Equilibrium solubility measurement of carbon dioxide in hybrid solvents of aqueous N-methyldiethanolamine blended with 1-Methyl-3-octyl-imidazolium tetrafluoroborate ionic liquid at high pressures

被引:8
作者
Damanafshan, Milad [1 ]
Mokhtarani, Babak [2 ]
Mirzaei, Mojtaba [2 ]
Sharifi, Ali [2 ]
机构
[1] Islamic Azad Univ, Dept Chem Engn, South Tehran Branch, Tehran, Iran
[2] Chem & Chem Engn Res Ctr Iran CCERCI, POB 14335-186, Tehran, Iran
关键词
N-methyldiethanolamine (MDEA); 1-methyl-3-octyl-imidazolium tetrafluoroborate; Gas-liquid equilibria; CO2; capture; Gas sweetening; CO2; CAPTURE; BINARY-MIXTURES; ABSORPTION; KINETICS; MDEA; MONOETHANOLAMINE; ALKANOLAMINES; PIPERAZINE; GAS; H2S;
D O I
10.1016/j.molliq.2021.116571
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Solubility of CO2 in the hybrid solvents composed of aqueous N-methyldiethanolamine (MDEA) blended with 1-methyl-3-octyl-imidazolium tetrafluoroborate ([Omim][BF4]) ionic liquid (IL) was measured at temperatures from (298.15-343.15 K) and pressures of (0.2-4 MPa). The experimental trials were performed in a static high pressure equilibrium cell to determine the CO2 absorption capacity of novel absorbent solutions based on the isochoric saturation technique. The experimental data showed that, by rising the concentration of IL in the absorbent solutions', the mole fraction of dissolved CO2 gas enhances gradually. Absorption capacity of these aqueous solutions was assessed and compared with pure ILs and alkanolamine solvents, which indicates the solutions studied in this research as better hybrid solvents in terms of CO2 loading. Furthermore, a semi empirical model is used to correlate the solubility data of this work, which presents a good agreement with an absolute average deviation (AAD %) of below 1%. (C) 2021 Elsevier B.V. All rights reserved.
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页数:11
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