Catalytic characteristics of innovative Ni/slag catalysts for syngas production and tar removal from biomass pyrolysis

被引:57
|
作者
Liu, Yang [1 ]
Yu, Haimiao [1 ]
Liu, Jiecheng [1 ]
Chen, Dezhen [1 ]
机构
[1] Tongji Univ, Inst Thermal & Environm Engn, 1239 Siping Rd, Shanghai, Peoples R China
关键词
Biomass pyrolysis; Catalytic reforming; Industrial waste; Catalyst activity; Coke deposition resistance; CHEMICAL LOOPING GASIFICATION; HYDROGEN-PRODUCTION; MODEL-COMPOUND; STEAM GASIFICATION; NICKEL FERRITE; FLUIDIZED-BED; CARBON; NI; TOLUENE; GAS;
D O I
10.1016/j.ijhydene.2019.03.024
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
In this study, innovative Ni-based catalysts supported by five typical slag carriers (magnesium slag (MS), steel slag (SS), blast furnace slag (BFS), pyrite cinder (PyC) and calcium silicate slag (CSS)) were prepared by wet impregnation. With the prepared catalysts and Ni/gamma-Al2O3 catalyst, catalytic reforming of pyrolysis volatiles from pine sawdust for syngas production and tar removal was investigated. The catalysts were characterized by BET, XRD, SEM, TEM and Raman. The catalytic performances of the six catalysts were decreasing in the following order: Ni/MS > Ni/gamma-Al2O3 > Ni/SS > Ni/BFS > Ni/CSS > Ni/PyC. Ni/MS catalyst exhibited excellent catalytic reactivity as well as thermal stability in terms of tar conversion (95.19%), gas yield (1.46 Nm(3)/kg) and CO2 capture ability (CO2 yield of 0.5%). Both amorphous carbon and graphite-type carbon were formed on the catalysts after catalytic reforming and the D/G ratio (the relative intensity ratio of the D-band to the G-band) was positively correlated to the catalytic activity. (C) 2019 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:11848 / 11860
页数:13
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