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›› 2010, Vol. 10 ›› Issue (4): 767-771.

• 生化工程专栏 • 上一篇    下一篇

酿酒酵母转化生成2-苯乙醇分批补料工艺优化

王航 董清风 孟春 石贤爱 郭养浩   

  1. 福州大学生物科学与工程学院 福州大学生物科学与工程学院 福州大学生物科学与工程学院 福州大学生物科学与工程学院 福州大学生物科学与工程学院
  • 收稿日期:2010-03-16 修回日期:2010-06-13 出版日期:2010-08-20 发布日期:2010-08-20
  • 通讯作者: 郭养浩

Optimization and Kinetics of the Fed-batch Bioconversion from L-phenylalanine to 2-Phenylethanol via Saccharomyces cerevisiae

WANG Hang DONG Qing-feng, MENG Chun SHI Xian-ai GUO Yang-hao   

  1. College of biological science and technology, Fuzhou University College of biological science and technology, Fuzhou University College of biological science and technologe , Fuzhou University College of biological science and technologe , Fuzhou University College of biological science and technologe , Fuzhou University
  • Received:2010-03-16 Revised:2010-06-13 Online:2010-08-20 Published:2010-08-20
  • Contact: GUO Yang-hao

摘要: 对酿酒酵母转化生成2-苯乙醇过程的碳氮源进行优化,选择葡萄糖为碳源,1 g/L脲为氮源,8 g/L L-苯丙氨酸为前体,以呼吸商达1.1±0.1为补糖控制依据,在5 L发酵罐水平建立分批补料工艺,2-苯乙醇终浓度达4.39 g/L,生成速率达0.314 g/(L×h),L-苯丙氨酸摩尔转化率为0.8,L-苯丙氨酸残留浓度仅为0.634 g/L.

关键词: 2-苯乙醇, 酿酒酵母, 呼吸商, 分批补料培养, 优化

Abstract: The carbon and nitrogen sources during the bioconversion from L-phenylalanine to 2-phenylethanol via Saccharomyces cerevisiae were optimized. In a 5-L fermentor, final 2-phenylethanol concentration of 4.39 g/L, space-time yield of 0.314 g/(L×h), molar yield of 0.8 and residual L-phenylalanine concentration of 0.634 g/L were achieved when respiratory quotient was controlled at 1.1±0.1 by feeding glucose, and 1 g/L urea and 8 g/L L-phenylalanine were selected as nitrogen source and precursor respectively.

Key words: 2-phenylethanol, Saccharomyces cerevisiae, respiratory quotient, fed-batch culture, optimization

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