Effect of H 2 O Vapor on the Adsorption and Desorption Behavior of CO 2 in a Solid Amine Sorbent
The effect of H 2 O vapor on the adsorption and desorption of CO 2 and vice versa, both on a commercially viable solid amine sorbent (SAS), were studied using a thermogravimetric analyzer at constant temperature. The SAS was prepared by physically immobilizing PEI (M n 423) in a porous silica (CARiACT G10). Studies were carried out at two concentrations of CO 2 (2 vol % in N 2 and 100 vol %), one concentration of H 2 O vapor (2 vol %), and four temperatures (40, 60, 80, and 100 °C). The results revealed three separate and identifiable mechanisms or processes taking place on the SAS, i.e., the individual adsorption of CO 2 or H 2 O and the coadsorption of H 2 O and CO 2 . The individual adsorption of either CO 2 or H 2 O was noncompetitive or completely independent of each other thermodynamically for both concentrations of CO2 and all four temperatures. In addition, the individual adsorption of CO 2 was fully reversible, while the individual adsorption of H 2 O was only partially reversible. The coadsorption of CO 2 and H 2 O was exothermic, with either irreversible or very slow desorption kinetics. Coadsorption was observed appreciably only at 60 and 40 °C at both CO 2 concentrations and only very slightly at 80 °C and 2 vol % CO 2 . It was not observed at 100 °C at either CO 2 concentration or at 80 °C at 100 vol % CO 2 . The influence of CO 2 or H 2 O on the kinetics of any of these processes was revealed only at the two lower temperatures, with H 2 O having a positive influence on the desorption kinetics of CO 2 at 40 °C and with CO 2 , if adsorbed previously, having a negative influence on the adsorption kinetics of both H 2 O and the coadsorption of both CO 2 and H 2 O at both 60 and 40 °C. When these effects existed, they were not that significant, at least not at 2 vol % H 2 O vapor. Finally, these results thus indicated that the effect of H 2 O vapor in the feed of a CO 2 stream does not have to be accounted for mechanistically when modeling a cycle adsorption process based on this commercially viable SAS.