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Fluidizing ultrafine powders with circulating fluidized bed
Alternative TitleChem. Eng. Sci.
Li, HZ; Hong, RY; Wang, ZL
1999-11-01
Source PublicationCHEMICAL ENGINEERING SCIENCE
ISSN0009-2509
Volume54Issue:22Pages:5609-5615
AbstractThe hydrodynamic behavior of a number of ultrafine powders in a circulating fluidized bed was investigated. Different ultrafine powders displayed different fluidization behaviors in the dipleg and the powder return system, but their hydrodynamic behaviors in the riser were almost the same. The addition of coarse particles could improve the quality of fluidization, showing, in addition, that for the powder return system the V-valve was much better than the inclined butterfly-valve, because blockage might occur in the latter. Ultrafine powders could be easily recovered from the exhaust vent by cyclones due to the formation of agglomerates. Fan-shaped baffles in the dipleg could suppress slugging and ensure stable operation. Experimental voidage profiles in the riser showed that the voidage was low at the bottom and high at the upper part. There was, however, a relatively dense zone at the top because of exit effect. Such axial voidage profile in a riser was successfully calculated by using a two-phase model. The reason for non-uniform distribution of voidage was also discussed. (C) 1999 Elsevier Science Ltd. All rights reserved.; The hydrodynamic behavior of a number of ultrafine powders in a circulating fluidized bed was investigated. Different ultrafine powders displayed different fluidization behaviors in the dipleg and the powder return system, but their hydrodynamic behaviors in the riser were almost the same. The addition of coarse particles could improve the quality of fluidization, showing, in addition, that for the powder return system the V-valve was much better than the inclined butterfly-valve, because blockage might occur in the latter. Ultrafine powders could be easily recovered from the exhaust vent by cyclones due to the formation of agglomerates. Fan-shaped baffles in the dipleg could suppress slugging and ensure stable operation. Experimental voidage profiles in the riser showed that the voidage was low at the bottom and high at the upper part. There was, however, a relatively dense zone at the top because of exit effect. Such axial voidage profile in a riser was successfully calculated by using a two-phase model. The reason for non-uniform distribution of voidage was also discussed. (C) 1999 Elsevier Science Ltd. All rights reserved.
KeywordUltrafine Powder Circulating Fluidized Bed Agglomerate
SubtypeArticle
WOS HeadingsScience & Technology ; Technology
URL查看原文
Indexed BySCI
Language英语
WOS Research AreaEngineering
WOS SubjectEngineering, Chemical
WOS IDWOS:000082287100026
Citation statistics
Cited Times:23[WOS]   [WOS Record]     [Related Records in WOS]
Document Type期刊论文
Version出版稿
Identifierhttp://ir.ipe.ac.cn/handle/122111/5941
Collection研究所(批量导入)
AffiliationChinese Acad Sci, Inst Chem Met, Multiphase React Lab, Beijing 100080, Peoples R China
Recommended Citation
GB/T 7714
Li, HZ,Hong, RY,Wang, ZL. Fluidizing ultrafine powders with circulating fluidized bed[J]. CHEMICAL ENGINEERING SCIENCE,1999,54(22):5609-5615.
APA Li, HZ,Hong, RY,&Wang, ZL.(1999).Fluidizing ultrafine powders with circulating fluidized bed.CHEMICAL ENGINEERING SCIENCE,54(22),5609-5615.
MLA Li, HZ,et al."Fluidizing ultrafine powders with circulating fluidized bed".CHEMICAL ENGINEERING SCIENCE 54.22(1999):5609-5615.
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