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In relation to this article, we declare that there is no conflict of interest.
Publication history
Received October 21, 2002
Accepted December 31, 2002
articles This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
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Micromixer as a Continuous Flow Reactor for the Synthesis of a Pharmaceutical Intermediate

LG Chem, Ltd./Research Park, 104-1 Moonji-dong, Yuseong-gu, Daejeon 305-380, Korea
khsong@lgchem.com
Korean Journal of Chemical Engineering, March 2003, 20(2), 268-272(5), 10.1007/BF02697239
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Abstract

A mixing device composed of a micron scale flow channel was applied as a continuous reactor to control exothermic reaction heat and to increase the product yield, in a synthesis of a pharmaceutical intermediate of quinolone antibiotics. The model reaction featured a fast reaction rate, high heat generation, and impurity formation due to a prolonged contact time between reactants and products. Using the micromixer reactor, the reaction heat was efficiently removed so that virtually no impurities were produced during the reaction. A product yield comparable to the theoretical value was achieved in a single micromixer unit. Optimum operating conditions were acquired from a statistical method by using factorial design, which was also verified by a CFD calculation.

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