| 1 |
A simple and reliable procedure to accurately estimate NRTL interaction parameters from liquid-liquid equilibrium data
Diaz I, Rodriguez M, Gonzalez EJ, Gonzalez-Miquel M
Chemical Engineering Science, 193, 370, 2019 |
| 2 |
Measurement of Isobaric Vapor-Liquid Equilibria for Binary Systems Containing Tetrahydrofuran Using an Automatic Apparatus
Matsuda H, Kamihama N, Kurihara K, Tochigi K, Yokoyama K
Journal of Chemical Engineering of Japan, 44(3), 131, 2011 |
| 3 |
Isobaric Vapor-Liquid Equilibria for Ethylbenzene plus p-Xylene System and Separation by Distillation
Matsuda H, Yokoyama K, Kyuzaki H, Kurihara K, Tochigi K
Journal of Chemical Engineering of Japan, 43(3), 247, 2010 |
| 4 |
Recommended NRTL Model Parameters by Simultaneous Correlation of VLE, Infinite Dilution Activity Coefficients and Excess Enthalpy Data
Tochigi K, Rarey J, Gmehling J
Journal of Chemical Engineering of Japan, 42(6), 376, 2009 |
| 5 |
Determination of NRTL parameters for aqueous solutions using a vapor hold-up compensable ebulliometer
Uno S, Matsuda H, Kurihara K, Tochigi K, Ochi K
KAGAKU KOGAKU RONBUNSHU, 33(5), 391, 2007 |
| 6 |
Estimation of isobaric vapor-liquid-liquid equilibria for partially miscible mixture of ternary system
Kosuge H, Iwakabe K
Fluid Phase Equilibria, 233(1), 47, 2005 |
