Mechanism of 2-propanol dehydrogenation with suspended nikel fine-particle catalyst.
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概要
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Selective dehydrogenation of 2-propanol was performed with a suspended nickel fine-particle catalyst at high activity under refluxing conditions. The isotope effects, <I>k</I><SUB>H</SUB>⁄<I>k</I><SUB>D</SUB> for (CH<SUB>3</SUB>)<SUB>2</SUB>CDOH and (CD<SUB>3</SUB>)<SUB>2</SUB>CDOD were found to be 2.56 and 2.69, respectively, in contrast to 1.68 for (CH<SUB>3</SUB>)<SUB>2</SUB>CHOD, suggesting that the C–H bond dissociation at the methine position is rate-determining. With regard to (CH<SUB>3</SUB>)<SUB>2</SUB>CHOD and (CH<SUB>3</SUB>)<SUB>2</SUB>CDOH, a distinct difference was observed for the deuterium distributions among the liquid-phase components after the reaction, since deuterium transfer from the hydroxyl to the methyl and other groups proceeded tremendously for (CH<SUB>3</SUB>)<SUB>2</SUB>CHOD, whereas the methine group of (CH<SUB>3</SUB>)<SUB>2</SUB>CDOH changed little, even after a 5-h reaction under refluxing conditions. This contrast was well accounted for by the difficult splitting of the methine C–H bond and the facile dissociation of the hydroxyl group, in addition to a gradual H–D exchange due to the keto–enol equilibriation of the adsorbed acetone and the hydrogen transfer from 2-propanol to acetone. Distributions of H<SUB>2</SUB>, HD, and D<SUB>2</SUB> were interpreted as well, which varied with the reaction periods and the kinds of substrates. Based on the proposed mechanism, strategies for a catalyst improvement suitable for a newly-proposed chemical heat pump system are discussed.
- 公益社団法人 日本化学会の論文
著者
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Saito Yasukazu
Department Of Industrial Chemistry Faculty Of Engineering The University Of Tokyo
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Suzuki Minoru
Department Of Applied Biological Chemistry Graduate School Of Agricultural And Life Sciences The Uni
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Yamashita Masaru
Department Of Agricultural Chemistry Faculty Of Agriculture Meijo University
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Dai Feng-Yuen
Department of Industrial Chemistry, Faculty of Engineering, The University of Tokyo
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