Journal
JOURNAL OF CHEMICAL AND ENGINEERING DATA
Volume 65, Issue 2, Pages 617-627Publisher
AMER CHEMICAL SOC
DOI: 10.1021/acs.jced.9b00833
Keywords
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Funding
- C1 Gas Refinery Program through the National Research Foundation of Korea (NRF) - Ministry of Science, ICT AMP
- Future Planning [NRF-2017M3D3A1A01037006-2]
- Human Resources Program in Energy Technology of the Korea Institute of Energy Technology Evaluation and Planning (KETEP) from the Ministry of Trade, Industry AMP
- Energy, Republic of Korea [20174010201150]
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The solubility of carbon dioxide (CO2) in three different ionic liquids (ILs): 1-ethyl-3-methylimidazolium 1,1,2,2-tetrafluoroethanesulfonate ([EMIM] [TFES]), 1-butyl-3-methylimidazolium 1,1,2,2-tetrafluoroethanesulfonate ([BMIM][TFESD, and 1-benzy1-3-methylimidazolium 1,1,2,2-tetrafluoroethanesulfonate ([BNMIM][TFES]) were measured. Measurements were done at temperatures ranging from 303.2 to 373.2 K (323.2 to 373.2 K for [BNMIM][TFES]) at pressures from 0.80 to 36.80 MPa. Measured data show that pressure, temperature, and characteristics of cation of ILs ([EMIM], [BMIM], and [BNMIM]) affect its CO2 solubility. We determined the CO, solubility of fixed CO2 mole fractions for three ionic liquids. Among the three ILs, CO2 solubility intensity was ranked [BMIM] TFES] > [EMIM] TFES] approximate to [BNMIM] [TFES]. The Peng Robinson equation of state, the conventional van der Waals one -fluid mixing rule, and the modified Lydersen Joback Reid method were used to correlate the experimental data. The average absolute deviations of pressure were 0.0164 for CO2 + [EMIM] [TFES], 0.0361 for CO2 + [BMIM] [TFES], and 0.0251 for CO2 + [BNMIM] [TFES] systems.
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