作者: S. R. Roffler , H. W. Blanch , C. R. Wilke
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摘要: The productivity of the acetone-butanol fermentation was increased by continuously removing acetone and butanol from broth during fed-batch culture. Whole containing viable cells Clostridium acetobutylicum cycled to a Karr reciprocating plate extraction column in which were extracted into oleyl alcohol flowing counter-currently through column. By these toxic metabolites broth, end product inhibition reduced, concentrated feed solution 300 g/L glucose fermented at an overall 1.0 h, 70% higher than normal batch fermentation. continuous process provides flexible operation lends itself scale-up.