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Coking causes of boiling-bed isobutane dehydrogenation reactor

โœ Scribed by V. V. Molchanov; V. N. Kashkin; N. A. Pakhomov; O. A. Parakhin


Book ID
111475202
Publisher
SP MAIK Nauka/Interperiodica
Year
2009
Tongue
English
Weight
509 KB
Volume
1
Category
Article
ISSN
2070-0504

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The dehydrogenation of isobutane to isobutene was conducted in a comparatively low-temperature range (from 623 to 723 K) using a hydrogen-permeable membrane reactor. An Al,O,-supported platinum catalyst exhibited high activity compared with a commercial Cr,Oa-Al,Oa catalyst in a conventional flow re