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Correlation and prediction of thermodynamic properties of dilute solutes in water up to high T and P. I. Simple fluids He, Ne, Ar, Kr, Xe, Rn, H-2, N-2, O-2, CO, CH4 Plyasunov AV, Korzhinskaya VS, O'Connell JP Fluid Phase Equilibria, 498, 9, 2019 |
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Thermodynamic properties of dilute hydrogen in supercritical water Plyasunov AV, Bazarkina EE Fluid Phase Equilibria, 470, 140, 2018 |
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Isothermal vapour-liquid equilibrium data for the binary systems 2-propanone + (2-butanol or propanoic acid) Pillay J, Iwarere SA, Raal JD, Naidoo P, Ramjugernath D Fluid Phase Equilibria, 433, 119, 2017 |
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ONE-DIMENSIONAL DIESEL SPRAY MODELING OF MULTICOMPONENT FUELS Pastor JV, Garcia-Oliver JM, Pastor JM, Vera-Tudela W Atomization and Sprays, 25(6), 485, 2015 |
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Theory-based constraints on variations of infinite dilution partial molar volumes of aqueous solutes at various temperatures and water densities Plyasunov AV Fluid Phase Equilibria, 375, 11, 2014 |
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Vapour-liquid equilibrium of propionic acid plus caproic acid, isobutyric acid plus caproic acid, valeric acid plus caproic acid and caproic acid plus enanthoic acid binary mixtures Hlengwere A, Iwarere SA, Naidoo P, Raal JD, Ramjugernath D Fluid Phase Equilibria, 375, 201, 2014 |
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Effect of composition and nonideal solution behavior on desalination calculations for mixed electrolyte solutions with comparison to seawater Mistry KH, Hunter HA, Lienhard JH Desalination, 318, 34, 2013 |
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Steam solubilities of solid MoO3, ZnO and Cu2O, calculated on a basis of a thermodynamic model Akinfiev NN, Plyasunov AV Fluid Phase Equilibria, 338, 232, 2013 |
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IMPLEMENTATION OF MATHEMATICA FOR DEVELOPMENT AND APPLICATION OF EOS MODELS. II: DERIVATION OF THE GENERALIZED EXPRESSION FOR THE FUGACITY COEFFICIENTS OF COMPOUNDS IN A MIXTURE Polishuk I, Kapry I, Madar M Chemical Engineering Communications, 196(4), 448, 2009 |
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Some useful expressions for deriving component fugacity coefficients from mixture fugacity coefficient Hu JW, Wang R, Mao SD Fluid Phase Equilibria, 268(1-2), 7, 2008 |