期刊
APPLIED CATALYSIS A-GENERAL
卷 349, 期 1-2, 页码 156-164出版社
ELSEVIER SCIENCE BV
DOI: 10.1016/j.apcata.2008.07.025
关键词
Reaction mechanism; Propane dehydrogenation; Pt-Sn-K/Al2O3 Catalyst; Catalyst deactivation; Coke formation rates; Reactor simulation
资金
- DGI (Spain) [CrQ2004-01721/PPQ]
A complete kinetic model of propane dehydrogenation to produce propene over a Pt-Sn-K/Al2O3 Catalyst was obtained. This has been investigated over the temperature range of 460-540 degrees C at atmospheric pressure. A Langmuir-Hinshelwood mechanism provides the best fit for propane dehydrogenation, while a monolayer-multilayer mechanism is proposed for modelling the coke formation. In addition, the reaction rate of coke formation and its influence on catalyst deactivation and subsequent regeneration have been studied. Finally, a suitable mathematical model is developed for simulating the process behaviour in a two-zone fluidized bed reactor (TZFBR). (c) 2008 Elsevier B.V. All rights reserved.
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