IP Library Granted Patent US 12,264,294
Granted Patent B2
US 12,264,294 · App. 18/761,026 · Granted Apr 1, 2025

Methods for producing a high protein corn meal from a whole stillage byproduct and system therefore

Inventor: Chie Ying Lee (San Jose, CA)
Assignee: Fluid Quip Technologies, LLC
C11B13/00A23K10/38A23K50/00A23L7/198B02C9/04B04B3/04B04B5/10C12F3/10A23V2002/00B04B2001/205Y02P60/87Y02W30/74
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Quick Facts
Patent No.
US 12,264,294
App. No.
18/761,026
Granted
Apr 1, 2025
Kind
B2
Abstract

The present invention relates generally to corn dry-milling, and more specifically, to methods for producing a high protein corn meal from a whole stillage byproduct produced in a corn dry-milling process for making ethanol and a system therefore. In one embodiment, a method for producing a high protein corn meal from a whole stillage byproduct includes, in a corn dry-milling process for making ethanol, separating the whole stillage byproduct into an insoluble solids portion and a thin stillage portion. The thin stillage portion is separated into a protein portion and a water soluble solids portion. Next, the protein portion is dewatered then dried to define a high protein corn meal that includes at least 40 wt % protein on a dry basis.

Claims (24)

1. A method for producing grain meal from a whole stillage comprising:

separating a whole stillage byproduct, via a plurality of in-line separation devices, into an insoluble solids portion and a thin stillage portion, which includes protein, wherein the insoluble solids portion is processed into distillers wet grain and/or distillers dried grain with or without solubles; and

prior to any evaporation step, separating the thin stillage portion, via a mechanical separation device, into only a protein portion and a water soluble solids portion,

wherein the protein portion is not subsequently subjected to an evaporator and the protein portion defines a grain meal that includes at least 40 wt % protein on a dry basis.

2. The method of claim 1 further comprising drying the protein portion to define a grain meal that includes at least 40 wt % protein on a dry basis.

3. The method of claim 2 wherein drying the protein portion comprises drying the protein portion to define a grain meal that includes from 40 wt % protein to 60 wt % protein on a dry basis.

4. The method of claim 2 wherein drying the protein portion comprises drying the protein portion to define a grain meal that includes from 40 wt % protein to 56 wt % protein on a dry basis.

5. The method of claim 1 wherein the mechanical separation device is a nozzle centrifuge or a cyclone apparatus.

6. The method of claim 1 wherein the plurality of in-line separation devices is selected from a filtration centrifuge, a decanter centrifuge, a pressure screen, a paddle screen, or any combination thereof.

7. The method of claim 1 wherein the plurality of in-line separation devices is selected from a filtration centrifuge, a decanter centrifuge, or a combination thereof.

8. The method of claim 1 wherein directly after separating a whole stillage byproduct and prior to any evaporation step, separating the thin stillage portion, via a mechanical separation device, into only a protein portion and a water soluble solids portion, wherein the protein portion is not subsequently subjected to an evaporator.

9. The method of claim 1 further comprising separating oil from the water soluble solids portion to provide an oil portion.

10. The method of claim 9 wherein the oil portion includes about 40 wt % to about 60 wt % of the total oil of the grain used in the method.

11. A method for producing grain meal from a whole stillage comprising:

separating a whole stillage byproduct, via a plurality of in-line separation devices, into an insoluble solids portion and a thin stillage portion, which includes protein, wherein the insoluble solids portion is processed into distillers wet grain and/or distillers dried grain with or without solubles and wherein the plurality of in-line separation devices is selected from a filtration centrifuge, a decanter centrifuge, a pressure screen, a paddle screen, or any combination thereof; and

prior to any evaporation step, separating the thin stillage portion, via a nozzle centrifuge or cyclone apparatus, into only a protein portion and a water soluble solids portion,

wherein the protein portion is not subsequently subjected to an evaporator and wherein the protein portion defines a grain meal that includes at least 40 wt % protein on a dry basis.

12. The method of claim 11 further comprising drying the protein portion to define a grain meal that includes at least 40 wt % protein on a dry basis.

13. The method of claim 12 wherein drying the protein portion comprises drying the protein portion to define a grain meal that includes from 40 wt % protein to 60 wt % protein on a dry basis.

14. The method of claim 12 wherein drying the protein portion comprises drying the protein portion to define a grain meal that includes from 40 wt % protein to 56 wt % protein on a dry basis.

15. The method of claim 11 wherein the plurality of in-line separation devices is selected from a filtration centrifuge, a decanter centrifuge, or a combination thereof.

16. The method of claim 11 wherein directly after separating a whole stillage byproduct and prior to any evaporation step, separating the thin stillage portion, via a nozzle centrifuge of cyclone apparatus, into only a protein portion and a water soluble solids portion, wherein the protein portion is not subsequently subjected to an evaporator.

17. The method of claim 11 further comprising separating oil from the water soluble solids portion to provide an oil portion.

18. The method of claim 17 wherein the oil portion includes about 40 wt % to about 60 wt % of the total oil of the grain used in the method.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 25, 2025
From: LEE, CHIE-YING
To: FLUID QUIP, INC.
Reel/Frame 070314/0467 →
CHANGE OF NAME Recorded Feb 25, 2025
From: FLUID QUIP, INC.
To: FLUID QUIP TECHNOLOGIES, LLC
Reel/Frame 070314/0470 →
Continuity (8)
Continuation 18062787 · Dec 7, 2022
Continuation 17062889 · Oct 5, 2020
Continuation 16390302 · Apr 22, 2019
Continuation 15691040 · Aug 30, 2017
Continuation 14632359 · Feb 26, 2015
Continuation 14330612 · Jul 14, 2014
Division 13321670
Related Publication 20240352377A1 · Oct 24, 2024
References Cited (2)
US 12031105B2 · Lee · 2024 [cited by applicant]
US 20080110577A1 · Winsness · 2008 [cited by examiner]