| 1 - 18 |
Prediction of phase equilibria for CO2-C2H5OH-H2O system using the SAFT equation of state
Zhang ZY, Yang JC, Li YG |
| 19 - 30 |
Equation of state for long-chain n-alkanes
Eslami H |
| 31 - 47 |
Evaluation of vapor-liquid equilibrium of ethane binary systems using UNIQUAC-based mixing rules and its extension to multicomponent systems
Saghafi A, Moshfeghian M |
| 49 - 64 |
Improving phase equilibrium calculation with the Peng-Robinson EOS for fats and oils related compounds/supercritical CO2 systems
Araujo ME, Meireles MAA |
| 65 - 73 |
Partial miscibility behavior of the ternary mixture carbon dioxide plus n-tetradecane plus acetone
Foreman CM, Luks KD |
| 75 - 84 |
Vapor-liquid equilibrium data and their correlation for binary systems consisting of ethanol, 2-propanol, 1,2-ethanediol and methyl benzoate
Li JD, Chen CX, Wang J |
| 85 - 99 |
Vapour-liquid equilibria - XIV. The ternary system cyclohexane-methanol-hexane at 293.15 K
Goral M, Oracz P, Warycha S |
| 101 - 115 |
Equilibrium data and thermodynamic modelling of isopentane and 2,2-dimethylpentane hydrates
Ostergaard KK, Tohidi B, Danesh A, Burgass RW, Todd AC |
| 117 - 125 |
Activity coefficients of hydrocarbons in polycarbonate by gas chromatography
Kikic I, Alessi P, Cortesi A |
