Abstract
The zero length column (ZLC) method has been applied to study the adsorption and diffusion of CO2 in a carbon monolith adsorbent. ZLC desorption curves, measured over a wide range of flow rates, are shown to be very well accounted for assuming a linear equilibrium isotherm with the kinetics controlled by diffusion into a parallel sided slab. The data, at all flow rates, are characterized by a single pair of parameters (K and D s). Diffusivities for a He carrier are about double those for a N2 carrier reflecting both the difference in molecular diffusivities and some contribution from Knudsen diffusion. Breakthrough curves for CO2-He and CO2-N2 were also measured for columns packed with the monolith adsorbent. Both the equilibrium and diffusion parameters derived from analysis of the breakthrough curves in accordance with the Golay/Spangler models are consistent with the values derived from the ZLC measurements. Dispersion in the monoliths is shown to be controlled by mass transfer resistance rather than axial mixing.
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Brandani, F., Rouse, A., Brandani, S. et al. Adsorption Kinetics and Dynamic Behavior of a Carbon Monolith. Adsorption 10, 99–109 (2004). https://doi.org/10.1023/B:ADSO.0000039866.37214.6a
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DOI: https://doi.org/10.1023/B:ADSO.0000039866.37214.6a