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Estimation of catalyst activity profiles in fixed bed reactors

โœ Scribed by G.R. Gavalas; G.C. Hsu; J.H. Seinfeld


Publisher
Elsevier Science
Year
1972
Tongue
English
Weight
736 KB
Volume
27
Category
Article
ISSN
0009-2509

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โœฆ Synopsis


The description of the steady state operation of a fixed bed catalytic reactor requires a certain amount of information about the catalyst activity distribution. For a monofunctional catalyst with no transport limitations the total catalyst activity is sufficient for describing the steady reactor operation. The total activity can be easily estimated from measurements at the reactor exit. In the presence of diffusional limitations, or in the case of bifunctional catalysts, the reactor description requires knowledge of the detailed activity profile. This can be approximately determined by parametrization and estimation of the parameters from a few measurements along the reactor. An application of the parametrization technique is made to a simplified model of naphtha reforming.


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Nonlinear dynamic estimation for a fixed
โœ Y.S. Cheng; T. Mongkhonsi; L.S. Kershenbaum ๐Ÿ“‚ Article ๐Ÿ“… 1996 ๐Ÿ› Elsevier Science ๐ŸŒ English โš– 677 KB

Experiments have been carried out in an industrial scale pilot plant reactor and a microreactor to investigate the reversible/irreversible deactivation of a V20~/Ti02 catalyst used for the partial oxidation of o-xylene to phthalic anhydride. The experimental results indicate that unless the catalyst