Numerical simulations on the effect of potassium on the biomass fast pyrolysis in fluidized bed reactor

被引:23
|
作者
Eri, Qitai [1 ]
Zhao, Xinjun [1 ]
Ranganathan, Panneerselvam [2 ]
Gu, Sai [3 ]
机构
[1] Beihang Univ, Sch Energy & Power Engn, Beijing 100191, Peoples R China
[2] CSIR, Natl Inst Interdisciplinary Sci & Technol, Environm Technol Div, Trivandrum, Kerala, India
[3] Univ Surrey, Dept Chem & Proc Engn, Guildford, Surrey, England
基金
英国工程与自然科学研究理事会;
关键词
Biomass fast pyrolysis; Potassium; Fluidized bed; Multi-fluid model; PARTICLES; ALKALI; METAL; HEAT; WOOD; MASS;
D O I
10.1016/j.fuel.2017.01.109
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
In this study, the effect of potassium on the cellulose fast pyrolysis in a fluidized bed reactor has been studied using Computational Fluid Dynamics (CFD). A multiphase pyrolysis model of cellulose has been implemented by integrating the hydrodynamics of the fluidized bed with an adjusted cellulose pyrolysis mechanism that accounts for the effect of potassium. The model has been validated with the reported experimental data. The simulation results show that potassium concentration and reactor temperature have a significant effect on the yield and component of cellulose pyrolysis products. The product yields fluctuate is caused by the unstable flow in the fluidized bed. The result shows that the increased potassium concentration in the cellulose causes a significant increase of the gas and char yields and reduction in the bio-oil. Also, the dramatic composition variations in bio-oil and gas were observed due to the inhibition of fragmentation, and the depolymerization reaction of activated cellulose, and the catalysis of the depolymerization reaction of cellulose. It is also found that the increase in reactor temperature greatly enhances the endothermic pyrolysis reaction, which leads to the significant changes in the yield and composition of cellulose pyrolysis products. (C) 2017 The Authors. Published by Elsevier Ltd.
引用
收藏
页码:290 / 297
页数:8
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