Scale-up effect of residence time distribution of polydisperse particles in continuously operated multiple-chamber fluidized beds

被引:28
|
作者
Lan, Bin [1 ,2 ]
Xu, Ji [1 ,2 ]
Zhao, Peng [1 ,2 ]
Zou, Zheng [1 ,2 ]
Wang, Junwu [1 ,2 ,3 ]
Zhu, Qingshan [1 ,2 ,3 ]
机构
[1] Chinese Acad Sci, Inst Proc Engn, State Key Lab Multiphase Complex Syst, POB 353, Beijing 100190, PR, Peoples R China
[2] Univ Chinese Acad Sci, Sch Chem Engn, Beijing 100049, PR, Peoples R China
[3] Chinese Acad Sci, Innovat Acad Green Mfg, Beijing 100190, Peoples R China
基金
中国国家自然科学基金;
关键词
Gas-solid flow; Polydisperse particles; Residence time distribution; Discrete simulation; Scale-up; EMMS DRAG MODEL; SIZE DISTRIBUTION; SIMULATION; CFD; GAS; FLOW; HYDRODYNAMICS;
D O I
10.1016/j.ces.2021.116809
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A GPU-based, massively parallel coarse-grained CFD-DEM method was adapted to study the scale-up effect of residence time distribution of polydisperse particles in continuously operated multiple chamber fluidized beds, where the bed is scaled up either by keeping a constant length of each chamber and increasing the number of chambers (Scaling method I) or by maintaining the number unchanged but increasing the length of each chamber (Scaling method II). It was shown that (i) the pressure drop and the residence time distribution of particles in a laboratory scale fluidized bed can be predicted reasonably well; (ii) when the solids feed rate is a constant (Operation I), the mean residence time of each type of particles scaled linearly as the bed length in both of Scaling methods I and II; (iii) when the solids feed rate is linearly increased with increasing bed length (Operation II), Scaling method I results in a continuously reduced ratio of mean residence time between coarse (medium) particles and fine particles, and the ratios level off with increasing bed length in Scaling method II; (iv) the mean residence time of particles can be inferred from the mean solids holdup obtained from CFD simulations and the mass fraction of particles at the inlet, thus offering a much faster way to estimate the mean residence time of particles; and (v) the equivalent number of perfect mixing tanks that corresponds to the mixing characteristics of real fluidized beds is linearly scaled as the bed length in Operation II, irrespective of Scaling methods. (c) 2021 Elsevier Ltd. All rights reserved.
引用
收藏
页数:11
相关论文
共 29 条
  • [1] Long-time coarse-grained CFD-DEM simulation of residence time distribution of polydisperse particles in a continuously operated multiple-chamber fluidized bed
    Lan, Bin
    Xu, Ji
    Zhao, Peng
    Zou, Zheng
    Zhu, Qingshan
    Wang, Junwu
    CHEMICAL ENGINEERING SCIENCE, 2020, 219
  • [2] Simulation of scale-up effect of particle residence time distribution characteristics in continuously operated dense-phase fluidized beds
    Lan B.
    Xu J.
    Liu Z.
    Wang J.
    Huagong Xuebao/CIESC Journal, 2021, 72 (01): : 521 - 533
  • [3] Regulation characteristics and law of residence time distribution of polydisperse particles in numbered-up multiple-chamber fluidized bed reactors
    Lu, Shuai
    Lan, Bin
    Li, Dandan
    Fan, Chuanlin
    Xu, Ji
    Zhao, Bidan
    Zou, Zheng
    Li, Hongzhong
    Wang, Junwu
    Zhu, Qingshan
    Powder Technology, 439
  • [4] Regulation characteristics and law of residence time distribution of polydisperse particles in numbered-up multiple-chamber fluidized bed reactors
    Lu, Shuai
    Lan, Bin
    Li, Dandan
    Fan, Chuanlin
    Xu, Ji
    Zhao, Bidan
    Zou, Zheng
    Li, Hongzhong
    Wang, Junwu
    Zhu, Qingshan
    POWDER TECHNOLOGY, 2024, 439
  • [5] Expanding the Controllable Range of the Mean Residence Time Ratio of Polydisperse Particles in Multiple-Chamber Fluidized Beds: A Coarse-Grained CFD-DEM Study
    Lu, Shuai
    Li, Dandan
    Lan, Bin
    Fan, Chuanlin
    Xu, Fan
    Xu, Ji
    Zhao, Bidan
    Zou, Zheng
    Li, Hongzhong
    Wang, Junwu
    Zhu, Qingshan
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2024, 63 (39) : 16753 - 16761
  • [6] Scale-up of bubbling fluidized beds with continuous particle flow based on particle-residence-time distribution
    Juwei Zhang
    Guangwen Xu
    Particuology, 2015, 19 (02) : 155 - 163
  • [7] Scale-up of bubbling fluidized beds with continuous particle flow based on particle-residence-time distribution
    Zhang, Juwei
    Xu, Guangwen
    PARTICUOLOGY, 2015, 19 : 155 - 163
  • [8] 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
  • [9] ON THE MEASUREMENT OF THE RESIDENCE TIME DISTRIBUTION OF PARTICLES IN FLUIDIZED-BEDS WITH GAS SOLID REACTION
    KLOSE, E
    HESCHEL, W
    CHEMISCHE TECHNIK, 1985, 37 (04): : 149 - 152
  • [10] Effect of Scale-up on Heat Transfer Characteristics of Cyclone Separators of Circulating Fluidized Beds
    Patil, R. S.
    Mahanta, P.
    Pandey, M.
    INTERNATIONAL ENERGY JOURNAL, 2010, 11 (03): : 123 - 130