𝔖 Bobbio Scriptorium
✦   LIBER   ✦

48 Catalytic oxidation of o-xylene in a slugging fluidised bed

✍ Scribed by J.G. Yates; J.-Y. Gregoire

Publisher
Elsevier Science
Year
1980
Tongue
English
Weight
440 KB
Volume
35
Category
Article
ISSN
0009-2509

No coin nor oath required. For personal study only.

✦ Synopsis

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 reaction in the pre-slugging region of the bed gives the closest agreement A further slΔ±ght modification of the model to account for, possibly, reaction on particles inside slugs would however seem to be necessary

πŸ“œ SIMILAR VOLUMES

The prediction of the performance of pac
The prediction of the performance of packed-bed catalytic reactors in the air-oxidation of o-xylene
✍ P.H. Calderbank; K. Chandrasekharan; C. Fumagalli πŸ“‚ Article πŸ“… 1977 πŸ› Elsevier Science 🌐 English βš– 805 KB

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

Kinetics of the catalytic air-oxidation
Kinetics of the catalytic air-oxidation of o-xylene measured in a tube-wall-catalytic reactor
✍ K. Chandrasekharan; P.H. Calderbank πŸ“‚ Article πŸ“… 1980 πŸ› Elsevier Science 🌐 English βš– 500 KB

The klnetlc parameters In a complex reaction network (oxldatlon of o-xylene over V205) were derived by multlresponse analysis of rate data from a tube-wall-catalytic reactor using two different catalysts The 2D model of thrs reactor was reduced to 1-D format by a systematic method of analysis which

A fluidised-bed membrane reactor for the
A fluidised-bed membrane reactor for the catalytic partial oxidation of methane to synthesis gas
✍ L. Mleczko; T. Ostrowski; T. Wurzel πŸ“‚ Article πŸ“… 1996 πŸ› Elsevier Science 🌐 English βš– 509 KB

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