A theoretical framework has been assembled for elucidation of the deactivation of a supported zeolite cracking catalyst used in a fixed bed, plug flow reactor. Intraparticle processes are based upon a parallel bundle model for the macropores and mesopores associated with the sihca alumina support. Z
Deactivation of a supported zeolitic catalyst: Diffusion, reaction and coke deposition in stochastic pore networks
โ Scribed by R. Mann; P.N. Sharratt; G. Thomson
- Publisher
- Elsevier Science
- Year
- 1986
- Tongue
- English
- Weight
- 862 KB
- Volume
- 41
- Category
- Article
- ISSN
- 0009-2509
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โฆ Synopsis
The decline in activity of a commercial* supported catalyst has been interpreted using a model of reolitic micropores uniformly distributed within a network of macropores representing the silica/alumina support. Using this model. simultaneous deactivation by site coverage end pore plugging can be simulated. Changes in network structure due-to fouling are monitored by generation of theoretical adsorption isotherms for both fresh and fouled networks. The observed deactivation for catalytic cumcua cracking in a plug flow reactor at 30DยฐC was modelled by a series coking mechanism with the coke reducing the macropore radii by approximately 30 Angstrom.
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