Fermentation process for the production of lipids
The invention provides methods and systems for the production of lipid products from a gaseous substrate using a two stage fermentation process. The method comprises providing a gaseous substrate comprising CO, CO 2 or H 2 or mixtures thereof, to a first bioreactor containing a culture or one or more microorganisms, and fermenting the substrate to produce acetate. The acetate from the first bioreactor is then provided to a second bioreactor, where it is used as a substrate for fermentation to lipids by one or more microalgae.
1. A method for producing at least one lipid product from a gaseous substrate, the method comprising:
i. receiving a gaseous substrate in a first bioreactor containing a culture of at least one microorganism in a liquid nutrient medium, and fermenting the gaseous substrate comprising CO and/or H 2 to produce acetate;
ii. passing at least a portion of the acetate product to a second bioreactor containing a culture of at least one microalgae in a liquid nutrient medium, and fermenting the acetate to produce at least one lipid product, wherein the microalgae is selected from the group consisting of Scenedesmus, Thraustochytrium, Japonochytrium, Aplanochytrium, Elina , and Labyrinthula;
iii obtaining a fermentation broth from the second bioreactor;
iv. passing the fermentation broth from the second bioreactor through an oxygen scrubber to remove oxygen; and
v. recycling at least a portion of the fermentation broth back to the first bioreactor.
2. The method of claim 1 , wherein the gaseous substrate further comprises CO 2 .
3. The method of claim 1 , wherein the production rate of acetate in the first bioreactor is at least 10 g/L/day.
4. The method of claim 1 , wherein the first bioreactor produces acetate and an alcohol, wherein the alcohol is selected from the group consisting of ethanol, butanol, methanol, propanol, and mixtures thereof.
5. The method of claim 1 , wherein the at least one microorganism in the first bioreactor is selected from the group consisting of Acetobacterium, Moorella, Clostridium, Pyrococcus, Eubacterium, Desulfobacterium, Carboxydothermus Acetogenium, Acetoanaerobium, Butyribacterium, Peptostreptococcus, Ruminococcus, Oxobacter , and Methanosarcina.
6. The method of claim 1 , wherein the at least one microalgae in the second bioreactor is Thraustochytrium.
7. The method of claim 1 , wherein the at least one lipid product produced in stage (ii) is used to produce at least one tertiary product selected from the group consisting of hydrogenation-derived renewable diesel (HDRD), fatty acid methyl esters (FAME), fatty acid ethyl esters (FAEE), and biodiesel.
8. The method of claim 1 , wherein lipid production is increased in the second bioreactor by limiting at least one nutrient in the liquid nutrient medium.
9. The method of claim 8 , wherein the limited nutrient is nitrogen.
10. The method of claim 1 , wherein the lipid product produced in stage (ii) is a polyunsaturated fatty acid.
11. The method of claim 10 , wherein the polyunsaturated fatty acid is an omega-3 fatty acid.
12. The method of claim 11 , wherein the omega-3 fatty acid is one or more of alpha-linolenic acid (ALA), eicosapentaenoic acid (EPA), and docosahexaenoic acid (DHA).
13. The method of claim 1 , wherein the first bioreactor is anaerobic.
14. The method of claim 1 , wherein the second bioreactor is aerobic.
15. The method of claim 1 , wherein the at least one microorganism in the first bioreactor comprises a Wood-Ljungdahl pathway.
16. The method of claim 1 , wherein the at least one microorganism in the first bioreactor is an acetogenic bacterium.
17. The method of claim 1 , wherein the microalgae is selected from the group consisting of Japonochytrium, Aplanochytrium, Elina, and Labyrinthula.
18. The method of claim 1 , wherein the liquid nutrient medium of the second bioreactor comprises nitrogen.
19. The method of claim 18 , wherein the liquid nutrient medium of the second bioreactor comprises an acetic acid to nitrogen ratio of at least 10:1.
20. The method of claim 18 , wherein the liquid nutrient medium of the second bioreactor comprises a carbon to nitrogen ratio of 49:1 or greater.