Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_ThermofluidStream.Examples.SimpleCoolingCycle.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 0.001676/0.001676, allocations: 104.3 kB / 19.77 MB, free: 2.051 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 0.001886/0.001886, allocations: 215.6 kB / 23.07 MB, free: 4.844 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 1.555/1.555, allocations: 230.7 MB / 256.9 MB, free: 7.727 MB / 206.1 MB " [Timeout remaining time 178] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.2.0/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.2.0/package.mo): time 0.8938/0.8938, allocations: 94.64 MB / 407.9 MB, free: 9.203 MB / 318.1 MB " [Timeout remaining time 179] Using package ThermofluidStream with version 1.2.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.2.0/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.Examples.SimpleCoolingCycle,tolerance=1e-06,outputFormat="mat",numberOfIntervals=1000,variableFilter="PI.x|PID.I.y|Time|combiTimeTable.nextTimeEvent|combiTimeTable.nextTimeEventScaled|fan.m_flow|flexVolume.M|flexVolume.U_med|heatCapacitor.T|heatExchange_CounterFlowNTU.h_out_A|heatExchange_CounterFlowNTU.h_out_B|pump.m_flow|pump.omega|speed.phi|speed1.phi|speed1.w",fileNamePrefix="ThermofluidStream_ThermofluidStream.Examples.SimpleCoolingCycle") translateModel(ThermofluidStream.Examples.SimpleCoolingCycle,tolerance=1e-06,outputFormat="mat",numberOfIntervals=1000,variableFilter="PI.x|PID.I.y|Time|combiTimeTable.nextTimeEvent|combiTimeTable.nextTimeEventScaled|fan.m_flow|flexVolume.M|flexVolume.U_med|heatCapacitor.T|heatExchange_CounterFlowNTU.h_out_A|heatExchange_CounterFlowNTU.h_out_B|pump.m_flow|pump.omega|speed.phi|speed1.phi|speed1.w",fileNamePrefix="ThermofluidStream_ThermofluidStream.Examples.SimpleCoolingCycle") [Timeout 660] "Notification: Performance of FrontEnd - Absyn->SCode: time 2.356e-05/2.356e-05, allocations: 2.281 kB / 0.5562 GB, free: 38.26 MB / 446.1 MB Notification: Performance of NFInst.instantiate(ThermofluidStream.Examples.SimpleCoolingCycle): time 0.2487/0.2487, allocations: 181.2 MB / 0.7332 GB, free: 2.938 MB / 0.5606 GB Notification: Performance of NFInst.instExpressions: time 0.4659/0.7147, allocations: 27.39 MB / 0.7599 GB, free: 4.023 MB / 0.5762 GB Notification: Performance of NFInst.updateImplicitVariability: time 0.002959/0.7176, allocations: 104.5 kB / 0.76 GB, free: 4.023 MB / 0.5762 GB Notification: Performance of NFTyping.typeComponents: time 0.003327/0.721, allocations: 0.9094 MB / 0.7609 GB, free: 4.023 MB / 0.5762 GB Notification: Performance of NFTyping.typeBindings: time 0.007238/0.7282, allocations: 1.701 MB / 0.7626 GB, free: 4.008 MB / 0.5762 GB Notification: Performance of NFTyping.typeClassSections: time 0.007985/0.7362, allocations: 2.175 MB / 0.7647 GB, free: 3.965 MB / 0.5762 GB Notification: Performance of NFFlatten.flatten: time 0.008013/0.7442, allocations: 3.649 MB / 0.7683 GB, free: 3.965 MB / 0.5762 GB Notification: Performance of NFFlatten.resolveConnections: time 0.002148/0.7463, allocations: 351.7 kB / 0.7686 GB, free: 3.883 MB / 0.5762 GB Notification: Performance of NFEvalConstants.evaluate: time 0.006142/0.7525, allocations: 1.59 MB / 0.7702 GB, free: 3.879 MB / 0.5762 GB Notification: Performance of NFSimplifyModel.simplify: time 0.003689/0.7562, allocations: 1.018 MB / 0.7712 GB, free: 3.879 MB / 0.5762 GB Notification: Performance of NFPackage.collectConstants: time 0.001368/0.7575, allocations: 172.2 kB / 0.7713 GB, free: 3.879 MB / 0.5762 GB Notification: Performance of NFFlatten.collectFunctions: time 0.009355/0.7669, allocations: 1.727 MB / 0.773 GB, free: 3.828 MB / 0.5762 GB Notification: Performance of combineBinaries: time 0.008438/0.7753, allocations: 4.5 MB / 0.7774 GB, free: 1.883 MB / 0.5762 GB Notification: Performance of replaceArrayConstructors: time 0.00403/0.7794, allocations: 2.979 MB / 0.7803 GB, free: 32 kB / 0.5762 GB Notification: Performance of NFVerifyModel.verify: time 0.001863/0.7812, allocations: 182.4 kB / 0.7805 GB, free: 32 kB / 0.5762 GB Notification: Performance of FrontEnd: time 0.00112/0.7823, allocations: 175.8 kB / 0.7807 GB, free: 4 kB / 0.5762 GB Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 405 (385) * Number of variables: 407 (407) Notification: Performance of [SIM] Bindings: time 0.02179/0.8041, allocations: 10.46 MB / 0.7909 GB, free: 11.77 MB / 0.5919 GB Notification: Performance of [SIM] FunctionAlias: time 0.003404/0.8075, allocations: 1.156 MB / 0.792 GB, free: 11.61 MB / 0.5919 GB Notification: Performance of [SIM] Early Inline: time 0.01495/0.8225, allocations: 5.729 MB / 0.7976 GB, free: 11.46 MB / 0.5919 GB Notification: Performance of [SIM] Simplify 1: time 0.003625/0.8261, allocations: 0.8987 MB / 0.7985 GB, free: 11.18 MB / 0.5919 GB Notification: Performance of [SIM] Alias: time 0.01448/0.8406, allocations: 7.308 MB / 0.8056 GB, free: 9.215 MB / 0.5919 GB Notification: Performance of [SIM] Simplify 2: time 0.001699/0.8423, allocations: 0.6399 MB / 0.8062 GB, free: 8.996 MB / 0.5919 GB Notification: Performance of [SIM] Remove Stream: time 0.0006683/0.843, allocations: 403.4 kB / 0.8066 GB, free: 8.902 MB / 0.5919 GB Notification: Performance of [SIM] Detect States: time 0.001658/0.8446, allocations: 1.05 MB / 0.8077 GB, free: 8.676 MB / 0.5919 GB Notification: Performance of [SIM] Events: time 0.0006334/0.8452, allocations: 304.4 kB / 0.8079 GB, free: 8.605 MB / 0.5919 GB Notification: Performance of [SIM] Partitioning: time 0.002421/0.8477, allocations: 1.712 MB / 0.8096 GB, free: 8.426 MB / 0.5919 GB Error: Internal error NBSorting.tarjan failed to sort system: System Variables (254/254) **************************** (1|1) [ALGB] (1) protected Real heatExchange_CounterFlowNTU.C_min (2|2) [ALGB] (1) Real PID.controlError = 353.15 - heatCapacitor.T (3|3) [ALGB] (1) output Real multiSensor_Tpm7.outlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (4|4) [ALGB] (1) Real thermalConvectionPipe.T = ThermofluidStream.Examples.SimpleCoolingCycle.thermalConvectionPipe.Medium.temperature(thermalConvectionPipe.center_state) (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0) (5|5) [ALGB] (1) output Real multiSensor_Tpm6.outlet.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0) (6|6) [ALGB] (1) input Real pump.inlet.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0) (7|7) [ALGB] (1) output Real multiSensor_Tpm5.outlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (8|8) [ALGB] (1) output Real multiSensor_Tpm4.outlet.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0) (9|9) [DER-] (1) Real $DER.flexVolume.U_med (10|10) [ALGB] (1) output Real multiSensor_Tpm3.outlet.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0) (11|11) [ALGB] (1) output Real multiSensor_Tpm2.outlet.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0) (12|12) [ALGB] (1) protected Real PID.limiter.simplifiedExpr (13|13) [ALGB] (1) output Real multiSensor_Tpm1.outlet.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0) (14|14) [ALGB] (1) Real speed1.w_ref (15|15) [ALGB] (1) Real PI.y (16|16) [ALGB] (1) input Real thermalConvectionPipe.inlet.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (17|17) [ALGB] (1) output Real fan.outlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (18|18) [ALGB] (1) protected Real flexVolume.state_in.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (19|19) [ALGB] (1) protected Real flowResistance.p_in = ThermofluidStream.Examples.SimpleCoolingCycle.flowResistance.Medium.pressure(flowResistance.inlet.state) (20|20) [ALGB] (1) Real heatExchange_CounterFlowNTU.outletA.r (21|21) [ALGB] (1) Real heatExchange_CounterFlowNTU.effectiveness (22|22) [DDER] (1) Real $DER.speed.w (StateSelect = avoid) (23|23) [ALGB] (1) input Real pump.inlet.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (24|24) [DISC] (1) Real $TEV_0 (25|25) [ALGB] (1) protected Real heatExchange_CounterFlowNTU.C_max (26|26) [ALGB] (1) protected Real fan.tau (27|27) [ALGB] (1) Real heatExchange_CounterFlowNTU.Delta_T_max (28|28) [DER-] (1) Real $DER.flexVolume.M (29|29) [ALGB] (1) Real PID.gainTrack.y (30|30) [ALGB] (1) Real pump.eta = if noEvent(abs(pump.W_t) > 1e-4) then (pump.v_in * pump.dp * heatExchange_CounterFlowNTU.m_flow_B) / pump.W_t else 0.0 (31|31) [ALGB] (1) Real heatExchange_CounterFlowNTU.dh_B (32|32) [ALGB] (1) flow Real heatCapacitor.port.Q_flow (33|33) [ALGB] (1) output Real fan.outlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (34|34) [DER-] (1) Real $DER.PID.I.y (35|35) [ALGB] (1) protected Real fan.h_in = ThermofluidStream.Examples.SimpleCoolingCycle.fan.Medium.specificEnthalpy(fan.inlet.state) (36|36) [ALGB] (1) protected Real fan.dh (37|37) [ALGB] (1) protected Real thermalConvectionPipe.A_cond = thermalConvectionPipe.r * 6.283185307179586 * thermalConvectionPipe.l (38|38) [ALGB] (1) protected Real fan.R_out = fan.p_out / (ThermofluidStream.Examples.SimpleCoolingCycle.fan.Medium.density(fan.outlet.state) * ThermofluidStream.Examples.SimpleCoolingCycle.fan.Medium.temperature(fan.outlet.state)) (39|39) [ALGB] (1) protected Real thermalConvectionPipe.Nu_turb (40|40) [ALGB] (1) Real PID.gainPID.y (41|41) [ALGB] (1) Real fan.dr_corr (42|42) [DISC] (1) Boolean $SEV_11 (43|43) [ALGB] (1) output Real multiSensor_Tpm1.outlet.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (44|44) [ALGB] (1) protected Real thermalConvectionPipe.Re_D (45|45) [DISC] (1) Boolean $SEV_10 (46|46) [ALGB] (1) output Real multiSensor_Tpm2.outlet.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (47|47) [ALGB] (1) output Real thermalConvectionPipe.outlet.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (48|48) [ALGB] (1) output Real multiSensor_Tpm3.outlet.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (49|49) [ALGB] (1) output Real multiSensor_Tpm4.outlet.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (50|50) [ALGB] (1) Real heatExchange_CounterFlowNTU.summary.Q_flow_B (51|51) [ALGB] (1) output Real multiSensor_Tpm5.outlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (52|52) [ALGB] (1) output Real multiSensor_Tpm6.outlet.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (53|53) [ALGB] (1) output Real multiSensor_Tpm7.outlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (54|54) [DDER] (1) Real $DER.fan.phi (StateSelect = avoid) (55|55) [ALGB] (1) Real source.outlet.r (56|56) [ALGB] (1) output Real pump.outlet.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (57|57) [ALGB] (1) Real heatExchange_CounterFlowNTU.summary.Tout_A (start = 288.15, min = 0.0, nominal = 300.0) (58|58) [ALGB] (1) Real heatExchange_CounterFlowNTU.NTU (59|59) [ALGB] (1) Real heatExchange_CounterFlowNTU.summary.Tin_B (start = 288.15, min = 0.0, nominal = 300.0) (60|60) [ALGB] (1) protected Real thermalConvectionPipe.v_m (61|61) [ALGB] (1) protected Real pump.h_in = ThermofluidStream.Examples.SimpleCoolingCycle.pump.Medium.specificEnthalpy(pump.inlet.state) (62|62) [ALGB] (1) Real heatExchange_CounterFlowNTU.summary.dh_A (63|63) [DDER] (1) Real $DER.fan.omega (StateSelect = avoid) (64|64) [ALGB] (1) output Real flowResistance.outlet.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0) (65|65) [ALGB] (1) Real heatExchange_CounterFlowNTU.summary.hout_A (66|66) [ALGB] (1) input Real sink.inlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (67|67) [ALGB] (1) output Real source.outlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (68|68) [ALGB] (1) protected Real flexVolume.T_heatPort (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0) (69|69) [ALGB] (1) protected Real heatExchange_CounterFlowNTU.C_r (70|70) [ALGB] (1) protected Real heatExchange_CounterFlowNTU.C_B (71|71) [ALGB] (1) Real PID.addPID.y (72|72) [ALGB] (1) protected Real heatExchange_CounterFlowNTU.h_in_B (73|73) [ALGB] (1) input Real sink.inlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (74|74) [ALGB] (1) Real $FUN_9 (75|75) [ALGB] (1) Real heatCapacitor.der_T (start = 0.0) (76|76) [ALGB] (1) Real $FUN_8 (77|77) [ALGB] (1) Real $FUN_3 (78|78) [DISS] (1) protected discrete Real combiTimeTable.nextTimeEventScaled (fixed = true, start = 0.0) (79|79) [ALGB] (1) Real $FUN_2 (80|80) [ALGB] (1) Real $FUN_1 (81|81) [ALGB] (1) Real heatExchange_CounterFlowNTU.summary.dT_A (82|82) [ALGB] (1) protected Real pump.v_in = 1.0 / max(pump.rho_min, ThermofluidStream.Examples.SimpleCoolingCycle.pump.Medium.density(pump.inlet.state)) (min = 0.0) (83|83) [ALGB] (1) Real pump.dr_corr (84|84) [DER-] (1) Real $DER.heatExchange_CounterFlowNTU.h_out_A (85|85) [ALGB] (1) protected Real heatExchange_CounterFlowNTU.p_A = ThermofluidStream.Examples.SimpleCoolingCycle.heatExchange_CounterFlowNTU.MediumA.pressure(heatExchange_CounterFlowNTU.inletA.state) (86|86) [ALGB] (1) protected Real pump.v_out = 1.0 / max(pump.rho_min, ThermofluidStream.Examples.SimpleCoolingCycle.pump.Medium.density(pump.inlet.state)) (min = 0.0) (87|87) [DDER] (1) Real $DER.pump.phi (StateSelect = avoid) (88|88) [DER-] (1) Real $DER.heatExchange_CounterFlowNTU.m_flow_B (89|89) [ALGB] (1) protected Real heatExchange_CounterFlowNTU.p_B = ThermofluidStream.Examples.SimpleCoolingCycle.heatExchange_CounterFlowNTU.MediumB.pressure(heatExchange_CounterFlowNTU.inletB.state) (90|90) [ALGB] (1) Real heatExchange_CounterFlowNTU.summary.hin_A (91|91) [DER-] (1) Real $DER.speed1.phi (92|92) [ALGB] (1) Real pump.W_t (93|93) [ALGB] (1) protected Real flexVolume.state_out.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0) (94|94) [ALGB] (1) protected Real fan.v_in = 1.0 / max(fan.rho_min, ThermofluidStream.Examples.SimpleCoolingCycle.fan.Medium.density(fan.inlet.state)) (min = 0.0) (95|95) [ALGB] (1) protected Real fan.R_in = fan.p_in / (ThermofluidStream.Examples.SimpleCoolingCycle.fan.Medium.density(fan.inlet.state) * ThermofluidStream.Examples.SimpleCoolingCycle.fan.Medium.temperature(fan.inlet.state)) (96|96) [ALGB] (1) input Real flowResistance.inlet.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (97|97) [ALGB] (1) input Real heatExchange_CounterFlowNTU.inletB.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0) (98|98) [ALGB] (1) flow Real prescribedHeatFlow.port.Q_flow (99|99) [ALGB] (1) Real PID.addSat.y (100|100) [ALGB] (1) input Real heatExchange_CounterFlowNTU.inletB.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (101|101) [ALGB] (1) output Real flowResistance.outlet.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (102|102) [ALGB] (1) Real speed.a (103|103) [ALGB] (1) Real fan.dp (104|104) [ALGB] (1) Real $FUN_11 (105|105) [DER-] (1) Real $DER.heatCapacitor.T (106|106) [ALGB] (1) protected Real pump.dh (107|107) [ALGB] (1) Real $FUN_10 (108|108) [ALGB] (1) Real heatExchange_CounterFlowNTU.T_in_MediumB (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0) (109|109) [ALGB] (1) Real heatExchange_CounterFlowNTU.summary.dT_B (110|110) [ALGB] (1) Real PID.addI.y (111|111) [ALGB] (1) protected Real thermalConvectionPipe.h_in = ThermofluidStream.Examples.SimpleCoolingCycle.thermalConvectionPipe.Medium.specificEnthalpy(thermalConvectionPipe.inlet.state) (112|112) [DISC] (1) Boolean $SEV_9 (113|113) [ALGB] (1) Real heatExchange_CounterFlowNTU.q_flow (114|114) [DISC] (1) Boolean $SEV_8 (115|115) [ALGB] (1) protected Real pump.h_out (116|116) [DISC] (1) Boolean $SEV_6 (117|117) [DISC] (1) Boolean $SEV_5 (118|118) [ALGB] (1) protected Real fan.p_out (119|119) [ALGB] (1) Real multiSensor_Tpm6.inlet.r (120|120) [DISC] (1) Boolean $SEV_4 (121|121) [ALGB] (1) Real PID.P.y (122|122) [DISC] (1) Boolean $SEV_3 (123|123) [DISC] (1) Boolean $SEV_2 (124|124) [DISC] (1) Boolean $SEV_1 (125|125) [DISC] (1) Boolean $SEV_0 (126|126) [ALGB] (1) protected Real flexVolume.r_damping = flexVolume.d * der(flexVolume.M) (127|127) [ALGB] (1) protected Real thermalConvectionPipe.p_in = ThermofluidStream.Examples.SimpleCoolingCycle.thermalConvectionPipe.Medium.pressure(thermalConvectionPipe.inlet.state) (128|128) [ALGB] (1) input Real thermalConvectionPipe.inlet.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0) (129|129) [ALGB] (1) Real flexVolume.V (130|130) [ALGB] (1) Real pump.Q_t (131|131) [ALGB] (1) protected Real flexVolume.state_out.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (132|132) [ALGB] (1) protected Real fan.p_in = ThermofluidStream.Examples.SimpleCoolingCycle.fan.Medium.pressure(fan.inlet.state) (133|133) [ALGB] (1) protected Real flexVolume.d = flexVolume.k_volume_damping * sqrt(abs((2.0 * flexVolume.L) / (flexVolume.V * max(flexVolume.density_derp_h, 1e-10)))) (134|134) [ALGB] (1) protected Real pump.p_out (135|135) [ALGB] (1) Real flexVolume.Q_flow (136|136) [ALGB] (1) protected Real heatExchange_CounterFlowNTU.q_flowA (137|137) [ALGB] (1) Real heatExchange_CounterFlowNTU.dh_A (138|138) [ALGB] (1) protected Real flexVolume.r (139|139) [ALGB] (1) protected Real heatExchange_CounterFlowNTU.q_flowB (140|140) [ALGB] (1) input Real flexVolume.inlet.state.p = flexVolume.state_in.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (141|141) [ALGB] (1) Real flowResistance.dr_corr (142|142) [ALGB] (1) output Real source.outlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (143|143) [ALGB] (1) Real multiSensor_Tpm1.T (144|144) [DER-] (1) Real $DER.PI.x (145|145) [ALGB] (1) input Real multiSensor_Tpm1.inlet.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (146|146) [ALGB] (1) protected Real heatExchange_CounterFlowNTU.q_max (147|147) [ALGB] (1) Real multiSensor_Tpm2.T (148|148) [ALGB] (1) input Real multiSensor_Tpm2.inlet.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (149|149) [ALGB] (1) Real multiSensor_Tpm3.T (150|150) [ALGB] (1) Real heatExchange_CounterFlowNTU.summary.Tout_B (start = 288.15, min = 0.0, nominal = 300.0) (151|151) [ALGB] (1) input Real multiSensor_Tpm3.inlet.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (152|152) [ALGB] (1) Real multiSensor_Tpm4.T (153|153) [DISS] (1) protected discrete Real combiTimeTable.nextTimeEvent (fixed = true, start = 0.0) (154|154) [ALGB] (1) input Real multiSensor_Tpm4.inlet.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (155|155) [ALGB] (1) Real multiSensor_Tpm5.T (156|156) [ALGB] (1) protected Real flowResistance.h_out (157|157) [ALGB] (1) input Real multiSensor_Tpm5.inlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (158|158) [ALGB] (1) Real multiSensor_Tpm6.T (159|159) [ALGB] (1) Real flexVolume.medium.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (160|160) [ALGB] (1) Real fan.Q_t (161|161) [ALGB] (1) input Real multiSensor_Tpm6.inlet.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (162|162) [ALGB] (1) Real multiSensor_Tpm7.T (163|163) [ALGB] (1) Real pump.dp (164|164) [ALGB] (1) input Real multiSensor_Tpm7.inlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (165|165) [ALGB] (1) Real prescribedHeatFlow.Q_flow (166|166) [ALGB] (1) protected Real thermalConvectionPipe.p_out (167|167) [ALGB] (1) Real PID.addP.y (168|168) [ALGB] (1) protected Real pump.tau (169|169) [ALGB] (1) protected Real heatExchange_CounterFlowNTU.cpA_in = ThermofluidStream.Examples.SimpleCoolingCycle.heatExchange_CounterFlowNTU.MediumA.specificHeatCapacityCp(heatExchange_CounterFlowNTU.inletA.state) (170|170) [ALGB] (1) flow Real thermalConvectionPipe.heatPort.Q_flow (171|171) [ALGB] (1) protected Real heatExchange_CounterFlowNTU.cp_B (172|172) [ALGB] (1) Real heatExchange_CounterFlowNTU.summary.hin_B (173|173) [ALGB] (1) Real pump.tau_st (174|174) [ALGB] (1) input Real fan.inlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (175|175) [ALGB] (1) protected Real flexVolume.r_out (176|176) [DER-] (1) Real $DER.speed.phi (177|177) [ALGB] (1) protected Real flexVolume.h_out = if noEvent((-(-heatExchange_CounterFlowNTU.m_flow_B)) >= 0.0) then ThermofluidStream.Examples.SimpleCoolingCycle.flexVolume.Medium.specificEnthalpy(flexVolume.state_out) else 4184.0 * ((-273.15) + flexVolume.T_heatPort) (178|178) [ALGB] (1) protected Real pump.tau_normalized (179|179) [ALGB] (1) Real gain1.y (180|180) [ALGB] (1) output Real flexVolume.outlet.state.T = flexVolume.state_out.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0) (181|181) [ALGB] (1) Real pump.outlet.r (182|182) [ALGB] (1) input Real fan.inlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (183|183) [ALGB] (1) Real showRealValue.numberPort (184|184) [ALGB] (1) protected Real thermalConvectionPipe.dh (185|185) [ALGB] (1) output Real pump.outlet.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0) (186|186) [ALGB] (1) protected Real thermalConvectionPipe.A_cross = 3.141592653589793 * thermalConvectionPipe.r ^ 2.0 (187|187) [ALGB] (1) protected Real heatExchange_CounterFlowNTU.cp_A (188|188) [ALGB] (1) Real multiSensor_Tpm1.p (189|189) [ALGB] (1) protected Real heatExchange_CounterFlowNTU.C_A (190|190) [ALGB] (1) Real multiSensor_Tpm2.p (191|191) [ALGB] (1) protected Real thermalConvectionPipe.V = thermalConvectionPipe.A_cross * thermalConvectionPipe.l (192|192) [ALGB] (1) Real multiSensor_Tpm3.p (193|193) [ALGB] (1) Real multiSensor_Tpm4.p (194|194) [ALGB] (1) Real multiSensor_Tpm5.p (195|195) [DER-] (1) Real $DER.pump.omega (196|196) [ALGB] (1) output Real heatExchange_CounterFlowNTU.outletB.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0) (197|197) [ALGB] (1) protected Real heatExchange_CounterFlowNTU.h_in_A (198|198) [ALGB] (1) Real multiSensor_Tpm6.p (199|199) [ALGB] (1) Real multiSensor_Tpm7.p (200|200) [ALGB] (1) Real heatExchange_CounterFlowNTU.summary.Q_flow_A (201|201) [ALGB] (1) output Real flexVolume.outlet.state.p = flexVolume.state_out.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (202|202) [ALGB] (1) output Real heatExchange_CounterFlowNTU.outletA.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (203|203) [ALGB] (1) Real sink.inlet.r (204|204) [ALGB] (1) protected Real flexVolume.density_derp_h (205|205) [DER-] (1) Real $DER.heatExchange_CounterFlowNTU.h_out_B (206|206) [ALGB] (1) Real fan.tau_st (207|207) [ALGB] (1) Real[1] combiTimeTable.y (208|208) [ALGB] (1) input Real multiSensor_Tpm7.inlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (209|209) [ALGB] (1) output Real heatExchange_CounterFlowNTU.outletA.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (210|210) [ALGB] (1) input Real multiSensor_Tpm6.inlet.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0) (211|211) [ALGB] (1) Real feedback.y (212|212) [ALGB] (1) Real heatExchange_CounterFlowNTU.summary.Tin_A (start = 288.15, min = 0.0, nominal = 300.0) (213|213) [ALGB] (1) Real heatExchange_CounterFlowNTU.summary.efficiency (214|214) [ALGB] (1) input Real flowResistance.inlet.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0) (215|215) [ALGB] (1) Real flexVolume.medium.p_bar = Modelica.Units.Conversions.to_bar(99999.99999999999 * flexVolume.medium.p_bar) (min = 0.0) (216|216) [ALGB] (1) input Real multiSensor_Tpm5.inlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (217|217) [ALGB] (1) Real speed1.a (218|218) [ALGB] (1) input Real multiSensor_Tpm4.inlet.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0) (219|219) [ALGB] (1) output Real heatExchange_CounterFlowNTU.outletB.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (220|220) [ALGB] (1) input Real multiSensor_Tpm3.inlet.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0) (221|221) [ALGB] (1) input Real multiSensor_Tpm2.inlet.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0) (222|222) [ALGB] (1) input Real multiSensor_Tpm1.inlet.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0) (223|223) [ALGB] (1) protected Real sink.p = ThermofluidStream.Examples.SimpleCoolingCycle.sink.Medium.pressure(sink.inlet.state) (224|224) [ALGB] (1) protected Real pump.p_in = ThermofluidStream.Examples.SimpleCoolingCycle.pump.Medium.pressure(pump.inlet.state) (225|225) [ALGB] (1) Real heatExchange_CounterFlowNTU.summary.dh_B (226|226) [ALGB] (1) Real thermalConvectionPipe.outlet.r (227|227) [ALGB] (1) Real heatExchange_CounterFlowNTU.summary.hout_B (228|228) [ALGB] (1) protected Real flexVolume.r_in (229|229) [ALGB] (1) protected Real flexVolume.p_in = ThermofluidStream.Examples.SimpleCoolingCycle.flexVolume.Medium.pressure(flexVolume.state_in) (230|230) [ALGB] (1) protected Real flexVolume.h_in = if noEvent(heatExchange_CounterFlowNTU.m_flow_B >= 0.0) then ThermofluidStream.Examples.SimpleCoolingCycle.flexVolume.Medium.specificEnthalpy(flexVolume.state_in) else 4184.0 * ((-273.15) + flexVolume.T_heatPort) (231|231) [ALGB] (1) protected Real flexVolume.state_in.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0) (232|232) [ALGB] (1) protected Real flowResistance.p_out (233|233) [ALGB] (1) Real fan.W_t (234|234) [ALGB] (1) protected Real fan.h_out (235|235) [ALGB] (1) protected Real sink.r (236|236) [ALGB] (1) Real thermalConvectionPipe.center_state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0) (237|237) [ALGB] (1) Real thermalConvectionPipe.center_state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (238|238) [ALGB] (1) Real flexVolume.medium.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0) (239|239) [ALGB] (1) output Real thermalConvectionPipe.outlet.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0) (240|240) [DER-] (1) Real $DER.speed1.w (241|241) [ALGB] (1) input Real heatExchange_CounterFlowNTU.inletA.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (242|242) [ALGB] (1) protected Real heatExchange_CounterFlowNTU.cpA_out = ThermofluidStream.Examples.SimpleCoolingCycle.heatExchange_CounterFlowNTU.MediumA.specificHeatCapacityCp(heatExchange_CounterFlowNTU.outletA.state) (243|243) [ALGB] (1) input Real flexVolume.inlet.state.T = flexVolume.state_in.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0) (244|244) [ALGB] (1) protected Real thermalConvectionPipe.M = thermalConvectionPipe.V * 995.586 (min = 0.0) (245|245) [ALGB] (1) protected Real thermalConvectionPipe.h_avg (246|246) [ALGB] (1) protected Real thermalConvectionPipe.h_out (247|247) [ALGB] (1) input Real heatExchange_CounterFlowNTU.inletA.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (248|248) [ALGB] (1) protected Real fan.tau_normalized (249|249) [ALGB] (1) Real heatExchange_CounterFlowNTU.T_in_MediumA (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (250|250) [DER-] (1) Real $DER.heatExchange_CounterFlowNTU.m_flow_A (251|251) [DSTA] (1) protected Real fan.phi (252|252) [DSTA] (1) protected Real pump.phi (253|253) [DSTA] (1) protected Real fan.omega (StateSelect = prefer) (254|254) [DSTA] (1) Real speed.w (StateSelect = prefer) System Equations (240/252) **************************** (1|1) [SCAL] (1) heatExchange_CounterFlowNTU.summary.efficiency = heatExchange_CounterFlowNTU.effectiveness ($RES_SIM_205) (2|2) [RECD] (2) multiSensor_Tpm3.outlet.state = multiSensor_Tpm3.inlet.state ($RES_SIM_120) (3|4) [SCAL] (1) speed1.a = $DER.speed1.w ($RES_SIM_80) (4|5) [SCAL] (1) heatExchange_CounterFlowNTU.summary.Q_flow_B = heatExchange_CounterFlowNTU.q_flowB ($RES_SIM_206) (5|6) [SCAL] (1) speed1.w = $DER.speed1.phi ($RES_SIM_81) (6|7) [SCAL] (1) pump.outlet.state.p = pump.p_out ($RES_SIM_449) (7|8) [SCAL] (1) heatExchange_CounterFlowNTU.summary.Q_flow_A = heatExchange_CounterFlowNTU.q_flowA ($RES_SIM_207) (8|9) [SCAL] (1) speed1.phi = fan.phi ($RES_SIM_82) (9|10) [SCAL] (1) heatExchange_CounterFlowNTU.summary.dh_B = heatExchange_CounterFlowNTU.summary.hout_B - heatExchange_CounterFlowNTU.summary.hin_B ($RES_SIM_208) (10|11) [SCAL] (1) heatExchange_CounterFlowNTU.summary.dh_A = heatExchange_CounterFlowNTU.summary.hout_A - heatExchange_CounterFlowNTU.summary.hin_A ($RES_SIM_209) (11|12) [SCAL] (1) speed.a = (PI.y - speed.w) * speed.w_crit ($RES_SIM_84) (12|13) [SCAL] (1) speed.a = $DER.speed.w ($RES_SIM_85) (13|14) [SCAL] (1) speed.w = $DER.speed.phi ($RES_SIM_86) (14|15) [SCAL] (1) speed.phi = pump.phi ($RES_SIM_87) (15|16) [SCAL] (1) multiSensor_Tpm2.p = multiSensor_Tpm2.inlet.state.p ($RES_SIM_127) (16|17) [SCAL] (1) prescribedHeatFlow.Q_flow = combiTimeTable.y[1] ($RES_SIM_286) (17|18) [SCAL] (1) sink.r + sink.p = sink.p0_par ($RES_SIM_88) (18|19) [SCAL] (1) multiSensor_Tpm2.T = (-273.15) + multiSensor_Tpm2.inlet.state.T ($RES_SIM_128) (19|20) [SCAL] (1) $DER.heatExchange_CounterFlowNTU.m_flow_A * sink.L = sink.inlet.r - sink.r ($RES_SIM_89) (20|21) [RECD] (2) multiSensor_Tpm2.outlet.state = multiSensor_Tpm2.inlet.state ($RES_SIM_129) (21|23) [SCAL] (1) fan.R_out = fan.p_out / ((0.0034836987724536205 * fan.outlet.state.p) / fan.outlet.state.T) / fan.outlet.state.T ($RES_BND_420) (22|24) [SCAL] (1) PID.controlError = 353.15 - heatCapacitor.T ($RES_BND_428) (23|25) [SCAL] (1) pump.outlet.state.T = 273.15 + 2.390057361376673e-4 * pump.h_out ($RES_SIM_450) (24|26) [SCAL] (1) PI.y = PI.k * (PI.x + feedback.y) ($RES_SIM_10) (25|27) [SCAL] (1) thermalConvectionPipe.outlet.state.p = thermalConvectionPipe.p_out ($RES_SIM_451) (26|28) [SCAL] (1) $DER.PI.x = feedback.y / PI.T ($RES_SIM_11) (27|29) [SCAL] (1) thermalConvectionPipe.outlet.state.T = 273.15 + 2.390057361376673e-4 * thermalConvectionPipe.h_out ($RES_SIM_452) (28|30) [SCAL] (1) heatExchange_CounterFlowNTU.summary.dT_B = heatExchange_CounterFlowNTU.summary.Tout_B - heatExchange_CounterFlowNTU.summary.Tin_B ($RES_SIM_210) (29|31) [SCAL] (1) feedback.y = gain1.y - heatExchange_CounterFlowNTU.m_flow_B ($RES_SIM_12) (30|32) [SCAL] (1) flowResistance.outlet.state.p = flowResistance.p_out ($RES_SIM_453) (31|33) [SCAL] (1) heatExchange_CounterFlowNTU.summary.dT_A = heatExchange_CounterFlowNTU.summary.Tout_A - heatExchange_CounterFlowNTU.summary.Tin_A ($RES_SIM_211) (32|34) [SCAL] (1) gain1.y = gain1.k * showRealValue.numberPort ($RES_SIM_13) (33|35) [SCAL] (1) flowResistance.outlet.state.T = 273.15 + 2.390057361376673e-4 * flowResistance.h_out ($RES_SIM_454) (34|36) [SCAL] (1) heatExchange_CounterFlowNTU.summary.hout_B = heatExchange_CounterFlowNTU.h_out_B ($RES_SIM_212) (35|37) [SCAL] (1) source.outlet.state.p = source.p0_par ($RES_SIM_455) (36|38) [SCAL] (1) heatExchange_CounterFlowNTU.summary.hin_B = heatExchange_CounterFlowNTU.h_in_B ($RES_SIM_213) (37|39) [SCAL] (1) PID.limiter.simplifiedExpr = PID.addFF.k1 * PID.gainPID.y + PID.addFF.k2 * PID.FFzero.k ($RES_SIM_15) (38|40) [SCAL] (1) source.outlet.state.T = source.T0_par ($RES_SIM_456) (39|41) [SCAL] (1) heatExchange_CounterFlowNTU.summary.hout_A = heatExchange_CounterFlowNTU.h_out_A ($RES_SIM_214) (40|42) [SCAL] (1) heatExchange_CounterFlowNTU.summary.hin_A = heatExchange_CounterFlowNTU.h_in_A ($RES_SIM_215) (41|43) [SCAL] (1) heatExchange_CounterFlowNTU.summary.Tout_A = heatExchange_CounterFlowNTU.outletA.state.T ($RES_SIM_216) (42|44) [SCAL] (1) showRealValue.numberPort = homotopy(smooth(0, if $SEV_2 then PID.limiter.uMax else if $SEV_3 then PID.limiter.uMin else PID.limiter.simplifiedExpr), PID.limiter.simplifiedExpr) ($RES_SIM_18) (43|45) [SCAL] (1) fan.outlet.state.p = fan.p_out ($RES_SIM_459) (44|46) [SCAL] (1) heatExchange_CounterFlowNTU.summary.Tout_B = heatExchange_CounterFlowNTU.outletB.state.T ($RES_SIM_217) (45|47) [SCAL] (1) heatExchange_CounterFlowNTU.summary.Tin_A = heatExchange_CounterFlowNTU.inletA.state.T ($RES_SIM_218) (46|48) [SCAL] (1) $FUN_11 = sqrt($FUN_10) ($RES_AUX_433) (47|49) [SCAL] (1) heatExchange_CounterFlowNTU.summary.Tin_B = heatExchange_CounterFlowNTU.inletB.state.T ($RES_SIM_219) (48|50) [SCAL] (1) $FUN_10 = abs((2.0 * flexVolume.L) / (flexVolume.V * max(flexVolume.density_derp_h, 1e-10))) ($RES_AUX_434) (49|51) [SCAL] (1) multiSensor_Tpm5.p = multiSensor_Tpm5.inlet.state.p ($RES_SIM_95) (50|52) [SCAL] (1) $FUN_9 = abs(pump.W_t) ($RES_AUX_435) (51|53) [SCAL] (1) multiSensor_Tpm5.T = (-273.15) + multiSensor_Tpm5.inlet.state.T ($RES_SIM_96) (52|54) [SCAL] (1) multiSensor_Tpm1.p = multiSensor_Tpm1.inlet.state.p ($RES_SIM_136) (53|55) [SCAL] (1) $FUN_8 = Modelica.Blocks.Tables.Internal.getTimeTableValueNoDer2(combiTimeTable.tableID, 1, time, combiTimeTable.nextTimeEventScaled, $TEV_0) ($RES_AUX_436) (54|56) [RECD] (2) multiSensor_Tpm5.outlet.state = multiSensor_Tpm5.inlet.state ($RES_SIM_97) (55|58) [SCAL] (1) multiSensor_Tpm1.T = (-273.15) + multiSensor_Tpm1.inlet.state.T ($RES_SIM_137) (56|59) [TUPL] (2) (fan.dp, fan.tau_st) = ThermofluidStream.Examples.SimpleCoolingCycle.fan.dp_tau(heatExchange_CounterFlowNTU.m_flow_A, fan.omega, fan.inlet.state, fan.m_flow_reg, fan.omega_reg, fan.rho_min, 100.0, 0.0, 0.25, 1.0, 2.0, 0.001, true, 1.4) ($RES_AUX_437) (57|61) [RECD] (2) multiSensor_Tpm1.outlet.state = multiSensor_Tpm1.inlet.state ($RES_SIM_138) (58|63) [TUPL] (2) (pump.dp, pump.tau_st) = ThermofluidStream.Examples.SimpleCoolingCycle.pump.dp_tau(heatExchange_CounterFlowNTU.m_flow_B, pump.omega, pump.inlet.state, pump.m_flow_reg, pump.omega_reg, pump.rho_min, true, 3.661, 0.00306, 314.2, 9.73e-6, 1, 0.016, 1000.0, 4.864e-5, -2.677, 396700.0, 0.5427, 27770.0, 1.218e-6, 1.832e-4, 100.0) ($RES_AUX_438) (59|65) [SCAL] (1) $FUN_3 = abs(heatExchange_CounterFlowNTU.m_flow_B) ($RES_AUX_439) (60|66) [RECD] (2) flexVolume.inlet.state = flexVolume.state_in ($RES_BND_430) (61|68) [RECD] (2) flexVolume.outlet.state = flexVolume.state_out ($RES_BND_431) (62|70) [SCAL] (1) fan.inlet.state.T = multiSensor_Tpm7.outlet.state.T ($RES_SIM_300) (63|71) [SCAL] (1) fan.inlet.state.p = multiSensor_Tpm7.outlet.state.p ($RES_SIM_301) (64|72) [SCAL] (1) fan.outlet.state.T = Modelica.Math.Nonlinear.solveOneNonlinearEquation(function ThermofluidStream.Examples.SimpleCoolingCycle.fan.Medium.T_h.f_nonlinear(data = ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"Air\", BOX(0.0289651159), BOX(-4333.833858403446), BOX(298609.6803431054), BOX(1000.0), BOX({10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}), BOX({-176.796731, -3.921504225}), BOX({241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}), BOX({6462.26319, -8.147411905}), BOX(287.0512249529787)), h = BOX(fan.h_out)), 200.0, 6000.0, 2.220446049250313e-14) ($RES_SIM_460) (65|73) [SCAL] (1) heatExchange_CounterFlowNTU.outletA.state.T = multiSensor_Tpm7.inlet.state.T ($RES_SIM_303) (66|74) [SCAL] (1) thermalConvectionPipe.center_state.p = thermalConvectionPipe.p_in ($RES_SIM_461) (67|75) [SCAL] (1) heatExchange_CounterFlowNTU.outletA.state.p = multiSensor_Tpm7.inlet.state.p ($RES_SIM_304) (68|76) [SCAL] (1) PID.gainTrack.y = PID.gainTrack.k * PID.addSat.y ($RES_SIM_21) (69|77) [SCAL] (1) thermalConvectionPipe.center_state.T = 273.15 + 2.390057361376673e-4 * (0.5 * thermalConvectionPipe.dh + thermalConvectionPipe.h_in) ($RES_SIM_462) (70|78) [SCAL] (1) PID.addSat.y = PID.addSat.k1 * showRealValue.numberPort + PID.addSat.k2 * PID.limiter.simplifiedExpr ($RES_SIM_22) (71|79) [SCAL] (1) multiSensor_Tpm6.inlet.state.T = flowResistance.outlet.state.T ($RES_SIM_306) (72|80) [SCAL] (1) PID.addI.y = PID.addI.k2 * heatCapacitor.T + 353.15 * PID.addI.k1 + PID.addI.k3 * PID.gainTrack.y ($RES_SIM_23) (73|81) [SCAL] (1) multiSensor_Tpm6.inlet.state.p = flowResistance.outlet.state.p ($RES_SIM_307) (74|82) [SCAL] (1) $DER.heatExchange_CounterFlowNTU.h_out_B * heatExchange_CounterFlowNTU.TC = heatExchange_CounterFlowNTU.h_in_B - (heatExchange_CounterFlowNTU.h_out_B + heatExchange_CounterFlowNTU.dh_B) ($RES_SIM_222) (75|83) [SCAL] (1) PID.addPID.y = PID.addPID.k2 * PID.Dzero.k + PID.addPID.k1 * PID.P.y + PID.addPID.k3 * PID.I.y ($RES_SIM_24) (76|84) [SCAL] (1) PID.gainPID.y = PID.gainPID.k * PID.addPID.y ($RES_SIM_25) (77|85) [SCAL] (1) heatExchange_CounterFlowNTU.inletB.state.T = multiSensor_Tpm6.outlet.state.T ($RES_SIM_309) (78|86) [SCAL] (1) $DER.PID.I.y = PID.I.k * PID.addI.y ($RES_SIM_26) (79|87) [SCAL] (1) $DER.heatExchange_CounterFlowNTU.h_out_A * heatExchange_CounterFlowNTU.TC = heatExchange_CounterFlowNTU.h_in_A - (heatExchange_CounterFlowNTU.h_out_A + heatExchange_CounterFlowNTU.dh_A) ($RES_SIM_225) (80|88) [SCAL] (1) $FUN_2 = abs(heatExchange_CounterFlowNTU.m_flow_A) ($RES_AUX_440) (81|89) [SCAL] (1) $FUN_1 = exp(-heatExchange_CounterFlowNTU.NTU * (1.0 - heatExchange_CounterFlowNTU.C_r)) ($RES_AUX_441) (82|90) [SCAL] (1) flowResistance.dr_corr = flowResistance.p_in - (flowResistance.p_out + 1e5 * heatExchange_CounterFlowNTU.m_flow_B) ($RES_SIM_142) (83|91) [SCAL] (1) PID.P.y = PID.P.k * PID.addP.y ($RES_SIM_29) (84|92) [SCAL] (1) heatExchange_CounterFlowNTU.q_flowB = if noEvent(heatExchange_CounterFlowNTU.C_A < heatExchange_CounterFlowNTU.C_B) then -heatExchange_CounterFlowNTU.q_flowA else heatExchange_CounterFlowNTU.m_flow_B * heatExchange_CounterFlowNTU.dh_B ($RES_SIM_228) (85|93) [SCAL] (1) flowResistance.p_out = max(flowResistance.p_min, flowResistance.p_in - 1e5 * heatExchange_CounterFlowNTU.m_flow_B) ($RES_SIM_143) (86|94) [SCAL] (1) multiSensor_Tpm6.inlet.r = (flowResistance.dr_corr + thermalConvectionPipe.outlet.r) - $DER.heatExchange_CounterFlowNTU.m_flow_B * flowResistance.L ($RES_SIM_144) (87|95) [SCAL] (1) $TEV_0 = $PRE.combiTimeTable.nextTimeEventScaled ($RES_EVT_470) (88|96) [SCAL] (1) $SEV_0 = noEvent(heatExchange_CounterFlowNTU.m_flow_A < heatExchange_CounterFlowNTU.m_flow_reg) and noEvent(heatExchange_CounterFlowNTU.m_flow_B < heatExchange_CounterFlowNTU.m_flow_reg) ($RES_EVT_471) (89|97) [SCAL] (1) $SEV_1 = time >= $PRE.combiTimeTable.nextTimeEvent ($RES_EVT_472) (90|98) [SCAL] (1) $SEV_2 = PID.limiter.simplifiedExpr > PID.limiter.uMax ($RES_EVT_473) (91|99) [SCAL] (1) $SEV_3 = PID.limiter.simplifiedExpr < PID.limiter.uMin ($RES_EVT_474) (92|100) [SCAL] (1) $SEV_4 = heatExchange_CounterFlowNTU.outletA.state.T < 1000.0 ($RES_EVT_475) (93|101) [SCAL] (1) $SEV_5 = heatExchange_CounterFlowNTU.inletA.state.T < 1000.0 ($RES_EVT_476) (94|102) [SCAL] (1) $SEV_6 = flexVolume.T_heatPort >= 272.15 and flexVolume.T_heatPort <= 403.15 ($RES_EVT_477) (95|103) [SCAL] (1) $SEV_8 = 99999.99999999999 * flexVolume.medium.p_bar >= 0.0 ($RES_EVT_479) (96|104) [SCAL] (1) heatExchange_CounterFlowNTU.inletB.state.p = multiSensor_Tpm6.outlet.state.p ($RES_SIM_310) (97|105) [SCAL] (1) PID.addP.y = 353.15 * PID.addP.k1 + PID.addP.k2 * heatCapacitor.T ($RES_SIM_30) (98|106) [SCAL] (1) sink.inlet.state.T = fan.outlet.state.T ($RES_SIM_314) (99|107) [SCAL] (1) speed1.w_ref = gain.k * showRealValue.numberPort ($RES_SIM_31) (100|108) [SCAL] (1) sink.inlet.state.p = fan.outlet.state.p ($RES_SIM_315) (101|109) [SCAL] (1) combiTimeTable.y[1] = combiTimeTable.p_offset[1] + $FUN_8 ($RES_SIM_32) (102|110) [SCAL] (1) heatExchange_CounterFlowNTU.q_flowA = if noEvent(heatExchange_CounterFlowNTU.C_A < heatExchange_CounterFlowNTU.C_B) then heatExchange_CounterFlowNTU.m_flow_A * heatExchange_CounterFlowNTU.dh_A else -heatExchange_CounterFlowNTU.q_flowB ($RES_SIM_231) (103|111) [WHEN] (1) ($RES_SIM_33) (103|111) [----] when {$SEV_1, initial()} then (103|111) [----] combiTimeTable.nextTimeEvent := if combiTimeTable.nextTimeEventScaled < 1e60 then combiTimeTable.nextTimeEventScaled else 1e60 (103|111) [----] end when; (104|112) [SCAL] (1) heatExchange_CounterFlowNTU.p_A = heatExchange_CounterFlowNTU.inletA.state.p ($RES_BND_367) (105|113) [SCAL] (1) multiSensor_Tpm5.outlet.state.T = heatExchange_CounterFlowNTU.inletA.state.T ($RES_SIM_317) (106|114) [WHEN] (1) ($RES_SIM_34) (106|114) [----] when {$SEV_1, initial()} then (106|114) [----] combiTimeTable.nextTimeEventScaled := Modelica.Blocks.Tables.Internal.getNextTimeEvent(combiTimeTable.tableID, time) (106|114) [----] end when; (107|115) [SCAL] (1) heatExchange_CounterFlowNTU.p_B = heatExchange_CounterFlowNTU.inletB.state.p ($RES_BND_368) (108|116) [SCAL] (1) multiSensor_Tpm5.outlet.state.p = heatExchange_CounterFlowNTU.inletA.state.p ($RES_SIM_318) (109|117) [SCAL] (1) heatExchange_CounterFlowNTU.dh_B = if noEvent(heatExchange_CounterFlowNTU.C_A < heatExchange_CounterFlowNTU.C_B) then (heatExchange_CounterFlowNTU.q_flowB * heatExchange_CounterFlowNTU.m_flow_B) / (heatExchange_CounterFlowNTU.m_flow_B ^ 2.0 + (heatExchange_CounterFlowNTU.m_flow_reg / 10.0) ^ 2.0) else if $SEV_0 then 0.0 else -heatExchange_CounterFlowNTU.cp_B * heatExchange_CounterFlowNTU.Delta_T_max * heatExchange_CounterFlowNTU.effectiveness ($RES_SIM_234) (110|118) [SCAL] (1) thermalConvectionPipe.p_out = thermalConvectionPipe.p_in ($RES_SIM_150) (111|119) [SCAL] (1) thermalConvectionPipe.outlet.r = pump.outlet.r - $DER.heatExchange_CounterFlowNTU.m_flow_B * thermalConvectionPipe.L ($RES_SIM_151) (112|120) [SCAL] (1) thermalConvectionPipe.h_out = thermalConvectionPipe.h_in + thermalConvectionPipe.dh ($RES_SIM_153) (113|121) [SCAL] (1) heatExchange_CounterFlowNTU.dh_A = if noEvent(heatExchange_CounterFlowNTU.C_A < heatExchange_CounterFlowNTU.C_B) then if $SEV_0 then 0.0 else heatExchange_CounterFlowNTU.cp_A * heatExchange_CounterFlowNTU.Delta_T_max * heatExchange_CounterFlowNTU.effectiveness else (heatExchange_CounterFlowNTU.q_flowA * heatExchange_CounterFlowNTU.m_flow_A) / (heatExchange_CounterFlowNTU.m_flow_A ^ 2.0 + (heatExchange_CounterFlowNTU.m_flow_reg / 10.0) ^ 2.0) ($RES_SIM_239) (114|122) [SCAL] (1) thermalConvectionPipe.dh = (thermalConvectionPipe.heatPort.Q_flow * heatExchange_CounterFlowNTU.m_flow_B) / (heatExchange_CounterFlowNTU.m_flow_B ^ 2.0 + (thermalConvectionPipe.m_flow_reg / 10.0) ^ 2.0) ($RES_SIM_155) (115|123) [SCAL] (1) thermalConvectionPipe.heatPort.Q_flow = thermalConvectionPipe.A_cond * thermalConvectionPipe.h_avg * (heatCapacitor.T - thermalConvectionPipe.T) ($RES_SIM_156) (116|124) [SCAL] (1) thermalConvectionPipe.h_avg = (0.299 * thermalConvectionPipe.Nu_turb) / thermalConvectionPipe.r ($RES_SIM_158) (117|125) [SCAL] (1) thermalConvectionPipe.Nu_turb = (6.9966555183946495 * (0.0396 * thermalConvectionPipe.Re_D + thermalConvectionPipe.eps) ^ 0.75) / (1.0 + 5.9966555183946495 * (2.44 * thermalConvectionPipe.Re_D + thermalConvectionPipe.eps) ^ (-0.125)) ($RES_SIM_159) (118|126) [SCAL] (1) $SEV_9 = heatExchange_CounterFlowNTU.m_flow_B > flexVolume.m_flow_assert ($RES_EVT_480) (119|127) [SCAL] (1) $SEV_10 = flexVolume.M > 0.0 ($RES_EVT_481) (120|128) [SCAL] (1) $SEV_11 = abs(pump.v_in - pump.v_out) / pump.v_in < pump.max_rel_volume ($RES_EVT_482) (121|129) [SCAL] (1) source.outlet.state.T = multiSensor_Tpm5.inlet.state.T ($RES_SIM_320) (122|130) [SCAL] (1) heatExchange_CounterFlowNTU.cpA_in = smooth(0, if $SEV_5 then 287.0512249529787 * (10099.5016 + heatExchange_CounterFlowNTU.inletA.state.T * ((-196.827561) + heatExchange_CounterFlowNTU.inletA.state.T * (5.00915511 + heatExchange_CounterFlowNTU.inletA.state.T * ((-0.00576101373) + heatExchange_CounterFlowNTU.inletA.state.T * (1.06685993e-5 + heatExchange_CounterFlowNTU.inletA.state.T * ((-7.94029797e-9) + 2.18523191e-12 * heatExchange_CounterFlowNTU.inletA.state.T)))))) * (1/(heatExchange_CounterFlowNTU.inletA.state.T * heatExchange_CounterFlowNTU.inletA.state.T)) else 287.0512249529787 * (241521.443 + heatExchange_CounterFlowNTU.inletA.state.T * ((-1257.8746) + heatExchange_CounterFlowNTU.inletA.state.T * (5.14455867 + heatExchange_CounterFlowNTU.inletA.state.T * ((-2.13854179e-4) + heatExchange_CounterFlowNTU.inletA.state.T * (7.06522784e-8 + heatExchange_CounterFlowNTU.inletA.state.T * ((-1.07148349e-11) + 6.57780015e-16 * heatExchange_CounterFlowNTU.inletA.state.T)))))) * (1/(heatExchange_CounterFlowNTU.inletA.state.T * heatExchange_CounterFlowNTU.inletA.state.T))) ($RES_BND_371) (123|131) [SCAL] (1) source.outlet.state.p = multiSensor_Tpm5.inlet.state.p ($RES_SIM_321) (124|132) [SCAL] (1) heatExchange_CounterFlowNTU.cpA_out = smooth(0, if $SEV_4 then 287.0512249529787 * (10099.5016 + heatExchange_CounterFlowNTU.outletA.state.T * ((-196.827561) + heatExchange_CounterFlowNTU.outletA.state.T * (5.00915511 + heatExchange_CounterFlowNTU.outletA.state.T * ((-0.00576101373) + heatExchange_CounterFlowNTU.outletA.state.T * (1.06685993e-5 + heatExchange_CounterFlowNTU.outletA.state.T * ((-7.94029797e-9) + 2.18523191e-12 * heatExchange_CounterFlowNTU.outletA.state.T)))))) * (1/(heatExchange_CounterFlowNTU.outletA.state.T * heatExchange_CounterFlowNTU.outletA.state.T)) else 287.0512249529787 * (241521.443 + heatExchange_CounterFlowNTU.outletA.state.T * ((-1257.8746) + heatExchange_CounterFlowNTU.outletA.state.T * (5.14455867 + heatExchange_CounterFlowNTU.outletA.state.T * ((-2.13854179e-4) + heatExchange_CounterFlowNTU.outletA.state.T * (7.06522784e-8 + heatExchange_CounterFlowNTU.outletA.state.T * ((-1.07148349e-11) + 6.57780015e-16 * heatExchange_CounterFlowNTU.outletA.state.T)))))) * (1/(heatExchange_CounterFlowNTU.outletA.state.T * heatExchange_CounterFlowNTU.outletA.state.T))) ($RES_BND_372) (125|133) [SCAL] (1) flowResistance.inlet.state.T = multiSensor_Tpm4.outlet.state.T ($RES_SIM_323) (126|134) [SCAL] (1) flowResistance.inlet.state.p = multiSensor_Tpm4.outlet.state.p ($RES_SIM_324) (127|135) [SCAL] (1) multiSensor_Tpm7.p = multiSensor_Tpm7.inlet.state.p ($RES_SIM_42) (128|136) [SCAL] (1) thermalConvectionPipe.outlet.state.T = multiSensor_Tpm4.inlet.state.T ($RES_SIM_326) (129|137) [SCAL] (1) multiSensor_Tpm7.T = (-273.15) + multiSensor_Tpm7.inlet.state.T ($RES_SIM_43) (130|138) [SCAL] (1) thermalConvectionPipe.outlet.state.p = multiSensor_Tpm4.inlet.state.p ($RES_SIM_327) (131|139) [RECD] (2) multiSensor_Tpm7.outlet.state = multiSensor_Tpm7.inlet.state ($RES_SIM_44) (132|141) [SCAL] (1) multiSensor_Tpm3.outlet.state.T = thermalConvectionPipe.inlet.state.T ($RES_SIM_329) (133|142) [SCAL] (1) heatExchange_CounterFlowNTU.q_flow = heatExchange_CounterFlowNTU.effectiveness * heatExchange_CounterFlowNTU.q_max ($RES_SIM_244) (134|143) [SCAL] (1) heatExchange_CounterFlowNTU.q_max = heatExchange_CounterFlowNTU.Delta_T_max * heatExchange_CounterFlowNTU.C_min ($RES_SIM_245) (135|144) [SCAL] (1) thermalConvectionPipe.Re_D = max(1.991172e6 * thermalConvectionPipe.r * thermalConvectionPipe.v_m, 1.0) ($RES_SIM_160) (136|145) [SCAL] (1) heatExchange_CounterFlowNTU.Delta_T_max = heatExchange_CounterFlowNTU.T_in_MediumA - heatExchange_CounterFlowNTU.T_in_MediumB ($RES_SIM_246) (137|146) [SCAL] (1) thermalConvectionPipe.v_m = (0.0010044335697769957 * heatExchange_CounterFlowNTU.m_flow_B) / thermalConvectionPipe.A_cross ($RES_SIM_161) (138|147) [SCAL] (1) heatExchange_CounterFlowNTU.NTU = (heatExchange_CounterFlowNTU.A * heatExchange_CounterFlowNTU.k_NTU) / max(heatExchange_CounterFlowNTU.C_min, 0.001) ($RES_SIM_247) (139|148) [SCAL] (1) heatExchange_CounterFlowNTU.C_r = heatExchange_CounterFlowNTU.C_min / max(heatExchange_CounterFlowNTU.C_max, 0.001) ($RES_SIM_248) (140|149) [SCAL] (1) pump.dr_corr = (pump.p_in + pump.dp) - pump.p_out ($RES_SIM_163) (141|150) [SCAL] (1) heatExchange_CounterFlowNTU.C_min = if noEvent(heatExchange_CounterFlowNTU.C_A > heatExchange_CounterFlowNTU.C_B) then heatExchange_CounterFlowNTU.C_B else heatExchange_CounterFlowNTU.C_A ($RES_SIM_249) (142|151) [SCAL] (1) pump.p_out = max(pump.p_min, pump.p_in + pump.dp) ($RES_SIM_164) (143|152) [SCAL] (1) pump.outlet.r = (pump.dr_corr + flexVolume.r_out) - $DER.heatExchange_CounterFlowNTU.m_flow_B * pump.L ($RES_SIM_165) (144|153) [SCAL] (1) pump.omega = $DER.pump.phi ($RES_SIM_167) (145|154) [SCAL] (1) pump.J_p * $DER.pump.omega = pump.tau - pump.tau_normalized ($RES_SIM_168) (146|155) [SCAL] (1) pump.tau_normalized = if noEvent(pump.W_t >= 0.0) then pump.tau_st else (heatExchange_CounterFlowNTU.m_flow_B * pump.dh) / noEvent(if abs(pump.omega) > pump.omega_reg then pump.omega else if pump.omega < 0.0 then -pump.omega_reg else pump.omega_reg) ($RES_SIM_169) (147|156) [SCAL] (1) multiSensor_Tpm3.outlet.state.p = thermalConvectionPipe.inlet.state.p ($RES_SIM_330) (148|157) [SCAL] (1) flexVolume.d = flexVolume.k_volume_damping * $FUN_11 ($RES_BND_381) (149|158) [SCAL] (1) flexVolume.r_damping = flexVolume.d * $DER.flexVolume.M ($RES_BND_382) (150|159) [SCAL] (1) pump.outlet.state.T = multiSensor_Tpm3.inlet.state.T ($RES_SIM_332) (151|160) [SCAL] (1) flexVolume.p_in = flexVolume.state_in.p ($RES_BND_383) (152|161) [SCAL] (1) pump.outlet.state.p = multiSensor_Tpm3.inlet.state.p ($RES_SIM_333) (153|162) [SCAL] (1) flexVolume.h_in = if noEvent(heatExchange_CounterFlowNTU.m_flow_B >= 0.0) then 4184.0 * ((-273.15) + flexVolume.state_in.T) else 4184.0 * ((-273.15) + flexVolume.T_heatPort) ($RES_BND_384) (154|163) [SCAL] (1) multiSensor_Tpm6.p = multiSensor_Tpm6.inlet.state.p ($RES_SIM_51) (155|164) [SCAL] (1) flexVolume.h_out = if noEvent(heatExchange_CounterFlowNTU.m_flow_B >= 0.0) then 4184.0 * ((-273.15) + flexVolume.state_out.T) else 4184.0 * ((-273.15) + flexVolume.T_heatPort) ($RES_BND_385) (156|165) [SCAL] (1) multiSensor_Tpm2.outlet.state.T = pump.inlet.state.T ($RES_SIM_335) (157|166) [SCAL] (1) multiSensor_Tpm6.T = (-273.15) + multiSensor_Tpm6.inlet.state.T ($RES_SIM_52) (158|167) [SCAL] (1) multiSensor_Tpm2.outlet.state.p = pump.inlet.state.p ($RES_SIM_336) (159|168) [RECD] (2) multiSensor_Tpm6.outlet.state = multiSensor_Tpm6.inlet.state ($RES_SIM_53) (160|170) [SCAL] (1) pump.p_in = pump.inlet.state.p ($RES_BND_387) (161|171) [SCAL] (1) heatExchange_CounterFlowNTU.C_max = if noEvent(heatExchange_CounterFlowNTU.C_A > heatExchange_CounterFlowNTU.C_B) then heatExchange_CounterFlowNTU.C_A else heatExchange_CounterFlowNTU.C_B ($RES_SIM_252) (162|172) [SCAL] (1) pump.h_in = 4184.0 * ((-273.15) + pump.inlet.state.T) ($RES_BND_388) (163|173) [SCAL] (1) flexVolume.outlet.state.T = multiSensor_Tpm2.inlet.state.T ($RES_SIM_338) (164|174) [SCAL] (1) flexVolume.outlet.state.p = multiSensor_Tpm2.inlet.state.p ($RES_SIM_339) (165|175) [SCAL] (1) prescribedHeatFlow.port.Q_flow = -prescribedHeatFlow.Q_flow * (1.0 + prescribedHeatFlow.alpha * (heatCapacitor.T - prescribedHeatFlow.T_ref)) ($RES_SIM_56) (166|176) [SCAL] (1) heatExchange_CounterFlowNTU.h_in_B = 4184.0 * ((-273.15) + heatExchange_CounterFlowNTU.inletB.state.T) ($RES_SIM_255) (167|177) [SCAL] (1) heatCapacitor.C * $DER.heatCapacitor.T = heatCapacitor.port.Q_flow ($RES_SIM_57) (168|178) [SCAL] (1) heatExchange_CounterFlowNTU.h_in_A = ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"Air\", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), heatExchange_CounterFlowNTU.inletA.state.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_SIM_256) (169|179) [SCAL] (1) heatCapacitor.der_T = $DER.heatCapacitor.T ($RES_SIM_58) (170|180) [SCAL] (1) heatExchange_CounterFlowNTU.T_in_MediumB = heatExchange_CounterFlowNTU.inletB.state.T ($RES_SIM_257) (171|181) [SCAL] (1) pump.Q_t = if noEvent(pump.W_t >= 0.0) then pump.W_t - heatExchange_CounterFlowNTU.m_flow_B * pump.dh else 0.0 ($RES_SIM_172) (172|182) [SCAL] (1) heatExchange_CounterFlowNTU.T_in_MediumA = heatExchange_CounterFlowNTU.inletA.state.T ($RES_SIM_258) (173|183) [SCAL] (1) heatExchange_CounterFlowNTU.C_B = (2.220446049250313e-16 + $FUN_3) * heatExchange_CounterFlowNTU.cp_B ($RES_SIM_259) (174|184) [SCAL] (1) pump.dh = (pump.W_t * heatExchange_CounterFlowNTU.m_flow_B) / (heatExchange_CounterFlowNTU.m_flow_B ^ 2.0 + pump.m_flow_reg ^ 2.0) ($RES_SIM_175) (175|185) [SCAL] (1) pump.W_t = pump.tau_st * pump.omega ($RES_SIM_176) (176|186) [SCAL] (1) pump.h_out = pump.h_in + pump.dh ($RES_SIM_177) (177|187) [SCAL] (1) pump.v_in = 1.0 / max(pump.rho_min, 995.586) ($RES_BND_391) (178|188) [SCAL] (1) multiSensor_Tpm1.outlet.state.T = flexVolume.inlet.state.T ($RES_SIM_341) (179|189) [SCAL] (1) pump.eta = if noEvent($FUN_9 > 1e-4) then pump.v_in * pump.dp * heatExchange_CounterFlowNTU.m_flow_B / pump.W_t else 0.0 ($RES_BND_392) (180|190) [SCAL] (1) multiSensor_Tpm1.outlet.state.p = flexVolume.inlet.state.p ($RES_SIM_342) (181|191) [SCAL] (1) pump.v_out = 1.0 / max(pump.rho_min, 995.586) ($RES_BND_393) (182|192) [SCAL] (1) multiSensor_Tpm1.inlet.state.T = heatExchange_CounterFlowNTU.outletB.state.T ($RES_SIM_344) (183|193) [SCAL] (1) source.L * (-$DER.heatExchange_CounterFlowNTU.m_flow_A) = source.outlet.r ($RES_SIM_101) (184|194) [SCAL] (1) fan.dr_corr = (fan.p_in + fan.dp) - fan.p_out ($RES_SIM_61) (185|195) [SCAL] (1) thermalConvectionPipe.p_in = thermalConvectionPipe.inlet.state.p ($RES_BND_395) (186|196) [SCAL] (1) multiSensor_Tpm1.inlet.state.p = heatExchange_CounterFlowNTU.outletB.state.p ($RES_SIM_345) (187|197) [SCAL] (1) heatExchange_CounterFlowNTU.C_A = (2.220446049250313e-16 + $FUN_2) * heatExchange_CounterFlowNTU.cp_A ($RES_SIM_260) (188|198) [SCAL] (1) fan.p_out = max(fan.p_min, fan.p_in + fan.dp) ($RES_SIM_62) (189|199) [SCAL] (1) thermalConvectionPipe.h_in = 4184.0 * ((-273.15) + thermalConvectionPipe.inlet.state.T) ($RES_BND_396) (190|200) [SCAL] (1) heatExchange_CounterFlowNTU.cp_B = 4184.0 ($RES_SIM_261) (191|201) [SCAL] (1) sink.inlet.r = (fan.dr_corr + heatExchange_CounterFlowNTU.outletA.r) - $DER.heatExchange_CounterFlowNTU.m_flow_A * fan.L ($RES_SIM_63) (192|202) [SCAL] (1) thermalConvectionPipe.T = thermalConvectionPipe.center_state.T ($RES_BND_397) (193|203) [SCAL] (1) heatExchange_CounterFlowNTU.cp_A = 0.5 * (heatExchange_CounterFlowNTU.cpA_in + heatExchange_CounterFlowNTU.cpA_out) ($RES_SIM_262) (194|204) [SCAL] (1) thermalConvectionPipe.A_cond = thermalConvectionPipe.r * 6.283185307179586 * thermalConvectionPipe.l ($RES_BND_398) (195|205) [SCAL] (1) multiSensor_Tpm6.inlet.r - flexVolume.r_in = $DER.heatExchange_CounterFlowNTU.m_flow_B * heatExchange_CounterFlowNTU.L ($RES_SIM_263) (196|206) [SCAL] (1) fan.omega = $DER.fan.phi ($RES_SIM_65) (197|207) [SCAL] (1) thermalConvectionPipe.A_cross = 3.141592653589793 * thermalConvectionPipe.r ^ 2.0 ($RES_BND_399) (198|208) [SCAL] (1) source.outlet.r - heatExchange_CounterFlowNTU.outletA.r = $DER.heatExchange_CounterFlowNTU.m_flow_A * heatExchange_CounterFlowNTU.L ($RES_SIM_264) (199|209) [SCAL] (1) fan.J_p * $DER.fan.omega = fan.tau - fan.tau_normalized ($RES_SIM_66) (200|210) [SCAL] (1) fan.tau_normalized = if noEvent(fan.W_t >= 0.0) then fan.tau_st else (heatExchange_CounterFlowNTU.m_flow_A * fan.dh) / noEvent(if abs(fan.omega) > fan.omega_reg then fan.omega else if fan.omega < 0.0 then -fan.omega_reg else fan.omega_reg) ($RES_SIM_67) (201|211) [SCAL] (1) flexVolume.Q_flow = 0.0 ($RES_SIM_181) (202|212) [SCAL] (1) heatExchange_CounterFlowNTU.effectiveness = if noEvent(heatExchange_CounterFlowNTU.C_r < 1.0) then (1.0 - $FUN_1) / (1.0 - heatExchange_CounterFlowNTU.C_r * $FUN_1) else heatExchange_CounterFlowNTU.NTU / (1.0 + heatExchange_CounterFlowNTU.NTU) ($RES_SIM_267) (203|213) [SCAL] (1) $DER.flexVolume.U_med = (flexVolume.h_in * heatExchange_CounterFlowNTU.m_flow_B + flexVolume.Q_flow) - flexVolume.h_out * heatExchange_CounterFlowNTU.m_flow_B ($RES_SIM_182) (204|214) [SCAL] (1) multiSensor_Tpm4.p = multiSensor_Tpm4.inlet.state.p ($RES_SIM_109) (205|215) [SCAL] (1) $DER.flexVolume.M = 0.0 ($RES_SIM_183) (206|216) [SCAL] (1) flexVolume.r + flexVolume.p_in = 99999.99999999999 * flexVolume.medium.p_bar ($RES_SIM_184) (207|217) [SCAL] (1) (-$DER.heatExchange_CounterFlowNTU.m_flow_B) * flexVolume.L = flexVolume.r_out - flexVolume.r_damping ($RES_SIM_185) (208|218) [SCAL] (1) $DER.heatExchange_CounterFlowNTU.m_flow_B * flexVolume.L = flexVolume.r_in - (flexVolume.r_damping + flexVolume.r) ($RES_SIM_186) (209|219) [SCAL] (1) thermalConvectionPipe.V = thermalConvectionPipe.A_cross * thermalConvectionPipe.l ($RES_BND_400) (210|220) [SCAL] (1) thermalConvectionPipe.M = thermalConvectionPipe.V * 995.586 ($RES_BND_403) (211|221) [SCAL] (1) flowResistance.p_in = flowResistance.inlet.state.p ($RES_BND_407) (212|222) [SCAL] (1) flowResistance.h_out = 4184.0 * ((-273.15) + flowResistance.inlet.state.T) ($RES_BND_408) (213|223) [SCAL] (1) multiSensor_Tpm4.T = (-273.15) + multiSensor_Tpm4.inlet.state.T ($RES_SIM_110) (214|224) [SCAL] (1) fan.Q_t = if noEvent(fan.W_t >= 0.0) then fan.W_t - heatExchange_CounterFlowNTU.m_flow_A * fan.dh else 0.0 ($RES_SIM_70) (215|225) [RECD] (2) multiSensor_Tpm4.outlet.state = multiSensor_Tpm4.inlet.state ($RES_SIM_111) (216|227) [SCAL] (1) fan.dh = (fan.W_t * heatExchange_CounterFlowNTU.m_flow_A) / (heatExchange_CounterFlowNTU.m_flow_A ^ 2.0 + fan.m_flow_reg ^ 2.0) ($RES_SIM_73) (217|228) [SCAL] (1) fan.W_t = fan.tau_st * fan.omega ($RES_SIM_74) (218|229) [SCAL] (1) fan.h_out = fan.h_in + fan.dh ($RES_SIM_75) (219|230) [RECD] (2) flexVolume.state_out = flexVolume.medium.state ($RES_SIM_190) (220|232) [SCAL] (1) multiSensor_Tpm3.p = multiSensor_Tpm3.inlet.state.p ($RES_SIM_118) (221|233) [SCAL] (1) 99999.99999999999 * flexVolume.medium.p_bar = flexVolume.p_ref + flexVolume.K * ((-1.0) + flexVolume.V / flexVolume.V_ref) ($RES_SIM_192) (222|234) [SCAL] (1) multiSensor_Tpm3.T = (-273.15) + multiSensor_Tpm3.inlet.state.T ($RES_SIM_119) (223|235) [SCAL] (1) speed1.a = (speed1.w_ref - speed1.w) * speed1.w_crit ($RES_SIM_79) (224|236) [SCAL] (1) flexVolume.density_derp_h = (995.586 * flexVolume.V_ref) / (flexVolume.K * flexVolume.V) ($RES_SIM_193) (225|237) [SCAL] (1) heatCapacitor.port.Q_flow + prescribedHeatFlow.port.Q_flow + thermalConvectionPipe.heatPort.Q_flow = 0.0 ($RES_SIM_279) (226|238) [SCAL] (1) flexVolume.medium.state.p = 99999.99999999999 * flexVolume.medium.p_bar ($RES_SIM_197) (227|239) [SCAL] (1) flexVolume.medium.state.T = flexVolume.T_heatPort ($RES_SIM_198) (228|240) [SCAL] (1) sink.p = sink.inlet.state.p ($RES_BND_412) (229|241) [SCAL] (1) fan.p_in = fan.inlet.state.p ($RES_BND_414) (230|242) [SCAL] (1) fan.h_in = ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"Air\", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), fan.inlet.state.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_BND_415) (231|243) [SCAL] (1) fan.v_in = 1.0 / max(fan.rho_min, (0.0034836987724536205 * fan.inlet.state.p) / fan.inlet.state.T) ($RES_BND_418) (232|244) [SCAL] (1) fan.R_in = fan.p_in / ((0.0034836987724536205 * fan.inlet.state.p) / fan.inlet.state.T) / fan.inlet.state.T ($RES_BND_419) (233|245) [SCAL] (1) heatExchange_CounterFlowNTU.outletA.state.p = heatExchange_CounterFlowNTU.p_A ($RES_SIM_442) (234|246) [SCAL] (1) heatExchange_CounterFlowNTU.outletA.state.T = Modelica.Math.Nonlinear.solveOneNonlinearEquation(function ThermofluidStream.Examples.SimpleCoolingCycle.heatExchange_CounterFlowNTU.MediumA.T_h.f_nonlinear(data = ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"Air\", BOX(0.0289651159), BOX(-4333.833858403446), BOX(298609.6803431054), BOX(1000.0), BOX({10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}), BOX({-176.796731, -3.921504225}), BOX({241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}), BOX({6462.26319, -8.147411905}), BOX(287.0512249529787)), h = BOX(heatExchange_CounterFlowNTU.h_out_A)), 200.0, 6000.0, 2.220446049250313e-14) ($RES_SIM_443) (235|247) [SCAL] (1) heatExchange_CounterFlowNTU.outletB.state.p = heatExchange_CounterFlowNTU.p_B ($RES_SIM_444) (236|248) [SCAL] (1) heatExchange_CounterFlowNTU.outletB.state.T = 273.15 + 2.390057361376673e-4 * heatExchange_CounterFlowNTU.h_out_B ($RES_SIM_445) (237|249) [SCAL] (1) speed.w = pump.omega ($RES_SIM_486) (238|250) [SCAL] (1) speed1.w = fan.omega ($RES_SIM_487) (239|251) [SCAL] (1) speed.a = $DER.pump.omega ($RES_SIM_488) (240|252) [SCAL] (1) speed1.a = $DER.fan.omega ($RES_SIM_489) =================== Scalar Matching =================== variable to equation ********************** var 1 --> eqn 150 var 2 --> eqn 24 var 3 --> eqn 140 var 4 --> eqn 123 var 5 --> eqn 85 var 6 --> eqn 63 var 7 --> eqn 57 var 8 --> eqn 133 var 9 --> eqn 213 var 10 --> eqn 141 var 11 --> eqn 165 var 12 --> eqn 39 var 13 --> eqn 62 var 14 --> eqn 107 var 15 --> eqn 26 var 16 --> eqn 156 var 17 --> eqn 72 var 18 --> eqn 66 var 19 --> eqn 221 var 20 --> eqn 208 var 21 --> eqn 212 var 22 --> eqn 13 var 23 --> eqn 64 var 24 --> eqn 95 var 25 --> eqn 171 var 26 --> eqn 209 var 27 --> eqn 121 var 28 --> eqn 215 var 29 --> eqn 76 var 30 --> eqn -1 var 31 --> eqn 82 var 32 --> eqn 237 var 33 --> eqn 45 var 34 --> eqn 86 var 35 --> eqn 242 var 36 --> eqn 227 var 37 --> eqn 204 var 38 --> eqn 23 var 39 --> eqn 125 var 40 --> eqn 84 var 41 --> eqn 194 var 42 --> eqn 128 var 43 --> eqn 61 var 44 --> eqn 144 var 45 --> eqn 127 var 46 --> eqn 167 var 47 --> eqn 27 var 48 --> eqn 2 var 49 --> eqn 225 var 50 --> eqn 5 var 51 --> eqn 56 var 52 --> eqn 168 var 53 --> eqn 139 var 54 --> eqn 206 var 55 --> eqn 193 var 56 --> eqn 7 var 57 --> eqn 43 var 58 --> eqn 147 var 59 --> eqn 49 var 60 --> eqn 146 var 61 --> eqn 172 var 62 --> eqn 11 var 63 --> eqn 252 var 64 --> eqn 79 var 65 --> eqn 41 var 66 --> eqn 106 var 67 --> eqn 37 var 68 --> eqn 239 var 69 --> eqn 148 var 70 --> eqn 183 var 71 --> eqn 83 var 72 --> eqn 176 var 73 --> eqn 108 var 74 --> eqn 52 var 75 --> eqn 179 var 76 --> eqn 55 var 77 --> eqn 65 var 78 --> eqn 114 var 79 --> eqn 88 var 80 --> eqn 89 var 81 --> eqn 33 var 82 --> eqn 187 var 83 --> eqn 149 var 84 --> eqn 87 var 85 --> eqn 112 var 86 --> eqn 191 var 87 --> eqn 153 var 88 --> eqn 217 var 89 --> eqn 115 var 90 --> eqn 42 var 91 --> eqn 6 var 92 --> eqn 184 var 93 --> eqn 69 var 94 --> eqn 243 var 95 --> eqn 244 var 96 --> eqn 134 var 97 --> eqn 180 var 98 --> eqn 175 var 99 --> eqn 78 var 100 --> eqn 104 var 101 --> eqn 32 var 102 --> eqn 12 var 103 --> eqn 59 var 104 --> eqn 48 var 105 --> eqn 177 var 106 --> eqn 186 var 107 --> eqn 50 var 108 --> eqn 145 var 109 --> eqn 30 var 110 --> eqn 80 var 111 --> eqn 77 var 112 --> eqn 126 var 113 --> eqn 142 var 114 --> eqn 103 var 115 --> eqn 25 var 116 --> eqn 102 var 117 --> eqn 101 var 118 --> eqn 198 var 119 --> eqn 205 var 120 --> eqn 100 var 121 --> eqn 91 var 122 --> eqn 99 var 123 --> eqn 98 var 124 --> eqn 97 var 125 --> eqn 96 var 126 --> eqn 158 var 127 --> eqn 195 var 128 --> eqn 199 var 129 --> eqn 233 var 130 --> eqn 181 var 131 --> eqn 68 var 132 --> eqn 241 var 133 --> eqn 157 var 134 --> eqn 151 var 135 --> eqn 211 var 136 --> eqn 92 var 137 --> eqn 110 var 138 --> eqn 216 var 139 --> eqn 117 var 140 --> eqn 190 var 141 --> eqn 90 var 142 --> eqn 40 var 143 --> eqn 58 var 144 --> eqn 28 var 145 --> eqn 196 var 146 --> eqn 143 var 147 --> eqn 19 var 148 --> eqn 21 var 149 --> eqn 234 var 150 --> eqn 46 var 151 --> eqn 161 var 152 --> eqn 223 var 153 --> eqn 111 var 154 --> eqn 138 var 155 --> eqn 53 var 156 --> eqn 35 var 157 --> eqn 131 var 158 --> eqn 166 var 159 --> eqn 230 var 160 --> eqn 224 var 161 --> eqn 81 var 162 --> eqn 137 var 163 --> eqn 189 var 164 --> eqn 75 var 165 --> eqn 17 var 166 --> eqn 118 var 167 --> eqn 105 var 168 --> eqn 154 var 169 --> eqn 130 var 170 --> eqn 122 var 171 --> eqn 200 var 172 --> eqn 38 var 173 --> eqn 185 var 174 --> eqn 71 var 175 --> eqn 152 var 176 --> eqn 14 var 177 --> eqn 164 var 178 --> eqn 155 var 179 --> eqn 34 var 180 --> eqn 173 var 181 --> eqn 119 var 182 --> eqn 70 var 183 --> eqn 44 var 184 --> eqn 120 var 185 --> eqn 159 var 186 --> eqn 207 var 187 --> eqn 203 var 188 --> eqn 54 var 189 --> eqn 197 var 190 --> eqn 16 var 191 --> eqn 219 var 192 --> eqn 232 var 193 --> eqn 214 var 194 --> eqn 51 var 195 --> eqn 251 var 196 --> eqn 248 var 197 --> eqn 178 var 198 --> eqn 163 var 199 --> eqn 135 var 200 --> eqn 8 var 201 --> eqn 174 var 202 --> eqn 246 var 203 --> eqn 201 var 204 --> eqn 236 var 205 --> eqn -1 var 206 --> eqn 60 var 207 --> eqn 109 var 208 --> eqn 73 var 209 --> eqn 245 var 210 --> eqn 169 var 211 --> eqn 31 var 212 --> eqn 47 var 213 --> eqn 1 var 214 --> eqn 222 var 215 --> eqn 238 var 216 --> eqn 129 var 217 --> eqn 235 var 218 --> eqn 226 var 219 --> eqn 247 var 220 --> eqn 3 var 221 --> eqn 22 var 222 --> eqn 192 var 223 --> eqn 240 var 224 --> eqn 170 var 225 --> eqn 10 var 226 --> eqn 94 var 227 --> eqn 36 var 228 --> eqn 218 var 229 --> eqn 160 var 230 --> eqn 162 var 231 --> eqn 67 var 232 --> eqn 93 var 233 --> eqn 228 var 234 --> eqn 229 var 235 --> eqn 18 var 236 --> eqn 202 var 237 --> eqn 74 var 238 --> eqn 231 var 239 --> eqn 136 var 240 --> eqn 4 var 241 --> eqn 113 var 242 --> eqn 132 var 243 --> eqn 188 var 244 --> eqn 220 var 245 --> eqn 124 var 246 --> eqn 29 var 247 --> eqn 116 var 248 --> eqn 210 var 249 --> eqn 182 var 250 --> eqn 20 var 251 --> eqn 9 var 252 --> eqn 15 var 253 --> eqn 250 var 254 --> eqn 249 equation to variable ********************** eqn 1 --> var 213 eqn 2 --> var 48 eqn 3 --> var 220 eqn 4 --> var 240 eqn 5 --> var 50 eqn 6 --> var 91 eqn 7 --> var 56 eqn 8 --> var 200 eqn 9 --> var 251 eqn 10 --> var 225 eqn 11 --> var 62 eqn 12 --> var 102 eqn 13 --> var 22 eqn 14 --> var 176 eqn 15 --> var 252 eqn 16 --> var 190 eqn 17 --> var 165 eqn 18 --> var 235 eqn 19 --> var 147 eqn 20 --> var 250 eqn 21 --> var 148 eqn 22 --> var 221 eqn 23 --> var 38 eqn 24 --> var 2 eqn 25 --> var 115 eqn 26 --> var 15 eqn 27 --> var 47 eqn 28 --> var 144 eqn 29 --> var 246 eqn 30 --> var 109 eqn 31 --> var 211 eqn 32 --> var 101 eqn 33 --> var 81 eqn 34 --> var 179 eqn 35 --> var 156 eqn 36 --> var 227 eqn 37 --> var 67 eqn 38 --> var 172 eqn 39 --> var 12 eqn 40 --> var 142 eqn 41 --> var 65 eqn 42 --> var 90 eqn 43 --> var 57 eqn 44 --> var 183 eqn 45 --> var 33 eqn 46 --> var 150 eqn 47 --> var 212 eqn 48 --> var 104 eqn 49 --> var 59 eqn 50 --> var 107 eqn 51 --> var 194 eqn 52 --> var 74 eqn 53 --> var 155 eqn 54 --> var 188 eqn 55 --> var 76 eqn 56 --> var 51 eqn 57 --> var 7 eqn 58 --> var 143 eqn 59 --> var 103 eqn 60 --> var 206 eqn 61 --> var 43 eqn 62 --> var 13 eqn 63 --> var 6 eqn 64 --> var 23 eqn 65 --> var 77 eqn 66 --> var 18 eqn 67 --> var 231 eqn 68 --> var 131 eqn 69 --> var 93 eqn 70 --> var 182 eqn 71 --> var 174 eqn 72 --> var 17 eqn 73 --> var 208 eqn 74 --> var 237 eqn 75 --> var 164 eqn 76 --> var 29 eqn 77 --> var 111 eqn 78 --> var 99 eqn 79 --> var 64 eqn 80 --> var 110 eqn 81 --> var 161 eqn 82 --> var 31 eqn 83 --> var 71 eqn 84 --> var 40 eqn 85 --> var 5 eqn 86 --> var 34 eqn 87 --> var 84 eqn 88 --> var 79 eqn 89 --> var 80 eqn 90 --> var 141 eqn 91 --> var 121 eqn 92 --> var 136 eqn 93 --> var 232 eqn 94 --> var 226 eqn 95 --> var 24 eqn 96 --> var 125 eqn 97 --> var 124 eqn 98 --> var 123 eqn 99 --> var 122 eqn 100 --> var 120 eqn 101 --> var 117 eqn 102 --> var 116 eqn 103 --> var 114 eqn 104 --> var 100 eqn 105 --> var 167 eqn 106 --> var 66 eqn 107 --> var 14 eqn 108 --> var 73 eqn 109 --> var 207 eqn 110 --> var 137 eqn 111 --> var 153 eqn 112 --> var 85 eqn 113 --> var 241 eqn 114 --> var 78 eqn 115 --> var 89 eqn 116 --> var 247 eqn 117 --> var 139 eqn 118 --> var 166 eqn 119 --> var 181 eqn 120 --> var 184 eqn 121 --> var 27 eqn 122 --> var 170 eqn 123 --> var 4 eqn 124 --> var 245 eqn 125 --> var 39 eqn 126 --> var 112 eqn 127 --> var 45 eqn 128 --> var 42 eqn 129 --> var 216 eqn 130 --> var 169 eqn 131 --> var 157 eqn 132 --> var 242 eqn 133 --> var 8 eqn 134 --> var 96 eqn 135 --> var 199 eqn 136 --> var 239 eqn 137 --> var 162 eqn 138 --> var 154 eqn 139 --> var 53 eqn 140 --> var 3 eqn 141 --> var 10 eqn 142 --> var 113 eqn 143 --> var 146 eqn 144 --> var 44 eqn 145 --> var 108 eqn 146 --> var 60 eqn 147 --> var 58 eqn 148 --> var 69 eqn 149 --> var 83 eqn 150 --> var 1 eqn 151 --> var 134 eqn 152 --> var 175 eqn 153 --> var 87 eqn 154 --> var 168 eqn 155 --> var 178 eqn 156 --> var 16 eqn 157 --> var 133 eqn 158 --> var 126 eqn 159 --> var 185 eqn 160 --> var 229 eqn 161 --> var 151 eqn 162 --> var 230 eqn 163 --> var 198 eqn 164 --> var 177 eqn 165 --> var 11 eqn 166 --> var 158 eqn 167 --> var 46 eqn 168 --> var 52 eqn 169 --> var 210 eqn 170 --> var 224 eqn 171 --> var 25 eqn 172 --> var 61 eqn 173 --> var 180 eqn 174 --> var 201 eqn 175 --> var 98 eqn 176 --> var 72 eqn 177 --> var 105 eqn 178 --> var 197 eqn 179 --> var 75 eqn 180 --> var 97 eqn 181 --> var 130 eqn 182 --> var 249 eqn 183 --> var 70 eqn 184 --> var 92 eqn 185 --> var 173 eqn 186 --> var 106 eqn 187 --> var 82 eqn 188 --> var 243 eqn 189 --> var 163 eqn 190 --> var 140 eqn 191 --> var 86 eqn 192 --> var 222 eqn 193 --> var 55 eqn 194 --> var 41 eqn 195 --> var 127 eqn 196 --> var 145 eqn 197 --> var 189 eqn 198 --> var 118 eqn 199 --> var 128 eqn 200 --> var 171 eqn 201 --> var 203 eqn 202 --> var 236 eqn 203 --> var 187 eqn 204 --> var 37 eqn 205 --> var 119 eqn 206 --> var 54 eqn 207 --> var 186 eqn 208 --> var 20 eqn 209 --> var 26 eqn 210 --> var 248 eqn 211 --> var 135 eqn 212 --> var 21 eqn 213 --> var 9 eqn 214 --> var 193 eqn 215 --> var 28 eqn 216 --> var 138 eqn 217 --> var 88 eqn 218 --> var 228 eqn 219 --> var 191 eqn 220 --> var 244 eqn 221 --> var 19 eqn 222 --> var 214 eqn 223 --> var 152 eqn 224 --> var 160 eqn 225 --> var 49 eqn 226 --> var 218 eqn 227 --> var 36 eqn 228 --> var 233 eqn 229 --> var 234 eqn 230 --> var 159 eqn 231 --> var 238 eqn 232 --> var 192 eqn 233 --> var 129 eqn 234 --> var 149 eqn 235 --> var 217 eqn 236 --> var 204 eqn 237 --> var 32 eqn 238 --> var 215 eqn 239 --> var 68 eqn 240 --> var 223 eqn 241 --> var 132 eqn 242 --> var 35 eqn 243 --> var 94 eqn 244 --> var 95 eqn 245 --> var 209 eqn 246 --> var 202 eqn 247 --> var 219 eqn 248 --> var 196 eqn 249 --> var 254 eqn 250 --> var 253 eqn 251 --> var 195 eqn 252 --> var 63 " [Timeout remaining time 659] [Calling sys.exit(0), Time elapsed: 4.6518588089966215] Failed to read output from testmodel.py, exit status != 0: 0.9006915770005435 0.915319362 0.129118268 Calling exit ...