Capturing low-carbon alcohols from CO2 gas with ionic liquids

被引:11
|
作者
Zhu, Ruisong [1 ]
Huang, Shuai [1 ]
Gui, Chengmin [1 ]
Li, Guoxuan [1 ]
Lei, Zhigang [1 ,2 ]
机构
[1] Beijing Univ Chem Technol, State Key Lab Chem Resource Engn, Box 266, Beijing 100029, Peoples R China
[2] Shihezi Univ, Sch Chem & Chem Engn, Shihezi 832003, Peoples R China
基金
中国国家自然科学基金;
关键词
Ionic liquids (ILs); Low-carbon alcohols; Vapor-liquid equilibrium (VLE); Weak interactions; Quantum chemistry calculation; METHANOL-ETHANOL; EXTRACTIVE DISTILLATION; COSMO-RS; SEPARATION; WATER; SYSTEMS; BINARY; MODEL; UNIFAC; BOND;
D O I
10.1016/j.ces.2022.117745
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Ionic liquids (ILs) as green solvents were first proposed to capture low-carbon alcohols (e.g., methanol, ethanol and 1-propanol) from the syngas tail gas. The vapor-liquid equilibrium (VLE) data for the binary mixtures of low-carbon alcohols with 1-ethyl-3-methyl-imidazolium diethyl phosphate ([EMIM][DEP]) were experimentally measured. The UNIFAC-Lei model demonstrated the best performance in predicting VLE data among all the investigated predictive molecular thermodynamic models. However, the COSMOSAC-UNIFAC model could reproduce the low-carbon alcohols gas absorption characteristics without any experimental data input, and was more accurate than the original UNIFAC and COSMO-SAC models in this case. Using quantum chemistry calculations and wave function analysis, the separation mechanism was revealed on a molecular level. The relationship between thermodynamic behaviors and hydrogen bond interactions in CO2-low-carbon alcohols-[EMIM][DEP] systems was systematically explored. Additionally, theoretical guidance for the design and screening of task-specific ILs in condensable gas separation processes was provided. (C) 2022 Elsevier Ltd. All rights reserved.
引用
收藏
页数:14
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