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Salt Effect on the Liquid-Liquid Equilibria for the Ternary System Water + N, N-Dimethylformamide (DMF) + Chloroform  ( EI收录)  

文献类型:期刊文献

英文题名:Salt Effect on the Liquid-Liquid Equilibria for the Ternary System Water + N, N-Dimethylformamide (DMF) + Chloroform

作者:Wang, Xiaoyu[1]; Wang, Jiale[2]; Ji, Lijun[1]; Wu, Bin[1]; Chen, Kui[1]; Wu, Yanyang[1]

机构:[1] School of Chemical and Engineering, East China University of Science and Technology, Shanghai, 200237, China; [2] Key Laboratory of Cigarette Smoke of State Tobacco Monopoly Administration, Technical Center of Shanghai Tobacco Corporation, Shanghai, 200082, China

年份:2021

卷号:66

期号:5

起止页码:2233

外文期刊名:Journal of Chemical and Engineering Data

收录:EI(收录号:20211910309819)

语种:英文

外文关键词:Phase equilibria - Ternary systems - Topology - Atmospheric pressure - Sodium sulfate - Solvent extraction - Dimethylformamide - Liquids - Organic solvents

摘要:Wastewater containing DMF (N,N-dimethylformamide) and salt is generated in production of many chemicals and medicines. The composition of phase equilibrium should be known primarily for the recovery of DMF from salt-containing wastewater by solvent extraction. In this study, liquid-liquid equilibrium (LLE) and solubility data of water + DMF + chloroform in the presence of NaCl with various concentrations of 0, 2.5, 5.0, 7.5, 10.0, and 13.3 wt % and Na2SO4 with concentrations of 1.5 and 2.5 wt % were determined at T = 298.2 K and atmospheric pressure. Besides, the salt effect on the LLE data was investigated. Compared with the salt-free system, the salt led to an enhancement in the maximum DMF distribution coefficient by 13.4-102.6% for 2.5-13.3 wt % NaCl and 16.2-31.7% for 1.5-2.5 wt % Na2SO4, respectively. Since the distribution coefficient of water increased concurrently, the separation factor barely changed and the two-phase region expanded outward slightly. At the same salt mass fraction, the order of salting-out effect strength on extraction was Na2SO4 > NaCl, which was in good agreement with the Hofmeister series. The reliability of the experimental values was verified through the Eisen-Joffe equation. The NRTL thermodynamic model was applied to correlate the experimental data with a root-mean-square deviation less than 0.0062. The coherent consistency of the model parameters for the salt-free system was checked by topological analysis based on the Gibbs tangent plane test. ?

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