LAPSE:2024.1819v1
Published Article

LAPSE:2024.1819v1
Efficient Bio-Oxidation of Cellobiose with Engineered Gluconobacter oxydans to Provide Highly Concentrated Cellobionic Acid
August 23, 2024
Abstract
Cellobionic acid (CBA) can be obtained through the oxidation of cellobiose, the monomer of cellulose. CBA serves as a plant-based alternative to its stereoisomer lactobionic acid, which is used in the pharmaceutical, cosmetic, and food industries. Gluconobacter oxydans is a well-established whole-cell biocatalyst with membrane-bound dehydrogenases (mDH) for regio-specific oxidations. As G. oxydans wildtype cells show low cellobiose oxidation activities, the glucose mDH from Pseudomonas taetrolens was overexpressed in G. oxydans BP9, a multi mDH deletion strain. Whole-cell biotransformation studies were performed with resting cells of the engineered G. oxydans in stirred tank bioreactors. Initial biomass specific cellobionate formation rates increased with increasing cellobiose concentrations up to 190 g L−1, and were constant until the solubility limit. The maximal volumetric CBA formation rates and the oxygen uptake rates increased linearly with the concentration of engineered G. oxydans. This enables the estimation of the maximum biocatalyst concentration limited by the maximum oxygen transfer rate of any bioreactor. Thus, 5.2 g L−1G. oxydans was sufficient to produce 502 g L−1 CBA with >99% yield in a simple aerobic batch process. The highly concentrated CBA will reduce downstream processing costs considerably after cell separation.
Cellobionic acid (CBA) can be obtained through the oxidation of cellobiose, the monomer of cellulose. CBA serves as a plant-based alternative to its stereoisomer lactobionic acid, which is used in the pharmaceutical, cosmetic, and food industries. Gluconobacter oxydans is a well-established whole-cell biocatalyst with membrane-bound dehydrogenases (mDH) for regio-specific oxidations. As G. oxydans wildtype cells show low cellobiose oxidation activities, the glucose mDH from Pseudomonas taetrolens was overexpressed in G. oxydans BP9, a multi mDH deletion strain. Whole-cell biotransformation studies were performed with resting cells of the engineered G. oxydans in stirred tank bioreactors. Initial biomass specific cellobionate formation rates increased with increasing cellobiose concentrations up to 190 g L−1, and were constant until the solubility limit. The maximal volumetric CBA formation rates and the oxygen uptake rates increased linearly with the concentration of engineered G. oxydans. This enables the estimation of the maximum biocatalyst concentration limited by the maximum oxygen transfer rate of any bioreactor. Thus, 5.2 g L−1G. oxydans was sufficient to produce 502 g L−1 CBA with >99% yield in a simple aerobic batch process. The highly concentrated CBA will reduce downstream processing costs considerably after cell separation.
Record ID
Keywords
aldobionic acid, bio-oxidation, cellobionic acid, Gluconobacter oxydans, multideletion strain, whole-cell biocatalysis
Subject
Suggested Citation
Bieringer E, Pütthoff L, Zimmermann A, de Souza Góes M, Yilmaz U, Ehrenreich A, Liebl W, Weuster-Botz D. Efficient Bio-Oxidation of Cellobiose with Engineered Gluconobacter oxydans to Provide Highly Concentrated Cellobionic Acid. (2024). LAPSE:2024.1819v1
Author Affiliations
Bieringer E: Chair of Biochemical Engineering, Technical University of Munich, Boltzmannstraße 15, 85748 Garching, Germany [ORCID]
Pütthoff L: Chair of Microbiology, Technical University of Munich, Emil-Ramann-Straße 4, 85354 Freising, Germany
Zimmermann A: Chair of Biochemical Engineering, Technical University of Munich, Boltzmannstraße 15, 85748 Garching, Germany
de Souza Góes M: Chair of Biochemical Engineering, Technical University of Munich, Boltzmannstraße 15, 85748 Garching, Germany [ORCID]
Yilmaz U: Chair of Biochemical Engineering, Technical University of Munich, Boltzmannstraße 15, 85748 Garching, Germany
Ehrenreich A: Chair of Microbiology, Technical University of Munich, Emil-Ramann-Straße 4, 85354 Freising, Germany [ORCID]
Liebl W: Chair of Microbiology, Technical University of Munich, Emil-Ramann-Straße 4, 85354 Freising, Germany [ORCID]
Weuster-Botz D: Chair of Biochemical Engineering, Technical University of Munich, Boltzmannstraße 15, 85748 Garching, Germany [ORCID]
Pütthoff L: Chair of Microbiology, Technical University of Munich, Emil-Ramann-Straße 4, 85354 Freising, Germany
Zimmermann A: Chair of Biochemical Engineering, Technical University of Munich, Boltzmannstraße 15, 85748 Garching, Germany
de Souza Góes M: Chair of Biochemical Engineering, Technical University of Munich, Boltzmannstraße 15, 85748 Garching, Germany [ORCID]
Yilmaz U: Chair of Biochemical Engineering, Technical University of Munich, Boltzmannstraße 15, 85748 Garching, Germany
Ehrenreich A: Chair of Microbiology, Technical University of Munich, Emil-Ramann-Straße 4, 85354 Freising, Germany [ORCID]
Liebl W: Chair of Microbiology, Technical University of Munich, Emil-Ramann-Straße 4, 85354 Freising, Germany [ORCID]
Weuster-Botz D: Chair of Biochemical Engineering, Technical University of Munich, Boltzmannstraße 15, 85748 Garching, Germany [ORCID]
Journal Name
Processes
Volume
12
Issue
7
First Page
1464
Year
2024
Publication Date
2024-07-13
ISSN
2227-9717
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Original Submission
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PII: pr12071464, Publication Type: Journal Article
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LAPSE:2024.1819v1
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https://doi.org/10.3390/pr12071464
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Aug 23, 2024
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Aug 23, 2024
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