Enhanced Aromatic Yield from WEEE via Ex Situ Catalytic Pyrolysis: A Comparative Study of HZSM-5, Fe/HZSM-5, and CaO Catalysts in Single and Dual Modes

IF 7.3 1区 化学 Q1 CHEMISTRY, MULTIDISCIPLINARY ACS Sustainable Chemistry & Engineering Pub Date : 2025-04-09 DOI:10.1021/acssuschemeng.4c08759
Samina Gulshan*, Hoda Shafaghat, Hanmin Yang, Panagiotis Evangelopoulos and Weihong Yang, 
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Abstract

This study investigated an efficient catalyst configuration to enhance the recycling of waste electrical and electronic equipment (WEEE) fractions into aromatic hydrocarbons. Two engineered WEEE fractions, low-grade (LGEW) and medium-grade (MGEW), were used as feedstock in an ex situ catalytic pyrolysis process conducted in a two-stage lab-scale reactor. The first stage involved a batch pyrolyzer, followed by a fixed-bed catalytic reactor. The interaction between catalyst active sites and pyrolysis vapors played a key role in determining the chemical functionality of the surface intermediates. Five catalytic modes were tested: CaO, HZSM-5, Fe/HZSM-5, and a combination of CaO and HZSM-5 in mixed and separate bed configurations, with a catalyst-to-feedstock ratio of 0.15 w/w. The iron-loaded zeolite favored gas production, while CaO effectively converted acids into ketones. The dual-catalyst mixed bed of CaO and HZSM-5 exhibited the best catalytic synergy, enhancing the production of aromatic hydrocarbons and decarbonizing the process. However, metal doping increased catalyst coke formation due to more Lewis acid sites and the production of polycyclic aromatic hydrocarbons. Overall, this study provides a comparative analysis of catalyst activity during the thermochemical conversion of WEEE.

Ex situ catalytic pyrolysis of WEEE using various catalyst configurations focuses on maximizing aromatic yields, supporting efficient recycling and energy recovery.

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HZSM-5、Fe/HZSM-5和CaO催化剂单、双模式催化热解提高WEEE芳烃产率的比较研究
本研究研究了一种有效的催化剂配置,以提高废弃电气电子设备(WEEE)馏分回收为芳烃的效率。在实验室规模的两级反应器中,以低品位(LGEW)和中品位(MGEW)两种工程WEEE馏分为原料,进行了非原位催化热解过程。第一阶段包括间歇式热解装置,随后是固定床催化反应器。催化剂活性位点与热解蒸汽之间的相互作用在决定表面中间体的化学功能方面起着关键作用。测试了CaO、HZSM-5、Fe/HZSM-5以及CaO和HZSM-5在混合床和分离床构型下的组合催化模式,催化剂进料比为0.15 w/w。载铁沸石有利于产气,而CaO则有效地将酸转化为酮。CaO和HZSM-5的双催化剂混合床表现出最佳的催化协同作用,促进了芳烃的生成和脱碳过程。然而,金属掺杂增加了催化剂焦炭的生成,因为产生了更多的路易斯酸位点和多环芳烃。总的来说,本研究对WEEE热化学转化过程中的催化剂活性进行了比较分析。使用不同催化剂配置的废旧电子电气设备的非原位催化热解的重点是最大限度地提高芳香收率,支持有效的循环利用和能量回收。
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来源期刊
ACS Sustainable Chemistry & Engineering
ACS Sustainable Chemistry & Engineering CHEMISTRY, MULTIDISCIPLINARY-ENGINEERING, CHEMICAL
CiteScore
13.80
自引率
4.80%
发文量
1470
审稿时长
1.7 months
期刊介绍: ACS Sustainable Chemistry & Engineering is a prestigious weekly peer-reviewed scientific journal published by the American Chemical Society. Dedicated to advancing the principles of green chemistry and green engineering, it covers a wide array of research topics including green chemistry, green engineering, biomass, alternative energy, and life cycle assessment. The journal welcomes submissions in various formats, including Letters, Articles, Features, and Perspectives (Reviews), that address the challenges of sustainability in the chemical enterprise and contribute to the advancement of sustainable practices. Join us in shaping the future of sustainable chemistry and engineering.
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