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ecent advances in selective acetylene hydrogenation using palladium containing catalysts

ecent advances in selective acetylene hydrogenation using palladium containing catalysts

作     者:Alan J. McCue James A. Anderson 

作者机构:Surface Chemistry and Catalysis Group Department of Chemistry University of Aberdeen Aberdeen AB24 3UE UK Materials and Chemical Engineering Group School of Engineering University of Aberdeen Aberdeen AB24 3UE UK 

出 版 物:《Frontiers of Chemical Science and Engineering》 (化学科学与工程前沿(英文版))

年 卷 期:2015年第9卷第2期

页      面:142-153页

核心收录:

学科分类:081702[工学-化学工艺] 081704[工学-应用化学] 07[理学] 08[工学] 0817[工学-化学工程与技术] 0703[理学-化学] 070301[理学-无机化学] 

主  题:acetylene ethylene selective hydrogenation,palladium bimetallic 

摘      要:Recent advances with Pd containing catalysts for the selective hydrogenation of acetylene are described. The overview classifies enhancement of catalytic proper- ties for monometallic and bimetallic Pd catalysts. Activity/ selectivity of Pd catalysts can be modified by controllingparticle shape/morphology or immobilisation on a support which interacts strongly with Pd particles. In both cases enhanced ethylene selectivity is generally associated with modifying ethylene adsorption strength and/or changes to hydride formation. Inorganic and organic selectivity modifiers (i.e., species adsorbed onto Pd particle surface) have also been shown to enhance ethylene selectivity. Inorganic modifiers such as TiO2 change Pd ensemble size and modify ethylene adsorption strength whereas organic modifiers such as diphenylsulfide are thought to create a surface template effect which favours acetylene adsorption with respect to ethylene. A number of metals and synthetic approaches have been explored to prepare Pd bimetallic catalysts. Examples where enhanced selectivity is observed are generally associated with decreased Pd ensemble size and/or hindering of the ease with which an unselective hydride phase is formed for Pd. A final class of bimetallic catalysts are discussed where Pd is not thought to be the primary reaction site but merely acts as a site where hydrogen dissociation and spillover occurs onto a second metal (Cu or Au) where the reaction takes place more selectively.

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