Cao, Enhong, Meenakshisundaram, Sankar ![]() ![]() ![]() ![]() ![]() ![]() |
Abstract
Disproportionation of benzyl alcohol has been identified as the source of toluene formation in the solvent free oxidation of benzyl alcohol using supported gold palladium catalysts. There is a slight increase in the disproportionation reaction, and hence the toluene selectivity, when this reaction is performed in a continuous mode using a micro-packed bed reactor when compared to the same reaction performed in a conventional glass stirred batch reactor. Oxidation and disproportionation reactions respond slightly differently to the changes in reaction parameters, like oxygen concentration and pressure, when a micro packed bed reactor was used instead of a conventional glass stirred reactor. When MgO supported gold–palladium catalysts were used for this reaction, the toluene selectivity reduced substantially at the cost of conversion.
Item Type: | Article |
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Date Type: | Publication |
Status: | Published |
Schools: | Cardiff Catalysis Institute (CCI) Chemistry |
Subjects: | Q Science > QD Chemistry |
Uncontrolled Keywords: | Gold palladium catalysts; Alcohol oxidation; Benzyl alcohol oxidation |
Publisher: | Elsevier |
ISSN: | 0920-5861 |
Funders: | EPSRC |
Last Modified: | 05 Feb 2025 22:26 |
URI: | https://orca.cardiff.ac.uk/id/eprint/38897 |
Citation Data
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