Recovery of higher alcohols from dilute aqueous solutions
View Patent ↗This invention is directed to methods for recovery of C3-C6 alcohols from dilute aqueous solutions, such as fermentation broths. Such methods provide improved volumetric productivity for the fermentation and allows recovery of the alcohol. Such methods also allow for reduced energy use in the production and drying of spent fermentation broth due to increased effective concentration of the alcohol product by the simultaneous fermentation and recovery process which increases the quantity of alcohol produced and recovered per quantity of fermentation broth dried. Thus, the invention allows for production and recovery of C3-C6 alcohols at low capital and reduced operating costs.
1. A method for producing isobutanol comprising:
(a) culturing a microorganism capable of producing isobutanol in a fermentor, thereby forming a fermentation broth comprising microorganisms and isobutanol;
(b) removing a portion of the fermentation broth from the fermentor;
(c) distilling the portion, thereby forming an isobutanol-depleted liquid phase and an isobutanol-enriched vapor phase comprising water and isobutanol;
(d) condensing the isobutanol-enriched vapor phase formed in step (c), thereby forming an isobutanol-rich liquid phase and a water-rich liquid phase; and
(e) separating the isobutanol-rich phase liquid from the water-rich liquid phase using a liquid-liquid separator;
wherein:
(1) said steps (b)-(e) are conducted simultaneously with step (a);
(2) the isobutanol-depleted liquid phase comprises viable microorganisms; and
(3) the isobutanol-depleted liquid phase is returned to the fermentor.
2. The method of claim 1 , wherein the isobutanol-enriched vapor phase has an isobutanol concentration at least about 5-fold greater than the isobutanol concentration of the portion of the fermentation broth.
3. The method of claim 1 , wherein the isobutanol-enriched vapor phase has an isobutanol concentration at least about 10-fold greater than the isobutanol concentration of the portion of the fermentation broth.
4. The method of claim 1 , wherein the isobutanol-enriched vapor phase has an isobutanol concentration at least about 11-fold greater than the isobutanol concentration of the portion of the fermentation broth.
5. The method of claim 1 , wherein the isobutanol-enriched vapor phase has an isobutanol concentration at least about 12-fold greater than the isobutanol concentration of the portion of the fermentation broth.
6. The method of claim 1 , wherein the isobutanol-enriched vapor phase has an isobutanol concentration at least about 13-fold greater than the isobutanol concentration of the portion of the fermentation broth.
7. The method of claim 1 , wherein the isobutanol-enriched vapor phase has an isobutanol concentration at least about 14-fold greater than the isobutanol concentration of the portion of the fermentation broth.
8. The method of claim 1 , wherein the isobutanol-enriched vapor phase has an isobutanol concentration at least about 15-fold greater than the isobutanol concentration of the portion of the fermentation broth.
9. The method of claim 1 , wherein the isobutanol-rich liquid phase of step (d) has a ratio of isobutanol to water of greater than about 2.
10. The method of claim 1 , wherein the isobutanol-rich liquid phase of step (d) has a ratio of isobutanol to water of greater than about 8.
11. The method of claim 1 , wherein the ratio of isobutanol to water in the isobutanol-rich liquid phase is greater than the ratio of isobutanol to water in the fermentation broth by at least about 5-fold.
12. The method of claim 1 , wherein the ratio of isobutanol to water in the isobutanol-rich liquid phase is greater than the ratio of isobutanol to water in the fermentation broth by at least about 25-fold.
13. The method of claim 1 , further comprising cooling the isobutanol-rich liquid phase, thereby increasing the ratio of isobutanol to water in the isobutanol-rich liquid phase.
14. The method of claim 1 , wherein said distilling is carried out at a temperature ranging from about 20° C. to about 95° C.
15. The method of claim 1 , wherein said distilling is carried out at a temperature ranging from about 25° C. to about 95° C.
16. The method of claim 1 , wherein said distilling is carried out at a temperature ranging from about 35° C. to about 95° C.
17. The method of claim 1 , wherein said distilling is carried out at a reduced pressure compared to the pressure of the fermentor.
18. The method of claim 1 , wherein:
the distilling is carried out at a reduced pressure compared to the pressure of the fermentor, and at a temperature ranging from about 35° C. to about 95° C.;
the isobutanol-enriched vapor phase comprises an azeotrope of isobutanol and water;
the isobutanol-enriched vapor phase has an isobutanol concentration at least about 5-fold greater than the isobutanol concentration of the portion of the fermentation broth; and
the isobutanol-rich liquid phase has a ratio of isobutanol to water of greater than about 8.