首页> 外文期刊>Applied biochemistry and biotechnology, Part A. enzyme engineering and biotechnology >Continuous Production of Butanol by Clostridium acetobutylicum Immobilized in a Fibrous Bed Bioreactor
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Continuous Production of Butanol by Clostridium acetobutylicum Immobilized in a Fibrous Bed Bioreactor

机译:固定在纤维床生物反应器中的丙酮丁醇梭菌连续生产丁醇

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We explored the influence of dilution rate and pH in continuous cultures of Clostridium acetobutylicum.A 200-mL fibrous bed bioreactor was used to produce high cell density and butyrate concentrations at pH 5.4 and 35 deg C.By feeding glucose and butyrate as a cosubstrate,the fermentation was maintained in the solventogenesis phase,and the optimal butanol productivity of 4.6 g/(L h) and a yield of 0.42 g/g were obtained at a dilution rate of 0.9 h~(-1) and pH 4.3.Compared to the conventional acetone-butanol-ethanol fermentation,the new fermentation process greatly improved butanol yield,making butanol production from corn an attractive alternative to ethanol fermentation.
机译:我们探索了稀释速率和pH值对丙酮丁醇梭菌连续培养的影响.200 mL纤维床生物反应器用于在pH 5.4和35℃下产生高细胞密度和丁酸盐浓度。通过进料葡萄糖和丁酸盐作为共底物,发酵维持在溶剂生成阶段,在0.9 h〜(-1)的稀释度和pH 4.3的条件下,最佳丁醇产率为4.6 g /(L h),产率为0.42 g / g。传统的丙酮-丁醇-乙醇发酵,新的发酵工艺大大提高了丁醇的收率,使玉米生产丁醇成为乙醇发酵的诱人替代品。

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