Abstract
A liquid–liquid phase transfer catalyzed (PTC) esterification reaction of 4-t-butylphenol in aqueous phase (1 M sodium hydroxide solution) and 4-methoxybenzoyl chloride in organic phase (dichloromethane) in a microchannel under parallel laminar flow conditions was studied in this work. Tetrabutylammonium bromide was used as the PTC. Stable liquid–liquid hydrodynamic flow and a defined specific interfacial area in a microreactor offer considerable benefits over conventional batch reactors and are crucial to study interactions between kinetics and mass transfer effects. Mentioned features were used to develop a 3D mathematical model considering convection in the flow direction, diffusion in all spatial directions, and reactions in organic and aqueous phases. Results have shown a much higher mass transfer rate of the PTC between both phases as the one predicted by the 3D mathematical model. It may be assumed that the instability of parallel flow, along with the mass transfer of catalyst between both phases, causes rippling and erratic pulsation at the interface which then leads to interfacial convection and increased mass transfer rates. With a proposed correlation for mass transfer enhancement due to interfacial convection, all the experimental data were successfully predicted by the model.
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The financial support for this work by the Slovenian Ministry of Higher Education, Science and Technology (Grant P2-0191), is gratefully acknowledged.
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Šinkovec, E., Pohar, A. & Krajnc, M. Phase transfer catalyzed esterification: modeling and experimental studies in a microreactor under parallel flow conditions. Microfluid Nanofluid 14, 489–498 (2013). https://doi.org/10.1007/s10404-012-1067-7
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DOI: https://doi.org/10.1007/s10404-012-1067-7