Effects of Reaction Operation Policies on Properties of Core–Shell Polymer Supports Used for Preparation of Highly Active Biocatalysts

Abstract Core–shell polymer supports with different morphological features and compositions are prepared through combined suspension and emulsion polymerizations. It is shown that proper manipulation of the divinylbenzene (DVB) feed content allows for maximization of specific areas, porosities, and...

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Bibliographic Details
Published in:Macromolecular Reaction Engineering
Main Authors: Pinto, Martina Costa Cerqueira, de Souza e Castro, Nathany Lisbôa, Cipolatti, Eliane Pereira, Fernandez‐Lafuente, Roberto, Manoel, Evelin Andrade, Freire, Denise Maria Guimarães, Pinto, José Carlos
Other Authors: Conselho Nacional de Desenvolvimento Científico e Tecnológico, Coordenação de Aperfeiçoamento de Pessoal de Nível Superior
Format: Article in Journal/Newspaper
Language:English
Published: Wiley 2018
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Online Access:http://dx.doi.org/10.1002/mren.201800055
https://api.wiley.com/onlinelibrary/tdm/v1/articles/10.1002%2Fmren.201800055
https://onlinelibrary.wiley.com/doi/pdf/10.1002/mren.201800055
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Summary:Abstract Core–shell polymer supports with different morphological features and compositions are prepared through combined suspension and emulsion polymerizations. It is shown that proper manipulation of the divinylbenzene (DVB) feed content allows for maximization of specific areas, porosities, and mechanical resistances. Additionally, it is shown that feeding of previously prepared miniemulsions leads to core–shell particles with smaller specific areas, due to less efficient coating of the cores. Particularly, the combined manipulation of polymerization times and DVB feed compositions allows for production of particles with pronounced specific area (50 m 2 g −1 ) and porosity (0.30 cm 3 g −1 ). Produced core–shell polymer particles are employed as supports for the immobilization of lipase B from Candida antarctica , and the obtained enzymatic activities for both hydrolysis ( A hyd ) and esterification ( A est ) reactions are very high ( A hyd = 34.7 ± 3.8 U/g; A est = 3564.6 ± 581 U/g), even when compared to activities obtained using the reference commercial biocatalyst Novozym 435 ( A hyd = 7.6 ± 1.8 U/g, A est = 2384.7 ± 307.2 U/g). Finally, biocatalysts prepared with the core–shell supports present higher enzymatic activities than biocatalysts prepared with supports of higher specific area obtained through conventional emulsion polymerizations, indicating that the porous structure of the shell can be beneficial for the immobilization and activity of the enzymes.