Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ModelicaTest_3.2.2_ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.conf.json loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo", uses=false) loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo", uses=false) loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.2.3+maint.om/package.mo", uses=false) loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaTest 3.2.2+maint.om/package.mo", uses=false) Using package ModelicaTest with version 3.2.2 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaTest 3.2.2+maint.om/package.mo) Using package Modelica with version 3.2.3 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.2.3+maint.om/package.mo) Using package Complex with version 4.0.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo) Using package ModelicaServices with version 4.0.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo) Running command: translateModel(ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ModelicaTest_3.2.2_ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18") translateModel(ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ModelicaTest_3.2.2_ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18") Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo): time 0.001163/0.001163, allocations: 108.1 kB / 16.42 MB, free: 6.52 MB / 14.72 MB Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo): time 0.001097/0.001097, allocations: 189.9 kB / 17.35 MB, free: 5.754 MB / 14.72 MB Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.2.3+maint.om/package.mo): time 1.266/1.266, allocations: 205.1 MB / 223.2 MB, free: 12.27 MB / 190.1 MB Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaTest 3.2.2+maint.om/package.mo): time 0.1762/0.1762, allocations: 39.96 MB / 310.5 MB, free: 4.031 MB / 254.1 MB Notification: Performance of FrontEnd - Absyn->SCode: time 2.058e-05/2.06e-05, allocations: 6.219 kB / 436.4 MB, free: 11.81 MB / 318.1 MB Notification: Performance of NFInst.instantiate(ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18): time 0.3154/0.3154, allocations: 112 MB / 0.5355 GB, free: 4.27 MB / 398.1 MB Notification: Performance of NFInst.instExpressions: time 0.03927/0.3548, allocations: 38.89 MB / 0.5735 GB, free: 2.676 MB / 398.1 MB Notification: Performance of NFInst.updateImplicitVariability: time 0.002692/0.3575, allocations: 101.6 kB / 0.5736 GB, free: 2.664 MB / 398.1 MB Notification: Performance of NFTyping.typeComponents: time 0.002505/0.36, allocations: 1.353 MB / 0.5749 GB, free: 1.703 MB / 398.1 MB Notification: Performance of NFTyping.typeBindings: time 0.02086/0.3809, allocations: 8.392 MB / 0.5831 GB, free: 12.59 MB / 414.1 MB Notification: Performance of NFTyping.typeClassSections: time 0.02106/0.402, allocations: 8.107 MB / 0.591 GB, free: 6.168 MB / 414.1 MB Notification: Performance of NFFlatten.flatten: time 0.01164/0.4137, allocations: 8.984 MB / 0.5998 GB, free: 13.59 MB / 430.1 MB Notification: Performance of NFFlatten.resolveConnections: time 0.002699/0.4164, allocations: 1.75 MB / 0.6015 GB, free: 11.85 MB / 430.1 MB Notification: Performance of NFEvalConstants.evaluate: time 0.005808/0.4222, allocations: 3.47 MB / 0.6049 GB, free: 8.656 MB / 430.1 MB Notification: Performance of NFSimplifyModel.simplify: time 0.02373/0.446, allocations: 12.32 MB / 0.6169 GB, free: 12.49 MB / 446.1 MB Notification: Performance of NFPackage.collectConstants: time 0.0008503/0.4468, allocations: 248 kB / 0.6172 GB, free: 12.25 MB / 446.1 MB Notification: Performance of NFFlatten.collectFunctions: time 0.01915/0.466, allocations: 9.69 MB / 0.6266 GB, free: 2.703 MB / 446.1 MB Notification: Performance of combineBinaries: time 0.006042/0.4721, allocations: 5.586 MB / 0.6321 GB, free: 13.21 MB / 462.1 MB Notification: Performance of replaceArrayConstructors: time 0.002882/0.475, allocations: 3.577 MB / 0.6356 GB, free: 9.594 MB / 462.1 MB Notification: Performance of NFVerifyModel.verify: time 0.0009533/0.476, allocations: 466.7 kB / 0.636 GB, free: 9.137 MB / 462.1 MB Notification: Performance of FrontEnd: time 0.0004723/0.4764, allocations: 75.67 kB / 0.6361 GB, free: 9.062 MB / 462.1 MB Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 575 (403) * Number of variables: 675 (474) Notification: Performance of Bindings: time 0.01527/0.4917, allocations: 16.25 MB / 0.652 GB, free: 8.508 MB / 478.1 MB Notification: Performance of FunctionAlias: time 0.001817/0.4936, allocations: 1.852 MB / 0.6538 GB, free: 6.645 MB / 478.1 MB Notification: Performance of Early Inline: time 0.008893/0.5025, allocations: 8.794 MB / 0.6624 GB, free: 13.77 MB / 494.1 MB Notification: Performance of simplify1: time 0.0007751/0.5033, allocations: 0.5851 MB / 0.6629 GB, free: 13.18 MB / 494.1 MB Notification: Performance of Alias: time 0.008488/0.5118, allocations: 6.673 MB / 0.6694 GB, free: 6.062 MB / 494.1 MB Notification: Performance of simplify2: time 0.001231/0.513, allocations: 0.5695 MB / 0.67 GB, free: 5.492 MB / 494.1 MB Notification: Performance of Events: time 0.002379/0.5154, allocations: 2.135 MB / 0.6721 GB, free: 3.352 MB / 494.1 MB Notification: Performance of Detect States: time 0.002044/0.5175, allocations: 2.179 MB / 0.6742 GB, free: 1.141 MB / 494.1 MB Notification: Performance of Partitioning: time 0.003602/0.5211, allocations: 3.239 MB / 0.6774 GB, free: 13.56 MB / 0.4981 GB Error: Internal error NBAdjacency.Matrix.create failed to create adjacency matrix for system: System Variables (440/646) **************************** (1) [ALGB] (1) Real pipe2.state_b.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (2) [ALGB] (1) Real[1] pipe2.mb_flows (min = {-1e5 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}) (3) [DISC] (1) Integer sink.medium.phase (fixed = false, start = 1, min = 0, max = 2) (4) [ALGB] (1) protected Real valve1.state_b.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (5) [ALGB] (1) Real[1] pipe2.mediums.T (start = {pipe2.T_start}, min = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}, StateSelect = default) (6) [ALGB] (1) Real pipe2.state_b.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (7) [DISC] (9) Integer[3, 3] pipe1.statesFM.phase (min = {0 for $i1 in 1:3}, max = {2 for $i1 in 1:3}) (8) [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}) (9) [DISC] (4) Integer[2, 2] pipe2.statesFM.phase (min = {0 for $i1 in 1:2}, max = {2 for $i1 in 1:2}) (10) [ALGB] (1) protected Real[1] pipe3.dheightsFM (11) [DISC] (1) final input Integer[1, 1] pipe3.heatTransfer.states.phase = {pipe3.mediums[1].state.phase} (min = {0 for $i1 in 1:1}, max = {2 for $i1 in 1:1}) (12) [ALGB] (1) protected Real valve1.state_b.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (13) [DISC] (1) protected Real valveOpening1.b (14) [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}) (15) [DISC] (1) protected Real valveOpening1.a (16) [ALGB] (1) protected Real valve1.state_b.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (17) [DISC] (1) protected Integer valve1.state_a.phase (min = 0, max = 2) (18) [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}) (19) [DISC] (1) Integer[1] pipe3.mediums.phase (fixed = {false for $i1 in 1:1}, start = {1 for $i1 in 1:1}, min = {0 for $i1 in 1:1}, max = {2 for $i1 in 1:1}) (20) [ALGB] (1) final Real[1] pipe3.flowModel.dheights = pipe3.dheightsFM (21) [DISC] (1) protected discrete Real valveOpening1.nextEvent (fixed = true, start = 0.0) (22) [ALGB] (2) final Real[2] pipe1.flowModel.dheights = pipe1.dheightsFM (23) [ALGB] (1) Real pipe2.state_b.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (24) [ALGB] (1) protected Real valve1.state_b.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (25) [ALGB] (1) stream Real pipe1.port_b.h_outflow (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (26) [DER-] (1) Real[1] $DER.pipe3.Us (27) [ALGB] (1) Real[1] pipe2.mediums.T_degC = {Modelica.SIunits.Conversions.to_degC(pipe2.mediums[1].T)} (28) [ALGB] (1) Real[1] pipe3.mediums.T_degC = {Modelica.SIunits.Conversions.to_degC(pipe3.mediums[1].T)} (29) [ALGB] (1) Real junctionVolume.medium.p_bar = Modelica.SIunits.Conversions.to_bar(99999.99999999999 * junctionVolume.medium.p_bar) (30) [ALGB] (3) final Real[3] pipe1.flowModel.crossAreas = pipe1.crossAreasFM (31) [ALGB] (3) final Real[3] pipe1.flowModel.dimensions = pipe1.dimensionsFM (32) [ALGB] (1) Real valve2.V_flow = valve2.m_flow / Modelica.Fluid.Utilities.regStep(valve2.m_flow, ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.valve2.Medium.density(valve2.state_a), ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.valve2.Medium.density(valve2.state_b), valve2.m_flow_small) (33) [ALGB] (1) Real[1] pipe1.Qb_flows (34) [ALGB] (1) Real pipe3.port_b.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (35) [ALGB] (1) stream Real junctionIdeal.port_3.h_outflow (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (36) [ALGB] (1) Real pipe2.state_a.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (37) [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 = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}) (38) [DER-] (1) Real[1] $DER.pipe2.Us (39) [ALGB] (1) Real valve1.m_flow (start = valve1.m_flow_start, min = -1e60, max = 1e5) (40) [ALGB] (1) Real pipe2.state_a.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (41) [DISC] (9) final input Integer[3, 3] pipe1.flowModel.states.phase = {pipe1.statesFM[1].phase, pipe1.statesFM[2].phase, pipe1.statesFM[3].phase} (min = {0 for $i1 in 1:3}, max = {2 for $i1 in 1:3}) (42) [ALGB] (1) protected Real valve1.state_a.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (43) [ALGB] (1) Real[1] pipe1.mediums.state.T (start = {500.0 for $i1 in 1:1}, min = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}) (44) [ALGB] (1) Real pipe2.state_a.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (45) [ALGB] (1) Real[1] pipe2.mediums.sat.Tsat (start = {500.0 for $i1 in 1:1}, min = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}) (46) [DER-] (1) Real[1] $DER.pipe1.Us (47) [ALGB] (1) protected Real valve1.state_a.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (48) [ALGB] (1) final input Real[1, 1] pipe2.heatTransfer.states.d = {pipe2.mediums[1].state.d} (start = {150.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}) (49) [DISC] (1) Integer[1] pipe2.mediums.phase (fixed = {false for $i1 in 1:1}, start = {1 for $i1 in 1:1}, min = {0 for $i1 in 1:1}, max = {2 for $i1 in 1:1}) (50) [ALGB] (1) protected Real valve1.state_a.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (51) [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}) (52) [ALGB] (2) final Real[2] pipe2.flowModel.roughnesses = pipe2.roughnessesFM (min = {0.0 for $i1 in 1:2}) (53) [ALGB] (1) final input Real[1, 1] pipe2.heatTransfer.states.h = {pipe2.mediums[1].state.h} (start = {1e5 for $i1 in 1:1}, min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {5e5 for $i1 in 1:1}) (54) [DISC] (1) Integer[1] pipe2.mediums.state.phase (min = {0 for $i1 in 1:1}, max = {2 for $i1 in 1:1}) (55) [ALGB] (1) final Real[1] pipe2.fluidVolumes = {pipe2.crossAreas[1] * 10.0} .* pipe2.nParallel (56) [ALGB] (1) protected Real[1] pipe2.pathLengths (57) [ALGB] (1) Real[1] pipe1.mediums.state.d (start = {150.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}) (58) [ALGB] (1) Real pipe2.state_a.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (59) [DISC] (1) Integer pipe2.state_a.phase (min = 0, max = 2) (60) [ALGB] (1) protected Real[1] pipe2.dheightsFM (61) [ALGB] (1) Real[1] pipe1.mediums.state.h (start = {1e5 for $i1 in 1:1}, min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {5e5 for $i1 in 1:1}) (62) [ALGB] (1) final input Real[1, 1] pipe2.heatTransfer.states.p = {pipe2.mediums[1].state.p} (start = {5e6 for $i1 in 1:1}, min = {611.657 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1}) (63) [ALGB] (1) final input Real[1, 1] pipe3.heatTransfer.states.p = {pipe3.mediums[1].state.p} (start = {5e6 for $i1 in 1:1}, min = {611.657 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1}) (64) [ALGB] (1) flow Real pipe1.port_a.m_flow (min = -1e60, max = 1e5) (65) [ALGB] (1) protected Real valve1.state_a.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (66) [DISC] (3) Boolean[3] $SEV_4[$i1] (67) [ALGB] (1) Real[1] pipe1.mediums.state.p (start = {5e6 for $i1 in 1:1}, min = {611.657 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1}) (68) [ALGB] (1) final input Real[1, 1] pipe3.heatTransfer.states.h = {pipe3.mediums[1].state.h} (start = {1e5 for $i1 in 1:1}, min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {5e5 for $i1 in 1:1}) (69) [ALGB] (1) Real[1] pipe1.Hb_flows (70) [ALGB] (1) final input Real[1, 1] pipe3.heatTransfer.states.d = {pipe3.mediums[1].state.d} (start = {150.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}) (71) [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}) (72) [ALGB] (2) final Real[2] pipe3.flowModel.crossAreas = pipe3.crossAreasFM (73) [ALGB] (2) final Real[2] pipe3.flowModel.dimensions = pipe3.dimensionsFM (74) [DISC] (1) Integer source.medium.state.phase (min = 0, max = 2) (75) [ALGB] (1) Real valve1.V_flow = valve1.m_flow / Modelica.Fluid.Utilities.regStep(valve1.m_flow, ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.valve1.Medium.density(valve1.state_a), ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.valve1.Medium.density(valve1.state_b), valve1.m_flow_small) (76) [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 = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}) (77) [ALGB] (1) Real source.medium.T_degC = Modelica.SIunits.Conversions.to_degC(-((-273.15) - source.medium.T_degC)) (78) [DISC] (1) Integer[1] pipe1.mediums.state.phase (min = {0 for $i1 in 1:1}, max = {2 for $i1 in 1:1}) (79) [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}) (80) [ALGB] (1) stream Real valve2.port_b.h_outflow (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (81) [DER-] (1) Real $DER.junctionIdeal.U (82) [ALGB] (2) Real[2] pipe1.flowModel.Fs_fg (83) [ALGB] (1) Real valve2.port_b_T = Modelica.Fluid.Utilities.regStep(-valve2.m_flow, ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.valve2.Medium.temperature(valve2.state_b), ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.valve2.Medium.temperature(ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.valve2.Medium.setState_phX(99999.99999999999 * junctionVolume.medium.p_bar, valve2.port_b.h_outflow, {}, 0, 0)), valve2.m_flow_small) (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (84) [ALGB] (1) Real source.medium.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (85) [DISC] (1) Integer sink.medium.state.phase (min = 0, max = 2) (86) [ALGB] (1) Real[1] pipe2.flowModel.Ib_flows (87) [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}) (88) [ALGB] (1) Real[1] pipe2.heatTransfer.Q_flows (89) [DISC] (1) Boolean[1] $SEV_30[$i1] (90) [ALGB] (2) protected Real[2] pipe1.dheightsFM (91) [DISC] (1) Integer junctionVolume.medium.phase (fixed = false, start = 1, min = 0, max = 2) (92) [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}) (93) [ALGB] (1) Real[1] pipe2.flowModel.Is (94) [ALGB] (1) Real source.medium.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (95) [DER-] (1) Real $DER.junctionIdeal.m (96) [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}) (97) [ALGB] (1) Real source.medium.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (98) [ALGB] (1) flow Real pipe1.port_b.m_flow (min = -1e5, max = 1e60) (99) [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) (100) [DISC] (1) Boolean $TEV_1 (101) [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}) (102) [DISC] (1) Boolean $TEV_0 (103) [ALGB] (2) protected Real[2] pipe1.pathLengths (104) [ALGB] (2) Real[2] pipe1.flowModel.rhos_act (start = {150.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2}) (105) [ALGB] (1) Real[1] pipe1.mediums.T_degC = {Modelica.SIunits.Conversions.to_degC(pipe1.mediums[1].T)} (106) [DISC] (1) protected Integer valve1.state_b.phase (min = 0, max = 2) (107) [DISC] (1) Integer[1] pipe3.mediums.state.phase (min = {0 for $i1 in 1:1}, max = {2 for $i1 in 1:1}) (108) [ALGB] (1) Real valve2.port_a_T = Modelica.Fluid.Utilities.regStep(valve2.m_flow, ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.valve2.Medium.temperature(valve2.state_a), ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.valve2.Medium.temperature(ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.valve2.Medium.setState_phX(pipe3.port_b.p, junctionVolume.port_3.h_outflow, {}, 0, 0)), valve2.m_flow_small) (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (109) [ALGB] (1) Real[1] pipe1.mediums.sat.psat (start = {5e6 for $i1 in 1:1}, min = {611.657 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1}) (110) [ALGB] (1) flow Real pipe3.port_a.m_flow (min = -1e60, max = 1e5) (111) [DISC] (1) Integer junctionVolume.medium.state.phase (min = 0, max = 2) (112) [ALGB] (1) Real[1] pipe3.mb_flows (min = {-1e5 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}) (113) [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 = {273.15 for $i1 in 1:2}, max = {2273.15 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2}) (114) [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) (115) [ALGB] (2) protected Real[2] pipe2.dimensionsFM (116) [ALGB] (2) protected Real[2] pipe2.crossAreasFM (117) [ALGB] (1) protected Real[1] pipe3.pathLengths (118) [ALGB] (1) stream Real junctionVolume.port_3.h_outflow (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (119) [ALGB] (1) Real junctionIdeal.Hb_flow (120) [ALGB] (9) final input Real[3, 3] pipe1.flowModel.states.p = {pipe1.statesFM[1].p, pipe1.statesFM[2].p, pipe1.statesFM[3].p} (start = {5e6 for $i1 in 1:3}, min = {611.657 for $i1 in 1:3}, max = {1e8 for $i1 in 1:3}, nominal = {1e6 for $i1 in 1:3}) (121) [ALGB] (4) Real[2, 2] pipe3.statesFM.p (start = {5e6 for $i1 in 1:2}, min = {611.657 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2}) (122) [ALGB] (1) Real[1] pipe1.Wb_flows (123) [ALGB] (1) Real junctionVolume.medium.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0, StateSelect = default) (124) [ALGB] (9) final input Real[3, 3] pipe1.flowModel.states.h = {pipe1.statesFM[1].h, pipe1.statesFM[2].h, pipe1.statesFM[3].h} (start = {1e5 for $i1 in 1:3}, min = {-1e10 for $i1 in 1:3}, max = {1e10 for $i1 in 1:3}, nominal = {5e5 for $i1 in 1:3}) (125) [ALGB] (4) final input Real[2, 2] pipe2.flowModel.states.d = {pipe2.statesFM[1].d, pipe2.statesFM[2].d} (start = {150.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2}) (126) [ALGB] (1) Real[1] pipe2.flowModel.Fs_fg (127) [ALGB] (4) Real[2, 2] pipe3.statesFM.h (start = {1e5 for $i1 in 1:2}, min = {-1e10 for $i1 in 1:2}, max = {1e10 for $i1 in 1:2}, nominal = {5e5 for $i1 in 1:2}) (128) [ALGB] (9) final input Real[3, 3] pipe1.flowModel.states.d = {pipe1.statesFM[1].d, pipe1.statesFM[2].d, pipe1.statesFM[3].d} (start = {150.0 for $i1 in 1:3}, min = {0.0 for $i1 in 1:3}, max = {1e5 for $i1 in 1:3}, nominal = {500.0 for $i1 in 1:3}) (129) [ALGB] (4) final input Real[2, 2] pipe2.flowModel.states.h = {pipe2.statesFM[1].h, pipe2.statesFM[2].h} (start = {1e5 for $i1 in 1:2}, min = {-1e10 for $i1 in 1:2}, max = {1e10 for $i1 in 1:2}, nominal = {5e5 for $i1 in 1:2}) (130) [ALGB] (4) Real[2, 2] pipe3.statesFM.d (start = {150.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2}) (131) [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 (132) [ALGB] (1) Real valve1.xs (133) [ALGB] (4) final input Real[2, 2] pipe2.flowModel.states.p = {pipe2.statesFM[1].p, pipe2.statesFM[2].p} (start = {5e6 for $i1 in 1:2}, min = {611.657 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2}) (134) [ALGB] (1) flow Real[1] pipe3.heatTransfer.heatPorts.Q_flow (135) [ALGB] (1) Real junctionVolume.medium.u (min = -1e8, max = 1e8, nominal = 1e6) (136) [ALGB] (1) Real source.medium.sat.psat (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (137) [ALGB] (1) protected Real valve1.minLimiter.y (138) [DISC] (1) final input Integer[1, 1] pipe2.heatTransfer.states.phase = {pipe2.mediums[1].state.phase} (min = {0 for $i1 in 1:1}, max = {2 for $i1 in 1:1}) (139) [ALGB] (1) Real[1] pipe2.Qb_flows (140) [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 = {273.15 for $i1 in 1:3}, max = {2273.15 for $i1 in 1:3}, nominal = {500.0 for $i1 in 1:3}) (141) [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 (142) [ALGB] (1) Real valve2.xs (143) [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}) (144) [ALGB] (4) Real[2, 2] pipe3.statesFM.T (start = {500.0 for $i1 in 1:2}, min = {273.15 for $i1 in 1:2}, max = {2273.15 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2}) (145) [DISC] (2) Boolean[2] $SEV_1[$i1] (146) [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}) (147) [ALGB] (2) final Real[2] pipe2.flowModel.vs = pipe2.vsFM (148) [ALGB] (1) Real[1] pipe3.mediums.state.p (start = {5e6 for $i1 in 1:1}, min = {611.657 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1}) (149) [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) (150) [ALGB] (1) Real[1] pipe2.flowModel.pathLengths_internal = pipe2.flowModel.pathLengths (151) [ALGB] (1) final Real[1] pipe1.heatTransfer.vs = pipe1.vs (152) [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 (153) [ALGB] (1) Real[1] pipe3.mediums.state.h (start = {1e5 for $i1 in 1:1}, min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {5e5 for $i1 in 1:1}) (154) [ALGB] (1) Real[1] pipe3.mediums.h (start = {pipe3.h_start}, StateSelect = prefer) (155) [ALGB] (1) Real[1] pipe2.flowModel.rhos_act (start = {150.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}) (156) [ALGB] (1) Real junctionVolume.Hb_flow (157) [ALGB] (2) Real[2] pipe3.flowModel.rhos = {ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.pipe3.flowModel.Medium.density(pipe3.flowModel.states[$i1]) for $i1 in 1:2} (start = {150.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2}) (158) [ALGB] (1) Real[1] pipe3.mediums.state.d (start = {150.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}) (159) [ALGB] (1) Real[1] pipe3.mediums.d (start = {150.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}, StateSelect = default) (160) [ALGB] (1) Real sink.medium.T_degC = Modelica.SIunits.Conversions.to_degC(-((-273.15) - sink.medium.T_degC)) (161) [ALGB] (1) Real pipe3.state_b.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (162) [ALGB] (1) Real[1] pipe3.flowModel.Fs_p (163) [ALGB] (2) Real[2] pipe1.flowModel.Res_turbulent_internal = pipe1.flowModel.Re_turbulent * {1.0 for $i1 in 1:2} (164) [DER-] (1) Real $DER.junctionVolume.U (165) [DISC] (1) protected Integer valveOpening2.last (start = 1) (166) [ALGB] (1) Real pipe3.state_b.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (167) [ALGB] (1) protected Real valve2.state_b.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (168) [ALGB] (4) Real[2, 2] pipe2.statesFM.p (start = {5e6 for $i1 in 1:2}, min = {611.657 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2}) (169) [ALGB] (1) Real[1] pipe3.mediums.state.T (start = {500.0 for $i1 in 1:1}, min = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}) (170) [ALGB] (1) Real[1] pipe3.mediums.T (start = {pipe3.T_start}, min = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}, StateSelect = default) (171) [ALGB] (1) Real pipe3.state_b.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (172) [ALGB] (1) flow Real junctionVolume.port_3.m_flow (min = -1e60, max = 1e60) (173) [ALGB] (1) protected Real[1] pipe2.flowModel.diameters = 0.5 * (pipe2.flowModel.dimensions[2:2] + pipe2.flowModel.dimensions[1:1]) (174) [ALGB] (1) protected Real valve2.state_b.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (175) [ALGB] (4) Real[2, 2] pipe2.statesFM.h (start = {1e5 for $i1 in 1:2}, min = {-1e10 for $i1 in 1:2}, max = {1e10 for $i1 in 1:2}, nominal = {5e5 for $i1 in 1:2}) (176) [DISC] (1) Boolean[1] $SEV_26[$i1] (177) [ALGB] (1) Real[1] pipe2.Hb_flows (178) [ALGB] (2) Real[2] pipe1.flowModel.Ib_flows (179) [ALGB] (1) protected Real valve2.state_b.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (180) [DISC] (2) Boolean[2] $SEV_0[$i1] (181) [ALGB] (4) Real[2, 2] pipe2.statesFM.d (start = {150.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2}) (182) [ALGB] (1) Real[1] pipe2.flowModel.Res_turbulent_internal = pipe2.flowModel.Re_turbulent * {1.0 for $i1 in 1:1} (183) [DER-] (1) Real $DER.junctionVolume.m (184) [ALGB] (1) Real pipe3.state_b.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (185) [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}) (186) [ALGB] (1) Real sink.medium.sat.psat (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (187) [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) (188) [ALGB] (1) Real valve2.dp_turbulent = max(valve2.dp_small, ((ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.valve2.Medium.dynamicViscosity(valve2.state_a) + ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.valve2.Medium.dynamicViscosity(valve2.state_b)) ^ 2.0 * 3.141592653589793 * 1.6e7) / (8.0 * valve2.Y * max(ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.valve2.valveCharacteristic(valveOpening2.y), 0.001) * valve2.Av * (ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.valve2.Medium.density(valve2.state_b) + ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.valve2.Medium.density(valve2.state_a)))) (min = 0.0, nominal = 1e5) (189) [ALGB] (1) protected Real valve2.state_b.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (190) [ALGB] (1) Real[1] pipe3.heatTransfer.Ts = {ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.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}) (191) [ALGB] (4) Real[2, 2] pipe2.statesFM.T (start = {500.0 for $i1 in 1:2}, min = {273.15 for $i1 in 1:2}, max = {2273.15 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2}) (192) [ALGB] (1) Real[1] pipe1.heatTransfer.Q_flows (193) [ALGB] (3) protected Real[3] pipe1.roughnessesFM (min = {0.0 for $i1 in 1:3}) (194) [ALGB] (1) flow Real[1] source.ports.m_flow (min = {-1e60}, max = {1e60}) (195) [ALGB] (1) Real[1] pipe1.mediums.h (start = {pipe1.h_start}, StateSelect = prefer) (196) [ALGB] (1) Real source.medium.u (min = -1e8, max = 1e8, nominal = 1e6) (197) [ALGB] (1) Real[1] pipe1.mediums.d (start = {150.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}, StateSelect = default) (198) [ALGB] (1) Real pipe3.state_a.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (199) [ALGB] (1) Real pipe1.port_a.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (200) [DISC] (1) protected Integer valveOpening1.last (start = 1) (201) [ALGB] (1) Real pipe1.state_b.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (202) [ALGB] (1) Real[1] pipe3.flowModel.dps_fg (start = {pipe3.flowModel.p_a_start - pipe3.flowModel.p_b_start for $i1 in 1:1}) (203) [ALGB] (1) final Real[1] pipe3.fluidVolumes = {pipe3.crossAreas[1] * 10.0} .* pipe3.nParallel (204) [ALGB] (1) Real junctionIdeal.medium.sat.Tsat (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (205) [ALGB] (1) Real[1] pipe3.mediums.sat.psat (start = {5e6 for $i1 in 1:1}, min = {611.657 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1}) (206) [ALGB] (2) protected Real[2] pipe1.flowModel.diameters = 0.5 * (pipe1.flowModel.dimensions[2:3] + pipe1.flowModel.dimensions[1:2]) (207) [ALGB] (1) Real pipe3.state_a.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (208) [ALGB] (1) protected Real valve2.state_a.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (209) [ALGB] (1) Real[1] pipe3.flowModel.pathLengths_internal = pipe3.flowModel.pathLengths (210) [ALGB] (1) Real pipe1.state_b.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (211) [ALGB] (1) Real pipe3.state_a.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (212) [ALGB] (1) Real source.medium.h (StateSelect = default) (213) [DISC] (1) protected discrete Real valveOpening1.nextEventScaled (fixed = true, start = 0.0) (214) [ALGB] (3) protected Real[3] pipe1.vsFM (215) [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) (216) [ALGB] (1) Real[1] pipe1.mediums.T (start = {pipe1.T_start}, min = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}, StateSelect = default) (217) [ALGB] (1) Real pipe1.state_b.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (218) [DISC] (1) Boolean $SEV_64 (219) [ALGB] (1) Real source.medium.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0, StateSelect = default) (220) [DISC] (1) Boolean $SEV_63 (221) [ALGB] (1) protected Real valve2.state_a.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (222) [ALGB] (2) protected Real[2] pipe2.roughnessesFM (min = {0.0 for $i1 in 1:2}) (223) [DISC] (1) Boolean $SEV_62 (224) [ALGB] (1) Real junctionIdeal.mb_flow (225) [ALGB] (1) Real junctionVolume.medium.sat.psat (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (226) [DISC] (1) Boolean $SEV_61 (227) [DISC] (1) Boolean $SEV_60 (228) [ALGB] (1) Real[1] pipe1.heatTransfer.Ts = {ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.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}) (229) [ALGB] (1) protected Real valve2.state_a.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (230) [ALGB] (9) Real[3, 3] pipe1.statesFM.p (start = {5e6 for $i1 in 1:3}, min = {611.657 for $i1 in 1:3}, max = {1e8 for $i1 in 1:3}, nominal = {1e6 for $i1 in 1:3}) (231) [ALGB] (1) Real pipe3.state_a.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (232) [DER-] (1) Real[1] $DER.pipe3.ms (233) [DISC] (1) protected discrete Real valveOpening2.nextEvent (fixed = true, start = 0.0) (234) [ALGB] (9) Real[3, 3] pipe1.statesFM.h (start = {1e5 for $i1 in 1:3}, min = {-1e10 for $i1 in 1:3}, max = {1e10 for $i1 in 1:3}, nominal = {5e5 for $i1 in 1:3}) (235) [ALGB] (1) Real pipe1.state_b.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (236) [ALGB] (1) Real[1] pipe3.flowModel.Ib_flows (237) [ALGB] (1) stream Real pipe2.port_a.h_outflow (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (238) [ALGB] (9) Real[3, 3] pipe1.statesFM.d (start = {150.0 for $i1 in 1:3}, min = {0.0 for $i1 in 1:3}, max = {1e5 for $i1 in 1:3}, nominal = {500.0 for $i1 in 1:3}) (239) [ALGB] (1) protected Real valve2.state_a.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (240) [ALGB] (1) Real sink.medium.u (min = -1e8, max = 1e8, nominal = 1e6) (241) [ALGB] (2) final Real[2] pipe3.flowModel.roughnesses = pipe3.roughnessesFM (min = {0.0 for $i1 in 1:2}) (242) [DER-] (1) Real[1] $DER.pipe2.ms (243) [DISC] (1) protected Integer valve2.state_b.phase (min = 0, max = 2) (244) [ALGB] (1) stream Real pipe1.port_a.h_outflow (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (245) [ALGB] (1) Real junctionVolume.medium.T_degC = Modelica.SIunits.Conversions.to_degC(-((-273.15) - junctionVolume.medium.T_degC)) (246) [DISC] (1) Boolean $SEV_59 (247) [DISC] (1) Boolean $SEV_58 (248) [DISC] (1) Boolean $SEV_57 (249) [DISC] (4) Integer[2, 2] pipe3.statesFM.phase (min = {0 for $i1 in 1:2}, max = {2 for $i1 in 1:2}) (250) [DISC] (4) final input Integer[2, 2] pipe3.flowModel.states.phase = {pipe3.statesFM[1].phase, pipe3.statesFM[2].phase} (min = {0 for $i1 in 1:2}, max = {2 for $i1 in 1:2}) (251) [DISC] (1) Boolean $SEV_56 (252) [DISC] (1) Boolean $SEV_55 (253) [DISC] (1) Boolean $SEV_54 (254) [ALGB] (1) Real sink.medium.h (StateSelect = default) (255) [ALGB] (1) Real[1] pipe2.mediums.state.p (start = {5e6 for $i1 in 1:1}, min = {611.657 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1}) (256) [ALGB] (1) Real pipe1.state_a.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (257) [ALGB] (9) Real[3, 3] pipe1.statesFM.T (start = {500.0 for $i1 in 1:3}, min = {273.15 for $i1 in 1:3}, max = {2273.15 for $i1 in 1:3}, nominal = {500.0 for $i1 in 1:3}) (258) [ALGB] (1) Real[1] pipe3.heatTransfer.Q_flows (259) [DISC] (1) Boolean $SEV_51 (260) [DER-] (1) Real[1] $DER.pipe1.ms (261) [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}) (262) [ALGB] (1) Real sink.medium.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0, StateSelect = default) (263) [ALGB] (2) protected Real[2] pipe2.vsFM (264) [ALGB] (1) Real[1] pipe2.mediums.state.h (start = {1e5 for $i1 in 1:1}, min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {5e5 for $i1 in 1:1}) (265) [ALGB] (1) Real pipe1.state_a.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (266) [ALGB] (1) Real valve1.dp (start = valve1.dp_start) (267) [ALGB] (2) protected Real[2] pipe3.roughnessesFM (min = {0.0 for $i1 in 1:2}) (268) [ALGB] (1) Real[1] pipe2.mediums.state.d (start = {150.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}) (269) [ALGB] (1) Real pipe1.state_a.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (270) [ALGB] (1) Real junctionVolume.mb_flow (271) [ALGB] (1) Real[1] pipe2.heatTransfer.Ts = {ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.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}) (272) [ALGB] (1) Real[1] pipe2.Wb_flows (273) [ALGB] (1) Real[1] pipe3.flowModel.Is (274) [ALGB] (1) final Real[1] pipe3.heatTransfer.vs = pipe3.vs (275) [ALGB] (1) Real valve2.dp (start = valve2.dp_start) (276) [ALGB] (1) Real[1] pipe1.mediums.sat.Tsat (start = {500.0 for $i1 in 1:1}, min = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}) (277) [ALGB] (1) Real[1] pipe2.flowModel.dps_fg (start = {pipe2.flowModel.p_a_start - pipe2.flowModel.p_b_start for $i1 in 1:1}) (278) [DISC] (1) Integer pipe1.state_b.phase (min = 0, max = 2) (279) [ALGB] (1) Real[1] pipe2.mediums.state.T (start = {500.0 for $i1 in 1:1}, min = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}) (280) [ALGB] (1) final Real[1] pipe2.flowModel.dheights = pipe2.dheightsFM (281) [ALGB] (1) Real pipe1.state_a.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (282) [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 = {273.15 for $i1 in 1:2}, max = {2273.15 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2}) (283) [ALGB] (1) Real junctionIdeal.medium.T_degC = Modelica.SIunits.Conversions.to_degC(-((-273.15) - junctionIdeal.medium.T_degC)) (284) [DISC] (1) Integer junctionIdeal.medium.phase (fixed = false, start = 1, min = 0, max = 2) (285) [DISC] (1) Boolean $SEV_47 (286) [DISC] (1) Boolean $SEV_46 (287) [DISC] (1) Boolean $SEV_45 (288) [ALGB] (1) Real[1] pipe1.mb_flows (min = {-1e5 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}) (289) [DISC] (1) Boolean $SEV_44 (290) [DISC] (1) Boolean $SEV_43 (291) [DISC] (1) Boolean $SEV_42 (292) [DISC] (1) Boolean $SEV_41 (293) [DISC] (1) Boolean $SEV_40 (294) [ALGB] (2) final Real[2] pipe2.flowModel.dimensions = pipe2.dimensionsFM (295) [ALGB] (2) final Real[2] pipe2.flowModel.crossAreas = pipe2.crossAreasFM (296) [DISC] (1) protected discrete Real valveOpening2.nextEventScaled (fixed = true, start = 0.0) (297) [DISC] (1) Integer source.medium.phase (fixed = false, start = 1, min = 0, max = 2) (298) [ALGB] (1) Real[1] pipe3.Qb_flows (299) [ALGB] (1) Real $FUN_9 (300) [ALGB] (4) final input Real[2, 2] pipe3.flowModel.states.d = {pipe3.statesFM[1].d, pipe3.statesFM[2].d} (start = {150.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2}) (301) [ALGB] (1) Real $FUN_8 (302) [ALGB] (1) Real $FUN_27 (303) [ALGB] (1) protected Real pipe3.flowModel.dp_fric_nominal = sum({ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.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) (304) [ALGB] (1) Real $FUN_7 (305) [ALGB] (1) Real $FUN_6 (306) [ALGB] (1) Real $FUN_25 (307) [ALGB] (1) final Real[1] pipe1.fluidVolumes = {pipe1.crossAreas[1] * 10.0} .* pipe1.nParallel (308) [ALGB] (1) Real $FUN_5 (309) [ALGB] (4) final input Real[2, 2] pipe3.flowModel.states.h = {pipe3.statesFM[1].h, pipe3.statesFM[2].h} (start = {1e5 for $i1 in 1:2}, min = {-1e10 for $i1 in 1:2}, max = {1e10 for $i1 in 1:2}, nominal = {5e5 for $i1 in 1:2}) (310) [ALGB] (1) Real $FUN_4 (311) [ALGB] (1) Real $FUN_23 (312) [ALGB] (1) Real $FUN_3 (313) [DISC] (1) Integer $FUN_22 (314) [ALGB] (2) protected Real[2] pipe3.vsFM (315) [ALGB] (1) Real $FUN_2 (316) [ALGB] (1) Real $FUN_21 (317) [ALGB] (1) Real $FUN_1 (318) [ALGB] (1) Real $FUN_20 (319) [ALGB] (4) final input Real[2, 2] pipe3.flowModel.states.p = {pipe3.statesFM[1].p, pipe3.statesFM[2].p} (start = {5e6 for $i1 in 1:2}, min = {611.657 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2}) (320) [DISC] (4) final input Integer[2, 2] pipe2.flowModel.states.phase = {pipe2.statesFM[1].phase, pipe2.statesFM[2].phase} (min = {0 for $i1 in 1:2}, max = {2 for $i1 in 1:2}) (321) [ALGB] (2) protected Real[2] pipe3.crossAreasFM (322) [ALGB] (2) protected Real[2] pipe3.dimensionsFM (323) [ALGB] (1) Real junctionVolume.medium.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (324) [DISC] (1) Boolean $SEV_39 (325) [DISC] (1) Boolean $SEV_38 (326) [DISC] (1) Boolean $SEV_37 (327) [ALGB] (1) Real[1] pipe2.mediums.sat.psat (start = {5e6 for $i1 in 1:1}, min = {611.657 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1}) (328) [DISC] (1) Boolean $SEV_36 (329) [DISC] (1) Boolean $SEV_35 (330) [ALGB] (1) Real junctionIdeal.medium.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0, StateSelect = default) (331) [DISC] (1) Boolean $SEV_32 (332) [ALGB] (1) Real[1] sink.ports.p (start = {5e6 for $i1 in 1:1}, min = {611.657 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1}) (333) [ALGB] (1) Real pipe2.port_b.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (334) [ALGB] (1) flow Real pipe2.port_a.m_flow (min = -1e60, max = 1e5) (335) [ALGB] (1) Real junctionVolume.medium.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (336) [ALGB] (1) Real $FUN_19 (337) [ALGB] (1) Real junctionIdeal.medium.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (338) [DISC] (1) Integer $FUN_18 (339) [ALGB] (1) Real $FUN_17 (340) [ALGB] (1) Real $FUN_16 (341) [ALGB] (1) Real junctionVolume.medium.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (342) [ALGB] (1) Real $FUN_15 (343) [ALGB] (1) Real[1] pipe3.flowModel.rhos_act (start = {150.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}) (344) [ALGB] (1) Real $FUN_14 (345) [DISC] (1) Boolean[1] $SEV_49[$i1] (346) [ALGB] (1) Real $FUN_13 (347) [ALGB] (1) Real $FUN_12 (348) [ALGB] (1) Real sink.medium.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (349) [ALGB] (1) Real junctionIdeal.medium.u (min = -1e8, max = 1e8, nominal = 1e6) (350) [DISC] (1) Integer junctionIdeal.medium.state.phase (min = 0, max = 2) (351) [ALGB] (1) Real $FUN_11 (352) [DISC] (1) Integer pipe3.state_a.phase (min = 0, max = 2) (353) [ALGB] (1) Real junctionIdeal.medium.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (354) [ALGB] (1) Real $FUN_10 (355) [ALGB] (1) final Real[1] pipe3.flowModel.pathLengths = pipe3.pathLengths (356) [ALGB] (1) Real sink.medium.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (357) [ALGB] (1) Real[1] pipe3.Hb_flows (358) [ALGB] (1) Real junctionVolume.medium.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (359) [ALGB] (1) Real junctionIdeal.medium.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (360) [ALGB] (3) final Real[3] pipe1.flowModel.roughnesses = pipe1.roughnessesFM (min = {0.0 for $i1 in 1:3}) (361) [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}) (362) [DISC] (1) Integer[1] pipe1.mediums.phase (fixed = {false for $i1 in 1:1}, start = {1 for $i1 in 1:1}, min = {0 for $i1 in 1:1}, max = {2 for $i1 in 1:1}) (363) [ALGB] (1) stream Real pipe3.port_a.h_outflow (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (364) [DISC] (1) Boolean $SEV_29 (365) [DISC] (1) Boolean $SEV_28 (366) [ALGB] (1) final Real[1] pipe2.heatTransfer.vs = pipe2.vs (367) [DISC] (1) Boolean $SEV_25 (368) [DISC] (1) Boolean $SEV_24 (369) [ALGB] (2) final Real[2] pipe3.flowModel.vs = pipe3.vsFM (370) [DISC] (1) Boolean $SEV_21 (371) [ALGB] (1) protected Real pipe1.flowModel.dp_fric_nominal = sum(ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.pipe1.flowModel.WallFriction.pressureLoss_m_flow(pipe1.flowModel.m_flow_nominal / pipe1.flowModel.nParallel, pipe1.flowModel.rho_nominal, pipe1.flowModel.rho_nominal, pipe1.flowModel.mu_nominal, pipe1.flowModel.mu_nominal, pipe1.flowModel.pathLengths_internal[$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) (372) [DISC] (1) Boolean $SEV_20 (373) [ALGB] (1) flow Real[1] sink.ports.m_flow (min = {-1e60}, max = {1e60}) (374) [ALGB] (1) Real sink.medium.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (375) [ALGB] (1) Real junctionIdeal.medium.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (376) [ALGB] (1) Real valve2.x (377) [ALGB] (1) Real[1] pipe3.flowModel.Res_turbulent_internal = pipe3.flowModel.Re_turbulent * {1.0 for $i1 in 1:1} (378) [ALGB] (2) Real[2] pipe1.flowModel.Is (379) [DISC] (1) final input Integer[1, 1] pipe1.heatTransfer.states.phase = {pipe1.mediums[1].state.phase} (min = {0 for $i1 in 1:1}, max = {2 for $i1 in 1:1}) (380) [ALGB] (1) Real valve2.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (381) [ALGB] (1) Real[1] pipe3.mediums.p_bar = {Modelica.SIunits.Conversions.to_bar(pipe3.mediums[1].p)} (382) [ALGB] (1) stream Real[1] sink.ports.h_outflow (start = {1e5 for $i1 in 1:1}, min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {5e5 for $i1 in 1:1}) (383) [ALGB] (1) Real junctionIdeal.medium.p_bar = Modelica.SIunits.Conversions.to_bar(99999.99999999999 * junctionIdeal.medium.p_bar) (384) [DISC] (2) Boolean[2] $SEV_48[$i1] (385) [ALGB] (1) Real[1] pipe3.flowModel.Fs_fg (386) [DISC] (1) Boolean $SEV_19 (387) [DISC] (1) Boolean $SEV_18 (388) [DISC] (1) Boolean $SEV_15 (389) [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}) (390) [DISC] (1) Boolean $SEV_14 (391) [DISC] (1) Boolean $SEV_13 (392) [DISC] (1) protected Integer valve2.state_a.phase (min = 0, max = 2) (393) [ALGB] (1) Real valveOpening2.y (394) [ALGB] (1) Real junctionIdeal.medium.sat.psat (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (395) [ALGB] (1) Real[1] pipe3.mediums.sat.Tsat (start = {500.0 for $i1 in 1:1}, min = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}) (396) [ALGB] (1) Real valve2.Y (397) [ALGB] (1) Real valve1.port_b_T = Modelica.Fluid.Utilities.regStep(-valve1.m_flow, ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.valve1.Medium.temperature(valve1.state_b), ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.valve1.Medium.temperature(ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.valve1.Medium.setState_phX(99999.99999999999 * junctionVolume.medium.p_bar, valve1.port_b.h_outflow, {}, 0, 0)), valve1.m_flow_small) (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (398) [ALGB] (1) stream Real[1] source.ports.h_outflow (start = {1e5 for $i1 in 1:1}, min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {5e5 for $i1 in 1:1}) (399) [ALGB] (3) protected Real[3] pipe1.dimensionsFM (400) [ALGB] (3) protected Real[3] pipe1.crossAreasFM (401) [ALGB] (1) Real valve1.dp_turbulent = max(valve1.dp_small, ((ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.valve1.Medium.dynamicViscosity(valve1.state_a) + ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.valve1.Medium.dynamicViscosity(valve1.state_b)) ^ 2.0 * 3.141592653589793 * 1.6e7) / (8.0 * valve1.Y * max(ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.valve1.valveCharacteristic(valveOpening1.y), 0.001) * valve1.Av * (ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.valve1.Medium.density(valve1.state_b) + ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.valve1.Medium.density(valve1.state_a)))) (min = 0.0, nominal = 1e5) (402) [ALGB] (1) Real junctionVolume.medium.sat.Tsat (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (403) [ALGB] (1) flow Real[1] pipe1.heatTransfer.heatPorts.Q_flow (404) [ALGB] (1) Real[1] pipe2.flowModel.Fs_p (405) [ALGB] (2) Real[2] pipe1.flowModel.Fs_p (406) [ALGB] (1) Real valve1.x (407) [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 $i1 in 1:1}) (408) [ALGB] (1) final Real[1] pipe2.flowModel.pathLengths = pipe2.pathLengths (409) [DISC] (1) protected Real valveOpening2.b (410) [ALGB] (1) Real[1] pipe2.mediums.p_bar = {Modelica.SIunits.Conversions.to_bar(pipe2.mediums[1].p)} (411) [DISC] (1) protected Real valveOpening2.a (412) [ALGB] (2) Real[2] pipe2.flowModel.rhos = {ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.pipe2.flowModel.Medium.density(pipe2.flowModel.states[$i1]) for $i1 in 1:2} (start = {150.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2}) (413) [ALGB] (3) Real[3] pipe1.flowModel.rhos = {ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.pipe1.flowModel.Medium.density(pipe1.flowModel.states[$i1]) for $i1 in 1:3} (start = {150.0 for $i1 in 1:3}, min = {0.0 for $i1 in 1:3}, max = {1e5 for $i1 in 1:3}, nominal = {500.0 for $i1 in 1:3}) (414) [ALGB] (1) Real valve1.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (415) [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}) (416) [ALGB] (1) protected Real pipe2.flowModel.dp_fric_nominal = sum({ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.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) (417) [ALGB] (1) final input Real[1, 1] pipe1.heatTransfer.states.p = {pipe1.mediums[1].state.p} (start = {5e6 for $i1 in 1:1}, min = {611.657 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1}) (418) [DISC] (1) Integer pipe1.state_a.phase (min = 0, max = 2) (419) [ALGB] (1) Real[1] source.ports.p (start = {5e6 for $i1 in 1:1}, min = {611.657 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1}) (420) [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) (421) [ALGB] (1) final input Real[1, 1] pipe1.heatTransfer.states.h = {pipe1.mediums[1].state.h} (start = {1e5 for $i1 in 1:1}, min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {5e5 for $i1 in 1:1}) (422) [ALGB] (1) protected Real[1] pipe3.flowModel.diameters = 0.5 * (pipe3.flowModel.dimensions[2:2] + pipe3.flowModel.dimensions[1:1]) (423) [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}) (424) [ALGB] (1) final input Real[1, 1] pipe1.heatTransfer.states.d = {pipe1.mediums[1].state.d} (start = {150.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}) (425) [ALGB] (1) Real valve2.m_flow (start = valve2.m_flow_start, min = -1e60, max = 1e5) (426) [ALGB] (1) flow Real[1] pipe2.heatTransfer.heatPorts.Q_flow (427) [ALGB] (1) Real[1] pipe2.mediums.h (start = {pipe2.h_start}, StateSelect = prefer) (428) [ALGB] (1) protected Real valve2.minLimiter.y (429) [ALGB] (1) Real[1] pipe2.mediums.d (start = {150.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}, StateSelect = default) (430) [ALGB] (1) Real[1] pipe3.Wb_flows (431) [ALGB] (1) Real valveOpening1.y (432) [ALGB] (2) final Real[2] pipe1.flowModel.pathLengths = pipe1.pathLengths (433) [ALGB] (1) Real[1] pipe1.mediums.p_bar = {Modelica.SIunits.Conversions.to_bar(pipe1.mediums[1].p)} (434) [ALGB] (1) Real pipe2.state_b.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (435) [ALGB] (1) Real valve1.Y (436) [ALGB] (3) final Real[3] pipe1.flowModel.vs = pipe1.vsFM (437) [ALGB] (2) Real[2] pipe1.flowModel.pathLengths_internal = pipe1.flowModel.pathLengths (438) [ALGB] (1) Real valve1.port_a_T = Modelica.Fluid.Utilities.regStep(valve1.m_flow, ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.valve1.Medium.temperature(valve1.state_a), ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.valve1.Medium.temperature(ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.valve1.Medium.setState_phX(pipe2.port_b.p, junctionVolume.port_3.h_outflow, {}, 0, 0)), valve1.m_flow_small) (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (439) [ALGB] (1) stream Real valve1.port_b.h_outflow (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (440) [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 = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}) System Equations (403/546) **************************** (1) [SCAL] (1) valve1.m_flow = homotopy(valve1.Y * valve1.Av * valveOpening1.y * smooth(2, if $SEV_42 then (if $SEV_43 then sqrt(valve1.state_a.d) else 0.0) * sqrt(valve1.xs * valve1.p) else if $SEV_44 then -(if $SEV_45 then sqrt(valve1.state_b.d) else 0.0) * sqrt(abs(valve1.xs * valve1.p)) else if $SEV_46 then Modelica.Fluid.Utilities.regRoot2.regRoot2_utility(valve1.xs * valve1.p, valve1.dp_turbulent, valve1.state_a.d, valve1.state_b.d, false, 1.0) else -Modelica.Fluid.Utilities.regRoot2.regRoot2_utility(-valve1.xs * valve1.p, valve1.dp_turbulent, valve1.state_b.d, valve1.state_a.d, false, 1.0)), (valve1.dp * valve1.m_flow_nominal * valveOpening1.y) / valve1.dp_nominal) ($RES_SIM_255) (2) [ARRY] (3) pipe1.flowModel.roughnesses = pipe1.roughnessesFM ($RES_BND_380) (3) [SCAL] (1) valve1.Y = 1.0 - (0.3333333333333333 * $FUN_5) / valve1.Fxt_full ($RES_SIM_256) (4) [ARRY] (2) pipe1.flowModel.dheights = pipe1.dheightsFM ($RES_BND_381) (5) [SCAL] (1) valve1.xs = max(-valve1.Fxt_full, min(valve1.x, valve1.Fxt_full)) ($RES_SIM_257) (6) [ARRY] (2) pipe1.flowModel.pathLengths = pipe1.pathLengths ($RES_BND_382) (7) [SCAL] (1) valve1.x = valve1.dp / valve1.p ($RES_SIM_258) (8) [FOR-] (3) ($RES_BND_383) (8) [----] for $i1 in 1:3 loop (8) [----] [SCAL] (1) pipe1.flowModel.rhos[$i1] = pipe1.flowModel.states.d ($RES_BND_384) (8) [----] end for; (9) [SCAL] (1) valve1.state_a.d = Modelica.Media.Water.IF97_Utilities.rho_ph(pipe2.port_b.p, valve1.port_b.h_outflow, 0, 0) ($RES_SIM_510) (10) [FOR-] (3) ($RES_BND_385) (10) [----] for $i1 in 1:3 loop (10) [----] [SCAL] (1) pipe1.flowModel.mus[$i1] = pipe1.flowModel.mu_nominal ($RES_BND_386) (10) [----] end for; (11) [SCAL] (1) valve1.state_a.T = Modelica.Media.Water.IF97_Utilities.T_ph(pipe2.port_b.p, valve1.port_b.h_outflow, 0, 0) ($RES_SIM_511) (12) [SCAL] (1) valve1.state_a.p = pipe2.port_b.p ($RES_SIM_512) (13) [ARRY] (2) pipe1.flowModel.pathLengths_internal = pipe1.flowModel.pathLengths ($RES_BND_387) (14) [SCAL] (1) valve1.state_b.phase = 0 ($RES_SIM_513) (15) [FOR-] (2) ($RES_BND_388) (15) [----] for $i1 in 1:2 loop (15) [----] [SCAL] (1) pipe1.flowModel.Res_turbulent_internal[$i1] = pipe1.flowModel.Re_turbulent ($RES_BND_389) (15) [----] end for; (16) [SCAL] (1) valve1.state_b.h = junctionVolume.port_3.h_outflow ($RES_SIM_514) (17) [SCAL] (1) valve1.state_b.d = Modelica.Media.Water.IF97_Utilities.rho_ph(99999.99999999999 * junctionVolume.medium.p_bar, junctionVolume.port_3.h_outflow, 0, 0) ($RES_SIM_515) (18) [SCAL] (1) -((-273.15) - source.medium.T_degC) = Modelica.Media.Water.IF97_Utilities.T_props_ph(source.p, source.medium.h, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(source.p, source.medium.h, source.medium.phase, 0)) ($RES_SIM_341) (19) [SCAL] (1) valve1.state_b.T = Modelica.Media.Water.IF97_Utilities.T_ph(99999.99999999999 * junctionVolume.medium.p_bar, junctionVolume.port_3.h_outflow, 0, 0) ($RES_SIM_516) (20) [SCAL] (1) source.medium.d = Modelica.Media.Water.IF97_Utilities.rho_props_ph(source.p, source.medium.h, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(source.p, source.medium.h, source.medium.phase, 0)) ($RES_SIM_342) (21) [SCAL] (1) valve1.state_b.p = 99999.99999999999 * junctionVolume.medium.p_bar ($RES_SIM_517) (22) [SCAL] (1) source.medium.phase = if $SEV_54 then 1 else 2 ($RES_SIM_343) (23) [SCAL] (1) valve2.state_a.phase = 0 ($RES_SIM_518) (24) [SCAL] (1) valve2.state_a.h = valve2.port_b.h_outflow ($RES_SIM_519) (25) [SCAL] (1) junctionVolume.port_3.m_flow + sink.ports[1].m_flow = 0.0 ($RES_SIM_345) (26) [SCAL] (1) pipe2.H_flows[2] = -$FUN_10 ($RES_SIM_170) (27) [SCAL] (1) pipe2.H_flows[1] = $FUN_9 ($RES_SIM_171) (28) [SCAL] (1) pipe3.heatTransfer.heatPorts[1].Q_flow = 0.0 ($RES_SIM_347) (29) [SCAL] (1) pipe2.mb_flows[1] = pipe2.m_flows[1] - pipe2.m_flows[2] ($RES_SIM_172) (30) [SCAL] (1) pipe2.Hb_flows[1] = pipe2.H_flows[1] - pipe2.H_flows[2] ($RES_SIM_173) (31) [SCAL] (1) pipe2.heatTransfer.heatPorts[1].Q_flow = 0.0 ($RES_SIM_349) (32) [ARRY] (2) pipe2.roughnessesFM[:] = {pipe2.roughnesses[1], pipe2.roughnesses[1]} ($RES_SIM_174) (33) [ARRY] (2) pipe2.dimensionsFM[:] = {pipe2.dimensions[1], pipe2.dimensions[1]} ($RES_SIM_175) (34) [ARRY] (2) pipe2.crossAreasFM[:] = {pipe2.crossAreas[1], pipe2.crossAreas[1]} ($RES_SIM_176) (35) [ARRY] (1) pipe2.dheightsFM[:] = {0.0} ($RES_SIM_177) (36) [ARRY] (1) pipe2.pathLengths[:] = {10.0} ($RES_SIM_178) (37) [ARRY] (1) pipe2.Wb_flows = (pipe2.crossAreas * pipe2.vs * (($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 ($RES_SIM_179) (38) [SCAL] (1) valve1.p = max(pipe2.port_b.p, 99999.99999999999 * junctionVolume.medium.p_bar) ($RES_SIM_260) (39) [SCAL] (1) valve1.minLimiter.y = smooth(0, noEvent(if $SEV_47 then valve1.minLimiter.uMin else valveOpening1.y)) ($RES_SIM_261) (40) [SCAL] (1) $DER.pipe1.ms[1] = pipe1.mb_flows[1] ($RES_SIM_262) (41) [SCAL] (1) $DER.pipe1.Us[1] = pipe1.Wb_flows[1] + pipe1.Hb_flows[1] + pipe1.Qb_flows[1] ($RES_SIM_263) (42) [SCAL] (1) pipe1.ms[1] = pipe1.fluidVolumes[1] * pipe1.mediums[1].d ($RES_SIM_264) (43) [SCAL] (1) pipe1.Us[1] = pipe1.ms[1] * pipe1.mediums[1].u ($RES_SIM_265) (44) [ARRY] (2) pipe1.flowModel.diameters = 0.5 * (pipe1.flowModel.dimensions[2:3] + pipe1.flowModel.dimensions[1:2]) ($RES_BND_390) (45) [SCAL] (1) pipe1.vsFM[3] = ((pipe1.m_flows[2] / pipe1.state_b.d) / pipe1.crossAreas[1]) / pipe1.nParallel ($RES_SIM_266) (46) [ARRY] (1) pipe1.vsFM[2:2] = pipe1.vs ($RES_SIM_267) (47) [ARRY] (1) pipe1.vs = {(0.5 * (pipe1.m_flows[2] + pipe1.m_flows[1])) / (pipe1.crossAreas[1] * pipe1.mediums[1].d)} / pipe1.nParallel ($RES_BND_392) (48) [SCAL] (1) pipe1.vsFM[1] = ((pipe1.m_flows[1] / pipe1.state_a.d) / pipe1.crossAreas[1]) / pipe1.nParallel ($RES_SIM_268) (49) [ARRY] (2) pipe1.m_flows[:] = pipe1.flowModel.m_flows[:] ($RES_SIM_269) (50) [ARRY] (1) pipe1.heatTransfer.Ts = {pipe1.heatTransfer.states.h} ($RES_BND_394) (51) [SCAL] (1) valve2.state_a.d = Modelica.Media.Water.IF97_Utilities.rho_ph(pipe3.port_b.p, valve2.port_b.h_outflow, 0, 0) ($RES_SIM_520) (52) [SCAL] (1) $TEV_0 = $PRE.valveOpening2.nextEvent ($RES_EVT_565) (53) [ARRY] (1) pipe1.heatTransfer.vs = pipe1.vs ($RES_BND_395) (54) [SCAL] (1) valve2.state_a.T = Modelica.Media.Water.IF97_Utilities.T_ph(pipe3.port_b.p, valve2.port_b.h_outflow, 0, 0) ($RES_SIM_521) (55) [SCAL] (1) $TEV_1 = $PRE.valveOpening1.nextEvent ($RES_EVT_566) (56) [SCAL] (1) valve2.state_a.p = pipe3.port_b.p ($RES_SIM_522) (57) [FOR-] (2) ($RES_EVT_567) (57) [----] for $i1 in 1:2 loop (57) [----] [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_568) (57) [----] end for; (58) [SCAL] (1) valve2.state_b.phase = 0 ($RES_SIM_523) (59) [SCAL] (1) valve2.state_b.h = junctionVolume.port_3.h_outflow ($RES_SIM_524) (60) [FOR-] (2) ($RES_EVT_569) (60) [----] for $i1 in 1:2 loop (60) [----] [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_570) (60) [----] end for; (61) [SCAL] (1) valve1.V_flow = valve1.m_flow / smooth(1, if $SEV_63 then valve1.state_a.d else if $SEV_64 then valve1.state_b.d else if $SEV_62 then 0.25 * (valve1.state_b.d - valve1.state_a.d) * ((-3.0) + (valve1.m_flow / valve1.m_flow_small) ^ 2.0) * (valve1.m_flow / valve1.m_flow_small) + 0.5 * (valve1.state_a.d + valve1.state_b.d) else 0.5 * (valve1.state_a.d + valve1.state_b.d)) ($RES_BND_399) (62) [SCAL] (1) valve2.state_b.d = Modelica.Media.Water.IF97_Utilities.rho_ph(99999.99999999999 * junctionVolume.medium.p_bar, junctionVolume.port_3.h_outflow, 0, 0) ($RES_SIM_525) (63) [SCAL] (1) valve2.state_b.T = Modelica.Media.Water.IF97_Utilities.T_ph(99999.99999999999 * junctionVolume.medium.p_bar, junctionVolume.port_3.h_outflow, 0, 0) ($RES_SIM_526) (64) [SCAL] (1) valve2.state_b.p = 99999.99999999999 * junctionVolume.medium.p_bar ($RES_SIM_527) (65) [SCAL] (1) pipe2.state_a.phase = 0 ($RES_SIM_528) (66) [SCAL] (1) pipe1.heatTransfer.heatPorts[1].Q_flow = 0.0 ($RES_SIM_354) (67) [SCAL] (1) pipe2.state_a.h = junctionIdeal.port_3.h_outflow ($RES_SIM_529) (68) [ARRY] (1) pipe2.Qb_flows = pipe2.heatTransfer.Q_flows ($RES_SIM_180) (69) [ARRY] (1) pipe2.heatTransfer.Q_flows = pipe2.heatTransfer.heatPorts.Q_flow ($RES_SIM_181) (70) [ARRY] (1) pipe2.heatTransfer.Ts = pipe2.heatTransfer.heatPorts.T ($RES_SIM_182) (71) [SCAL] (1) 99999.99999999999 * junctionVolume.medium.p_bar = sink.ports[1].p ($RES_SIM_358) (72) [ARRY] (1) {0.0} = pipe2.flowModel.Ib_flows - (pipe2.flowModel.Fs_fg + pipe2.flowModel.Fs_p) ($RES_SIM_183) (73) [ARRY] (1) pipe2.flowModel.Is = {pipe2.flowModel.m_flows[1] * pipe2.flowModel.pathLengths[1]} ($RES_SIM_184) (74) [ARRY] (1) pipe2.flowModel.dps_fg = {(2.0 * (pipe2.flowModel.Fs_fg[1] / pipe2.flowModel.nParallel)) / (pipe2.flowModel.crossAreas[1] + pipe2.flowModel.crossAreas[2])} ($RES_SIM_185) (75) [ARRY] (1) pipe2.flowModel.Fs_p = pipe2.flowModel.nParallel * {0.5 * (pipe2.flowModel.crossAreas[1] + pipe2.flowModel.crossAreas[2]) * (pipe2.flowModel.states.phase - pipe2.flowModel.states.phase)} ($RES_SIM_186) (76) [ARRY] (1) pipe2.flowModel.Ib_flows = {0.0} ($RES_SIM_187) (77) [SCAL] (1) pipe2.flowModel.rhos_act[1] = noEvent(if $SEV_29 then pipe2.flowModel.rhos[1] else pipe2.flowModel.rhos[2]) ($RES_SIM_188) (78) [SCAL] (1) pipe2.flowModel.mus_act[1] = noEvent(if $SEV_29 then pipe2.flowModel.mus[1] else pipe2.flowModel.mus[2]) ($RES_SIM_189) (79) [RECD] (5) pipe1.statesFM[3] = pipe1.state_b ($RES_SIM_270) (80) [ARRY] (5) pipe1.statesFM[2:2] = pipe1.mediums[:].state ($RES_SIM_271) (81) [RECD] (5) pipe1.statesFM[1] = pipe1.state_a ($RES_SIM_272) (82) [SCAL] (1) pipe1.port_b.h_outflow = pipe1.mediums[1].h ($RES_SIM_275) (83) [SCAL] (1) pipe1.port_a.h_outflow = pipe1.mediums[1].h ($RES_SIM_276) (84) [SCAL] (1) pipe1.port_b.m_flow = -pipe1.m_flows[2] ($RES_SIM_277) (85) [FOR-] (3) ($RES_EVT_573) (85) [----] for $i1 in 1:3 loop (85) [----] [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_574) (85) [----] end for; (86) [SCAL] (1) pipe1.port_a.m_flow = pipe1.m_flows[1] ($RES_SIM_278) (87) [SCAL] (1) pipe1.H_flows[2] = -$FUN_4 ($RES_SIM_279) (88) [SCAL] (1) pipe2.state_a.d = Modelica.Media.Water.IF97_Utilities.rho_ph(99999.99999999999 * junctionIdeal.medium.p_bar, junctionIdeal.port_3.h_outflow, 0, 0) ($RES_SIM_530) (89) [SCAL] (1) $SEV_13 = valve1.m_flow > 0.0 ($RES_EVT_575) (90) [SCAL] (1) pipe2.state_a.T = Modelica.Media.Water.IF97_Utilities.T_ph(99999.99999999999 * junctionIdeal.medium.p_bar, junctionIdeal.port_3.h_outflow, 0, 0) ($RES_SIM_531) (91) [SCAL] (1) $SEV_14 = valve2.m_flow > 0.0 ($RES_EVT_576) (92) [SCAL] (1) pipe2.state_a.p = 99999.99999999999 * junctionIdeal.medium.p_bar ($RES_SIM_532) (93) [SCAL] (1) $SEV_15 = junctionVolume.port_3.m_flow > 0.0 ($RES_EVT_577) (94) [SCAL] (1) pipe2.state_b.h = junctionVolume.port_3.h_outflow ($RES_SIM_534) (95) [SCAL] (1) pipe2.state_b.d = Modelica.Media.Water.IF97_Utilities.rho_ph(pipe2.port_b.p, junctionVolume.port_3.h_outflow, 0, 0) ($RES_SIM_535) (96) [SCAL] (1) pipe2.state_b.T = Modelica.Media.Water.IF97_Utilities.T_ph(pipe2.port_b.p, junctionVolume.port_3.h_outflow, 0, 0) ($RES_SIM_536) (97) [SCAL] (1) pipe2.state_b.p = pipe2.port_b.p ($RES_SIM_537) (98) [SCAL] (1) pipe3.state_a.phase = 0 ($RES_SIM_538) (99) [SCAL] (1) pipe3.state_a.h = junctionIdeal.port_3.h_outflow ($RES_SIM_539) (100) [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_190) (101) [SCAL] (1) pipe1.port_a.m_flow + source.ports[1].m_flow = 0.0 ($RES_SIM_366) (102) [SCAL] (1) source.ports[1].p = pipe1.port_a.p ($RES_SIM_367) (103) [ARRY] (1) pipe2.mediums.phase = pipe2.mediums.state.phase ($RES_SIM_196) (104) [ARRY] (1) pipe2.mediums.d = pipe2.mediums.state.d ($RES_SIM_197) (105) [ARRY] (1) pipe2.mediums.T = pipe2.mediums.state.T ($RES_SIM_198) (106) [ARRY] (1) pipe2.mediums.p = pipe2.mediums.state.p ($RES_SIM_199) (107) [SCAL] (1) pipe1.H_flows[1] = $FUN_3 ($RES_SIM_280) (108) [SCAL] (1) pipe1.mb_flows[1] = pipe1.m_flows[1] - pipe1.m_flows[2] ($RES_SIM_281) (109) [SCAL] (1) pipe1.Hb_flows[1] = pipe1.H_flows[1] - pipe1.H_flows[2] ($RES_SIM_282) (110) [ARRY] (3) pipe1.roughnessesFM[:] = {pipe1.roughnesses[1], pipe1.roughnesses[1], pipe1.roughnesses[1]} ($RES_SIM_283) (111) [ARRY] (3) pipe1.dimensionsFM[:] = {pipe1.dimensions[1], pipe1.dimensions[1], pipe1.dimensions[1]} ($RES_SIM_284) (112) [SCAL] (1) $SEV_18 = (junctionVolume.port_3.h_outflow < Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(junctionVolume.medium.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.boilingcurve_p(junctionVolume.medium.sat.psat)) or junctionVolume.port_3.h_outflow > Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(junctionVolume.medium.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.dewcurve_p(junctionVolume.medium.sat.psat))) or 99999.99999999999 * junctionVolume.medium.p_bar > 2.2064e7 ($RES_EVT_580) (113) [ARRY] (3) pipe1.crossAreasFM[:] = {pipe1.crossAreas[1], pipe1.crossAreas[1], pipe1.crossAreas[1]} ($RES_SIM_285) (114) [SCAL] (1) $SEV_19 = (-pipe2.port_a.m_flow) > 0.0 ($RES_EVT_581) (115) [ARRY] (2) pipe1.dheightsFM[:] = {0.0, 0.0} ($RES_SIM_286) (116) [SCAL] (1) $SEV_20 = (-pipe3.port_a.m_flow) > 0.0 ($RES_EVT_582) (117) [ARRY] (2) pipe1.pathLengths[:] = {5.0, 5.0} ($RES_SIM_287) (118) [SCAL] (1) $SEV_21 = (-pipe1.port_b.m_flow) > 0.0 ($RES_EVT_583) (119) [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_288) (120) [ARRY] (1) pipe1.Qb_flows = pipe1.heatTransfer.Q_flows ($RES_SIM_289) (121) [SCAL] (1) pipe3.state_a.d = Modelica.Media.Water.IF97_Utilities.rho_ph(99999.99999999999 * junctionIdeal.medium.p_bar, junctionIdeal.port_3.h_outflow, 0, 0) ($RES_SIM_540) (122) [SCAL] (1) pipe3.state_a.T = Modelica.Media.Water.IF97_Utilities.T_ph(99999.99999999999 * junctionIdeal.medium.p_bar, junctionIdeal.port_3.h_outflow, 0, 0) ($RES_SIM_541) (123) [SCAL] (1) $SEV_24 = (junctionIdeal.port_3.h_outflow < Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(junctionIdeal.medium.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.boilingcurve_p(junctionIdeal.medium.sat.psat)) or junctionIdeal.port_3.h_outflow > Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(junctionIdeal.medium.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.dewcurve_p(junctionIdeal.medium.sat.psat))) or 99999.99999999999 * junctionIdeal.medium.p_bar > 2.2064e7 ($RES_EVT_586) (124) [SCAL] (1) pipe3.state_a.p = 99999.99999999999 * junctionIdeal.medium.p_bar ($RES_SIM_542) (125) [SCAL] (1) $SEV_25 = pipe3.flowModel.m_flows[1] > 0.0 ($RES_EVT_587) (126) [SCAL] (1) $SEV_26[1] = pipe3.mediums[1].p >= 0.0 ($RES_EVT_588) (127) [SCAL] (1) pipe3.state_b.h = junctionVolume.port_3.h_outflow ($RES_SIM_544) (128) [SCAL] (1) pipe3.state_b.d = Modelica.Media.Water.IF97_Utilities.rho_ph(pipe3.port_b.p, junctionVolume.port_3.h_outflow, 0, 0) ($RES_SIM_545) (129) [SCAL] (1) pipe3.state_b.T = Modelica.Media.Water.IF97_Utilities.T_ph(pipe3.port_b.p, junctionVolume.port_3.h_outflow, 0, 0) ($RES_SIM_546) (130) [SCAL] (1) pipe3.state_b.p = pipe3.port_b.p ($RES_SIM_547) (131) [ARRY] (1) pipe1.heatTransfer.Q_flows = pipe1.heatTransfer.heatPorts.Q_flow ($RES_SIM_290) (132) [ARRY] (1) pipe1.heatTransfer.Ts = pipe1.heatTransfer.heatPorts.T ($RES_SIM_291) (133) [ARRY] (2) {0.0 for $i1 in 1:2} = pipe1.flowModel.Ib_flows - (pipe1.flowModel.Fs_fg + pipe1.flowModel.Fs_p) ($RES_SIM_292) (134) [ARRY] (2) pipe1.flowModel.Is = {pipe1.flowModel.m_flows[i] * pipe1.flowModel.pathLengths[i] for i in 1:2} ($RES_SIM_293) (135) [ARRY] (2) pipe1.flowModel.dps_fg = {pipe1.flowModel.Fs_fg[i] / pipe1.flowModel.nParallel * 2.0 / (pipe1.flowModel.crossAreas[i] + pipe1.flowModel.crossAreas[i + 1]) for i in 1:2} ($RES_SIM_294) (136) [SCAL] (1) $SEV_28 = (pipe3.mediums[1].h < Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(pipe3.mediums.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.boilingcurve_p(pipe3.mediums.sat.psat)) or pipe3.mediums[1].h > Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(pipe3.mediums.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.dewcurve_p(pipe3.mediums.sat.psat))) or pipe3.mediums[1].p > 2.2064e7 ($RES_EVT_590) (137) [ARRY] (2) pipe1.flowModel.Fs_p = pipe1.flowModel.nParallel * {0.0 for i in 1:2} ($RES_SIM_295) (138) [SCAL] (1) $SEV_29 = pipe2.flowModel.m_flows[1] > 0.0 ($RES_EVT_591) (139) [ARRY] (2) pipe1.flowModel.Ib_flows = {0.0 for $i1 in 1:2} ($RES_SIM_296) (140) [SCAL] (1) $SEV_30[1] = pipe2.mediums[1].p >= 0.0 ($RES_EVT_592) (141) [FOR-] (2) ($RES_SIM_297) (141) [----] for $i1 in 1:2 loop (141) [----] [SCAL] (1) pipe1.flowModel.rhos_act[$i1] = noEvent(if $SEV_48[$i1] then pipe1.flowModel.rhos[$i1] else pipe1.flowModel.rhos[$i1 + 1]) ($RES_SIM_298) (141) [----] end for; (142) [SCAL] (1) $SEV_32 = (pipe2.mediums[1].h < Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(pipe2.mediums.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.boilingcurve_p(pipe2.mediums.sat.psat)) or pipe2.mediums[1].h > Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(pipe2.mediums.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.dewcurve_p(pipe2.mediums.sat.psat))) or pipe2.mediums[1].p > 2.2064e7 ($RES_EVT_594) (143) [FOR-] (2) ($RES_SIM_299) (143) [----] for $i1 in 1:2 loop (143) [----] [SCAL] (1) pipe1.flowModel.mus_act[$i1] = noEvent(if $SEV_48[$i1] then pipe1.flowModel.mus[$i1] else pipe1.flowModel.mus[$i1 + 1]) ($RES_SIM_300) (143) [----] end for; (144) [SCAL] (1) $SEV_35 = (sink.medium.h < Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(sink.medium.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.boilingcurve_p(sink.medium.sat.psat)) or sink.medium.h > Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(sink.medium.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.dewcurve_p(sink.medium.sat.psat))) or sink.p > 2.2064e7 ($RES_EVT_597) (145) [SCAL] (1) $SEV_36 = valve2.xs * valve2.p >= valve2.dp_turbulent ($RES_EVT_598) (146) [SCAL] (1) $SEV_37 = valve2.state_a.d > 0.0 ($RES_EVT_599) (147) [ALGO] (5) ($RES_SIM_31) (147) [----] 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); (147) [----] when {time >= $PRE.valveOpening2.nextEvent, initial()} then (147) [----] (valveOpening2.a, valveOpening2.b, valveOpening2.nextEventScaled, valveOpening2.last) := ($FUN_19, $FUN_20, $FUN_21, $FUN_22); (147) [----] valveOpening2.nextEvent := valveOpening2.nextEventScaled; (147) [----] end when; (148) [ALGO] (5) ($RES_SIM_32) (148) [----] 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); (148) [----] when {time >= $PRE.valveOpening1.nextEvent, initial()} then (148) [----] (valveOpening1.a, valveOpening1.b, valveOpening1.nextEventScaled, valveOpening1.last) := ($FUN_15, $FUN_16, $FUN_17, $FUN_18); (148) [----] valveOpening1.nextEvent := valveOpening1.nextEventScaled; (148) [----] end when; (149) [SCAL] (1) $DER.junctionVolume.m = junctionVolume.mb_flow ($RES_SIM_33) (150) [SCAL] (1) $DER.junctionVolume.U = junctionVolume.Hb_flow ($RES_SIM_34) (151) [SCAL] (1) junctionVolume.U = junctionVolume.m * junctionVolume.medium.u ($RES_SIM_35) (152) [SCAL] (1) junctionVolume.m = junctionVolume.V * junctionVolume.medium.d ($RES_SIM_36) (153) [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) (154) [SCAL] (1) pipe1.state_a.phase = 0 ($RES_SIM_498) (155) [SCAL] (1) pipe1.state_a.h = source.ports[1].h_outflow ($RES_SIM_499) (156) [SCAL] (1) junctionVolume.mb_flow = valve1.m_flow + valve2.m_flow + junctionVolume.port_3.m_flow ($RES_SIM_43) (157) [SCAL] (1) junctionVolume.medium.phase = junctionVolume.medium.state.phase ($RES_SIM_51) (158) [SCAL] (1) junctionVolume.medium.d = junctionVolume.medium.state.d ($RES_SIM_52) (159) [SCAL] (1) -((-273.15) - junctionVolume.medium.T_degC) = junctionVolume.medium.state.T ($RES_SIM_53) (160) [SCAL] (1) 99999.99999999999 * junctionVolume.medium.p_bar = junctionVolume.medium.state.p ($RES_SIM_54) (161) [SCAL] (1) junctionVolume.port_3.h_outflow = junctionVolume.medium.state.h ($RES_SIM_55) (162) [SCAL] (1) junctionVolume.medium.u = junctionVolume.port_3.h_outflow - (99999.99999999999 * junctionVolume.medium.p_bar) / junctionVolume.medium.d ($RES_SIM_57) (163) [SCAL] (1) junctionVolume.medium.sat.psat = 99999.99999999999 * junctionVolume.medium.p_bar ($RES_SIM_58) (164) [SCAL] (1) junctionVolume.medium.sat.Tsat = Modelica.Media.Water.IF97_Utilities.BaseIF97.Basic.tsat(99999.99999999999 * junctionVolume.medium.p_bar) ($RES_SIM_59) (165) [SCAL] (1) $DER.pipe3.Us[1] = pipe3.Wb_flows[1] + pipe3.Hb_flows[1] + pipe3.Qb_flows[1] ($RES_SIM_100) (166) [SCAL] (1) valve1.port_a_T = smooth(1, if $SEV_63 then valve1.state_a.T else if $SEV_64 then Modelica.Media.Water.IF97_Utilities.T_ph(pipe2.port_b.p, junctionVolume.port_3.h_outflow, 0, 0) else if $SEV_62 then 0.25 * (Modelica.Media.Water.IF97_Utilities.T_ph(pipe2.port_b.p, junctionVolume.port_3.h_outflow, 0, 0) - valve1.state_a.T) * ((-3.0) + (valve1.m_flow / valve1.m_flow_small) ^ 2.0) * (valve1.m_flow / valve1.m_flow_small) + 0.5 * (valve1.state_a.T + Modelica.Media.Water.IF97_Utilities.T_ph(pipe2.port_b.p, junctionVolume.port_3.h_outflow, 0, 0)) else 0.5 * (valve1.state_a.T + Modelica.Media.Water.IF97_Utilities.T_ph(pipe2.port_b.p, junctionVolume.port_3.h_outflow, 0, 0))) ($RES_BND_400) (167) [SCAL] (1) pipe3.ms[1] = pipe3.fluidVolumes[1] * pipe3.mediums[1].d ($RES_SIM_101) (168) [SCAL] (1) valve1.port_b_T = smooth(1, if $SEV_60 then valve1.state_b.T else if $SEV_61 then Modelica.Media.Water.IF97_Utilities.T_ph(99999.99999999999 * junctionVolume.medium.p_bar, valve1.port_b.h_outflow, 0, 0) else if $SEV_62 then 0.5 * (valve1.state_b.T + Modelica.Media.Water.IF97_Utilities.T_ph(99999.99999999999 * junctionVolume.medium.p_bar, valve1.port_b.h_outflow, 0, 0)) - 0.25 * (Modelica.Media.Water.IF97_Utilities.T_ph(99999.99999999999 * junctionVolume.medium.p_bar, valve1.port_b.h_outflow, 0, 0) - valve1.state_b.T) * ((-3.0) + (valve1.m_flow / (-valve1.m_flow_small)) ^ 2.0) * (valve1.m_flow / valve1.m_flow_small) else 0.5 * (valve1.state_b.T + Modelica.Media.Water.IF97_Utilities.T_ph(99999.99999999999 * junctionVolume.medium.p_bar, valve1.port_b.h_outflow, 0, 0))) ($RES_BND_401) (169) [SCAL] (1) pipe3.Us[1] = pipe3.ms[1] * pipe3.mediums[1].u ($RES_SIM_102) (170) [SCAL] (1) valve1.dp_turbulent = max(valve1.dp_small, (6.283185307179586e6 * (Modelica.Media.Water.IF97_Utilities.dynamicViscosity(valve1.state_a.d, valve1.state_a.T, valve1.state_a.p, valve1.state_a.phase) + Modelica.Media.Water.IF97_Utilities.dynamicViscosity(valve1.state_b.d, valve1.state_b.T, valve1.state_b.p, valve1.state_b.phase)) ^ 2.0) / (valve1.Y * max(valveOpening1.y, 0.001) * valve1.Av * (valve1.state_b.d + valve1.state_a.d))) ($RES_BND_402) (171) [SCAL] (1) pipe3.port_b.p = pipe3.mediums[1].p ($RES_SIM_103) (172) [SCAL] (1) valve2.V_flow = valve2.m_flow / smooth(1, if $SEV_58 then valve2.state_a.d else if $SEV_59 then valve2.state_b.d else if $SEV_57 then 0.25 * (valve2.state_b.d - valve2.state_a.d) * ((-3.0) + (valve2.m_flow / valve2.m_flow_small) ^ 2.0) * (valve2.m_flow / valve2.m_flow_small) + 0.5 * (valve2.state_a.d + valve2.state_b.d) else 0.5 * (valve2.state_a.d + valve2.state_b.d)) ($RES_BND_403) (173) [ARRY] (1) pipe3.vsFM[2:2] = pipe3.vs ($RES_SIM_104) (174) [SCAL] (1) valve2.port_a_T = smooth(1, if $SEV_58 then valve2.state_a.T else if $SEV_59 then Modelica.Media.Water.IF97_Utilities.T_ph(pipe3.port_b.p, junctionVolume.port_3.h_outflow, 0, 0) else if $SEV_57 then 0.25 * (Modelica.Media.Water.IF97_Utilities.T_ph(pipe3.port_b.p, junctionVolume.port_3.h_outflow, 0, 0) - valve2.state_a.T) * ((-3.0) + (valve2.m_flow / valve2.m_flow_small) ^ 2.0) * (valve2.m_flow / valve2.m_flow_small) + 0.5 * (valve2.state_a.T + Modelica.Media.Water.IF97_Utilities.T_ph(pipe3.port_b.p, junctionVolume.port_3.h_outflow, 0, 0)) else 0.5 * (valve2.state_a.T + Modelica.Media.Water.IF97_Utilities.T_ph(pipe3.port_b.p, junctionVolume.port_3.h_outflow, 0, 0))) ($RES_BND_404) (175) [SCAL] (1) valve2.port_b_T = smooth(1, if $SEV_55 then valve2.state_b.T else if $SEV_56 then Modelica.Media.Water.IF97_Utilities.T_ph(99999.99999999999 * junctionVolume.medium.p_bar, valve2.port_b.h_outflow, 0, 0) else if $SEV_57 then 0.5 * (valve2.state_b.T + Modelica.Media.Water.IF97_Utilities.T_ph(99999.99999999999 * junctionVolume.medium.p_bar, valve2.port_b.h_outflow, 0, 0)) - 0.25 * (Modelica.Media.Water.IF97_Utilities.T_ph(99999.99999999999 * junctionVolume.medium.p_bar, valve2.port_b.h_outflow, 0, 0) - valve2.state_b.T) * ((-3.0) + (valve2.m_flow / (-valve2.m_flow_small)) ^ 2.0) * (valve2.m_flow / valve2.m_flow_small) else 0.5 * (valve2.state_b.T + Modelica.Media.Water.IF97_Utilities.T_ph(99999.99999999999 * junctionVolume.medium.p_bar, valve2.port_b.h_outflow, 0, 0))) ($RES_BND_405) (176) [SCAL] (1) pipe3.vsFM[1] = ((pipe3.m_flows[1] / pipe3.state_a.d) / pipe3.crossAreas[1]) / pipe3.nParallel ($RES_SIM_105) (177) [SCAL] (1) valve2.dp_turbulent = max(valve2.dp_small, (6.283185307179586e6 * (Modelica.Media.Water.IF97_Utilities.dynamicViscosity(valve2.state_a.d, valve2.state_a.T, valve2.state_a.p, valve2.state_a.phase) + Modelica.Media.Water.IF97_Utilities.dynamicViscosity(valve2.state_b.d, valve2.state_b.T, valve2.state_b.p, valve2.state_b.phase)) ^ 2.0) / (valve2.Y * max(valveOpening2.y, 0.001) * valve2.Av * (valve2.state_b.d + valve2.state_a.d))) ($RES_BND_406) (178) [ARRY] (1) pipe3.m_flows[1:1] = pipe3.flowModel.m_flows[:] ($RES_SIM_106) (179) [ARRY] (5) pipe3.statesFM[2:2] = pipe3.mediums[:].state ($RES_SIM_107) (180) [RECD] (5) pipe3.statesFM[1] = pipe3.state_a ($RES_SIM_108) (181) [ARRY] (1) pipe2.fluidVolumes = {10.0 * pipe2.crossAreas[1]} .* pipe2.nParallel ($RES_BND_409) (182) [SCAL] (1) -((-273.15) - junctionVolume.medium.T_degC) = Modelica.Media.Water.IF97_Utilities.T_props_ph(99999.99999999999 * junctionVolume.medium.p_bar, junctionVolume.port_3.h_outflow, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(99999.99999999999 * junctionVolume.medium.p_bar, junctionVolume.port_3.h_outflow, junctionVolume.medium.phase, 0)) ($RES_SIM_60) (183) [SCAL] (1) junctionVolume.medium.d = Modelica.Media.Water.IF97_Utilities.rho_props_ph(99999.99999999999 * junctionVolume.medium.p_bar, junctionVolume.port_3.h_outflow, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(99999.99999999999 * junctionVolume.medium.p_bar, junctionVolume.port_3.h_outflow, junctionVolume.medium.phase, 0)) ($RES_SIM_61) (184) [SCAL] (1) junctionVolume.medium.phase = if $SEV_18 then 1 else 2 ($RES_SIM_62) (185) [SCAL] (1) $DER.junctionIdeal.m = junctionIdeal.mb_flow ($RES_SIM_64) (186) [SCAL] (1) $DER.junctionIdeal.U = junctionIdeal.Hb_flow ($RES_SIM_65) (187) [SCAL] (1) junctionIdeal.U = junctionIdeal.m * junctionIdeal.medium.u ($RES_SIM_66) (188) [SCAL] (1) junctionIdeal.m = junctionIdeal.V * junctionIdeal.medium.d ($RES_SIM_67) (189) [SCAL] (1) $FUN_1 = ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.pipe1.flowModel.WallFriction.massFlowRate_dp_staticHead(pipe1.flowModel.dps_fg[$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_490) (190) [ARRY] (1) pipe2.mediums.p_bar = {1e-5 * pipe2.mediums[1].p} ($RES_BND_410) (191) [ARRY] (1) pipe2.mediums.T_degC = {(-273.15) + pipe2.mediums[1].T} ($RES_BND_411) (192) [SCAL] (1) valve2.port_b.h_outflow = pipe3.mediums[1].h ($RES_SIM_111) (193) [ARRY] (2) pipe2.flowModel.vs = pipe2.vsFM ($RES_BND_412) (194) [SCAL] (1) pipe3.port_a.h_outflow = pipe3.mediums[1].h ($RES_SIM_112) (195) [ARRY] (2) pipe2.flowModel.crossAreas = pipe2.crossAreasFM ($RES_BND_413) (196) [SCAL] (1) -valve2.m_flow = -pipe3.m_flows[2] ($RES_SIM_113) (197) [ARRY] (2) pipe2.flowModel.dimensions = pipe2.dimensionsFM ($RES_BND_414) (198) [SCAL] (1) pipe3.port_a.m_flow = pipe3.m_flows[1] ($RES_SIM_114) (199) [ARRY] (2) pipe2.flowModel.roughnesses = pipe2.roughnessesFM ($RES_BND_415) (200) [SCAL] (1) pipe3.H_flows[2] = -$FUN_14 ($RES_SIM_115) (201) [ARRY] (1) pipe2.flowModel.dheights = pipe2.dheightsFM ($RES_BND_416) (202) [SCAL] (1) pipe3.H_flows[1] = $FUN_13 ($RES_SIM_116) (203) [ARRY] (1) pipe2.flowModel.pathLengths = pipe2.pathLengths ($RES_BND_417) (204) [SCAL] (1) pipe3.mb_flows[1] = pipe3.m_flows[1] - pipe3.m_flows[2] ($RES_SIM_117) (205) [FOR-] (2) ($RES_BND_418) (205) [----] for $i1 in 1:2 loop (205) [----] [SCAL] (1) pipe2.flowModel.rhos[$i1] = pipe2.flowModel.states.d ($RES_BND_419) (205) [----] end for; (206) [SCAL] (1) pipe3.Hb_flows[1] = pipe3.H_flows[1] - pipe3.H_flows[2] ($RES_SIM_118) (207) [ARRY] (2) pipe3.roughnessesFM[:] = {pipe3.roughnesses[1], pipe3.roughnesses[1]} ($RES_SIM_119) (208) [SCAL] (1) $FUN_2 = sum(pipe1.flowModel.dps_fg) ($RES_$AUX_489) (209) [SCAL] (1) $FUN_3 = semiLinear(pipe1.port_a.m_flow, source.ports[1].h_outflow, pipe1.mediums[1].h) ($RES_$AUX_488) (210) [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_70) (211) [SCAL] (1) $FUN_4 = semiLinear(pipe1.port_b.m_flow, junctionIdeal.port_3.h_outflow, pipe1.mediums[1].h) ($RES_$AUX_487) (212) [SCAL] (1) $FUN_5 = abs(valve1.xs) ($RES_$AUX_486) (213) [ARRY] (1) pipe2.mediums.h = pipe2.mediums.state.h ($RES_SIM_200) (214) [SCAL] (1) $FUN_6 = abs(valve2.xs) ($RES_$AUX_485) (215) [SCAL] (1) $FUN_7 = ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.pipe2.flowModel.WallFriction.massFlowRate_dp_staticHead(pipe2.flowModel.dps_fg[1], pipe2.flowModel.rhos[1], pipe2.flowModel.rhos[2], pipe2.flowModel.mus[1], pipe2.flowModel.mus[2], pipe2.flowModel.pathLengths_internal[1], pipe2.flowModel.diameters[1], (pipe2.flowModel.g * pipe2.flowModel.dheights)[1], (0.5 .* (pipe2.flowModel.crossAreas[1:1] + pipe2.flowModel.crossAreas[2:2]))[1], (0.5 .* (pipe2.flowModel.roughnesses[1:1] + pipe2.flowModel.roughnesses[2:2]))[1], pipe2.flowModel.dp_small, pipe2.flowModel.Res_turbulent_internal[1]) ($RES_$AUX_484) (216) [SCAL] (1) pipe2.mediums[1].u = pipe2.mediums[1].h - pipe2.mediums[1].p / pipe2.mediums[1].d ($RES_SIM_202) (217) [SCAL] (1) junctionIdeal.mb_flow = -(pipe2.port_a.m_flow + pipe3.port_a.m_flow + pipe1.port_b.m_flow) ($RES_SIM_74) (218) [SCAL] (1) $FUN_8 = sum(pipe2.flowModel.dps_fg) ($RES_$AUX_483) (219) [ARRY] (1) pipe2.mediums.sat.psat = pipe2.mediums.p ($RES_SIM_203) (220) [SCAL] (1) $FUN_9 = semiLinear(pipe2.port_a.m_flow, junctionIdeal.port_3.h_outflow, pipe2.mediums[1].h) ($RES_$AUX_482) (221) [SCAL] (1) pipe2.mediums[1].sat.Tsat = Modelica.Media.Water.IF97_Utilities.BaseIF97.Basic.tsat(pipe2.mediums[1].p) ($RES_SIM_204) (222) [SCAL] (1) $FUN_10 = semiLinear(-valve1.m_flow, junctionVolume.port_3.h_outflow, pipe2.mediums[1].h) ($RES_$AUX_481) (223) [SCAL] (1) pipe2.mediums[1].T = Modelica.Media.Water.IF97_Utilities.T_props_ph(pipe2.mediums[1].p, pipe2.mediums[1].h, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(pipe2.mediums[1].p, pipe2.mediums[1].h, pipe2.mediums[1].phase, 0)) ($RES_SIM_205) (224) [SCAL] (1) $FUN_11 = ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.pipe3.flowModel.WallFriction.massFlowRate_dp_staticHead(pipe3.flowModel.dps_fg[1], pipe3.flowModel.rhos[1], pipe3.flowModel.rhos[2], pipe3.flowModel.mus[1], pipe3.flowModel.mus[2], pipe3.flowModel.pathLengths_internal[1], pipe3.flowModel.diameters[1], (pipe3.flowModel.g * pipe3.flowModel.dheights)[1], (0.5 .* (pipe3.flowModel.crossAreas[1:1] + pipe3.flowModel.crossAreas[2:2]))[1], (0.5 .* (pipe3.flowModel.roughnesses[1:1] + pipe3.flowModel.roughnesses[2:2]))[1], pipe3.flowModel.dp_small, pipe3.flowModel.Res_turbulent_internal[1]) ($RES_$AUX_480) (225) [SCAL] (1) pipe2.mediums[1].d = Modelica.Media.Water.IF97_Utilities.rho_props_ph(pipe2.mediums[1].p, pipe2.mediums[1].h, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(pipe2.mediums[1].p, pipe2.mediums[1].h, pipe2.mediums[1].phase, 0)) ($RES_SIM_206) (226) [SCAL] (1) pipe2.mediums[1].phase = if $SEV_32 then 1 else 2 ($RES_SIM_207) (227) [SCAL] (1) sink.ports[1].p = sink.p ($RES_SIM_209) (228) [FOR-] (2) ($RES_BND_420) (228) [----] for $i1 in 1:2 loop (228) [----] [SCAL] (1) pipe2.flowModel.mus[$i1] = pipe2.flowModel.mu_nominal ($RES_BND_421) (228) [----] end for; (229) [ARRY] (2) pipe3.dimensionsFM[:] = {pipe3.dimensions[1], pipe3.dimensions[1]} ($RES_SIM_120) (230) [ARRY] (2) pipe3.crossAreasFM[:] = {pipe3.crossAreas[1], pipe3.crossAreas[1]} ($RES_SIM_121) (231) [ARRY] (1) pipe2.flowModel.pathLengths_internal = pipe2.flowModel.pathLengths ($RES_BND_422) (232) [ARRY] (1) pipe3.dheightsFM[:] = {0.0} ($RES_SIM_122) (233) [SCAL] (1) pipe2.flowModel.Res_turbulent_internal[1] = pipe2.flowModel.Re_turbulent ($RES_BND_423) (234) [ARRY] (1) pipe3.pathLengths[:] = {10.0} ($RES_SIM_123) (235) [ARRY] (1) pipe2.flowModel.diameters = 0.5 * (pipe2.flowModel.dimensions[2:2] + pipe2.flowModel.dimensions[1:1]) ($RES_BND_424) (236) [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_124) (237) [ARRY] (1) pipe3.Qb_flows = pipe3.heatTransfer.Q_flows ($RES_SIM_125) (238) [ARRY] (1) pipe2.vs = {(0.5 * (pipe2.m_flows[2] + pipe2.m_flows[1])) / (pipe2.crossAreas[1] * pipe2.mediums[1].d)} / pipe2.nParallel ($RES_BND_426) (239) [ARRY] (1) pipe3.heatTransfer.Q_flows = pipe3.heatTransfer.heatPorts.Q_flow ($RES_SIM_126) (240) [ARRY] (1) pipe3.heatTransfer.Ts = pipe3.heatTransfer.heatPorts.T ($RES_SIM_127) (241) [ARRY] (1) pipe2.heatTransfer.Ts = {pipe2.heatTransfer.states.h} ($RES_BND_428) (242) [ARRY] (1) {0.0} = pipe3.flowModel.Ib_flows - (pipe3.flowModel.Fs_fg + pipe3.flowModel.Fs_p) ($RES_SIM_128) (243) [ARRY] (1) pipe2.heatTransfer.vs = pipe2.vs ($RES_BND_429) (244) [ARRY] (1) pipe3.flowModel.Is = {pipe3.flowModel.m_flows[1] * pipe3.flowModel.pathLengths[1]} ($RES_SIM_129) (245) [SCAL] (1) $FUN_12 = sum(pipe3.flowModel.dps_fg) ($RES_$AUX_479) (246) [SCAL] (1) $FUN_13 = semiLinear(pipe3.port_a.m_flow, junctionIdeal.port_3.h_outflow, pipe3.mediums[1].h) ($RES_$AUX_478) (247) [SCAL] (1) $FUN_14 = semiLinear(-valve2.m_flow, junctionVolume.port_3.h_outflow, pipe3.mediums[1].h) ($RES_$AUX_477) (248) [TUPL] (4) ($FUN_15, $FUN_16, $FUN_17, $FUN_18) = ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.valveOpening1.getInterpolationCoefficients(valveOpening1.table, valveOpening1.offset, valveOpening1.startTime, time, valveOpening1.last, 1e-13, valveOpening1.shiftTime) ($RES_$AUX_476) (249) [SCAL] (1) sink.ports[1].h_outflow = sink.medium.h ($RES_SIM_210) (250) [SCAL] (1) junctionIdeal.medium.phase = junctionIdeal.medium.state.phase ($RES_SIM_82) (251) [TUPL] (4) ($FUN_19, $FUN_20, $FUN_21, $FUN_22) = ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.valveOpening2.getInterpolationCoefficients(valveOpening2.table, valveOpening2.offset, valveOpening2.startTime, time, valveOpening2.last, 1e-13, valveOpening2.shiftTime) ($RES_$AUX_475) (252) [SCAL] (1) sink.medium.h = Modelica.Media.Water.IF97_Utilities.h_pT(sink.p, sink.T, 0) ($RES_SIM_211) (253) [SCAL] (1) junctionIdeal.medium.d = junctionIdeal.medium.state.d ($RES_SIM_83) (254) [SCAL] (1) $FUN_23 = ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.pipe3.flowModel.WallFriction.pressureLoss_m_flow(pipe3.flowModel.m_flow_nominal / pipe3.flowModel.nParallel, pipe3.flowModel.rho_nominal, pipe3.flowModel.rho_nominal, pipe3.flowModel.mu_nominal, pipe3.flowModel.mu_nominal, pipe3.flowModel.pathLengths_internal[1], pipe3.flowModel.diameters[1], (0.5 .* (pipe3.flowModel.crossAreas[2:2] + pipe3.flowModel.crossAreas[1:1]))[1], (0.5 .* (pipe3.flowModel.roughnesses[2:2] + pipe3.flowModel.roughnesses[1:1]))[1], pipe3.flowModel.m_flow_small / pipe3.flowModel.nParallel, pipe3.flowModel.Res_turbulent_internal[1]) ($RES_$AUX_474) (255) [SCAL] (1) -((-273.15) - junctionIdeal.medium.T_degC) = junctionIdeal.medium.state.T ($RES_SIM_84) (256) [SCAL] (1) pipe3.flowModel.dp_fric_nominal = sum({$FUN_23}) ($RES_$AUX_473) (257) [SCAL] (1) 99999.99999999999 * junctionIdeal.medium.p_bar = junctionIdeal.medium.state.p ($RES_SIM_85) (258) [SCAL] (1) $FUN_25 = ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.pipe2.flowModel.WallFriction.pressureLoss_m_flow(pipe2.flowModel.m_flow_nominal / pipe2.flowModel.nParallel, pipe2.flowModel.rho_nominal, pipe2.flowModel.rho_nominal, pipe2.flowModel.mu_nominal, pipe2.flowModel.mu_nominal, pipe2.flowModel.pathLengths_internal[1], pipe2.flowModel.diameters[1], (0.5 .* (pipe2.flowModel.crossAreas[2:2] + pipe2.flowModel.crossAreas[1:1]))[1], (0.5 .* (pipe2.flowModel.roughnesses[2:2] + pipe2.flowModel.roughnesses[1:1]))[1], pipe2.flowModel.m_flow_small / pipe2.flowModel.nParallel, pipe2.flowModel.Res_turbulent_internal[1]) ($RES_$AUX_472) (259) [SCAL] (1) junctionIdeal.port_3.h_outflow = junctionIdeal.medium.state.h ($RES_SIM_86) (260) [SCAL] (1) pipe2.flowModel.dp_fric_nominal = sum({$FUN_25}) ($RES_$AUX_471) (261) [SCAL] (1) $FUN_27 = ModelicaTest.Fluid.TestPipesAndValves.BranchingPipes18.pipe1.flowModel.WallFriction.pressureLoss_m_flow(pipe1.flowModel.m_flow_nominal / pipe1.flowModel.nParallel, pipe1.flowModel.rho_nominal, pipe1.flowModel.rho_nominal, pipe1.flowModel.mu_nominal, pipe1.flowModel.mu_nominal, pipe1.flowModel.pathLengths_internal[$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_470) (262) [SCAL] (1) junctionIdeal.medium.u = junctionIdeal.port_3.h_outflow - (99999.99999999999 * junctionIdeal.medium.p_bar) / junctionIdeal.medium.d ($RES_SIM_88) (263) [SCAL] (1) junctionIdeal.medium.sat.psat = 99999.99999999999 * junctionIdeal.medium.p_bar ($RES_SIM_89) (264) [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_301) (265) [SCAL] (1) $SEV_38 = valve2.xs * valve2.p <= (-valve2.dp_turbulent) ($RES_EVT_600) (266) [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_130) (267) [SCAL] (1) $SEV_39 = valve2.state_b.d > 0.0 ($RES_EVT_601) (268) [ARRY] (1) pipe3.flowModel.Fs_p = pipe3.flowModel.nParallel * {0.5 * (pipe3.flowModel.crossAreas[1] + pipe3.flowModel.crossAreas[2]) * (pipe3.flowModel.states.phase - pipe3.flowModel.states.phase)} ($RES_SIM_131) (269) [SCAL] (1) $SEV_40 = valve2.state_a.d >= valve2.state_b.d ($RES_EVT_602) (270) [ARRY] (1) pipe1.mediums.phase = pipe1.mediums.state.phase ($RES_SIM_307) (271) [ARRY] (1) pipe3.flowModel.Ib_flows = {0.0} ($RES_SIM_132) (272) [SCAL] (1) $SEV_41 = valveOpening2.y < valve2.minLimiter.uMin ($RES_EVT_603) (273) [ARRY] (1) pipe1.mediums.d = pipe1.mediums.state.d ($RES_SIM_308) (274) [ARRY] (1) pipe3.fluidVolumes = {10.0 * pipe3.crossAreas[1]} .* pipe3.nParallel ($RES_BND_433) (275) [SCAL] (1) pipe3.flowModel.rhos_act[1] = noEvent(if $SEV_25 then pipe3.flowModel.rhos[1] else pipe3.flowModel.rhos[2]) ($RES_SIM_133) (276) [SCAL] (1) $SEV_42 = valve1.xs * valve1.p >= valve1.dp_turbulent ($RES_EVT_604) (277) [ARRY] (1) pipe1.mediums.T = pipe1.mediums.state.T ($RES_SIM_309) (278) [ARRY] (1) pipe3.mediums.p_bar = {1e-5 * pipe3.mediums[1].p} ($RES_BND_434) (279) [SCAL] (1) pipe3.flowModel.mus_act[1] = noEvent(if $SEV_25 then pipe3.flowModel.mus[1] else pipe3.flowModel.mus[2]) ($RES_SIM_134) (280) [SCAL] (1) $SEV_43 = valve1.state_a.d > 0.0 ($RES_EVT_605) (281) [ARRY] (1) pipe3.mediums.T_degC = {(-273.15) + pipe3.mediums[1].T} ($RES_BND_435) (282) [ARRY] (1) pipe3.flowModel.m_flows = {homotopy(({$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_135) (283) [SCAL] (1) $SEV_44 = valve1.xs * valve1.p <= (-valve1.dp_turbulent) ($RES_EVT_606) (284) [ARRY] (2) pipe3.flowModel.vs = pipe3.vsFM ($RES_BND_436) (285) [SCAL] (1) $SEV_45 = valve1.state_b.d > 0.0 ($RES_EVT_607) (286) [ARRY] (2) pipe3.flowModel.crossAreas = pipe3.crossAreasFM ($RES_BND_437) (287) [SCAL] (1) $SEV_46 = valve1.state_a.d >= valve1.state_b.d ($RES_EVT_608) (288) [ARRY] (2) pipe3.flowModel.dimensions = pipe3.dimensionsFM ($RES_BND_438) (289) [SCAL] (1) $SEV_47 = valveOpening1.y < valve1.minLimiter.uMin ($RES_EVT_609) (290) [ARRY] (2) pipe3.flowModel.roughnesses = pipe3.roughnessesFM ($RES_BND_439) (291) [SCAL] (1) pipe1.flowModel.dp_fric_nominal = sum($FUN_27 for $i1 in 1:2) ($RES_$AUX_469) (292) [SCAL] (1) junctionIdeal.medium.sat.Tsat = Modelica.Media.Water.IF97_Utilities.BaseIF97.Basic.tsat(99999.99999999999 * junctionIdeal.medium.p_bar) ($RES_SIM_90) (293) [SCAL] (1) -((-273.15) - junctionIdeal.medium.T_degC) = Modelica.Media.Water.IF97_Utilities.T_props_ph(99999.99999999999 * junctionIdeal.medium.p_bar, junctionIdeal.port_3.h_outflow, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(99999.99999999999 * junctionIdeal.medium.p_bar, junctionIdeal.port_3.h_outflow, junctionIdeal.medium.phase, 0)) ($RES_SIM_91) (294) [SCAL] (1) junctionIdeal.medium.d = Modelica.Media.Water.IF97_Utilities.rho_props_ph(99999.99999999999 * junctionIdeal.medium.p_bar, junctionIdeal.port_3.h_outflow, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(99999.99999999999 * junctionIdeal.medium.p_bar, junctionIdeal.port_3.h_outflow, junctionIdeal.medium.phase, 0)) ($RES_SIM_92) (295) [SCAL] (1) sink.medium.phase = sink.medium.state.phase ($RES_SIM_221) (296) [SCAL] (1) junctionIdeal.medium.phase = if $SEV_24 then 1 else 2 ($RES_SIM_93) (297) [SCAL] (1) sink.medium.d = sink.medium.state.d ($RES_SIM_222) (298) [SCAL] (1) -((-273.15) - sink.medium.T_degC) = sink.medium.state.T ($RES_SIM_223) (299) [SCAL] (1) valveOpening2.y = valveOpening2.a * time + valveOpening2.b ($RES_SIM_95) (300) [SCAL] (1) sink.medium.h = sink.medium.state.h ($RES_SIM_225) (301) [SCAL] (1) valveOpening1.y = valveOpening1.a * time + valveOpening1.b ($RES_SIM_97) (302) [SCAL] (1) sink.medium.u = sink.medium.h - sink.p / sink.medium.d ($RES_SIM_227) (303) [SCAL] (1) $DER.pipe3.ms[1] = pipe3.mb_flows[1] ($RES_SIM_99) (304) [SCAL] (1) sink.medium.sat.psat = sink.p ($RES_SIM_228) (305) [ARRY] (1) pipe1.mediums.p = pipe1.mediums.state.p ($RES_SIM_310) (306) [ARRY] (1) pipe1.mediums.h = pipe1.mediums.state.h ($RES_SIM_311) (307) [SCAL] (1) pipe1.mediums[1].u = pipe1.mediums[1].h - pipe1.mediums[1].p / pipe1.mediums[1].d ($RES_SIM_313) (308) [ARRY] (1) pipe1.mediums.sat.psat = pipe1.mediums.p ($RES_SIM_314) (309) [FOR-] (2) ($RES_EVT_610) (309) [----] for $i1 in 1:2 loop (309) [----] [SCAL] (1) $SEV_48[$i1] = pipe1.flowModel.m_flows[$i1] > 0.0 ($RES_EVT_611) (309) [----] end for; (310) [SCAL] (1) pipe1.mediums[1].sat.Tsat = Modelica.Media.Water.IF97_Utilities.BaseIF97.Basic.tsat(pipe1.mediums[1].p) ($RES_SIM_315) (311) [ARRY] (1) pipe3.flowModel.dheights = pipe3.dheightsFM ($RES_BND_440) (312) [SCAL] (1) pipe1.mediums[1].T = Modelica.Media.Water.IF97_Utilities.T_props_ph(pipe1.mediums[1].p, pipe1.mediums[1].h, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(pipe1.mediums[1].p, pipe1.mediums[1].h, pipe1.mediums[1].phase, 0)) ($RES_SIM_316) (313) [ARRY] (1) pipe3.flowModel.pathLengths = pipe3.pathLengths ($RES_BND_441) (314) [ARRY] (1) pipe3.mediums.phase = pipe3.mediums.state.phase ($RES_SIM_141) (315) [SCAL] (1) $SEV_49[1] = pipe1.mediums[1].p >= 0.0 ($RES_EVT_612) (316) [SCAL] (1) pipe1.mediums[1].d = Modelica.Media.Water.IF97_Utilities.rho_props_ph(pipe1.mediums[1].p, pipe1.mediums[1].h, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(pipe1.mediums[1].p, pipe1.mediums[1].h, pipe1.mediums[1].phase, 0)) ($RES_SIM_317) (317) [FOR-] (2) ($RES_BND_442) (317) [----] for $i1 in 1:2 loop (317) [----] [SCAL] (1) pipe3.flowModel.rhos[$i1] = pipe3.flowModel.states.d ($RES_BND_443) (317) [----] end for; (318) [ARRY] (1) pipe3.mediums.d = pipe3.mediums.state.d ($RES_SIM_142) (319) [SCAL] (1) pipe1.mediums[1].phase = if $SEV_51 then 1 else 2 ($RES_SIM_318) (320) [ARRY] (1) pipe3.mediums.T = pipe3.mediums.state.T ($RES_SIM_143) (321) [SCAL] (1) $SEV_51 = (pipe1.mediums[1].h < Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(pipe1.mediums.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.boilingcurve_p(pipe1.mediums.sat.psat)) or pipe1.mediums[1].h > Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(pipe1.mediums.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.dewcurve_p(pipe1.mediums.sat.psat))) or pipe1.mediums[1].p > 2.2064e7 ($RES_EVT_614) (322) [FOR-] (2) ($RES_BND_444) (322) [----] for $i1 in 1:2 loop (322) [----] [SCAL] (1) pipe3.flowModel.mus[$i1] = pipe3.flowModel.mu_nominal ($RES_BND_445) (322) [----] end for; (323) [ARRY] (1) pipe3.mediums.p = pipe3.mediums.state.p ($RES_SIM_144) (324) [ARRY] (1) pipe3.mediums.h = pipe3.mediums.state.h ($RES_SIM_145) (325) [ARRY] (1) pipe3.flowModel.pathLengths_internal = pipe3.flowModel.pathLengths ($RES_BND_446) (326) [SCAL] (1) $SEV_54 = (source.medium.h < Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(source.medium.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.boilingcurve_p(source.medium.sat.psat)) or source.medium.h > Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(source.medium.sat.psat, Modelica.Media.Water.IF97_Utilities.BaseIF97.Regions.dewcurve_p(source.medium.sat.psat))) or source.p > 2.2064e7 ($RES_EVT_617) (327) [SCAL] (1) pipe3.flowModel.Res_turbulent_internal[1] = pipe3.flowModel.Re_turbulent ($RES_BND_447) (328) [SCAL] (1) pipe3.mediums[1].u = pipe3.mediums[1].h - pipe3.mediums[1].p / pipe3.mediums[1].d ($RES_SIM_147) (329) [SCAL] (1) $SEV_55 = (-valve2.m_flow) > valve2.m_flow_small ($RES_EVT_618) (330) [ARRY] (1) pipe3.flowModel.diameters = 0.5 * (pipe3.flowModel.dimensions[2:2] + pipe3.flowModel.dimensions[1:1]) ($RES_BND_448) (331) [ARRY] (1) pipe3.mediums.sat.psat = pipe3.mediums.p ($RES_SIM_148) (332) [SCAL] (1) $SEV_56 = (-valve2.m_flow) < (-valve2.m_flow_small) ($RES_EVT_619) (333) [SCAL] (1) pipe3.mediums[1].sat.Tsat = Modelica.Media.Water.IF97_Utilities.BaseIF97.Basic.tsat(pipe3.mediums[1].p) ($RES_SIM_149) (334) [SCAL] (1) -((-273.15) - sink.medium.T_degC) = Modelica.Media.Water.IF97_Utilities.T_props_ph(sink.p, sink.medium.h, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(sink.p, sink.medium.h, sink.medium.phase, 0)) ($RES_SIM_230) (335) [SCAL] (1) sink.medium.d = Modelica.Media.Water.IF97_Utilities.rho_props_ph(sink.p, sink.medium.h, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(sink.p, sink.medium.h, sink.medium.phase, 0)) ($RES_SIM_231) (336) [SCAL] (1) sink.medium.phase = if $SEV_35 then 1 else 2 ($RES_SIM_232) (337) [SCAL] (1) valve2.dp = pipe3.port_b.p - 99999.99999999999 * junctionVolume.medium.p_bar ($RES_SIM_236) (338) [SCAL] (1) source.ports[1].p = source.p ($RES_SIM_320) (339) [SCAL] (1) source.ports[1].h_outflow = source.medium.h ($RES_SIM_321) (340) [SCAL] (1) source.medium.h = Modelica.Media.Water.IF97_Utilities.h_pT(source.p, source.T, 0) ($RES_SIM_322) (341) [SCAL] (1) $SEV_57 = valve2.m_flow_small > 0.0 ($RES_EVT_620) (342) [ARRY] (1) pipe3.vs = {(0.5 * (pipe3.m_flows[2] + pipe3.m_flows[1])) / (pipe3.crossAreas[1] * pipe3.mediums[1].d)} / pipe3.nParallel ($RES_BND_450) (343) [SCAL] (1) pipe3.mediums[1].T = Modelica.Media.Water.IF97_Utilities.T_props_ph(pipe3.mediums[1].p, pipe3.mediums[1].h, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(pipe3.mediums[1].p, pipe3.mediums[1].h, pipe3.mediums[1].phase, 0)) ($RES_SIM_150) (344) [SCAL] (1) $SEV_58 = valve2.m_flow > valve2.m_flow_small ($RES_EVT_621) (345) [SCAL] (1) pipe3.mediums[1].d = Modelica.Media.Water.IF97_Utilities.rho_props_ph(pipe3.mediums[1].p, pipe3.mediums[1].h, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(pipe3.mediums[1].p, pipe3.mediums[1].h, pipe3.mediums[1].phase, 0)) ($RES_SIM_151) (346) [SCAL] (1) $SEV_59 = valve2.m_flow < (-valve2.m_flow_small) ($RES_EVT_622) (347) [ARRY] (1) pipe3.heatTransfer.Ts = {pipe3.heatTransfer.states.h} ($RES_BND_452) (348) [SCAL] (1) pipe3.mediums[1].phase = if $SEV_28 then 1 else 2 ($RES_SIM_152) (349) [SCAL] (1) $SEV_60 = (-valve1.m_flow) > valve1.m_flow_small ($RES_EVT_623) (350) [ARRY] (1) pipe3.heatTransfer.vs = pipe3.vs ($RES_BND_453) (351) [SCAL] (1) $SEV_61 = (-valve1.m_flow) < (-valve1.m_flow_small) ($RES_EVT_624) (352) [SCAL] (1) $DER.pipe2.ms[1] = pipe2.mb_flows[1] ($RES_SIM_154) (353) [SCAL] (1) $SEV_62 = valve1.m_flow_small > 0.0 ($RES_EVT_625) (354) [SCAL] (1) $DER.pipe2.Us[1] = pipe2.Wb_flows[1] + pipe2.Hb_flows[1] + pipe2.Qb_flows[1] ($RES_SIM_155) (355) [SCAL] (1) $SEV_63 = valve1.m_flow > valve1.m_flow_small ($RES_EVT_626) (356) [SCAL] (1) pipe2.ms[1] = pipe2.fluidVolumes[1] * pipe2.mediums[1].d ($RES_SIM_156) (357) [SCAL] (1) $SEV_64 = valve1.m_flow < (-valve1.m_flow_small) ($RES_EVT_627) (358) [SCAL] (1) pipe2.Us[1] = pipe2.ms[1] * pipe2.mediums[1].u ($RES_SIM_157) (359) [SCAL] (1) pipe2.port_b.p = pipe2.mediums[1].p ($RES_SIM_158) (360) [ARRY] (1) pipe2.vsFM[2:2] = pipe2.vs ($RES_SIM_159) (361) [SCAL] (1) valve2.m_flow = homotopy(valve2.Y * valve2.Av * valveOpening2.y * smooth(2, if $SEV_36 then (if $SEV_37 then sqrt(valve2.state_a.d) else 0.0) * sqrt(valve2.xs * valve2.p) else if $SEV_38 then -(if $SEV_39 then sqrt(valve2.state_b.d) else 0.0) * sqrt(abs(valve2.xs * valve2.p)) else if $SEV_40 then Modelica.Fluid.Utilities.regRoot2.regRoot2_utility(valve2.xs * valve2.p, valve2.dp_turbulent, valve2.state_a.d, valve2.state_b.d, false, 1.0) else -Modelica.Fluid.Utilities.regRoot2.regRoot2_utility(-valve2.xs * valve2.p, valve2.dp_turbulent, valve2.state_b.d, valve2.state_a.d, false, 1.0)), (valve2.dp * valve2.m_flow_nominal * valveOpening2.y) / valve2.dp_nominal) ($RES_SIM_241) (362) [SCAL] (1) valve2.Y = 1.0 - (0.3333333333333333 * $FUN_6) / valve2.Fxt_full ($RES_SIM_242) (363) [SCAL] (1) valve2.xs = max(-valve2.Fxt_full, min(valve2.x, valve2.Fxt_full)) ($RES_SIM_243) (364) [SCAL] (1) valve2.x = valve2.dp / valve2.p ($RES_SIM_244) (365) [SCAL] (1) valve2.p = max(pipe3.port_b.p, 99999.99999999999 * junctionVolume.medium.p_bar) ($RES_SIM_246) (366) [SCAL] (1) valve2.minLimiter.y = smooth(0, noEvent(if $SEV_41 then valve2.minLimiter.uMin else valveOpening2.y)) ($RES_SIM_247) (367) [ARRY] (1) pipe1.fluidVolumes = {10.0 * pipe1.crossAreas[1]} .* pipe1.nParallel ($RES_BND_374) (368) [SCAL] (1) pipe1.state_a.d = Modelica.Media.Water.IF97_Utilities.rho_ph(pipe1.port_a.p, source.ports[1].h_outflow, 0, 0) ($RES_SIM_500) (369) [ARRY] (1) pipe1.mediums.p_bar = {1e-5 * pipe1.mediums[1].p} ($RES_BND_375) (370) [SCAL] (1) pipe1.state_a.T = Modelica.Media.Water.IF97_Utilities.T_ph(pipe1.port_a.p, source.ports[1].h_outflow, 0, 0) ($RES_SIM_501) (371) [ARRY] (1) pipe1.mediums.T_degC = {(-273.15) + pipe1.mediums[1].T} ($RES_BND_376) (372) [SCAL] (1) pipe1.state_a.p = pipe1.port_a.p ($RES_SIM_502) (373) [ARRY] (3) pipe1.flowModel.vs = pipe1.vsFM ($RES_BND_377) (374) [SCAL] (1) pipe1.state_b.phase = 0 ($RES_SIM_503) (375) [ARRY] (3) pipe1.flowModel.crossAreas = pipe1.crossAreasFM ($RES_BND_378) (376) [SCAL] (1) pipe1.state_b.h = junctionIdeal.port_3.h_outflow ($RES_SIM_504) (377) [ARRY] (3) pipe1.flowModel.dimensions = pipe1.dimensionsFM ($RES_BND_379) (378) [SCAL] (1) pipe1.state_b.d = Modelica.Media.Water.IF97_Utilities.rho_ph(99999.99999999999 * junctionIdeal.medium.p_bar, junctionIdeal.port_3.h_outflow, 0, 0) ($RES_SIM_505) (379) [SCAL] (1) pipe1.state_b.T = Modelica.Media.Water.IF97_Utilities.T_ph(99999.99999999999 * junctionIdeal.medium.p_bar, junctionIdeal.port_3.h_outflow, 0, 0) ($RES_SIM_506) (380) [SCAL] (1) source.medium.phase = source.medium.state.phase ($RES_SIM_332) (381) [SCAL] (1) pipe1.state_b.p = 99999.99999999999 * junctionIdeal.medium.p_bar ($RES_SIM_507) (382) [SCAL] (1) source.medium.d = source.medium.state.d ($RES_SIM_333) (383) [SCAL] (1) valve1.state_a.phase = 0 ($RES_SIM_508) (384) [SCAL] (1) -((-273.15) - source.medium.T_degC) = source.medium.state.T ($RES_SIM_334) (385) [SCAL] (1) valve1.state_a.h = valve1.port_b.h_outflow ($RES_SIM_509) (386) [SCAL] (1) pipe2.vsFM[1] = ((pipe2.m_flows[1] / pipe2.state_a.d) / pipe2.crossAreas[1]) / pipe2.nParallel ($RES_SIM_160) (387) [SCAL] (1) source.medium.h = source.medium.state.h ($RES_SIM_336) (388) [ARRY] (1) pipe2.m_flows[1:1] = pipe2.flowModel.m_flows[:] ($RES_SIM_161) (389) [ARRY] (5) pipe2.statesFM[2:2] = pipe2.mediums[:].state ($RES_SIM_162) (390) [SCAL] (1) source.medium.u = source.medium.h - source.p / source.medium.d ($RES_SIM_338) (391) [RECD] (5) pipe2.statesFM[1] = pipe2.state_a ($RES_SIM_163) (392) [ARRY] (15) pipe1.flowModel.states = pipe1.statesFM ($RES_BND_463) (393) [SCAL] (1) source.medium.sat.psat = source.p ($RES_SIM_339) (394) [ARRY] (5) pipe1.heatTransfer.states = pipe1.mediums.state ($RES_BND_464) (395) [ARRY] (10) pipe2.flowModel.states = pipe2.statesFM ($RES_BND_465) (396) [SCAL] (1) valve1.port_b.h_outflow = pipe2.mediums[1].h ($RES_SIM_166) (397) [ARRY] (5) pipe2.heatTransfer.states = pipe2.mediums.state ($RES_BND_466) (398) [SCAL] (1) pipe2.port_a.h_outflow = pipe2.mediums[1].h ($RES_SIM_167) (399) [ARRY] (10) pipe3.flowModel.states = pipe3.statesFM ($RES_BND_467) (400) [SCAL] (1) -valve1.m_flow = -pipe2.m_flows[2] ($RES_SIM_168) (401) [ARRY] (5) pipe3.heatTransfer.states = pipe3.mediums.state ($RES_BND_468) (402) [SCAL] (1) pipe2.port_a.m_flow = pipe2.m_flows[1] ($RES_SIM_169) (403) [SCAL] (1) valve1.dp = pipe2.port_b.p - 99999.99999999999 * junctionVolume.medium.p_bar ($RES_SIM_250)