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

被引:6
|
作者
Zhang, Xuemei [1 ]
Hao, Xin [1 ]
Yang, Xiaojie [1 ]
Jian, Chungui [2 ,3 ]
机构
[1] Tianjin Univ, Sch Chem Engn & Technol, Tianjin 300072, Peoples R China
[2] Tianjin Univ Co Ltd, Beiyang Chem Equipment, Tianjin 300072, Peoples R China
[3] Tianjin ZhonghaoUnitech Co Ltd, Tianjin 300072, Peoples R China
来源
JOURNAL OF CHEMICAL THERMODYNAMICS | 2019年 / 136卷
关键词
Vapour-liquid equilibrium; Sec-butyl acetate; Sec-butyl alcohol; N; N-dimethyl acetamide; Dimethyl sulfoxide; TERNARY-SYSTEM; EXTRACTIVE DISTILLATION; IONIC LIQUIDS; FORMAMIDE; 2-BUTANOL; MIXTURES; N; N-DIMETHYLACETAMIDE; DEHYDROGENATION; EXPRESSION; REDUCTION;
D O I
10.1016/j.jct.2019.05.005
中图分类号
O414.1 [热力学];
学科分类号
摘要
Isobaric vapour-liquid equilibrium (VLE) data for the binary system of {N, N-dimethyl acetamide (DMAC) + dimethyl sulfoxide (DMSO)} and the quaternary system of {sec-butyl acetate (SBAC) + sec-butyl alcohol (SBA) + DMAC + DMSO} were measured at 101.3 kPa using a modified Othmer still. The thermodynamic consistency test for the binary experimental data was checked by Van Ness point test. The experimental VLE data of the binary system were correlated with Wilson, NRTL and UNIQUAC activity coefficient models. The binary and quaternary VLE data predicted by the binary interaction parameters agreed well with the experimental data. And the mixed solvent (DMAC + DMSO) can eliminate the pseudo-azeotrope of SBAC and SBA. Thus the mixture of (DMAC + DMSO) is a potential extractive solvent in the separation of the pseudo-azeotrope of SBAC and SBA by extractive distillation. (C) 2019 Elsevier Ltd.
引用
收藏
页码:132 / 140
页数:9
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