) was prepared and the vapor pressures of three set of binary solutions H
2
O(1)/CH
3
OH(1)/C
2
H
5
OH(1) + [BMIM
]
[DBP
]
(2) were measured at different temperature and in the ILs mole fraction range from 0.1 to 0.6 with a static equilibrium apparatus. The measured vapor pressures were correlated with Non-Random Two Liquid (NRTL) activity coefficient model and the average relative deviations (ARD) between experimental and correlated vapor pressures for these binary solutions were 3.19%
2.42% and 2.95%
respectively. Then
the vapor pressures of two set of ternary solutions H
2
O(1) + CH
3
OH(2)/C
2
H
5
OH(2) + [BMIM
]
[DBP
]
(3) were measured with an inclined boiling apparatus and further predicted with NRTL activity coefficient model based on the binary interaction parameters coming from fitting the vapor pressures of the binary solutions. The results indicated that the ternary solutions containing [BMIM
]
[DBP
]
were shown a strong negative deviation from Raoult's Law when the mole fraction of [BMIM
]
[DBP
]
was larger than 0.2
which meant that ternary solutions coul
d absorb the refrigerant vapors at the same or below solution temperature. Meanwhile
the average relative deviations between experimental and predicted vapor pressures for ternary solutions were 2.92% and 3.06%
respectively. Consequently
the NRTL active coefficient model used for non-electrolyte solutions was still valid for predicting vapor-liquid equilibrium of binary or ternary solutions containing ILs.
关键词
Keywords
references
The trial reading is over, you can activate your VIP account to continue reading.
Vapor pressure measurement and correlation of acetonitrile +1-butyl-3-methylimidazolium chloride, +1-butyl-3-methylimidazolium tetrafluoroborate, and +1-hexyl-3-methylimidazolium chloride
Effect of Mono- and Di-ethanolammonium Formate Ionic Liquids on the Volatility of Water, Ethanol, and Methanol
Vapor Pressure Measurement of Water+1,3-Dimethylimidazolium Tetrafluoroborate System
Impact of CO2 cycloaddition reaction on hydrodynamics and mass transfer behavior of CO2-ionic liquid system in a capillary reactor
Mass transfer and kinetic behavior studies on cycloaddition of carbon dioxide with propylene oxide catalyzed by ionic liquid in microchannel reactor
Related Author
Qing Yang
Kexia Chen
Changchun He
Changjun Peng
Honglai Liu
李雪梅
沈冲
李春喜
Related Institution
State Key Laboratory of Chemical Engineering and Department of Chemistry, East China University of Science and Technology
2 College of Chemical Engineering, Beijing University of Chemical Technology
3 Liming Research Institute of Chemical Industry
College of Chemical Engineering, Beijing University of Chemical Technology
Institute of Process Systems Engineering, College of Chemical Engineering, Qingdao University of Science and Technology