Abstract
Membrane materials with high permeability and high selectivity are preferred for gas separations. However, there exists a trade-off (or upper bound): polymers with higher permeability often exhibit lower selectivity, and vice versa. The upper bounds have been empirically drawn and theoretically predicted. While the upper bounds for light gas pairs such as O2/N2 can accurately describe the limit of membrane materials, the upper bound for CO2/CH4 separation does not depict state-of-the-art of material research. For example, the performance of commercial CO2/CH4 separation membrane (cellulose acetate, CA) is way below the upper bound, and there seem to be many materials showing much better separation properties. This paper presents experimental data of CA membranes tested with simulated CO2/CH4 mixtures. The effect of feed pressure and composition on CO2/CH4 separation properties is interpreted with a free volume model, which is then used to predict a more realistic upper bound for industrial CO2/CH4 separations.
| Original language | English |
|---|---|
| Journal | ACS National Meeting Book of Abstracts |
| State | Published - 2010 |
| Event | 240th ACS National Meeting and Exposition - Boston, MA, United States Duration: Aug 22 2010 → Aug 26 2010 |
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