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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![]() ![]() ![]() | |
2009-09-01 | |
Source Publication | BIOTECHNOLOGY ADVANCES
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ISSN | 0734-9750 |
Volume | 27Issue:5Pages:612-615 |
Corresponding Author | wucz@ms.giec.ac.cn |
Abstract | 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. |
Subtype | Article |
Other Abstract | 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. |
Keyword | Biomass Gasification Clapboard-type Internal Circulating Fluidized Bed Gasifier |
WOS Headings | Science & Technology ; Life Sciences & Biomedicine |
DOI | 10.1016/j.biotechadv.2009.04.016 |
WOS Subject Extended | Biotechnology & Applied Microbiology |
URL | 查看原文 |
WOS Keyword | DRAFT TUBE ; SOLIDS |
Indexed By | SCI ; ISTP |
Language | 英语 |
WOS Subject | Biotechnology & Applied Microbiology |
WOS ID | WOS:000267741300014 |
Citation statistics | |
Document Type | 期刊论文 |
Identifier | http://ir.giec.ac.cn/handle/344007/3330 |
Collection | 中国科学院广州能源研究所 |
Affiliation | Chinese Acad Sci, Guangzhou Inst Energy Convers, CAS Key Lab Renewable Energy & Gas Hydrate, Guangzhou 510640, Guangdong, Peoples R China |
First Author Affilication | GuangZhou 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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