(537f) Effect of Ionic Liquid Molar Volume on CO2/N2 and CO2/CH4 Pure and Mixed Gas Solubility Selectivity
AIChE Annual Meeting
2024
2024 AIChE Annual Meeting
Innovations in Process Engineering
Ionic Liquids: Novel Separation, Catalytic reaction and Electrochemical Processes
Wednesday, October 30, 2024 - 1:45pm to 2:00pm
Ionic liquids (ILs) are alternative candidates for CO2 capture due to their negligible vapor pressure, and ability to tune the cations and anions based on the application needs. This class of solvents have been evaluated extensively to capture CO2 from post-combustion and natural gas. However, solubility data of the less soluble N2 and CH4 are very scarce, which makes it difficult to select the right IL that would yield the best CO2/N2 and CO2/CH4 solubility selectivity for these industrial applications. Using COSMO-RS and available literature data, we screened multiple ILs and selected eight candidates ([bmim][Tf2N], [bmim][DCA], [bmim][TfO], [bmim][SCN], [bmim][NO3], [bmim][TCM], [amim][DCA], [10201mim][Tf2N]) based on estimated solubility selectivity. We measured N2 and CH4 solubility in these ILs, using a gravimetric apparatus up to 140 bar to reduce uncertainty, and obtain more accurate solubilities, and pure gas CO2/N2 and CO2/CH4 selectivities. ILs with small molar volumes yield higher solubility selectivity because N2 and CH4 solubilities are lower, presumably due to less free volume in the IL. We have also investigated mixed gas solubility selectivity for the ILs with the highest selectivities based on the pure gas measurements since real mixed gas selectivities are frequently lower than the estimates from pure gas solubilities. For this purpose, we developed a mixed gas sorption system to investigate the phase behavior of ILs with CO2/CH4 and CO2/N2 mixtures. In particular, we seek to gain a fundamental understanding on the effect of highly soluble CO2 dissolution on the solubility of the less soluble gas (CH4 or N2). We have investigated CO2/CH4 and CO2/N2 mixtures at various gas compositions in ILs at partial pressures up to 30 bar at 35 ËC. The mixed gas solubilities in the IL are obtained by analyzing the number of moles of desorbed gas from the IL in a 5 cm3 sample chamber that expands into a 500 cm3 ballast volume, with the compositions determined with gas chromatography. The real mixed gas selectivity is compared to the ideal pure gas selectivity of these gases previously measured gravimetrically and the subsequent Henryâs law constants derived from these isotherms.