IP Library Granted Patent US 8,778,433
Granted Patent B2
US 8,778,433 · App. 13/321,670 · Granted Jul 15, 2014

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

Inventor: Chie Ying Lee (Fremont, CA)
Assignee: Fluid Quip, Inc.
View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 8,778,433
App. No.
13/321,670
Granted
Jul 15, 2014
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 (42)

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

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

separating the thin stillage portion, via constituent weights, into a protein portion and a water soluble solids portion, which is lighter than the protein portion;

dewatering the protein portion; and

drying the dewatered protein portion 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 into an insoluble solids portion and a thin stillage portion includes subjecting the whole stillage to a filtration centrifuge, a decanter centrifuge, a pressure screen, or a paddle screen to separate the whole stillage into the solids portion and the thin stillage portion.

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

4. The method of claim 3 wherein the filtration centrifuge comprises:

a first housing having at least one wall with a plurality of openings formed therein;

a conveyor disposed in the first housing for moving at least the insoluble solids portion therealong; and

at least one conduit line in fluid communication with an interior of the first housing for supplying a medium including the insoluble solids portion to the apparatus,

wherein at least one of the first housing and conveyor rotate relative to a central axis to direct the medium toward the at least one wall so as to filter the insoluble solids portion from the medium.

5. The method of claim 3 wherein the filtration centrifuge comprises a plurality of filtration centrifuges to separate the whole stillage into the insoluble solids portion and the thin stillage portion.

6. 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.

7. The method of claim 6 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.

8. 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.

9. The method of claim 8 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.

10. The method of claim 1 wherein dewatering the protein portion includes subjecting the protein portion to a decanter centrifuge to dewater the protein portion.

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

12. The method of claim 11 further including combining the soluble solids portion with the insoluble solids portion to provide distillers wet or dry grains with solubles.

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

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

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

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

subjecting the thin stillage to a nozzle centrifuge or a cyclone apparatus to separate the thin stillage portion, via constituent weights, into a protein portion and a water soluble solids portion, which is lighter than the protein portion;

subjecting the protein portion to a decanter centrifuge to dewater the protein portion; and

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

16. The method of claim 15 wherein subjecting the whole stillage to a filtration centrifuge, a decanter centrifuge, a pressure screen, or a paddle screen includes subjecting the whole stillage to the filtration centrifuge to separate the whole stillage into the insoluble solids portion and the thin stillage portion.

17. The method of claim 16 wherein the filtration centrifuge comprises:

a first housing having at least one wall with a plurality of openings formed therein;

a conveyor disposed in the first housing for moving at least the insoluble solids portion therealong; and

at least one conduit line in fluid communication with an interior of the first housing for supplying a medium including the insoluble solids portion to the apparatus,

wherein at least one of the first housing and conveyor rotate relative to a central axis to direct the medium toward the at least one wall so as to filter the insoluble solids portion from the medium.

18. The method of claim 16 wherein the filtration centrifuge includes a plurality of filtration centrifuges to separate the whole stillage into the insoluble solids portion and the thin stillage portion.

19. The method of claim 16 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.

20. The method of claim 16 further comprising, prior to subjecting the whole stillage to the filtration centrifuge, subjecting the whole stillage to a paddle screen to aid in separating the whole stillage into the insoluble solids portion and the thin stillage portion.

21. The method of claim 20 wherein the paddle screen includes openings therein of no greater than 150 microns.

22. The method of claim 15 further comprising, after subjecting the whole stillage byproduct to a filtration centrifuge, a first decanter centrifuge, a pressure screen, or a paddle screen to separate the whole stillage 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.

23. The method of claim 15 further including separating soluble solids from the water soluble solids portion to provide a soluble solids portion.

24. The method of claim 23 further including combining the soluble solids portion with the insoluble solids portion to provide distillers wet or dry grains with solubles.

25. The method of claim 15 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.

26. The method of claim 15 wherein the high protein corn meal includes at least 50 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 Jun 12, 2012
From: LEE, CHIE YING
To: FLUID QUIP, INC.
Reel/Frame 028359/0555 →
Continuity (1)
Related Publication 20120064213A1 · Mar 15, 2012