Three-dimensional numerical modelling of interactions between a gas-liquid jet and a fluidized bed

被引:19
|
作者
Pougatch, K. [1 ]
Salcudean, M. [1 ]
McMillan, J. [2 ]
机构
[1] Univ British Columbia, Dept Mech Engn, Vancouver, BC V6T 1Z4, Canada
[2] Syncrude Canada Ltd, Edmonton Res Ctr, Edmonton, AB T6N 1H4, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
Multiphase flow; Mathematical modelling; Fluidization; Particle Gas-liquid jet; Liquid transport; TURBULENT-FLOW; KINETIC-THEORY; GRANULAR FLOW; SPRAY; SIMULATION; AIR; PARTICLES; CONTACT; DROPLET; VAPORIZATION;
D O I
10.1016/j.ces.2011.09.037
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This paper presents the development of a novel mathematical model that describes spray injection and spreading into a fluidized bed of solid particles. The model also includes the gas-liquid flow through the nozzle followed by the gas-assisted atomization. An Eulerian approach that is independent of the nature of the continuous phase is adopted for all phases, which are gas (or bubbles), liquid (or droplets), and solid particles that may be covered with a liquid layer. Variation in sizes of bubbles and droplets is represented by the particle number density approach that takes into account both break-up and coalescence. The atomization is considered as a catastrophic phase inversion triggered by a critical local volume fraction. New relationships were obtained for liquid spreading due to wet particle collisions and for heat conduction between a solid particle and a surrounding liquid layer. The model is applied to simulate liquid injection into the fluidized bed for conditions that were previously experimentally studied and published. The comparison reveals a reasonable agreement in prediction of the cumulative liquid distribution for two experimental cases. In addition, we evaluated a jet penetration distance with the model to compare it with the one measured in another set of experiments. This comparison also yields a good qualitative agreement. Finally, we evaluated the influence of the fluidization velocity on liquid distribution in the bed. (C) 2011 Elsevier Ltd. All rights reserved.
引用
收藏
页码:258 / 277
页数:20
相关论文
共 50 条
  • [41] Gas-liquid mass transfer in a three-phase fluidized bed containing low density particles
    Tang, Wen-Tzung
    Fan, Liang-Shih
    Industrial and Engineering Chemistry Research, 1990, 29 (01): : 128 - 133
  • [42] Numerical simulation and verification of a gas-solid jet fluidized bed
    Hong, RY
    Li, HZ
    Cheng, MY
    Zhang, JY
    POWDER TECHNOLOGY, 1996, 87 (01) : 73 - 81
  • [44] Numerical simulation and structure optimization on fluid flow behavior of three-dimensional integral multi-jet spout-fluidized bed
    Yang C.-L.
    Bai J.-H.
    Wu F.
    Ma X.-X.
    Yang J.
    Gao Xiao Hua Xue Gong Cheng Xue Bao/Journal of Chemical Engineering of Chinese Universities, 2019, 33 (06): : 1415 - 1423
  • [45] Numerical simulation of the gas-liquid interaction of a liquid jet in supersonic crossflow
    Li, Peibo
    Wang, Zhenguo
    Sun, Mingbo
    Wang, Hongbo
    ACTA ASTRONAUTICA, 2017, 134 : 333 - 344
  • [46] APPROXIMATING A THREE-DIMENSIONAL FLUIDIZED BED WITH TWO-DIMENSIONAL SIMULATIONS
    Deza, Mirka
    Battaglia, Francine
    Heindel, Theodore J.
    IMECE 2008: HEAT TRANSFER, FLUID FLOWS, AND THERMAL SYSTEMS, VOL 10, PTS A-C, 2009, : 387 - 394
  • [47] Three-dimensional interface structures and characteristics in a stratified gas-liquid pipe flow
    Hou, Lin-tong
    Yang, Meng
    Wang, Li-song
    Liu, Shuo
    Xu, Jing-yu
    CHEMICAL ENGINEERING SCIENCE, 2023, 277
  • [48] SOLID LIQUID MASS-TRANSFER IN A GAS-LIQUID SOLID FLUIDIZED-BED
    ARTERS, DC
    FAN, LS
    CHEMICAL ENGINEERING SCIENCE, 1986, 41 (01) : 107 - 115
  • [49] DYNAMIC THREE-DIMENSIONAL SIMULATION OF GAS-LIQUID FLOW IN A CYLINDRICAL BUBBLE COLUMN
    Lain, S.
    LATIN AMERICAN APPLIED RESEARCH, 2009, 39 (04) : 317 - 326
  • [50] Three-dimensional numerical simulation of a circulating fluidized bed reactor for multi-pollutant control
    Mao, DM
    Edwards, JR
    Kuznetsov, AV
    Srivastava, RK
    CHEMICAL ENGINEERING SCIENCE, 2004, 59 (20) : 4279 - 4289