Catalytic dehydrogenation of ethanol in a metal-modified alumina membrane reactor
โ Scribed by Jingfa Deng; Zhao Cao; Bo Zhou
- Publisher
- Elsevier Science
- Year
- 1995
- Tongue
- English
- Weight
- 946 KB
- Volume
- 132
- Category
- Article
- ISSN
- 0926-860X
No coin nor oath required. For personal study only.
โฆ Synopsis
Alumina membranes
modified by metals (Pd, Pt, Cu, Ni) were prepared by the sol-gel method, and characterized by adsorption of N2, scanning electron microscopy, X-ray diffraction and hydrogenoxygen titration. The average pore diameters of the membranes were 4-7 nm, which is larger than for a pure alumina membrane, but still within the range of a Knudsen process. For the membranes modified by copper, nickel, the separation factor of H,/Ar was close to that of pure Al,O, membrane, but for the membranes modified by palladium, platinum. the separation factor of H,/Ar was not only better than the pure Al,O, membrane, but also than the Knudsen value. This suggested that the increase of the selectivity for hydrogen permeation through the membranes was caused by adsorption of hydrogen to palladium or platinum. The catalytic dehydrogenation of ethanol to acetaldehyde was performed in these membrane reactors. For the palladium, platinum modified membrane reactor, the yield of acetaldehyde was higher than that in the pure A1203 membrane reactor, and increased with the flow-rate of sweeping argon.
๐ SIMILAR VOLUMES
The dehydrogenation of isobutane on a commercial chromia-alumina catalyst was studied using a conventional and a membrane reactor. A series of differential runs were conducted varying the temperature and feed composition. Extensive loss of catalyst activity was observed within the first two or three
Accurate simulation of fixed-bed catalytic reactors requires the computation of the effectiveness factors at each point along the length of the reactor. This requires the formulation and solution of rigorous diffusion-reaction models for the porous pellets based on the more rigorous Stefan-Maxwell e