Characterizing fluid dynamics in a bubble column aimed for the determination of reactive mass transfer

被引:29
|
作者
Kovats, Peter [1 ]
Thevenin, Dominique [1 ]
Zaehringer, Katharina [1 ]
机构
[1] Otto von Guericke Univ, Lab Fluid Dynam & Tech Flows, Univ Pl 2, D-39106 Magdeburg, Germany
关键词
Bubble column reactor; CO2; PIV; Shadowgraphy; Two-phase flow; Two-tracer-LIF; PARTICLE IMAGE VELOCIMETRY; FLOW STRUCTURE; LIQUID; TURBULENCE; BEHAVIOR; PARAMETERS; DESIGN; WAKE; PIV;
D O I
10.1007/s00231-017-2142-0
中图分类号
O414.1 [热力学];
学科分类号
摘要
Bubble column reactors are multiphase reactors that are used in many process engineering applications. In these reactors a gas phase comes into contact with a fluid phase to initiate or support reactions. The transport process from the gas to the liquid phase is often the limiting factor. Characterizing this process is therefore essential for the optimization of multiphase reactors. For a better understanding of the transfer mechanisms and subsequent chemical reactions, a laboratory-scale bubble column reactor was investigated. First, to characterize the flow field in the reactor, two different methods have been applied. The shadowgraphy technique is used for the characterisation of the bubbles (bubble diameter, velocity, shape or position) for various process conditions. This technique is based on particle recognition with backlight illumination, combined with particle tracking velocimetry (PTV). The bubble trajectories in the column can also be obtained in this manner. Secondly, the liquid phase flow has been analysed by particle image velocimetry (PIV). The combination of both methods, delivering relevant information concerning disperse (bubbles) and continuous (liquid) phases, leads to a complete fluid dynamical characterization of the reactor, which is the pre-condition for the analysis of mass transfer between both phases.
引用
收藏
页码:453 / 461
页数:9
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