Kinetics of the catalytic reaction of methane and hydrogen sulphide over a PtAl2O3 catalyst
β Scribed by S.K. Megalofonos; N.G. Papayannakos
- Publisher
- Elsevier Science
- Year
- 1996
- Tongue
- English
- Weight
- 684 KB
- Volume
- 138
- Category
- Article
- ISSN
- 0926-860X
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β¦ Synopsis
The reaction of methane and hydrogen sulphide over a Pt-A1203 catalyst has been studied in a fixed bed tubular reactor over a temperature range of 973 to 1073 K under atmospheric pressure and for space times between 0.1 and 1 s. The Langmuir-Hinshelwood-Hougen-Watson theory has been employed to obtain eighteen (18) rival kinetic models. The kinetic parameters are determined for all models and discrimination of the prevailing model is attempted by using statistical and thermodynamic constraints. According to that model the rate-controlling step is the reaction between one chemisorbed CH 2 and two S on the catalytic surface with the participation of three catalytic sites.
π SIMILAR VOLUMES
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.
Perovskite oxide structured (YBCO) has been Γrst pre-YBa 2 Cu 3 O 7vx pared by carbonate precipitation and then modiΓed with palladium or ruthenium by impregnation on the perovskite oxide, while cobalt was co-precipitated simultaneously in the same pH range with perovskite oxide. After characterizat