An experiment study of biomass steam gasification over NiO/Dolomite for hydrogen-rich gas production

被引:65
|
作者
Zhang, Bo [1 ,2 ,3 ]
Zhang, Li [1 ,2 ]
Yang, Zhongqing [1 ,2 ]
He, Zhixia [3 ]
机构
[1] Chongqing Univ, Minist Educ China, Key Lab Low Grade Energy Utilizat Technol & Syst, Chongqing 400044, Peoples R China
[2] Chongqing Univ, Coll Power Engn, Chongqing 400044, Peoples R China
[3] Jiangsu Univ, Inst Energy Res, Zhenjiang 212013, Peoples R China
基金
中国国家自然科学基金;
关键词
NiO; Gasification; Dolomite; Hydrogen; CO2; CAPTURE; COKE CHARACTERIZATION; MODEL-COMPOUND; FLUIDIZED-BED; CATALYSTS; TAR; TEMPERATURE; PARAMETERS; TOLUENE; YIELD;
D O I
10.1016/j.ijhydene.2016.10.044
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
The reactivity of dolomite, limestone and NiO/Dolomite toward hydrogen production during high temperature steam gasification of biomass were evaluated. NiO/Dolomite additive was prepared from impregnation of NiO on dolomite surface. Reactor with gasification bed operated at 900 degrees C and sorption/reforming bed operated at 730 degrees C at downstream was applied in this paper. Results show that co-gasification of biomass and additive increased overall gas yield and also the CO2 concentration. With dolomite in the sorption/reforming bed and none additive in gasification bed, the highest hydrogen concentration was achieved (71.8 vol.%). With 2wt.% NiO/Dolomite in the sorption/reforming bed and dolomite in the gasification bed separately, the highest hydrogen yield (510 cm(3)/g) was reached. Further increasing NiO content decreased hydrogen yield, sorption capacity and increased coke deposition. Calcination of NiO/Dolomite at 950 degrees C led to formation of NiO-MgO phase and reduced to Ni-MgO phase during gasification which increased the catalysis of the additive. (C) 2016 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:76 / 85
页数:10
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