| 1 |
Modelling of planar and spherical phase interfaces for multicomponent systems using density gradient theory
Celny D, Vins V, Hruby J
Fluid Phase Equilibria, 483, 70, 2019 |
| 2 |
Isobaric vapour-liquid equilibrium for binary systems of ethyl iodide with ethanol, propionic acid and ethyl propionate at 101.3 kPa
Pan JH, Li XJ, Zhang WJ, Cui W, Zhou ZH, Liu DH
Journal of Chemical Thermodynamics, 132, 23, 2019 |
| 3 |
Vapour-liquid equilibrium and extractive distillation for separation of azeotrope isopropyl alcohol and diisopropyl ether
Zhang Y, Liu K, Wang ZJ, Gao J, Zhang LZ, Xu DM, Wang YL
Journal of Chemical Thermodynamics, 131, 294, 2019 |
| 4 |
Experimental and predicted vapor-liquid equilibrium for binary systems with diethanolamine, m-cresol and p-cresol at 20.0 kPa
Wang J, Wang DY, Huang CX, Sun XN, Yue XY, Shao H, Leng YX
Journal of Chemical Thermodynamics, 130, 1, 2019 |
| 5 |
Separation of the mixture (isopropyl alcohol plus diisopropyl ether plus n-propanol): Entrainer selection, interaction exploration and vapour-liquid equilibrium measurements
Zhang Y, Diao BT, Xu DM, Jiang HH, Zhang LZ, Gao J, Wang YL
Journal of Chemical Thermodynamics, 135, 27, 2019 |
| 6 |
Vapour-liquid equilibrium measurements and extractive distillation process design for separation of azeotropic mixture (dimethyl carbonate plus ethanol)
Liu K, Wang ZJ, Zhang Y, Xu DM, Gao J, Ma Z, Wang YL
Journal of Chemical Thermodynamics, 133, 10, 2019 |
| 7 |
Separation of azeotropic mixture (2, 2, 3, 3-Tetrafluoro-1-propanol + water) by extractive distillation: Entrainers selection and vapour-liquid equilibrium measurements
Li R, Meng XL, Liu XW, Gao J, Xu DM, Wang YL
Journal of Chemical Thermodynamics, 138, 205, 2019 |
| 8 |
Measurement and correlation of isobaric vapour-liquid equilibrium for the (acetonitrile plus water) system containing different ionic liquids at atmospheric pressure
Li JL, Li JS, Zheng YL, Peng CJ, Liu HL
Journal of Chemical Thermodynamics, 138, 366, 2019 |
| 9 |
Experimental isobaric vapour-liquid equilibrium data for the binary system (N, N-dimethyl acetamide plus dimethyl sulfoxide) and the quaternary system (sec-butyl acetate plus sec-butyl alcohol plus N, N-dimethyl acetamide plus dimethyl sulfoxide) at 101.3 kPa
Zhang XM, Hao X, Yang XJ, Jian CG
Journal of Chemical Thermodynamics, 136, 132, 2019 |
| 10 |
Measurement and correlation of isobaric vapour-liquid equilibrium for systems of o-cresol, m-cresol and 2, 6-dimethylphenol at 20.0 kPa
Wang J, Ou J, Sun XN, Huang CX, Sun JR, Shao H, Leng YX
Fluid Phase Equilibria, 459, 44, 2018 |
