IP Library Granted Patent US 10,160,932
Granted Patent B2
US 10,160,932 · App. 14/632,359 · Granted Dec 25, 2018

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, Inc.
C11B13/00A23K10/38A23K50/00A23L7/198B02C9/04B04B3/04B04B5/10C12F3/10A23V2002/00B04B2001/205Y02P60/873Y02W30/74
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Quick Facts
Patent No.
US 10,160,932
App. No.
14/632,359
Granted
Dec 25, 2018
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 (36)

1. A method for producing a high protein corn meal from a whole stillage byproduct comprising:

in a corn dry-milling process for making alcohol, separating the whole stillage byproduct into an insoluble solids portion and a thin stillage portion, which includes protein;

prior to any evaporation step, separating the thin stillage portion, via weights, into a protein portion and a water soluble solids portion, which is lighter than the protein portion, wherein the protein portion is not subsequently subjected to an evaporator; and

drying the protein portion via a dryer to define a high protein corn meal that includes at least 40 wt % protein on a dry basis.

2. The method of claim 1 wherein separating the whole stillage byproduct into an insoluble solids portion and a thin stillage portion includes subjecting the whole stillage byproduct to a filtration centrifuge, a decanter centrifuge, a pressure screen, or a paddle screen to separate the whole stillage byproduct into the insoluble solids portion and the thin stillage portion.

3. The method of claim 2 wherein subjecting the whole stillage byproduct to a filtration centrifuge, a decanter centrifuge, a pressure screen, or a paddle screen includes subjecting the whole stillage byproduct to the filtration centrifuge to separate the whole stillage byproduct into the insoluble solids portion and the thin stillage portion.

4. The method of claim 1 further comprising, after separating the whole stillage byproduct into an insoluble solids portion and a thin stillage portion and before separating the thin stillage portion into a protein portion and a water soluble solids portion, separating fine fiber from the thin stillage portion.

5. The method of claim 4 wherein separating fine fiber from the thin stillage portion includes subjecting the thin stillage portion to a decanter centrifuge, a pressure screen, or a paddle screen to separate fine fiber from the thin stillage portion.

6. The method of claim 1 wherein separating the thin stillage portion into a protein portion and a water soluble solids portion includes subjecting the thin stillage to a nozzle centrifuge or a cyclone apparatus to separate the thin stillage portion into the protein portion and the water soluble solids portion.

7. The method of claim 6 wherein subjecting the thin stillage to a nozzle centrifuge or a cyclone apparatus includes subjecting the thin stillage to the nozzle centrifuge to separate the thin stillage portion into the protein portion and the water soluble solids portion.

8. The method of claim 1 further comprising dewatering the protein portion followed by drying the dewatered protein via the dryer to define the high protein corn meal.

9. The method of claim 1 further including separating soluble solids from the water soluble solids portion to provide a soluble solids portion.

10. The method of claim 9 further including combining the soluble solids portion with the insoluble solids portion to provide distillers wet or dry grains with solubles.

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

12. The method of claim 1 wherein the alcohol is ethanol.

13. The method of claim 1 wherein the high protein corn meal includes at least 50 wt % protein on a dry basis.

14. The method of claim 1 wherein the high protein corn meal defines an animal feed.

15. The method of claim 1 wherein the high protein corn meal defines a pig and/or chicken feed.

16. The method of claim 1 further comprising separating out water from the water soluble solids portion to yield a soluble solids portion.

17. The method of claim 16 wherein the soluble solids portion defines a natural fertilizer.

18. The method of claim 1 wherein separating the whole stillage byproduct includes separating the whole stillage byproduct, via particle sizes, into an insoluble solids portion and a thin stillage portion, which includes protein and oil, and wherein separating the thin stillage portion includes prior to any evaporation of the thin stillage, separating the thin stillage portion, via weights, into a protein portion and a water soluble solids portion, which includes the oil and is lighter than the protein portion.

19. A method for producing a high protein corn meal from a whole stillage byproduct comprising:

in a corn dry-milling process for making alcohol, subjecting the whole stillage byproduct to a filtration centrifuge, decanter centrifuge, a pressure screen, or a paddle screen to separate the whole stillage into an insoluble solids portion and a thin stillage portion, which includes protein;

prior to any evaporation step, subjecting the thin stillage to a nozzle centrifuge or a cyclone apparatus to separate the thin stillage portion, via weights, into a protein portion and a water soluble solids portion, which is lighter than the protein portion, wherein the protein portion is not subsequently subjected to an evaporator; and

drying the protein portion via a dryer to define a high protein corn meal that includes at least 40 wt % protein on a dry basis.

20. The method of claim 19 wherein subjecting the whole stillage byproduct to a filtration centrifuge, decanter centrifuge, a pressure screen, or a paddle screen includes subjecting the whole stillage byproduct to the filtration centrifuge to separate the whole stillage byproduct into the insoluble solids portion and the thin stillage portion.

21. The method of claim 19 wherein subjecting the thin stillage to a nozzle centrifuge or a cyclone apparatus includes subjecting the thin stillage to the nozzle centrifuge to separate the thin stillage portion into the protein portion and the water soluble solids portion.

22. The method of claim 19 further comprising, prior to subjecting the whole stillage byproduct to a filtration centrifuge, decanter centrifuge, a pressure screen, or a paddle screen, subjecting the whole stillage byproduct to a paddle screen to aid in separating the whole stillage byproduct into the insoluble solids portion and the thin stillage portion.

23. The method of claim 19 further comprising, after subjecting the whole stillage byproduct to a filtration centrifuge, decanter centrifuge, a pressure screen, or a paddle screen to separate the whole stillage byproduct into an insoluble solids portion and a thin stillage portion and before subjecting the thin stillage to a nozzle centrifuge or a cyclone apparatus to separate the thin stillage portion into a protein portion and a water soluble solids portion, subjecting the thin stillage portion to a decanter centrifuge, a pressure screen, or a paddle screen to separate fine fiber from the thin stillage portion.

24. The method of claim 19 further including separating soluble solids from the water soluble solids portion to provide a soluble solids portion.

25. The method of claim 24 further including combining the soluble solids portion with the insoluble solids portion to provide distillers wet or dry grains with solubles.

26. The method of claim 19 further including subjecting the water soluble solids portion to an oil recovery centrifuge to separate oil from the water soluble solids portion to provide an oil portion.

27. The method of claim 19 further comprising subjecting the protein portion to a decanter centrifuge to dewater the protein portion followed by drying the dewatered protein portion via the dryer to define the high protein corn meal.

28. The method of claim 19 wherein the alcohol is ethanol.

29. The method of claim 19 wherein the high protein corn meal includes at least 50 wt % protein on a dry basis.

30. The method of claim 19 wherein subjecting the whole stillage byproduct includes subjecting the whole stillage byproduct to a filtration centrifuge, a pressure screen, or a paddle screen to separate the whole stillage byproduct, via particle sizes, into an insoluble solids portion and a thin stillage portion, which includes protein and oil, and wherein subjecting the thin stillage includes prior to any evaporation of the thin stillage, subjecting the thin stillage to a nozzle centrifuge or a cyclone apparatus to separate the thin stillage portion, via weights, into a protein portion and a water soluble solids portion, which includes the oil and is lighter than the protein portion.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 14, 2020
From: FLUID QUIP, INC.
To: FLUID QUIP TECHNOLOGIES, LLC
Reel/Frame 053493/0697 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 12, 2020
From: LEE, CHIE-YING
To: FLUID QUIP, INC.
Reel/Frame 053467/0170 →
Continuity (3)
Continuation 14330612 · Jul 14, 2014
Division 13321670
Related Publication 20150164114A1 · Jun 18, 2015
Cited By (1)
US 12,213,497