Segregation of binary particles in gas-solid fluidized bed

被引:1
|
作者
Yu, Yaxiong [1 ]
Lu, Feng [1 ]
He, Xuan [2 ]
Wei, Fei [1 ,3 ]
Zhang, Chenxi [1 ,3 ,4 ]
机构
[1] Tsinghua Univ, Dept Chem Engn, Beijing Key Lab Green Chem React Engn & Technol, Beijing 100084, Peoples R China
[2] Xi An Jiao Tong Univ, Sch Chem Engn & Technol, Xian 710049, Peoples R China
[3] Ordos Lab, Ordos 017010, Peoples R China
[4] Tsinghua Univ, Inst Carbon Neutral, Beijing 100084, Peoples R China
基金
中国国家自然科学基金;
关键词
fluidized bed; segregation; binary; bubbles; entrainment; MIXTURES; MODEL; VELOCITY; FLOW;
D O I
10.1007/s11705-024-2426-0
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Particle segregation and mixing behavior play a crucial role in industrial processes. This study investigates the saturated jetsam fraction, which indicates the maximum capacity of flotsam to entrain jetsam, in an initially separated binary fluidized bed with particle size differences. According to the value of saturated jetsam fraction, three distinct regimes-segregation, mixing, and an intermediate regime-are identified. Moreover, intriguing relationships between the saturated jetsam fraction and superficial gas velocity are observed, exhibiting monotonic trends in both the segregation and mixing regimes, while a unique volcano-shaped curve in the intermediate regime. Additionally, a comprehensive entrainment model based on two-fluid model elucidates the observed phenomena, emphasizing the significance of mixing behavior in fluidized layer on the saturated jetsam fraction. This work offers potential insights for evaluating segregation in industrial applications.
引用
收藏
页数:9
相关论文
共 50 条
  • [41] CFD simulation of gas-solid bubbling fluidized bed containing FCC particles
    Hosseini, Seyyed Hossein
    Rahimi, Rahbar
    Zivdar, Mortaza
    Samimi, Abdolreza
    KOREAN JOURNAL OF CHEMICAL ENGINEERING, 2009, 26 (05) : 1405 - 1413
  • [42] Flow pattern and its transition of different particles in gas-solid fluidized bed
    Ren C.-J.
    Wang J.-D.
    Yang Y.-R.
    Zhejiang Daxue Xuebao(Gongxue Ban)/Journal of Zhejiang University (Engineering Science), 2010, 44 (02): : 305 - 309
  • [43] Numerical simulation of flow behavior of particles in a gas-solid stirred fluidized bed
    Wang, Shuyan
    Chen, Yujia
    Jia, Yubin
    Tian, Ruichao
    Sun, Qiji
    Fan, Jiawei
    Ma, Yimei
    POWDER TECHNOLOGY, 2018, 338 : 119 - 128
  • [44] Mixing characteristics of large cylindrical particles (RDF) in a gas-solid fluidized bed
    Yu, YH
    Oh, JH
    Lee, JY
    Choi, HW
    JOURNAL OF INDUSTRIAL AND ENGINEERING CHEMISTRY, 2003, 9 (06) : 798 - 803
  • [45] Electrostatic charging behaviour of dielectric particles in a pressurized gas-solid fluidized bed
    Liu, Zhengliang
    Bi, Xiaotao T.
    Grace, John R.
    JOURNAL OF ELECTROSTATICS, 2010, 68 (04) : 321 - 327
  • [46] Fluidization characteristics of wide-size-distribution particles in a gas-solid fluidized bed reactor
    Li, Chaojie
    Wang, Weiwen
    Guo, Xiuling
    Duan, Jihai
    INTERNATIONAL JOURNAL OF CHEMICAL REACTOR ENGINEERING, 2020, 18 (12)
  • [47] Mixing/separation characteristics of great different particles in gas-solid fluidized bed
    Jin W.
    Yan J.
    Chenglin E.
    Fan Y.
    Lu C.
    Huagong Xuebao/CIESC Journal, 2022, 73 (11): : 4872 - 4883
  • [48] Segregation and mixing of binary mixtures of spherical particles in a bubbling fluidized bed
    Ren, Shan
    Zheng, Zhong
    Chen, Hongsheng
    INTERNATIONAL JOURNAL OF CHEMICAL REACTOR ENGINEERING, 2024, 22 (06) : 609 - 620
  • [49] A modified model for predicting bed density of air dense medium gas-solid fluidized bed (ADMGFB) using binary dense media
    Liu, Chengguo
    Lu, Shuai
    He, Jingfeng
    Zhao, Yuemin
    Zhu, Lingtao
    POWDER TECHNOLOGY, 2019, 355 : 363 - 371
  • [50] CFD simulation of gas-solid fluidized bed hydrodynamics; prediction accuracy study
    Mofakham, Atefeh Sadri
    Rasteh, Mojtaba
    INTERNATIONAL JOURNAL OF CHEMICAL REACTOR ENGINEERING, 2023, 21 (03) : 391 - 407