Numerical Study of the Orientation of Cylindrical Particles in a Circulating Fluidized Bed

被引:14
|
作者
Cai, Jie [1 ,2 ,3 ]
Peng, Zhengbiao [4 ]
Wu, Charley [3 ]
Zhao, Xiaobao [2 ]
Yuan, Zhulin [1 ]
Moghtaderi, Behdad [4 ]
Doroodchi, Elham [4 ]
机构
[1] Southeast Univ, Sch Energy & Environm, Nanjing 210096, Jiangsu, Peoples R China
[2] Nanjing Normal Univ, Sch Energy & Mech Engn, Nanjing 210042, Jiangsu, Peoples R China
[3] Univ Surrey, Dept Chem & Proc Engn, Guildford GU2 7XH, Surrey, England
[4] Univ Newcastle, Sch Engn, Discipline Chem Engn, Univ Dr, Callaghan, NSW 2308, Australia
基金
中国博士后科学基金; 中国国家自然科学基金;
关键词
ELLIPSOIDAL PARTICLES; SLENDER PARTICLES; FLOW; SIMULATION; MOTION; TURBULENCE; BREAKAGE; DYNAMICS; FIBER; PIPE;
D O I
10.1021/acs.iecr.6b04022
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Orientation is pivotal in circulating fluidized beds using cylinder-shaped particles. This study developed a three-dimensional multiway coupling model for predicting the orientation of cylindrical particles in circulating fluidized beds. The coupling algorithm between motorial cylindrical particles and the turbulence was established by incorporating the correlation between Lagrangian time scales and the k-epsilon model. Collisions among cylindrical particles were solved by combining rigid body impact dynamics with the hard sphere model. The results showed that the majority of cylindrical particles are prone to align with the streamline, which is in good agreement with the experimental observation. Cylindrical particles become more oriented along rising height position in the riser, increasing the slenderness ratio and decreasing the distance to the wall. Under turbulence conditions, the effect of Reynolds number on the orientation of cylindrical particles was found to be marginal.
引用
收藏
页码:12806 / 12817
页数:12
相关论文
共 50 条
  • [31] Orientation of cylindrical particles in a fluidized bed based on stereo X-ray particle tracking velocimetry (XPTV)
    Chen, Xi
    Zhong, Wenqi
    Heindel, Theodore J.
    CHEMICAL ENGINEERING SCIENCE, 2019, 203 : 104 - 112
  • [32] Residence time distribution of particles in circulating fluidized bed risers
    Hua, Leina
    Wang, Junwu
    CHEMICAL ENGINEERING SCIENCE, 2018, 186 : 168 - 190
  • [33] Saturation Carrying Capacity for Group A Particles in a Circulating Fluidized Bed
    Breault, Ronald W.
    Weber, Justin
    ENERGIES, 2021, 14 (10)
  • [34] HYDRODYNAMIC BEHAVIOR OF CIRCULATING FLUIDIZED-BED WITH POLYMERIC PARTICLES
    JIANG, PJ
    BI, HT
    LIANG, SC
    FAN, LS
    AICHE JOURNAL, 1994, 40 (02) : 193 - 206
  • [35] Synthesis of diamond particles with an acetylene fired circulating fluidized bed
    Horio, M
    Saito, A
    Unou, K
    Nakazono, H
    Shibuya, N
    Shima, S
    Kosaka, A
    CHEMICAL ENGINEERING SCIENCE, 1996, 51 (11) : 3033 - 3038
  • [36] Comparative study of flow structure in circulating fluidized bed risers with FCC and sand particles
    Qi, Xiao-Bo
    Huang, Wei-Xing
    Zhu, Jesse
    CHEMICAL ENGINEERING & TECHNOLOGY, 2008, 31 (04) : 542 - 553
  • [37] Study on residence time distribution of particles in double-dipleg circulating fluidized bed
    Yun, Xiao-Yin
    Lin, Wei-Gang
    Wu, Shao-Hua
    Qu, Feng-Zuo
    Zhongguo Dianji Gongcheng Xuebao/Proceedings of the Chinese Society of Electrical Engineering, 2003, 23 (05): : 156 - 160
  • [38] Numerical Study on Coal Gasification in the Downer Reactor of a Triple-Bed Combined Circulating Fluidized Bed
    Cheng, Yongpan
    Wang, Chi-Hwa
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2014, 53 (16) : 6624 - 6635
  • [39] Experimental study and characterization of a two-compartment cylindrical internally circulating fluidized bed gasifier
    Simanjuntak, J. P.
    Zainal, Z. A.
    BIOMASS & BIOENERGY, 2015, 77 : 147 - 154
  • [40] Numerical study of mixing and heat transfer of SRF particles in a bubbling fluidized bed
    Alagha, Mohamed Sobhi
    Szucs, Botond
    Szentannai, Pal
    JOURNAL OF THERMAL ANALYSIS AND CALORIMETRY, 2020, 142 (02) : 1087 - 1096