Purification of the C 8 aromatics (xylenes and ethylbenzene) is particularly challenging because of their similar physical properties.I ti sa lso relevant because of their industrial utility.Physisorptive separation of C 8 aromatics has long been suggested as an energy efficient solution but no physisorbent has yet combined high selectivity (> 5) with high adsorption capacity (> 50 wt %). Now ac ounterintuitive approach to the adsorptive separation of o-xylene from other C 8 aromatics involves the study of aknownnonporous layered material, [Co(bipy) 2 (NCS) 2 ] n (sql-1-Co-NCS), whichc an reversibly switch to C 8 aromatics loaded phases with different switching pressures and kinetics,m anifesting benchmark oxylene selectivity (S OX/EB % 60) and high saturation capacity (> 80 wt %). Structural insight into the observed selectivity and capacity is gained by analysis of the crystal structures of C 8 aromatics loaded phases.The separation and purification of chemical feedstocks currently uses 10-15 %o fw orldwide energy production; traditional separation processes (for example,d istillation, drying, evaporation) account for more than 80 %o ft his energy. [1] Given that there will be ever-increasing demand for commodities in the coming decades,m ore energy-efficient purification technologies are urgently required for large-scale separation processes.O ne of the most challenging and important separations in this context involves xylene isomers and ethylbenzene,t he C 8 aromatics.T hese compounds are used for the industrial production of fibers,plastics,solvents, and fuel additives. [2] However,t heir similar sizes and boiling points make their separation difficult. Presently,h igherboiling ortho-xylene (OX) is the main component isolated by distillation with more than 150 theoretical plates,w hile meta-xylene (MX) and para-xylene (PX) are separated by (complexation-based) fractional crystallization and/or adsorption. Ethylbenzene (EB) is mainly produced by alkylation of benzene with ethylene,b ecause it is extremely energy-intensive to isolate it by superfractionation with more than 300 theoretical plates. [3] Although adsorption-based technology has been well studied for C 8 aromatics separa-tion, [4] widespread implementation is hindered by the capacity and selectivity limitations of the current generation of adsorbents.F or example,z eolites only offer moderate capacity (ca. 10-20 wt %) and selectivity (ca. 5), [5] overshadowing their advantages of low cost and ready availability.