Study of the flow characteristics of the dense bed and its enhancing effect on coal particles separation by CFD-DEM applied in Teeter bed separator

被引:0
|
作者
Liu, Junli [1 ]
Zhu, Xueshuai [2 ]
Lv, Fakui [1 ]
Ye, Guichuan [3 ]
Yao, Geng [1 ]
Qi, Xin [1 ]
Cong, Xingshun [1 ]
机构
[1] Zaozhuang Univ, Coll Chem Chem Engn & Mat Sci, Zaozhuang 277160, Shandong, Peoples R China
[2] China Univ Min & Technol Beijing, Sch Chem & Environm Engn, Beijing, Peoples R China
[3] Taiyuan Univ Technol, Coll Min Engn, Taiyuan, Peoples R China
基金
中国国家自然科学基金;
关键词
Teeter bed separator; CFD-DEM simulation; flow characteristics of the dense bed; particle separation; LIQUID-FLUIDIZED-BEDS; CLASSIFICATION; HYDRODYNAMICS; SIMULATION; RECOVERY; VELOCITY; MODEL; DRAG;
D O I
10.1080/19392699.2024.2390507
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
Teeter bed separator (TBS) plays an important role in coal and mineral fines beneficiation. It is believed that a favorable dense concentrated bed is the key to ensuring the effective particle separation. This paper mainly presents the investigation of the flow characteristics of the dense bed and its enhancing effect on particle fines separation by CFD-DEM to reveal the complex separation behavior of TBS. First, the enhancing effect of the dense bed for separating real fine coal is experimentally studied. The specific simulation for particle motion is further verified by the literature experiment. The simulated dynamic behavior of the mismatch-prone particles reveals that the dense bed in the concentration range of 20-47% could promote particle separation by density. The fact is that a certain velocity difference is generated between mismatch-prone particles, and the smaller heavier particles move faster than the larger lighter particles. It is especially beneficial for separating fine coal material in TBS. The enhancing mechanism of the dense bed is further revealed by analyzing the mismatch-prone particle forces of collision and fluid drag force. Comprehensively, the appropriate bed concentration of 35-45% is suggested for the actual TBS operation.
引用
收藏
页数:21
相关论文
共 50 条
  • [41] CFD-DEM study of gas-solid flow regimes in a Wurster type fluidized bed with experimental validation by electrical capacitance tomography
    Che, H. Q.
    Liu, D.
    Tian, W. B.
    Gao, S.
    Sun, J. T.
    Xu, L. J.
    CHEMICAL ENGINEERING JOURNAL, 2020, 389
  • [42] CFD-DEM study of the effect of ring baffles on system performance of a full-loop circulating fluidized bed
    Wang, Shuai
    Luo, Kun
    Hu, Chenshu
    Fan, Jianren
    CHEMICAL ENGINEERING SCIENCE, 2019, 196 : 130 - 144
  • [43] Super-quadric CFD-DEM study of spout deflection behaviour of non-spherical particles in a spout fluidized bed
    Luo, Zhan
    Wang, Shuai
    Shen, Yansong
    POWDER TECHNOLOGY, 2024, 433
  • [44] CFD-DEM study of bubble properties in a cylindrical fluidized bed of Geldart Group D particles and comparison with prior MRI data
    Xi, Kenan
    Kovar, Thomas
    Fullmer, William D.
    Penn, Alexander
    Musser, Jordan
    Boyce, Christopher M.
    POWDER TECHNOLOGY, 2021, 389 : 75 - 84
  • [45] CFD-DEM study of segregation and mixing characteristics under a bi-disperse solid-liquid fluidised bed
    Xie, Zhouzun
    Wang, Shuai
    Shen, Yansong
    ADVANCED POWDER TECHNOLOGY, 2021, 32 (11) : 4078 - 4095
  • [46] Investigation of the Multi-particle Arch Formation on the Single Slot of a Sand Filter: CFD-DEM Study in Packed-Bed of Sand Particles
    Razavi, Fatemeh
    Mohammadtabar, Ali
    Lange, Carlos F.
    TRANSPORT IN POROUS MEDIA, 2024, 151 (12) : 2455 - 2475
  • [47] Pulsation effects on mixing behaviour of binary particles with different densities in supercritical water fluidized bed reactors: A CFD-DEM study
    Zhang, Hao
    Wang, Yang
    Li, Chao
    Guo, Pengyue
    An, Xizhong
    Jiang, Shengqiang
    POWDER TECHNOLOGY, 2024, 433
  • [48] Effect of Packing Structure Evolution on the Flow Characteristics in a Binary Composite Packed Bed Based on DEM-CFD Method
    Shen, Cunliang
    Li, Mingchun
    Ji, Jie
    Yang, Xin
    Li, Laishi
    Wu, Yusheng
    PROCESSES, 2023, 11 (03)
  • [49] CFD-DEM modeling the effect of column size and bed height on minimum fluidization velocity in micro fluidized beds with Geldart B particles
    Xu, Yupeng
    Li, Tingwen
    Musser, Jordan
    Liu, Xiaoxing
    Xu, Guangwen
    Rogers, William A.
    POWDER TECHNOLOGY, 2017, 318 : 321 - 328
  • [50] CFD-DEM coupled study on the characteristics of entrained air and particles dispersion during the particles flow impacting on a heap surface process
    Sun, Hongfa
    Zhou, Siliang
    Long, Jibo
    Zeng, Li
    POWDER TECHNOLOGY, 2025, 457