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

delete2023-08-01
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PRE
AI
C
Chuanqi Geng
X
Xiaojia Wu
H
Hui Yu
X
Xinyu Li
C
Chencan Du
Z
Zhiyong Zhou
Z
Zhongqi Ren *
DOI:10.1016/j.ces.2023.118918delete
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Abstract

Abstract

En 中文
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.
Keywords:
Switchable phase-change extraction
Temperature-responsive solvent
Distribution and selectivity coefficients
[BPy][FeCl4]

Journal

Chemical Engineering Science cover
Chemical Engineering Science
IF:
4.3
Papers:
2.2W
Citations:
5.5W

Organization

B
Beijing University of Chemical Technology
Scholars:
3.1W
Papers: 2.2W
Citations: 4.5W
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