文献类型：期刊文献

英文题名：Measurement and thermodynamic modeling of ternary (liquid + liquid) equilibria for extraction of 2,3-butanediol from aqueous solution with different solvents at T = 298.2 K, T = 308.2 K, and T = 318.2 K

作者：Wu, Yanyang[1]; Chen, Weipeng[1]; Li, Renlong[1]; Wu, Bin[1]; Ji, Lijun[1]; Chen, Kui[1]

机构：[1] State Key Laboratory of Chemical Engineering, School of Chemical Engineering, East China University of Science and Technology, Shanghai, China

年份：2022

卷号：209

期号：5

起止页码：636

外文期刊名：Chemical Engineering Communications

收录：EI(收录号：20211110064904)

语种：英文

外文关键词：Liquids - Topology - Alcohols

摘要：Liquid ? liquid equilibrium (LLE) data for the water + 2,3-butanediol (2,3-BD) + solvent (n-hexanol or iso-pentanol) ternary systems were obtained at different temperatures (298.2, 308.2, and 318.2 K) under 101.3 kPa. Distribution coefficients and separation factors were calculated accordingly. Distribution coefficients and separation factors were greater than 0.2 and 2.5, respectively, for both n-hexanol and iso-pentanol, which indicated that they were feasible to extract 2,3-BD from aqueous solution. Meanwhile, the reliability of the experimental LLE data was confirmed by both Othmer ? Tobias equation and Hand equation. Lastly, the LLE data were correlated by both thermodynamic nonrandom two-liquid (NRTL) and universal quasi-chemical (UNIQUAC) models, and their binary interaction parameters were correlated from the data. In addition, topological analysis related to the Gibbs minor common tangent test was applied to validate the binary interaction parameters. Supplemental data for this article is available online at here. ? 2021 Taylor & Francis Group, LLC.