选择性
烯烃纤维
沸石
合成气
化学
硅酸铝
乙烯
产品分销
甲醇
催化作用
无机化学
有机化学
化学工程
工程类
作者
Jie Tuo,Yaqi Fan,Yan Wang,Yudan Gong,Chengwei Zhai,Xianchen Gong,Teng Yang,Hao Xu,Jingang Jiang,Yejun Guan,Yanhang Ma,Peng Wu
出处
期刊:Angewandte Chemie
[Wiley]
日期:2023-11-14
卷期号:62 (52): e202313785-e202313785
被引量:8
标识
DOI:10.1002/anie.202313785
摘要
Abstract Selective conversion of syngas to value‐added olefins has attracted considerable research interest. Regulating product distribution remains challenging, such as achieving higher olefin selectivity, propylene/ethylene ( P/E ) and olefin/paraffin ( O/P ) ratios. A new pentasil zeolite Al‐IDM‐1 with recently approved − ION structure, composed of 17‐membered‐ring (MR) extra‐large lobed pores and intersected 10‐MR medium pores, shows a C 2–6 = selectivity up to 85 % and a high O/P value of 14 in the conversion of syngas when being combined with Zn a Al b O x oxide. Moreover, for the high‐silica Al‐IDM‐1 with Si/Al ratio of 400, the selectivity of propylene and butene accounts for 88 % in C 2–4 = , resulting in high P/E (>4) and butene/ethylene ( B/E >3) ratios. The high C 3–4 = selectivity is contributed by two main reasons, that is, the relatively weak acidity of Al‐IDM‐1 zeolite enhances the olefin‐based cycle revealed by the probe reactions of methanol‐to‐propylene (MTP) and 1‐hexene cracking, and the rich isolated internal SiOH groups in Al‐IDM‐1 promote the desorption of C 3–4 = , once they are formed inside zeolite pores.
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