2012
DOI: 10.1021/jp306828x
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Adsorption and Separation of Xylene Isomers: CPO-27-Ni vs HKUST-1 vs NaY

Abstract: The separation of xylene isomers is one of the most difficult separations in petrochemistry. Adsorbents have to preferentially adsorb para or meta isomers, but there are only a few zeolites which fulfill the criteria of selectivity and adsorption capacity. In this study, we evaluate two metal− organic frameworks (MOF) with coordinatively unsaturated metal sites (cus), i.e., CPO-27-Ni and HKUST-1, in the adsorption and separation of p-xylene, m-xylene, and o-xylene in the gas phase. The results are compared wit… Show more

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Cited by 73 publications
(96 citation statements)
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“…At lower temperatures, NaY prefers m-xylene while higher temperatures lead to the preferential adsorption of oxylene. This change was also attributed to packing/arrangement effect [41]. A similar mechanism as observed in MIL-47 and MIL-53 is expected to occur in DUT-5 materials, given their similar pore structure.…”
Section: Separation Of Alkanes Alkenes and Aromaticssupporting
confidence: 53%
“…At lower temperatures, NaY prefers m-xylene while higher temperatures lead to the preferential adsorption of oxylene. This change was also attributed to packing/arrangement effect [41]. A similar mechanism as observed in MIL-47 and MIL-53 is expected to occur in DUT-5 materials, given their similar pore structure.…”
Section: Separation Of Alkanes Alkenes and Aromaticssupporting
confidence: 53%
“…The result shows that o-xylene with a dipole moment interacts more strongly with the electric field of Beta zeolite than p-xylene without dipole moment. Thus, the ortho adsorption is further enhanced by electrostatic effects [27]. However, as to m-xylene, the electrostatic interaction seems to be only of secondary importance in the adsorption.…”
Section: Modeling Of Equilibrium Isothermsmentioning
confidence: 97%
“…Binding energies of guest molecules with the framework walls or non-framework cations do not solely determine the separation performance. As pointed out by Peralta et al, 40 adsorbents selective to p-xylene are desirable for high productivities; they need to adsorb only B20% of the feed, whereas an adsorbent that rejects p-xylene would have to adsorb 80% of the feed. In current industrial practice the adsorbent used is BaX zeolite, which selectively adsorbs p-xylene.…”
Section: Separation Of C8 Aromaticsmentioning
confidence: 99%