Development of fed-batch cultivation strategy for efficient oxytetracycline production by streptomyces rimosus at semi-industrial scale

Oxytetracycline (OTC) production by Streptomyces rimosus was studied in batch and fed-batch cultures in shake flask and bioreactor levels using semi-defined medium. First, the effect of glucose concentration on OTC production and growth kinetics was studied intensively. The optimal glucose concentra...

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Main Authors: Elsayed, Elsayed Ahmed, Omar, Hoda Gamal, El-Enshasy, Hesham Ali
Format: Article
Language:English
Published: Instituto de Tecnologia do Parana 2015
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Online Access:http://eprints.utm.my/id/eprint/58292/1/ElsayedAhmedElsayed2015_DevelopmentofFed-BatchCultivationStrategyforEfficientOxytetracycline.pdf
http://eprints.utm.my/id/eprint/58292/
http://dx.doi.org/10.1590/S1516-89132015050184
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spelling my.utm.582922021-12-15T07:57:29Z http://eprints.utm.my/id/eprint/58292/ Development of fed-batch cultivation strategy for efficient oxytetracycline production by streptomyces rimosus at semi-industrial scale Elsayed, Elsayed Ahmed Omar, Hoda Gamal El-Enshasy, Hesham Ali TP Chemical technology Oxytetracycline (OTC) production by Streptomyces rimosus was studied in batch and fed-batch cultures in shake flask and bioreactor levels using semi-defined medium. First, the effect of glucose concentration on OTC production and growth kinetics was studied intensively. The optimal glucose concentration in the medium was 15 g/L. Higher glucose concentrations supported higher biomass production by less volumetric and specific antibiotic production. Based on these data, cultivations were carried out at semi-industrial scale 15 L bioreactor in batch culture. At bioreactor level, cell growth and OTC production were higher compared to the shake flask culture by about 18 and 38%, respectively. During the bioreactor cultivation, glucose was totally consumed after only 48 h. Thus, the fed-batch experiment was designed for mono-glucose feeding and complete medium feeding to increase the OTC production by overcoming carbon limitations. The results showed that the fed-batch culture using constant glucose feeding strategy with rate of 0.33 g/L/h produced 1072 mg/L. On the other hand, feeding with complete medium resulted in 45% higher biomass but less OTC production by about 26% compared to mono-glucose fed culture. A further improvement in this process was achieved in by keeping the dissolved oxygen (DO) value at 60% saturation by cascading the glucose feeding pump with the DO controller. The later feeding strategy resulted in higher antibiotic production, reaching 1414 mg/L after 108 h. Instituto de Tecnologia do Parana 2015 Article PeerReviewed application/pdf en http://eprints.utm.my/id/eprint/58292/1/ElsayedAhmedElsayed2015_DevelopmentofFed-BatchCultivationStrategyforEfficientOxytetracycline.pdf Elsayed, Elsayed Ahmed and Omar, Hoda Gamal and El-Enshasy, Hesham Ali (2015) Development of fed-batch cultivation strategy for efficient oxytetracycline production by streptomyces rimosus at semi-industrial scale. Brazilian Archives of Biology and Technology, 58 (5). pp. 676-685. ISSN 1516-8913 http://dx.doi.org/10.1590/S1516-89132015050184 DOI:10.1590/S1516-89132015050184
institution Universiti Teknologi Malaysia
building UTM Library
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Teknologi Malaysia
content_source UTM Institutional Repository
url_provider http://eprints.utm.my/
language English
topic TP Chemical technology
spellingShingle TP Chemical technology
Elsayed, Elsayed Ahmed
Omar, Hoda Gamal
El-Enshasy, Hesham Ali
Development of fed-batch cultivation strategy for efficient oxytetracycline production by streptomyces rimosus at semi-industrial scale
description Oxytetracycline (OTC) production by Streptomyces rimosus was studied in batch and fed-batch cultures in shake flask and bioreactor levels using semi-defined medium. First, the effect of glucose concentration on OTC production and growth kinetics was studied intensively. The optimal glucose concentration in the medium was 15 g/L. Higher glucose concentrations supported higher biomass production by less volumetric and specific antibiotic production. Based on these data, cultivations were carried out at semi-industrial scale 15 L bioreactor in batch culture. At bioreactor level, cell growth and OTC production were higher compared to the shake flask culture by about 18 and 38%, respectively. During the bioreactor cultivation, glucose was totally consumed after only 48 h. Thus, the fed-batch experiment was designed for mono-glucose feeding and complete medium feeding to increase the OTC production by overcoming carbon limitations. The results showed that the fed-batch culture using constant glucose feeding strategy with rate of 0.33 g/L/h produced 1072 mg/L. On the other hand, feeding with complete medium resulted in 45% higher biomass but less OTC production by about 26% compared to mono-glucose fed culture. A further improvement in this process was achieved in by keeping the dissolved oxygen (DO) value at 60% saturation by cascading the glucose feeding pump with the DO controller. The later feeding strategy resulted in higher antibiotic production, reaching 1414 mg/L after 108 h.
format Article
author Elsayed, Elsayed Ahmed
Omar, Hoda Gamal
El-Enshasy, Hesham Ali
author_facet Elsayed, Elsayed Ahmed
Omar, Hoda Gamal
El-Enshasy, Hesham Ali
author_sort Elsayed, Elsayed Ahmed
title Development of fed-batch cultivation strategy for efficient oxytetracycline production by streptomyces rimosus at semi-industrial scale
title_short Development of fed-batch cultivation strategy for efficient oxytetracycline production by streptomyces rimosus at semi-industrial scale
title_full Development of fed-batch cultivation strategy for efficient oxytetracycline production by streptomyces rimosus at semi-industrial scale
title_fullStr Development of fed-batch cultivation strategy for efficient oxytetracycline production by streptomyces rimosus at semi-industrial scale
title_full_unstemmed Development of fed-batch cultivation strategy for efficient oxytetracycline production by streptomyces rimosus at semi-industrial scale
title_sort development of fed-batch cultivation strategy for efficient oxytetracycline production by streptomyces rimosus at semi-industrial scale
publisher Instituto de Tecnologia do Parana
publishDate 2015
url http://eprints.utm.my/id/eprint/58292/1/ElsayedAhmedElsayed2015_DevelopmentofFed-BatchCultivationStrategyforEfficientOxytetracycline.pdf
http://eprints.utm.my/id/eprint/58292/
http://dx.doi.org/10.1590/S1516-89132015050184
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score 13.214268