沸石
催化作用
双功能
化学
选择性
合成气
位阻效应
双功能催化剂
钴
分子筛
无机化学
初湿浸渍
化学工程
有机化学
工程类
作者
S. Vijayanand,Vladimir Zholobenko,Kang Cheng,Christine Lancelot,Svetlana Heyte,Joelle Thuriot,Sébastien Paul,Vitaly V. Ordomsky,Andreï Y. Khodakov
出处
期刊:Chemcatchem
[Wiley]
日期:2015-11-03
卷期号:8 (2): 380-389
被引量:58
标识
DOI:10.1002/cctc.201500777
摘要
Abstract This study focuses on the effects of the localization of Co species, zeolite structure, and acidity on the performance of Co bifunctional catalysts promoted with Pt for the direct synthesis of iso ‐paraffins from syngas. ZSM‐5, MOR, and BEA were chosen as zeolites with different structures and pore diameters. The catalysts were prepared either by incipient wetness impregnation or by the mechanical mixing of the zeolite with a conventional silica‐supported Co catalyst. The increase in the pore size and open character of the zeolite structure from ZSM‐5 to BEA resulted in a higher fraction of Co located inside the pores of the catalysts prepared by impregnation. The catalytic performance was affected strongly by the zeolite acidity, pore structure, and Co distribution between the pores and the external surface. The selectivity to short‐chain iso ‐paraffins is affected principally by the zeolite acidity, whereas the selectivity to long‐chain branched hydrocarbons mostly depends on steric effects.
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