Mass transfer characteristics of liquid films flowing down a vertical wire in a counter current gas flow

被引:28
作者
Gruenig, J. [1 ]
Lyagin, E. [1 ]
Horn, S. [1 ]
Skale, T. [1 ]
Kraume, M. [1 ]
机构
[1] Tech Univ Berlin, Chair Chem & Proc Engn, D-10623 Berlin, Germany
关键词
Wetted wire packing; Films; Mass transfer; Multiphase flow; Absorption; Distillation; WETTED-WALL COLUMNS; DISTILLATION-COLUMNS; STRUCTURED PACKINGS; VISCOUS BEADS; WAVY FILMS; ABSORPTION; DIFFUSION; SURFACE; COEFFICIENTS; INSTABILITY;
D O I
10.1016/j.ces.2011.10.049
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The wetted-wire packing, mainly consisting of a bundle of vertical parallel wires, is a promising concept for the use in separation columns. To investigate the multiphase flow inside the packing in detail and to estimate the performance of the packing, experiments on liquid films on a single vertical wire in a counter current gas flow were carried out. To get information about the interfacial area, an optical measurement of the film thickness was carried out with a digital high speed camera and image recognition tools. By measuring the evaporation of water and aqueous polyvinylpyrrolidone solutions into air, the gas-side mass transfer was determined. The liquid-side mass transfer was examined by measuring the desorption of CO(2) from water into air. The results show that the mass transfer coefficients are comparable to those appearing in common structured packings. When assuming a sufficiently high wire packing density, a specific interfacial area similar to corrugated sheet structured packings can be reached. Previous studies predicted a low pressure drop per packing height and extended capacity limits compared to common packings. In consideration of these results, the wetted wire packing therefore is shown to be suitable especially for absorption processes where a low pressure drop is favourable. (C) 2011 Elsevier Ltd. All rights reserved.
引用
收藏
页码:329 / 339
页数:11
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