芳构化
热气腾腾的
催化作用
ZSM-5型
沸石
乙烯
化学
酸强度
焦炭
产量(工程)
无机化学
化学工程
有机化学
材料科学
冶金
工程类
食品科学
作者
Aihua Zhang,Hui Wang,Hua Liu,Amin Sardar,Junjun Shan,Louis Guillen
标识
DOI:10.1016/j.mcat.2022.112313
摘要
• A research paper on Ga-ZSM-5 based catalyst performance upgrading for ethylene aromatization through steaming treatment. • Reported that steaming treatment for the base catalyst could lower the total zeolite acidity and reduce the acid strength of the strong acid site as well, and the catalysts prepared in this way exhibited excellent catalytic performance in terms of target product yield, lifetime etc. • Examined reaction mechanism and revealed the root cause that results in such remarkable positive impact. • The findings of this work would provide insights and solutions for zeolite based acidic catalyst design. In continuation of our two-step process development for the conversion of ethane to aromatics, this work focuses on catalyst performance improvement for ethylene aromatization. The approach is to apply steaming dealumination method to tailor ZSM-5 acidity to optimize its catalytic performance. Our results indicate that applying steaming treatment for the base Ga-ZSM-5 catalyst at specified conditions could reduce the total acid amount from 0.46 to 0.15–0.25 mmol/g, with 46–67% acidity loss, accompanied with the decrease of the acid strength for the strong acid sites. As a result, the catalyst prepared in this way exhibited a step-change performance enhancement in terms of cycle lifetime, target product yield/capacity, byproduct, coke formation and so on. Through examining the reaction mechanism and acid strength requirements for individual steps involved in ethylene aromatization, we conclude that steps that require strong acid strength – such as cracking and aromatics alkylation (both leading to catalyst deactivation) are effectively suppressed due to the lower acid amount/strength obtained after steaming treatment. The findings and this zeolite acidity tailoring technique will provide insights and solutions for zeolite-based acidic catalyst design. .
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