Sequential modular simulation of circulating fluidized bed reactors

被引:2
|
作者
Jafari, Hasan [1 ]
Sheikhi, Amir [2 ]
Sotudeh-Gharebagh, Rahmat [1 ]
机构
[1] Univ Tehran, Coll Engn, Sch Chem Engn, Proc Design & Simulat Res Ctr, POB 11155-4563, Tehran, Iran
[2] Penn State Univ, Dept Chem Engn, University Pk, PA 16802 USA
来源
基金
美国国家科学基金会;
关键词
catalytic ozone decomposition; circulating fluidized beds; sequential modular simulation; GROUP-B PARTICLES; CLUSTER CHARACTERISTICS; OZONE DECOMPOSITION; VOIDAGE PROFILES; FLOW STRUCTURE; RISER; HYDRODYNAMICS; MODEL; DENSE; PERFORMANCE;
D O I
10.1002/cjce.23683
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Bypassing the mathematical complexity of equation-oriented approaches in predicting the performance of chemical reactors has recently stimulated a significant amount of interest. Among chemical reactors, circulating fluidized bed reactors (CFBRs) have secured an important role in a broad range of applications in energy sectors due to their advantages, including high fluid-solid contact efficiency, uniform temperature, and enhanced heat and mass transfer rates. Accordingly, modelling and predicting the performance of these reactors is of great importance. In this study, a sequence-based model was developed to predict the behaviour of CFBRs. Complex phenomena in CFBRs were mimicked by two sub-models, namely the hydrodynamics module, which addressed the physical changes, and the reaction kinetics module, which described the chemical evolution of species. The performance of the proposed model was validated with a library of catalytic ozone decomposition experimental data in CFBRs. This work introduces a new infrastructure for modelling CFBRs, which may be combined with the current process simulation software, such as Aspen Plus (c), for advanced process modelling applications.
引用
收藏
页码:1003 / 1016
页数:14
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