化学
丁酮
催化作用
溶剂
传质
反应速率
溶解
溶剂效应
异丙醇
相(物质)
选择性
吸附
动力学
丁醇
热力学
有机化学
色谱法
乙醇
物理
量子力学
作者
Belinda S. Akpa,Carmine D’Agostino,Lynn F. Gladden,Kenneth J. Hindle,Haresh Manyar,James McGregor,R. Li,Matthew Neurock,Nishant K. Sinha,E. Hugh Stitt,Daniel Weber,J. Axel Zeitler,David W. Rooney
标识
DOI:10.1016/j.jcat.2012.01.011
摘要
In liquid-phase reaction systems, the role of the solvent is often limited to the simple requirement of dissolving and/or diluting substrates. However, the correct choice, either pure or mixed, can significantly influence both reaction rate and selectivity. For multi-phase heterogeneously catalysed reactions observed variations may be due to changes in mass transfer rates, reaction mechanism, reaction kinetics, adsorption properties and combinations thereof. The liquid-phase hydrogenation of 2-butanone to 2-butanol over a Ru/SiO2 catalyst, for example, shows such complex rate behaviour when varying water/isopropyl alcohol (IPA) solvent ratios. In this paper, we outline a strategy which combines measured rate data with physical property measurements and molecular simulation in order to gain a more fundamental understanding of mixed solvent effects for this heterogeneously catalysed reaction. By combining these techniques, the observed complex behaviour of rate against water fraction is shown to be a combination of both mass transfer and chemical effects.
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