IP Library Granted Patent US 11,517,028
Granted Patent B2
US 11,517,028 · App. 17/683,011 · Granted Dec 6, 2022

Fractionated stillage separation

Inventors: Charles C. Gallop (Gower, MO); Christopher Riley William Gerken (Helena, MO)
Assignee: ICM, Inc.
A23K10/10A23J1/005A23J1/12A23J1/125A23J1/16A23K10/38A23K40/00A23K50/10A23K50/30A23K50/75A23K50/80B01D5/006B01D17/0205B01D17/0217B01D21/26B01D21/262B01D21/267B03B9/00C12N1/16Y02P60/87
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Quick Facts
Patent No.
US 11,517,028
App. No.
17/683,011
Granted
Dec 6, 2022
Kind
B2
Abstract

This disclosure describes methods to separate solids from liquids in a production facility. A process separates components in the process stream by using a mechanical device to separate the solids from the liquids based on a density difference. The process produces the liquids and solids, which may be further processed to create valuable animal feed products.

Claims (28)

1. A method for separating components in a fractionated process stream, the method comprising:

receiving the fractionated process stream from a production facility, where the fractionated process stream comprises a mixture of components of liquids and solids;

adding a non-condensable media to the mixture of components to increase a density differential between the components,

separating the solids from the liquids in the mixture of components with a first mechanical separation device, to provide a separated solids stream and a separated liquids stream, wherein the separated solids stream is approximately 10% to approximately 40% total solids, and

sending the separated liquids stream through a second mechanical separation device, to create a suspended solids concentrate from the separated liquids stream.

2. The method of claim 1 , wherein the fractionated process stream comprises about 4% to about 12% total solids.

3. The method of claim 1 , wherein the fractionated process stream comprises a stillage with fiber removed.

4. The method of claim 1 , wherein the non-condensable media comprises at least one of air, carbon dioxide, nitrogen, or oxygen.

5. The method of claim 1 , wherein the first mechanical separation device comprises at least one of a sedicanter centrifuge, a decanter centrifuge, a disk stack centrifuge, a hydrocyclone, or a settling tank.

6. The method of claim 1 , wherein the separated solids stream comprises at least approximately 38% protein.

7. The method of claim 1 , wherein the second mechanical separation device comprises at least one of a centrifuge, and a hydrocyclone.

8. The method of claim 1 , further comprising sending the suspended solids concentrate for further processing through a third mechanical separation device.

9. A method for processing a stream, the method comprising:

receiving a process stream from a production facility, the process stream comprising a mixture of one or more liquids and one or more solids;

adding a non-condensable media to the mixture of the process stream to increase a density differential between the one or more solids and the one or more liquids; and

separating the one or more solids from the one or more liquids in the mixture with a mechanical separation device based on a difference in density between the one or more solids and the one or more liquids, to provide a separated solids stream and a separated liquids stream, wherein the separated solids stream is at least approximately 38% protein.

10. The method of claim 9 , wherein the separated solids stream comprises approximately 15% to approximately 39% total solids.

11. The method of claim 9 , wherein the separated solids stream comprises at least one of zein, germ, insoluble fiber, insoluble starch, inorganic acids, non-fermentable carbohydrates, or a combination thereof.

12. The method of claim 9 , wherein the separated liquids stream comprises approximately 4% to approximately 12% total solids.

13. The method of claim 9 , wherein the separating of the one or more solids from the one or more liquids is via the use of centrifugal forces, wherein the centrifugal forces are in a range of from approximately 3,000 g forces to approximately 10,000 g forces.

14. The method of claim 9 , further comprising sending the separated liquids stream through a second mechanical separation device, to create a suspended solids concentrate from the liquids stream.

15. A method comprising:

receiving a process stream comprising a mixture of one or more liquids and one or more solids:

adding a non-condensable media to the mixture of the process stream to increase a density differential between the one or more solids and the one or more liquids, and

separating the one or more liquids from the one or more solids in the process stream using at least one of a sedicanter centrifuge, a decanter centrifuge, a disk stack centrifuge, a hydrocyclone, or a settling tank to create a light emulsion phase and a heavy phase with suspended solids, wherein the light emulsion phase comprises from about 20% to about 55% total solids.

16. The method of claim 15 , further comprising sending the light emulsion phase through another separation device.

17. The method of claim 16 , wherein the another separation device comprises at least one of a centrifuge, and a hydrocyclone.

18. The method of claim 17 , wherein the non-condensable media comprises at least one of air, carbon dioxide, nitrogen, oxygen, or sulfur.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 28, 2022
From: GALLOP, CHARLES C.; GERKEN, CHRISTOPHER RILEY WILLIAM
To: ICM, INC.
Reel/Frame 059124/0524 →
Continuity (3)
Continuation 16624811
Provisional Application 62521542 · Jun 19, 2017
Related Publication 20220183318A1 · Jun 16, 2022