Capturing VOCs in the pharmaceutical industry with ionic liquids

被引:23
|
作者
Gui, Chengmin [1 ]
Li, Guoxuan [1 ]
Zhu, Ruisong [1 ]
Lei, Zhigang [1 ,2 ]
Dong, Yichun [3 ]
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
[3] Hefei Univ Technol, Sch Chem & Chem Engn, Hefei 230009, Peoples R China
基金
中国国家自然科学基金;
关键词
Ionic liquids; Absorption; Volatile organic compounds; Quantum chemical calculation; SCREENING MODEL; BINARY-SYSTEMS; VAPOR; SOLVENTS; TOLUENE; UNIFAC; WATER; EQUILIBRIUM; ABSORPTION; BENZENE;
D O I
10.1016/j.ces.2022.117504
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
1-ethyl-3-methylimidazolium acetate ([EMIM][Ac]) was adopted to absorb two common pharmaceutical volatile organic compounds (VOCs), dichloromethane (DCM) and ethanol. The vapor-liquid equilibrium experimental data of the VOC-ionic liquid (IL) systems were measured. The absorption experiment was carried out at 20 degrees C and at ambient pressure, with a gas flow rate of 1 L/min and an absorbent flow rate of 20 mL/min. The results showed that the removal ratios of DCM and ethanol reached 91.82% and 97.01%, respectively. Furthermore, the mechanism of IL capturing DCM and ethanol was systematically studied using the COSMO-RS model and a quantum chemical calculation. The results demonstrated that the separation capability of [EMIM][Ac] mainly depended on the strong [Ac](-)-VOC interaction. Finally, industrial-scale VOC capture processes were established and optimized. The results showed that IL process achieved a lower total heat duty and a higher increase in green degree compared with triethylene glycol process. (C) 2022 Elsevier Ltd. All rights reserved.
引用
收藏
页数:11
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