Reversible phase-change extraction process based on temperature-responsive solvent

被引:0
|
作者
Geng, Chuanqi [1 ,2 ]
Wu, Xiaojia [1 ]
Yu, Hui [1 ]
Li, Xinyu [1 ]
Du, Chencan [1 ]
Zhou, Zhiyong [1 ,2 ]
Ren, Zhongqi [1 ,2 ]
机构
[1] Beijing Univ Chem Technol, State Key Lab Chem Resource Engn, Beijing 100029, Peoples R China
[2] Beijing Univ Chem Technol, Engn Res Ctr Preparat Technol Ultrapure Chem Integ, Minist Educ, Beijing 100029, Peoples R China
基金
中国国家自然科学基金;
关键词
Switchable phase-change extraction; Temperature-responsive solvent; Distribution and selectivity coefficients; BPy][FeCl4; LIQUID-LIQUID-EXTRACTION; IONIC LIQUID; LIPID EXTRACTION; OXIDATIVE DESULFURIZATION; SWITCHABLE SOLVENTS; TOLUENE; HEPTANE; OIL;
D O I
10.1016/j.ces.2023.118918
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In this study, N-butylpyridinium tetrachloroferrate ([Bpy][FeCl4]), a temperature-responsive solvent, was applied to achieve reversible phase-change extraction with simultaneous solvent recycling for the ethanol/ heptane and toluene/heptane systems. The distribution and selectivity coefficients were 7.87 and 0.862, respectively, for ethanol in the 60 mass% ethanol/heptane system; the corresponding values for toluene in the 20 mass% toluene/heptane system were 1.34 and 44.3, respectively, which are significantly better than those for existing conventional solvents. [BPy][FeCl4] was reused five times in each system, and the extraction efficiency remained stable at high values. The experimental results as a function of temperature and solvent:solute mass ratio showed that the reversible phase-change process by [BPy][FeCl4] could be achieved under a range of conditions. This process achieves switchable phase-change extraction and simultaneous solvent recovery, thus offering the possibility of saving energy, reducing equipment requirements, and simplifying operations.
引用
收藏
页数:9
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