Abstract
Cation-exchanged zeolites are of potential use in pressure swing adsorption (PSA) technologies for CO(2) capture applications. Published experimental data for CO(2)/CH(4), CO(2)/N(2), and CO(2)/C(3)H(8) mixture adsorption in NaX zeolite, also commonly referred to by its trade name 13X, have demonstrated that the ideal adsorbed solution theory (IAST) fails to provide adequately accurate estimates of mixture adsorption equilibrium. In particular, the IAST estimates of CO(2)/CH(4) and CO(2)/N(2) selectivities are significantly higher than those realized in experiments. For CO(2)/C(3)H(8) mixtures, the IAST fails to anticipate the selectivity reversal phenomena observed in experiments. In this article, configurational-bias Monte Carlo (CBMC) simulations are employed to provide confirmation of the observed thermodynamic nonidealities in adsorption of CO(2)/CH(4), CO(2)/N(2), and CO(2)/C(3)H(8) mixtures in NaX zeolite. The CBMC simulations provide valuable insights into the root cause of the failure of the IAST, whose applicability mandates a homogeneous distribution of adsorbates within the pore landscape. By sampling 10(5) equilibrated spatial locations of individual guest molecules within the cages of NaX zeolite, the radial distribution functions (RDFs) of each of the pairs of guest molecules are determined. Examination of the RDFs clearly reveals congregation effects, wherein the CO(2) guests occupy positions in close proximity to the Na(+) cations. The positioning of the partner molecules (CH(4), N(2), or C(3)H(8)) is further removed from the CO(2) guest molecules; consequently, the competition in mixture adsorption faced by the partner molecules is less severe than that anticipated by the IAST. The important message to emerge from this article is the need for quantification of thermodynamic nonideality effects in mixture adsorption.