The gas-phase oxidation of o-xylene over a commercial V205-Ti02 catalyst was studied in tied bed non-isothermal reactor. The experiments were carried out at initial o-xylene concentrations which differed greatly from each other. The following reaction network was suggested.
β¦ LIBER β¦
Effect of the reaction bath temperature in a fixed-bed reactor for oxidation of oxylene over V2O5/TiO2catalysts
β Scribed by Yeung Ho Park; Seung Jun Kim; Shin Choon Kang
- Publisher
- Springer US
- Year
- 2000
- Tongue
- English
- Weight
- 721 KB
- Volume
- 17
- Category
- Article
- ISSN
- 0256-1115
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