Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr Chemical_master_Chemical.Obsolete.Examples.SimpleReaction2.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 0.001216/0.001216, allocations: 100.4 kB / 19.72 MB, free: 2.121 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 0.001227/0.001227, allocations: 213.2 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 1.327/1.327, allocations: 230.6 MB / 256.8 MB, free: 7.805 MB / 206.1 MB " [Timeout remaining time 178] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Chemical master/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Chemical master/package.mo): time 0.13/0.13, allocations: 23.93 MB / 337.1 MB, free: 10.91 MB / 270.1 MB " [Timeout remaining time 180] Using package Chemical with version 2.0.1 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Chemical master/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.SimpleReaction2,tolerance=1e-06,outputFormat="empty",numberOfIntervals=2500,variableFilter="",fileNamePrefix="Chemical_master_Chemical.Obsolete.Examples.SimpleReaction2") translateModel(Chemical.Obsolete.Examples.SimpleReaction2,tolerance=1e-06,outputFormat="empty",numberOfIntervals=2500,variableFilter="",fileNamePrefix="Chemical_master_Chemical.Obsolete.Examples.SimpleReaction2") [Timeout 660] "Notification: Performance of FrontEnd - Absyn->SCode: time 2.078e-05/2.078e-05, allocations: 2.281 kB / 472.4 MB, free: 7.016 MB / 334.1 MB [/home/hudson/saved_omc/libraries/.openmodelica/libraries/Chemical master/Obsolete.mo:14335:7-14335:66:writable] Warning: An inner declaration for outer component system could not be found and was automatically generated. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/Chemical master/Obsolete.mo:14335:7-14335:66:writable] Notification: The diagnostics message for the missing inner is: Your model is using an outer \"system\" component but an inner \"system\" component is not defined. For simulation drag Modelica.Fluid.System into your model to specify system properties. Notification: Performance of NFInst.instantiate(Chemical.Obsolete.Examples.SimpleReaction2): time 0.06865/0.06867, allocations: 25.45 MB / 497.8 MB, free: 13.69 MB / 366.1 MB Notification: Performance of NFInst.instExpressions: time 0.01289/0.08157, allocations: 10.26 MB / 0.4962 GB, free: 3.387 MB / 366.1 MB Notification: Performance of NFInst.updateImplicitVariability: time 0.0004683/0.08203, allocations: 15.88 kB / 0.4962 GB, free: 3.371 MB / 366.1 MB Notification: Performance of NFTyping.typeComponents: time 0.000535/0.08257, allocations: 242.1 kB / 0.4964 GB, free: 3.133 MB / 366.1 MB Notification: Performance of NFTyping.typeBindings: time 0.001887/0.08446, allocations: 0.9969 MB / 0.4974 GB, free: 2.129 MB / 366.1 MB Notification: Performance of NFTyping.typeClassSections: time 0.002999/0.08745, allocations: 1.534 MB / 0.4989 GB, free: 0.5859 MB / 366.1 MB Notification: Performance of NFFlatten.flatten: time 0.001382/0.08884, allocations: 1.462 MB / 0.5003 GB, free: 15.12 MB / 382.1 MB Notification: Performance of NFFlatten.resolveConnections: time 0.00072/0.08956, allocations: 0.5808 MB / 0.5009 GB, free: 14.52 MB / 382.1 MB Notification: Performance of NFEvalConstants.evaluate: time 0.0006235/0.09018, allocations: 0.6273 MB / 0.5015 GB, free: 13.89 MB / 382.1 MB Notification: Performance of NFSimplifyModel.simplify: time 0.0007042/0.09088, allocations: 0.6696 MB / 0.5022 GB, free: 13.22 MB / 382.1 MB Notification: Performance of NFPackage.collectConstants: time 0.0001477/0.09103, allocations: 104 kB / 0.5023 GB, free: 13.12 MB / 382.1 MB Notification: Performance of NFFlatten.collectFunctions: time 0.00228/0.09331, allocations: 1.252 MB / 0.5035 GB, free: 11.86 MB / 382.1 MB Notification: Performance of combineBinaries: time 0.001669/0.09498, allocations: 2.083 MB / 0.5055 GB, free: 9.762 MB / 382.1 MB Notification: Performance of replaceArrayConstructors: time 0.000759/0.09574, allocations: 1.18 MB / 0.5067 GB, free: 8.566 MB / 382.1 MB Notification: Performance of NFVerifyModel.verify: time 0.0001328/0.09587, allocations: 96 kB / 0.5068 GB, free: 8.473 MB / 382.1 MB Notification: Performance of FrontEnd: time 0.0001237/0.096, allocations: 35.92 kB / 0.5068 GB, free: 8.438 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: 222 (220) * Number of variables: 222 (219) Notification: Performance of [SIM] Bindings: time 0.004303/0.1003, allocations: 4.922 MB / 0.5116 GB, free: 3.32 MB / 382.1 MB Notification: Performance of [SIM] FunctionAlias: time 0.0007207/0.101, allocations: 0.7317 MB / 0.5123 GB, free: 2.574 MB / 382.1 MB Notification: Performance of [SIM] Early Inline: time 0.1713/0.2723, allocations: 4.188 MB / 0.5164 GB, free: 37.88 MB / 382.1 MB Notification: Performance of [SIM] Simplify 1: time 0.001504/0.2738, allocations: 0.659 MB / 0.517 GB, free: 37.71 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 0.005696/0.2795, allocations: 4.314 MB / 0.5213 GB, free: 36.75 MB / 382.1 MB Notification: Performance of [SIM] Simplify 2: time 0.000633/0.2802, allocations: 484.3 kB / 0.5217 GB, free: 36.59 MB / 382.1 MB Notification: Performance of [SIM] Remove Stream: time 0.0001822/0.2803, allocations: 201.7 kB / 0.5219 GB, free: 36.52 MB / 382.1 MB Notification: Performance of [SIM] Detect States: time 0.0004872/0.2808, allocations: 478.4 kB / 0.5224 GB, free: 36.39 MB / 382.1 MB Notification: Performance of [SIM] Events: time 0.0001688/0.281, allocations: 128.4 kB / 0.5225 GB, free: 36.39 MB / 382.1 MB Notification: Performance of [SIM] Partitioning: time 0.0009101/0.2819, allocations: 0.8294 MB / 0.5233 GB, free: 36.33 MB / 382.1 MB Error: Internal error NBSorting.tarjan failed to sort system: System Variables (185/191) **************************** (1|1) [DSTA] (1) protected Real A.amountOfParticles (start = A.m_start * Chemical.Obsolete.Examples.SimpleReaction2.A.stateOfMatter.specificAmountOfParticles(Chemical.Obsolete.Examples.SimpleReaction2.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) (2|2) [DDER] (1) Real $DER.C.molarVolume (3|3) [DSTA] (1) protected Real B.amountOfParticles (start = B.m_start * Chemical.Obsolete.Examples.SimpleReaction2.B.stateOfMatter.specificAmountOfParticles(Chemical.Obsolete.Examples.SimpleReaction2.B.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 C.amountOfParticles (start = C.m_start * Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.specificAmountOfParticles(Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.SubstanceData(0.01801528, 0.0, -11675.08030005653, 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) (5|5) [DSTA] (2) flow Real[2] reaction.substrates.q (6|7) [DDER] (1) Real $DER.B.molarVolume (7|8) [DSTA] (1) Real C.q (8|9) [DSTA] (1) Real B.q (9|10) [DSTA] (1) flow Real A.solution.Ij (min = 0.0, max = 1.0) (10|11) [DSTA] (1) Real A.q (11|12) [DSTA] (1) flow Real B.solution.Ij (min = 0.0, max = 1.0) (12|13) [DDER] (1) Real $DER.C.temperature (13|14) [DSTA] (1) flow Real C.solution.Ij (min = 0.0, max = 1.0) (14|15) [DDER] (1) Real $DER.A.molarVolume (15|16) [DSTA] (1) flow Real A.solution.dV (16|17) [DSTA] (1) flow Real B.solution.dV (17|18) [STAT] (1) flow Real C.solution.dV (18|19) [DSTA] (1) flow Real[1] reaction.products.q (19|20) [DSTA] (1) flow Real A.solution.dH (20|21) [DSTA] (1) flow Real B.solution.dH (21|22) [DSTA] (1) Real C.port_a.u (22|23) [DSTA] (1) protected Real C.u0 (23|24) [DSTA] (1) protected Real B.u0 (24|25) [DSTA] (1) Real B.port_a.u (25|26) [DSTA] (1) flow Real C.solution.dH (26|27) [DSTA] (1) protected Real A.u0 (27|28) [DSTA] (1) Real A.port_a.u (28|29) [DSTA] (1) Real C.a (29|30) [DSTA] (1) Real B.a (30|31) [DSTA] (1) Real A.a (31|32) [DSTA] (1) Real C.x (min = 0.0, max = 1.0) (32|33) [DSTA] (1) Real B.x (min = 0.0, max = 1.0) (33|34) [DSTA] (1) protected Real C.pressure (34|35) [DSTA] (1) Real A.x (min = 0.0, max = 1.0) (35|36) [ALGB] (1) protected Real A.SelfClustering_K = exp(-0.0 / (C.temperature * 8.31446261815324)) (min = 0.0, max = 1.0) (36|37) [ALGB] (1) protected Real B.SelfClustering_K = exp(-0.0 / (C.temperature * 8.31446261815324)) (min = 0.0, max = 1.0) (37|38) [ALGB] (1) protected Real C.SelfClustering_K = exp(-0.0 / (C.temperature * 8.31446261815324)) (min = 0.0, max = 1.0) (38|39) [DSTA] (2) stream Real[2] reaction.substrates.h_outflow (nominal = {2e4 for $f1 in 1:2}) (39|41) [DSTA] (1) Real $FUN_8 (40|42) [DSTA] (1) Real $FUN_6 (41|43) [DSTA] (1) Real $FUN_4 (42|44) [DSTA] (1) flow Real A.solution.Gj (43|45) [DSTA] (1) Real $FUN_3 (44|46) [DSTA] (1) protected Real solution.top_s (45|47) [DSTA] (1) flow Real B.solution.Gj (46|48) [DSTA] (1) Real $FUN_2 (47|49) [DSTA] (1) Real solution.volume (48|50) [DSTA] (1) flow Real C.solution.Gj (49|51) [DSTA] (1) Real solution.mass (min = 0.0, StateSelect = prefer) (50|52) [DSTA] (1) flow Real A.solution.mj (min = 0.0) (51|53) [DSTA] (1) flow Real B.solution.mj (min = 0.0) (52|54) [DSTA] (1) flow Real C.solution.mj (min = 0.0) (53|55) [DSTA] (1) Real[1] reaction.products.u (54|56) [DSTA] (1) Real reaction.rr (start = 0.0) (55|57) [DSTA] (1) Real reaction.h_mix (nominal = 2e4) (56|58) [DSTA] (1) protected Real solution.gibbsEnergy (57|59) [STAT] (1) protected Real A.molarEntropyPure (58|60) [DSTA] (1) protected Real B.molarEntropyPure (59|61) [DSTA] (1) protected Real C.moleFractionBasedIonicStrength (min = 0.0, max = 0.0) (60|62) [DSTA] (1) protected Real solution.volume_der (61|63) [DSTA] (1) protected Real C.molarEntropyPure (62|64) [DSTA] (1) Real C.port_c.c (63|65) [DSTA] (1) Real B.port_c.c (64|66) [DSTA] (1) Real A.port_c.c (65|67) [DSTA] (1) protected Real C.uPure (66|68) [DSTA] (1) protected Real B.uPure (67|69) [DSTA] (1) protected Real A.uPure (68|70) [DSTA] (1) Real C.c (69|71) [DSTA] (1) Real B.c (70|72) [DSTA] (1) Real A.c (71|73) [DISC] (1) Boolean $SEV_4 (72|74) [DISC] (1) Boolean $SEV_3 (73|75) [DISC] (1) Boolean $SEV_2 (74|76) [DISC] (1) Boolean $SEV_1 (75|77) [DISC] (1) Boolean $SEV_0 (76|78) [DSTA] (1) protected Real reaction.du (77|79) [DSTA] (2) Real[2] reaction.substrates.u (78|81) [DSTA] (1) protected Real C.amountOfSolution (min = 0.0) (79|82) [DSTA] (1) flow Real C.port_a.q (80|83) [DSTA] (1) Real C.port_m.x_mass (min = 0.0, max = 1.0) (81|84) [DSTA] (1) flow Real B.port_a.q (82|85) [DSTA] (1) Real B.port_m.x_mass (min = 0.0, max = 1.0) (83|86) [DSTA] (1) flow Real A.port_a.q (84|87) [DSTA] (1) Real A.port_m.x_mass (min = 0.0, max = 1.0) (85|88) [DSTA] (1) protected Real solution.heatFromEnvironment (86|89) [DSTA] (1) Real C.mass = C.amountOfParticles * C.molarMassOfBaseMolecule (min = 0.0) (87|90) [DSTA] (1) flow Real A.solution.Vj (88|91) [DSTA] (1) Real B.mass = B.amountOfParticles * B.molarMassOfBaseMolecule (min = 0.0) (89|92) [DSTA] (1) flow Real B.solution.Vj (90|93) [DSTA] (1) Real A.mass = A.amountOfParticles * A.molarMassOfBaseMolecule (min = 0.0) (91|94) [DSTA] (1) Real $DER.A.logn (92|95) [DSTA] (1) flow Real C.solution.Vj (93|96) [DSTA] (1) Real $DER.B.logn (94|97) [DSTA] (1) stream Real[1] reaction.products.h_outflow (nominal = {2e4 for $f1 in 1:1}) (95|98) [DSTA] (1) Real $DER.C.logn (96|99) [DDER] (1) Real $DER.solution.heatFromEnvironment (97|100) [DDER] (1) Real $DER.B.mass (98|101) [DDER] (1) Real $DER.solution.top_s (99|102) [DDER] (1) Real $DER.C.mass (100|103) [DDER] (1) Real $DER.B.port_c.c (101|104) [DDER] (1) Real $DER.A.uPure (102|105) [DDER] (1) Real $DER.B.port_m.x_mass (103|106) [DDER] (1) Real $DER.A.u0 (104|107) [DER-] (1) Real $DER.A.molarEntropyPure (105|108) [DDER] (1) Real $DER.C.port_c.c (106|109) [DDER] (1) Real $DER.A.port_c.c (107|110) [DDER] (1) Real $DER.C.port_m.x_mass (108|111) [DDER] (1) Real $DER.A.port_m.x_mass (109|112) [DER-] (1) Real $DER.$DER.B.molarVolume (110|113) [DDER] (1) Real $DER.$FUN_3 (111|114) [DDER] (1) Real $DER.B.c (112|115) [DDER] (1) Real $DER.A.a (113|116) [DDER] (1) Real $DER.$DER.C.molarVolume (114|117) [DER-] (1) Real $DER.$DER.A.molarVolume (115|118) [DDER] (1) Real $DER.C.c (116|119) [DDER] (1) Real $DER.A.c (117|120) [DDER] (1) Real $DER.A.x (118|121) [DDER] (1) Real $DER.$DER.C.logn (119|122) [DDER] (1) Real $DER.$DER.A.logn (120|123) [DDER] (1) Real $DER.$DER.B.logn (121|124) [DDER] (1) Real $DER.C.q (122|125) [DDER] (1) flow Real $DER.C.solution.dH (123|126) [DDER] (1) Real $DER.B.q (124|127) [DDER] (1) flow Real $DER.B.solution.dH (125|128) [DDER] (1) flow Real $DER.B.port_a.q (126|129) [DDER] (1) flow Real $DER.C.port_a.q (127|130) [DDER] (1) Real $DER.A.q (128|131) [DDER] (1) flow Real $DER.A.solution.dH (129|132) [DDER] (1) Real $DER.$FUN_6 (130|133) [DDER] (1) Real $DER.B.port_a.u (131|134) [DDER] (1) Real $DER.B.x (132|135) [DDER] (1) Real $DER.B.a (133|136) [DDER] (1) flow Real $DER.A.port_a.q (134|137) [DDER] (1) flow Real $DER.A.solution.Ij (135|138) [DDER] (1) flow Real $DER.B.solution.Ij (136|139) [DDER] (1) flow Real $DER.C.solution.Ij (137|140) [DDER] (1) stream Real[1] $DER.reaction.products.h_outflow (138|141) [DDER] (1) Real $DER.B.uPure (139|142) [DDER] (1) Real $DER.solution.gibbsEnergy (140|143) [DDER] (1) flow Real $DER.A.solution.Gj (141|144) [DDER] (1) flow Real $DER.B.solution.Gj (142|145) [DDER] (1) flow Real $DER.C.solution.Gj (143|146) [DDER] (1) Real $DER.reaction.h_mix (144|147) [DDER] (2) stream Real[2] $DER.reaction.substrates.h_outflow (145|149) [DDER] (1) Real $DER.B.u0 (146|150) [DDER] (1) Real $DER.solution.volume (147|151) [DDER] (1) flow Real $DER.A.solution.Vj (148|152) [DDER] (1) flow Real $DER.B.solution.Vj (149|153) [DDER] (1) flow Real $DER.C.solution.Vj (150|154) [DDER] (1) flow Real[1] $DER.reaction.products.q (151|155) [DDER] (1) Real $DER.B.molarEntropyPure (152|156) [DDER] (1) Real $DER.solution.mass (153|157) [DDER] (1) flow Real $DER.A.solution.mj (154|158) [DDER] (1) flow Real $DER.B.solution.mj (155|159) [DDER] (1) flow Real $DER.C.solution.mj (156|160) [DDER] (2) flow Real[2] $DER.reaction.substrates.q (157|162) [DDER] (1) Real $DER.C.amountOfSolution (158|163) [DDER] (1) Real $DER.B.amountOfParticles (159|164) [DDER] (1) Real $DER.C.amountOfParticles (160|165) [DDER] (1) Real $DER.$FUN_4 (161|166) [DDER] (1) Real $DER.reaction.rr (162|167) [DDER] (1) Real $DER.A.amountOfParticles (163|168) [DDER] (1) Real $DER.A.mass (164|169) [DDER] (2) Real[2] $DER.reaction.substrates.u (165|171) [DDER] (1) Real[1] $DER.reaction.products.u (166|172) [DDER] (1) Real $DER.reaction.du (167|173) [DDER] (1) Real $DER.solution.volume_der (168|174) [DDER] (1) flow Real $DER.A.solution.dV (169|175) [DDER] (1) flow Real $DER.B.solution.dV (170|176) [DER-] (1) flow Real $DER.C.solution.dV (171|177) [DDER] (1) Real $DER.$FUN_2 (172|178) [DDER] (1) Real $DER.A.port_a.u (173|179) [DDER] (1) Real $DER.C.x (174|180) [DDER] (1) Real $DER.C.a (175|181) [DDER] (1) Real $DER.$FUN_8 (176|182) [DDER] (1) Real $DER.C.port_a.u (177|183) [DDER] (1) Real $DER.C.uPure (178|184) [DDER] (1) Real $DER.C.moleFractionBasedIonicStrength (179|185) [DDER] (1) Real $DER.C.u0 (180|186) [DDER] (1) Real $DER.C.pressure (181|187) [DDER] (1) Real $DER.C.molarEntropyPure (182|188) [DSTA] (1) protected Real B.molarVolume (min = 0.0) (183|189) [DSTA] (1) protected Real A.molarVolume (min = 0.0) (184|190) [DSTA] (1) protected Real C.temperature (start = 288.15, min = 0.0, nominal = 300.0) (185|191) [DSTA] (1) protected Real C.molarVolume (min = 0.0) System Equations (183/187) **************************** (1|1) [SCAL] (1) $DER.C.temperature = 0.0 ($RES_SIM_133) (2|2) [SCAL] (1) (A.solution.dH + B.solution.dH + C.solution.dH) - solution.heatFromEnvironment = 0.0 ($RES_SIM_170) (3|3) [SCAL] (1) C.pressure = solution.BasePressure ($RES_SIM_136) (4|4) [SCAL] (1) A.port_a.u = reaction.substrates[2].u ($RES_SIM_171) (5|5) [SCAL] (1) B.mass = B.amountOfParticles * B.molarMassOfBaseMolecule ($RES_BND_222) (6|6) [SCAL] (1) solution.top_s = solution.volume / solution.SurfaceArea - solution.positionShift ($RES_SIM_137) (7|7) [SCAL] (1) A.a = A.x ($RES_SIM_90) (8|8) [SCAL] (1) B.port_a.u = reaction.substrates[1].u ($RES_SIM_172) (9|9) [SCAL] (1) C.mass = C.amountOfParticles * C.molarMassOfBaseMolecule ($RES_BND_225) (10|10) [SCAL] (1) A.molarVolume = 1.8015280000000002e-5 + Chemical.Obsolete.Examples.SimpleReaction2.A.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.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), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength) * log(Chemical.Obsolete.Examples.SimpleReaction2.A.stateOfMatter.activityCoefficient(Chemical.Obsolete.Examples.SimpleReaction2.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), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength)) ($RES_SIM_93) (11|11) [SCAL] (1) B.port_c.c = B.amountOfParticles / solution.volume ($RES_SIM_58) (12|12) [SCAL] (1) A.uPure = Chemical.Obsolete.Examples.SimpleReaction2.A.stateOfMatter.molarEnthalpyElectroneutral(Chemical.Obsolete.Examples.SimpleReaction2.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), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength) - C.temperature * Chemical.Obsolete.Examples.SimpleReaction2.A.stateOfMatter.molarEntropyPure(Chemical.Obsolete.Examples.SimpleReaction2.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), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength) ($RES_SIM_94) (13|13) [SCAL] (1) B.port_m.x_mass = B.solution.mj / solution.mass ($RES_SIM_59) (14|14) [SCAL] (1) A.SelfClustering_K = exp(-0.0 / C.temperature / 8.31446261815324) ($RES_AUX_228) (15|15) [SCAL] (1) A.u0 = C.temperature * ((Chemical.Obsolete.Examples.SimpleReaction2.A.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.A.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength) / C.temperature) * ((-1e5) + C.pressure)) ($RES_SIM_95) (16|16) [SCAL] (1) B.SelfClustering_K = exp(-0.0 / C.temperature / 8.31446261815324) ($RES_AUX_229) (17|17) [SCAL] (1) A.molarEntropyPure = -(1.8015280000000002e-5 / C.temperature) * ((-1e5) + C.pressure) ($RES_SIM_96) (18|18) [SCAL] (1) C.port_c.c = C.amountOfParticles / solution.volume ($RES_SIM_22) (19|19) [SCAL] (1) A.port_c.c = A.amountOfParticles / solution.volume ($RES_SIM_105) (20|20) [SCAL] (1) C.port_m.x_mass = C.solution.mj / solution.mass ($RES_SIM_23) (21|21) [SCAL] (1) A.port_m.x_mass = A.solution.mj / solution.mass ($RES_SIM_106) (22|22) [SCAL] (1) C.q = C.port_a.q ($RES_SIM_24) (23|23) [SCAL] (1) B.q = B.port_a.q ($RES_SIM_60) (24|24) [SCAL] (1) A.q = A.port_a.q ($RES_SIM_107) (25|25) [SCAL] (1) C.solution.Ij = 0.0 ($RES_SIM_25) (26|26) [SCAL] (1) B.solution.Ij = 0.0 ($RES_SIM_61) (27|27) [SCAL] (1) A.solution.Ij = 0.0 ($RES_SIM_108) (28|28) [SCAL] (1) C.SelfClustering_K = exp(-0.0 / C.temperature / 8.31446261815324) ($RES_AUX_230) (29|29) [SCAL] (1) C.solution.Vj = C.amountOfParticles * C.molarVolume ($RES_SIM_27) (30|30) [SCAL] (1) $FUN_8 = log(C.a) ($RES_AUX_231) (31|31) [SCAL] (1) B.solution.Vj = B.amountOfParticles * B.molarVolume ($RES_SIM_63) (32|32) [SCAL] (1) C.solution.mj = C.amountOfParticles * C.molarMassOfBaseMolecule ($RES_SIM_28) (33|33) [SCAL] (1) C.amountOfParticles = exp(C.logn) ($RES_AUX_232) (34|34) [SCAL] (1) B.solution.mj = B.amountOfParticles * B.molarMassOfBaseMolecule ($RES_SIM_64) (35|35) [SCAL] (1) $FUN_6 = log(B.a) ($RES_AUX_233) (36|36) [SCAL] (1) B.amountOfParticles = exp(B.logn) ($RES_AUX_234) (37|37) [SCAL] (1) B.solution.dV = B.molarVolume * B.q + $DER.B.molarVolume * B.amountOfParticles ($RES_SIM_66) (38|38) [SCAL] (1) $FUN_4 = exp(-reaction.kE * $FUN_3) ($RES_AUX_235) (39|39) [SCAL] (1) $FUN_3 = abs(reaction.du) ($RES_AUX_236) (40|40) [SCAL] (1) B.c = B.amountOfParticles / solution.volume ($RES_SIM_68) (41|41) [SCAL] (1) $FUN_2 = log(A.a) ($RES_AUX_237) (42|42) [SCAL] (1) B.x = B.amountOfParticles / C.amountOfSolution ($RES_SIM_69) (43|43) [SCAL] (1) A.amountOfParticles = exp(A.logn) ($RES_AUX_238) (44|44) [SCAL] (1) A.solution.Vj = A.amountOfParticles * A.molarVolume ($RES_SIM_110) (45|45) [SCAL] (1) A.solution.mj = A.amountOfParticles * A.molarMassOfBaseMolecule ($RES_SIM_111) (46|46) [SCAL] (1) C.solution.dV = C.molarVolume * C.q + $DER.C.molarVolume * C.amountOfParticles ($RES_SIM_30) (47|47) [SCAL] (1) A.solution.dV = A.molarVolume * A.q + $DER.A.molarVolume * A.amountOfParticles ($RES_SIM_113) (48|48) [SCAL] (1) C.c = C.amountOfParticles / solution.volume ($RES_SIM_32) (49|49) [SCAL] (1) A.c = A.amountOfParticles / solution.volume ($RES_SIM_115) (50|50) [SCAL] (1) C.x = C.amountOfParticles / C.amountOfSolution ($RES_SIM_33) (51|51) [SCAL] (1) A.x = A.amountOfParticles / C.amountOfSolution ($RES_SIM_116) (52|52) [SCAL] (1) $DER.C.logn = C.q / C.amountOfParticles ($RES_SIM_35) (53|53) [SCAL] (1) $DER.A.logn = A.q / A.amountOfParticles ($RES_SIM_118) (54|54) [SCAL] (1) $DER.B.logn = B.q / B.amountOfParticles ($RES_SIM_71) (55|55) [SCAL] (1) C.solution.dH = -C.q * (if $SEV_4 then reaction.products[1].h_outflow else 0.0) ($RES_SIM_39) (56|56) [SCAL] (1) B.solution.dH = -B.q * (if $SEV_3 then reaction.substrates[1].h_outflow else 0.0) ($RES_SIM_75) (57|57) [SCAL] (1) B.port_a.q + reaction.substrates[1].q = 0.0 ($RES_SIM_157) (58|58) [SCAL] (1) B.solution.Gj = B.amountOfParticles * B.port_a.u ($RES_SIM_76) (59|59) [SCAL] (1) C.port_a.q + reaction.products[1].q = 0.0 ($RES_SIM_158) (60|60) [-IF-] (1) ($RES_SIM_78) (60|60) [----] if $SEV_1 then (60|60) [----] [SCAL] (1) reaction.h_mix * (fill(1.0, 1))[1] * reaction.products[1].q = 0.0 ($RES_SIM_79) (60|60) [----] elseif $SEV_2 then (60|60) [----] [SCAL] (1) reaction.h_mix * (reaction.substrates.q * fill(1.0, 2)) = 0.0 ($RES_SIM_80) (60|60) [----] else (60|60) [----] [SCAL] (1) reaction.h_mix = 0.0 ($RES_SIM_81) (60|60) [----] end if; (61|61) [SCAL] (1) $SEV_0 = A.port_a.q > 0.0 ($RES_EVT_239) (62|62) [SCAL] (1) C.solution.Gj = C.amountOfParticles * C.port_a.u ($RES_SIM_40) (63|63) [SCAL] (1) A.solution.dH = -A.q * (if $SEV_0 then reaction.substrates[2].h_outflow else 0.0) ($RES_SIM_122) (64|64) [SCAL] (1) A.solution.Gj = A.amountOfParticles * A.port_a.u ($RES_SIM_123) (65|65) [SCAL] (1) B.port_a.u = 8.31446261815324 * C.temperature * $FUN_6 + C.temperature * ((Chemical.Obsolete.Examples.SimpleReaction2.B.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.B.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength) / C.temperature) * ((-1e5) + C.pressure)) ($RES_SIM_42) (66|66) [SCAL] (1) B.a = B.x ($RES_SIM_43) (67|67) [SCAL] (1) reaction.substrates[2].q + A.port_a.q = 0.0 ($RES_SIM_161) (68|68) [SCAL] (1) (A.solution.Ij + B.solution.Ij + C.solution.Ij) - C.moleFractionBasedIonicStrength = 0.0 ($RES_SIM_162) (69|69) [SCAL] (1) reaction.products[1].u = C.port_a.u ($RES_SIM_200) (70|70) [SCAL] (1) B.molarVolume = 1.8015280000000002e-5 + Chemical.Obsolete.Examples.SimpleReaction2.B.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.B.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), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength) * log(Chemical.Obsolete.Examples.SimpleReaction2.B.stateOfMatter.activityCoefficient(Chemical.Obsolete.Examples.SimpleReaction2.B.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), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength)) ($RES_SIM_46) (71|71) [ARRY] (1) reaction.products.h_outflow = reaction.h_mix * fill(1.0, 1) ($RES_SIM_82) (72|72) [SCAL] (1) B.uPure = Chemical.Obsolete.Examples.SimpleReaction2.B.stateOfMatter.molarEnthalpyElectroneutral(Chemical.Obsolete.Examples.SimpleReaction2.B.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), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength) - C.temperature * Chemical.Obsolete.Examples.SimpleReaction2.B.stateOfMatter.molarEntropyPure(Chemical.Obsolete.Examples.SimpleReaction2.B.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), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength) ($RES_SIM_47) (73|73) [SCAL] (1) (A.solution.Gj + B.solution.Gj + C.solution.Gj) - solution.gibbsEnergy = 0.0 ($RES_SIM_164) (74|74) [ARRY] (2) reaction.substrates.h_outflow = reaction.h_mix * fill(1.0, 2) ($RES_SIM_83) (75|76) [SCAL] (1) B.u0 = C.temperature * ((Chemical.Obsolete.Examples.SimpleReaction2.B.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.B.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength) / C.temperature) * ((-1e5) + C.pressure)) ($RES_SIM_48) (76|77) [SCAL] (1) (A.solution.Vj + B.solution.Vj + C.solution.Vj) - solution.volume = 0.0 ($RES_SIM_165) (77|78) [ARRY] (1) reaction.rr * reaction.p = -reaction.products.q ($RES_SIM_84) (78|79) [SCAL] (1) B.molarEntropyPure = -(1.8015280000000002e-5 / C.temperature) * ((-1e5) + C.pressure) ($RES_SIM_49) (79|80) [SCAL] (1) (A.solution.mj + B.solution.mj + C.solution.mj) - solution.mass = 0.0 ($RES_SIM_166) (80|81) [ARRY] (2) reaction.rr * reaction.s = reaction.substrates.q ($RES_SIM_85) (81|83) [SCAL] (1) (A.amountOfParticles + B.amountOfParticles + C.amountOfParticles) - C.amountOfSolution = 0.0 ($RES_SIM_167) (82|84) [SCAL] (1) reaction.rr = -reaction.du * reaction.KC * $FUN_4 ($RES_SIM_86) (83|85) [SCAL] (1) A.mass = A.amountOfParticles * A.molarMassOfBaseMolecule ($RES_BND_219) (84|86) [SCAL] (1) reaction.du = reaction.p[1] * reaction.products[1].u - reaction.s * reaction.substrates.u ($RES_SIM_87) (85|87) [SCAL] (1) (A.solution.dV + B.solution.dV + C.solution.dV) - solution.volume_der = 0.0 ($RES_SIM_169) (86|88) [SCAL] (1) A.port_a.u = 8.31446261815324 * C.temperature * $FUN_2 + C.temperature * ((Chemical.Obsolete.Examples.SimpleReaction2.A.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.A.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength) / C.temperature) * ((-1e5) + C.pressure)) ($RES_SIM_89) (87|89) [SCAL] (1) $SEV_1 = reaction.rr > 0.0 ($RES_EVT_240) (88|90) [SCAL] (1) C.a = C.x ($RES_SIM_7) (89|91) [SCAL] (1) $SEV_2 = reaction.rr < 0.0 ($RES_EVT_241) (90|92) [SCAL] (1) C.port_a.u = 8.31446261815324 * C.temperature * $FUN_8 - C.temperature * (39.1584112026045 - (Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.SubstanceData(0.01801528, 0.0, -11675.08030005653, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength) / C.temperature) * ((-1e5) + C.pressure)) ($RES_SIM_6) (91|93) [SCAL] (1) $SEV_3 = B.port_a.q > 0.0 ($RES_EVT_242) (92|94) [SCAL] (1) $SEV_4 = C.port_a.q > 0.0 ($RES_EVT_243) (93|95) [SCAL] (1) C.molarVolume = 1.8015280000000002e-5 + Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.SubstanceData(0.01801528, 0.0, -11675.08030005653, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength) * log(Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.activityCoefficient(Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.SubstanceData(0.01801528, 0.0, -11675.08030005653, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength)) ($RES_SIM_10) (94|96) [SCAL] (1) C.uPure = Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.molarEnthalpyElectroneutral(Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.SubstanceData(0.01801528, 0.0, -11675.08030005653, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength) - C.temperature * Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.molarEntropyPure(Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.SubstanceData(0.01801528, 0.0, -11675.08030005653, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength) ($RES_SIM_11) (95|97) [SCAL] (1) C.u0 = -C.temperature * (39.1584112026045 - (Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.SubstanceData(0.01801528, 0.0, -11675.08030005653, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength) / C.temperature) * ((-1e5) + C.pressure)) ($RES_SIM_12) (96|98) [SCAL] (1) C.molarEntropyPure = 39.1584112026045 - (1.8015280000000002e-5 / C.temperature) * ((-1e5) + C.pressure) ($RES_SIM_13) (97|99) [SCAL] (1) ($DER.A.solution.dH + $DER.B.solution.dH + $DER.C.solution.dH) - $DER.solution.heatFromEnvironment = 0.0 ($RES_SIM_244) (98|100) [SCAL] (1) $DER.C.pressure = 0.0 ($RES_SIM_245) (99|101) [SCAL] (1) $DER.A.port_a.u = $DER.reaction.substrates[2].u ($RES_SIM_246) (100|102) [SCAL] (1) $DER.B.mass = $DER.B.amountOfParticles * B.molarMassOfBaseMolecule ($RES_SIM_247) (101|103) [SCAL] (1) $DER.solution.top_s = ($DER.solution.volume * solution.SurfaceArea) / solution.SurfaceArea ^ 2.0 ($RES_SIM_248) (102|104) [SCAL] (1) $DER.A.a = $DER.A.x ($RES_SIM_249) (103|105) [SCAL] (1) $DER.B.port_a.u = $DER.reaction.substrates[1].u ($RES_SIM_250) (104|106) [SCAL] (1) $DER.C.mass = $DER.C.amountOfParticles * C.molarMassOfBaseMolecule ($RES_SIM_251) (105|107) [SCAL] (1) $DER.A.molarVolume = $fDER0.Chemical.Obsolete.Examples.SimpleReaction2.A.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.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), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength, $DER.C.temperature, $DER.C.pressure, 0.0, $DER.C.moleFractionBasedIonicStrength) * log(Chemical.Obsolete.Examples.SimpleReaction2.A.stateOfMatter.activityCoefficient(Chemical.Obsolete.Examples.SimpleReaction2.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), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength)) + Chemical.Obsolete.Examples.SimpleReaction2.A.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.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), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength) * ((1/Chemical.Obsolete.Examples.SimpleReaction2.A.stateOfMatter.activityCoefficient(Chemical.Obsolete.Examples.SimpleReaction2.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), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength)) * $fDER0.Chemical.Obsolete.Examples.SimpleReaction2.A.stateOfMatter.activityCoefficient(Chemical.Obsolete.Examples.SimpleReaction2.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), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength, $DER.C.temperature, $DER.C.pressure, 0.0, $DER.C.moleFractionBasedIonicStrength)) ($RES_SIM_252) (106|108) [SCAL] (1) $DER.B.port_c.c = ($DER.B.amountOfParticles * solution.volume - $DER.solution.volume * B.amountOfParticles) / solution.volume ^ 2.0 ($RES_SIM_253) (107|109) [SCAL] (1) $DER.A.uPure = $fDER0.Chemical.Obsolete.Examples.SimpleReaction2.A.stateOfMatter.molarEnthalpyElectroneutral(Chemical.Obsolete.Examples.SimpleReaction2.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), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength, $DER.C.temperature, $DER.C.pressure, 0.0, $DER.C.moleFractionBasedIonicStrength) - ($DER.C.temperature * Chemical.Obsolete.Examples.SimpleReaction2.A.stateOfMatter.molarEntropyPure(Chemical.Obsolete.Examples.SimpleReaction2.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), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength) + C.temperature * $fDER0.Chemical.Obsolete.Examples.SimpleReaction2.A.stateOfMatter.molarEntropyPure(Chemical.Obsolete.Examples.SimpleReaction2.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), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength, $DER.C.temperature, $DER.C.pressure, 0.0, $DER.C.moleFractionBasedIonicStrength)) ($RES_SIM_254) (108|110) [SCAL] (1) $DER.B.port_m.x_mass = ($DER.B.solution.mj * solution.mass - $DER.solution.mass * B.solution.mj) / solution.mass ^ 2.0 ($RES_SIM_255) (109|111) [SCAL] (1) $DER.A.u0 = $DER.C.temperature * ((Chemical.Obsolete.Examples.SimpleReaction2.A.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.A.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength) / C.temperature) * ((-1e5) + C.pressure)) + C.temperature * ((($fDER0.Chemical.Obsolete.Examples.SimpleReaction2.A.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.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), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength, $DER.C.temperature, $DER.C.pressure, 0.0, $DER.C.moleFractionBasedIonicStrength) * C.temperature - $DER.C.temperature * Chemical.Obsolete.Examples.SimpleReaction2.A.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.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), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength)) / C.temperature ^ 2.0) * ((-1e5) + C.pressure) + (Chemical.Obsolete.Examples.SimpleReaction2.A.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.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), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength) / C.temperature) * $DER.C.pressure) ($RES_SIM_256) (110|112) [SCAL] (1) $DER.A.molarEntropyPure = -((1.8015280000000002e-5 / C.temperature) * $DER.C.pressure - ((1.8015280000000002e-5 * $DER.C.temperature) / C.temperature ^ 2.0) * ((-1e5) + C.pressure)) ($RES_SIM_257) (111|113) [SCAL] (1) $DER.C.port_c.c = ($DER.C.amountOfParticles * solution.volume - $DER.solution.volume * C.amountOfParticles) / solution.volume ^ 2.0 ($RES_SIM_258) (112|114) [SCAL] (1) $DER.A.port_c.c = ($DER.A.amountOfParticles * solution.volume - $DER.solution.volume * A.amountOfParticles) / solution.volume ^ 2.0 ($RES_SIM_259) (113|115) [SCAL] (1) $DER.C.port_m.x_mass = ($DER.C.solution.mj * solution.mass - $DER.solution.mass * C.solution.mj) / solution.mass ^ 2.0 ($RES_SIM_260) (114|116) [SCAL] (1) $DER.A.port_m.x_mass = ($DER.A.solution.mj * solution.mass - $DER.solution.mass * A.solution.mj) / solution.mass ^ 2.0 ($RES_SIM_261) (115|117) [SCAL] (1) $DER.C.q = $DER.C.port_a.q ($RES_SIM_262) (116|118) [SCAL] (1) $DER.B.q = $DER.B.port_a.q ($RES_SIM_263) (117|119) [SCAL] (1) $DER.A.q = $DER.A.port_a.q ($RES_SIM_264) (118|120) [SCAL] (1) $DER.C.solution.Ij = 0.0 ($RES_SIM_265) (119|121) [SCAL] (1) $DER.B.solution.Ij = 0.0 ($RES_SIM_266) (120|122) [SCAL] (1) $DER.A.solution.Ij = 0.0 ($RES_SIM_267) (121|123) [SCAL] (1) $DER.C.solution.Vj = $DER.C.amountOfParticles * C.molarVolume + C.amountOfParticles * $DER.C.molarVolume ($RES_SIM_268) (122|124) [SCAL] (1) $DER.$FUN_8 = (1/C.a) * $DER.C.a ($RES_SIM_269) (123|125) [SCAL] (1) $DER.B.solution.Vj = $DER.B.amountOfParticles * B.molarVolume + B.amountOfParticles * $DER.B.molarVolume ($RES_SIM_270) (124|126) [SCAL] (1) $DER.C.solution.mj = $DER.C.amountOfParticles * C.molarMassOfBaseMolecule ($RES_SIM_271) (125|127) [SCAL] (1) $DER.C.amountOfParticles = exp(C.logn) * $DER.C.logn ($RES_SIM_272) (126|128) [SCAL] (1) $DER.B.solution.mj = $DER.B.amountOfParticles * B.molarMassOfBaseMolecule ($RES_SIM_273) (127|129) [SCAL] (1) $DER.$FUN_6 = (1/B.a) * $DER.B.a ($RES_SIM_274) (128|130) [SCAL] (1) $DER.B.amountOfParticles = exp(B.logn) * $DER.B.logn ($RES_SIM_275) (129|131) [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_276) (130|132) [SCAL] (1) $DER.$FUN_4 = -exp(-reaction.kE * $FUN_3) * (reaction.kE * $DER.$FUN_3) ($RES_SIM_277) (131|133) [SCAL] (1) $DER.$FUN_3 = sign(reaction.du) * $DER.reaction.du ($RES_SIM_278) (132|134) [SCAL] (1) $DER.B.c = ($DER.B.amountOfParticles * solution.volume - $DER.solution.volume * B.amountOfParticles) / solution.volume ^ 2.0 ($RES_SIM_279) (133|135) [SCAL] (1) $DER.$FUN_2 = (1/A.a) * $DER.A.a ($RES_SIM_280) (134|136) [SCAL] (1) $DER.B.x = ($DER.B.amountOfParticles * C.amountOfSolution - $DER.C.amountOfSolution * B.amountOfParticles) / C.amountOfSolution ^ 2.0 ($RES_SIM_281) (135|137) [SCAL] (1) $DER.A.amountOfParticles = exp(A.logn) * $DER.A.logn ($RES_SIM_282) (136|138) [SCAL] (1) $DER.A.solution.Vj = $DER.A.amountOfParticles * A.molarVolume + A.amountOfParticles * $DER.A.molarVolume ($RES_SIM_283) (137|139) [SCAL] (1) $DER.A.solution.mj = $DER.A.amountOfParticles * A.molarMassOfBaseMolecule ($RES_SIM_284) (138|140) [SCAL] (1) $DER.C.solution.dV = ($DER.C.molarVolume * C.q + C.molarVolume * $DER.C.q) + ($DER.$DER.C.molarVolume * C.amountOfParticles + $DER.C.molarVolume * $DER.C.amountOfParticles) ($RES_SIM_285) (139|141) [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_286) (140|142) [SCAL] (1) $DER.C.c = ($DER.C.amountOfParticles * solution.volume - $DER.solution.volume * C.amountOfParticles) / solution.volume ^ 2.0 ($RES_SIM_287) (141|143) [SCAL] (1) $DER.A.c = ($DER.A.amountOfParticles * solution.volume - $DER.solution.volume * A.amountOfParticles) / solution.volume ^ 2.0 ($RES_SIM_288) (142|144) [SCAL] (1) $DER.C.x = ($DER.C.amountOfParticles * C.amountOfSolution - $DER.C.amountOfSolution * C.amountOfParticles) / C.amountOfSolution ^ 2.0 ($RES_SIM_289) (143|145) [SCAL] (1) $DER.A.x = ($DER.A.amountOfParticles * C.amountOfSolution - $DER.C.amountOfSolution * A.amountOfParticles) / C.amountOfSolution ^ 2.0 ($RES_SIM_290) (144|146) [SCAL] (1) $DER.$DER.C.logn = ($DER.C.q * C.amountOfParticles - $DER.C.amountOfParticles * C.q) / C.amountOfParticles ^ 2.0 ($RES_SIM_291) (145|147) [SCAL] (1) $DER.$DER.A.logn = ($DER.A.q * A.amountOfParticles - $DER.A.amountOfParticles * A.q) / A.amountOfParticles ^ 2.0 ($RES_SIM_292) (146|148) [SCAL] (1) $DER.$DER.B.logn = ($DER.B.q * B.amountOfParticles - $DER.B.amountOfParticles * B.q) / B.amountOfParticles ^ 2.0 ($RES_SIM_293) (147|149) [SCAL] (1) $DER.C.solution.dH = -($DER.C.q * (if $SEV_4 then reaction.products[1].h_outflow else 0.0) + C.q * (if $SEV_4 then $DER.reaction.products[1].h_outflow else 0.0)) ($RES_SIM_294) (148|150) [SCAL] (1) $DER.B.solution.dH = -($DER.B.q * (if $SEV_3 then reaction.substrates[1].h_outflow else 0.0) + B.q * (if $SEV_3 then $DER.reaction.substrates[1].h_outflow else 0.0)) ($RES_SIM_295) (149|151) [SCAL] (1) $DER.B.port_a.q + $DER.reaction.substrates[1].q = 0.0 ($RES_SIM_296) (150|152) [SCAL] (1) $DER.B.solution.Gj = $DER.B.amountOfParticles * B.port_a.u + B.amountOfParticles * $DER.B.port_a.u ($RES_SIM_297) (151|153) [SCAL] (1) $DER.C.port_a.q + $DER.reaction.products[1].q = 0.0 ($RES_SIM_298) (152|154) [-IF-] (1) ($RES_SIM_299) (152|154) [----] if $SEV_1 then (152|154) [----] [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_300) (152|154) [----] elseif $SEV_2 then (152|154) [----] [SCAL] (1) $DER.reaction.h_mix * (reaction.substrates.q * fill(1.0, 2)) + reaction.h_mix * (reaction.substrates.q * fill(0.0, 2) + $DER.reaction.substrates.q * fill(1.0, 2)) = 0.0 ($RES_SIM_301) (152|154) [----] else (152|154) [----] [SCAL] (1) $DER.reaction.h_mix = 0.0 ($RES_SIM_302) (152|154) [----] end if; (153|155) [SCAL] (1) $DER.C.solution.Gj = $DER.C.amountOfParticles * C.port_a.u + C.amountOfParticles * $DER.C.port_a.u ($RES_SIM_303) (154|156) [SCAL] (1) $DER.A.solution.dH = -($DER.A.q * (if $SEV_0 then reaction.substrates[2].h_outflow else 0.0) + A.q * (if $SEV_0 then $DER.reaction.substrates[2].h_outflow else 0.0)) ($RES_SIM_304) (155|157) [SCAL] (1) $DER.A.solution.Gj = $DER.A.amountOfParticles * A.port_a.u + A.amountOfParticles * $DER.A.port_a.u ($RES_SIM_305) (156|158) [SCAL] (1) $DER.B.port_a.u = (8.31446261815324 * $DER.C.temperature * $FUN_6 + 8.31446261815324 * C.temperature * $DER.$FUN_6) + ($DER.C.temperature * ((Chemical.Obsolete.Examples.SimpleReaction2.B.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.B.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength) / C.temperature) * ((-1e5) + C.pressure)) + C.temperature * ((($fDER0.Chemical.Obsolete.Examples.SimpleReaction2.B.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.B.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), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength, $DER.C.temperature, $DER.C.pressure, 0.0, $DER.C.moleFractionBasedIonicStrength) * C.temperature - $DER.C.temperature * Chemical.Obsolete.Examples.SimpleReaction2.B.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.B.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), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength)) / C.temperature ^ 2.0) * ((-1e5) + C.pressure) + (Chemical.Obsolete.Examples.SimpleReaction2.B.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.B.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), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength) / C.temperature) * $DER.C.pressure)) ($RES_SIM_306) (157|159) [SCAL] (1) $DER.B.a = $DER.B.x ($RES_SIM_307) (158|160) [SCAL] (1) $DER.reaction.substrates[2].q + $DER.A.port_a.q = 0.0 ($RES_SIM_308) (159|161) [SCAL] (1) ($DER.A.solution.Ij + $DER.B.solution.Ij + $DER.C.solution.Ij) - $DER.C.moleFractionBasedIonicStrength = 0.0 ($RES_SIM_309) (160|162) [SCAL] (1) $DER.reaction.products[1].u = $DER.C.port_a.u ($RES_SIM_310) (161|163) [SCAL] (1) $DER.B.molarVolume = $fDER0.Chemical.Obsolete.Examples.SimpleReaction2.B.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.B.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), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength, $DER.C.temperature, $DER.C.pressure, 0.0, $DER.C.moleFractionBasedIonicStrength) * log(Chemical.Obsolete.Examples.SimpleReaction2.B.stateOfMatter.activityCoefficient(Chemical.Obsolete.Examples.SimpleReaction2.B.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), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength)) + Chemical.Obsolete.Examples.SimpleReaction2.B.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.B.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), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength) * ((1/Chemical.Obsolete.Examples.SimpleReaction2.B.stateOfMatter.activityCoefficient(Chemical.Obsolete.Examples.SimpleReaction2.B.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), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength)) * $fDER0.Chemical.Obsolete.Examples.SimpleReaction2.B.stateOfMatter.activityCoefficient(Chemical.Obsolete.Examples.SimpleReaction2.B.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), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength, $DER.C.temperature, $DER.C.pressure, 0.0, $DER.C.moleFractionBasedIonicStrength)) ($RES_SIM_311) (162|164) [ARRY] (1) $DER.reaction.products.h_outflow = $DER.reaction.h_mix * fill(1.0, 1) .+ reaction.h_mix * fill(0.0, 1) ($RES_SIM_312) (163|165) [SCAL] (1) $DER.B.uPure = $fDER0.Chemical.Obsolete.Examples.SimpleReaction2.B.stateOfMatter.molarEnthalpyElectroneutral(Chemical.Obsolete.Examples.SimpleReaction2.B.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), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength, $DER.C.temperature, $DER.C.pressure, 0.0, $DER.C.moleFractionBasedIonicStrength) - ($DER.C.temperature * Chemical.Obsolete.Examples.SimpleReaction2.B.stateOfMatter.molarEntropyPure(Chemical.Obsolete.Examples.SimpleReaction2.B.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), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength) + C.temperature * $fDER0.Chemical.Obsolete.Examples.SimpleReaction2.B.stateOfMatter.molarEntropyPure(Chemical.Obsolete.Examples.SimpleReaction2.B.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), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength, $DER.C.temperature, $DER.C.pressure, 0.0, $DER.C.moleFractionBasedIonicStrength)) ($RES_SIM_313) (164|166) [SCAL] (1) ($DER.A.solution.Gj + $DER.B.solution.Gj + $DER.C.solution.Gj) - $DER.solution.gibbsEnergy = 0.0 ($RES_SIM_314) (165|167) [ARRY] (2) $DER.reaction.substrates.h_outflow = $DER.reaction.h_mix * fill(1.0, 2) .+ reaction.h_mix * fill(0.0, 2) ($RES_SIM_315) (166|169) [SCAL] (1) $DER.B.u0 = $DER.C.temperature * ((Chemical.Obsolete.Examples.SimpleReaction2.B.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.B.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength) / C.temperature) * ((-1e5) + C.pressure)) + C.temperature * ((($fDER0.Chemical.Obsolete.Examples.SimpleReaction2.B.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.B.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), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength, $DER.C.temperature, $DER.C.pressure, 0.0, $DER.C.moleFractionBasedIonicStrength) * C.temperature - $DER.C.temperature * Chemical.Obsolete.Examples.SimpleReaction2.B.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.B.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), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength)) / C.temperature ^ 2.0) * ((-1e5) + C.pressure) + (Chemical.Obsolete.Examples.SimpleReaction2.B.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.B.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), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength) / C.temperature) * $DER.C.pressure) ($RES_SIM_316) (167|170) [SCAL] (1) ($DER.A.solution.Vj + $DER.B.solution.Vj + $DER.C.solution.Vj) - $DER.solution.volume = 0.0 ($RES_SIM_317) (168|171) [ARRY] (1) $DER.reaction.rr * reaction.p = -$DER.reaction.products.q ($RES_SIM_318) (169|172) [SCAL] (1) $DER.B.molarEntropyPure = -((1.8015280000000002e-5 / C.temperature) * $DER.C.pressure - ((1.8015280000000002e-5 * $DER.C.temperature) / C.temperature ^ 2.0) * ((-1e5) + C.pressure)) ($RES_SIM_319) (170|173) [SCAL] (1) ($DER.A.solution.mj + $DER.B.solution.mj + $DER.C.solution.mj) - $DER.solution.mass = 0.0 ($RES_SIM_320) (171|174) [ARRY] (2) $DER.reaction.rr * reaction.s = $DER.reaction.substrates.q ($RES_SIM_321) (172|176) [SCAL] (1) ($DER.A.amountOfParticles + $DER.B.amountOfParticles + $DER.C.amountOfParticles) - $DER.C.amountOfSolution = 0.0 ($RES_SIM_322) (173|177) [SCAL] (1) $DER.reaction.rr = -($DER.reaction.du * reaction.KC * $FUN_4 + reaction.du * reaction.KC * $DER.$FUN_4) ($RES_SIM_323) (174|178) [SCAL] (1) $DER.A.mass = $DER.A.amountOfParticles * A.molarMassOfBaseMolecule ($RES_SIM_324) (175|179) [SCAL] (1) $DER.reaction.du = reaction.p[1] * $DER.reaction.products[1].u - reaction.s * $DER.reaction.substrates.u ($RES_SIM_325) (176|180) [SCAL] (1) ($DER.A.solution.dV + $DER.B.solution.dV + $DER.C.solution.dV) - $DER.solution.volume_der = 0.0 ($RES_SIM_326) (177|181) [SCAL] (1) $DER.A.port_a.u = (8.31446261815324 * $DER.C.temperature * $FUN_2 + 8.31446261815324 * C.temperature * $DER.$FUN_2) + ($DER.C.temperature * ((Chemical.Obsolete.Examples.SimpleReaction2.A.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.A.stateOfMatter.SubstanceData(0.01801528, 0.0, 0.0, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength) / C.temperature) * ((-1e5) + C.pressure)) + C.temperature * ((($fDER0.Chemical.Obsolete.Examples.SimpleReaction2.A.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.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), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength, $DER.C.temperature, $DER.C.pressure, 0.0, $DER.C.moleFractionBasedIonicStrength) * C.temperature - $DER.C.temperature * Chemical.Obsolete.Examples.SimpleReaction2.A.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.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), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength)) / C.temperature ^ 2.0) * ((-1e5) + C.pressure) + (Chemical.Obsolete.Examples.SimpleReaction2.A.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.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), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength) / C.temperature) * $DER.C.pressure)) ($RES_SIM_327) (178|182) [SCAL] (1) $DER.C.a = $DER.C.x ($RES_SIM_328) (179|183) [SCAL] (1) $DER.C.port_a.u = (8.31446261815324 * $DER.C.temperature * $FUN_8 + 8.31446261815324 * C.temperature * $DER.$FUN_8) - ($DER.C.temperature * (39.1584112026045 - (Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.SubstanceData(0.01801528, 0.0, -11675.08030005653, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength) / C.temperature) * ((-1e5) + C.pressure)) - C.temperature * ((($fDER0.Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.SubstanceData(0.01801528, 0.0, -11675.08030005653, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength, $DER.C.temperature, $DER.C.pressure, 0.0, $DER.C.moleFractionBasedIonicStrength) * C.temperature - $DER.C.temperature * Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.SubstanceData(0.01801528, 0.0, -11675.08030005653, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength)) / C.temperature ^ 2.0) * ((-1e5) + C.pressure) + (Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.SubstanceData(0.01801528, 0.0, -11675.08030005653, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength) / C.temperature) * $DER.C.pressure)) ($RES_SIM_329) (180|184) [SCAL] (1) $DER.C.molarVolume = $fDER0.Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.SubstanceData(0.01801528, 0.0, -11675.08030005653, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength, $DER.C.temperature, $DER.C.pressure, 0.0, $DER.C.moleFractionBasedIonicStrength) * log(Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.activityCoefficient(Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.SubstanceData(0.01801528, 0.0, -11675.08030005653, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength)) + Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.SubstanceData(0.01801528, 0.0, -11675.08030005653, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength) * ((1/Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.activityCoefficient(Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.SubstanceData(0.01801528, 0.0, -11675.08030005653, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength)) * $fDER0.Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.activityCoefficient(Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.SubstanceData(0.01801528, 0.0, -11675.08030005653, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength, $DER.C.temperature, $DER.C.pressure, 0.0, $DER.C.moleFractionBasedIonicStrength)) ($RES_SIM_330) (181|185) [SCAL] (1) $DER.C.uPure = $fDER0.Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.molarEnthalpyElectroneutral(Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.SubstanceData(0.01801528, 0.0, -11675.08030005653, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength, $DER.C.temperature, $DER.C.pressure, 0.0, $DER.C.moleFractionBasedIonicStrength) - ($DER.C.temperature * Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.molarEntropyPure(Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.SubstanceData(0.01801528, 0.0, -11675.08030005653, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength) + C.temperature * $fDER0.Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.molarEntropyPure(Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.SubstanceData(0.01801528, 0.0, -11675.08030005653, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength, $DER.C.temperature, $DER.C.pressure, 0.0, $DER.C.moleFractionBasedIonicStrength)) ($RES_SIM_331) (182|186) [SCAL] (1) $DER.C.u0 = -($DER.C.temperature * (39.1584112026045 - (Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.SubstanceData(0.01801528, 0.0, -11675.08030005653, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength) / C.temperature) * ((-1e5) + C.pressure)) - C.temperature * ((($fDER0.Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.SubstanceData(0.01801528, 0.0, -11675.08030005653, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength, $DER.C.temperature, $DER.C.pressure, 0.0, $DER.C.moleFractionBasedIonicStrength) * C.temperature - $DER.C.temperature * Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.SubstanceData(0.01801528, 0.0, -11675.08030005653, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength)) / C.temperature ^ 2.0) * ((-1e5) + C.pressure) + (Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.molarVolumePure(Chemical.Obsolete.Examples.SimpleReaction2.C.stateOfMatter.SubstanceData(0.01801528, 0.0, -11675.08030005653, 0.0, 1.0, 0.0, {\"\"}, 0.0, 0.0, false, 0.0, 0.0, 1000.0), C.temperature, C.pressure, 0.0, C.moleFractionBasedIonicStrength) / C.temperature) * $DER.C.pressure)) ($RES_SIM_332) (183|187) [SCAL] (1) $DER.C.molarEntropyPure = -((1.8015280000000002e-5 / C.temperature) * $DER.C.pressure - ((1.8015280000000002e-5 * $DER.C.temperature) / C.temperature ^ 2.0) * ((-1e5) + C.pressure)) ($RES_SIM_333) =================== Scalar Matching =================== variable to equation ********************** var 1 --> eqn 43 var 2 --> eqn 184 var 3 --> eqn 36 var 4 --> eqn 33 var 5 --> eqn 81 var 6 --> eqn 82 var 7 --> eqn 163 var 8 --> eqn 52 var 9 --> eqn 23 var 10 --> eqn 27 var 11 --> eqn 24 var 12 --> eqn 26 var 13 --> eqn 1 var 14 --> eqn 25 var 15 --> eqn 107 var 16 --> eqn 47 var 17 --> eqn 37 var 18 --> eqn 46 var 19 --> eqn 59 var 20 --> eqn 63 var 21 --> eqn 56 var 22 --> eqn 69 var 23 --> eqn 97 var 24 --> eqn 76 var 25 --> eqn 65 var 26 --> eqn 55 var 27 --> eqn 15 var 28 --> eqn 88 var 29 --> eqn 90 var 30 --> eqn 66 var 31 --> eqn 7 var 32 --> eqn 50 var 33 --> eqn 42 var 34 --> eqn 3 var 35 --> eqn 51 var 36 --> eqn 14 var 37 --> eqn 16 var 38 --> eqn 28 var 39 --> eqn 74 var 40 --> eqn 75 var 41 --> eqn 30 var 42 --> eqn 35 var 43 --> eqn 84 var 44 --> eqn 64 var 45 --> eqn 38 var 46 --> eqn 6 var 47 --> eqn 58 var 48 --> eqn 41 var 49 --> eqn 77 var 50 --> eqn 62 var 51 --> eqn 80 var 52 --> eqn 45 var 53 --> eqn 34 var 54 --> eqn 32 var 55 --> eqn 86 var 56 --> eqn 78 var 57 --> eqn 60 var 58 --> eqn 73 var 59 --> eqn 17 var 60 --> eqn 79 var 61 --> eqn 68 var 62 --> eqn 87 var 63 --> eqn 98 var 64 --> eqn 18 var 65 --> eqn 11 var 66 --> eqn 19 var 67 --> eqn 96 var 68 --> eqn 72 var 69 --> eqn 12 var 70 --> eqn 48 var 71 --> eqn 40 var 72 --> eqn 49 var 73 --> eqn 94 var 74 --> eqn 93 var 75 --> eqn 91 var 76 --> eqn 89 var 77 --> eqn 61 var 78 --> eqn 39 var 79 --> eqn 8 var 80 --> eqn 4 var 81 --> eqn 83 var 82 --> eqn 22 var 83 --> eqn 20 var 84 --> eqn 57 var 85 --> eqn 13 var 86 --> eqn 67 var 87 --> eqn 21 var 88 --> eqn 2 var 89 --> eqn 9 var 90 --> eqn 44 var 91 --> eqn 5 var 92 --> eqn 31 var 93 --> eqn 85 var 94 --> eqn 53 var 95 --> eqn 29 var 96 --> eqn 54 var 97 --> eqn 71 var 98 --> eqn 127 var 99 --> eqn 99 var 100 --> eqn 102 var 101 --> eqn 103 var 102 --> eqn 106 var 103 --> eqn 108 var 104 --> eqn 109 var 105 --> eqn 110 var 106 --> eqn 111 var 107 --> eqn 112 var 108 --> eqn 113 var 109 --> eqn 114 var 110 --> eqn 115 var 111 --> eqn 116 var 112 --> eqn 131 var 113 --> eqn 132 var 114 --> eqn 134 var 115 --> eqn 104 var 116 --> eqn -1 var 117 --> eqn -1 var 118 --> eqn 142 var 119 --> eqn 143 var 120 --> eqn 145 var 121 --> eqn 146 var 122 --> eqn 147 var 123 --> eqn 148 var 124 --> eqn -1 var 125 --> eqn 149 var 126 --> eqn 118 var 127 --> eqn 150 var 128 --> eqn 151 var 129 --> eqn 117 var 130 --> eqn 119 var 131 --> eqn 156 var 132 --> eqn 129 var 133 --> eqn 158 var 134 --> eqn 136 var 135 --> eqn 159 var 136 --> eqn 160 var 137 --> eqn 122 var 138 --> eqn 121 var 139 --> eqn 120 var 140 --> eqn 164 var 141 --> eqn 165 var 142 --> eqn 166 var 143 --> eqn 157 var 144 --> eqn 152 var 145 --> eqn 155 var 146 --> eqn 154 var 147 --> eqn 167 var 148 --> eqn 168 var 149 --> eqn 169 var 150 --> eqn 170 var 151 --> eqn 138 var 152 --> eqn 125 var 153 --> eqn 123 var 154 --> eqn 153 var 155 --> eqn 172 var 156 --> eqn 173 var 157 --> eqn 139 var 158 --> eqn 128 var 159 --> eqn 126 var 160 --> eqn 174 var 161 --> eqn 175 var 162 --> eqn 176 var 163 --> eqn 130 var 164 --> eqn 144 var 165 --> eqn 177 var 166 --> eqn 171 var 167 --> eqn 137 var 168 --> eqn 178 var 169 --> eqn 105 var 170 --> eqn 101 var 171 --> eqn 179 var 172 --> eqn 133 var 173 --> eqn -1 var 174 --> eqn 141 var 175 --> eqn 180 var 176 --> eqn 140 var 177 --> eqn 135 var 178 --> eqn 181 var 179 --> eqn 182 var 180 --> eqn 124 var 181 --> eqn 183 var 182 --> eqn 162 var 183 --> eqn 185 var 184 --> eqn 161 var 185 --> eqn 186 var 186 --> eqn 100 var 187 --> eqn 187 var 188 --> eqn 70 var 189 --> eqn 10 var 190 --> eqn 92 var 191 --> eqn 95 equation to variable ********************** eqn 1 --> var 13 eqn 2 --> var 88 eqn 3 --> var 34 eqn 4 --> var 80 eqn 5 --> var 91 eqn 6 --> var 46 eqn 7 --> var 31 eqn 8 --> var 79 eqn 9 --> var 89 eqn 10 --> var 189 eqn 11 --> var 65 eqn 12 --> var 69 eqn 13 --> var 85 eqn 14 --> var 36 eqn 15 --> var 27 eqn 16 --> var 37 eqn 17 --> var 59 eqn 18 --> var 64 eqn 19 --> var 66 eqn 20 --> var 83 eqn 21 --> var 87 eqn 22 --> var 82 eqn 23 --> var 9 eqn 24 --> var 11 eqn 25 --> var 14 eqn 26 --> var 12 eqn 27 --> var 10 eqn 28 --> var 38 eqn 29 --> var 95 eqn 30 --> var 41 eqn 31 --> var 92 eqn 32 --> var 54 eqn 33 --> var 4 eqn 34 --> var 53 eqn 35 --> var 42 eqn 36 --> var 3 eqn 37 --> var 17 eqn 38 --> var 45 eqn 39 --> var 78 eqn 40 --> var 71 eqn 41 --> var 48 eqn 42 --> var 33 eqn 43 --> var 1 eqn 44 --> var 90 eqn 45 --> var 52 eqn 46 --> var 18 eqn 47 --> var 16 eqn 48 --> var 70 eqn 49 --> var 72 eqn 50 --> var 32 eqn 51 --> var 35 eqn 52 --> var 8 eqn 53 --> var 94 eqn 54 --> var 96 eqn 55 --> var 26 eqn 56 --> var 21 eqn 57 --> var 84 eqn 58 --> var 47 eqn 59 --> var 19 eqn 60 --> var 57 eqn 61 --> var 77 eqn 62 --> var 50 eqn 63 --> var 20 eqn 64 --> var 44 eqn 65 --> var 25 eqn 66 --> var 30 eqn 67 --> var 86 eqn 68 --> var 61 eqn 69 --> var 22 eqn 70 --> var 188 eqn 71 --> var 97 eqn 72 --> var 68 eqn 73 --> var 58 eqn 74 --> var 39 eqn 75 --> var 40 eqn 76 --> var 24 eqn 77 --> var 49 eqn 78 --> var 56 eqn 79 --> var 60 eqn 80 --> var 51 eqn 81 --> var 5 eqn 82 --> var 6 eqn 83 --> var 81 eqn 84 --> var 43 eqn 85 --> var 93 eqn 86 --> var 55 eqn 87 --> var 62 eqn 88 --> var 28 eqn 89 --> var 76 eqn 90 --> var 29 eqn 91 --> var 75 eqn 92 --> var 190 eqn 93 --> var 74 eqn 94 --> var 73 eqn 95 --> var 191 eqn 96 --> var 67 eqn 97 --> var 23 eqn 98 --> var 63 eqn 99 --> var 99 eqn 100 --> var 186 eqn 101 --> var 170 eqn 102 --> var 100 eqn 103 --> var 101 eqn 104 --> var 115 eqn 105 --> var 169 eqn 106 --> var 102 eqn 107 --> var 15 eqn 108 --> var 103 eqn 109 --> var 104 eqn 110 --> var 105 eqn 111 --> var 106 eqn 112 --> var 107 eqn 113 --> var 108 eqn 114 --> var 109 eqn 115 --> var 110 eqn 116 --> var 111 eqn 117 --> var 129 eqn 118 --> var 126 eqn 119 --> var 130 eqn 120 --> var 139 eqn 121 --> var 138 eqn 122 --> var 137 eqn 123 --> var 153 eqn 124 --> var 180 eqn 125 --> var 152 eqn 126 --> var 159 eqn 127 --> var 98 eqn 128 --> var 158 eqn 129 --> var 132 eqn 130 --> var 163 eqn 131 --> var 112 eqn 132 --> var 113 eqn 133 --> var 172 eqn 134 --> var 114 eqn 135 --> var 177 eqn 136 --> var 134 eqn 137 --> var 167 eqn 138 --> var 151 eqn 139 --> var 157 eqn 140 --> var 176 eqn 141 --> var 174 eqn 142 --> var 118 eqn 143 --> var 119 eqn 144 --> var 164 eqn 145 --> var 120 eqn 146 --> var 121 eqn 147 --> var 122 eqn 148 --> var 123 eqn 149 --> var 125 eqn 150 --> var 127 eqn 151 --> var 128 eqn 152 --> var 144 eqn 153 --> var 154 eqn 154 --> var 146 eqn 155 --> var 145 eqn 156 --> var 131 eqn 157 --> var 143 eqn 158 --> var 133 eqn 159 --> var 135 eqn 160 --> var 136 eqn 161 --> var 184 eqn 162 --> var 182 eqn 163 --> var 7 eqn 164 --> var 140 eqn 165 --> var 141 eqn 166 --> var 142 eqn 167 --> var 147 eqn 168 --> var 148 eqn 169 --> var 149 eqn 170 --> var 150 eqn 171 --> var 166 eqn 172 --> var 155 eqn 173 --> var 156 eqn 174 --> var 160 eqn 175 --> var 161 eqn 176 --> var 162 eqn 177 --> var 165 eqn 178 --> var 168 eqn 179 --> var 171 eqn 180 --> var 175 eqn 181 --> var 178 eqn 182 --> var 179 eqn 183 --> var 181 eqn 184 --> var 2 eqn 185 --> var 183 eqn 186 --> var 185 eqn 187 --> var 187 " [Timeout remaining time 660] [Calling sys.exit(0), Time elapsed: 2.5861127888783813] Failed to read output from testmodel.py, exit status != 0: 0.3039963007904589 0.311875958 0.213867198 Calling exit ...