IP Library Granted Patent US 11,618,910
Granted Patent B2
US 11,618,910 · App. 16/353,263 · Granted Apr 4, 2023

Methods and systems for the production of alcohols and/or acids

Inventor: Michael Anthony Schultz (Indianapolis, IN)
Assignee: LanzaTech NZ, Inc.
C12P7/54B65D81/32C07C29/1518C07C51/12C12M21/04C12M21/12C12M43/00C12P7/065C12P7/08C12P7/18Y02E50/10Y02E50/30
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Quick Facts
Patent No.
US 11,618,910
App. No.
16/353,263
Granted
Apr 4, 2023
Kind
B2
Abstract

Methods and systems for the production of one or more products from a gas stream produced in a methanol production process. The method comprises converting at least a portion of a methane feedstock to a substrate comprising CO and H2. The substrate comprising CO and H2 is anaerobically fermented in a bioreactor to produce one or more alcohols. The method and system may further include process for the production of methanol processes for the production of acetic acid.

Claims (20)

1. A method comprising:

a. converting a gas stream comprising methane to a substrate stream comprising CO and H 2 ;

b. passing a portion of the substrate stream to a methanol synthesis process to convert at least a portion of the CO and H 2 in the substrate stream to methanol;

c. passing a portion of an exit stream comprising methanol and CO from the methanol synthesis process to a methanol carbonylation process to convert the methanol and CO to acetic acid;

d. passing an exit gas stream comprising CO and H 2 from the methanol synthesis process to a first bioreactor containing a culture of at least one carboxydotrophic bacteria and anaerobically fermenting at least a portion of the exit gas stream comprising CO and H 2 from the methanol synthesis process to produce at least one product selected from alcohols, acids 2,3-butanediol and combinations thereof;

e. passing an exit stream from the carbonylation process comprising acetic acid, by-products and waste products, to a separation vessel operated at conditions to produce an acetic acid product stream and a gaseous stream comprising CO;

f. passing the gaseous stream comprising CO from step (e) to the first bioreactor;

g. passing a portion of the substrate stream comprising CO and H 2 from step (a) to the first bioreactor;

h. passing an exit gas stream from the first bioreactor comprising H 2 and CO 2 , the exit gas stream being rich in H 2 , to a second bioreactor comprising a culture of at least one carboxydotrophic bacteria and anaerobically fermenting at least a portion of the H 2 and CO 2 to acetic acid.

2. The method of claim 1 , wherein the methane is converted to CO and H 2 by catalytic oxidation.

3. The method of claim 1 , wherein the at least one product produced in step (d) is selected from ethanol, 2,3-butanediol, acetic acid and any combination thereof.

4. The method of claim 1 , further comprising passing a CO 2 comprising stream to the second bioreactor.

5. The method of claim 1 , wherein the carboxydotrophic bacteria of step (d) is selected from Clostridium, Moorella, Carboxydothermus , and any combination thereof.

6. The method of claim 5 , wherein the carboxydotrophic bacteria is Clostridium.

7. The method of claim 6 , wherein the carboxydotrophic bacteria is Clostridium autoethanogenum.

8. The method of claim 1 , further comprising passing the H 2 rich exit gas stream from the first bioreactor to a recovery zone where at least a portion of the H 2 is recovered before passing the exit gas stream to the second bioreactor.

9. The method of claim 1 , wherein the at least one carboxydotrophic bacteria of step (h) is selected from Acetobacterium, Moorella, Clostridium, Ruminococcus, Eubacterium , Butyribacterium, Oxobacter, Methanosarcina, Desulfotomaculum , and any combination thereof.

10. The method of claim 9 , wherein the carboxydotrophic bacteria is Acetobacterium.

11. The method of claim 10 , wherein carboxydotrophic bacteria is Acetobacterium woodii.

12. The method of claim 1 , wherein the acetic acid produced by the carbonylation process is recovered.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 17, 2023
From: SCHULTZ, MICHAEL ANTHONY
To: LANZATECH NEW ZEALAND LIMITED
Reel/Frame 062734/0428 →
CHANGE OF NAME Recorded Apr 13, 2022
From: LANZATECH NEW ZEALAND LIMITED
To: LANZATECH NZ, INC.
Reel/Frame 059695/0018 →