Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_dev_ThermofluidStream.FlowControl.Tests.PCV.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 0.001348/0.001348, allocations: 104.3 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 0.00154/0.00154, allocations: 210.2 kB / 23.06 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 1.521/1.521, allocations: 230.6 MB / 256.9 MB, free: 7.773 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 0.9258/0.9258, allocations: 100.9 MB / 414.2 MB, free: 2.828 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.FlowControl.Tests.PCV,tolerance=1e-06,outputFormat="mat",numberOfIntervals=2500,variableFilter="Time|pCV.inlet.m_flow|source.outlet.m_flow|source1.outlet.m_flow|source2.outlet.m_flow|volumeFlex.M|volumeFlex.U_med|volumeFlex1.M|volumeFlex1.U_med|volumeFlex2.M|volumeFlex2.U_med|volumeFlex2.m_flow_out|volumeFlex3.M|volumeFlex3.U_med",fileNamePrefix="ThermofluidStream_dev_ThermofluidStream.FlowControl.Tests.PCV") translateModel(ThermofluidStream.FlowControl.Tests.PCV,tolerance=1e-06,outputFormat="mat",numberOfIntervals=2500,variableFilter="Time|pCV.inlet.m_flow|source.outlet.m_flow|source1.outlet.m_flow|source2.outlet.m_flow|volumeFlex.M|volumeFlex.U_med|volumeFlex1.M|volumeFlex1.U_med|volumeFlex2.M|volumeFlex2.U_med|volumeFlex2.m_flow_out|volumeFlex3.M|volumeFlex3.U_med",fileNamePrefix="ThermofluidStream_dev_ThermofluidStream.FlowControl.Tests.PCV") [Timeout 660] "Notification: Performance of FrontEnd - Absyn->SCode: time 2.243e-05/2.243e-05, allocations: 5.234 kB / 0.5654 GB, free: 35.49 MB / 446.1 MB Notification: Performance of NFInst.instantiate(ThermofluidStream.FlowControl.Tests.PCV): time 0.2122/0.2122, allocations: 165.7 MB / 0.7271 GB, free: 10.45 MB / 0.5606 GB Notification: Performance of NFInst.instExpressions: time 0.02523/0.2374, allocations: 16.34 MB / 0.7431 GB, free: 10.06 MB / 0.5762 GB Notification: Performance of NFInst.updateImplicitVariability: time 0.002995/0.2404, allocations: 99.12 kB / 0.7432 GB, free: 9.965 MB / 0.5762 GB Notification: Performance of NFTyping.typeComponents: time 0.003117/0.2435, allocations: 0.8924 MB / 0.7441 GB, free: 9.066 MB / 0.5762 GB Notification: Performance of NFTyping.typeBindings: time 0.00806/0.2516, allocations: 2.381 MB / 0.7464 GB, free: 6.672 MB / 0.5762 GB Notification: Performance of NFTyping.typeClassSections: time 0.005866/0.2574, allocations: 1.866 MB / 0.7482 GB, free: 4.812 MB / 0.5762 GB Notification: Performance of NFFlatten.flatten: time 0.006821/0.2643, allocations: 4.178 MB / 0.7523 GB, free: 0.6172 MB / 0.5762 GB Notification: Performance of NFFlatten.resolveConnections: time 0.0007308/0.265, allocations: 259.3 kB / 0.7525 GB, free: 348 kB / 0.5762 GB Notification: Performance of NFEvalConstants.evaluate: time 0.4379/0.7029, allocations: 1.823 MB / 0.7543 GB, free: 7.461 MB / 0.5762 GB Notification: Performance of NFSimplifyModel.simplify: time 0.00391/0.7068, allocations: 1.493 MB / 0.7558 GB, free: 7.461 MB / 0.5762 GB Notification: Performance of NFPackage.collectConstants: time 0.0008763/0.7076, allocations: 177.5 kB / 0.7559 GB, free: 7.461 MB / 0.5762 GB Notification: Performance of NFFlatten.collectFunctions: time 0.007674/0.7153, allocations: 2.557 MB / 0.7584 GB, free: 7.461 MB / 0.5762 GB Notification: Performance of combineBinaries: time 0.006831/0.7221, allocations: 4.637 MB / 0.763 GB, free: 5.953 MB / 0.5762 GB Notification: Performance of replaceArrayConstructors: time 0.003034/0.7252, allocations: 2.917 MB / 0.7658 GB, free: 4.191 MB / 0.5762 GB Notification: Performance of NFVerifyModel.verify: time 0.001216/0.7264, allocations: 208.7 kB / 0.766 GB, free: 4.191 MB / 0.5762 GB Notification: Performance of FrontEnd: time 0.0006339/0.727, allocations: 161.6 kB / 0.7662 GB, free: 4.172 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: 356 (333) * Number of variables: 364 (364) Notification: Performance of [SIM] Bindings: time 0.01506/0.7421, allocations: 10.38 MB / 0.7763 GB, free: 96 kB / 0.5762 GB Notification: Performance of [SIM] FunctionAlias: time 0.002535/0.7446, allocations: 1.169 MB / 0.7774 GB, free: 15.94 MB / 0.5919 GB Notification: Performance of [SIM] Early Inline: time 0.009568/0.7542, allocations: 5.646 MB / 0.783 GB, free: 15.79 MB / 0.5919 GB Notification: Performance of [SIM] Simplify 1: time 0.003176/0.7574, allocations: 0.939 MB / 0.7839 GB, free: 15.53 MB / 0.5919 GB Notification: Performance of [SIM] Alias: time 0.01305/0.7704, allocations: 6.587 MB / 0.7903 GB, free: 13.68 MB / 0.5919 GB Notification: Performance of [SIM] Simplify 2: time 0.001849/0.7723, allocations: 0.8049 MB / 0.7911 GB, free: 13.42 MB / 0.5919 GB Notification: Performance of [SIM] Remove Stream: time 0.0008066/0.7731, allocations: 446.7 kB / 0.7915 GB, free: 13.3 MB / 0.5919 GB Notification: Performance of [SIM] Detect States: time 0.001373/0.7744, allocations: 1.043 MB / 0.7925 GB, free: 13.1 MB / 0.5919 GB Notification: Performance of [SIM] Events: time 0.001023/0.7755, allocations: 0.5599 MB / 0.7931 GB, free: 12.91 MB / 0.5919 GB Notification: Performance of [SIM] Partitioning: time 0.002432/0.7779, allocations: 1.951 MB / 0.795 GB, free: 12.58 MB / 0.5919 GB Error: Internal error NBSorting.tarjan failed to sort system: System Variables (85/85) ************************** (1|1) [ALGB] (1) output Real pCV1.outlet.state.T (start = 288.15, min = 273.15, max = 373.15, nominal = 300.0) (2|2) [ALGB] (1) Real volumeFlex.Q_flow (3|3) [ALGB] (1) Real flowResistance.inlet.r (4|4) [ALGB] (1) protected Real flowResistance.h_out (5|5) [ALGB] (1) Real $FUN_13 (6|6) [DER-] (1) Real $DER.volumeFlex2.U_med (7|7) [ALGB] (1) Real $FUN_12 (8|8) [ALGB] (1) Real volumeFlex2.medium.state.T (start = 288.15, min = 273.15, max = 373.15, nominal = 300.0) (9|9) [ALGB] (1) Real volumeFlex.medium.d (start = 1.0, min = 0.0, max = 1e5, nominal = 1.0) (10|10) [ALGB] (1) Real $FUN_11 (11|11) [ALGB] (1) Real $FUN_10 (12|12) [ALGB] (1) Real volumeFlex.medium.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (13|13) [ALGB] (1) protected Real volumeFlex2.h_out = if noEvent((-volumeFlex2.m_flow_out) >= 0.0) then ThermofluidStream.FlowControl.Tests.PCV.volumeFlex2.Medium.specificEnthalpy(volumeFlex2.state_out) else 1005.45 * ((-298.15) + volumeFlex2.T_heatPort) (14|14) [ALGB] (1) protected Real pCV1.h_out (15|15) [ALGB] (1) protected Real flowResistance.p_out (16|16) [ALGB] (1) output Real flowResistance.outlet.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (17|17) [ALGB] (1) protected Real pCV1.p_in = ThermofluidStream.FlowControl.Tests.PCV.pCV1.Medium.pressure(pCV1.inlet.state) (18|18) [DER-] (1) Real $DER.volumeFlex2.M (19|19) [ALGB] (1) protected Real volumeFlex2.state_out.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (20|20) [ALGB] (1) Real volumeFlex.medium.u (min = -1e8, max = 1e8, nominal = 1e6) (21|21) [ALGB] (1) Real volumeFlex.V (22|22) [ALGB] (1) Real volumeFlex2.medium.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (23|23) [ALGB] (1) input Real flowResistance.inlet.state.T (start = 288.15, min = 273.15, max = 373.15, nominal = 300.0) (24|24) [ALGB] (1) Real flowResistance.dp (25|25) [ALGB] (1) input Real pCV1.inlet.state.T (start = 288.15, min = 273.15, max = 373.15, nominal = 300.0) (26|26) [ALGB] (1) input Real flowResistance.inlet.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (27|27) [ALGB] (1) output Real volumeFlex2.outlet.state.T = volumeFlex2.state_out.T (start = 288.15, min = 273.15, max = 373.15, nominal = 300.0) (28|28) [ALGB] (1) input Real volumeFlex.inlet.state.p = volumeFlex.state_in.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (29|29) [DISC] (1) Boolean $SEV_26 (30|30) [ALGB] (1) protected Real volumeFlex.h_out = if noEvent((-0.0) >= 0.0) then ThermofluidStream.FlowControl.Tests.PCV.volumeFlex.Medium.specificEnthalpy(volumeFlex.state_out) else 1005.45 * ((-298.15) + volumeFlex.T_heatPort) (31|31) [DISC] (1) Boolean $SEV_24 (32|32) [ALGB] (1) Real volumeFlex.medium.p_bar = Modelica.Units.Conversions.to_bar(99999.99999999999 * volumeFlex.medium.p_bar) (min = 0.0) (33|33) [DISC] (1) Boolean $SEV_23 (34|34) [ALGB] (1) output Real volumeFlex2.outlet.state.p = volumeFlex2.state_out.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (35|35) [ALGB] (1) protected Real flowResistance.rho_in = max(flowResistance.rho_min, ThermofluidStream.FlowControl.Tests.PCV.flowResistance.Medium.density(flowResistance.inlet.state)) (min = 0.0) (36|36) [DISC] (1) Boolean $SEV_21 (37|37) [DISC] (1) Boolean $SEV_20 (38|38) [ALGB] (1) protected Real volumeFlex.state_in.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (39|39) [ALGB] (1) protected Real volumeFlex.d = volumeFlex.k_volume_damping * sqrt(abs((2.0 * volumeFlex.L) / (volumeFlex.V * max(volumeFlex.density_derp_h, 1e-10)))) (40|40) [ALGB] (1) Real volumeFlex2.medium.u (min = -1e8, max = 1e8, nominal = 1e6) (41|41) [ALGB] (1) protected Real volumeFlex2.density_derp_h (42|42) [ALGB] (1) protected Real volumeFlex2.p_in = ThermofluidStream.FlowControl.Tests.PCV.volumeFlex2.Medium.pressure(volumeFlex2.state_in) (43|43) [ALGB] (1) protected Real volumeFlex2.r_out (44|44) [ALGB] (1) protected Real volumeFlex2.T_heatPort (start = 288.15, min = 273.15, max = 373.15, nominal = 300.0) (45|45) [ALGB] (1) Real volumeFlex2.medium.d (start = 1.0, min = 0.0, max = 1e5, nominal = 1.0) (46|46) [ALGB] (1) output Real pCV1.outlet.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (47|47) [ALGB] (1) protected Real volumeFlex.density_derp_h (48|48) [ALGB] (1) output Real flowResistance.outlet.state.T (start = 288.15, min = 273.15, max = 373.15, nominal = 300.0) (49|49) [DISC] (1) Boolean $SEV_19 (50|50) [ALGB] (1) protected Real volumeFlex.r (51|51) [ALGB] (1) protected Real pCV1.p_out (52|52) [DISC] (1) Boolean $SEV_17 (53|53) [DISC] (1) Boolean $SEV_15 (54|54) [ALGB] (1) protected Real volumeFlex2.r_in (55|55) [ALGB] (1) protected Real volumeFlex.r_damping = volumeFlex.d * der(volumeFlex.M) (56|56) [ALGB] (1) input Real volumeFlex.inlet.state.T = volumeFlex.state_in.T (start = 288.15, min = 273.15, max = 373.15, nominal = 300.0) (57|57) [ALGB] (1) protected Real volumeFlex2.r_damping = volumeFlex2.d * der(volumeFlex2.M) (58|58) [ALGB] (1) Real volumeFlex.medium.state.T (start = 288.15, min = 273.15, max = 373.15, nominal = 300.0) (59|59) [ALGB] (1) protected Real volumeFlex.h_in = if noEvent((-volumeFlex2.m_flow_out) >= 0.0) then ThermofluidStream.FlowControl.Tests.PCV.volumeFlex.Medium.specificEnthalpy(volumeFlex.state_in) else 1005.45 * ((-298.15) + volumeFlex.T_heatPort) (60|60) [ALGB] (1) Real volumeFlex2.Q_flow (61|61) [ALGB] (1) protected Real pCV1.dp_raw (62|62) [ALGB] (1) protected Real volumeFlex.state_in.T (start = 288.15, min = 273.15, max = 373.15, nominal = 300.0) (63|63) [ALGB] (1) Real pCV1.dp (64|64) [ALGB] (1) protected Real volumeFlex.r_out (65|65) [ALGB] (1) protected Real volumeFlex2.r (66|66) [ALGB] (1) Real pCV1.dr_corr (67|67) [ALGB] (1) protected Real volumeFlex2.d = volumeFlex2.k_volume_damping * sqrt(abs((2.0 * volumeFlex2.L) / (volumeFlex2.V * max(volumeFlex2.density_derp_h, 1e-10)))) (68|68) [ALGB] (1) protected Real volumeFlex2.state_out.T (start = 288.15, min = 273.15, max = 373.15, nominal = 300.0) (69|69) [ALGB] (1) protected Real flowResistance.p_in = ThermofluidStream.FlowControl.Tests.PCV.flowResistance.Medium.pressure(flowResistance.inlet.state) (70|70) [ALGB] (1) Real volumeFlex2.V (71|71) [DISC] (1) Boolean $SEV_5 (72|72) [ALGB] (1) protected Real volumeFlex.T_heatPort (start = 288.15, min = 273.15, max = 373.15, nominal = 300.0) (73|73) [DISC] (1) Boolean $SEV_4 (74|74) [DISC] (1) Boolean $SEV_3 (75|75) [ALGB] (1) protected Real volumeFlex.state_out.T (start = 288.15, min = 273.15, max = 373.15, nominal = 300.0) (76|76) [DER-] (1) Real $DER.volumeFlex.U_med (77|77) [ALGB] (1) protected Real volumeFlex2.state_in.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (78|78) [ALGB] (1) protected Real volumeFlex.p_in = ThermofluidStream.FlowControl.Tests.PCV.volumeFlex.Medium.pressure(volumeFlex.state_in) (79|79) [ALGB] (1) Real volumeFlex2.medium.p_bar = Modelica.Units.Conversions.to_bar(99999.99999999999 * volumeFlex2.medium.p_bar) (min = 0.0) (80|80) [ALGB] (1) protected Real volumeFlex.state_out.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (81|81) [ALGB] (1) Real flowResistance.dr_corr (82|82) [ALGB] (1) protected Real volumeFlex.r_in (83|83) [DER-] (1) Real $DER.volumeFlex.M (84|84) [ALGB] (1) input Real pCV1.inlet.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (85|85) [DER-] (1) Real $DER.volumeFlex2.m_flow_out System Equations (77/81) ************************** (1|1) [RECD] (2) volumeFlex.state_out = volumeFlex.medium.state ($RES_SIM_172) (2|3) [SCAL] (1) volumeFlex2.medium.u = 1005.45 * ((-298.15) + volumeFlex2.T_heatPort) - 287.0509010514002 * volumeFlex2.T_heatPort ($RES_SIM_211) (3|4) [SCAL] (1) 99999.99999999999 * volumeFlex.medium.p_bar = volumeFlex.p_ref + volumeFlex.K * ((-1.0) + volumeFlex.V / volumeFlex.V_ref) ($RES_SIM_174) (4|5) [SCAL] (1) volumeFlex.density_derp_h = (volumeFlex.medium.d * volumeFlex.V_ref) / (volumeFlex.K * volumeFlex.V) ($RES_SIM_175) (5|6) [SCAL] (1) volumeFlex.d = volumeFlex.k_volume_damping * $FUN_11 ($RES_BND_303) (6|7) [SCAL] (1) volumeFlex.medium.state.p = 99999.99999999999 * volumeFlex.medium.p_bar ($RES_SIM_179) (7|8) [SCAL] (1) volumeFlex.r_damping = volumeFlex.d * $DER.volumeFlex.M ($RES_BND_304) (8|9) [SCAL] (1) $SEV_15 = volumeFlex2.T_heatPort >= 273.15 and volumeFlex2.T_heatPort <= 373.15 ($RES_EVT_448) (9|10) [SCAL] (1) volumeFlex.p_in = volumeFlex.state_in.p ($RES_BND_305) (10|11) [SCAL] (1) volumeFlex.h_in = if noEvent((-volumeFlex2.m_flow_out) >= 0.0) then 1005.45 * ((-298.15) + volumeFlex.state_in.T) else 1005.45 * ((-298.15) + volumeFlex.T_heatPort) ($RES_BND_306) (11|12) [SCAL] (1) volumeFlex.h_out = 1005.45 * ((-298.15) + volumeFlex.state_out.T) ($RES_BND_307) (12|13) [SCAL] (1) pCV1.p_in = pCV1.inlet.state.p ($RES_BND_309) (13|14) [SCAL] (1) -flowResistance.dp = ThermofluidStream.FlowControl.Tests.PCV.flowResistance.pLoss(-volumeFlex2.m_flow_out, flowResistance.rho_in, 1.82e-5, 0.5 * flowResistance.D_h, flowResistance.l, 1e-7, ThermofluidStream.Processes.Internal.Material.other) ($RES_AUX_382) (14|15) [SCAL] (1) volumeFlex.medium.state.T = volumeFlex.T_heatPort ($RES_SIM_180) (15|16) [SCAL] (1) volumeFlex.medium.d = (0.0034837027033785095 * (99999.99999999999 * volumeFlex.medium.p_bar)) / volumeFlex.T_heatPort ($RES_SIM_182) (16|17) [SCAL] (1) $SEV_17 = 99999.99999999999 * volumeFlex2.medium.p_bar >= 0.0 ($RES_EVT_450) (17|18) [SCAL] (1) volumeFlex.medium.u = 1005.45 * ((-298.15) + volumeFlex.T_heatPort) - 287.0509010514002 * volumeFlex.T_heatPort ($RES_SIM_184) (18|19) [SCAL] (1) $SEV_19 = (-volumeFlex2.m_flow_out) > volumeFlex2.m_flow_assert ($RES_EVT_452) (19|20) [SCAL] (1) $SEV_20 = volumeFlex2.M > 0.0 ($RES_EVT_453) (20|21) [SCAL] (1) pCV1.h_out = 1005.45 * ((-298.15) + pCV1.inlet.state.T) ($RES_BND_310) (21|22) [SCAL] (1) $SEV_21 = volumeFlex.T_heatPort >= 273.15 and volumeFlex.T_heatPort <= 373.15 ($RES_EVT_454) (22|23) [SCAL] (1) $SEV_23 = 99999.99999999999 * volumeFlex.medium.p_bar >= 0.0 ($RES_EVT_456) (23|24) [SCAL] (1) $SEV_24 = (-volumeFlex2.m_flow_out) > volumeFlex.m_flow_assert ($RES_EVT_457) (24|25) [SCAL] (1) $SEV_26 = volumeFlex.M > 0.0 ($RES_EVT_459) (25|26) [SCAL] (1) volumeFlex2.state_in.p = 101325.0 ($RES_SIM_386) (26|27) [SCAL] (1) pCV1.outlet.state.p = pCV1.p_out ($RES_SIM_389) (27|28) [SCAL] (1) pCV1.dr_corr = (pCV1.p_in + pCV1.dp) - pCV1.p_out ($RES_SIM_153) (28|29) [SCAL] (1) pCV1.p_out = max(pCV1.p_min, pCV1.p_in + pCV1.dp) ($RES_SIM_154) (29|30) [SCAL] (1) volumeFlex2.Q_flow = 0.0 ($RES_SIM_190) (30|31) [SCAL] (1) flowResistance.inlet.r = (pCV1.dr_corr + volumeFlex2.r_out) - (-$DER.volumeFlex2.m_flow_out) * pCV1.L ($RES_SIM_155) (31|32) [SCAL] (1) $DER.volumeFlex2.U_med = volumeFlex2.Q_flow + volumeFlex2.h_out * volumeFlex2.m_flow_out ($RES_SIM_191) (32|33) [SCAL] (1) $DER.volumeFlex2.M = volumeFlex2.m_flow_out ($RES_SIM_192) (33|34) [SCAL] (1) volumeFlex2.r + volumeFlex2.p_in = 99999.99999999999 * volumeFlex2.medium.p_bar ($RES_SIM_193) (34|35) [SCAL] (1) pCV1.dp_raw = pCV1.pressure_set_par - pCV1.p_in ($RES_SIM_158) (35|36) [SCAL] (1) $DER.volumeFlex2.m_flow_out * volumeFlex2.L = volumeFlex2.r_out - volumeFlex2.r_damping ($RES_SIM_194) (36|37) [SCAL] (1) pCV1.dp = smooth(1, if $SEV_3 then min(0.0, pCV1.dp_raw) else if $SEV_4 then 0.0 else if $SEV_5 then 0.5 * min(0.0, pCV1.dp_raw) - 0.25 * min(0.0, pCV1.dp_raw) * ((-3.0) + ((-(pCV1.m_flow_reg + volumeFlex2.m_flow_out)) / pCV1.m_flow_reg) ^ 2.0) * ((-(pCV1.m_flow_reg + volumeFlex2.m_flow_out)) / pCV1.m_flow_reg) else 0.5 * min(0.0, pCV1.dp_raw)) ($RES_SIM_159) (37|38) [SCAL] (1) 0.0 = volumeFlex2.r_in - (volumeFlex2.r_damping + volumeFlex2.r) ($RES_SIM_195) (38|39) [SCAL] (1) flowResistance.p_in = flowResistance.inlet.state.p ($RES_BND_321) (39|40) [SCAL] (1) flowResistance.h_out = 1005.45 * ((-298.15) + flowResistance.inlet.state.T) ($RES_BND_322) (40|41) [SCAL] (1) flowResistance.rho_in = max(flowResistance.rho_min, (0.0034837027033785095 * flowResistance.inlet.state.p) / flowResistance.inlet.state.T) ($RES_BND_323) (41|42) [RECD] (2) volumeFlex2.state_out = volumeFlex2.medium.state ($RES_SIM_199) (42|44) [SCAL] (1) flowResistance.inlet.state.T = pCV1.outlet.state.T ($RES_SIM_276) (43|45) [SCAL] (1) flowResistance.inlet.state.p = pCV1.outlet.state.p ($RES_SIM_277) (44|46) [SCAL] (1) volumeFlex.inlet.state.T = flowResistance.outlet.state.T ($RES_SIM_279) (45|47) [RECD] (2) volumeFlex2.outlet.state = volumeFlex2.state_out ($RES_BND_366) (46|49) [RECD] (2) volumeFlex.inlet.state = volumeFlex.state_in ($RES_BND_367) (47|51) [SCAL] (1) pCV1.outlet.state.T = 298.15 + 9.945795414988312e-4 * pCV1.h_out ($RES_SIM_390) (48|52) [SCAL] (1) flowResistance.outlet.state.p = flowResistance.p_out ($RES_SIM_392) (49|53) [SCAL] (1) flowResistance.outlet.state.T = 298.15 + 9.945795414988312e-4 * flowResistance.h_out ($RES_SIM_393) (50|54) [SCAL] (1) flowResistance.dr_corr = (flowResistance.p_in + flowResistance.dp) - flowResistance.p_out ($RES_SIM_120) (51|55) [SCAL] (1) flowResistance.p_out = max(flowResistance.p_min, flowResistance.p_in + flowResistance.dp) ($RES_SIM_121) (52|56) [SCAL] (1) volumeFlex.r_in = (flowResistance.dr_corr + flowResistance.inlet.r) - (-$DER.volumeFlex2.m_flow_out) * flowResistance.L ($RES_SIM_122) (53|57) [SCAL] (1) volumeFlex.Q_flow = 0.0 ($RES_SIM_163) (54|58) [SCAL] (1) 99999.99999999999 * volumeFlex2.medium.p_bar = volumeFlex2.p_ref + volumeFlex2.K * ((-1.0) + volumeFlex2.V / volumeFlex2.V_ref) ($RES_SIM_201) (55|59) [SCAL] (1) $DER.volumeFlex.U_med = volumeFlex.Q_flow - volumeFlex.h_in * volumeFlex2.m_flow_out ($RES_SIM_164) (56|60) [SCAL] (1) volumeFlex2.density_derp_h = (volumeFlex2.medium.d * volumeFlex2.V_ref) / (volumeFlex2.K * volumeFlex2.V) ($RES_SIM_202) (57|61) [SCAL] (1) $DER.volumeFlex.M = -volumeFlex2.m_flow_out ($RES_SIM_165) (58|62) [SCAL] (1) volumeFlex.r + volumeFlex.p_in = 99999.99999999999 * volumeFlex.medium.p_bar ($RES_SIM_166) (59|63) [SCAL] (1) 0.0 = volumeFlex.r_out - volumeFlex.r_damping ($RES_SIM_167) (60|64) [SCAL] (1) (-$DER.volumeFlex2.m_flow_out) * volumeFlex.L = volumeFlex.r_in - (volumeFlex.r_damping + volumeFlex.r) ($RES_SIM_168) (61|65) [SCAL] (1) volumeFlex2.medium.state.p = 99999.99999999999 * volumeFlex2.medium.p_bar ($RES_SIM_206) (62|66) [SCAL] (1) $SEV_3 = -(pCV1.m_flow_reg + volumeFlex2.m_flow_out) > pCV1.m_flow_reg ($RES_EVT_436) (63|67) [SCAL] (1) volumeFlex2.medium.state.T = volumeFlex2.T_heatPort ($RES_SIM_207) (64|68) [SCAL] (1) $SEV_4 = -(pCV1.m_flow_reg + volumeFlex2.m_flow_out) < (-pCV1.m_flow_reg) ($RES_EVT_437) (65|69) [SCAL] (1) $SEV_5 = pCV1.m_flow_reg > 0.0 ($RES_EVT_438) (66|70) [SCAL] (1) volumeFlex2.medium.d = (0.0034837027033785095 * (99999.99999999999 * volumeFlex2.medium.p_bar)) / volumeFlex2.T_heatPort ($RES_SIM_209) (67|71) [SCAL] (1) volumeFlex.inlet.state.p = flowResistance.outlet.state.p ($RES_SIM_280) (68|72) [SCAL] (1) volumeFlex2.d = volumeFlex2.k_volume_damping * $FUN_13 ($RES_BND_294) (69|73) [SCAL] (1) volumeFlex2.outlet.state.T = pCV1.inlet.state.T ($RES_SIM_282) (70|74) [SCAL] (1) volumeFlex2.r_damping = volumeFlex2.d * $DER.volumeFlex2.M ($RES_BND_295) (71|75) [SCAL] (1) volumeFlex2.outlet.state.p = pCV1.inlet.state.p ($RES_SIM_283) (72|76) [SCAL] (1) volumeFlex2.p_in = volumeFlex2.state_in.p ($RES_BND_296) (73|77) [SCAL] (1) $FUN_13 = sqrt($FUN_12) ($RES_AUX_370) (74|78) [SCAL] (1) $FUN_12 = abs((2.0 * volumeFlex2.L) / (volumeFlex2.V * max(volumeFlex2.density_derp_h, 1e-10))) ($RES_AUX_371) (75|79) [SCAL] (1) volumeFlex2.h_out = if noEvent((-volumeFlex2.m_flow_out) >= 0.0) then 1005.45 * ((-298.15) + volumeFlex2.state_out.T) else 1005.45 * ((-298.15) + volumeFlex2.T_heatPort) ($RES_BND_298) (76|80) [SCAL] (1) $FUN_11 = sqrt($FUN_10) ($RES_AUX_372) (77|81) [SCAL] (1) $FUN_10 = abs((2.0 * volumeFlex.L) / (volumeFlex.V * max(volumeFlex.density_derp_h, 1e-10))) ($RES_AUX_373) =================== Scalar Matching =================== variable to equation ********************** var 1 --> eqn 51 var 2 --> eqn 57 var 3 --> eqn 31 var 4 --> eqn 40 var 5 --> eqn 72 var 6 --> eqn 32 var 7 --> eqn 77 var 8 --> eqn 67 var 9 --> eqn 5 var 10 --> eqn 6 var 11 --> eqn 80 var 12 --> eqn 7 var 13 --> eqn 79 var 14 --> eqn 21 var 15 --> eqn 55 var 16 --> eqn 52 var 17 --> eqn 13 var 18 --> eqn 33 var 19 --> eqn 42 var 20 --> eqn 18 var 21 --> eqn -1 var 22 --> eqn 65 var 23 --> eqn 44 var 24 --> eqn 14 var 25 --> eqn 73 var 26 --> eqn 45 var 27 --> eqn 48 var 28 --> eqn 71 var 29 --> eqn 25 var 30 --> eqn 12 var 31 --> eqn 24 var 32 --> eqn 4 var 33 --> eqn 23 var 34 --> eqn 47 var 35 --> eqn 41 var 36 --> eqn 22 var 37 --> eqn 20 var 38 --> eqn 49 var 39 --> eqn -1 var 40 --> eqn 3 var 41 --> eqn 78 var 42 --> eqn 76 var 43 --> eqn 36 var 44 --> eqn 70 var 45 --> eqn 60 var 46 --> eqn 27 var 47 --> eqn 81 var 48 --> eqn 53 var 49 --> eqn 19 var 50 --> eqn 62 var 51 --> eqn 29 var 52 --> eqn 17 var 53 --> eqn 9 var 54 --> eqn -1 var 55 --> eqn 8 var 56 --> eqn 46 var 57 --> eqn 38 var 58 --> eqn 15 var 59 --> eqn 11 var 60 --> eqn 30 var 61 --> eqn 35 var 62 --> eqn 50 var 63 --> eqn 37 var 64 --> eqn 63 var 65 --> eqn -1 var 66 --> eqn 28 var 67 --> eqn 74 var 68 --> eqn 43 var 69 --> eqn 39 var 70 --> eqn 58 var 71 --> eqn 69 var 72 --> eqn 16 var 73 --> eqn 68 var 74 --> eqn 66 var 75 --> eqn 2 var 76 --> eqn 59 var 77 --> eqn 26 var 78 --> eqn 10 var 79 --> eqn 34 var 80 --> eqn 1 var 81 --> eqn 54 var 82 --> eqn 56 var 83 --> eqn 61 var 84 --> eqn 75 var 85 --> eqn 64 equation to variable ********************** eqn 1 --> var 80 eqn 2 --> var 75 eqn 3 --> var 40 eqn 4 --> var 32 eqn 5 --> var 9 eqn 6 --> var 10 eqn 7 --> var 12 eqn 8 --> var 55 eqn 9 --> var 53 eqn 10 --> var 78 eqn 11 --> var 59 eqn 12 --> var 30 eqn 13 --> var 17 eqn 14 --> var 24 eqn 15 --> var 58 eqn 16 --> var 72 eqn 17 --> var 52 eqn 18 --> var 20 eqn 19 --> var 49 eqn 20 --> var 37 eqn 21 --> var 14 eqn 22 --> var 36 eqn 23 --> var 33 eqn 24 --> var 31 eqn 25 --> var 29 eqn 26 --> var 77 eqn 27 --> var 46 eqn 28 --> var 66 eqn 29 --> var 51 eqn 30 --> var 60 eqn 31 --> var 3 eqn 32 --> var 6 eqn 33 --> var 18 eqn 34 --> var 79 eqn 35 --> var 61 eqn 36 --> var 43 eqn 37 --> var 63 eqn 38 --> var 57 eqn 39 --> var 69 eqn 40 --> var 4 eqn 41 --> var 35 eqn 42 --> var 19 eqn 43 --> var 68 eqn 44 --> var 23 eqn 45 --> var 26 eqn 46 --> var 56 eqn 47 --> var 34 eqn 48 --> var 27 eqn 49 --> var 38 eqn 50 --> var 62 eqn 51 --> var 1 eqn 52 --> var 16 eqn 53 --> var 48 eqn 54 --> var 81 eqn 55 --> var 15 eqn 56 --> var 82 eqn 57 --> var 2 eqn 58 --> var 70 eqn 59 --> var 76 eqn 60 --> var 45 eqn 61 --> var 83 eqn 62 --> var 50 eqn 63 --> var 64 eqn 64 --> var 85 eqn 65 --> var 22 eqn 66 --> var 74 eqn 67 --> var 8 eqn 68 --> var 73 eqn 69 --> var 71 eqn 70 --> var 44 eqn 71 --> var 28 eqn 72 --> var 5 eqn 73 --> var 25 eqn 74 --> var 67 eqn 75 --> var 84 eqn 76 --> var 42 eqn 77 --> var 7 eqn 78 --> var 41 eqn 79 --> var 13 eqn 80 --> var 11 eqn 81 --> var 47 " [Timeout remaining time 659] [Calling sys.exit(0), Time elapsed: 4.448509696987458] Failed to read output from testmodel.py, exit status != 0: 0.7938018569839187 0.808150426 0.077668517 Calling exit ...