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Theoretical analysis of Heat and Mass Transfer Phenomena during Fluidized Bed Sublimation

 

作者: R. Joulié,   G.M. Rios,  

 

期刊: Drying Technology  (Taylor Available online 1993)
卷期: Volume 11, issue 1  

页码: 157-182

 

ISSN:0737-3937

 

年代: 1993

 

DOI:10.1080/07373939308916807

 

出版商: Taylor & Francis Group

 

关键词: Gas-Solid Fluidization;Heat and Mass Transfer;Molecular sieves;Naphthalene;Sublimation / Adsorption

 

数据来源: Taylor

 

摘要:

This work present. a detailed study of heat and mass transport phenomena between a large sublimable object and a gas-solid fluidized bed of either inert or adsorbent fine panicles. Heat (h) and mass (k)transfer coefficients are related to the size and adsorption capacity of the fine particles, as well as to the diameter of the spherical immersed object and to the bed temperature. Convective and conductive components are also identified, and correlations are proposed to predict all of them. The significant differences which appear for the various working conditions may be accounted for considering the particular mechanisms that prevail in every case. A simple "surface renewal" model clearly shows the leading role of the object surface temperature. For adsorbent panicles, a local overheating phenomenon at the exchange surface is demonstrated.

 

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