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- 2009 Annual Meeting
- Separations Division
- Poster Session On Fundamentals and Applications of Adsorption and Ion Exchange
- (709d) CO2/CH4 Separation Using Adsorbent/Membrane Hybrid System
The permeation and separation performance of binary mixture in the AHM system were compared to those in the FAU zeolite membrane. Since the concentration of adsorptive molecules was enriched in the packed zeolite 5A inside the AHM system, its feed partial pressure outside the AHM system (FAU zeolite membrane) became far higher than weak adsorptive molecules. As a result, the selectivity of strongly adsorptive molecules could be increased. In addition, the effects of stage cut and sweeping gas flow rate on the AMH system were investigated. In the AMH system, the inside propagation profiles by different adsorption affinity gave a significant contribution to the separation. And, the separation factor in the AMH system was higher than the membrane system. The mathematical model and simulator for the AMH system, considering axial and radial simultaneously, were successfully developed. The permeation and separation of multi-component permeation in the AMH system were well-predicted by the combined packed bed model and tubular type membrane model.