Method for increasing backset recycle in dry grind alcohol production

Patent metadata

Field	Value
Publication number	US-12338478-B2
Application number	US-202017641507-A
Country	US
Kind code	B2
Filing date	Sep 9, 2020
Priority date	Sep 13, 2019
Publication date	Jun 24, 2025
Grant date	Jun 24, 2025

Abstract

The present invention relates to a dry grind ethanol process in which post-distillation backset is subjected to aerobic fermentation to remove components that are inhibitory to an ethanolagen, such as yeast, allowing the utilization of an increased amount of post-distillation backset during the initial preparation of starch-containing substrates for the dry grind ethanol process. Aerobic fermentation of the post-distillation backset allows substantially higher backset recycle, resulting in fresh water savings and increased sustainability.

First claim

What is claimed is:

1. A method for increasing utilization of recycled liquid backset in a dry grind ethanol process, comprising:
(a) hydrolyzing a starch-containing feedstock with an α-amylase in the presence of recycled liquid backset to produce a starch liquefact;
(b) saccharifying the starch liquefact with a glucoamylase to produce glucose;
(c) fermenting the glucose with an organism under anaerobic conditions to produce an ethanol-containing fermented mash;
(d) distilling the fermented mash to recover an ethanol product resulting in an ethanol-depleted, post-distillation slurry;
(e) separating the solid and liquid portions of the post-distillation slurry;
(f) subjecting the liquid portion of the post-distillation slurry to aerobic fermentation using a non-pathogenic bacteria capable of consuming lactic acid and/or glycerol to produce a post-aerobic-fermentation backset; and
(g) recycling the post-aerobic-fermentation backset for use as recycled liquid backset in step (a);
wherein the amount of recycled liquid backset used in step (a) is greater than the amount of backset in an otherwise identical method lacking step (f).

2. The method of claim 1 , wherein step (b) and step (c) are combined to perform simultaneous saccharification and fermentation.

3. The method of claim 1 , wherein the non-pathogenic bacteria produce a protein of interest.

4. The method of claim 3 , wherein the protein of interest is an α-amylase.

5. The method of claim 3 , further comprising recovering the protein of interest from the post-aerobic-fermentation backset prior to step (g).

6. The method of claim 3 , wherein the protein of interest is not naturally-produced by the non-pathogenic bacteria.

7. The method of claim 1 , wherein the non-pathogenic bacteria is a Bacillus sp.

8. The method of claim 1 , wherein the non-pathogenic bacteria is B. subtilis or licheniformis.

9. The method of claim 1 , wherein the non-pathogenic bacteria do not produce an endotoxin.

10. The method of claim 1 , wherein the non-pathogenic bacteria do not sporulate.

11. The method of claim 1 , wherein the organism used in step (c) is a Saccharomyces sp.

Assignees

• Danisco Us Inc

Inventors

• Chotani Gopal K
• Demartini Jaclyn Diana
• Latone Jacob Andrew
• Sharma Vivek
• Shetty Jayarama K

Classifications

• C12Y302/01003

  Glucan 1,4-alpha-glucosidase (3.2.1.3), i.e. glucoamylase · CPC title

• C12Y302/01001

  Alpha-amylase (3.2.1.1) · CPC title

• C12P19/14

  produced by the action of a carbohydrase {(EC 3.2.x)}, e.g. by alpha-amylase {, e.g. by cellulase, hemicellulase} · CPC title

• Y02E50/10

  Biofuels, e.g. bio-diesel · CPC title

• Y02P60/87

  Re-use of by-products of food processing for fodder production · CPC title