Catalytic fast pyrolysis of biomass over core-shell HZSM-5@silicalite-1 in a bench-scale two-stage fluidized-bed/fixed-bed reactor

被引:20
|
作者
Hu, Changsong [1 ]
Zhang, Huiyan [1 ]
Xiao, Rui [1 ]
机构
[1] Southeast Univ, Sch Energy & Environm, Minist Educ, Key Lab Energy Thermal Convers & Control, Nanjing 210096, Jiangsu, Peoples R China
基金
中国国家自然科学基金; 美国国家科学基金会;
关键词
Biomass; Catalytic fast pyrolysis; Modified HZSM-5; Core-shell; Silicalite-1; Fluidized-bed; CHEMICAL LIQUID DEPOSITION; SIZED HZSM-5 ZEOLITE; P-XYLENE; BIO-OIL; SELECTIVE PRODUCTION; MODEL COMPOUNDS; TOLUENE; ZSM-5; SITU; GENERATION;
D O I
10.1016/j.jaap.2018.11.005
中图分类号
O65 [分析化学];
学科分类号
070302 ; 081704 ;
摘要
In order to inhibit the coke formation on the external surface of HZSM-5 during catalytic fast pyrolysis (CFP) of biomass, core-shell structured HZSM-5@silicalite-1 zeolite catalysts were hydrothermally synthesized through the growth of silicalite-1 along the surface of a commercial HZSM-5. The catalyst characterization results indicate that silicalite-1 outer shell layer was successfully formed on the HZSM-5 core particles. Silicalite-1 coating was proved to be effective to reduce the external acidity as well as keep the internal acidity and channel patency of core HZSM-5 by catalytic probe reactions. The catalytic performances of HZSM-5@silicalite-1 samples in CFP of biomass were investigated using a bench-scale continuous feeding two-stage fluidized-bed/fixed-bed combination reactor. The results show that the productions of olefins and BTX were promoted (especially BTX), while the formations of catalyst coke and PAHs were significantly inhibited after silicalite-1 coating.
引用
收藏
页码:27 / 34
页数:8
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