𝔖 Bobbio Scriptorium
✦   LIBER   ✦

Kinetics of the catalytic air-oxidation of o-xylene measured in a tube-wall-catalytic reactor

✍ Scribed by K. Chandrasekharan; P.H. Calderbank

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

No coin nor oath required. For personal study only.

✦ Synopsis

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 was computatlonally acceptable KEYWORDS o-xylene oxldatlon, klnetlc study, tubular wall coated reactor

πŸ“œ SIMILAR VOLUMES

Kinetics of the catalytic air oxidation
Kinetics of the catalytic air oxidation of o-xylene over a commercial V2O5-TiO2 catalyst
✍ J. Skrzypek; M. Grzesik; M. Galantowicz; J. SoliΕ„ski πŸ“‚ Article πŸ“… 1985 πŸ› Elsevier Science 🌐 English βš– 836 KB

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.

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

48 Catalytic oxidation of o-xylene in a
48 Catalytic oxidation of o-xylene in a slugging fluidised bed
✍ J.G. Yates; J.-Y. Gregoire πŸ“‚ Article πŸ“… 1980 πŸ› Elsevier Science 🌐 English βš– 440 KB

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