Article ID | Journal | Published Year | Pages | File Type |
---|---|---|---|---|
204076 | Fluid Phase Equilibria | 2008 | 6 Pages |
Abstract
(Liquid–liquid) equilibrium (LLE) data of the solubility curves and tie-line compositions have been determined for mixtures of (water + 2,3-butanediol + 1-butanol) at 298.15, 308.15 and 318.15 K and atmospheric pressure. Distribution coefficients and separation factors have been evaluated for the immiscibility region. The reliability of the experimental tie-lines has been confirmed by using Othmer–Tobias correlation. The LLE data of the ternary systems have been predicted by UNIFAC method.
Related Topics
Physical Sciences and Engineering
Chemical Engineering
Chemical Engineering (General)
Authors
Yan-Yang Wu, Jia-Wen Zhu, Kui Chen, Bin Wu, Jiang Fang, Ya-Ling Shen,