IP Library Granted Patent US 9,701,987
Granted Patent B2
US 9,701,987 · App. 14/283,287 · Granted Jul 11, 2017

Fermentation process for the production and control of pyruvate-derived products

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Quick Facts
Patent No.
US 9,701,987
App. No.
14/283,287
Granted
Jul 11, 2017
Kind
B2
Abstract

A process for producing and controlling pyruvate derived products during the fermentation of a CO containing substrate by an acetogenic carboxydotrophic microorganism has been developed. The process involves increasing the concentration of at least one nutrient selected from the group consisting of vitamin B1, vitamin B5, vitamin B7 and mixtures thereof above the cellular requirement of the microorganism. When the concentration is increased, the production of 2,3-butanediol (2,3-BDO) increases whereas the production of the other metabolites is virtually unchanged. The effect is reversible so that when the concentration is decreased, the production of 2,3-BDO is also decreased. This allows one to control the ratio of ethanol:2,3-BDO to a desired value which can vary from about 4:1 to about 1:2.

Claims (17)

1. A method for the production of at least one product by microbial fermentation, the method comprising:

providing a gaseous substrate comprising at least one of CO, CO 2 , or CO 2 plus H 2 to a bioreactor comprising a culture of at least one acetogenic carboxydotrophic microorganism in a liquid nutrient medium to produce at least one product selected from the group consisting of ethanol, 2,3-butanediol, lactate, succinate, methyl ethyl ketone, 2-butanol, isopropanol, propanediol, and acetoin, the process characterized in that the concentration of at least one nutrient selected from the group consisting of vitamin B1, vitamin B5, and vitamin B7; wherein the concentration of vitamins B5 and B7 is maintained at about 100 to about 4000 μg/g biomass and the concentration of B1 is maintained from about 20 to about 500 μg/g biomass from about.

2. The method of claim 1 where the products are ethanol and 2,3-butanediol.

3. The method of claim 2 , wherein the production of 2,3-butanediol is at least 10 g/L per day.

4. The method of claim 2 , wherein the production of 2,3-butanediol is at least 20 g/L per day.

5. The method of claim 2 where the ratio of ethanol: 2 , 3 -butanediol varies from about 4:1 to about 1:1.

6. The method of claim 1 , wherein the at least one acetogenic carboxydotrophic microorganism is selected from the group consisting of Clostridium, and Acetobacterium.

7. The method of claim 1 , wherein the at least one acetogenic carboxydotrophic microorganism is selected from the group consisting of Clostridium autoethanogenum, Clostridium ljungdahli, Clostridium carboxidivorans, Clostridium drakei, Clostridium coskatii, Clostridium ragsdalei , and Acetobacterium woodii.

8. The method of claim 1 where the concentration of vitamin B5 in the liquid nutrient medium varies from about 200 to about 4000 μg/g biomass.

9. The method of claim 1 where the concentration of vitamin B5 in the liquid nutrient medium varies from about 200 to about 3000 μg/g biomass.

10. A method for the production of ethanol and 2,3-butanediol by a microbial fermentation, the method comprising:

providing a gaseous substrate comprising at least one of CO, CO 2 , or CO 2 plus H2 to a bioreactor comprising a culture of Clostridium autoethanogenum in a liquid nutrient medium to produce at least 2,3-butanediol and ethanol; the process characterized in that the concentration of vitamin B5, is maintained at a concentration from about 2 to about 80 times above a concentration of about 198 μg B5/g-biomass.

11. The method of claim 10 where the ratio of ethanol: 2,3-butanediol varies from about 4:1 to 1:1.

12. A method for the production of ethanol and 2,3-butanediol by a microbial fermentation, the method comprising:

providing a gaseous substrate comprising at least one of CO, CO 2 , or CO 2 plus H2 to a bioreactor comprising a culture of Clostridium autoethanogenum in a liquid nutrient medium to produce at least 2,3-butanediol and ethanol; the process characterized in that the concentration of vitamin B5, is maintained at a concentration from about 200 to about 4000 μg/g biomass.

13. The method of claim 12 where the ratio of ethanol: 2,3-butanediol varies from about 4:1 to about 1:1.

14. The method of claim 12 where the concentration of vitamin B5 in the liquid nutrient medium varies from about 200 to about 3000 μg/g biomass.

Assignments (9)
CORRECTIVE ASSIGNMENT TO CORRECT THE THE PATENT NUMBE 9,5348,20 PREVIOUSLY RECORDED AT REEL: 059911 FRAME: 0400. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Recorded Aug 4, 2022
From: LANZATECH NEW ZEALAND LIMITED
To: LANZATECH NZ INC.
Reel/Frame 061084/0646 →
CORRECTIVE ASSIGNMENT TO CORRECT THE U.S. PATENT NUMBER 8,979,228 PREVIOUSLY RECORDED AT REEL: 059911 FRAME: 0400. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Recorded Aug 3, 2022
From: LANZATECH NEW ZEALAND LIMITED
To: LANZATECH NZ, INC.
Reel/Frame 061058/0076 →
CORRECTIVE ASSIGNMENT TO CORRECT THE THE APPPLICATION 13467969 PREVIOUSLY RECORDED AT REEL: 042051 FRAME: 0377. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Recorded Aug 2, 2022
From: VENTURE LENDING & LEASING VI, INC.
To: LANZATECH NEW ZEALAND; LANZATECH, INC.; LANZATECH FREEDOM PINES BIOREFINERY LLC; LANZATECH HONG KONG LIMITED; LANZATECH PRIVATE LIMITED
Reel/Frame 061053/0481 →
RELEASE OF SECURITY INTEREST Recorded May 9, 2022
From: VENTURE LENDING & LEASING VII, INC.; VENTURE LENDING & LEASING VIII, INC.
To: LANZATECH NEW ZEALAND LIMITED; LANZATECH, INC.; LANZATECH FREEDOM PINES BIOREFINERY LLC; LANZATECH HONG KONG LIMITED; LANZATECH PRIVATE LIMITED; LANZATECH UK LIMITED
Reel/Frame 059910/0789 →
CHANGE OF NAME Recorded May 9, 2022
From: LANZATECH NEW ZEALAND LIMITED
To: LANZATECH NZ, INC.
Reel/Frame 059911/0400 →
RELEASE OF SECURITY INTEREST Recorded Mar 21, 2017
From: VENTURE LENDING & LEASING VI, INC.
To: LANZATECH NEW ZEALAND; LANZATECH, INC.; LANZATECH FREEDOM PINES BIOREFINERY LLC; LANZATECH HONG KONG LIMITED; LANZATECH PRIVATE LIMITED
Reel/Frame 042051/0377 →
SECURITY INTEREST Recorded Nov 28, 2016
From: LANZATECH NEW ZEALAND LIMITED; LANZATECH, INC.; LANZATECH FREEDOM PINES BIOREFINERY LLC; LANZATECH HONG KONG LIMITED; LANZATECH PRIVATE LIMITED; LANZATECH UK LIMITED
To: VENTURE LENDING & LEASING VII, INC.; VENTURE LENDING & LEASING VIII, INC.
Reel/Frame 040731/0573 →
SECURITY INTEREST Recorded Sep 30, 2014
From: LANZATECH, INC.
To: VENTURE LENDING & LEASING VI, INC.
Reel/Frame 033849/0572 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 22, 2014
From: SMART, KATHLEEN FRANCES; LY, BOI SAN
To: LANZATECH NEW ZEALAND LIMITED
Reel/Frame 032953/0283 →