Gas holdup and bubble dynamics in a three-phase internal loop reactor with external slurry circulation

被引:21
|
作者
Zhang, Kai [1 ,2 ]
Qi, Nana [1 ]
Jin, Jiaqi [1 ]
Lu, Chunxi [1 ]
Zhang, Hu [3 ]
机构
[1] China Univ Petr, State Key Lab Heavy Oil Proc, Beijing 102249, Peoples R China
[2] N China Elect Power Univ, Natl Engn Lab Biomass Power Generat Equipment, Beijing 102206, Peoples R China
[3] Univ Adelaide, Dept Chem Engn, Adelaide, SA 5005, Australia
关键词
Three-phase internal loop reactor; External slurry circulation; Gas holdup; Bubble size; Bubble rise velocity; TEMPERATURE METHANOL SYNTHESIS; AIRLIFT REACTOR; COLUMN REACTORS; FLUIDIZED-BEDS; LIQUID; HYDRODYNAMICS; DISTRIBUTIONS; BEHAVIOR; VELOCITY; PHASE;
D O I
10.1016/j.fuel.2009.09.009
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
As modified three-phase fluidized reactors, loop reactors have been widely used in the area of chemical and energy processes. An external slurry circulation is introduced into a traditional internal loop reactor to improve the transfer between gas and slurry phases. Gas holdup and bubble dynamics are investigated by using the double-sensor conductivity probe technique in the present work. The results show that gas holdup inside the draft tube is greatly affected by the geometrical configuration and is much higher than that in the corresponding section of the annular region. Local, section-averaged, and overall gas holdups increase with increasing superficial gas velocity, while the effects of solid loading and external slurry circulation velocity are less significant than that of superficial gas velocity. Both local bubble size and bubble rise velocity vary significantly in different regions. (C) 2009 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1361 / 1369
页数:9
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