Mixing mechanisms in a low-sheared inhomogeneous bubble column

被引:9
作者
Almeras, Elise [1 ,2 ]
Plais, Cecile [2 ]
Roig, Veronique [1 ]
Risso, Frederic [1 ]
Augier, Frederic [2 ]
机构
[1] Univ Toulouse, CNRS, IMFT, INPT,UPS, Toulouse, France
[2] IFP Energies Nouvelles, BP 3, F-69360 Solaize, France
关键词
Bubble column; Mixing; Bubble-induced agitation; Buoyancy-driven flow;
D O I
10.1016/j.ces.2018.04.026
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This paper reports an experimental study of the mixing of a passive scalar in a bubble column at high Reynolds number and average gas volume fractions ranging from 2.0% to 7.5%. Starting from a homogeneous bubble column, the bubbly flow is progressively destabilized by imposing a gradient of gas volume fraction at the bottom of the tank. In that way, a single recirculation is produced, which allows to investigate the impact of a large-scale buoyancy-driven flow on the mixing of a passive scalar. It is shown that, as long as the shear-induced turbulence generated by the recirculation is negligible, mixing results from two main mixing mechanisms: the transport by the mean liquid velocity and the mixing induced by the bubbles. While the transport by the liquid recirculation can be accounted for by an advection term, the mixing induced by the bubbles is a diffusive process, the effective diffusivity of which has been measured in a homogeneous bubble column by Almeras et al. (2015). However, once the shear-induced turbulence produced by the shear develops, its role upon the mixing has to be taken into account too. (C) 2018 Elsevier Ltd. All rights reserved.
引用
收藏
页码:52 / 61
页数:10
相关论文
共 39 条
  • [31] LIQUID MIXING AND GAS-LIQUID MASS-TRANSFER OF BUBBLE-COLUMN WITH PACKED DOUBLE PERFORATED DRAFT TUBE
    BANDO, Y
    NISHIMURA, M
    HAYAKAWA, H
    KAWASE, N
    IDOTA, A
    KAGAKU KOGAKU RONBUNSHU, 1995, 21 (02) : 279 - 285
  • [32] Cultivation of aerobic granules in a bubble column and an airlift reactor with divided draft tubes at low aeration rate
    Liu, Yong-Qiang
    Tay, Joo-Hwa
    BIOCHEMICAL ENGINEERING JOURNAL, 2007, 34 (01) : 1 - 7
  • [33] Axial and Radial Dispersion in a Large-Diameter Bubble Column Reactor at Low Height-to-Diameter Ratios
    Bloch, Gregor
    Zander, Hans-Joerg
    Wunderlich, Bernd
    Acher, Thomas
    CHEMIE INGENIEUR TECHNIK, 2015, 87 (06) : 756 - 761
  • [34] Effect of pressure on the hydrodynamics of a pilot-scale bubble column operating with low and moderate viscosity Newtonian liquids
    Lakhdissi, El Mahdi
    Shu, Shuli
    Farag, Sherif
    Guy, Christophe
    Chaouki, Jamal
    CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 2021, 99 (11) : 2320 - 2332
  • [35] Effects of multiple draft tubes with perforated plates on average gas holdup, volumetric mass transfer coefficient and liquid mixing time in a bubble column
    Kawasaki, Hiroyuki
    Yamamoto, Tatsurni
    KAGAKU KOGAKU RONBUNSHU, 2007, 33 (03) : 208 - 210
  • [36] Bubble characterization and gas-liquid interfacial area in two phase gas-liquid system in bubble column at low Reynolds number and high temperature and pressure
    Feng, Dan
    Ferrasse, Jean-Henry
    Soric, Audrey
    Boutin, Olivier
    CHEMICAL ENGINEERING RESEARCH & DESIGN, 2019, 144 : 95 - 106
  • [37] Gas holdup and liquid mixing time in a bubble column (0.32 m i.d.) equipped with perforated plates having various types of hole arrangements
    Kawasaki, Hiroyuki
    Yamamoto, Tatsumi
    Seekkuarachchi, Isuru
    Kumazawa, Hidehiro
    KAGAKU KOGAKU RONBUNSHU, 2006, 32 (03) : 207 - 210
  • [38] A Bubble Column Dehumidifier using Ionic Liquid Desiccant for Low-Humidity Industries: Insights into Transfer Processes Integrating Experiment and CFD Modelling
    Cao, Bowen
    Yin, Yonggao
    Saito, Kiyoshi
    JOURNAL OF THERMAL SCIENCE, 2024, 33 (06) : 2348 - 2371
  • [39] VOLUMETRIC MASS-TRANSFER COEFFICIENT IN SOLID-SUSPENDED BUBBLE-COLUMN WITH DRAFT TUBE CONTAINING LOW-DENSITY PARTICLES
    MIYAHARA, T
    TATSUMI, N
    KAGAKU KOGAKU RONBUNSHU, 1993, 19 (03) : 529 - 532