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Study on biomass circulation and gasification performance in a clapboard-type internal circulating fluidized bed gasifier
Zhou, Zhao-qiu; Ma, Long-long; Yin, Xiu-li; Wu, Chuang-zhi; Huang, Li-cheng; Wang, Chu
2009-09-01
发表期刊BIOTECHNOLOGY ADVANCES
ISSN0734-9750
卷号27期号:5页码:612-615
通讯作者wucz@ms.giec.ac.cn
摘要We investigated the solid particle flow characteristics and biomass gasification in a clapboard-type internal circulating fluidized bed reactor. The effect of fluidization velocity on particle circulation rate and pressure distribution in the bed showed that fluidization velocities in the high and low velocity zones were the main operational parameters controlling particle circulation. The maximum internal circulation rates in the low velocity zone came almost within the range of velocities in the high velocity zone, when u(H)/u(mf) = 2.2-2.4 for rice husk and u(H)/u(mf) = 3.5-4.5 for quartz sand. In the gasification experiment. the air equvalence ratio (ER) was the main controlling parameter. Rice husk gasification gas had a maximum heating value of around 5000 kJ/m(3) when ER = 0.22-0.26, and sawdust gasification gas reached around 6000-6500 kJ/m(3) when ER = 0.175-0.24. The gasification efficiency of rice husk reached a maximum of 77% at ER = 0.28, while the gasification efficiency of sawdust reached a maximum of 81 % at ER = 0.25. (C) 2009 Elsevier Inc. All rights reserved.
文章类型Article
其他摘要We investigated the solid particle flow characteristics and biomass gasification in a clapboard-type internal circulating fluidized bed reactor. The effect of fluidization velocity on particle circulation rate and pressure distribution in the bed showed that fluidization velocities in the high and low velocity zones were the main operational parameters controlling particle circulation. The maximum internal circulation rates in the low velocity zone came almost within the range of velocities in the high velocity zone, when uH/umf = 2.2-2.4 for rice husk and uH/umf = 3.5-4.5 for quartz sand. In the gasification experiment, the air equvalence ratio (ER) was the main controlling parameter. Rice husk gasification gas had a maximum heating value of around 5000 kJ/m3 when ER = 0.22-0.26, and sawdust gasification gas reached around 6000-6500 kJ/m3 when ER = 0.175-0.24. The gasification efficiency of rice husk reached a maximum of 77% at ER = 0.28, while the gasification efficiency of sawdust reached a maximum of 81% at ER = 0.25.
关键词Biomass Gasification Clapboard-type Internal Circulating Fluidized Bed Gasifier
WOS标题词Science & Technology ; Life Sciences & Biomedicine
DOI10.1016/j.biotechadv.2009.04.016
研究领域[WOS]Biotechnology & Applied Microbiology
URL查看原文
关键词[WOS]DRAFT TUBE ; SOLIDS
收录类别SCI ; ISTP
语种英语
WOS类目Biotechnology & Applied Microbiology
WOS记录号WOS:000267741300014
引用统计
被引频次:23[WOS]   [WOS记录]     [WOS相关记录]
文献类型期刊论文
条目标识符http://ir.giec.ac.cn/handle/344007/3330
专题中国科学院广州能源研究所
作者单位Chinese Acad Sci, Guangzhou Inst Energy Convers, CAS Key Lab Renewable Energy & Gas Hydrate, Guangzhou 510640, Guangdong, Peoples R China
第一作者单位中国科学院广州能源研究所
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Zhou, Zhao-qiu,Ma, Long-long,Yin, Xiu-li,et al. Study on biomass circulation and gasification performance in a clapboard-type internal circulating fluidized bed gasifier[J]. BIOTECHNOLOGY ADVANCES,2009,27(5):612-615.
APA Zhou, Zhao-qiu,Ma, Long-long,Yin, Xiu-li,Wu, Chuang-zhi,Huang, Li-cheng,&Wang, Chu.(2009).Study on biomass circulation and gasification performance in a clapboard-type internal circulating fluidized bed gasifier.BIOTECHNOLOGY ADVANCES,27(5),612-615.
MLA Zhou, Zhao-qiu,et al."Study on biomass circulation and gasification performance in a clapboard-type internal circulating fluidized bed gasifier".BIOTECHNOLOGY ADVANCES 27.5(2009):612-615.
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