DISC] (2) Boolean[2] $SEV_1[$i1]
(104)     [ALGB] (1) Real[1] pipe2.flowModel.mus_act (start = {0.001 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {0.001 for $i1 in 1:1})
(105)     [ALGB] (2) final Real[2] pipe2.flowModel.vs = pipe2.vsFM
(106)     [ALGB] (1) Real[1] pipe3.mediums.state.p (start = {1e6 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(107)     [ALGB] (1) Real[1] pipe3.mediums.p (start = {pipe3.ps_start[1]}, min = {0.0 for $i1 in 1:1}, nominal = {1e5 for $i1 in 1:1}, StateSelect = prefer)
(108)     [ALGB] (1) Real[1] pipe2.flowModel.pathLengths_internal = pipe2.flowModel.pathLengths
(109)     [ALGB] (1) final Real[1] pipe1.heatTransfer.vs = pipe1.vs
(110)     [ALGB] (1) Real[1] pipe3.vs = {(0.5 * (pipe3.m_flows[2] + pipe3.m_flows[1])) / (pipe3.crossAreas[1] * pipe3.mediums[1].d)} / pipe3.nParallel
(111)     [ALGB] (1) Real[1] pipe3.mediums.h (start = {pipe3.h_start})
(112)     [ALGB] (1) Real[1] pipe2.flowModel.rhos_act (start = {10.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {10.0 for $i1 in 1:1})
(113)     [ALGB] (1) Real junctionVolume.Hb_flow
(114)     [ALGB] (2) Real[2] pipe3.flowModel.rhos = {ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.pipe3.flowModel.Medium.density(pipe3.flowModel.states[$i1]) for $i1 in 1:2} (start = {10.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {10.0 for $i1 in 1:2})
(115)     [ALGB] (1) Real[1] pipe3.mediums.d (start = {10.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {10.0 for $i1 in 1:1})
(116)     [ALGB] (1) Real pipe3.state_b.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(117)     [ALGB] (1) Real[1] pipe3.flowModel.Fs_p
(118)     [ALGB] (2) Real[2] pipe1.flowModel.Res_turbulent_internal = pipe1.flowModel.Re_turbulent * {1.0 for $i1 in 1:2}
(119)     [DER-] (1) Real $DER.junctionVolume.U
(120)     [DISC] (1) protected Integer valveOpening2.last (start = 1)
(121)     [ALGB] (1) protected Real valve2.state_b.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(122)     [ALGB] (4) Real[2, 2] pipe2.statesFM.p (start = {1e6 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2})
(123)     [ALGB] (1) Real[1] pipe3.mediums.state.T (start = {500.0 for $i1 in 1:1}, min = {200.0 for $i1 in 1:1}, max = {6000.0 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(124)     [ALGB] (1) Real[1] pipe3.mediums.T (start = {pipe3.T_start}, min = {200.0 for $i1 in 1:1}, max = {6000.0 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}, StateSelect = prefer)
(125)     [ALGB] (1) Real[1] pipe3.mediums.R (start = {1000.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e7 for $i1 in 1:1}, nominal = {1000.0 for $i1 in 1:1})
(126)     [ALGB] (1) flow Real junctionVolume.port_3.m_flow (min = -1e60, max = 1e60)
(127)     [ALGB] (1) protected Real[1] pipe2.flowModel.diameters = 0.5 * (pipe2.flowModel.dimensions[2:2] + pipe2.flowModel.dimensions[1:1])
(128)     [DISC] (1) Boolean[1] $SEV_26[$i1]
(129)     [ALGB] (1) Real[1] pipe2.Hb_flows
(130)     [ALGB] (2) Real[2] pipe1.flowModel.Ib_flows
(131)     [DISC] (2) Boolean[2] $SEV_0[$i1]
(132)     [ALGB] (1) Real[1] pipe2.flowModel.Res_turbulent_internal = pipe2.flowModel.Re_turbulent * {1.0 for $i1 in 1:1}
(133)     [DER-] (1) Real $DER.junctionVolume.m
(134)     [ALGB] (1) Real pipe3.state_b.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(135)     [ALGB] (1) Real[1] pipe1.mediums.u (min = {-1e8 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(136)     [ALGB] (1) Real[1] pipe1.mediums.p (start = {pipe1.ps_start[1]}, min = {0.0 for $i1 in 1:1}, nominal = {1e5 for $i1 in 1:1}, StateSelect = prefer)
(137)     [ALGB] (1) Real valve2.dp_turbulent = max(valve2.dp_small, ((ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve2.Medium.dynamicViscosity(valve2.state_a) + ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve2.Medium.dynamicViscosity(valve2.state_b)) ^ 2.0 * 3.141592653589793 * 1.6e7) / (8.0 * valve2.Y * max(ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve2.valveCharacteristic(valveOpening2.y), 0.001) * valve2.Av * (ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve2.Medium.density(valve2.state_b) + ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve2.Medium.density(valve2.state_a)))) (min = 0.0, nominal = 1e5)
(138)     [ALGB] (1) protected Real valve2.state_b.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(139)     [ALGB] (1) Real[1] pipe3.heatTransfer.Ts = {ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.pipe3.heatTransfer.Medium.temperature(pipe3.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})
(140)     [ALGB] (4) Real[2, 2] pipe2.statesFM.T (start = {500.0 for $i1 in 1:2}, min = {200.0 for $i1 in 1:2}, max = {6000.0 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2})
(141)     [ALGB] (1) Real[1] pipe1.heatTransfer.Q_flows
(142)     [ALGB] (3) protected Real[3] pipe1.roughnessesFM (min = {0.0 for $i1 in 1:3})
(143)     [ALGB] (1) flow Real[1] source.ports.m_flow (min = {-1e60}, max = {1e60})
(144)     [ALGB] (1) Real[1] pipe1.mediums.h (start = {pipe1.h_start})
(145)     [ALGB] (1) Real source.medium.u (min = -1e8, max = 1e8, nominal = 1e6)
(146)     [ALGB] (1) Real pipe3.state_a.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(147)     [ALGB] (1) Real[1] pipe1.mediums.d (start = {10.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {10.0 for $i1 in 1:1})
(148)     [ALGB] (1) Real pipe1.port_a.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(149)     [DISC] (1) protected Integer valveOpening1.last (start = 1)
(150)     [ALGB] (1) Real[1] pipe3.flowModel.dps_fg (start = {pipe3.flowModel.p_a_start - pipe3.flowModel.p_b_start for $i1 in 1:1})
(151)     [ALGB] (1) Real pipe1.state_b.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(152)     [ALGB] (1) final Real[1] pipe3.fluidVolumes = {pipe3.crossAreas[1] * 10.0} .* pipe3.nParallel
(153)     [ALGB] (2) protected Real[2] pipe1.flowModel.diameters = 0.5 * (pipe1.flowModel.dimensions[2:3] + pipe1.flowModel.dimensions[1:2])
(154)     [ALGB] (1) protected Real valve2.state_a.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(155)     [ALGB] (1) Real[1] pipe3.flowModel.pathLengths_internal = pipe3.flowModel.pathLengths
(156)     [ALGB] (1) Real source.medium.h
(157)     [DISC] (1) protected discrete Real valveOpening1.nextEventScaled (fixed = true, start = 0.0)
(158)     [ALGB] (3) protected Real[3] pipe1.vsFM
(159)     [ALGB] (2) Real[2] pipe1.flowModel.m_flows (start = {0.0 for $i1 in 1:2}, min = {-1e60 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, StateSelect = default)
(160)     [ALGB] (1) Real[1] pipe1.mediums.T (start = {pipe1.T_start}, min = {200.0 for $i1 in 1:1}, max = {6000.0 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}, StateSelect = prefer)
(161)     [DISC] (1) Boolean $SEV_64
(162)     [DISC] (1) Boolean $SEV_63
(163)     [ALGB] (1) Real[1] pipe1.mediums.R (start = {1000.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e7 for $i1 in 1:1}, nominal = {1000.0 for $i1 in 1:1})
(164)     [ALGB] (2) protected Real[2] pipe2.roughnessesFM (min = {0.0 for $i1 in 1:2})
(165)     [DISC] (1) Boolean $SEV_62
(166)     [ALGB] (1) Real junctionIdeal.mb_flow
(167)     [DISC] (1) Boolean $SEV_61
(168)     [DISC] (1) Boolean $SEV_60
(169)     [ALGB] (1) Real[1] pipe1.heatTransfer.Ts = {ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.pipe1.heatTransfer.Medium.temperature(pipe1.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})
(170)     [ALGB] (9) Real[3, 3] pipe1.statesFM.p (start = {1e6 for $i1 in 1:3}, min = {0.0 for $i1 in 1:3}, max = {1e8 for $i1 in 1:3}, nominal = {1e6 for $i1 in 1:3})
(171)     [ALGB] (1) Real pipe3.state_a.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(172)     [DER-] (1) Real[1] $DER.pipe3.ms
(173)     [DISC] (1) protected discrete Real valveOpening2.nextEvent (fixed = true, start = 0.0)
(174)     [ALGB] (1) Real pipe1.state_b.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(175)     [ALGB] (1) Real[1] pipe3.flowModel.Ib_flows
(176)     [ALGB] (1) stream Real pipe2.port_a.h_outflow (start = 298609.6803431054, min = -1e10, max = 1e10, nominal = 1e5)
(177)     [ALGB] (1) protected Real valve2.state_a.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(178)     [ALGB] (1) Real sink.medium.u (min = -1e8, max = 1e8, nominal = 1e6)
(179)     [ALGB] (2) final Real[2] pipe3.flowModel.roughnesses = pipe3.roughnessesFM (min = {0.0 for $i1 in 1:2})
(180)     [DER-] (1) Real[1] $DER.pipe2.ms
(181)     [ALGB] (1) Real junctionVolume.medium.T_degC = Modelica.SIunits.Conversions.to_degC(-((-273.15) - junctionVolume.medium.T_degC))
(182)     [ALGB] (1) stream Real pipe1.port_a.h_outflow (start = 298609.6803431054, min = -1e10, max = 1e10, nominal = 1e5)
(183)     [DISC] (1) Boolean $SEV_59
(184)     [DISC] (1) Boolean $SEV_58
(185)     [DISC] (1) Boolean $SEV_57
(186)     [DISC] (1) Boolean $SEV_56
(187)     [DISC] (1) Boolean $SEV_55
(188)     [ALGB] (1) Real sink.medium.h
(189)     [ALGB] (1) Real[1] pipe2.mediums.state.p (start = {1e6 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(190)     [ALGB] (1) Real pipe1.state_a.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(191)     [ALGB] (1) Real[1] pipe3.heatTransfer.Q_flows
(192)     [ALGB] (9) Real[3, 3] pipe1.statesFM.T (start = {500.0 for $i1 in 1:3}, min = {200.0 for $i1 in 1:3}, max = {6000.0 for $i1 in 1:3}, nominal = {500.0 for $i1 in 1:3})
(193)     [DER-] (1) Real[1] $DER.pipe1.ms
(194)     [ALGB] (2) Real[2] pipe1.flowModel.mus_act (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})
(195)     [ALGB] (2) protected Real[2] pipe2.vsFM
(196)     [ALGB] (1) Real valve1.dp (start = 10.0)
(197)     [ALGB] (2) protected Real[2] pipe3.roughnessesFM (min = {0.0 for $i1 in 1:2})
(198)     [ALGB] (1) Real junctionVolume.mb_flow
(199)     [ALGB] (1) Real[1] pipe2.heatTransfer.Ts = {ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.pipe2.heatTransfer.Medium.temperature(pipe2.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})
(200)     [ALGB] (1) Real[1] pipe2.Wb_flows
(201)     [ALGB] (1) final Real[1] pipe3.heatTransfer.vs = pipe3.vs
(202)     [ALGB] (1) Real[1] pipe3.flowModel.Is
(203)     [ALGB] (1) Real valve2.dp (start = valve2.dp_start)
(204)     [ALGB] (1) Real[1] pipe2.flowModel.dps_fg (start = {pipe2.flowModel.p_a_start - pipe2.flowModel.p_b_start for $i1 in 1:1})
(205)     [ALGB] (1) Real[1] pipe2.mediums.state.T (start = {500.0 for $i1 in 1:1}, min = {200.0 for $i1 in 1:1}, max = {6000.0 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})
(206)     [ALGB] (1) final Real[1] pipe2.flowModel.dheights = pipe2.dheightsFM
(207)     [ALGB] (1) Real junctionIdeal.medium.T_degC = Modelica.SIunits.Conversions.to_degC(-((-273.15) - junctionIdeal.medium.T_degC))
(208)     [ALGB] (1) Real pipe1.state_a.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(209)     [ALGB] (4) final input Real[2, 2] pipe3.flowModel.states.T = {pipe3.statesFM[1].T, pipe3.statesFM[2].T} (start = {500.0 for $i1 in 1:2}, min = {200.0 for $i1 in 1:2}, max = {6000.0 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2})
(210)     [DISC] (1) Boolean $SEV_47
(211)     [DISC] (1) Boolean $SEV_46
(212)     [DISC] (1) Boolean $SEV_45
(213)     [ALGB] (1) Real[1] pipe1.mb_flows (min = {-1e5 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1})
(214)     [DISC] (1) Boolean $SEV_44
(215)     [DISC] (1) Boolean $SEV_43
(216)     [DISC] (1) Boolean $SEV_42
(217)     [DISC] (1) Boolean $SEV_41
(218)     [DISC] (1) Boolean $SEV_40
(219)     [ALGB] (2) final Real[2] pipe2.flowModel.dimensions = pipe2.dimensionsFM
(220)     [ALGB] (2) final Real[2] pipe2.flowModel.crossAreas = pipe2.crossAreasFM
(221)     [DISC] (1) protected discrete Real valveOpening2.nextEventScaled (fixed = true, start = 0.0)
(222)     [ALGB] (1) Real[1] pipe3.Qb_flows
(223)     [ALGB] (1) Real $FUN_9
(224)     [ALGB] (1) Real $FUN_8
(225)     [ALGB] (1) Real $FUN_27
(226)     [ALGB] (1) protected Real pipe3.flowModel.dp_fric_nominal = sum({ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.pipe3.flowModel.WallFriction.pressureLoss_m_flow(pipe3.flowModel.m_flow_nominal / pipe3.flowModel.nParallel, pipe3.flowModel.rho_nominal, pipe3.flowModel.rho_nominal, pipe3.flowModel.mu_nominal, pipe3.flowModel.mu_nominal, pipe3.flowModel.pathLengths_internal[1], pipe3.flowModel.diameters[1], ((pipe3.flowModel.crossAreas[2:2] + pipe3.flowModel.crossAreas[1:1]) / 2.0)[1], ((pipe3.flowModel.roughnesses[2:2] + pipe3.flowModel.roughnesses[1:1]) / 2.0)[1], pipe3.flowModel.m_flow_small / pipe3.flowModel.nParallel, pipe3.flowModel.Res_turbulent_internal[1])}) (min = 0.0, nominal = 1e5)
(227)     [ALGB] (1) Real $FUN_7
(228)     [ALGB] (1) Real $FUN_6
(229)     [ALGB] (1) Real $FUN_25
(230)     [ALGB] (1) final Real[1] pipe1.fluidVolumes = {pipe1.crossAreas[1] * 10.0} .* pipe1.nParallel
(231)     [ALGB] (1) Real $FUN_5
(232)     [DISC] (1) Boolean[1] $SEV_51[$i1]
(233)     [ALGB] (1) Real $FUN_4
(234)     [ALGB] (1) Real $FUN_23
(235)     [ALGB] (1) Real $FUN_3
(236)     [DISC] (1) Integer $FUN_22
(237)     [ALGB] (2) protected Real[2] pipe3.vsFM
(238)     [ALGB] (1) Real $FUN_2
(239)     [ALGB] (1) Real $FUN_21
(240)     [ALGB] (1) Real $FUN_1
(241)     [ALGB] (1) Real $FUN_20
(242)     [ALGB] (4) final input Real[2, 2] pipe3.flowModel.states.p = {pipe3.statesFM[1].p, pipe3.statesFM[2].p} (start = {1e6 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2})
(243)     [ALGB] (2) protected Real[2] pipe3.dimensionsFM
(244)     [ALGB] (2) protected Real[2] pipe3.crossAreasFM
(245)     [ALGB] (1) Real junctionVolume.medium.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(246)     [DISC] (1) Boolean $SEV_39
(247)     [DISC] (1) Boolean $SEV_38
(248)     [DISC] (1) Boolean $SEV_37
(249)     [DISC] (1) Boolean $SEV_36
(250)     [ALGB] (1) Real junctionIdeal.medium.d (start = 10.0, min = 0.0, max = 1e5, nominal = 10.0)
(251)     [ALGB] (1) Real[1] sink.ports.p (start = {1e6 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(252)     [ALGB] (1) Real pipe2.port_b.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(253)     [ALGB] (1) flow Real pipe2.port_a.m_flow (min = -1e60, max = 1e5)
(254)     [ALGB] (1) Real $FUN_19
(255)     [ALGB] (1) Real junctionIdeal.medium.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(256)     [DISC] (1) Integer $FUN_18
(257)     [ALGB] (1) Real $FUN_17
(258)     [ALGB] (1) Real $FUN_16
(259)     [ALGB] (1) Real $FUN_15
(260)     [ALGB] (1) Real[1] pipe3.flowModel.rhos_act (start = {10.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {10.0 for $i1 in 1:1})
(261)     [ALGB] (1) Real $FUN_14
(262)     [DISC] (1) Boolean[1] $SEV_49[$i1]
(263)     [ALGB] (1) Real $FUN_13
(264)     [ALGB] (1) Real $FUN_12
(265)     [ALGB] (1) Real junctionIdeal.medium.u (min = -1e8, max = 1e8, nominal = 1e6)
(266)     [ALGB] (1) Real $FUN_11
(267)     [ALGB] (1) Real $FUN_10
(268)     [ALGB] (1) final Real[1] pipe3.flowModel.pathLengths = pipe3.pathLengths
(269)     [ALGB] (1) Real junctionVolume.medium.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(270)     [ALGB] (1) Real[1] pipe3.Hb_flows
(271)     [ALGB] (3) final Real[3] pipe1.flowModel.roughnesses = pipe1.roughnessesFM (min = {0.0 for $i1 in 1:3})
(272)     [ALGB] (3) Real[3] pipe1.flowModel.mus = {pipe1.flowModel.mu_nominal for $i1 in 1:3} (start = {0.001 for $i1 in 1:3}, min = {0.0 for $i1 in 1:3}, max = {1e8 for $i1 in 1:3}, nominal = {0.001 for $i1 in 1:3})
(273)     [ALGB] (1) stream Real pipe3.port_a.h_outflow (start = 298609.6803431054, min = -1e10, max = 1e10, nominal = 1e5)
(274)     [DISC] (1) Boolean $SEV_29
(275)     [ALGB] (1) final Real[1] pipe2.heatTransfer.vs = pipe2.vs
(276)     [DISC] (1) Boolean $SEV_25
(277)     [ALGB] (2) final Real[2] pipe3.flowModel.vs = pipe3.vsFM
(278)     [DISC] (1) Boolean $SEV_21
(279)     [ALGB] (1) protected Real pipe1.flowModel.dp_fric_nominal = sum(ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.pipe1.flowModel.WallFriction.pressureLoss_m_flow(pipe1.flowModel.m_flow_nominal / pipe1.flowModel.nParallel, pipe1.flowModel.rho_nominal, pipe1.flowModel.rho_nominal, pipe1.flowModel.mu_nominal, pipe1.flowModel.mu_nominal, pipe1.flowModel.pathLengths_internal[$i1], pipe1.flowModel.diameters[$i1], ((pipe1.flowModel.crossAreas[2:3] + pipe1.flowModel.crossAreas[1:2]) / 2.0)[$i1], ((pipe1.flowModel.roughnesses[2:3] + pipe1.flowModel.roughnesses[1:2]) / 2.0)[$i1], pipe1.flowModel.m_flow_small / pipe1.flowModel.nParallel, pipe1.flowModel.Res_turbulent_internal[$i1]) for $i1 in 1:2) (min = 0.0, nominal = 1e5)
(280)     [DISC] (1) Boolean $SEV_20
(281)     [ALGB] (1) flow Real[1] sink.ports.m_flow (min = {-1e60}, max = {1e60})
(282)     [ALGB] (1) Real junctionIdeal.medium.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(283)     [ALGB] (1) Real valve2.x
(284)     [ALGB] (1) Real[1] pipe3.flowModel.Res_turbulent_internal = pipe3.flowModel.Re_turbulent * {1.0 for $i1 in 1:1}
(285)     [ALGB] (2) Real[2] pipe1.flowModel.Is
(286)     [ALGB] (1) Real valve2.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(287)     [ALGB] (1) Real[1] pipe3.mediums.p_bar = {Modelica.SIunits.Conversions.to_bar(pipe3.mediums[1].p)}
(288)     [ALGB] (1) stream Real[1] sink.ports.h_outflow (start = {298609.6803431054}, min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {1e5 for $i1 in 1:1})
(289)     [ALGB] (1) Real junctionIdeal.medium.p_bar = Modelica.SIunits.Conversions.to_bar(99999.99999999999 * junctionIdeal.medium.p_bar)
(290)     [DISC] (2) Boolean[2] $SEV_48[$i1]
(291)     [ALGB] (1) Real[1] pipe3.flowModel.Fs_fg
(292)     [DISC] (1) Boolean $SEV_19
(293)     [DISC] (1) Boolean $SEV_15
(294)     [ALGB] (2) Real[2] pipe1.flowModel.dps_fg (start = {(pipe1.flowModel.p_a_start - pipe1.flowModel.p_b_start) / 2.0 for $i1 in 1:2})
(295)     [DISC] (1) Boolean $SEV_14
(296)     [DISC] (1) Boolean $SEV_13
(297)     [ALGB] (1) Real valveOpening2.y
(298)     [ALGB] (1) Real valve2.Y
(299)     [ALGB] (1) Real valve1.port_b_T = Modelica.Fluid.Utilities.regStep(-valve1.m_flow, ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve1.Medium.temperature(valve1.state_b), ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve1.Medium.temperature(ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve1.Medium.setState_phX(99999.99999999999 * junctionVolume.medium.p_bar, valve1.port_b.h_outflow, {})), valve1.m_flow_small) (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(300)     [ALGB] (1) stream Real[1] source.ports.h_outflow (start = {298609.6803431054}, min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {1e5 for $i1 in 1:1})
(301)     [ALGB] (3) protected Real[3] pipe1.dimensionsFM
(302)     [ALGB] (3) protected Real[3] pipe1.crossAreasFM
(303)     [ALGB] (1) Real valve1.dp_turbulent = max(valve1.dp_small, ((ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve1.Medium.dynamicViscosity(valve1.state_a) + ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve1.Medium.dynamicViscosity(valve1.state_b)) ^ 2.0 * 3.141592653589793 * 1.6e7) / (8.0 * valve1.Y * max(ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve1.valveCharacteristic(valveOpening1.y), 0.001) * valve1.Av * (ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve1.Medium.density(valve1.state_b) + ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve1.Medium.density(valve1.state_a)))) (min = 0.0, nominal = 1e5)
(304)     [ALGB] (1) flow Real[1] pipe1.heatTransfer.heatPorts.Q_flow
(305)     [ALGB] (1) Real[1] pipe2.flowModel.Fs_p
(306)     [ALGB] (2) Real[2] pipe1.flowModel.Fs_p
(307)     [ALGB] (1) Real valve1.x
(308)     [ALGB] (1) Real[1] pipe3.heatTransfer.heatPorts.T (start = {288.15 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, nominal = {300.0 for $i1 in 1:1})
(309)     [ALGB] (1) final Real[1] pipe2.flowModel.pathLengths = pipe2.pathLengths
(310)     [DISC] (1) protected Real valveOpening2.b
(311)     [DISC] (1) protected Real valveOpening2.a
(312)     [ALGB] (1) Real[1] pipe2.mediums.p_bar = {Modelica.SIunits.Conversions.to_bar(pipe2.mediums[1].p)}
(313)     [ALGB] (2) Real[2] pipe2.flowModel.rhos = {ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.pipe2.flowModel.Medium.density(pipe2.flowModel.states[$i1]) for $i1 in 1:2} (start = {10.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {10.0 for $i1 in 1:2})
(314)     [ALGB] (3) Real[3] pipe1.flowModel.rhos = {ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.pipe1.flowModel.Medium.density(pipe1.flowModel.states[$i1]) for $i1 in 1:3} (start = {10.0 for $i1 in 1:3}, min = {0.0 for $i1 in 1:3}, max = {1e5 for $i1 in 1:3}, nominal = {10.0 for $i1 in 1:3})
(315)     [ALGB] (1) Real valve1.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(316)     [ALGB] (1) Real[1] pipe2.mediums.u (min = {-1e8 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(317)     [ALGB] (1) protected Real pipe2.flowModel.dp_fric_nominal = sum({ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.pipe2.flowModel.WallFriction.pressureLoss_m_flow(pipe2.flowModel.m_flow_nominal / pipe2.flowModel.nParallel, pipe2.flowModel.rho_nominal, pipe2.flowModel.rho_nominal, pipe2.flowModel.mu_nominal, pipe2.flowModel.mu_nominal, pipe2.flowModel.pathLengths_internal[1], pipe2.flowModel.diameters[1], ((pipe2.flowModel.crossAreas[2:2] + pipe2.flowModel.crossAreas[1:1]) / 2.0)[1], ((pipe2.flowModel.roughnesses[2:2] + pipe2.flowModel.roughnesses[1:1]) / 2.0)[1], pipe2.flowModel.m_flow_small / pipe2.flowModel.nParallel, pipe2.flowModel.Res_turbulent_internal[1])}) (min = 0.0, nominal = 1e5)
(318)     [ALGB] (1) final input Real[1, 1] pipe1.heatTransfer.states.p = {pipe1.mediums[1].state.p} (start = {1e6 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(319)     [ALGB] (1) Real[1] source.ports.p (start = {1e6 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1})
(320)     [ALGB] (1) Real[1] pipe2.mediums.p (start = {pipe2.ps_start[1]}, min = {0.0 for $i1 in 1:1}, nominal = {1e5 for $i1 in 1:1}, StateSelect = prefer)
(321)     [ALGB] (1) protected Real[1] pipe3.flowModel.diameters = 0.5 * (pipe3.flowModel.dimensions[2:2] + pipe3.flowModel.dimensions[1:1])
(322)     [ALGB] (2) Real[2] pipe3.flowModel.mus = {pipe3.flowModel.mu_nominal 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})
(323)     [ALGB] (1) Real valve2.m_flow (start = valve2.m_flow_start, min = -1e60, max = 1e5)
(324)     [ALGB] (1) flow Real[1] pipe2.heatTransfer.heatPorts.Q_flow
(325)     [ALGB] (1) Real[1] pipe2.mediums.h (start = {pipe2.h_start})
(326)     [ALGB] (1) protected Real valve2.minLimiter.y
(327)     [ALGB] (1) Real[1] pipe2.mediums.d (start = {10.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {10.0 for $i1 in 1:1})
(328)     [ALGB] (1) Real[1] pipe3.Wb_flows
(329)     [ALGB] (1) Real valveOpening1.y
(330)     [ALGB] (2) final Real[2] pipe1.flowModel.pathLengths = pipe1.pathLengths
(331)     [ALGB] (1) Real[1] pipe1.mediums.p_bar = {Modelica.SIunits.Conversions.to_bar(pipe1.mediums[1].p)}
(332)     [ALGB] (1) Real pipe2.state_b.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(333)     [ALGB] (1) Real valve1.Y
(334)     [ALGB] (3) final Real[3] pipe1.flowModel.vs = pipe1.vsFM
(335)     [ALGB] (2) Real[2] pipe1.flowModel.pathLengths_internal = pipe1.flowModel.pathLengths
(336)     [ALGB] (1) Real valve1.port_a_T = Modelica.Fluid.Utilities.regStep(valve1.m_flow, ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve1.Medium.temperature(valve1.state_a), ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve1.Medium.temperature(ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve1.Medium.setState_phX(pipe2.port_b.p, junctionVolume.port_3.h_outflow, {})), valve1.m_flow_small) (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(337)     [ALGB] (1) stream Real valve1.port_b.h_outflow (start = 298609.6803431054, min = -1e10, max = 1e10, nominal = 1e5)
(338)     [ALGB] (1) final input Real[1, 1] pipe1.heatTransfer.states.T = {pipe1.mediums[1].state.T} (start = {500.0 for $i1 in 1:1}, min = {200.0 for $i1 in 1:1}, max = {6000.0 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1})


System Equations (328/420)
****************************
(1)       [SCAL] (1) pipe1.port_b.m_flow = -pipe1.m_flows[2] ($RES_SIM_254)
(2)       [SCAL] (1) $SEV_51[1] = pipe1.mediums[1].T >= 200.0 and pipe1.mediums[1].T <= 6000.0 ($RES_EVT_550)
(3)       [SCAL] (1) pipe1.port_a.m_flow = pipe1.m_flows[1] ($RES_SIM_255)
(4)       [ARRY] (2) pipe2.flowModel.vs = pipe2.vsFM ($RES_BND_380)
(5)       [SCAL] (1) pipe1.H_flows[2] = -$FUN_4 ($RES_SIM_256)
(6)       [ARRY] (2) pipe2.flowModel.crossAreas = pipe2.crossAreasFM ($RES_BND_381)
(7)       [SCAL] (1) pipe1.H_flows[1] = $FUN_3 ($RES_SIM_257)
(8)       [ARRY] (2) pipe2.flowModel.dimensions = pipe2.dimensionsFM ($RES_BND_382)
(9)       [SCAL] (1) pipe1.mb_flows[1] = pipe1.m_flows[1] - pipe1.m_flows[2] ($RES_SIM_258)
(10)      [ARRY] (2) pipe2.flowModel.roughnesses = pipe2.roughnessesFM ($RES_BND_383)
(11)      [SCAL] (1) $SEV_55 = (-valve2.m_flow) > valve2.m_flow_small ($RES_EVT_554)
(12)      [SCAL] (1) pipe1.Hb_flows[1] = pipe1.H_flows[1] - pipe1.H_flows[2] ($RES_SIM_259)
(13)      [ARRY] (1) pipe2.flowModel.dheights = pipe2.dheightsFM ($RES_BND_384)
(14)      [SCAL] (1) $SEV_56 = (-valve2.m_flow) < (-valve2.m_flow_small) ($RES_EVT_555)
(15)      [ARRY] (1) pipe2.flowModel.pathLengths = pipe2.pathLengths ($RES_BND_385)
(16)      [SCAL] (1) $SEV_57 = valve2.m_flow_small > 0.0 ($RES_EVT_556)
(17)      [FOR-] (2) ($RES_BND_386)
(17)      [----] for $i1 in 1:2 loop
(17)      [----]   [SCAL] (1) pipe2.flowModel.rhos[$i1] = (0.0034836987724536205 * pipe2.flowModel.states.T) / pipe2.flowModel.states.p ($RES_BND_387)
(17)      [----] end for;
(18)      [SCAL] (1) $SEV_58 = valve2.m_flow > valve2.m_flow_small ($RES_EVT_557)
(19)      [SCAL] (1) $SEV_59 = valve2.m_flow < (-valve2.m_flow_small) ($RES_EVT_558)
(20)      [FOR-] (2) ($RES_BND_388)
(20)      [----] for $i1 in 1:2 loop
(20)      [----]   [SCAL] (1) pipe2.flowModel.mus[$i1] = pipe2.flowModel.mu_nominal ($RES_BND_389)
(20)      [----] end for;
(21)      [SCAL] (1) $SEV_60 = (-valve1.m_flow) > valve1.m_flow_small ($RES_EVT_559)
(22)      [ARRY] (1) pipe2.flowModel.Is = {pipe2.flowModel.m_flows[1] * pipe2.flowModel.pathLengths[1]} ($RES_SIM_170)
(23)      [ARRY] (1) pipe2.flowModel.dps_fg = {(2.0 * (pipe2.flowModel.Fs_fg[1] / pipe2.flowModel.nParallel)) / (pipe2.flowModel.crossAreas[1] + pipe2.flowModel.crossAreas[2])} ($RES_SIM_171)
(24)      [ARRY] (1) pipe2.flowModel.Fs_p = pipe2.flowModel.nParallel * {0.5 * (pipe2.flowModel.crossAreas[1] + pipe2.flowModel.crossAreas[2]) * (pipe2.flowModel.states.T - pipe2.flowModel.states.T)} ($RES_SIM_172)
(25)      [ARRY] (1) pipe2.flowModel.Ib_flows = {0.0} ($RES_SIM_173)
(26)      [SCAL] (1) pipe2.flowModel.rhos_act[1] = noEvent(if $SEV_29 then pipe2.flowModel.rhos[1] else pipe2.flowModel.rhos[2]) ($RES_SIM_174)
(27)      [SCAL] (1) pipe2.flowModel.mus_act[1] = noEvent(if $SEV_29 then pipe2.flowModel.mus[1] else pipe2.flowModel.mus[2]) ($RES_SIM_175)
(28)      [ARRY] (1) pipe2.flowModel.m_flows = {homotopy(({$FUN_7} .* pipe2.flowModel.nParallel)[1], (pipe2.flowModel.m_flow_nominal / pipe2.flowModel.dp_nominal * (pipe2.flowModel.dps_fg - (pipe2.flowModel.g * pipe2.flowModel.dheights) .* pipe2.flowModel.rho_nominal))[1])} ($RES_SIM_176)
(29)      [ARRY] (3) pipe1.roughnessesFM[:] = {pipe1.roughnesses[1], pipe1.roughnesses[1], pipe1.roughnesses[1]} ($RES_SIM_260)
(30)      [ARRY] (3) pipe1.dimensionsFM[:] = {pipe1.dimensions[1], pipe1.dimensions[1], pipe1.dimensions[1]} ($RES_SIM_261)
(31)      [ARRY] (3) pipe1.crossAreasFM[:] = {pipe1.crossAreas[1], pipe1.crossAreas[1], pipe1.crossAreas[1]} ($RES_SIM_262)
(32)      [ARRY] (2) pipe1.dheightsFM[:] = {0.0, 0.0} ($RES_SIM_263)
(33)      [ARRY] (2) pipe1.pathLengths[:] = {5.0, 5.0} ($RES_SIM_264)
(34)      [SCAL] (1) $SEV_61 = (-valve1.m_flow) < (-valve1.m_flow_small) ($RES_EVT_560)
(35)      [ARRY] (1) pipe1.Wb_flows = (pipe1.crossAreas * pipe1.vs * (($FUN_2 + 99999.99999999999 * junctionIdeal.medium.p_bar) - ((system.g * {0.0}) / pipe1.mediums.d + pipe1.port_a.p))) / ({1.0} * {1.0}) .* {1.0} .* pipe1.nParallel ($RES_SIM_265)
(36)      [ARRY] (1) pipe2.flowModel.pathLengths_internal = pipe2.flowModel.pathLengths ($RES_BND_390)
(37)      [SCAL] (1) $SEV_62 = valve1.m_flow_small > 0.0 ($RES_EVT_561)
(38)      [ARRY] (1) pipe1.Qb_flows = pipe1.heatTransfer.Q_flows ($RES_SIM_266)
(39)      [SCAL] (1) pipe2.flowModel.Res_turbulent_internal[1] = pipe2.flowModel.Re_turbulent ($RES_BND_391)
(40)      [SCAL] (1) $SEV_63 = valve1.m_flow > valve1.m_flow_small ($RES_EVT_562)
(41)      [ARRY] (1) pipe1.heatTransfer.Q_flows = pipe1.heatTransfer.heatPorts.Q_flow ($RES_SIM_267)
(42)      [ARRY] (1) pipe2.flowModel.diameters = 0.5 * (pipe2.flowModel.dimensions[2:2] + pipe2.flowModel.dimensions[1:1]) ($RES_BND_392)
(43)      [SCAL] (1) $SEV_64 = valve1.m_flow < (-valve1.m_flow_small) ($RES_EVT_563)
(44)      [ARRY] (1) pipe1.heatTransfer.Ts = pipe1.heatTransfer.heatPorts.T ($RES_SIM_268)
(45)      [ARRY] (2) {0.0 for $i1 in 1:2} = pipe1.flowModel.Ib_flows - (pipe1.flowModel.Fs_fg + pipe1.flowModel.Fs_p) ($RES_SIM_269)
(46)      [ARRY] (1) pipe2.vs = {(0.5 * (pipe2.m_flows[2] + pipe2.m_flows[1])) / (pipe2.crossAreas[1] * pipe2.mediums[1].d)} / pipe2.nParallel ($RES_BND_394)
(47)      [ARRY] (1) pipe2.heatTransfer.Ts = {pipe2.heatTransfer.states.p} ($RES_BND_396)
(48)      [ARRY] (1) pipe2.heatTransfer.vs = pipe2.vs ($RES_BND_397)
(49)      [ARRY] (1) pipe2.mediums.state.p = pipe2.mediums.p ($RES_SIM_182)
(50)      [ARRY] (1) pipe2.mediums.state.T = pipe2.mediums.T ($RES_SIM_183)
(51)      [SCAL] (1) pipe2.mediums[1].d = pipe2.mediums[1].p / (pipe2.mediums[1].T * pipe2.mediums[1].R) ($RES_SIM_184)
(52)      [SCAL] (1) pipe2.mediums[1].u = pipe2.mediums[1].h - pipe2.mediums[1].R * pipe2.mediums[1].T ($RES_SIM_185)
(53)      [SCAL] (1) pipe2.mediums[1].h = Modelica.Media.IdealGases.Common.Functions.h_T(Modelica.Media.IdealGases.Common.DataRecord("Air", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), pipe2.mediums[1].T, true, Modelica.Media.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_SIM_186)
(54)      [ARRY] (1) pipe2.mediums.R = {287.0512249529787} ($RES_SIM_187)
(55)      [ARRY] (2) pipe1.flowModel.Is = {pipe1.flowModel.m_flows[i] * pipe1.flowModel.pathLengths[i] for i in 1:2} ($RES_SIM_270)
(56)      [ARRY] (2) pipe1.flowModel.dps_fg = {pipe1.flowModel.Fs_fg[i] / pipe1.flowModel.nParallel * 2.0 / (pipe1.flowModel.crossAreas[i] + pipe1.flowModel.crossAreas[i + 1]) for i in 1:2} ($RES_SIM_271)
(57)      [ARRY] (2) pipe1.flowModel.Fs_p = pipe1.flowModel.nParallel * {0.0 for i in 1:2} ($RES_SIM_272)
(58)      [ARRY] (2) pipe1.flowModel.Ib_flows = {0.0 for $i1 in 1:2} ($RES_SIM_273)
(59)      [FOR-] (2) ($RES_SIM_274)
(59)      [----] for $i1 in 1:2 loop
(59)      [----]   [SCAL] (1) pipe1.flowModel.rhos_act[$i1] = noEvent(if $SEV_48[$i1] then pipe1.flowModel.rhos[$i1] else pipe1.flowModel.rhos[$i1 + 1]) ($RES_SIM_275)
(59)      [----] end for;
(60)      [FOR-] (2) ($RES_SIM_276)
(60)      [----] for $i1 in 1:2 loop
(60)      [----]   [SCAL] (1) pipe1.flowModel.mus_act[$i1] = noEvent(if $SEV_48[$i1] then pipe1.flowModel.mus[$i1] else pipe1.flowModel.mus[$i1 + 1]) ($RES_SIM_277)
(60)      [----] end for;
(61)      [ARRY] (2) pipe1.flowModel.m_flows = {homotopy(({$FUN_1 for $i1 in 1:2} .* pipe1.flowModel.nParallel)[$i1], (pipe1.flowModel.m_flow_nominal / pipe1.flowModel.dp_nominal * (pipe1.flowModel.dps_fg - pipe1.flowModel.g * pipe1.flowModel.dheights .* pipe1.flowModel.rho_nominal))[$i1]) for $i1 in 1:2} ($RES_SIM_278)
(62)      [SCAL] (1) sink.ports[1].p = sink.p ($RES_SIM_191)
(63)      [SCAL] (1) sink.ports[1].h_outflow = sink.medium.h ($RES_SIM_192)
(64)      [ARRY] (1) pipe1.mediums.state.p = pipe1.mediums.p ($RES_SIM_284)
(65)      [ARRY] (1) pipe1.mediums.state.T = pipe1.mediums.T ($RES_SIM_285)
(66)      [SCAL] (1) pipe1.mediums[1].d = pipe1.mediums[1].p / (pipe1.mediums[1].T * pipe1.mediums[1].R) ($RES_SIM_286)
(67)      [SCAL] (1) pipe1.mediums[1].u = pipe1.mediums[1].h - pipe1.mediums[1].R * pipe1.mediums[1].T ($RES_SIM_287)
(68)      [SCAL] (1) pipe1.mediums[1].h = Modelica.Media.IdealGases.Common.Functions.h_T(Modelica.Media.IdealGases.Common.DataRecord("Air", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), pipe1.mediums[1].T, true, Modelica.Media.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_SIM_288)
(69)      [ARRY] (1) pipe1.mediums.R = {287.0512249529787} ($RES_SIM_289)
(70)      [SCAL] (1) pipe1.state_a.p = pipe1.port_a.p ($RES_SIM_466)
(71)      [SCAL] (1) pipe1.state_a.T = ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.pipe1.Medium.T_h.Internal.solve(source.ports[1].h_outflow, 200.0, 6000.0, 1e5, {1.0}, Modelica.Media.IdealGases.Common.DataRecord("Air", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), 1e-13) ($RES_SIM_467)
(72)      [SCAL] (1) source.ports[1].p = source.p ($RES_SIM_293)
(73)      [SCAL] (1) pipe1.state_b.p = 99999.99999999999 * junctionIdeal.medium.p_bar ($RES_SIM_468)
(74)      [SCAL] (1) source.ports[1].h_outflow = source.medium.h ($RES_SIM_294)
(75)      [SCAL] (1) pipe1.state_b.T = ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.pipe1.Medium.T_h.Internal.solve(junctionIdeal.port_3.h_outflow, 200.0, 6000.0, 1e5, {1.0}, Modelica.Media.IdealGases.Common.DataRecord("Air", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), 1e-13) ($RES_SIM_469)
(76)      [SCAL] (1) valve1.state_a.p = pipe2.port_b.p ($RES_SIM_470)
(77)      [SCAL] (1) valve1.state_a.T = ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve1.Medium.T_h.Internal.solve(valve1.port_b.h_outflow, 200.0, 6000.0, 1e5, {1.0}, Modelica.Media.IdealGases.Common.DataRecord("Air", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), 1e-13) ($RES_SIM_471)
(78)      [SCAL] (1) valve1.state_b.p = 99999.99999999999 * junctionVolume.medium.p_bar ($RES_SIM_472)
(79)      [SCAL] (1) valve1.state_b.T = ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve1.Medium.T_h.Internal.solve(junctionVolume.port_3.h_outflow, 200.0, 6000.0, 1e5, {1.0}, Modelica.Media.IdealGases.Common.DataRecord("Air", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), 1e-13) ($RES_SIM_473)
(80)      [SCAL] (1) valve2.state_a.p = pipe3.port_b.p ($RES_SIM_474)
(81)      [SCAL] (1) valve2.state_a.T = ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve2.Medium.T_h.Internal.solve(valve2.port_b.h_outflow, 200.0, 6000.0, 1e5, {1.0}, Modelica.Media.IdealGases.Common.DataRecord("Air", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), 1e-13) ($RES_SIM_475)
(82)      [SCAL] (1) valve2.state_b.p = 99999.99999999999 * junctionVolume.medium.p_bar ($RES_SIM_476)
(83)      [SCAL] (1) valve2.state_b.T = ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve2.Medium.T_h.Internal.solve(junctionVolume.port_3.h_outflow, 200.0, 6000.0, 1e5, {1.0}, Modelica.Media.IdealGases.Common.DataRecord("Air", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), 1e-13) ($RES_SIM_477)
(84)      [SCAL] (1) pipe2.state_a.p = 99999.99999999999 * junctionIdeal.medium.p_bar ($RES_SIM_478)
(85)      [SCAL] (1) pipe2.state_a.T = ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.pipe2.Medium.T_h.Internal.solve(junctionIdeal.port_3.h_outflow, 200.0, 6000.0, 1e5, {1.0}, Modelica.Media.IdealGases.Common.DataRecord("Air", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), 1e-13) ($RES_SIM_479)
(86)      [SCAL] (1) pipe2.state_b.p = pipe2.port_b.p ($RES_SIM_480)
(87)      [SCAL] (1) pipe2.state_b.T = ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.pipe2.Medium.T_h.Internal.solve(junctionVolume.port_3.h_outflow, 200.0, 6000.0, 1e5, {1.0}, Modelica.Media.IdealGases.Common.DataRecord("Air", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), 1e-13) ($RES_SIM_481)
(88)      [SCAL] (1) pipe3.state_a.p = 99999.99999999999 * junctionIdeal.medium.p_bar ($RES_SIM_482)
(89)      [SCAL] (1) pipe3.state_a.T = ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.pipe3.Medium.T_h.Internal.solve(junctionIdeal.port_3.h_outflow, 200.0, 6000.0, 1e5, {1.0}, Modelica.Media.IdealGases.Common.DataRecord("Air", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), 1e-13) ($RES_SIM_483)
(90)      [SCAL] (1) pipe3.state_b.p = pipe3.port_b.p ($RES_SIM_484)
(91)      [SCAL] (1) pipe3.state_b.T = ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.pipe3.Medium.T_h.Internal.solve(junctionVolume.port_3.h_outflow, 200.0, 6000.0, 1e5, {1.0}, Modelica.Media.IdealGases.Common.DataRecord("Air", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), 1e-13) ($RES_SIM_485)
(92)      [ALGO] (5) ($RES_SIM_31)
(92)      [----] assert(not (valveOpening2.table[1, 1] > 0.0 or valveOpening2.table[1, 1] < 0.0), "The first point in time has to be set to 0, but is table[1,1] = " + String(valveOpening2.table[1, 1], 6, 0, true), AssertionLevel.error);

(92)      [----] when {time >= $PRE.valveOpening2.nextEvent, initial()} then
(92)      [----]   (valveOpening2.a, valveOpening2.b, valveOpening2.nextEventScaled, valveOpening2.last) := ($FUN_19, $FUN_20, $FUN_21, $FUN_22);
(92)      [----]   valveOpening2.nextEvent := valveOpening2.nextEventScaled;
(92)      [----] end when;

(93)      [ALGO] (5) ($RES_SIM_32)
(93)      [----] assert(not (valveOpening1.table[1, 1] > 0.0 or valveOpening1.table[1, 1] < 0.0), "The first point in time has to be set to 0, but is table[1,1] = " + String(valveOpening1.table[1, 1], 6, 0, true), AssertionLevel.error);

(93)      [----] when {time >= $PRE.valveOpening1.nextEvent, initial()} then
(93)      [----]   (valveOpening1.a, valveOpening1.b, valveOpening1.nextEventScaled, valveOpening1.last) := ($FUN_15, $FUN_16, $FUN_17, $FUN_18);
(93)      [----]   valveOpening1.nextEvent := valveOpening1.nextEventScaled;
(93)      [----] end when;

(94)      [SCAL] (1) $DER.junctionVolume.m = junctionVolume.mb_flow ($RES_SIM_33)
(95)      [SCAL] (1) $DER.junctionVolume.U = junctionVolume.Hb_flow ($RES_SIM_34)
(96)      [SCAL] (1) junctionVolume.U = junctionVolume.m * junctionVolume.medium.u ($RES_SIM_35)
(97)      [SCAL] (1) junctionVolume.m = junctionVolume.V * junctionVolume.medium.d ($RES_SIM_36)
(98)      [SCAL] (1) junctionVolume.Hb_flow = smooth(0, valve1.m_flow * (if $SEV_13 then valve1.port_b.h_outflow else junctionVolume.port_3.h_outflow)) + smooth(0, valve2.m_flow * (if $SEV_14 then valve2.port_b.h_outflow else junctionVolume.port_3.h_outflow)) + smooth(0, junctionVolume.port_3.m_flow * (if $SEV_15 then sink.ports[1].h_outflow else junctionVolume.port_3.h_outflow)) ($RES_SIM_39)
(99)      [SCAL] (1) junctionVolume.mb_flow = valve1.m_flow + valve2.m_flow + junctionVolume.port_3.m_flow ($RES_SIM_43)
(100)     [SCAL] (1) junctionVolume.medium.state.p = 99999.99999999999 * junctionVolume.medium.p_bar ($RES_SIM_51)
(101)     [SCAL] (1) junctionVolume.medium.state.T = -((-273.15) - junctionVolume.medium.T_degC) ($RES_SIM_52)
(102)     [SCAL] (1) junctionVolume.medium.d = -(0.0034836987724536205 * (99999.99999999999 * junctionVolume.medium.p_bar)) / ((-273.15) - junctionVolume.medium.T_degC) ($RES_SIM_53)
(103)     [SCAL] (1) junctionVolume.medium.u = 287.0512249529787 * ((-273.15) - junctionVolume.medium.T_degC) + junctionVolume.port_3.h_outflow ($RES_SIM_54)
(104)     [SCAL] (1) junctionVolume.port_3.h_outflow = Modelica.Media.IdealGases.Common.Functions.h_T(Modelica.Media.IdealGases.Common.DataRecord("Air", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), -((-273.15) - junctionVolume.medium.T_degC), true, Modelica.Media.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_SIM_55)
(105)     [SCAL] (1) $DER.junctionIdeal.m = junctionIdeal.mb_flow ($RES_SIM_59)
(106)     [ARRY] (1) pipe3.fluidVolumes = {10.0 * pipe3.crossAreas[1]} .* pipe3.nParallel ($RES_BND_401)
(107)     [SCAL] (1) valve2.port_b.h_outflow = pipe3.mediums[1].h ($RES_SIM_101)
(108)     [ARRY] (1) pipe3.mediums.p_bar = {1e-5 * pipe3.mediums[1].p} ($RES_BND_402)
(109)     [SCAL] (1) pipe3.port_a.h_outflow = pipe3.mediums[1].h ($RES_SIM_102)
(110)     [ARRY] (1) pipe3.mediums.T_degC = {(-273.15) + pipe3.mediums[1].T} ($RES_BND_403)
(111)     [SCAL] (1) -valve2.m_flow = -pipe3.m_flows[2] ($RES_SIM_103)
(112)     [ARRY] (2) pipe3.flowModel.vs = pipe3.vsFM ($RES_BND_404)
(113)     [SCAL] (1) pipe3.port_a.m_flow = pipe3.m_flows[1] ($RES_SIM_104)
(114)     [ARRY] (2) pipe3.flowModel.crossAreas = pipe3.crossAreasFM ($RES_BND_405)
(115)     [SCAL] (1) pipe3.H_flows[2] = -$FUN_14 ($RES_SIM_105)
(116)     [ARRY] (2) pipe3.flowModel.dimensions = pipe3.dimensionsFM ($RES_BND_406)
(117)     [SCAL] (1) pipe3.H_flows[1] = $FUN_13 ($RES_SIM_106)
(118)     [ARRY] (2) pipe3.flowModel.roughnesses = pipe3.roughnessesFM ($RES_BND_407)
(119)     [SCAL] (1) pipe3.mb_flows[1] = pipe3.m_flows[1] - pipe3.m_flows[2] ($RES_SIM_107)
(120)     [ARRY] (1) pipe3.flowModel.dheights = pipe3.dheightsFM ($RES_BND_408)
(121)     [SCAL] (1) pipe3.Hb_flows[1] = pipe3.H_flows[1] - pipe3.H_flows[2] ($RES_SIM_108)
(122)     [ARRY] (1) pipe3.flowModel.pathLengths = pipe3.pathLengths ($RES_BND_409)
(123)     [ARRY] (2) pipe3.roughnessesFM[:] = {pipe3.roughnesses[1], pipe3.roughnesses[1]} ($RES_SIM_109)
(124)     [SCAL] (1) $DER.junctionIdeal.U = junctionIdeal.Hb_flow ($RES_SIM_60)
(125)     [SCAL] (1) junctionIdeal.U = junctionIdeal.m * junctionIdeal.medium.u ($RES_SIM_61)
(126)     [SCAL] (1) junctionIdeal.m = junctionIdeal.V * junctionIdeal.medium.d ($RES_SIM_62)
(127)     [SCAL] (1) junctionIdeal.Hb_flow = smooth(0, -pipe2.port_a.m_flow * (if $SEV_19 then pipe2.port_a.h_outflow else junctionIdeal.port_3.h_outflow)) + smooth(0, -pipe3.port_a.m_flow * (if $SEV_20 then pipe3.port_a.h_outflow else junctionIdeal.port_3.h_outflow)) + smooth(0, -pipe1.port_b.m_flow * (if $SEV_21 then pipe1.port_b.h_outflow else junctionIdeal.port_3.h_outflow)) ($RES_SIM_65)
(128)     [SCAL] (1) junctionIdeal.mb_flow = -(pipe2.port_a.m_flow + pipe3.port_a.m_flow + pipe1.port_b.m_flow) ($RES_SIM_69)
(129)     [FOR-] (2) ($RES_BND_410)
(129)     [----] for $i1 in 1:2 loop
(129)     [----]   [SCAL] (1) pipe3.flowModel.rhos[$i1] = (0.0034836987724536205 * pipe3.flowModel.states.T) / pipe3.flowModel.states.p ($RES_BND_411)
(129)     [----] end for;
(130)     [ARRY] (2) pipe3.dimensionsFM[:] = {pipe3.dimensions[1], pipe3.dimensions[1]} ($RES_SIM_110)
(131)     [ARRY] (2) pipe3.crossAreasFM[:] = {pipe3.crossAreas[1], pipe3.crossAreas[1]} ($RES_SIM_111)
(132)     [FOR-] (2) ($RES_BND_412)
(132)     [----] for $i1 in 1:2 loop
(132)     [----]   [SCAL] (1) pipe3.flowModel.mus[$i1] = pipe3.flowModel.mu_nominal ($RES_BND_413)
(132)     [----] end for;
(133)     [ARRY] (1) pipe3.dheightsFM[:] = {0.0} ($RES_SIM_112)
(134)     [ARRY] (1) pipe3.pathLengths[:] = {10.0} ($RES_SIM_113)
(135)     [ARRY] (1) pipe3.flowModel.pathLengths_internal = pipe3.flowModel.pathLengths ($RES_BND_414)
(136)     [ARRY] (1) pipe3.Wb_flows = (pipe3.crossAreas * pipe3.vs * (($FUN_12 + pipe3.port_b.p) - ((system.g * {0.0}) / pipe3.mediums.d + 99999.99999999999 * junctionIdeal.medium.p_bar))) / ({1.0} * {1.0}) .* {1.0} .* pipe3.nParallel ($RES_SIM_114)
(137)     [SCAL] (1) pipe3.flowModel.Res_turbulent_internal[1] = pipe3.flowModel.Re_turbulent ($RES_BND_415)
(138)     [ARRY] (1) pipe3.Qb_flows = pipe3.heatTransfer.Q_flows ($RES_SIM_115)
(139)     [ARRY] (1) pipe3.flowModel.diameters = 0.5 * (pipe3.flowModel.dimensions[2:2] + pipe3.flowModel.dimensions[1:1]) ($RES_BND_416)
(140)     [ARRY] (1) pipe3.heatTransfer.Q_flows = pipe3.heatTransfer.heatPorts.Q_flow ($RES_SIM_116)
(141)     [ARRY] (1) pipe3.heatTransfer.Ts = pipe3.heatTransfer.heatPorts.T ($RES_SIM_117)
(142)     [ARRY] (1) pipe3.vs = {(0.5 * (pipe3.m_flows[2] + pipe3.m_flows[1])) / (pipe3.crossAreas[1] * pipe3.mediums[1].d)} / pipe3.nParallel ($RES_BND_418)
(143)     [ARRY] (1) {0.0} = pipe3.flowModel.Ib_flows - (pipe3.flowModel.Fs_fg + pipe3.flowModel.Fs_p) ($RES_SIM_118)
(144)     [ARRY] (1) pipe3.flowModel.Is = {pipe3.flowModel.m_flows[1] * pipe3.flowModel.pathLengths[1]} ($RES_SIM_119)
(145)     [SCAL] (1) junctionIdeal.medium.state.p = 99999.99999999999 * junctionIdeal.medium.p_bar ($RES_SIM_77)
(146)     [SCAL] (1) $TEV_0 = $PRE.valveOpening2.nextEvent ($RES_EVT_501)
(147)     [SCAL] (1) junctionIdeal.medium.state.T = -((-273.15) - junctionIdeal.medium.T_degC) ($RES_SIM_78)
(148)     [SCAL] (1) sink.medium.u = sink.medium.h - 287.0512249529787 * sink.T ($RES_SIM_206)
(149)     [SCAL] (1) $TEV_1 = $PRE.valveOpening1.nextEvent ($RES_EVT_502)
(150)     [SCAL] (1) junctionIdeal.medium.d = -(0.0034836987724536205 * (99999.99999999999 * junctionIdeal.medium.p_bar)) / ((-273.15) - junctionIdeal.medium.T_degC) ($RES_SIM_79)
(151)     [SCAL] (1) sink.medium.h = Modelica.Media.IdealGases.Common.Functions.h_T(Modelica.Media.IdealGases.Common.DataRecord("Air", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), sink.T, true, Modelica.Media.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_SIM_207)
(152)     [FOR-] (2) ($RES_EVT_503)
(152)     [----] for $i1 in 1:2 loop
(152)     [----]   [SCAL] (1) $SEV_0[$i1] = abs(pipe3.flowModel.crossAreas[$i1] - 0.7853981633974483 * pipe3.flowModel.dimensions[$i1] ^ 2.0) < 1e-10 * pipe3.flowModel.crossAreas[$i1] ($RES_EVT_504)
(152)     [----] end for;
(153)     [FOR-] (2) ($RES_EVT_505)
(153)     [----] for $i1 in 1:2 loop
(153)     [----]   [SCAL] (1) $SEV_1[$i1] = abs(pipe2.flowModel.crossAreas[$i1] - 0.7853981633974483 * pipe2.flowModel.dimensions[$i1] ^ 2.0) < 1e-10 * pipe2.flowModel.crossAreas[$i1] ($RES_EVT_506)
(153)     [----] end for;
(154)     [FOR-] (3) ($RES_EVT_509)
(154)     [----] for $i1 in 1:3 loop
(154)     [----]   [SCAL] (1) $SEV_4[$i1] = abs(pipe1.flowModel.crossAreas[$i1] - 0.7853981633974483 * pipe1.flowModel.dimensions[$i1] ^ 2.0) < 1e-10 * pipe1.flowModel.crossAreas[$i1] ($RES_EVT_510)
(154)     [----] end for;
(155)     [ARRY] (1) pipe3.heatTransfer.Ts = {pipe3.heatTransfer.states.p} ($RES_BND_420)
(156)     [ARRY] (1) pipe3.flowModel.dps_fg = {(2.0 * (pipe3.flowModel.Fs_fg[1] / pipe3.flowModel.nParallel)) / (pipe3.flowModel.crossAreas[1] + pipe3.flowModel.crossAreas[2])} ($RES_SIM_120)
(157)     [ARRY] (1) pipe3.heatTransfer.vs = pipe3.vs ($RES_BND_421)
(158)     [ARRY] (1) pipe3.flowModel.Fs_p = pipe3.flowModel.nParallel * {0.5 * (pipe3.flowModel.crossAreas[1] + pipe3.flowModel.crossAreas[2]) * (pipe3.flowModel.states.T - pipe3.flowModel.states.T)} ($RES_SIM_121)
(159)     [ARRY] (1) pipe3.flowModel.Ib_flows = {0.0} ($RES_SIM_122)
(160)     [SCAL] (1) pipe3.flowModel.rhos_act[1] = noEvent(if $SEV_25 then pipe3.flowModel.rhos[1] else pipe3.flowModel.rhos[2]) ($RES_SIM_123)
(161)     [SCAL] (1) pipe3.flowModel.mus_act[1] = noEvent(if $SEV_25 then pipe3.flowModel.mus[1] else pipe3.flowModel.mus[2]) ($RES_SIM_124)
(162)     [ARRY] (1) pipe3.flowModel.m_flows = {homotopy(({$FUN_11} .* pipe3.flowModel.nParallel)[1], (pipe3.flowModel.m_flow_nominal / pipe3.flowModel.dp_nominal * (pipe3.flowModel.dps_fg - (pipe3.flowModel.g * pipe3.flowModel.dheights) .* pipe3.flowModel.rho_nominal))[1])} ($RES_SIM_125)
(163)     [SCAL] (1) junctionIdeal.medium.u = 287.0512249529787 * ((-273.15) - junctionIdeal.medium.T_degC) + junctionIdeal.port_3.h_outflow ($RES_SIM_80)
(164)     [SCAL] (1) junctionIdeal.port_3.h_outflow = Modelica.Media.IdealGases.Common.Functions.h_T(Modelica.Media.IdealGases.Common.DataRecord("Air", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), -((-273.15) - junctionIdeal.medium.T_degC), true, Modelica.Media.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_SIM_81)
(165)     [SCAL] (1) valve2.dp = pipe3.port_b.p - 99999.99999999999 * junctionVolume.medium.p_bar ($RES_SIM_213)
(166)     [SCAL] (1) valveOpening2.y = valveOpening2.a * time + valveOpening2.b ($RES_SIM_85)
(167)     [SCAL] (1) valveOpening1.y = valveOpening1.a * time + valveOpening1.b ($RES_SIM_87)
(168)     [SCAL] (1) $SEV_13 = valve1.m_flow > 0.0 ($RES_EVT_511)
(169)     [SCAL] (1) $SEV_14 = valve2.m_flow > 0.0 ($RES_EVT_512)
(170)     [ARRY] (1) pipe1.fluidVolumes = {10.0 * pipe1.crossAreas[1]} .* pipe1.nParallel ($RES_BND_342)
(171)     [SCAL] (1) $DER.pipe3.ms[1] = pipe3.mb_flows[1] ($RES_SIM_89)
(172)     [SCAL] (1) $SEV_15 = junctionVolume.port_3.m_flow > 0.0 ($RES_EVT_513)
(173)     [SCAL] (1) valve2.m_flow = homotopy(valve2.Y * valve2.Av * valveOpening2.y * smooth(2, if $SEV_36 then (if $SEV_37 then sqrt((0.0034836987724536205 * valve2.state_a.p) / valve2.state_a.T) else 0.0) * sqrt(valve2.xs * valve2.p) else if $SEV_38 then -(if $SEV_39 then sqrt((0.0034836987724536205 * valve2.state_b.p) / valve2.state_b.T) else 0.0) * sqrt(abs(valve2.xs * valve2.p)) else if $SEV_40 then Modelica.Fluid.Utilities.regRoot2.regRoot2_utility(valve2.xs * valve2.p, valve2.dp_turbulent, (0.0034836987724536205 * valve2.state_a.p) / valve2.state_a.T, (0.0034836987724536205 * valve2.state_b.p) / valve2.state_b.T, false, 1.0) else -Modelica.Fluid.Utilities.regRoot2.regRoot2_utility(-valve2.xs * valve2.p, valve2.dp_turbulent, (0.0034836987724536205 * valve2.state_b.p) / valve2.state_b.T, (0.0034836987724536205 * valve2.state_a.p) / valve2.state_a.T, false, 1.0)), (valve2.dp * valve2.m_flow_nominal * valveOpening2.y) / valve2.dp_nominal) ($RES_SIM_218)
(174)     [ARRY] (1) pipe1.mediums.p_bar = {1e-5 * pipe1.mediums[1].p} ($RES_BND_343)
(175)     [SCAL] (1) valve2.Y = 1.0 - (0.3333333333333333 * $FUN_6) / valve2.Fxt_full ($RES_SIM_219)
(176)     [ARRY] (1) pipe1.mediums.T_degC = {(-273.15) + pipe1.mediums[1].T} ($RES_BND_344)
(177)     [ARRY] (3) pipe1.flowModel.vs = pipe1.vsFM ($RES_BND_345)
(178)     [ARRY] (3) pipe1.flowModel.crossAreas = pipe1.crossAreasFM ($RES_BND_346)
(179)     [SCAL] (1) $SEV_19 = (-pipe2.port_a.m_flow) > 0.0 ($RES_EVT_517)
(180)     [ARRY] (3) pipe1.flowModel.dimensions = pipe1.dimensionsFM ($RES_BND_347)
(181)     [SCAL] (1) $SEV_20 = (-pipe3.port_a.m_flow) > 0.0 ($RES_EVT_518)
(182)     [ARRY] (3) pipe1.flowModel.roughnesses = pipe1.roughnessesFM ($RES_BND_348)
(183)     [SCAL] (1) $SEV_21 = (-pipe1.port_b.m_flow) > 0.0 ($RES_EVT_519)
(184)     [ARRY] (2) pipe1.flowModel.dheights = pipe1.dheightsFM ($RES_BND_349)
(185)     [ARRY] (6) pipe1.flowModel.states = pipe1.statesFM ($RES_BND_431)
(186)     [ARRY] (1) pipe3.mediums.state.p = pipe3.mediums.p ($RES_SIM_131)
(187)     [ARRY] (2) pipe1.heatTransfer.states = pipe1.mediums.state ($RES_BND_432)
(188)     [ARRY] (1) pipe3.mediums.state.T = pipe3.mediums.T ($RES_SIM_132)
(189)     [SCAL] (1) source.medium.u = source.medium.h - 287.0512249529787 * source.T ($RES_SIM_308)
(190)     [ARRY] (4) pipe2.flowModel.states = pipe2.statesFM ($RES_BND_433)
(191)     [SCAL] (1) pipe3.mediums[1].d = pipe3.mediums[1].p / (pipe3.mediums[1].T * pipe3.mediums[1].R) ($RES_SIM_133)
(192)     [SCAL] (1) source.medium.h = Modelica.Media.IdealGases.Common.Functions.h_T(Modelica.Media.IdealGases.Common.DataRecord("Air", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), source.T, true, Modelica.Media.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_SIM_309)
(193)     [ARRY] (2) pipe2.heatTransfer.states = pipe2.mediums.state ($RES_BND_434)
(194)     [SCAL] (1) pipe3.mediums[1].u = pipe3.mediums[1].h - pipe3.mediums[1].R * pipe3.mediums[1].T ($RES_SIM_134)
(195)     [ARRY] (4) pipe3.flowModel.states = pipe3.statesFM ($RES_BND_435)
(196)     [SCAL] (1) pipe3.mediums[1].h = Modelica.Media.IdealGases.Common.Functions.h_T(Modelica.Media.IdealGases.Common.DataRecord("Air", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), pipe3.mediums[1].T, true, Modelica.Media.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_SIM_135)
(197)     [ARRY] (2) pipe3.heatTransfer.states = pipe3.mediums.state ($RES_BND_436)
(198)     [ARRY] (1) pipe3.mediums.R = {287.0512249529787} ($RES_SIM_136)
(199)     [SCAL] (1) $DER.pipe3.Us[1] = pipe3.Wb_flows[1] + pipe3.Hb_flows[1] + pipe3.Qb_flows[1] ($RES_SIM_90)
(200)     [SCAL] (1) pipe3.ms[1] = pipe3.fluidVolumes[1] * pipe3.mediums[1].d ($RES_SIM_91)
(201)     [SCAL] (1) valve2.xs = max(-valve2.Fxt_full, min(valve2.x, valve2.Fxt_full)) ($RES_SIM_220)
(202)     [SCAL] (1) pipe3.Us[1] = pipe3.ms[1] * pipe3.mediums[1].u ($RES_SIM_92)
(203)     [SCAL] (1) valve2.x = valve2.dp / valve2.p ($RES_SIM_221)
(204)     [SCAL] (1) pipe3.port_b.p = pipe3.mediums[1].p ($RES_SIM_93)
(205)     [ARRY] (1) pipe3.vsFM[2:2] = pipe3.vs ($RES_SIM_94)
(206)     [SCAL] (1) valve2.p = max(pipe3.port_b.p, 99999.99999999999 * junctionVolume.medium.p_bar) ($RES_SIM_223)
(207)     [SCAL] (1) pipe3.vsFM[1] = ((pipe3.m_flows[1] / ((0.0034836987724536205 * pipe3.state_a.p) / pipe3.state_a.T)) / pipe3.crossAreas[1]) / pipe3.nParallel ($RES_SIM_95)
(208)     [SCAL] (1) valve2.minLimiter.y = smooth(0, noEvent(if $SEV_41 then valve2.minLimiter.uMin else valveOpening2.y)) ($RES_SIM_224)
(209)     [ARRY] (1) pipe3.m_flows[1:1] = pipe3.flowModel.m_flows[:] ($RES_SIM_96)
(210)     [ARRY] (2) pipe1.flowModel.pathLengths = pipe1.pathLengths ($RES_BND_350)
(211)     [ARRY] (2) pipe3.statesFM[2:2] = pipe3.mediums[:].state ($RES_SIM_97)
(212)     [FOR-] (3) ($RES_BND_351)
(212)     [----] for $i1 in 1:3 loop
(212)     [----]   [SCAL] (1) pipe1.flowModel.rhos[$i1] = (0.0034836987724536205 * pipe1.flowModel.states.T) / pipe1.flowModel.states.p ($RES_BND_352)
(212)     [----] end for;
(213)     [RECD] (2) pipe3.statesFM[1] = pipe3.state_a ($RES_SIM_98)
(214)     [SCAL] (1) valve1.dp = pipe2.port_b.p - 99999.99999999999 * junctionVolume.medium.p_bar ($RES_SIM_227)
(215)     [SCAL] (1) $SEV_25 = pipe3.flowModel.m_flows[1] > 0.0 ($RES_EVT_523)
(216)     [FOR-] (3) ($RES_BND_353)
(216)     [----] for $i1 in 1:3 loop
(216)     [----]   [SCAL] (1) pipe1.flowModel.mus[$i1] = pipe1.flowModel.mu_nominal ($RES_BND_354)
(216)     [----] end for;
(217)     [SCAL] (1) $SEV_26[1] = pipe3.mediums[1].p >= 0.0 ($RES_EVT_524)
(218)     [ARRY] (2) pipe1.flowModel.pathLengths_internal = pipe1.flowModel.pathLengths ($RES_BND_355)
(219)     [SCAL] (1) $SEV_28[1] = pipe3.mediums[1].T >= 200.0 and pipe3.mediums[1].T <= 6000.0 ($RES_EVT_526)
(220)     [FOR-] (2) ($RES_BND_356)
(220)     [----] for $i1 in 1:2 loop
(220)     [----]   [SCAL] (1) pipe1.flowModel.Res_turbulent_internal[$i1] = pipe1.flowModel.Re_turbulent ($RES_BND_357)
(220)     [----] end for;
(221)     [SCAL] (1) $SEV_29 = pipe2.flowModel.m_flows[1] > 0.0 ($RES_EVT_527)
(222)     [SCAL] (1) $SEV_30[1] = pipe2.mediums[1].p >= 0.0 ($RES_EVT_528)
(223)     [ARRY] (2) pipe1.flowModel.diameters = 0.5 * (pipe1.flowModel.dimensions[2:3] + pipe1.flowModel.dimensions[1:2]) ($RES_BND_358)
(224)     [SCAL] (1) junctionVolume.port_3.m_flow + sink.ports[1].m_flow = 0.0 ($RES_SIM_313)
(225)     [SCAL] (1) pipe3.heatTransfer.heatPorts[1].Q_flow = 0.0 ($RES_SIM_315)
(226)     [SCAL] (1) $DER.pipe2.ms[1] = pipe2.mb_flows[1] ($RES_SIM_140)
(227)     [SCAL] (1) $DER.pipe2.Us[1] = pipe2.Wb_flows[1] + pipe2.Hb_flows[1] + pipe2.Qb_flows[1] ($RES_SIM_141)
(228)     [SCAL] (1) pipe2.heatTransfer.heatPorts[1].Q_flow = 0.0 ($RES_SIM_317)
(229)     [SCAL] (1) pipe2.ms[1] = pipe2.fluidVolumes[1] * pipe2.mediums[1].d ($RES_SIM_142)
(230)     [SCAL] (1) pipe2.Us[1] = pipe2.ms[1] * pipe2.mediums[1].u ($RES_SIM_143)
(231)     [SCAL] (1) pipe2.port_b.p = pipe2.mediums[1].p ($RES_SIM_144)
(232)     [ARRY] (1) pipe2.vsFM[2:2] = pipe2.vs ($RES_SIM_145)
(233)     [SCAL] (1) pipe2.vsFM[1] = ((pipe2.m_flows[1] / ((0.0034836987724536205 * pipe2.state_a.p) / pipe2.state_a.T)) / pipe2.crossAreas[1]) / pipe2.nParallel ($RES_SIM_146)
(234)     [ARRY] (1) pipe2.m_flows[1:1] = pipe2.flowModel.m_flows[:] ($RES_SIM_147)
(235)     [ARRY] (2) pipe2.statesFM[2:2] = pipe2.mediums[:].state ($RES_SIM_148)
(236)     [RECD] (2) pipe2.statesFM[1] = pipe2.state_a ($RES_SIM_149)
(237)     [SCAL] (1) $FUN_1 = ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.pipe1.flowModel.WallFriction.massFlowRate_dp_staticHead(pipe1.flowModel.dps_fg[$i1], pipe1.flowModel.rhos[(1:2)[$i1]], pipe1.flowModel.rhos[(2:3)[$i1]], pipe1.flowModel.mus[(1:2)[$i1]], pipe1.flowModel.mus[(2:3)[$i1]], pipe1.flowModel.pathLengths_internal[$i1], pipe1.flowModel.diameters[$i1], (pipe1.flowModel.g * pipe1.flowModel.dheights)[$i1], ((pipe1.flowModel.crossAreas[1:2] + pipe1.flowModel.crossAreas[2:3]) / 2.0)[$i1], ((pipe1.flowModel.roughnesses[1:2] + pipe1.flowModel.roughnesses[2:3]) / 2.0)[$i1], pipe1.flowModel.dp_small / 2.0, pipe1.flowModel.Res_turbulent_internal[$i1]) ($RES_$AUX_458)
(238)     [SCAL] (1) $FUN_2 = sum(pipe1.flowModel.dps_fg) ($RES_$AUX_457)
(239)     [SCAL] (1) $FUN_3 = semiLinear(pipe1.port_a.m_flow, source.ports[1].h_outflow, pipe1.mediums[1].h) ($RES_$AUX_456)
(240)     [SCAL] (1) $FUN_4 = semiLinear(pipe1.port_b.m_flow, junctionIdeal.port_3.h_outflow, pipe1.mediums[1].h) ($RES_$AUX_455)
(241)     [SCAL] (1) $FUN_5 = abs(valve1.xs) ($RES_$AUX_454)
(242)     [SCAL] (1) $FUN_6 = abs(valve2.xs) ($RES_$AUX_453)
(243)     [SCAL] (1) valve1.m_flow = homotopy(valve1.Y * valve1.Av * valveOpening1.y * smooth(2, if $SEV_42 then (if $SEV_43 then sqrt((0.0034836987724536205 * valve1.state_a.p) / valve1.state_a.T) else 0.0) * sqrt(valve1.xs * valve1.p) else if $SEV_44 then -(if $SEV_45 then sqrt((0.0034836987724536205 * valve1.state_b.p) / valve1.state_b.T) else 0.0) * sqrt(abs(valve1.xs * valve1.p)) else if $SEV_46 then Modelica.Fluid.Utilities.regRoot2.regRoot2_utility(valve1.xs * valve1.p, valve1.dp_turbulent, (0.0034836987724536205 * valve1.state_a.p) / valve1.state_a.T, (0.0034836987724536205 * valve1.state_b.p) / valve1.state_b.T, false, 1.0) else -Modelica.Fluid.Utilities.regRoot2.regRoot2_utility(-valve1.xs * valve1.p, valve1.dp_turbulent, (0.0034836987724536205 * valve1.state_b.p) / valve1.state_b.T, (0.0034836987724536205 * valve1.state_a.p) / valve1.state_a.T, false, 1.0)), (valve1.dp * valve1.m_flow_nominal * valveOpening1.y) / valve1.dp_nominal) ($RES_SIM_232)
(244)     [SCAL] (1) $FUN_7 = ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.pipe2.flowModel.WallFriction.massFlowRate_dp_staticHead(pipe2.flowModel.dps_fg[1], pipe2.flowModel.rhos[1], pipe2.flowModel.rhos[2], pipe2.flowModel.mus[1], pipe2.flowModel.mus[2], pipe2.flowModel.pathLengths_internal[1], pipe2.flowModel.diameters[1], (pipe2.flowModel.g * pipe2.flowModel.dheights)[1], (0.5 .* (pipe2.flowModel.crossAreas[1:1] + pipe2.flowModel.crossAreas[2:2]))[1], (0.5 .* (pipe2.flowModel.roughnesses[1:1] + pipe2.flowModel.roughnesses[2:2]))[1], pipe2.flowModel.dp_small, pipe2.flowModel.Res_turbulent_internal[1]) ($RES_$AUX_452)
(245)     [SCAL] (1) valve1.Y = 1.0 - (0.3333333333333333 * $FUN_5) / valve1.Fxt_full ($RES_SIM_233)
(246)     [SCAL] (1) $FUN_8 = sum(pipe2.flowModel.dps_fg) ($RES_$AUX_451)
(247)     [SCAL] (1) valve1.xs = max(-valve1.Fxt_full, min(valve1.x, valve1.Fxt_full)) ($RES_SIM_234)
(248)     [SCAL] (1) $SEV_32[1] = pipe2.mediums[1].T >= 200.0 and pipe2.mediums[1].T <= 6000.0 ($RES_EVT_530)
(249)     [SCAL] (1) $FUN_9 = semiLinear(pipe2.port_a.m_flow, junctionIdeal.port_3.h_outflow, pipe2.mediums[1].h) ($RES_$AUX_450)
(250)     [SCAL] (1) valve1.x = valve1.dp / valve1.p ($RES_SIM_235)
(251)     [ARRY] (1) pipe1.vs = {(0.5 * (pipe1.m_flows[2] + pipe1.m_flows[1])) / (pipe1.crossAreas[1] * pipe1.mediums[1].d)} / pipe1.nParallel ($RES_BND_360)
(252)     [SCAL] (1) valve1.p = max(pipe2.port_b.p, 99999.99999999999 * junctionVolume.medium.p_bar) ($RES_SIM_237)
(253)     [ARRY] (1) pipe1.heatTransfer.Ts = {pipe1.heatTransfer.states.p} ($RES_BND_362)
(254)     [SCAL] (1) valve1.minLimiter.y = smooth(0, noEvent(if $SEV_47 then valve1.minLimiter.uMin else valveOpening1.y)) ($RES_SIM_238)
(255)     [ARRY] (1) pipe1.heatTransfer.vs = pipe1.vs ($RES_BND_363)
(256)     [SCAL] (1) $SEV_36 = valve2.xs * valve2.p >= valve2.dp_turbulent ($RES_EVT_534)
(257)     [SCAL] (1) $DER.pipe1.ms[1] = pipe1.mb_flows[1] ($RES_SIM_239)
(258)     [SCAL] (1) $SEV_37 = (0.0034836987724536205 * valve2.state_a.p) / valve2.state_a.T > 0.0 ($RES_EVT_535)
(259)     [SCAL] (1) $SEV_38 = valve2.xs * valve2.p <= (-valve2.dp_turbulent) ($RES_EVT_536)
(260)     [SCAL] (1) $SEV_39 = (0.0034836987724536205 * valve2.state_b.p) / valve2.state_b.T > 0.0 ($RES_EVT_537)
(261)     [SCAL] (1) valve1.V_flow = valve1.m_flow / smooth(1, if $SEV_63 then (0.0034836987724536205 * valve1.state_a.p) / valve1.state_a.T else if $SEV_64 then (0.0034836987724536205 * valve1.state_b.p) / valve1.state_b.T else if $SEV_62 then 0.25 * ((0.0034836987724536205 * valve1.state_b.p) / valve1.state_b.T - (0.0034836987724536205 * valve1.state_a.p) / valve1.state_a.T) * ((-3.0) + (valve1.m_flow / valve1.m_flow_small) ^ 2.0) * (valve1.m_flow / valve1.m_flow_small) + 0.5 * ((0.0034836987724536205 * valve1.state_a.p) / valve1.state_a.T + (0.0034836987724536205 * valve1.state_b.p) / valve1.state_b.T) else 0.5 * ((0.0034836987724536205 * valve1.state_a.p) / valve1.state_a.T + (0.0034836987724536205 * valve1.state_b.p) / valve1.state_b.T)) ($RES_BND_367)
(262)     [SCAL] (1) $SEV_40 = (0.0034836987724536205 * valve2.state_a.p) / valve2.state_a.T >= (0.0034836987724536205 * valve2.state_b.p) / valve2.state_b.T ($RES_EVT_538)
(263)     [SCAL] (1) valve1.port_a_T = smooth(1, if $SEV_63 then valve1.state_a.T else if $SEV_64 then ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve1.Medium.T_h.Internal.solve(junctionVolume.port_3.h_outflow, 200.0, 6000.0, 1e5, {1.0}, Modelica.Media.IdealGases.Common.DataRecord("Air", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), 1e-13) else if $SEV_62 then 0.25 * (ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve1.Medium.T_h.Internal.solve(junctionVolume.port_3.h_outflow, 200.0, 6000.0, 1e5, {1.0}, Modelica.Media.IdealGases.Common.DataRecord("Air", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), 1e-13) - valve1.state_a.T) * ((-3.0) + (valve1.m_flow / valve1.m_flow_small) ^ 2.0) * (valve1.m_flow / valve1.m_flow_small) + 0.5 * (valve1.state_a.T + ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve1.Medium.T_h.Internal.solve(junctionVolume.port_3.h_outflow, 200.0, 6000.0, 1e5, {1.0}, Modelica.Media.IdealGases.Common.DataRecord("Air", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), 1e-13)) else 0.5 * (valve1.state_a.T + ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve1.Medium.T_h.Internal.solve(junctionVolume.port_3.h_outflow, 200.0, 6000.0, 1e5, {1.0}, Modelica.Media.IdealGases.Common.DataRecord("Air", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), 1e-13))) ($RES_BND_368)
(264)     [SCAL] (1) $SEV_41 = valveOpening2.y < valve2.minLimiter.uMin ($RES_EVT_539)
(265)     [SCAL] (1) valve1.port_b_T = smooth(1, if $SEV_60 then valve1.state_b.T else if $SEV_61 then ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve1.Medium.T_h.Internal.solve(valve1.port_b.h_outflow, 200.0, 6000.0, 1e5, {1.0}, Modelica.Media.IdealGases.Common.DataRecord("Air", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), 1e-13) else if $SEV_62 then 0.5 * (valve1.state_b.T + ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve1.Medium.T_h.Internal.solve(valve1.port_b.h_outflow, 200.0, 6000.0, 1e5, {1.0}, Modelica.Media.IdealGases.Common.DataRecord("Air", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), 1e-13)) - 0.25 * (ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve1.Medium.T_h.Internal.solve(valve1.port_b.h_outflow, 200.0, 6000.0, 1e5, {1.0}, Modelica.Media.IdealGases.Common.DataRecord("Air", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), 1e-13) - valve1.state_b.T) * ((-3.0) + (valve1.m_flow / (-valve1.m_flow_small)) ^ 2.0) * (valve1.m_flow / valve1.m_flow_small) else 0.5 * (valve1.state_b.T + ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve1.Medium.T_h.Internal.solve(valve1.port_b.h_outflow, 200.0, 6000.0, 1e5, {1.0}, Modelica.Media.IdealGases.Common.DataRecord("Air", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), 1e-13))) ($RES_BND_369)
(266)     [SCAL] (1) pipe1.heatTransfer.heatPorts[1].Q_flow = 0.0 ($RES_SIM_322)
(267)     [SCAL] (1) 99999.99999999999 * junctionVolume.medium.p_bar = sink.ports[1].p ($RES_SIM_326)
(268)     [SCAL] (1) valve1.port_b.h_outflow = pipe2.mediums[1].h ($RES_SIM_152)
(269)     [SCAL] (1) pipe2.port_a.h_outflow = pipe2.mediums[1].h ($RES_SIM_153)
(270)     [SCAL] (1) -valve1.m_flow = -pipe2.m_flows[2] ($RES_SIM_154)
(271)     [SCAL] (1) pipe2.port_a.m_flow = pipe2.m_flows[1] ($RES_SIM_155)
(272)     [SCAL] (1) pipe2.H_flows[2] = -$FUN_10 ($RES_SIM_156)
(273)     [SCAL] (1) pipe2.H_flows[1] = $FUN_9 ($RES_SIM_157)
(274)     [SCAL] (1) pipe2.mb_flows[1] = pipe2.m_flows[1] - pipe2.m_flows[2] ($RES_SIM_158)
(275)     [SCAL] (1) pipe2.Hb_flows[1] = pipe2.H_flows[1] - pipe2.H_flows[2] ($RES_SIM_159)
(276)     [SCAL] (1) $FUN_10 = semiLinear(-valve1.m_flow, junctionVolume.port_3.h_outflow, pipe2.mediums[1].h) ($RES_$AUX_449)
(277)     [SCAL] (1) $FUN_11 = ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.pipe3.flowModel.WallFriction.massFlowRate_dp_staticHead(pipe3.flowModel.dps_fg[1], pipe3.flowModel.rhos[1], pipe3.flowModel.rhos[2], pipe3.flowModel.mus[1], pipe3.flowModel.mus[2], pipe3.flowModel.pathLengths_internal[1], pipe3.flowModel.diameters[1], (pipe3.flowModel.g * pipe3.flowModel.dheights)[1], (0.5 .* (pipe3.flowModel.crossAreas[1:1] + pipe3.flowModel.crossAreas[2:2]))[1], (0.5 .* (pipe3.flowModel.roughnesses[1:1] + pipe3.flowModel.roughnesses[2:2]))[1], pipe3.flowModel.dp_small, pipe3.flowModel.Res_turbulent_internal[1]) ($RES_$AUX_448)
(278)     [SCAL] (1) $FUN_12 = sum(pipe3.flowModel.dps_fg) ($RES_$AUX_447)
(279)     [SCAL] (1) $FUN_13 = semiLinear(pipe3.port_a.m_flow, junctionIdeal.port_3.h_outflow, pipe3.mediums[1].h) ($RES_$AUX_446)
(280)     [SCAL] (1) $DER.pipe1.Us[1] = pipe1.Wb_flows[1] + pipe1.Hb_flows[1] + pipe1.Qb_flows[1] ($RES_SIM_240)
(281)     [SCAL] (1) $FUN_14 = semiLinear(-valve2.m_flow, junctionVolume.port_3.h_outflow, pipe3.mediums[1].h) ($RES_$AUX_445)
(282)     [SCAL] (1) pipe1.ms[1] = pipe1.fluidVolumes[1] * pipe1.mediums[1].d ($RES_SIM_241)
(283)     [TUPL] (4) ($FUN_15, $FUN_16, $FUN_17, $FUN_18) = ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valveOpening1.getInterpolationCoefficients(valveOpening1.table, valveOpening1.offset, valveOpening1.startTime, time, valveOpening1.last, 1e-13, valveOpening1.shiftTime) ($RES_$AUX_444)
(284)     [SCAL] (1) pipe1.Us[1] = pipe1.ms[1] * pipe1.mediums[1].u ($RES_SIM_242)
(285)     [TUPL] (4) ($FUN_19, $FUN_20, $FUN_21, $FUN_22) = ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valveOpening2.getInterpolationCoefficients(valveOpening2.table, valveOpening2.offset, valveOpening2.startTime, time, valveOpening2.last, 1e-13, valveOpening2.shiftTime) ($RES_$AUX_443)
(286)     [SCAL] (1) pipe1.vsFM[3] = ((pipe1.m_flows[2] / ((0.0034836987724536205 * pipe1.state_b.p) / pipe1.state_b.T)) / pipe1.crossAreas[1]) / pipe1.nParallel ($RES_SIM_243)
(287)     [SCAL] (1) $FUN_23 = ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.pipe3.flowModel.WallFriction.pressureLoss_m_flow(pipe3.flowModel.m_flow_nominal / pipe3.flowModel.nParallel, pipe3.flowModel.rho_nominal, pipe3.flowModel.rho_nominal, pipe3.flowModel.mu_nominal, pipe3.flowModel.mu_nominal, pipe3.flowModel.pathLengths_internal[1], pipe3.flowModel.diameters[1], (0.5 .* (pipe3.flowModel.crossAreas[2:2] + pipe3.flowModel.crossAreas[1:1]))[1], (0.5 .* (pipe3.flowModel.roughnesses[2:2] + pipe3.flowModel.roughnesses[1:1]))[1], pipe3.flowModel.m_flow_small / pipe3.flowModel.nParallel, pipe3.flowModel.Res_turbulent_internal[1]) ($RES_$AUX_442)
(288)     [ARRY] (1) pipe1.vsFM[2:2] = pipe1.vs ($RES_SIM_244)
(289)     [SCAL] (1) pipe3.flowModel.dp_fric_nominal = sum({$FUN_23}) ($RES_$AUX_441)
(290)     [SCAL] (1) $SEV_42 = valve1.xs * valve1.p >= valve1.dp_turbulent ($RES_EVT_540)
(291)     [SCAL] (1) pipe1.vsFM[1] = ((pipe1.m_flows[1] / ((0.0034836987724536205 * pipe1.state_a.p) / pipe1.state_a.T)) / pipe1.crossAreas[1]) / pipe1.nParallel ($RES_SIM_245)
(292)     [SCAL] (1) valve1.dp_turbulent = max(valve1.dp_small, (6.283185307179586e6 * (1e-6 * Modelica.Media.Incompressible.TableBased.Polynomials_Temp.evaluateWithRange({9.739110288630587e-15, -3.1353724870333906e-11, 4.3004876595642225e-8, -3.822801629175824e-5, 0.05042787436718076, 17.23926013924253}, -149.99999999999997, 1000.0000000000001, (-273.15) + valve1.state_a.T) + 1e-6 * Modelica.Media.Incompressible.TableBased.Polynomials_Temp.evaluateWithRange({9.739110288630587e-15, -3.1353724870333906e-11, 4.3004876595642225e-8, -3.822801629175824e-5, 0.05042787436718076, 17.23926013924253}, -149.99999999999997, 1000.0000000000001, (-273.15) + valve1.state_b.T)) ^ 2.0) / (valve1.Y * max(valveOpening1.y, 0.001) * valve1.Av * ((0.0034836987724536205 * valve1.state_b.p) / valve1.state_b.T + (0.0034836987724536205 * valve1.state_a.p) / valve1.state_a.T))) ($RES_BND_370)
(293)     [SCAL] (1) $FUN_25 = ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.pipe2.flowModel.WallFriction.pressureLoss_m_flow(pipe2.flowModel.m_flow_nominal / pipe2.flowModel.nParallel, pipe2.flowModel.rho_nominal, pipe2.flowModel.rho_nominal, pipe2.flowModel.mu_nominal, pipe2.flowModel.mu_nominal, pipe2.flowModel.pathLengths_internal[1], pipe2.flowModel.diameters[1], (0.5 .* (pipe2.flowModel.crossAreas[2:2] + pipe2.flowModel.crossAreas[1:1]))[1], (0.5 .* (pipe2.flowModel.roughnesses[2:2] + pipe2.flowModel.roughnesses[1:1]))[1], pipe2.flowModel.m_flow_small / pipe2.flowModel.nParallel, pipe2.flowModel.Res_turbulent_internal[1]) ($RES_$AUX_440)
(294)     [SCAL] (1) $SEV_43 = (0.0034836987724536205 * valve1.state_a.p) / valve1.state_a.T > 0.0 ($RES_EVT_541)
(295)     [ARRY] (2) pipe1.m_flows[:] = pipe1.flowModel.m_flows[:] ($RES_SIM_246)
(296)     [SCAL] (1) valve2.V_flow = valve2.m_flow / smooth(1, if $SEV_58 then (0.0034836987724536205 * valve2.state_a.p) / valve2.state_a.T else if $SEV_59 then (0.0034836987724536205 * valve2.state_b.p) / valve2.state_b.T else if $SEV_57 then 0.25 * ((0.0034836987724536205 * valve2.state_b.p) / valve2.state_b.T - (0.0034836987724536205 * valve2.state_a.p) / valve2.state_a.T) * ((-3.0) + (valve2.m_flow / valve2.m_flow_small) ^ 2.0) * (valve2.m_flow / valve2.m_flow_small) + 0.5 * ((0.0034836987724536205 * valve2.state_a.p) / valve2.state_a.T + (0.0034836987724536205 * valve2.state_b.p) / valve2.state_b.T) else 0.5 * ((0.0034836987724536205 * valve2.state_a.p) / valve2.state_a.T + (0.0034836987724536205 * valve2.state_b.p) / valve2.state_b.T)) ($RES_BND_371)
(297)     [SCAL] (1) $SEV_44 = valve1.xs * valve1.p <= (-valve1.dp_turbulent) ($RES_EVT_542)
(298)     [RECD] (2) pipe1.statesFM[3] = pipe1.state_b ($RES_SIM_247)
(299)     [SCAL] (1) valve2.port_a_T = smooth(1, if $SEV_58 then valve2.state_a.T else if $SEV_59 then ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve2.Medium.T_h.Internal.solve(junctionVolume.port_3.h_outflow, 200.0, 6000.0, 1e5, {1.0}, Modelica.Media.IdealGases.Common.DataRecord("Air", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), 1e-13) else if $SEV_57 then 0.25 * (ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve2.Medium.T_h.Internal.solve(junctionVolume.port_3.h_outflow, 200.0, 6000.0, 1e5, {1.0}, Modelica.Media.IdealGases.Common.DataRecord("Air", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), 1e-13) - valve2.state_a.T) * ((-3.0) + (valve2.m_flow / valve2.m_flow_small) ^ 2.0) * (valve2.m_flow / valve2.m_flow_small) + 0.5 * (valve2.state_a.T + ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve2.Medium.T_h.Internal.solve(junctionVolume.port_3.h_outflow, 200.0, 6000.0, 1e5, {1.0}, Modelica.Media.IdealGases.Common.DataRecord("Air", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), 1e-13)) else 0.5 * (valve2.state_a.T + ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve2.Medium.T_h.Internal.solve(junctionVolume.port_3.h_outflow, 200.0, 6000.0, 1e5, {1.0}, Modelica.Media.IdealGases.Common.DataRecord("Air", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), 1e-13))) ($RES_BND_372)
(300)     [SCAL] (1) $SEV_45 = (0.0034836987724536205 * valve1.state_b.p) / valve1.state_b.T > 0.0 ($RES_EVT_543)
(301)     [ARRY] (2) pipe1.statesFM[2:2] = pipe1.mediums[:].state ($RES_SIM_248)
(302)     [SCAL] (1) valve2.port_b_T = smooth(1, if $SEV_55 then valve2.state_b.T else if $SEV_56 then ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve2.Medium.T_h.Internal.solve(valve2.port_b.h_outflow, 200.0, 6000.0, 1e5, {1.0}, Modelica.Media.IdealGases.Common.DataRecord("Air", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), 1e-13) else if $SEV_57 then 0.5 * (valve2.state_b.T + ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve2.Medium.T_h.Internal.solve(valve2.port_b.h_outflow, 200.0, 6000.0, 1e5, {1.0}, Modelica.Media.IdealGases.Common.DataRecord("Air", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), 1e-13)) - 0.25 * (ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve2.Medium.T_h.Internal.solve(valve2.port_b.h_outflow, 200.0, 6000.0, 1e5, {1.0}, Modelica.Media.IdealGases.Common.DataRecord("Air", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), 1e-13) - valve2.state_b.T) * ((-3.0) + (valve2.m_flow / (-valve2.m_flow_small)) ^ 2.0) * (valve2.m_flow / valve2.m_flow_small) else 0.5 * (valve2.state_b.T + ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.valve2.Medium.T_h.Internal.solve(valve2.port_b.h_outflow, 200.0, 6000.0, 1e5, {1.0}, Modelica.Media.IdealGases.Common.DataRecord("Air", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), 1e-13))) ($RES_BND_373)
(303)     [SCAL] (1) $SEV_46 = (0.0034836987724536205 * valve1.state_a.p) / valve1.state_a.T >= (0.0034836987724536205 * valve1.state_b.p) / valve1.state_b.T ($RES_EVT_544)
(304)     [RECD] (2) pipe1.statesFM[1] = pipe1.state_a ($RES_SIM_249)
(305)     [SCAL] (1) valve2.dp_turbulent = max(valve2.dp_small, (6.283185307179586e6 * (1e-6 * Modelica.Media.Incompressible.TableBased.Polynomials_Temp.evaluateWithRange({9.739110288630587e-15, -3.1353724870333906e-11, 4.3004876595642225e-8, -3.822801629175824e-5, 0.05042787436718076, 17.23926013924253}, -149.99999999999997, 1000.0000000000001, (-273.15) + valve2.state_a.T) + 1e-6 * Modelica.Media.Incompressible.TableBased.Polynomials_Temp.evaluateWithRange({9.739110288630587e-15, -3.1353724870333906e-11, 4.3004876595642225e-8, -3.822801629175824e-5, 0.05042787436718076, 17.23926013924253}, -149.99999999999997, 1000.0000000000001, (-273.15) + valve2.state_b.T)) ^ 2.0) / (valve2.Y * max(valveOpening2.y, 0.001) * valve2.Av * ((0.0034836987724536205 * valve2.state_b.p) / valve2.state_b.T + (0.0034836987724536205 * valve2.state_a.p) / valve2.state_a.T))) ($RES_BND_374)
(306)     [SCAL] (1) $SEV_47 = valveOpening1.y < valve1.minLimiter.uMin ($RES_EVT_545)
(307)     [FOR-] (2) ($RES_EVT_546)
(307)     [----] for $i1 in 1:2 loop
(307)     [----]   [SCAL] (1) $SEV_48[$i1] = pipe1.flowModel.m_flows[$i1] > 0.0 ($RES_EVT_547)
(307)     [----] end for;
(308)     [ARRY] (1) pipe2.fluidVolumes = {10.0 * pipe2.crossAreas[1]} .* pipe2.nParallel ($RES_BND_377)
(309)     [SCAL] (1) $SEV_49[1] = pipe1.mediums[1].p >= 0.0 ($RES_EVT_548)
(310)     [ARRY] (1) pipe2.mediums.p_bar = {1e-5 * pipe2.mediums[1].p} ($RES_BND_378)
(311)     [ARRY] (1) pipe2.mediums.T_degC = {(-273.15) + pipe2.mediums[1].T} ($RES_BND_379)
(312)     [SCAL] (1) pipe1.port_a.m_flow + source.ports[1].m_flow = 0.0 ($RES_SIM_334)
(313)     [SCAL] (1) source.ports[1].p = pipe1.port_a.p ($RES_SIM_335)
(314)     [ARRY] (2) pipe2.roughnessesFM[:] = {pipe2.roughnesses[1], pipe2.roughnesses[1]} ($RES_SIM_160)
(315)     [ARRY] (2) pipe2.dimensionsFM[:] = {pipe2.dimensions[1], pipe2.dimensions[1]} ($RES_SIM_161)
(316)     [ARRY] (2) pipe2.crossAreasFM[:] = {pipe2.crossAreas[1], pipe2.crossAreas[1]} ($RES_SIM_162)
(317)     [ARRY] (1) pipe2.dheightsFM[:] = {0.0} ($RES_SIM_163)
(318)     [ARRY] (1) pipe2.pathLengths[:] = {10.0} ($RES_SIM_164)
(319)     [ARRY] (1) pipe2.Wb_flows = (pipe2.crossAreas * pipe2.vs * (($FUN_8 + pipe2.port_b.p) - ((system.g * {0.0}) / pipe2.mediums.d + 99999.99999999999 * junctionIdeal.medium.p_bar))) / ({1.0} * {1.0}) .* {1.0} .* pipe2.nParallel ($RES_SIM_165)
(320)     [ARRY] (1) pipe2.Qb_flows = pipe2.heatTransfer.Q_flows ($RES_SIM_166)
(321)     [ARRY] (1) pipe2.heatTransfer.Q_flows = pipe2.heatTransfer.heatPorts.Q_flow ($RES_SIM_167)
(322)     [ARRY] (1) pipe2.heatTransfer.Ts = pipe2.heatTransfer.heatPorts.T ($RES_SIM_168)
(323)     [ARRY] (1) {0.0} = pipe2.flowModel.Ib_flows - (pipe2.flowModel.Fs_fg + pipe2.flowModel.Fs_p) ($RES_SIM_169)
(324)     [SCAL] (1) pipe2.flowModel.dp_fric_nominal = sum({$FUN_25}) ($RES_$AUX_439)
(325)     [SCAL] (1) $FUN_27 = ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes17.pipe1.flowModel.WallFriction.pressureLoss_m_flow(pipe1.flowModel.m_flow_nominal / pipe1.flowModel.nParallel, pipe1.flowModel.rho_nominal, pipe1.flowModel.rho_nominal, pipe1.flowModel.mu_nominal, pipe1.flowModel.mu_nominal, pipe1.flowModel.pathLengths_internal[$i1], pipe1.flowModel.diameters[$i1], (0.5 .* (pipe1.flowModel.crossAreas[2:3] + pipe1.flowModel.crossAreas[1:2]))[$i1], (0.5 .* (pipe1.flowModel.roughnesses[2:3] + pipe1.flowModel.roughnesses[1:2]))[$i1], pipe1.flowModel.m_flow_small / pipe1.flowModel.nParallel, pipe1.flowModel.Res_turbulent_internal[$i1]) ($RES_$AUX_438)
(326)     [SCAL] (1) pipe1.flowModel.dp_fric_nominal = sum($FUN_27 for $i1 in 1:2) ($RES_$AUX_437)
(327)     [SCAL] (1) pipe1.port_b.h_outflow = pipe1.mediums[1].h ($RES_SIM_252)
(328)     [SCAL] (1) pipe1.port_a.h_outflow = pipe1.mediums[1].h ($RES_SIM_253)