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
  • [21] Hydrodynamics characteristics and gas-liquid mass transfer in a three phase fluidized bed reactor
    Silva, Edson L.
    Revista Brasileira de Ciencias Mecanicas/Journal of the Brazilian Society of Mechanical Sciences, 2001, 23 (04): : 503 - 512
  • [22] Numerical study of statistically developed gas-liquid intermittent flows by the lens of three-dimensional simulations
    Rocha, Pedro Roberto B.
    Nieckele, Angela O.
    JOURNAL OF PETROLEUM SCIENCE AND ENGINEERING, 2022, 217
  • [23] Transition to three-dimensional waves in cocurrent gas-liquid flows
    Kuru, WC
    Sangalli, M
    McCready, MJ
    ADVANCES IN MULTI-FLUID FLOWS, 1996, : 52 - 69
  • [24] A three-dimensional CFD model for gas-liquid bubble columns
    Delnoij, E
    Kuipers, JAM
    van Swaaij, WPM
    CHEMICAL ENGINEERING SCIENCE, 1999, 54 (13-14) : 2217 - 2226
  • [25] High-resolution three-dimensional numerical simulation of a circulating fluidized bed
    Zhang, DZ
    VanderHeyden, WB
    POWDER TECHNOLOGY, 2001, 116 (2-3) : 133 - 141
  • [26] Estimation of bed expansions in a freely-bubbling three-dimensional gas-fluidized bed
    Hepbasli, A
    INTERNATIONAL JOURNAL OF ENERGY RESEARCH, 1998, 22 (15) : 1365 - 1380
  • [27] Three-dimensional measurement of gas dissolution process in gas-liquid microchannel flow
    Ichiyanagi, Mitsuhisa
    Tsutsui, Issei
    Kakinuma, Yasuhiro
    Sato, Yohei
    Hishida, Koichi
    INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2012, 55 (11-12) : 2872 - 2878
  • [28] Modeling the mixing of a gas-liquid spray jet injected in a gas-solid fluidized bed: The effect of the draft tube
    Ariyapadi, S
    McMillan, J
    Zhou, D
    Berruti, F
    Briens, C
    Chan, E
    CHEMICAL ENGINEERING SCIENCE, 2005, 60 (21) : 5738 - 5750
  • [29] A Three-Dimensional Model Frame for Modelling Combustion and Gasification in Circulating Fluidized Bed Furnaces
    Myohanen, Kari
    Hyppanen, Timo
    INTERNATIONAL JOURNAL OF CHEMICAL REACTOR ENGINEERING, 2011, 9
  • [30] VISUALIZATION OF GAS VOIDS BEHAVIOR ABOVE THE DISTRIBUTOR IN A THREE-DIMENSIONAL GAS FLUIDIZED BED.
    Abdel, Ibrahim
    Khattab, Hamid
    Ishida, Masaru
    Journal of Chemical Engineering of Japan, 1986, 19 (05): : 367 - 374