## Abstrac -For a fixed set of physlco-chemlcal parameters, an Isothermal substrate-mhlblted enzyme reactton in a tubular reactor with axed dlsperslon can pve nse to multrple steady states Cntena previously developed for non-isothermal reactions are apphed to this case to develop analytic condltlo
First order consecutive reactions in a tubular reactor with axial dispersion
โ Scribed by T.S. Chung; J.A. Howell
- Publisher
- Elsevier Science
- Year
- 1970
- Tongue
- English
- Weight
- 149 KB
- Volume
- 25
- Category
- Article
- ISSN
- 0009-2509
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โฆ Synopsis
Shorter Corn] munications more than one rate controlling step exists should be particularly useful. This concept, originated by Horiuti [4,5], has been extended to include rate controlling paths by Happel[6]. A recent study [7] employed 14C as a tracer to demonstrate the applicability of a reaction rate expression of the following form to butane dehydrogenation: ethanol could be treated in an entirely similar way. The obtaining of a stoichiometric number of unity with '% as a tracer would be tantamount to proving that hydrogen desorption or adsorption is not rate controlling. Then a potential term could be extracted as in the case of butane dehydrogenation with consequent simplification. We believe that in modeling of chemical reactions both experimental and mathematical approaches can be advantageously combined in this fashion, though this has rarely been done in the past.
ture and composition. The catalytic dehydrogenati& of where ti is an undetermined function of pressure, tempera-Bronx
๐ SIMILAR VOLUMES
Using boundary conditions more general than those due to Danckwerts, the authors recently showed that significant variations may be encountered in the global stability characteristics of an axially dispersed adiabatic tubular reactor. The numerical results presented in this communication demonstrate