Hesham A El-Enshasy, Usama I Beshay, Ahmed I El-Diwany, Hoda M Omar, Abdel Ghany E El-Kholy, Rabab El-Najar
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引用次数: 0
摘要
研究了以葡萄糖为主要c源的地中海支霉分批培养和补料分批培养生产利福霉素B和SV的方法。使用葡萄糖作为单一喂养底物的间歇培养,无论是在摇瓶中以脉冲添加的形式,还是在生物反应器水平上以恒定的进料速率,都被证明是一种可替代的生产系统,在体积和特异性抗生素生产方面都有显着增加。在非限氧条件下,利福霉素B和SV的最大浓度分别为1146 mg/l和2500 mg/l。另一方面,利福霉素B的产率从传统摇瓶分批培养提高到搅拌槽生物反应器补料分批培养,利福霉素SV的产率从9.47提高到31.83 mg/l x h,利福霉素B的产率从6.58提高到12.13 mg/l x h。
Improvement of rifemycins production by Amycolatopsis mediterranei in batch and fed-batch cultures.
The production of rifamycins B and SV using glucose as main C-source by Amycolatopsis mediterranei in batch and fed-batch culture was investigated. Fed-batch culture using glucose as mono feeding substrate either in the form of pulse addition, in case of shake flask, or with constant feeding rate, in bioreactor level, proved to be an alternative production system with a significant increase in both volumetric and specific antibiotic production. The maximal concentrations of about 1146 mg/l and 2500 mg/l of rifamycins B and SV, respectively, was obtained in fed-batch culture in bioreactor level under non-oxygen limitation. On the other hand, the rate of rifamycins production was increased from 6.58 to 12.13 mg/l x h for rifamycin B and from 9.47 to 31.83 mg/l x h for rifamycin SV on the bioprocess transfer and improvement from the conventional batch cultivation in shake flask to fed-batch cultivation in stirred tank bioreactor.