Capturing Condensable Gases with Ionic Liquids

被引:44
|
作者
Yu, Gangqiang [1 ]
Dai, Chengna [1 ]
Gao, Hui [1 ]
Zhu, Ruisong [1 ]
Du, Xiaoxiao [1 ]
Lei, Zhigang [1 ]
机构
[1] Beijing Univ Chem Technol, State Key Lab Chem Resource Engn, Beijing Key Lab Energy Environm Catalysis, Box 266, Beijing 100029, Peoples R China
基金
国家重点研发计划; 中国国家自然科学基金;
关键词
VOLATILE ORGANIC-COMPOUNDS; COSMO-RS; THERMAL-STABILITY; PHASE-EQUILIBRIA; SCREENING MODEL; BINARY-MIXTURES; UNIFAC MODEL; ABSORPTION; SOLVENTS; EXTRACTION;
D O I
10.1021/acs.iecr.8b02420
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Ionic liquids (ILs) have been proposed to simultaneously capture a variety of condensable gases for the first time. The hydrophobic IL [EMIM][Tf2N] was selected as a suitable absorbent screened by the COSMO-RS (conductor-like screening model for real solvents) model, which in combination with the quantum chemistry calculation provided some theoretical insight into mechanisms with respect to condensable gas capture. Considering the simultaneous capture of volatile organic compounds (VOCs) and water, we selected benzene, toluene, and p-xylene (BTX) as three kinds of VOC representatives, measured the vapor-liquid equilibrium (VLE) of BTX + [EMIM][Tf2N] mixture systems, and compared them with the predicted results by the UNIFAC-Lei model. The experiment of capturing condensable gases with [EMIM][Tf2N] as the absorbent was conducted. Furthermore, the conceptual design of continuous processes with [EMIM][Tf2N] and the conventional benchmark solvent triethylene glycol as absorbents at the industrial scale was performed using a rigorous equilibrium stage model with the UNIFAC-Lei model parameter input. It reveals that condensable gas capture with an IL belongs to a typical process intensification technology in chemical engineering.
引用
收藏
页码:12202 / 12214
页数:13
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