Investigation of non-uniform characteristics in a 300 MWth circulating fluidized bed with different coal feeding modes

被引:8
作者
Kong, Dali [1 ]
Wang, Shuai [1 ]
Yu, Jiahui [1 ]
Li, Debo [3 ]
Luo, Kun [1 ,2 ]
Fan, Jianren [1 ,2 ]
机构
[1] Zhejiang Univ, State Key Lab Clean Energy Utilizat, Hangzhou 310027, Peoples R China
[2] Zhejiang Univ, Shanghai Inst Adv Study, Shanghai 200120, Peoples R China
[3] Guangdong Diankeyuan Energy Technol Co Ltd, Guangzhou 510080, Guangdong, Peoples R China
基金
中国国家自然科学基金;
关键词
Circulating fluidized bed; Coal combustion; Coal feeding mode; Numerical simulation; Gas pollutants; GAS-SOLID FLOW; RESIDENCE TIME DISTRIBUTION; CFD-DEM; OPERATING PARAMETERS; REACTING FLOW; COMBUSTION; SIMULATION; GASIFICATION; PARTICLES; DYNAMICS;
D O I
10.1016/j.apt.2023.104036
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Circulating fluidized bed (CFB) has been practised in many engineering fields, but the non-uniform char-acteristics deteriorate combustion performance and system control. In this study, the improvement of external-loop and in-furnace non-uniformity of a 300 MWth industrial-scale CFB with multiple cyclones by a dual-side coal feeding mode was numerically quantified. The results show that the pressure is non-uniformly distributed among three external loops, where the pressure in the middle loop seal is lower than that in the corner loop seals by 4.5 %. The pressure gradient positively correlates with the solid holdup. As compared with the traditional single-side coal feeding mode, the dual-side coal feeding mode: (i) promotes the final mixing degree by 11.15 %; (ii) extends the residence time of coal particles by 10.3 %; (iii) reduces the magnitude and fluctuation of the horizontal solid flux by 28.5 % and 77%, respectively; (iv) narrows the temperature range and reduces the mean temperature by 7 degrees C; (v) enhances the com-bustion of coal particles by consuming more O2; (vi) decreases the concentrations of SO2 and NO by 3 % and 5 %, respectively. The present study shows the superiority of the dual-side coal feeding mode to the traditional single-side coal feeding mode in the optimization of CFBs in practical industrial processes.(c) 2023 The Society of Powder Technology Japan. Published by Elsevier B.V. and The Society of Powder Technology Japan. All rights reserved.
引用
收藏
页数:18
相关论文
共 61 条
[41]  
0099:GCEWTPandgt
[42]  
2.3.CO
[43]  
2]
[44]   Eulerian-Lagrangian method for three-dimensional thermal reacting flow with application to coal gasifiers [J].
Snider, Dale M. ;
Clark, Samuel M. ;
O'Rourke, Peter J. .
CHEMICAL ENGINEERING SCIENCE, 2011, 66 (06) :1285-1295
[45]   Distribution and particle-scale thermochemical property of biomass in the gasifier of a dual fluidized bed [J].
Wan, Zhanghao ;
Yang, Shiliang ;
Sun, Yuhao ;
Wei, Yonggang ;
Hu, Jianhang ;
Wang, Hua .
ENERGY CONVERSION AND MANAGEMENT, 2020, 209
[46]  
Wang S., 2022, RESOUR CONSERV RECY, V183
[47]   Particle-scale study of heat and mass transfer in a bubbling fluidised bed [J].
Wang, Shuai ;
Shen, Yansong .
CHEMICAL ENGINEERING SCIENCE, 2021, 240
[48]   CFD-DEM coupled with thermochemical sub-models for biomass gasification: Validation and sensitivity analysis [J].
Wang, Shuai ;
Luo, Kun ;
Fan, Jianren .
CHEMICAL ENGINEERING SCIENCE, 2020, 217
[49]   Effect of superficial gas velocity on solid behaviors in a full-loop CFB [J].
Wang, Shuai ;
Luo, Kun ;
Hu, Chenshu ;
Sun, Liyan ;
Fan, Jianren .
POWDER TECHNOLOGY, 2018, 333 :91-105
[50]   Particle-Scale Investigation of Heat Transfer and Erosion Characteristics in a Three-Dimensional Circulating Fluidized Bed [J].
Wang, Shuai ;
Luo, Kun ;
Hu, Chenshu ;
Fan, Jianren .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2018, 57 (19) :6774-6789