Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr Annex60_1.0.0_Annex60.Fluid.MixingVolumes.Validation.MixingVolumeTraceSubstanceReverseFlowPrescribedHeatFlowRate.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/Annex60 1.0.0/package.mo", uses=false)
Using package Annex60 with version 1.0.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Annex60 1.0.0/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(Annex60.Fluid.MixingVolumes.Validation.MixingVolumeTraceSubstanceReverseFlowPrescribedHeatFlowRate,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="Annex60_1.0.0_Annex60.Fluid.MixingVolumes.Validation.MixingVolumeTraceSubstanceReverseFlowPrescribedHeatFlowRate")
translateModel(Annex60.Fluid.MixingVolumes.Validation.MixingVolumeTraceSubstanceReverseFlowPrescribedHeatFlowRate,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="Annex60_1.0.0_Annex60.Fluid.MixingVolumes.Validation.MixingVolumeTraceSubstanceReverseFlowPrescribedHeatFlowRate")
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo): time 0.001187/0.001187, allocations: 105.8 kB / 16.42 MB, free: 6.461 MB / 14.72 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo): time 0.001131/0.001131, allocations: 189.9 kB / 17.36 MB, free: 5.73 MB / 14.72 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.2.3+maint.om/package.mo): time 1.26/1.26, allocations: 205.1 MB / 223.2 MB, free: 12.25 MB / 190.1 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Annex60 1.0.0/package.mo): time 0.2525/0.2525, allocations: 54.95 MB / 325.5 MB, free: 4.859 MB / 270.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 2.533e-05/2.534e-05, allocations: 2.281 kB / 456.8 MB, free: 2.691 MB / 334.1 MB
Notification: Performance of NFInst.instantiate(Annex60.Fluid.MixingVolumes.Validation.MixingVolumeTraceSubstanceReverseFlowPrescribedHeatFlowRate): time 0.42/0.42, allocations: 190.5 MB / 0.6321 GB, free: 12.41 MB / 462.1 MB
Notification: Performance of NFInst.instExpressions: time 0.008779/0.4288, allocations: 5.614 MB / 0.6376 GB, free: 6.781 MB / 462.1 MB
Notification: Performance of NFInst.updateImplicitVariability: time 0.001197/0.4301, allocations: 39.75 kB / 0.6377 GB, free: 6.742 MB / 462.1 MB
Notification: Performance of NFTyping.typeComponents: time 0.001568/0.4316, allocations: 0.6214 MB / 0.6383 GB, free: 6.117 MB / 462.1 MB
Notification: Performance of NFTyping.typeBindings: time 0.003897/0.4356, allocations: 1.664 MB / 0.6399 GB, free: 4.445 MB / 462.1 MB
Notification: Performance of NFTyping.typeClassSections: time 0.002818/0.4385, allocations: 1.217 MB / 0.6411 GB, free: 3.242 MB / 462.1 MB
Notification: Performance of NFFlatten.flatten: time 0.003471/0.442, allocations: 3.018 MB / 0.644 GB, free: 220 kB / 462.1 MB
Notification: Performance of NFFlatten.resolveConnections: time 0.001389/0.4434, allocations: 1.174 MB / 0.6452 GB, free: 15.02 MB / 478.1 MB
Notification: Performance of NFEvalConstants.evaluate: time 0.001814/0.4452, allocations: 1.156 MB / 0.6463 GB, free: 13.86 MB / 478.1 MB
Notification: Performance of NFSimplifyModel.simplify: time 0.001569/0.4468, allocations: 0.9207 MB / 0.6472 GB, free: 12.95 MB / 478.1 MB
Notification: Performance of NFPackage.collectConstants: time 0.0001627/0.4469, allocations: 112 kB / 0.6473 GB, free: 12.84 MB / 478.1 MB
Notification: Performance of NFFlatten.collectFunctions: time 0.002581/0.4495, allocations: 1.399 MB / 0.6487 GB, free: 11.44 MB / 478.1 MB
Notification: Performance of combineBinaries: time 0.001718/0.4513, allocations: 2.171 MB / 0.6508 GB, free: 9.246 MB / 478.1 MB
Notification: Performance of replaceArrayConstructors: time 0.0009451/0.4522, allocations: 1.377 MB / 0.6521 GB, free: 7.855 MB / 478.1 MB
Notification: Performance of NFVerifyModel.verify: time 0.0003144/0.4525, allocations: 211.4 kB / 0.6524 GB, free: 7.648 MB / 478.1 MB
Notification: Performance of FrontEnd: time 0.0002416/0.4528, allocations: 51.69 kB / 0.6524 GB, free: 7.598 MB / 478.1 MB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 231 (214)
 * Number of variables: 231 (197)
Notification: Performance of Bindings: time 0.005466/0.4582, allocations: 6.192 MB / 0.6584 GB, free: 1.23 MB / 478.1 MB
Notification: Performance of FunctionAlias: time 0.0004087/0.4587, allocations: 385 kB / 0.6588 GB, free: 0.8633 MB / 478.1 MB
Notification: Performance of Early Inline: time 0.00291/0.4616, allocations: 3.15 MB / 0.6619 GB, free: 13.67 MB / 494.1 MB
Notification: Performance of simplify1: time 0.0002955/0.4619, allocations: 247.7 kB / 0.6621 GB, free: 13.43 MB / 494.1 MB
Notification: Performance of Alias: time 0.003819/0.4657, allocations: 3.574 MB / 0.6656 GB, free: 9.582 MB / 494.1 MB
Notification: Performance of simplify2: time 0.0002486/0.466, allocations: 219.7 kB / 0.6658 GB, free: 9.367 MB / 494.1 MB
Notification: Performance of Events: time 0.0007412/0.4667, allocations: 0.6075 MB / 0.6664 GB, free: 8.758 MB / 494.1 MB
Notification: Performance of Detect States: time 0.0008137/0.4676, allocations: 0.818 MB / 0.6672 GB, free: 7.91 MB / 494.1 MB
Notification: Performance of Partitioning: time 0.001226/0.4688, allocations: 1.22 MB / 0.6684 GB, free: 6.543 MB / 494.1 MB
Error: Internal error NBSlice.fillDependencyArray failed because number of flattened indices 1 for dependency bou.C_in_internal could not be divided by the body size 2 without rest.
Error: Internal error NBAdjacency.Matrix.createPseudo failed for:
[ARRY] (2) bou.ports.C_outflow = {bou.C_in_internal for $i1 in 1:2} ($RES_SIM_115)
Error: Internal error NBAdjacency.Matrix.create failed to create adjacency matrix for system:
System Variables (156/194)
****************************
(1)       [ALGB] (1) Real gain.y
(2)       [ALGB] (1) flow Real[1] sou.ports.m_flow (min = {-1e60}, max = {1e60})
(3)       [ALGB] (1) Real sou1.medium.u (min = -1e8, max = 1e8, nominal = 1e6)
(4)       [ALGB] (1) Real[1] volDyn.mXi
(5)       [ALGB] (2) stream Real[2, 1] bou.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] (1) protected Real[1] volDyn.dynBal.C (start = {1.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, nominal = volDyn.dynBal.C_nominal)
(7)       [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}})
(8)       [ALGB] (1) Real bou.medium.u (min = -1e8, max = 1e8, nominal = 1e6)
(9)       [ALGB] (1) protected Real[1] volSte.steBal.C_flow_internal
(10)      [DISC] (1) Boolean $SEV_20
(11)      [ALGB] (1) protected Real volSte.steBal.port_a.p (start = 101325.0, min = 0.0, max = 1e8, nominal = 1e5)
(12)      [ALGB] (1) Real sou.medium.state.p (start = 101325.0, min = 0.0, max = 1e8, nominal = 1e5)
(13)      [DISC] (1) Boolean $TEV_1
(14)      [ALGB] (1) protected Real[1] volDyn.dynBal.medium.Xi (start = volDyn.dynBal.X_start[1:1], min = {0.0 for $i1 in 1:1}, max = {1.0 for $i1 in 1:1}, StateSelect = default)
(15)      [DISC] (1) Boolean $TEV_0
(16)      [ALGB] (1) protected Real volSte.steBal.m_flow = volSte.steBal.m_flow (start = volSte.steBal._m_flow_start)
(17)      [ALGB] (2) protected Real[2] sou.X_in_internal
(18)      [ALGB] (2) stream Real[2, 1] volSte.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})
(19)      [ALGB] (1) stream Real[1, 1] sou.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}})
(20)      [ALGB] (1) protected Real volDyn.dynBal.Hb_flow
(21)      [ALGB] (2) flow Real[2] volSte.ports.m_flow (min = {-1e5 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2})
(22)      [ALGB] (1) protected stream Real[1] volSte.steBal.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})
(23)      [ALGB] (2) stream Real[2] volDyn.ports.h_outflow (min = {-1e10 for $i1 in 1:2}, max = {1e10 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2})
(24)      [ALGB] (2) Real[2] sou1.medium.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})
(25)      [ALGB] (1) protected Real[1] volSte.steBal.COut (min = {0.0 for $i1 in 1:1})
(26)      [ALGB] (1) protected Real volDyn.dynBal.medium.R (start = 1000.0, min = 0.0, max = 1e7, nominal = 1000.0)
(27)      [ALGB] (1) Real[1] volSte.C_flow
(28)      [DISC] (1) Boolean $SEV_13
(29)      [DISC] (1) Boolean $SEV_12
(30)      [ALGB] (1) Real sou1.medium.R (start = 1000.0, min = 0.0, max = 1e7, nominal = 1000.0)
(31)      [DISC] (1) Boolean $SEV_11
(32)      [ALGB] (2) protected Real[2] volDyn.dynBal.medium.X (start = volDyn.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})
(33)      [ALGB] (1) protected Real volDyn.dynBal.medium.X_air (min = 0.0, max = 1.0, nominal = 0.1)
(34)      [ALGB] (2) Real[2] bou.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})
(35)      [ALGB] (1) protected Real[1] volDyn.dynBal.mXiOut (min = {0.0 for $i1 in 1:1})
(36)      [ALGB] (1) Real volDyn.p = volDyn.ports[1].p
(37)      [ALGB] (1) Real bou.medium.MM (min = 0.001, max = 0.25, nominal = 0.032)
(38)      [ALGB] (1) protected Real volDyn.dynBal.medium.X_steam (min = 0.0, max = 1.0, nominal = 0.1)
(39)      [ALGB] (2) protected stream Real[2, 1] volDyn.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})
(40)      [ALGB] (2) stream Real[2, 1] volDyn.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})
(41)      [ALGB] (2) protected Real[2, 1] volDyn.dynBal.ports_mC_flow
(42)      [ALGB] (2) Real[2] volSte.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})
(43)      [ALGB] (1) protected Real sou.medium.X_steam (min = 0.0, max = 1.0, nominal = 0.1)
(44)      [ALGB] (2) Real[2] volDyn.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})
(45)      [ALGB] (1) protected Real volDyn.dynBal.medium.u (min = -1e8, max = 1e8, nominal = 1e6)
(46)      [ALGB] (2) protected stream Real[2, 1] volDyn.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})
(47)      [DER-] (1) Real[1] $DER.volDyn.dynBal.mXi
(48)      [ALGB] (1) protected Real sou.medium.X_air (min = 0.0, max = 1.0, nominal = 0.1)
(49)      [ALGB] (1) Real $FUN_9
(50)      [ALGB] (1) protected Real volSte.steBal.dp = volSte.steBal.port_a.p - volSte.steBal.port_a.p (start = volSte.steBal._dp_start)
(51)      [ALGB] (1) Real $FUN_8
(52)      [ALGB] (1) Real volDyn.T = Annex60.Fluid.MixingVolumes.Validation.MixingVolumeTraceSubstanceReverseFlowPrescribedHeatFlowRate.volDyn.Medium.temperature_phX(volDyn.p, -((-84437.5) - volDyn.dynBal.medium.u), {volDyn.Xi[1], 1.0 - sum(volDyn.Xi)}) (start = 293.15, min = 1.0, max = 1e4, nominal = 300.0)
(53)      [ALGB] (1) Real $FUN_7
(54)      [ALGB] (1) Real $FUN_6
(55)      [ALGB] (1) Real $FUN_5
(56)      [ALGB] (1) Real volSte.p = volSte.ports[1].p
(57)      [ALGB] (1) Real $FUN_4
(58)      [DISC] (2) Boolean[2] $SEV_18[$i1]
(59)      [ALGB] (2) protected stream Real[2] volDyn.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})
(60)      [ALGB] (1) Real $FUN_3
(61)      [ALGB] (1) Real $FUN_1
(62)      [ALGB] (1) protected Real[1] volDyn.dynBal.mbC_flow
(63)      [ALGB] (1) protected Real[1] volDyn.dynBal.mCOut (min = {0.0 for $i1 in 1:1})
(64)      [ALGB] (1) Real[1] sou.medium.Xi (start = {0.01}, min = {0.0 for $i1 in 1:1}, max = {1.0 for $i1 in 1:1}, StateSelect = default)
(65)      [ALGB] (1) Real[1] volDyn.C = volDyn.COut_internal (start = {1.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, nominal = volDyn.C_nominal)
(66)      [ALGB] (1) flow Real[1] sou1.ports.m_flow (min = {-1e60}, max = {1e60})
(67)      [DISC] (2) Boolean[2] $SEV_4[$i1]
(68)      [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})
(69)      [ALGB] (1) protected Real[1] volDyn.XiOut_internal
(70)      [ALGB] (1) Real[1] volDyn.mC
(71)      [ALGB] (1) Real volSte.T = Annex60.Fluid.MixingVolumes.Validation.MixingVolumeTraceSubstanceReverseFlowPrescribedHeatFlowRate.volSte.Medium.temperature_phX(volSte.p, volSte.hOut_internal, {volSte.Xi[1], 1.0 - sum(volSte.Xi)}) (start = 293.15, min = 1.0, max = 1e4, nominal = 300.0)
(72)      [ALGB] (1) protected Real volDyn.dynBal.medium.state.p (start = 101325.0, min = 0.0, max = 1e8, nominal = 1e5)
(73)      [ALGB] (1) Real $FUN_18
(74)      [ALGB] (2) protected flow Real[2] volDyn.dynBal.ports.m_flow (min = {-1e5 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2})
(75)      [ALGB] (1) Real $FUN_17
(76)      [ALGB] (1) Real $FUN_15
(77)      [ALGB] (1) Real $FUN_12
(78)      [ALGB] (1) Real $FUN_11
(79)      [ALGB] (1) Real[1] sou1.medium.Xi (start = {0.01}, min = {0.0 for $i1 in 1:1}, max = {1.0 for $i1 in 1:1}, StateSelect = default)
(80)      [ALGB] (1) Real $FUN_10
(81)      [ALGB] (1) Real[1] volSte.C = volSte.COut_internal (start = {1.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, nominal = volSte.C_nominal)
(82)      [DISC] (1) Boolean $SEV_9
(83)      [ALGB] (1) stream Real[1, 1] sou.ports.C_outflow (start = {{1.0 for $i1 in 1:1}}, min = {{0.0 for $i1 in 1:1}})
(84)      [DISC] (1) Boolean $SEV_8
(85)      [ALGB] (1) protected Real bou.medium.X_steam (min = 0.0, max = 1.0, nominal = 0.1)
(86)      [DISC] (1) Boolean $SEV_7
(87)      [DISC] (1) Boolean $SEV_6
(88)      [ALGB] (1) protected Real[1] sou1.C_in_internal
(89)      [DER-] (1) Real $DER.volDyn.dynBal.U
(90)      [ALGB] (1) protected Real[1] volDyn.dynBal.C_flow_internal
(91)      [DISC] (1) Boolean $SEV_2
(92)      [ALGB] (2) protected Real[2] volDyn.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})
(93)      [ALGB] (1) protected Real volDyn.dynBal.medium.MM (min = 0.001, max = 0.25, nominal = 0.032)
(94)      [ALGB] (1) protected stream Real[1] volSte.steBal.port_b.C_outflow (start = {1.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1})
(95)      [ALGB] (1) protected Real[1] volDyn.dynBal.C_flow
(96)      [ALGB] (1) protected Real volDyn.dynBal.medium.state.T (start = 293.15, min = 1.0, max = 1e4, nominal = 300.0)
(97)      [ALGB] (1) protected Real[1] volDyn.dynBal.COut (min = {0.0 for $i1 in 1:1})
(98)      [ALGB] (1) protected Real sou1.medium.X_steam (min = 0.0, max = 1.0, nominal = 0.1)
(99)      [ALGB] (1) Real sou.medium.p_bar = Modelica.SIunits.Conversions.to_bar(99999.99999999999 * sou.medium.p_bar)
(100)     [ALGB] (1) Real sou.medium.R (start = 1000.0, min = 0.0, max = 1e7, nominal = 1000.0)
(101)     [ALGB] (2) stream Real[2, 1] volSte.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})
(102)     [ALGB] (1) protected stream Real[1] volSte.steBal.port_a.C_outflow (start = {1.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1})
(103)     [ALGB] (2) protected Real[2] volDyn.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})
(104)     [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})
(105)     [ALGB] (2) Real[2] sou.medium.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})
(106)     [ALGB] (1) protected stream Real volSte.steBal.port_b.h_outflow (start = 45300.945, min = -1e10, max = 1e10, nominal = 1e6)
(107)     [ALGB] (1) protected Real sou1.medium.X_air (min = 0.0, max = 1.0, nominal = 0.1)
(108)     [ALGB] (1) protected Real[1] volSte.COut_internal
(109)     [ALGB] (2) flow Real[2] bou.ports.m_flow (min = {-1e60 for $ports1 in 1:2}, max = {1e60 for $ports1 in 1:2})
(110)     [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}})
(111)     [ALGB] (1) protected Real volSte.hOut_internal
(112)     [DER-] (1) Real $DER.volDyn.dynBal.medium.p_bar
(113)     [ALGB] (1) protected Real[1] volSte.steBal.XiOut (min = {0.0 for $i1 in 1:1}, max = {1.0 for $i1 in 1:1})
(114)     [ALGB] (2) stream Real[2] volSte.ports.h_outflow (min = {-1e10 for $i1 in 1:2}, max = {1e10 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2})
(115)     [ALGB] (1) protected Real volSte.steBal.m_flowInv
(116)     [ALGB] (1) protected stream Real volSte.steBal.port_a.h_outflow (start = 45300.945, min = -1e10, max = 1e10, nominal = 1e6)
(117)     [ALGB] (1) Real[1] bou.medium.Xi (start = {0.01}, min = {0.0 for $i1 in 1:1}, max = {1.0 for $i1 in 1:1}, StateSelect = default)
(118)     [ALGB] (1) Real sou.medium.u (min = -1e8, max = 1e8, nominal = 1e6)
(119)     [ALGB] (2) protected Real[2] bou.X_in_internal
(120)     [ALGB] (1) protected Real[1] volSte.steBal.C_flow
(121)     [ALGB] (1) protected Real[1] volDyn.dynBal.XiOut (min = {0.0 for $i1 in 1:1}, max = {1.0 for $i1 in 1:1})
(122)     [ALGB] (1) Real[1] volDyn.C_flow
(123)     [DISC] (2) Boolean[2] $SEV_22[$i1]
(124)     [ALGB] (2) stream Real[2, 1] volDyn.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})
(125)     [ALGB] (1) protected Real[1] volSte.XiOut_internal
(126)     [ALGB] (1) Real[1] sou.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})
(127)     [ALGB] (2) protected Real[2] sou1.X_in_internal
(128)     [ALGB] (2) stream Real[2] bou.ports.h_outflow (min = {-1e10 for $i1 in 1:2}, max = {1e10 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2})
(129)     [ALGB] (1) protected stream Real[1] volSte.steBal.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})
(130)     [ALGB] (2) protected Real[2, 1] volDyn.dynBal.ports_mXi_flow
(131)     [ALGB] (1) Real sou1.medium.state.p (start = 101325.0, min = 0.0, max = 1e8, nominal = 1e5)
(132)     [DER-] (1) Real[1] $DER.volDyn.dynBal.mC
(133)     [ALGB] (1) Real sou.m_flow_in
(134)     [ALGB] (1) protected Real[1] volDyn.dynBal.mbXi_flow
(135)     [ALGB] (1) protected Real[1] sou.C_in_internal
(136)     [ALGB] (2) flow Real[2] volDyn.ports.m_flow (min = {-1e5 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2})
(137)     [ALGB] (1) Real sou.medium.MM (min = 0.001, max = 0.25, nominal = 0.032)
(138)     [ALGB] (1) Real bou.medium.R (start = 1000.0, min = 0.0, max = 1e7, nominal = 1000.0)
(139)     [ALGB] (1) protected Real volDyn.dynBal.mb_flow
(140)     [ALGB] (2) stream Real[2, 1] bou.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})
(141)     [ALGB] (1) protected Real[1] volDyn.COut_internal
(142)     [ALGB] (2) Real[2] sou1.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})
(143)     [ALGB] (2) Real[2] bou.medium.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})
(144)     [ALGB] (1) protected Real[1] volSte.steBal.mXi_flow
(145)     [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})
(146)     [DISC] (2) Boolean[2] $SEV_15[$i1]
(147)     [ALGB] (2) Real[2] sou.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})
(148)     [ALGB] (1) Real[1] volSte.Xi = volSte.XiOut_internal (min = {0.0 for $i1 in 1:1}, max = {1.0 for $i1 in 1:1})
(149)     [ALGB] (1) Real sou1.medium.MM (min = 0.001, max = 0.25, nominal = 0.032)
(150)     [ALGB] (2) protected Real[2] volDyn.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})
(151)     [ALGB] (1) protected Real volDyn.dynBal.medium.T_degC = Modelica.SIunits.Conversions.to_degC(-((-273.15) - volDyn.dynBal.medium.T_degC))
(152)     [ALGB] (1) Real sou1.medium.p_bar = Modelica.SIunits.Conversions.to_bar(99999.99999999999 * sou1.medium.p_bar)
(153)     [ALGB] (1) protected Real bou.medium.X_air (min = 0.0, max = 1.0, nominal = 0.1)
(154)     [ALGB] (1) protected Real[1] bou.C_in_internal
(155)     [ALGB] (1) Real[1] volDyn.Xi = volDyn.XiOut_internal (min = {0.0 for $i1 in 1:1}, max = {1.0 for $i1 in 1:1})
(156)     [ALGB] (2) Real[2] bou.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})


System Equations (173/194)
****************************
(1)       [ARRY] (1) volSte.steBal.C_flow = volSte.steBal.C_flow_internal ($RES_SIM_205)
(2)       [SCAL] (1) volDyn.dynBal.ports_H_flow[2] = $FUN_8 ($RES_SIM_80)
(3)       [ARRY] (2) bou.X_in_internal = bou.X ($RES_SIM_120)
(4)       [SCAL] (1) volDyn.dynBal.ports_mC_flow[1, 1] = $FUN_7 ($RES_SIM_81)
(5)       [SCAL] (1) volDyn.dynBal.ports_mXi_flow[1, 1] = $FUN_6 ($RES_SIM_82)
(6)       [ARRY] (1) volDyn.dynBal.C_flow = volDyn.C_flow ($RES_SIM_208)
(7)       [SCAL] (1) volDyn.dynBal.ports_H_flow[1] = $FUN_5 ($RES_SIM_83)
(8)       [ARRY] (1) volDyn.COut_internal = volDyn.dynBal.COut ($RES_SIM_209)
(9)       [ARRY] (1) volDyn.dynBal.COut = volDyn.dynBal.C ($RES_SIM_84)
(10)      [ARRY] (1) volDyn.dynBal.XiOut = volDyn.dynBal.medium.Xi ($RES_SIM_85)
(11)      [ARRY] (1) volDyn.dynBal.mC = 1.1843079200592153e-5 * (99999.99999999999 * volDyn.dynBal.medium.p_bar) * volDyn.dynBal.C ($RES_SIM_87)
(12)      [SCAL] (1) bou.medium.X[2] = 1.0 - $FUN_3 ($RES_SIM_127)
(13)      [SCAL] (1) volDyn.dynBal.U = (1.1843079200592153e-5 * (99999.99999999999 * volDyn.dynBal.medium.p_bar)) * volDyn.dynBal.medium.u ($RES_SIM_88)
(14)      [ARRY] (1) bou.medium.Xi = bou.medium.X[1:1] ($RES_SIM_128)
(15)      [ARRY] (1) volDyn.dynBal.mXi = 1.1843079200592153e-5 * (99999.99999999999 * volDyn.dynBal.medium.p_bar) * volDyn.dynBal.medium.Xi ($RES_SIM_89)
(16)      [ARRY] (2) bou.medium.state.X = bou.medium.X ($RES_SIM_129)
(17)      [FOR-] (2) ($RES_EVT_291)
(17)      [----] for $i1 in 1:2 loop
(17)      [----]   [SCAL] (1) $SEV_4[$i1] = sou1.medium.X[$i1] >= (-1e-5) and sou1.medium.X[$i1] <= 1.00001 ($RES_EVT_292)
(17)      [----] end for;
(18)      [SCAL] (1) $SEV_6 = volSte.steBal.m_flow > 0.001 * volSte.steBal.m_flow_small ($RES_EVT_294)
(19)      [SCAL] (1) $SEV_7 = volSte.steBal.m_flow < (-0.001 * volSte.steBal.m_flow_small) ($RES_EVT_295)
(20)      [ARRY] (1) sou1.ports.C_outflow = {sou1.C_in_internal} ($RES_SIM_11)
(21)      [SCAL] (1) $SEV_8 = 0.001 * volSte.steBal.m_flow_small > 0.0 ($RES_EVT_296)
(22)      [ARRY] (1) sou1.medium.Xi = sou1.X_in_internal[1:1] ($RES_SIM_12)
(23)      [ARRY] (1) volDyn.XiOut_internal = volDyn.dynBal.XiOut ($RES_SIM_210)
(24)      [SCAL] (1) $SEV_9 = abs(volSte.steBal.m_flow) < 1e-60 ($RES_EVT_297)
(25)      [ARRY] (1) volDyn.mC = volDyn.dynBal.mCOut ($RES_SIM_212)
(26)      [SCAL] (1) $SEV_11 = abs((volSte.steBal.Q_flow / volSte.steBal.cp_default) / volSte.steBal.m_flow) < 200.0 ($RES_EVT_299)
(27)      [ARRY] (1) sou1.C_in_internal = sou1.C ($RES_SIM_15)
(28)      [ARRY] (1) volDyn.mXi = volDyn.dynBal.mXiOut ($RES_SIM_214)
(29)      [ARRY] (2) sou1.X_in_internal = sou1.X ($RES_SIM_16)
(30)      [SCAL] (1) volDyn.dynBal.ports[2].h_outflow = volDyn.ports[2].h_outflow ($RES_SIM_216)
(31)      [SCAL] (1) volDyn.dynBal.ports[1].h_outflow = volDyn.ports[1].h_outflow ($RES_SIM_217)
(32)      [SCAL] (1) volDyn.dynBal.ports[2].Xi_outflow[1] = volDyn.ports[2].Xi_outflow[1] ($RES_SIM_218)
(33)      [SCAL] (1) volDyn.dynBal.ports[1].Xi_outflow[1] = volDyn.ports[1].Xi_outflow[1] ($RES_SIM_219)
(34)      [SCAL] (1) bou.medium.R = 287.0512249529787 * bou.medium.X_air + 461.5233290850878 * bou.medium.X_steam ($RES_SIM_134)
(35)      [SCAL] (1) volDyn.dynBal.medium.X[2] = 1.0 - $FUN_4 ($RES_SIM_95)
(36)      [SCAL] (1) -((-84437.5) - bou.medium.u) = 1006.0 * ((-273.15) + bou.T) * bou.medium.X_air + (2.5010145e6 + 1860.0 * ((-273.15) + bou.T)) * bou.medium.X_steam ($RES_SIM_135)
(37)      [ARRY] (1) volDyn.dynBal.medium.Xi = volDyn.dynBal.medium.X[1:1] ($RES_SIM_96)
(38)      [ARRY] (2) volDyn.dynBal.medium.state.X = volDyn.dynBal.medium.X ($RES_SIM_97)
(39)      [SCAL] (1) bou.medium.X_air = 1.0 - bou.medium.Xi[1] ($RES_SIM_137)
(40)      [SCAL] (1) volDyn.dynBal.medium.state.T = -((-273.15) - volDyn.dynBal.medium.T_degC) ($RES_SIM_98)
(41)      [SCAL] (1) bou.medium.X_steam = bou.medium.Xi[1] ($RES_SIM_138)
(42)      [SCAL] (1) volDyn.dynBal.medium.state.p = 99999.99999999999 * volDyn.dynBal.medium.p_bar ($RES_SIM_99)
(43)      [SCAL] (1) bou.medium.MM = 1/(55.508435061791985 * bou.medium.Xi[1] + 34.52428788658843 * (1.0 - bou.medium.Xi[1])) ($RES_SIM_139)
(44)      [SCAL] (1) $SEV_12 = volSte.steBal.m_flow > volSte.steBal.deltaReg or volSte.steBal.m_flow < (-volSte.steBal.deltaReg) ($RES_EVT_300)
(45)      [SCAL] (1) $SEV_13 = volSte.steBal.m_flow < 0.5 * volSte.steBal.deltaReg and volSte.steBal.m_flow > (-0.5 * volSte.steBal.deltaReg) ($RES_EVT_301)
(46)      [FOR-] (2) ($RES_EVT_303)
(46)      [----] for $i1 in 1:2 loop
(46)      [----]   [SCAL] (1) $SEV_15[$i1] = volDyn.dynBal.medium.X[$i1] >= (-1e-5) and volDyn.dynBal.medium.X[$i1] <= 1.00001 ($RES_EVT_304)
(46)      [----] end for;
(47)      [FOR-] (2) ($RES_EVT_307)
(47)      [----] for $i1 in 1:2 loop
(47)      [----]   [SCAL] (1) $SEV_18[$i1] = bou.medium.X[$i1] >= (-1e-5) and bou.medium.X[$i1] <= 1.00001 ($RES_EVT_308)
(47)      [----] end for;
(48)      [SCAL] (1) volDyn.dynBal.ports[2].C_outflow[1] = volDyn.ports[2].C_outflow[1] ($RES_SIM_220)
(49)      [SCAL] (1) sou1.medium.X[2] = 1.0 - $FUN_15 ($RES_SIM_22)
(50)      [SCAL] (1) volDyn.dynBal.ports[1].C_outflow[1] = volDyn.ports[1].C_outflow[1] ($RES_SIM_221)
(51)      [ARRY] (1) sou1.medium.Xi = sou1.medium.X[1:1] ($RES_SIM_23)
(52)      [FOR-] (2) ($RES_SIM_222)
(52)      [----] for $i1 in 1:2 loop
(52)      [----]   [SCAL] (1) volDyn.dynBal.ports[$i1].m_flow - volDyn.ports[$i1].m_flow = 0.0 ($RES_SIM_223)
(52)      [----] end for;
(53)      [ARRY] (2) sou1.medium.state.X = sou1.medium.X ($RES_SIM_24)
(54)      [ARRY] (2) volDyn.dynBal.ports.p = volDyn.ports.p ($RES_SIM_224)
(55)      [SCAL] (1) sou1.medium.state.p = 99999.99999999999 * sou1.medium.p_bar ($RES_SIM_26)
(56)      [ARRY] (1) volDyn.dynBal.C_flow = volDyn.dynBal.C_flow_internal ($RES_SIM_226)
(57)      [SCAL] (1) sou.ports[1].p = 99999.99999999999 * sou.medium.p_bar ($RES_SIM_141)
(58)      [SCAL] (1) sou1.medium.R = 287.0512249529787 * sou1.medium.X_air + 461.5233290850878 * sou1.medium.X_steam ($RES_SIM_29)
(59)      [SCAL] (1) sou.ports[1].h_outflow = -((-84437.5) - sou.medium.u) ($RES_SIM_142)
(60)      [ARRY] (1) sou.ports[1].Xi_outflow = sou.medium.Xi ($RES_SIM_143)
(61)      [SCAL] (1) $FUN_1 = sum(sou.medium.Xi) ($RES_$AUX_267)
(62)      [ARRY] (1) sou.ports.C_outflow = {sou.C_in_internal} ($RES_SIM_145)
(63)      [SCAL] (1) -sou.m_flow_in = sum(sou.ports.m_flow) ($RES_$AUX_266)
(64)      [ARRY] (1) sou.medium.Xi = sou.X_in_internal[1:1] ($RES_SIM_146)
(65)      [SCAL] (1) $FUN_3 = sum(bou.medium.Xi) ($RES_$AUX_265)
(66)      [SCAL] (1) $FUN_4 = sum(volDyn.dynBal.medium.Xi) ($RES_$AUX_264)
(67)      [SCAL] (1) $FUN_5 = semiLinear(volDyn.dynBal.ports[1].m_flow, sou.ports[1].h_outflow, volDyn.dynBal.ports[1].h_outflow) ($RES_$AUX_263)
(68)      [ARRY] (1) sou.C_in_internal = sou.C ($RES_SIM_149)
(69)      [SCAL] (1) $FUN_6 = semiLinear(volDyn.dynBal.ports[1].m_flow, sou.ports[1].Xi_outflow[1], volDyn.dynBal.ports[1].Xi_outflow[1]) ($RES_$AUX_262)
(70)      [SCAL] (1) $SEV_20 = abs(sum({abs(sou.ports[1].m_flow)}) - abs(sou.ports[1].m_flow)) <= 1e-60 ($RES_EVT_310)
(71)      [SCAL] (1) $FUN_7 = semiLinear(volDyn.dynBal.ports[1].m_flow, sou.ports[1].C_outflow[1], volDyn.dynBal.ports[1].C_outflow[1]) ($RES_$AUX_261)
(72)      [SCAL] (1) $FUN_8 = semiLinear(volDyn.dynBal.ports[2].m_flow, bou.ports[2].h_outflow, volDyn.dynBal.ports[2].h_outflow) ($RES_$AUX_260)
(73)      [FOR-] (2) ($RES_EVT_312)
(73)      [----] for $i1 in 1:2 loop
(73)      [----]   [SCAL] (1) $SEV_22[$i1] = sou.medium.X[$i1] >= (-1e-5) and sou.medium.X[$i1] <= 1.00001 ($RES_EVT_313)
(73)      [----] end for;
(74)      [SCAL] (1) -((-84437.5) - sou1.medium.u) = 1006.0 * ((-273.15) + sou1.T) * sou1.medium.X_air + (2.5010145e6 + 1860.0 * ((-273.15) + sou1.T)) * sou1.medium.X_steam ($RES_SIM_30)
(75)      [SCAL] (1) sou1.medium.X_air = 1.0 - sou1.medium.Xi[1] ($RES_SIM_32)
(76)      [SCAL] (1) sou1.medium.X_steam = sou1.medium.Xi[1] ($RES_SIM_33)
(77)      [SCAL] (1) sou1.medium.MM = 1/(55.508435061791985 * sou1.medium.Xi[1] + 34.52428788658843 * (1.0 - sou1.medium.Xi[1])) ($RES_SIM_34)
(78)      [SCAL] (1) gain.y = gain.k * sou.m_flow_in ($RES_SIM_36)
(79)      [ARRY] (2) sou.X_in_internal = sou.X ($RES_SIM_150)
(80)      [SCAL] (1) $FUN_9 = semiLinear(volDyn.dynBal.ports[2].m_flow, bou.ports[2].Xi_outflow[1], volDyn.dynBal.ports[2].Xi_outflow[1]) ($RES_$AUX_259)
(81)      [SCAL] (1) $FUN_10 = semiLinear(volDyn.dynBal.ports[2].m_flow, bou.ports[2].C_outflow[1], volDyn.dynBal.ports[2].C_outflow[1]) ($RES_$AUX_258)
(82)      [SCAL] (1) $FUN_11 = sum(volDyn.dynBal.ports_mXi_flow[:, 1]) ($RES_$AUX_257)
(83)      [SCAL] (1) $FUN_12 = sum(volDyn.dynBal.ports_mC_flow[:, 1]) ($RES_$AUX_256)
(84)      [SCAL] (1) sou.medium.X[2] = 1.0 - $FUN_1 ($RES_SIM_156)
(85)      [SCAL] (1) volDyn.dynBal.mb_flow = sum(volDyn.dynBal.ports.m_flow) ($RES_$AUX_255)
(86)      [ARRY] (1) sou.medium.Xi = sou.medium.X[1:1] ($RES_SIM_157)
(87)      [SCAL] (1) volDyn.dynBal.Hb_flow = sum(volDyn.dynBal.ports_H_flow) ($RES_$AUX_254)
(88)      [ARRY] (2) sou.medium.state.X = sou.medium.X ($RES_SIM_158)
(89)      [SCAL] (1) $FUN_15 = sum(sou1.medium.Xi) ($RES_$AUX_253)
(90)      [SCAL] (1) -sou.m_flow_in = sum(sou1.ports.m_flow) ($RES_$AUX_252)
(91)      [SCAL] (1) $FUN_17 = sum(volSte.Xi) ($RES_$AUX_251)
(92)      [SCAL] (1) $FUN_18 = sum(volDyn.Xi) ($RES_$AUX_250)
(93)      [ARRY] (1) volSte.steBal.port_a.C_outflow = {bou.ports[1].C_outflow[1]} - volSte.steBal.C_flow_internal .* volSte.steBal.m_flowInv ($RES_SIM_43)
(94)      [ARRY] (1) volSte.steBal.port_b.C_outflow = {sou1.ports[1].C_outflow[1]} + volSte.steBal.C_flow_internal .* volSte.steBal.m_flowInv ($RES_SIM_44)
(95)      [SCAL] (1) volSte.steBal.port_a.h_outflow = bou.ports[1].h_outflow ($RES_SIM_45)
(96)      [SCAL] (1) volSte.steBal.port_b.h_outflow = sou1.ports[1].h_outflow ($RES_SIM_46)
(97)      [ARRY] (1) volSte.steBal.port_a.Xi_outflow = {bou.ports[1].Xi_outflow[1]} - volSte.steBal.mXi_flow .* volSte.steBal.m_flowInv ($RES_SIM_47)
(98)      [SCAL] (1) sou.medium.state.p = 99999.99999999999 * sou.medium.p_bar ($RES_SIM_160)
(99)      [ARRY] (1) volSte.steBal.port_b.Xi_outflow = {sou1.ports[1].Xi_outflow[1]} + volSte.steBal.mXi_flow .* volSte.steBal.m_flowInv ($RES_SIM_48)
(100)     [SCAL] (1) sou.medium.R = 287.0512249529787 * sou.medium.X_air + 461.5233290850878 * sou.medium.X_steam ($RES_SIM_163)
(101)     [SCAL] (1) -((-84437.5) - sou.medium.u) = 1006.0 * ((-273.15) + sou.T) * sou.medium.X_air + (2.5010145e6 + 1860.0 * ((-273.15) + sou.T)) * sou.medium.X_steam ($RES_SIM_164)
(102)     [SCAL] (1) sou.medium.X_air = 1.0 - sou.medium.Xi[1] ($RES_SIM_166)
(103)     [SCAL] (1) sou.medium.X_steam = sou.medium.Xi[1] ($RES_SIM_167)
(104)     [SCAL] (1) sou.medium.MM = 1/(55.508435061791985 * sou.medium.Xi[1] + 34.52428788658843 * (1.0 - sou.medium.Xi[1])) ($RES_SIM_168)
(105)     [ARRY] (1) volSte.steBal.COut = {smooth(1, if $SEV_6 then volSte.steBal.port_b.C_outflow[1] else if $SEV_7 then volSte.steBal.port_a.C_outflow[1] else if $SEV_8 then 0.25 * (volSte.steBal.port_a.C_outflow[1] - volSte.steBal.port_b.C_outflow[1]) * ((-3.0) + (volSte.steBal.m_flow / (0.001 * volSte.steBal.m_flow_small)) ^ 2.0) * ((1000.0 * volSte.steBal.m_flow) / volSte.steBal.m_flow_small) + 0.5 * (volSte.steBal.port_b.C_outflow[1] + volSte.steBal.port_a.C_outflow[1]) else 0.5 * (volSte.steBal.port_b.C_outflow[1] + volSte.steBal.port_a.C_outflow[1]))} ($RES_SIM_50)
(106)     [ARRY] (1) volSte.steBal.XiOut = {smooth(1, if $SEV_6 then volSte.steBal.port_b.Xi_outflow[1] else if $SEV_7 then volSte.steBal.port_a.Xi_outflow[1] else if $SEV_8 then 0.25 * (volSte.steBal.port_a.Xi_outflow[1] - volSte.steBal.port_b.Xi_outflow[1]) * ((-3.0) + (volSte.steBal.m_flow / (0.001 * volSte.steBal.m_flow_small)) ^ 2.0) * ((1000.0 * volSte.steBal.m_flow) / volSte.steBal.m_flow_small) + 0.5 * (volSte.steBal.port_b.Xi_outflow[1] + volSte.steBal.port_a.Xi_outflow[1]) else 0.5 * (volSte.steBal.port_b.Xi_outflow[1] + volSte.steBal.port_a.Xi_outflow[1]))} ($RES_SIM_51)
(107)     [SCAL] (1) volSte.hOut_internal = smooth(1, if $SEV_6 then volSte.steBal.port_b.h_outflow else if $SEV_7 then volSte.steBal.port_a.h_outflow else if $SEV_8 then 0.25 * (volSte.steBal.port_a.h_outflow - volSte.steBal.port_b.h_outflow) * ((-3.0) + (volSte.steBal.m_flow / (0.001 * volSte.steBal.m_flow_small)) ^ 2.0) * ((1000.0 * volSte.steBal.m_flow) / volSte.steBal.m_flow_small) + 0.5 * (volSte.steBal.port_b.h_outflow + volSte.steBal.port_a.h_outflow) else 0.5 * (volSte.steBal.port_b.h_outflow + volSte.steBal.port_a.h_outflow)) ($RES_SIM_52)
(108)     [ARRY] (1) sou1.ports[1].Xi_outflow = sou1.medium.Xi ($RES_SIM_9)
(109)     [SCAL] (1) volSte.steBal.m_flowInv = if $SEV_12 then 1/volSte.steBal.m_flow else if $SEV_13 then volSte.steBal.m_flow / (volSte.steBal.deltaReg * volSte.steBal.deltaReg) else Annex60.Utilities.Math.Functions.BaseClasses.smoothTransition(volSte.steBal.m_flow, volSte.steBal.deltaReg, volSte.steBal.deltaInvReg, volSte.steBal.aReg, volSte.steBal.bReg, volSte.steBal.cReg, volSte.steBal.dReg, volSte.steBal.eReg, volSte.steBal.fReg) ($RES_SIM_54)
(110)     [ARRY] (1) volSte.steBal.mXi_flow = 0.0 ($RES_SIM_55)
(111)     [SCAL] (1) sou1.ports[1].h_outflow = -((-84437.5) - sou1.medium.u) ($RES_SIM_8)
(112)     [SCAL] (1) sou1.ports[1].p = 99999.99999999999 * sou1.medium.p_bar ($RES_SIM_7)
(113)     [SCAL] (1) sou.m_flow_in = m_flow.offset + (if $TEV_0 then 0.0 else if $TEV_1 then (m_flow.height * (time - m_flow.startTime)) / m_flow.duration else m_flow.height) ($RES_SIM_6)
(114)     [ARRY] (1) volDyn.dynBal.mCOut = volDyn.dynBal.mC ($RES_SIM_58)
(115)     [SCAL] (1) -(volSte.ports[2].m_flow + volSte.steBal.m_flow) = 0.0 ($RES_SIM_171)
(116)     [SCAL] (1) volSte.steBal.m_flow - volSte.ports[1].m_flow = 0.0 ($RES_SIM_172)
(117)     [SCAL] (1) volSte.ports[2].m_flow + bou.ports[1].m_flow = 0.0 ($RES_SIM_174)
(118)     [SCAL] (1) volDyn.ports[2].m_flow + bou.ports[2].m_flow = 0.0 ($RES_SIM_177)
(119)     [SCAL] (1) volDyn.T = 273.15 + (-(2.5010145e6 * volDyn.Xi[1] + ((-84437.5) - volDyn.dynBal.medium.u))) / (1006.0 * (1.0 - volDyn.Xi[1]) + 1860.0 * volDyn.Xi[1]) ($RES_BND_232)
(120)     [SCAL] (1) volDyn.p = volDyn.ports[1].p ($RES_BND_233)
(121)     [ARRY] (1) volDyn.Xi = volDyn.XiOut_internal ($RES_BND_234)
(122)     [ARRY] (1) volDyn.C = volDyn.COut_internal ($RES_BND_235)
(123)     [ARRY] (1) volDyn.dynBal.mXiOut = volDyn.dynBal.mXi ($RES_SIM_60)
(124)     [FOR-] (2) ($RES_SIM_62)
(124)     [----] for $i1 in 1:2 loop
(124)     [----]   [SCAL] (1) volDyn.dynBal.ports[$i1].p = 99999.99999999999 * volDyn.dynBal.medium.p_bar ($RES_SIM_63)
(124)     [----] end for;
(125)     [SCAL] (1) volDyn.dynBal.medium.R = 287.0512249529787 * volDyn.dynBal.medium.X_air + 461.5233290850878 * volDyn.dynBal.medium.X_steam ($RES_SIM_102)
(126)     [SCAL] (1) -((-84437.5) - volDyn.dynBal.medium.u) = 1006.0 * ((-273.15) - ((-273.15) - volDyn.dynBal.medium.T_degC)) * volDyn.dynBal.medium.X_air + (2.5010145e6 + 1860.0 * ((-273.15) - ((-273.15) - volDyn.dynBal.medium.T_degC))) * volDyn.dynBal.medium.X_steam ($RES_SIM_103)
(127)     [FOR-] (2) ($RES_SIM_64)
(127)     [----] for $i1 in 1:2 loop
(127)     [----]   [SCAL] (1) volDyn.dynBal.ports[$i1].h_outflow = -((-84437.5) - volDyn.dynBal.medium.u) ($RES_SIM_65)
(127)     [----] end for;
(128)     [SCAL] (1) volDyn.dynBal.medium.X_air = 1.0 - volDyn.dynBal.medium.Xi[1] ($RES_SIM_105)
(129)     [FOR-] (2) ($RES_SIM_66)
(129)     [----] for $i1 in 1:2 loop
(129)     [----]   [ARRY] (1) volDyn.dynBal.ports[$i1].Xi_outflow = volDyn.dynBal.medium.Xi ($RES_SIM_67)
(129)     [----] end for;
(130)     [SCAL] (1) volDyn.dynBal.medium.X_steam = volDyn.dynBal.medium.Xi[1] ($RES_SIM_106)
(131)     [SCAL] (1) volDyn.dynBal.medium.MM = 1/(55.508435061791985 * volDyn.dynBal.medium.Xi[1] + 34.52428788658843 * (1.0 - volDyn.dynBal.medium.Xi[1])) ($RES_SIM_107)
(132)     [FOR-] (2) ($RES_SIM_68)
(132)     [----] for $i1 in 1:2 loop
(132)     [----]   [ARRY] (1) volDyn.dynBal.ports[$i1].C_outflow = volDyn.dynBal.C ($RES_SIM_69)
(132)     [----] end for;
(133)     [SCAL] (1) volDyn.ports[2].p = bou.ports[2].p ($RES_SIM_181)
(134)     [SCAL] (1) volSte.ports[2].p = bou.ports[1].p ($RES_SIM_182)
(135)     [FOR-] (2) ($RES_SIM_109)
(135)     [----] for $i1 in 1:2 loop
(135)     [----]   [SCAL] (1) bou.ports[$i1].p = bou.p ($RES_SIM_110)
(135)     [----] end for;
(136)     [SCAL] (1) volSte.ports[1].m_flow + sou1.ports[1].m_flow = 0.0 ($RES_SIM_183)
(137)     [SCAL] (1) sou1.ports[1].p = volSte.ports[1].p ($RES_SIM_184)
(138)     [SCAL] (1) volDyn.ports[1].m_flow + sou.ports[1].m_flow = 0.0 ($RES_SIM_185)
(139)     [SCAL] (1) sou.ports[1].p = volDyn.ports[1].p ($RES_SIM_186)
(140)     [SCAL] (1) gain.y = volSte.C_flow[1] ($RES_SIM_187)
(141)     [SCAL] (1) gain.y = volDyn.C_flow[1] ($RES_SIM_188)
(142)     [SCAL] (1) volSte.T = 273.15 + (volSte.hOut_internal - 2.5010145e6 * volSte.Xi[1]) / (1006.0 * (1.0 - volSte.Xi[1]) + 1860.0 * volSte.Xi[1]) ($RES_BND_240)
(143)     [SCAL] (1) volSte.p = volSte.ports[1].p ($RES_BND_241)
(144)     [ARRY] (1) volSte.Xi = volSte.XiOut_internal ($RES_BND_242)
(145)     [ARRY] (1) volSte.C = volSte.COut_internal ($RES_BND_243)
(146)     [SCAL] (1) volSte.steBal.dp = volSte.steBal.port_a.p - volSte.steBal.port_a.p ($RES_BND_245)
(147)     [ARRY] (1) $DER.volDyn.dynBal.mC = volDyn.dynBal.mbC_flow + volDyn.dynBal.C_flow_internal ($RES_SIM_70)
(148)     [ARRY] (1) $DER.volDyn.dynBal.mXi = volDyn.dynBal.mbXi_flow ($RES_SIM_71)
(149)     [FOR-] (2) ($RES_SIM_111)
(149)     [----] for $i1 in 1:2 loop
(149)     [----]   [SCAL] (1) bou.ports[$i1].h_outflow = -((-84437.5) - bou.medium.u) ($RES_SIM_112)
(149)     [----] end for;
(150)     [SCAL] (1) 1.1843079200592153e-5 * (99999.99999999999 * $DER.volDyn.dynBal.medium.p_bar) = volDyn.dynBal.mb_flow ($RES_SIM_72)
(151)     [SCAL] (1) $DER.volDyn.dynBal.U = volDyn.dynBal.Hb_flow ($RES_SIM_73)
(152)     [FOR-] (2) ($RES_SIM_113)
(152)     [----] for $i1 in 1:2 loop
(152)     [----]   [ARRY] (1) bou.ports[$i1].Xi_outflow = bou.medium.Xi ($RES_SIM_114)
(152)     [----] end for;
(153)     [ARRY] (2) bou.ports.C_outflow = {bou.C_in_internal for $i1 in 1:2} ($RES_SIM_115)
(154)     [SCAL] (1) volDyn.dynBal.mbC_flow[1] = $FUN_12 ($RES_SIM_76)
(155)     [ARRY] (1) bou.medium.Xi = bou.X_in_internal[1:1] ($RES_SIM_116)
(156)     [SCAL] (1) volDyn.dynBal.mbXi_flow[1] = $FUN_11 ($RES_SIM_77)
(157)     [SCAL] (1) volDyn.dynBal.ports_mC_flow[2, 1] = $FUN_10 ($RES_SIM_78)
(158)     [SCAL] (1) volDyn.dynBal.ports_mXi_flow[2, 1] = $FUN_9 ($RES_SIM_79)
(159)     [ARRY] (1) volSte.steBal.C_flow = volSte.C_flow ($RES_SIM_192)
(160)     [ARRY] (1) bou.C_in_internal = bou.C ($RES_SIM_119)
(161)     [ARRY] (1) volSte.COut_internal = volSte.steBal.COut ($RES_SIM_193)
(162)     [ARRY] (1) volSte.XiOut_internal = volSte.steBal.XiOut ($RES_SIM_194)
(163)     [SCAL] (1) volSte.steBal.port_b.h_outflow = volSte.ports[2].h_outflow ($RES_SIM_196)
(164)     [SCAL] (1) volSte.steBal.port_b.Xi_outflow[1] = volSte.ports[2].Xi_outflow[1] ($RES_SIM_197)
(165)     [SCAL] (1) volSte.steBal.port_b.C_outflow[1] = volSte.ports[2].C_outflow[1] ($RES_SIM_198)
(166)     [SCAL] (1) volSte.steBal.port_a.p = volSte.ports[2].p ($RES_SIM_199)
(167)     [SCAL] (1) $TEV_0 = time < m_flow.startTime ($RES_EVT_285)
(168)     [SCAL] (1) $TEV_1 = time < (m_flow.startTime + m_flow.duration) ($RES_EVT_286)
(169)     [SCAL] (1) volSte.steBal.port_a.h_outflow = volSte.ports[1].h_outflow ($RES_SIM_200)
(170)     [SCAL] (1) volSte.steBal.port_a.Xi_outflow[1] = volSte.ports[1].Xi_outflow[1] ($RES_SIM_201)
(171)     [SCAL] (1) volSte.steBal.port_a.C_outflow[1] = volSte.ports[1].C_outflow[1] ($RES_SIM_202)
(172)     [SCAL] (1) $SEV_2 = abs(sum({abs(sou1.ports[1].m_flow)}) - abs(sou1.ports[1].m_flow)) <= 1e-60 ($RES_EVT_289)
(173)     [SCAL] (1) volSte.steBal.port_a.p = volSte.ports[1].p ($RES_SIM_203)