Abstract
The superior permselectivity of microporous ceramic membranes commercially available are ideal as supports for catalytic membrane reactors, which can overcome the catalytic conversion limited by thermodynamic equilibrium. Dehydrogenation reactions are the focus of our study. Gas permeations using ceramic membranes with or without catalysts are presented. Conversion enhancement for dehydrogenation is discussed with mathematical simulation and experimental results.
Original language | English |
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Pages (from-to) | 537 |
Number of pages | 1 |
Journal | American Chemical Society, Division of Petroleum Chemistry, Preprints |
Volume | 34 |
Issue number | 3 |
State | Published - Aug 1989 |
Externally published | Yes |
Event | Preprints of the Division of Petroleum Chemistry, Inc., American Chemical Society: General Papers (Poster Session) - Miami, FL, USA Duration: Sep 10 1989 → Sep 15 1989 |