Isobutane pyrolysis is studied in an unpacked Pyrex reactor at 20-100 torr initial pressures and Results are interpreted in terms of a long chain radical mechanism 750-793 K. and the reaction is modeled. The reaction selectivity or ratio of the initial production rate of isobutene (or hydrogen) to t
Kinetic study and modeling of the hetero-homogeneous pyrolysis and oxidation of isobutane around 800 K. Part II. Pyrolysis in pyrex reactors packed with platinum foils or PbO-treated pyrex rods
โ Scribed by R. Zils; R. Martin; D. Perrin
- Publisher
- John Wiley and Sons
- Year
- 1998
- Tongue
- English
- Weight
- 231 KB
- Volume
- 30
- Category
- Article
- ISSN
- 0538-8066
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โฆ Synopsis
Isobutane pyrolysis has been studied at initial pressures and 20-200 torr in a packed reactor treated with PbO and in a reactor packed with platinum foils. 773-793 K, These packings strongly inhibit product formation and this effect is explained by the occurrence of the heterogeneous termination step: walls Hโข 9 9 : product (w)
at the reactor walls. The reaction has been modeled in the temperature and pressure range on the basis of a kinetic scheme which has been proposed for the homogeneous reaction and step (w) with the following values of k : w 9000 8 ฯช1 (k ) ฯญ 3.7 10 exp ฯช s w PbO
๐ SIMILAR VOLUMES
Isobutane pyrolysis has been studied in the presence of oxygen at about in 773 K unpacked and in PbO-coated packed Pyrex reactors. The reaction is shown to be accelerated by oxygen in reactors of low surface-to-volume ratio and strongly inhibited in packed PbOcoated reactors. These oxygen effects ar