Get 20M+ Full-Text Papers For Less Than $1.50/day. Start a 14-Day Trial for You or Your Team.

Learn More →

Dehydration of isobutane in fixed bed on the stable to carbon deposition chromia-alumina catalysts

Dehydration of isobutane in fixed bed on the stable to carbon deposition chromia-alumina catalysts Study of chromia-alumina catalysts obtained from products of a thermochemical activation of aluminum trihydroxide for fixed-bed dehydrogenation of light paraffin hydrocarbons demonstrated that an increase in activity is observed in dehydrogenation of isobutane at a temperature of 590°C during the first 30 min of the catalytic process and then the activity slightly decreases. It was shown that the amount of carbon-deposition products on the surface of the synthesized catalysts after 120 min of isobutene dehydrogenation is 1–2 wt %. One of reasons for the high stability of chromia-alumina catalysts against carbon deposition is their porous structure. The use of the proposed catalysts in industry can improve the efficiency of the paraffin dehydrogenation processes by increasing the time of the reaction, while regeneration time is reduced. http://www.deepdyve.com/assets/images/DeepDyve-Logo-lg.png Russian Journal of Applied Chemistry Springer Journals

Dehydration of isobutane in fixed bed on the stable to carbon deposition chromia-alumina catalysts

Loading next page...
1
 
/lp/springer_journal/dehydration-of-isobutane-in-fixed-bed-on-the-stable-to-carbon-Kmmp5hXrlz

References (16)

Publisher
Springer Journals
Copyright
Copyright © 2016 by Pleiades Publishing, Ltd.
Subject
Chemistry; Chemistry/Food Science, general; Industrial Chemistry/Chemical Engineering
ISSN
1070-4272
eISSN
1608-3296
DOI
10.1134/S1070427216110094
Publisher site
See Article on Publisher Site

Abstract

Study of chromia-alumina catalysts obtained from products of a thermochemical activation of aluminum trihydroxide for fixed-bed dehydrogenation of light paraffin hydrocarbons demonstrated that an increase in activity is observed in dehydrogenation of isobutane at a temperature of 590°C during the first 30 min of the catalytic process and then the activity slightly decreases. It was shown that the amount of carbon-deposition products on the surface of the synthesized catalysts after 120 min of isobutene dehydrogenation is 1–2 wt %. One of reasons for the high stability of chromia-alumina catalysts against carbon deposition is their porous structure. The use of the proposed catalysts in industry can improve the efficiency of the paraffin dehydrogenation processes by increasing the time of the reaction, while regeneration time is reduced.

Journal

Russian Journal of Applied ChemistrySpringer Journals

Published: Feb 24, 2017

There are no references for this article.