Application of the Aldolization Reaction in Separating the Mixture of Ethylene Glycol and 1,2-Butanediol: Thermodynamics and New Separation Process

被引:33
作者
Li, Hong [1 ,2 ,3 ]
Huang, Weijin [1 ,3 ]
Li, Xingang [1 ,2 ,3 ]
Gao, Xin [1 ,2 ,3 ]
机构
[1] Tianjin Univ, Sch Chem Engn & Technol, Tianjin 300072, Peoples R China
[2] Natl Engn Res Ctr Distillat Technol, Tianjin 300072, Peoples R China
[3] Collaborat Innovat Ctr Chem Sci & Engn Tianjin, Tianjin 300072, Peoples R China
基金
国家高技术研究发展计划(863计划); 中国国家自然科学基金;
关键词
VAPOR-LIQUID-EQUILIBRIUM; DIMETHYL OXALATE; BINARY-SYSTEM; EXTRACTIVE DISTILLATION; CU/SIO2; CATALYSTS; HYDROGENATION; PRESSURE; ACETATE; KPA;
D O I
10.1021/acs.iecr.6b02469
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The separation of ethylene glycol (EG) and 1,2-butanediol (1,2-BDO) azeotrope is a key technical problem in the synthesis process of EG via dimethyl oxalate (DMO) from syngas. On the basis of systematic investigation, aldolization is expected to be the solution to this industrial problem. Thus, the essential thermodynamics data were determined and correlated well by the corresponding thermodynamic equation, including the vapor pressure of 2-methyl-1,3-dioxolane (2MD) and 4-ethyl-2-methyl-1,3-dioxolane (4EMD), vapor-liquid equilibrium (VLE) data of binary mixture 2MD-4EMD at 101.3 kPa, and liquid-liquid equilibrium (LLE) data of binary system 4EMD-water at atmospheric conditions. The vapor-liquid-liquid equilibrium (VLLE) of binary system 4EMD-water has been successful predicted by LLE experimental data. Finally, the thermodynamics parameters were provided as a reference to design a separation process of the EG and 1,2-BDO mixture. The simulation and optimization results indicate that EG and 1,2-BDO could been separated effectively, which presents the potential of applying aldolization in synthesis of EG basic coal.
引用
收藏
页码:9994 / 10003
页数:10
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