Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ModelicaTest_3.2.2_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 3.2.2+maint.om/package.mo", uses=false)
Using package ModelicaTest with version 3.2.2 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaTest 3.2.2+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_3.2.2_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_3.2.2_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 0.001272/0.001272, allocations: 105.8 kB / 16.42 MB, free: 6.512 MB / 14.72 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo): time 0.00122/0.00122, allocations: 187.2 kB / 17.35 MB, free: 5.754 MB / 14.72 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.2.3+maint.om/package.mo): time 1.262/1.262, allocations: 205.1 MB / 223.2 MB, free: 12.24 MB / 190.1 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaTest 3.2.2+maint.om/package.mo): time 0.1843/0.1843, allocations: 39.96 MB / 310.5 MB, free: 4.027 MB / 254.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 1.434e-05/1.434e-05, allocations: 2.281 kB / 436.4 MB, free: 11.78 MB / 318.1 MB
Notification: Performance of NFInst.instantiate(ModelicaTest.Fluid.Dissipation.Verifications.PressureLoss.Bend.dp_curvedOverall_DPMFLOW): time 0.002255/0.002277, allocations: 2.139 MB / 438.6 MB, free: 9.625 MB / 318.1 MB
Notification: Performance of NFInst.instExpressions: time 0.002038/0.004328, allocations: 1.89 MB / 440.5 MB, free: 7.723 MB / 318.1 MB
Notification: Performance of NFInst.updateImplicitVariability: time 6.288e-05/0.004402, allocations: 4 kB / 440.5 MB, free: 7.719 MB / 318.1 MB
Notification: Performance of NFTyping.typeComponents: time 0.0002182/0.004625, allocations: 67.61 kB / 440.5 MB, free: 7.652 MB / 318.1 MB
Notification: Performance of NFTyping.typeBindings: time 0.0002677/0.004901, allocations: 143.3 kB / 440.7 MB, free: 7.512 MB / 318.1 MB
Notification: Performance of NFTyping.typeClassSections: time 0.0007851/0.005709, allocations: 0.5726 MB / 441.2 MB, free: 6.941 MB / 318.1 MB
Notification: Performance of NFFlatten.flatten: time 0.0002763/0.005994, allocations: 366.7 kB / 441.6 MB, free: 6.582 MB / 318.1 MB
Notification: Performance of NFFlatten.resolveConnections: time 4.289e-05/0.006044, allocations: 13.45 kB / 441.6 MB, free: 6.566 MB / 318.1 MB
Notification: Performance of NFEvalConstants.evaluate: time 0.0001494/0.006199, allocations: 175.5 kB / 441.8 MB, free: 6.395 MB / 318.1 MB
Notification: Performance of NFSimplifyModel.simplify: time 0.0001616/0.006368, allocations: 195.3 kB / 442 MB, free: 6.203 MB / 318.1 MB
Notification: Performance of NFPackage.collectConstants: time 1.892e-05/0.006393, allocations: 8 kB / 442 MB, free: 6.195 MB / 318.1 MB
Notification: Performance of NFFlatten.collectFunctions: time 0.001242/0.00764, allocations: 1.603 MB / 443.6 MB, free: 4.59 MB / 318.1 MB
Notification: Performance of combineBinaries: time 0.0002349/0.007883, allocations: 416.4 kB / 444 MB, free: 4.18 MB / 318.1 MB
Notification: Performance of replaceArrayConstructors: time 0.000131/0.008021, allocations: 296.9 kB / 444.3 MB, free: 3.887 MB / 318.1 MB
Notification: Performance of NFVerifyModel.verify: time 3.412e-05/0.00806, allocations: 19.94 kB / 444.3 MB, free: 3.867 MB / 318.1 MB
Notification: Performance of FrontEnd: time 1.628e-05/0.008081, allocations: 4 kB / 444.3 MB, free: 3.863 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 0.001202/0.009288, allocations: 1.794 MB / 446.1 MB, free: 1.957 MB / 318.1 MB
Notification: Performance of FunctionAlias: time 0.0001246/0.009419, allocations: 91.8 kB / 446.2 MB, free: 1.867 MB / 318.1 MB
Notification: Performance of Early Inline: time 0.0004661/0.009893, allocations: 0.7642 MB / 446.9 MB, free: 1.074 MB / 318.1 MB
Notification: Performance of simplify1: time 1.542e-05/0.009915, allocations: 19.97 kB / 447 MB, free: 1.055 MB / 318.1 MB
Notification: Performance of Alias: time 0.0004177/0.01034, allocations: 428.6 kB / 447.4 MB, free: 0.582 MB / 318.1 MB
Notification: Performance of simplify2: time 1.113e-05/0.01036, allocations: 11.98 kB / 447.4 MB, free: 0.5703 MB / 318.1 MB
Notification: Performance of Events: time 7.636e-05/0.01044, allocations: 63.94 kB / 447.5 MB, free: 0.5078 MB / 318.1 MB
Notification: Performance of Detect States: time 0.0001255/0.01057, allocations: 162.2 kB / 447.6 MB, free: 340 kB / 318.1 MB
Notification: Performance of Partitioning: time 0.0001812/0.01076, allocations: 223.4 kB / 447.8 MB, free: 112 kB / 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)