Study of hydrogen surface mobility and hydrogenation reactions over alumina-supported palladium catalysts

被引:35
|
作者
Benkhaled, Mersaka [1 ,3 ]
Descorme, Claude [2 ,3 ]
Duprez, Daniel [3 ]
Morin, Stephane [1 ]
Thomazeau, Cecile [1 ]
Uzio, Denis [1 ]
机构
[1] IFP Lyon, F-69390 Vernaison, France
[2] Inst Rech Catalyse & Environm Lyon, F-69626 Villeurbanne, France
[3] Univ Poitiers, CNRS, Lab Catalyse Chim Organ, F-86022 Poitiers, France
关键词
highly dispersed Pd catalysts; particle surface density; butadiene hydrogenation; orthoxylene hydrogenation; surface mobility; H/D exchange;
D O I
10.1016/j.apcata.2008.04.043
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Alumina-supported Pd catalysts with different particle surface densities have been prepared using incipient wetness impregnation of aqueous solution of a palladium nitrite complex. Buta-1,3-diene and orthoxylene hydrogenation reactions were performed both in a batch and a fixed bed reactor. Hydrogen surface mobility was studied using H-2-D-2 isotopic exchange. The influence of (i) the particle surface density and (ii) the surface area of the support on the catalytic properties are discussed. The turnover frequency (TOF) of the but-1,3-diene hydrogenation was highly sensitive to the surface density of Pd particles (D-sp). Moreover, for a given surface density, TOF also depend on the nature of the alumina support. For a given support, modifications of the electronic properties of palladium can explain the increase of the reaction rate with D-sp while changes in the kinetics of hydrogen surface diffusion are proposed to explain the support effect. (C) 2008 Elsevier B.V. All rights reserved.
引用
收藏
页码:36 / 43
页数:8
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