Effective interfacial area for mass transfer in the liquid-liquid slug flow capillary microreactors

被引:146
作者
Ghaini, A. [1 ]
Kashid, M. N. [2 ]
Agar, D. W.
机构
[1] Dortmund Univ Technol, Dept Bio & Chem Engn, Lab Tech Chem TCB B, D-44227 Dortmund, Germany
[2] Ecole Polytech Fed Lausanne, Grp Catalyt React Engn GGRC, CH-1015 Lausanne, Switzerland
关键词
Capillary microreactor; Liquid-liquid slug flow; Extraction; Mass transfer; Interfacial area; CHEMICAL-REACTION; EXTRACTION; REACTOR; SYSTEM;
D O I
10.1016/j.cep.2010.03.009
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Liquid-liquid biphasic reactions play an important role in the chemical and pharmaceutical Industries The liquid-liquid slug flow capillary microreactor offers considerable potential benefits over the conventional liquid-liquid contactors Though the hydrodynamics and mass transfer have been investigated for this reactor concept, so fat the effective interfacial area available for mass transfer has not been experimentally quantified Despite the well-defined flow patterns arising in the capillary microreactor, the wetting behaviour of the liquids at the capillary wall is inadequately integrated into the models and thus, the true Interfacial area being used for mass transfer is uncertain In the present work, experiments were carried out to determine the mass transfer rates and effective interfacial area using physical and chemical methods The effective interfacial areas measured by physical and chemical methods were compared and it confirms the presence of the previously conjectured organic wall film. which provides a much higher Interfacial area including both. the ends and sides of the non-wetting slugs Overall volumetric mass transfer coefficients were obtained by physical extraction and compared to the chemical method The organic wall film is visualised by a light induced fluorescence method, which shows the organic phase completely coveting the hydrophobic capillary wall. indicating that the effective interfacial at ea lot mass transfer in this reactor concept can significantly differ from the physical Interfacial area (C) 2010 Elsevier B V All rights reserved
引用
收藏
页码:358 / 366
页数:9
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