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Shake flask methodology for assessing the influence of the maximum oxygen transfer capacity on 2,3-butanediol production

BACKGROUND: Production of 2,3-butanediol from renewable resources is a promising measure to decrease the consumption of fossil resources in the chemical industry. One of the most influential parameters on biotechnological 2,3-butanediol production is the oxygen availability during the cultivation. A...

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Autores principales: Heyman, Benedikt, Lamm, Robin, Tulke, Hannah, Regestein, Lars, Büchs, Jochen
Formato: Online Artículo Texto
Lenguaje:English
Publicado: BioMed Central 2019
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC6498610/
https://www.ncbi.nlm.nih.gov/pubmed/31053124
http://dx.doi.org/10.1186/s12934-019-1126-9
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author Heyman, Benedikt
Lamm, Robin
Tulke, Hannah
Regestein, Lars
Büchs, Jochen
author_facet Heyman, Benedikt
Lamm, Robin
Tulke, Hannah
Regestein, Lars
Büchs, Jochen
author_sort Heyman, Benedikt
collection PubMed
description BACKGROUND: Production of 2,3-butanediol from renewable resources is a promising measure to decrease the consumption of fossil resources in the chemical industry. One of the most influential parameters on biotechnological 2,3-butanediol production is the oxygen availability during the cultivation. As 2,3-butanediol is produced under microaerobic process conditions, a well-controlled oxygen supply is the key parameter to control biomass formation and 2,3-butanediol production. As biomass is on the one hand not the final product, but on the other hand the essential biocatalyst, the optimal compromise between biomass formation and 2,3-butanediol production has to be defined. RESULTS: A shake flask methodology is presented to evaluate the effects of oxygen availability on 2,3-butanediol production with Bacillus licheniformis DSM 8785 by variation of the filling volume. A defined two-stage cultivation strategy was developed to investigate the metabolic response to different defined maximum oxygen transfer capacities at equal initial growth conditions. The respiratory quotient was measured online to determine the point of glucose depletion, as 2,3-butanediol is consumed afterwards. Based on this strategy, comparable results to stirred tank reactors were achieved. The highest space–time yield (1.3 g/L/h) and a 2,3-butanediol concentration of 68 g/L combined with low acetoin concentrations and avoided glycerol formation were achieved at a maximum oxygen transfer capacity of 13 mmol/L/h. The highest overall 2,3-butanediol concentration of 78 g/L was observed at a maximum oxygen transfer capacity of 4 mmol/L/h. CONCLUSIONS: The presented shake flask approach reduces the experimental effort and costs providing a fast and reliable methodology to investigate the effects of oxygen availability. This can be applied especially on product and by-product formation under microaerobic conditions. Utilization of the maximum oxygen transfer capacity as measure for the oxygen availability allows for an easy adaption to other bioreactor setups and scales. ELECTRONIC SUPPLEMENTARY MATERIAL: The online version of this article (10.1186/s12934-019-1126-9) contains supplementary material, which is available to authorized users.
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spelling pubmed-64986102019-05-09 Shake flask methodology for assessing the influence of the maximum oxygen transfer capacity on 2,3-butanediol production Heyman, Benedikt Lamm, Robin Tulke, Hannah Regestein, Lars Büchs, Jochen Microb Cell Fact Research BACKGROUND: Production of 2,3-butanediol from renewable resources is a promising measure to decrease the consumption of fossil resources in the chemical industry. One of the most influential parameters on biotechnological 2,3-butanediol production is the oxygen availability during the cultivation. As 2,3-butanediol is produced under microaerobic process conditions, a well-controlled oxygen supply is the key parameter to control biomass formation and 2,3-butanediol production. As biomass is on the one hand not the final product, but on the other hand the essential biocatalyst, the optimal compromise between biomass formation and 2,3-butanediol production has to be defined. RESULTS: A shake flask methodology is presented to evaluate the effects of oxygen availability on 2,3-butanediol production with Bacillus licheniformis DSM 8785 by variation of the filling volume. A defined two-stage cultivation strategy was developed to investigate the metabolic response to different defined maximum oxygen transfer capacities at equal initial growth conditions. The respiratory quotient was measured online to determine the point of glucose depletion, as 2,3-butanediol is consumed afterwards. Based on this strategy, comparable results to stirred tank reactors were achieved. The highest space–time yield (1.3 g/L/h) and a 2,3-butanediol concentration of 68 g/L combined with low acetoin concentrations and avoided glycerol formation were achieved at a maximum oxygen transfer capacity of 13 mmol/L/h. The highest overall 2,3-butanediol concentration of 78 g/L was observed at a maximum oxygen transfer capacity of 4 mmol/L/h. CONCLUSIONS: The presented shake flask approach reduces the experimental effort and costs providing a fast and reliable methodology to investigate the effects of oxygen availability. This can be applied especially on product and by-product formation under microaerobic conditions. Utilization of the maximum oxygen transfer capacity as measure for the oxygen availability allows for an easy adaption to other bioreactor setups and scales. ELECTRONIC SUPPLEMENTARY MATERIAL: The online version of this article (10.1186/s12934-019-1126-9) contains supplementary material, which is available to authorized users. BioMed Central 2019-05-03 /pmc/articles/PMC6498610/ /pubmed/31053124 http://dx.doi.org/10.1186/s12934-019-1126-9 Text en © The Author(s) 2019 Open AccessThis article is distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution, and reproduction in any medium, provided you give appropriate credit to the original author(s) and the source, provide a link to the Creative Commons license, and indicate if changes were made. The Creative Commons Public Domain Dedication waiver (http://creativecommons.org/publicdomain/zero/1.0/) applies to the data made available in this article, unless otherwise stated.
spellingShingle Research
Heyman, Benedikt
Lamm, Robin
Tulke, Hannah
Regestein, Lars
Büchs, Jochen
Shake flask methodology for assessing the influence of the maximum oxygen transfer capacity on 2,3-butanediol production
title Shake flask methodology for assessing the influence of the maximum oxygen transfer capacity on 2,3-butanediol production
title_full Shake flask methodology for assessing the influence of the maximum oxygen transfer capacity on 2,3-butanediol production
title_fullStr Shake flask methodology for assessing the influence of the maximum oxygen transfer capacity on 2,3-butanediol production
title_full_unstemmed Shake flask methodology for assessing the influence of the maximum oxygen transfer capacity on 2,3-butanediol production
title_short Shake flask methodology for assessing the influence of the maximum oxygen transfer capacity on 2,3-butanediol production
title_sort shake flask methodology for assessing the influence of the maximum oxygen transfer capacity on 2,3-butanediol production
topic Research
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC6498610/
https://www.ncbi.nlm.nih.gov/pubmed/31053124
http://dx.doi.org/10.1186/s12934-019-1126-9
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