详细信息

Preparation of Syngas via Catalytic Gasification of Biomass with a Nickel-based Catalyst  ( SCI-EXPANDED收录 EI收录)  

文献类型:期刊文献

英文题名:Preparation of Syngas via Catalytic Gasification of Biomass with a Nickel-based Catalyst

作者:Xu, Q.[1];Lan, P.[1,2];Zhang, B.[1];Ren, Z.[1];Yan, Y.[1]

机构:[1]E China Univ Sci & Technol, Res Ctr Biomass Energy, Minist Educ, Key Lab Coal Gasificat & Energy Chem Engn, Shanghai 200237, Peoples R China;[2]Guangxi Univ, Guangxi Univ Nationalities, Sch Chem & Ecoengn, Key Lab Chem & Biol Transforming Proc, Nanning 530004, Peoples R China

年份:2013

卷号:35

期号:9

起止页码:848

外文期刊名:ENERGY SOURCES PART A-RECOVERY UTILIZATION AND ENVIRONMENTAL EFFECTS

收录:;EI(收录号:20131616216377);WOS:【SCI-EXPANDED(收录号:WOS:000316393000008)】;

基金:This project was funded by the "973" State Key Fundamental Research Development Program of China (No. 2007CB210206).

语种:英文

外文关键词:biomass; catalyst; dolomite; gasification; modified

摘要:Biomass gasification to produce syngas was carried out in a fluidized bed reactor and a catalytic fixed bed reactor. The feedstock was sawdust and the cracking catalyst included the calcined dolomite, Ni/dolomite, Ni/modified dolomite, and reforming catalyst. The Ni/modified dolomite catalyst showed better performance and low cost. The optimum technological conditions were as follows: fluidized bed temperature, 1,073 K; catalytic fixed bed temperature, 1,073 K; the mass ratio of steam to biomass, 2.0.

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