IP Library Granted Patent US 10,519,398
Granted Patent B1
US 10,519,398 · App. 16/543,829 · Granted Dec 31, 2019

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 10,519,398
App. No.
16/543,829
Granted
Dec 31, 2019
Kind
B1
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 (32)

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

separating the whole stillage byproduct into a wet cake portion and a thin stillage portion, which includes protein;

prior to any evaporation step, separating out a solids portion, including the protein, from the thin stillage portion, wherein the solids portion, including the protein, is not subsequently subjected to an evaporator; and

drying the solids portion, including the protein, to define a grain 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 a wet cake portion and a thin stillage portion, which includes protein, comprises in a grain dry-milling process for making alcohol, separating the whole stillage byproduct into a wet cake portion and a thin stillage portion, which includes protein.

3. The method of claim 2 wherein the alcohol is ethanol.

4. The method of claim 1 wherein separating out the solids portion, including the protein, from the thin stillage portion comprises separating out, via weights, the solids portion, including the protein, from the thin stillage portion, wherein the solids portion, including the protein, is not subsequently subjected to an evaporator.

5. The method of claim 1 wherein drying the solids portion, including the protein, to define a grain meal that includes at least 40 wt % protein on a dry basis comprises drying the solids portion, including the protein, via a dryer to define a grain meal that includes at least 40 wt % protein on a dry basis.

6. The method of claim 1 further comprising dewatering the solids portion, including the protein, followed by drying the dewatered solids portion, including the protein, to define the grain meal.

7. The method of claim 1 wherein separating the whole stillage byproduct into a wet cake 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 wet cake portion and the thin stillage portion.

8. The method of claim 1 wherein the grain meal includes at least 45 wt % protein on a dry basis.

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

10. The method of claim 1 further comprising, after separating the whole stillage byproduct into a wet cake portion and a thin stillage portion and before separating out the solids portion, including the protein, from the thin stillage portion, separating out fine fiber from the thin stillage portion.

11. The method of claim 10 further comprising recovering the fine fiber.

12. The method of claim 1 wherein separating out the solids portion, including the protein, from the thin stillage portion includes subjecting the thin stillage portion to a nozzle centrifuge or a cyclone apparatus to separate out the solids portion, including the protein, from the thin stillage portion.

13. The method of claim 1 further comprising drying the wet cake portion, which includes fiber.

14. The method of claim 1 further comprising transporting the wet cake portion, which includes fiber, to a remote site.

15. The method of claim 1 for producing a corn meal from the whole stillage byproduct and wherein drying the solids portion comprises drying the solids portion, including the protein, to define a corn meal that includes at least 40 wt % protein on a dry basis.

16. The method of claim 1 wherein separating the whole stillage byproduct into a wet cake portion and a thin stillage portion, which includes protein, comprises filtering the thin stillage portion from the wet cake portion, which includes fiber, followed by separating additional protein from the wet cake portion.

17. The method of claim 1 wherein separating the whole stillage byproduct into a wet cake portion and a thin stillage portion, which includes protein, comprises filtering the thin stillage portion from the wet cake portion, which includes fiber, followed by washing the wet cake portion then dewatering the washed wet cake portion to remove protein therefrom.

18. The method of claim 17 wherein the thin stillage portion includes the removed protein from the dewatered wet cake portion.

19. The method of claim 17 further comprising drying the dewatered wet cake portion.

20. A system for producing grain meal from a whole stillage byproduct, the system comprising:

a first apparatus that receives a whole stillage byproduct, wherein the first apparatus separates the whole stillage byproduct into a wet cake portion and a thin stillage portion, which includes protein;

a second apparatus that is situated after the first apparatus and prior to any evaporator and that receives the thin stillage from the first apparatus, wherein the second apparatus separates out a solids portion, including the protein, from the thin stillage portion; and

an evaporator that is situated after the second apparatus and that receives the remaining thin stillage portion but does not receive the separated solids portion, including the protein, wherein the evaporator separates soluble solids from the remaining thin stillage portion, via evaporation, and wherein the separated solids portion, including the protein, defines a grain meal that includes at least 40 wt % protein on a dry basis.

21. The system of claim 20 further comprising a dryer that is situated after the second apparatus and that dries the separated out solids portion, including the protein, to define the grain meal that includes at least 40 wt % protein on a dry basis.

22. The system of claim 20 wherein the first apparatus is situated after a distillation column and receives the whole stillage byproduct produced via a grain dry-milling process.

23. The system of claim 20 wherein the second apparatus separates out, via weights, the solids portion, including the protein, from the thin stillage portion.

24. The system of claim 20 wherein the first apparatus is selected from a filtration centrifuge, a decanter centrifuge, a pressure screen, or a paddle screen and the second apparatus is selected from a nozzle centrifuge or a cyclone apparatus.

25. The system of claim 20 further comprising a second dryer that receives and dries the separated wet cake portion, which includes fiber.

26. The system of claim 20 for producing a corn meal from the whole stillage byproduct and wherein the separated solids portion, including the protein, defines a corn meal that includes at least 40 wt % protein on a dry basis.

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 (5)
Continuation 16390302 · Apr 22, 2019
Continuation 15691040 · Aug 30, 2017
Continuation 14632359 · Feb 26, 2015
Continuation 14330612 · Jul 14, 2014
Division 13321670
Cited By (1)
US 12,213,497