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Highly efficient fermentation of 5-keto-d-fructose with Gluconobacter oxydans at different scales
BACKGROUND: The global market for sweeteners is increasing, and the food industry is constantly looking for new low-caloric sweeteners. The natural sweetener 5-keto-d-fructose is one such candidate. 5-Keto-d-fructose has a similar sweet taste quality as fructose. Developing a highly efficient 5-keto...
Autores principales: | , , , , , , , , |
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Formato: | Online Artículo Texto |
Lenguaje: | English |
Publicado: |
BioMed Central
2022
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Materias: | |
Acceso en línea: | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC9741787/ https://www.ncbi.nlm.nih.gov/pubmed/36496372 http://dx.doi.org/10.1186/s12934-022-01980-5 |
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author | Battling, Svenja Engel, Tobias Herweg, Elena Niehoff, Paul-Joachim Pesch, Matthias Scholand, Theresa Schöpping, Marie Sonntag, Nina Büchs, Jochen |
author_facet | Battling, Svenja Engel, Tobias Herweg, Elena Niehoff, Paul-Joachim Pesch, Matthias Scholand, Theresa Schöpping, Marie Sonntag, Nina Büchs, Jochen |
author_sort | Battling, Svenja |
collection | PubMed |
description | BACKGROUND: The global market for sweeteners is increasing, and the food industry is constantly looking for new low-caloric sweeteners. The natural sweetener 5-keto-d-fructose is one such candidate. 5-Keto-d-fructose has a similar sweet taste quality as fructose. Developing a highly efficient 5-keto-d-fructose production process is key to being competitive with established sweeteners. Hence, the 5-keto-d-fructose production process was optimised regarding titre, yield, and productivity. RESULTS: For production of 5-keto-d-fructose with G. oxydans 621H ΔhsdR pBBR1-p264-fdhSCL-ST an extended-batch fermentation was conducted. During fructose feeding, a decreasing respiratory activity occurred, despite sufficient carbon supply. Oxygen and second substrate limitation could be excluded as reasons for the decreasing respiration. It was demonstrated that a short period of oxygen limitation has no significant influence on 5-keto-d-fructose production, showing the robustness of this process. Increasing the medium concentration increased initial biomass formation. Applying a fructose feeding solution with a concentration of approx. 1200 g/L, a titre of 545 g/L 5-keto-d-fructose was reached. The yield was with 0.98 g(5-keto-d-fructose)/g(fructose) close to the theoretical maximum. A 1200 g/L fructose solution has a viscosity of 450 mPa∙s at a temperature of 55 °C. Hence, the solution itself and the whole peripheral feeding system need to be heated, to apply such a highly concentrated feeding solution. Thermal treatment of highly concentrated fructose solutions led to the formation of 5-hydroxymethylfurfural, which inhibited the 5-keto-d-fructose production. Therefore, fructose solutions were only heated to about 100 °C for approx. 10 min. An alternative feeding strategy was investigated using solid fructose cubes, reaching the highest productivities above 10 g(5-keto-d-fructose)/L/h during feeding. Moreover, the scale-up of the 5-keto-d-fructose production to a 150 L pressurised fermenter was successfully demonstrated using liquid fructose solutions (745 g/L). CONCLUSION: We optimised the 5-keto-d-fructose production process and successfully increased titre, yield and productivity. By using solid fructose, we presented a second feeding strategy, which can be of great interest for further scale-up experiments. A first scale-up of this process was performed, showing the possibility for an industrial production of 5-keto-d-fructose. SUPPLEMENTARY INFORMATION: The online version contains supplementary material available at 10.1186/s12934-022-01980-5. |
format | Online Article Text |
id | pubmed-9741787 |
institution | National Center for Biotechnology Information |
language | English |
publishDate | 2022 |
publisher | BioMed Central |
record_format | MEDLINE/PubMed |
spelling | pubmed-97417872022-12-12 Highly efficient fermentation of 5-keto-d-fructose with Gluconobacter oxydans at different scales Battling, Svenja Engel, Tobias Herweg, Elena Niehoff, Paul-Joachim Pesch, Matthias Scholand, Theresa Schöpping, Marie Sonntag, Nina Büchs, Jochen Microb Cell Fact Research BACKGROUND: The global market for sweeteners is increasing, and the food industry is constantly looking for new low-caloric sweeteners. The natural sweetener 5-keto-d-fructose is one such candidate. 5-Keto-d-fructose has a similar sweet taste quality as fructose. Developing a highly efficient 5-keto-d-fructose production process is key to being competitive with established sweeteners. Hence, the 5-keto-d-fructose production process was optimised regarding titre, yield, and productivity. RESULTS: For production of 5-keto-d-fructose with G. oxydans 621H ΔhsdR pBBR1-p264-fdhSCL-ST an extended-batch fermentation was conducted. During fructose feeding, a decreasing respiratory activity occurred, despite sufficient carbon supply. Oxygen and second substrate limitation could be excluded as reasons for the decreasing respiration. It was demonstrated that a short period of oxygen limitation has no significant influence on 5-keto-d-fructose production, showing the robustness of this process. Increasing the medium concentration increased initial biomass formation. Applying a fructose feeding solution with a concentration of approx. 1200 g/L, a titre of 545 g/L 5-keto-d-fructose was reached. The yield was with 0.98 g(5-keto-d-fructose)/g(fructose) close to the theoretical maximum. A 1200 g/L fructose solution has a viscosity of 450 mPa∙s at a temperature of 55 °C. Hence, the solution itself and the whole peripheral feeding system need to be heated, to apply such a highly concentrated feeding solution. Thermal treatment of highly concentrated fructose solutions led to the formation of 5-hydroxymethylfurfural, which inhibited the 5-keto-d-fructose production. Therefore, fructose solutions were only heated to about 100 °C for approx. 10 min. An alternative feeding strategy was investigated using solid fructose cubes, reaching the highest productivities above 10 g(5-keto-d-fructose)/L/h during feeding. Moreover, the scale-up of the 5-keto-d-fructose production to a 150 L pressurised fermenter was successfully demonstrated using liquid fructose solutions (745 g/L). CONCLUSION: We optimised the 5-keto-d-fructose production process and successfully increased titre, yield and productivity. By using solid fructose, we presented a second feeding strategy, which can be of great interest for further scale-up experiments. A first scale-up of this process was performed, showing the possibility for an industrial production of 5-keto-d-fructose. SUPPLEMENTARY INFORMATION: The online version contains supplementary material available at 10.1186/s12934-022-01980-5. BioMed Central 2022-12-10 /pmc/articles/PMC9741787/ /pubmed/36496372 http://dx.doi.org/10.1186/s12934-022-01980-5 Text en © The Author(s) 2022 https://creativecommons.org/licenses/by/4.0/Open AccessThis article is licensed under a Creative Commons Attribution 4.0 International License, which permits use, sharing, adaptation, distribution and reproduction in any medium or format, as long as you give appropriate credit to the original author(s) and the source, provide a link to the Creative Commons licence, and indicate if changes were made. The images or other third party material in this article are included in the article's Creative Commons licence, unless indicated otherwise in a credit line to the material. If material is not included in the article's Creative Commons licence and your intended use is not permitted by statutory regulation or exceeds the permitted use, you will need to obtain permission directly from the copyright holder. To view a copy of this licence, visit http://creativecommons.org/licenses/by/4.0/ (https://creativecommons.org/licenses/by/4.0/) . The Creative Commons Public Domain Dedication waiver (http://creativecommons.org/publicdomain/zero/1.0/ (https://creativecommons.org/publicdomain/zero/1.0/) ) applies to the data made available in this article, unless otherwise stated in a credit line to the data. |
spellingShingle | Research Battling, Svenja Engel, Tobias Herweg, Elena Niehoff, Paul-Joachim Pesch, Matthias Scholand, Theresa Schöpping, Marie Sonntag, Nina Büchs, Jochen Highly efficient fermentation of 5-keto-d-fructose with Gluconobacter oxydans at different scales |
title | Highly efficient fermentation of 5-keto-d-fructose with Gluconobacter oxydans at different scales |
title_full | Highly efficient fermentation of 5-keto-d-fructose with Gluconobacter oxydans at different scales |
title_fullStr | Highly efficient fermentation of 5-keto-d-fructose with Gluconobacter oxydans at different scales |
title_full_unstemmed | Highly efficient fermentation of 5-keto-d-fructose with Gluconobacter oxydans at different scales |
title_short | Highly efficient fermentation of 5-keto-d-fructose with Gluconobacter oxydans at different scales |
title_sort | highly efficient fermentation of 5-keto-d-fructose with gluconobacter oxydans at different scales |
topic | Research |
url | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC9741787/ https://www.ncbi.nlm.nih.gov/pubmed/36496372 http://dx.doi.org/10.1186/s12934-022-01980-5 |
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