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抗霉素A发酵。II. 在通气搅拌发酵罐中的发酵

Antimycin A fermentation. II. Fermentation in aerated-agitated fermenters.

作者信息

Sehgal S N, Saucier R, Vézina C

出版信息

J Antibiot (Tokyo). 1976 Mar;29(3):265-74. doi: 10.7164/antibiotics.29.265.

Abstract

Fermentation characteristics, previously studied in shake flasks, were reproduced in aerated-agitated fermenters, using three strains of Streptomyces sp. which had been selected for their high antimycin A productivity in shake flasks. Fermentation in fermenters was run in three stages. The medium consisted of soy flour, glucose, ammonium sulfate and calcium carbonate; initial pH was 7.2 approximately 7.5, and temperature 25 degrees C. The course of fermentation was then modified to encourage maximal growth and eliminate the intermediate lag period observed in shake flasks. Useful corrections included continuous addition of soybean oil at 1.25 %/day and maintenance of pH at 6 by addition of ammonium hydroxide on demand. The ammonium hydroxide added also served as a rapidly utilized nitrogen source and could not be replace by NaOH or KOH. Under optimal conditions antimycin A was produced at constant rate from the second to the sixth day, when maximum yields of more than 9 g/liter were attained. A procedure for antimycin A extraction is described.

摘要

在摇瓶中预先研究过的发酵特性,在通气搅拌发酵罐中得以重现,使用的是三株链霉菌属菌株,这些菌株是因其在摇瓶中具有高抗霉素A产量而被挑选出来的。发酵罐中的发酵分三个阶段进行。培养基由大豆粉、葡萄糖、硫酸铵和碳酸钙组成;初始pH约为7.2至7.5,温度为25摄氏度。随后对发酵过程进行了改进,以促进最大生长并消除在摇瓶中观察到的中间延迟期。有用的改进措施包括每天以1.25%的比例连续添加大豆油,并根据需要添加氢氧化铵将pH维持在6。添加的氢氧化铵还用作快速利用的氮源,不能用氢氧化钠或氢氧化钾替代。在最佳条件下,从第二天到第六天抗霉素A以恒定速率产生,此时可获得超过9克/升的最大产量。文中描述了抗霉素A的提取方法。

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