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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...
Autores principales: | , , , , |
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Formato: | Online Artículo Texto |
Lenguaje: | English |
Publicado: |
BioMed Central
2019
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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. |
format | Online Article Text |
id | pubmed-6498610 |
institution | National Center for Biotechnology Information |
language | English |
publishDate | 2019 |
publisher | BioMed Central |
record_format | MEDLINE/PubMed |
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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