Methods for Increasing the Production of Ethanol from Microbial Fermentation

• US 20120122173A1
• Filed: 12/13/2011
• Published: 05/17/2012
• Est. Priority Date: 07/25/2000
• Status: Abandoned Application

• Current Assignee: INEOS Bio SA
• Original Assignee: INEOS Bio Limited (Ineos AG)
• Inventors: GADDY, James L., ARORA, Dinesh K., KO, Ching-Whan, PHILLIPS, John Randall, BASU, Rahul, WIKSTROM, Carl V., CLAUSEN, Edgar C.
• Application Number:
  US13/323,913
• Publication Number:
  US 20120122173A1
• Time in Patent Office: Days
• US Class Current: 435/161
• CPC Class Codes: C12M 21/04 for producing gas, e.g. biogas digesters for manure with production of biogas A01C3/028, biological treatment of water, waste water or sewage C02F3/00, C02F11/02, preparation of natural gas or syngas C10L3/06, C10L3/10
• CPC Class Codes: C12M 21/12 for producing fuels or solvents C12M21/04 takes precedence; liquid carbonaceous fuels C10L1/00, solid fuels C10L5/00
• CPC Class Codes: C12M 29/02 Percolation
• CPC Class Codes: C12M 29/18 External loop; Means for reintroduction of fermented biomass or liquid percolate loop type reactors for chemical or physical processes B01J19/2435
• CPC Class Codes: C12M 43/02 Bioreactors or fermenters combined with devices for liquid fuel extraction; Biorefineries
• CPC Class Codes: C12P 7/065 with microorganisms other than yeasts
• CPC Class Codes: Y02E 50/10 Biofuels, e.g. bio-diesel
• CPC Class Codes: Y02E 50/30 Fuel from waste, e.g. synthetic alcohol or diesel

Abstract

A stable continuous method for producing ethanol from the anaerobic bacterial fermentation of a gaseous substrate containing at least one reducing gas involves culturing in a fermentation bioreactor anaerobic, acetogenic bacteria in a liquid nutrient medium; supplying the gaseous substrate to the bioreactor; and manipulating the bacteria in the bioreactor by reducing the redox potential, or increasing the NAD(P)H TO NAD(P) ratio, in the fermentation broth after the bacteria achieves a steady state and stable cell concentration in the bioreactor. The free acetic acid concentration in the bioreactor is maintained at less than 5 g/L free acid. This method allows ethanol to be produced in the fermentation broth in the bioreactor at a productivity of greater than 10 g/L per day. Both ethanol and acetate are produced in a ratio of ethanol to acetate ranging from 1:1 to 20:1.

Claims

1. A continuous method for producing ethanol comprising:

culturing in a fermentation bioreactor at least one strain of Clostridium ljungdahlii bacteria in a continuously fed liquid nutrient medium to provide a fermentation broth;

supplying to said fermentation bioreactor a gaseous substrate comprising carbon monoxide; and

maintaining a specific rate of CO uptake in said fermentation bioreactor at an amount of 0.3 to 2 mmol CO/gram dry cells weight of bacteria per minute in the fermentation broth after the bacteria achieve a stable cell concentration in the fermentation bioreactor;

wherein the bacteria produce both ethanol and acetate in a ratio of ethanol to acetate ranging from 1;

1 to 20;

1; and

wherein cell recycle provides increased ethanol productivity by ratio ranging from 1.465 to 1.85.

2. The method of claim 1, wherein the strain of Clostridium ljungdahlii bacteria is Clostridium ljungdahlii PETC, Clostridium ljungdahlii ER 12, Clostridium ljungdahlii C-01, Clostridium ljungdahlii O-52, or mixed strains.

3. The method of claim 1, wherein the ratio of ethanol to acetate and the ratio of free acetic acid to ethanol is measured after the bacteria achieve a stable cell concentration in the bioreactor.

4. The method of claim 1, wherein said gaseous substrate is selected from the group consisting of (a) carbon monoxide, (b) carbon monoxide and hydrogen, and (c) carbon monoxide, carbon dioxide and hydrogen.

5. The method of claim 1, wherein the gaseous substrate comprises carbon monoxide and hydrogen in a ratio of carbon monoxide to hydrogen ranging from 0.25 to 3.25.

6. The method of claim 1, wherein the gaseous substrate additionally comprises at least one gas chosen from nitrogen and methane.

7. The method of claim 1 further comprising supplying calcium pantothenate in an amount ranging from 2 to 50 μ

g calcium pantothenate per gram of dry cells of bacteria in the fermentation bioreactor.

8. The method of claim 1 further comprising supplying calcium pantothenate, wherein the amount of calcium pantothenate ranges from 2 to 25 μ

g calcium pantothenate per gram of dry cells of bacteria.

9. The method of claim 1 further comprising supplying calcium pantothenate, wherein the amount of calcium pantothenate ranges from 10 to 30 μ

g calcium pantothenate per gram of dry cells of bacteria.

10. The method of claim 1 further comprising supplying calcium pantothenate, wherein the amount of calcium pantothenate ranges from 10 to 50 μ

g calcium pantothenate per gram of dry cells of bacteria.

11. The method of claim 1 further comprising supplying cobalt in an amount ranging from 5 to 100 μ

g cobalt per gram of dry cells of bacteria in the fermentation bioreactor.

12. The method of claim 1 further comprising supplying cobalt, wherein the amount of cobalt ranges from 20 to 50 μ

g cobalt per gram of dry cells of bacteria.

13. The method of claim 1 further comprising supplying cobalt, wherein the cobalt is maintained at a constant concentration.

14. The method of claim 1, wherein the free acetic acid concentration after the bacteria achieve a stable cell concentration in the bioreactor is less than 5 g/L free acetic acid.

15. The method of claim 1, wherein the fermentation bioreactor consists of one or more continuous stirred tank reactor (CSTR), immobilized cell reactor (ICR), trickle bed reactor (TBR), bubble column, gas lift fermenter, static mixer, or other device suitable for gas-liquid contact.

16. The method of claim 1, wherein the fermentation bioreactor comprises a growth reactor that feeds the fermentation broth to a second fermentation bioreactor in which some or all of the ethanol is produced.

17. The method of claim 1 further comprising:

removing the fermentation broth from the fermentation bioreactor;

distilling ethanol from the broth; and

recovering the ethanol.

18. The method of claim 1 further comprising purging the bacteria from the fermentation bioreactor.

19. The method of claim 1, wherein the pH is greater than 4.5.

20. The method of claim 1, wherein the pH ranges from 4.5 to 5.5.