Three-dimensional full-loop simulation of a dual fluidized-bed biomass gasifier

被引:111
作者
Liu, Hui [1 ]
Cattolica, Robert J. [1 ]
Seiser, Reinhard [1 ]
Liao, Chang-hsien [2 ]
机构
[1] Univ Calif San Diego, Dept Mech & Aerosp Engn, La Jolla, CA 92093 USA
[2] West Biofuels LLC, Woodland Biomass Res Ctr, Woodland, CA 95776 USA
基金
芬兰科学院;
关键词
Biomass gasification; Fluidization; CFD modeling; CFD-DEM SIMULATION; GAS-SOLID FLOW; COAL-GASIFICATION; EXPERIMENTAL-VERIFICATION; PARTICLE-SIZE; MODEL; BIOENERGY; STEAM; HYDRODYNAMICS; VALIDATION;
D O I
10.1016/j.apenergy.2015.09.065
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
A three-dimensional CFD model was developed to simulate the full-loop of a dual fluidized-bed biomass gasification system consisting of a gasifier, a combustor, a cyclone separator, and a loop-seal. This full-loop simulation includes the chemical kinetic modeling of biomass drying and pyrolysis, heterogeneous char reactions, and homogeneous gas-phase reactions. In the model, the gas phase is described using Large Eddy Simulation (LES) and the particle phase is described with the Multiphase Particle-In-Cell (MP-PIC) method. The simulation was performed using the CPU-accelerated computing and the simulation results were compared with the gas composition and temperature measurements from a pilot-scale biomass gasification power plant (1 MWth, 6 tons biomass/day). The independence of the accuracy of the model on mesh resolution and computational particle number was determined. The impacts of the particle size distributions (PSD) and drag models on the reactive flows were also investigated. (C) 2015 Elsevier Ltd. All rights reserved.
引用
收藏
页码:489 / 501
页数:13
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