Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ModelicaTest_3.2.1_ModelicaTest.Fluid.Dissipation.Verifications.PressureLoss.Bend.dp_curvedOverall_DPMFLOW.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/ModelicaTest 3.2.1+maint.om/package.mo", uses=false)
Using package ModelicaTest with version 3.2.1 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaTest 3.2.1+maint.om/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(ModelicaTest.Fluid.Dissipation.Verifications.PressureLoss.Bend.dp_curvedOverall_DPMFLOW,tolerance=1e-05,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ModelicaTest_3.2.1_ModelicaTest.Fluid.Dissipation.Verifications.PressureLoss.Bend.dp_curvedOverall_DPMFLOW")
translateModel(ModelicaTest.Fluid.Dissipation.Verifications.PressureLoss.Bend.dp_curvedOverall_DPMFLOW,tolerance=1e-05,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ModelicaTest_3.2.1_ModelicaTest.Fluid.Dissipation.Verifications.PressureLoss.Bend.dp_curvedOverall_DPMFLOW")
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo): time 0.001005/0.001005, allocations: 107.4 kB / 16.42 MB, free: 6.453 MB / 14.72 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo): time 0.001133/0.001133, allocations: 190 kB / 17.36 MB, free: 5.707 MB / 14.72 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.2.3+maint.om/package.mo): time 1.204/1.204, allocations: 205.1 MB / 223.2 MB, free: 12.22 MB / 190.1 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaTest 3.2.1+maint.om/package.mo): time 0.1527/0.1527, allocations: 38 MB / 308.6 MB, free: 5.977 MB / 254.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 1.892e-05/1.892e-05, allocations: 5.797 kB / 433.7 MB, free: 14.46 MB / 318.1 MB
Notification: Performance of NFInst.instantiate(ModelicaTest.Fluid.Dissipation.Verifications.PressureLoss.Bend.dp_curvedOverall_DPMFLOW): time 0.002345/0.002372, allocations: 2.127 MB / 435.8 MB, free: 12.32 MB / 318.1 MB
Notification: Performance of NFInst.instExpressions: time 0.002148/0.004533, allocations: 1.894 MB / 437.7 MB, free: 10.41 MB / 318.1 MB
Notification: Performance of NFInst.updateImplicitVariability: time 0.0001304/0.004675, allocations: 0 / 437.7 MB, free: 10.41 MB / 318.1 MB
Notification: Performance of NFTyping.typeComponents: time 0.0002716/0.004954, allocations: 75.59 kB / 437.7 MB, free: 10.34 MB / 318.1 MB
Notification: Performance of NFTyping.typeBindings: time 0.0003314/0.005293, allocations: 143.3 kB / 437.9 MB, free: 10.2 MB / 318.1 MB
Notification: Performance of NFTyping.typeClassSections: time 0.0009664/0.006287, allocations: 0.5601 MB / 438.4 MB, free: 9.637 MB / 318.1 MB
Notification: Performance of NFFlatten.flatten: time 0.000278/0.006574, allocations: 374.6 kB / 438.8 MB, free: 9.27 MB / 318.1 MB
Notification: Performance of NFFlatten.resolveConnections: time 3.848e-05/0.006619, allocations: 5.453 kB / 438.8 MB, free: 9.262 MB / 318.1 MB
Notification: Performance of NFEvalConstants.evaluate: time 0.0001493/0.006773, allocations: 187.4 kB / 439 MB, free: 9.078 MB / 318.1 MB
Notification: Performance of NFSimplifyModel.simplify: time 0.0001645/0.006946, allocations: 195.3 kB / 439.2 MB, free: 8.887 MB / 318.1 MB
Notification: Performance of NFPackage.collectConstants: time 1.959e-05/0.006971, allocations: 4 kB / 439.2 MB, free: 8.883 MB / 318.1 MB
Notification: Performance of NFFlatten.collectFunctions: time 0.001193/0.008168, allocations: 1.603 MB / 440.8 MB, free: 7.277 MB / 318.1 MB
Notification: Performance of combineBinaries: time 0.0002313/0.008409, allocations: 416.4 kB / 441.2 MB, free: 6.867 MB / 318.1 MB
Notification: Performance of replaceArrayConstructors: time 0.0001284/0.008543, allocations: 292.9 kB / 441.5 MB, free: 6.578 MB / 318.1 MB
Notification: Performance of NFVerifyModel.verify: time 3.411e-05/0.008582, allocations: 23.94 kB / 441.5 MB, free: 6.555 MB / 318.1 MB
Notification: Performance of FrontEnd: time 1.73e-05/0.008604, allocations: 7.984 kB / 441.5 MB, free: 6.547 MB / 318.1 MB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 103 (43)
 * Number of variables: 199 (43)
Notification: Performance of Bindings: time 0.001116/0.009725, allocations: 1.778 MB / 443.3 MB, free: 4.656 MB / 318.1 MB
Notification: Performance of FunctionAlias: time 0.0001007/0.009832, allocations: 99.69 kB / 443.4 MB, free: 4.559 MB / 318.1 MB
Notification: Performance of Early Inline: time 0.0004655/0.0103, allocations: 0.7681 MB / 444.2 MB, free: 3.762 MB / 318.1 MB
Notification: Performance of simplify1: time 1.56e-05/0.01033, allocations: 15.97 kB / 444.2 MB, free: 3.746 MB / 318.1 MB
Notification: Performance of Alias: time 0.0003929/0.01073, allocations: 432.5 kB / 444.6 MB, free: 3.27 MB / 318.1 MB
Notification: Performance of simplify2: time 1.138e-05/0.01075, allocations: 15.91 kB / 444.6 MB, free: 3.254 MB / 318.1 MB
Notification: Performance of Events: time 7.407e-05/0.01082, allocations: 71.92 kB / 444.7 MB, free: 3.184 MB / 318.1 MB
Notification: Performance of Detect States: time 0.0003066/0.01114, allocations: 146.4 kB / 444.8 MB, free: 3.023 MB / 318.1 MB
Notification: Performance of Partitioning: time 0.0001776/0.01132, allocations: 231.3 kB / 445.1 MB, free: 2.793 MB / 318.1 MB
Error: Internal error NBAdjacency.Matrix.createPseudo failed for:
[ARRY] (2) DP_1 = {Modelica.Fluid.Dissipation.PressureLoss.Bend.dp_curvedOverall_DP(m_flow_IN_con_1[i], m_flow_IN_var_1[i], input_mdot_1[i]) for i in 1:2} ($RES_SIM_3)
Error: Internal error NBAdjacency.Matrix.create failed to create adjacency matrix for system:
System Variables (45/204)
***************************
(1)       [ALGB] (2) Real[2] $FUN_2
(2)       [ALGB] (3) Real[3] $FUN_1
(3)       [ALGB] (3) Real[3] M_FLOW_2 (start = {0.0 for $i1 in 1:3})
(4)       [ALGB] (2) Real[2] M_FLOW_1 (start = {0.0 for $i1 in 1:2})
(5)       [ALGB] (4) Real[2, 2] m_flow_IN_con_1.delta = {delta[3] * 3.141592653589793 for $m_flow_IN_con_11 in 1:2}
(6)       [ALGB] (9) Real[3, 3] dp_IN_var_2.rho = {rho for $dp_IN_var_21 in 1:3} (min = {0.0 for $i1 in 1:3})
(7)       [ALGB] (3) Real[3] input_dp_2 = {1.0 for $i1 in 1:3} .* input_DP.y (start = {0.0 for $i1 in 1:3})
(8)       [ALGB] (9) Real[3, 3] m_flow_IN_con_2.delta = {delta[$m_flow_IN_con_21] for $m_flow_IN_con_21 in 1:3}
(9)       [ALGB] (9) Real[3, 3] m_flow_IN_con_2.K = {K for $m_flow_IN_con_21 in 1:3}
(10)      [ALGB] (2) Real[2] input_dp_1 = {1.0 for $i1 in 1:2} .* input_DP.y (start = {0.0 for $i1 in 1:2})
(11)      [ALGB] (9) Real[3, 3] dp_IN_con_2.delta = {delta[$dp_IN_con_21] for $dp_IN_con_21 in 1:3}
(12)      [ALGB] (4) Real[2, 2] m_flow_IN_var_1.rho = {rho for $m_flow_IN_var_11 in 1:2} (min = {0.0 for $i1 in 1:2})
(13)      [ALGB] (4) Real[2, 2] dp_IN_con_1.delta = {delta[3] for $dp_IN_con_11 in 1:2}
(14)      [ALGB] (4) Real[2, 2] dp_IN_var_1.eta = {eta for $dp_IN_var_11 in 1:2} (min = {0.0 for $i1 in 1:2})
(15)      [ALGB] (9) Real[3, 3] m_flow_IN_con_2.R_0 = {2.26 * d_hyd for $m_flow_IN_con_21 in 1:3} (min = {0.0 for $i1 in 1:3})
(16)      [ALGB] (4) Real[2, 2] m_flow_IN_con_1.K = {K for $m_flow_IN_con_11 in 1:2}
(17)      [ALGB] (9) Real[3, 3] dp_IN_con_2.R_0 = {2.26 * d_hyd for $dp_IN_con_21 in 1:3} (min = {0.0 for $i1 in 1:3})
(18)      [ALGB] (3) Real[3] DP_2 = {input_dp_2[i] for i in 1:3} (start = {0.0 for $i1 in 1:3})
(19)      [ALGB] (4) Real[2, 2] m_flow_IN_var_1.eta = {eta for $m_flow_IN_var_11 in 1:2} (min = {0.0 for $i1 in 1:2})
(20)      [ALGB] (2) Real[2] DP_1 = {input_dp_1[i] for i in 1:2} (start = {0.0 for $i1 in 1:2})
(21)      [ALGB] (3) protected Real[3] zeta_TOT_2 = {(abs(DP_plot_2[i]) * 2.0) / max(1000.0 * velocity_2[i] ^ 2.0, 1e-5) for i in 1:3}
(22)      [ALGB] (4) Real[2, 2] dp_IN_var_1.rho = {rho for $dp_IN_var_11 in 1:2} (min = {0.0 for $i1 in 1:2})
(23)      [ALGB] (2) protected Real[2] zeta_TOT_1 = {(abs(DP_plot_1[i]) * 2.0) / max(1000.0 * velocity_1[i] ^ 2.0, 1e-5) for i in 1:2}
(24)      [ALGB] (2) Real[2] input_mdot_1 (start = {0.0 for $i1 in 1:2})
(25)      [ALGB] (9) Real[3, 3] m_flow_IN_var_2.rho = {rho for $m_flow_IN_var_21 in 1:3} (min = {0.0 for $i1 in 1:3})
(26)      [ALGB] (3) Real[3] input_mdot_2 (start = {0.0 for $i1 in 1:3})
(27)      [ALGB] (3) protected Real[3] DP_plot_2 = {DP_2[i] for i in 1:3}
(28)      [ALGB] (9) Real[3, 3] dp_IN_con_2.K = {K for $dp_IN_con_21 in 1:3}
(29)      [ALGB] (2) protected Real[2] DP_plot_1 = {DP_1[i] for i in 1:2}
(30)      [ALGB] (9) Real[3, 3] dp_IN_con_2.d_hyd = {d_hyd for $dp_IN_con_21 in 1:3} (min = {1e-15 for $dp_IN_con_21 in 1:3})
(31)      [ALGB] (4) Real[2, 2] m_flow_IN_con_1.d_hyd = {d_hyd for $m_flow_IN_con_11 in 1:2} (min = {1e-15 for $m_flow_IN_con_11 in 1:2})
(32)      [ALGB] (3) protected Real[3] Re_2 = {(d_hyd * 1000.0 * velocity_2[i]) / 0.001 for i in 1:3}
(33)      [ALGB] (4) Real[2, 2] dp_IN_con_1.R_0 = {R_0[$dp_IN_con_11] for $dp_IN_con_11 in 1:2} (min = {0.0 for $i1 in 1:2})
(34)      [ALGB] (4) Real[2, 2] dp_IN_con_1.d_hyd = {d_hyd for $dp_IN_con_11 in 1:2} (min = {1e-15 for $dp_IN_con_11 in 1:2})
(35)      [ALGB] (2) protected Real[2] Re_1 = {(d_hyd * 1000.0 * velocity_1[i]) / 0.001 for i in 1:2}
(36)      [ALGB] (9) Real[3, 3] m_flow_IN_con_2.d_hyd = {d_hyd for $m_flow_IN_con_21 in 1:3} (min = {1e-15 for $m_flow_IN_con_21 in 1:3})
(37)      [ALGB] (3) protected Real[3] velocity_2 = {input_mdot_2[i] / (A_cross * 1000.0) for i in 1:3}
(38)      [ALGB] (9) Real[3, 3] m_flow_IN_var_2.eta = {eta for $m_flow_IN_var_21 in 1:3} (min = {0.0 for $i1 in 1:3})
(39)      [ALGB] (2) protected Real[2] velocity_1 = {input_mdot_1[i] / (A_cross * 1000.0) for i in 1:2}
(40)      [DISC] (1) Boolean $TEV_1
(41)      [ALGB] (4) Real[2, 2] dp_IN_con_1.K = {K for $dp_IN_con_11 in 1:2}
(42)      [DISC] (1) Boolean $TEV_0
(43)      [ALGB] (9) Real[3, 3] dp_IN_var_2.eta = {eta for $dp_IN_var_21 in 1:3} (min = {0.0 for $i1 in 1:3})
(44)      [ALGB] (1) Real input_DP.y
(45)      [ALGB] (4) Real[2, 2] m_flow_IN_con_1.R_0 = {R_0[$m_flow_IN_con_11] for $m_flow_IN_con_11 in 1:2} (min = {0.0 for $i1 in 1:2})


System Equations (45/108)
***************************
(1)       [FOR-] (2) ($RES_BND_21)
(1)       [----] for $i1 in 1:2 loop
(1)       [----]   [SCAL] (1) m_flow_IN_con_1[$i1].R_0 = R_0[$i1] ($RES_BND_22)
(1)       [----] end for;
(2)       [FOR-] (2) ($RES_BND_23)
(2)       [----] for $i1 in 1:2 loop
(2)       [----]   [SCAL] (1) m_flow_IN_var_1[$i1].eta = 0.001 ($RES_BND_24)
(2)       [----] end for;
(3)       [FOR-] (2) ($RES_BND_25)
(3)       [----] for $i1 in 1:2 loop
(3)       [----]   [SCAL] (1) m_flow_IN_var_1[$i1].rho = 1000.0 ($RES_BND_26)
(3)       [----] end for;
(4)       [FOR-] (2) ($RES_BND_41)
(4)       [----] for $i1 in 1:2 loop
(4)       [----]   [SCAL] (1) dp_IN_con_1[$i1].delta = delta[3] ($RES_BND_42)
(4)       [----] end for;
(5)       [FOR-] (3) ($RES_BND_27)
(5)       [----] for $i1 in 1:3 loop
(5)       [----]   [SCAL] (1) m_flow_IN_con_2[$i1].d_hyd = d_hyd ($RES_BND_28)
(5)       [----] end for;
(6)       [FOR-] (2) ($RES_BND_43)
(6)       [----] for $i1 in 1:2 loop
(6)       [----]   [SCAL] (1) dp_IN_con_1[$i1].K = K ($RES_BND_44)
(6)       [----] end for;
(7)       [FOR-] (2) ($RES_$AUX_79)
(7)       [----] for $i1 in 1:2 loop
(7)       [----]   [SCAL] (1) $FUN_2[$i1] = abs(DP_plot_1[$i1]) ($RES_$AUX_80)
(7)       [----] end for;
(8)       [FOR-] (3) ($RES_BND_29)
(8)       [----] for $i1 in 1:3 loop
(8)       [----]   [SCAL] (1) m_flow_IN_con_2[$i1].delta = delta[$i1] ($RES_BND_30)
(8)       [----] end for;
(9)       [FOR-] (2) ($RES_BND_45)
(9)       [----] for $i1 in 1:2 loop
(9)       [----]   [SCAL] (1) dp_IN_con_1[$i1].R_0 = R_0[$i1] ($RES_BND_46)
(9)       [----] end for;
(10)      [FOR-] (3) ($RES_BND_61)
(10)      [----] for $i1 in 1:3 loop
(10)      [----]   [SCAL] (1) dp_IN_var_2[$i1].rho = 1000.0 ($RES_BND_62)
(10)      [----] end for;
(11)      [FOR-] (2) ($RES_BND_47)
(11)      [----] for $i1 in 1:2 loop
(11)      [----]   [SCAL] (1) dp_IN_var_1[$i1].eta = 0.001 ($RES_BND_48)
(11)      [----] end for;
(12)      [FOR-] (2) ($RES_BND_63)
(12)      [----] for $i1 in 1:2 loop
(12)      [----]   [SCAL] (1) velocity_1[$i1] = input_mdot_1[$i1] / (A_cross * 1000.0) ($RES_BND_64)
(12)      [----] end for;
(13)      [FOR-] (2) ($RES_BND_49)
(13)      [----] for $i1 in 1:2 loop
(13)      [----]   [SCAL] (1) dp_IN_var_1[$i1].rho = 1000.0 ($RES_BND_50)
(13)      [----] end for;
(14)      [FOR-] (2) ($RES_BND_65)
(14)      [----] for $i1 in 1:2 loop
(14)      [----]   [SCAL] (1) Re_1[$i1] = (d_hyd * 1000.0 * velocity_1[$i1]) / 0.001 ($RES_BND_66)
(14)      [----] end for;
(15)      [FOR-] (3) ($RES_BND_67)
(15)      [----] for $i1 in 1:3 loop
(15)      [----]   [SCAL] (1) velocity_2[$i1] = input_mdot_2[$i1] / (A_cross * 1000.0) ($RES_BND_68)
(15)      [----] end for;
(16)      [FOR-] (2) ($RES_BND_9)
(16)      [----] for $i1 in 1:2 loop
(16)      [----]   [SCAL] (1) DP_1[$i1] = input_dp_1[$i1] ($RES_BND_10)
(16)      [----] end for;
(17)      [FOR-] (3) ($RES_BND_69)
(17)      [----] for $i1 in 1:3 loop
(17)      [----]   [SCAL] (1) Re_2[$i1] = (d_hyd * 1000.0 * velocity_2[$i1]) / 0.001 ($RES_BND_70)
(17)      [----] end for;
(18)      [FOR-] (2) ($RES_BND_7)
(18)      [----] for $i1 in 1:2 loop
(18)      [----]   [SCAL] (1) input_dp_1[$i1] = input_DP.y ($RES_BND_8)
(18)      [----] end for;
(19)      [FOR-] (3) ($RES_BND_11)
(19)      [----] for $i1 in 1:3 loop
(19)      [----]   [SCAL] (1) input_dp_2[$i1] = input_DP.y ($RES_BND_12)
(19)      [----] end for;
(20)      [SCAL] (1) $TEV_0 = time < input_DP.startTime ($RES_EVT_83)
(21)      [SCAL] (1) $TEV_1 = time < (input_DP.startTime + input_DP.duration) ($RES_EVT_84)
(22)      [FOR-] (3) ($RES_BND_13)
(22)      [----] for $i1 in 1:3 loop
(22)      [----]   [SCAL] (1) DP_2[$i1] = input_dp_2[$i1] ($RES_BND_14)
(22)      [----] end for;
(23)      [FOR-] (2) ($RES_BND_15)
(23)      [----] for $i1 in 1:2 loop
(23)      [----]   [SCAL] (1) m_flow_IN_con_1[$i1].d_hyd = d_hyd ($RES_BND_16)
(23)      [----] end for;
(24)      [FOR-] (3) ($RES_$AUX_81)
(24)      [----] for $i1 in 1:3 loop
(24)      [----]   [SCAL] (1) $FUN_1[$i1] = abs(DP_plot_2[$i1]) ($RES_$AUX_82)
(24)      [----] end for;
(25)      [FOR-] (3) ($RES_BND_31)
(25)      [----] for $i1 in 1:3 loop
(25)      [----]   [SCAL] (1) m_flow_IN_con_2[$i1].K = K ($RES_BND_32)
(25)      [----] end for;
(26)      [FOR-] (2) ($RES_BND_17)
(26)      [----] for $i1 in 1:2 loop
(26)      [----]   [SCAL] (1) m_flow_IN_con_1[$i1].delta = 3.141592653589793 * delta[3] ($RES_BND_18)
(26)      [----] end for;
(27)      [FOR-] (3) ($RES_BND_33)
(27)      [----] for $i1 in 1:3 loop
(27)      [----]   [SCAL] (1) m_flow_IN_con_2[$i1].R_0 = 2.26 * d_hyd ($RES_BND_34)
(27)      [----] end for;
(28)      [FOR-] (2) ($RES_BND_19)
(28)      [----] for $i1 in 1:2 loop
(28)      [----]   [SCAL] (1) m_flow_IN_con_1[$i1].K = K ($RES_BND_20)
(28)      [----] end for;
(29)      [FOR-] (3) ($RES_BND_35)
(29)      [----] for $i1 in 1:3 loop
(29)      [----]   [SCAL] (1) m_flow_IN_var_2[$i1].eta = 0.001 ($RES_BND_36)
(29)      [----] end for;
(30)      [FOR-] (3) ($RES_BND_51)
(30)      [----] for $i1 in 1:3 loop
(30)      [----]   [SCAL] (1) dp_IN_con_2[$i1].d_hyd = d_hyd ($RES_BND_52)
(30)      [----] end for;
(31)      [FOR-] (3) ($RES_BND_37)
(31)      [----] for $i1 in 1:3 loop
(31)      [----]   [SCAL] (1) m_flow_IN_var_2[$i1].rho = 1000.0 ($RES_BND_38)
(31)      [----] end for;
(32)      [FOR-] (3) ($RES_BND_53)
(32)      [----] for $i1 in 1:3 loop
(32)      [----]   [SCAL] (1) dp_IN_con_2[$i1].delta = delta[$i1] ($RES_BND_54)
(32)      [----] end for;
(33)      [FOR-] (2) ($RES_BND_39)
(33)      [----] for $i1 in 1:2 loop
(33)      [----]   [SCAL] (1) dp_IN_con_1[$i1].d_hyd = d_hyd ($RES_BND_40)
(33)      [----] end for;
(34)      [FOR-] (3) ($RES_BND_55)
(34)      [----] for $i1 in 1:3 loop
(34)      [----]   [SCAL] (1) dp_IN_con_2[$i1].K = K ($RES_BND_56)
(34)      [----] end for;
(35)      [FOR-] (2) ($RES_BND_71)
(35)      [----] for $i1 in 1:2 loop
(35)      [----]   [SCAL] (1) DP_plot_1[$i1] = DP_1[$i1] ($RES_BND_72)
(35)      [----] end for;
(36)      [FOR-] (3) ($RES_BND_57)
(36)      [----] for $i1 in 1:3 loop
(36)      [----]   [SCAL] (1) dp_IN_con_2[$i1].R_0 = 2.26 * d_hyd ($RES_BND_58)
(36)      [----] end for;
(37)      [FOR-] (3) ($RES_BND_73)
(37)      [----] for $i1 in 1:3 loop
(37)      [----]   [SCAL] (1) DP_plot_2[$i1] = DP_2[$i1] ($RES_BND_74)
(37)      [----] end for;
(38)      [FOR-] (3) ($RES_BND_59)
(38)      [----] for $i1 in 1:3 loop
(38)      [----]   [SCAL] (1) dp_IN_var_2[$i1].eta = 0.001 ($RES_BND_60)
(38)      [----] end for;
(39)      [SCAL] (1) input_DP.y = input_DP.offset + (if $TEV_0 then 0.0 else if $TEV_1 then (input_DP.height * (time - input_DP.startTime)) / input_DP.duration else input_DP.height) ($RES_SIM_4)
(40)      [FOR-] (2) ($RES_BND_75)
(40)      [----] for $i1 in 1:2 loop
(40)      [----]   [SCAL] (1) zeta_TOT_1[$i1] = (2.0 * $FUN_2[$i1]) / max(1000.0 * velocity_1[$i1] ^ 2.0, 1e-5) ($RES_BND_76)
(40)      [----] end for;
(41)      [ARRY] (2) DP_1 = {Modelica.Fluid.Dissipation.PressureLoss.Bend.dp_curvedOverall_DP(m_flow_IN_con_1[i], m_flow_IN_var_1[i], input_mdot_1[i]) for i in 1:2} ($RES_SIM_3)
(42)      [ARRY] (2) M_FLOW_1 = {Modelica.Fluid.Dissipation.PressureLoss.Bend.dp_curvedOverall_MFLOW(dp_IN_con_1[i], dp_IN_var_1[i], input_dp_1[i]) for i in 1:2} ($RES_SIM_2)
(43)      [FOR-] (3) ($RES_BND_77)
(43)      [----] for $i1 in 1:3 loop
(43)      [----]   [SCAL] (1) zeta_TOT_2[$i1] = (2.0 * $FUN_1[$i1]) / max(1000.0 * velocity_2[$i1] ^ 2.0, 1e-5) ($RES_BND_78)
(43)      [----] end for;
(44)      [ARRY] (3) DP_2 = {Modelica.Fluid.Dissipation.PressureLoss.Bend.dp_curvedOverall_DP(m_flow_IN_con_2[i], m_flow_IN_var_2[i], input_mdot_2[i]) for i in 1:3} ($RES_SIM_1)
(45)      [ARRY] (3) M_FLOW_2 = {Modelica.Fluid.Dissipation.PressureLoss.Bend.dp_curvedOverall_MFLOW(dp_IN_con_2[i], dp_IN_var_2[i], input_dp_2[i]) for i in 1:3} ($RES_SIM_0)