Numerical simulation of reactive transfers in spouted beds at high temperature: Application to coal gasification

被引:20
作者
Mendes, A. [1 ,2 ,3 ]
Dollet, A. [1 ,2 ]
Ablitzer, C. [3 ]
Perrais, C. [3 ]
Flamant, G. [1 ,2 ]
机构
[1] CNRS, Lab Procedes Mat & Energie Solaire, Odeillo Font Romeu, France
[2] CNRS, Lab Procedes Mat & Energie Solaire, Perpignan, France
[3] CEA, Ctr Cadarache, Lab Combustibles Uranium, Cadarache, France
关键词
spouted bed; fluidized bed; coal gasification; modelling; heat transfer; mass transfer; high temperature;
D O I
10.1016/j.jaap.2008.02.001
中图分类号
O65 [分析化学];
学科分类号
070302 ; 081704 ;
摘要
Spouted beds are used in many physical and chemical processes that involve large particles (drying, combustion, film deposition, gasification, etc.). Understanding of bed hydrodynamics, coupled heat and mass transfer and chemical reaction phenomena is mandatory for designing, scaling up and optimizing spouted beds. In this work, a spouted bed reactor operating at high temperature has been modelled through one-dimensional model in which heat transfer has been carefully described at different levels of complexity. The process of coal gasification has been selected to demonstrate the models achievements and predictions have been compared to previous spouted bed reactor experimental results. Calculations have shown that a particular attention must be paid to describe heat transfer in spouted bed reactors operating at high temperature. (C) 2008 Elsevier B.V. All rights reserved.
引用
收藏
页码:117 / 128
页数:12
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