Numerical investigation of the cluster property and flux distribution in three-dimensional full-loop circulating fluidized bed with multiple parallel cyclones

被引:13
|
作者
Yang, Shiliang [1 ,2 ]
Wang, Shuai [1 ]
Luo, Kun [1 ]
Fan, Jianren [1 ]
Chew, Jia Wei [2 ,3 ]
机构
[1] Zhejiang Univ, Energy Dept, State Key Lab Clean Energy Utilizat, Hangzhou 310027, Zhejiang, Peoples R China
[2] Nanyang Technol Univ, Sch Chem & Biomed Engn, Singapore 637459, Singapore
[3] Nanyang Technol Univ, Nanyang Environm & Water Res Inst, Singapore Membrane Technol Ctr, Singapore 637141, Singapore
基金
新加坡国家研究基金会; 中国国家自然科学基金;
关键词
Circulating fluidized bed; Cluster; Slip velocity; Granular temperature; Discrete element method; Multiple cyclones; GAS-SOLID FLOW; GROUP-B PARTICLES; STRUCTURE-DEPENDENT DRAG; HIGH-DENSITY CFB; MULTIRESOLUTION ANALYSIS; PARTICULATE SYSTEMS; SIMULATION; RISER; DEM; BEHAVIOR;
D O I
10.1016/j.powtec.2018.10.009
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Circulating fluidized beds have been widely utilized in many industrial applications due to their excellent heat and mass transfer performance. By means of computational fluid dynamics coupled with discrete element method, numerical simulation of the three-dimensionalfull-loop circulating fluidized bed with six parallel cyclones is conducted, with a focus on the cluster behavior, flux and granular temperature. The results agree with past studies that the particle clusters dynamically evolve with time and space, and the upward-rising and downward-falling clusters tend to be in respectively the central core and near-wall regions. Notably, the frequency distribution of the cluster volume is shown to be approximately normal; and the aspect ratios of the clusters are consistently larger than one, and tend to increase before decreasing with riser height. Furthermore, the slip velocity is the most significant in the cross-sectional center of the riser and upper part of the cyclone. Finally, the granular temperatures are greatest at the cross-sectional center of the riser inlet, at the top of four of the six cyclones, and also at the middle one-third portion of the standpipe height. Moreover, the granular temperature of the solid phase increases with solid concentration in the dilute regions, but decreases with solid concentration in the dense regions. The results obtained provide insights regarding the important aspects in the CFB with multiple cyclones. (C) 2018 Elsevier B.V. All rights reserved.
引用
收藏
页码:253 / 266
页数:14
相关论文
共 45 条
  • [1] CFD investigation of maldistribution in a full-loop circulating fluidized bed with double parallel cyclones
    Li, Shuyue
    Shen, Yansong
    [J]. POWDER TECHNOLOGY, 2021, 381 : 665 - 684
  • [2] Numerical investigation of the back-mixing and non-uniform characteristics in the three-dimensional full-loop circulating fluidized bed combustor with six parallel cyclones
    Yang, Shiliang
    Wang, Shuai
    Luo, Kun
    Fan, Jianren
    Chew, Jia Wei
    [J]. APPLIED THERMAL ENGINEERING, 2019, 153 : 524 - 535
  • [3] Numerical investigation of the back-mixing and non-uniform characteristics in the three-dimensional full-loop circulating fluidized bed combustor with six parallel cyclones
    Yang, Shiliang
    Wang, Shuai
    Luo, Kun
    Fan, Jianren
    Chew, Jia Wei
    [J]. Applied Thermal Engineering, 2019, 153 : 524 - 535
  • [4] Three-dimensional full-loop numerical simulation of coal and sludge co-combustion in a circulating fluidized bed
    Wu, Wanqiang
    Duan, Lunbo
    Duan, Yuanqiang
    Li, Lin
    Liu, Daoyin
    Pallares, David
    [J]. FUEL, 2023, 337
  • [5] Application of three-dimensional full-loop CFD simulation in circulating fluidized bed combustion reactors - A review
    Tu, Qiuya
    Wang, Haigang
    Ocone, Raffaella
    [J]. POWDER TECHNOLOGY, 2022, 399
  • [6] Shape Effect of the Riser Cross Section on the Full-Loop Hydrodynamics of a Three-Dimensional Circulating Fluidized Bed
    Yang, Shiliang
    Wang, Shuai
    [J]. ACS OMEGA, 2020, 5 (11): : 5784 - 5795
  • [7] Three-dimensional full-loop simulation of biomass gasification in dual fluidized bed
    Kong, Dali
    Luo, Kun
    Lin, Junjie
    Wang, Shuai
    Hu, Chenshu
    Li, Debo
    Fan, Jianren
    [J]. Huagong Xuebao/CIESC Journal, 2019, 70 (08): : 3167 - 3176
  • [8] Three-dimensional full-loop simulation of a dual fluidized-bed biomass gasifier
    Liu, Hui
    Cattolica, Robert J.
    Seiser, Reinhard
    Liao, Chang-hsien
    [J]. APPLIED ENERGY, 2015, 160 : 489 - 501
  • [9] Three-Dimensional Full-Loop Hydrodynamic Simulation of a Circulating Fluidized-Bed Gasifier: A Quantitative Assessment of Drag Models
    Sharma, Vikrant
    Agarwal, Vijay Kumar
    [J]. ARABIAN JOURNAL FOR SCIENCE AND ENGINEERING, 2019, 44 (12) : 9837 - 9850
  • [10] Three-Dimensional Full-Loop Hydrodynamic Simulation of a Circulating Fluidized-Bed Gasifier: A Quantitative Assessment of Drag Models
    Vikrant Sharma
    Vijay Kumar Agarwal
    [J]. Arabian Journal for Science and Engineering, 2019, 44 : 9837 - 9850