Room-temperature ionic liquids (RT-ILs) generally have negligibly small vapor pressure, high thermal and chemical stability, and can have higher solubilities of acidic gases such as CO
2, H
2S, NO
x and SO
x than those of normal gases, N
2, H
2, and O
2. These attractive properties could lead the way to clean gas separation technologies that eliminate emissions of the liquid absorbent into the atmosphere. We have proposed an effective CO
2 separation process from gas mixtures by physical absorption using ionic liquids. Since the efficiency in the physical absorption process is predominantly determined by the gas solubility in a unit volume/weight of absorbent, it is of primary importance to develop highly CO
2 absorbing ILs.
In the present study, we have investigated the effect of anions (i.e., TFSA-; = bis(trifluoromethanesulfonyl)amide, BETA-; = bis(tetrafluoroethanesulfonyl)amide, and NFBS-; = nonafluorobutanesulfonate) for 1-ethyl-3-methylimidazolium cation [Emim] on CO2 absorption using a Magnetic Suspension Balance at 313.2 K and up to 6 MPa.
The CO2 solubility in ionic liquids increased with increasing pressure. [Emim][BETA] showed highest CO2 solubility compared with the other ones, especially, the solubility is increased about 4% in comparison with [TFSA] which have a similar structure. On the other hand, [Emim][NFBS] showed 30% higher CO2 solubility at 3 MPa, compared with [Emim][OTf] (1-ethyl-3-methylimidazolium trifluoromethanesulfonate). The symmetrical structure such as TFSA- and BETA- shows a higher CO2 solubility rather than the asymmetric structure such as NFBS- and OTf-. CO2 solubility was increased with the extension of the perfluoroalkyl chain length of the anion.