Use of the two-liquid phase concept to exploit kinetically controlled multistep biocatalysis

The two‐liquid phase concept was used to develop a whole cell biocatalytic system for the efficient multistep oxidation of pseudocumene to 3,4‐dimethylbenzaldehyde. Recombinant Escherichia coli cells were employed to express the Pseudomonas putida genes encoding xylene monooxygenase, which catalyzes...

Full description

Saved in:
Bibliographic Details
Published inBiotechnology and bioengineering Vol. 81; no. 6; pp. 683 - 694
Main Authors Bühler, Bruno, Bollhalder, Irene, Hauer, Bernhard, Witholt, Bernard, Schmid, Andreas
Format Journal Article
LanguageEnglish
Published New York Wiley Subscription Services, Inc., A Wiley Company 20.03.2003
Wiley
Subjects
Online AccessGet full text

Cover

Loading…
More Information
Summary:The two‐liquid phase concept was used to develop a whole cell biocatalytic system for the efficient multistep oxidation of pseudocumene to 3,4‐dimethylbenzaldehyde. Recombinant Escherichia coli cells were employed to express the Pseudomonas putida genes encoding xylene monooxygenase, which catalyzes the multistep oxygenation of one methyl group of toluene and xylenes to corresponding alcohols, aldehydes, and acids. A fed‐batch based two‐liquid phase bioconversion was established with bis(2‐ethylhexyl)‐ phthalate as organic carrier solvent and a phase ratio of 0.5; the product formation pattern, the impact of the nutrient feeding strategy, and the partitioning behavior of the reactants were studied. On the basis of the favorable conditions provided by the two‐liquid phase system, engineering of the initial pseudocumene concentration allowed exploiting the complex kinetics of the multistep reaction for the exclusive production of 3,4‐dimethyl‐ benzaldehyde. Further oxidation of the product to 3,4‐dimethylbenzoic acid could be inhibited by suitable concentrations of pseudocumene or 3,4‐dimethylbenzyl alcohol. The optimized biotransformation setup includes a completely defined medium with high iron content and a nutrient feeding strategy that avoids severe glucose limitation as well as high inhibitory glucose levels. Using such a system on a 2‐liter scale, we were able to produce, within 14.5 h, 30 g of 3,4‐dimethylbenzaldehyde as predominant reactant in the organic phase and reached a maximal productivity of 1.6 g per liter liquid volume per hour. The present study implicates that the two‐liquid phase concept is an efficient tool to exploit the kinetics of multistep biotransformations in general. © 2003 Wiley Periodicals. Biotechnol Bioeng 81: 683–694, 2003.
Bibliography:ArticleID:BIT10512
ark:/67375/WNG-DH3TP2NN-X
istex:4764A4480591CEF4AC50A48E888B2BA0228D36AC
ObjectType-Article-2
SourceType-Scholarly Journals-1
ObjectType-Feature-1
content type line 23
ObjectType-Article-1
ObjectType-Feature-2
ISSN:0006-3592
1097-0290
DOI:10.1002/bit.10512