IP Library Granted Patent US 7,993,889
Granted Patent B1
US 7,993,889 · App. 12/018,216 · Granted Aug 9, 2011

Fermentive production of four carbon alcohols

View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 7,993,889
App. No.
12/018,216
Granted
Aug 9, 2011
Kind
B1
Abstract

Methods for the fermentative production of four carbon alcohols is provided. Specifically, butanol, preferably isobutanol is produced by the fermentative growth of a recombinant bacterium expressing an isobutanol biosynthetic pathway.

Claims (33)

1. A method for producing isobutanol comprising;

a. providing a fermentation media comprising carbon substrate; and

b. contacting said media with a recombinant yeast microorganism expressing an engineered isobutanol biosynthetic pathway wherein said pathway comprises the following substrate to product conversions;

i. pyruvate to acetolactate (pathway step a);

ii. acetolactate to 2,3-dihydroxyisovalerate (pathway step b);

iii. 2,3-dihydroxyisovalerate to α-ketoisovalerate (pathway step c);

iv. α-ketoisovalerate to isobutyraldehyde (pathway step d); and

v. isobutyraldehyde to isobutanol (pathway step e);

and wherein

a) the substrate to product conversion of step (i) is performed by an acetolactate synthase enzyme;

b) the substrate to product conversion of step (ii) is performed by an acetohydroxy acid isomeroreductase enzyme;

c) the substrate to product conversion of step (iii) is performed by an acetohydroxy acid dehydratase enzyme;

d) the substrate to product conversion of step (iv) is performed by a decarboxylase enzyme; and

e) the substrate to product conversion of step (v) is performed by an alcohol dehydrogenase enzyme;

whereby isobutanol is produced.

2. The method of claim 1 , wherein contacting said media with a recombinant microorganism is performed under anaerobic or microaerobic conditions.

3. The method of claim 1 , wherein contacting said media with a recombinant microorganism is performed as a batch fermentation.

4. The method of claim 1 , wherein the contacting said media with a recombinant microorganism is performed as a continuous fermentation.

5. The method of claim 1 , further comprising recovering the isobutanol from the fermentation media by distillation, liquid-liquid extraction, adsorption, decantation, pervaporation or combinations thereof.

6. The method of claim 1 , wherein the fermentation media further comprises water and wherein said isobutanol and water form a heterogeneous azeotrope.

7. The method of claim 6 , further comprising recovering the isobutanol from the azeotrope by distillation and decantation.

8. The method of claim 1 , wherein the microorganism produces isobutanol as a single product.

9. The method of claim 1 , wherein the fermentation media further comprises mixtures of carbon substrates.

10. The method of claim 1 , wherein the fermentation media further comprises unpurified carbon substrates.

11. The method of claim 1 , wherein the contacting said media with a recombinant microorganism is performed at a temperature range of about 25° C. to about 40° C.

12. The recombinant yeast microorganism of claim 1 wherein the said microorganism further comprises inactivated genes thereby reducing yield loss from competing pathways for carbon flow.

13. The recombinant yeast microorganism of claim 12 , wherein said inactivated genes reduce pyruvate decarboxylase activity.

14. The method of claim 1 , wherein one or more enzymes of said engineered isobutanol biosynthetic pathway uses NADH as an electron donor.

15. The method of claim 1 , wherein said alcohol dehydrogenase enzyme of step (e) is a native enzyme to the yeast microorganism.

16. The method of claim 1 , wherein steps (i)-(v) are performed by separate and distinct enzymes.

17. The method of claim 1 , wherein said isobutanol is produced in the fermentation media.

18. The method of claim 17 , wherein said isobutanol is produced in one or more of the following growth phases, high growth log phase, moderate through static lag phase, stationary phase, steady state growth phase, and combinations thereof.

19. The method of claim 17 , wherein the recombinant yeast microorganism is a whole cell catalyst subjected to conditions for isobutanol production.

Assignments (3)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 17, 2023
From: DONALDSON, GAIL K.; ELIOT, ANDREW C.; FLINT, DENNIS; MAGGIO-HALL, LORI ANN; NAGARAJAN, VASANTHA
To: E. I. DU PONT DE NEMOURS AND COMPANY
Reel/Frame 062400/0709 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 30, 2021
From: BUTAMAX ADVANCED BIOFUELS LLC
To: GEVO, INC.
Reel/Frame 057677/0477 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 12, 2010
From: E. I. DU PONT DE NEMOURS AND COMPANY
To: BUTAMAX ADVANCED BIOFUELS LLC
Reel/Frame 024216/0243 →