Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr Chemical_Chemical.Obsolete.Examples.ExothermicReaction.conf.json loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo): time 0.001386/0.001386, allocations: 96.42 kB / 19.71 MB, free: 2.125 MB / 14.72 MB " [Timeout remaining time 180] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo): time 0.001525/0.001525, allocations: 210.4 kB / 23.01 MB, free: 4.93 MB / 14.72 MB " [Timeout remaining time 180] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo): time 1.293/1.293, allocations: 230.6 MB / 256.8 MB, free: 7.797 MB / 206.1 MB " [Timeout remaining time 179] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Chemical 2.0.0/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Chemical 2.0.0/package.mo): time 0.1192/0.1192, allocations: 23.88 MB / 337.1 MB, free: 10.96 MB / 270.1 MB " [Timeout remaining time 180] Using package Chemical with version 2.0.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Chemical 2.0.0/package.mo) Using package Modelica with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo) Using package Complex with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo) Using package ModelicaServices with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo) Running command: translateModel(Chemical.Obsolete.Examples.ExothermicReaction,tolerance=1e-06,outputFormat="empty",numberOfIntervals=2500,variableFilter="",fileNamePrefix="Chemical_Chemical.Obsolete.Examples.ExothermicReaction") translateModel(Chemical.Obsolete.Examples.ExothermicReaction,tolerance=1e-06,outputFormat="empty",numberOfIntervals=2500,variableFilter="",fileNamePrefix="Chemical_Chemical.Obsolete.Examples.ExothermicReaction") [Timeout 660] "Notification: Performance of FrontEnd - Absyn->SCode: time 1.923e-05/1.923e-05, allocations: 9.734 kB / 472.3 MB, free: 7.078 MB / 334.1 MB Notification: Performance of NFInst.instantiate(Chemical.Obsolete.Examples.ExothermicReaction): time 0.008583/0.008603, allocations: 7.589 MB / 479.9 MB, free: 15.45 MB / 350.1 MB Notification: Performance of NFInst.instExpressions: time 0.02315/0.03176, allocations: 20.51 MB / 0.4887 GB, free: 10.86 MB / 366.1 MB Notification: Performance of NFInst.updateImplicitVariability: time 0.0006862/0.03244, allocations: 31.75 kB / 0.4887 GB, free: 10.83 MB / 366.1 MB Notification: Performance of NFTyping.typeComponents: time 0.001067/0.03351, allocations: 472.3 kB / 0.4892 GB, free: 10.37 MB / 366.1 MB Notification: Performance of NFTyping.typeBindings: time 0.004044/0.03755, allocations: 2.044 MB / 0.4912 GB, free: 8.309 MB / 366.1 MB Notification: Performance of NFTyping.typeClassSections: time 0.006202/0.04375, allocations: 3.057 MB / 0.4941 GB, free: 5.234 MB / 366.1 MB Notification: Performance of NFFlatten.flatten: time 0.002747/0.0465, allocations: 2.937 MB / 0.497 GB, free: 2.285 MB / 366.1 MB Notification: Performance of NFFlatten.resolveConnections: time 0.001388/0.04789, allocations: 1.158 MB / 0.4981 GB, free: 1.078 MB / 366.1 MB Notification: Performance of NFEvalConstants.evaluate: time 0.001235/0.04912, allocations: 1.294 MB / 0.4994 GB, free: 15.78 MB / 382.1 MB Notification: Performance of NFSimplifyModel.simplify: time 0.001408/0.05053, allocations: 1.359 MB / 0.5007 GB, free: 14.42 MB / 382.1 MB Notification: Performance of NFPackage.collectConstants: time 0.0002846/0.05082, allocations: 212 kB / 0.5009 GB, free: 14.21 MB / 382.1 MB Notification: Performance of NFFlatten.collectFunctions: time 0.004738/0.05556, allocations: 2.539 MB / 0.5034 GB, free: 11.67 MB / 382.1 MB Notification: Performance of combineBinaries: time 0.003271/0.05883, allocations: 4.194 MB / 0.5075 GB, free: 7.438 MB / 382.1 MB Notification: Performance of replaceArrayConstructors: time 0.001505/0.06033, allocations: 2.348 MB / 0.5098 GB, free: 5.059 MB / 382.1 MB Notification: Performance of NFVerifyModel.verify: time 0.0002805/0.06061, allocations: 192 kB / 0.51 GB, free: 4.871 MB / 382.1 MB Notification: Performance of FrontEnd: time 0.0002259/0.06084, allocations: 83.8 kB / 0.5101 GB, free: 4.789 MB / 382.1 MB Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 455 (455) * Number of variables: 455 (455) Notification: Performance of [SIM] Bindings: time 0.1683/0.2291, allocations: 9.94 MB / 0.5198 GB, free: 25.84 MB / 382.1 MB Notification: Performance of [SIM] FunctionAlias: time 0.001776/0.2309, allocations: 1.568 MB / 0.5213 GB, free: 25.71 MB / 382.1 MB Notification: Performance of [SIM] Early Inline: time 0.008701/0.2396, allocations: 8.827 MB / 0.5299 GB, free: 23.09 MB / 382.1 MB Notification: Performance of [SIM] Simplify 1: time 0.002103/0.2417, allocations: 1.509 MB / 0.5314 GB, free: 22.36 MB / 382.1 MB Warning: NBAlias.setStartFixed: Alias set with conflicting unfixed start values detected. Use -d=dumprepl for more information. Notification: Performance of [SIM] Alias: time 0.009447/0.2511, allocations: 8.996 MB / 0.5402 GB, free: 18.23 MB / 382.1 MB Notification: Performance of [SIM] Simplify 2: time 0.001177/0.2523, allocations: 1.116 MB / 0.5413 GB, free: 17.68 MB / 382.1 MB Notification: Performance of [SIM] Remove Stream: time 0.0003422/0.2527, allocations: 376.1 kB / 0.5416 GB, free: 17.46 MB / 382.1 MB Notification: Performance of [SIM] Detect States: time 0.0007858/0.2534, allocations: 0.9753 MB / 0.5426 GB, free: 16.91 MB / 382.1 MB Notification: Performance of [SIM] Events: time 0.0002463/0.2537, allocations: 277.6 kB / 0.5429 GB, free: 16.8 MB / 382.1 MB Notification: Performance of [SIM] Partitioning: time 0.001425/0.2551, allocations: 1.794 MB / 0.5446 GB, free: 16.14 MB / 382.1 MB Error: Internal error NBSorting.tarjan failed to sort system: System Variables (193/193) **************************** (1|1) [DSTA] (1) protected Real H2O1.uPure (2|2) [DSTA] (1) Real $FUN_18 (3|3) [DSTA] (1) protected Real A.amountOfParticles (start = A.m_start * Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.specificAmountOfParticles(Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), system.T_ambient, system.p_ambient, 0.0, 0.0), min = 0.0) (4|4) [DSTA] (1) protected Real B.amountOfParticles (start = B.m_start * Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.specificAmountOfParticles(Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, -55000.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), system.T_ambient, system.p_ambient, 0.0, 0.0), min = 0.0) (5|5) [DSTA] (1) Real $FUN_16 (6|6) [DSTA] (1) flow Real[1] reaction.substrates.q (7|7) [DDER] (1) Real $DER.B.molarVolume (8|8) [DSTA] (1) Real B.q (9|9) [DSTA] (1) flow Real A.solution.Ij (min = 0.0, max = 1.0) (10|10) [DDER] (1) Real $DER.t (11|11) [DSTA] (1) Real A.q (12|12) [DSTA] (1) flow Real B.solution.Ij (min = 0.0, max = 1.0) (13|13) [DDER] (1) Real $DER.A.molarVolume (14|14) [DSTA] (1) Real H2O1.q (15|15) [DSTA] (1) protected Real thermal_isolated_solution.gibbsEnergy (16|16) [DSTA] (1) flow Real A.solution.dV (17|17) [DSTA] (1) flow Real B.solution.dV (18|18) [DSTA] (1) Real H2O1.port_a.u (19|19) [DSTA] (1) flow Real H2O1.solution.dV (20|20) [DSTA] (1) Real thermal_isolated_solution.volume (21|21) [DSTA] (1) flow Real[1] reaction.products.q (22|22) [DSTA] (1) protected Real H2O1.amountOfBaseMolecules (start = H2O1.m_start / H2O1.molarMassOfBaseMolecule, min = 0.0) (23|23) [DSTA] (1) flow Real A.solution.dH (24|24) [DSTA] (1) flow Real B.solution.dH (25|25) [DSTA] (1) flow Real H2O1.solution.Gj (26|26) [DSTA] (1) protected Real B.u0 (27|27) [DSTA] (1) Real B.port_a.u (28|28) [DSTA] (1) protected Real A.u0 (29|29) [DSTA] (1) Real A.port_a.u (30|30) [DSTA] (1) protected Real H2O1.amountOfSolution (min = 0.0) (31|31) [DSTA] (1) Real B.a (32|32) [DSTA] (1) Real H2O1.port_m.x_mass (min = 0.0, max = 1.0) (33|33) [DSTA] (1) Real A.a (34|34) [DSTA] (1) flow Real H2O1.solution.mj (min = 0.0) (35|35) [DSTA] (1) Real B.x (min = 0.0, max = 1.0) (36|36) [DSTA] (1) protected Real thermal_isolated_solution.ds (37|37) [DSTA] (1) Real A.x (min = 0.0, max = 1.0) (38|38) [DSTA] (1) flow Real H2O1.solution.Ij (min = 0.0, max = 1.0) (39|39) [DSTA] (1) protected Real H2O1.SelfClustering_K = exp(-(-(t * 32.845554 + 81.6348)) / (t * 8.31446261815324)) (min = 0.0, max = 1.0) (40|40) [ALGB] (1) protected Real A.SelfClustering_K = exp(-0.0 / (t * 8.31446261815324)) (min = 0.0, max = 1.0) (41|41) [ALGB] (1) protected Real B.SelfClustering_K = exp(-0.0 / (t * 8.31446261815324)) (min = 0.0, max = 1.0) (42|42) [DSTA] (1) stream Real[1] reaction.substrates.h_outflow (nominal = {2e4 for $f1 in 1:1}) (43|43) [DSTA] (1) Real $FUN_6 (44|44) [DSTA] (1) protected Real H2O1.amountOfParticles (start = H2O1.m_start * Chemical.Obsolete.Examples.ExothermicReaction.H2O1.stateOfMatter.specificAmountOfParticles(Chemical.Obsolete.Substances.Water_liquid(0.018015, 0.0, -227230.0, -285830.0, 1.0, 75.3, {\"http://www.vias.org/genchem/standard_enthalpies_table.html\"}, 0.0, 0.0, true, -81.6348, 32.845554, 1000.0), system.T_ambient, system.p_ambient, 0.0, 0.0), min = 0.0) (45|45) [DSTA] (1) Real $FUN_4 (46|46) [DSTA] (1) flow Real A.solution.Gj (47|47) [DSTA] (1) Real $FUN_3 (48|48) [DSTA] (1) flow Real B.solution.Gj (49|49) [DSTA] (1) Real $FUN_2 (50|50) [DSTA] (1) Real H2O1.x (min = 0.0, max = 1.0) (51|51) [DDER] (1) Real $DER.H2O1.amountOfBonds (52|52) [DSTA] (1) flow Real A.solution.mj (min = 0.0) (53|53) [DSTA] (1) flow Real B.solution.mj (min = 0.0) (54|54) [DSTA] (1) protected Real thermal_isolated_solution.volume_der (55|55) [DSTA] (1) Real H2O1.port_c.c (56|56) [DSTA] (1) Real[1] reaction.products.u (57|57) [DSTA] (1) Real reaction.rr (start = 0.0) (58|58) [DSTA] (1) Real $DER.H2O1.logn (59|59) [DSTA] (1) Real H2O1.a (60|60) [DSTA] (1) Real reaction.h_mix (nominal = 2e4) (61|61) [DSTA] (1) protected Real A.molarEntropyPure (62|62) [STAT] (1) protected Real B.molarEntropyPure (63|63) [DSTA] (1) protected Real H2O1.moleFractionBasedIonicStrength (min = 0.0, max = 0.0) (64|64) [DSTA] (1) Real B.port_c.c (65|65) [DSTA] (1) Real A.port_c.c (66|66) [DSTA] (1) Real H2O1.c (67|67) [DSTA] (1) protected Real H2O1.u0 (68|68) [DSTA] (1) protected Real B.uPure (69|69) [DSTA] (1) protected Real A.uPure (70|70) [DSTA] (1) protected Real thermal_isolated_solution.top_s (71|71) [DSTA] (1) Real B.c (72|72) [DSTA] (1) Real A.c (73|73) [DISC] (1) Boolean $SEV_3 (74|74) [DISC] (1) Boolean $SEV_2 (75|75) [DISC] (1) Boolean $SEV_1 (76|76) [DISC] (1) Boolean $SEV_0 (77|77) [DSTA] (1) protected Real reaction.du (78|78) [DSTA] (1) Real[1] reaction.substrates.u (79|79) [DDER] (1) Real $DER.H2O1.molarVolume (80|80) [DSTA] (1) flow Real H2O1.solution.Vj (81|81) [DSTA] (1) flow Real B.port_a.q (82|82) [DSTA] (1) Real B.port_m.x_mass (min = 0.0, max = 1.0) (83|83) [DSTA] (1) flow Real A.port_a.q (84|84) [DSTA] (1) Real A.port_m.x_mass (min = 0.0, max = 1.0) (85|85) [DSTA] (1) flow Real A.solution.Vj (86|86) [DSTA] (1) Real B.mass = B.amountOfParticles * B.molarMassOfBaseMolecule (min = 0.0) (87|87) [DSTA] (1) flow Real B.solution.Vj (88|88) [DSTA] (1) Real A.mass = A.amountOfParticles * A.molarMassOfBaseMolecule (min = 0.0) (89|89) [DSTA] (1) Real H2O1.mass = H2O1.amountOfBaseMolecules * H2O1.molarMassOfBaseMolecule (min = 0.0) (90|90) [DSTA] (1) Real $DER.A.logn (91|91) [DSTA] (1) Real $DER.B.logn (92|92) [DSTA] (1) protected Real H2O1.pressure (93|93) [DSTA] (1) Real thermal_isolated_solution.mass (min = 0.0, StateSelect = prefer) (94|94) [DSTA] (1) stream Real[1] reaction.products.h_outflow (nominal = {2e4 for $f1 in 1:1}) (95|95) [DSTA] (1) protected Real H2O1.molarEntropyPure (96|96) [DSTA] (1) flow Real H2O1.solution.dH (97|97) [DSTA] (1) protected Real H2O1.amountOfFreeMolecule (start = H2O1.m_start * Chemical.Obsolete.Examples.ExothermicReaction.H2O1.stateOfMatter.specificAmountOfFreeBaseMolecule(Chemical.Obsolete.Substances.Water_liquid(0.018015, 0.0, -227230.0, -285830.0, 1.0, 75.3, {\"http://www.vias.org/genchem/standard_enthalpies_table.html\"}, 0.0, 0.0, true, -81.6348, 32.845554, 1000.0), system.T_ambient, system.p_ambient, 0.0, 0.0, 1.0, 1.0), min = 0.0) (98|98) [DDER] (1) Real $DER.B.port_c.c (99|99) [DDER] (1) Real $DER.B.port_m.x_mass (100|100) [DDER] (1) Real $DER.A.molarEntropyPure (101|101) [DDER] (1) flow Real $DER.B.solution.Ij (102|102) [DDER] (1) Real $DER.A.port_c.c (103|103) [DDER] (1) Real $DER.thermal_isolated_solution.gibbsEnergy (104|104) [DDER] (1) flow Real $DER.B.solution.Vj (105|105) [DDER] (1) flow Real $DER.B.solution.mj (106|106) [DDER] (1) Real $DER.thermal_isolated_solution.volume_der (107|107) [DDER] (1) Real $DER.H2O1.uPure (108|108) [DDER] (1) Real $DER.H2O1.u0 (109|109) [DDER] (1) Real $DER.H2O1.molarEntropyPure (110|110) [DDER] (1) Real $DER.H2O1.mass (111|111) [DER-] (1) Real $DER.$DER.B.molarVolume (112|112) [DDER] (1) flow Real $DER.B.solution.dV (113|113) [DDER] (1) Real $DER.B.c (114|114) [DDER] (1) Real $DER.A.port_m.x_mass (115|115) [DDER] (1) Real $DER.$DER.B.logn (116|116) [DDER] (1) flow Real $DER.A.solution.Ij (117|117) [DDER] (1) flow Real $DER.A.solution.Vj (118|118) [DDER] (1) Real $DER.B.q (119|119) [DDER] (1) flow Real $DER.B.solution.dH (120|120) [DDER] (1) flow Real $DER.A.solution.mj (121|121) [DER-] (1) Real $DER.$DER.A.molarVolume (122|122) [DDER] (1) flow Real $DER.A.solution.dV (123|123) [DDER] (1) flow Real $DER.B.port_a.q (124|124) [DDER] (1) Real $DER.A.c (125|125) [DDER] (1) flow Real $DER.A.port_a.q (126|126) [DDER] (1) Real $DER.H2O1.port_c.c (127|127) [DDER] (1) Real $DER.thermal_isolated_solution.mass (128|128) [DDER] (1) Real $DER.H2O1.port_m.x_mass (129|129) [DDER] (1) flow Real $DER.H2O1.solution.Ij (130|130) [DDER] (1) Real $DER.H2O1.a (131|131) [DDER] (1) Real $DER.$FUN_18 (132|132) [DDER] (1) flow Real $DER.H2O1.solution.Vj (133|133) [DDER] (1) flow Real $DER.H2O1.solution.mj (134|134) [DER-] (1) Real $DER.$DER.H2O1.molarVolume (135|135) [DDER] (1) flow Real $DER.H2O1.solution.dV (136|136) [DDER] (1) flow Real $DER.B.solution.Gj (137|137) [DDER] (1) Real $DER.B.x (138|138) [DDER] (1) stream Real[1] $DER.reaction.products.h_outflow (139|139) [DDER] (1) Real $DER.$DER.A.logn (140|140) [DDER] (1) Real $DER.reaction.h_mix (141|141) [DDER] (1) flow Real[1] $DER.reaction.products.q (142|142) [DDER] (1) flow Real[1] $DER.reaction.substrates.q (143|143) [DDER] (1) stream Real[1] $DER.reaction.substrates.h_outflow (144|144) [DDER] (1) Real $DER.A.q (145|145) [DDER] (1) flow Real $DER.A.solution.dH (146|146) [DDER] (1) flow Real $DER.A.solution.Gj (147|147) [DDER] (1) Real $DER.thermal_isolated_solution.top_s (148|148) [DDER] (1) Real $DER.A.amountOfParticles (149|149) [DDER] (1) Real $DER.A.mass (150|150) [DDER] (1) Real $DER.H2O1.c (151|151) [DDER] (1) Real $DER.H2O1.q (152|152) [DDER] (1) Real $DER.$DER.H2O1.logn (153|153) [DDER] (1) Real $DER.H2O1.amountOfFreeMolecule (154|154) [DDER] (1) Real $DER.H2O1.amountOfParticles (155|155) [DDER] (1) Real $DER.$FUN_16 (156|156) [DDER] (1) Real $DER.H2O1.amountOfSolution (157|157) [DDER] (1) Real $DER.B.uPure (158|158) [DDER] (1) Real $DER.B.a (159|159) [DDER] (1) Real $DER.$FUN_6 (160|160) [DDER] (1) Real $DER.H2O1.SelfClustering_K (161|161) [DDER] (1) Real $DER.H2O1.x (162|162) [DDER] (1) Real $DER.B.u0 (163|163) [DER-] (1) Real $DER.$DER.H2O1.amountOfBonds (164|164) [DDER] (1) Real $DER.$DER.t (165|165) [DDER] (1) flow Real $DER.H2O1.solution.dH (166|166) [DER-] (1) Real $DER.B.molarEntropyPure (167|167) [DDER] (1) Real $DER.H2O1.port_a.u (168|168) [DDER] (1) Real $DER.H2O1.amountOfBaseMolecules (169|169) [DDER] (1) flow Real $DER.H2O1.solution.Gj (170|170) [DDER] (1) Real $DER.reaction.rr (171|171) [DDER] (1) Real $DER.$FUN_2 (172|172) [DDER] (1) Real $DER.A.x (173|173) [DDER] (1) Real $DER.A.a (174|174) [DDER] (1) Real $DER.A.uPure (175|175) [DDER] (1) Real $DER.H2O1.moleFractionBasedIonicStrength (176|176) [DDER] (1) Real $DER.A.u0 (177|177) [DDER] (1) Real $DER.H2O1.pressure (178|178) [DDER] (1) Real $DER.thermal_isolated_solution.volume (179|179) [DDER] (1) Real $DER.thermal_isolated_solution.ds (180|180) [DDER] (1) Real $DER.B.mass (181|181) [DDER] (1) Real $DER.B.port_a.u (182|182) [DDER] (1) Real[1] $DER.reaction.products.u (183|183) [DDER] (1) Real[1] $DER.reaction.substrates.u (184|184) [DDER] (1) Real $DER.A.port_a.u (185|185) [DDER] (1) Real $DER.B.amountOfParticles (186|186) [DDER] (1) Real $DER.$FUN_4 (187|187) [DDER] (1) Real $DER.reaction.du (188|188) [DDER] (1) Real $DER.$FUN_3 (189|189) [DSTA] (1) protected Real B.molarVolume (min = 0.0) (190|190) [DSTA] (1) protected Real A.molarVolume (min = 0.0) (191|191) [DSTA] (1) protected Real H2O1.molarVolume (min = 0.0) (192|192) [DSTA] (1) protected Real H2O1.amountOfBonds (min = 0.0) (193|193) [DSTA] (1) Real t (start = 288.15, min = 0.0, nominal = 300.0) System Equations (188/188) **************************** (1|1) [SCAL] (1) H2O1.port_a.u = 8.31446261815324 * t * $FUN_18 + (((-285830.0) + 75.3 * ((-298.15) + t)) - t * (((-196.54536307227906) + 75.3 * log(0.0033540164346805303 * t)) - (Chemical.Obsolete.Examples.ExothermicReaction.H2O1.stateOfMatter.molarVolumePure(Chemical.Obsolete.Substances.Water_liquid(0.018015, 0.0, -227230.0, -285830.0, 1.0, 75.3, {\"http://www.vias.org/genchem/standard_enthalpies_table.html\"}, 0.0, 0.0, true, -81.6348, 32.845554, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength) / t) * ((-1e5) + H2O1.pressure))) ($RES_SIM_15) (2|2) [SCAL] (1) $FUN_2 = log(A.a) ($RES_AUX_493) (3|3) [SCAL] (1) H2O1.a = H2O1.x ($RES_SIM_16) (4|4) [SCAL] (1) A.amountOfParticles = exp(A.logn) ($RES_AUX_494) (5|5) [SCAL] (1) H2O1.molarVolume = 1.8015e-5 + Chemical.Obsolete.Examples.ExothermicReaction.H2O1.stateOfMatter.molarVolumePure(Chemical.Obsolete.Substances.Water_liquid(0.018015, 0.0, -227230.0, -285830.0, 1.0, 75.3, {\"http://www.vias.org/genchem/standard_enthalpies_table.html\"}, 0.0, 0.0, true, -81.6348, 32.845554, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength) * log(Chemical.Obsolete.Examples.ExothermicReaction.H2O1.stateOfMatter.activityCoefficient(Chemical.Obsolete.Substances.Water_liquid(0.018015, 0.0, -227230.0, -285830.0, 1.0, 75.3, {\"http://www.vias.org/genchem/standard_enthalpies_table.html\"}, 0.0, 0.0, true, -81.6348, 32.845554, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength)) ($RES_SIM_19) (6|6) [SCAL] (1) B.port_c.c = B.amountOfParticles / thermal_isolated_solution.volume ($RES_SIM_212) (7|7) [SCAL] (1) B.port_m.x_mass = B.solution.mj / thermal_isolated_solution.mass ($RES_SIM_213) (8|8) [SCAL] (1) B.q = B.port_a.q ($RES_SIM_214) (9|9) [SCAL] (1) A.molarEntropyPure = -(1.8015280000000002e-5 / t) * ((-1e5) + H2O1.pressure) ($RES_SIM_250) (10|10) [SCAL] (1) B.solution.Ij = 0.0 ($RES_SIM_215) (11|11) [SCAL] (1) B.solution.Vj = B.amountOfParticles * B.molarVolume ($RES_SIM_217) (12|12) [SCAL] (1) B.solution.mj = B.amountOfParticles * B.molarMassOfBaseMolecule ($RES_SIM_218) (13|13) [SCAL] (1) (A.solution.Ij + B.solution.Ij + H2O1.solution.Ij) - H2O1.moleFractionBasedIonicStrength = 0.0 ($RES_SIM_331) (14|14) [SCAL] (1) A.port_c.c = A.amountOfParticles / thermal_isolated_solution.volume ($RES_SIM_259) (15|15) [SCAL] (1) (A.solution.Gj + B.solution.Gj + H2O1.solution.Gj) - thermal_isolated_solution.gibbsEnergy = 0.0 ($RES_SIM_333) (16|16) [SCAL] (1) (A.solution.Vj + B.solution.Vj + H2O1.solution.Vj) - thermal_isolated_solution.volume = 0.0 ($RES_SIM_334) (17|17) [SCAL] (1) (A.solution.mj + B.solution.mj + H2O1.solution.mj) - thermal_isolated_solution.mass = 0.0 ($RES_SIM_335) (18|18) [SCAL] (1) (A.amountOfParticles + B.amountOfParticles + H2O1.amountOfParticles) - H2O1.amountOfSolution = 0.0 ($RES_SIM_336) (19|19) [SCAL] (1) (A.solution.dV + B.solution.dV + H2O1.solution.dV) - thermal_isolated_solution.volume_der = 0.0 ($RES_SIM_338) (20|20) [SCAL] (1) A.solution.dH + B.solution.dH + H2O1.solution.dH = 0.0 ($RES_SIM_339) (21|21) [SCAL] (1) H2O1.uPure = Chemical.Obsolete.Examples.ExothermicReaction.H2O1.stateOfMatter.molarEnthalpyElectroneutral(Chemical.Obsolete.Substances.Water_liquid(0.018015, 0.0, -227230.0, -285830.0, 1.0, 75.3, {\"http://www.vias.org/genchem/standard_enthalpies_table.html\"}, 0.0, 0.0, true, -81.6348, 32.845554, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength) - t * Chemical.Obsolete.Examples.ExothermicReaction.H2O1.stateOfMatter.molarEntropyPure(Chemical.Obsolete.Substances.Water_liquid(0.018015, 0.0, -227230.0, -285830.0, 1.0, 75.3, {\"http://www.vias.org/genchem/standard_enthalpies_table.html\"}, 0.0, 0.0, true, -81.6348, 32.845554, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength) ($RES_SIM_20) (22|22) [SCAL] (1) H2O1.u0 = ((-285830.0) + 75.3 * ((-298.15) + t)) - t * (((-196.54536307227906) + 75.3 * log(0.0033540164346805303 * t)) - (Chemical.Obsolete.Examples.ExothermicReaction.H2O1.stateOfMatter.molarVolumePure(Chemical.Obsolete.Substances.Water_liquid(0.018015, 0.0, -227230.0, -285830.0, 1.0, 75.3, {\"http://www.vias.org/genchem/standard_enthalpies_table.html\"}, 0.0, 0.0, true, -81.6348, 32.845554, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength) / t) * ((-1e5) + H2O1.pressure)) ($RES_SIM_21) (23|23) [SCAL] (1) H2O1.molarEntropyPure = ((-196.54536307227906) + 75.3 * log(0.0033540164346805303 * t)) - (1.8015e-5 / t) * ((-1e5) + H2O1.pressure) ($RES_SIM_22) (24|24) [SCAL] (1) H2O1.mass = H2O1.amountOfBaseMolecules * H2O1.molarMassOfBaseMolecule ($RES_BND_468) (25|25) [SCAL] (1) B.solution.dV = B.molarVolume * B.q + $DER.B.molarVolume * B.amountOfParticles ($RES_SIM_220) (26|26) [SCAL] (1) B.c = B.amountOfParticles / thermal_isolated_solution.volume ($RES_SIM_222) (27|27) [SCAL] (1) B.x = B.amountOfParticles / H2O1.amountOfSolution ($RES_SIM_223) (28|28) [SCAL] (1) A.port_m.x_mass = A.solution.mj / thermal_isolated_solution.mass ($RES_SIM_260) (29|29) [SCAL] (1) $DER.B.logn = B.q / B.amountOfParticles ($RES_SIM_225) (30|30) [SCAL] (1) A.q = A.port_a.q ($RES_SIM_261) (31|31) [SCAL] (1) A.solution.Ij = 0.0 ($RES_SIM_262) (32|32) [SCAL] (1) A.solution.Vj = A.amountOfParticles * A.molarVolume ($RES_SIM_264) (33|33) [SCAL] (1) B.solution.dH = -(B.q * (if $SEV_3 then reaction.products[1].h_outflow else -55000.0) + 55000.0 * B.q) ($RES_SIM_229) (34|34) [SCAL] (1) A.solution.mj = A.amountOfParticles * A.molarMassOfBaseMolecule ($RES_SIM_265) (35|35) [SCAL] (1) A.solution.dV = A.molarVolume * A.q + $DER.A.molarVolume * A.amountOfParticles ($RES_SIM_267) (36|36) [SCAL] (1) B.port_a.q + reaction.products[1].q = 0.0 ($RES_SIM_340) (37|37) [SCAL] (1) $SEV_0 = A.port_a.q > 0.0 ($RES_EVT_498) (38|38) [SCAL] (1) A.c = A.amountOfParticles / thermal_isolated_solution.volume ($RES_SIM_269) (39|39) [SCAL] (1) $SEV_1 = reaction.rr > 0.0 ($RES_EVT_499) (40|40) [SCAL] (1) reaction.substrates[1].q + A.port_a.q = 0.0 ($RES_SIM_343) (41|41) [SCAL] (1) A.SelfClustering_K = exp(-0.0 / t / 8.31446261815324) ($RES_AUX_471) (42|42) [SCAL] (1) B.SelfClustering_K = exp(-0.0 / t / 8.31446261815324) ($RES_AUX_472) (43|43) [SCAL] (1) H2O1.port_c.c = H2O1.amountOfParticles / thermal_isolated_solution.volume ($RES_SIM_31) (44|44) [SCAL] (1) H2O1.port_m.x_mass = H2O1.solution.mj / thermal_isolated_solution.mass ($RES_SIM_32) (45|45) [SCAL] (1) H2O1.q = 0.0 ($RES_SIM_33) (46|46) [SCAL] (1) H2O1.SelfClustering_K = exp(-(t * 32.845554 + 81.6348) / (-t) / 8.31446261815324) ($RES_AUX_476) (47|47) [SCAL] (1) H2O1.solution.Ij = 0.0 ($RES_SIM_34) (48|48) [SCAL] (1) $FUN_18 = log(H2O1.a) ($RES_AUX_477) (49|49) [SCAL] (1) H2O1.amountOfBaseMolecules = exp(H2O1.logn) ($RES_AUX_478) (50|50) [SCAL] (1) H2O1.solution.Vj = H2O1.amountOfBaseMolecules * H2O1.molarVolume ($RES_SIM_36) (51|51) [SCAL] (1) $FUN_16 = sqrt((4.0 * H2O1.amountOfSolution * H2O1.SelfClustering_K) / H2O1.amountOfBaseMolecules + (H2O1.amountOfSolution / H2O1.amountOfBaseMolecules) ^ 2.0) ($RES_AUX_479) (52|52) [SCAL] (1) H2O1.solution.mj = H2O1.amountOfBaseMolecules * H2O1.molarMassOfBaseMolecule ($RES_SIM_37) (53|53) [SCAL] (1) H2O1.solution.dV = H2O1.molarVolume * H2O1.q + $DER.H2O1.molarVolume * H2O1.amountOfBaseMolecules ($RES_SIM_39) (54|54) [SCAL] (1) B.solution.Gj = B.amountOfParticles * B.port_a.u ($RES_SIM_230) (55|55) [-IF-] (1) ($RES_SIM_232) (55|55) [----] if $SEV_1 then (55|55) [----] [SCAL] (1) reaction.h_mix * (fill(1.0, 1))[1] * reaction.products[1].q = 0.0 ($RES_SIM_233) (55|55) [----] elseif $SEV_2 then (55|55) [----] [SCAL] (1) reaction.h_mix * (fill(1.0, 1))[1] * reaction.substrates[1].q - 55000.0 * reaction.products[1].q = 0.0 ($RES_SIM_234) (55|55) [----] else (55|55) [----] [SCAL] (1) reaction.h_mix = 0.0 ($RES_SIM_235) (55|55) [----] end if; (56|56) [SCAL] (1) $SEV_2 = reaction.rr < 0.0 ($RES_EVT_500) (57|57) [SCAL] (1) $SEV_3 = B.port_a.q > 0.0 ($RES_EVT_501) (58|58) [SCAL] (1) B.port_a.u = 8.31446261815324 * t * $FUN_6 + ((-55000.0) - t * ((-184.47090390742915) - (Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, -55000.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength) / t) * ((-1e5) + H2O1.pressure))) ($RES_SIM_196) (59|59) [SCAL] (1) A.x = A.amountOfParticles / H2O1.amountOfSolution ($RES_SIM_270) (60|60) [SCAL] (1) B.a = B.x ($RES_SIM_197) (61|61) [ARRY] (1) reaction.products.h_outflow = reaction.h_mix * fill(1.0, 1) ($RES_SIM_236) (62|62) [SCAL] (1) $DER.A.logn = A.q / A.amountOfParticles ($RES_SIM_272) (63|63) [ARRY] (1) reaction.substrates.h_outflow = reaction.h_mix * fill(1.0, 1) ($RES_SIM_237) (64|64) [ARRY] (1) reaction.rr * reaction.p = -reaction.products.q ($RES_SIM_238) (65|65) [ARRY] (1) reaction.rr * reaction.s = reaction.substrates.q ($RES_SIM_239) (66|66) [SCAL] (1) A.solution.dH = -A.q * (if $SEV_0 then reaction.substrates[1].h_outflow else 0.0) ($RES_SIM_276) (67|67) [SCAL] (1) A.solution.Gj = A.amountOfParticles * A.port_a.u ($RES_SIM_277) (68|68) [SCAL] (1) fixed2.s0 = thermal_isolated_solution.top_s - thermal_isolated_solution.ds ($RES_BND_445) (69|69) [SCAL] (1) A.mass = A.amountOfParticles * A.molarMassOfBaseMolecule ($RES_BND_447) (70|70) [SCAL] (1) H2O1.c = H2O1.amountOfParticles / thermal_isolated_solution.volume ($RES_SIM_41) (71|71) [SCAL] (1) H2O1.x = H2O1.amountOfFreeMolecule / H2O1.amountOfSolution ($RES_SIM_42) (72|72) [SCAL] (1) $DER.H2O1.logn = H2O1.q / H2O1.amountOfBaseMolecules ($RES_SIM_44) (73|73) [SCAL] (1) H2O1.amountOfParticles * (1.0 - H2O1.SelfClustering_K * H2O1.x) = H2O1.amountOfFreeMolecule ($RES_SIM_45) (74|74) [SCAL] (1) B.molarVolume = 1.8015280000000002e-5 + Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, -55000.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength) * log(Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.activityCoefficient(Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, -55000.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength)) ($RES_SIM_200) (75|75) [SCAL] (1) H2O1.x = (0.5 * ((H2O1.amountOfSolution / H2O1.amountOfBaseMolecules + 2.0 * H2O1.SelfClustering_K) - $FUN_16)) / H2O1.SelfClustering_K ^ 2.0 ($RES_SIM_46) (76|76) [SCAL] (1) B.uPure = Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.molarEnthalpyElectroneutral(Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, -55000.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength) - t * Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.molarEntropyPure(Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, -55000.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength) ($RES_SIM_201) (77|77) [SCAL] (1) $FUN_6 = log(B.a) ($RES_AUX_489) (78|78) [SCAL] (1) H2O1.amountOfBonds = H2O1.x * H2O1.amountOfBaseMolecules * H2O1.SelfClustering_K ($RES_SIM_47) (79|79) [SCAL] (1) B.u0 = (-55000.0) - t * ((-184.47090390742915) - (Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, -55000.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength) / t) * ((-1e5) + H2O1.pressure)) ($RES_SIM_202) (80|80) [SCAL] (1) H2O1.solution.dH = (75.3 * $DER.t) * H2O1.amountOfBaseMolecules - 81.6348 * $DER.H2O1.amountOfBonds ($RES_SIM_48) (81|81) [SCAL] (1) B.molarEntropyPure = (-184.47090390742915) - (1.8015280000000002e-5 / t) * ((-1e5) + H2O1.pressure) ($RES_SIM_203) (82|82) [SCAL] (1) H2O1.solution.Gj = H2O1.amountOfBaseMolecules * H2O1.port_a.u - H2O1.amountOfBonds * (t * 32.845554 + 81.6348) ($RES_SIM_49) (83|83) [SCAL] (1) reaction.rr = -reaction.du * reaction.KC * $FUN_4 ($RES_SIM_240) (84|84) [SCAL] (1) reaction.du = reaction.p[1] * reaction.products[1].u - reaction.s[1] * reaction.substrates[1].u ($RES_SIM_241) (85|85) [SCAL] (1) A.port_a.u = 8.31446261815324 * t * $FUN_2 + t * ((Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength) / t) * ((-1e5) + H2O1.pressure)) ($RES_SIM_243) (86|86) [SCAL] (1) A.a = A.x ($RES_SIM_244) (87|87) [SCAL] (1) A.molarVolume = 1.8015280000000002e-5 + Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength) * log(Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.activityCoefficient(Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength)) ($RES_SIM_247) (88|88) [SCAL] (1) A.uPure = Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.molarEnthalpyElectroneutral(Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength) - t * Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.molarEntropyPure(Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength) ($RES_SIM_248) (89|89) [SCAL] (1) A.u0 = t * ((Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength) / t) * ((-1e5) + H2O1.pressure)) ($RES_SIM_249) (90|90) [SCAL] (1) H2O1.pressure = thermal_isolated_solution.BasePressure ($RES_SIM_288) (91|91) [SCAL] (1) thermal_isolated_solution.ds = thermal_isolated_solution.volume / thermal_isolated_solution.SurfaceArea - thermal_isolated_solution.positionShift ($RES_SIM_289) (92|92) [SCAL] (1) B.mass = B.amountOfParticles * B.molarMassOfBaseMolecule ($RES_BND_450) (93|93) [SCAL] (1) reaction.products[1].u = B.port_a.u ($RES_SIM_405) (94|94) [SCAL] (1) A.port_a.u = reaction.substrates[1].u ($RES_SIM_406) (95|95) [SCAL] (1) B.amountOfParticles = exp(B.logn) ($RES_AUX_490) (96|96) [SCAL] (1) $FUN_4 = exp(-reaction.kE * $FUN_3) ($RES_AUX_491) (97|97) [SCAL] (1) $FUN_3 = abs(reaction.du) ($RES_AUX_492) (98|98) [SCAL] (1) $DER.H2O1.port_a.u = (8.31446261815324 * $DER.t * $FUN_18 + 8.31446261815324 * t * $DER.$FUN_18) + (75.3 * $DER.t - ($DER.t * (((-196.54536307227906) + 75.3 * log(0.0033540164346805303 * t)) - (Chemical.Obsolete.Examples.ExothermicReaction.H2O1.stateOfMatter.molarVolumePure(Chemical.Obsolete.Substances.Water_liquid(0.018015, 0.0, -227230.0, -285830.0, 1.0, 75.3, {\"http://www.vias.org/genchem/standard_enthalpies_table.html\"}, 0.0, 0.0, true, -81.6348, 32.845554, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength) / t) * ((-1e5) + H2O1.pressure)) + t * (75.3 * ((1/(0.0033540164346805303 * t)) * (0.0033540164346805303 * $DER.t)) - ((($fDER0.Chemical.Obsolete.Examples.ExothermicReaction.H2O1.stateOfMatter.molarVolumePure(Chemical.Obsolete.Substances.Water_liquid(0.018015, 0.0, -227230.0, -285830.0, 1.0, 75.3, {\"http://www.vias.org/genchem/standard_enthalpies_table.html\"}, 0.0, 0.0, true, -81.6348, 32.845554, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength, $DER.t, $DER.H2O1.pressure, 0.0, $DER.H2O1.moleFractionBasedIonicStrength) * t - $DER.t * Chemical.Obsolete.Examples.ExothermicReaction.H2O1.stateOfMatter.molarVolumePure(Chemical.Obsolete.Substances.Water_liquid(0.018015, 0.0, -227230.0, -285830.0, 1.0, 75.3, {\"http://www.vias.org/genchem/standard_enthalpies_table.html\"}, 0.0, 0.0, true, -81.6348, 32.845554, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength)) / t ^ 2.0) * ((-1e5) + H2O1.pressure) + (Chemical.Obsolete.Examples.ExothermicReaction.H2O1.stateOfMatter.molarVolumePure(Chemical.Obsolete.Substances.Water_liquid(0.018015, 0.0, -227230.0, -285830.0, 1.0, 75.3, {\"http://www.vias.org/genchem/standard_enthalpies_table.html\"}, 0.0, 0.0, true, -81.6348, 32.845554, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength) / t) * $DER.H2O1.pressure)))) ($RES_SIM_506) (99|99) [SCAL] (1) $DER.$FUN_2 = (1/A.a) * $DER.A.a ($RES_SIM_507) (100|100) [SCAL] (1) $DER.H2O1.a = $DER.H2O1.x ($RES_SIM_508) (101|101) [SCAL] (1) $DER.A.amountOfParticles = exp(A.logn) * $DER.A.logn ($RES_SIM_509) (102|102) [SCAL] (1) $DER.H2O1.molarVolume = $fDER0.Chemical.Obsolete.Examples.ExothermicReaction.H2O1.stateOfMatter.molarVolumePure(Chemical.Obsolete.Substances.Water_liquid(0.018015, 0.0, -227230.0, -285830.0, 1.0, 75.3, {\"http://www.vias.org/genchem/standard_enthalpies_table.html\"}, 0.0, 0.0, true, -81.6348, 32.845554, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength, $DER.t, $DER.H2O1.pressure, 0.0, $DER.H2O1.moleFractionBasedIonicStrength) * log(Chemical.Obsolete.Examples.ExothermicReaction.H2O1.stateOfMatter.activityCoefficient(Chemical.Obsolete.Substances.Water_liquid(0.018015, 0.0, -227230.0, -285830.0, 1.0, 75.3, {\"http://www.vias.org/genchem/standard_enthalpies_table.html\"}, 0.0, 0.0, true, -81.6348, 32.845554, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength)) + Chemical.Obsolete.Examples.ExothermicReaction.H2O1.stateOfMatter.molarVolumePure(Chemical.Obsolete.Substances.Water_liquid(0.018015, 0.0, -227230.0, -285830.0, 1.0, 75.3, {\"http://www.vias.org/genchem/standard_enthalpies_table.html\"}, 0.0, 0.0, true, -81.6348, 32.845554, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength) * ((1/Chemical.Obsolete.Examples.ExothermicReaction.H2O1.stateOfMatter.activityCoefficient(Chemical.Obsolete.Substances.Water_liquid(0.018015, 0.0, -227230.0, -285830.0, 1.0, 75.3, {\"http://www.vias.org/genchem/standard_enthalpies_table.html\"}, 0.0, 0.0, true, -81.6348, 32.845554, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength)) * $fDER0.Chemical.Obsolete.Examples.ExothermicReaction.H2O1.stateOfMatter.activityCoefficient(Chemical.Obsolete.Substances.Water_liquid(0.018015, 0.0, -227230.0, -285830.0, 1.0, 75.3, {\"http://www.vias.org/genchem/standard_enthalpies_table.html\"}, 0.0, 0.0, true, -81.6348, 32.845554, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength, $DER.t, $DER.H2O1.pressure, 0.0, $DER.H2O1.moleFractionBasedIonicStrength)) ($RES_SIM_510) (103|103) [SCAL] (1) $DER.B.port_c.c = ($DER.B.amountOfParticles * thermal_isolated_solution.volume - $DER.thermal_isolated_solution.volume * B.amountOfParticles) / thermal_isolated_solution.volume ^ 2.0 ($RES_SIM_511) (104|104) [SCAL] (1) $DER.B.port_m.x_mass = ($DER.B.solution.mj * thermal_isolated_solution.mass - $DER.thermal_isolated_solution.mass * B.solution.mj) / thermal_isolated_solution.mass ^ 2.0 ($RES_SIM_512) (105|105) [SCAL] (1) $DER.B.q = $DER.B.port_a.q ($RES_SIM_513) (106|106) [SCAL] (1) $DER.A.molarEntropyPure = -((1.8015280000000002e-5 / t) * $DER.H2O1.pressure - ((1.8015280000000002e-5 * $DER.t) / t ^ 2.0) * ((-1e5) + H2O1.pressure)) ($RES_SIM_514) (107|107) [SCAL] (1) $DER.B.solution.Ij = 0.0 ($RES_SIM_515) (108|108) [SCAL] (1) $DER.B.solution.Vj = $DER.B.amountOfParticles * B.molarVolume + B.amountOfParticles * $DER.B.molarVolume ($RES_SIM_516) (109|109) [SCAL] (1) $DER.B.solution.mj = $DER.B.amountOfParticles * B.molarMassOfBaseMolecule ($RES_SIM_517) (110|110) [SCAL] (1) ($DER.A.solution.Ij + $DER.B.solution.Ij + $DER.H2O1.solution.Ij) - $DER.H2O1.moleFractionBasedIonicStrength = 0.0 ($RES_SIM_518) (111|111) [SCAL] (1) $DER.A.port_c.c = ($DER.A.amountOfParticles * thermal_isolated_solution.volume - $DER.thermal_isolated_solution.volume * A.amountOfParticles) / thermal_isolated_solution.volume ^ 2.0 ($RES_SIM_519) (112|112) [SCAL] (1) ($DER.A.solution.Gj + $DER.B.solution.Gj + $DER.H2O1.solution.Gj) - $DER.thermal_isolated_solution.gibbsEnergy = 0.0 ($RES_SIM_520) (113|113) [SCAL] (1) ($DER.A.solution.Vj + $DER.B.solution.Vj + $DER.H2O1.solution.Vj) - $DER.thermal_isolated_solution.volume = 0.0 ($RES_SIM_521) (114|114) [SCAL] (1) ($DER.A.solution.mj + $DER.B.solution.mj + $DER.H2O1.solution.mj) - $DER.thermal_isolated_solution.mass = 0.0 ($RES_SIM_522) (115|115) [SCAL] (1) ($DER.A.amountOfParticles + $DER.B.amountOfParticles + $DER.H2O1.amountOfParticles) - $DER.H2O1.amountOfSolution = 0.0 ($RES_SIM_523) (116|116) [SCAL] (1) ($DER.A.solution.dV + $DER.B.solution.dV + $DER.H2O1.solution.dV) - $DER.thermal_isolated_solution.volume_der = 0.0 ($RES_SIM_524) (117|117) [SCAL] (1) $DER.A.solution.dH + $DER.B.solution.dH + $DER.H2O1.solution.dH = 0.0 ($RES_SIM_525) (118|118) [SCAL] (1) $DER.H2O1.uPure = $fDER0.Chemical.Obsolete.Examples.ExothermicReaction.H2O1.stateOfMatter.molarEnthalpyElectroneutral(Chemical.Obsolete.Substances.Water_liquid(0.018015, 0.0, -227230.0, -285830.0, 1.0, 75.3, {\"http://www.vias.org/genchem/standard_enthalpies_table.html\"}, 0.0, 0.0, true, -81.6348, 32.845554, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength, $DER.t, $DER.H2O1.pressure, 0.0, $DER.H2O1.moleFractionBasedIonicStrength) - ($DER.t * Chemical.Obsolete.Examples.ExothermicReaction.H2O1.stateOfMatter.molarEntropyPure(Chemical.Obsolete.Substances.Water_liquid(0.018015, 0.0, -227230.0, -285830.0, 1.0, 75.3, {\"http://www.vias.org/genchem/standard_enthalpies_table.html\"}, 0.0, 0.0, true, -81.6348, 32.845554, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength) + t * $fDER0.Chemical.Obsolete.Examples.ExothermicReaction.H2O1.stateOfMatter.molarEntropyPure(Chemical.Obsolete.Substances.Water_liquid(0.018015, 0.0, -227230.0, -285830.0, 1.0, 75.3, {\"http://www.vias.org/genchem/standard_enthalpies_table.html\"}, 0.0, 0.0, true, -81.6348, 32.845554, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength, $DER.t, $DER.H2O1.pressure, 0.0, $DER.H2O1.moleFractionBasedIonicStrength)) ($RES_SIM_526) (119|119) [SCAL] (1) $DER.H2O1.u0 = 75.3 * $DER.t - ($DER.t * (((-196.54536307227906) + 75.3 * log(0.0033540164346805303 * t)) - (Chemical.Obsolete.Examples.ExothermicReaction.H2O1.stateOfMatter.molarVolumePure(Chemical.Obsolete.Substances.Water_liquid(0.018015, 0.0, -227230.0, -285830.0, 1.0, 75.3, {\"http://www.vias.org/genchem/standard_enthalpies_table.html\"}, 0.0, 0.0, true, -81.6348, 32.845554, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength) / t) * ((-1e5) + H2O1.pressure)) + t * (75.3 * ((1/(0.0033540164346805303 * t)) * (0.0033540164346805303 * $DER.t)) - ((($fDER0.Chemical.Obsolete.Examples.ExothermicReaction.H2O1.stateOfMatter.molarVolumePure(Chemical.Obsolete.Substances.Water_liquid(0.018015, 0.0, -227230.0, -285830.0, 1.0, 75.3, {\"http://www.vias.org/genchem/standard_enthalpies_table.html\"}, 0.0, 0.0, true, -81.6348, 32.845554, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength, $DER.t, $DER.H2O1.pressure, 0.0, $DER.H2O1.moleFractionBasedIonicStrength) * t - $DER.t * Chemical.Obsolete.Examples.ExothermicReaction.H2O1.stateOfMatter.molarVolumePure(Chemical.Obsolete.Substances.Water_liquid(0.018015, 0.0, -227230.0, -285830.0, 1.0, 75.3, {\"http://www.vias.org/genchem/standard_enthalpies_table.html\"}, 0.0, 0.0, true, -81.6348, 32.845554, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength)) / t ^ 2.0) * ((-1e5) + H2O1.pressure) + (Chemical.Obsolete.Examples.ExothermicReaction.H2O1.stateOfMatter.molarVolumePure(Chemical.Obsolete.Substances.Water_liquid(0.018015, 0.0, -227230.0, -285830.0, 1.0, 75.3, {\"http://www.vias.org/genchem/standard_enthalpies_table.html\"}, 0.0, 0.0, true, -81.6348, 32.845554, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength) / t) * $DER.H2O1.pressure))) ($RES_SIM_527) (120|120) [SCAL] (1) $DER.H2O1.molarEntropyPure = 75.3 * ((1/(0.0033540164346805303 * t)) * (0.0033540164346805303 * $DER.t)) - ((1.8015e-5 / t) * $DER.H2O1.pressure - ((1.8015e-5 * $DER.t) / t ^ 2.0) * ((-1e5) + H2O1.pressure)) ($RES_SIM_528) (121|121) [SCAL] (1) $DER.H2O1.mass = $DER.H2O1.amountOfBaseMolecules * H2O1.molarMassOfBaseMolecule ($RES_SIM_529) (122|122) [SCAL] (1) $DER.B.solution.dV = ($DER.B.molarVolume * B.q + B.molarVolume * $DER.B.q) + ($DER.$DER.B.molarVolume * B.amountOfParticles + $DER.B.molarVolume * $DER.B.amountOfParticles) ($RES_SIM_530) (123|123) [SCAL] (1) $DER.B.c = ($DER.B.amountOfParticles * thermal_isolated_solution.volume - $DER.thermal_isolated_solution.volume * B.amountOfParticles) / thermal_isolated_solution.volume ^ 2.0 ($RES_SIM_531) (124|124) [SCAL] (1) $DER.B.x = ($DER.B.amountOfParticles * H2O1.amountOfSolution - $DER.H2O1.amountOfSolution * B.amountOfParticles) / H2O1.amountOfSolution ^ 2.0 ($RES_SIM_532) (125|125) [SCAL] (1) $DER.A.port_m.x_mass = ($DER.A.solution.mj * thermal_isolated_solution.mass - $DER.thermal_isolated_solution.mass * A.solution.mj) / thermal_isolated_solution.mass ^ 2.0 ($RES_SIM_533) (126|126) [SCAL] (1) $DER.$DER.B.logn = ($DER.B.q * B.amountOfParticles - $DER.B.amountOfParticles * B.q) / B.amountOfParticles ^ 2.0 ($RES_SIM_534) (127|127) [SCAL] (1) $DER.A.q = $DER.A.port_a.q ($RES_SIM_535) (128|128) [SCAL] (1) $DER.A.solution.Ij = 0.0 ($RES_SIM_536) (129|129) [SCAL] (1) $DER.A.solution.Vj = $DER.A.amountOfParticles * A.molarVolume + A.amountOfParticles * $DER.A.molarVolume ($RES_SIM_537) (130|130) [SCAL] (1) $DER.B.solution.dH = -(($DER.B.q * (if $SEV_3 then reaction.products[1].h_outflow else -55000.0) + B.q * (if $SEV_3 then $DER.reaction.products[1].h_outflow else 0.0)) + 55000.0 * $DER.B.q) ($RES_SIM_538) (131|131) [SCAL] (1) $DER.A.solution.mj = $DER.A.amountOfParticles * A.molarMassOfBaseMolecule ($RES_SIM_539) (132|132) [SCAL] (1) $DER.A.solution.dV = ($DER.A.molarVolume * A.q + A.molarVolume * $DER.A.q) + ($DER.$DER.A.molarVolume * A.amountOfParticles + $DER.A.molarVolume * $DER.A.amountOfParticles) ($RES_SIM_540) (133|133) [SCAL] (1) $DER.B.port_a.q + $DER.reaction.products[1].q = 0.0 ($RES_SIM_541) (134|134) [SCAL] (1) $DER.A.c = ($DER.A.amountOfParticles * thermal_isolated_solution.volume - $DER.thermal_isolated_solution.volume * A.amountOfParticles) / thermal_isolated_solution.volume ^ 2.0 ($RES_SIM_542) (135|135) [SCAL] (1) $DER.reaction.substrates[1].q + $DER.A.port_a.q = 0.0 ($RES_SIM_543) (136|136) [SCAL] (1) $DER.H2O1.port_c.c = ($DER.H2O1.amountOfParticles * thermal_isolated_solution.volume - $DER.thermal_isolated_solution.volume * H2O1.amountOfParticles) / thermal_isolated_solution.volume ^ 2.0 ($RES_SIM_544) (137|137) [SCAL] (1) $DER.H2O1.port_m.x_mass = ($DER.H2O1.solution.mj * thermal_isolated_solution.mass - $DER.thermal_isolated_solution.mass * H2O1.solution.mj) / thermal_isolated_solution.mass ^ 2.0 ($RES_SIM_545) (138|138) [SCAL] (1) $DER.H2O1.q = 0.0 ($RES_SIM_546) (139|139) [SCAL] (1) $DER.H2O1.SelfClustering_K = exp(-(t * 32.845554 + 81.6348) / (-t) / 8.31446261815324) * (0.014465439387523548 * (((t * 32.845554 + 81.6348) * (-$DER.t) - $DER.t * 32.845554 * (-t)) / (-t) ^ 2.0 * 8.31446261815324)) ($RES_SIM_547) (140|140) [SCAL] (1) $DER.H2O1.solution.Ij = 0.0 ($RES_SIM_548) (141|141) [SCAL] (1) $DER.$FUN_18 = (1/H2O1.a) * $DER.H2O1.a ($RES_SIM_549) (142|142) [SCAL] (1) $DER.H2O1.amountOfBaseMolecules = exp(H2O1.logn) * $DER.H2O1.logn ($RES_SIM_550) (143|143) [SCAL] (1) $DER.H2O1.solution.Vj = $DER.H2O1.amountOfBaseMolecules * H2O1.molarVolume + H2O1.amountOfBaseMolecules * $DER.H2O1.molarVolume ($RES_SIM_551) (144|144) [SCAL] (1) $DER.$FUN_16 = (0.5 / ((4.0 * H2O1.amountOfSolution * H2O1.SelfClustering_K) / H2O1.amountOfBaseMolecules + (H2O1.amountOfSolution / H2O1.amountOfBaseMolecules) ^ 2.0) ^ 0.5) * (((4.0 * $DER.H2O1.amountOfSolution * H2O1.SelfClustering_K + 4.0 * H2O1.amountOfSolution * $DER.H2O1.SelfClustering_K) * H2O1.amountOfBaseMolecules - 4.0 * $DER.H2O1.amountOfBaseMolecules * H2O1.amountOfSolution * H2O1.SelfClustering_K) / H2O1.amountOfBaseMolecules ^ 2.0 + 2.0 * (H2O1.amountOfSolution / H2O1.amountOfBaseMolecules) * ((H2O1.amountOfSolution * $DER.H2O1.amountOfBaseMolecules - $DER.H2O1.amountOfSolution * H2O1.amountOfBaseMolecules) / H2O1.amountOfBaseMolecules ^ 2.0)) ($RES_SIM_552) (145|145) [SCAL] (1) $DER.H2O1.solution.mj = $DER.H2O1.amountOfBaseMolecules * H2O1.molarMassOfBaseMolecule ($RES_SIM_553) (146|146) [SCAL] (1) $DER.H2O1.solution.dV = ($DER.H2O1.molarVolume * H2O1.q + H2O1.molarVolume * $DER.H2O1.q) + ($DER.$DER.H2O1.molarVolume * H2O1.amountOfBaseMolecules + $DER.H2O1.molarVolume * $DER.H2O1.amountOfBaseMolecules) ($RES_SIM_554) (147|147) [SCAL] (1) $DER.B.solution.Gj = $DER.B.amountOfParticles * B.port_a.u + B.amountOfParticles * $DER.B.port_a.u ($RES_SIM_555) (148|148) [-IF-] (1) ($RES_SIM_556) (148|148) [----] if $SEV_1 then (148|148) [----] [SCAL] (1) $DER.reaction.h_mix * (fill(1.0, 1))[1] * reaction.products[1].q + reaction.h_mix * (fill(0.0, 1))[1] * reaction.products[1].q + reaction.h_mix * (fill(1.0, 1))[1] * $DER.reaction.products[1].q = 0.0 ($RES_SIM_557) (148|148) [----] elseif $SEV_2 then (148|148) [----] [SCAL] (1) ($DER.reaction.h_mix * (fill(1.0, 1))[1] * reaction.substrates[1].q + reaction.h_mix * (fill(0.0, 1))[1] * reaction.substrates[1].q + reaction.h_mix * (fill(1.0, 1))[1] * $DER.reaction.substrates[1].q) - 55000.0 * $DER.reaction.products[1].q = 0.0 ($RES_SIM_558) (148|148) [----] else (148|148) [----] [SCAL] (1) $DER.reaction.h_mix = 0.0 ($RES_SIM_559) (148|148) [----] end if; (149|149) [SCAL] (1) $DER.B.port_a.u = (8.31446261815324 * $DER.t * $FUN_6 + 8.31446261815324 * t * $DER.$FUN_6) - ($DER.t * ((-184.47090390742915) - (Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, -55000.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength) / t) * ((-1e5) + H2O1.pressure)) - t * ((($fDER0.Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, -55000.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength, $DER.t, $DER.H2O1.pressure, 0.0, $DER.H2O1.moleFractionBasedIonicStrength) * t - $DER.t * Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, -55000.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength)) / t ^ 2.0) * ((-1e5) + H2O1.pressure) + (Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, -55000.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength) / t) * $DER.H2O1.pressure)) ($RES_SIM_560) (150|150) [SCAL] (1) $DER.A.x = ($DER.A.amountOfParticles * H2O1.amountOfSolution - $DER.H2O1.amountOfSolution * A.amountOfParticles) / H2O1.amountOfSolution ^ 2.0 ($RES_SIM_561) (151|151) [SCAL] (1) $DER.B.a = $DER.B.x ($RES_SIM_562) (152|152) [ARRY] (1) $DER.reaction.products.h_outflow = $DER.reaction.h_mix * fill(1.0, 1) .+ reaction.h_mix * fill(0.0, 1) ($RES_SIM_563) (153|153) [SCAL] (1) $DER.$DER.A.logn = ($DER.A.q * A.amountOfParticles - $DER.A.amountOfParticles * A.q) / A.amountOfParticles ^ 2.0 ($RES_SIM_564) (154|154) [ARRY] (1) $DER.reaction.substrates.h_outflow = $DER.reaction.h_mix * fill(1.0, 1) .+ reaction.h_mix * fill(0.0, 1) ($RES_SIM_565) (155|155) [ARRY] (1) $DER.reaction.rr * reaction.p = -$DER.reaction.products.q ($RES_SIM_566) (156|156) [ARRY] (1) $DER.reaction.rr * reaction.s = $DER.reaction.substrates.q ($RES_SIM_567) (157|157) [SCAL] (1) $DER.A.solution.dH = -($DER.A.q * (if $SEV_0 then reaction.substrates[1].h_outflow else 0.0) + A.q * (if $SEV_0 then $DER.reaction.substrates[1].h_outflow else 0.0)) ($RES_SIM_568) (158|158) [SCAL] (1) $DER.A.solution.Gj = $DER.A.amountOfParticles * A.port_a.u + A.amountOfParticles * $DER.A.port_a.u ($RES_SIM_569) (159|159) [SCAL] (1) 0.0 = $DER.thermal_isolated_solution.top_s - $DER.thermal_isolated_solution.ds ($RES_SIM_570) (160|160) [SCAL] (1) $DER.A.mass = $DER.A.amountOfParticles * A.molarMassOfBaseMolecule ($RES_SIM_571) (161|161) [SCAL] (1) $DER.H2O1.c = ($DER.H2O1.amountOfParticles * thermal_isolated_solution.volume - $DER.thermal_isolated_solution.volume * H2O1.amountOfParticles) / thermal_isolated_solution.volume ^ 2.0 ($RES_SIM_572) (162|162) [SCAL] (1) $DER.H2O1.x = ($DER.H2O1.amountOfFreeMolecule * H2O1.amountOfSolution - $DER.H2O1.amountOfSolution * H2O1.amountOfFreeMolecule) / H2O1.amountOfSolution ^ 2.0 ($RES_SIM_573) (163|163) [SCAL] (1) $DER.$DER.H2O1.logn = ($DER.H2O1.q * H2O1.amountOfBaseMolecules - $DER.H2O1.amountOfBaseMolecules * H2O1.q) / H2O1.amountOfBaseMolecules ^ 2.0 ($RES_SIM_574) (164|164) [SCAL] (1) $DER.H2O1.amountOfParticles * (1.0 - H2O1.SelfClustering_K * H2O1.x) - H2O1.amountOfParticles * ($DER.H2O1.SelfClustering_K * H2O1.x + H2O1.SelfClustering_K * $DER.H2O1.x) = $DER.H2O1.amountOfFreeMolecule ($RES_SIM_575) (165|165) [SCAL] (1) $DER.B.molarVolume = $fDER0.Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, -55000.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength, $DER.t, $DER.H2O1.pressure, 0.0, $DER.H2O1.moleFractionBasedIonicStrength) * log(Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.activityCoefficient(Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, -55000.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength)) + Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, -55000.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength) * ((1/Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.activityCoefficient(Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, -55000.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength)) * $fDER0.Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.activityCoefficient(Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, -55000.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength, $DER.t, $DER.H2O1.pressure, 0.0, $DER.H2O1.moleFractionBasedIonicStrength)) ($RES_SIM_576) (166|166) [SCAL] (1) $DER.H2O1.x = ((0.5 * ((($DER.H2O1.amountOfSolution * H2O1.amountOfBaseMolecules - $DER.H2O1.amountOfBaseMolecules * H2O1.amountOfSolution) / H2O1.amountOfBaseMolecules ^ 2.0 + 2.0 * $DER.H2O1.SelfClustering_K) - $DER.$FUN_16)) * H2O1.SelfClustering_K ^ 2.0 - 0.5 * (2.0 * H2O1.SelfClustering_K * $DER.H2O1.SelfClustering_K) * ((H2O1.amountOfSolution / H2O1.amountOfBaseMolecules + 2.0 * H2O1.SelfClustering_K) - $FUN_16)) / (H2O1.SelfClustering_K ^ 2.0) ^ 2.0 ($RES_SIM_577) (167|167) [SCAL] (1) $DER.B.uPure = $fDER0.Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.molarEnthalpyElectroneutral(Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, -55000.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength, $DER.t, $DER.H2O1.pressure, 0.0, $DER.H2O1.moleFractionBasedIonicStrength) - ($DER.t * Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.molarEntropyPure(Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, -55000.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength) + t * $fDER0.Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.molarEntropyPure(Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, -55000.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength, $DER.t, $DER.H2O1.pressure, 0.0, $DER.H2O1.moleFractionBasedIonicStrength)) ($RES_SIM_578) (168|168) [SCAL] (1) $DER.$FUN_6 = (1/B.a) * $DER.B.a ($RES_SIM_579) (169|169) [SCAL] (1) $DER.H2O1.amountOfBonds = $DER.H2O1.x * H2O1.amountOfBaseMolecules * H2O1.SelfClustering_K + H2O1.x * $DER.H2O1.amountOfBaseMolecules * H2O1.SelfClustering_K + H2O1.x * H2O1.amountOfBaseMolecules * $DER.H2O1.SelfClustering_K ($RES_SIM_580) (170|170) [SCAL] (1) $DER.B.u0 = -($DER.t * ((-184.47090390742915) - (Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, -55000.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength) / t) * ((-1e5) + H2O1.pressure)) - t * ((($fDER0.Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, -55000.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength, $DER.t, $DER.H2O1.pressure, 0.0, $DER.H2O1.moleFractionBasedIonicStrength) * t - $DER.t * Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, -55000.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength)) / t ^ 2.0) * ((-1e5) + H2O1.pressure) + (Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.ExothermicReaction.B.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, -55000.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength) / t) * $DER.H2O1.pressure)) ($RES_SIM_581) (171|171) [SCAL] (1) $DER.H2O1.solution.dH = ((75.3 * $DER.$DER.t) * H2O1.amountOfBaseMolecules + (75.3 * $DER.t) * $DER.H2O1.amountOfBaseMolecules) - 81.6348 * $DER.$DER.H2O1.amountOfBonds ($RES_SIM_582) (172|172) [SCAL] (1) $DER.B.molarEntropyPure = -((1.8015280000000002e-5 / t) * $DER.H2O1.pressure - ((1.8015280000000002e-5 * $DER.t) / t ^ 2.0) * ((-1e5) + H2O1.pressure)) ($RES_SIM_583) (173|173) [SCAL] (1) $DER.H2O1.solution.Gj = ($DER.H2O1.amountOfBaseMolecules * H2O1.port_a.u + H2O1.amountOfBaseMolecules * $DER.H2O1.port_a.u) - ($DER.H2O1.amountOfBonds * (t * 32.845554 + 81.6348) + H2O1.amountOfBonds * ($DER.t * 32.845554)) ($RES_SIM_584) (174|174) [SCAL] (1) $DER.reaction.rr = -($DER.reaction.du * reaction.KC * $FUN_4 + reaction.du * reaction.KC * $DER.$FUN_4) ($RES_SIM_585) (175|175) [SCAL] (1) $DER.reaction.du = reaction.p[1] * $DER.reaction.products[1].u - reaction.s[1] * $DER.reaction.substrates[1].u ($RES_SIM_586) (176|176) [SCAL] (1) $DER.A.port_a.u = (8.31446261815324 * $DER.t * $FUN_2 + 8.31446261815324 * t * $DER.$FUN_2) + ($DER.t * ((Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength) / t) * ((-1e5) + H2O1.pressure)) + t * ((($fDER0.Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength, $DER.t, $DER.H2O1.pressure, 0.0, $DER.H2O1.moleFractionBasedIonicStrength) * t - $DER.t * Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength)) / t ^ 2.0) * ((-1e5) + H2O1.pressure) + (Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength) / t) * $DER.H2O1.pressure)) ($RES_SIM_587) (177|177) [SCAL] (1) $DER.A.a = $DER.A.x ($RES_SIM_588) (178|178) [SCAL] (1) $DER.A.molarVolume = $fDER0.Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength, $DER.t, $DER.H2O1.pressure, 0.0, $DER.H2O1.moleFractionBasedIonicStrength) * log(Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.activityCoefficient(Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength)) + Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength) * ((1/Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.activityCoefficient(Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength)) * $fDER0.Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.activityCoefficient(Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength, $DER.t, $DER.H2O1.pressure, 0.0, $DER.H2O1.moleFractionBasedIonicStrength)) ($RES_SIM_589) (179|179) [SCAL] (1) $DER.A.uPure = $fDER0.Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.molarEnthalpyElectroneutral(Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength, $DER.t, $DER.H2O1.pressure, 0.0, $DER.H2O1.moleFractionBasedIonicStrength) - ($DER.t * Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.molarEntropyPure(Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength) + t * $fDER0.Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.molarEntropyPure(Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength, $DER.t, $DER.H2O1.pressure, 0.0, $DER.H2O1.moleFractionBasedIonicStrength)) ($RES_SIM_590) (180|180) [SCAL] (1) $DER.A.u0 = $DER.t * ((Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength) / t) * ((-1e5) + H2O1.pressure)) + t * ((($fDER0.Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength, $DER.t, $DER.H2O1.pressure, 0.0, $DER.H2O1.moleFractionBasedIonicStrength) * t - $DER.t * Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength)) / t ^ 2.0) * ((-1e5) + H2O1.pressure) + (Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.ExothermicReaction.A.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), t, H2O1.pressure, 0.0, H2O1.moleFractionBasedIonicStrength) / t) * $DER.H2O1.pressure) ($RES_SIM_591) (181|181) [SCAL] (1) $DER.H2O1.pressure = 0.0 ($RES_SIM_592) (182|182) [SCAL] (1) $DER.thermal_isolated_solution.ds = ($DER.thermal_isolated_solution.volume * thermal_isolated_solution.SurfaceArea) / thermal_isolated_solution.SurfaceArea ^ 2.0 ($RES_SIM_593) (183|183) [SCAL] (1) $DER.B.mass = $DER.B.amountOfParticles * B.molarMassOfBaseMolecule ($RES_SIM_594) (184|184) [SCAL] (1) $DER.reaction.products[1].u = $DER.B.port_a.u ($RES_SIM_595) (185|185) [SCAL] (1) $DER.A.port_a.u = $DER.reaction.substrates[1].u ($RES_SIM_596) (186|186) [SCAL] (1) $DER.B.amountOfParticles = exp(B.logn) * $DER.B.logn ($RES_SIM_597) (187|187) [SCAL] (1) $DER.$FUN_4 = -exp(-reaction.kE * $FUN_3) * (reaction.kE * $DER.$FUN_3) ($RES_SIM_598) (188|188) [SCAL] (1) $DER.$FUN_3 = sign(reaction.du) * $DER.reaction.du ($RES_SIM_599) =================== Scalar Matching =================== variable to equation ********************** var 1 --> eqn 21 var 2 --> eqn 48 var 3 --> eqn 4 var 4 --> eqn 95 var 5 --> eqn 75 var 6 --> eqn 65 var 7 --> eqn 165 var 8 --> eqn 8 var 9 --> eqn 31 var 10 --> eqn 102 var 11 --> eqn 30 var 12 --> eqn 10 var 13 --> eqn 178 var 14 --> eqn 45 var 15 --> eqn 15 var 16 --> eqn 35 var 17 --> eqn 25 var 18 --> eqn 1 var 19 --> eqn 53 var 20 --> eqn 16 var 21 --> eqn 64 var 22 --> eqn 49 var 23 --> eqn 66 var 24 --> eqn 33 var 25 --> eqn 82 var 26 --> eqn 79 var 27 --> eqn 58 var 28 --> eqn 89 var 29 --> eqn 85 var 30 --> eqn 51 var 31 --> eqn 60 var 32 --> eqn 44 var 33 --> eqn 86 var 34 --> eqn 52 var 35 --> eqn 27 var 36 --> eqn 91 var 37 --> eqn 59 var 38 --> eqn 47 var 39 --> eqn 46 var 40 --> eqn 41 var 41 --> eqn 42 var 42 --> eqn 63 var 43 --> eqn 77 var 44 --> eqn 18 var 45 --> eqn 96 var 46 --> eqn 67 var 47 --> eqn 97 var 48 --> eqn 54 var 49 --> eqn 2 var 50 --> eqn 73 var 51 --> eqn 80 var 52 --> eqn 34 var 53 --> eqn 12 var 54 --> eqn 19 var 55 --> eqn 43 var 56 --> eqn 93 var 57 --> eqn 83 var 58 --> eqn 72 var 59 --> eqn 3 var 60 --> eqn 55 var 61 --> eqn 9 var 62 --> eqn 81 var 63 --> eqn 13 var 64 --> eqn 6 var 65 --> eqn 14 var 66 --> eqn 70 var 67 --> eqn 22 var 68 --> eqn 76 var 69 --> eqn 88 var 70 --> eqn 68 var 71 --> eqn 26 var 72 --> eqn 38 var 73 --> eqn 57 var 74 --> eqn 56 var 75 --> eqn 39 var 76 --> eqn 37 var 77 --> eqn 84 var 78 --> eqn 94 var 79 --> eqn 143 var 80 --> eqn 50 var 81 --> eqn 36 var 82 --> eqn 7 var 83 --> eqn 40 var 84 --> eqn 28 var 85 --> eqn 32 var 86 --> eqn 92 var 87 --> eqn 11 var 88 --> eqn 69 var 89 --> eqn 24 var 90 --> eqn 62 var 91 --> eqn 29 var 92 --> eqn 90 var 93 --> eqn 17 var 94 --> eqn 61 var 95 --> eqn 23 var 96 --> eqn 20 var 97 --> eqn 71 var 98 --> eqn 103 var 99 --> eqn 104 var 100 --> eqn 106 var 101 --> eqn 107 var 102 --> eqn -1 var 103 --> eqn 112 var 104 --> eqn 108 var 105 --> eqn 109 var 106 --> eqn -1 var 107 --> eqn 118 var 108 --> eqn 119 var 109 --> eqn 120 var 110 --> eqn 121 var 111 --> eqn 122 var 112 --> eqn -1 var 113 --> eqn 123 var 114 --> eqn 125 var 115 --> eqn 126 var 116 --> eqn 128 var 117 --> eqn 129 var 118 --> eqn 105 var 119 --> eqn 130 var 120 --> eqn 131 var 121 --> eqn 132 var 122 --> eqn 116 var 123 --> eqn 133 var 124 --> eqn 134 var 125 --> eqn 135 var 126 --> eqn 136 var 127 --> eqn 114 var 128 --> eqn 137 var 129 --> eqn 140 var 130 --> eqn 100 var 131 --> eqn 141 var 132 --> eqn 113 var 133 --> eqn 145 var 134 --> eqn -1 var 135 --> eqn 146 var 136 --> eqn 147 var 137 --> eqn 124 var 138 --> eqn 152 var 139 --> eqn 153 var 140 --> eqn 148 var 141 --> eqn 155 var 142 --> eqn 156 var 143 --> eqn 154 var 144 --> eqn 127 var 145 --> eqn 157 var 146 --> eqn 158 var 147 --> eqn 159 var 148 --> eqn 101 var 149 --> eqn 160 var 150 --> eqn 161 var 151 --> eqn 138 var 152 --> eqn 163 var 153 --> eqn 164 var 154 --> eqn 115 var 155 --> eqn 144 var 156 --> eqn 166 var 157 --> eqn 167 var 158 --> eqn 151 var 159 --> eqn 168 var 160 --> eqn 169 var 161 --> eqn 162 var 162 --> eqn 170 var 163 --> eqn 171 var 164 --> eqn -1 var 165 --> eqn 117 var 166 --> eqn 172 var 167 --> eqn 98 var 168 --> eqn 142 var 169 --> eqn 173 var 170 --> eqn 174 var 171 --> eqn 99 var 172 --> eqn 150 var 173 --> eqn 177 var 174 --> eqn 179 var 175 --> eqn 110 var 176 --> eqn 180 var 177 --> eqn 181 var 178 --> eqn 111 var 179 --> eqn 182 var 180 --> eqn 183 var 181 --> eqn 149 var 182 --> eqn 184 var 183 --> eqn 185 var 184 --> eqn 176 var 185 --> eqn 186 var 186 --> eqn 187 var 187 --> eqn 175 var 188 --> eqn 188 var 189 --> eqn 74 var 190 --> eqn 87 var 191 --> eqn 5 var 192 --> eqn 78 var 193 --> eqn 139 equation to variable ********************** eqn 1 --> var 18 eqn 2 --> var 49 eqn 3 --> var 59 eqn 4 --> var 3 eqn 5 --> var 191 eqn 6 --> var 64 eqn 7 --> var 82 eqn 8 --> var 8 eqn 9 --> var 61 eqn 10 --> var 12 eqn 11 --> var 87 eqn 12 --> var 53 eqn 13 --> var 63 eqn 14 --> var 65 eqn 15 --> var 15 eqn 16 --> var 20 eqn 17 --> var 93 eqn 18 --> var 44 eqn 19 --> var 54 eqn 20 --> var 96 eqn 21 --> var 1 eqn 22 --> var 67 eqn 23 --> var 95 eqn 24 --> var 89 eqn 25 --> var 17 eqn 26 --> var 71 eqn 27 --> var 35 eqn 28 --> var 84 eqn 29 --> var 91 eqn 30 --> var 11 eqn 31 --> var 9 eqn 32 --> var 85 eqn 33 --> var 24 eqn 34 --> var 52 eqn 35 --> var 16 eqn 36 --> var 81 eqn 37 --> var 76 eqn 38 --> var 72 eqn 39 --> var 75 eqn 40 --> var 83 eqn 41 --> var 40 eqn 42 --> var 41 eqn 43 --> var 55 eqn 44 --> var 32 eqn 45 --> var 14 eqn 46 --> var 39 eqn 47 --> var 38 eqn 48 --> var 2 eqn 49 --> var 22 eqn 50 --> var 80 eqn 51 --> var 30 eqn 52 --> var 34 eqn 53 --> var 19 eqn 54 --> var 48 eqn 55 --> var 60 eqn 56 --> var 74 eqn 57 --> var 73 eqn 58 --> var 27 eqn 59 --> var 37 eqn 60 --> var 31 eqn 61 --> var 94 eqn 62 --> var 90 eqn 63 --> var 42 eqn 64 --> var 21 eqn 65 --> var 6 eqn 66 --> var 23 eqn 67 --> var 46 eqn 68 --> var 70 eqn 69 --> var 88 eqn 70 --> var 66 eqn 71 --> var 97 eqn 72 --> var 58 eqn 73 --> var 50 eqn 74 --> var 189 eqn 75 --> var 5 eqn 76 --> var 68 eqn 77 --> var 43 eqn 78 --> var 192 eqn 79 --> var 26 eqn 80 --> var 51 eqn 81 --> var 62 eqn 82 --> var 25 eqn 83 --> var 57 eqn 84 --> var 77 eqn 85 --> var 29 eqn 86 --> var 33 eqn 87 --> var 190 eqn 88 --> var 69 eqn 89 --> var 28 eqn 90 --> var 92 eqn 91 --> var 36 eqn 92 --> var 86 eqn 93 --> var 56 eqn 94 --> var 78 eqn 95 --> var 4 eqn 96 --> var 45 eqn 97 --> var 47 eqn 98 --> var 167 eqn 99 --> var 171 eqn 100 --> var 130 eqn 101 --> var 148 eqn 102 --> var 10 eqn 103 --> var 98 eqn 104 --> var 99 eqn 105 --> var 118 eqn 106 --> var 100 eqn 107 --> var 101 eqn 108 --> var 104 eqn 109 --> var 105 eqn 110 --> var 175 eqn 111 --> var 178 eqn 112 --> var 103 eqn 113 --> var 132 eqn 114 --> var 127 eqn 115 --> var 154 eqn 116 --> var 122 eqn 117 --> var 165 eqn 118 --> var 107 eqn 119 --> var 108 eqn 120 --> var 109 eqn 121 --> var 110 eqn 122 --> var 111 eqn 123 --> var 113 eqn 124 --> var 137 eqn 125 --> var 114 eqn 126 --> var 115 eqn 127 --> var 144 eqn 128 --> var 116 eqn 129 --> var 117 eqn 130 --> var 119 eqn 131 --> var 120 eqn 132 --> var 121 eqn 133 --> var 123 eqn 134 --> var 124 eqn 135 --> var 125 eqn 136 --> var 126 eqn 137 --> var 128 eqn 138 --> var 151 eqn 139 --> var 193 eqn 140 --> var 129 eqn 141 --> var 131 eqn 142 --> var 168 eqn 143 --> var 79 eqn 144 --> var 155 eqn 145 --> var 133 eqn 146 --> var 135 eqn 147 --> var 136 eqn 148 --> var 140 eqn 149 --> var 181 eqn 150 --> var 172 eqn 151 --> var 158 eqn 152 --> var 138 eqn 153 --> var 139 eqn 154 --> var 143 eqn 155 --> var 141 eqn 156 --> var 142 eqn 157 --> var 145 eqn 158 --> var 146 eqn 159 --> var 147 eqn 160 --> var 149 eqn 161 --> var 150 eqn 162 --> var 161 eqn 163 --> var 152 eqn 164 --> var 153 eqn 165 --> var 7 eqn 166 --> var 156 eqn 167 --> var 157 eqn 168 --> var 159 eqn 169 --> var 160 eqn 170 --> var 162 eqn 171 --> var 163 eqn 172 --> var 166 eqn 173 --> var 169 eqn 174 --> var 170 eqn 175 --> var 187 eqn 176 --> var 184 eqn 177 --> var 173 eqn 178 --> var 13 eqn 179 --> var 174 eqn 180 --> var 176 eqn 181 --> var 177 eqn 182 --> var 179 eqn 183 --> var 180 eqn 184 --> var 182 eqn 185 --> var 183 eqn 186 --> var 185 eqn 187 --> var 186 eqn 188 --> var 188 " [Timeout remaining time 660] [Calling sys.exit(0), Time elapsed: 2.45597190503031] Failed to read output from testmodel.py, exit status != 0: 0.278782285284251 0.291484461 0.22791433600000002 Calling exit ...