Engineering non-noble Ni/WOx-ZrO2 towards boosted fuels production by catalytic upcycling of polyethylene at mild conditions

被引:8
|
作者
Shang, Jingyuan [1 ]
Li, Yan [1 ]
Zhang, Tong [1 ]
Zhang, Jinqing [1 ,3 ]
Liu, Yibin [1 ]
Chen, Xiaobo [1 ]
Feng, Xiang [1 ]
Zhang, Xingong [3 ]
Yang, Chaohe [1 ]
Chen, De [1 ,2 ]
机构
[1] China Univ Petr, State Key Lab Heavy Oil Proc, Qingdao 266580, Peoples R China
[2] Norwegian Univ Sci & Technol, Dept Chem Engn, Trondheim, Norway
[3] Qingdao Huicheng Environm Technol Co Ltd, Qingdao 266500, Peoples R China
基金
中国国家自然科学基金;
关键词
WO x surface density; Non -noble metal catalyst; Br onsted/Lewis acid sites ratio; Polyethylene; Hydrocracking; HIGH-DENSITY POLYETHYLENE; THERMAL-CRACKING; SUPPORTED NI; BIO-OIL; HYDROCRACKING; PYROLYSIS; WO3/ZRO2; HYDROISOMERIZATION; CONVERSION; GLYCEROL;
D O I
10.1016/j.jcat.2024.115302
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
Chemical upcycling through catalytic hydrocracking to fuels has potential to mitigate the serious environmental issues caused by plastic waste. Herein, non -noble tungstate-zirconia supported nickel catalyst (Ni/WOx-ZrO2) with tunable Bronsted/Lewis (B/L) ratio was firstly proposed for the hydrocracking of low -density polyethylene (LDPE), which achieves hydrogenation/dehydrogenation on Ni sites and cracking/isomerization on WOx-ZrO2, respectively. Excellent 100 % LDPE conversion with 76.9 % liquid yield was achieved, which is comparable to noble Ru-based and Pt -based catalysts. Quantitative linear relationship between B/L ratio and hydrocracking performance was established, and the key to boost performance was keenly controlling the volcanic -shape relationship between surface WOx density and B/L ratio of catalyst. Moderate WOx surface density with higher B/L ratio enhances LDPE hydrocracking, and inhibits the hydrogenation of the primary products. However, excessive WOx polymerized and formed WO3 crystals, compensating acid sites and inhibiting LDPE hydrocracking. This work is of prime scientific and industrial significance to the rational design of catalysts for industrial plastic hydrocracking.
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页数:11
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