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High-level Production of Ethanol during Fedbatch Ethanol Fermentation with a Controlled Aeration Rate and Non-sterile Glucose Powder Feeding of Saccharomyces cerevisiae
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  • High-level Production of Ethanol during Fedbatch Ethanol Fermentation with a Controlled Aeration Rate and Non-sterile Glucose Powder Feeding of Saccharomyces cerevisiae
  • High-level Production of Ethanol during Fedbatch Ethanol Fermentation with a Controlled Aeration Rate and Non-sterile Glucose Powder Feeding of Saccharomyces cerevisiae
저자명
Seo. Hyeon-Beom,Kim. Seung-Seop,Lee. Hyeon-Yong,Jung. Kyung-Hwan
간행물명
Biotechnology and bioprocess engineering
권/호정보
2009년|14권 5호|pp.591-598 (8 pages)
발행정보
한국생물공학회
파일정보
정기간행물|ENG|
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이 논문은 한국과학기술정보연구원과 논문 연계를 통해 무료로 제공되는 원문입니다.
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기타언어초록

In this study, we utilized a unique strategy for fed-batch fermentation using ethanol-tolerant Saccharomyces cerevisiae to achieve a high-level of ethanol production that could be practically applied on an industrial scale. During this study, the aeration rate was controlled at 0.0, 0.13, 0.33, and 0.8 vvm to determine the optimal aeration conditions for the production of ethanol. Additionally, non-sterile glucose powder was fed during fed-batch ethanol fermentation and corn-steep liquor (CSL) in the medium was used as an organic N-source. When aeration was conducted, the ethanol production and productivity were superior to that when aeration was not conducted. Specifically, the maximum ethanol production reached approximately 160 g/L, when the fermentor was aerated at 0.13 vvm. These findings indicate that the use of a much less expensive C-source may enable the fermentation process to be directed towards the improvement of overall ethanol production and productivity in fermentors that are aerated at 0.13 vvm. Furthermore, if a repeated fed-batch process in which the withdrawal and fill is conducted prior to 36 h can be employed, aeration at a rate of 0.33 and/or 0.8 vvm may improve the overall ethanol productivity.