A mathematical model for the description of the non-steady state process of decoking of a fixed bed catalytic reactor is presented. The relevant dimensionless groups are identified and their influence on the process discussed. Appropriate relationships are given for the estimation of the maximum tem
โฆ LIBER โฆ
On the optimization of tubular fixed-bed catalytic reactors
โ Scribed by S.Feyo de Azevedo; A. Rodrigues; A.P. Wardle
- Publisher
- Elsevier Science
- Year
- 1988
- Weight
- 755 KB
- Volume
- 38
- Category
- Article
- ISSN
- 0300-9467
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