CFD Simulation of a Bubbling Fluidized Bed Gasifier Using a Bubble-Based Drag Model

被引:30
作者
Chen, Juhui [1 ,2 ]
Yu, Guangbin [1 ,2 ,3 ]
Dai, Bing [2 ]
Liu, Di [2 ]
Zhao, Lei [2 ]
机构
[1] Harbin Univ Sci & Technol, Higher Educ Key Lab Measuring & Control Technol &, Harbin 150080, Peoples R China
[2] Harbin Univ Sci & Technol, Sch Mech Engn, Harbin 150080, Peoples R China
[3] Harbin Inst Technol, Harbin 150001, Peoples R China
基金
黑龙江省自然科学基金;
关键词
BIOMASS GASIFICATION; NUMERICAL-SIMULATION; HEAT; WOOD; COMBUSTION; PARTICLES; PYROLYSIS; SYSTEM; SCALE; FLOW;
D O I
10.1021/ef501134e
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
Wood gasification in a fluidized bed reactor is regards as a promising technique to efficiently exploit the energy from biomass, which has attracted great attention. To further understand complex fluid mechanics and thermal behaviors of wood during the gasification process, a multiphase reactive model is presented, and a computational fluid dynamics (CFD) simulation of wood gasification in a bubbling fluidized bed gasifier is implemented. To account for the impact of bubble-structure on the gassolid interaction, a revised bubble-based energy minimization multiscale (EMMS) drag model is developed and incorporated into a two-fluid model. Flow behaviors and reactive characteristics in a bubbling fluidized bed gasifier are analyzed. Profiles of temperature and concentration of gas and solid phase are also obtained. By comparisons of the outlet gas species concentrations, the prediction by a revised bubble-based EMMS drag model agrees better with experimental results than that by the conventional drag model.
引用
收藏
页码:6351 / 6360
页数:10
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