Selective aromatization of 1-hexene to BTX over core-shell structured Silicalite-1@ZSM-5 catalyst

被引:3
|
作者
Cui, Xingxing [1 ]
Lyu, Hongyang [2 ]
Chai, Yongming [2 ]
Liu, Bin [2 ]
Zhao, Dongfeng [1 ]
Liu, Chenguang [2 ]
机构
[1] China Univ Petr East China, Coll Chem & Chem Engn, Qingdao 266580, Peoples R China
[2] China Univ Petr East China, State Key Lab Heavy Oil Proc, Qingdao 266580, Peoples R China
基金
中国国家自然科学基金;
关键词
ZSM-5; zeolite; Core-shell; BTX; Shape-selective; Acidity; Aromatization; HIERARCHICAL ZSM-5; SINGLE-CRYSTALLINE; MESOPOROUS ZSM-5; ACID SITES; METHANOL; ZSM-5-AT-SILICALITE-1; TOLUENE; HYDROCARBONS; ENHANCEMENT; ALKYLATION;
D O I
10.1016/j.seppur.2024.127881
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The strong acidity on the external surface of ZSM-5 is a primary factor resulting in the low BTX selectivity and catalyst deactivation during the olefin aromatization. In this study, a membrane-restricted Silicalite-1@ZSM-5 core-shell structured catalytic catalyst was designed and constructed for 1-hexene aromatization using a hydrothermal coating method. TEM and NMR results confirmed the complete coverage of Silicalite-1 on the surface of ZSM-5, with a shell thickness of 50 nm. The further reaction of the TIPB (1,3,5-triisopropylbenzene) molecular probe reactions demonstrated the passivation of the acid sites on ZSM-5 external surface. The inert shell layer passivated the acid sites on the external surface, thereby suppressing the isomerization of PX and the side-chain alkylation reaction of light aromatics. Compared to ZSM-5, the Silicalite-1@ZSM-5 catalyst exhibited a 37.15 % increase in BTX selectivity, a 58.65 % increase in PX selectivity, significantly reduced coke deposition, and demonstrated better stability. This strategy of in-situ epitaxial growth of inert shell layers holds significant promise for enhancing the selectivity of shape-selective catalysts and extending catalyst lifetime.
引用
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页数:12
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