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1. Simulation of a multi-step pressure swing adsorption process was performed to purify hydrogen from a steam reformer off-gas mixture. 2. Using a two-layer activated carbon/zeolite bed, 75.7% hydrogen in the feed could be concentrated to over 99.95% in the product with 82.5% recovery by cycling the pressure between 1 and 22.5 bar. 3. The process was optimized by investigating the effects of feed flow rate, purge to feed ratio, and lengths and diameters of the adsorbent layers on hydrogen purity and recove

Author

Agam Hanasichula

Language

EN