期刊
ACS SUSTAINABLE CHEMISTRY & ENGINEERING
卷 9, 期 7, 页码 2705-2716出版社
AMER CHEMICAL SOC
DOI: 10.1021/acssuschemeng.0c07866
关键词
Hierarchical ionic liquids screening; IDAC database; QSPR; Liquid-liquid extraction experiment; Process simulation and evaluation; Extractive desulfurization
资金
- China Scholarship Council [201606740070]
A hierarchical hybrid method is proposed to screen suitable ionic liquid (IL) solvents for different extractions, combining experimental database, model, and process simulation, with extractive desulfurization (EDS) as a case study for validation.
A hierarchical hybrid method combining experimental-database-derived estimation of extraction performance, quantitative structure-property relationship (QSPR)-based assessment of IL physical and environmental properties, liquid-liquid extraction (LLE) measurement, and process evaluation is proposed to screen practically suitable ionic liquid (IL) solvents for different extractions. From the literature, 47 424 infinite dilution activity coefficient (IDAC) data including 12 IL families (e.g., imidazolium, pyridinium, ammonium, etc.) and 13 organic families (e.g., alkanes, aromatics, alcohols, etc.) are collected. On the basis of the IDAC data, the extraction performance of ILs for a specific separation can be estimated in terms of the distribution ratio and selectivity at infinite dilution. The ILs with potentially high extraction performance and meeting the physical and environmental properties criteria are selected to perform LLE experiments. Subsequently, process simulation and evaluation using the selected IL solvents are performed by Aspen Plus. To exemplify the proposed method, the extractive desulfurization (EDS) process is taken as a case study, where [EMIM][MESO3] (1-ethyl-3-methylimidazolium methanesulfonate) and [EIM][NO3] (1-ethylimidazolium nitrate) are selected after IDAC database searching and QSPR analysis. Experimental LLE with the two ILs are determined, demonstrating their promising extraction performance with the maximum selectivity (S-23(max)) for thiophene/heptane of 420 and 281.9, respectively. By fitting the NRTL model correspondingly, two processes using the screened ILs and sulfolane are developed and compared using Aspen Plus. It turns out that the two ILs save 66% and 48% in solvent requirements and 54% and 55% in energy consumption compared to those of sulfolane for the EDS task, respectively.
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