Multiscale Description of Mass Transfer Processes for Gas-Liquid Reactions

被引:5
|
作者
Kueck, Ulf Daniel [1 ]
Kroeger, Michael [2 ]
Bothe, Dieter [2 ]
Raebiger, Norbert [3 ]
Schlueter, Michael [1 ]
Warnecke, Hans-Joachim [4 ]
机构
[1] Tech Univ Hamburg, Inst Mehrphasenstromungen, D-21073 Hamburg, Germany
[2] Tech Univ Darmstadt, Ctr Smart Interfaces, D-64287 Darmstadt, Germany
[3] Univ Bremen, Inst Umweltverfahrenstech, D-28359 Bremen, Germany
[4] Univ Gesamthsch Paderborn, D-33098 Paderborn, Germany
关键词
Bubble; Gas-liquid reaction; Mass transfer; Sulfite-sulfate reaction; Volume-of-fluid (VOF) method; BUBBLES; SYSTEMS; WATER;
D O I
10.1002/cite.201100036
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This work focuses on the investigation of multiscale mass transfer processes at freely rising single spherical bubbles with superimposed chemical reaction. For this purpose, the oxygen mass transfer without chemical reaction, calculated from numerical simulations and experimental investigations is compared quantitatively. Moreover the impact of the sulfite-sulfate reaction on the concentration field is shown qualitatively. It becomes obvious that numerical simulations provide more detailed information of the velocity field, while experiments represent a valid analysis of the concentration field. Thus bidirectional validation and combined usage of the more significant results lead to an improved calculation of the local oxygen mass flow.
引用
收藏
页码:1084 / 1095
页数:12
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