(a) a water-immiscible solvent comprising greater than 50% by volume of a mixture of isomers of highly branched di-alkyl amines and less than about 1% by volume of mono-alkyl amines, said solvent having a coefficient of distribution greater than 10; and(b) at least 10% by volume of a non-alcoholic co-solvent having a boiling point lower than the boiling point of said solvent (a). Preferred water-immiscible solvent useful in the extraction of acetic acid from aqueous streams comprises about 91% by volume of a mixture of isomers of highly branched di-alkyl amines, about 0.2% by volume of mono-alkyl amines, and about 9% by volume tri-alkyl amines said solvent having a coefficient of distribution of greater than 10. An anaerobic microbial fermentation process for the production of acetic acid comprises the steps of:(a) fermenting in a bioreactor a gas stream comprising a least one gas selected from (1) carbon monoxide, (2) carbon dioxide and hydrogen, (3) carbon monoxide, carbon dioxide and hydrogen and (4) carbon monoxide and hydrogen in the presence of an aqueous stream comprising an anaerobic acetogenic bacteria in a nutrient medium, thereby producing a fermentation broth comprising acetic acid;(b) separating said bacteria from other components in said broth to provide a substantially cell-free stream;(c) continuously extracting acetic acid from said cell-free stream into a solvent phase by contacting said cell-free stream with a water-immiscible solvent/co-solvent mixture of the invention;(d) recycling said aqueous phase to said bioreactor and passing said solvent phase to a distillation column; and(e) continuously distilling from the product of (d) the acetic acid separately from the solvent phase under a temperature not exceeding 160°C; said extracting and distilling steps occurring without substantially degrading said amine to an amide, thus enhancing the efficiency of production of acetic acid."/> Solvent for extraction of acetic acid from aqueous streams and anaerobic microbial fermentation process for producing acetic acid
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Solvent for extraction of acetic acid from aqueous streams and anaerobic microbial fermentation process for producing acetic acid

机译:从水流中提取乙酸的溶剂和厌氧微生物发酵法生产乙酸

摘要

A water-immiscible solvent/co-solvent mixture which extracts acetic acid from aqueous streams comprises(a) a water-immiscible solvent comprising greater than 50% by volume of a mixture of isomers of highly branched di-alkyl amines and less than about 1% by volume of mono-alkyl amines, said solvent having a coefficient of distribution greater than 10; and(b) at least 10% by volume of a non-alcoholic co-solvent having a boiling point lower than the boiling point of said solvent (a). Preferred water-immiscible solvent useful in the extraction of acetic acid from aqueous streams comprises about 91% by volume of a mixture of isomers of highly branched di-alkyl amines, about 0.2% by volume of mono-alkyl amines, and about 9% by volume tri-alkyl amines said solvent having a coefficient of distribution of greater than 10. An anaerobic microbial fermentation process for the production of acetic acid comprises the steps of:(a) fermenting in a bioreactor a gas stream comprising a least one gas selected from (1) carbon monoxide, (2) carbon dioxide and hydrogen, (3) carbon monoxide, carbon dioxide and hydrogen and (4) carbon monoxide and hydrogen in the presence of an aqueous stream comprising an anaerobic acetogenic bacteria in a nutrient medium, thereby producing a fermentation broth comprising acetic acid;(b) separating said bacteria from other components in said broth to provide a substantially cell-free stream;(c) continuously extracting acetic acid from said cell-free stream into a solvent phase by contacting said cell-free stream with a water-immiscible solvent/co-solvent mixture of the invention;(d) recycling said aqueous phase to said bioreactor and passing said solvent phase to a distillation column; and(e) continuously distilling from the product of (d) the acetic acid separately from the solvent phase under a temperature not exceeding 160°C; said extracting and distilling steps occurring without substantially degrading said amine to an amide, thus enhancing the efficiency of production of acetic acid.
机译:一种与水不混溶的溶剂/助溶剂混合物,其从水流中提取乙酸,其包括 (a)与水不混溶的溶剂,该溶剂与高支链二烷基胺的异构体混合物组成,占体积的50%以上小于约1%(体积)的单烷基胺,所述溶剂的分布系数大于10。 (b)至少10体积%的沸点低于所述溶剂(a)的沸点的非醇类共溶剂。用于从水流中提取乙酸的优选的与水不混溶的溶剂包含约91体积%的高度支化的二烷基胺的异构体的混合物,约0.2体积%的单烷基胺和约9体积%的单烷基胺。体积的三烷基胺,所述溶剂的分布系数大于10。用于生产乙酸的厌氧微生物发酵工艺包括以下步骤: (a)在生物反应器中发酵一种气流,该气流包含至少一种选自以下的气体:(1)一氧化碳,(2)二氧化碳和氢气,(3)一氧化碳,二氧化碳和氢气以及( 4)在营养培养基中,在包含厌氧产乙酸细菌的水流的存在下,产生一氧化碳和氢气,从而产生包含乙酸的发酵液; (b)将所述细菌与所述细菌中的其他成分分离肉汤提供基本上无细胞的物流; (c)通过使所述无细胞物流与不与水混溶的溶剂/助溶剂混合物接触,将所述无细胞物流中的乙酸连续萃取到溶剂相中 (d)将所述水相再循环至所述生物反应器,并使所述溶剂相进入蒸馏塔; (e)在不超过160℃的温度下,从(d)的产物中与溶剂相分开连续蒸馏出乙酸。所述提取和蒸馏步骤的发生基本上没有将所述胺降解为酰胺,从而提高了乙酸的生产效率。

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