Granted Patent B2

US 12,480,142 · App. 18/210,805 · Granted Nov 25, 2025

Inventor: Jason Bootsma (Wichita, KS)

Assignee: POET Grain (Octane), LLC

C12P7/10B01D17/0217B01D33/00C11B1/10C12M47/10C12P7/14C12P7/6409C12P19/02C12P19/14C12M45/04C12M47/06C12N9/2437C12P2201/00

Abstract

Claims (43)

1 . A process for recovering an oil product, a protein meal product, and a corn fiber product from corn pieces comprising:

introducing the corn pieces into an ethanol production process to produce a whole stillage;

introducing the whole stillage into a filtration device comprising a flexible screen and a mechanical agitation mechanism to produce a filtrate and a fibrous solid stream;

introducing the filtrate into a three-phase centrifuge to produce the oil product, a high protein solids stream, and a solubles stream;

dewatering the fibrous solid stream to produce a wet fibrous stream;

drying the high protein solids stream to produce the protein meal product;

evaporating the solubles stream to produce a condensed solubles stream;

mixing the wet fibrous stream and the condensed solubles stream to produce a mixture;

drying the mixture to produce the corn fiber with solubles product; and

recycling at least a portion of the filtrate to the whole stillage.

2 . The process of claim 1 , wherein:

the filtration device comprises a washing nozzle housed inside the flexible screen and positioned to provide counter-current washing of solids in the

filtration device;

and

the filtration device does not comprise a conveying element.

3 . The process of claim 1 , wherein the three-phase centrifuge is a three-phase decanter.

4 . The process of claim 1 , wherein the fibrous solid stream is washed and dewatered to produce additional filtrate.

5 . The process of claim 1 , wherein the filtrate is heated before introduction into the three-phase centrifuge.

6 . The process of claim 1 , wherein the filtrate is evaporated before introduction into the three-phase centrifuge.

7 . A process for separating at least a protein meal product from whole stillage, wherein the process comprises:

separating a first stream and a second stream from whole stillage, wherein the first stream is a fiber rich stream;

separating at least a portion of the second stream via one or more separators into at least a protein rich stream and a clarified stillage;

removing water from the protein rich stream to form at least a protein rich product stream and a water stream; and

recycling at least a portion of the water stream to the whole stillage.

8 . The process of claim 7 , wherein the whole stillage is separated via one or more pressure screens, one or more centrifuges, one or more paddle screens, one or more fiber filters, one or more rotary drum screens, one or more rotary vacuum drum filters, one or more brush strainers, one or more vibratory separators, one or more centrifugal screeners, one or more linear motion screens, one or more vacu-deck screens, and combinations thereof.

9 . The process of claim 7 , wherein the whole stillage is separated via one or more fiber filters, wherein each fiber filter comprises:

a flexible screen; and

a mechanical agitation mechanism to produce the fiber rich stream and a filtrate as the second stream, wherein the flexible screen is coupled to the filter device via one or more elastic supports.

10 . The process of claim 7 , wherein the whole stillage is separated via one or more fiber filters, wherein each fiber filter comprises:

a flexible screen;

a rotor positioned inside the flexible screen;

one or more paddles coupled to the rotor, wherein each paddle pulses the whole stillage radially outward against the flexible screen; and

flighting coupled to the rotor, wherein the flighting conveys solids present in the whole stillage toward a discharge outlet of the fiber filter to form the fiber rich stream.

11 . The process of claim 10 , wherein the flexible screen comprises a flexible, filtering sleeve, and wherein the whole stillage flows into the flexible, filtering sleeve so that the second stream flows through openings in the flexible, filtering sleeve and separates from the whole stillage.

12 . The process of claim 11 , wherein the flexible, filtering sleeve comprises polymer fabric.

13 . The process of claim 11 , wherein the fiber filter is configured to permit the flexible, filtering sleeve to expand and contract along a longitudinal axis of the flexible, filtering sleeve.

14 . The process of claim 11 , wherein the rotor rotates in a manner that pulses whole stillage radially outward against the flexible, filtering sleeve.

15 . The process of claim 7 , wherein the one or more separators comprise one or more two-phase centrifuges.

16 . The process of claim 7 , wherein removing water from the protein rich stream to form at least a protein rich product stream and a water stream comprises separating the protein rich stream into the protein rich product stream and the water stream via one or more decanter centrifuges.

17 . The process of claim 7 , further comprising removing water from the protein rich product stream via one or more dryers to form a dried protein rich product.

18 . The process of claim 7 , further comprising separating a water stream from the fiber rich stream via one or more centrifuges.

19 . The process of claim 9 , wherein the filter device comprises a washing nozzle inside the flexible screen positioned for counter-current washing of solids contained in the filter device.

20 . The process of claim 9 , wherein the whole stillage is from an ethanol process.

Assignments (3)

Continuity (8)

References Cited (276)