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Bioconversion of xylose to xylonic acid via co-immobilized dehydrogenases for conjunct cofactor regeneration.
Bachosz, Karolina; Synoradzki, Karol; Staszak, Maciej; Pinelo, Manuel; Meyer, Anne S; Zdarta, Jakub; Jesionowski, Teofil.
Afiliación
  • Bachosz K; Institute of Chemical Technology and Engineering, Faculty of Chemical Technology, Poznan University of Technology, Berdychowo 4, PL-60965 Poznan, Poland.
  • Synoradzki K; Institute of Molecular Physics, Polish Academy of Sciences, Smoluchowskiego 17, PL-60179 Poznan, Poland; Institute of Low Temperature and Structure Research, Polish Academy of Sciences, Okolna 2, PL-50422 Wroclaw, Poland.
  • Staszak M; Institute of Chemical Technology and Engineering, Faculty of Chemical Technology, Poznan University of Technology, Berdychowo 4, PL-60965 Poznan, Poland.
  • Pinelo M; Department of Chemical and Biochemical Engineering, DTU Chemical Engineering, Technical University of Denmark, Soltofts Plads 229, DK-2800 Kgs. Lyngby, Denmark.
  • Meyer AS; Department of Biotechnology and Biomedicine, DTU Bioengineering, Technical University of Denmark, Soltofts Plads 227, DK-2800 Kgs. Lyngby, Denmark.
  • Zdarta J; Institute of Chemical Technology and Engineering, Faculty of Chemical Technology, Poznan University of Technology, Berdychowo 4, PL-60965 Poznan, Poland. Electronic address: jakub.zdarta@put.poznan.pl.
  • Jesionowski T; Institute of Chemical Technology and Engineering, Faculty of Chemical Technology, Poznan University of Technology, Berdychowo 4, PL-60965 Poznan, Poland. Electronic address: teofil.jesionowski@put.poznan.pl.
Bioorg Chem ; 93: 102747, 2019 12.
Article en En | MEDLINE | ID: mdl-30739714
ABSTRACT
Enzymatic cofactor-dependent conversion of monosaccharides can be used in the bioproduction of value-added compounds. In this study, we demonstrate co-immobilization of xylose dehydrogenase (XDH, EC 1.1.1.175) and alcohol dehydrogenase (ADH, EC 1.1.1.1) using magnetite-silica core-shell particles for simultaneous conversion of xylose into xylonic acid (XA) and in situ cofactor regeneration. The reaction conditions were optimized by factorial design, and were found to be XDHADH ratio 21, temperature 25 °C, pH 7, and process duration 60 min. Under these conditions enzymatic production of xylonic acid exceeded 4.1 mM and was more than 25% higher than in the case of a free enzymes system. Moreover, the pH and temperature tolerance as well as the thermo- and storage stability of the co-immobilized enzymes were significantly enhanced. Co-immobilized XDH and ADH make it possible to obtain higher xylonic acid concentration over broad ranges of pH (6-8) and temperature (15-35 °C) as compared to free enzymes, and retained over 60% of their initial activity after 20 days of storage. In addition, the half-life of the co-immobilized system was 4.5 times longer, and the inactivation constant (kD = 0.0141 1/min) four times smaller, than those of the free biocatalysts (kD = 0.0046 1/min). Furthermore, after five reaction cycles, immobilized XDH and ADH retained over 65% of their initial properties, with a final biocatalytic productivity of 1.65 mM of xylonic acid per 1 U of co-immobilized XDH. The results demonstrate the advantages of the use of co-immobilized enzymes over a free enzyme system in terms of enhanced activity and stability.
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Texto completo: 1 Banco de datos: MEDLINE Asunto principal: Xilosa / Alcohol Deshidrogenasa / Coenzimas / Oxidorreductasas de Alcohol Idioma: En Revista: Bioorg Chem Año: 2019 Tipo del documento: Article País de afiliación: Polonia

Texto completo: 1 Banco de datos: MEDLINE Asunto principal: Xilosa / Alcohol Deshidrogenasa / Coenzimas / Oxidorreductasas de Alcohol Idioma: En Revista: Bioorg Chem Año: 2019 Tipo del documento: Article País de afiliación: Polonia