| Article ID | Journal | Published Year | Pages | File Type |
|---|---|---|---|---|
| 9623856 | Chemical Engineering Journal | 2005 | 9 Pages |
Abstract
On the basis of the experimental data, mathematical modelling has been performed for the process flow sheet with the unreacted gas recycled. The influence of various parameters of the process on the catalyst productivity with regard to liquid hydrocarbons was studied.
Related Topics
Physical Sciences and Engineering
Chemical Engineering
Chemical Engineering (General)
Authors
V.M. Mysov, S.I. Reshetnikov, V.G. Stepanov, K.G. Ione,