沸石
烯烃纤维
催化作用
费托法
选择性
微型多孔材料
吸附
化学工程
分子
化学
材料科学
无机化学
有机化学
工程类
作者
Chengtao Wang,Wei Fang,Zhiqiang Liu,Liang Wang,Zuwei Liao,Yongrong Yang,Hangjie Li,Lu Liu,Hang Zhou,Xuedi Qin,Shaodan Xu,Xuefeng Chu,Yan Wang,Anmin Zheng,Feng‐Shou Xiao
标识
DOI:10.1038/s41565-022-01154-9
摘要
Catalytic reactions are severely restricted by the strong adsorption of product molecules on the catalyst surface, where promoting desorption of the product and hindering its re-adsorption benefit the formation of free sites on the catalyst surface for continuous substrate conversion1,2. A solution to this issue is constructing a robust nanochannel for the rapid escape of products. We demonstrate here that MFI zeolite crystals with a short b-axis of 90–110 nm and a finely controllable microporous environment can effectively boost the Fischer–Tropsch synthesis to olefins by shipping the olefin molecules. The ferric carbide catalyst (Na-FeCx) physically mixed with a zeolite promoter exhibited a CO conversion of 82.5% with an olefin selectivity of 72.0% at the low temperature of 260 °C. By contrast, Na-FeCx alone without the zeolite promoter is poorly active under equivalent conditions, and shows the significantly improved olefin productivity achieved through the zeolite promoter. These results show that the well-designed zeolite, as a promising promoter, significantly boosts Fischer–Tropsch synthesis to olefins by accelerating escape of the product from the catalyst surface.
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