Multiphase fixed-bed reactors have complex hydrodynamic and mass transfer characteristics. The modeling and scale-up are therefore difficult. The present work focuses on the role of mass transfer on the effective reaction rate. The catalytic 1-octene hydrogenation was taken as a model reaction. The
Experimental and Theoretical Studies on Hydrogenation in Multiphase Fixed Bed Reactors
โ Scribed by B. Battsengel; L. Datsevich; A. Jess
- Publisher
- John Wiley and Sons
- Year
- 2001
- Tongue
- German
- Weight
- 94 KB
- Volume
- 73
- Category
- Article
- ISSN
- 0009-286X
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