Equilibrium modeling of gasification: Gibbs free energy minimization approach and its application to spouted bed and spout-fluid bed gasifiers

被引:263
作者
Jarungthammachote, S. [1 ]
Dutta, A. [1 ]
机构
[1] Asian Inst Technol, Sch Environm Resources & Dev, Energy Field Study, Klonghuang 12120, Pathumthani, Thailand
关键词
thermodynamic equilibrium model; minimization of Gibbs free energy; spouted bed; spout-fluid bed;
D O I
10.1016/j.enconman.2008.01.006
中图分类号
O414.1 [热力学];
学科分类号
摘要
Spouted beds have been found in many applications, one of which is gasification. In this paper, the gasification processes of conventional and modified spouted bed gasifiers were considered. The conventional spouted bed is a central jet spouted bed, while the modified spouted beds are circular split spouted bed and spout-fluid bed. The Gibbs free energy minimization method was used to predict the composition of the producer gas. The major six components, CO, CO2, CH4, H2O, H-2 and N-2, were determined in the mixture of the producer gas. The results showed that the carbon conversion in the gasification process plays an important role in the model. A modified model was developed by considering the carbon conversion in the constraint equations and in the energy balance calculation. The results from the modified model showed improvements. The higher heating values (HHV) were also calculated and compared with the ones from experiments. The agreements of the calculated and experimental values of HHV, especially in the case of the circular split spouted bed and the spout-fluid bed were observed. (C) 2008 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1345 / 1356
页数:12
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