Preparation of ethanol from corn

Patent metadata

Field	Value
Publication number	US-11034923-B2
Application number	US-201716311256-A
Country	US
Kind code	B2
Filing date	Jun 20, 2017
Priority date	Jun 20, 2016
Publication date	Jun 15, 2021
Grant date	Jun 15, 2021

Abstract

A corn-to-ethanol production process is disclosed. The process includes the steps of dry-milling corn kernels to form a corn flour; combining the corn flour with water to form a mash; extracting corn oil from the mash; fermenting the mash thereby producing beer and carbon dioxide; distilling the beer to produce ethanol and whole stillage; and processing the whole stillage to produce wet distiller's grains with solubles (WDGS) and/or dried distiller's grains with solubles (DDGS). The step of extracting corn oil from the mash includes the sub steps of: optionally wet-milling the mash; separating the mash to produce a light phase and a heavy phase; adding an alkanesulfonic acid to the light phase; extracting corn oil from the light phase; and combining the light phase having the corn oil extracted therefrom with the heavy phase to reform the mash.

First claim

What is claimed is:

1. A corn-to-ethanol process comprising the steps of:
(A) dry-milling corn kernels to form a corn flour;
(B) combining the corn flour with water to form a mash;
(C) extracting corn oil from the mash via the sub steps of:
(i) optionally wet-milling the mash;
(ii) separating the mash to produce a light phase and a heavy phase;
(iii) adding an alkanesulfonic acid to the light phase;
(iv) extracting corn oil from the light phase; and
(v) combining the light phase having the corn oil extracted therefrom with the heavy phase to reform the mash;

(D) fermenting the mash thereby producing beer and carbon dioxide;
(E) distilling the beer to produce ethanol and whole stillage; and
(F) processing the whole stillage to produce wet distiller's grains with solubles (WDGS) and/or dried distiller's grains with solubles (DDGS).

2. A process as set forth in claim 1 wherein the alkanesulfonic acid is methanesulfonic acid (MSA).

3. A process as set forth in claim 1 wherein the step of adding an alkanesulfonic acid to the light phase is further defined as adding said alkanesulfonic acid and a natural oil polyol to the light phase.

4. A process as set forth in claim 3 wherein the natural oil polyol has a hydrophilic-lipophilic balance (HLB) value of greater than about 8.

5. A process as set forth in claim 1 wherein the alkanesulfonic acid is added to the light phase in an amount sufficient to adjust a pH to a range of from about 3 to about 5.

6. A process as set forth in claim 1 wherein the step of adding an alkanesulfonic acid to the light phase is further defined as adding the alkanesulfonic acid in an amount of from 0.05 to about 2 parts by weight based on 100 parts by weight of the light phase.

7. A process as set forth in claim 1 wherein the step of extracting corn oil from the mash further comprises the sub step of fermenting the heavy phase to produce alcohol.

8. A process as set forth in claim 1 wherein the sub-step of adding the alkanesulfonic acid to the light phase is further described as adding the alkanesulfonic acid to the light phase to form a mixture, and aging the mixture from about 0.5 to about 5 hours.

9. A process as set forth in claim 1 wherein the separating the mash to produce a light phase and a heavy phase is further defined as separating the mash to produce a light phase and a heavy phase via centrifugation.

10. A process as set forth in claim 1 wherein the separating the mash to produce a light phase and a heavy phase is further defined as separating the mash to produce a light phase and a heavy phase via a first centrifugation and a second centrifugation.

11. A process as set forth in claim 1 wherein the step of processing the whole stillage to form WDGS and/or DDGS includes the sub steps of: centrifuging the whole stillage to produce wet cake and thin stillage; evaporating water from the thin stillage to form a syrup; extracting corn oil from the syrup; combining the wet cake and the syrup having the corn oil removed therefrom to form WDGS; and drying WDGS to produce DDGS.

12. A process as set forth in claim 11 further comprising the step of adding alkanesulfonic acid to thin stillage prior to the step of evaporating water from the thin stillage to form a syrup.

13. A process as set forth in claim 1 wherein step (B) is further defined as comprising the sub-steps of separating a corn fiber from the mash, treating the separated corn fiber with a composition, recombining the treated corn fiber with the mash having the corn fiber removed therefrom to form a slurry, and fermenting the slurry thereby producing beer and carbon dioxide.

14. A process as set forth in claim 13 wherein the composition comprises:
a. alkanesulfonic acid,
b. water,
c. an enzyme, and
d. optionally a surfactant.

15. A process as set forth in claim 14 wherein the alkanesulfonic acid is methanesulfonic acid (MSA) and is present in the composition in an amount of from about 0.1 to about 5 parts by weight based on 100 parts by weight of the composition.

16. A process as set forth in claim 14 wherein the enzyme is selected from the group consisting of an acid cellulase, an acid protease, an alpha amylase, a beta glucanase, a glucoamylase, a xylanase, and combinations thereof.

17. A process as set forth in claim 14 wherein the enzyme is present in an amount of from about 0.001 to about 0.2, wt. % based on a total weight of the corn.

18. A process as set forth in claim 13 wherein the composition comprises a surfactant selected from the group consisting of polyalkyleneoxides, alkylpolyalkyleneoxides, polyoxyethylene sorbitan monolaurates, alkylpolyglycosides, anionic derivatives of alkylpolyglycosides, fatty alcohols, anionic derivatives of fatty alcohols, phosphate esters, and combinations thereof.

19. A process as set forth in claim 1 further comprising the step of adding an alkanesulfonic acid to the beer to adjust a pH to a range of from about 3 to about 5 prior to and/or during the step of distilling the beer.

20. A process as set forth in claim 19 wherein the step of distilling the beer is conducted at a temperature of from about 80 to about 130° C.

21. A process as set forth in claim 1 wherein the step of fermenting the mash is conducted in the presence of phytase, and an alkanesulfonic acid is subsequently added to the beer.

22. A process as set forth in claim 1 producing DDGS having a Hunter L* color score of greater than about 50.

Assignees

• Basf Se

Inventors

• Zack Kenneth L
• Borst Joseph P
• Newton Anthony

Classifications

• Y02W30/74

  Recovery of fats, fatty oils, fatty acids or other fatty substances, e.g. lanolin or waxes · CPC title

• C12F3/10 Primary

  from distillery slops · CPC title

• C11B13/00

  Recovery of fats, fatty oils or fatty acids from waste materials · CPC title

• C12P7/06 Primary

  Ethanol, i.e. non-beverage · CPC title

• C12C7/04

  Preparation or treatment of the mash · CPC title