IP Library Granted Patent US 8,409,639
Granted Patent B2
US 8,409,639 · App. 12/944,618 · Granted Apr 2, 2013

Methods and systems for producing ethanol using raw starch and fractionation

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Quick Facts
Patent No.
US 8,409,639
App. No.
12/944,618
Granted
Apr 2, 2013
Kind
B2
Abstract

The present invention relates to methods for producing high levels of alcohol during fermentation of plant material, and to the high alcohol beer produced. The method can include fractionating the plant material. The present invention also relates to methods for producing high protein distiller's dried grain from fermentation of plant material, and to the high protein distiller's dried grain produced. The method can include drying a co-product by ring drying, flash drying, or fluid bed drying. The present invention further relates to reduced stack emissions from drying distillation products from the production of ethanol.

Claims (26)

1. A fermentation method comprising

dry fractionating plant material comprising endosperm into components including fiber, germ and endosperm;

separating the germ and fiber components of the fractionated plant material to form a remaining portion which includes the endosperm;

reducing the size of particles in the remaining portion to form a reduced portion, wherein more than 50% of the particles fit through a sieve with a 0.5 mm mesh; and

fermenting the reduced portion in a reaction mixture under acidic conditions to form a liquid comprising ethanol and a solid material, wherein the reaction mixture comprises acid stable fungal alpha amylase and yeast.

2. The method of claim 1 , wherein the plant material is corn.

3. The method of claim 1 , wherein the amount of said acid stable fungal alpha amylase to dry solids in said reduced portion ranges from about 0.1 to about 10 acid stable fungal alpha amylase units per gram of dry solids.

4. The method of claim 1 , wherein the reaction mixture further comprises glucoamylase.

5. The method of claim 4 , wherein the amount of said glucoamylase to dry solids in said reduced portion ranges from about 0.5 to about 6 glucoamylase units per gram of said dry solids.

6. The method of claim 1 , wherein the acidic conditions comprise a pH of about 3 to about 6.

7. The method of claim 6 , wherein the acidic conditions comprise a pH of about 4 to about 5.

8. The method of claim 1 , wherein the fermentation is carried out at a temperature of about 25° C. to about 40° C.

9. A method of producing distiller's dried grains (DDG) and/or distiller's dried grains plus solubles (DDGS), the method comprising:

dry fractionating plant material comprising endosperm into components including fiber, germ and endosperm;

separating the germ and fiber components of the fractionated plant material to form a remaining portion which includes the endosperm;

reducing the size of particles in the remaining portion to form a reduced portion, wherein more than 50% of the particles fit through a sieve with a 0.5 mm mesh;

fermenting the reduced portion in a reaction mixture under acidic conditions to form a liquid comprising ethanol and a solid material, wherein the reaction mixture comprises acid stable fungal alpha amylase and yeast; and

removing the liquid comprising ethanol and drying the solid material to produce distiller's dried grains and/or distiller's dried grains plus solubles.

10. The method of claim 9 , wherein drying the solid material is achieved with a flash or a ring dryer.

11. The method of claim 9 , wherein the plant material is corn.

12. The method of claim 9 , wherein the amount of said acid stable fungal alpha amylase to dry solids in said reduced portion ranges from about 0.1 to about 10 acid stable fungal alpha amylase units per gram of dry solids.

13. The method of claim 9 , wherein the reaction mixture further comprises glucoamylase.

14. The method of claim 13 , wherein the amount of said glucoamylase to dry solids in said reduced portion ranges from about 0.5 to about 6 glucoamylase units per gram of said dry solids.

15. The method of claim 9 , wherein the acidic conditions include a pH of about 3 to about 6.

16. The method of claim 15 , wherein the acidic conditions include a pH of about 4 to about 5.

17. The method of claim 9 , wherein the fermentation is carried out at a temperature of about 25° C. to about 40° C.

Assignments (5)
SECURITY INTEREST Recorded Apr 3, 2020
From: POET RESEARCH, INC.
To: COBANK, ACB, AS ADMINISTRATIVE AGENT
Reel/Frame 052312/0801 →
SECURITY INTEREST Recorded Apr 2, 2020
From: POET RESEARCH, INC.
To: JPMORGAN CHASE BANK, N.A., AS ADMINISTRATIVE AGENT
Reel/Frame 052295/0712 →
RELEASE OF SECURITY INTEREST RECORDED AT REEL/FRAME 035603/0778 Recorded Apr 2, 2020
From: JPMORGAN CHASE BANK N.A., AS ADMINISTRATIVE AGENT
To: POET, LLC; POET RESEARCH, INC.; POET PLANT MANAGEMENT, LLC; POET INVESTMENTS, INC.; POET BIOMASS, LLC; POET DESIGN AND CONSTRUCTION, INC.; RISK MANAGEMENT ASSOCIATES, INC.; POET NUTRITION, INC.; POET RESEARCH CENTER, LLC (FORMERLY KNOWN AS POET RESEARCH CENTER, INC.); POET LEASING, LLC; POET NUTRITION INTERNATIONAL, INC.
Reel/Frame 052299/0676 →
RELEASE OF PATENT, TRADEMARK AND COPYRIGHT SECURITY INTEREST Recorded May 6, 2015
From: BOKF, N.A., DBA BANK OF OKLAHOMA
To: POET RESEARCH, INC. F/K/A BROIN AND ASSOCIATES, INC.; POET, LLC F/K/A BROIN COMPANIES, LLC; POET INVESTMENTS, INC. F/K/A BROIN ENTERPRISES, INC.; POET PLANT MANAGEMENT, LLC
Reel/Frame 035603/0610 →
ACKNOWLEDGEMENT OF SECURITY INTEREST IN PATENTS Recorded May 6, 2015
From: POET, LLC; POET RESEARCH, INC.; POET PLANT MANAGEMENT, LLC; POET INVESTMENTS, INC.; POET BIOMASS, LLC; POET DESIGN AND CONSTRUCTION, INC.; RISK MANAGEMENT ASSOCIATES, INC.; POET NUTRITION, INC.; POET RESEARCH CENTER, INC.; POET LEASING, LLC; POET NUTRITION INTERNATIONAL, INC.
To: JPMORGAN CHASE BANK, N.A.
Reel/Frame 035603/0778 →