Monitoring of particle motions in gas-solid fluidized beds by electrostatic sensors

被引:18
|
作者
Yang, Yao [1 ]
Zhang, Qing [1 ]
Zi, Can [1 ]
Huang, Zhengliang [1 ]
Zhang, Wenbiao [2 ]
Liao, Zuwei [1 ]
Wang, Jingdai [1 ]
Yang, Yongrong [1 ]
Yan, Yong [2 ,3 ]
Han, Guodong [4 ]
机构
[1] Zhejiang Univ, Coll Chem & Biol Engn, State Key Lab Chem Engn, Hangzhou 310027, Zhejiang, Peoples R China
[2] North China Elect Power Univ, Sch Control & Comp Engn, Beijing 102206, Peoples R China
[3] Univ Kent, Sch Engn & Digital Arts, Canterbury CT2 7NT, Kent, England
[4] Tianjin Branch Co SINOPEC, Tianjin 300271, Peoples R China
基金
英国工程与自然科学研究理事会; 中国国家自然科学基金;
关键词
Induced electrostatic signal; Gas-solid fluidized bed; Cross-correlation method; Correlation velocity; VELOCITY-MEASUREMENT; PULVERIZED COAL; 2-PHASE FLOW; BUBBLE; HYDRODYNAMICS; REACTOR; TRACKING; BEHAVIOR;
D O I
10.1016/j.powtec.2016.11.034
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Gas-solid fluidized beds are widely applied in numerous industrial processes. Particle motions significantly affect the performance of fluidized bed reactors and the characterization of particle movements is therefore important for fluidization quality monitoring and scale-up of reactors. Electrostatic charge signals in the fluidized bed contain much dynamic information on particle motions, which are poorly understood and explored. In this work, correlation velocities of Geldart B and D particles were measured, analyzed and compared by induced electrostatic sensors combined with cross-correlation method in the fluidized bed. The results indicated that the average correlation velocity of particle clouds increased and the normalized probability density distributions of correlation velocities broadened when the superficial gas velocity increased in the dense-phase region. Both upward and downward correlation velocities could be acquired in the dynamic bed level region. Under the same excess gas velocity, the average correlation velocity of Geldart D particles was significantly smaller than that of Geldart B particles, which was caused by the smaller bubble sizes caused by the dominant bubble split over coalescence and less volume of gas forming bubbles for Geldart D particles. The experimental results verified the reliability and repeatability of particle correlation velocity measurement by induced electrostatic sensors in the gas-solid fluidized bed, which provides definite potential in monitoring of particle motions. (C) 2016 Elsevier B.V. All rights reserved.
引用
收藏
页码:461 / 471
页数:11
相关论文
共 50 条
  • [41] Electrostatic potentials in gas-solid fluidized beds influenced by the injection of charge inducing agents
    Wang, Jingdai
    Xu, Yi
    Li, Wei
    Yang, Yongrong
    Wang, Fang
    [J]. JOURNAL OF ELECTROSTATICS, 2009, 67 (05) : 815 - 826
  • [42] A Neural Network Method for Characterizing Particle Clusters in Gas-Solid Fluidized Beds
    Jin, Nani
    Hu, Shanwei
    Liu, Xinhua
    Guo, Li
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2024, 63 (38) : 16598 - 16608
  • [43] Critical comparison of hydrodynamic models for gas-solid fluidized beds - Part I: bubbling gas-solid fluidized beds operated with a jet
    Patil, DJ
    Annaland, MV
    Kuipers, JAM
    [J]. CHEMICAL ENGINEERING SCIENCE, 2005, 60 (01) : 57 - 72
  • [44] Tomographic diagnosis of gas maldistribution in gas-solid fluidized beds
    Patel, Ashutosh K.
    Waje, Sunil S.
    Thorat, Bhaskar N.
    Mujumdar, Arun S.
    [J]. POWDER TECHNOLOGY, 2008, 185 (03) : 239 - 250
  • [45] Numerical Investigation of Gas Mixing in Gas-Solid Fluidized Beds
    Li, Tingwen
    Zhang, Yongmin
    Grace, John R.
    Bi, Xiaotao
    [J]. AICHE JOURNAL, 2010, 56 (09) : 2280 - 2296
  • [46] Characterization of dynamic gas-solid distribution in fluidized beds
    Cui, Heping
    Mostoufi, Navid
    Chaouki, Jamal
    [J]. 1600, Elsevier S.A. (79):
  • [47] BUBBLE MEASUREMENT IN GAS-SOLID FLUIDIZED-BEDS
    SITNAI, O
    DENT, DC
    WHITEHEAD, AB
    [J]. CHEMICAL ENGINEERING SCIENCE, 1981, 36 (09) : 1583 - 1583
  • [48] Flow structure of the solids in gas-solid fluidized beds
    Mostoufi, N
    Chaouki, J
    [J]. CHEMICAL ENGINEERING SCIENCE, 2004, 59 (20) : 4217 - 4227
  • [49] Characterization of dynamic gas-solid distribution in fluidized beds
    Cui, HP
    Mostoufi, N
    Chaouki, J
    [J]. CHEMICAL ENGINEERING JOURNAL, 2000, 79 (02) : 133 - 143
  • [50] DISTRIBUTOR STABILITY IN GAS-SOLID FLUIDIZED-BEDS
    WHITEHEAD, AB
    DENT, DC
    GARTSIDE, G
    [J]. CHEMICAL ENGINEERING SCIENCE, 1982, 37 (01) : 124 - 125