A novel reactor for determination of kinetics for solid catalyzed gas reactions


Borman, P.C. and Bos, A.N.R. and Westerterp, K.R. (1994) A novel reactor for determination of kinetics for solid catalyzed gas reactions. AIChE Journal, 40 (5). pp. 862-869. ISSN 0001-1541

open access
Abstract:A novel perfectly mixed laboratory reactor for determining kinetics of heterogeneously catalyzed gas-phase reactions has been developed. Perfect mixing is achieved by circulating the gas in the reactor using an axial flow impeller in a well streamlined enclosure. Pellets are fixed in a rectangular opening in the blades of the impeller. They rotate with the impeller, thus realizing high particle velocities in the reactor. Interparticle mass transfer was studied experimentally by vaporization of naphthalene pellets. The mass-transfer coefficient in the novel reactor was found to depend on the velocity of a particle in the reactor. Mass-transfer coefficients in an internal recycle reactor at equal impeller tip speeds are 4-6 times lower than those in the novel reactor, and conditions can be chosen easily where at higher rotational speeds the mass- and heat-transfer rates are 8-10 times higher than in classical recycle reactors. The recycle flow rate in a recycle reactor was found to depend strongly on the resistance to flow caused by the catalyst bed itself. The novel reactor was tested under reacting conditions using the hydrogenation of ethene.
Item Type:Article
Copyright:© 1994 Wiley InterScience
Research Group:
Link to this item:http://purl.utwente.nl/publications/71091
Official URL:https://doi.org/10.1002/aic.690400512
Export this item as:BibTeX
HTML Citation
Reference Manager


Repository Staff Only: item control page

Metis ID: 105828