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Solubility of CO2 in Acetone, 1-Butyl-3-methylimidazolium Tetrafluoroborate, and Their Mixtures
被引:32
作者:
Lei, Zhigang
[1
]
Qi, Xiaoxi
[1
]
Zhu, Jiqin
[1
]
Li, Qunsheng
[1
]
Chen, Biaohua
[1
]
机构:
[1] Beijing Univ Chem Technol, State Key Lab Chem Resource Engn, Beijing 100029, Peoples R China
关键词:
PRESSURE PHASE-BEHAVIOR;
VAPOR-LIQUID-EQUILIBRIUM;
CARBON-DIOXIDE;
IONIC LIQUID;
THERMODYNAMIC PROPERTIES;
SYSTEMS;
PLUS;
TEMPERATURE;
SOLVENTS;
HYDROGEN;
D O I:
10.1021/je300611q
中图分类号:
O414.1 [热力学];
学科分类号:
摘要:
The phase behavior of binary and ternary mixtures consisting of carbon dioxide (CO2) (1), acetone (2), and 1-butyl-3-methylimidazolium tetrafluoroborate ([BMIM](+)[BF4](-)) (3) was studied experimentally. A high-pressure view-cell technique was used to measure the solubility data in the solvent mixtures of acetone and [BMIM](+)[BF4](-) at various mole contents at temperatures of (298.2, 313.2 and 323.2) K and pressures up to 6.0 MPa. The experimental solubility data were correlated using the Henry's law and Peng-Robinson equation of state (PR EOS), and the magnitude of Henry's constants is in the order of H-X3=0.0 < H-X3=0.060 < H-X3=0.204 < H-X3=0.507 < H-X3=1.0 at a given temperature. Moreover, at a fixed mole ratio of organic solvent to ionic liquid (IL), the solubility of CO2 in the mixture of acetone and [BMIM](+)[BF4](-) is the highest when compared with other previously reported organic solvent + IL separating agents. The mixtures of acetone and [BMIM](+)[BF4](-) may be used as a potential solvent for industrial application for capturing CO2 efficiently and effectively.
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页码:3458 / 3466
页数:9
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