Prediction of distribution behavior of particles with wide size distribution in baffled fluidized beds

被引:3
|
作者
Zhang, Libo [1 ,2 ,3 ]
Li, Hongzhong [1 ]
Hu, Chaoquan [1 ]
Zhu, Qingshan [1 ,2 ]
机构
[1] Chinese Acad Sci, Inst Proc Engn, State Key Lab Multiphase Complex Syst, POB 353, Beijing 100190, Peoples R China
[2] Univ Chinese Acad Sci, Beijing 100049, Peoples R China
[3] SINOPEC, Res Inst Petr Proc, Beijing 100083, Peoples R China
基金
中国国家自然科学基金;
关键词
Mean residence time; Wide size distribution particles; Relative elutriation degree; RESIDENCE TIME DISTRIBUTION; PRESSURE-DROP; SOLIDS; SEGREGATION; FLOW;
D O I
10.1016/j.powtec.2019.03.012
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Multi-baffle fluidized beds are recognized as efficient for controlling the difference in the mean residence time (MRT) of particles with a wide size distribution (WSD). Modeling the MRT of the particles of the each size is of great importance in the design of baffled fluidized beds for various applications. An analogy to the gas-liquid distillation model, based on the relative elutriation degree, was proposed herein for predicting the MRT of the particles of each size. The model was validated by comparison of the predicted and measured composition of the particles of each size in baffle-free and baffled fluidized beds. Moreover, the effects of the gas velocity, number of baffles, and baffle structure on the difference in the MRT for the WSD particles were investigated by applying the proposed model. (C) 2019 Published by Elsevier B.V.
引用
收藏
页码:24 / 32
页数:9
相关论文
共 50 条
  • [1] Control of mean residence time difference for particles with wide size distribution in fluidized beds
    Zhang, Libo
    Li, Jun
    Zhu, Qingshan
    Hu, Chaoquan
    Li, Hongzhong
    POWDER TECHNOLOGY, 2017, 312 : 270 - 276
  • [2] DISTRIBUTION OF SOLIDS BETWEEN STAGES IN BAFFLED FLUIDIZED-BEDS
    NGUYEN, XT
    BERGOUGN.MA
    BAKER, CGJ
    CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1973, 51 (05): : 573 - 577
  • [3] SIZE DISTRIBUTION OF PARTICLES ENTRAINED FROM FLUIDIZED-BEDS - ELECTROSTATIC EFFECTS
    BRIENS, CL
    BERGOUGNOU, MA
    INCULET, II
    BARON, T
    HAZLETT, JD
    POWDER TECHNOLOGY, 1992, 70 (01) : 57 - 62
  • [5] Effects of Particle Size Distribution of Low-Density Particles on Gas-Solid Behavior in Fluidized Beds
    Goshima, Takashi
    Nishida, Yuki
    Mizuta, Kei
    Nii, Susumu
    CHEMICAL ENGINEERING & TECHNOLOGY, 2022, 45 (12) : 2273 - 2283
  • [6] A METHOD TO DETECT AND CONTROL FULLY FLUIDIZED CONICAL BEDS WITH A WIDE SIZE DISTRIBUTION OF PARTICLES IN THE VICINITY OF THE MINIMUM FLUIDIZATION VELOCITY
    Mele, Jernej
    Golobic, Iztok
    Senegacnik, Andrej
    THERMAL SCIENCE, 2015, 19 (01): : 267 - 276
  • [7] Temperature Distribution in Fluidized Beds of Porous Particles with LiquidInjection
    Milacic, Evan
    Rantong, Dylan R.
    Kuipers, J. A. M.
    Baltussen, Maike W.
    CHEMIE INGENIEUR TECHNIK, 2023, 95 (1-2) : 129 - 135
  • [8] DISTRIBUTION OF SOLID PARTICLES IN LIQUID FLUIDIZED-BEDS
    PATWARDHAN, VS
    TIEN, C
    CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1984, 62 (01): : 46 - 54
  • [9] STUDIES ON BATCH FLUIDIZED BEDS - DISTRIBUTION OF PARTICLES IN FLUIDS
    RAJU, GJV
    RAJU, KS
    RAO, CV
    INDIAN JOURNAL OF TECHNOLOGY, 1966, 4 (12): : 359 - &
  • [10] SIZE DISTRIBUTION OF THE PARTICLES ENTRAINED FROM FLUIDIZED-BEDS - GAS HUMIDITY EFFECTS
    BARON, T
    BRIENS, CL
    HAZLETT, JD
    BERGOUGNOU, MA
    GALTIER, P
    CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1992, 70 (04): : 631 - 635