Exploiting Adsorption/Diffusion Synergy in MFI-Catalyzed Hexane Isomerization Reactor
| Authors | |
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| Publication date | 11-2023 |
| Journal | Chemie-Ingenieur-Technik |
| Volume | Issue number | 95 | 11 |
| Pages (from-to) | 1794-1799 |
| Number of pages | 6 |
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| Abstract |
The 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. |
| Document type | Article |
| Note | With supplementary file. |
| Language | English |
| Published at | https://doi.org/10.1002/cite.202300005 |
| Other links | https://www.scopus.com/pages/publications/85159897439 |
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