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Continuous supply of glucose and glycerol enhances biotransformation of ricinoleic acid to (E)-11-(heptanoyloxy) undec-9-enoic acid in recombinant Escherichia coli

Authors
Cho, Yong-HanKim, Soo-JungKim, Hyun-WooKim, Ji YoungGwak, Jun SeokChung, DonghwaKim, Kyoung HeonPark, KyungmoonPark, Yong-Cheol
Issue Date
10-7월-2017
Publisher
ELSEVIER SCIENCE BV
Keywords
Ricinoleic acid; (E)-11-(Heptanoyloxy) undec-9-enoic acid; Recombinant Escherichia coli; Alcohol dehydrogenase; Baeyer-Villiger monooxygenase; Fed-batch
Citation
JOURNAL OF BIOTECHNOLOGY, v.253, pp.34 - 39
Indexed
SCIE
SCOPUS
Journal Title
JOURNAL OF BIOTECHNOLOGY
Volume
253
Start Page
34
End Page
39
URI
https://scholar.korea.ac.kr/handle/2021.sw.korea/82843
DOI
10.1016/j.jbiotec.2017.05.014
ISSN
0168-1656
Abstract
This study aimed at the development of biotransformation strategies with feeding of energy sources for bioconversion of ricinoleic acid to (E)-11-(heptanoyloxy) undec-9-enoic acid (11-HOUA), a key intermediate of brassylic acid, by recombinant Escherichia coli overexpressing an alcohol dehydrogenase from Micrococcus luteus and a Baeyer-Villiger monooxygenase from Pseudomonas putida KT2440. Feeding of glucose or glycerol facilitated both the preparation of high-density cell biocatalyst and supply of the NAD(+) and NADPH cofactors. By the glucose feeding strategy, 30.8 g/L of the engineered E. coli cells produced 29.7 mM of 11-HOUA with 1.9 mM/h of productivity, which were 1.8 and 1.6 times higher than the same biotransformation without the glucose feeding, respectively. Intermittent addition of glycerol increased 11-HOUA productivity by 16% compared to that by the glucose feeding. Finally, 34.5 mM of 11-HOUA concentration, 77% conversion and 2.2 mM/h productivity were obtained using 31.6 g/L of cell biocatalyst along with the glycerol addition. It was concluded that supplementation of additional carbon sources in biotransformation process would be a potent strategy to increase the performance of fatty acid conversion.
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