Bioprocess and microbe engineering for total carbon utilization in biofuel production
Some aspects of this invention provide methods and bioreactors for converting a carbon source into a lipid. In some embodiments, lipid production is carried out in an aerobic fermentor and carbon dioxide generated during lipid production is converted into a carbon substrate by CO 2 fixation in an anaerobic fermentor. In some embodiments, the carbon substrate generated by CO2 fixation is used as the carbon source for lipid production, thus achieving total carbon utilization in lipid production.
1. A method comprising
(a) culturing in a liquid medium a first organism in the presence of a carbon source under aerobic conditions suitable for the first organism to oxidize the carbon source, wherein the conditions are oxidizing conditions, wherein the first organism produces CO 2 as part of the oxidation process; and
(b) culturing in a liquid medium a second organism in the presence of CO 2 produced in (a) under anaerobic conditions suitable for the second organism to reduce the CO 2 , wherein the conditions are reducing conditions, wherein the second organism produces a carbon substrate as part of the reduction process;
wherein the culturing of (a) and of (b) is carried out in separate fermenters; and
wherein the carbon substrate produced in (b) is used as a carbon source by the organism of (a).
2. The method of claim 1 , further comprising contacting the first organism with an oxidizing agent, optionally wherein the oxidizing agent is O 2 .
3. The method of claim 1 , further comprising contacting the second organism with a reducing agent, optionally wherein the reducing agent is H 2 , CO, syngas, or H 2 S.
4. The method of claim 1 , further comprising providing electrons to the second organism of (b) by contacting the second organism of (b) with an electric current.
5. The method of claim 1 , wherein the carbon source is a carbohydrate, optionally glucose, fructose, ethanol, butyrate, butanol, acetate, acetic acid, biomass, cellulose, or hemicellulose.
6. The method of claim 1 , wherein the product of the carbon source oxidization process in (a) is a lipid, optionally an edible lipid, or a precursor thereof.
7. The method of claim 1 , wherein the carbon substrate produced in (b) is a biofuel or ethanol.
8. The method of claim 1 , wherein the organism of (a) is an oleaginous yeast, optionally Y. lipolytica.
9. The method of claim 1 , wherein the organism of (b) is an acetogenic bacterium , optionally a Clostridium sp. bacterium, C. acetobutylicum, C. ljungdahlii, C. carboxydivorans , or C. autoethanogenum, C. thermohydrosulfuricum, C. thermocellum , or C. thermoanaerofacter ethanoliticus.
10. The method of claim 1 , wherein the organism of (a) and/or (b) is genetically modified, optionally wherein the organism of (a) overexpresses a stearoyl-CoA desaturase gene.
11. A method of producing lipids comprising:
providing CO 2 to a first organism in an anaerobic fermentor, wherein the first organism converts the CO 2 to a carbon substrate;
removing the carbon substrate from the anaerobic fermentor; and
providing the carbon substrate to a second organism in an aerobic fermentor, wherein the second organism converts the carbon substrate to a lipid or a precursor thereof and CO 2 ;
wherein the anaerobic fermentor and the aerobic fermentor are separate fermentors.
12. The method of claim 11 , further comprising
removing the CO 2 from the aerobic fermentor; and
providing the CO 2 to the first organism in the anaerobic fermentor.
13. The method of claim 11 , wherein the first organism is a CO 2 -fixing bacterium , optionally a Clostridium sp. bacterium, C. acetobutylicum, C. ljungdahlii, C. carboxydivorans, C. autoethanogenum, C. thermohydrosulfuricum, C. thermocellum , or C. thermoanaerofacter ethanoliticus.
14. The method of claim 11 , wherein the second organism is an oleaginous yeast, optionally Y. lipolytica.
15. The method of claim 11 , wherein the first and/or second organisms are genetically modified.
16. The method of claim 11 , wherein the carbon substrate is ethanol, butyrate, butanol, acetate, or acetic acid.
17. The method of claim 11 , wherein the anaerobic fermentor comprises a reducing agent, optionally H 2 , CO, syngas, or H 2 S.
18. The method of claim 11 , further comprising providing electrons to the first organism by contacting the first organism with an electrical current, optionally wherein the electrical current is provided by at least one electrode.