Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries/ --ompython_omhome=/usr ThermoPower_ThermoPower.Test.WaterComponents.TestExpansionTankIdeal.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.WaterComponents.TestExpansionTankIdeal,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoPower_ThermoPower.Test.WaterComponents.TestExpansionTankIdeal") translateModel(ThermoPower.Test.WaterComponents.TestExpansionTankIdeal,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoPower_ThermoPower.Test.WaterComponents.TestExpansionTankIdeal") Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo): time 0.001194/0.001194, allocations: 103.4 kB / 17.64 MB, free: 5.379 MB / 14.72 MB Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo): time 0.001187/0.001187, allocations: 189.8 kB / 18.56 MB, free: 4.461 MB / 14.72 MB Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.2.3+maint.om/package.mo): time 1.398/1.398, 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 0.2808/0.2808, allocations: 48.85 MB / 320.6 MB, free: 11.1 MB / 270.1 MB Notification: Performance of FrontEnd - Absyn->SCode: time 1.94e-05/1.941e-05, allocations: 4.031 kB / 390.8 MB, free: 48.83 MB / 318.1 MB Notification: Performance of NFInst.instantiate(ThermoPower.Test.WaterComponents.TestExpansionTankIdeal): time 0.03135/0.03139, allocations: 45.39 MB / 436.2 MB, free: 7.289 MB / 318.1 MB Notification: Performance of NFInst.instExpressions: time 0.01064/0.04206, allocations: 11.57 MB / 447.7 MB, free: 11.71 MB / 334.1 MB Notification: Performance of NFInst.updateImplicitVariability: time 0.0005582/0.04265, allocations: 15.88 kB / 447.7 MB, free: 11.7 MB / 334.1 MB Notification: Performance of NFTyping.typeComponents: time 0.0008821/0.04354, allocations: 341.9 kB / 448.1 MB, free: 11.36 MB / 334.1 MB Notification: Performance of NFTyping.typeBindings: time 0.00129/0.04493, allocations: 0.6219 MB / 448.7 MB, free: 10.73 MB / 334.1 MB Notification: Performance of NFTyping.typeClassSections: time 0.009973/0.05492, allocations: 4.223 MB / 452.9 MB, free: 6.52 MB / 334.1 MB Notification: Performance of NFFlatten.flatten: time 0.003041/0.05797, allocations: 2.333 MB / 455.3 MB, free: 4.188 MB / 334.1 MB Notification: Performance of NFFlatten.resolveConnections: time 0.0009807/0.05896, allocations: 493 kB / 455.7 MB, free: 3.707 MB / 334.1 MB Notification: Performance of NFEvalConstants.evaluate: time 0.001497/0.06047, allocations: 0.7441 MB / 456.5 MB, free: 2.961 MB / 334.1 MB Notification: Performance of NFSimplifyModel.simplify: time 0.001117/0.06159, allocations: 0.6658 MB / 457.1 MB, free: 2.293 MB / 334.1 MB Notification: Performance of NFPackage.collectConstants: time 0.0001877/0.06179, allocations: 68 kB / 457.2 MB, free: 2.227 MB / 334.1 MB Notification: Performance of NFFlatten.collectFunctions: time 0.007726/0.06952, allocations: 5.717 MB / 462.9 MB, free: 12.5 MB / 350.1 MB Notification: Performance of combineBinaries: time 0.002096/0.07163, allocations: 1.591 MB / 464.5 MB, free: 10.9 MB / 350.1 MB Notification: Performance of replaceArrayConstructors: time 0.001166/0.07281, allocations: 1.032 MB / 465.5 MB, free: 9.855 MB / 350.1 MB Notification: Performance of NFVerifyModel.verify: time 0.000451/0.07327, allocations: 135.6 kB / 465.7 MB, free: 9.723 MB / 350.1 MB Notification: Performance of FrontEnd: time 0.0001299/0.07341, allocations: 19.94 kB / 465.7 MB, free: 9.703 MB / 350.1 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: 193 (133) * Number of variables: 173 (137) Notification: Performance of Bindings: time 0.005314/0.07873, allocations: 4.633 MB / 470.3 MB, free: 4.91 MB / 350.1 MB Notification: Performance of FunctionAlias: time 0.0005458/0.07928, allocations: 314.4 kB / 470.6 MB, free: 4.59 MB / 350.1 MB Notification: Performance of Early Inline: time 0.001217/0.08051, allocations: 0.6247 MB / 471.3 MB, free: 3.926 MB / 350.1 MB Notification: Performance of simplify1: time 0.0002824/0.0808, allocations: 167.8 kB / 471.4 MB, free: 3.762 MB / 350.1 MB Notification: Performance of Alias: time 0.002758/0.08357, allocations: 2.136 MB / 473.6 MB, free: 1.398 MB / 350.1 MB Notification: Performance of simplify2: time 0.0002362/0.08382, allocations: 139.8 kB / 473.7 MB, free: 1.262 MB / 350.1 MB Notification: Performance of Events: time 0.0003471/0.08417, allocations: 247.6 kB / 473.9 MB, free: 1.016 MB / 350.1 MB Notification: Performance of Detect States: time 0.0006456/0.08483, allocations: 0.5295 MB / 474.5 MB, free: 500 kB / 350.1 MB Notification: Performance of Partitioning: time 0.000975/0.08581, allocations: 0.7579 MB / 475.2 MB, free: 15.66 MB / 366.1 MB Error: Internal error NBSorting.tarjan failed to sort system: system vars Variables (110/146) ********************************* (1) [ALGB] (2) Real[2] heater.u (2) [ALGB] (1) Real[1] heater.heatTransfer.Tvol (start = {500.0 for $i1 in 1:1}, min = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}) (3) [ALGB] (1) Real[1] heater.Q_single (4) [ALGB] (2) Real[2] boiler.T (start = {500.0 for $i1 in 1:2}, min = {273.15 for $i1 in 1:2}, max = {2273.15 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2}) (5) [ALGB] (2) Real[2] boiler.fluidState.d (start = {150.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2}) (6) [ALGB] (1) Real[1] boiler.heatTransfer.Qw (7) [ALGB] (1) Real boiler.Q (8) [ALGB] (1) Real $FUN_14 (9) [ALGB] (1) stream Real boiler.infl.h_outflow (start = boiler.hstartin, min = -1e10, max = 1e10, nominal = 5e5) (10) [ALGB] (1) Real $FUN_13 (11) [ALGB] (2) Real[2] boiler.fluidState.h (start = {1e5 for $i1 in 1:2}, min = {-1e10 for $i1 in 1:2}, max = {1e10 for $i1 in 1:2}, nominal = {5e5 for $i1 in 1:2}) (12) [ALGB] (1) Real $FUN_11 (13) [ALGB] (1) Real boiler.M (min = 0.0) (14) [ALGB] (1) Real $FUN_10 (15) [ALGB] (1) Real[1] heater.heatTransfer.Qvol (16) [ALGB] (2) Real[2] heater.h (start = {heater.hstart[$h1] for $h1 in 1:2}, min = {-1e10 for $i1 in 1:2}, max = {1e10 for $i1 in 1:2}, nominal = {5e5 for $i1 in 1:2}) (17) [ALGB] (2) Real[2] boiler.fluidState.p (start = {5e6 for $i1 in 1:2}, min = {611.657 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2}) (18) [ALGB] (2) Real[2] boiler.heatTransfer.T (start = {500.0 for $i1 in 1:2}, min = {273.15 for $i1 in 1:2}, max = {2273.15 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2}) (19) [ALGB] (1) stream Real heater.infl.h_outflow (start = heater.hstartin, min = -1e10, max = 1e10, nominal = 5e5) (20) [ALGB] (1) Real heater.Tr (21) [ALGB] (1) Real[1] heater.wbar (start = {heater.wnom / heater.Nt}, min = {-1e5 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}) (22) [DER-] (1) Real[1] $DER.boiler.htilde (23) [ALGB] (1) protected Real[1] heater.vbar (min = {0.0 for $i1 in 1:1}) (24) [ALGB] (1) Real[1] boiler.wbar (start = {boiler.wnom / boiler.Nt}, min = {-1e5 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}) (25) [ALGB] (1) Real boiler.Dpfric (26) [ALGB] (2) Real[2] heater.T (start = {500.0 for $i1 in 1:2}, min = {273.15 for $i1 in 1:2}, max = {2273.15 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2}) (27) [ALGB] (1) protected Real[1] boiler.vbar (min = {0.0 for $i1 in 1:1}) (28) [ALGB] (1) Real[1] boiler.heatTransfer.Tw (start = {500.0 for $i1 in 1:1}, min = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}) (29) [ALGB] (1) flow Real[1] heatFlowSource.wall.Q (30) [ALGB] (2) final input Real[2] boiler.heatTransfer.fluidState.T = {boiler.fluidState[1].T, boiler.fluidState[2].T} (start = {500.0 for $i1 in 1:2}, min = {273.15 for $i1 in 1:2}, max = {2273.15 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2}) (31) [ALGB] (1) Real heater.Q (32) [DISC] (2) final input Integer[2] heater.heatTransfer.fluidState.phase = {heater.fluidState[1].phase, heater.fluidState[2].phase} (min = {0 for $i1 in 1:2}, max = {2 for $i1 in 1:2}) (33) [ALGB] (1) Real $FUN_8 (34) [ALGB] (1) Real heater.M (min = 0.0) (35) [ALGB] (1) Real $FUN_7 (36) [ALGB] (1) Real $FUN_6 (37) [ALGB] (1) Real $FUN_5 (38) [ALGB] (1) Real $FUN_3 (39) [ALGB] (1) Real $FUN_2 (40) [ALGB] (1) protected Real[1] boiler.rhobar (start = {150.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}) (41) [DISC] (2) Integer[2] boiler.fluidState.phase (min = {0 for $i1 in 1:2}, max = {2 for $i1 in 1:2}) (42) [ALGB] (1) Real boiler.Tr (43) [ALGB] (2) final input Real[2] boiler.heatTransfer.fluidState.d = {boiler.fluidState[1].d, boiler.fluidState[2].d} (start = {150.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2}) (44) [ALGB] (1) protected Real[1] boiler.drbdh (45) [ALGB] (2) final input Real[2] boiler.heatTransfer.fluidState.h = {boiler.fluidState[1].h, boiler.fluidState[2].h} (start = {1e5 for $i1 in 1:2}, min = {-1e10 for $i1 in 1:2}, max = {1e10 for $i1 in 1:2}, nominal = {5e5 for $i1 in 1:2}) (46) [ALGB] (1) Real[1] heater.heatTransfer.Qw (47) [ALGB] (1) Real heater.heatTransfer.w_wnom (48) [ALGB] (1) Real[1] boiler.heatTransfer.Qvol (49) [ALGB] (1) Real[1] boiler.Q_single (50) [ALGB] (1) flow Real boiler.outfl.m_flow (start = -boiler.wnom, min = -1e5, max = 0.0) (51) [ALGB] (1) flow Real[1] boiler.wall.Q (52) [ALGB] (1) protected Real[1] boiler.drbdp (53) [ALGB] (2) final input Real[2] heater.heatTransfer.fluidState.p = {heater.fluidState[1].p, heater.fluidState[2].p} (start = {5e6 for $i1 in 1:2}, min = {611.657 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2}) (54) [ALGB] (2) final input Real[2] boiler.heatTransfer.fluidState.p = {boiler.fluidState[1].p, boiler.fluidState[2].p} (start = {5e6 for $i1 in 1:2}, min = {611.657 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2}) (55) [DER-] (1) Real $DER.heater.p (56) [ALGB] (1) Real heater.Mtot (min = 0.0) (57) [ALGB] (1) Real[1] heater.dMdt (58) [ALGB] (1) flow Real[1] heater.wall.Q (59) [ALGB] (1) Real boiler.omega_hyd (60) [ALGB] (2) final input Real[2] heater.heatTransfer.fluidState.h = {heater.fluidState[1].h, heater.fluidState[2].h} (start = {1e5 for $i1 in 1:2}, min = {-1e10 for $i1 in 1:2}, max = {1e10 for $i1 in 1:2}, nominal = {5e5 for $i1 in 1:2}) (61) [ALGB] (1) Real boiler.Mtot (min = 0.0) (62) [ALGB] (1) Real[1] boiler.dMdt (63) [ALGB] (2) Real[2] heater.heatTransfer.T (start = {500.0 for $i1 in 1:2}, min = {273.15 for $i1 in 1:2}, max = {2273.15 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2}) (64) [ALGB] (2) final input Real[2] heater.heatTransfer.fluidState.d = {heater.fluidState[1].d, heater.fluidState[2].d} (start = {150.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2}) (65) [ALGB] (1) flow Real[1] temperatureSource.wall.Q (66) [ALGB] (1) stream Real boiler.outfl.h_outflow (start = boiler.hstartout, min = -1e10, max = 1e10, nominal = 5e5) (67) [ALGB] (1) Real heater.omega_hyd (68) [ALGB] (1) protected Real[1] heater.drbdh (69) [ALGB] (1) Real heater.Kf (70) [ALGB] (1) protected Real[1] heater.rhobar (start = {150.0 for $i1 in 1:1}, min = {0.0 for $i1 in 1:1}, max = {1e5 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}) (71) [ALGB] (1) Real[1] heater.heatTransfer.Tw (start = {500.0 for $i1 in 1:1}, min = {273.15 for $i1 in 1:1}, max = {2273.15 for $i1 in 1:1}, nominal = {500.0 for $i1 in 1:1}) (72) [ALGB] (1) protected Real[1] heater.drbdp (73) [ALGB] (2) protected Real[2] heater.drdh (74) [ALGB] (1) Real heater.Cf (75) [ALGB] (2) final input Real[2] heater.heatTransfer.fluidState.T = {heater.fluidState[1].T, heater.fluidState[2].T} (start = {500.0 for $i1 in 1:2}, min = {273.15 for $i1 in 1:2}, max = {2273.15 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2}) (76) [DISC] (1) Boolean $SEV_9 (77) [DISC] (1) Boolean $SEV_8 (78) [ALGB] (2) Real[2] boiler.rho (start = {150.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2}) (79) [DISC] (1) Boolean $SEV_7 (80) [ALGB] (2) protected Real[2] boiler.drdh (81) [DISC] (2) Integer[2] heater.fluidState.phase (min = {0 for $i1 in 1:2}, max = {2 for $i1 in 1:2}) (82) [DISC] (1) Boolean $SEV_6 (83) [DER-] (1) Real $DER.boiler.p (84) [ALGB] (1) flow Real expTankIdeal.WaterOutfl.m_flow (min = -1e5, max = 0.0) (85) [ALGB] (2) protected Real[2] heater.drdp (86) [DER-] (1) Real[1] $DER.heater.htilde (87) [ALGB] (1) Real heater.Dpfric (88) [ALGB] (1) Real boiler.w (start = boiler.wnom / boiler.Nt, min = -1e5, max = 1e5) (89) [ALGB] (2) Real[2] heater.fluidState.p (start = {5e6 for $i1 in 1:2}, min = {611.657 for $i1 in 1:2}, max = {1e8 for $i1 in 1:2}, nominal = {1e6 for $i1 in 1:2}) (90) [ALGB] (2) Real[2] boiler.u (91) [ALGB] (1) Real expTankIdeal.wn (min = -1e5, max = 1e5) (92) [ALGB] (2) protected Real[2] boiler.drdp (93) [ALGB] (1) Real boiler.Kf (94) [ALGB] (2) Real[2] heater.fluidState.h (start = {1e5 for $i1 in 1:2}, min = {-1e10 for $i1 in 1:2}, max = {1e10 for $i1 in 1:2}, nominal = {5e5 for $i1 in 1:2}) (95) [DISC] (1) Boolean $TEV_0 (96) [ALGB] (2) Real[2] heater.fluidState.d (start = {150.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2}) (97) [ALGB] (2) final Real[2] heater.heatTransfer.w (min = {-1e5 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}) (98) [ALGB] (1) Real boiler.Dpfric1 (99) [ALGB] (2) Real[2] boiler.h (start = {boiler.hstart[$h1] for $h1 in 1:2}, min = {-1e10 for $i1 in 1:2}, max = {1e10 for $i1 in 1:2}, nominal = {5e5 for $i1 in 1:2}) (100) [ALGB] (2) final Real[2] boiler.heatTransfer.w (min = {-1e5 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}) (101) [DISC] (2) final input Integer[2] boiler.heatTransfer.fluidState.phase = {boiler.fluidState[1].phase, boiler.fluidState[2].phase} (min = {0 for $i1 in 1:2}, max = {2 for $i1 in 1:2}) (102) [ALGB] (1) Real boiler.Cf (103) [ALGB] (1) Real heater.Dpfric1 (104) [ALGB] (2) Real[2] boiler.fluidState.T (start = {500.0 for $i1 in 1:2}, min = {273.15 for $i1 in 1:2}, max = {2273.15 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2}) (105) [ALGB] (1) Real boiler.wout (min = -1e5, max = 1e5) (106) [ALGB] (1) Real step.y (107) [ALGB] (2) Real[2] heater.rho (start = {150.0 for $i1 in 1:2}, min = {0.0 for $i1 in 1:2}, max = {1e5 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2}) (108) [ALGB] (2) Real[2] heater.fluidState.T (start = {500.0 for $i1 in 1:2}, min = {273.15 for $i1 in 1:2}, max = {2273.15 for $i1 in 1:2}, nominal = {500.0 for $i1 in 1:2}) (109) [ALGB] (1) stream Real heater.outfl.h_outflow (start = heater.hstartout, min = -1e10, max = 1e10, nominal = 5e5) (110) [ALGB] (1) Real heater.w (start = heater.wnom / heater.Nt, min = -1e5, max = 1e5) system eqns Equations (114/156) ********************************* (1) [SCAL] (1) heater.M = heater.A * $FUN_14 * heater.l ($RES_SIM_15) (2) [SCAL] (1) heater.Kf = (5.0 * heater.omega_hyd * heater.Cf) / heater.A ^ 3.0 ($RES_SIM_52) (3) [SCAL] (1) heater.h[2:2] = heater.htilde ($RES_SIM_17) (4) [SCAL] (1) heater.Kf = ((heater.rhonom * heater.dpnom) / (heater.wnom / heater.Nt) ^ 2.0) * heater.Kfc ($RES_SIM_53) (5) [SCAL] (1) heater.h[1] = boiler.outfl.h_outflow ($RES_SIM_18) (6) [SCAL] (1) heater.omega_hyd = (4.0 * heater.A) / heater.Dhyd ($RES_SIM_54) (7) [SCAL] (1) heater.outfl.h_outflow = heater.htilde[1] ($RES_SIM_19) (8) [FOR-] (2) ($RES_SIM_91) (8) [----] for j in 1:2 loop (8) [----] [SCAL] (1) boiler.u[j] = boiler.w / (boiler.A * boiler.rho[j]) ($RES_SIM_92) (8) [----] end for; (9) [SCAL] (1) heatFlowSource.wall.Q[1] + boiler.wall.Q[1] = 0.0 ($RES_SIM_139) (10) [SCAL] (1) (boiler.wbar[1] * (boiler.h[2] - boiler.h[1]) + boiler.rhobar[1] * boiler.l * boiler.A * $DER.boiler.htilde[1]) - boiler.l * boiler.A * $DER.boiler.p = boiler.Q_single[1] ($RES_SIM_93) (11) [FOR-] (2) ($RES_SIM_58) (11) [----] for j in 1:2 loop (11) [----] [SCAL] (1) heater.heatTransfer.T[j] = heater.heatTransfer.fluidState.h ($RES_SIM_59) (11) [----] end for; (12) [SCAL] (1) boiler.fluidState[j].phase = 0 ($RES_SIM_175) (13) [SCAL] (1) boiler.dMdt[1] = boiler.l * boiler.A * (boiler.drbdh[1] * $DER.boiler.htilde[1] + boiler.drbdp[1] * $DER.boiler.p) ($RES_SIM_94) (14) [SCAL] (1) boiler.fluidState[j].h = boiler.h[j] ($RES_SIM_176) (15) [SCAL] (1) boiler.rhobar[1] = 0.5 * (boiler.rho[1] + boiler.rho[2]) ($RES_SIM_95) (16) [SCAL] (1) boiler.fluidState[j].d = Modelica.Media.Water.IF97_Utilities.rho_ph(boiler.p, boiler.h[j], 0, 0) ($RES_SIM_177) (17) [SCAL] (1) boiler.drbdp[1] = 0.5 * (boiler.drdp[1] + boiler.drdp[2]) ($RES_SIM_96) (18) [SCAL] (1) boiler.fluidState[j].T = Modelica.Media.Water.IF97_Utilities.T_ph(boiler.p, boiler.h[j], 0, 0) ($RES_SIM_178) (19) [SCAL] (1) boiler.drbdh[1] = 0.5 * (boiler.drdh[1] + boiler.drdh[2]) ($RES_SIM_97) (20) [SCAL] (1) boiler.fluidState[j].p = boiler.p ($RES_SIM_179) (21) [SCAL] (1) boiler.vbar[1] = 1/boiler.rhobar[1] ($RES_SIM_98) (22) [SCAL] (1) boiler.wbar[1] = -(0.5 * boiler.dMdt[1] + $FUN_5 + expTankIdeal.WaterOutfl.m_flow / boiler.Nt) ($RES_SIM_99) (23) [SCAL] (1) heater.infl.h_outflow = heater.h[1] ($RES_SIM_20) (24) [ARRY] (2) boiler.heatTransfer.fluidState.phase = {boiler.fluidState[1].phase, boiler.fluidState[2].phase} ($RES_BND_150) (25) [SCAL] (1) boiler.Q = sum(boiler.heatTransfer.Qw) ($RES_$AUX_174) (26) [SCAL] (1) boiler.Dpfric = boiler.Dpfric1 ($RES_SIM_103) (27) [ARRY] (2) boiler.heatTransfer.fluidState.h = {boiler.fluidState[1].h, boiler.fluidState[2].h} ($RES_BND_151) (28) [SCAL] (1) $FUN_2 = sum(boiler.dMdt) ($RES_$AUX_173) (29) [SCAL] (1) (boiler.p + boiler.Dpfric) - expTankIdeal.pf = 0.0 ($RES_SIM_104) (30) [ARRY] (2) boiler.heatTransfer.fluidState.d = {boiler.fluidState[1].d, boiler.fluidState[2].d} ($RES_BND_152) (31) [SCAL] (1) $FUN_3 = sum(boiler.vbar) ($RES_$AUX_172) (32) [SCAL] (1) $FUN_2 = (boiler.outfl.m_flow - expTankIdeal.WaterOutfl.m_flow) / boiler.Nt ($RES_SIM_105) (33) [ARRY] (2) boiler.heatTransfer.fluidState.T = {boiler.fluidState[1].T, boiler.fluidState[2].T} ($RES_BND_153) (34) [SCAL] (1) boiler.Dpfric1 = homotopy((boiler.w * sqrt(boiler.w * boiler.w + (boiler.wnom / boiler.Nt) * boiler.wnf * ((boiler.wnom / boiler.Nt) * boiler.wnf))) * boiler.Kf * $FUN_3, (boiler.dpnom / (boiler.wnom / boiler.Nt)) * boiler.w) ($RES_$AUX_171) (35) [SCAL] (1) heater.wall.Q[1] + temperatureSource.wall.Q[1] = 0.0 ($RES_SIM_141) (36) [SCAL] (1) heater.w = -boiler.outfl.m_flow / heater.Nt ($RES_SIM_24) (37) [ARRY] (2) boiler.heatTransfer.fluidState.p = {boiler.fluidState[1].p, boiler.fluidState[2].p} ($RES_BND_154) (38) [SCAL] (1) $FUN_5 = sum(boiler.dMdt[1:0]) ($RES_$AUX_170) (39) [SCAL] (1) heater.heatTransfer.Tvol[1] = if not heater.heatTransfer.useAverageTemperature then heater.heatTransfer.T[2] else if not heater.heatTransfer.adaptiveAverageTemperature then 0.5 * (heater.heatTransfer.T[1] + heater.heatTransfer.T[2]) else 0.5 * (heater.heatTransfer.T[1] + heater.heatTransfer.T[2]) + (0.5 * (heater.heatTransfer.T[2] - heater.heatTransfer.T[1])) * $FUN_8 ($RES_SIM_60) (40) [SCAL] (1) heater.heatTransfer.Qw[1] = heater.heatTransfer.gamma * heater.heatTransfer.kc * heater.heatTransfer.l * heater.heatTransfer.omega * (heater.heatTransfer.Tw[1] - heater.heatTransfer.Tvol[1]) * heater.heatTransfer.Nt ($RES_SIM_61) (41) [SCAL] (1) boiler.Kf = (5.0 * boiler.omega_hyd * boiler.Cf) / boiler.A ^ 3.0 ($RES_SIM_108) (42) [ARRY] (2) heater.heatTransfer.fluidState.phase = {heater.fluidState[1].phase, heater.fluidState[2].phase} ($RES_BND_156) (43) [SCAL] (1) heater.heatTransfer.w_wnom = $FUN_7 / heater.heatTransfer.wnom ($RES_SIM_62) (44) [SCAL] (1) boiler.Kf = ((boiler.rhonom * boiler.dpnom) / (boiler.wnom / boiler.Nt) ^ 2.0) * boiler.Kfc ($RES_SIM_109) (45) [FOR-] (2) ($RES_SIM_27) (45) [----] for j in 1:2 loop (45) [----] [SCAL] (1) heater.T[j] = heater.fluidState.h ($RES_SIM_28) (45) [----] end for; (46) [ARRY] (2) heater.heatTransfer.fluidState.h = {heater.fluidState[1].h, heater.fluidState[2].h} ($RES_BND_157) (47) [ARRY] (1) heater.heatTransfer.Qvol = heater.heatTransfer.Qw ($RES_SIM_63) (48) [ARRY] (2) heater.heatTransfer.fluidState.d = {heater.fluidState[1].d, heater.fluidState[2].d} ($RES_BND_158) (49) [SCAL] (1) heater.fluidState[j].phase = 0 ($RES_SIM_180) (50) [ARRY] (2) heater.heatTransfer.w = heater.w * fill(1.0, 2) ($RES_SIM_64) (51) [SCAL] (1) heater.heatTransfer.Qw[1] - heater.wall.Q[1] = 0.0 ($RES_SIM_146) (52) [FOR-] (2) ($RES_SIM_29) (52) [----] for j in 1:2 loop (52) [----] [SCAL] (1) heater.rho[j] = heater.fluidState.d ($RES_SIM_30) (52) [----] end for; (53) [ARRY] (2) heater.heatTransfer.fluidState.T = {heater.fluidState[1].T, heater.fluidState[2].T} ($RES_BND_159) (54) [SCAL] (1) heater.fluidState[j].h = heater.h[j] ($RES_SIM_181) (55) [ARRY] (10) heater.heatTransfer.fluidState = heater.fluidState ($RES_SIM_65) (56) [SCAL] (1) heater.fluidState[j].d = Modelica.Media.Water.IF97_Utilities.rho_ph(heater.p, heater.h[j], 0, 0) ($RES_SIM_182) (57) [ARRY] (1) heater.Q_single = heater.heatTransfer.Qvol / heater.Nt ($RES_SIM_66) (58) [SCAL] (1) boiler.heatTransfer.Qw[1] - boiler.wall.Q[1] = 0.0 ($RES_SIM_148) (59) [SCAL] (1) heater.fluidState[j].T = Modelica.Media.Water.IF97_Utilities.T_ph(heater.p, heater.h[j], 0, 0) ($RES_SIM_183) (60) [SCAL] (1) heater.heatTransfer.Tw[1] = system.T_amb ($RES_SIM_67) (61) [SCAL] (1) heater.fluidState[j].p = heater.p ($RES_SIM_184) (62) [SCAL] (1) boiler.Tr = noEvent(boiler.M / max(boiler.w, 1e-15)) ($RES_SIM_69) (63) [SCAL] (1) $TEV_0 = time < step.startTime ($RES_EVT_185) (64) [SCAL] (1) $FUN_6 = sum(boiler.rhobar) ($RES_$AUX_169) (65) [SCAL] (1) $FUN_7 = abs(heater.heatTransfer.w[1]) ($RES_$AUX_168) (66) [SCAL] (1) $FUN_8 = exp(-heater.heatTransfer.w_wnom / heater.heatTransfer.sigma) ($RES_$AUX_167) (67) [SCAL] (1) boiler.omega_hyd = (4.0 * boiler.A) / boiler.Dhyd ($RES_SIM_110) (68) [SCAL] (1) heater.Q = sum(heater.heatTransfer.Qw) ($RES_$AUX_166) (69) [SCAL] (1) $FUN_10 = sum(heater.dMdt) ($RES_$AUX_165) (70) [ARRY] (2) heater.heatTransfer.fluidState.p = {heater.fluidState[1].p, heater.fluidState[2].p} ($RES_BND_160) (71) [SCAL] (1) $FUN_11 = sum(heater.vbar) ($RES_$AUX_164) (72) [FOR-] (2) ($RES_SIM_31) (72) [----] for j in 1:2 loop (72) [----] [SCAL] (1) heater.drdp[j] = Modelica.Media.Water.IF97_Utilities.ddph_props(heater.fluidState.phase, heater.fluidState.T, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(heater.fluidState.phase, heater.fluidState.T, heater.fluidState.p, 0)) ($RES_SIM_32) (72) [----] end for; (73) [SCAL] (1) heater.Dpfric1 = homotopy((heater.w * sqrt(heater.w * heater.w + (heater.wnom / heater.Nt) * heater.wnf * ((heater.wnom / heater.Nt) * heater.wnf))) * heater.Kf * $FUN_11, (heater.dpnom / (heater.wnom / heater.Nt)) * heater.w) ($RES_$AUX_163) (74) [FOR-] (2) ($RES_SIM_114) (74) [----] for j in 1:2 loop (74) [----] [SCAL] (1) boiler.heatTransfer.T[j] = boiler.heatTransfer.fluidState.h ($RES_SIM_115) (74) [----] end for; (75) [SCAL] (1) $FUN_13 = sum(heater.dMdt[1:0]) ($RES_$AUX_162) (76) [FOR-] (2) ($RES_SIM_33) (76) [----] for j in 1:2 loop (76) [----] [SCAL] (1) heater.drdh[j] = Modelica.Media.Water.IF97_Utilities.ddhp_props(heater.fluidState.phase, heater.fluidState.T, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(heater.fluidState.phase, heater.fluidState.T, heater.fluidState.p, 0)) ($RES_SIM_34) (76) [----] end for; (77) [SCAL] (1) $FUN_14 = sum(heater.rhobar) ($RES_$AUX_161) (78) [SCAL] (1) boiler.heatTransfer.Tw[1] = boiler.heatTransfer.T[2] ($RES_SIM_116) (79) [ARRY] (1) boiler.heatTransfer.Qvol = boiler.heatTransfer.Qw ($RES_SIM_117) (80) [SCAL] (1) boiler.Mtot = boiler.M * boiler.Nt ($RES_SIM_70) (81) [FOR-] (2) ($RES_SIM_35) (81) [----] for j in 1:2 loop (81) [----] [SCAL] (1) heater.u[j] = heater.w / (heater.A * heater.rho[j]) ($RES_SIM_36) (81) [----] end for; (82) [ARRY] (2) boiler.heatTransfer.w = boiler.w * fill(1.0, 2) ($RES_SIM_118) (83) [SCAL] (1) boiler.M = boiler.A * $FUN_6 * boiler.l ($RES_SIM_71) (84) [ARRY] (10) boiler.heatTransfer.fluidState = boiler.fluidState ($RES_SIM_119) (85) [SCAL] (1) (heater.wbar[1] * (heater.h[2] - heater.h[1]) + heater.rhobar[1] * heater.l * heater.A * $DER.heater.htilde[1]) - heater.l * heater.A * $DER.heater.p = heater.Q_single[1] ($RES_SIM_37) (86) [SCAL] (1) boiler.h[2:2] = boiler.htilde ($RES_SIM_73) (87) [SCAL] (1) heater.dMdt[1] = heater.l * heater.A * (heater.drbdh[1] * $DER.heater.htilde[1] + heater.drbdp[1] * $DER.heater.p) ($RES_SIM_38) (88) [SCAL] (1) boiler.h[1] = heater.outfl.h_outflow ($RES_SIM_74) (89) [SCAL] (1) heater.rhobar[1] = 0.5 * (heater.rho[1] + heater.rho[2]) ($RES_SIM_39) (90) [SCAL] (1) boiler.outfl.h_outflow = boiler.htilde[1] ($RES_SIM_75) (91) [SCAL] (1) boiler.infl.h_outflow = boiler.h[1] ($RES_SIM_76) (92) [SCAL] (1) boiler.wout = -boiler.outfl.m_flow / boiler.Nt ($RES_SIM_79) (93) [SCAL] (1) $SEV_6 = heater.w > (-heater.wnom * heater.wnm) ($RES_EVT_192) (94) [SCAL] (1) $SEV_7 = heater.Kf >= 0.0 ($RES_EVT_193) (95) [SCAL] (1) $SEV_8 = boiler.w > (-boiler.wnom * boiler.wnm) ($RES_EVT_194) (96) [SCAL] (1) $SEV_9 = boiler.Kf >= 0.0 ($RES_EVT_195) (97) [ARRY] (1) boiler.Q_single = boiler.heatTransfer.Qvol / boiler.Nt ($RES_SIM_120) (98) [SCAL] (1) heater.drbdp[1] = 0.5 * (heater.drdp[1] + heater.drdp[2]) ($RES_SIM_40) (99) [SCAL] (1) heater.drbdh[1] = 0.5 * (heater.drdh[1] + heater.drdh[2]) ($RES_SIM_41) (100) [SCAL] (1) heater.vbar[1] = 1/heater.rhobar[1] ($RES_SIM_42) (101) [SCAL] (1) heater.wbar[1] = -(0.5 * heater.dMdt[1] + $FUN_13 + boiler.outfl.m_flow / heater.Nt) ($RES_SIM_43) (102) [SCAL] (1) boiler.w = -expTankIdeal.WaterOutfl.m_flow / boiler.Nt ($RES_SIM_80) (103) [SCAL] (1) expTankIdeal.wn = idealPump.w0 + expTankIdeal.WaterOutfl.m_flow ($RES_SIM_127) (104) [SCAL] (1) heater.Dpfric = heater.Dpfric1 ($RES_SIM_47) (105) [FOR-] (2) ($RES_SIM_83) (105) [----] for j in 1:2 loop (105) [----] [SCAL] (1) boiler.T[j] = boiler.fluidState.h ($RES_SIM_84) (105) [----] end for; (106) [SCAL] (1) (heater.p + heater.Dpfric) - boiler.p = 0.0 ($RES_SIM_48) (107) [SCAL] (1) $FUN_10 = (-(boiler.outfl.m_flow + idealPump.w0)) / heater.Nt ($RES_SIM_49) (108) [FOR-] (2) ($RES_SIM_85) (108) [----] for j in 1:2 loop (108) [----] [SCAL] (1) boiler.rho[j] = boiler.fluidState.d ($RES_SIM_86) (108) [----] end for; (109) [FOR-] (2) ($RES_SIM_87) (109) [----] for j in 1:2 loop (109) [----] [SCAL] (1) boiler.drdp[j] = Modelica.Media.Water.IF97_Utilities.ddph_props(boiler.fluidState.phase, boiler.fluidState.T, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(boiler.fluidState.phase, boiler.fluidState.T, boiler.fluidState.p, 0)) ($RES_SIM_88) (109) [----] end for; (110) [FOR-] (2) ($RES_SIM_89) (110) [----] for j in 1:2 loop (110) [----] [SCAL] (1) boiler.drdh[j] = Modelica.Media.Water.IF97_Utilities.ddhp_props(boiler.fluidState.phase, boiler.fluidState.T, Modelica.Media.Water.IF97_Utilities.waterBaseProp_ph(boiler.fluidState.phase, boiler.fluidState.T, boiler.fluidState.p, 0)) ($RES_SIM_90) (110) [----] end for; (111) [SCAL] (1) step.y = step.offset + (if $TEV_0 then 0.0 else step.height) ($RES_SIM_10) (112) [SCAL] (1) heatFlowSource.wall.Q[1] = -step.y ($RES_SIM_11) (113) [SCAL] (1) heater.Tr = noEvent(heater.M / max(heater.w, 1e-15)) ($RES_SIM_13) (114) [SCAL] (1) heater.Mtot = heater.M * heater.Nt ($RES_SIM_14) =================== Scalar Matching =================== variable to equation ********************** var 1 --> eqn 108 var 2 --> eqn 109 var 3 --> eqn 46 var 4 --> eqn 80 var 5 --> eqn 143 var 6 --> eqn 144 var 7 --> eqn 18 var 8 --> eqn 118 var 9 --> eqn 81 var 10 --> eqn 28 var 11 --> eqn 104 var 12 --> eqn 129 var 13 --> eqn 101 var 14 --> eqn 117 var 15 --> eqn 116 var 16 --> eqn 95 var 17 --> eqn 112 var 18 --> eqn 146 var 19 --> eqn 57 var 20 --> eqn 68 var 21 --> eqn 3 var 22 --> eqn 22 var 23 --> eqn 115 var 24 --> eqn 99 var 25 --> eqn 100 var 26 --> eqn 25 var 27 --> eqn 155 var 28 --> eqn 139 var 29 --> eqn 11 var 30 --> eqn 138 var 31 --> eqn 24 var 32 --> eqn 33 var 33 --> eqn 53 var 34 --> eqn 54 var 35 --> eqn 23 var 36 --> eqn 105 var 37 --> eqn 154 var 38 --> eqn 114 var 39 --> eqn 39 var 40 --> eqn 91 var 41 --> eqn 50 var 42 --> eqn 78 var 43 --> eqn 89 var 44 --> eqn 1 var 45 --> eqn 88 var 46 --> eqn 87 var 47 --> eqn 45 var 48 --> eqn 36 var 49 --> eqn 37 var 50 --> eqn 17 var 51 --> eqn 14 var 52 --> eqn 113 var 53 --> eqn 85 var 54 --> eqn 35 var 55 --> eqn 34 var 56 --> eqn 21 var 57 --> eqn 31 var 58 --> eqn 30 var 59 --> eqn 47 var 60 --> eqn 51 var 61 --> eqn 106 var 62 --> eqn 135 var 63 --> eqn 42 var 64 --> eqn 10 var 65 --> eqn 19 var 66 --> eqn 77 var 67 --> eqn 76 var 68 --> eqn 44 var 69 --> eqn 43 var 70 --> eqn 125 var 71 --> eqn 156 var 72 --> eqn 92 var 73 --> eqn 63 var 74 --> eqn 90 var 75 --> eqn 75 var 76 --> eqn 56 var 77 --> eqn 107 var 78 --> eqn 32 var 79 --> eqn 12 var 80 --> eqn 13 var 81 --> eqn 59 var 82 --> eqn 74 var 83 --> eqn 41 var 84 --> eqn 5 var 85 --> eqn 6 var 86 --> eqn 137 var 87 --> eqn 4 var 88 --> eqn 127 var 89 --> eqn 83 var 90 --> eqn 136 var 91 --> eqn 102 var 92 --> eqn 103 var 93 --> eqn 2 var 94 --> eqn 73 var 95 --> eqn 72 var 96 --> eqn 134 var 97 --> eqn 133 var 98 --> eqn 147 var 99 --> eqn 148 var 100 --> eqn 132 var 101 --> eqn 151 var 102 --> eqn 152 var 103 --> eqn 60 var 104 --> eqn 49 var 105 --> eqn 131 var 106 --> eqn 15 var 107 --> eqn 140 var 108 --> eqn 96 var 109 --> eqn 97 var 110 --> eqn 123 var 111 --> eqn 145 var 112 --> eqn 40 var 113 --> eqn 71 var 114 --> eqn 70 var 115 --> eqn 8 var 116 --> eqn 9 var 117 --> eqn 141 var 118 --> eqn 149 var 119 --> eqn 150 var 120 --> eqn 52 var 121 --> eqn 55 var 122 --> eqn 69 var 123 --> eqn 86 var 124 --> eqn 79 var 125 --> eqn 58 var 126 --> eqn 62 var 127 --> eqn 61 var 128 --> eqn 29 var 129 --> eqn 16 var 130 --> eqn 124 var 131 --> eqn 111 var 132 --> eqn 110 var 133 --> eqn 27 var 134 --> eqn 26 var 135 --> eqn 48 var 136 --> eqn 142 var 137 --> eqn 20 var 138 --> eqn 38 var 139 --> eqn 130 var 140 --> eqn 153 var 141 --> eqn 64 var 142 --> eqn 65 var 143 --> eqn 67 var 144 --> eqn 66 var 145 --> eqn 7 var 146 --> eqn 98 equation to variable ********************** eqn 1 --> var 44 eqn 2 --> var 93 eqn 3 --> var 21 eqn 4 --> var 87 eqn 5 --> var 84 eqn 6 --> var 85 eqn 7 --> var 145 eqn 8 --> var 115 eqn 9 --> var 116 eqn 10 --> var 64 eqn 11 --> var 29 eqn 12 --> var 79 eqn 13 --> var 80 eqn 14 --> var 51 eqn 15 --> var 106 eqn 16 --> var 129 eqn 17 --> var 50 eqn 18 --> var 7 eqn 19 --> var 65 eqn 20 --> var 137 eqn 21 --> var 56 eqn 22 --> var 22 eqn 23 --> var 35 eqn 24 --> var 31 eqn 25 --> var 26 eqn 26 --> var 134 eqn 27 --> var 133 eqn 28 --> var 10 eqn 29 --> var 128 eqn 30 --> var 58 eqn 31 --> var 57 eqn 32 --> var 78 eqn 33 --> var 32 eqn 34 --> var 55 eqn 35 --> var 54 eqn 36 --> var 48 eqn 37 --> var 49 eqn 38 --> var 138 eqn 39 --> var 39 eqn 40 --> var 112 eqn 41 --> var 83 eqn 42 --> var 63 eqn 43 --> var 69 eqn 44 --> var 68 eqn 45 --> var 47 eqn 46 --> var 3 eqn 47 --> var 59 eqn 48 --> var 135 eqn 49 --> var 104 eqn 50 --> var 41 eqn 51 --> var 60 eqn 52 --> var 120 eqn 53 --> var 33 eqn 54 --> var 34 eqn 55 --> var 121 eqn 56 --> var 76 eqn 57 --> var 19 eqn 58 --> var 125 eqn 59 --> var 81 eqn 60 --> var 103 eqn 61 --> var 127 eqn 62 --> var 126 eqn 63 --> var 73 eqn 64 --> var 141 eqn 65 --> var 142 eqn 66 --> var 144 eqn 67 --> var 143 eqn 68 --> var 20 eqn 69 --> var 122 eqn 70 --> var 114 eqn 71 --> var 113 eqn 72 --> var 95 eqn 73 --> var 94 eqn 74 --> var 82 eqn 75 --> var 75 eqn 76 --> var 67 eqn 77 --> var 66 eqn 78 --> var 42 eqn 79 --> var 124 eqn 80 --> var 4 eqn 81 --> var 9 eqn 82 --> var -1 eqn 83 --> var 89 eqn 84 --> var -1 eqn 85 --> var 53 eqn 86 --> var 123 eqn 87 --> var 46 eqn 88 --> var 45 eqn 89 --> var 43 eqn 90 --> var 74 eqn 91 --> var 40 eqn 92 --> var 72 eqn 93 --> var -1 eqn 94 --> var -1 eqn 95 --> var 16 eqn 96 --> var 108 eqn 97 --> var 109 eqn 98 --> var 146 eqn 99 --> var 24 eqn 100 --> var 25 eqn 101 --> var 13 eqn 102 --> var 91 eqn 103 --> var 92 eqn 104 --> var 11 eqn 105 --> var 36 eqn 106 --> var 61 eqn 107 --> var 77 eqn 108 --> var 1 eqn 109 --> var 2 eqn 110 --> var 132 eqn 111 --> var 131 eqn 112 --> var 17 eqn 113 --> var 52 eqn 114 --> var 38 eqn 115 --> var 23 eqn 116 --> var 15 eqn 117 --> var 14 eqn 118 --> var 8 eqn 119 --> var -1 eqn 120 --> var -1 eqn 121 --> var -1 eqn 122 --> var -1 eqn 123 --> var 110 eqn 124 --> var 130 eqn 125 --> var 70 eqn 126 --> var -1 eqn 127 --> var 88 eqn 128 --> var -1 eqn 129 --> var 12 eqn 130 --> var 139 eqn 131 --> var 105 eqn 132 --> var 100 eqn 133 --> var 97 eqn 134 --> var 96 eqn 135 --> var 62 eqn 136 --> var 90 eqn 137 --> var 86 eqn 138 --> var 30 eqn 139 --> var 28 eqn 140 --> var 107 eqn 141 --> var 117 eqn 142 --> var 136 eqn 143 --> var 5 eqn 144 --> var 6 eqn 145 --> var 111 eqn 146 --> var 18 eqn 147 --> var 98 eqn 148 --> var 99 eqn 149 --> var 118 eqn 150 --> var 119 eqn 151 --> var 101 eqn 152 --> var 102 eqn 153 --> var 140 eqn 154 --> var 37 eqn 155 --> var 27 eqn 156 --> var 71