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丙酮和丁醇的原位萃取发酵

In situ extractive fermentation of acetone and butanol.

作者信息

Roffler S R, Blanch H W, Wilke C R

机构信息

Department of Chemical Engineering, University of California, Berkeley, California 94720.

出版信息

Biotechnol Bioeng. 1988 Feb 5;31(2):135-43. doi: 10.1002/bit.260310207.

Abstract

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

摘要

在分批补料培养过程中,通过不断从发酵液中去除丙酮和丁醇,提高了丙酮-丁醇发酵的生产率。含有丙酮丁醇梭菌活细胞的全发酵液被循环至Karr往复板式萃取柱,在该柱中,丙酮和丁醇被萃取到逆流通过该柱的油醇中。通过不断从发酵液中去除这些有毒代谢产物,减少了终产物抑制,并且以1.0 g/L·h的总丁醇生产率发酵了含有300 g/L葡萄糖的浓缩进料溶液,该生产率比正常分批发酵的生产率高70%。连续萃取过程提供了灵活的操作,并且适合工艺放大。

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