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A modified water-immiscible solvent useful in the extraction of acetic acid from aqueous streams is a substantially pure mixture of isomers of highly branched di-alkyl amines. Solvent mixtures formed of such a modified solvent with a desired co-solvent, preferably a low boiling hydrocarbon, are usef

A modified water-immiscible solvent useful in the extraction of acetic acid from aqueous streams is a substantially pure mixture of isomers of highly branched di-alkyl amines. Solvent mixtures formed of such a modified solvent with a desired co-solvent, preferably a low boiling hydrocarbon, are useful in the extraction of acetic acid from aqueous gaseous streams. An anaerobic microbial fermentation process for the production of acetic acid employs such solvents, under conditions which limit amide formation by the solvent and thus increase the efficiency of acetic acid recovery. Methods for the direct extraction of acetic acid and the extractive fermentation of acetic acid also employ the modified solvents and increase efficiency of acetic acid production. Such increases in efficiency are also obtained where the energy source for the microbial fermentation contains carbon dioxide and the method includes a carbon dioxide stripping step prior to extraction of acetic acid in solvent.

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1. An anaerobic microbial fermentation process for the production of acetic acid, said process comprising the steps of:(a) fermenting in a bioreactor at least one gas selected from the group consisting of (1) carbon monoxide, (2) carbon dioxide and hydrogen, (3) carbon monoxide, carbon dioxide, and

1. An anaerobic microbial fermentation process for the production of acetic acid, said process comprising the steps of:(a) fermenting in a bioreactor at least one gas selected from the group consisting of (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 a nutrient mixture with an anaerobic acetogenic bacteria, thereby producing a fermentation broth comprising acetic acid and dissolved hydrogen sulfide;(b) removing said hydrogen sulfide from said fermentation broth;(c) contacting said fermentation broth with a solvent comprising an amine for a time sufficient to cause the formation of a solvent phase containing acetic acid, said solvent and water and an aqueous phase;(d) continuously distilling acetic acid from said solvent phase; and(e) recycling said solvent to said contacting step (b). 2. The process according to claim 1, wherein said removing step comprises contacting said fermentation broth with a gas which does not contain carbon dioxide, oxygen or hydrogen sulfide. 3. The process according to claim 2 wherein said gas is selected from the group consisting of nitrogen, methane, helium, carbon monoxide, argon, hydrogen, a non-reactive gas, and a mixture thereof. 4. The process according to claim 2, wherein said removing step occurs in a countercurrent stripper column. 5. The process according to claim 1, wherein said removing step comprises reducing the pressure on said fermentation broth in a container separate from said bioreactor. 6. The process according to claim 1 further comprising separating said bacteria from other components in said broth to provide a substantially cell-free stream. 7. The process according to claim 1, wherein said removing step comprises heating said cell-free stream to about 80° C. in a container separate from said bioreactor. 8. An anaerobic microbial fermentation process for the production of acetic acid, said process comprising the steps of:(a) fermenting in a bioreactor at least one gas selected from the group consisting of (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 a nutrient mixture with an anaerobic acetogenic bacteria, thereby producing a fermentation broth comprising acetic acid:(b) contacting said fermentation broth with a solvent for a time sufficient to cause the formation of a solvent phase containing acetic acid, said solvent and water and an aqueous phase, wherein said solvent comprises:(i) a water immiscible solvent comprising greater than 50% by volume of a mixture of isomers of highly branched di-alkyl amines, and from about 0.01% to 20% by volume of mono-alkyl amines, said solvent having a coefficient of distribution greater than 10; and(ii) at least 10% by volume of a non-alcohol co-solvent having a boiling point lower than the boiling point of said solvent (i),wherein said mixture extracts acetic acid from aqueous streams;(c) continuously distilling acetic acid from said solvent phase; and(d) recycling said solvent to said contacting step (b). 9. The process according to claim 8, wherein said distilling step occurs at a temperature less than about 160° C., without substantially degrading said amine to an amide, thus enhancing the efficiency of production of acetic acid. 10. The process according to claim 6, further comprising recycling said separated bacteria into said bioreactor. 11. The process according to claim 1, wherein said anaerobic bacteria is selected from the group consisting of Acetobacterium kivui, A. woodii, Butyribacterium methylotrophicum, Clostridium aceticum, C. acetobutylicum, C. formicaceticum, C. kluyveri, C. thermoaceticum, C. thermocellum, C. thermohydrosulfuricum, C. thermosaccharolyticum, Eubacterium limosum, Peptostreptococcus productus, C. ljungdahlii, and mixtures thereof. 12. The process according to claim 11, wherein said C. ljungdahlii is selected from the group consisting of: PETC ATCC 5538, O-52 ATCC 55989, ERI2 ATCC 55380, C-01 ATCC 55988, and mixtures thereof. 13. The process according to claim 1, wherein said contact with solvent occurs in a countercurrent column. 14. An anaerobic microbial fermentation process for the production of acetic acid, said process comprising the steps of:(a) fermenting in a bioreactor at least one gas selected from the group consisting of (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 a nutrient mixture with an anaerobic acetogenic bacteria, thereby producing a fermentation broth comprising acetic acid and dissolved carbon dioxide;(b) removing said carbon dioxide from said fermentation broth;(c) contacting said broth of (b) with a solvent comprising an amine for a time sufficient to cause the formation of a solvent phase containing acetic acid, said solvent and water and an aqueous phase;(d) continuously distilling acetic acid from said solvent phase; and(e) recycling said solvent to said contacting step (c). 15. An anaerobic microbial fermentation process for the production of acetic acid, said process comprising the steps of:(a) fermenting in a bioreactor at least one gas selected from the group consisting of (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 a nutrient mixture with an anaerobic acetogenic bacteria, thereby producing a fermentation broth comprising acetic acid;(b) contacting said broth of (a) with a solvent for a time sufficient to cause the formation of a solvent phase containing acetic acid, said solvent and water and an aqueous phase, wherein said solvent comprises:(i) a water immiscible solvent comprising greater than 50% by volume of a mixture of isomers of highly branched di-alkyl amines, and from about 0.01% to 20% by volume of mono-alkyl amines, said solvent having a coefficient of distribution greater than 10; and(ii) at least 10% by volume of a linear hydrocarbon co-solvent having a boiling point lower than the boiling point of said solvent (i),wherein said mixture extracts acetic acid from aqueous streams;(c) continuously distilling acetic acid from said solvent phase; and(d) recycling said solvent to said contacting step (b). 16. The process according to claim 1, wherein said bacteria is Clostridium. 17. The process according to claim 1, wherein said aqueous phase is recycled to said bioreactor. 18. The process according to claim 8, wherein said bacteria is Clostridium. 19. The process according to claim 14, wherein said bacteria is Clostridium. 20. The process according to claim 15, wherein said bacteria is Clostridium. 21. The process according to claim 8, wherein said aqueous phase is recycled to said bioreactor. 22. The process according to claim 14, wherein said aqueous phase is recycled to said bioreactor. 23. The process according to claim 15, wherein said aqueous phase is recycled to said bioreactor.