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Chemcial Industry and Engineering 2013, Vol. 30 Issue (3) :66-70    DOI:
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Pressure Drop and Particles Distribution in the Vapor-Liquid-Solid Multi-Pipe Circulating Fluidized Bed Evaporator
 QI  Guo-Peng1, WANG  Bing-Bing2, JIANG  Feng2, LI  Xiu-Lun2,
1.School of Biology and Environment Engineering, Tianjin Vocational Institute;2.School of Chemical Engineering and Technology, Tianjin University

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Abstract A transparent multi-tube vapor-liquid-solid circulating fluidized bed evaporator was designed and built to research the pressure drop and distribution of solid particles in the heating pipe bundle. The effects of circulating flow rate, heat flux and amount of additive particle on pressure drop and distribution of solid particles in the heating pipe bundle were investigated using the pressure sensors and CCD image gathering and processing system. The results show that as the circulating flow rate and additive particle amount increase, the nonhomogeneity of particle distribution decreases and the pipe bundle pressure drop increases; while the heat flux increases, the nonhomogeneity of particle distribution decreases and the pipe bundle pressure drop fluctuates, but the pipe bundle pressure drop value is always less than the value gathered when the heating power is zero.
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QI Guo-Peng
WANG Bing-Bing
JIANG Feng
LI Xiu-Lun
Keywordsvapor-liquid-solid   circulating fluidized bed evaporator   visualization   pressure drop   particle distribution     
Received 2012-05-02;
Fund:

天津市科技支撑计划重点项目(09ZCKFGX01900)。

Corresponding Authors: 姜峰,电话:(022)78401722,E-mail:jiangfeng@tju.edu.cn。     Email: jiangfeng@tju.edu.cn
Cite this article:   
QI Guo-Peng, WANG Bing-Bing, JIANG Feng, LI Xiu-Lun.Pressure Drop and Particles Distribution in the Vapor-Liquid-Solid Multi-Pipe Circulating Fluidized Bed Evaporator[J]  Chemcial Industry and Engineering, 2013,V30(3): 66-70
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