催化作用
脱氢
选择性
沸石
化学
无机化学
硅酸盐
丙烷
钴
费托法
化学工程
有机化学
工程类
作者
Dingmei Han,Meiyu Liu,Chengming Huang,Xinyu Sun,Linjie Guan,Binbin He,Yi Mei,Yun Zu
标识
DOI:10.1016/j.micromeso.2023.112516
摘要
Co-based catalysts are promising alternatives to replace expensive Pt- and toxic Cr-based catalysts for propane dehydrogenation (PDH), while the catalytic stability and propylene selectivity have been subjected to the diversity of Co speciations. Given the situation, uniformly stable hydroxylated Co2+ silicate sites (depicted as {OH–Si–(OH)–Co–O–Si-(OH)3}) are successfully embedded into the silicalite-1 zeolite framework located in the straight and intersection channels ([email protected]1) with the assistance of Co precursors and geminal silanols via a facile hydrothermal synthesis, as revealed by detail characterizations. Under comparable conditions, a superior catalytic PDH performance with attractive propylene formation rate of 14.6 mmol·gcat−1·h−1, propylene selectivity higher than 93% and very low deactivation rate of 0.0206 h−1 after 7 h is achieved over the [email protected](EDA) catalyst. Furthermore, the catalytic performance can be restored to the same as that of the fresh catalyst after 3 successive regenerations. In situ FTIR spectra analysis further reveals the dynamic changes in the characteristic absorption bands associated with the hydroxylated Co2+ silicate sites and the intermediate product (2-propyl) during the PDH reaction and a reaction mechanism is proposed accordingly. This work provides a new insight for designing high-efficiency nonprecious metal PDH catalysts.
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