A slugging-bed reactor has been used to study the catalytic oxidation of o-xylene Predictions of conversion based on published theoretical reactor models have been compared with the experimental results and it has been found that the model of Raghuraman and Potter suitably modified to account for re
Some Dynamic Features of Fluidised Bed Reactors for Partial Oxidation of o-Xylene.
โ Scribed by Abashar, M.E.E.
- Publisher
- Curtin University of Technology
- Year
- 2008
- Tongue
- English
- Weight
- 518 KB
- Volume
- 11
- Category
- Article
- ISSN
- 0969-1855
No coin nor oath required. For personal study only.
๐ SIMILAR VOLUMES
The influences of "in-pore" diffusion and film heat and mass transfer on catalyst effectiveness and selectivity are examined for a system of highly exothermic parallel and consecutive reactions, typified, for example, by the partial oxidation of o-oxylene to phthalic anhydride. Parametric sensitivit
A fluidised-bed membrane reactor was proposed as reaction engineering meam for performing the catalytic partial oxidation of methane to synthesm gas (syngas) in a safe and stable nuumer, and to achieve high syng~ yields at elevated pressures and low temperatures. In ocder to analyse the potential of
Absfract-The kmetlcs of the catalytic au-oxldatlon of o-xylene to phthahc anhydrIde over various commercial V,O, and T10rV205 catalysts are extended and a model derived which correctly predicts the temperature and yield profiles m a quasi-Isothermal fixed-bed reactor of commercial dlmenslons The mod