乙酰丁酸梭菌对丙酮-丁醇发酵的原位吸附强化

Xiaoping Yang , Gow-Jen Tsai , George T. Tsao
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引用次数: 90

摘要

开发了丙酮-丁醇分批发酵-原位脱毒一体化工艺。结果表明,以聚乙烯吡啶为吸附剂的原位吸附工艺提高了乙酰丁酸梭菌的发酵速率和反应器产率。在典型的传统丙酮-丁醇发酵过程中,批量操作模式下只能使用约60.0 g/L的葡萄糖,因此最多只能达到最终产物总浓度的21 g/L。在吸附耦合体系中,当吸附剂与发酵液的质量比为3/10时,初始葡萄糖浓度为94.0 g/L。该吸附间歇发酵体系的总产物浓度为29.8 g/L,产率为0.92 g/L·h。与传统间歇式控制丙酮-丁醇发酵相比,该工艺提高了最终产物浓度54%,生产效率提高了130%。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Enhancement of in situ adsorption on the acetone-butanol fermentation by Clostridium acetobutylicum

An integrated process of the acetone-butanol batch fermentation coupled with in situ toxic products removal was developed. It was found that the in situ adsorption process using polyvinylpyridine as the adsorbent enhanced the fermentation rates and the reactor productivity by Clostridium acetobutylicum. In a typical traditional acetone-butanol fermentation process, only about 60.0 g/L of glucose could be used in a batch operation mode and thus at maximum only 21 g/L of the total final products concentration could be achieved. In the adsorption-coupled system, an initial glucose concentration of 94.0 g/L was fermented when a weight ratio of the adsorbent to the fermentation broth of 3/10 was used. An overall product concentration of 29.8 g/L and a productivity of 0.92 g/L · h were achieved in the adsorptive batch fermentation system. Compared with the controlled traditional batch acetone-butanol fermentation, the integrated process increased the final product concentration by 54% and the productivity by 130%.

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