Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries/ --ompython_omhome=/usr ThermoPower_ThermoPower.Test.DistributedParameterComponents.TestWaterFlow1DFV_B.conf.json
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo", uses=false)
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo", uses=false)
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.2.3+maint.om/package.mo", uses=false)
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoPower 3.1.0-master/package.mo", uses=false)
Using package ThermoPower with version 3.1 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoPower 3.1.0-master/package.mo)
Using package Modelica with version 3.2.3 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.2.3+maint.om/package.mo)
Using package Complex with version 4.0.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo)
Using package ModelicaServices with version 4.0.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo)
Running command: translateModel(ThermoPower.Test.DistributedParameterComponents.TestWaterFlow1DFV_B,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoPower_ThermoPower.Test.DistributedParameterComponents.TestWaterFlow1DFV_B")
translateModel(ThermoPower.Test.DistributedParameterComponents.TestWaterFlow1DFV_B,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoPower_ThermoPower.Test.DistributedParameterComponents.TestWaterFlow1DFV_B")
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo): time 0.001251/0.001251, allocations: 102.7 kB / 17.63 MB, free: 5.527 MB / 14.72 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo): time 0.001338/0.001338, allocations: 193.9 kB / 18.56 MB, free: 4.602 MB / 14.72 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.2.3+maint.om/package.mo): time 1.407/1.407, allocations: 205.1 MB / 224.4 MB, free: 12.3 MB / 190.1 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoPower 3.1.0-master/package.mo): time 0.2917/0.2917, allocations: 48.85 MB / 320.6 MB, free: 11.08 MB / 270.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 2.994e-05/2.995e-05, allocations: 4.359 kB / 390.8 MB, free: 48.89 MB / 318.1 MB
Notification: Performance of NFInst.instantiate(ThermoPower.Test.DistributedParameterComponents.TestWaterFlow1DFV_B): time 0.03742/0.03747, allocations: 51.93 MB / 442.7 MB, free: 0.7305 MB / 318.1 MB
Notification: Performance of NFInst.instExpressions: time 0.01816/0.05569, allocations: 15.66 MB / 458.3 MB, free: 1.051 MB / 334.1 MB
Notification: Performance of NFInst.updateImplicitVariability: time 0.0007852/0.0565, allocations: 15.88 kB / 458.4 MB, free: 1.035 MB / 334.1 MB
Notification: Performance of NFTyping.typeComponents: time 0.0009853/0.0575, allocations: 329.9 kB / 458.7 MB, free: 0.7109 MB / 334.1 MB
Notification: Performance of NFTyping.typeBindings: time 0.01397/0.07159, allocations: 4.652 MB / 463.3 MB, free: 12.07 MB / 350.1 MB
Notification: Performance of NFTyping.typeClassSections: time 0.004456/0.07606, allocations: 1.449 MB / 464.8 MB, free: 10.62 MB / 350.1 MB
Notification: Performance of NFFlatten.flatten: time 0.002329/0.07841, allocations: 1.761 MB / 466.5 MB, free: 8.852 MB / 350.1 MB
Notification: Performance of NFFlatten.resolveConnections: time 0.000609/0.07903, allocations: 397.8 kB / 466.9 MB, free: 8.465 MB / 350.1 MB
Notification: Performance of NFEvalConstants.evaluate: time 0.0007662/0.0798, allocations: 0.5609 MB / 467.5 MB, free: 7.902 MB / 350.1 MB
Notification: Performance of NFSimplifyModel.simplify: time 0.0005482/0.08036, allocations: 0.5022 MB / 468 MB, free: 7.398 MB / 350.1 MB
Notification: Performance of NFPackage.collectConstants: time 7.25e-05/0.08044, allocations: 48 kB / 468 MB, free: 7.352 MB / 350.1 MB
Notification: Performance of NFFlatten.collectFunctions: time 0.01047/0.09092, allocations: 5.775 MB / 473.8 MB, free: 1.57 MB / 350.1 MB
Notification: Performance of combineBinaries: time 0.001136/0.09209, allocations: 1.246 MB / 475.1 MB, free: 320 kB / 350.1 MB
Notification: Performance of replaceArrayConstructors: time 0.0005268/0.09263, allocations: 0.7847 MB / 475.8 MB, free: 15.52 MB / 366.1 MB
Notification: Performance of NFVerifyModel.verify: time 0.0002308/0.09286, allocations: 111.7 kB / 476 MB, free: 15.41 MB / 366.1 MB
Notification: Performance of FrontEnd: time 0.0002142/0.09309, allocations: 19.78 kB / 476 MB, free: 15.39 MB / 366.1 MB
Notification: Could not parse annotation "Evaluate" in the backend.
Notification: Could not parse annotation "choices" in the backend.
Notification: Could not parse annotation "Evaluate" in the backend.
Notification: Could not parse annotation "choices" in the backend.
Notification: Could not parse annotation "Evaluate" in the backend.
Notification: Could not parse annotation "choices" in the backend.
Notification: Could not parse annotation "Evaluate" in the backend.
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 430 (104)
 * Number of variables: 420 (114)
Notification: Performance of Bindings: time 0.003094/0.09619, allocations: 3.478 MB / 479.5 MB, free: 11.79 MB / 366.1 MB
Notification: Performance of FunctionAlias: time 0.0003035/0.0965, allocations: 233.5 kB / 479.7 MB, free: 11.58 MB / 366.1 MB
Notification: Performance of Early Inline: time 0.0008291/0.09734, allocations: 0.5945 MB / 480.3 MB, free: 10.94 MB / 366.1 MB
Notification: Performance of simplify1: time 0.0001009/0.09745, allocations: 107.8 kB / 480.4 MB, free: 10.84 MB / 366.1 MB
Notification: Performance of Alias: time 0.002278/0.09973, allocations: 2.058 MB / 482.4 MB, free: 8.543 MB / 366.1 MB
Notification: Performance of simplify2: time 7.072e-05/0.09982, allocations: 71.89 kB / 482.5 MB, free: 8.473 MB / 366.1 MB
Notification: Performance of Events: time 0.0002327/0.1001, allocations: 187.6 kB / 482.7 MB, free: 8.289 MB / 366.1 MB
Notification: Performance of Detect States: time 0.0004326/0.1005, allocations: 388.6 kB / 483.1 MB, free: 7.898 MB / 366.1 MB
Notification: Performance of Partitioning: time 0.000586/0.1011, allocations: 0.5413 MB / 483.6 MB, free: 7.32 MB / 366.1 MB
Error: Internal error NBAdjacency.Matrix.createPseudo failed for [FOR-] (9) ($RES_$AUX_132)
[----] for j in 1:9 loop
[----]   [SCAL] (1) $FUN_9[integer(1.0 + ((-1.0) + j))] = sum(hex.dMdt[1:j - 1]) ($RES_$AUX_133)
[----] end for;
Error: Internal error NBAdjacency.Matrix.create failed to create adjacency matrix for system:
System Variables (74/388)
***************************
(1)       [ALGB] (1) Real T_out.fluidState.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(2)       [ALGB] (1) Real T_out.fluidState.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0)
(3)       [ALGB] (10) Real[10] hex.fluidState.p (start = {5e6 for $i1 in 1:10}, min = {611.657 for $i1 in 1:10}, max = {1e8 for $i1 in 1:10}, nominal = {1e6 for $i1 in 1:10})
(4)       [ALGB] (1) Real $FUN_10
(5)       [ALGB] (1) Real hex.omega_hyd
(6)       [ALGB] (10) protected Real[10] hex.drdp
(7)       [ALGB] (1) Real alpha = 1.0 - exp(-NTU)
(8)       [ALGB] (1) Real hex.Dpfric1
(9)       [ALGB] (10) Real[10] hex.fluidState.h (start = {1e5 for $i1 in 1:10}, min = {-1e10 for $i1 in 1:10}, max = {1e10 for $i1 in 1:10}, nominal = {5e5 for $i1 in 1:10})
(10)      [ALGB] (1) Real NTU = (gamma * Dihex * Nt * 2.0 * 3.1415) / (ThermoPower.Test.DistributedParameterComponents.TestWaterFlow1DFV_B.Medium.specificHeatCapacityCp(hex.fluidState[1]) * whex)
(11)      [ALGB] (9) Real[9] hex.heatTransfer.Qvol
(12)      [ALGB] (1) stream Real T_in.inlet.h_outflow (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(13)      [ALGB] (1) stream Real T_out.outlet.h_outflow (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(14)      [ALGB] (10) Real[10] hex.fluidState.d (start = {150.0 for $i1 in 1:10}, min = {0.0 for $i1 in 1:10}, max = {1e5 for $i1 in 1:10}, nominal = {500.0 for $i1 in 1:10})
(15)      [ALGB] (10) protected Real[10] hex.drdh
(16)      [ALGB] (9) Real[9] hex.heatTransfer.wall.T (start = {288.15 for $i1 in 1:9}, min = {0.0 for $i1 in 1:9}, nominal = {300.0 for $i1 in 1:9})
(17)      [ALGB] (1) Real T_out.T
(18)      [ALGB] (1) Real hex.Kf
(19)      [ALGB] (9) flow Real[9] hex.heatTransfer.wall.Q
(20)      [ALGB] (1) Real hex.heatTransfer.w_wnom
(21)      [ALGB] (9) Real[9] hex.heatTransfer.Tvol (start = {500.0 for $i1 in 1:9}, min = {273.15 for $i1 in 1:9}, max = {2273.15 for $i1 in 1:9}, nominal = {500.0 for $i1 in 1:9})
(22)      [ALGB] (10) Real[10] hex.heatTransfer.T (start = {500.0 for $i1 in 1:10}, min = {273.15 for $i1 in 1:10}, max = {2273.15 for $i1 in 1:10}, nominal = {500.0 for $i1 in 1:10})
(23)      [ALGB] (9) protected Real[9] hex.drbdp
(24)      [ALGB] (10) Real[10] hex.fluidState.T (start = {500.0 for $i1 in 1:10}, min = {273.15 for $i1 in 1:10}, max = {2273.15 for $i1 in 1:10}, nominal = {500.0 for $i1 in 1:10})
(25)      [ALGB] (1) Real hex.Cf
(26)      [DER-] (9) Real[9] $DER.hex.htilde
(27)      [ALGB] (10) final input Real[10] hex.heatTransfer.fluidState.p = {hex.fluidState[1].p, hex.fluidState[2].p, hex.fluidState[3].p, hex.fluidState[4].p, hex.fluidState[5].p, hex.fluidState[6].p, hex.fluidState[7].p, hex.fluidState[8].p, hex.fluidState[9].p, hex.fluidState[10].p} (start = {5e6 for $i1 in 1:10}, min = {611.657 for $i1 in 1:10}, max = {1e8 for $i1 in 1:10}, nominal = {1e6 for $i1 in 1:10})
(28)      [ALGB] (9) Real[9] $FUN_9
(29)      [ALGB] (1) Real $FUN_7
(30)      [ALGB] (1) Real $FUN_6
(31)      [ALGB] (9) protected Real[9] hex.drbdh
(32)      [ALGB] (9) Real[9] hex.dMdt
(33)      [ALGB] (1) Real hex.Mtot (min = 0.0)
(34)      [ALGB] (1) Real $FUN_4
(35)      [ALGB] (1) Real $FUN_3
(36)      [ALGB] (10) final input Real[10] hex.heatTransfer.fluidState.h = {hex.fluidState[1].h, hex.fluidState[2].h, hex.fluidState[3].h, hex.fluidState[4].h, hex.fluidState[5].h, hex.fluidState[6].h, hex.fluidState[7].h, hex.fluidState[8].h, hex.fluidState[9].h, hex.fluidState[10].h} (start = {1e5 for $i1 in 1:10}, min = {-1e10 for $i1 in 1:10}, max = {1e10 for $i1 in 1:10}, nominal = {5e5 for $i1 in 1:10})
(37)      [ALGB] (1) Real cp = ThermoPower.Test.DistributedParameterComponents.TestWaterFlow1DFV_B.Medium.specificHeatCapacityCp(hex.fluidState[1])
(38)      [ALGB] (10) final input Real[10] hex.heatTransfer.fluidState.d = {hex.fluidState[1].d, hex.fluidState[2].d, hex.fluidState[3].d, hex.fluidState[4].d, hex.fluidState[5].d, hex.fluidState[6].d, hex.fluidState[7].d, hex.fluidState[8].d, hex.fluidState[9].d, hex.fluidState[10].d} (start = {150.0 for $i1 in 1:10}, min = {0.0 for $i1 in 1:10}, max = {1e5 for $i1 in 1:10}, nominal = {500.0 for $i1 in 1:10})
(39)      [DER-] (1) Real $DER.hex.p
(40)      [ALGB] (1) Real T_in.T
(41)      [ALGB] (10) Real[10] hex.rho (start = {150.0 for $i1 in 1:10}, min = {0.0 for $i1 in 1:10}, max = {1e5 for $i1 in 1:10}, nominal = {500.0 for $i1 in 1:10})
(42)      [ALGB] (1) Real hex.w (start = hex.wnom / hex.Nt, min = -1e5, max = 1e5)
(43)      [ALGB] (10) Real[10] hex.u
(44)      [ALGB] (10) final input Real[10] hex.heatTransfer.fluidState.T = {hex.fluidState[1].T, hex.fluidState[2].T, hex.fluidState[3].T, hex.fluidState[4].T, hex.fluidState[5].T, hex.fluidState[6].T, hex.fluidState[7].T, hex.fluidState[8].T, hex.fluidState[9].T, hex.fluidState[10].T} (start = {500.0 for $i1 in 1:10}, min = {273.15 for $i1 in 1:10}, max = {2273.15 for $i1 in 1:10}, nominal = {500.0 for $i1 in 1:10})
(45)      [ALGB] (10) final Real[10] hex.heatTransfer.w (min = {-1e5 for $i1 in 1:10}, max = {1e5 for $i1 in 1:10})
(46)      [ALGB] (9) flow Real[9] tempSource.wall.Q
(47)      [ALGB] (9) Real[9] tempSource.wall.T (start = {288.15 for $i1 in 1:9}, min = {0.0 for $i1 in 1:9}, nominal = {300.0 for $i1 in 1:9})
(48)      [ALGB] (9) Real[9] hex.wall.T (start = {288.15 for $i1 in 1:9}, min = {0.0 for $i1 in 1:9}, nominal = {300.0 for $i1 in 1:9})
(49)      [ALGB] (10) Real[10] hex.h (start = {hex.hstart[$h1] for $h1 in 1:10}, min = {-1e10 for $i1 in 1:10}, max = {1e10 for $i1 in 1:10}, nominal = {5e5 for $i1 in 1:10})
(50)      [ALGB] (9) flow Real[9] hex.wall.Q
(51)      [ALGB] (9) protected Real[9] hex.vbar (min = {0.0 for $i1 in 1:9})
(52)      [ALGB] (9) Real[9] hex.heatTransfer.Qw
(53)      [ALGB] (9) Real[9] hex.wbar (start = {hex.wnom / hex.Nt for $wbar1 in 1:9}, min = {-1e5 for $i1 in 1:9}, max = {1e5 for $i1 in 1:9})
(54)      [DISC] (10) Integer[10] hex.fluidState.phase (min = {0 for $i1 in 1:10}, max = {2 for $i1 in 1:10})
(55)      [ALGB] (9) protected Real[9] hex.rhobar (start = {150.0 for $i1 in 1:9}, min = {0.0 for $i1 in 1:9}, max = {1e5 for $i1 in 1:9}, nominal = {500.0 for $i1 in 1:9})
(56)      [ALGB] (1) Real Temperature.y
(57)      [ALGB] (10) Real[10] hex.T (start = {500.0 for $i1 in 1:10}, min = {273.15 for $i1 in 1:10}, max = {2273.15 for $i1 in 1:10}, nominal = {500.0 for $i1 in 1:10})
(58)      [DISC] (1) Boolean $SEV_6
(59)      [DISC] (1) Boolean $SEV_5
(60)      [DISC] (1) Boolean $SEV_4
(61)      [ALGB] (1) Real hex.Q
(62)      [DISC] (1) Boolean $SEV_3
(63)      [ALGB] (1) Real valve.w (min = -1e5, max = 1e5)
(64)      [ALGB] (1) Real hex.Tr
(65)      [ALGB] (1) Real hex.M (min = 0.0)
(66)      [ALGB] (1) Real hex.Dpfric
(67)      [DISC] (1) Boolean $TEV_0
(68)      [ALGB] (1) Real T_in.fluidState.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0)
(69)      [ALGB] (1) Real T_in.fluidState.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(70)      [ALGB] (9) Real[9] hex.heatTransfer.Tw (start = {500.0 for $i1 in 1:9}, min = {273.15 for $i1 in 1:9}, max = {2273.15 for $i1 in 1:9}, nominal = {500.0 for $i1 in 1:9})
(71)      [ALGB] (9) Real[9] hex.Q_single
(72)      [DISC] (10) final input Integer[10] hex.heatTransfer.fluidState.phase = {hex.fluidState[1].phase, hex.fluidState[2].phase, hex.fluidState[3].phase, hex.fluidState[4].phase, hex.fluidState[5].phase, hex.fluidState[6].phase, hex.fluidState[7].phase, hex.fluidState[8].phase, hex.fluidState[9].phase, hex.fluidState[10].phase} (min = {0 for $i1 in 1:10}, max = {2 for $i1 in 1:10})
(73)      [ALGB] (1) Real T_in.fluidState.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(74)      [ALGB] (1) Real hex.wout (min = -1e5, max = 1e5)


System Equations (76/353)
***************************
(1)       [SCAL] (1) hex.wout = valve.w / hex.Nt ($RES_SIM_16)
(2)       [SCAL] (1) hex.Kf = (hex.omega_hyd * hex.Cf) / hex.A ^ 3.0 ($RES_SIM_52)
(3)       [SCAL] (1) hex.w = fluidSource.w0 / hex.Nt ($RES_SIM_17)
(4)       [SCAL] (1) hex.Cf = hex.Cfnom * hex.Kfc ($RES_SIM_53)
(5)       [SCAL] (1) T_in.fluidState.h = homotopy(if $SEV_5 then fluidSource.h else T_in.inlet.h_outflow, fluidSource.h) ($RES_$AUX_141)
(6)       [SCAL] (1) hex.omega_hyd = (4.0 * hex.A) / hex.Dhyd ($RES_SIM_54)
(7)       [SCAL] (1) T_out.fluidState.h = homotopy(if $SEV_6 then T_out.outlet.h_outflow else fluidSink.h, T_out.outlet.h_outflow) ($RES_$AUX_140)
(8)       [SCAL] (1) hex.heatTransfer.Qw = hex.heatTransfer.wall.Q ($RES_SIM_56)
(9)       [SCAL] (1) hex.heatTransfer.Tw = hex.heatTransfer.wall.T ($RES_SIM_57)
(10)      [FOR-] (10) ($RES_SIM_58)
(10)      [----] for j in 1:10 loop
(10)      [----]   [SCAL] (1) hex.heatTransfer.T[j] = hex.heatTransfer.fluidState.h ($RES_SIM_59)
(10)      [----] end for;
(11)      [SCAL] (1) $FUN_3 = abs(hex.heatTransfer.w[1]) ($RES_$AUX_139)
(12)      [FOR-] (10) ($RES_SIM_20)
(12)      [----] for j in 1:10 loop
(12)      [----]   [SCAL] (1) hex.T[j] = hex.fluidState.h ($RES_SIM_21)
(12)      [----] end for;
(13)      [SCAL] (1) valve.w = Constant1.k * valve.Kv * (hex.p - fluidSink.p0) ($RES_SIM_102)
(14)      [SCAL] (1) $FUN_4 = exp(-hex.heatTransfer.w_wnom / hex.heatTransfer.sigma) ($RES_$AUX_138)
(15)      [SCAL] (1) hex.Q = sum(hex.heatTransfer.wall.Q) ($RES_$AUX_137)
(16)      [FOR-] (10) ($RES_SIM_22)
(16)      [----] for j in 1:10 loop
(16)      [----]   [SCAL] (1) hex.rho[j] = hex.fluidState.d ($RES_SIM_23)
(16)      [----] end for;
(17)      [SCAL] (1) $FUN_6 = sum(hex.dMdt) ($RES_$AUX_136)
(18)      [SCAL] (1) $FUN_7 = sum(hex.vbar) ($RES_$AUX_135)
(19)      [FOR-] (10) ($RES_SIM_24)
(19)      [----] for j in 1:10 loop
(19)      [----]   [SCAL] (1) hex.drdp[j] = Modelica.Media.Water.IF97_Utilities.ddph_props(hex.fluidState.phase, hex.fluidState.T, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(hex.fluidState.phase, hex.fluidState.T, hex.fluidState.p, 0)) ($RES_SIM_25)
(19)      [----] end for;
(20)      [FOR-] (9) ($RES_SIM_60)
(20)      [----] for j in 1:9 loop
(20)      [----]   [SCAL] (1) hex.heatTransfer.Tvol[j] = if not hex.heatTransfer.useAverageTemperature then hex.heatTransfer.T[j + 1] else if not hex.heatTransfer.adaptiveAverageTemperature then (hex.heatTransfer.T[j] + hex.heatTransfer.T[j + 1]) / 2.0 else (hex.heatTransfer.T[j] + hex.heatTransfer.T[j + 1]) / 2.0 + ((hex.heatTransfer.T[j + 1] - hex.heatTransfer.T[j]) / 2.0) * $FUN_4 ($RES_SIM_61)
(20)      [----] end for;
(21)      [SCAL] (1) hex.Dpfric1 = homotopy(0.1111111111111111 * $FUN_7 * (hex.w * sqrt(hex.w * hex.w + (hex.wnom / hex.Nt) * hex.wnf * ((hex.wnom / hex.Nt) * hex.wnf))) * hex.Kf, (hex.dpnom / (hex.wnom / hex.Nt)) * hex.w) ($RES_$AUX_134)
(22)      [FOR-] (10) ($RES_SIM_26)
(22)      [----] for j in 1:10 loop
(22)      [----]   [SCAL] (1) hex.drdh[j] = Modelica.Media.Water.IF97_Utilities.ddhp_props(hex.fluidState.phase, hex.fluidState.T, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(hex.fluidState.phase, hex.fluidState.T, hex.fluidState.p, 0)) ($RES_SIM_27)
(22)      [----] end for;
(23)      [FOR-] (9) ($RES_SIM_62)
(23)      [----] for j in 1:9 loop
(23)      [----]   [SCAL] (1) hex.heatTransfer.Qw[j] = hex.heatTransfer.gamma * hex.heatTransfer.kc * hex.heatTransfer.l * hex.heatTransfer.omega * (hex.heatTransfer.Tw[j] - hex.heatTransfer.Tvol[j]) * hex.heatTransfer.Nt ($RES_SIM_63)
(23)      [----] end for;
(24)      [FOR-] (9) ($RES_$AUX_132)
(24)      [----] for j in 1:9 loop
(24)      [----]   [SCAL] (1) $FUN_9[integer(1.0 + ((-1.0) + j))] = sum(hex.dMdt[1:j - 1]) ($RES_$AUX_133)
(24)      [----] end for;
(25)      [SCAL] (1) T_in.fluidState.d = Modelica.Media.Water.IF97_Utilities.rho_ph(T_in.fluidState.p, T_in.fluidState.h, 0, 0) ($RES_SIM_144)
(26)      [SCAL] (1) $FUN_10 = sum(hex.rhobar) ($RES_$AUX_131)
(27)      [FOR-] (10) ($RES_SIM_28)
(27)      [----] for j in 1:10 loop
(27)      [----]   [SCAL] (1) hex.u[j] = hex.w / (hex.A * hex.rho[j]) ($RES_SIM_29)
(27)      [----] end for;
(28)      [SCAL] (1) T_in.T = Modelica.Media.Water.IF97_Utilities.T_ph(T_in.fluidState.p, T_in.fluidState.h, 0, 0) ($RES_SIM_145)
(29)      [SCAL] (1) hex.heatTransfer.w_wnom = $FUN_3 / hex.heatTransfer.wnom ($RES_SIM_64)
(30)      [SCAL] (1) 1.0 - alpha = exp(-NTU) ($RES_$AUX_130)
(31)      [ARRY] (9) hex.heatTransfer.Qvol = hex.heatTransfer.Qw ($RES_SIM_65)
(32)      [ARRY] (10) hex.heatTransfer.w = hex.w * fill(1.0, 10) ($RES_SIM_66)
(33)      [ARRY] (50) hex.heatTransfer.fluidState = hex.fluidState ($RES_SIM_67)
(34)      [SCAL] (1) T_out.fluidState.d = Modelica.Media.Water.IF97_Utilities.rho_ph(fluidSink.p0, T_out.fluidState.h, 0, 0) ($RES_SIM_149)
(35)      [ARRY] (9) hex.Q_single = hex.heatTransfer.Qvol / hex.Nt ($RES_SIM_68)
(36)      [FOR-] (9) ($RES_SIM_69)
(36)      [----] for i in 1:9 loop
(36)      [----]   [SCAL] (1) tempSource.wall.T[i] = Temperature.y ($RES_SIM_70)
(36)      [----] end for;
(37)      [SCAL] (1) cp = Modelica.Media.Water.IF97_Utilities.cp_props_ph(hex.fluidState.phase, hex.fluidState.T, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(hex.fluidState.phase, hex.fluidState.T, 0, 0)) ($RES_BND_122)
(38)      [FOR-] (9) ($RES_SIM_110)
(38)      [----] for $i1 in 1:9 loop
(38)      [----]   [SCAL] (1) tempSource.wall.Q[$i1] + hex.wall.Q[$i1] = 0.0 ($RES_SIM_111)
(38)      [----] end for;
(39)      [SCAL] (1) NTU = (6.283 * gamma * Dihex * Nt) / (Modelica.Media.Water.IF97_Utilities.cp_props_ph(hex.fluidState.phase, hex.fluidState.T, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(hex.fluidState.phase, hex.fluidState.T, 0, 0)) * whex) ($RES_BND_123)
(40)      [SCAL] (1) tempSource.wall.T = hex.wall.T ($RES_SIM_112)
(41)      [ARRY] (10) hex.heatTransfer.fluidState.phase = {hex.fluidState[1].phase, hex.fluidState[2].phase, hex.fluidState[3].phase, hex.fluidState[4].phase, hex.fluidState[5].phase, hex.fluidState[6].phase, hex.fluidState[7].phase, hex.fluidState[8].phase, hex.fluidState[9].phase, hex.fluidState[10].phase} ($RES_BND_125)
(42)      [FOR-] (9) ($RES_SIM_30)
(42)      [----] for j in 1:9 loop
(42)      [----]   [SCAL] (1) (hex.wbar[j] * (hex.h[j + 1] - hex.h[j]) + hex.rhobar[j] * hex.l * hex.A * $DER.hex.htilde[j]) - hex.l * hex.A * $DER.hex.p = hex.Q_single[j] ($RES_SIM_31)
(42)      [----] end for;
(43)      [ARRY] (10) hex.heatTransfer.fluidState.h = {hex.fluidState[1].h, hex.fluidState[2].h, hex.fluidState[3].h, hex.fluidState[4].h, hex.fluidState[5].h, hex.fluidState[6].h, hex.fluidState[7].h, hex.fluidState[8].h, hex.fluidState[9].h, hex.fluidState[10].h} ($RES_BND_126)
(44)      [ARRY] (10) hex.heatTransfer.fluidState.d = {hex.fluidState[1].d, hex.fluidState[2].d, hex.fluidState[3].d, hex.fluidState[4].d, hex.fluidState[5].d, hex.fluidState[6].d, hex.fluidState[7].d, hex.fluidState[8].d, hex.fluidState[9].d, hex.fluidState[10].d} ($RES_BND_127)
(45)      [FOR-] (9) ($RES_SIM_32)
(45)      [----] for j in 1:9 loop
(45)      [----]   [SCAL] (1) hex.dMdt[j] = hex.l * hex.A * (hex.drbdh[j] * $DER.hex.htilde[j] + hex.drbdp[j] * $DER.hex.p) ($RES_SIM_33)
(45)      [----] end for;
(46)      [ARRY] (10) hex.heatTransfer.fluidState.T = {hex.fluidState[1].T, hex.fluidState[2].T, hex.fluidState[3].T, hex.fluidState[4].T, hex.fluidState[5].T, hex.fluidState[6].T, hex.fluidState[7].T, hex.fluidState[8].T, hex.fluidState[9].T, hex.fluidState[10].T} ($RES_BND_128)
(47)      [SCAL] (1) T_out.T = Modelica.Media.Water.IF97_Utilities.T_ph(fluidSink.p0, T_out.fluidState.h, 0, 0) ($RES_SIM_150)
(48)      [ARRY] (10) hex.heatTransfer.fluidState.p = {hex.fluidState[1].p, hex.fluidState[2].p, hex.fluidState[3].p, hex.fluidState[4].p, hex.fluidState[5].p, hex.fluidState[6].p, hex.fluidState[7].p, hex.fluidState[8].p, hex.fluidState[9].p, hex.fluidState[10].p} ($RES_BND_129)
(49)      [FOR-] (9) ($RES_SIM_34)
(49)      [----] for j in 1:9 loop
(49)      [----]   [SCAL] (1) hex.rhobar[j] = (hex.rho[j] + hex.rho[j + 1]) / 2.0 ($RES_SIM_35)
(49)      [----] end for;
(50)      [SCAL] (1) hex.fluidState[j].phase = 0 ($RES_SIM_152)
(51)      [FOR-] (9) ($RES_SIM_36)
(51)      [----] for j in 1:9 loop
(51)      [----]   [SCAL] (1) hex.drbdp[j] = (hex.drdp[j] + hex.drdp[j + 1]) / 2.0 ($RES_SIM_37)
(51)      [----] end for;
(52)      [SCAL] (1) hex.fluidState[j].h = hex.h[j] ($RES_SIM_153)
(53)      [FOR-] (9) ($RES_SIM_119)
(53)      [----] for $i1 in 1:9 loop
(53)      [----]   [SCAL] (1) (-hex.wall.Q[$i1]) + hex.heatTransfer.wall.Q[$i1] = 0.0 ($RES_SIM_120)
(53)      [----] end for;
(54)      [SCAL] (1) hex.fluidState[j].d = Modelica.Media.Water.IF97_Utilities.rho_ph(hex.p, hex.h[j], 0, 0) ($RES_SIM_154)
(55)      [FOR-] (9) ($RES_SIM_38)
(55)      [----] for j in 1:9 loop
(55)      [----]   [SCAL] (1) hex.drbdh[j] = (hex.drdh[j] + hex.drdh[j + 1]) / 2.0 ($RES_SIM_39)
(55)      [----] end for;
(56)      [SCAL] (1) hex.fluidState[j].T = Modelica.Media.Water.IF97_Utilities.T_ph(hex.p, hex.h[j], 0, 0) ($RES_SIM_155)
(57)      [SCAL] (1) hex.fluidState[j].p = hex.p ($RES_SIM_156)
(58)      [SCAL] (1) $TEV_0 = time < Temperature.startTime ($RES_EVT_158)
(59)      [SCAL] (1) hex.wall.T = hex.heatTransfer.wall.T ($RES_SIM_121)
(60)      [FOR-] (9) ($RES_SIM_40)
(60)      [----] for j in 1:9 loop
(60)      [----]   [SCAL] (1) hex.vbar[j] = 1.0 / hex.rhobar[j] ($RES_SIM_41)
(60)      [----] end for;
(61)      [FOR-] (9) ($RES_SIM_42)
(61)      [----] for j in 1:9 loop
(61)      [----]   [SCAL] (1) hex.wbar[j] = fluidSource.w0 / hex.Nt - (hex.dMdt[j] / 2.0 + $FUN_9[integer(1.0 + ((-1.0) + j))]) ($RES_SIM_43)
(61)      [----] end for;
(62)      [SCAL] (1) hex.Dpfric = hex.Dpfric1 ($RES_SIM_47)
(63)      [SCAL] (1) (hex.p + hex.Dpfric) - T_in.fluidState.p = 0.0 ($RES_SIM_48)
(64)      [SCAL] (1) $FUN_6 = (fluidSource.w0 - valve.w) / hex.Nt ($RES_SIM_49)
(65)      [SCAL] (1) Temperature.y = Temperature.offset + (if $TEV_0 then 0.0 else Temperature.height) ($RES_SIM_86)
(66)      [SCAL] (1) $SEV_3 = hex.w > (-hex.wnom * hex.wnm) ($RES_EVT_162)
(67)      [SCAL] (1) $SEV_4 = hex.Kf >= 0.0 ($RES_EVT_163)
(68)      [SCAL] (1) $SEV_5 = fluidSource.w0 > 0.0 ($RES_EVT_164)
(69)      [SCAL] (1) $SEV_6 = valve.w > 0.0 ($RES_EVT_165)
(70)      [SCAL] (1) hex.M = hex.A * $FUN_10 * hex.l ($RES_SIM_8)
(71)      [SCAL] (1) hex.Mtot = hex.M * hex.Nt ($RES_SIM_7)
(72)      [SCAL] (1) hex.Tr = noEvent(hex.M / max(hex.w, 1e-15)) ($RES_SIM_6)
(73)      [SCAL] (1) hex.h[2:10] = hex.htilde ($RES_SIM_10)
(74)      [SCAL] (1) hex.h[1] = fluidSource.h ($RES_SIM_11)
(75)      [SCAL] (1) T_out.outlet.h_outflow = hex.htilde[9] ($RES_SIM_12)
(76)      [SCAL] (1) T_in.inlet.h_outflow = hex.h[1] ($RES_SIM_13)