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
The dynamic behavior of a fixed-bed catalytic reactor
โ Scribed by Frederic Leder; John B. Butt
- Publisher
- American Institute of Chemical Engineers
- Year
- 1966
- Tongue
- English
- Weight
- 798 KB
- Volume
- 12
- Category
- Article
- ISSN
- 0001-1541
No coin nor oath required. For personal study only.
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