Controlling metabolism by substrate cofeeding
The disclosure provides methods using mixed substrate cofeeding for bioproduct synthesis, which enables faster, more efficient, and higher yield carbon conversion in various organisms.
1. A method for converting carbon dioxide into organic compounds, comprising:
culturing non-photosynthetic autotrophic cells in a culture vessel containing a fermentation medium comprising:
a controlled, limiting amount of a first preferentially utilized carbon substrate,
a controlled amount of carbon dioxide (CO 2 ), and
a controlled amount of diatomic hydrogen (H 2 ),
wherein the controlled, limiting amount of the first preferentially utilized carbon substrate is added to the culture vessel at a rate such that the culture vessel maintains a concentration of the first preferentially utilized carbon substrate such that the CO 2 , which is not preferentially utilized by the cells, provides more than 50% of carbon in organic compounds produced by the cells, optionally wherein the non-photosynthetic autotrophic cells are acetogenic cells; and
wherein the limiting amount of the first preferentially utilized carbon substrate is an amount that provides less than 25% of the quantity of electrons in the culture.
2. The method of claim 1 , wherein the first preferentially utilized carbon substrate comprises one or more sugars.
3. The method of claim 1 , wherein the limiting amount of the first preferentially utilized carbon substrate is an amount that provides less than about 20%, less than about 15%, less than about 10%, less than about 5%, less than about 2%, or less than about 1% of the quantity of electrons in the culture.
4. The method of claim 1 , wherein the quantity of electrons provided by H 2 is at least about 75%, at least about 80%, at least about 85%, at least about 90%, at least about 95%, at least about 98%, or at least about 99% of the quantity of electrons in the culture.
5. The method of claim 1 , wherein the acetogenic cells comprise Moorella thermoacetica, Clostridium ljungdahlii , or Acetobacterium woodii.
6. The method of claim 1 , wherein the controlled, limiting amount of the first preferentially utilized carbon substrate is added to the culture vessel at a rate such that the culture vessel maintains a concentration of the first preferentially utilized carbon substrate such that catabolite repression is not induced.
7. A method for converting carbon dioxide into lipids comprising:
(a) culturing non-photosynthetic autotrophic cells according to the method of claim 1 to produce acetate, and
(b) culturing oleaginous cells in a culture vessel containing a fermentation medium comprising: a controlled, limiting amount of a second preferentially utilized carbon substrate, and the acetate produced in (a) to produce lipids, wherein the second preferentially utilized carbon substrate is added to the culture vessel at a rate such that the culture vessel maintains a concentration of the second preferentially utilized carbon substrate such that the acetate, which is not preferentially utilized by the cells, provides the majority of carbon for organic compounds produced by the cells, optionally wherein the oleaginous cells are oleaginous yeast cells;
wherein the second preferentially utilized carbon substrate of (b) provides NADPH and/or another cofactor with reducing capabilities to the cells of (b), optionally wherein the cofactor with reducing capabilities is a ferredoxin, NADH, and/or FADH2; and/or
wherein the second preferentially utilized carbon substrate of (b) provides ATP and/or another cofactor with high-energy phosphate bond(s) to the cells of (b), optionally wherein the cofactor with high-energy phosphate bond(s) is GTP and/or pyrophosphate.
8. The method of claim 7 , wherein the oleaginous cells overexpress a kinase that phosphorylates the second preferentially utilized carbon substrate.
9. The method of claim 7 , wherein the amount of the second preferentially utilized carbon substrate is sufficient to generate reduced nicotinamide adenine dinucleotide phosphate (NADPH) through the oxidative pentose phosphate pathway (oxPPP) and convert acetyl-CoA into lipids, but is insufficient to be incorporated into the lipids as a major component.
10. The method of claim 7 , wherein the initial supplied concentration of acetate is at least 34 grams per liter.
11. The method of claim 7 , wherein the second preferentially utilized carbon substrate is one or more of gluconate, glycerol, and/or a hexose, optionally glucose or fructose.
12. The method of claim 7 , wherein the acetate provides acetyl-CoA and ATP necessary for converting acetyl-CoA into lipids.
13. The method of claim 7 , wherein the controlled, limiting amount of the second preferentially utilized carbon substrate is added to the culture vessel at a rate such that the culture vessel maintains a concentration of the second preferentially utilized carbon substrate such that catabolite repression is not induced.
14. A method of producing bioproducts comprising
(a) culturing non-photosynthetic autotrophic cells according to the method of claim 1 to produce acetate, and
(b) culturing cells that utilize acetate to produce bioproducts in a culture vessel containing a fermentation medium comprising: a controlled, limiting amount of a second preferentially utilized carbon substrate utilized by the cells that utilize acetate, and the acetate produced in (a) to produce the bioproducts, wherein the second preferentially utilized carbon substrate utilized by the cells that utilize acetate is added to the culture vessel at a rate such that the culture vessel maintains a concentration of the second preferentially utilized carbon substrate utilized by the cells that utilize acetate such that the acetate, which is not preferentially utilized by the cells, provides the majority of carbon for organic compounds produced by the cells;
wherein the second preferentially utilized carbon substrate of (b) provides NADPH and/or another cofactor with reducing capabilities to the cells, optionally wherein the cofactor with reducing capabilities is a ferredoxin, NADH, and/or FADH2; and/or
wherein the second preferentially utilized carbon substrate of (b) provides ATP and/or another cofactor with high-energy phosphate bond(s) to the cells, optionally wherein the cofactor with high-energy phosphate bond(s) is GTP and/or pyrophosphate.
15. The method of claim 14 , wherein the bioproducts are oleochemicals, polyketides, or mevalonate pathway derived natural products.
16. The method of claim 15 , wherein the mevalonate pathway derived natural products are terpenoids or derivatives thereof.
17. The method of claim 14 , wherein the second preferentially utilized carbon substrate is one or more of gluconate, glycerol, and/or a hexose, optionally glucose or fructose.
18. The method of claim 14 , wherein the controlled, limiting amount of the second preferentially utilized carbon substrate is added to the culture vessel at a rate such that the culture vessel maintains a concentration of the second preferentially utilized carbon substrate such that catabolite repression is not induced.