Modeling and Optimization for Gas Distribution Patterns on Biomass Gasification Performance of a Bubbling Spout Fluidized Bed

被引:7
|
作者
Kang, Panxing [2 ]
Hu, Xiayi Eric [2 ,3 ]
Lu, Yujian [2 ]
Wang, Kuang [2 ]
Zhang, Rui [2 ]
Han, Luchang [2 ]
Yuan, Haizhuan [1 ]
Chen, Hongbo [2 ]
Luo, Xiao [4 ]
Zhou, Yefeng Jeffrey [2 ,3 ]
机构
[1] Xiangtan Univ, Hunan Key Lab Computat & Simulat Sci & Engn, Xiangtan 411105, Hunan, Peoples R China
[2] Xiangtan Univ, Chem Proc Simulat & Optimizat Engn Res Ctr, Chinese Minist Educ, Natl & Local United Engn Res Ctr Chem Proc Simula, Xiangtan 411105, Peoples R China
[3] Hunan Prov Engn Res Ctr Sepiolite Resource Effici, Xiangtan 411105, Peoples R China
[4] Hunan Univ, Coll Chem & Chem Engn, Changsha 410082, Peoples R China
基金
中国国家自然科学基金;
关键词
WOOD GASIFICATION; CFD SIMULATION; COAL; COMBUSTION; HYDRODYNAMICS; PYROLYSIS; REACTOR; TAR; PARTICLES; GASIFIER;
D O I
10.1021/acs.energyfuels.9b02512
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
Gas distribution patterns exert a great impact on the gas-solid flow, heat and mass transfer, and reaction characteristics and thus affect significantly the thermal conversion efficiency inside the biomass gasifier. In this study, a twodimensional biomass gasification model for a bubbling spout fluidized-bed gasifier (BSFBG) is established based on the kinetic theory of granular mixture (KTGM), and the prediction accuracy of the model is verified through a comparison between simulation values and experimental values. Furthermore, with the total mass flow rate of the inlet gas set constant, the study has investigated how the ratio of the inlet cross-sectional area to reactor area (A(m)/A) and the auxiliary gas velocity (U-f) affect the gas-solid flow, heat transfer, and gasification performance in the BSFBG. As the results indicate, with A(m)/A increasing, the local particle flow structure becomes increasingly complex, particle volume fraction and temperature get more evenly distributed, and the volume fraction of outlet key gas species (CO, H-2, and CH4) and the lower heating value (LHV) is gradually rising. Besides, compared with the even gas distribution condition (A(m)/A = 100%), the formation of overall and local counterclockwise particle circulation is facilitated by either a relatively high U-f with a low A(m)/A (<= 50%) or a relatively low U-f with a high A(m)/A (>= 75%). The circulation structure strengthens the gas-solid mixing in the pyrolysis zone and gasification zone in the middle-upper part of the dense phase bed, which makes the volume fraction of outlet key gas species and LHV increase significantly. In the meanwhile, when A(m)/A = 75% and U-f = 1.0U mf , both the volume fraction and LHV reach the maximums, indicating that the overall gasification performance achieves the optimal state. In conclusion, this study is of reference value for the investigation and intensification of the gasification process, which helps to optimize BSFBG design and thus improve the biomass thermal conversion efficiency.
引用
收藏
页码:1750 / 1763
页数:14
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