OPTIMAL CATALYST DISTRIBUTION AND DILUTION IN NONISOTHERMAL PACKED BED REACTORS
- 1 April 1987
- journal article
- research article
- Published by Taylor & Francis in Chemical Engineering Communications
- Vol. 52 (1-3) , 33-51
- https://doi.org/10.1080/00986448708911856
Abstract
The problem of the optimal distribution of two different catalysts in a nonisothermal packed bed reactor is analyzed. State variable constraints, such as maximum allowable temperature, may be incorporated through a penalty function approach into the steepest ascent solution of this problem. Loading a wall-cooled reactor with two chemically different catalysts is compared to dilution of a single catalyst with inerts for temperature moderation. A criterion is presented for estimating whether catalyst dilution may be necessary in order to keep reactor temperature below some maximum allowable value. Conditions for optimal loading with a two-dimensional reactor model are presented and applied to catalyst dilution in a butane oxidation reactor. Suboptimal catalyst loadings are compared with the optimal loading.Keywords
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