Gasification of biomass char with air-steam in a cyclone furnace

被引:27
|
作者
He, Pi-wen [1 ,2 ]
Luo, Si-yi [3 ]
Cheng, Gong [1 ]
Xiao, Bo [1 ]
Cai, Lei [1 ]
Wang, Jin-bo [1 ]
机构
[1] Huazhong Univ Sci & Technol, Sch Environm Sci & Engn, Wuhan 430074, Peoples R China
[2] Yangtze Univ, Sch Urban Construct, Jinzhou 434023, Peoples R China
[3] Qingdao Technol Univ, Sch Environm & Municipal Engn, Qingdao 266035, Peoples R China
基金
中国国家自然科学基金;
关键词
Gasification; Char; Cyclone furnace; RICH GAS-PRODUCTION; FLUIDIZED-BED; PYROLYSIS; GASIFIER; TEMPERATURE; WOOD;
D O I
10.1016/j.renene.2011.07.001
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Biomass char, obtained from the residues of biomass pyrolysis, was employed as feedstock for the gasification using an air-steam agent. The gasification with the energy self-sufficiency was carried out in a cyclone furnace where combustor and gasifier were combined into one reactor. The effects of equivalence ratio (ER) and steam to char ratio (S/C) on gasification performance were investigated. The results showed that the increasing ER led to the increasing reactor temperature and increased dry gas yield, H(2) yield and carbon conversion efficiency. The introduction of steam promoted the gas quality, but excessive steam would lower reactor temperature and degrade gas quality. Under the optimum experimental conditions (ER = 0.36, S/C = 0.45), the yield of the tar-free gas reached 3.72 N m(3)/kg and the LHV of the fuel gas was 4163 kJ/N m(3). (C) 2011 Elsevier Ltd. All rights reserved.
引用
收藏
页码:398 / 402
页数:5
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