A core/shell catalyst produces a spatially confined effect and shape selectivity in a consecutive reaction
A core/shell catalyst produces a spatially confined effect and shape selectivity in a consecutive reaction
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DOI:
10.1002/anie.200703335
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发表时间:
2008-01-01
影响因子:
16.6
通讯作者:
Tsubaki, Noritatsu
中科院分区:
文献类型:
--
作者:
Bao, Jun;He, Jingjiang;Tsubaki, Noritatsu
In general, an active catalyst for a consecutive reaction (A! B! C) usually has two types of active sites, one of which accelerates the reaction of A to B and the other the reaction of B to C. Taking the synthesis of isoparaffins from syngas (CO+ H2) as an example, the most efficient catalysts usually contain both Fischer–Tropsch synthesis (FTS) sites and acidic sites.[1] The FTS sites convert the syngas into linear hydrocarbons, which then migrate to the acidic sites where they undergo further hydrocracking and isomerization to form branched hydrocarbons.Improving the dispersion of these two kinds of active sites whilst ensuring they are still close to each other is the most efficient approach to enhancing catalytic performance.[2] However, a crucial factor that affects the product selectivity of this consecutive reaction is the ease of migration of the first reaction products to the active sites of the second reaction. The different active sites in conventional bifunctional catalysts are randomly distributed on their surface, which provides an unrestricted, open reaction environment where the coupled reactions occur independently and randomly even though the distance between the two active sites is very short. This means that the products desorbed from the first reaction sites can leave the catalyst without reacting further at the other active sites.