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Scaling up a virginiamycin production by a high-yield Streptomyces virginiae VKM Ac-2738D strain using adsorbing resin addition and fed-batch fermentation under controlled conditions

Virginiamycin produced by Streptomyces virginiae as a natural mix of macrocyclic peptidolactones M and S is widely used in the industrial production of ethanol fuel and as an antibiotic feed additive for cattle and poultry. Its main antimicrobial components, M1 and S1 factors, act synergistically if...

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Autores principales: Dzhavakhiya, Vakhtang, Savushkin, Vyacheslav, Ovchinnikov, Alexander, Glagolev, Vladislav, Savelyeva, Veronika, Popova, Evgeniya, Novak, Nikita, Glagoleva, Elena
Formato: Online Artículo Texto
Lenguaje:English
Publicado: Springer Berlin Heidelberg 2016
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC5234532/
https://www.ncbi.nlm.nih.gov/pubmed/28330311
http://dx.doi.org/10.1007/s13205-016-0566-8
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author Dzhavakhiya, Vakhtang
Savushkin, Vyacheslav
Ovchinnikov, Alexander
Glagolev, Vladislav
Savelyeva, Veronika
Popova, Evgeniya
Novak, Nikita
Glagoleva, Elena
author_facet Dzhavakhiya, Vakhtang
Savushkin, Vyacheslav
Ovchinnikov, Alexander
Glagolev, Vladislav
Savelyeva, Veronika
Popova, Evgeniya
Novak, Nikita
Glagoleva, Elena
author_sort Dzhavakhiya, Vakhtang
collection PubMed
description Virginiamycin produced by Streptomyces virginiae as a natural mix of macrocyclic peptidolactones M and S is widely used in the industrial production of ethanol fuel and as an antibiotic feed additive for cattle and poultry. Its main antimicrobial components, M1 and S1 factors, act synergistically if the M1:S1 ratio in the final product is 70–75:25–30. This fact significantly complicates the development of stable high-yield strains suitable for industrial application. In the previous work, authors obtained a mutant S. virginiae VKM Ac-2738D strain, characterized by a high productivity in flasks and the optimum M1:S1 ratio (75:25) in the final product. In this study, the scale-up of the virginiamycin production by VKM AC-2738D from shake flasks to a pilot-scale (100 L) stirred fermentor was carried out and the possibility of the in situ use of synthetic adsorbing resins to remove virginiamycin from culture broth was assessed. After the optimization of pH and dissolved oxygen concentration (6.8–7.0 and 50%, respectively), the fed-batch fermentation of VKM Ac-2738D with continuous addition of 50% sucrose solution (5 g/L/day starting from 48 h of fermentation) resulted in a final virginiamycin titer of 4.9 g/L. Among four tested resins, Diaion(®) HP21 added to fermentation medium prior to sterilization absorbed 98.5% of the total virginiamycin that simplifies its further recovery procedure and increased its total titer to 5.6 g/L at the M1:S1 ratio of 74:26. The developed technology has several important advantages, which include (1) the optimum M1:S1 ratio in the final product, (2) the possibility to use sucrose as a carbon source instead of traditionally used and more expensive glucose or d-maltose, and (3) selective binding of up to 98.5% of produced virginiamycin on the adsorbing resin.
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spelling pubmed-52345322017-01-13 Scaling up a virginiamycin production by a high-yield Streptomyces virginiae VKM Ac-2738D strain using adsorbing resin addition and fed-batch fermentation under controlled conditions Dzhavakhiya, Vakhtang Savushkin, Vyacheslav Ovchinnikov, Alexander Glagolev, Vladislav Savelyeva, Veronika Popova, Evgeniya Novak, Nikita Glagoleva, Elena 3 Biotech Original Article Virginiamycin produced by Streptomyces virginiae as a natural mix of macrocyclic peptidolactones M and S is widely used in the industrial production of ethanol fuel and as an antibiotic feed additive for cattle and poultry. Its main antimicrobial components, M1 and S1 factors, act synergistically if the M1:S1 ratio in the final product is 70–75:25–30. This fact significantly complicates the development of stable high-yield strains suitable for industrial application. In the previous work, authors obtained a mutant S. virginiae VKM Ac-2738D strain, characterized by a high productivity in flasks and the optimum M1:S1 ratio (75:25) in the final product. In this study, the scale-up of the virginiamycin production by VKM AC-2738D from shake flasks to a pilot-scale (100 L) stirred fermentor was carried out and the possibility of the in situ use of synthetic adsorbing resins to remove virginiamycin from culture broth was assessed. After the optimization of pH and dissolved oxygen concentration (6.8–7.0 and 50%, respectively), the fed-batch fermentation of VKM Ac-2738D with continuous addition of 50% sucrose solution (5 g/L/day starting from 48 h of fermentation) resulted in a final virginiamycin titer of 4.9 g/L. Among four tested resins, Diaion(®) HP21 added to fermentation medium prior to sterilization absorbed 98.5% of the total virginiamycin that simplifies its further recovery procedure and increased its total titer to 5.6 g/L at the M1:S1 ratio of 74:26. The developed technology has several important advantages, which include (1) the optimum M1:S1 ratio in the final product, (2) the possibility to use sucrose as a carbon source instead of traditionally used and more expensive glucose or d-maltose, and (3) selective binding of up to 98.5% of produced virginiamycin on the adsorbing resin. Springer Berlin Heidelberg 2016-11-12 2016-12 /pmc/articles/PMC5234532/ /pubmed/28330311 http://dx.doi.org/10.1007/s13205-016-0566-8 Text en © The Author(s) 2016 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.
spellingShingle Original Article
Dzhavakhiya, Vakhtang
Savushkin, Vyacheslav
Ovchinnikov, Alexander
Glagolev, Vladislav
Savelyeva, Veronika
Popova, Evgeniya
Novak, Nikita
Glagoleva, Elena
Scaling up a virginiamycin production by a high-yield Streptomyces virginiae VKM Ac-2738D strain using adsorbing resin addition and fed-batch fermentation under controlled conditions
title Scaling up a virginiamycin production by a high-yield Streptomyces virginiae VKM Ac-2738D strain using adsorbing resin addition and fed-batch fermentation under controlled conditions
title_full Scaling up a virginiamycin production by a high-yield Streptomyces virginiae VKM Ac-2738D strain using adsorbing resin addition and fed-batch fermentation under controlled conditions
title_fullStr Scaling up a virginiamycin production by a high-yield Streptomyces virginiae VKM Ac-2738D strain using adsorbing resin addition and fed-batch fermentation under controlled conditions
title_full_unstemmed Scaling up a virginiamycin production by a high-yield Streptomyces virginiae VKM Ac-2738D strain using adsorbing resin addition and fed-batch fermentation under controlled conditions
title_short Scaling up a virginiamycin production by a high-yield Streptomyces virginiae VKM Ac-2738D strain using adsorbing resin addition and fed-batch fermentation under controlled conditions
title_sort scaling up a virginiamycin production by a high-yield streptomyces virginiae vkm ac-2738d strain using adsorbing resin addition and fed-batch fermentation under controlled conditions
topic Original Article
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC5234532/
https://www.ncbi.nlm.nih.gov/pubmed/28330311
http://dx.doi.org/10.1007/s13205-016-0566-8
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