Affiliation:
1. University of Amsterdam Van 't Hoff Institute for Molecular Sciences Science Park 904 1098 XH Amsterdam The Netherlands
Abstract
AbstractThe isomerization of n‐hexane to produce mono‐ and di‐branched isomers is an important process for octane enhancement of gasoline. In a fixed bed reactor, packed with MFI catalyst, there is synergy between mixture adsorption equilibrium and intra‐crystalline diffusion. This synergy is best exploited by operating the reactor in a transient manner, whereby the desired products consisting of the branched isomers can be recovered from the exiting gas mixture during the early stages of transience. This strategy essentially results in a combination of reaction and separation in a single fixed bed device.
Subject
Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry
Cited by
1 articles.
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