Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries/ --ompython_omhome=/usr IDEAS_IDEAS.Fluid.FixedResistances.Validation.PlugFlowPipes.TransportWaterAir.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 4.0.0+maint.om/package.mo", uses=false) loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/IDEAS 3.0.0/package.mo", uses=false) Using package IDEAS with version 3.0.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/IDEAS 3.0.0/package.mo) Using package Modelica with version 4.0.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.0.0+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(IDEAS.Fluid.FixedResistances.Validation.PlugFlowPipes.TransportWaterAir,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="IDEAS_IDEAS.Fluid.FixedResistances.Validation.PlugFlowPipes.TransportWaterAir") translateModel(IDEAS.Fluid.FixedResistances.Validation.PlugFlowPipes.TransportWaterAir,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="IDEAS_IDEAS.Fluid.FixedResistances.Validation.PlugFlowPipes.TransportWaterAir") Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo): time 0.001276/0.001276, allocations: 103.5 kB / 16.37 MB, free: 6.367 MB / 14.72 MB Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo): time 0.001285/0.001285, allocations: 195.2 kB / 17.31 MB, free: 5.91 MB / 14.72 MB Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.0.0+maint.om/package.mo): time 1.274/1.274, allocations: 222.9 MB / 241 MB, free: 15.18 MB / 206.1 MB Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/IDEAS 3.0.0/package.mo): time 0.748/0.748, allocations: 132.2 MB / 423.4 MB, free: 6.594 MB / 334.1 MB Notification: Performance of FrontEnd - Absyn->SCode: time 1.854e-05/1.857e-05, allocations: 2.281 kB / 0.5031 GB, free: 11.01 MB / 430.1 MB Notification: Performance of NFInst.instantiate(IDEAS.Fluid.FixedResistances.Validation.PlugFlowPipes.TransportWaterAir): time 0.7565/0.7565, allocations: 310.2 MB / 0.8061 GB, free: 7.277 MB / 0.545 GB Notification: Performance of NFInst.instExpressions: time 0.03228/0.7888, allocations: 26.52 MB / 0.832 GB, free: 6.348 MB / 0.545 GB Notification: Performance of NFInst.updateImplicitVariability: time 0.005584/0.7944, allocations: 126.8 kB / 0.8321 GB, free: 6.348 MB / 0.545 GB Notification: Performance of NFTyping.typeComponents: time 0.005007/0.7994, allocations: 1.653 MB / 0.8337 GB, free: 5.68 MB / 0.545 GB Notification: Performance of NFTyping.typeBindings: time 0.01607/0.8156, allocations: 5.591 MB / 0.8392 GB, free: 3.25 MB / 0.545 GB Notification: Performance of NFTyping.typeClassSections: time 0.009501/0.8251, allocations: 3.687 MB / 0.8428 GB, free: 1.129 MB / 0.545 GB Notification: Performance of NFFlatten.flatten: time 0.01362/0.8387, allocations: 9.577 MB / 0.8521 GB, free: 11.73 MB / 0.5606 GB Notification: Performance of NFFlatten.resolveConnections: time 0.006417/0.8452, allocations: 3.166 MB / 0.8552 GB, free: 8.68 MB / 0.5606 GB Notification: Performance of NFEvalConstants.evaluate: time 0.01094/0.8562, allocations: 3.954 MB / 0.8591 GB, free: 5.34 MB / 0.5606 GB Notification: Performance of NFSimplifyModel.simplify: time 0.006127/0.8623, allocations: 2.559 MB / 0.8616 GB, free: 3.047 MB / 0.5606 GB Notification: Performance of NFPackage.collectConstants: time 0.001492/0.8638, allocations: 336 kB / 0.8619 GB, free: 2.719 MB / 0.5606 GB Notification: Performance of NFFlatten.collectFunctions: time 0.01258/0.8764, allocations: 5.108 MB / 0.8669 GB, free: 14.54 MB / 0.5762 GB Notification: Performance of combineBinaries: time 0.01034/0.8868, allocations: 6.175 MB / 0.8729 GB, free: 8.633 MB / 0.5762 GB Notification: Performance of replaceArrayConstructors: time 0.004793/0.8916, allocations: 3.867 MB / 0.8767 GB, free: 4.891 MB / 0.5762 GB Notification: Performance of NFVerifyModel.verify: time 0.002396/0.894, allocations: 0.6389 MB / 0.8773 GB, free: 4.25 MB / 0.5762 GB Notification: Performance of FrontEnd: time 0.001045/0.8951, allocations: 112.1 kB / 0.8774 GB, free: 4.152 MB / 0.5762 GB Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 547 (515) * Number of variables: 547 (499) Notification: Performance of Bindings: time 0.02163/0.9167, allocations: 17.14 MB / 0.8942 GB, free: 2.98 MB / 0.5919 GB Notification: Performance of FunctionAlias: time 0.002451/0.9192, allocations: 1.843 MB / 0.896 GB, free: 1.23 MB / 0.5919 GB Notification: Performance of Early Inline: time 0.01112/0.9304, allocations: 8.268 MB / 0.904 GB, free: 9.047 MB / 0.6075 GB Notification: Performance of simplify1: time 0.001084/0.9315, allocations: 0.5322 MB / 0.9045 GB, free: 8.535 MB / 0.6075 GB Notification: Performance of Alias: time 0.01505/0.9465, allocations: 11.87 MB / 0.9161 GB, free: 11.96 MB / 0.6231 GB Notification: Performance of simplify2: time 0.0007983/0.9474, allocations: 421 kB / 0.9165 GB, free: 11.57 MB / 0.6231 GB Notification: Performance of Events: time 0.001699/0.9491, allocations: 1.473 MB / 0.918 GB, free: 10.13 MB / 0.6231 GB Notification: Performance of Detect States: time 0.002309/0.9514, allocations: 1.743 MB / 0.9197 GB, free: 8.422 MB / 0.6231 GB Notification: Performance of Partitioning: time 0.003463/0.9549, allocations: 2.437 MB / 0.9221 GB, free: 5.789 MB / 0.6231 GB Error: Internal error NBSlice.fillDependencyArray failed because number of flattened indices 1 for dependency $FUN_21[$i1] could not be devided by the body size 2 without rest. Error: Internal error NBAdjacency.Matrix.createPseudo failed for: [FOR-] (2) ($RES_$AUX_604) [----] for $i1 in 1:1 loop [----] [TUPL] (2) ($FUN_20[$i1], $FUN_21[$i1]) = spatialDistribution(duc.del.Xi_inflow_a[$i1], duc.del.Xi_inflow_b[$i1], duc.del.x / duc.del.length, $SEV_39[$i1], {0.0, 1.0}, {0.01, 0.01}) ($RES_$AUX_605) [----] end for; Error: Internal error NBAdjacency.Matrix.create failed to create adjacency matrix for system: System Variables (327/376) **************************** (1) [ALGB] (1) final Real duc.res.dp = duc.senMasFlo.port_b.p - duc.heaLos_b.port_a.p (start = duc.res._dp_start, nominal = 200.0 * duc.fac * duc.length) (2) [ALGB] (2) protected Real[2] duc.vol_a.dynBal.ports.p (start = {101325.0 for $ports1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e5 for $i1 in 1:2}) (3) [ALGB] (1) Real senTemIn.port_a.p (start = 3e5, min = 0.0, max = 1e8, nominal = 1e5) (4) [ALGB] (2) protected flow Real[2] duc.vol_b.ports.m_flow (min = {-1e5 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}) (5) [ALGB] (2) protected stream Real[2, 1] duc.vol_a.ports.Xi_outflow (min = {{0.0 for $i1 in 1:1} for $ports1 in 1:2}, max = {{1.0 for $i1 in 1:1} for $ports1 in 1:2}, nominal = {{0.1 for $i1 in 1:1} for $ports1 in 1:2}) (6) [ALGB] (2) protected flow Real[2] pip.vol_a.ports.m_flow (min = {-1e5 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}) (7) [ALGB] (1) protected stream Real duc.heaLos_a.port_b.h_outflow (start = 45300.945, min = -1e10, max = 1e10, nominal = 45300.945) (8) [ALGB] (1) stream Real[1] senTemOutA.port_a.Xi_outflow (min = {0.0 for $i1 in 1:1}, max = {1.0 for $i1 in 1:1}, nominal = {0.1 for $i1 in 1:1}) (9) [ALGB] (1) protected flow Real pip.heaLos_b.heatPort.Q_flow (10) [ALGB] (1) protected stream Real[1] duc.heaLos_b.port_a.C_outflow (start = {1.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}) (11) [ALGB] (1) protected Real duc.vol_a.T = IDEAS.Fluid.FixedResistances.Validation.PlugFlowPipes.TransportWaterAir.duc.vol_a.Medium.temperature_phX(duc.vol_a.p, -((-84437.5) - duc.vol_a.dynBal.medium.u), {duc.vol_a.Xi[1], 1.0 - sum(duc.vol_a.Xi)}) (start = 293.15, min = 1.0, max = 1e4, nominal = 300.0) (12) [ALGB] (1) protected Real pip.vol_a.dynBal.Hb_flow (13) [ALGB] (2) protected stream Real[2] pip.vol_a.ports.h_outflow (min = {-1e10 for $i1 in 1:2}, max = {1e10 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2}) (14) [ALGB] (1) flow Real[1] sin.ports.m_flow (min = {-1e60}, max = {1e60}) (15) [ALGB] (2) protected Real[2] pip.vol_b.dynBal.ports_H_flow (min = {-1e8 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1000.0 for $i1 in 1:2}) (16) [ALGB] (1) protected Real pip.vol_b.dynBal.medium.state.T (start = 293.15, min = 1.0, max = 1e4, nominal = 300.0) (17) [ALGB] (1) protected Real[1] duc.vol_a.dynBal.mXiOut (min = {0.0 for $i1 in 1:1}) (18) [ALGB] (2) protected Real[2] pip.vol_b.ports.p (start = {3e5 for $ports1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e5 for $i1 in 1:2}) (19) [ALGB] (1) protected Real[1] duc.vol_a.dynBal.COut (min = {0.0 for $i1 in 1:1}) (20) [ALGB] (1) protected Real duc.timDel.u (21) [ALGB] (1) protected Real[1] duc.vol_b.dynBal.mCOut (min = {0.0 for $i1 in 1:1}) (22) [ALGB] (2) protected Real[2] sin1.X_in_internal (23) [ALGB] (1) stream Real senTemIn1.port_a.h_outflow (start = 45300.945, min = -1e10, max = 1e10, nominal = 45300.945) (24) [ALGB] (2) protected Real[2] pip.vol_a.ports.p (start = {3e5 for $ports1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e5 for $i1 in 1:2}) (25) [ALGB] (1) protected stream Real[1] duc.heaLos_b.port_b.Xi_outflow (min = {0.0 for $i1 in 1:1}, max = {1.0 for $i1 in 1:1}, nominal = {0.1 for $i1 in 1:1}) (26) [ALGB] (1) protected Real[1] duc.vol_a.dynBal.mbC_flow (27) [ALGB] (1) protected Real duc.vol_b.dynBal.Hb_flow (28) [ALGB] (1) protected stream Real[1] duc.del.port_b.C_outflow (start = {1.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}) (29) [ALGB] (1) stream Real[1] duc.port_b.Xi_outflow (min = {0.0 for $i1 in 1:1}, max = {1.0 for $i1 in 1:1}, nominal = {0.1 for $i1 in 1:1}) (30) [ALGB] (1) protected Real duc.vol_a.p = duc.vol_a.ports[1].p (31) [ALGB] (1) protected Real[1] duc.vol_b.C = duc.vol_b.COut_internal (start = {1.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, nominal = duc.vol_b.C_nominal) (32) [ALGB] (2) Real[2] sou1.X_in (33) [ALGB] (1) final Real pip.res.m_flow = pip.res.m_flow (start = pip.res._m_flow_start, nominal = 1.0) (34) [ALGB] (1) protected Real duc.vol_b.dynBal.medium.T_degC = Modelica.Units.Conversions.to_degC(-((-273.15) - duc.vol_b.dynBal.medium.T_degC)) (35) [ALGB] (1) stream Real[1] senTemIn1.port_b.Xi_outflow (min = {0.0 for $i1 in 1:1}, max = {1.0 for $i1 in 1:1}, nominal = {0.1 for $i1 in 1:1}) (36) [DER-] (1) Real[1] $DER.duc.vol_b.dynBal.mC (37) [ALGB] (1) final Real pip.res.dp = pip.senMasFlo.port_b.p - pip.heaLos_b.port_a.p (start = pip.res._dp_start, nominal = 200.0 * pip.fac * pip.length) (38) [ALGB] (1) protected Real duc.vol_b.T = IDEAS.Fluid.FixedResistances.Validation.PlugFlowPipes.TransportWaterAir.duc.vol_b.Medium.temperature_phX(duc.vol_b.p, -((-84437.5) - duc.vol_b.dynBal.medium.u), {duc.vol_b.Xi[1], 1.0 - sum(duc.vol_b.Xi)}) (start = 293.15, min = 1.0, max = 1e4, nominal = 300.0) (39) [ALGB] (1) protected Real[1] duc.vol_b.dynBal.C (start = {1.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, nominal = duc.vol_b.dynBal.C_nominal) (40) [ALGB] (2) protected stream Real[2] duc.vol_b.ports.h_outflow (min = {-1e10 for $i1 in 1:2}, max = {1e10 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2}) (41) [ALGB] (1) stream Real[1] senTemOutA.port_b.Xi_outflow (min = {0.0 for $i1 in 1:1}, max = {1.0 for $i1 in 1:1}, nominal = {0.1 for $i1 in 1:1}) (42) [ALGB] (1) protected Real[1] duc.vol_b.dynBal.COut (min = {0.0 for $i1 in 1:1}) (43) [ALGB] (1) protected Real duc.del.V_flow = duc.res.m_flow / Modelica.Fluid.Utilities.regStep(duc.res.m_flow, IDEAS.Fluid.FixedResistances.Validation.PlugFlowPipes.TransportWaterAir.duc.del.Medium.density(IDEAS.Fluid.FixedResistances.Validation.PlugFlowPipes.TransportWaterAir.duc.del.Medium.setState_phX(duc.heaLos_b.port_a.p, duc.heaLos_a.port_a.h_outflow, {duc.res.port_b.Xi_outflow[1]})), IDEAS.Fluid.FixedResistances.Validation.PlugFlowPipes.TransportWaterAir.duc.del.Medium.density(IDEAS.Fluid.FixedResistances.Validation.PlugFlowPipes.TransportWaterAir.duc.del.Medium.setState_phX(duc.heaLos_b.port_a.p, duc.heaLos_b.port_a.h_outflow, {duc.heaLos_b.port_a.Xi_outflow[1]})), duc.del.m_flow_small) (44) [ALGB] (2) protected flow Real[2] duc.vol_b.dynBal.ports.m_flow (min = {-1e5 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}) (45) [ALGB] (1) protected Real duc.vol_b.dynBal.medium.p_bar = Modelica.Units.Conversions.to_bar(99999.99999999999 * duc.vol_b.dynBal.medium.p_bar) (46) [ALGB] (2) protected Real[2] duc.vol_a.dynBal.medium.X (start = duc.vol_a.dynBal.X_start, min = {0.0 for $i1 in 1:2}, max = {1.0 for $i1 in 1:2}, nominal = {0.1 for $i1 in 1:2}) (47) [ALGB] (1) protected Real[1] duc.vol_a.dynBal.mbXi_flow (48) [ALGB] (1) stream Real[1] duc.res.port_a.C_outflow (start = {1.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}) (49) [ALGB] (1) protected Real[1] duc.vol_b.dynBal.C_flow_internal (50) [ALGB] (1) protected Real[1] duc.del.Xi_inflow_b = {duc.heaLos_b.port_a.Xi_outflow[1]} (min = {0.0 for $i1 in 1:1}, max = {1.0 for $i1 in 1:1}, nominal = {0.1 for $i1 in 1:1}) (51) [ALGB] (1) protected Real[1] duc.del.Xi_inflow_a = {duc.res.port_b.Xi_outflow[1]} (min = {0.0 for $i1 in 1:1}, max = {1.0 for $i1 in 1:1}, nominal = {0.1 for $i1 in 1:1}) (52) [ALGB] (1) stream Real[1] senTemIn1.port_b.C_outflow (start = {1.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}) (53) [ALGB] (1) protected Real duc.vol_b.p = duc.vol_b.ports[1].p (54) [DER-] (1) Real $DER.duc.vol_b.dynBal.U (55) [ALGB] (2) protected stream Real[2] pip.vol_b.ports.h_outflow (min = {-1e10 for $i1 in 1:2}, max = {1e10 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2}) (56) [ALGB] (1) protected stream Real pip.heaLos_b.port_b.h_outflow (start = 83680.0, min = -1e10, max = 1e10, nominal = 83680.0) (57) [ALGB] (1) protected Real duc.vol_a.dynBal.medium.MM (min = 0.001, max = 0.25, nominal = 0.032) (58) [ALGB] (1) protected Real[1] sin1.C_in_internal (59) [ALGB] (1) protected Real pip.vol_b.dynBal.mb_flow (60) [ALGB] (1) protected stream Real[1] duc.heaLos_a.port_a.Xi_outflow (min = {0.0 for $i1 in 1:1}, max = {1.0 for $i1 in 1:1}, nominal = {0.1 for $i1 in 1:1}) (61) [ALGB] (1) protected Real duc.vol_a.dynBal.medium.u (min = -1e8, max = 1e8, nominal = 1e6) (62) [ALGB] (1) Real senTemIn1.T (start = senTemIn1.T_start, min = 0.0) (63) [ALGB] (1) protected stream Real duc.heaLos_b.port_b.h_outflow (start = 45300.945, min = -1e10, max = 1e10, nominal = 45300.945) (64) [ALGB] (2) protected flow Real[2] duc.vol_a.dynBal.ports.m_flow (min = {-1e5 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}) (65) [ALGB] (1) protected Real duc.vol_a.dynBal.medium.p_bar = Modelica.Units.Conversions.to_bar(99999.99999999999 * duc.vol_a.dynBal.medium.p_bar) (66) [ALGB] (1) protected Real pip.senMasFlo.port_b.p (start = 3e5, min = 0.0, max = 1e8, nominal = 1e5) (67) [DER-] (1) Real $DER.duc.vol_b.dynBal.m (68) [ALGB] (1) stream Real[1] senTemIn1.port_a.Xi_outflow (min = {0.0 for $i1 in 1:1}, max = {1.0 for $i1 in 1:1}, nominal = {0.1 for $i1 in 1:1}) (69) [ALGB] (1) protected Real duc.heaLos_a.TAmb = duc.heaLos_a.TAmb (start = 288.15, min = 0.0, nominal = 300.0) (70) [ALGB] (1) protected Real sou1.p_in_internal (71) [ALGB] (1) stream Real[1, 1] sin1.ports.Xi_outflow (min = {{0.0 for $i1 in 1:1}}, max = {{1.0 for $i1 in 1:1}}, nominal = {{0.1 for $i1 in 1:1}}) (72) [ALGB] (1) protected Real duc.timDel.tau (73) [ALGB] (1) protected Real senTemOutA.T_b_inflow (start = 293.15, min = 1.0, max = 1e4, nominal = 300.0) (74) [ALGB] (2) protected stream Real[2, 1] duc.vol_a.ports.C_outflow (start = {{1.0 for $i1 in 1:1} for $ports1 in 1:2}, min = {{0.0 for $i1 in 1:1} for $ports1 in 1:2}) (75) [ALGB] (1) stream Real[1] senTemOutA.port_a.C_outflow (start = {1.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}) (76) [ALGB] (1) flow Real[1] sin1.ports.m_flow (min = {-1e60}, max = {1e60}) (77) [ALGB] (1) stream Real[1, 1] sou1.ports.C_outflow (start = {{1.0 for $i1 in 1:1}}, min = {{0.0 for $i1 in 1:1}}) (78) [DISC] (1) Boolean $TEV_1 (79) [DISC] (1) Boolean $TEV_0 (80) [ALGB] (1) protected Real duc.timDel.tauRev (81) [ALGB] (1) protected Real duc.heaLos_b.T_b_outflow (start = duc.heaLos_b.T_start, min = 0.0, nominal = 300.0) (82) [ALGB] (1) protected Real duc.vol_a.dynBal.Hb_flow (83) [ALGB] (1) protected Real pip.heaLos_a.port_b.p (start = 3e5, min = 0.0, max = 1e8, nominal = 1e5) (84) [ALGB] (1) stream Real pip.port_b.h_outflow (start = 83680.0, min = -1e10, max = 1e10, nominal = 83680.0) (85) [ALGB] (1) protected stream Real[1] duc.senMasFlo.port_a.C_outflow (start = {1.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}) (86) [ALGB] (1) protected stream Real[1] duc.heaLos_a.port_b.Xi_outflow (min = {0.0 for $i1 in 1:1}, max = {1.0 for $i1 in 1:1}, nominal = {0.1 for $i1 in 1:1}) (87) [ALGB] (2) protected Real[2, 1] duc.vol_a.dynBal.ports_mXi_flow (88) [ALGB] (1) Real[1] sin1.ports.p (start = {101325.0}, min = {0.0 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e5 for $i1 in 1:1}) (89) [ALGB] (1) protected Real[1] sou1.C_in_internal (90) [ALGB] (2) protected Real[2, 1] duc.vol_a.dynBal.ports_mC_flow (91) [ALGB] (2) protected stream Real[2, 1] duc.vol_b.dynBal.ports.C_outflow (start = {{1.0 for $i1 in 1:1} for $ports1 in 1:2}, min = {{0.0 for $i1 in 1:1} for $ports1 in 1:2}) (92) [ALGB] (2) protected Real[2] pip.vol_a.dynBal.ports.p (start = {3e5 for $ports1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e5 for $i1 in 1:2}) (93) [ALGB] (1) protected Real senTemIn.T_a_inflow (start = 293.15, min = 1.0, max = 1e4, nominal = 300.0) (94) [ALGB] (1) flow Real[1] sou.ports.m_flow (min = {-1e60}, max = {1e60}) (95) [ALGB] (1) flow Real senTemOutA.port_b.m_flow (min = -1e5, max = 1e60) (96) [ALGB] (1) stream Real[1, 1] sou1.ports.Xi_outflow (min = {{0.0 for $i1 in 1:1}}, max = {{1.0 for $i1 in 1:1}}, nominal = {{0.1 for $i1 in 1:1}}) (97) [ALGB] (1) protected Real pip.vol_a.p = pip.vol_a.ports[1].p (98) [ALGB] (1) protected Real duc.vol_b.dynBal.medium.R_s (start = 1000.0, min = 0.0, max = 1e7, nominal = 1000.0) (99) [ALGB] (2) protected Real[2] duc.vol_b.dynBal.ports.p (start = {101325.0 for $ports1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e5 for $i1 in 1:2}) (100) [ALGB] (1) protected Real pip.vol_a.dynBal.medium.T_degC = Modelica.Units.Conversions.to_degC(-((-273.15) - pip.vol_a.dynBal.medium.T_degC)) (101) [ALGB] (1) stream Real[1] duc.port_a.C_outflow (start = {1.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}) (102) [ALGB] (1) protected stream Real[1] duc.heaLos_a.port_b.C_outflow (start = {1.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}) (103) [ALGB] (1) protected Real senTemOutA.T_a_inflow (start = 293.15, min = 1.0, max = 1e4, nominal = 300.0) (104) [ALGB] (1) protected Real pip.vol_a.dynBal.medium.p_bar = Modelica.Units.Conversions.to_bar(99999.99999999999 * pip.vol_a.dynBal.medium.p_bar) (105) [ALGB] (2) protected flow Real[2] pip.vol_a.dynBal.ports.m_flow (min = {-1e5 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}) (106) [DER-] (1) Real[1] $DER.duc.vol_b.dynBal.mXi (107) [ALGB] (1) protected Real duc.senMasFlo.port_b.p (start = 101325.0, min = 0.0, max = 1e8, nominal = 1e5) (108) [ALGB] (1) Real senTemOutW.T (start = senTemOutW.T_start, min = 0.0) (109) [ALGB] (1) protected stream Real pip.heaLos_a.port_b.h_outflow (start = 83680.0, min = -1e10, max = 1e10, nominal = 83680.0) (110) [ALGB] (1) Real[1] sou1.ports.p (start = {101325.0}, min = {0.0 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e5 for $i1 in 1:1}) (111) [ALGB] (1) Real senTemOutA.T (start = senTemOutA.T_start, min = 0.0) (112) [ALGB] (2) protected Real[2, 1] duc.vol_b.dynBal.ports_mXi_flow (113) [ALGB] (1) Real pip.v = pip.v (114) [ALGB] (2) Real[2] XiIn.y (115) [ALGB] (1) Real duc.m_flow = duc.m_flow (start = duc.m_flow_start) (116) [ALGB] (2) protected stream Real[2, 1] duc.vol_a.dynBal.ports.Xi_outflow (min = {{0.0 for $i1 in 1:1} for $ports1 in 1:2}, max = {{1.0 for $i1 in 1:1} for $ports1 in 1:2}, nominal = {{0.1 for $i1 in 1:1} for $ports1 in 1:2}) (117) [ALGB] (1) protected Real sou1.h_internal = IDEAS.Fluid.FixedResistances.Validation.PlugFlowPipes.TransportWaterAir.sou1.Medium.specificEnthalpy(IDEAS.Fluid.FixedResistances.Validation.PlugFlowPipes.TransportWaterAir.sou1.Medium.setState_pTX(sou1.p_in_internal, -2.390057361376673e-4 * ((-1.1428595999999999e6) - sou.h_internal), sou1.X_in_internal)) (118) [ALGB] (1) protected Real[1] duc.vol_a.dynBal.medium.Xi (start = duc.vol_a.dynBal.X_start[1:1], min = {0.0 for $i1 in 1:1}, max = {1.0 for $i1 in 1:1}, StateSelect = default) (119) [ALGB] (1) protected Real[1] duc.vol_b.XiOut_internal (120) [ALGB] (1) protected Real pip.vol_b.p = pip.vol_b.ports[1].p (121) [ALGB] (1) protected Real[1] duc.vol_a.XiOut_internal (122) [ALGB] (2) protected Real[2, 1] duc.vol_b.dynBal.ports_mC_flow (123) [ALGB] (1) protected Real pip.vol_b.dynBal.medium.p_bar = Modelica.Units.Conversions.to_bar(99999.99999999999 * pip.vol_b.dynBal.medium.p_bar) (124) [ALGB] (2) protected flow Real[2] pip.vol_b.dynBal.ports.m_flow (min = {-1e5 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}) (125) [ALGB] (1) stream Real senTemOutA.port_b.h_outflow (start = 45300.945, min = -1e10, max = 1e10, nominal = 45300.945) (126) [ALGB] (1) protected stream Real duc.heaLos_a.port_a.h_outflow (start = 45300.945, min = -1e10, max = 1e10, nominal = 45300.945) (127) [ALGB] (1) protected Real duc.heaLos_a.T_b_outflow (start = duc.heaLos_a.T_start, min = 0.0, nominal = 300.0) (128) [ALGB] (1) protected Real duc.heaLos_b.port_a.p (start = 101325.0, min = 0.0, max = 1e8, nominal = 1e5) (129) [ALGB] (2) protected stream Real[2, 1] duc.vol_b.ports.C_outflow (start = {{1.0 for $i1 in 1:1} for $ports1 in 1:2}, min = {{0.0 for $i1 in 1:1} for $ports1 in 1:2}) (130) [ALGB] (1) protected Real[1] duc.del.C_inflow_a = {duc.res.port_b.C_outflow[1]} (start = {1.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}) (131) [ALGB] (2) protected stream Real[2] pip.vol_a.dynBal.ports.h_outflow (min = {-1e10 for $i1 in 1:2}, max = {1e10 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2}) (132) [ALGB] (1) protected Real[1] duc.del.C_inflow_b = {duc.heaLos_b.port_a.C_outflow[1]} (start = {1.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}) (133) [DER-] (1) Real $DER.duc.vol_a.dynBal.U (134) [DER-] (1) Real[1] $DER.duc.vol_a.dynBal.mXi (135) [DISC] (1) Boolean $SEV_9 (136) [ALGB] (1) Real duc.dp = senTemIn1.port_a.p - senTemOutA.port_b.p (start = duc._dp_start) (137) [DISC] (1) Boolean $SEV_8 (138) [DISC] (1) Boolean[1] $SEV_39[$i1] (139) [DISC] (1) Boolean $SEV_7 (140) [ALGB] (1) Real senTemIn.T (start = senTemIn.T_start, min = 0.0) (141) [ALGB] (1) protected Real pip.vol_b.dynBal.medium.T_degC = Modelica.Units.Conversions.to_degC(-((-273.15) - pip.vol_b.dynBal.medium.T_degC)) (142) [ALGB] (1) protected Real duc.vol_a.dynBal.mb_flow (143) [ALGB] (1) protected Real[1] duc.vol_a.dynBal.C_flow_internal (144) [ALGB] (1) protected Real pip.timDel.tau (145) [ALGB] (1) stream Real senTemIn1.port_b.h_outflow (start = 45300.945, min = -1e10, max = 1e10, nominal = 45300.945) (146) [ALGB] (1) Real $FUN_52 (147) [ALGB] (1) protected stream Real[1] duc.del.port_a.C_outflow (start = {1.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}) (148) [ALGB] (1) Real $FUN_51 (149) [ALGB] (1) Real pip.m_flow = pip.m_flow (start = pip.m_flow_start) (150) [DER-] (1) Real $DER.duc.vol_a.dynBal.m (151) [ALGB] (2) protected Real[2] duc.vol_b.dynBal.ports_H_flow (min = {-1e8 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1000.0 for $i1 in 1:2}) (152) [DER-] (1) Real[1] $DER.duc.vol_a.dynBal.mC (153) [ALGB] (1) flow Real senTemOutW.port_b.m_flow (min = -1e5, max = 1e60) (154) [ALGB] (2) protected Real[2] sou1.X_in_internal (155) [ALGB] (1) protected Real duc.heaLos_b.port_b.p (start = 101325.0, min = 0.0, max = 1e8, nominal = 1e5) (156) [ALGB] (1) protected Real duc.vol_b.dynBal.medium.u (min = -1e8, max = 1e8, nominal = 1e6) (157) [DER-] (1) Real $DER.pip.timDel.x (158) [ALGB] (1) protected Real[1] duc.vol_a.dynBal.XiOut (min = {0.0 for $i1 in 1:1}, max = {1.0 for $i1 in 1:1}) (159) [ALGB] (1) protected stream Real[1] duc.heaLos_b.port_b.C_outflow (start = {1.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}) (160) [ALGB] (1) protected Real duc.heaLos_b.T_a_inflow (start = duc.heaLos_b.T_start, min = 0.0, nominal = 300.0) (161) [ALGB] (2) protected stream Real[2, 1] duc.vol_b.ports.Xi_outflow (min = {{0.0 for $i1 in 1:1} for $ports1 in 1:2}, max = {{1.0 for $i1 in 1:1} for $ports1 in 1:2}, nominal = {{0.1 for $i1 in 1:1} for $ports1 in 1:2}) (162) [ALGB] (1) protected flow Real duc.heaLos_a.heatPort.Q_flow (163) [ALGB] (1) protected Real[1] duc.vol_a.mXi (164) [DER-] (1) Real $DER.pip.vol_a.dynBal.m (165) [ALGB] (1) protected Real[1] duc.vol_b.dynBal.mbXi_flow (166) [ALGB] (1) Real $FUN_47 (167) [ALGB] (1) Real $FUN_46 (168) [ALGB] (1) Real $FUN_45 (169) [ALGB] (1) Real senTemIn1.port_a.p (start = 101325.0, min = 0.0, max = 1e8, nominal = 1e5) (170) [ALGB] (1) Real $FUN_44 (171) [ALGB] (1) Real $FUN_43 (172) [ALGB] (1) stream Real[1, 1] sin1.ports.C_outflow (start = {{1.0 for $i1 in 1:1}}, min = {{0.0 for $i1 in 1:1}}) (173) [ALGB] (1) Real $FUN_42 (174) [ALGB] (1) Real $FUN_41 (175) [ALGB] (2) protected flow Real[2] duc.vol_a.ports.m_flow (min = {-1e5 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}) (176) [ALGB] (1) Real $FUN_40 (177) [ALGB] (2) protected flow Real[2] pip.vol_b.ports.m_flow (min = {-1e5 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}) (178) [ALGB] (2) protected stream Real[2] duc.vol_a.dynBal.ports.h_outflow (min = {-1e10 for $i1 in 1:2}, max = {1e10 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2}) (179) [ALGB] (1) stream Real[1] duc.res.port_a.Xi_outflow (min = {0.0 for $i1 in 1:1}, max = {1.0 for $i1 in 1:1}, nominal = {0.1 for $i1 in 1:1}) (180) [ALGB] (1) stream Real[1] duc.res.port_b.C_outflow (start = {1.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}) (181) [DER-] (1) Real $DER.duc.timDel.x (182) [ALGB] (1) protected Real duc.vol_b.dynBal.medium.MM (min = 0.001, max = 0.25, nominal = 0.032) (183) [ALGB] (1) Real[1] sou1.C_in (184) [ALGB] (1) stream Real[1] sou.ports.h_outflow (min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1}) (185) [ALGB] (1) protected Real senTemIn1.T_b_inflow (start = 293.15, min = 1.0, max = 1e4, nominal = 300.0) (186) [ALGB] (2) protected Real[2] duc.vol_a.dynBal.ports_H_flow (min = {-1e8 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1000.0 for $i1 in 1:2}) (187) [ALGB] (2) protected Real[2] duc.vol_b.dynBal.medium.X (start = duc.vol_b.dynBal.X_start, min = {0.0 for $i1 in 1:2}, max = {1.0 for $i1 in 1:2}, nominal = {0.1 for $i1 in 1:2}) (188) [DER-] (1) Real $DER.pip.vol_a.dynBal.U (189) [ALGB] (1) stream Real[1] sou1.ports.h_outflow (min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1}) (190) [ALGB] (1) protected Real[1] duc.vol_b.Xi = duc.vol_b.XiOut_internal (min = {0.0 for $i1 in 1:1}, max = {1.0 for $i1 in 1:1}) (191) [ALGB] (1) protected flow Real duc.heaLos_b.heatPort.Q_flow (192) [ALGB] (1) Real $FUN_37 (193) [ALGB] (1) Real $FUN_36 (194) [ALGB] (1) Real[1] CIn.y (195) [ALGB] (1) Real $FUN_35 (196) [ALGB] (1) Real $FUN_34 (197) [ALGB] (1) Real $FUN_33 (198) [ALGB] (1) Real $FUN_32 (199) [ALGB] (1) final Real duc.res.m_flow = duc.res.m_flow (start = duc.res._m_flow_start, nominal = 1.0) (200) [ALGB] (1) Real $FUN_31 (201) [ALGB] (1) protected Real[1] duc.vol_a.dynBal.mCOut (min = {0.0 for $i1 in 1:1}) (202) [ALGB] (1) Real $FUN_30 (203) [ALGB] (1) protected Real[1] duc.vol_a.Xi = duc.vol_a.XiOut_internal (min = {0.0 for $i1 in 1:1}, max = {1.0 for $i1 in 1:1}) (204) [ALGB] (1) protected Real duc.timDel.time_out_rev (205) [ALGB] (1) Real pip.dp = senTemIn.port_a.p - senTemOutW.port_b.p (start = pip._dp_start) (206) [ALGB] (1) protected stream Real duc.heaLos_b.port_a.h_outflow (start = 45300.945, min = -1e10, max = 1e10, nominal = 45300.945) (207) [ALGB] (2) protected Real[2] pip.vol_b.dynBal.ports.p (start = {3e5 for $ports1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e5 for $i1 in 1:2}) (208) [ALGB] (2) protected Real[2] duc.vol_b.ports.p (start = {101325.0 for $ports1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e5 for $i1 in 1:2}) (209) [ALGB] (1) protected Real duc.heaLos_a.T_a_inflow (start = duc.heaLos_a.T_start, min = 0.0, nominal = 300.0) (210) [ALGB] (2) protected Real[2] duc.vol_a.ports.p (start = {101325.0 for $ports1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e5 for $i1 in 1:2}) (211) [DISC] (1) Boolean $SEV_40 (212) [ALGB] (1) protected Real[1] duc.vol_b.dynBal.mbC_flow (213) [ALGB] (1) Real senTemOutW.port_b.p (start = 3e5, min = 0.0, max = 1e8, nominal = 1e5) (214) [ALGB] (1) protected Real pip.timDel.time_out_des (215) [ALGB] (1) Real $FUN_9 (216) [ALGB] (1) Real $FUN_27 (217) [ALGB] (1) Real $FUN_26 (218) [ALGB] (1) Real $FUN_6 (219) [ALGB] (1) Real $FUN_25 (220) [ALGB] (1) Real $FUN_5 (221) [ALGB] (1) Real $FUN_24 (222) [ALGB] (1) Real $FUN_4 (223) [ALGB] (1) Real[1] $FUN_23 (224) [ALGB] (1) protected Real senTemOutW.T_b_inflow (start = 293.15, min = 1.0, max = 1e4, nominal = 300.0) (225) [ALGB] (1) stream Real[1] senTemIn1.port_a.C_outflow (start = {1.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}) (226) [ALGB] (1) Real $FUN_3 (227) [ALGB] (1) Real[1] $FUN_22 (228) [ALGB] (1) stream Real[1] duc.res.port_b.Xi_outflow (min = {0.0 for $i1 in 1:1}, max = {1.0 for $i1 in 1:1}, nominal = {0.1 for $i1 in 1:1}) (229) [ALGB] (1) Real[1] $FUN_21 (230) [ALGB] (1) Real[1] $FUN_20 (231) [ALGB] (1) protected stream Real duc.del.port_b.h_outflow (start = 45300.945, min = -1e10, max = 1e10, nominal = 45300.945) (232) [ALGB] (1) protected stream Real pip.heaLos_b.port_a.h_outflow (start = 83680.0, min = -1e10, max = 1e10, nominal = 83680.0) (233) [ALGB] (1) Real senTemOutA.port_b.p (start = 101325.0, min = 0.0, max = 1e8, nominal = 1e5) (234) [ALGB] (1) protected stream Real[1] duc.del.port_b.Xi_outflow (min = {0.0 for $i1 in 1:1}, max = {1.0 for $i1 in 1:1}, nominal = {0.1 for $i1 in 1:1}) (235) [DER-] (1) Real $DER.pip.del.x (236) [DISC] (1) Boolean $SEV_38 (237) [DISC] (1) Boolean $SEV_37 (238) [ALGB] (1) Real duc.v = duc.v (239) [ALGB] (1) protected Real pip.timDel.u (240) [ALGB] (1) protected Real senTemIn1.T_a_inflow (start = 293.15, min = 1.0, max = 1e4, nominal = 300.0) (241) [DISC] (1) Boolean $SEV_36 (242) [DISC] (1) Boolean $SEV_35 (243) [DISC] (1) Boolean $SEV_34 (244) [DISC] (1) Boolean $SEV_33 (245) [ALGB] (1) protected flow Real pip.heaLos_a.heatPort.Q_flow (246) [DER-] (1) Real $DER.duc.del.x (247) [ALGB] (1) protected Real duc.vol_a.dynBal.medium.R_s (start = 1000.0, min = 0.0, max = 1e7, nominal = 1000.0) (248) [ALGB] (1) protected Real duc.vol_a.dynBal.medium.T_degC = Modelica.Units.Conversions.to_degC(-((-273.15) - duc.vol_a.dynBal.medium.T_degC)) (249) [ALGB] (1) protected Real duc.vol_b.dynBal.medium.state.T (start = 293.15, min = 1.0, max = 1e4, nominal = 300.0) (250) [ALGB] (1) protected Real[1] sou1.Xi_in_internal (251) [ALGB] (2) protected Real[2] duc.vol_b.dynBal.medium.state.X (start = {0.01, 0.99}, min = {0.0 for $i1 in 1:2}, max = {1.0 for $i1 in 1:2}, nominal = {0.1 for $i1 in 1:2}) (252) [ALGB] (1) Real $FUN_14 (253) [ALGB] (1) Real $FUN_13 (254) [ALGB] (1) Real $FUN_10 (255) [ALGB] (1) flow Real[1] sou1.ports.m_flow (min = {-1e60}, max = {1e60}) (256) [ALGB] (1) protected Real[1] sin1.Xi_in_internal (257) [ALGB] (1) protected Real[1] duc.vol_a.dynBal.C (start = {1.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, nominal = duc.vol_a.dynBal.C_nominal) (258) [DISC] (1) Boolean $SEV_26 (259) [ALGB] (1) protected Real pip.vol_a.dynBal.mb_flow (260) [DISC] (1) Boolean $SEV_25 (261) [ALGB] (1) protected stream Real[1] duc.senMasFlo.port_b.Xi_outflow (min = {0.0 for $i1 in 1:1}, max = {1.0 for $i1 in 1:1}, nominal = {0.1 for $i1 in 1:1}) (262) [DISC] (1) Boolean $SEV_24 (263) [DISC] (1) Boolean $SEV_23 (264) [DISC] (1) Boolean $SEV_22 (265) [ALGB] (1) stream Real[1] duc.port_b.C_outflow (start = {1.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}) (266) [DISC] (1) Boolean $SEV_21 (267) [ALGB] (1) stream Real[1] senTemOutA.port_b.C_outflow (start = {1.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}) (268) [DISC] (1) Boolean $SEV_20 (269) [ALGB] (1) protected stream Real[1] duc.heaLos_a.port_a.C_outflow (start = {1.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}) (270) [ALGB] (1) protected Real[1] duc.vol_b.mXi (271) [ALGB] (1) protected Real duc.vol_b.dynBal.medium.state.p (start = 101325.0, min = 0.0, max = 1e8, nominal = 1e5) (272) [ALGB] (1) protected Real sou.p_in_internal (273) [ALGB] (1) stream Real pip.res.port_a.h_outflow (start = 83680.0, min = -1e10, max = 1e10, nominal = 83680.0) (274) [ALGB] (1) protected Real[1] duc.vol_a.COut_internal (275) [ALGB] (1) final Real pip.res.v = pip.res.m_flow / (pip.res.ARound * pip.res.rho_default) (276) [ALGB] (1) stream Real pip.port_a.h_outflow (start = 83680.0, min = -1e10, max = 1e10, nominal = 83680.0) (277) [ALGB] (2) protected stream Real[2] pip.vol_b.dynBal.ports.h_outflow (min = {-1e10 for $i1 in 1:2}, max = {1e10 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2}) (278) [ALGB] (1) protected Real pip.heaLos_a.TAmb = pip.heaLos_a.TAmb (start = 288.15, min = 0.0, nominal = 300.0) (279) [ALGB] (1) protected stream Real[1] duc.del.port_a.Xi_outflow (min = {0.0 for $i1 in 1:1}, max = {1.0 for $i1 in 1:1}, nominal = {0.1 for $i1 in 1:1}) (280) [ALGB] (1) protected stream Real[1] duc.senMasFlo.port_b.C_outflow (start = {1.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}) (281) [ALGB] (1) protected Real duc.vol_b.dynBal.mb_flow (282) [ALGB] (1) protected Real[1] duc.vol_b.dynBal.mXiOut (min = {0.0 for $i1 in 1:1}) (283) [ALGB] (1) protected Real pip.vol_a.dynBal.medium.state.T (start = 293.15, min = 1.0, max = 1e4, nominal = 300.0) (284) [ALGB] (1) final Real duc.res.v = duc.res.m_flow / (duc.res.ARound * duc.res.rho_default) (285) [ALGB] (1) protected Real[1] duc.vol_b.dynBal.medium.Xi (start = duc.vol_b.dynBal.X_start[1:1], min = {0.0 for $i1 in 1:1}, max = {1.0 for $i1 in 1:1}, StateSelect = default) (286) [DISC] (1) Boolean $SEV_16 (287) [ALGB] (1) protected Real pip.heaLos_b.port_a.p (start = 3e5, min = 0.0, max = 1e8, nominal = 1e5) (288) [DISC] (1) Boolean $SEV_12 (289) [DISC] (1) Boolean $SEV_11 (290) [DISC] (1) Boolean $SEV_10 (291) [ALGB] (1) protected Real duc.heaLos_a.port_b.p (start = 101325.0, min = 0.0, max = 1e8, nominal = 1e5) (292) [ALGB] (1) protected Real duc.vol_a.dynBal.medium.state.p (start = 101325.0, min = 0.0, max = 1e8, nominal = 1e5) (293) [ALGB] (1) protected Real pip.timDel.tauRev (294) [ALGB] (1) protected Real[1] duc.vol_b.mC (295) [DER-] (1) Real $DER.pip.vol_b.dynBal.m (296) [ALGB] (2) protected stream Real[2, 1] duc.vol_b.dynBal.ports.Xi_outflow (min = {{0.0 for $i1 in 1:1} for $ports1 in 1:2}, max = {{1.0 for $i1 in 1:1} for $ports1 in 1:2}, nominal = {{0.1 for $i1 in 1:1} for $ports1 in 1:2}) (297) [ALGB] (2) protected stream Real[2] duc.vol_a.ports.h_outflow (min = {-1e10 for $i1 in 1:2}, max = {1e10 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2}) (298) [ALGB] (1) protected Real pip.vol_a.dynBal.medium.state.p (start = 3e5, min = 0.0, max = 1e8, nominal = 1e5) (299) [ALGB] (1) protected Real[1] duc.vol_b.COut_internal (300) [ALGB] (1) stream Real senTemOutA.port_a.h_outflow (start = 45300.945, min = -1e10, max = 1e10, nominal = 45300.945) (301) [ALGB] (1) protected Real[1] duc.vol_a.mC (302) [ALGB] (1) protected stream Real[1] duc.senMasFlo.port_a.Xi_outflow (min = {0.0 for $i1 in 1:1}, max = {1.0 for $i1 in 1:1}, nominal = {0.1 for $i1 in 1:1}) (303) [ALGB] (1) protected Real sin1.h_internal = IDEAS.Fluid.FixedResistances.Validation.PlugFlowPipes.TransportWaterAir.sin1.Medium.specificEnthalpy(IDEAS.Fluid.FixedResistances.Validation.PlugFlowPipes.TransportWaterAir.sin1.Medium.setState_pTX(sin1.p, sin1.T, sin1.X_in_internal)) (304) [ALGB] (1) protected Real pip.heaLos_b.T_a_inflow (start = pip.heaLos_b.T_start, min = 0.0, nominal = 300.0) (305) [ALGB] (1) Real[1] sin.ports.p (start = {3e5}, min = {0.0 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e5 for $i1 in 1:1}) (306) [ALGB] (1) protected stream Real pip.heaLos_a.port_a.h_outflow (start = 83680.0, min = -1e10, max = 1e10, nominal = 83680.0) (307) [ALGB] (1) protected Real duc.timDel.time_out_des (308) [ALGB] (2) protected Real[2] duc.vol_a.dynBal.medium.state.X (start = {0.01, 0.99}, min = {0.0 for $i1 in 1:2}, max = {1.0 for $i1 in 1:2}, nominal = {0.1 for $i1 in 1:2}) (309) [DER-] (1) Real $DER.pip.vol_b.dynBal.U (310) [ALGB] (1) protected stream Real duc.senMasFlo.port_a.h_outflow (start = 45300.945, min = -1e10, max = 1e10, nominal = 45300.945) (311) [ALGB] (1) stream Real[1] sin1.ports.h_outflow (min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1}) (312) [ALGB] (1) protected Real duc.vol_a.dynBal.medium.state.T (start = 293.15, min = 1.0, max = 1e4, nominal = 300.0) (313) [ALGB] (2) protected stream Real[2, 1] duc.vol_a.dynBal.ports.C_outflow (start = {{1.0 for $i1 in 1:1} for $ports1 in 1:2}, min = {{0.0 for $i1 in 1:1} for $ports1 in 1:2}) (314) [ALGB] (2) protected stream Real[2] duc.vol_b.dynBal.ports.h_outflow (min = {-1e10 for $i1 in 1:2}, max = {1e10 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2}) (315) [ALGB] (1) protected Real pip.vol_b.dynBal.Hb_flow (316) [ALGB] (1) protected stream Real[1] duc.heaLos_b.port_a.Xi_outflow (min = {0.0 for $i1 in 1:1}, max = {1.0 for $i1 in 1:1}, nominal = {0.1 for $i1 in 1:1}) (317) [ALGB] (1) Real[1] sou.ports.p (start = {3e5}, min = {0.0 for $i1 in 1:1}, max = {1e8 for $i1 in 1:1}, nominal = {1e5 for $i1 in 1:1}) (318) [ALGB] (1) stream Real[1] duc.port_a.Xi_outflow (min = {0.0 for $i1 in 1:1}, max = {1.0 for $i1 in 1:1}, nominal = {0.1 for $i1 in 1:1}) (319) [ALGB] (1) protected Real sou.h_internal = IDEAS.Fluid.FixedResistances.Validation.PlugFlowPipes.TransportWaterAir.sou.Medium.specificEnthalpy(IDEAS.Fluid.FixedResistances.Validation.PlugFlowPipes.TransportWaterAir.sou.Medium.setState_pTX(sou.p_in_internal, -2.390057361376673e-4 * ((-1.1428595999999999e6) - sou.h_internal), sou.X_in_internal)) (320) [ALGB] (1) protected Real pip.heaLos_b.port_b.p (start = 3e5, min = 0.0, max = 1e8, nominal = 1e5) (321) [ALGB] (1) stream Real[1] sin.ports.h_outflow (min = {-1e10 for $i1 in 1:1}, max = {1e10 for $i1 in 1:1}, nominal = {1e6 for $i1 in 1:1}) (322) [ALGB] (1) protected Real pip.timDel.time_out_rev (323) [ALGB] (2) protected Real[2] pip.vol_a.dynBal.ports_H_flow (min = {-1e8 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1000.0 for $i1 in 1:2}) (324) [ALGB] (1) protected Real[1] duc.vol_b.dynBal.XiOut (min = {0.0 for $i1 in 1:1}, max = {1.0 for $i1 in 1:1}) (325) [DISC] (2) Boolean[2] $SEV_6[$i1] (326) [ALGB] (1) protected Real[1] duc.vol_a.C = duc.vol_a.COut_internal (start = {1.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, nominal = duc.vol_a.C_nominal) (327) [ALGB] (1) protected Real pip.vol_b.dynBal.medium.state.p (start = 3e5, min = 0.0, max = 1e8, nominal = 1e5) System Equations (343/376) **************************** (1) [ARRY] (1) duc.del.Xi_inflow_b = {duc.heaLos_b.port_a.Xi_outflow[1]} ($RES_BND_554) (2) [TUPL] (2) (duc.senMasFlo.port_a.h_outflow, duc.del.port_b.h_outflow) = spatialDistribution(duc.heaLos_a.port_a.h_outflow, duc.heaLos_b.port_a.h_outflow, duc.del.x / duc.del.length, $SEV_38, {0.0, 1.0}, {duc.del.h_ini_in, duc.del.h_ini_out}) ($RES_$AUX_606) (3) [SCAL] (1) $SEV_33 = duc.res.m_flow > duc.del.m_flow_small ($RES_EVT_725) (4) [ARRY] (1) duc.del.C_inflow_a = {duc.res.port_b.C_outflow[1]} ($RES_BND_555) (5) [SCAL] (1) senTemOutW.T = smooth(1, if $SEV_24 then 273.15 + 2.390057361376673e-4 * pip.port_b.h_outflow else if $SEV_25 then senTemOutW.T_b_inflow else if $SEV_26 then 0.5 * ((273.15 + 2.390057361376673e-4 * pip.port_b.h_outflow) + senTemOutW.T_b_inflow) - 0.25 * (senTemOutW.T_b_inflow - (273.15 + 2.390057361376673e-4 * pip.port_b.h_outflow)) * ((-3.0) + (senTemOutW.port_b.m_flow / (-senTemOutW.m_flow_small)) ^ 2.0) * (senTemOutW.port_b.m_flow / senTemOutW.m_flow_small) else 0.5 * ((273.15 + 2.390057361376673e-4 * pip.port_b.h_outflow) + senTemOutW.T_b_inflow)) ($RES_SIM_255) (6) [SCAL] (1) $SEV_34 = duc.res.m_flow < (-duc.del.m_flow_small) ($RES_EVT_726) (7) [ARRY] (1) duc.del.C_inflow_b = {duc.heaLos_b.port_a.C_outflow[1]} ($RES_BND_556) (8) [FOR-] (2) ($RES_$AUX_604) (8) [----] for $i1 in 1:1 loop (8) [----] [TUPL] (2) ($FUN_20[$i1], $FUN_21[$i1]) = spatialDistribution(duc.del.Xi_inflow_a[$i1], duc.del.Xi_inflow_b[$i1], duc.del.x / duc.del.length, $SEV_39[$i1], {0.0, 1.0}, {0.01, 0.01}) ($RES_$AUX_605) (8) [----] end for; (9) [SCAL] (1) $SEV_35 = duc.del.m_flow_small > 0.0 ($RES_EVT_727) (10) [SCAL] (1) $SEV_36 = pip.v >= 0.0 ($RES_EVT_728) (11) [FOR-] (2) ($RES_$AUX_602) (11) [----] for $i1 in 1:1 loop (11) [----] [TUPL] (2) ($FUN_22[$i1], $FUN_23[$i1]) = spatialDistribution(duc.del.C_inflow_a[$i1], duc.del.C_inflow_b[$i1], duc.del.x / duc.del.length, $SEV_39[$i1], {0.0, 1.0}, {0.0, 0.0}) ($RES_$AUX_603) (11) [----] end for; (12) [SCAL] (1) $SEV_37 = pip.timDel.u >= 0.0 ($RES_EVT_729) (13) [FOR-] (2) ($RES_SIM_510) (13) [----] for $i1 in 1:2 loop (13) [----] [SCAL] (1) pip.vol_b.dynBal.ports[$i1].m_flow - pip.vol_b.ports[$i1].m_flow = 0.0 ($RES_SIM_511) (13) [----] end for; (14) [SCAL] (1) duc.vol_b.T = 273.15 + (-(2.5010145e6 * duc.vol_b.Xi[1] + ((-84437.5) - duc.vol_b.dynBal.medium.u))) / (1006.0 * (1.0 - duc.vol_b.Xi[1]) + 1860.0 * duc.vol_b.Xi[1]) ($RES_BND_559) (15) [SCAL] (1) sou.ports[1].h_outflow = sou.h_internal ($RES_SIM_259) (16) [SCAL] (1) $FUN_24 = exp(-duc.timDel.tauRev / duc.heaLos_a.tau_char) ($RES_$AUX_601) (17) [SCAL] (1) $FUN_25 = IDEAS.Utilities.Math.Functions.spliceFunction((duc.heaLos_a.T_a_inflow - duc.heaLos_a.T_b_outflow) * duc.heaLos_a.cp_default, 0.0, -duc.res.m_flow, 0.001) ($RES_$AUX_600) (18) [ARRY] (2) pip.vol_b.dynBal.ports.p = pip.vol_b.ports.p ($RES_SIM_512) (19) [SCAL] (1) -2.390057361376673e-4 * ((-1.1428595999999999e6) - pip.heaLos_a.port_b.h_outflow) = pip.heaLos_a.TAmb + ((273.15 + 2.390057361376673e-4 * pip.res.port_a.h_outflow) - pip.heaLos_a.TAmb) * $FUN_3 ($RES_SIM_340) (20) [SCAL] (1) pip.heaLos_a.port_a.h_outflow = pip.vol_a.ports[2].h_outflow ($RES_SIM_343) (21) [SCAL] (1) pip.v = (0.0010044335697769957 * pip.res.m_flow) / pip.del.A ($RES_SIM_346) (22) [SCAL] (1) duc.vol_b.dynBal.medium.MM = 1/(55.508435061791985 * duc.vol_b.dynBal.medium.X[1] + 34.52428788658843 * duc.vol_b.dynBal.medium.X[2]) ($RES_SIM_171) (23) [SCAL] (1) $DER.pip.del.x = pip.v ($RES_SIM_347) (24) [SCAL] (1) duc.timDel.tauRev = max(0.0, time - duc.timDel.time_out_rev) ($RES_SIM_172) (25) [SCAL] (1) duc.timDel.tau = max(0.0, time - duc.timDel.time_out_des) ($RES_SIM_173) (26) [SCAL] (1) $DER.duc.timDel.x = duc.timDel.u ($RES_SIM_175) (27) [SCAL] (1) duc.timDel.u = duc.res.m_flow * duc.timDel.conUM ($RES_SIM_176) (28) [ARRY] (1) duc.senMasFlo.port_b.C_outflow = {duc.heaLos_a.port_a.C_outflow[1]} ($RES_SIM_177) (29) [ARRY] (1) duc.senMasFlo.port_a.C_outflow = {duc.res.port_a.C_outflow[1]} ($RES_SIM_178) (30) [ARRY] (1) duc.senMasFlo.port_b.Xi_outflow = {duc.heaLos_a.port_a.Xi_outflow[1]} ($RES_SIM_179) (31) [SCAL] (1) $SEV_38 = duc.v >= 0.0 ($RES_EVT_730) (32) [SCAL] (1) duc.vol_b.p = duc.vol_b.ports[1].p ($RES_BND_560) (33) [SCAL] (1) $SEV_39[1] = duc.v >= 0.0 ($RES_EVT_731) (34) [ARRY] (1) duc.vol_a.COut_internal = duc.vol_a.dynBal.COut ($RES_SIM_436) (35) [ARRY] (1) duc.vol_b.Xi = duc.vol_b.XiOut_internal ($RES_BND_561) (36) [SCAL] (1) sou.ports[1].p = sou.p_in_internal ($RES_SIM_261) (37) [SCAL] (1) $SEV_40 = duc.timDel.u >= 0.0 ($RES_EVT_732) (38) [ARRY] (1) duc.vol_a.XiOut_internal = duc.vol_a.dynBal.XiOut ($RES_SIM_437) (39) [ARRY] (1) duc.vol_b.C = duc.vol_b.COut_internal ($RES_BND_562) (40) [ARRY] (1) duc.vol_a.mC = duc.vol_a.dynBal.mCOut ($RES_SIM_439) (41) [SCAL] (1) duc.vol_a.T = 273.15 + (-(2.5010145e6 * duc.vol_a.Xi[1] + ((-84437.5) - duc.vol_a.dynBal.medium.u))) / (1006.0 * (1.0 - duc.vol_a.Xi[1]) + 1860.0 * duc.vol_a.Xi[1]) ($RES_BND_566) (42) [SCAL] (1) duc.vol_a.p = duc.vol_a.ports[1].p ($RES_BND_567) (43) [ARRY] (1) duc.vol_a.Xi = duc.vol_a.XiOut_internal ($RES_BND_568) (44) [ARRY] (1) duc.vol_a.C = duc.vol_a.COut_internal ($RES_BND_569) (45) [FOR-] (2) ($RES_SIM_269) (45) [----] for $i1 in 1:2 loop (45) [----] [SCAL] (1) pip.vol_a.dynBal.ports[$i1].p = 99999.99999999999 * pip.vol_a.dynBal.medium.p_bar ($RES_SIM_270) (45) [----] end for; (46) [SCAL] (1) pip.res.dp = homotopy(IDEAS.Fluid.BaseClasses.FlowModels.basicFlowFunction_m_flow(pip.res.m_flow, pip.res.k, pip.res.m_flow_turbulent), pip.res.dp_nominal_pos * pip.res.m_flow) ($RES_SIM_353) (47) [SCAL] (1) sin.ports[1].h_outflow = 4184.0 * ((-273.15) + sin.T) ($RES_SIM_355) (48) [ARRY] (1) duc.senMasFlo.port_a.Xi_outflow = {duc.res.port_a.Xi_outflow[1]} ($RES_SIM_180) (49) [SCAL] (1) sin.ports[1].p = sin.p ($RES_SIM_357) (50) [SCAL] (1) -2.390057361376673e-4 * ((-1.1428595999999999e6) - sou.h_internal) = Tin.offset + (if $TEV_1 then 0.0 else Tin.height) ($RES_SIM_359) (51) [ARRY] (1) duc.heaLos_b.port_b.C_outflow = {duc.del.port_b.C_outflow[1]} ($RES_SIM_186) (52) [ARRY] (1) duc.heaLos_b.port_a.C_outflow = {duc.vol_b.ports[1].C_outflow[1]} ($RES_SIM_187) (53) [ARRY] (1) duc.heaLos_b.port_b.Xi_outflow = {duc.del.port_b.Xi_outflow[1]} ($RES_SIM_188) (54) [ARRY] (1) duc.heaLos_b.port_a.Xi_outflow = {duc.vol_b.ports[1].Xi_outflow[1]} ($RES_SIM_189) (55) [ARRY] (1) duc.vol_a.mXi = duc.vol_a.dynBal.mXiOut ($RES_SIM_441) (56) [SCAL] (1) duc.vol_a.dynBal.ports[2].h_outflow = duc.vol_a.ports[2].h_outflow ($RES_SIM_443) (57) [SCAL] (1) duc.vol_a.dynBal.ports[1].h_outflow = duc.vol_a.ports[1].h_outflow ($RES_SIM_444) (58) [SCAL] (1) duc.vol_a.dynBal.ports[2].Xi_outflow[1] = duc.vol_a.ports[2].Xi_outflow[1] ($RES_SIM_445) (59) [SCAL] (1) duc.vol_a.dynBal.ports[1].Xi_outflow[1] = duc.vol_a.ports[1].Xi_outflow[1] ($RES_SIM_446) (60) [FOR-] (2) ($RES_SIM_271) (60) [----] for $i1 in 1:2 loop (60) [----] [SCAL] (1) pip.vol_a.dynBal.ports[$i1].h_outflow = 4184.0 * ((-273.15) - ((-273.15) - pip.vol_a.dynBal.medium.T_degC)) ($RES_SIM_272) (60) [----] end for; (61) [SCAL] (1) duc.vol_a.dynBal.ports[2].C_outflow[1] = duc.vol_a.ports[2].C_outflow[1] ($RES_SIM_447) (62) [SCAL] (1) sou1.h_internal = 1006.0 * ((-273.15) - 2.390057361376673e-4 * ((-1.1428595999999999e6) - sou.h_internal)) * (1.0 - sou1.X_in_internal[1]) + (2.5010145e6 + 1860.0 * ((-273.15) - 2.390057361376673e-4 * ((-1.1428595999999999e6) - sou.h_internal))) * sou1.X_in_internal[1] ($RES_BND_573) (63) [SCAL] (1) $DER.pip.vol_a.dynBal.m = pip.vol_a.dynBal.mb_flow ($RES_SIM_273) (64) [SCAL] (1) duc.vol_a.dynBal.ports[1].C_outflow[1] = duc.vol_a.ports[1].C_outflow[1] ($RES_SIM_448) (65) [SCAL] (1) $DER.pip.vol_a.dynBal.U = pip.vol_a.dynBal.Hb_flow ($RES_SIM_274) (66) [FOR-] (2) ($RES_SIM_449) (66) [----] for $i1 in 1:2 loop (66) [----] [SCAL] (1) duc.vol_a.dynBal.ports[$i1].m_flow - duc.vol_a.ports[$i1].m_flow = 0.0 ($RES_SIM_450) (66) [----] end for; (67) [SCAL] (1) pip.vol_a.dynBal.ports_H_flow[2] = $FUN_14 ($RES_SIM_277) (68) [SCAL] (1) pip.vol_a.dynBal.ports_H_flow[1] = $FUN_13 ($RES_SIM_278) (69) [SCAL] (1) senTemOutA.port_b.m_flow + sin1.ports[1].m_flow = 0.0 ($RES_SIM_361) (70) [SCAL] (1) duc.vol_a.ports[2].m_flow + duc.res.m_flow = 0.0 ($RES_SIM_365) (71) [SCAL] (1) 0.0 = duc.heaLos_b.port_a.p - duc.heaLos_b.port_b.p ($RES_SIM_192) (72) [SCAL] (1) duc.heaLos_b.heatPort.Q_flow = -$FUN_27 * duc.res.m_flow ($RES_SIM_193) (73) [SCAL] (1) duc.heaLos_b.T_b_outflow = duc.heaLos_a.TAmb + (duc.heaLos_b.T_a_inflow - duc.heaLos_a.TAmb) * $FUN_26 ($RES_SIM_194) (74) [SCAL] (1) duc.vol_b.ports[2].m_flow - senTemOutA.port_b.m_flow = 0.0 ($RES_SIM_369) (75) [SCAL] (1) duc.heaLos_b.T_a_inflow = 273.15 + (duc.del.port_b.h_outflow - 2.5010145e6 * duc.heaLos_b.port_b.Xi_outflow[1]) / (1006.0 * (1.0 - duc.heaLos_b.port_b.Xi_outflow[1]) + 1860.0 * duc.heaLos_b.port_b.Xi_outflow[1]) ($RES_SIM_195) (76) [SCAL] (1) duc.heaLos_b.port_b.h_outflow = 1006.0 * ((-273.15) + duc.heaLos_b.T_b_outflow) * (1.0 - duc.heaLos_b.port_b.Xi_outflow[1]) + (2.5010145e6 + 1860.0 * ((-273.15) + duc.heaLos_b.T_b_outflow)) * duc.heaLos_b.port_b.Xi_outflow[1] ($RES_SIM_196) (77) [SCAL] (1) duc.heaLos_b.port_a.h_outflow = duc.vol_b.ports[1].h_outflow ($RES_SIM_197) (78) [ARRY] (1) duc.heaLos_a.port_b.C_outflow = {duc.senMasFlo.port_a.C_outflow[1]} ($RES_SIM_199) (79) [ARRY] (2) duc.vol_a.dynBal.ports.p = duc.vol_a.ports.p ($RES_SIM_451) (80) [SCAL] (1) pip.vol_a.dynBal.U = pip.vol_a.dynBal.m * (4184.0 * ((-273.15) - ((-273.15) - pip.vol_a.dynBal.medium.T_degC))) ($RES_SIM_280) (81) [ARRY] (1) duc.vol_b.COut_internal = duc.vol_b.dynBal.COut ($RES_SIM_456) (82) [SCAL] (1) pip.vol_a.dynBal.m = 995.586 * pip.vol_a.dynBal.fluidVolume ($RES_SIM_281) (83) [ARRY] (1) duc.vol_b.XiOut_internal = duc.vol_b.dynBal.XiOut ($RES_SIM_457) (84) [ARRY] (1) duc.vol_b.mC = duc.vol_b.dynBal.mCOut ($RES_SIM_459) (85) [SCAL] (1) pip.vol_a.dynBal.medium.state.p = 99999.99999999999 * pip.vol_a.dynBal.medium.p_bar ($RES_SIM_286) (86) [SCAL] (1) pip.vol_a.dynBal.medium.state.T = -((-273.15) - pip.vol_a.dynBal.medium.T_degC) ($RES_SIM_287) (87) [SCAL] (1) duc.heaLos_a.heatPort.Q_flow + duc.heaLos_b.heatPort.Q_flow = 0.0 ($RES_SIM_371) (88) [SCAL] (1) duc.vol_b.ports[1].m_flow - duc.res.m_flow = 0.0 ($RES_SIM_372) (89) [SCAL] (1) senTemOutW.port_b.m_flow + sin.ports[1].m_flow = 0.0 ($RES_SIM_379) (90) [ARRY] (1) duc.vol_b.mXi = duc.vol_b.dynBal.mXiOut ($RES_SIM_461) (91) [SCAL] (1) duc.vol_b.dynBal.ports[2].h_outflow = duc.vol_b.ports[2].h_outflow ($RES_SIM_463) (92) [SCAL] (1) duc.vol_b.dynBal.ports[1].h_outflow = duc.vol_b.ports[1].h_outflow ($RES_SIM_464) (93) [SCAL] (1) duc.vol_b.dynBal.ports[2].Xi_outflow[1] = duc.vol_b.ports[2].Xi_outflow[1] ($RES_SIM_465) (94) [SCAL] (1) duc.vol_b.dynBal.ports[1].Xi_outflow[1] = duc.vol_b.ports[1].Xi_outflow[1] ($RES_SIM_466) (95) [SCAL] (1) duc.vol_b.dynBal.ports[2].C_outflow[1] = duc.vol_b.ports[2].C_outflow[1] ($RES_SIM_467) (96) [SCAL] (1) duc.vol_b.dynBal.ports[1].C_outflow[1] = duc.vol_b.ports[1].C_outflow[1] ($RES_SIM_468) (97) [FOR-] (2) ($RES_SIM_469) (97) [----] for $i1 in 1:2 loop (97) [----] [SCAL] (1) duc.vol_b.dynBal.ports[$i1].m_flow - duc.vol_b.ports[$i1].m_flow = 0.0 ($RES_SIM_470) (97) [----] end for; (98) [FOR-] (2) ($RES_SIM_296) (98) [----] for $i1 in 1:2 loop (98) [----] [SCAL] (1) pip.vol_b.dynBal.ports[$i1].p = 99999.99999999999 * pip.vol_b.dynBal.medium.p_bar ($RES_SIM_297) (98) [----] end for; (99) [FOR-] (2) ($RES_SIM_298) (99) [----] for $i1 in 1:2 loop (99) [----] [SCAL] (1) pip.vol_b.dynBal.ports[$i1].h_outflow = 4184.0 * ((-273.15) - ((-273.15) - pip.vol_b.dynBal.medium.T_degC)) ($RES_SIM_299) (99) [----] end for; (100) [SCAL] (1) pip.vol_a.ports[2].m_flow + pip.res.m_flow = 0.0 ($RES_SIM_383) (101) [SCAL] (1) pip.vol_b.ports[2].m_flow - senTemOutW.port_b.m_flow = 0.0 ($RES_SIM_387) (102) [SCAL] (1) pip.heaLos_a.heatPort.Q_flow + pip.heaLos_b.heatPort.Q_flow = 0.0 ($RES_SIM_389) (103) [SCAL] (1) $TEV_0 = time < CIn[1].startTime ($RES_EVT_689) (104) [ARRY] (2) duc.vol_b.dynBal.ports.p = duc.vol_b.ports.p ($RES_SIM_471) (105) [SCAL] (1) pip.vol_a.ports[2].p = pip.heaLos_a.port_b.p ($RES_SIM_474) (106) [SCAL] (1) pip.vol_a.ports[1].h_outflow = pip.port_a.h_outflow ($RES_SIM_475) (107) [SCAL] (1) pip.vol_a.ports[1].m_flow - pip.m_flow = 0.0 ($RES_SIM_476) (108) [SCAL] (1) senTemIn.port_a.p = pip.vol_a.ports[1].p ($RES_SIM_477) (109) [SCAL] (1) pip.vol_b.ports[2].h_outflow = pip.port_b.h_outflow ($RES_SIM_478) (110) [SCAL] (1) pip.vol_b.ports[2].p = senTemOutW.port_b.p ($RES_SIM_479) (111) [SCAL] (1) pip.vol_b.ports[1].m_flow - pip.res.m_flow = 0.0 ($RES_SIM_390) (112) [SCAL] (1) $TEV_1 = time < Tin.startTime ($RES_EVT_690) (113) [ARRY] (1) sou1.C_in = CIn.y ($RES_SIM_396) (114) [ARRY] (2) sou1.X_in = XiIn.y ($RES_SIM_397) (115) [SCAL] (1) duc.m_flow + sou1.ports[1].m_flow = 0.0 ($RES_SIM_399) (116) [FOR-] (2) ($RES_EVT_697) (116) [----] for $i1 in 1:2 loop (116) [----] [SCAL] (1) $SEV_6[$i1] = time < XiIn[$i1].startTime ($RES_EVT_698) (116) [----] end for; (117) [SCAL] (1) $SEV_7 = duc.m_flow > senTemIn1.m_flow_small ($RES_EVT_699) (118) [SCAL] (1) pip.heaLos_b.port_b.p = pip.vol_b.ports[1].p ($RES_SIM_480) (119) [SCAL] (1) CIn[1].y = CIn[1].offset + (if $TEV_0 then 0.0 else CIn[1].height) ($RES_SIM_25) (120) [FOR-] (2) ($RES_SIM_26) (120) [----] for $i1 in 1:2 loop (120) [----] [SCAL] (1) XiIn[$i1].y = XiIn[$i1].offset + (if $SEV_6[$i1] then 0.0 else XiIn[$i1].height) ($RES_SIM_27) (120) [----] end for; (121) [ARRY] (1) senTemIn1.port_b.C_outflow = {sou1.ports[1].C_outflow[1]} ($RES_SIM_28) (122) [ARRY] (1) senTemIn1.port_a.C_outflow = {duc.port_a.C_outflow[1]} ($RES_SIM_29) (123) [ARRY] (1) senTemIn1.port_b.Xi_outflow = {sou1.ports[1].Xi_outflow[1]} ($RES_SIM_30) (124) [ARRY] (1) senTemIn1.port_a.Xi_outflow = {duc.port_a.Xi_outflow[1]} ($RES_SIM_31) (125) [SCAL] (1) senTemIn1.port_b.h_outflow = sou1.ports[1].h_outflow ($RES_SIM_32) (126) [SCAL] (1) senTemIn1.T = smooth(1, if $SEV_7 then senTemIn1.T_a_inflow else if $SEV_8 then senTemIn1.T_b_inflow else if $SEV_9 then 0.25 * (senTemIn1.T_b_inflow - senTemIn1.T_a_inflow) * ((-3.0) + (duc.m_flow / senTemIn1.m_flow_small) ^ 2.0) * (duc.m_flow / senTemIn1.m_flow_small) + 0.5 * (senTemIn1.T_a_inflow + senTemIn1.T_b_inflow) else 0.5 * (senTemIn1.T_a_inflow + senTemIn1.T_b_inflow)) ($RES_SIM_39) (127) [SCAL] (1) pip.vol_a.dynBal.ports[2].h_outflow = pip.vol_a.ports[2].h_outflow ($RES_SIM_496) (128) [SCAL] (1) pip.vol_a.dynBal.ports[1].h_outflow = pip.vol_a.ports[1].h_outflow ($RES_SIM_497) (129) [FOR-] (2) ($RES_SIM_498) (129) [----] for $i1 in 1:2 loop (129) [----] [SCAL] (1) pip.vol_a.dynBal.ports[$i1].m_flow - pip.vol_a.ports[$i1].m_flow = 0.0 ($RES_SIM_499) (129) [----] end for; (130) [SCAL] (1) senTemIn1.T_b_inflow = 273.15 + (senTemIn1.port_a.h_outflow - 2.5010145e6 * senTemIn1.port_a.Xi_outflow[1]) / (1006.0 * (1.0 - senTemIn1.port_a.Xi_outflow[1]) + 1860.0 * senTemIn1.port_a.Xi_outflow[1]) ($RES_SIM_40) (131) [SCAL] (1) senTemIn1.T_a_inflow = 273.15 + (senTemIn1.port_b.h_outflow - 2.5010145e6 * senTemIn1.port_b.Xi_outflow[1]) / (1006.0 * (1.0 - senTemIn1.port_b.Xi_outflow[1]) + 1860.0 * senTemIn1.port_b.Xi_outflow[1]) ($RES_SIM_41) (132) [ARRY] (1) senTemOutA.port_b.C_outflow = {duc.port_b.C_outflow[1]} ($RES_SIM_42) (133) [ARRY] (1) senTemOutA.port_a.C_outflow = {sin1.ports[1].C_outflow[1]} ($RES_SIM_43) (134) [ARRY] (1) senTemOutA.port_b.Xi_outflow = {duc.port_b.Xi_outflow[1]} ($RES_SIM_44) (135) [ARRY] (1) senTemOutA.port_a.Xi_outflow = {sin1.ports[1].Xi_outflow[1]} ($RES_SIM_45) (136) [SCAL] (1) senTemOutA.port_a.h_outflow = sin1.ports[1].h_outflow ($RES_SIM_47) (137) [SCAL] (1) $FUN_26 = exp(-duc.timDel.tau / duc.heaLos_b.tau_char) ($RES_$AUX_599) (138) [SCAL] (1) $FUN_27 = IDEAS.Utilities.Math.Functions.spliceFunction((duc.heaLos_b.T_a_inflow - duc.heaLos_b.T_b_outflow) * duc.heaLos_b.cp_default, 0.0, duc.res.m_flow, 0.001) ($RES_$AUX_598) (139) [TUPL] (2) (duc.timDel.time_out_rev, duc.timDel.time_out_des) = spatialDistribution(time, time, duc.timDel.x, $SEV_40, {0.0, 1.0}, {duc.timDel.t0 + duc.timDel.t_in_start, duc.timDel.t0 + duc.timDel.t_out_start}) ($RES_$AUX_597) (140) [SCAL] (1) $FUN_30 = semiLinear(duc.vol_b.dynBal.ports[1].m_flow, duc.heaLos_b.port_b.h_outflow, duc.vol_b.dynBal.ports[1].h_outflow) ($RES_$AUX_596) (141) [SCAL] (1) $FUN_31 = semiLinear(duc.vol_b.dynBal.ports[1].m_flow, duc.heaLos_b.port_b.Xi_outflow[1], duc.vol_b.dynBal.ports[1].Xi_outflow[1]) ($RES_$AUX_595) (142) [SCAL] (1) $FUN_32 = semiLinear(duc.vol_b.dynBal.ports[1].m_flow, duc.heaLos_b.port_b.C_outflow[1], duc.vol_b.dynBal.ports[1].C_outflow[1]) ($RES_$AUX_594) (143) [SCAL] (1) $FUN_33 = semiLinear(duc.vol_b.dynBal.ports[2].m_flow, senTemOutA.port_a.h_outflow, duc.vol_b.dynBal.ports[2].h_outflow) ($RES_$AUX_593) (144) [SCAL] (1) $FUN_34 = semiLinear(duc.vol_b.dynBal.ports[2].m_flow, senTemOutA.port_a.Xi_outflow[1], duc.vol_b.dynBal.ports[2].Xi_outflow[1]) ($RES_$AUX_592) (145) [SCAL] (1) $FUN_35 = semiLinear(duc.vol_b.dynBal.ports[2].m_flow, senTemOutA.port_a.C_outflow[1], duc.vol_b.dynBal.ports[2].C_outflow[1]) ($RES_$AUX_591) (146) [SCAL] (1) $FUN_36 = sum(duc.vol_b.dynBal.ports_mXi_flow[:, 1]) ($RES_$AUX_590) (147) [SCAL] (1) senTemOutA.T = smooth(1, if $SEV_10 then senTemOutA.T_a_inflow else if $SEV_11 then senTemOutA.T_b_inflow else if $SEV_12 then 0.5 * (senTemOutA.T_a_inflow + senTemOutA.T_b_inflow) - 0.25 * (senTemOutA.T_b_inflow - senTemOutA.T_a_inflow) * ((-3.0) + (senTemOutA.port_b.m_flow / (-senTemOutA.m_flow_small)) ^ 2.0) * (senTemOutA.port_b.m_flow / senTemOutA.m_flow_small) else 0.5 * (senTemOutA.T_a_inflow + senTemOutA.T_b_inflow)) ($RES_SIM_53) (148) [SCAL] (1) senTemOutA.T_b_inflow = 273.15 + (senTemOutA.port_a.h_outflow - 2.5010145e6 * senTemOutA.port_a.Xi_outflow[1]) / (1006.0 * (1.0 - senTemOutA.port_a.Xi_outflow[1]) + 1860.0 * senTemOutA.port_a.Xi_outflow[1]) ($RES_SIM_54) (149) [SCAL] (1) senTemOutA.T_a_inflow = 273.15 + (senTemOutA.port_b.h_outflow - 2.5010145e6 * senTemOutA.port_b.Xi_outflow[1]) / (1006.0 * (1.0 - senTemOutA.port_b.Xi_outflow[1]) + 1860.0 * senTemOutA.port_b.Xi_outflow[1]) ($RES_SIM_55) (150) [ARRY] (1) sou1.ports[1].Xi_outflow = sou1.Xi_in_internal ($RES_SIM_56) (151) [ARRY] (1) sou1.ports[1].C_outflow = sou1.C_in_internal ($RES_SIM_57) (152) [ARRY] (1) sou1.X_in_internal[1:1] = sou1.Xi_in_internal[:] ($RES_SIM_58) (153) [SCAL] (1) $FUN_37 = sum(duc.vol_b.dynBal.ports_mC_flow[:, 1]) ($RES_$AUX_589) (154) [SCAL] (1) duc.vol_b.dynBal.mb_flow = sum(duc.vol_b.dynBal.ports.m_flow) ($RES_$AUX_588) (155) [SCAL] (1) duc.vol_b.dynBal.Hb_flow = sum(duc.vol_b.dynBal.ports_H_flow) ($RES_$AUX_587) (156) [SCAL] (1) $FUN_40 = semiLinear(duc.vol_a.dynBal.ports[1].m_flow, senTemIn1.port_b.h_outflow, duc.vol_a.dynBal.ports[1].h_outflow) ($RES_$AUX_586) (157) [SCAL] (1) duc.vol_a.dynBal.m = duc.vol_a.dynBal.fluidVolume * (1.1843079200592153e-5 * (99999.99999999999 * duc.vol_a.dynBal.medium.p_bar)) ($RES_SIM_100) (158) [SCAL] (1) $FUN_41 = semiLinear(duc.vol_a.dynBal.ports[1].m_flow, senTemIn1.port_b.Xi_outflow[1], duc.vol_a.dynBal.ports[1].Xi_outflow[1]) ($RES_$AUX_585) (159) [ARRY] (1) duc.vol_a.dynBal.C_flow_internal = {0.0} ($RES_SIM_101) (160) [SCAL] (1) $FUN_42 = semiLinear(duc.vol_a.dynBal.ports[1].m_flow, senTemIn1.port_b.C_outflow[1], duc.vol_a.dynBal.ports[1].C_outflow[1]) ($RES_$AUX_584) (161) [SCAL] (1) $FUN_43 = semiLinear(duc.vol_a.dynBal.ports[2].m_flow, duc.heaLos_a.port_b.h_outflow, duc.vol_a.dynBal.ports[2].h_outflow) ($RES_$AUX_583) (162) [SCAL] (1) $FUN_44 = semiLinear(duc.vol_a.dynBal.ports[2].m_flow, duc.heaLos_a.port_b.Xi_outflow[1], duc.vol_a.dynBal.ports[2].Xi_outflow[1]) ($RES_$AUX_582) (163) [SCAL] (1) $FUN_45 = semiLinear(duc.vol_a.dynBal.ports[2].m_flow, duc.heaLos_a.port_b.C_outflow[1], duc.vol_a.dynBal.ports[2].C_outflow[1]) ($RES_$AUX_581) (164) [SCAL] (1) $FUN_46 = sum(duc.vol_a.dynBal.ports_mXi_flow[:, 1]) ($RES_$AUX_580) (165) [SCAL] (1) duc.vol_a.dynBal.medium.X[2] = 1.0 - duc.vol_a.dynBal.medium.X[1] ($RES_SIM_107) (166) [SCAL] (1) duc.vol_a.dynBal.medium.X[1] = duc.vol_a.dynBal.medium.Xi[1] ($RES_SIM_108) (167) [ARRY] (2) duc.vol_a.dynBal.medium.state.X = duc.vol_a.dynBal.medium.X ($RES_SIM_109) (168) [SCAL] (1) sou1.ports[1].h_outflow = sou1.h_internal ($RES_SIM_60) (169) [SCAL] (1) sou1.ports[1].p = sou1.p_in_internal ($RES_SIM_62) (170) [ARRY] (1) duc.vol_a.dynBal.mCOut = duc.vol_a.dynBal.mC ($RES_SIM_68) (171) [SCAL] (1) $FUN_47 = sum(duc.vol_a.dynBal.ports_mC_flow[:, 1]) ($RES_$AUX_579) (172) [SCAL] (1) duc.vol_a.dynBal.mb_flow = sum(duc.vol_a.dynBal.ports.m_flow) ($RES_$AUX_578) (173) [SCAL] (1) duc.vol_a.dynBal.Hb_flow = sum(duc.vol_a.dynBal.ports_H_flow) ($RES_$AUX_577) (174) [SCAL] (1) -sou1.m_flow = sum(sou1.ports.m_flow) ($RES_$AUX_576) (175) [SCAL] (1) duc.vol_a.dynBal.medium.state.T = -((-273.15) - duc.vol_a.dynBal.medium.T_degC) ($RES_SIM_110) (176) [SCAL] (1) $FUN_51 = sum(duc.vol_a.Xi) ($RES_$AUX_575) (177) [SCAL] (1) duc.vol_a.dynBal.medium.state.p = 99999.99999999999 * duc.vol_a.dynBal.medium.p_bar ($RES_SIM_111) (178) [SCAL] (1) $FUN_52 = sum(duc.vol_b.Xi) ($RES_$AUX_574) (179) [SCAL] (1) duc.vol_a.dynBal.medium.R_s = 287.0512249529787 * duc.vol_a.dynBal.medium.X[2] + 461.5233290850878 * duc.vol_a.dynBal.medium.X[1] ($RES_SIM_114) (180) [SCAL] (1) -((-84437.5) - duc.vol_a.dynBal.medium.u) = 1006.0 * ((-273.15) - ((-273.15) - duc.vol_a.dynBal.medium.T_degC)) * duc.vol_a.dynBal.medium.X[2] + (2.5010145e6 + 1860.0 * ((-273.15) - ((-273.15) - duc.vol_a.dynBal.medium.T_degC))) * duc.vol_a.dynBal.medium.X[1] ($RES_SIM_115) (181) [SCAL] (1) duc.vol_a.dynBal.medium.MM = 1/(55.508435061791985 * duc.vol_a.dynBal.medium.X[1] + 34.52428788658843 * duc.vol_a.dynBal.medium.X[2]) ($RES_SIM_117) (182) [ARRY] (1) duc.vol_a.dynBal.mXiOut = duc.vol_a.dynBal.mXi ($RES_SIM_70) (183) [ARRY] (1) duc.heaLos_a.port_a.C_outflow = {duc.vol_a.ports[2].C_outflow[1]} ($RES_SIM_200) (184) [FOR-] (2) ($RES_SIM_72) (184) [----] for $i1 in 1:2 loop (184) [----] [SCAL] (1) duc.vol_a.dynBal.ports[$i1].p = 99999.99999999999 * duc.vol_a.dynBal.medium.p_bar ($RES_SIM_73) (184) [----] end for; (185) [ARRY] (1) duc.heaLos_a.port_b.Xi_outflow = {duc.senMasFlo.port_a.Xi_outflow[1]} ($RES_SIM_201) (186) [ARRY] (1) duc.heaLos_a.port_a.Xi_outflow = {duc.vol_a.ports[2].Xi_outflow[1]} ($RES_SIM_202) (187) [FOR-] (2) ($RES_SIM_74) (187) [----] for $i1 in 1:2 loop (187) [----] [SCAL] (1) duc.vol_a.dynBal.ports[$i1].h_outflow = -((-84437.5) - duc.vol_a.dynBal.medium.u) ($RES_SIM_75) (187) [----] end for; (188) [FOR-] (2) ($RES_SIM_76) (188) [----] for $i1 in 1:2 loop (188) [----] [ARRY] (1) duc.vol_a.dynBal.ports[$i1].Xi_outflow = duc.vol_a.dynBal.medium.Xi ($RES_SIM_77) (188) [----] end for; (189) [SCAL] (1) 0.0 = duc.senMasFlo.port_b.p - duc.heaLos_a.port_b.p ($RES_SIM_205) (190) [FOR-] (2) ($RES_SIM_78) (190) [----] for $i1 in 1:2 loop (190) [----] [ARRY] (1) duc.vol_a.dynBal.ports[$i1].C_outflow = duc.vol_a.dynBal.C ($RES_SIM_79) (190) [----] end for; (191) [SCAL] (1) duc.heaLos_a.heatPort.Q_flow = $FUN_25 * duc.res.m_flow ($RES_SIM_206) (192) [SCAL] (1) duc.heaLos_a.T_b_outflow = duc.heaLos_a.TAmb + (duc.heaLos_a.T_a_inflow - duc.heaLos_a.TAmb) * $FUN_24 ($RES_SIM_207) (193) [SCAL] (1) duc.heaLos_a.T_a_inflow = 273.15 + (duc.senMasFlo.port_a.h_outflow - 2.5010145e6 * duc.heaLos_a.port_b.Xi_outflow[1]) / (1006.0 * (1.0 - duc.heaLos_a.port_b.Xi_outflow[1]) + 1860.0 * duc.heaLos_a.port_b.Xi_outflow[1]) ($RES_SIM_208) (194) [SCAL] (1) duc.heaLos_a.port_b.h_outflow = 1006.0 * ((-273.15) + duc.heaLos_a.T_b_outflow) * (1.0 - duc.heaLos_a.port_b.Xi_outflow[1]) + (2.5010145e6 + 1860.0 * ((-273.15) + duc.heaLos_a.T_b_outflow)) * duc.heaLos_a.port_b.Xi_outflow[1] ($RES_SIM_209) (195) [ARRY] (1) duc.vol_b.dynBal.mCOut = duc.vol_b.dynBal.mC ($RES_SIM_122) (196) [ARRY] (1) duc.vol_b.dynBal.mXiOut = duc.vol_b.dynBal.mXi ($RES_SIM_124) (197) [FOR-] (2) ($RES_SIM_126) (197) [----] for $i1 in 1:2 loop (197) [----] [SCAL] (1) duc.vol_b.dynBal.ports[$i1].p = 99999.99999999999 * duc.vol_b.dynBal.medium.p_bar ($RES_SIM_127) (197) [----] end for; (198) [FOR-] (2) ($RES_SIM_128) (198) [----] for $i1 in 1:2 loop (198) [----] [SCAL] (1) duc.vol_b.dynBal.ports[$i1].h_outflow = -((-84437.5) - duc.vol_b.dynBal.medium.u) ($RES_SIM_129) (198) [----] end for; (199) [ARRY] (1) $DER.duc.vol_a.dynBal.mC = duc.vol_a.dynBal.mbC_flow + duc.vol_a.dynBal.C_flow_internal ($RES_SIM_80) (200) [ARRY] (1) $DER.duc.vol_a.dynBal.mXi = duc.vol_a.dynBal.mbXi_flow ($RES_SIM_81) (201) [SCAL] (1) duc.heaLos_a.port_a.h_outflow = duc.vol_a.ports[2].h_outflow ($RES_SIM_210) (202) [SCAL] (1) $DER.duc.vol_a.dynBal.m = duc.vol_a.dynBal.mb_flow ($RES_SIM_82) (203) [SCAL] (1) $DER.duc.vol_a.dynBal.U = duc.vol_a.dynBal.Hb_flow ($RES_SIM_83) (204) [SCAL] (1) duc.vol_a.dynBal.mbC_flow[1] = $FUN_47 ($RES_SIM_86) (205) [SCAL] (1) duc.vol_a.dynBal.mbXi_flow[1] = $FUN_46 ($RES_SIM_87) (206) [SCAL] (1) duc.vol_a.dynBal.ports_mC_flow[2, 1] = $FUN_45 ($RES_SIM_88) (207) [SCAL] (1) pip.dp = senTemIn.port_a.p - senTemOutW.port_b.p ($RES_BND_516) (208) [SCAL] (1) duc.v = duc.del.V_flow / duc.del.A ($RES_SIM_217) (209) [SCAL] (1) duc.vol_a.dynBal.ports_mXi_flow[2, 1] = $FUN_44 ($RES_SIM_89) (210) [SCAL] (1) $DER.duc.del.x = duc.v ($RES_SIM_218) (211) [SCAL] (1) $DER.pip.vol_b.dynBal.m = pip.vol_b.dynBal.mb_flow ($RES_SIM_300) (212) [SCAL] (1) $DER.pip.vol_b.dynBal.U = pip.vol_b.dynBal.Hb_flow ($RES_SIM_301) (213) [SCAL] (1) pip.vol_b.dynBal.ports_H_flow[2] = $FUN_10 ($RES_SIM_304) (214) [SCAL] (1) pip.vol_b.dynBal.ports_H_flow[1] = $FUN_9 ($RES_SIM_305) (215) [FOR-] (2) ($RES_SIM_130) (215) [----] for $i1 in 1:2 loop (215) [----] [ARRY] (1) duc.vol_b.dynBal.ports[$i1].Xi_outflow = duc.vol_b.dynBal.medium.Xi ($RES_SIM_131) (215) [----] end for; (216) [SCAL] (1) pip.vol_b.dynBal.U = pip.vol_b.dynBal.m * (4184.0 * ((-273.15) - ((-273.15) - pip.vol_b.dynBal.medium.T_degC))) ($RES_SIM_307) (217) [FOR-] (2) ($RES_SIM_132) (217) [----] for $i1 in 1:2 loop (217) [----] [ARRY] (1) duc.vol_b.dynBal.ports[$i1].C_outflow = duc.vol_b.dynBal.C ($RES_SIM_133) (217) [----] end for; (218) [SCAL] (1) pip.vol_b.dynBal.m = 995.586 * pip.vol_b.dynBal.fluidVolume ($RES_SIM_308) (219) [ARRY] (1) $DER.duc.vol_b.dynBal.mC = duc.vol_b.dynBal.mbC_flow + duc.vol_b.dynBal.C_flow_internal ($RES_SIM_134) (220) [ARRY] (1) $DER.duc.vol_b.dynBal.mXi = duc.vol_b.dynBal.mbXi_flow ($RES_SIM_135) (221) [SCAL] (1) $DER.duc.vol_b.dynBal.m = duc.vol_b.dynBal.mb_flow ($RES_SIM_136) (222) [SCAL] (1) $DER.duc.vol_b.dynBal.U = duc.vol_b.dynBal.Hb_flow ($RES_SIM_137) (223) [SCAL] (1) duc.vol_a.dynBal.ports_H_flow[2] = $FUN_43 ($RES_SIM_90) (224) [SCAL] (1) duc.vol_a.dynBal.ports_mC_flow[1, 1] = $FUN_42 ($RES_SIM_91) (225) [SCAL] (1) duc.vol_a.dynBal.ports_mXi_flow[1, 1] = $FUN_41 ($RES_SIM_92) (226) [SCAL] (1) pip.res.dp = pip.senMasFlo.port_b.p - pip.heaLos_b.port_a.p ($RES_BND_520) (227) [ARRY] (1) duc.res.port_b.C_outflow = {duc.senMasFlo.port_b.C_outflow[1]} ($RES_SIM_221) (228) [SCAL] (1) duc.vol_a.dynBal.ports_H_flow[1] = $FUN_40 ($RES_SIM_93) (229) [SCAL] (1) pip.res.v = pip.res.m_flow / (pip.res.ARound * pip.res.rho_default) ($RES_BND_521) (230) [ARRY] (1) duc.res.port_a.C_outflow = {duc.del.port_a.C_outflow[1]} ($RES_SIM_222) (231) [ARRY] (1) duc.vol_a.dynBal.COut = duc.vol_a.dynBal.C ($RES_SIM_94) (232) [ARRY] (1) duc.res.port_b.Xi_outflow = {duc.senMasFlo.port_b.Xi_outflow[1]} ($RES_SIM_223) (233) [ARRY] (1) duc.vol_a.dynBal.XiOut = duc.vol_a.dynBal.medium.Xi ($RES_SIM_95) (234) [ARRY] (1) duc.res.port_a.Xi_outflow = {duc.del.port_a.Xi_outflow[1]} ($RES_SIM_224) (235) [ARRY] (1) duc.vol_a.dynBal.mC = duc.vol_a.dynBal.m * duc.vol_a.dynBal.C ($RES_SIM_97) (236) [SCAL] (1) duc.vol_a.dynBal.U = duc.vol_a.dynBal.m * duc.vol_a.dynBal.medium.u + duc.vol_a.dynBal.CSen * ((-273.15) - ((-273.15) - duc.vol_a.dynBal.medium.T_degC)) ($RES_SIM_98) (237) [SCAL] (1) pip.vol_b.p = pip.vol_b.ports[1].p ($RES_BND_526) (238) [ARRY] (1) duc.vol_a.dynBal.mXi = duc.vol_a.dynBal.m * duc.vol_a.dynBal.medium.Xi ($RES_SIM_99) (239) [SCAL] (1) duc.res.dp = homotopy(IDEAS.Fluid.BaseClasses.FlowModels.basicFlowFunction_m_flow(duc.res.m_flow, duc.res.k, duc.res.m_flow_turbulent), duc.res.dp_nominal_pos * duc.res.m_flow) ($RES_SIM_228) (240) [ARRY] (1) sin1.ports[1].Xi_outflow = sin1.Xi_in_internal ($RES_SIM_229) (241) [SCAL] (1) duc.del.port_b.C_outflow[1] = $FUN_23[1] ($RES_$AUX_631) (242) [SCAL] (1) duc.del.port_a.C_outflow[1] = $FUN_22[1] ($RES_$AUX_630) (243) [SCAL] (1) pip.vol_b.dynBal.medium.state.p = 99999.99999999999 * pip.vol_b.dynBal.medium.p_bar ($RES_SIM_313) (244) [SCAL] (1) pip.vol_b.dynBal.medium.state.T = -((-273.15) - pip.vol_b.dynBal.medium.T_degC) ($RES_SIM_314) (245) [SCAL] (1) duc.vol_b.dynBal.mbC_flow[1] = $FUN_37 ($RES_SIM_140) (246) [SCAL] (1) duc.vol_b.dynBal.mbXi_flow[1] = $FUN_36 ($RES_SIM_141) (247) [SCAL] (1) pip.timDel.tauRev = max(0.0, time - pip.timDel.time_out_rev) ($RES_SIM_317) (248) [SCAL] (1) duc.vol_b.dynBal.ports_mC_flow[2, 1] = $FUN_35 ($RES_SIM_142) (249) [SCAL] (1) pip.timDel.tau = max(0.0, time - pip.timDel.time_out_des) ($RES_SIM_318) (250) [SCAL] (1) duc.vol_b.dynBal.ports_mXi_flow[2, 1] = $FUN_34 ($RES_SIM_143) (251) [SCAL] (1) duc.vol_b.dynBal.ports_H_flow[2] = $FUN_33 ($RES_SIM_144) (252) [SCAL] (1) duc.vol_b.dynBal.ports_mC_flow[1, 1] = $FUN_32 ($RES_SIM_145) (253) [SCAL] (1) duc.vol_b.dynBal.ports_mXi_flow[1, 1] = $FUN_31 ($RES_SIM_146) (254) [SCAL] (1) duc.vol_b.dynBal.ports_H_flow[1] = $FUN_30 ($RES_SIM_147) (255) [ARRY] (1) duc.vol_b.dynBal.COut = duc.vol_b.dynBal.C ($RES_SIM_148) (256) [SCAL] (1) sou1.ports[1].p = senTemIn1.port_a.p ($RES_SIM_400) (257) [ARRY] (1) duc.vol_b.dynBal.XiOut = duc.vol_b.dynBal.medium.Xi ($RES_SIM_149) (258) [SCAL] (1) senTemOutA.port_b.p = sin1.ports[1].p ($RES_SIM_401) (259) [SCAL] (1) pip.m_flow + sou.ports[1].m_flow = 0.0 ($RES_SIM_404) (260) [SCAL] (1) $SEV_8 = duc.m_flow < (-senTemIn1.m_flow_small) ($RES_EVT_700) (261) [SCAL] (1) sou.ports[1].p = senTemIn.port_a.p ($RES_SIM_405) (262) [ARRY] (1) sin1.ports[1].C_outflow = sin1.C_in_internal ($RES_SIM_230) (263) [SCAL] (1) $SEV_9 = senTemIn1.m_flow_small > 0.0 ($RES_EVT_701) (264) [SCAL] (1) senTemOutW.port_b.p = sin.ports[1].p ($RES_SIM_406) (265) [ARRY] (1) sin1.C_in_internal = sin1.C ($RES_SIM_231) (266) [SCAL] (1) duc.del.port_b.Xi_outflow[1] = $FUN_21[1] ($RES_$AUX_629) (267) [SCAL] (1) $SEV_10 = (-senTemOutA.port_b.m_flow) > senTemOutA.m_flow_small ($RES_EVT_702) (268) [ARRY] (1) sin1.Xi_in_internal = sin1.X[1:1] ($RES_SIM_232) (269) [SCAL] (1) duc.del.port_a.Xi_outflow[1] = $FUN_20[1] ($RES_$AUX_628) (270) [SCAL] (1) $SEV_11 = (-senTemOutA.port_b.m_flow) < (-senTemOutA.m_flow_small) ($RES_EVT_703) (271) [ARRY] (2) sin1.X_in_internal = sin1.X ($RES_SIM_233) (272) [SCAL] (1) $SEV_12 = senTemOutA.m_flow_small > 0.0 ($RES_EVT_704) (273) [SCAL] (1) sin1.ports[1].h_outflow = sin1.h_internal ($RES_SIM_234) (274) [SCAL] (1) pip.vol_a.p = pip.vol_a.ports[1].p ($RES_BND_535) (275) [SCAL] (1) sin1.ports[1].p = sin1.p ($RES_SIM_236) (276) [SCAL] (1) $SEV_16 = noEvent(duc.vol_a.dynBal.medium.X[1] >= (-1e-5)) and noEvent(duc.vol_a.dynBal.medium.X[1] <= 1.00001) ($RES_EVT_708) (277) [SCAL] (1) -4184.0 * (273.15 - senTemIn.T_a_inflow) = sou.ports[1].h_outflow ($RES_SIM_238) (278) [TUPL] (2) (pip.res.port_a.h_outflow, -4184.0 * (273.15 - pip.heaLos_b.T_a_inflow)) = spatialDistribution(pip.heaLos_a.port_a.h_outflow, pip.heaLos_b.port_a.h_outflow, pip.del.x / pip.del.length, $SEV_36, {0.0, 1.0}, {pip.del.h_ini_in, pip.del.h_ini_out}) ($RES_$AUX_621) (279) [SCAL] (1) $FUN_3 = exp(-pip.timDel.tauRev / pip.heaLos_a.tau_char) ($RES_$AUX_620) (280) [SCAL] (1) $DER.pip.timDel.x = pip.timDel.u ($RES_SIM_320) (281) [SCAL] (1) pip.timDel.u = pip.res.m_flow * pip.timDel.conUM ($RES_SIM_321) (282) [ARRY] (1) duc.vol_b.dynBal.mC = duc.vol_b.dynBal.m * duc.vol_b.dynBal.C ($RES_SIM_151) (283) [SCAL] (1) duc.vol_b.dynBal.U = duc.vol_b.dynBal.m * duc.vol_b.dynBal.medium.u + duc.vol_b.dynBal.CSen * ((-273.15) - ((-273.15) - duc.vol_b.dynBal.medium.T_degC)) ($RES_SIM_152) (284) [ARRY] (1) duc.vol_b.dynBal.mXi = duc.vol_b.dynBal.m * duc.vol_b.dynBal.medium.Xi ($RES_SIM_153) (285) [SCAL] (1) 0.0 = pip.heaLos_b.port_a.p - pip.heaLos_b.port_b.p ($RES_SIM_329) (286) [SCAL] (1) duc.vol_b.dynBal.m = duc.vol_b.dynBal.fluidVolume * (1.1843079200592153e-5 * (99999.99999999999 * duc.vol_b.dynBal.medium.p_bar)) ($RES_SIM_154) (287) [ARRY] (1) duc.vol_b.dynBal.C_flow_internal = {0.0} ($RES_SIM_155) (288) [ARRY] (1) sou1.C_in = sou1.C_in_internal ($RES_SIM_410) (289) [ARRY] (2) sou1.X_in = sou1.X_in_internal ($RES_SIM_411) (290) [SCAL] (1) duc.vol_a.ports[2].p = duc.heaLos_a.port_b.p ($RES_SIM_413) (291) [SCAL] (1) duc.vol_a.ports[1].h_outflow = senTemIn1.port_a.h_outflow ($RES_SIM_414) (292) [SCAL] (1) duc.vol_a.ports[1].Xi_outflow[1] = duc.port_a.Xi_outflow[1] ($RES_SIM_415) (293) [SCAL] (1) duc.vol_a.ports[1].C_outflow[1] = duc.port_a.C_outflow[1] ($RES_SIM_416) (294) [SCAL] (1) $FUN_4 = IDEAS.Utilities.Math.Functions.spliceFunction((2.390057361376673e-4 * ((-1.1428595999999999e6) - pip.heaLos_a.port_b.h_outflow) + (273.15 + 2.390057361376673e-4 * pip.res.port_a.h_outflow)) * pip.heaLos_a.cp_default, 0.0, -pip.res.m_flow, 0.001) ($RES_$AUX_619) (295) [SCAL] (1) $SEV_20 = noEvent(duc.vol_b.dynBal.medium.X[1] >= (-1e-5)) and noEvent(duc.vol_b.dynBal.medium.X[1] <= 1.00001) ($RES_EVT_712) (296) [SCAL] (1) duc.vol_a.ports[1].m_flow - duc.m_flow = 0.0 ($RES_SIM_417) (297) [SCAL] (1) $FUN_5 = exp(-pip.timDel.tau / pip.heaLos_b.tau_char) ($RES_$AUX_618) (298) [SCAL] (1) $SEV_21 = pip.m_flow > senTemIn.m_flow_small ($RES_EVT_713) (299) [SCAL] (1) senTemIn1.port_a.p = duc.vol_a.ports[1].p ($RES_SIM_418) (300) [SCAL] (1) $FUN_6 = IDEAS.Utilities.Math.Functions.spliceFunction((2.390057361376673e-4 * ((-1.1428595999999999e6) - pip.heaLos_b.port_b.h_outflow) + pip.heaLos_b.T_a_inflow) * pip.heaLos_b.cp_default, 0.0, pip.res.m_flow, 0.001) ($RES_$AUX_617) (301) [SCAL] (1) $SEV_22 = pip.m_flow < (-senTemIn.m_flow_small) ($RES_EVT_714) (302) [SCAL] (1) duc.vol_b.ports[2].h_outflow = senTemOutA.port_b.h_outflow ($RES_SIM_419) (303) [SCAL] (1) sin1.h_internal = 1006.0 * ((-273.15) + sin1.T) * (1.0 - sin1.X_in_internal[1]) + (2.5010145e6 + 1860.0 * ((-273.15) + sin1.T)) * sin1.X_in_internal[1] ($RES_BND_544) (304) [TUPL] (2) (pip.timDel.time_out_rev, pip.timDel.time_out_des) = spatialDistribution(time, time, pip.timDel.x, $SEV_37, {0.0, 1.0}, {pip.timDel.t0 + pip.timDel.t_in_start, pip.timDel.t0 + pip.timDel.t_out_start}) ($RES_$AUX_616) (305) [SCAL] (1) $SEV_23 = senTemIn.m_flow_small > 0.0 ($RES_EVT_715) (306) [SCAL] (1) senTemIn.T = smooth(1, if $SEV_21 then senTemIn.T_a_inflow else if $SEV_22 then 273.15 + 2.390057361376673e-4 * pip.port_a.h_outflow else if $SEV_23 then 0.25 * ((273.15 + 2.390057361376673e-4 * pip.port_a.h_outflow) - senTemIn.T_a_inflow) * ((-3.0) + (pip.m_flow / senTemIn.m_flow_small) ^ 2.0) * (pip.m_flow / senTemIn.m_flow_small) + 0.5 * (senTemIn.T_a_inflow + (273.15 + 2.390057361376673e-4 * pip.port_a.h_outflow)) else 0.5 * (senTemIn.T_a_inflow + (273.15 + 2.390057361376673e-4 * pip.port_a.h_outflow))) ($RES_SIM_245) (307) [SCAL] (1) $FUN_9 = semiLinear(pip.vol_b.dynBal.ports[1].m_flow, pip.heaLos_b.port_b.h_outflow, pip.vol_b.dynBal.ports[1].h_outflow) ($RES_$AUX_615) (308) [SCAL] (1) $SEV_24 = (-senTemOutW.port_b.m_flow) > senTemOutW.m_flow_small ($RES_EVT_716) (309) [SCAL] (1) duc.dp = senTemIn1.port_a.p - senTemOutA.port_b.p ($RES_BND_546) (310) [SCAL] (1) $FUN_10 = semiLinear(pip.vol_b.dynBal.ports[2].m_flow, -4184.0 * (273.15 - senTemOutW.T_b_inflow), pip.vol_b.dynBal.ports[2].h_outflow) ($RES_$AUX_614) (311) [SCAL] (1) $SEV_25 = (-senTemOutW.port_b.m_flow) < (-senTemOutW.m_flow_small) ($RES_EVT_717) (312) [SCAL] (1) pip.vol_b.dynBal.mb_flow = sum(pip.vol_b.dynBal.ports.m_flow) ($RES_$AUX_613) (313) [SCAL] (1) $SEV_26 = senTemOutW.m_flow_small > 0.0 ($RES_EVT_718) (314) [SCAL] (1) pip.vol_b.dynBal.Hb_flow = sum(pip.vol_b.dynBal.ports_H_flow) ($RES_$AUX_612) (315) [ARRY] (2) pip.vol_a.dynBal.ports.p = pip.vol_a.ports.p ($RES_SIM_500) (316) [SCAL] (1) -4184.0 * (273.15 - senTemOutW.T_b_inflow) = sin.ports[1].h_outflow ($RES_SIM_249) (317) [SCAL] (1) $FUN_13 = semiLinear(pip.vol_a.dynBal.ports[1].m_flow, -4184.0 * (273.15 - senTemIn.T_a_inflow), pip.vol_a.dynBal.ports[1].h_outflow) ($RES_$AUX_611) (318) [SCAL] (1) $FUN_14 = semiLinear(pip.vol_a.dynBal.ports[2].m_flow, pip.heaLos_a.port_b.h_outflow, pip.vol_a.dynBal.ports[2].h_outflow) ($RES_$AUX_610) (319) [SCAL] (1) pip.heaLos_b.heatPort.Q_flow = -$FUN_6 * pip.res.m_flow ($RES_SIM_330) (320) [SCAL] (1) -2.390057361376673e-4 * ((-1.1428595999999999e6) - pip.heaLos_b.port_b.h_outflow) = pip.heaLos_a.TAmb + (pip.heaLos_b.T_a_inflow - pip.heaLos_a.TAmb) * $FUN_5 ($RES_SIM_331) (321) [SCAL] (1) pip.vol_b.dynBal.ports[2].h_outflow = pip.vol_b.ports[2].h_outflow ($RES_SIM_508) (322) [SCAL] (1) pip.vol_b.dynBal.ports[1].h_outflow = pip.vol_b.ports[1].h_outflow ($RES_SIM_509) (323) [SCAL] (1) pip.heaLos_b.port_a.h_outflow = pip.vol_b.ports[1].h_outflow ($RES_SIM_334) (324) [SCAL] (1) duc.vol_b.dynBal.medium.X[2] = 1.0 - duc.vol_b.dynBal.medium.X[1] ($RES_SIM_161) (325) [SCAL] (1) duc.vol_b.dynBal.medium.X[1] = duc.vol_b.dynBal.medium.Xi[1] ($RES_SIM_162) (326) [SCAL] (1) 0.0 = pip.senMasFlo.port_b.p - pip.heaLos_a.port_b.p ($RES_SIM_338) (327) [ARRY] (2) duc.vol_b.dynBal.medium.state.X = duc.vol_b.dynBal.medium.X ($RES_SIM_163) (328) [SCAL] (1) pip.heaLos_a.heatPort.Q_flow = $FUN_4 * pip.res.m_flow ($RES_SIM_339) (329) [SCAL] (1) duc.vol_b.dynBal.medium.state.T = -((-273.15) - duc.vol_b.dynBal.medium.T_degC) ($RES_SIM_164) (330) [SCAL] (1) duc.vol_b.dynBal.medium.state.p = 99999.99999999999 * duc.vol_b.dynBal.medium.p_bar ($RES_SIM_165) (331) [SCAL] (1) duc.vol_b.dynBal.medium.R_s = 287.0512249529787 * duc.vol_b.dynBal.medium.X[2] + 461.5233290850878 * duc.vol_b.dynBal.medium.X[1] ($RES_SIM_168) (332) [SCAL] (1) duc.vol_b.ports[2].Xi_outflow[1] = duc.port_b.Xi_outflow[1] ($RES_SIM_420) (333) [SCAL] (1) -((-84437.5) - duc.vol_b.dynBal.medium.u) = 1006.0 * ((-273.15) - ((-273.15) - duc.vol_b.dynBal.medium.T_degC)) * duc.vol_b.dynBal.medium.X[2] + (2.5010145e6 + 1860.0 * ((-273.15) - ((-273.15) - duc.vol_b.dynBal.medium.T_degC))) * duc.vol_b.dynBal.medium.X[1] ($RES_SIM_169) (334) [SCAL] (1) duc.vol_b.ports[2].C_outflow[1] = duc.port_b.C_outflow[1] ($RES_SIM_421) (335) [SCAL] (1) duc.vol_b.ports[2].p = senTemOutA.port_b.p ($RES_SIM_422) (336) [SCAL] (1) duc.heaLos_b.port_b.p = duc.vol_b.ports[1].p ($RES_SIM_423) (337) [SCAL] (1) duc.res.dp = duc.senMasFlo.port_b.p - duc.heaLos_b.port_a.p ($RES_BND_550) (338) [SCAL] (1) duc.res.v = duc.res.m_flow / (duc.res.ARound * duc.res.rho_default) ($RES_BND_551) (339) [SCAL] (1) pip.vol_a.dynBal.mb_flow = sum(pip.vol_a.dynBal.ports.m_flow) ($RES_$AUX_609) (340) [SCAL] (1) duc.del.V_flow = duc.res.m_flow / smooth(1, if $SEV_33 then 1.1843079200592153e-5 * duc.heaLos_b.port_a.p else if $SEV_34 then 1.1843079200592153e-5 * duc.heaLos_b.port_a.p else if $SEV_35 then 0.25 * (1.1843079200592153e-5 * duc.heaLos_b.port_a.p - 1.1843079200592153e-5 * duc.heaLos_b.port_a.p) * ((-3.0) + (duc.res.m_flow / duc.del.m_flow_small) ^ 2.0) * (duc.res.m_flow / duc.del.m_flow_small) + 0.5 * (1.1843079200592153e-5 * duc.heaLos_b.port_a.p + 1.1843079200592153e-5 * duc.heaLos_b.port_a.p) else 0.5 * (1.1843079200592153e-5 * duc.heaLos_b.port_a.p + 1.1843079200592153e-5 * duc.heaLos_b.port_a.p)) ($RES_BND_552) (341) [SCAL] (1) pip.vol_a.dynBal.Hb_flow = sum(pip.vol_a.dynBal.ports_H_flow) ($RES_$AUX_608) (342) [ARRY] (1) duc.del.Xi_inflow_a = {duc.res.port_b.Xi_outflow[1]} ($RES_BND_553) (343) [SCAL] (1) -sou.m_flow = sum(sou.ports.m_flow) ($RES_$AUX_607)