Microbial alcohol production process
View Patent ↗The invention relates to the production of alcohols by microbial fermentation, particularly to production of alcohols by microbial fermentation of substrates comprising CO. It more particularly relates to processes for the production of alcohols from their corresponding acids in the presence of a substrate comprising CO. In particular embodiments, a fermentation reaction producing acid(s) and optionally alcohol(s) is perturbed such that at least a portion one or more of acid(s) is converted to alcohol.
1. A method for converting acid(s) to corresponding alcohol(s) using a microbial culture in the presence of a substrate comprising CO or CO and H 2 , said method comprising:
(a) culturing, in a bioreactor, one or more strains of carboxydotrophic bacteria in the presence of said substrate to produce one or more acids and optionally one or more alcohols; and
(b) perturbing the microbial culture, such that at least a portion of the microbial culture is switched from a substantially production phase to a substantially conversion phase, whereby at least a portion of at least one of the one or more of said acids is converted to its corresponding alcohol; and
(c) recovering at least a portion of the alcohol(s).
2. The method of claim 1 , wherein the concentration of H 2 in the substrate is less than 40% by volume.
3. The method of claim 2 , wherein the concentration of H 2 in the substrate is less than 5% by volume.
4. The method of claim 1 , wherein the bacteria are selected from the group consisting of Clostridium, Moorella, Pyrococcus, Eubacterium, Desulfobacterium, Carboxvdothermus, Acetogenium, Acetobacterium, Acetoanaerobium, Butyribacterium and Peptostreptococcus.
5. The method of claim 1 , wherein the carboxydotrophic bacteria has all the defining features of Clostridium autoethanogenum strain deposited at the German Resource Centre for Biological Material (DSMZ) under the identifying deposit number DSMZ 10061.
6. The method of claim 1 , wherein the one or more acids of step (a) are produced continuously, and, the one or more acids are continuously converted to the corresponding alcohol in step (b).
7. The method of claim 1 , wherein said one or more alcohols are produced in step (a) and a substantially greater amount of acid is produced in step (a) relative to the quantity of alcohol produced in step (a).
8. The method of claim 1 , wherein the acid produced in step (a) is acetate and the corresponding alcohol is ethanol.
9. The method of claim 1 , further comprising adding an acid to the bioreactor during step (a) and/or step (b) and converting said added acid to its corresponding alcohol.
10. The method of claim 1 , wherein the acid(s) in steps (a) or (b) are mono or di-carboxylic acids.
11. The method of claim 1 , wherein the perturbing step is carried out by one or more of:
i. adjusting the pH of a liquid nutrient medium containing the microbial culture;
ii. adjusting the open redox potential of a liquid nutrient medium containing the microbial culture;
iii. adding a second acid to the bioreactor;
iv. adding one or more reducing agents to the bioreactor;
v. adjusting the CO concentration in a liquid nutrient medium containing the microbial culture;
vi. adjusting the CO partial pressure in the bioreactor.
12. The method of claim 1 , further comprising carrying out step (a) in a first bioreactor and step (b) in a second bioreactor.
13. The method of claim 1 , wherein the substrate comprising CO comprises at least 15% to about 100% CO by volume.
14. The method of claim 11 , wherein the perturbing step comprises the addition of a second acid and the acid is selected from the group consisting of formate, acetate and mixtures thereof.
15. The method of claim 11 , wherein the perturbing step comprises the addition of a reducing agent and the reducing agent is selected from the group consisting of sodium dithionite, cysteine sodium sulphide and mixtures thereof.
16. The method of claim 11 , wherein the perturbing step comprises adjusting the CO concentration by increasing the CO concentration in the liquid nutrient medium by at least 1 mmol.
17. The method of claim 11 , wherein the perturbing step comprises adjusting the CO partial pressure by increasing the partial pressure by at least 15 psi.
18. The method of claim 11 , wherein the perturbing step comprises adjusting the CO partial pressure by increasing the partial pressure above a sufficient threshold pressure of at least 37 psia.