CAS OpenIR  > 研究所(批量导入)
Lignite upgrading by multi-stage fluidized bed pyrolysis
Zhou, Qi1,2; Zou, Tao1,3; Zhong, Mei4; Zhang, Yuming1,2; Wu, Rongcheng1; Gao, Shiqiu1; Xu, Guangwen1
2013-12-01
Source PublicationFUEL PROCESSING TECHNOLOGY
Volume116Issue:0Pages:35-43
AbstractThis study is devoted to demonstrating experimentally the technical advantages of the multi-stage fluidized bed pyrolysis for upgrading lignite. A Chinese lignite was pyrolyzed and partially gasified in a three-stage laboratory-scale fluidized bed, with an overflow standpipe between its neighboring stages, to clarify the improvement on the pyrolysis product quality by increasing the number of the stages. While the bottom stage had the highest temperature of about 900 degrees C for fuel gasification, the upper stage had temperatures of 550-650 degrees C for coal pyrolysis. The multi-stage fluidized bed was operated with a continuous feed in the modes with one to three stages. The resulting yields of gas and tar were higher, whereas the yield of char was lower for the operations with multiple stages. The produced CO, H-2 and CH4 in the two- and three-stage modes were more than that in the single-stage mode, having thus the higher gas heating value as well. The tar from the three-stage fluidized bed pyrolysis contained more light oil, and it plus phenol oil reached 99.5 wt.% of the tar. The char produced in the multi-stage pyrolysis showed the higher thermal stability in terms of its higher ignition temperature and suppressed spontaneous combustion propensity. (C) 2013 Elsevier B.V. All rights reserved.
KeywordMulti-stage Fluidized Bed Lignite Upgrading Pyrolysis Gasification Lignite
SubtypeArticle
WOS HeadingsScience & Technology ; Physical Sciences ; Technology
Indexed BySCI
Language英语
WOS KeywordCOAL PYROLYSIS ; STEAM GASIFICATION ; FLASH PYROLYSIS ; BROWN-COAL ; CHAR ; DEVOLATILIZATION ; REACTIVITY ; REACTOR ; BEHAVIOR
WOS Research AreaChemistry ; Energy & Fuels ; Engineering
WOS SubjectChemistry, Applied ; Energy & Fuels ; Engineering, Chemical
WOS IDWOS:000325844100005
Citation statistics
Cited Times:32[WOS]   [WOS Record]     [Related Records in WOS]
Document Type期刊论文
Identifierhttp://ir.ipe.ac.cn/handle/122111/13688
Collection研究所(批量导入)
Affiliation1.Chinese Acad Sci, Inst Proc Engn, State Key Lab Multiphase Complex Syst, Beijing 100190, Peoples R China
2.Univ Chinese Acad Sci, Beijing 100049, Peoples R China
3.China Univ Min & Technol, Beijing 100083, Peoples R China
4.Xinjiang Univ, Dept Chem & Chem Engn, Xinjiang 830046, Peoples R China
Recommended Citation
GB/T 7714
Zhou, Qi,Zou, Tao,Zhong, Mei,et al. Lignite upgrading by multi-stage fluidized bed pyrolysis[J]. FUEL PROCESSING TECHNOLOGY,2013,116(0):35-43.
APA Zhou, Qi.,Zou, Tao.,Zhong, Mei.,Zhang, Yuming.,Wu, Rongcheng.,...&Xu, Guangwen.(2013).Lignite upgrading by multi-stage fluidized bed pyrolysis.FUEL PROCESSING TECHNOLOGY,116(0),35-43.
MLA Zhou, Qi,et al."Lignite upgrading by multi-stage fluidized bed pyrolysis".FUEL PROCESSING TECHNOLOGY 116.0(2013):35-43.
Files in This Item:
File Name/Size DocType Version Access License
Lignite upgrading by(1188KB)期刊论文出版稿限制开放CC BY-NC-SAApplication Full Text
Related Services
Recommend this item
Bookmark
Usage statistics
Export to Endnote
Google Scholar
Similar articles in Google Scholar
[Zhou, Qi]'s Articles
[Zou, Tao]'s Articles
[Zhong, Mei]'s Articles
Baidu academic
Similar articles in Baidu academic
[Zhou, Qi]'s Articles
[Zou, Tao]'s Articles
[Zhong, Mei]'s Articles
Bing Scholar
Similar articles in Bing Scholar
[Zhou, Qi]'s Articles
[Zou, Tao]'s Articles
[Zhong, Mei]'s Articles
Terms of Use
No data!
Social Bookmark/Share
All comments (0)
No comment.
 

Items in the repository are protected by copyright, with all rights reserved, unless otherwise indicated.