The
adsorption of pure SO2 and H2S and their
selective adsorption from various gas mixtures by porous aromatic
frameworks (PAFs) are investigated using grand canonical Monte Carlo
(GCMC) simulations and first-principles density functional theory
calculations. The influence of functional groups including −CH3, −CN, −COOH, −COOCH3, −OH,
−OCH3, −NH2, and −NO2 on the adsorption of pure SO2 and H2S as well as selective capture of SO2 and H2S from SO2/N2, SO2/CO2, H2S/CO2, and H2S/CH4 mixtures is explored. Our calculations indicate that PAFs exhibit
high loadings for pure SO2 and H2S gas adsorption
at 298 K up to 40 bar compare to other gases such as CH4 and CO2. Additional functional groups enhance gas uptake
at low pressures because of stronger interaction with the gas molecules
while reducing gas uptake at high pressures because of a decrease
in pore volume. The contributions of electrostatic interactions to
gas adsorption loadings are analyzed in GCMC simulations. Ideal adsorbed
solution theory calculations generally overestimate SO2 and H2S adsorption selectivity in gas mixtures but qualitatively
predict the trends seen in GCMC simulations for these systems. The
GCMC simulations further show that the inclusion of any of the functional
groups we considered increases the selectivity of SO2/N2, SO2/CO2, H2S/CO2, and H2S/CH4 relative to unfunctionalized
materials. Electron-withdrawing groups such as −CN, −COOH,
−COOCH3, and −NO2 are more effective
at enhancing adsorption selectivity in this work. The highest selectivity
in the PAFs functionalized by these groups is predicted at the lowest
temperature we considered (273 K), whereas it occurs at 298 K for
PAFs with other functional groups.