Bubble size distribution and void fraction in the wake region below a ventilated gas cavity in downward pipe flow

被引:11
|
作者
Evans, GM
Machniewski, PM
Bin, AK
机构
[1] Univ Newcastle, Dept Chem Engn, Callaghan, NSW 2308, Australia
[2] Warsaw Univ Technol, Dept Chem & Proc Engn, Warsaw, Poland
来源
CHEMICAL ENGINEERING RESEARCH & DESIGN | 2004年 / 82卷 / A9期
关键词
bubble breakup and coalescence; population balance equation; ventilated cavities; downflowing liquid;
D O I
10.1205/cerd.82.9.1095.44168
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The aim of this study was to develop a population balance model to predict the resultant bubble size distribution and gas void fraction in the wake region below a ventilated cavity in down-flowing liquid inside a pipe. The model includes (1) the gas entrainment process from the ventilated cavity; (2) fluid flow and specific energy dissipation rate in the wake region, comprising both wall-jet and recirculation-vortex zones; (3) bubble breakup and coalescence events, determined by a critical Weber number criterion and bubble interaction and film drainage times, respectively; and finally (4) gas void fraction in the wake and recirculation of gas back into the base of the ventilated cavity. The model predictions are compared with experimental measurements for an air-water system. The model successfully predicts the length of the wake region and the gas void fraction within it, and the average and resultant bubble size distributions immediately downstream of the wake. The average bubble diameter was of the order 2-3 mm for each of the cases studied. In applying the model, attention was focused on the specific energy dissipation rate distribution between the wall-jet and recirculating-vortex zones within the wake. As part of the analysis Fluent computational fluid dynamics simulation was carried out and the results from this work are also presented in the paper.
引用
收藏
页码:1095 / 1104
页数:10
相关论文
共 50 条
  • [1] Liquid recirculation and bubble breakup beneath ventilated gas cavities in downward pipe flow
    Thorpe, RB
    Evans, GM
    Zhang, K
    Machniewski, PM
    CHEMICAL ENGINEERING SCIENCE, 2001, 56 (21-22) : 6399 - 6409
  • [2] STRUCTURE OF AIR WATER BUBBLY FLOW IN A VERTICAL PIPE .2. VOID FRACTION, BUBBLE VELOCITY AND BUBBLE-SIZE DISTRIBUTION
    LIU, TJ
    BANKOFF, SG
    INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 1993, 36 (04) : 1061 - 1072
  • [3] Distribution of void fraction for gas-liquid slug flow in aninclined pipe
    XIA Guo-Dong1
    2 State Key Laboratory of Multiphase Flow in Power Engineering
    NuclearScienceandTechniques, 2001, (02) : 143 - 148
  • [4] Gas liquid flow of sub-millimeter bubbles at low void fractions: Experimental study of bubble size distribution and void fraction
    Evgenidis, Sotiris P.
    Karapantsios, Thodoris D.
    INTERNATIONAL JOURNAL OF HEAT AND FLUID FLOW, 2018, 71 : 353 - 365
  • [5] On the prediction of bubble size distribution and void fraction in vertical gas-liquid flows
    Yeoh, G.H.
    Cheung, Sherman C.P.
    Tu, J.Y.
    Journal of Computational Multiphase Flows, 2012, 4 (01): : 1 - 22
  • [6] VOID FRACTION, BUBBLE VELOCITY AND BUBBLE-SIZE IN 2-PHASE FLOW
    VANDERWELLE, R
    INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1985, 11 (03) : 317 - 345
  • [7] Vertically downward gas-liquid flow: Void fraction and pressure drop
    Bouyahiaoui, Hiba
    Saidj, Faiza
    Arabi, Abderraouf
    Al-Sarkhi, Abdelsalam
    Azzi, Abdelwahid
    INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 2024, 172
  • [8] The effect of bubble size on the radial distribution of void fraction in two-phase flow in a circular tube
    Horie, H
    Shirakawa, N
    Tobita, Y
    Morita, K
    Kondo, S
    JOURNAL OF NUCLEAR SCIENCE AND TECHNOLOGY, 2001, 38 (09) : 711 - 720
  • [9] VERTICALLY DOWNWARD 2-PHASE FLOW .1. VOID DISTRIBUTION AND AVERAGE VOID FRACTION
    USUI, K
    SATO, K
    JOURNAL OF NUCLEAR SCIENCE AND TECHNOLOGY, 1989, 26 (07) : 670 - 680
  • [10] Prediction of radial gas profiles in vertical pipe flow an the basis of bubble size distribution
    Lucas, D
    Krepper, E
    Prasser, HM
    INTERNATIONAL JOURNAL OF THERMAL SCIENCES, 2001, 40 (03) : 217 - 225