Enhanced Catalytic Performance of Fe-containing HZSM-5 for Ethane Non-Oxidative Dehydrogenation via Hydrothermal Post-Treatment

被引:23
|
作者
Wu, Lizhi [1 ]
Fu, Zhiyuan [1 ]
Ren, Zhuangzhuang [1 ]
Wei, Jinhe [1 ]
Gao, Xinhua [2 ]
Tan, Li [1 ]
Tang, Yu [1 ]
机构
[1] Fuzhou Univ, Coll Chem, Inst Mol Catalysis & In Situ Operando Studies, Fuzhou 350108, Peoples R China
[2] Ningxia Univ, Coll Chem & Chem Engn, State Key Lab High Efficiency Utilizat Coal & Gre, Yinchuan 750021, Ningxia, Peoples R China
基金
中国国家自然科学基金;
关键词
Ethane dehydrogenation; Fe; ZSM-5; hydrothermal post-treatment; highly dispersed Fe; METAL-OXIDE CATALYSTS; OXIDATIVE DEHYDROGENATION; PROPANE DEHYDROGENATION; ACTIVE-SITES; NITROUS-OXIDE; FE-ZSM-5; CONVERSION; ACIDITY; N2O; PT/MG(GA)(AL)O;
D O I
10.1002/cctc.202100752
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
A facile strategy is applied to construct Fe supported ZSM-5 (Fe/HZ5-HTS) via hydrothermal post-treatment and applied to ethane non-oxidative dehydrogenation. Compared with Fe/HZ5-IWI prepared by incipient wetness impregnation, Fe/HZ5-HTS exhibits superior catalytic activity and long catalyst stability with 6000 minutes time-on-stream. An obvious volcanic curve is observed between the ethylene generation rate and Fe content, and 1.0Fe/HZ5-HTS exhibits the highest ethylene generation rate with 0.166 mmol C2H4 s(-1) g(Fe)(-1) over different Fe loading, which is twice as much as that of 1.0Fe/HZ5-IWI. According to various characterizations, isolated Fe3+ species and carburized Fe species are active sites, and the better catalytic performance over 1.0Fe/HZ5-HTS is ascribed to more disperse Fe species and exposing more Fe species in the surface. Besides, the lower ethylene desorption temperature and higher ethane desorption temperature over Fe/HZ5-HTS could suppress the overreaction of the ethylene to generate coke and increase ethane residence reaction time, resulting in less coke deposition and facilitating the catalytic performance.
引用
收藏
页码:4019 / 4028
页数:10
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