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
Kinetic study and modeling of the hetero-homogeneous pyrolysis and oxidation of isobutane around 800 K. Part I. Pyrolysis in an unpacked pyrex reactor
โ Scribed by R. Zils; R. Martin; D. Perrin
- Publisher
- John Wiley and Sons
- Year
- 1998
- Tongue
- English
- Weight
- 234 KB
- Volume
- 30
- Category
- Article
- ISSN
- 0538-8066
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โฆ Synopsis
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 that of propene (or methane) is practically given by the ratio of the rate constant of abstraction of a tertiary hydrogen atom of isobutane to that of a primary one.
A sensitivity analysis clearly shows that self-inhibition is essentially due to methylallyl radicals produced by hydrogen abstraction from isobutene. The model has been manually adjusted to experimental results and most of the adjusted rate constants are in agreement with literature data.
๐ SIMILAR VOLUMES
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 ste