| Article ID | Journal | Published Year | Pages | File Type |
|---|---|---|---|---|
| 9623858 | Chemical Engineering Journal | 2005 | 9 Pages |
Abstract
Modeling of the large-scale reactor revealed that the catalyst productivity could be improved using the fluidized bed reactor in comparison to that in the tubular reactor due to the much more concentrated inlet flow. The inlet concentrations of ammonia could be much higher than that used in a tubular reactor (35-50 and 7-8%, respectively).
Keywords
Related Topics
Physical Sciences and Engineering
Chemical Engineering
Chemical Engineering (General)
Authors
A.S. Noskov, I.A. Zolotarskii, S.A. Pokrovskaya, V.N. Kashkin, E.M. Slavinskaya, V.V. Mokrinskii, V.N. Korotkikh,