Improvement of the operational stability of the Novozym 435® biocatalyst in the oxidation of 2,5-furandicarboxaldehyde to 2,5-furandicarboxylic acid in a continuous packed-bed microbioreactor
[Display omitted] The present work reports the evaluation of the yield, productivity and operational stability of the chemoenzymatic oxidation of 2,5-furandicarboxaldehyde (DFF) to 2,5-furan dicarboxylic acid (FDCA) catalyzed by immobilized lipase B from Candida antarctica (Novozym® 435) in a contin...
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Published in | Tetrahedron letters Vol. 121; p. 154475 |
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Main Authors | , , |
Format | Journal Article |
Language | English |
Published |
Elsevier Ltd
17.05.2023
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Subjects | |
Online Access | Get full text |
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Summary: | [Display omitted]
The present work reports the evaluation of the yield, productivity and operational stability of the chemoenzymatic oxidation of 2,5-furandicarboxaldehyde (DFF) to 2,5-furan dicarboxylic acid (FDCA) catalyzed by immobilized lipase B from Candida antarctica (Novozym® 435) in a continuous packed bed microbioreactor. The highest yields and productivities were achieved using a feed for the reaction medium at 36 µL/min flow. The yield and specific productivity in continuous packed bed microbioreactor were approximately 20% and 1000 times higher than that obtained by operating in millibioreactors. The operational stability of the biocatalyst in the microbioreactor was higher than that achieved in a millibioreactor in continuous operation for 24 h. Finally, the packed bed microbioreactor is an interesting and straightforward strategy to increase the stability of the biocatalyst in continuous mode. |
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ISSN: | 0040-4039 1873-3581 |
DOI: | 10.1016/j.tetlet.2023.154475 |