CFD Simulation of Pyrolysis of Lignite in a Downstream Fluidized Bed

被引:2
|
作者
Sun, Yongli [1 ]
Zhang, Rong [1 ]
Zhang, Lvhong [1 ]
Zhang, Yanan [1 ]
机构
[1] Tianjin Univ, Sch Chem Engn & Technol, Tianjin 300072, Peoples R China
关键词
CFD simulation; lignite particle; pyrolysis; fluidized bed; MASS-TRANSPORT; MOMENTUM; BIOMASS; HEAT; FLOW; PART;
D O I
10.4028/www.scientific.net/AMR.457-458.515
中图分类号
T [工业技术];
学科分类号
08 ;
摘要
This paper works with the CFD simulation of the process of pyrolysis of lignite particles in a downstream fluidized bed, which actually means the particles would fall down from the injection point and escape the furnace from the bottom. The particle track is solved by using the Lagrangian approach, while the flow of the inert gas (nitrogen) is dealt with by the Eulerian approach. The heat transferred from the nitrogen gas to the surface of particle is computed by means of the famous Ranz-Marshall correlation. The chemical reactions are simulated using part of the coal combustion model inserted in the commercial software used.
引用
收藏
页码:515 / 520
页数:6
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