Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_ThermofluidStream.Processes.Tests.CentrifugalPump.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 0.00133/0.00133, allocations: 76.22 kB / 19.95 MB, free: 1.945 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 0.001466/0.001466, allocations: 170.9 kB / 23.22 MB, free: 4.949 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 1.469/1.469, allocations: 177.2 MB / 203.6 MB, free: 9.184 MB / 190.1 MB
"
[Timeout remaining time 178]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.3.0/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.3.0/package.mo): time 0.8095/0.8095, allocations: 80.22 MB / 340.2 MB, free: 10.89 MB / 318.1 MB
"
[Timeout remaining time 179]
Using package ThermofluidStream with version 1.3.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.3.0/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.Processes.Tests.CentrifugalPump,tolerance=1e-06,outputFormat="mat",numberOfIntervals=1000,variableFilter="CPUtime|EventCounter|Time|V_flow_sine.amplitude|V_flow_sine.f|V_flow_sine.offset|V_flow_sine.phase|V_flow_sine.startTime|V_flow_sine.y|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.H0|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.Hf|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.MM|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.R_s|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.Tlimit|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh.1.|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh.2.|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh.3.|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh.4.|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh.5.|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh.6.|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh.7.|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow.1.|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow.2.|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow.3.|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow.4.|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow.5.|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow.6.|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow.7.|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.bhigh.1.|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.bhigh.2.|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.blow.1.|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.blow.2.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.H0|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.Hf|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.MM|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.R_s|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.Tlimit|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh.1.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh.2.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh.3.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh.4.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh.5.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh.6.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh.7.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow.1.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow.2.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow.3.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow.4.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow.5.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow.6.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow.7.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.bhigh.1.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.bhigh.2.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.blow.1.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.blow.2.|centrifugalPump1.L|centrifugalPump1.P|centrifugalPump1.P_ref|centrifugalPump1.P_reg|centrifugalPump1.TC|centrifugalPump1.V_flow|centrifugalPump1.V_flow_par|centrifugalPump1.V_flow_ref|centrifugalPump1.V_n|centrifugalPump1.c_head.1.|centrifugalPump1.c_head.2.|centrifugalPump1.c_head.3.|centrifugalPump1.c_power.1.|centrifugalPump1.c_power.2.|centrifugalPump1.c_power.3.|centrifugalPump1.clip_p_out|centrifugalPump1.coeff.P_ref|centrifugalPump1.coeff.V_flow_ref|centrifugalPump1.coeff.c_head.1.|centrifugalPump1.coeff.c_head.2.|centrifugalPump1.coeff.c_head.3.|centrifugalPump1.coeff.c_power.1.|centrifugalPump1.coeff.c_power.2.|centrifugalPump1.coeff.c_power.3.|centrifugalPump1.coeff.eta_ref|centrifugalPump1.coeff.head_ref|centrifugalPump1.coeff.rho_ref|centrifugalPump1.coeff.tau_ref|centrifugalPump1.coeff.w_ref|centrifugalPump1.coefficients.P_0n|centrifugalPump1.coefficients.V_0n|centrifugalPump1.coefficients.V_flow_peak|centrifugalPump1.coefficients.dp_peak|centrifuga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malConvectionPipe.m_flow|thermalConvectionPipe.m_flowStateSelect|thermalConvectionPipe.m_flow_0|thermalConvectionPipe.m_flow_reg|thermalConvectionPipe.mu|thermalConvectionPipe.outlet.m_flow|thermalConvectionPipe.outlet.r|thermalConvectionPipe.outlet.state.T|thermalConvectionPipe.outlet.state.p|thermalConvectionPipe.p_in|thermalConvectionPipe.p_min|thermalConvectionPipe.p_out|thermalConvectionPipe.r|thermalConvectionPipe.rho|thermalConvectionPipe.turb_flag|thermalConvectionPipe.v_m|torque.flange.phi|torque.flange.tau|torque.phi_support|torque.tau|w_sine.amplitude|w_sine.f|w_sine.offset|w_sine.phase|w_sine.startTime|w_sine.y|w_sine1.amplitude|w_sine1.f|w_sine1.offset|w_sine1.phase|w_sine1.startTime|w_sine1.y",fileNamePrefix="ThermofluidStream_ThermofluidStream.Processes.Tests.CentrifugalPump") [Timeout 660]
"Notification: Performance of FrontEnd - Absyn->SCode: time 2.778e-05/2.778e-05, allocations: 6.109 kB / 0.4938 GB, free: 25.5 MB / 446.1 MB
Notification: Performance of NFInst.instantiate(ThermofluidStream.Processes.Tests.CentrifugalPump): time 0.2438/0.2439, allocations: 183.4 MB / 0.6729 GB, free: 7.461 MB / 0.5762 GB
Notification: Performance of NFInst.instExpressions: time 0.02945/0.2733, allocations: 19.12 MB / 0.6916 GB, free: 4.281 MB / 0.5919 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.001936/0.2753, allocations: 99.06 kB / 0.6917 GB, free: 4.184 MB / 0.5919 GB
Notification: Performance of NFTyping.typeComponents: time 0.003286/0.2785, allocations: 1.013 MB / 0.6927 GB, free: 3.164 MB / 0.5919 GB
Notification: Performance of NFTyping.typeBindings: time 0.007798/0.2863, allocations: 2.453 MB / 0.6951 GB, free: 0.6992 MB / 0.5919 GB
Notification: Performance of NFTyping.typeClassSections: time 0.3021/0.5885, allocations: 1.591 MB / 0.6966 GB, free: 7.109 MB / 0.5919 GB
Notification: Performance of NFFlatten.flatten: time 0.005474/0.5939, allocations: 3.875 MB / 0.7004 GB, free: 7.109 MB / 0.5919 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.0008165/0.5947, allocations: 274 kB / 0.7007 GB, free: 7.031 MB / 0.5919 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.003574/0.5983, allocations: 2.142 MB / 0.7028 GB, free: 7.031 MB / 0.5919 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.001029/0.5994, allocations: 0.8708 MB / 0.7036 GB, free: 7.031 MB / 0.5919 GB
Notification: Performance of NFPackage.collectConstants: time 0.0002168/0.5996, allocations: 151.8 kB / 0.7037 GB, free: 7.031 MB / 0.5919 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.003756/0.6033, allocations: 1.783 MB / 0.7055 GB, free: 7.031 MB / 0.5919 GB
Notification: Performance of combineBinaries: time 0.002713/0.606, allocations: 3.841 MB / 0.7092 GB, free: 5.75 MB / 0.5919 GB
Notification: Performance of replaceArrayConstructors: time 0.00159/0.6076, allocations: 2.525 MB / 0.7117 GB, free: 4.469 MB / 0.5919 GB
Notification: Performance of NFVerifyModel.verify: time 0.000573/0.6082, allocations: 197.8 kB / 0.7119 GB, free: 4.469 MB / 0.5919 GB
Notification: Performance of FrontEnd: time 0.0004781/0.6087, allocations: 150.5 kB / 0.712 GB, free: 4.469 MB / 0.5919 GB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 355 (337)
 * Number of variables: 357 (357)
Notification: Performance of [SIM] Bindings: time 0.009746/0.6184, allocations: 10.04 MB / 0.7218 GB, free: 1.125 MB / 0.5919 GB
Notification: Performance of [SIM] FunctionAlias: time 0.002007/0.6204, allocations: 1.328 MB / 0.7231 GB, free: 0.9375 MB / 0.5919 GB
Notification: Performance of [SIM] Early Inline: time 0.00601/0.6264, allocations: 5.504 MB / 0.7285 GB, free: 0.793 MB / 0.5919 GB
Notification: Performance of [SIM] Simplify 1: time 0.00161/0.6281, allocations: 0.7584 MB / 0.7293 GB, free: 0.5391 MB / 0.5919 GB
Warning: NBAlias.setStartFixed: Multiple variables are fixed and have identical start values. Use -d=dumprepl for more information.
Notification: Performance of [SIM] Alias: time 0.008899/0.6369, allocations: 6.162 MB / 0.7353 GB, free: 14.98 MB / 0.6075 GB
Notification: Performance of [SIM] Simplify 2: time 0.001123/0.6381, allocations: 0.5858 MB / 0.7359 GB, free: 14.77 MB / 0.6075 GB
Notification: Performance of [SIM] Remove Stream: time 0.0005281/0.6386, allocations: 382 kB / 0.7362 GB, free: 14.67 MB / 0.6075 GB
Notification: Performance of [SIM] Detect States: time 0.001639/0.6402, allocations: 1.429 MB / 0.7376 GB, free: 14.36 MB / 0.6075 GB
Notification: Performance of [SIM] Events: time 0.0004374/0.6407, allocations: 298.8 kB / 0.7379 GB, free: 14.31 MB / 0.6075 GB
Notification: Performance of [SIM] Partitioning: time 0.002507/0.6432, allocations: 2.032 MB / 0.7399 GB, free: 13.91 MB / 0.6075 GB
Error: Internal error NBSorting.tarjan failed to sort system:
System Variables (224/224)
****************************
(1|1)          [ALGB] (1) Real heatExchanger.NTU
(2|2)          [DER-] (1) Real $DER.inertia.w
(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.Processes.Tests.CentrifugalPump.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) output Real multiSensor_Tpm5.outlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(7|7)          [ALGB] (1) output Real multiSensor_Tpm4.outlet.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(8|8)          [DER-] (1) Real $DER.flexVolume.U_med
(9|9)          [ALGB] (1) output Real multiSensor_Tpm3.outlet.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(10|10)        [ALGB] (1) output Real multiSensor_Tpm2.outlet.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(11|11)        [ALGB] (1) output Real multiSensor_Tpm1.outlet.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(12|12)        [ALGB] (1) Real flowResistance.dp
(13|13)        [DISC] (1) Real $TEV_8
(14|14)        [ALGB] (1) Real heatExchanger.T_in_MediumA (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(15|15)        [ALGB] (1) Real heatExchanger.T_in_MediumB (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(16|16)        [ALGB] (1) Real heatExchanger.summary.Tout_A (start = 288.15, min = 0.0, nominal = 300.0)
(17|17)        [ALGB] (1) input Real thermalConvectionPipe.inlet.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(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.Processes.Tests.CentrifugalPump.flowResistance.Medium.pressure(flowResistance.inlet.state) (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(20|20)        [ALGB] (1) output Real heatExchanger.outletA.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(21|21)        [ALGB] (1) output Real heatExchanger.outletB.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(22|22)        [DISC] (1) Boolean $TEV_1
(23|23)        [ALGB] (1) Real centrifugalPump1.w_t (min = -1e10, max = 1e10, nominal = 1e6)
(24|24)        [DER-] (1) Real $DER.flexVolume.M
(25|25)        [ALGB] (1) protected Real centrifugalPump1.pr = centrifugalPump1.p_out / centrifugalPump1.p_in
(26|26)        [ALGB] (1) flow Real heatCapacitor.port.Q_flow
(27|27)        [ALGB] (1) protected Real heatExchanger.cpA_out = ThermofluidStream.Processes.Tests.CentrifugalPump.heatExchanger.MediumA.specificHeatCapacityCp(heatExchanger.outletA.state) (start = 1000.0, min = 0.0, max = 1e7, nominal = 1000.0)
(28|28)        [ALGB] (1) protected Real heatExchanger.p_B = ThermofluidStream.Processes.Tests.CentrifugalPump.heatExchanger.MediumB.pressure(heatExchanger.inletB.state) (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(29|29)        [ALGB] (1) protected Real heatExchanger.p_A = ThermofluidStream.Processes.Tests.CentrifugalPump.heatExchanger.MediumA.pressure(heatExchanger.inletA.state) (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(30|30)        [DER-] (1) Real $DER.heatExchanger.h_out_A
(31|31)        [ALGB] (1) Real heatExchanger.summary.hin_A
(32|32)        [DER-] (1) Real $DER.heatExchanger.h_out_B
(33|33)        [ALGB] (1) protected Real flowResistance.rho_in = max(flowResistance.rho_min, ThermofluidStream.Processes.Tests.CentrifugalPump.flowResistance.Medium.density(flowResistance.inlet.state)) (start = 1.0, min = 0.0, max = 1e5, nominal = 1.0)
(34|34)        [ALGB] (1) protected Real thermalConvectionPipe.A_cond = thermalConvectionPipe.r * 6.283185307179586 * thermalConvectionPipe.l
(35|35)        [ALGB] (1) protected Real flowResistance1.p_in = ThermofluidStream.Processes.Tests.CentrifugalPump.flowResistance1.Medium.pressure(flowResistance1.inlet.state) (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(36|36)        [ALGB] (1) protected Real thermalConvectionPipe.Nu_turb
(37|37)        [ALGB] (1) Real heatExchanger.summary.dT_A
(38|38)        [ALGB] (1) Real centrifugalPump1.V_flow = heatExchanger.m_flow_B / 995.586
(39|39)        [ALGB] (1) output Real multiSensor_Tpm1.outlet.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(40|40)        [ALGB] (1) protected Real thermalConvectionPipe.Re_D
(41|41)        [ALGB] (1) output Real multiSensor_Tpm2.outlet.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(42|42)        [ALGB] (1) output Real thermalConvectionPipe.outlet.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(43|43)        [ALGB] (1) output Real multiSensor_Tpm3.outlet.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(44|44)        [ALGB] (1) output Real multiSensor_Tpm4.outlet.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(45|45)        [ALGB] (1) output Real multiSensor_Tpm5.outlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(46|46)        [ALGB] (1) output Real multiSensor_Tpm6.outlet.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(47|47)        [ALGB] (1) output Real multiSensor_Tpm7.outlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(48|48)        [DER-] (1) Real $DER.centrifugalPump1.phi
(49|49)        [ALGB] (1) Real source.outlet.r
(50|50)        [ALGB] (1) output Real flowResistance1.outlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(51|51)        [ALGB] (1) protected Real thermalConvectionPipe.v_m
(52|52)        [ALGB] (1) output Real centrifugalPump1.outlet.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(53|53)        [ALGB] (1) output Real flowResistance1.outlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(54|54)        [ALGB] (1) output Real flowResistance.outlet.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(55|55)        [ALGB] (1) input Real sink.inlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(56|56)        [ALGB] (1) protected Real heatExchanger.C_B
(57|57)        [ALGB] (1) protected Real heatExchanger.C_A
(58|58)        [ALGB] (1) output Real source.outlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(59|59)        [ALGB] (1) protected Real flexVolume.T_heatPort (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(60|60)        [ALGB] (1) protected Real centrifugalPump1.tau_n = centrifugalPump1.tau / centrifugalPump1.tau_ref (start = 1.0)
(61|61)        [ALGB] (1) Real centrifugalPump1.dr_corr
(62|62)        [ALGB] (1) input Real sink.inlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(63|63)        [ALGB] (1) Real $FUN_9
(64|64)        [ALGB] (1) Real heatCapacitor.der_T (start = 0.0)
(65|65)        [ALGB] (1) Real $FUN_8
(66|66)        [ALGB] (1) Real heatExchanger.summary.Tin_B (start = 288.15, min = 0.0, nominal = 300.0)
(67|67)        [ALGB] (1) Real $FUN_7
(68|68)        [ALGB] (1) protected Real centrifugalPump1.V_n = centrifugalPump1.V_flow / centrifugalPump1.V_flow_ref
(69|69)        [ALGB] (1) Real $FUN_6
(70|70)        [ALGB] (1) Real $FUN_5
(71|71)        [ALGB] (1) protected Real centrifugalPump1.p_in = ThermofluidStream.Processes.Tests.CentrifugalPump.centrifugalPump1.Medium.pressure(centrifugalPump1.inlet.state) (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(72|72)        [ALGB] (1) protected Real flowResistance1.rho_in = max(flowResistance1.rho_min, ThermofluidStream.Processes.Tests.CentrifugalPump.flowResistance1.Medium.density(flowResistance1.inlet.state)) (start = 10.0, min = 0.0, max = 1e5, nominal = 10.0)
(73|73)        [ALGB] (1) Real $FUN_3
(74|74)        [DISS] (1) protected discrete Real combiTimeTable.nextTimeEventScaled (fixed = true, start = 0.0)
(75|75)        [ALGB] (1) Real $FUN_2
(76|76)        [ALGB] (1) Real $FUN_1
(77|77)        [ALGB] (1) Real heatExchanger.summary.Q_flow_A
(78|78)        [ALGB] (1) protected Real heatExchanger.h_in_A (start = 298609.6803431054, min = -1e10, max = 1e10, nominal = 1e5)
(79|79)        [ALGB] (1) protected Real heatExchanger.h_in_B (min = -1e10, max = 1e10, nominal = 1e6)
(80|80)        [ALGB] (1) protected Real heatExchanger.cp_A
(81|81)        [ALGB] (1) protected Real heatExchanger.cp_B
(82|82)        [ALGB] (1) protected Real flexVolume.state_out.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(83|83)        [ALGB] (1) Real centrifugalPump1.eta_is
(84|84)        [DER-] (1) Real $DER.heatExchanger.m_flow_B
(85|85)        [ALGB] (1) input Real flowResistance.inlet.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(86|86)        [ALGB] (1) flow Real prescribedHeatFlow.port.Q_flow
(87|87)        [ALGB] (1) protected Real centrifugalPump1.h_in = ThermofluidStream.Processes.Tests.CentrifugalPump.centrifugalPump1.Medium.specificEnthalpy(centrifugalPump1.inlet.state) (min = -1e10, max = 1e10, nominal = 1e6)
(88|88)        [ALGB] (1) input Real flowResistance1.inlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(89|89)        [ALGB] (1) protected Real centrifugalPump1.h_n = centrifugalPump1.head / centrifugalPump1.head_ref
(90|90)        [ALGB] (1) input Real heatExchanger.inletB.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(91|91)        [ALGB] (1) input Real heatExchanger.inletA.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(92|92)        [ALGB] (1) input Real heatExchanger.inletA.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(93|93)        [ALGB] (1) input Real heatExchanger.inletB.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(94|94)        [ALGB] (1) output Real flowResistance.outlet.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(95|95)        [DER-] (1) Real $DER.heatCapacitor.T
(96|96)        [ALGB] (1) Real heatExchanger.summary.hout_B
(97|97)        [ALGB] (1) protected Real flowResistance1.h_out (start = 298609.6803431054, min = -1e10, max = 1e10, nominal = 1e5)
(98|98)        [ALGB] (1) protected Real centrifugalPump1.rho_n = 995.586 / centrifugalPump1.rho_ref
(99|99)        [ALGB] (1) protected Real thermalConvectionPipe.h_in = ThermofluidStream.Processes.Tests.CentrifugalPump.thermalConvectionPipe.Medium.specificEnthalpy(thermalConvectionPipe.inlet.state) (min = -1e10, max = 1e10, nominal = 1e6)
(100|100)      [ALGB] (1) Real heatExchanger.summary.Tout_B (start = 288.15, min = 0.0, nominal = 300.0)
(101|101)      [DISC] (1) Boolean $SEV_8
(102|102)      [DISC] (1) Boolean $SEV_7
(103|103)      [DISC] (1) Boolean $SEV_6
(104|104)      [ALGB] (1) Real multiSensor_Tpm6.inlet.r
(105|105)      [DISC] (1) Boolean $SEV_4
(106|106)      [ALGB] (1) Real heatExchanger.summary.hin_B
(107|107)      [ALGB] (1) output Real centrifugalPump1.outlet.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(108|108)      [DISC] (1) Boolean $SEV_3
(109|109)      [DISC] (1) Boolean $SEV_2
(110|110)      [ALGB] (1) Real multiSensor_Tpm3.inlet.r
(111|111)      [ALGB] (1) Real heatExchanger.effectiveness
(112|112)      [DISC] (1) Boolean $SEV_1
(113|113)      [DISC] (1) Boolean $SEV_0
(114|114)      [ALGB] (1) protected Real flexVolume.r_damping = flexVolume.d * der(flexVolume.M)
(115|115)      [ALGB] (1) protected Real thermalConvectionPipe.p_in = ThermofluidStream.Processes.Tests.CentrifugalPump.thermalConvectionPipe.Medium.pressure(thermalConvectionPipe.inlet.state) (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(116|116)      [ALGB] (1) input Real thermalConvectionPipe.inlet.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(117|117)      [ALGB] (1) Real flexVolume.V
(118|118)      [ALGB] (1) protected Real centrifugalPump1.p_out (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(119|119)      [ALGB] (1) protected Real flexVolume.state_out.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(120|120)      [ALGB] (1) Real heatExchanger.outletA.r
(121|121)      [ALGB] (1) Real heatExchanger.Delta_T_max
(122|122)      [ALGB] (1) Real centrifugalPump1.tau
(123|123)      [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))))
(124|124)      [ALGB] (1) Real flexVolume.Q_flow
(125|125)      [ALGB] (1) protected Real flexVolume.r
(126|126)      [ALGB] (1) Real heatExchanger.summary.dh_B
(127|127)      [ALGB] (1) protected Real heatExchanger.C_max
(128|128)      [ALGB] (1) input Real flexVolume.inlet.state.p = flexVolume.state_in.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(129|129)      [ALGB] (1) Real flowResistance.dr_corr
(130|130)      [ALGB] (1) protected Real heatExchanger.C_min
(131|131)      [ALGB] (1) output Real source.outlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(132|132)      [ALGB] (1) Real multiSensor_Tpm1.T
(133|133)      [ALGB] (1) input Real multiSensor_Tpm1.inlet.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(134|134)      [ALGB] (1) Real multiSensor_Tpm2.T
(135|135)      [ALGB] (1) input Real multiSensor_Tpm2.inlet.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(136|136)      [ALGB] (1) Real multiSensor_Tpm3.T
(137|137)      [ALGB] (1) protected Real flowResistance1.mu_in = ThermofluidStream.Processes.Tests.CentrifugalPump.flowResistance1.Medium.dynamicViscosity(flowResistance1.inlet.state) (start = 0.001, min = 0.0, max = 1e8, nominal = 0.001)
(138|138)      [ALGB] (1) input Real multiSensor_Tpm3.inlet.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(139|139)      [ALGB] (1) Real multiSensor_Tpm4.T
(140|140)      [DISS] (1) protected discrete Real combiTimeTable.nextTimeEvent (fixed = true, start = 0.0)
(141|141)      [ALGB] (1) input Real multiSensor_Tpm4.inlet.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(142|142)      [ALGB] (1) Real multiSensor_Tpm5.T
(143|143)      [ALGB] (1) protected Real flowResistance.h_out (min = -1e10, max = 1e10, nominal = 1e6)
(144|144)      [ALGB] (1) input Real multiSensor_Tpm5.inlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(145|145)      [ALGB] (1) Real multiSensor_Tpm6.T
(146|146)      [ALGB] (1) Real flexVolume.medium.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(147|147)      [ALGB] (1) input Real multiSensor_Tpm6.inlet.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(148|148)      [ALGB] (1) Real multiSensor_Tpm7.T
(149|149)      [ALGB] (1) input Real multiSensor_Tpm7.inlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(150|150)      [ALGB] (1) input Real flowResistance1.inlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(151|151)      [ALGB] (1) Real prescribedHeatFlow.Q_flow
(152|152)      [ALGB] (1) protected Real thermalConvectionPipe.p_out (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(153|153)      [ALGB] (1) input Real centrifugalPump1.inlet.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(154|154)      [ALGB] (1) flow Real thermalConvectionPipe.heatPort.Q_flow
(155|155)      [ALGB] (1) protected Real flowResistance1.p_out (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(156|156)      [ALGB] (1) Real inertia.a
(157|157)      [ALGB] (1) protected Real flexVolume.r_out
(158|158)      [ALGB] (1) protected Real centrifugalPump1.h_out (min = -1e10, max = 1e10, nominal = 1e6)
(159|159)      [ALGB] (1) protected Real flexVolume.h_out = if noEvent((-(-heatExchanger.m_flow_B)) >= 0.0) then ThermofluidStream.Processes.Tests.CentrifugalPump.flexVolume.Medium.specificEnthalpy(flexVolume.state_out) else 4184.0 * ((-273.15) + flexVolume.T_heatPort) (min = -1e10, max = 1e10, nominal = 1e6)
(160|160)      [ALGB] (1) Real heatExchanger.summary.Tin_A (start = 288.15, min = 0.0, nominal = 300.0)
(161|161)      [ALGB] (1) Real heatExchanger.summary.dT_B
(162|162)      [ALGB] (1) input Real centrifugalPump1.inlet.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(163|163)      [ALGB] (1) protected Real heatExchanger.C_r
(164|164)      [ALGB] (1) output Real flexVolume.outlet.state.T = flexVolume.state_out.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(165|165)      [ALGB] (1) protected Real thermalConvectionPipe.dh (min = -1e10, max = 1e10, nominal = 1e6)
(166|166)      [ALGB] (1) Real heatExchanger.summary.Q_flow_B
(167|167)      [ALGB] (1) protected Real thermalConvectionPipe.A_cross = 3.141592653589793 * thermalConvectionPipe.r ^ 2.0
(168|168)      [ALGB] (1) Real multiSensor_Tpm1.p
(169|169)      [ALGB] (1) Real centrifugalPump1.w (start = centrifugalPump1.w_ref)
(170|170)      [ALGB] (1) Real multiSensor_Tpm2.p
(171|171)      [ALGB] (1) Real multiSensor_Tpm3.p
(172|172)      [ALGB] (1) protected Real thermalConvectionPipe.V = thermalConvectionPipe.A_cross * thermalConvectionPipe.l
(173|173)      [ALGB] (1) Real multiSensor_Tpm4.p
(174|174)      [ALGB] (1) Real multiSensor_Tpm5.p
(175|175)      [ALGB] (1) protected Real heatExchanger.q_max
(176|176)      [ALGB] (1) Real multiSensor_Tpm6.p
(177|177)      [ALGB] (1) Real multiSensor_Tpm7.p
(178|178)      [ALGB] (1) output Real flexVolume.outlet.state.p = flexVolume.state_out.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(179|179)      [ALGB] (1) Real sink.inlet.r
(180|180)      [ALGB] (1) protected Real flexVolume.density_derp_h
(181|181)      [ALGB] (1) Real centrifugalPump1.head (min = 0.0)
(182|182)      [ALGB] (1) Real[1] combiTimeTable.y
(183|183)      [ALGB] (1) input Real multiSensor_Tpm7.inlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(184|184)      [ALGB] (1) input Real multiSensor_Tpm6.inlet.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(185|185)      [ALGB] (1) input Real flowResistance.inlet.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(186|186)      [ALGB] (1) Real flexVolume.medium.p_bar = Modelica.Units.Conversions.to_bar(99999.99999999999 * flexVolume.medium.p_bar) (min = 0.0)
(187|187)      [ALGB] (1) input Real multiSensor_Tpm5.inlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0)
(188|188)      [ALGB] (1) Real heatExchanger.q_flow
(189|189)      [ALGB] (1) input Real multiSensor_Tpm4.inlet.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(190|190)      [ALGB] (1) Real centrifugalPump1.P
(191|191)      [ALGB] (1) input Real multiSensor_Tpm3.inlet.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(192|192)      [ALGB] (1) output Real heatExchanger.outletA.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(193|193)      [ALGB] (1) input Real multiSensor_Tpm2.inlet.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(194|194)      [ALGB] (1) output Real heatExchanger.outletB.state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(195|195)      [ALGB] (1) input Real multiSensor_Tpm1.inlet.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(196|196)      [ALGB] (1) protected Real sink.p = ThermofluidStream.Processes.Tests.CentrifugalPump.sink.Medium.pressure(sink.inlet.state) (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6)
(197|197)      [ALGB] (1) Real heatExchanger.dh_B (min = -1e10, max = 1e10, nominal = 1e6)
(198|198)      [ALGB] (1) Real heatExchanger.dh_A (start = 298609.6803431054, min = -1e10, max = 1e10, nominal = 1e5)
(199|199)      [ALGB] (1) Real thermalConvectionPipe.outlet.r
(200|200)      [ALGB] (1) protected Real flexVolume.r_in
(201|201)      [ALGB] (1) protected Real flexVolume.p_in = ThermofluidStream.Processes.Tests.CentrifugalPump.flexVolume.Medium.pressure(flexVolume.state_in) (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(202|202)      [ALGB] (1) protected Real flexVolume.h_in = if noEvent(heatExchanger.m_flow_B >= 0.0) then ThermofluidStream.Processes.Tests.CentrifugalPump.flexVolume.Medium.specificEnthalpy(flexVolume.state_in) else 4184.0 * ((-273.15) + flexVolume.T_heatPort) (min = -1e10, max = 1e10, nominal = 1e6)
(203|203)      [ALGB] (1) Real centrifugalPump1.dp (fixed = false, start = 0.0)
(204|204)      [ALGB] (1) protected Real flexVolume.state_in.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(205|205)      [ALGB] (1) protected Real flowResistance.p_out (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(206|206)      [ALGB] (1) protected Real heatExchanger.q_flowB
(207|207)      [ALGB] (1) protected Real heatExchanger.q_flowA
(208|208)      [ALGB] (1) Real heatExchanger.summary.hout_A
(209|209)      [ALGB] (1) protected Real sink.r
(210|210)      [ALGB] (1) Real thermalConvectionPipe.center_state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(211|211)      [ALGB] (1) Real thermalConvectionPipe.center_state.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5)
(212|212)      [ALGB] (1) Real flexVolume.medium.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(213|213)      [ALGB] (1) output Real thermalConvectionPipe.outlet.state.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(214|214)      [DER-] (1) Real $DER.heatExchanger.m_flow_A
(215|215)      [ALGB] (1) input Real flexVolume.inlet.state.T = flexVolume.state_in.T (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0)
(216|216)      [ALGB] (1) protected Real centrifugalPump1.w_n = centrifugalPump1.w / centrifugalPump1.w_ref (start = 1.0)
(217|217)      [ALGB] (1) Real heatExchanger.summary.efficiency
(218|218)      [ALGB] (1) protected Real thermalConvectionPipe.M = thermalConvectionPipe.V * 995.586 (min = 0.0)
(219|219)      [ALGB] (1) protected Real heatExchanger.cpA_in = ThermofluidStream.Processes.Tests.CentrifugalPump.heatExchanger.MediumA.specificHeatCapacityCp(heatExchanger.inletA.state) (start = 1000.0, min = 0.0, max = 1e7, nominal = 1000.0)
(220|220)      [ALGB] (1) Real heatExchanger.summary.dh_A
(221|221)      [ALGB] (1) Real flowResistance1.dr_corr
(222|222)      [ALGB] (1) protected Real thermalConvectionPipe.h_avg
(223|223)      [ALGB] (1) protected Real thermalConvectionPipe.h_out (min = -1e10, max = 1e10, nominal = 1e6)
(224|224)      [ALGB] (1) Real tau_sine.y


System Equations (212/222)
****************************
(1|1)          [SCAL] (1) heatExchanger.dh_A = if noEvent(heatExchanger.C_A < heatExchanger.C_B) then if $SEV_0 then 0.0 else heatExchanger.cp_A * heatExchanger.Delta_T_max * heatExchanger.effectiveness else (heatExchanger.q_flowA * heatExchanger.m_flow_A) / (heatExchanger.m_flow_A ^ 2.0 + (heatExchanger.m_flow_reg / 10.0) ^ 2.0) ($RES_SIM_206)
(2|2)          [SCAL] (1) multiSensor_Tpm5.p = multiSensor_Tpm5.inlet.state.p ($RES_SIM_83)
(3|3)          [SCAL] (1) multiSensor_Tpm5.outlet.state.T = heatExchanger.inletA.state.T ($RES_SIM_282)
(4|4)          [SCAL] (1) multiSensor_Tpm5.T = (-273.15) + multiSensor_Tpm5.inlet.state.T ($RES_SIM_84)
(5|5)          [SCAL] (1) multiSensor_Tpm1.p = multiSensor_Tpm1.inlet.state.p ($RES_SIM_124)
(6|6)          [SCAL] (1) multiSensor_Tpm5.outlet.state.p = heatExchanger.inletA.state.p ($RES_SIM_283)
(7|7)          [RECD] (2) multiSensor_Tpm5.outlet.state = multiSensor_Tpm5.inlet.state ($RES_SIM_85)
(8|9)          [SCAL] (1) multiSensor_Tpm1.T = (-273.15) + multiSensor_Tpm1.inlet.state.T ($RES_SIM_125)
(9|10)         [RECD] (2) multiSensor_Tpm1.outlet.state = multiSensor_Tpm1.inlet.state ($RES_SIM_126)
(10|12)        [SCAL] (1) source.outlet.state.T = multiSensor_Tpm5.inlet.state.T ($RES_SIM_285)
(11|13)        [SCAL] (1) source.outlet.state.p = multiSensor_Tpm5.inlet.state.p ($RES_SIM_286)
(12|14)        [SCAL] (1) source.L * (-$DER.heatExchanger.m_flow_A) = source.outlet.r ($RES_SIM_89)
(13|15)        [SCAL] (1) flowResistance.inlet.state.T = multiSensor_Tpm4.outlet.state.T ($RES_SIM_288)
(14|16)        [SCAL] (1) flowResistance.inlet.state.p = multiSensor_Tpm4.outlet.state.p ($RES_SIM_289)
(15|17)        [SCAL] (1) flowResistance.rho_in = max(flowResistance.rho_min, 995.586) ($RES_BND_340)
(16|18)        [SCAL] (1) sink.p = sink.inlet.state.p ($RES_BND_342)
(17|19)        [SCAL] (1) centrifugalPump1.p_in = centrifugalPump1.inlet.state.p ($RES_BND_344)
(18|20)        [SCAL] (1) centrifugalPump1.h_in = 4184.0 * ((-273.15) + centrifugalPump1.inlet.state.T) ($RES_BND_345)
(19|21)        [SCAL] (1) heatExchanger.q_flow = heatExchanger.effectiveness * heatExchanger.q_max ($RES_SIM_211)
(20|22)        [SCAL] (1) inertia.J * inertia.a = tau_sine.y - centrifugalPump1.tau ($RES_SIM_13)
(21|23)        [SCAL] (1) heatExchanger.q_max = heatExchanger.Delta_T_max * heatExchanger.C_min ($RES_SIM_212)
(22|24)        [SCAL] (1) inertia.a = $DER.inertia.w ($RES_SIM_14)
(23|25)        [SCAL] (1) centrifugalPump1.pr = centrifugalPump1.p_out / centrifugalPump1.p_in ($RES_BND_348)
(24|26)        [SCAL] (1) heatExchanger.Delta_T_max = heatExchanger.T_in_MediumA - heatExchanger.T_in_MediumB ($RES_SIM_213)
(25|27)        [SCAL] (1) inertia.w = $DER.centrifugalPump1.phi ($RES_SIM_15)
(26|28)        [SCAL] (1) heatExchanger.NTU = (heatExchanger.A * heatExchanger.k_NTU) / max(heatExchanger.C_min, 0.001) ($RES_SIM_214)
(27|29)        [SCAL] (1) flowResistance.dr_corr = (flowResistance.p_in + flowResistance.dp) - flowResistance.p_out ($RES_SIM_130)
(28|30)        [SCAL] (1) heatExchanger.C_r = heatExchanger.C_min / max(heatExchanger.C_max, 0.001) ($RES_SIM_215)
(29|31)        [SCAL] (1) flowResistance.p_out = max(flowResistance.p_min, flowResistance.p_in + flowResistance.dp) ($RES_SIM_131)
(30|32)        [SCAL] (1) heatExchanger.C_min = if noEvent(heatExchanger.C_A > heatExchanger.C_B) then heatExchanger.C_B else heatExchanger.C_A ($RES_SIM_216)
(31|33)        [SCAL] (1) tau_sine.y = tau_sine.offset + (if $TEV_1 then 0.0 else tau_sine.amplitude * sin(tau_sine.phase + 6.283185307179586 * (time - tau_sine.startTime) * tau_sine.f)) ($RES_SIM_18)
(32|34)        [SCAL] (1) multiSensor_Tpm6.inlet.r = (flowResistance.dr_corr + thermalConvectionPipe.outlet.r) - $DER.heatExchanger.m_flow_B * flowResistance.L ($RES_SIM_132)
(33|35)        [SCAL] (1) thermalConvectionPipe.outlet.state.T = multiSensor_Tpm4.inlet.state.T ($RES_SIM_291)
(34|36)        [SCAL] (1) thermalConvectionPipe.outlet.state.p = multiSensor_Tpm4.inlet.state.p ($RES_SIM_292)
(35|37)        [SCAL] (1) heatExchanger.C_max = if noEvent(heatExchanger.C_A > heatExchanger.C_B) then heatExchanger.C_A else heatExchanger.C_B ($RES_SIM_219)
(36|38)        [SCAL] (1) heatExchanger.outletA.state.p = heatExchanger.p_A ($RES_SIM_378)
(37|39)        [SCAL] (1) multiSensor_Tpm3.outlet.state.T = thermalConvectionPipe.inlet.state.T ($RES_SIM_294)
(38|40)        [SCAL] (1) heatExchanger.outletA.state.T = Modelica.Math.Nonlinear.solveOneNonlinearEquation(function ThermofluidStream.Processes.Tests.CentrifugalPump.heatExchanger.MediumA.T_h.f_nonlinear(data = ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"Air\", BOX(0.0289651159), BOX(-4333.833858403446), BOX(298609.6803431054), BOX(1000.0), BOX({10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}), BOX({-176.796731, -3.921504225}), BOX({241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}), BOX({6462.26319, -8.147411905}), BOX(287.0512249529787)), h = BOX(heatExchanger.h_out_A)), 200.0, 6000.0, 2.220446049250313e-14) ($RES_SIM_379)
(39|41)        [SCAL] (1) multiSensor_Tpm3.outlet.state.p = thermalConvectionPipe.inlet.state.p ($RES_SIM_295)
(40|42)        [SCAL] (1) multiSensor_Tpm4.p = multiSensor_Tpm4.inlet.state.p ($RES_SIM_97)
(41|43)        [SCAL] (1) multiSensor_Tpm4.T = (-273.15) + multiSensor_Tpm4.inlet.state.T ($RES_SIM_98)
(42|44)        [SCAL] (1) flexVolume.outlet.state.T = multiSensor_Tpm2.inlet.state.T ($RES_SIM_297)
(43|45)        [RECD] (2) multiSensor_Tpm4.outlet.state = multiSensor_Tpm4.inlet.state ($RES_SIM_99)
(44|47)        [SCAL] (1) thermalConvectionPipe.p_out = thermalConvectionPipe.p_in ($RES_SIM_139)
(45|48)        [SCAL] (1) flexVolume.outlet.state.p = multiSensor_Tpm2.inlet.state.p ($RES_SIM_298)
(46|49)        [SCAL] (1) multiSensor_Tpm1.outlet.state.T = flexVolume.inlet.state.T ($RES_SIM_300)
(47|50)        [SCAL] (1) centrifugalPump1.V_flow = heatExchanger.m_flow_B / 995.586 ($RES_BND_351)
(48|51)        [SCAL] (1) multiSensor_Tpm1.outlet.state.p = flexVolume.inlet.state.p ($RES_SIM_301)
(49|52)        [SCAL] (1) centrifugalPump1.w_n = centrifugalPump1.w / centrifugalPump1.w_ref ($RES_BND_352)
(50|53)        [SCAL] (1) centrifugalPump1.V_n = centrifugalPump1.V_flow / centrifugalPump1.V_flow_ref ($RES_BND_353)
(51|54)        [SCAL] (1) multiSensor_Tpm1.inlet.state.T = heatExchanger.outletB.state.T ($RES_SIM_303)
(52|55)        [SCAL] (1) centrifugalPump1.h_n = centrifugalPump1.head / centrifugalPump1.head_ref ($RES_BND_354)
(53|56)        [SCAL] (1) multiSensor_Tpm1.inlet.state.p = heatExchanger.outletB.state.p ($RES_SIM_304)
(54|57)        [SCAL] (1) centrifugalPump1.tau_n = centrifugalPump1.tau / centrifugalPump1.tau_ref ($RES_BND_355)
(55|58)        [SCAL] (1) centrifugalPump1.rho_n = 995.586 / centrifugalPump1.rho_ref ($RES_BND_356)
(56|59)        [SCAL] (1) heatExchanger.h_in_B = 4184.0 * ((-273.15) + heatExchanger.inletB.state.T) ($RES_SIM_222)
(57|60)        [SCAL] (1) heatExchanger.outletB.state.p = heatExchanger.p_B ($RES_SIM_380)
(58|61)        [SCAL] (1) heatExchanger.h_in_A = ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"Air\", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), heatExchanger.inletA.state.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_SIM_223)
(59|62)        [SCAL] (1) flowResistance1.p_in = flowResistance1.inlet.state.p ($RES_BND_359)
(60|63)        [SCAL] (1) heatExchanger.outletB.state.T = 273.15 + 2.390057361376673e-4 * heatExchanger.h_out_B ($RES_SIM_381)
(61|64)        [SCAL] (1) heatExchanger.T_in_MediumB = heatExchanger.inletB.state.T ($RES_SIM_224)
(62|65)        [SCAL] (1) heatExchanger.T_in_MediumA = heatExchanger.inletA.state.T ($RES_SIM_225)
(63|66)        [SCAL] (1) thermalConvectionPipe.outlet.r = multiSensor_Tpm3.inlet.r - $DER.heatExchanger.m_flow_B * thermalConvectionPipe.L ($RES_SIM_140)
(64|67)        [SCAL] (1) thermalConvectionPipe.outlet.state.p = thermalConvectionPipe.p_out ($RES_SIM_383)
(65|68)        [SCAL] (1) heatExchanger.C_B = (2.220446049250313e-16 + $FUN_3) * heatExchanger.cp_B ($RES_SIM_226)
(66|69)        [SCAL] (1) flowResistance1.dr_corr = flowResistance1.p_in - (flowResistance1.p_out + 1e5 * heatExchanger.m_flow_A) ($RES_SIM_28)
(67|70)        [SCAL] (1) thermalConvectionPipe.outlet.state.T = 273.15 + 2.390057361376673e-4 * thermalConvectionPipe.h_out ($RES_SIM_384)
(68|71)        [SCAL] (1) heatExchanger.C_A = (2.220446049250313e-16 + $FUN_2) * heatExchanger.cp_A ($RES_SIM_227)
(69|72)        [SCAL] (1) thermalConvectionPipe.h_out = thermalConvectionPipe.h_in + thermalConvectionPipe.dh ($RES_SIM_142)
(70|73)        [SCAL] (1) flowResistance1.p_out = max(flowResistance1.p_min, flowResistance1.p_in - 1e5 * heatExchanger.m_flow_A) ($RES_SIM_29)
(71|74)        [SCAL] (1) flowResistance.outlet.state.p = flowResistance.p_out ($RES_SIM_385)
(72|75)        [SCAL] (1) heatExchanger.cp_B = 4184.0 ($RES_SIM_228)
(73|76)        [SCAL] (1) flowResistance.outlet.state.T = 273.15 + 2.390057361376673e-4 * flowResistance.h_out ($RES_SIM_386)
(74|77)        [SCAL] (1) heatExchanger.cp_A = 0.5 * (heatExchanger.cpA_in + heatExchanger.cpA_out) ($RES_SIM_229)
(75|78)        [SCAL] (1) thermalConvectionPipe.dh = (thermalConvectionPipe.heatPort.Q_flow * heatExchanger.m_flow_B) / (heatExchanger.m_flow_B ^ 2.0 + (thermalConvectionPipe.m_flow_reg / 10.0) ^ 2.0) ($RES_SIM_144)
(76|79)        [SCAL] (1) source.outlet.state.p = source.p0_par ($RES_SIM_387)
(77|80)        [SCAL] (1) thermalConvectionPipe.heatPort.Q_flow = thermalConvectionPipe.A_cond * thermalConvectionPipe.h_avg * (heatCapacitor.T - thermalConvectionPipe.T) ($RES_SIM_145)
(78|81)        [SCAL] (1) source.outlet.state.T = source.T0_par ($RES_SIM_388)
(79|82)        [SCAL] (1) centrifugalPump1.outlet.state.p = centrifugalPump1.p_out ($RES_SIM_389)
(80|83)        [SCAL] (1) thermalConvectionPipe.h_avg = (0.299 * thermalConvectionPipe.Nu_turb) / thermalConvectionPipe.r ($RES_SIM_147)
(81|84)        [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)) ($RES_SIM_148)
(82|85)        [SCAL] (1) thermalConvectionPipe.Re_D = max(1.991172e6 * thermalConvectionPipe.r * thermalConvectionPipe.v_m, 1.0) ($RES_SIM_149)
(83|86)        [SCAL] (1) $FUN_9 = sqrt($FUN_8) ($RES_AUX_366)
(84|87)        [SCAL] (1) $FUN_8 = abs((2.0 * flexVolume.L) / (flexVolume.V * max(flexVolume.density_derp_h, 1e-10))) ($RES_AUX_367)
(85|88)        [SCAL] (1) $FUN_7 = Modelica.Blocks.Tables.Internal.getTimeTableValueNoDer2(combiTimeTable.tableID, 1, time, combiTimeTable.nextTimeEventScaled, $TEV_8) ($RES_AUX_368)
(86|89)        [SCAL] (1) $FUN_6 = abs(centrifugalPump1.V_n) ($RES_AUX_369)
(87|90)        [SCAL] (1) flowResistance1.h_out = 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), flowResistance1.inlet.state.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_BND_360)
(88|91)        [SCAL] (1) flowResistance1.rho_in = max(flowResistance1.rho_min, (0.0034836987724536205 * flowResistance1.inlet.state.p) / flowResistance1.inlet.state.T) ($RES_BND_361)
(89|92)        [SCAL] (1) flowResistance1.mu_in = 1e-6 * Modelica.Math.Polynomials.evaluateWithRange({9.739110288630587e-15, -3.1353724870333906e-11, 4.3004876595642225e-8, -3.822801629175824e-5, 0.05042787436718076, 17.23926013924253}, -149.99999999999997, 1000.0000000000001, (-273.15) + flowResistance1.inlet.state.T) ($RES_BND_362)
(90|93)        [RECD] (2) flexVolume.inlet.state = flexVolume.state_in ($RES_BND_363)
(91|95)        [SCAL] (1) sink.inlet.r = (flowResistance1.dr_corr + heatExchanger.outletA.r) - $DER.heatExchanger.m_flow_A * flowResistance1.L ($RES_SIM_30)
(92|96)        [RECD] (2) flexVolume.outlet.state = flexVolume.state_out ($RES_BND_364)
(93|98)        [SCAL] (1) multiSensor_Tpm6.inlet.r - flexVolume.r_in = $DER.heatExchanger.m_flow_B * heatExchanger.L ($RES_SIM_230)
(94|99)        [SCAL] (1) source.outlet.r - heatExchanger.outletA.r = $DER.heatExchanger.m_flow_A * heatExchanger.L ($RES_SIM_231)
(95|100)       [SCAL] (1) centrifugalPump1.outlet.state.T = 273.15 + 2.390057361376673e-4 * centrifugalPump1.h_out ($RES_SIM_390)
(96|101)       [SCAL] (1) combiTimeTable.y[1] = combiTimeTable.p_offset[1] + $FUN_7 ($RES_SIM_35)
(97|102)       [SCAL] (1) flowResistance1.outlet.state.p = flowResistance1.p_out ($RES_SIM_391)
(98|103)       [SCAL] (1) heatExchanger.effectiveness = if noEvent(heatExchanger.C_r < 1.0) then (1.0 - $FUN_1) / (1.0 - heatExchanger.C_r * $FUN_1) else heatExchanger.NTU / (1.0 + heatExchanger.NTU) ($RES_SIM_234)
(99|104)       [WHEN] (1) ($RES_SIM_36)
(99|104)       [----] when {$SEV_1, initial()} then
(99|104)       [----]   combiTimeTable.nextTimeEvent := if combiTimeTable.nextTimeEventScaled < 1e60 then combiTimeTable.nextTimeEventScaled else 1e60
(99|104)       [----] end when;
(100|105)      [SCAL] (1) flowResistance1.outlet.state.T = Modelica.Math.Nonlinear.solveOneNonlinearEquation(function ThermofluidStream.Processes.Tests.CentrifugalPump.flowResistance1.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(flowResistance1.h_out)), 200.0, 6000.0, 2.220446049250313e-14) ($RES_SIM_392)
(101|106)      [SCAL] (1) thermalConvectionPipe.v_m = (0.0010044335697769957 * heatExchanger.m_flow_B) / thermalConvectionPipe.A_cross ($RES_SIM_150)
(102|107)      [WHEN] (1) ($RES_SIM_37)
(102|107)      [----] when {$SEV_1, initial()} then
(102|107)      [----]   combiTimeTable.nextTimeEventScaled := Modelica.Blocks.Tables.Internal.getNextTimeEvent(combiTimeTable.tableID, time)
(102|107)      [----] end when;
(103|108)      [SCAL] (1) thermalConvectionPipe.center_state.p = thermalConvectionPipe.p_in ($RES_SIM_393)
(104|109)      [SCAL] (1) thermalConvectionPipe.center_state.T = 273.15 + 2.390057361376673e-4 * (0.5 * thermalConvectionPipe.dh + thermalConvectionPipe.h_in) ($RES_SIM_394)
(105|110)      [SCAL] (1) flexVolume.Q_flow = 0.0 ($RES_SIM_152)
(106|111)      [SCAL] (1) $DER.flexVolume.U_med = (flexVolume.h_in * heatExchanger.m_flow_B + flexVolume.Q_flow) - flexVolume.h_out * heatExchanger.m_flow_B ($RES_SIM_153)
(107|112)      [SCAL] (1) $DER.flexVolume.M = 0.0 ($RES_SIM_154)
(108|113)      [SCAL] (1) flexVolume.r + flexVolume.p_in = 99999.99999999999 * flexVolume.medium.p_bar ($RES_SIM_155)
(109|114)      [SCAL] (1) $FUN_5 = abs(centrifugalPump1.w_n) ($RES_AUX_370)
(110|115)      [SCAL] (1) (-$DER.heatExchanger.m_flow_B) * flexVolume.L = flexVolume.r_out - flexVolume.r_damping ($RES_SIM_156)
(111|116)      [SCAL] (1) -flowResistance.dp = ThermofluidStream.Processes.Tests.CentrifugalPump.flowResistance.pLoss(heatExchanger.m_flow_B, flowResistance.rho_in, 0.001, 0.5 * flowResistance.D_h, flowResistance.l, 1e-7, ThermofluidStream.Processes.Internal.Material.other) ($RES_AUX_371)
(112|117)      [SCAL] (1) $TEV_1 = time < tau_sine.startTime ($RES_EVT_402)
(113|118)      [SCAL] (1) $DER.heatExchanger.m_flow_B * flexVolume.L = flexVolume.r_in - (flexVolume.r_damping + flexVolume.r) ($RES_SIM_157)
(114|119)      [SCAL] (1) $FUN_3 = abs(heatExchanger.m_flow_B) ($RES_AUX_372)
(115|120)      [SCAL] (1) $FUN_2 = abs(heatExchanger.m_flow_A) ($RES_AUX_373)
(116|121)      [SCAL] (1) $FUN_1 = exp(-heatExchanger.NTU * (1.0 - heatExchanger.C_r)) ($RES_AUX_374)
(117|122)      [SCAL] (1) $TEV_8 = $PRE.combiTimeTable.nextTimeEventScaled ($RES_EVT_409)
(118|123)      [SCAL] (1) multiSensor_Tpm7.p = multiSensor_Tpm7.inlet.state.p ($RES_SIM_44)
(119|124)      [SCAL] (1) multiSensor_Tpm7.T = (-273.15) + multiSensor_Tpm7.inlet.state.T ($RES_SIM_45)
(120|125)      [RECD] (2) multiSensor_Tpm7.outlet.state = multiSensor_Tpm7.inlet.state ($RES_SIM_46)
(121|127)      [RECD] (2) flexVolume.state_out = flexVolume.medium.state ($RES_SIM_161)
(122|129)      [SCAL] (1) 99999.99999999999 * flexVolume.medium.p_bar = flexVolume.p_ref + flexVolume.K * ((-1.0) + flexVolume.V / flexVolume.V_ref) ($RES_SIM_163)
(123|130)      [SCAL] (1) heatCapacitor.port.Q_flow + prescribedHeatFlow.port.Q_flow + thermalConvectionPipe.heatPort.Q_flow = 0.0 ($RES_SIM_249)
(124|131)      [SCAL] (1) flexVolume.density_derp_h = (995.586 * flexVolume.V_ref) / (flexVolume.K * flexVolume.V) ($RES_SIM_164)
(125|132)      [SCAL] (1) $SEV_0 = noEvent(heatExchanger.m_flow_A < heatExchanger.m_flow_reg) and noEvent(heatExchanger.m_flow_B < heatExchanger.m_flow_reg) ($RES_EVT_410)
(126|133)      [SCAL] (1) $SEV_1 = time >= $PRE.combiTimeTable.nextTimeEvent ($RES_EVT_411)
(127|134)      [SCAL] (1) $SEV_2 = heatExchanger.outletA.state.T < 1000.0 ($RES_EVT_412)
(128|135)      [SCAL] (1) $SEV_3 = heatExchanger.inletA.state.T < 1000.0 ($RES_EVT_413)
(129|136)      [SCAL] (1) flexVolume.medium.state.p = 99999.99999999999 * flexVolume.medium.p_bar ($RES_SIM_168)
(130|137)      [SCAL] (1) $SEV_4 = flexVolume.T_heatPort >= 272.15 and flexVolume.T_heatPort <= 403.15 ($RES_EVT_414)
(131|138)      [SCAL] (1) flexVolume.medium.state.T = flexVolume.T_heatPort ($RES_SIM_169)
(132|139)      [SCAL] (1) $SEV_6 = 99999.99999999999 * flexVolume.medium.p_bar >= 0.0 ($RES_EVT_416)
(133|140)      [SCAL] (1) $SEV_7 = heatExchanger.m_flow_B > flexVolume.m_flow_assert ($RES_EVT_417)
(134|141)      [SCAL] (1) $SEV_8 = flexVolume.M > 0.0 ($RES_EVT_418)
(135|142)      [SCAL] (1) heatExchanger.p_A = heatExchanger.inletA.state.p ($RES_BND_306)
(136|143)      [SCAL] (1) heatExchanger.p_B = heatExchanger.inletB.state.p ($RES_BND_307)
(137|144)      [SCAL] (1) multiSensor_Tpm6.p = multiSensor_Tpm6.inlet.state.p ($RES_SIM_53)
(138|145)      [SCAL] (1) multiSensor_Tpm6.T = (-273.15) + multiSensor_Tpm6.inlet.state.T ($RES_SIM_54)
(139|146)      [RECD] (2) multiSensor_Tpm6.outlet.state = multiSensor_Tpm6.inlet.state ($RES_SIM_55)
(140|148)      [SCAL] (1) centrifugalPump1.dr_corr = (centrifugalPump1.p_in + centrifugalPump1.dp) - centrifugalPump1.p_out ($RES_SIM_59)
(141|149)      [SCAL] (1) centrifugalPump1.inlet.state.T = multiSensor_Tpm2.outlet.state.T ($RES_SIM_258)
(142|150)      [SCAL] (1) centrifugalPump1.inlet.state.p = multiSensor_Tpm2.outlet.state.p ($RES_SIM_259)
(143|151)      [SCAL] (1) heatExchanger.summary.efficiency = heatExchanger.effectiveness ($RES_SIM_176)
(144|152)      [SCAL] (1) heatExchanger.summary.Q_flow_B = heatExchanger.q_flowB ($RES_SIM_177)
(145|153)      [SCAL] (1) heatExchanger.summary.Q_flow_A = heatExchanger.q_flowA ($RES_SIM_178)
(146|154)      [SCAL] (1) heatExchanger.summary.dh_B = heatExchanger.summary.hout_B - heatExchanger.summary.hin_B ($RES_SIM_179)
(147|155)      [SCAL] (1) heatExchanger.cpA_in = smooth(0, if $SEV_3 then 287.0512249529787 * (10099.5016 + heatExchanger.inletA.state.T * ((-196.827561) + heatExchanger.inletA.state.T * (5.00915511 + heatExchanger.inletA.state.T * ((-0.00576101373) + heatExchanger.inletA.state.T * (1.06685993e-5 + heatExchanger.inletA.state.T * ((-7.94029797e-9) + 2.18523191e-12 * heatExchanger.inletA.state.T)))))) * (1/(heatExchanger.inletA.state.T * heatExchanger.inletA.state.T)) else 287.0512249529787 * (241521.443 + heatExchanger.inletA.state.T * ((-1257.8746) + heatExchanger.inletA.state.T * (5.14455867 + heatExchanger.inletA.state.T * ((-2.13854179e-4) + heatExchanger.inletA.state.T * (7.06522784e-8 + heatExchanger.inletA.state.T * ((-1.07148349e-11) + 6.57780015e-16 * heatExchanger.inletA.state.T)))))) * (1/(heatExchanger.inletA.state.T * heatExchanger.inletA.state.T))) ($RES_BND_310)
(148|156)      [SCAL] (1) heatExchanger.cpA_out = smooth(0, if $SEV_2 then 287.0512249529787 * (10099.5016 + heatExchanger.outletA.state.T * ((-196.827561) + heatExchanger.outletA.state.T * (5.00915511 + heatExchanger.outletA.state.T * ((-0.00576101373) + heatExchanger.outletA.state.T * (1.06685993e-5 + heatExchanger.outletA.state.T * ((-7.94029797e-9) + 2.18523191e-12 * heatExchanger.outletA.state.T)))))) * (1/(heatExchanger.outletA.state.T * heatExchanger.outletA.state.T)) else 287.0512249529787 * (241521.443 + heatExchanger.outletA.state.T * ((-1257.8746) + heatExchanger.outletA.state.T * (5.14455867 + heatExchanger.outletA.state.T * ((-2.13854179e-4) + heatExchanger.outletA.state.T * (7.06522784e-8 + heatExchanger.outletA.state.T * ((-1.07148349e-11) + 6.57780015e-16 * heatExchanger.outletA.state.T)))))) * (1/(heatExchanger.outletA.state.T * heatExchanger.outletA.state.T))) ($RES_BND_311)
(149|157)      [SCAL] (1) centrifugalPump1.p_out = max(centrifugalPump1.p_min, centrifugalPump1.p_in + centrifugalPump1.dp) ($RES_SIM_60)
(150|158)      [SCAL] (1) multiSensor_Tpm3.inlet.r = (centrifugalPump1.dr_corr + flexVolume.r_out) - $DER.heatExchanger.m_flow_B * centrifugalPump1.L ($RES_SIM_61)
(151|159)      [SCAL] (1) multiSensor_Tpm3.inlet.state.T = centrifugalPump1.outlet.state.T ($RES_SIM_261)
(152|160)      [SCAL] (1) centrifugalPump1.w_t = centrifugalPump1.P / max(heatExchanger.m_flow_B, centrifugalPump1.m_flow_reg) ($RES_SIM_63)
(153|161)      [SCAL] (1) multiSensor_Tpm3.inlet.state.p = centrifugalPump1.outlet.state.p ($RES_SIM_262)
(154|162)      [SCAL] (1) centrifugalPump1.eta_is = if noEvent(centrifugalPump1.P >= centrifugalPump1.P_reg) then (centrifugalPump1.V_flow * centrifugalPump1.dp) / centrifugalPump1.P else 0.0 ($RES_SIM_64)
(155|163)      [SCAL] (1) centrifugalPump1.h_out = centrifugalPump1.h_in + centrifugalPump1.w_t ($RES_SIM_65)
(156|164)      [SCAL] (1) sink.inlet.state.T = flowResistance1.outlet.state.T ($RES_SIM_264)
(157|165)      [SCAL] (1) centrifugalPump1.P = centrifugalPump1.tau * centrifugalPump1.w ($RES_SIM_66)
(158|166)      [SCAL] (1) multiSensor_Tpm3.p = multiSensor_Tpm3.inlet.state.p ($RES_SIM_106)
(159|167)      [SCAL] (1) sink.inlet.state.p = flowResistance1.outlet.state.p ($RES_SIM_265)
(160|168)      [SCAL] (1) centrifugalPump1.dp = 9763.363446899999 * centrifugalPump1.head ($RES_SIM_67)
(161|169)      [SCAL] (1) heatExchanger.summary.dh_A = heatExchanger.summary.hout_A - heatExchanger.summary.hin_A ($RES_SIM_180)
(162|170)      [SCAL] (1) multiSensor_Tpm3.T = (-273.15) + multiSensor_Tpm3.inlet.state.T ($RES_SIM_107)
(163|171)      [SCAL] (1) centrifugalPump1.tau_n = smooth(0, if noEvent(centrifugalPump1.V_n > 0.0) then centrifugalPump1.rho_n * ($FUN_5 * centrifugalPump1.c_power[2] * centrifugalPump1.V_n + centrifugalPump1.c_power[1] * centrifugalPump1.w_n ^ 2.0 + centrifugalPump1.c_power[3] * centrifugalPump1.V_n ^ 2.0) else centrifugalPump1.c_power[1] * centrifugalPump1.rho_n * centrifugalPump1.w_n ^ 2.0) ($RES_SIM_68)
(164|172)      [SCAL] (1) heatExchanger.summary.dT_B = heatExchanger.summary.Tout_B - heatExchanger.summary.Tin_B ($RES_SIM_181)
(165|173)      [RECD] (2) multiSensor_Tpm3.outlet.state = multiSensor_Tpm3.inlet.state ($RES_SIM_108)
(166|175)      [SCAL] (1) multiSensor_Tpm7.outlet.state.T = flowResistance1.inlet.state.T ($RES_SIM_267)
(167|176)      [SCAL] (1) centrifugalPump1.h_n = $FUN_5 * centrifugalPump1.c_head[2] * centrifugalPump1.V_n + centrifugalPump1.c_head[1] * centrifugalPump1.w_n ^ 2.0 + centrifugalPump1.V_n * centrifugalPump1.c_head[3] * $FUN_6 ($RES_SIM_69)
(168|177)      [SCAL] (1) heatExchanger.summary.dT_A = heatExchanger.summary.Tout_A - heatExchanger.summary.Tin_A ($RES_SIM_182)
(169|178)      [SCAL] (1) multiSensor_Tpm7.outlet.state.p = flowResistance1.inlet.state.p ($RES_SIM_268)
(170|179)      [SCAL] (1) heatExchanger.summary.hout_B = heatExchanger.h_out_B ($RES_SIM_183)
(171|180)      [SCAL] (1) heatExchanger.summary.hin_B = heatExchanger.h_in_B ($RES_SIM_184)
(172|181)      [SCAL] (1) heatExchanger.summary.hout_A = heatExchanger.h_out_A ($RES_SIM_185)
(173|182)      [SCAL] (1) heatExchanger.summary.hin_A = heatExchanger.h_in_A ($RES_SIM_186)
(174|183)      [SCAL] (1) heatExchanger.summary.Tout_A = heatExchanger.outletA.state.T ($RES_SIM_187)
(175|184)      [SCAL] (1) heatExchanger.summary.Tout_B = heatExchanger.outletB.state.T ($RES_SIM_188)
(176|185)      [SCAL] (1) heatExchanger.summary.Tin_A = heatExchanger.inletA.state.T ($RES_SIM_189)
(177|186)      [SCAL] (1) flexVolume.d = flexVolume.k_volume_damping * $FUN_9 ($RES_BND_320)
(178|187)      [SCAL] (1) flexVolume.r_damping = flexVolume.d * $DER.flexVolume.M ($RES_BND_321)
(179|188)      [SCAL] (1) flexVolume.p_in = flexVolume.state_in.p ($RES_BND_322)
(180|189)      [SCAL] (1) flexVolume.h_in = if noEvent(heatExchanger.m_flow_B >= 0.0) then 4184.0 * ((-273.15) + flexVolume.state_in.T) else 4184.0 * ((-273.15) + flexVolume.T_heatPort) ($RES_BND_323)
(181|190)      [SCAL] (1) flexVolume.h_out = if noEvent(heatExchanger.m_flow_B >= 0.0) then 4184.0 * ((-273.15) + flexVolume.state_out.T) else 4184.0 * ((-273.15) + flexVolume.T_heatPort) ($RES_BND_324)
(182|191)      [SCAL] (1) thermalConvectionPipe.p_in = thermalConvectionPipe.inlet.state.p ($RES_BND_326)
(183|192)      [SCAL] (1) thermalConvectionPipe.h_in = 4184.0 * ((-273.15) + thermalConvectionPipe.inlet.state.T) ($RES_BND_327)
(184|193)      [SCAL] (1) thermalConvectionPipe.T = thermalConvectionPipe.center_state.T ($RES_BND_328)
(185|194)      [SCAL] (1) thermalConvectionPipe.A_cond = thermalConvectionPipe.r * 6.283185307179586 * thermalConvectionPipe.l ($RES_BND_329)
(186|195)      [SCAL] (1) centrifugalPump1.w = $DER.centrifugalPump1.phi ($RES_SIM_70)
(187|196)      [SCAL] (1) prescribedHeatFlow.Q_flow = combiTimeTable.y[1] ($RES_SIM_270)
(188|197)      [SCAL] (1) prescribedHeatFlow.port.Q_flow = -prescribedHeatFlow.Q_flow * (1.0 + prescribedHeatFlow.alpha * (heatCapacitor.T - prescribedHeatFlow.T_ref)) ($RES_SIM_72)
(189|198)      [SCAL] (1) heatExchanger.outletA.state.T = multiSensor_Tpm7.inlet.state.T ($RES_SIM_271)
(190|199)      [SCAL] (1) heatCapacitor.C * $DER.heatCapacitor.T = heatCapacitor.port.Q_flow ($RES_SIM_73)
(191|200)      [SCAL] (1) heatExchanger.outletA.state.p = multiSensor_Tpm7.inlet.state.p ($RES_SIM_272)
(192|201)      [SCAL] (1) heatCapacitor.der_T = $DER.heatCapacitor.T ($RES_SIM_74)
(193|202)      [SCAL] (1) multiSensor_Tpm2.p = multiSensor_Tpm2.inlet.state.p ($RES_SIM_115)
(194|203)      [SCAL] (1) multiSensor_Tpm6.inlet.state.T = flowResistance.outlet.state.T ($RES_SIM_274)
(195|204)      [SCAL] (1) sink.r + sink.p = sink.p0_par ($RES_SIM_76)
(196|205)      [SCAL] (1) multiSensor_Tpm2.T = (-273.15) + multiSensor_Tpm2.inlet.state.T ($RES_SIM_116)
(197|206)      [SCAL] (1) multiSensor_Tpm6.inlet.state.p = flowResistance.outlet.state.p ($RES_SIM_275)
(198|207)      [SCAL] (1) $DER.heatExchanger.m_flow_A * sink.L = sink.inlet.r - sink.r ($RES_SIM_77)
(199|208)      [SCAL] (1) heatExchanger.summary.Tin_B = heatExchanger.inletB.state.T ($RES_SIM_190)
(200|209)      [RECD] (2) multiSensor_Tpm2.outlet.state = multiSensor_Tpm2.inlet.state ($RES_SIM_117)
(201|211)      [SCAL] (1) heatExchanger.inletB.state.T = multiSensor_Tpm6.outlet.state.T ($RES_SIM_277)
(202|212)      [SCAL] (1) heatExchanger.inletB.state.p = multiSensor_Tpm6.outlet.state.p ($RES_SIM_278)
(203|213)      [SCAL] (1) $DER.heatExchanger.h_out_B * heatExchanger.TC = heatExchanger.h_in_B - (heatExchanger.h_out_B + heatExchanger.dh_B) ($RES_SIM_193)
(204|214)      [SCAL] (1) $DER.heatExchanger.h_out_A * heatExchanger.TC = heatExchanger.h_in_A - (heatExchanger.h_out_A + heatExchanger.dh_A) ($RES_SIM_194)
(205|215)      [SCAL] (1) heatExchanger.q_flowB = if noEvent(heatExchanger.C_A < heatExchanger.C_B) then -heatExchanger.q_flowA else heatExchanger.m_flow_B * heatExchanger.dh_B ($RES_SIM_195)
(206|216)      [SCAL] (1) heatExchanger.q_flowA = if noEvent(heatExchanger.C_A < heatExchanger.C_B) then heatExchanger.m_flow_A * heatExchanger.dh_A else -heatExchanger.q_flowB ($RES_SIM_198)
(207|217)      [SCAL] (1) thermalConvectionPipe.A_cross = 3.141592653589793 * thermalConvectionPipe.r ^ 2.0 ($RES_BND_330)
(208|218)      [SCAL] (1) thermalConvectionPipe.V = thermalConvectionPipe.A_cross * thermalConvectionPipe.l ($RES_BND_331)
(209|219)      [SCAL] (1) thermalConvectionPipe.M = thermalConvectionPipe.V * 995.586 ($RES_BND_334)
(210|220)      [SCAL] (1) heatExchanger.dh_B = if noEvent(heatExchanger.C_A < heatExchanger.C_B) then (heatExchanger.q_flowB * heatExchanger.m_flow_B) / (heatExchanger.m_flow_B ^ 2.0 + (heatExchanger.m_flow_reg / 10.0) ^ 2.0) else if $SEV_0 then 0.0 else -heatExchanger.cp_B * heatExchanger.Delta_T_max * heatExchanger.effectiveness ($RES_SIM_201)
(211|221)      [SCAL] (1) flowResistance.p_in = flowResistance.inlet.state.p ($RES_BND_338)
(212|222)      [SCAL] (1) flowResistance.h_out = 4184.0 * ((-273.15) + flowResistance.inlet.state.T) ($RES_BND_339)


===================
  Scalar Matching
===================

variable to equation
**********************
	var 1 --> eqn 28
	var 2 --> eqn 24
	var 3 --> eqn 126
	var 4 --> eqn 80
	var 5 --> eqn 211
	var 6 --> eqn 8
	var 7 --> eqn 15
	var 8 --> eqn 111
	var 9 --> eqn 39
	var 10 --> eqn 149
	var 11 --> eqn 11
	var 12 --> eqn 116
	var 13 --> eqn 122
	var 14 --> eqn 65
	var 15 --> eqn 26
	var 16 --> eqn 183
	var 17 --> eqn 41
	var 18 --> eqn 93
	var 19 --> eqn 221
	var 20 --> eqn 40
	var 21 --> eqn 63
	var 22 --> eqn 117
	var 23 --> eqn 160
	var 24 --> eqn 112
	var 25 --> eqn 25
	var 26 --> eqn 130
	var 27 --> eqn 156
	var 28 --> eqn 143
	var 29 --> eqn 142
	var 30 --> eqn 214
	var 31 --> eqn 182
	var 32 --> eqn 213
	var 33 --> eqn 17
	var 34 --> eqn 194
	var 35 --> eqn 62
	var 36 --> eqn 84
	var 37 --> eqn 177
	var 38 --> eqn 50
	var 39 --> eqn 10
	var 40 --> eqn 85
	var 41 --> eqn 209
	var 42 --> eqn 67
	var 43 --> eqn 173
	var 44 --> eqn 45
	var 45 --> eqn 7
	var 46 --> eqn 146
	var 47 --> eqn 125
	var 48 --> eqn 27
	var 49 --> eqn 14
	var 50 --> eqn 105
	var 51 --> eqn 106
	var 52 --> eqn 82
	var 53 --> eqn 102
	var 54 --> eqn 203
	var 55 --> eqn 164
	var 56 --> eqn 68
	var 57 --> eqn 71
	var 58 --> eqn 79
	var 59 --> eqn 138
	var 60 --> eqn 171
	var 61 --> eqn 148
	var 62 --> eqn 167
	var 63 --> eqn 86
	var 64 --> eqn 201
	var 65 --> eqn 87
	var 66 --> eqn 208
	var 67 --> eqn 88
	var 68 --> eqn 53
	var 69 --> eqn 89
	var 70 --> eqn 114
	var 71 --> eqn 19
	var 72 --> eqn 91
	var 73 --> eqn 119
	var 74 --> eqn 107
	var 75 --> eqn 120
	var 76 --> eqn 121
	var 77 --> eqn 153
	var 78 --> eqn 61
	var 79 --> eqn 59
	var 80 --> eqn 77
	var 81 --> eqn 75
	var 82 --> eqn 97
	var 83 --> eqn 162
	var 84 --> eqn 34
	var 85 --> eqn 16
	var 86 --> eqn 197
	var 87 --> eqn 163
	var 88 --> eqn 175
	var 89 --> eqn 176
	var 90 --> eqn 212
	var 91 --> eqn 6
	var 92 --> eqn 3
	var 93 --> eqn 64
	var 94 --> eqn 74
	var 95 --> eqn 199
	var 96 --> eqn 179
	var 97 --> eqn 90
	var 98 --> eqn 58
	var 99 --> eqn 72
	var 100 --> eqn 184
	var 101 --> eqn 141
	var 102 --> eqn 140
	var 103 --> eqn 139
	var 104 --> eqn 98
	var 105 --> eqn 137
	var 106 --> eqn 180
	var 107 --> eqn 159
	var 108 --> eqn 135
	var 109 --> eqn 134
	var 110 --> eqn 158
	var 111 --> eqn 103
	var 112 --> eqn 133
	var 113 --> eqn 132
	var 114 --> eqn 187
	var 115 --> eqn 191
	var 116 --> eqn 192
	var 117 --> eqn 129
	var 118 --> eqn 157
	var 119 --> eqn 127
	var 120 --> eqn 95
	var 121 --> eqn 23
	var 122 --> eqn 57
	var 123 --> eqn 186
	var 124 --> eqn 110
	var 125 --> eqn 118
	var 126 --> eqn 154
	var 127 --> eqn 37
	var 128 --> eqn 51
	var 129 --> eqn 29
	var 130 --> eqn 32
	var 131 --> eqn 81
	var 132 --> eqn 9
	var 133 --> eqn 56
	var 134 --> eqn 205
	var 135 --> eqn 48
	var 136 --> eqn 170
	var 137 --> eqn 92
	var 138 --> eqn 161
	var 139 --> eqn 43
	var 140 --> eqn 104
	var 141 --> eqn 36
	var 142 --> eqn 4
	var 143 --> eqn 76
	var 144 --> eqn 13
	var 145 --> eqn 145
	var 146 --> eqn 136
	var 147 --> eqn 206
	var 148 --> eqn 124
	var 149 --> eqn 200
	var 150 --> eqn 178
	var 151 --> eqn 196
	var 152 --> eqn 47
	var 153 --> eqn 20
	var 154 --> eqn 78
	var 155 --> eqn 73
	var 156 --> eqn 22
	var 157 --> eqn 115
	var 158 --> eqn 100
	var 159 --> eqn 190
	var 160 --> eqn 185
	var 161 --> eqn 172
	var 162 --> eqn 150
	var 163 --> eqn 30
	var 164 --> eqn 44
	var 165 --> eqn 109
	var 166 --> eqn 152
	var 167 --> eqn 217
	var 168 --> eqn 5
	var 169 --> eqn 195
	var 170 --> eqn 202
	var 171 --> eqn 166
	var 172 --> eqn 218
	var 173 --> eqn 42
	var 174 --> eqn 2
	var 175 --> eqn 21
	var 176 --> eqn 144
	var 177 --> eqn 123
	var 178 --> eqn 96
	var 179 --> eqn 207
	var 180 --> eqn 131
	var 181 --> eqn 55
	var 182 --> eqn 101
	var 183 --> eqn 198
	var 184 --> eqn 147
	var 185 --> eqn 222
	var 186 --> eqn 113
	var 187 --> eqn 12
	var 188 --> eqn -1
	var 189 --> eqn 46
	var 190 --> eqn 165
	var 191 --> eqn 174
	var 192 --> eqn 38
	var 193 --> eqn 210
	var 194 --> eqn 60
	var 195 --> eqn 54
	var 196 --> eqn 18
	var 197 --> eqn 220
	var 198 --> eqn 1
	var 199 --> eqn 66
	var 200 --> eqn -1
	var 201 --> eqn 188
	var 202 --> eqn 189
	var 203 --> eqn 168
	var 204 --> eqn 94
	var 205 --> eqn 31
	var 206 --> eqn 215
	var 207 --> eqn 216
	var 208 --> eqn 181
	var 209 --> eqn 204
	var 210 --> eqn 193
	var 211 --> eqn 108
	var 212 --> eqn 128
	var 213 --> eqn 35
	var 214 --> eqn 99
	var 215 --> eqn 49
	var 216 --> eqn 52
	var 217 --> eqn 151
	var 218 --> eqn 219
	var 219 --> eqn 155
	var 220 --> eqn 169
	var 221 --> eqn 69
	var 222 --> eqn 83
	var 223 --> eqn 70
	var 224 --> eqn 33

equation to variable
**********************
	eqn 1 --> var 198
	eqn 2 --> var 174
	eqn 3 --> var 92
	eqn 4 --> var 142
	eqn 5 --> var 168
	eqn 6 --> var 91
	eqn 7 --> var 45
	eqn 8 --> var 6
	eqn 9 --> var 132
	eqn 10 --> var 39
	eqn 11 --> var 11
	eqn 12 --> var 187
	eqn 13 --> var 144
	eqn 14 --> var 49
	eqn 15 --> var 7
	eqn 16 --> var 85
	eqn 17 --> var 33
	eqn 18 --> var 196
	eqn 19 --> var 71
	eqn 20 --> var 153
	eqn 21 --> var 175
	eqn 22 --> var 156
	eqn 23 --> var 121
	eqn 24 --> var 2
	eqn 25 --> var 25
	eqn 26 --> var 15
	eqn 27 --> var 48
	eqn 28 --> var 1
	eqn 29 --> var 129
	eqn 30 --> var 163
	eqn 31 --> var 205
	eqn 32 --> var 130
	eqn 33 --> var 224
	eqn 34 --> var 84
	eqn 35 --> var 213
	eqn 36 --> var 141
	eqn 37 --> var 127
	eqn 38 --> var 192
	eqn 39 --> var 9
	eqn 40 --> var 20
	eqn 41 --> var 17
	eqn 42 --> var 173
	eqn 43 --> var 139
	eqn 44 --> var 164
	eqn 45 --> var 44
	eqn 46 --> var 189
	eqn 47 --> var 152
	eqn 48 --> var 135
	eqn 49 --> var 215
	eqn 50 --> var 38
	eqn 51 --> var 128
	eqn 52 --> var 216
	eqn 53 --> var 68
	eqn 54 --> var 195
	eqn 55 --> var 181
	eqn 56 --> var 133
	eqn 57 --> var 122
	eqn 58 --> var 98
	eqn 59 --> var 79
	eqn 60 --> var 194
	eqn 61 --> var 78
	eqn 62 --> var 35
	eqn 63 --> var 21
	eqn 64 --> var 93
	eqn 65 --> var 14
	eqn 66 --> var 199
	eqn 67 --> var 42
	eqn 68 --> var 56
	eqn 69 --> var 221
	eqn 70 --> var 223
	eqn 71 --> var 57
	eqn 72 --> var 99
	eqn 73 --> var 155
	eqn 74 --> var 94
	eqn 75 --> var 81
	eqn 76 --> var 143
	eqn 77 --> var 80
	eqn 78 --> var 154
	eqn 79 --> var 58
	eqn 80 --> var 4
	eqn 81 --> var 131
	eqn 82 --> var 52
	eqn 83 --> var 222
	eqn 84 --> var 36
	eqn 85 --> var 40
	eqn 86 --> var 63
	eqn 87 --> var 65
	eqn 88 --> var 67
	eqn 89 --> var 69
	eqn 90 --> var 97
	eqn 91 --> var 72
	eqn 92 --> var 137
	eqn 93 --> var 18
	eqn 94 --> var 204
	eqn 95 --> var 120
	eqn 96 --> var 178
	eqn 97 --> var 82
	eqn 98 --> var 104
	eqn 99 --> var 214
	eqn 100 --> var 158
	eqn 101 --> var 182
	eqn 102 --> var 53
	eqn 103 --> var 111
	eqn 104 --> var 140
	eqn 105 --> var 50
	eqn 106 --> var 51
	eqn 107 --> var 74
	eqn 108 --> var 211
	eqn 109 --> var 165
	eqn 110 --> var 124
	eqn 111 --> var 8
	eqn 112 --> var 24
	eqn 113 --> var 186
	eqn 114 --> var 70
	eqn 115 --> var 157
	eqn 116 --> var 12
	eqn 117 --> var 22
	eqn 118 --> var 125
	eqn 119 --> var 73
	eqn 120 --> var 75
	eqn 121 --> var 76
	eqn 122 --> var 13
	eqn 123 --> var 177
	eqn 124 --> var 148
	eqn 125 --> var 47
	eqn 126 --> var 3
	eqn 127 --> var 119
	eqn 128 --> var 212
	eqn 129 --> var 117
	eqn 130 --> var 26
	eqn 131 --> var 180
	eqn 132 --> var 113
	eqn 133 --> var 112
	eqn 134 --> var 109
	eqn 135 --> var 108
	eqn 136 --> var 146
	eqn 137 --> var 105
	eqn 138 --> var 59
	eqn 139 --> var 103
	eqn 140 --> var 102
	eqn 141 --> var 101
	eqn 142 --> var 29
	eqn 143 --> var 28
	eqn 144 --> var 176
	eqn 145 --> var 145
	eqn 146 --> var 46
	eqn 147 --> var 184
	eqn 148 --> var 61
	eqn 149 --> var 10
	eqn 150 --> var 162
	eqn 151 --> var 217
	eqn 152 --> var 166
	eqn 153 --> var 77
	eqn 154 --> var 126
	eqn 155 --> var 219
	eqn 156 --> var 27
	eqn 157 --> var 118
	eqn 158 --> var 110
	eqn 159 --> var 107
	eqn 160 --> var 23
	eqn 161 --> var 138
	eqn 162 --> var 83
	eqn 163 --> var 87
	eqn 164 --> var 55
	eqn 165 --> var 190
	eqn 166 --> var 171
	eqn 167 --> var 62
	eqn 168 --> var 203
	eqn 169 --> var 220
	eqn 170 --> var 136
	eqn 171 --> var 60
	eqn 172 --> var 161
	eqn 173 --> var 43
	eqn 174 --> var 191
	eqn 175 --> var 88
	eqn 176 --> var 89
	eqn 177 --> var 37
	eqn 178 --> var 150
	eqn 179 --> var 96
	eqn 180 --> var 106
	eqn 181 --> var 208
	eqn 182 --> var 31
	eqn 183 --> var 16
	eqn 184 --> var 100
	eqn 185 --> var 160
	eqn 186 --> var 123
	eqn 187 --> var 114
	eqn 188 --> var 201
	eqn 189 --> var 202
	eqn 190 --> var 159
	eqn 191 --> var 115
	eqn 192 --> var 116
	eqn 193 --> var 210
	eqn 194 --> var 34
	eqn 195 --> var 169
	eqn 196 --> var 151
	eqn 197 --> var 86
	eqn 198 --> var 183
	eqn 199 --> var 95
	eqn 200 --> var 149
	eqn 201 --> var 64
	eqn 202 --> var 170
	eqn 203 --> var 54
	eqn 204 --> var 209
	eqn 205 --> var 134
	eqn 206 --> var 147
	eqn 207 --> var 179
	eqn 208 --> var 66
	eqn 209 --> var 41
	eqn 210 --> var 193
	eqn 211 --> var 5
	eqn 212 --> var 90
	eqn 213 --> var 32
	eqn 214 --> var 30
	eqn 215 --> var 206
	eqn 216 --> var 207
	eqn 217 --> var 167
	eqn 218 --> var 172
	eqn 219 --> var 218
	eqn 220 --> var 197
	eqn 221 --> var 19
	eqn 222 --> var 185
"
[Timeout remaining time 659]
[Calling sys.exit(0), Time elapsed: 4.0597941018640995]
Failed to read output from testmodel.py, exit status != 0:
0.6713059470057487 0.681087156 0.069578584
Calling exit ...
<OMPython.OMCSessionZMQ object at 0x7fb6a91451b0>