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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
Source PublicationBIOTECHNOLOGY ADVANCES
ISSN0734-9750
Volume27Issue:5Pages:612-615
Corresponding Authorwucz@ms.giec.ac.cn
AbstractWe 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.
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Other AbstractWe 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.
KeywordBiomass Gasification Clapboard-type Internal Circulating Fluidized Bed Gasifier
WOS HeadingsScience & Technology ; Life Sciences & Biomedicine
DOI10.1016/j.biotechadv.2009.04.016
WOS Subject ExtendedBiotechnology & Applied Microbiology
URL查看原文
WOS KeywordDRAFT TUBE ; SOLIDS
Indexed BySCI ; ISTP
Language英语
WOS SubjectBiotechnology & Applied Microbiology
WOS IDWOS:000267741300014
Citation statistics
Cited Times:26[WOS]   [WOS Record]     [Related Records in WOS]
Document Type期刊论文
Identifierhttp://ir.giec.ac.cn/handle/344007/3330
Collection中国科学院广州能源研究所
AffiliationChinese Acad Sci, Guangzhou Inst Energy Convers, CAS Key Lab Renewable Energy & Gas Hydrate, Guangzhou 510640, Guangdong, Peoples R China
First Author AffilicationGuangZhou Institute of Energy Conversion,Chinese Academy of Sciences
Recommended Citation
GB/T 7714
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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