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@article{MM_2023_35_4_a2, author = {S. A. Zakharov and V. V. Pisarev}, title = {Quasi-Newton single-phase stability testing without explicit {Hessian} calculation}, journal = {Matemati\v{c}eskoe modelirovanie}, pages = {51--64}, publisher = {mathdoc}, volume = {35}, number = {4}, year = {2023}, language = {ru}, url = {http://geodesic.mathdoc.fr/item/MM_2023_35_4_a2/} }
TY - JOUR AU - S. A. Zakharov AU - V. V. Pisarev TI - Quasi-Newton single-phase stability testing without explicit Hessian calculation JO - Matematičeskoe modelirovanie PY - 2023 SP - 51 EP - 64 VL - 35 IS - 4 PB - mathdoc UR - http://geodesic.mathdoc.fr/item/MM_2023_35_4_a2/ LA - ru ID - MM_2023_35_4_a2 ER -
S. A. Zakharov; V. V. Pisarev. Quasi-Newton single-phase stability testing without explicit Hessian calculation. Matematičeskoe modelirovanie, Tome 35 (2023) no. 4, pp. 51-64. http://geodesic.mathdoc.fr/item/MM_2023_35_4_a2/
[1] Z. Chen Z., G. Huan, Y. Ma, Computational methods for multiphase flows in porous media, Society for Industrial and Applied Mathematics, Philadelphia, 2006, 531 pp.
[2] O. Polivka, J. Mikyska, “Compositional Modeling of Two-Phase Flow in Porous Media Using Semi-Implicit Scheme”, IAENG Internat. J. of Applied Mathematics, 45:3 (2015), 9
[3] E. V. Usov et al, “Modelling Multiphase Flows of Hydrocarbons in Gas-Condensate and Oil Wells”, Math. Models. Comput. Simul., 12 (2020), 1005–1013
[4] M. J. Assael et al, “Correlation and prediction of dense fluid transport coefficients. III. n-alkane mixtures”, Int. J. Thermophys., 13:4 (1992), 659–669
[5] F. Ciotta, J. P.M. Trusler, V. Vesovic, “Extended hard-sphere model for the viscosity of dense fluids”, Fluid Phase Equilibria, 363 (2014), 239–247
[6] A. Gerasimov, I. Alexandrov, B. Grigoriev, “Modeling and calculation of thermodynamic properties and phase equilibria of oil and gas condensate fractions based on two generalized multiparameter equations of state”, Fluid Phase Equilibria, 418 (2016), 204–223
[7] B. Grigoriev, I. Alexandrov, A. Gerasimov, “Application of multiparameter fundamental equations of state to predict the thermodynamic properties and phase equilibria of technological oil fractions”, Fuel, 215 (2018), 80–89
[8] O. Iu. Batalin, A. I. Brusilovski, M. Iu. Zakharov, Fazovye ravnovesiia v sistemakh prirodnykh uglevodorodov, Nedra, M., 1992, 272 pp.
[9] T. Jindrova, J. Mikyska, “Fast and robust algorithm for calculation of two-phase equilibria at given volume, temperature, and moles”, Fluid Phase Equilibria, 353 (2013), 101–114
[10] J. Mikyska, A. Firoozabadi, “Investigation of mixture stability at given volume, temperature, and number of moles”, Fluid Phase Equilibria, 321 (2012), 1–9
[11] J. Mikyska, A. Firoozabadi, “A new thermodynamic function for phase-splitting at constant temperature, moles, and volume”, AIChE J., 57:7 (2011), 1897–1904
[12] M. Cismondi, P. M. Ndiaye, F. W. Tavares, “A new simple and efficient flash algorithm for T-v specifications”, Fluid Phase Equilibria, 464 (2018), 32–39
[13] D. V. Nichita, M. Petitfrere, “Phase equilibrium calculations with quasi-Newton methods”, Fluid Phase Equilibria, 406 (2015), 194–208
[14] D. V. Nichita, “Fast and robust phase stability testing at isothermal-isochoric conditions”, Fluid Phase Equilibria, 447 (2017), 107–124
[15] M. Petitfrere, D. V. Nichita, “On a choice of independent variables in Newton iterations for multiphase flash calculations”, Fluid Phase Equilibria, 427 (2016), 147–151
[16] M. Petitfrere, D. V. Nichita, “A comparison of conventional and reduction approaches for phase equilibrium calculations”, Fluid Phase Equilibria, 386 (2015), 30–46
[17] M. Fathi, S. Hickel, “Rapid multi-component pase-split calculations using volume functions and reduction methods”, AIChE J., 67:6 (2021)
[18] M. Benedict, G. B. Webb, L. C. Rubin, “An Empirical Equation for Thermodynamic Propeties of Light Hydrocarbons and Their Mixtures I. Methane, Ethane, Propane and n-Butane”, The Journal of Chemical Physics, 8:4 (1940), 334–345
[19] O. Kunz, W. Wagner, “The GERG-2008 Wide-Range Equation of State for Natural Gases and Other Mixtures: An Expansion of GERG-2004”, J. Chem. Eng. Data, 57:11 (2012), 3032–3091
[20] I. Alexandrov, A. Gerasimov, B. Grigor'ev, “Generalized Fundamental Equation of State for the Normal Alkanes C5-C50”, Int. J. Thermophys., 34:10 (2013), 1865–1905
[21] J. Gross, G. Sadowski, “Perturbed-Chain SAFT: An Equation of State Based on a Perturbation Theory for Chain Molecules”, Ind. Eng. Chem. Res., 40:4 (2001), 1244–1260
[22] J. Nocedal, S. J. Wright, Numerical optimization, 2nd ed., Springer, NY, 2006, 664 pp.
[23] A. I. Brusilovsky, “Mathematical Simulation of Phase Behavior of Natural Multicomponent Systems at High Pressures with an Equation of State”, SPE Reservoir Engineering, 7:01 (1992), 117–122
[24] I. Polishuk, “Standardized Critical Point-Based Numerical Solution of Statistical Association Fluid Theory Parameters: The Perturbed Chain-Statistical Association Fluid Theory Equation of State Revisited”, Ind. Eng. Chem. Res., 53:36 (2014), 14127–14141
[25] W. W. Hager, H. Zhang, “A New Conjugate Gradient Method with Guaranteed Descent and an Efficient Line Search”, SIAM J. Optim., 16:1 (2005), 170–192
[26] J. F. Blinn, “How to Solve a Cubic Equation, Part 5: Back to Numerics”, IEEE Comput. Graph. Appl., 27:3 (2007), 78–89
[27] V. Pisarev, C. Zakharov, CubicEoS.jl., https://github.com/vvpisarev/CubicEoS.jl
[28] V. Pisarev, C. Zakharov, Downhill.jl., https://github.com/vvpisarev/Downhill.jl
[29] V. Pisarev, C. Zakharov, CP_PC_SAFT.jl., https://github.com/vvpisarev/CP_PC_SAFT.jl
[30] J. Bezanson et al, “Julia: A Fresh Approach to Numerical Computing”, SIAM Rev, 59:1 (2017), 65–98
[31] P. Linstrom, NIST Chemistry WebBook, NIST Standard Reference Database 69, National Institute of Standards and Technology, 1997
[32] A. Chiko et al, “Comparison of CP-PC-SAFT and SAFT-VR-Mie in Predicting Phase Equilibria of Binary Systems Comprising Gases and 1-Alkyl-3-methylimidazolium Ionic Liquids”, Molecules, 26:21 (2021), 6621
[33] V. P. Voronov et al, “Phase Behavior of Methane-Pentane Mixture in Bulk and in Porous Media”, Transport in Porous Media, 52 (2003), 18