Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.PhaseSeperator.conf.json loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo): time 0.002147/0.002147, allocations: 100.4 kB / 19.76 MB, free: 1.906 MB / 14.72 MB " [Timeout remaining time 180] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo): time 0.002513/0.002513, allocations: 221.5 kB / 23.07 MB, free: 4.984 MB / 14.72 MB " [Timeout remaining time 180] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo): time 1.519/1.519, allocations: 230.7 MB / 256.9 MB, free: 7.762 MB / 206.1 MB " [Timeout remaining time 178] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo): time 0.9619/0.9619, allocations: 100.9 MB / 414.2 MB, free: 2.844 MB / 318.1 MB " [Timeout remaining time 179] Using package ThermofluidStream with version 1.2.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo) Using package Modelica with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo) Using package Complex with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo) Using package ModelicaServices with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo) Running command: translateModel(ThermofluidStream.Boundaries.Tests.PhaseSeperator,tolerance=1e-06,outputFormat="mat",numberOfIntervals=1000,variableFilter="Time|accumulator.M|accumulator.U_med|accumulator.m_flow_in|accumulator.m_flow_out|receiver.M|receiver.U_med|receiver.m_flow_out|source.outlet.m_flow|timeTable.a|timeTable.b|timeTable.last|timeTable.nextEvent|timeTable.nextEventScaled",fileNamePrefix="ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.PhaseSeperator") translateModel(ThermofluidStream.Boundaries.Tests.PhaseSeperator,tolerance=1e-06,outputFormat="mat",numberOfIntervals=1000,variableFilter="Time|accumulator.M|accumulator.U_med|accumulator.m_flow_in|accumulator.m_flow_out|receiver.M|receiver.U_med|receiver.m_flow_out|source.outlet.m_flow|timeTable.a|timeTable.b|timeTable.last|timeTable.nextEvent|timeTable.nextEventScaled",fileNamePrefix="ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.PhaseSeperator") [Timeout 660] "Notification: Performance of FrontEnd - Absyn->SCode: time 2.044e-05/2.044e-05, allocations: 2.281 kB / 0.5654 GB, free: 35.26 MB / 446.1 MB Notification: Performance of NFInst.instantiate(ThermofluidStream.Boundaries.Tests.PhaseSeperator): time 0.1073/0.1073, allocations: 100.7 MB / 0.6637 GB, free: 11.67 MB / 0.4981 GB Notification: Performance of NFInst.instExpressions: time 0.1152/0.2225, allocations: 80.4 MB / 0.7422 GB, free: 11.01 MB / 0.5762 GB Notification: Performance of NFInst.updateImplicitVariability: time 0.003299/0.2258, allocations: 95.06 kB / 0.7423 GB, free: 10.91 MB / 0.5762 GB Notification: Performance of NFTyping.typeComponents: time 0.005064/0.2309, allocations: 1.223 MB / 0.7435 GB, free: 9.684 MB / 0.5762 GB Notification: Performance of NFTyping.typeBindings: time 0.01764/0.2485, allocations: 3.768 MB / 0.7472 GB, free: 5.906 MB / 0.5762 GB Notification: Performance of NFTyping.typeClassSections: time 0.5138/0.7623, allocations: 10.3 MB / 0.7573 GB, free: 10.73 MB / 0.5762 GB Notification: Performance of NFFlatten.flatten: time 0.009421/0.7717, allocations: 4.154 MB / 0.7613 GB, free: 10.71 MB / 0.5762 GB Notification: Performance of NFFlatten.resolveConnections: time 0.001544/0.7733, allocations: 400.3 kB / 0.7617 GB, free: 10.63 MB / 0.5762 GB Notification: Performance of NFEvalConstants.evaluate: time 0.01538/0.7887, allocations: 5.121 MB / 0.7667 GB, free: 9.691 MB / 0.5762 GB Notification: Performance of NFSimplifyModel.simplify: time 0.004394/0.7931, allocations: 1.305 MB / 0.768 GB, free: 9.691 MB / 0.5762 GB Notification: Performance of NFPackage.collectConstants: time 0.001079/0.7941, allocations: 210.2 kB / 0.7682 GB, free: 9.691 MB / 0.5762 GB Notification: Performance of NFFlatten.collectFunctions: time 0.03041/0.8245, allocations: 9.614 MB / 0.7776 GB, free: 9.676 MB / 0.5762 GB Notification: Performance of combineBinaries: time 0.009552/0.8341, allocations: 6.45 MB / 0.7839 GB, free: 7.625 MB / 0.5762 GB Notification: Performance of replaceArrayConstructors: time 0.00331/0.8374, allocations: 3.212 MB / 0.787 GB, free: 5.715 MB / 0.5762 GB Notification: Performance of NFVerifyModel.verify: time 0.001206/0.8386, allocations: 224.1 kB / 0.7872 GB, free: 5.715 MB / 0.5762 GB Notification: Performance of FrontEnd: time 0.0006322/0.8392, allocations: 170 kB / 0.7874 GB, free: 5.695 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: 417 (365) * Number of variables: 421 (421) Notification: Performance of [SIM] Bindings: time 0.0139/0.8531, allocations: 12.53 MB / 0.7996 GB, free: 0.8281 MB / 0.5762 GB Notification: Performance of [SIM] FunctionAlias: time 0.002104/0.8552, allocations: 1.353 MB / 0.8009 GB, free: 0.6133 MB / 0.5762 GB Notification: Performance of [SIM] Early Inline: time 0.007624/0.8629, allocations: 6.104 MB / 0.8069 GB, free: 452 kB / 0.5762 GB Notification: Performance of [SIM] Simplify 1: time 0.002388/0.8653, allocations: 0.7576 MB / 0.8076 GB, free: 188 kB / 0.5762 GB Warning: NBAlias.setStartFixed: Alias set with conflicting unfixed start values detected. Use -d=dumprepl for more information. Notification: Performance of [SIM] Alias: time 0.01304/0.8783, allocations: 6.629 MB / 0.8141 GB, free: 14.41 MB / 0.5919 GB Notification: Performance of [SIM] Simplify 2: time 0.001548/0.8798, allocations: 0.6915 MB / 0.8148 GB, free: 14.12 MB / 0.5919 GB Notification: Performance of [SIM] Remove Stream: time 0.0007145/0.8806, allocations: 0.4983 MB / 0.8153 GB, free: 13.97 MB / 0.5919 GB Notification: Performance of [SIM] Detect States: time 0.001758/0.8823, allocations: 1.277 MB / 0.8165 GB, free: 13.69 MB / 0.5919 GB Notification: Performance of [SIM] Events: time 0.0007596/0.8831, allocations: 403.6 kB / 0.8169 GB, free: 13.54 MB / 0.5919 GB Notification: Performance of [SIM] Partitioning: time 0.002682/0.8858, allocations: 2.061 MB / 0.8189 GB, free: 13.36 MB / 0.5919 GB Error: Internal error NBSorting.tarjan failed to sort system: System Variables (344/344) **************************** (1|1) [DISC] (1) protected discrete Real timeTable.nextEvent (fixed = true, start = 0.0) (2|2) [ALGB] (1) protected Real accumulator.r_damping = accumulator.d * der(accumulator.M) (3|3) [ALGB] (1) protected Real receiver.h_pipe (4|4) [ALGB] (1) input Real twoPhaseSensorSelect.inlet.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (5|5) [ALGB] (1) protected Real sink1.p = ThermofluidStream.Boundaries.Tests.PhaseSeperator.sink1.Medium.pressure(sink1.inlet.state) (6|6) [ALGB] (1) protected Real flowResistance.p_out (7|7) [DISC] (1) protected Integer accumulator.state_in.phase (min = 0, max = 2) (8|8) [ALGB] (1) output Real flowResistance1.outlet.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (9|9) [ALGB] (1) output Real flowResistance2.outlet.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (10|10) [ALGB] (1) output Real flowResistance3.outlet.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (11|11) [ALGB] (1) input Real flowResistance1.inlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (12|12) [ALGB] (1) input Real flowResistance2.inlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (13|13) [ALGB] (1) input Real flowResistance3.inlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (14|14) [DER-] (1) Real $DER.flowResistance.dp (15|15) [ALGB] (1) protected Real receiver.state_in.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (16|16) [ALGB] (1) input Real sink1.inlet.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (17|17) [DDER] (1) Real $DER.accumulator.m_flow_in (StateSelect = avoid) (18|18) [ALGB] (1) Real accumulator.medium.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (19|19) [DISC] (1) input Integer flowResistance3.inlet.state.phase (min = 0, max = 2) (20|20) [DISC] (1) input Integer flowResistance2.inlet.state.phase (min = 0, max = 2) (21|21) [DISC] (1) input Integer flowResistance1.inlet.state.phase (min = 0, max = 2) (22|22) [DER-] (1) Real $DER.flowResistance2.dp (23|23) [ALGB] (1) Real receiver.medium.sat.psat (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (24|24) [ALGB] (1) protected Real accumulator.p_in = ThermofluidStream.Boundaries.Tests.PhaseSeperator.accumulator.Medium.pressure(accumulator.state_in) (25|25) [ALGB] (1) protected Real flowResistance1.p_in = ThermofluidStream.Boundaries.Tests.PhaseSeperator.flowResistance1.Medium.pressure(flowResistance1.inlet.state) (26|26) [ALGB] (1) input Real sink1.inlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (27|27) [ALGB] (1) protected Real flowResistance2.p_in = ThermofluidStream.Boundaries.Tests.PhaseSeperator.flowResistance2.Medium.pressure(flowResistance2.inlet.state) (28|28) [ALGB] (1) protected Real flowResistance3.p_in = ThermofluidStream.Boundaries.Tests.PhaseSeperator.flowResistance3.Medium.pressure(flowResistance3.inlet.state) (29|29) [ALGB] (1) protected Real accumulator.d_liq = ThermofluidStream.Boundaries.Tests.PhaseSeperator.accumulator.Medium.bubbleDensity(ThermofluidStream.Boundaries.Tests.PhaseSeperator.accumulator.Medium.setSat_p(99999.99999999999 * accumulator.medium.p_bar)) (min = 0.0) (30|30) [DISC] (1) protected Integer receiver.state_out.phase (min = 0, max = 2) (31|31) [DISC] (1) output Integer source.outlet.state.phase (min = 0, max = 2) (32|32) [ALGB] (1) input Real twoPhaseSensorSelect1.inlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (33|33) [ALGB] (1) protected Real flowResistance3.rho_in = max(flowResistance3.rho_min, ThermofluidStream.Boundaries.Tests.PhaseSeperator.flowResistance3.Medium.density(flowResistance3.inlet.state)) (min = 0.0) (34|34) [ALGB] (1) input Real twoPhaseSensorSelect2.inlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (35|35) [ALGB] (1) protected Real flowResistance2.rho_in = max(flowResistance2.rho_min, ThermofluidStream.Boundaries.Tests.PhaseSeperator.flowResistance2.Medium.density(flowResistance2.inlet.state)) (min = 0.0) (36|36) [ALGB] (1) input Real twoPhaseSensorSelect3.inlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (37|37) [ALGB] (1) protected Real flowResistance1.rho_in = max(flowResistance1.rho_min, ThermofluidStream.Boundaries.Tests.PhaseSeperator.flowResistance1.Medium.density(flowResistance1.inlet.state)) (min = 0.0) (38|38) [DISC] (1) output Integer accumulator.outlet.state.phase = accumulator.state_out.phase (min = 0, max = 2) (39|39) [ALGB] (1) protected Real flowResistance3.mu_in = ThermofluidStream.Boundaries.Tests.PhaseSeperator.flowResistance3.Medium.dynamicViscosity(flowResistance3.inlet.state) (min = 0.0) (40|40) [ALGB] (1) input Real twoPhaseSensorSelect4.inlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (41|41) [ALGB] (1) protected Real flowResistance2.mu_in = ThermofluidStream.Boundaries.Tests.PhaseSeperator.flowResistance2.Medium.dynamicViscosity(flowResistance2.inlet.state) (min = 0.0) (42|42) [ALGB] (1) input Real twoPhaseSensorSelect5.inlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (43|43) [ALGB] (1) input Real accumulator.inlet.state.d = accumulator.state_in.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (44|44) [ALGB] (1) protected Real flowResistance1.mu_in = ThermofluidStream.Boundaries.Tests.PhaseSeperator.flowResistance1.Medium.dynamicViscosity(flowResistance1.inlet.state) (min = 0.0) (45|45) [ALGB] (1) input Real twoPhaseSensorSelect6.inlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (46|46) [ALGB] (1) input Real twoPhaseSensorSelect7.inlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (47|47) [ALGB] (1) input Real sink1.inlet.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (48|48) [ALGB] (1) protected Real accumulator.h_dew = ThermofluidStream.Boundaries.Tests.PhaseSeperator.accumulator.Medium.dewEnthalpy(ThermofluidStream.Boundaries.Tests.PhaseSeperator.accumulator.Medium.setSat_p(99999.99999999999 * accumulator.medium.p_bar)) + 1.0 (49|49) [ALGB] (1) input Real flowResistance3.inlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (50|50) [ALGB] (1) input Real flowResistance2.inlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (51|51) [ALGB] (1) input Real flowResistance1.inlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (52|52) [ALGB] (1) Real source.outlet.r (53|53) [ALGB] (1) Real receiver.medium.h (StateSelect = default) (54|54) [ALGB] (1) Real receiver.medium.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (55|55) [DDER] (1) flow Real $DER.source.outlet.m_flow (StateSelect = avoid) (56|56) [DISC] (1) input Integer sink.inlet.state.phase (min = 0, max = 2) (57|57) [ALGB] (1) Real singleSensorSelect.value (58|58) [ALGB] (1) protected Real sink1.r (59|59) [ALGB] (1) input Real flowResistance3.inlet.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (60|60) [ALGB] (1) Real accumulator.medium.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (61|61) [ALGB] (1) input Real flowResistance2.inlet.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (62|62) [ALGB] (1) protected Real accumulator.h_out = if noEvent((-accumulator.m_flow_out) >= 0.0) then ThermofluidStream.Boundaries.Tests.PhaseSeperator.accumulator.Medium.specificEnthalpy(accumulator.state_out) else accumulator.medium.h (63|63) [ALGB] (1) input Real flowResistance1.inlet.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (64|64) [ALGB] (1) Real receiver.medium.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0, StateSelect = default) (65|65) [ALGB] (1) Real accumulator.liquid_level (66|66) [ALGB] (1) Real accumulator.medium.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (67|67) [ALGB] (1) protected Real accumulator.h_in = if noEvent(accumulator.m_flow_in >= 0.0) then ThermofluidStream.Boundaries.Tests.PhaseSeperator.accumulator.Medium.specificEnthalpy(accumulator.state_in) else accumulator.medium.h (68|68) [ALGB] (1) input Real sink1.inlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (69|69) [ALGB] (1) Real sink1.inlet.r (70|70) [DISC] (1) input Integer receiver.inlet.state.phase = receiver.state_in.phase (min = 0, max = 2) (71|71) [ALGB] (1) Real sink.inlet.r (72|72) [ALGB] (1) protected Real sink.p = ThermofluidStream.Boundaries.Tests.PhaseSeperator.sink.Medium.pressure(sink.inlet.state) (73|73) [ALGB] (1) input Real receiver.inlet.state.p = receiver.state_in.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (74|74) [ALGB] (1) protected Real accumulator.r_in (75|75) [ALGB] (1) protected Real flowResistance.p_in = ThermofluidStream.Boundaries.Tests.PhaseSeperator.flowResistance.Medium.pressure(flowResistance.inlet.state) (76|76) [ALGB] (1) input Real twoPhaseSensorSelect1.inlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (77|77) [ALGB] (1) input Real twoPhaseSensorSelect2.inlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (78|78) [ALGB] (1) input Real twoPhaseSensorSelect3.inlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (79|79) [ALGB] (1) input Real twoPhaseSensorSelect4.inlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (80|80) [ALGB] (1) Real receiver.medium.p_bar = Modelica.Units.Conversions.to_bar(99999.99999999999 * receiver.medium.p_bar) (min = 0.0) (81|81) [ALGB] (1) input Real twoPhaseSensorSelect5.inlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (82|82) [ALGB] (1) input Real twoPhaseSensorSelect6.inlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (83|83) [ALGB] (1) input Real singleSensorSelect7.inlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (84|84) [ALGB] (1) protected Real receiver.h_dew = ThermofluidStream.Boundaries.Tests.PhaseSeperator.receiver.Medium.dewEnthalpy(ThermofluidStream.Boundaries.Tests.PhaseSeperator.receiver.Medium.setSat_p(99999.99999999999 * receiver.medium.p_bar)) + 1.0 (85|85) [ALGB] (1) protected Real accumulator.state_out.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (86|86) [ALGB] (1) protected Real receiver.h_out = if noEvent((-receiver.m_flow_out) >= 0.0) then ThermofluidStream.Boundaries.Tests.PhaseSeperator.receiver.Medium.specificEnthalpy(receiver.state_out) else receiver.medium.h (87|87) [ALGB] (1) input Real singleSensorSelect6.inlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (88|88) [ALGB] (1) input Real twoPhaseSensorSelect7.inlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (89|89) [ALGB] (1) input Real singleSensorSelect5.inlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (90|90) [ALGB] (1) protected Real receiver.h_bubble = ThermofluidStream.Boundaries.Tests.PhaseSeperator.receiver.Medium.bubbleEnthalpy(ThermofluidStream.Boundaries.Tests.PhaseSeperator.receiver.Medium.setSat_p(99999.99999999999 * receiver.medium.p_bar)) - 1.0 (91|91) [ALGB] (1) protected Real accumulator.r (92|92) [ALGB] (1) output Real receiver.outlet.state.h = receiver.state_out.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (93|93) [ALGB] (1) input Real singleSensorSelect4.inlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (94|94) [ALGB] (1) Real $FUN_17.psat (95|95) [ALGB] (1) input Real singleSensorSelect3.inlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (96|96) [ALGB] (1) input Real singleSensorSelect2.inlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (97|97) [DISC] (1) input Integer singleSensorSelect.inlet.state.phase (min = 0, max = 2) (98|98) [ALGB] (1) input Real singleSensorSelect1.inlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (99|99) [ALGB] (1) Real twoPhaseSensorSelect.value (100|100) [ALGB] (1) protected Real accumulator.state_out.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (101|101) [ALGB] (1) protected Real receiver.state_in.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (102|102) [DISC] (1) protected discrete Real timeTable.a (103|103) [ALGB] (1) protected Real flowResistance3.p_out (104|104) [ALGB] (1) protected Real flowResistance2.p_out (105|105) [DDER] (1) Real $DER.flowResistance1.dp (StateSelect = avoid) (106|106) [ALGB] (1) protected Real flowResistance1.p_out (107|107) [ALGB] (1) output Real accumulator.outlet.state.T = accumulator.state_out.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (108|108) [ALGB] (1) Real $FUN_20.psat (109|109) [ALGB] (1) Real twoPhaseSensorSelect1.value (110|110) [ALGB] (1) Real twoPhaseSensorSelect2.value (111|111) [ALGB] (1) Real twoPhaseSensorSelect3.value (112|112) [ALGB] (1) Real twoPhaseSensorSelect4.value (113|113) [ALGB] (1) Real twoPhaseSensorSelect5.value (114|114) [ALGB] (1) input Real sink.inlet.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (115|115) [ALGB] (1) Real twoPhaseSensorSelect6.value (116|116) [ALGB] (1) Real twoPhaseSensorSelect7.value (117|117) [ALGB] (1) input Real flowResistance.inlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (118|118) [DISC] (1) Integer accumulator.medium.state.phase (min = 0, max = 2) (119|119) [ALGB] (1) output Real source.outlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (120|120) [ALGB] (1) input Real singleSensorSelect.inlet.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (121|121) [ALGB] (1) output Real source.outlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (122|122) [ALGB] (1) protected Real accumulator.d_gas = ThermofluidStream.Boundaries.Tests.PhaseSeperator.accumulator.Medium.dewDensity(ThermofluidStream.Boundaries.Tests.PhaseSeperator.accumulator.Medium.setSat_p(99999.99999999999 * accumulator.medium.p_bar)) (min = 0.0) (123|123) [ALGB] (1) input Real twoPhaseSensorSelect1.inlet.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (124|124) [ALGB] (1) input Real twoPhaseSensorSelect2.inlet.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (125|125) [ALGB] (1) input Real twoPhaseSensorSelect3.inlet.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (126|126) [ALGB] (1) protected Real receiver.state_out.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (127|127) [ALGB] (1) input Real twoPhaseSensorSelect4.inlet.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (128|128) [ALGB] (1) protected Real flowResistance.rho_in = max(flowResistance.rho_min, ThermofluidStream.Boundaries.Tests.PhaseSeperator.flowResistance.Medium.density(flowResistance.inlet.state)) (min = 0.0) (129|129) [ALGB] (1) input Real twoPhaseSensorSelect5.inlet.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (130|130) [ALGB] (1) input Real twoPhaseSensorSelect6.inlet.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (131|131) [ALGB] (1) input Real twoPhaseSensorSelect7.inlet.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (132|132) [ALGB] (1) protected Real accumulator.T_heatPort (start = 288.15, min = 273.15, max = 2273.15, nominal = 300.0) (133|133) [ALGB] (1) Real accumulator.medium.p_bar = Modelica.Units.Conversions.to_bar(99999.99999999999 * accumulator.medium.p_bar) (min = 0.0) (134|134) [ALGB] (1) protected Real accumulator.state_in.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (135|135) [ALGB] (1) input Real accumulator.inlet.state.p = accumulator.state_in.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (136|136) [ALGB] (1) Real accumulator.medium.u (min = -1e8, max = 1e8, nominal = 1e6) (137|137) [ALGB] (1) input Real flowResistance3.inlet.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (138|138) [ALGB] (1) input Real flowResistance2.inlet.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (139|139) [ALGB] (1) protected Real receiver.state_out.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (140|140) [ALGB] (1) input Real flowResistance1.inlet.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (141|141) [ALGB] (1) output Real source.outlet.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (142|142) [ALGB] (1) input Real flowResistance.inlet.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (143|143) [ALGB] (1) input Real singleSensorSelect1.inlet.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (144|144) [ALGB] (1) input Real singleSensorSelect2.inlet.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (145|145) [ALGB] (1) input Real singleSensorSelect3.inlet.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (146|146) [ALGB] (1) input Real singleSensorSelect4.inlet.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (147|147) [ALGB] (1) input Real singleSensorSelect5.inlet.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (148|148) [ALGB] (1) input Real singleSensorSelect6.inlet.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (149|149) [ALGB] (1) input Real singleSensorSelect7.inlet.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (150|150) [ALGB] (1) Real receiver.Q_flow (151|151) [ALGB] (1) protected Real receiver.state_in.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (152|152) [ALGB] (1) protected Real receiver.d_gas = ThermofluidStream.Boundaries.Tests.PhaseSeperator.receiver.Medium.dewDensity(ThermofluidStream.Boundaries.Tests.PhaseSeperator.receiver.Medium.setSat_p(99999.99999999999 * receiver.medium.p_bar)) (min = 0.0) (153|153) [ALGB] (1) protected Real receiver.r_damping = receiver.d * der(receiver.M) (154|154) [ALGB] (1) Real receiver.medium.sat.Tsat (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (155|155) [ALGB] (1) protected Real accumulator.state_out.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (156|156) [DISC] (1) input Integer sink1.inlet.state.phase (min = 0, max = 2) (157|157) [DISC] (1) input Integer flowResistance.inlet.state.phase (min = 0, max = 2) (158|158) [DISC] (1) Boolean $SEV_9 (159|159) [ALGB] (1) Real accumulator.medium.sat.psat (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (160|160) [ALGB] (1) Real accumulator.Q_flow (161|161) [DISC] (1) Boolean $SEV_7 (162|162) [DISC] (1) output Integer flowResistance3.outlet.state.phase (min = 0, max = 2) (163|163) [DISC] (1) Boolean $SEV_6 (164|164) [DISC] (1) output Integer flowResistance2.outlet.state.phase (min = 0, max = 2) (165|165) [DISC] (1) Boolean $SEV_5 (166|166) [DISC] (1) output Integer flowResistance1.outlet.state.phase (min = 0, max = 2) (167|167) [DISC] (1) protected Integer accumulator.state_out.phase (min = 0, max = 2) (168|168) [DISC] (1) Boolean $SEV_4 (169|169) [DER-] (1) Real $DER.accumulator.M (170|170) [ALGB] (1) protected Real receiver.d = receiver.k_volume_damping * sqrt(abs((2.0 * receiver.L) / (receiver.V_par * max(receiver.density_derp_h_set, 1e-10)))) (171|171) [DISC] (1) Boolean $SEV_3 (172|172) [DISC] (1) Boolean $SEV_2 (173|173) [DISC] (1) Boolean $SEV_1 (174|174) [DISC] (1) Boolean $SEV_0 (175|175) [ALGB] (1) protected Real accumulator.h_bubble = ThermofluidStream.Boundaries.Tests.PhaseSeperator.accumulator.Medium.bubbleEnthalpy(ThermofluidStream.Boundaries.Tests.PhaseSeperator.accumulator.Medium.setSat_p(99999.99999999999 * accumulator.medium.p_bar)) - 1.0 (176|176) [ALGB] (1) input Real flowResistance.inlet.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (177|177) [ALGB] (1) protected Real receiver.p_in = ThermofluidStream.Boundaries.Tests.PhaseSeperator.receiver.Medium.pressure(receiver.state_in) (178|178) [DER-] (1) Real $DER.accumulator.m_flow_out (179|179) [DISC] (1) input Integer accumulator.inlet.state.phase = accumulator.state_in.phase (min = 0, max = 2) (180|180) [ALGB] (1) protected Real receiver.r_out (181|181) [DER-] (1) Real $DER.accumulator.U_med (182|182) [ALGB] (1) Real accumulator.medium.h (StateSelect = default) (183|183) [ALGB] (1) output Real flowResistance.outlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (184|184) [DISC] (1) output Integer source1.outlet.state.phase (min = 0, max = 2) (185|185) [DER-] (1) Real $DER.receiver.m_flow_in (186|186) [DISC] (1) Integer receiver.medium.state.phase (min = 0, max = 2) (187|187) [ALGB] (1) input Real twoPhaseSensorSelect.inlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (188|188) [ALGB] (1) input Real accumulator.inlet.state.T = accumulator.state_in.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (189|189) [ALGB] (1) output Real receiver.outlet.state.d = receiver.state_out.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (190|190) [ALGB] (1) input Real singleSensorSelect7.inlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (191|191) [ALGB] (1) output Real flowResistance.outlet.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (192|192) [ALGB] (1) input Real singleSensorSelect6.inlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (193|193) [ALGB] (1) input Real singleSensorSelect5.inlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (194|194) [ALGB] (1) Real source1.outlet.r (195|195) [ALGB] (1) input Real singleSensorSelect4.inlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (196|196) [ALGB] (1) input Real singleSensorSelect3.inlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (197|197) [ALGB] (1) input Real singleSensorSelect2.inlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (198|198) [ALGB] (1) input Real singleSensorSelect1.inlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (199|199) [ALGB] (1) input Real twoPhaseSensorSelect7.inlet.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (200|200) [ALGB] (1) input Real twoPhaseSensorSelect6.inlet.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (201|201) [ALGB] (1) input Real twoPhaseSensorSelect5.inlet.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (202|202) [ALGB] (1) input Real twoPhaseSensorSelect4.inlet.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (203|203) [ALGB] (1) input Real twoPhaseSensorSelect3.inlet.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (204|204) [ALGB] (1) protected Real receiver.h_in = if noEvent(receiver.m_flow_in >= 0.0) then ThermofluidStream.Boundaries.Tests.PhaseSeperator.receiver.Medium.specificEnthalpy(receiver.state_in) else receiver.medium.h (205|205) [ALGB] (1) input Real twoPhaseSensorSelect2.inlet.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (206|206) [ALGB] (1) input Real twoPhaseSensorSelect1.inlet.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (207|207) [ALGB] (1) Real accumulator.medium.sat.Tsat (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (208|208) [ALGB] (1) output Real source1.outlet.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (209|209) [ALGB] (1) input Real sink.inlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (210|210) [ALGB] (1) output Real flowResistance.outlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (211|211) [DISC] (1) protected discrete Real timeTable.b (212|212) [ALGB] (1) protected Real accumulator.state_in.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (213|213) [ALGB] (1) output Real source1.outlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (214|214) [DISC] (1) input Integer twoPhaseSensorSelect7.inlet.state.phase (min = 0, max = 2) (215|215) [ALGB] (1) protected Real accumulator.state_in.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (216|216) [DISC] (1) input Integer twoPhaseSensorSelect6.inlet.state.phase (min = 0, max = 2) (217|217) [ALGB] (1) protected Real receiver.r (218|218) [DISC] (1) input Integer twoPhaseSensorSelect5.inlet.state.phase (min = 0, max = 2) (219|219) [DISC] (1) input Integer twoPhaseSensorSelect4.inlet.state.phase (min = 0, max = 2) (220|220) [ALGB] (1) protected Real receiver.state_out.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (221|221) [DISC] (1) input Integer twoPhaseSensorSelect3.inlet.state.phase (min = 0, max = 2) (222|222) [ALGB] (1) output Real receiver.outlet.state.p = receiver.state_out.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (223|223) [ALGB] (1) Real accumulator.vapor_quality = max(0.0, min(1.0, accumulator.x)) (224|224) [DISC] (1) input Integer twoPhaseSensorSelect2.inlet.state.phase (min = 0, max = 2) (225|225) [ALGB] (1) input Real twoPhaseSensorSelect.inlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (226|226) [DISC] (1) input Integer twoPhaseSensorSelect1.inlet.state.phase (min = 0, max = 2) (227|227) [ALGB] (1) protected Real accumulator.r_out (228|228) [ALGB] (1) Real singleSensorSelect7.value (229|229) [ALGB] (1) protected Real flowResistance.h_out (230|230) [ALGB] (1) Real singleSensorSelect6.value (231|231) [ALGB] (1) output Real source.outlet.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (232|232) [ALGB] (1) Real singleSensorSelect5.value (233|233) [ALGB] (1) Real singleSensorSelect4.value (234|234) [ALGB] (1) Real singleSensorSelect3.value (235|235) [DISC] (1) Integer accumulator.medium.phase (fixed = false, start = 1, min = 0, max = 2) (236|236) [ALGB] (1) Real singleSensorSelect2.value (237|237) [ALGB] (1) protected Real receiver.state_out.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (238|238) [DER-] (1) Real $DER.receiver.U_med (239|239) [ALGB] (1) Real singleSensorSelect1.value (240|240) [ALGB] (1) protected Real accumulator.d = accumulator.k_volume_damping * sqrt(abs((2.0 * accumulator.L) / (accumulator.V_par * max(accumulator.density_derp_h_set, 1e-10)))) (241|241) [ALGB] (1) input Real singleSensorSelect.inlet.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (242|242) [ALGB] (1) output Real source1.outlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (243|243) [DDER] (1) flow Real $DER.sink1.inlet.m_flow (StateSelect = avoid) (244|244) [ALGB] (1) input Real singleSensorSelect.inlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (245|245) [ALGB] (1) input Real sink.inlet.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (246|246) [ALGB] (1) protected Real receiver.d_liq = ThermofluidStream.Boundaries.Tests.PhaseSeperator.receiver.Medium.bubbleDensity(ThermofluidStream.Boundaries.Tests.PhaseSeperator.receiver.Medium.setSat_p(99999.99999999999 * receiver.medium.p_bar)) (min = 0.0) (247|247) [ALGB] (1) protected Real receiver.x = (receiver.medium.h - receiver.h_bubble) / (receiver.h_dew - receiver.h_bubble) (min = 0.0, max = 1.0, nominal = 0.1) (248|248) [DISC] (1) protected Integer timeTable.last (start = 1) (249|249) [ALGB] (1) input Real receiver.inlet.state.T = receiver.state_in.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (250|250) [ALGB] (1) output Real accumulator.outlet.state.p = accumulator.state_out.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (251|251) [ALGB] (1) Real receiver.liquid_level_pipe (252|252) [ALGB] (1) output Real receiver.outlet.state.T = receiver.state_out.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (253|253) [ALGB] (1) input Real accumulator.inlet.state.h = accumulator.state_in.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (254|254) [ALGB] (1) output Real source1.outlet.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (255|255) [ALGB] (1) Real $FUN_22 (256|256) [ALGB] (1) Real $FUN_21 (257|257) [DISC] (1) protected discrete Real timeTable.nextEventScaled (fixed = true, start = 0.0) (258|258) [ALGB] (1) Real source.h0_var (259|259) [ALGB] (1) protected Real accumulator.h_pipe (260|260) [ALGB] (1) Real accumulator.medium.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0, StateSelect = default) (261|261) [ALGB] (1) protected Real flowResistance1.h_out (262|262) [ALGB] (1) protected Real flowResistance2.h_out (263|263) [ALGB] (1) protected Real flowResistance3.h_out (264|264) [DISC] (1) output Integer flowResistance.outlet.state.phase (min = 0, max = 2) (265|265) [DER-] (1) Real $DER.receiver.M (266|266) [DDER] (1) flow Real $DER.sink.inlet.m_flow (StateSelect = avoid) (267|267) [DDER] (1) Real $DER.receiver.m_flow_out (StateSelect = avoid) (268|268) [ALGB] (1) protected Real sink.r (269|269) [ALGB] (1) Real $FUN_19 (270|270) [ALGB] (1) protected Real receiver.r_in (271|271) [ALGB] (1) Real $FUN_18 (272|272) [DISC] (1) input Integer singleSensorSelect1.inlet.state.phase (min = 0, max = 2) (273|273) [DISC] (1) input Integer singleSensorSelect2.inlet.state.phase (min = 0, max = 2) (274|274) [DDER] (1) flow Real $DER.source1.outlet.m_flow (StateSelect = avoid) (275|275) [DISC] (1) input Integer singleSensorSelect3.inlet.state.phase (min = 0, max = 2) (276|276) [DISC] (1) input Integer singleSensorSelect4.inlet.state.phase (min = 0, max = 2) (277|277) [ALGB] (1) output Real accumulator.outlet.state.h = accumulator.state_out.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (278|278) [ALGB] (1) Real accumulator.liquid_level_pipe (279|279) [DISC] (1) input Integer singleSensorSelect5.inlet.state.phase (min = 0, max = 2) (280|280) [DISC] (1) input Integer singleSensorSelect6.inlet.state.phase (min = 0, max = 2) (281|281) [DISC] (1) input Integer singleSensorSelect7.inlet.state.phase (min = 0, max = 2) (282|282) [ALGB] (1) output Real flowResistance3.outlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (283|283) [ALGB] (1) output Real flowResistance2.outlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (284|284) [ALGB] (1) output Real flowResistance1.outlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (285|285) [ALGB] (1) Real flowResistance1.dr_corr (286|286) [ALGB] (1) output Real flowResistance1.outlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (287|287) [ALGB] (1) Real flowResistance2.dr_corr (288|288) [ALGB] (1) output Real flowResistance2.outlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (289|289) [ALGB] (1) input Real singleSensorSelect7.inlet.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (290|290) [ALGB] (1) Real flowResistance3.dr_corr (291|291) [ALGB] (1) input Real twoPhaseSensorSelect.inlet.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (292|292) [ALGB] (1) output Real flowResistance3.outlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (293|293) [ALGB] (1) input Real singleSensorSelect6.inlet.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (294|294) [ALGB] (1) input Real singleSensorSelect5.inlet.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (295|295) [ALGB] (1) input Real singleSensorSelect4.inlet.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (296|296) [ALGB] (1) input Real singleSensorSelect3.inlet.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (297|297) [ALGB] (1) input Real singleSensorSelect2.inlet.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (298|298) [ALGB] (1) input Real singleSensorSelect1.inlet.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (299|299) [ALGB] (1) protected Real flowResistance.mu_in = ThermofluidStream.Boundaries.Tests.PhaseSeperator.flowResistance.Medium.dynamicViscosity(flowResistance.inlet.state) (min = 0.0) (300|300) [ALGB] (1) Real accumulator.medium.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (301|301) [ALGB] (1) output Real flowResistance.outlet.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (302|302) [DISC] (1) Integer receiver.medium.phase (fixed = false, start = 1, min = 0, max = 2) (303|303) [DDER] (1) Real $DER.flowResistance3.dp (StateSelect = avoid) (304|304) [ALGB] (1) input Real flowResistance.inlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (305|305) [ALGB] (1) Real receiver.medium.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (306|306) [ALGB] (1) protected Real receiver.state_in.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (307|307) [ALGB] (1) protected Real accumulator.state_in.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (308|308) [ALGB] (1) Real receiver.medium.u (min = -1e8, max = 1e8, nominal = 1e6) (309|309) [ALGB] (1) Real receiver.liquid_level (310|310) [DISC] (1) Boolean $SEV_17 (311|311) [DISC] (1) Boolean $SEV_16 (312|312) [DISC] (1) Boolean $SEV_15 (313|313) [DISC] (1) Boolean $SEV_14 (314|314) [DISC] (1) Boolean $SEV_12 (315|315) [DISC] (1) Boolean $SEV_11 (316|316) [DISC] (1) protected Integer receiver.state_in.phase (min = 0, max = 2) (317|317) [DISC] (1) Boolean $SEV_10 (318|318) [ALGB] (1) protected Real receiver.T_heatPort (start = 288.15, min = 273.15, max = 2273.15, nominal = 300.0) (319|319) [ALGB] (1) output Real flowResistance3.outlet.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (320|320) [ALGB] (1) output Real flowResistance2.outlet.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (321|321) [ALGB] (1) output Real flowResistance1.outlet.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (322|322) [ALGB] (1) input Real singleSensorSelect.inlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (323|323) [ALGB] (1) protected Real accumulator.state_out.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (324|324) [ALGB] (1) Real $FUN_17.Tsat (325|325) [ALGB] (1) Real receiver.medium.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (326|326) [ALGB] (1) Real receiver.vapor_quality = max(0.0, min(1.0, receiver.x)) (327|327) [ALGB] (1) input Real sink.inlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (328|328) [ALGB] (1) input Real receiver.inlet.state.h = receiver.state_in.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (329|329) [ALGB] (1) input Real receiver.inlet.state.d = receiver.state_in.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (330|330) [ALGB] (1) Real flowResistance.dr_corr (331|331) [ALGB] (1) Real $FUN_20.Tsat (332|332) [ALGB] (1) output Real accumulator.outlet.state.d = accumulator.state_out.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (333|333) [ALGB] (1) protected Real accumulator.x = (accumulator.medium.h - accumulator.h_bubble) / (accumulator.h_dew - accumulator.h_bubble) (min = 0.0, max = 1.0, nominal = 0.1) (334|334) [ALGB] (1) Real receiver.medium.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (335|335) [DISC] (1) input Integer twoPhaseSensorSelect.inlet.state.phase (min = 0, max = 2) (336|336) [DISC] (1) output Integer receiver.outlet.state.phase = receiver.state_out.phase (min = 0, max = 2) (337|337) [DSTA] (1) flow Real sink1.inlet.m_flow (338|338) [DSTA] (1) flow Real sink.inlet.m_flow (339|339) [DSTA] (1) Real flowResistance1.dp (340|340) [DSTA] (1) flow Real source.outlet.m_flow (341|341) [DSTA] (1) Real flowResistance3.dp (342|342) [DSTA] (1) protected Real receiver.m_flow_out (343|343) [DSTA] (1) protected Real accumulator.m_flow_in (344|344) [DSTA] (1) flow Real source1.outlet.m_flow System Equations (318/340) **************************** (1|1) [SCAL] (1) singleSensorSelect2.inlet.state.T = flowResistance2.outlet.state.T ($RES_SIM_254) (2|2) [SCAL] (1) flowResistance2.outlet.state.phase = 0 ($RES_SIM_429) (3|3) [SCAL] (1) singleSensorSelect2.inlet.state.d = accumulator.inlet.state.d ($RES_SIM_255) (4|4) [SCAL] (1) sink1.p = sink1.inlet.state.p ($RES_BND_380) (5|5) [SCAL] (1) singleSensorSelect2.inlet.state.d = twoPhaseSensorSelect4.inlet.state.d ($RES_SIM_256) (6|6) [RECD] (5) receiver.inlet.state = receiver.state_in ($RES_BND_381) (7|11) [SCAL] (1) singleSensorSelect2.inlet.state.d = flowResistance2.outlet.state.d ($RES_SIM_257) (8|12) [RECD] (5) receiver.outlet.state = receiver.state_out ($RES_BND_382) (9|17) [SCAL] (1) singleSensorSelect2.inlet.state.h = accumulator.inlet.state.h ($RES_SIM_258) (10|18) [RECD] (5) accumulator.inlet.state = accumulator.state_in ($RES_BND_383) (11|23) [SCAL] (1) singleSensorSelect2.inlet.state.h = twoPhaseSensorSelect4.inlet.state.h ($RES_SIM_259) (12|24) [RECD] (5) accumulator.outlet.state = accumulator.state_out ($RES_BND_384) (13|29) [SCAL] (1) singleSensorSelect7.value = ThermofluidStream.Boundaries.Tests.PhaseSeperator.singleSensorSelect7.getQuantity(singleSensorSelect7.inlet.state, sink1.inlet.r, singleSensorSelect7.quantity, singleSensorSelect7.rho_min) ($RES_AUX_391) (14|30) [SCAL] (1) twoPhaseSensorSelect7.value = ThermofluidStream.Boundaries.Tests.PhaseSeperator.twoPhaseSensorSelect7.getQuantity(twoPhaseSensorSelect7.inlet.state, twoPhaseSensorSelect7.quantity) ($RES_AUX_392) (15|31) [SCAL] (1) singleSensorSelect6.value = ThermofluidStream.Boundaries.Tests.PhaseSeperator.singleSensorSelect6.getQuantity(singleSensorSelect6.inlet.state, source.outlet.r, singleSensorSelect6.quantity, singleSensorSelect6.rho_min) ($RES_AUX_393) (16|32) [SCAL] (1) twoPhaseSensorSelect6.value = ThermofluidStream.Boundaries.Tests.PhaseSeperator.twoPhaseSensorSelect6.getQuantity(twoPhaseSensorSelect6.inlet.state, twoPhaseSensorSelect6.quantity) ($RES_AUX_394) (17|33) [SCAL] (1) singleSensorSelect5.value = ThermofluidStream.Boundaries.Tests.PhaseSeperator.singleSensorSelect5.getQuantity(singleSensorSelect5.inlet.state, source1.outlet.r, singleSensorSelect5.quantity, singleSensorSelect5.rho_min) ($RES_AUX_395) (18|34) [SCAL] (1) singleSensorSelect4.value = ThermofluidStream.Boundaries.Tests.PhaseSeperator.singleSensorSelect4.getQuantity(singleSensorSelect4.inlet.state, sink.inlet.r, singleSensorSelect4.quantity, singleSensorSelect4.rho_min) ($RES_AUX_396) (19|35) [SCAL] (1) singleSensorSelect3.value = ThermofluidStream.Boundaries.Tests.PhaseSeperator.singleSensorSelect3.getQuantity(singleSensorSelect3.inlet.state, accumulator.r_out, singleSensorSelect3.quantity, singleSensorSelect3.rho_min) ($RES_AUX_397) (20|36) [SCAL] (1) singleSensorSelect2.value = ThermofluidStream.Boundaries.Tests.PhaseSeperator.singleSensorSelect2.getQuantity(singleSensorSelect2.inlet.state, accumulator.r_in, singleSensorSelect2.quantity, singleSensorSelect2.rho_min) ($RES_AUX_398) (21|37) [SCAL] (1) singleSensorSelect1.value = ThermofluidStream.Boundaries.Tests.PhaseSeperator.singleSensorSelect1.getQuantity(singleSensorSelect1.inlet.state, receiver.r_out, singleSensorSelect1.quantity, singleSensorSelect1.rho_min) ($RES_AUX_399) (22|38) [SCAL] (1) source1.outlet.m_flow - 2e-4 * flowResistance2.dp = 0.0 ($RES_SIM_170) (23|39) [SCAL] (1) 2e-4 * flowResistance1.dp + receiver.m_flow_in = 0.0 ($RES_SIM_171) (24|40) [SCAL] (1) receiver.m_flow_out - 2e-4 * flowResistance.dp = 0.0 ($RES_SIM_172) (25|41) [SCAL] (1) accumulator.m_flow_out - 2e-4 * flowResistance3.dp = 0.0 ($RES_SIM_173) (26|42) [SCAL] (1) 2e-4 * flowResistance3.dp + sink.inlet.m_flow = 0.0 ($RES_SIM_174) (27|43) [SCAL] (1) $SEV_1 = receiver.x < 0.0 ($RES_EVT_470) (28|44) [SCAL] (1) 2e-4 * flowResistance2.dp + accumulator.m_flow_in = 0.0 ($RES_SIM_175) (29|45) [SCAL] (1) $SEV_2 = receiver.x <= 1.0 ($RES_EVT_471) (30|46) [SCAL] (1) source.outlet.m_flow - 2e-4 * flowResistance1.dp = 0.0 ($RES_SIM_176) (31|47) [SCAL] (1) $SEV_3 = (accumulator.medium.h < ThermofluidStream.Media.myMedia.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(accumulator.medium.sat.psat, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.BaseIF97.Regions.boilingcurve_p(accumulator.medium.sat.psat)) or accumulator.medium.h > ThermofluidStream.Media.myMedia.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(accumulator.medium.sat.psat, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.BaseIF97.Regions.dewcurve_p(accumulator.medium.sat.psat))) or 99999.99999999999 * accumulator.medium.p_bar > 2.2064e7 ($RES_EVT_472) (32|48) [SCAL] (1) singleSensorSelect7.inlet.state.p = sink1.inlet.state.p ($RES_SIM_177) (33|49) [SCAL] (1) $SEV_4 = accumulator.x < 0.0 ($RES_EVT_473) (34|50) [SCAL] (1) singleSensorSelect7.inlet.state.p = twoPhaseSensorSelect7.inlet.state.p ($RES_SIM_178) (35|51) [SCAL] (1) $SEV_5 = accumulator.x <= 1.0 ($RES_EVT_474) (36|52) [SCAL] (1) singleSensorSelect7.inlet.state.p = flowResistance.outlet.state.p ($RES_SIM_179) (37|53) [SCAL] (1) flowResistance2.outlet.state.h = flowResistance2.h_out ($RES_SIM_430) (38|54) [SCAL] (1) flowResistance2.outlet.state.d = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.rho_props_ph(flowResistance2.p_out, flowResistance2.h_out, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.waterBaseProp_ph(flowResistance2.p_out, flowResistance2.h_out, 0, 0)) ($RES_SIM_431) (39|55) [SCAL] (1) $SEV_9 = 99999.99999999999 * receiver.medium.p_bar >= 0.0 ($RES_EVT_476) (40|56) [SCAL] (1) flowResistance2.outlet.state.T = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.T_props_ph(flowResistance2.p_out, flowResistance2.h_out, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.waterBaseProp_ph(flowResistance2.p_out, flowResistance2.h_out, 0, 0)) ($RES_SIM_432) (41|57) [SCAL] (1) $SEV_10 = receiver.m_flow_in > receiver.m_flow_assert ($RES_EVT_477) (42|58) [SCAL] (1) flowResistance2.outlet.state.p = flowResistance2.p_out ($RES_SIM_433) (43|59) [SCAL] (1) $SEV_11 = (-receiver.m_flow_out) > receiver.m_flow_assert ($RES_EVT_478) (44|60) [SCAL] (1) flowResistance.outlet.state.phase = 0 ($RES_SIM_434) (45|61) [SCAL] (1) $SEV_12 = receiver.M > 0.0 ($RES_EVT_479) (46|62) [SCAL] (1) singleSensorSelect2.inlet.state.h = flowResistance2.outlet.state.h ($RES_SIM_260) (47|63) [SCAL] (1) flowResistance.outlet.state.h = flowResistance.h_out ($RES_SIM_435) (48|64) [SCAL] (1) singleSensorSelect2.inlet.state.phase = accumulator.inlet.state.phase ($RES_SIM_261) (49|65) [SCAL] (1) flowResistance.outlet.state.d = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.rho_props_ph(flowResistance.p_out, flowResistance.h_out, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.waterBaseProp_ph(flowResistance.p_out, flowResistance.h_out, 0, 0)) ($RES_SIM_436) (50|66) [SCAL] (1) singleSensorSelect2.inlet.state.phase = twoPhaseSensorSelect4.inlet.state.phase ($RES_SIM_262) (51|67) [SCAL] (1) flowResistance.outlet.state.T = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.T_props_ph(flowResistance.p_out, flowResistance.h_out, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.waterBaseProp_ph(flowResistance.p_out, flowResistance.h_out, 0, 0)) ($RES_SIM_437) (52|68) [SCAL] (1) singleSensorSelect2.inlet.state.phase = flowResistance2.outlet.state.phase ($RES_SIM_263) (53|69) [SCAL] (1) flowResistance.outlet.state.p = flowResistance.p_out ($RES_SIM_438) (54|70) [SCAL] (1) flowResistance3.outlet.state.phase = 0 ($RES_SIM_439) (55|71) [SCAL] (1) singleSensorSelect.inlet.state.p = flowResistance1.outlet.state.p ($RES_SIM_267) (56|72) [SCAL] (1) singleSensorSelect.inlet.state.p = twoPhaseSensorSelect5.inlet.state.p ($RES_SIM_268) (57|73) [SCAL] (1) singleSensorSelect.inlet.state.p = receiver.inlet.state.p ($RES_SIM_269) (58|74) [SCAL] (1) singleSensorSelect7.inlet.state.T = sink1.inlet.state.T ($RES_SIM_180) (59|75) [SCAL] (1) singleSensorSelect7.inlet.state.T = twoPhaseSensorSelect7.inlet.state.T ($RES_SIM_181) (60|76) [SCAL] (1) singleSensorSelect7.inlet.state.T = flowResistance.outlet.state.T ($RES_SIM_182) (61|77) [SCAL] (1) singleSensorSelect7.inlet.state.d = sink1.inlet.state.d ($RES_SIM_183) (62|78) [SCAL] (1) singleSensorSelect7.inlet.state.d = twoPhaseSensorSelect7.inlet.state.d ($RES_SIM_184) (63|79) [SCAL] (1) singleSensorSelect7.inlet.state.d = flowResistance.outlet.state.d ($RES_SIM_185) (64|80) [SCAL] (1) $SEV_14 = 99999.99999999999 * accumulator.medium.p_bar >= 0.0 ($RES_EVT_481) (65|81) [SCAL] (1) singleSensorSelect7.inlet.state.h = sink1.inlet.state.h ($RES_SIM_186) (66|82) [SCAL] (1) $SEV_15 = accumulator.m_flow_in > accumulator.m_flow_assert ($RES_EVT_482) (67|83) [SCAL] (1) singleSensorSelect7.inlet.state.h = twoPhaseSensorSelect7.inlet.state.h ($RES_SIM_187) (68|84) [SCAL] (1) $SEV_16 = (-accumulator.m_flow_out) > accumulator.m_flow_assert ($RES_EVT_483) (69|85) [SCAL] (1) singleSensorSelect7.inlet.state.h = flowResistance.outlet.state.h ($RES_SIM_188) (70|86) [SCAL] (1) $SEV_17 = accumulator.M > 0.0 ($RES_EVT_484) (71|87) [SCAL] (1) singleSensorSelect7.inlet.state.phase = sink1.inlet.state.phase ($RES_SIM_189) (72|88) [SCAL] (1) flowResistance3.outlet.state.h = flowResistance3.h_out ($RES_SIM_440) (73|89) [SCAL] (1) flowResistance3.outlet.state.d = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.rho_props_ph(flowResistance3.p_out, flowResistance3.h_out, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.waterBaseProp_ph(flowResistance3.p_out, flowResistance3.h_out, 0, 0)) ($RES_SIM_441) (74|90) [SCAL] (1) flowResistance3.outlet.state.T = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.T_props_ph(flowResistance3.p_out, flowResistance3.h_out, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.waterBaseProp_ph(flowResistance3.p_out, flowResistance3.h_out, 0, 0)) ($RES_SIM_442) (75|91) [SCAL] (1) flowResistance3.outlet.state.p = flowResistance3.p_out ($RES_SIM_443) (76|92) [SCAL] (1) source1.outlet.state.phase = 0 ($RES_SIM_444) (77|93) [SCAL] (1) singleSensorSelect.inlet.state.T = flowResistance1.outlet.state.T ($RES_SIM_270) (78|94) [SCAL] (1) source1.outlet.state.h = source.h0_var ($RES_SIM_445) (79|95) [SCAL] (1) singleSensorSelect.inlet.state.T = twoPhaseSensorSelect5.inlet.state.T ($RES_SIM_271) (80|96) [SCAL] (1) source1.outlet.state.d = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.rho_props_ph(source1.p0_par, source.h0_var, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.waterBaseProp_ph(source1.p0_par, source.h0_var, 0, 0)) ($RES_SIM_446) (81|97) [SCAL] (1) singleSensorSelect.inlet.state.T = receiver.inlet.state.T ($RES_SIM_272) (82|98) [SCAL] (1) source1.outlet.state.T = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.T_props_ph(source1.p0_par, source.h0_var, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.waterBaseProp_ph(source1.p0_par, source.h0_var, 0, 0)) ($RES_SIM_447) (83|99) [SCAL] (1) singleSensorSelect.inlet.state.d = flowResistance1.outlet.state.d ($RES_SIM_273) (84|100) [SCAL] (1) source1.outlet.state.p = source1.p0_par ($RES_SIM_448) (85|101) [SCAL] (1) singleSensorSelect.inlet.state.d = twoPhaseSensorSelect5.inlet.state.d ($RES_SIM_274) (86|102) [SCAL] (1) $FUN_17.psat = (ThermofluidStream.Boundaries.Tests.PhaseSeperator.accumulator.Medium.setSat_p(99999.99999999999 * accumulator.medium.p_bar)).psat ($RES_SIM_449) (87|103) [SCAL] (1) singleSensorSelect.inlet.state.d = receiver.inlet.state.d ($RES_SIM_275) (88|104) [SCAL] (1) singleSensorSelect.inlet.state.h = flowResistance1.outlet.state.h ($RES_SIM_276) (89|105) [SCAL] (1) singleSensorSelect.inlet.state.h = twoPhaseSensorSelect5.inlet.state.h ($RES_SIM_277) (90|106) [SCAL] (1) singleSensorSelect.inlet.state.h = receiver.inlet.state.h ($RES_SIM_278) (91|107) [SCAL] (1) singleSensorSelect.inlet.state.phase = flowResistance1.outlet.state.phase ($RES_SIM_279) (92|108) [SCAL] (1) singleSensorSelect7.inlet.state.phase = twoPhaseSensorSelect7.inlet.state.phase ($RES_SIM_190) (93|109) [SCAL] (1) singleSensorSelect7.inlet.state.phase = flowResistance.outlet.state.phase ($RES_SIM_191) (94|110) [SCAL] (1) twoPhaseSensorSelect3.inlet.state.p = sink.inlet.state.p ($RES_SIM_195) (95|111) [SCAL] (1) twoPhaseSensorSelect3.inlet.state.p = singleSensorSelect4.inlet.state.p ($RES_SIM_196) (96|112) [SCAL] (1) twoPhaseSensorSelect3.inlet.state.p = flowResistance3.outlet.state.p ($RES_SIM_197) (97|113) [SCAL] (1) twoPhaseSensorSelect3.inlet.state.T = sink.inlet.state.T ($RES_SIM_198) (98|114) [SCAL] (1) twoPhaseSensorSelect3.inlet.state.T = singleSensorSelect4.inlet.state.T ($RES_SIM_199) (99|115) [SCAL] (1) $FUN_17.Tsat = (ThermofluidStream.Boundaries.Tests.PhaseSeperator.accumulator.Medium.setSat_p(99999.99999999999 * accumulator.medium.p_bar)).Tsat ($RES_SIM_450) (100|116) [SCAL] (1) $FUN_20.psat = (ThermofluidStream.Boundaries.Tests.PhaseSeperator.receiver.Medium.setSat_p(99999.99999999999 * receiver.medium.p_bar)).psat ($RES_SIM_451) (101|117) [SCAL] (1) $FUN_20.Tsat = (ThermofluidStream.Boundaries.Tests.PhaseSeperator.receiver.Medium.setSat_p(99999.99999999999 * receiver.medium.p_bar)).Tsat ($RES_SIM_452) (102|118) [SCAL] (1) singleSensorSelect.inlet.state.phase = twoPhaseSensorSelect5.inlet.state.phase ($RES_SIM_280) (103|119) [SCAL] (1) singleSensorSelect.inlet.state.phase = receiver.inlet.state.phase ($RES_SIM_281) (104|120) [SCAL] (1) singleSensorSelect1.inlet.state.p = twoPhaseSensorSelect2.inlet.state.p ($RES_SIM_285) (105|121) [SCAL] (1) singleSensorSelect1.inlet.state.p = flowResistance.inlet.state.p ($RES_SIM_286) (106|122) [SCAL] (1) singleSensorSelect1.inlet.state.p = receiver.outlet.state.p ($RES_SIM_287) (107|123) [SCAL] (1) singleSensorSelect1.inlet.state.T = twoPhaseSensorSelect2.inlet.state.T ($RES_SIM_288) (108|124) [SCAL] (1) singleSensorSelect1.inlet.state.T = flowResistance.inlet.state.T ($RES_SIM_289) (109|125) [SCAL] (1) singleSensorSelect1.inlet.state.T = receiver.outlet.state.T ($RES_SIM_290) (110|126) [SCAL] (1) singleSensorSelect1.inlet.state.d = twoPhaseSensorSelect2.inlet.state.d ($RES_SIM_291) (111|127) [SCAL] (1) singleSensorSelect1.inlet.state.d = flowResistance.inlet.state.d ($RES_SIM_292) (112|128) [SCAL] (1) singleSensorSelect1.inlet.state.d = receiver.outlet.state.d ($RES_SIM_293) (113|129) [SCAL] (1) singleSensorSelect1.inlet.state.h = twoPhaseSensorSelect2.inlet.state.h ($RES_SIM_294) (114|130) [SCAL] (1) singleSensorSelect1.inlet.state.h = flowResistance.inlet.state.h ($RES_SIM_295) (115|131) [SCAL] (1) singleSensorSelect1.inlet.state.h = receiver.outlet.state.h ($RES_SIM_296) (116|132) [SCAL] (1) singleSensorSelect1.inlet.state.phase = twoPhaseSensorSelect2.inlet.state.phase ($RES_SIM_297) (117|133) [SCAL] (1) singleSensorSelect1.inlet.state.phase = flowResistance.inlet.state.phase ($RES_SIM_298) (118|134) [SCAL] (1) singleSensorSelect1.inlet.state.phase = receiver.outlet.state.phase ($RES_SIM_299) (119|135) [ALGO] (7) ($RES_SIM_10) (119|135) [----] $SEV_6 := not (timeTable.table[1, 1] > 0.0 or timeTable.table[1, 1] < 0.0); (119|135) [----] assert($SEV_6, \"The first point in time has to be set to 0, but is table[1,1] = \" + String(timeTable.table[1, 1], 6, 0, true), AssertionLevel.error); (119|135) [----] $SEV_7 := time >= $PRE.timeTable.nextEvent; (119|135) [----] when {$SEV_7, initial()} then (119|135) [----] (timeTable.a, timeTable.b, timeTable.nextEventScaled, timeTable.last) := ThermofluidStream.Boundaries.Tests.PhaseSeperator.timeTable.getInterpolationCoefficients(timeTable.table, timeTable.offset, timeTable.startTime, time, timeTable.last, 2.220446049250313e-14, timeTable.shiftTime); (119|135) [----] timeTable.nextEvent := timeTable.nextEventScaled; (119|135) [----] end when; (120|142) [SCAL] (1) sink1.r + sink1.p = sink1.p0_par ($RES_SIM_17) (121|143) [SCAL] (1) $DER.sink1.inlet.m_flow * sink1.L = sink1.inlet.r - sink1.r ($RES_SIM_18) (122|144) [SCAL] (1) source1.L * $DER.source1.outlet.m_flow = source1.outlet.r ($RES_SIM_27) (123|145) [SCAL] (1) singleSensorSelect.value = ThermofluidStream.Boundaries.Tests.PhaseSeperator.singleSensorSelect.getQuantity(singleSensorSelect.inlet.state, receiver.r_in, singleSensorSelect.quantity, singleSensorSelect.rho_min) ($RES_AUX_400) (124|146) [SCAL] (1) twoPhaseSensorSelect5.value = ThermofluidStream.Boundaries.Tests.PhaseSeperator.twoPhaseSensorSelect5.getQuantity(twoPhaseSensorSelect5.inlet.state, twoPhaseSensorSelect5.quantity) ($RES_AUX_401) (125|147) [SCAL] (1) twoPhaseSensorSelect4.value = ThermofluidStream.Boundaries.Tests.PhaseSeperator.twoPhaseSensorSelect4.getQuantity(twoPhaseSensorSelect4.inlet.state, twoPhaseSensorSelect4.quantity) ($RES_AUX_402) (126|148) [SCAL] (1) twoPhaseSensorSelect3.value = ThermofluidStream.Boundaries.Tests.PhaseSeperator.twoPhaseSensorSelect3.getQuantity(twoPhaseSensorSelect3.inlet.state, twoPhaseSensorSelect3.quantity) ($RES_AUX_403) (127|149) [SCAL] (1) twoPhaseSensorSelect2.value = ThermofluidStream.Boundaries.Tests.PhaseSeperator.twoPhaseSensorSelect2.getQuantity(twoPhaseSensorSelect2.inlet.state, twoPhaseSensorSelect2.quantity) ($RES_AUX_404) (128|150) [SCAL] (1) twoPhaseSensorSelect1.value = ThermofluidStream.Boundaries.Tests.PhaseSeperator.twoPhaseSensorSelect1.getQuantity(twoPhaseSensorSelect1.inlet.state, twoPhaseSensorSelect1.quantity) ($RES_AUX_405) (129|151) [SCAL] (1) twoPhaseSensorSelect.value = ThermofluidStream.Boundaries.Tests.PhaseSeperator.twoPhaseSensorSelect.getQuantity(twoPhaseSensorSelect.inlet.state, twoPhaseSensorSelect.quantity) ($RES_AUX_406) (130|152) [SCAL] (1) flowResistance3.dr_corr = (flowResistance3.p_in + flowResistance3.dp) - flowResistance3.p_out ($RES_SIM_55) (131|153) [SCAL] (1) flowResistance3.p_out = max(flowResistance3.p_min, flowResistance3.p_in + flowResistance3.dp) ($RES_SIM_56) (132|154) [SCAL] (1) sink.inlet.r = (flowResistance3.dr_corr + accumulator.r_out) - (-2e-4 * $DER.flowResistance3.dp) * flowResistance3.L ($RES_SIM_57) (133|155) [SCAL] (1) accumulator.Q_flow = 0.0 ($RES_SIM_100) (134|156) [SCAL] (1) $DER.accumulator.U_med = accumulator.h_in * accumulator.m_flow_in + accumulator.Q_flow + accumulator.h_out * accumulator.m_flow_out ($RES_SIM_101) (135|157) [SCAL] (1) $DER.accumulator.M = accumulator.m_flow_in + accumulator.m_flow_out ($RES_SIM_102) (136|158) [SCAL] (1) accumulator.r + accumulator.p_in = 99999.99999999999 * accumulator.medium.p_bar ($RES_SIM_103) (137|159) [SCAL] (1) $DER.accumulator.m_flow_out * accumulator.L = accumulator.r_out - accumulator.r_damping ($RES_SIM_104) (138|160) [SCAL] (1) $DER.accumulator.m_flow_in * accumulator.L = accumulator.r_in - (accumulator.r_damping + accumulator.r) ($RES_SIM_105) (139|161) [SCAL] (1) flowResistance.dr_corr = (flowResistance.p_in + flowResistance.dp) - flowResistance.p_out ($RES_SIM_62) (140|162) [SCAL] (1) flowResistance.p_out = max(flowResistance.p_min, flowResistance.p_in + flowResistance.dp) ($RES_SIM_63) (141|163) [SCAL] (1) sink1.inlet.r = (flowResistance.dr_corr + receiver.r_out) - (-2e-4 * $DER.flowResistance.dp) * flowResistance.L ($RES_SIM_64) (142|164) [SCAL] (1) flowResistance2.dr_corr = (flowResistance2.p_in + flowResistance2.dp) - flowResistance2.p_out ($RES_SIM_69) (143|165) [SCAL] (1) accumulator.h_pipe = smooth(1, if $SEV_4 then accumulator.medium.h else if $SEV_5 then accumulator.liquid_level_pipe * accumulator.h_bubble + (1.0 - accumulator.liquid_level_pipe) * accumulator.h_dew else accumulator.medium.h) ($RES_SIM_110) (144|166) [SCAL] (1) accumulator.liquid_level_pipe = max(0.0, min(1.0, (accumulator.liquid_level - accumulator.pipe_low) / (accumulator.pipe_high - accumulator.pipe_low))) ($RES_SIM_111) (145|167) [SCAL] (1) accumulator.liquid_level = max(0.0, min(1.0, (((1.0 - accumulator.x) * accumulator.M) / accumulator.d_liq) / accumulator.V_par)) ($RES_SIM_112) (146|168) [SCAL] (1) accumulator.medium.phase = accumulator.medium.state.phase ($RES_SIM_119) (147|169) [SCAL] (1) flowResistance2.p_out = max(flowResistance2.p_min, flowResistance2.p_in + flowResistance2.dp) ($RES_SIM_70) (148|170) [SCAL] (1) accumulator.r_in = (flowResistance2.dr_corr + source1.outlet.r) - (-2e-4 * $DER.flowResistance2.dp) * flowResistance2.L ($RES_SIM_71) (149|171) [SCAL] (1) twoPhaseSensorSelect3.inlet.state.T = flowResistance3.outlet.state.T ($RES_SIM_200) (150|172) [SCAL] (1) twoPhaseSensorSelect3.inlet.state.d = sink.inlet.state.d ($RES_SIM_201) (151|173) [SCAL] (1) twoPhaseSensorSelect3.inlet.state.d = singleSensorSelect4.inlet.state.d ($RES_SIM_202) (152|174) [SCAL] (1) twoPhaseSensorSelect3.inlet.state.d = flowResistance3.outlet.state.d ($RES_SIM_203) (153|175) [SCAL] (1) flowResistance1.dr_corr = (flowResistance1.p_in + flowResistance1.dp) - flowResistance1.p_out ($RES_SIM_76) (154|176) [SCAL] (1) twoPhaseSensorSelect3.inlet.state.h = sink.inlet.state.h ($RES_SIM_204) (155|177) [SCAL] (1) flowResistance1.p_out = max(flowResistance1.p_min, flowResistance1.p_in + flowResistance1.dp) ($RES_SIM_77) (156|178) [SCAL] (1) twoPhaseSensorSelect3.inlet.state.h = singleSensorSelect4.inlet.state.h ($RES_SIM_205) (157|179) [SCAL] (1) receiver.d = receiver.k_volume_damping * $FUN_22 ($RES_BND_331) (158|180) [SCAL] (1) receiver.r_in = (flowResistance1.dr_corr + source.outlet.r) - (-2e-4 * $DER.flowResistance1.dp) * flowResistance1.L ($RES_SIM_78) (159|181) [SCAL] (1) twoPhaseSensorSelect3.inlet.state.h = flowResistance3.outlet.state.h ($RES_SIM_206) (160|182) [SCAL] (1) receiver.r_damping = receiver.d * $DER.receiver.M ($RES_BND_332) (161|183) [SCAL] (1) twoPhaseSensorSelect3.inlet.state.phase = sink.inlet.state.phase ($RES_SIM_207) (162|184) [SCAL] (1) receiver.p_in = receiver.state_in.p ($RES_BND_333) (163|185) [SCAL] (1) twoPhaseSensorSelect3.inlet.state.phase = singleSensorSelect4.inlet.state.phase ($RES_SIM_208) (164|186) [SCAL] (1) receiver.h_in = if noEvent(receiver.m_flow_in >= 0.0) then receiver.state_in.h else receiver.medium.h ($RES_BND_334) (165|187) [SCAL] (1) twoPhaseSensorSelect3.inlet.state.phase = flowResistance3.outlet.state.phase ($RES_SIM_209) (166|188) [SCAL] (1) receiver.h_out = if noEvent((-receiver.m_flow_out) >= 0.0) then receiver.state_out.h else receiver.medium.h ($RES_BND_335) (167|189) [SCAL] (1) receiver.vapor_quality = max(0.0, min(1.0, receiver.x)) ($RES_BND_336) (168|190) [SCAL] (1) receiver.x = (receiver.medium.h - receiver.h_bubble) / (receiver.h_dew - receiver.h_bubble) ($RES_BND_337) (169|191) [SCAL] (1) receiver.d_liq = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.BaseIF97.Regions.rhovl_p($FUN_20.psat, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.BaseIF97.Regions.boilingcurve_p($FUN_20.psat)) ($RES_BND_338) (170|192) [SCAL] (1) receiver.d_gas = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.BaseIF97.Regions.rhovl_p($FUN_20.psat, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.BaseIF97.Regions.dewcurve_p($FUN_20.psat)) ($RES_BND_339) (171|193) [SCAL] (1) accumulator.medium.d = accumulator.medium.state.d ($RES_SIM_120) (172|194) [SCAL] (1) accumulator.T_heatPort = accumulator.medium.state.T ($RES_SIM_121) (173|195) [SCAL] (1) 99999.99999999999 * accumulator.medium.p_bar = accumulator.medium.state.p ($RES_SIM_122) (174|196) [SCAL] (1) accumulator.medium.h = accumulator.medium.state.h ($RES_SIM_123) (175|197) [SCAL] (1) accumulator.medium.u = accumulator.medium.h - (99999.99999999999 * accumulator.medium.p_bar) / accumulator.medium.d ($RES_SIM_125) (176|198) [SCAL] (1) accumulator.medium.sat.psat = 99999.99999999999 * accumulator.medium.p_bar ($RES_SIM_126) (177|199) [SCAL] (1) accumulator.medium.sat.Tsat = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.BaseIF97.Basic.tsat(99999.99999999999 * accumulator.medium.p_bar) ($RES_SIM_127) (178|200) [SCAL] (1) accumulator.T_heatPort = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.T_props_ph(99999.99999999999 * accumulator.medium.p_bar, accumulator.medium.h, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.waterBaseProp_ph(99999.99999999999 * accumulator.medium.p_bar, accumulator.medium.h, accumulator.medium.phase, 0)) ($RES_SIM_128) (179|201) [SCAL] (1) accumulator.medium.d = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.rho_props_ph(99999.99999999999 * accumulator.medium.p_bar, accumulator.medium.h, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.waterBaseProp_ph(99999.99999999999 * accumulator.medium.p_bar, accumulator.medium.h, accumulator.medium.phase, 0)) ($RES_SIM_129) (180|202) [SCAL] (1) source.h0_var = timeTable.a * time + timeTable.b ($RES_SIM_82) (181|203) [SCAL] (1) singleSensorSelect5.inlet.state.p = source1.outlet.state.p ($RES_SIM_213) (182|204) [SCAL] (1) singleSensorSelect5.inlet.state.p = twoPhaseSensorSelect.inlet.state.p ($RES_SIM_214) (183|205) [SCAL] (1) singleSensorSelect5.inlet.state.p = flowResistance2.inlet.state.p ($RES_SIM_215) (184|206) [SCAL] (1) receiver.h_bubble = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.BaseIF97.Regions.hvl_p($FUN_20.psat, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.BaseIF97.Regions.boilingcurve_p($FUN_20.psat)) - 1.0 ($RES_BND_340) (185|207) [SCAL] (1) singleSensorSelect5.inlet.state.T = source1.outlet.state.T ($RES_SIM_216) (186|208) [SCAL] (1) receiver.h_dew = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.BaseIF97.Regions.hvl_p($FUN_20.psat, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.BaseIF97.Regions.dewcurve_p($FUN_20.psat)) + 1.0 ($RES_BND_341) (187|209) [SCAL] (1) singleSensorSelect5.inlet.state.T = twoPhaseSensorSelect.inlet.state.T ($RES_SIM_217) (188|210) [SCAL] (1) singleSensorSelect5.inlet.state.T = flowResistance2.inlet.state.T ($RES_SIM_218) (189|211) [SCAL] (1) singleSensorSelect5.inlet.state.d = source1.outlet.state.d ($RES_SIM_219) (190|212) [SCAL] (1) accumulator.d = accumulator.k_volume_damping * $FUN_19 ($RES_BND_348) (191|213) [SCAL] (1) accumulator.r_damping = accumulator.d * $DER.accumulator.M ($RES_BND_349) (192|214) [SCAL] (1) singleSensorSelect3.inlet.state.p = twoPhaseSensorSelect1.inlet.state.p ($RES_SIM_303) (193|215) [SCAL] (1) singleSensorSelect3.inlet.state.p = flowResistance3.inlet.state.p ($RES_SIM_304) (194|216) [SCAL] (1) singleSensorSelect3.inlet.state.p = accumulator.outlet.state.p ($RES_SIM_305) (195|217) [SCAL] (1) accumulator.medium.phase = if $SEV_3 then 1 else 2 ($RES_SIM_130) (196|218) [SCAL] (1) singleSensorSelect3.inlet.state.T = twoPhaseSensorSelect1.inlet.state.T ($RES_SIM_306) (197|219) [SCAL] (1) singleSensorSelect3.inlet.state.T = flowResistance3.inlet.state.T ($RES_SIM_307) (198|220) [SCAL] (1) singleSensorSelect3.inlet.state.T = accumulator.outlet.state.T ($RES_SIM_308) (199|221) [SCAL] (1) receiver.Q_flow = 0.0 ($RES_SIM_133) (200|222) [SCAL] (1) singleSensorSelect3.inlet.state.d = twoPhaseSensorSelect1.inlet.state.d ($RES_SIM_309) (201|223) [SCAL] (1) $DER.receiver.U_med = receiver.h_in * receiver.m_flow_in + receiver.Q_flow + receiver.h_out * receiver.m_flow_out ($RES_SIM_134) (202|224) [SCAL] (1) $DER.receiver.M = receiver.m_flow_in + receiver.m_flow_out ($RES_SIM_135) (203|225) [SCAL] (1) receiver.r + receiver.p_in = 99999.99999999999 * receiver.medium.p_bar ($RES_SIM_136) (204|226) [SCAL] (1) $DER.receiver.m_flow_out * receiver.L = receiver.r_out - receiver.r_damping ($RES_SIM_137) (205|227) [SCAL] (1) $DER.receiver.m_flow_in * receiver.L = receiver.r_in - (receiver.r_damping + receiver.r) ($RES_SIM_138) (206|228) [SCAL] (1) singleSensorSelect5.inlet.state.d = twoPhaseSensorSelect.inlet.state.d ($RES_SIM_220) (207|229) [SCAL] (1) singleSensorSelect5.inlet.state.d = flowResistance2.inlet.state.d ($RES_SIM_221) (208|230) [SCAL] (1) singleSensorSelect5.inlet.state.h = source1.outlet.state.h ($RES_SIM_222) (209|231) [SCAL] (1) singleSensorSelect5.inlet.state.h = twoPhaseSensorSelect.inlet.state.h ($RES_SIM_223) (210|232) [SCAL] (1) singleSensorSelect5.inlet.state.h = flowResistance2.inlet.state.h ($RES_SIM_224) (211|233) [SCAL] (1) sink.r + sink.p = sink.p0_par ($RES_SIM_96) (212|234) [SCAL] (1) singleSensorSelect5.inlet.state.phase = source1.outlet.state.phase ($RES_SIM_225) (213|235) [SCAL] (1) accumulator.p_in = accumulator.state_in.p ($RES_BND_350) (214|236) [SCAL] (1) $DER.sink.inlet.m_flow * sink.L = sink.inlet.r - sink.r ($RES_SIM_97) (215|237) [SCAL] (1) singleSensorSelect5.inlet.state.phase = twoPhaseSensorSelect.inlet.state.phase ($RES_SIM_226) (216|238) [SCAL] (1) accumulator.h_in = if noEvent(accumulator.m_flow_in >= 0.0) then accumulator.state_in.h else accumulator.medium.h ($RES_BND_351) (217|239) [SCAL] (1) singleSensorSelect5.inlet.state.phase = flowResistance2.inlet.state.phase ($RES_SIM_227) (218|240) [SCAL] (1) accumulator.h_out = if noEvent((-accumulator.m_flow_out) >= 0.0) then accumulator.state_out.h else accumulator.medium.h ($RES_BND_352) (219|241) [SCAL] (1) accumulator.vapor_quality = max(0.0, min(1.0, accumulator.x)) ($RES_BND_353) (220|242) [SCAL] (1) accumulator.x = (accumulator.medium.h - accumulator.h_bubble) / (accumulator.h_dew - accumulator.h_bubble) ($RES_BND_354) (221|243) [SCAL] (1) accumulator.d_liq = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.BaseIF97.Regions.rhovl_p($FUN_17.psat, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.BaseIF97.Regions.boilingcurve_p($FUN_17.psat)) ($RES_BND_355) (222|244) [SCAL] (1) accumulator.d_gas = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.BaseIF97.Regions.rhovl_p($FUN_17.psat, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.BaseIF97.Regions.dewcurve_p($FUN_17.psat)) ($RES_BND_356) (223|245) [SCAL] (1) accumulator.h_bubble = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.BaseIF97.Regions.hvl_p($FUN_17.psat, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.BaseIF97.Regions.boilingcurve_p($FUN_17.psat)) - 1.0 ($RES_BND_357) (224|246) [SCAL] (1) accumulator.h_dew = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.BaseIF97.Regions.hvl_p($FUN_17.psat, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.BaseIF97.Regions.dewcurve_p($FUN_17.psat)) + 1.0 ($RES_BND_358) (225|247) [SCAL] (1) singleSensorSelect3.inlet.state.d = flowResistance3.inlet.state.d ($RES_SIM_310) (226|248) [SCAL] (1) sink.p = sink.inlet.state.p ($RES_BND_359) (227|249) [SCAL] (1) singleSensorSelect3.inlet.state.d = accumulator.outlet.state.d ($RES_SIM_311) (228|250) [SCAL] (1) singleSensorSelect3.inlet.state.h = twoPhaseSensorSelect1.inlet.state.h ($RES_SIM_312) (229|251) [SCAL] (1) singleSensorSelect3.inlet.state.h = flowResistance3.inlet.state.h ($RES_SIM_313) (230|252) [SCAL] (1) singleSensorSelect3.inlet.state.h = accumulator.outlet.state.h ($RES_SIM_314) (231|253) [SCAL] (1) singleSensorSelect3.inlet.state.phase = twoPhaseSensorSelect1.inlet.state.phase ($RES_SIM_315) (232|254) [SCAL] (1) singleSensorSelect3.inlet.state.phase = flowResistance3.inlet.state.phase ($RES_SIM_316) (233|255) [SCAL] (1) singleSensorSelect3.inlet.state.phase = accumulator.outlet.state.phase ($RES_SIM_317) (234|256) [SCAL] (1) receiver.h_pipe = smooth(1, if $SEV_1 then receiver.medium.h else if $SEV_2 then receiver.liquid_level_pipe * receiver.h_bubble + (1.0 - receiver.liquid_level_pipe) * receiver.h_dew else receiver.medium.h) ($RES_SIM_143) (235|257) [SCAL] (1) receiver.liquid_level_pipe = max(0.0, min(1.0, (receiver.liquid_level - receiver.pipe_low) / (receiver.pipe_high - receiver.pipe_low))) ($RES_SIM_144) (236|258) [SCAL] (1) receiver.liquid_level = max(0.0, min(1.0, (((1.0 - receiver.x) * receiver.M) / receiver.d_liq) / receiver.V_par)) ($RES_SIM_145) (237|259) [SCAL] (1) twoPhaseSensorSelect6.inlet.state.p = source.outlet.state.p ($RES_SIM_231) (238|260) [SCAL] (1) source.outlet.state.phase = 0 ($RES_SIM_407) (239|261) [SCAL] (1) twoPhaseSensorSelect6.inlet.state.p = singleSensorSelect6.inlet.state.p ($RES_SIM_232) (240|262) [SCAL] (1) source.outlet.state.h = source.h0_var ($RES_SIM_408) (241|263) [SCAL] (1) twoPhaseSensorSelect6.inlet.state.p = flowResistance1.inlet.state.p ($RES_SIM_233) (242|264) [SCAL] (1) source.outlet.state.d = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.rho_props_ph(source.p0_par, source.h0_var, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.waterBaseProp_ph(source.p0_par, source.h0_var, 0, 0)) ($RES_SIM_409) (243|265) [SCAL] (1) twoPhaseSensorSelect6.inlet.state.T = source.outlet.state.T ($RES_SIM_234) (244|266) [SCAL] (1) twoPhaseSensorSelect6.inlet.state.T = singleSensorSelect6.inlet.state.T ($RES_SIM_235) (245|267) [SCAL] (1) twoPhaseSensorSelect6.inlet.state.T = flowResistance1.inlet.state.T ($RES_SIM_236) (246|268) [SCAL] (1) flowResistance1.p_in = flowResistance1.inlet.state.p ($RES_BND_361) (247|269) [SCAL] (1) twoPhaseSensorSelect6.inlet.state.d = source.outlet.state.d ($RES_SIM_237) (248|270) [SCAL] (1) flowResistance1.h_out = flowResistance1.inlet.state.h ($RES_BND_362) (249|271) [SCAL] (1) twoPhaseSensorSelect6.inlet.state.d = singleSensorSelect6.inlet.state.d ($RES_SIM_238) (250|272) [SCAL] (1) flowResistance1.rho_in = max(flowResistance1.rho_min, flowResistance1.inlet.state.d) ($RES_BND_363) (251|273) [SCAL] (1) twoPhaseSensorSelect6.inlet.state.d = flowResistance1.inlet.state.d ($RES_SIM_239) (252|274) [SCAL] (1) flowResistance1.mu_in = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.dynamicViscosity(flowResistance1.inlet.state.d, flowResistance1.inlet.state.T, flowResistance1.inlet.state.p, flowResistance1.inlet.state.phase, true) ($RES_BND_364) (253|275) [SCAL] (1) flowResistance2.p_in = flowResistance2.inlet.state.p ($RES_BND_366) (254|276) [SCAL] (1) flowResistance2.h_out = flowResistance2.inlet.state.h ($RES_BND_367) (255|277) [SCAL] (1) flowResistance2.rho_in = max(flowResistance2.rho_min, flowResistance2.inlet.state.d) ($RES_BND_368) (256|278) [SCAL] (1) flowResistance2.mu_in = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.dynamicViscosity(flowResistance2.inlet.state.d, flowResistance2.inlet.state.T, flowResistance2.inlet.state.p, flowResistance2.inlet.state.phase, true) ($RES_BND_369) (257|279) [SCAL] (1) receiver.medium.phase = receiver.medium.state.phase ($RES_SIM_152) (258|280) [SCAL] (1) receiver.medium.d = receiver.medium.state.d ($RES_SIM_153) (259|281) [SCAL] (1) receiver.T_heatPort = receiver.medium.state.T ($RES_SIM_154) (260|282) [SCAL] (1) 99999.99999999999 * receiver.medium.p_bar = receiver.medium.state.p ($RES_SIM_155) (261|283) [SCAL] (1) receiver.medium.h = receiver.medium.state.h ($RES_SIM_156) (262|284) [SCAL] (1) receiver.medium.u = receiver.medium.h - (99999.99999999999 * receiver.medium.p_bar) / receiver.medium.d ($RES_SIM_158) (263|285) [SCAL] (1) source.outlet.state.T = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.T_props_ph(source.p0_par, source.h0_var, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.waterBaseProp_ph(source.p0_par, source.h0_var, 0, 0)) ($RES_SIM_410) (264|286) [SCAL] (1) receiver.medium.sat.psat = 99999.99999999999 * receiver.medium.p_bar ($RES_SIM_159) (265|287) [SCAL] (1) source.outlet.state.p = source.p0_par ($RES_SIM_411) (266|288) [SCAL] (1) receiver.state_out.phase = 0 ($RES_SIM_413) (267|289) [SCAL] (1) receiver.state_out.h = receiver.h_pipe ($RES_SIM_414) (268|290) [SCAL] (1) twoPhaseSensorSelect6.inlet.state.h = source.outlet.state.h ($RES_SIM_240) (269|291) [SCAL] (1) receiver.state_out.d = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.rho_props_ph(99999.99999999999 * receiver.medium.p_bar, receiver.h_pipe, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.waterBaseProp_ph(99999.99999999999 * receiver.medium.p_bar, receiver.h_pipe, 0, 0)) ($RES_SIM_415) (270|292) [SCAL] (1) twoPhaseSensorSelect6.inlet.state.h = singleSensorSelect6.inlet.state.h ($RES_SIM_241) (271|293) [SCAL] (1) receiver.state_out.T = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.T_props_ph(99999.99999999999 * receiver.medium.p_bar, receiver.h_pipe, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.waterBaseProp_ph(99999.99999999999 * receiver.medium.p_bar, receiver.h_pipe, 0, 0)) ($RES_SIM_416) (272|294) [SCAL] (1) twoPhaseSensorSelect6.inlet.state.h = flowResistance1.inlet.state.h ($RES_SIM_242) (273|295) [SCAL] (1) receiver.state_out.p = 99999.99999999999 * receiver.medium.p_bar ($RES_SIM_417) (274|296) [SCAL] (1) twoPhaseSensorSelect6.inlet.state.phase = source.outlet.state.phase ($RES_SIM_243) (275|297) [SCAL] (1) twoPhaseSensorSelect6.inlet.state.phase = singleSensorSelect6.inlet.state.phase ($RES_SIM_244) (276|298) [SCAL] (1) accumulator.state_out.phase = 0 ($RES_SIM_419) (277|299) [SCAL] (1) twoPhaseSensorSelect6.inlet.state.phase = flowResistance1.inlet.state.phase ($RES_SIM_245) (278|300) [SCAL] (1) flowResistance.p_in = flowResistance.inlet.state.p ($RES_BND_371) (279|301) [SCAL] (1) flowResistance.h_out = flowResistance.inlet.state.h ($RES_BND_372) (280|302) [SCAL] (1) flowResistance.rho_in = max(flowResistance.rho_min, flowResistance.inlet.state.d) ($RES_BND_373) (281|303) [SCAL] (1) singleSensorSelect2.inlet.state.p = accumulator.inlet.state.p ($RES_SIM_249) (282|304) [SCAL] (1) flowResistance.mu_in = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.dynamicViscosity(flowResistance.inlet.state.d, flowResistance.inlet.state.T, flowResistance.inlet.state.p, flowResistance.inlet.state.phase, true) ($RES_BND_374) (283|305) [SCAL] (1) flowResistance3.p_in = flowResistance3.inlet.state.p ($RES_BND_376) (284|306) [SCAL] (1) flowResistance3.h_out = flowResistance3.inlet.state.h ($RES_BND_377) (285|307) [SCAL] (1) flowResistance3.rho_in = max(flowResistance3.rho_min, flowResistance3.inlet.state.d) ($RES_BND_378) (286|308) [SCAL] (1) $FUN_22 = sqrt($FUN_21) ($RES_AUX_385) (287|309) [SCAL] (1) flowResistance3.mu_in = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.dynamicViscosity(flowResistance3.inlet.state.d, flowResistance3.inlet.state.T, flowResistance3.inlet.state.p, flowResistance3.inlet.state.phase, true) ($RES_BND_379) (288|310) [SCAL] (1) $FUN_21 = abs((2.0 * receiver.L) / (receiver.V_par * max(receiver.density_derp_h_set, 1e-10))) ($RES_AUX_386) (289|311) [SCAL] (1) $FUN_19 = sqrt($FUN_18) ($RES_AUX_388) (290|312) [SCAL] (1) $FUN_18 = abs((2.0 * accumulator.L) / (accumulator.V_par * max(accumulator.density_derp_h_set, 1e-10))) ($RES_AUX_389) (291|313) [SCAL] (1) receiver.medium.sat.Tsat = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.BaseIF97.Basic.tsat(99999.99999999999 * receiver.medium.p_bar) ($RES_SIM_160) (292|314) [SCAL] (1) receiver.T_heatPort = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.T_props_ph(99999.99999999999 * receiver.medium.p_bar, receiver.medium.h, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.waterBaseProp_ph(99999.99999999999 * receiver.medium.p_bar, receiver.medium.h, receiver.medium.phase, 0)) ($RES_SIM_161) (293|315) [SCAL] (1) receiver.medium.d = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.rho_props_ph(99999.99999999999 * receiver.medium.p_bar, receiver.medium.h, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.waterBaseProp_ph(99999.99999999999 * receiver.medium.p_bar, receiver.medium.h, receiver.medium.phase, 0)) ($RES_SIM_162) (294|316) [SCAL] (1) receiver.medium.phase = if $SEV_0 then 1 else 2 ($RES_SIM_163) (295|317) [SCAL] (1) source.L * $DER.source.outlet.m_flow = source.outlet.r ($RES_SIM_166) (296|318) [SCAL] (1) sink1.inlet.m_flow + 2e-4 * flowResistance.dp = 0.0 ($RES_SIM_169) (297|319) [SCAL] (1) accumulator.state_out.h = accumulator.h_pipe ($RES_SIM_420) (298|320) [SCAL] (1) accumulator.state_out.d = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.rho_props_ph(99999.99999999999 * accumulator.medium.p_bar, accumulator.h_pipe, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.waterBaseProp_ph(99999.99999999999 * accumulator.medium.p_bar, accumulator.h_pipe, 0, 0)) ($RES_SIM_421) (299|321) [SCAL] (1) accumulator.state_out.T = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.T_props_ph(99999.99999999999 * accumulator.medium.p_bar, accumulator.h_pipe, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.waterBaseProp_ph(99999.99999999999 * accumulator.medium.p_bar, accumulator.h_pipe, 0, 0)) ($RES_SIM_422) (300|322) [SCAL] (1) accumulator.state_out.p = 99999.99999999999 * accumulator.medium.p_bar ($RES_SIM_423) (301|323) [SCAL] (1) flowResistance1.outlet.state.phase = 0 ($RES_SIM_424) (302|324) [SCAL] (1) $SEV_0 = (receiver.medium.h < ThermofluidStream.Media.myMedia.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(receiver.medium.sat.psat, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.BaseIF97.Regions.boilingcurve_p(receiver.medium.sat.psat)) or receiver.medium.h > ThermofluidStream.Media.myMedia.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(receiver.medium.sat.psat, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.BaseIF97.Regions.dewcurve_p(receiver.medium.sat.psat))) or 99999.99999999999 * receiver.medium.p_bar > 2.2064e7 ($RES_EVT_469) (303|325) [SCAL] (1) singleSensorSelect2.inlet.state.p = twoPhaseSensorSelect4.inlet.state.p ($RES_SIM_250) (304|326) [SCAL] (1) flowResistance1.outlet.state.h = flowResistance1.h_out ($RES_SIM_425) (305|327) [SCAL] (1) singleSensorSelect2.inlet.state.p = flowResistance2.outlet.state.p ($RES_SIM_251) (306|328) [SCAL] (1) flowResistance1.outlet.state.d = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.rho_props_ph(flowResistance1.p_out, flowResistance1.h_out, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.waterBaseProp_ph(flowResistance1.p_out, flowResistance1.h_out, 0, 0)) ($RES_SIM_426) (307|329) [SCAL] (1) singleSensorSelect2.inlet.state.T = accumulator.inlet.state.T ($RES_SIM_252) (308|330) [SCAL] (1) flowResistance1.outlet.state.T = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.T_props_ph(flowResistance1.p_out, flowResistance1.h_out, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.waterBaseProp_ph(flowResistance1.p_out, flowResistance1.h_out, 0, 0)) ($RES_SIM_427) (309|331) [SCAL] (1) singleSensorSelect2.inlet.state.T = twoPhaseSensorSelect4.inlet.state.T ($RES_SIM_253) (310|332) [SCAL] (1) flowResistance1.outlet.state.p = flowResistance1.p_out ($RES_SIM_428) (311|333) [SCAL] (1) 2e-4 * $DER.flowResistance3.dp + $DER.sink.inlet.m_flow = 0.0 ($RES_SIM_485) (312|334) [SCAL] (1) 2e-4 * $DER.flowResistance2.dp + $DER.accumulator.m_flow_in = 0.0 ($RES_SIM_486) (313|335) [SCAL] (1) $DER.source.outlet.m_flow - 2e-4 * $DER.flowResistance1.dp = 0.0 ($RES_SIM_487) (314|336) [SCAL] (1) $DER.source1.outlet.m_flow - 2e-4 * $DER.flowResistance2.dp = 0.0 ($RES_SIM_488) (315|337) [SCAL] (1) 2e-4 * $DER.flowResistance1.dp + $DER.receiver.m_flow_in = 0.0 ($RES_SIM_489) (316|338) [SCAL] (1) $DER.sink1.inlet.m_flow + 2e-4 * $DER.flowResistance.dp = 0.0 ($RES_SIM_490) (317|339) [SCAL] (1) $DER.receiver.m_flow_out - 2e-4 * $DER.flowResistance.dp = 0.0 ($RES_SIM_491) (318|340) [SCAL] (1) $DER.accumulator.m_flow_out - 2e-4 * $DER.flowResistance3.dp = 0.0 ($RES_SIM_492) =================== Scalar Matching =================== variable to equation ********************** var 1 --> eqn 139 var 2 --> eqn 213 var 3 --> eqn 289 var 4 --> eqn 209 var 5 --> eqn 4 var 6 --> eqn 162 var 7 --> eqn 18 var 8 --> eqn 330 var 9 --> eqn 56 var 10 --> eqn 90 var 11 --> eqn 294 var 12 --> eqn 232 var 13 --> eqn 251 var 14 --> eqn 163 var 15 --> eqn 9 var 16 --> eqn 77 var 17 --> eqn 334 var 18 --> eqn 196 var 19 --> eqn 254 var 20 --> eqn 239 var 21 --> eqn 299 var 22 --> eqn 336 var 23 --> eqn 286 var 24 --> eqn 235 var 25 --> eqn 268 var 26 --> eqn 48 var 27 --> eqn 275 var 28 --> eqn 305 var 29 --> eqn 243 var 30 --> eqn 288 var 31 --> eqn 260 var 32 --> eqn 250 var 33 --> eqn 307 var 34 --> eqn 129 var 35 --> eqn 277 var 36 --> eqn 181 var 37 --> eqn 272 var 38 --> eqn 24 var 39 --> eqn 309 var 40 --> eqn 23 var 41 --> eqn 278 var 42 --> eqn 105 var 43 --> eqn 3 var 44 --> eqn 274 var 45 --> eqn 290 var 46 --> eqn 83 var 47 --> eqn -1 var 48 --> eqn 246 var 49 --> eqn 215 var 50 --> eqn 205 var 51 --> eqn 263 var 52 --> eqn 317 var 53 --> eqn 186 var 54 --> eqn 283 var 55 --> eqn 335 var 56 --> eqn 183 var 57 --> eqn 145 var 58 --> eqn 142 var 59 --> eqn 247 var 60 --> eqn 193 var 61 --> eqn 229 var 62 --> eqn 240 var 63 --> eqn 273 var 64 --> eqn 315 var 65 --> eqn 167 var 66 --> eqn 195 var 67 --> eqn 156 var 68 --> eqn 81 var 69 --> eqn 143 var 70 --> eqn 119 var 71 --> eqn 236 var 72 --> eqn 248 var 73 --> eqn 73 var 74 --> eqn 160 var 75 --> eqn 300 var 76 --> eqn 214 var 77 --> eqn 120 var 78 --> eqn 112 var 79 --> eqn 325 var 80 --> eqn 116 var 81 --> eqn 72 var 82 --> eqn 259 var 83 --> eqn 85 var 84 --> eqn 190 var 85 --> eqn 319 var 86 --> eqn 188 var 87 --> eqn 292 var 88 --> eqn 50 var 89 --> eqn 230 var 90 --> eqn 206 var 91 --> eqn 158 var 92 --> eqn 131 var 93 --> eqn 178 var 94 --> eqn 102 var 95 --> eqn 252 var 96 --> eqn 62 var 97 --> eqn 107 var 98 --> eqn 130 var 99 --> eqn 151 var 100 --> eqn 322 var 101 --> eqn 8 var 102 --> eqn 138 var 103 --> eqn 153 var 104 --> eqn 169 var 105 --> eqn 337 var 106 --> eqn 177 var 107 --> eqn 27 var 108 --> eqn 208 var 109 --> eqn 150 var 110 --> eqn 149 var 111 --> eqn 148 var 112 --> eqn 147 var 113 --> eqn 146 var 114 --> eqn 113 var 115 --> eqn 32 var 116 --> eqn 30 var 117 --> eqn 121 var 118 --> eqn 168 var 119 --> eqn 287 var 120 --> eqn 93 var 121 --> eqn 262 var 122 --> eqn 244 var 123 --> eqn 218 var 124 --> eqn 123 var 125 --> eqn 171 var 126 --> eqn 13 var 127 --> eqn 331 var 128 --> eqn 302 var 129 --> eqn 95 var 130 --> eqn 265 var 131 --> eqn 75 var 132 --> eqn 200 var 133 --> eqn 201 var 134 --> eqn 22 var 135 --> eqn 303 var 136 --> eqn -1 var 137 --> eqn 219 var 138 --> eqn 210 var 139 --> eqn 291 var 140 --> eqn 267 var 141 --> eqn 264 var 142 --> eqn 127 var 143 --> eqn 125 var 144 --> eqn 1 var 145 --> eqn 220 var 146 --> eqn 114 var 147 --> eqn 207 var 148 --> eqn 266 var 149 --> eqn 74 var 150 --> eqn 221 var 151 --> eqn 7 var 152 --> eqn 192 var 153 --> eqn 182 var 154 --> eqn 313 var 155 --> eqn 321 var 156 --> eqn 87 var 157 --> eqn 133 var 158 --> eqn 55 var 159 --> eqn 198 var 160 --> eqn 155 var 161 --> eqn 135 var 162 --> eqn 70 var 163 --> eqn 136 var 164 --> eqn 2 var 165 --> eqn 51 var 166 --> eqn 323 var 167 --> eqn 298 var 168 --> eqn 49 var 169 --> eqn 157 var 170 --> eqn 179 var 171 --> eqn 47 var 172 --> eqn 45 var 173 --> eqn 43 var 174 --> eqn 324 var 175 --> eqn 245 var 176 --> eqn 124 var 177 --> eqn 184 var 178 --> eqn 159 var 179 --> eqn 64 var 180 --> eqn 226 var 181 --> eqn -1 var 182 --> eqn 238 var 183 --> eqn 69 var 184 --> eqn 92 var 185 --> eqn 227 var 186 --> eqn 279 var 187 --> eqn 231 var 188 --> eqn 329 var 189 --> eqn 14 var 190 --> eqn 52 var 191 --> eqn 65 var 192 --> eqn 261 var 193 --> eqn 203 var 194 --> eqn 170 var 195 --> eqn 111 var 196 --> eqn 216 var 197 --> eqn 327 var 198 --> eqn 122 var 199 --> eqn 78 var 200 --> eqn 269 var 201 --> eqn 101 var 202 --> eqn 5 var 203 --> eqn 174 var 204 --> eqn 223 var 205 --> eqn 126 var 206 --> eqn 222 var 207 --> eqn 199 var 208 --> eqn 96 var 209 --> eqn 176 var 210 --> eqn 63 var 211 --> eqn 140 var 212 --> eqn 21 var 213 --> eqn 94 var 214 --> eqn 108 var 215 --> eqn 19 var 216 --> eqn 296 var 217 --> eqn 225 var 218 --> eqn 118 var 219 --> eqn 66 var 220 --> eqn 295 var 221 --> eqn 187 var 222 --> eqn 16 var 223 --> eqn 241 var 224 --> eqn 132 var 225 --> eqn 204 var 226 --> eqn 253 var 227 --> eqn 154 var 228 --> eqn 29 var 229 --> eqn 67 var 230 --> eqn 31 var 231 --> eqn 285 var 232 --> eqn 33 var 233 --> eqn 34 var 234 --> eqn 35 var 235 --> eqn 217 var 236 --> eqn 36 var 237 --> eqn 293 var 238 --> eqn -1 var 239 --> eqn 37 var 240 --> eqn 212 var 241 --> eqn 99 var 242 --> eqn 100 var 243 --> eqn 338 var 244 --> eqn 71 var 245 --> eqn 172 var 246 --> eqn 191 var 247 --> eqn 258 var 248 --> eqn 137 var 249 --> eqn 97 var 250 --> eqn 28 var 251 --> eqn 256 var 252 --> eqn 15 var 253 --> eqn 17 var 254 --> eqn 98 var 255 --> eqn 308 var 256 --> eqn 310 var 257 --> eqn 141 var 258 --> eqn 202 var 259 --> eqn 165 var 260 --> eqn 197 var 261 --> eqn 270 var 262 --> eqn 276 var 263 --> eqn 306 var 264 --> eqn 60 var 265 --> eqn 224 var 266 --> eqn 333 var 267 --> eqn 339 var 268 --> eqn 233 var 269 --> eqn 311 var 270 --> eqn 180 var 271 --> eqn 312 var 272 --> eqn 134 var 273 --> eqn 68 var 274 --> eqn 144 var 275 --> eqn 255 var 276 --> eqn 185 var 277 --> eqn 25 var 278 --> eqn 166 var 279 --> eqn 234 var 280 --> eqn 297 var 281 --> eqn 109 var 282 --> eqn 91 var 283 --> eqn 58 var 284 --> eqn 332 var 285 --> eqn 175 var 286 --> eqn 326 var 287 --> eqn 164 var 288 --> eqn 53 var 289 --> eqn 79 var 290 --> eqn 152 var 291 --> eqn 228 var 292 --> eqn 88 var 293 --> eqn 271 var 294 --> eqn 211 var 295 --> eqn 173 var 296 --> eqn 249 var 297 --> eqn 11 var 298 --> eqn 128 var 299 --> eqn 304 var 300 --> eqn 194 var 301 --> eqn 76 var 302 --> eqn 316 var 303 --> eqn 340 var 304 --> eqn 301 var 305 --> eqn 281 var 306 --> eqn 10 var 307 --> eqn 20 var 308 --> eqn 284 var 309 --> eqn 257 var 310 --> eqn 86 var 311 --> eqn 84 var 312 --> eqn 82 var 313 --> eqn 80 var 314 --> eqn 61 var 315 --> eqn 59 var 316 --> eqn 6 var 317 --> eqn 57 var 318 --> eqn 314 var 319 --> eqn 89 var 320 --> eqn 54 var 321 --> eqn 328 var 322 --> eqn 104 var 323 --> eqn 320 var 324 --> eqn 115 var 325 --> eqn 282 var 326 --> eqn 189 var 327 --> eqn 110 var 328 --> eqn 106 var 329 --> eqn 103 var 330 --> eqn 161 var 331 --> eqn 117 var 332 --> eqn 26 var 333 --> eqn 242 var 334 --> eqn 280 var 335 --> eqn 237 var 336 --> eqn 12 var 337 --> eqn 318 var 338 --> eqn 42 var 339 --> eqn 39 var 340 --> eqn 46 var 341 --> eqn 41 var 342 --> eqn 40 var 343 --> eqn 44 var 344 --> eqn 38 equation to variable ********************** eqn 1 --> var 144 eqn 2 --> var 164 eqn 3 --> var 43 eqn 4 --> var 5 eqn 5 --> var 202 eqn 6 --> var 316 eqn 7 --> var 151 eqn 8 --> var 101 eqn 9 --> var 15 eqn 10 --> var 306 eqn 11 --> var 297 eqn 12 --> var 336 eqn 13 --> var 126 eqn 14 --> var 189 eqn 15 --> var 252 eqn 16 --> var 222 eqn 17 --> var 253 eqn 18 --> var 7 eqn 19 --> var 215 eqn 20 --> var 307 eqn 21 --> var 212 eqn 22 --> var 134 eqn 23 --> var 40 eqn 24 --> var 38 eqn 25 --> var 277 eqn 26 --> var 332 eqn 27 --> var 107 eqn 28 --> var 250 eqn 29 --> var 228 eqn 30 --> var 116 eqn 31 --> var 230 eqn 32 --> var 115 eqn 33 --> var 232 eqn 34 --> var 233 eqn 35 --> var 234 eqn 36 --> var 236 eqn 37 --> var 239 eqn 38 --> var 344 eqn 39 --> var 339 eqn 40 --> var 342 eqn 41 --> var 341 eqn 42 --> var 338 eqn 43 --> var 173 eqn 44 --> var 343 eqn 45 --> var 172 eqn 46 --> var 340 eqn 47 --> var 171 eqn 48 --> var 26 eqn 49 --> var 168 eqn 50 --> var 88 eqn 51 --> var 165 eqn 52 --> var 190 eqn 53 --> var 288 eqn 54 --> var 320 eqn 55 --> var 158 eqn 56 --> var 9 eqn 57 --> var 317 eqn 58 --> var 283 eqn 59 --> var 315 eqn 60 --> var 264 eqn 61 --> var 314 eqn 62 --> var 96 eqn 63 --> var 210 eqn 64 --> var 179 eqn 65 --> var 191 eqn 66 --> var 219 eqn 67 --> var 229 eqn 68 --> var 273 eqn 69 --> var 183 eqn 70 --> var 162 eqn 71 --> var 244 eqn 72 --> var 81 eqn 73 --> var 73 eqn 74 --> var 149 eqn 75 --> var 131 eqn 76 --> var 301 eqn 77 --> var 16 eqn 78 --> var 199 eqn 79 --> var 289 eqn 80 --> var 313 eqn 81 --> var 68 eqn 82 --> var 312 eqn 83 --> var 46 eqn 84 --> var 311 eqn 85 --> var 83 eqn 86 --> var 310 eqn 87 --> var 156 eqn 88 --> var 292 eqn 89 --> var 319 eqn 90 --> var 10 eqn 91 --> var 282 eqn 92 --> var 184 eqn 93 --> var 120 eqn 94 --> var 213 eqn 95 --> var 129 eqn 96 --> var 208 eqn 97 --> var 249 eqn 98 --> var 254 eqn 99 --> var 241 eqn 100 --> var 242 eqn 101 --> var 201 eqn 102 --> var 94 eqn 103 --> var 329 eqn 104 --> var 322 eqn 105 --> var 42 eqn 106 --> var 328 eqn 107 --> var 97 eqn 108 --> var 214 eqn 109 --> var 281 eqn 110 --> var 327 eqn 111 --> var 195 eqn 112 --> var 78 eqn 113 --> var 114 eqn 114 --> var 146 eqn 115 --> var 324 eqn 116 --> var 80 eqn 117 --> var 331 eqn 118 --> var 218 eqn 119 --> var 70 eqn 120 --> var 77 eqn 121 --> var 117 eqn 122 --> var 198 eqn 123 --> var 124 eqn 124 --> var 176 eqn 125 --> var 143 eqn 126 --> var 205 eqn 127 --> var 142 eqn 128 --> var 298 eqn 129 --> var 34 eqn 130 --> var 98 eqn 131 --> var 92 eqn 132 --> var 224 eqn 133 --> var 157 eqn 134 --> var 272 eqn 135 --> var 161 eqn 136 --> var 163 eqn 137 --> var 248 eqn 138 --> var 102 eqn 139 --> var 1 eqn 140 --> var 211 eqn 141 --> var 257 eqn 142 --> var 58 eqn 143 --> var 69 eqn 144 --> var 274 eqn 145 --> var 57 eqn 146 --> var 113 eqn 147 --> var 112 eqn 148 --> var 111 eqn 149 --> var 110 eqn 150 --> var 109 eqn 151 --> var 99 eqn 152 --> var 290 eqn 153 --> var 103 eqn 154 --> var 227 eqn 155 --> var 160 eqn 156 --> var 67 eqn 157 --> var 169 eqn 158 --> var 91 eqn 159 --> var 178 eqn 160 --> var 74 eqn 161 --> var 330 eqn 162 --> var 6 eqn 163 --> var 14 eqn 164 --> var 287 eqn 165 --> var 259 eqn 166 --> var 278 eqn 167 --> var 65 eqn 168 --> var 118 eqn 169 --> var 104 eqn 170 --> var 194 eqn 171 --> var 125 eqn 172 --> var 245 eqn 173 --> var 295 eqn 174 --> var 203 eqn 175 --> var 285 eqn 176 --> var 209 eqn 177 --> var 106 eqn 178 --> var 93 eqn 179 --> var 170 eqn 180 --> var 270 eqn 181 --> var 36 eqn 182 --> var 153 eqn 183 --> var 56 eqn 184 --> var 177 eqn 185 --> var 276 eqn 186 --> var 53 eqn 187 --> var 221 eqn 188 --> var 86 eqn 189 --> var 326 eqn 190 --> var 84 eqn 191 --> var 246 eqn 192 --> var 152 eqn 193 --> var 60 eqn 194 --> var 300 eqn 195 --> var 66 eqn 196 --> var 18 eqn 197 --> var 260 eqn 198 --> var 159 eqn 199 --> var 207 eqn 200 --> var 132 eqn 201 --> var 133 eqn 202 --> var 258 eqn 203 --> var 193 eqn 204 --> var 225 eqn 205 --> var 50 eqn 206 --> var 90 eqn 207 --> var 147 eqn 208 --> var 108 eqn 209 --> var 4 eqn 210 --> var 138 eqn 211 --> var 294 eqn 212 --> var 240 eqn 213 --> var 2 eqn 214 --> var 76 eqn 215 --> var 49 eqn 216 --> var 196 eqn 217 --> var 235 eqn 218 --> var 123 eqn 219 --> var 137 eqn 220 --> var 145 eqn 221 --> var 150 eqn 222 --> var 206 eqn 223 --> var 204 eqn 224 --> var 265 eqn 225 --> var 217 eqn 226 --> var 180 eqn 227 --> var 185 eqn 228 --> var 291 eqn 229 --> var 61 eqn 230 --> var 89 eqn 231 --> var 187 eqn 232 --> var 12 eqn 233 --> var 268 eqn 234 --> var 279 eqn 235 --> var 24 eqn 236 --> var 71 eqn 237 --> var 335 eqn 238 --> var 182 eqn 239 --> var 20 eqn 240 --> var 62 eqn 241 --> var 223 eqn 242 --> var 333 eqn 243 --> var 29 eqn 244 --> var 122 eqn 245 --> var 175 eqn 246 --> var 48 eqn 247 --> var 59 eqn 248 --> var 72 eqn 249 --> var 296 eqn 250 --> var 32 eqn 251 --> var 13 eqn 252 --> var 95 eqn 253 --> var 226 eqn 254 --> var 19 eqn 255 --> var 275 eqn 256 --> var 251 eqn 257 --> var 309 eqn 258 --> var 247 eqn 259 --> var 82 eqn 260 --> var 31 eqn 261 --> var 192 eqn 262 --> var 121 eqn 263 --> var 51 eqn 264 --> var 141 eqn 265 --> var 130 eqn 266 --> var 148 eqn 267 --> var 140 eqn 268 --> var 25 eqn 269 --> var 200 eqn 270 --> var 261 eqn 271 --> var 293 eqn 272 --> var 37 eqn 273 --> var 63 eqn 274 --> var 44 eqn 275 --> var 27 eqn 276 --> var 262 eqn 277 --> var 35 eqn 278 --> var 41 eqn 279 --> var 186 eqn 280 --> var 334 eqn 281 --> var 305 eqn 282 --> var 325 eqn 283 --> var 54 eqn 284 --> var 308 eqn 285 --> var 231 eqn 286 --> var 23 eqn 287 --> var 119 eqn 288 --> var 30 eqn 289 --> var 3 eqn 290 --> var 45 eqn 291 --> var 139 eqn 292 --> var 87 eqn 293 --> var 237 eqn 294 --> var 11 eqn 295 --> var 220 eqn 296 --> var 216 eqn 297 --> var 280 eqn 298 --> var 167 eqn 299 --> var 21 eqn 300 --> var 75 eqn 301 --> var 304 eqn 302 --> var 128 eqn 303 --> var 135 eqn 304 --> var 299 eqn 305 --> var 28 eqn 306 --> var 263 eqn 307 --> var 33 eqn 308 --> var 255 eqn 309 --> var 39 eqn 310 --> var 256 eqn 311 --> var 269 eqn 312 --> var 271 eqn 313 --> var 154 eqn 314 --> var 318 eqn 315 --> var 64 eqn 316 --> var 302 eqn 317 --> var 52 eqn 318 --> var 337 eqn 319 --> var 85 eqn 320 --> var 323 eqn 321 --> var 155 eqn 322 --> var 100 eqn 323 --> var 166 eqn 324 --> var 174 eqn 325 --> var 79 eqn 326 --> var 286 eqn 327 --> var 197 eqn 328 --> var 321 eqn 329 --> var 188 eqn 330 --> var 8 eqn 331 --> var 127 eqn 332 --> var 284 eqn 333 --> var 266 eqn 334 --> var 17 eqn 335 --> var 55 eqn 336 --> var 22 eqn 337 --> var 105 eqn 338 --> var 243 eqn 339 --> var 267 eqn 340 --> var 303 " [Timeout remaining time 659] [Calling sys.exit(0), Time elapsed: 4.68084289401304] Failed to read output from testmodel.py, exit status != 0: 0.953410931979306 0.970460085 0.12701307 Calling exit ...