Chemisorption of CO2 in a gas-liquid vortex reactor: An interphase mass transfer efficiency assessment

被引:12
|
作者
Ouyang, Yi [1 ]
Manzano, Manuel Nunez [1 ]
Chen, Siyuan [1 ]
Wetzels, Ruben [1 ]
Verspeelt, Tom [1 ]
Van Geem, Kevin M. [1 ]
Heynderickx, Geraldine J. [1 ]
机构
[1] Univ Ghent, Lab Chem Technol, Technol Pk 125, B-9052 Ghent, Belgium
基金
欧洲研究理事会;
关键词
CO2; capture; gas-liquid vortex reactor; interphase mass transfer; process intensification; CARBON-DIOXIDE ABSORPTION; AQUEOUS MONOETHANOLAMINE SOLUTIONS; EFFECTIVE INTERFACIAL AREA; PROCESS INTENSIFICATION; TRANSFER COEFFICIENT; CAPTURE; KINETICS; DESIGN; BEDS;
D O I
10.1002/aic.17608
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
To develop cost-effective CO2 capture technology process intensification will play a vital role. In this work, the capabilities of a gas-liquid vortex reactor (GLVR) as novel process intensification equipment are evaluated by studying its interphase mass transfer parameters to build up the fundamentals for its future application to for example, CO2 capture. The NaOH-CO2 chemisorption system and Danckwerts' model are applied to obtain the effective interfacial area and liquid-side mass transfer coefficient. Results show that the gas-liquid contact in the GLVR is capable of both generating a large interfacial area in a small reactor volume and creating a region with high-energy dissipation to improve mass transfer. A comparison of the volumetric mass transfer coefficients with data reported in literature for conventional and intensified reactor types confirms a superior mass transfer efficiency and, most importantly, a favorable energetic efficiency of the GLVR.
引用
收藏
页数:12
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