Computational fluid dynamics modelling of biomass fast pyrolysis in fluidised bed reactors, focusing different kinetic schemes

被引:63
作者
Ranganathan, Panneerselvam [1 ]
Gu, Sai [2 ]
机构
[1] CSIR Natl Inst Interdisciplinary Sci & Technol, Proc Engn & Environm Technol, Trivandrum, Kerala, India
[2] Univ Surrey, Dept Chem & Proc Engn, Guildford GU2 5XH, Surrey, England
基金
英国工程与自然科学研究理事会;
关键词
Biomass; Fast pyrolysis; Fluidised bed; CFD; Multiphase flows; HEAT; PARTICLES; TRANSPORT; MASS;
D O I
10.1016/j.biortech.2016.02.042
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
The present work concerns with CFD modelling of biomass fast pyrolysis in a fluidised bed reactor. Initially, a study was conducted to understand the hydrodynamics of the fluidised bed reactor by investigating the particle density and size, and gas velocity effect. With the basic understanding of hydrodynamics, the study was further extended to investigate the different kinetic schemes for biomass fast pyrolysis process. The Eulerian-Eulerian approach was used to model the complex multiphase flows in the reactor. The yield of the products from the simulation was compared with the experimental data. A good comparison was obtained between the literature results and CFD simulation. It is also found that CFD prediction with the advanced kinetic scheme is better when compared to other schemes. With the confidence obtained from the CFD models, a parametric study was carried out to study the effect of biomass particle type and size and temperature on the yield of the products. (C) 2016 The Authors. Published by Elsevier Ltd.
引用
收藏
页码:333 / 341
页数:9
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