Isobutane/butene alkylation: regeneration of solid acid catalysts

Authors
Citation
Ca. Querini, Isobutane/butene alkylation: regeneration of solid acid catalysts, CATAL TODAY, 62(2-3), 2000, pp. 135-143
Citations number
23
Categorie Soggetti
Physical Chemistry/Chemical Physics
Journal title
CATALYSIS TODAY
ISSN journal
09205861 → ACNP
Volume
62
Issue
2-3
Year of publication
2000
Pages
135 - 143
Database
ISI
SICI code
0920-5861(20001010)62:2-3<135:IAROSA>2.0.ZU;2-7
Abstract
The regeneration of Y-zeolite catalysts used during the isobutane alkylatio n reaction is studied. Coke is characterized by temperature-programmed tech niques and measuring the WC ratio. The coke deposited under supercritical c onditions is very similar (TPO profile and amount) to the coke deposited in liquid phase. The regeneration was carried out in many ways. Air was used for heating with at a low rate, and holding the temperature at low values f or long times. Platinum was incorporated in the zeolite to catalyze the cok e combustion or to provide an additional route for coke gasification, such as hydrogenation. Ozone was used to remove most of the coke, followed by a second step with H-2 or He. Hydrogen peroxide was studied as an alternative low-temperature oxidation compound. It was found that the ozone treatment, followed by a hydrogen treatment, is an effective way to regenerate this m icroporous catalyst. The ozone not only eliminates a large fraction of the coke but also changes the characteristics of the small amount of coke left on the catalyst, making it easier to be burnt. The treatment with hydrogen peroxide at 90 degreesC also removes a large fraction of coke, but without changing significantly the characteristics of the coke left after the treat ment. (C) 2000 Elsevier Science B.V. All rights reserved.