IP Library Granted Patent US 10,980,263
Granted Patent B2
US 10,980,263 · App. 15/969,133 · Granted Apr 20, 2021

Bio-based oil composition and method for producing the same

Inventors: Christopher S. Froderman (Avon, IN); William C. Hildebrand (Indianapolis, IN)
Assignee: SOLENIS TECHNOLOGIES, L.P.
A23L29/04A23K10/38C11B1/10C11B3/16C11B13/00A23V2002/00Y02P60/87Y02W30/74
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Quick Facts
Patent No.
US 10,980,263
App. No.
15/969,133
Granted
Apr 20, 2021
Kind
B2
Abstract

A method of extracting oil from a byproduct stream of a bio-based ethanol production process and a organic composition resulting from the method is provided. The method includes applying an oil concentrator to a byproduct stream, mixing the oil concentrator with the byproduct stream, and separating the oil from the byproduct stream. An organic composition comprising oil derived from a byproduct stream of a bio-based ethanol production process and an oil concentrator is also provided.

Claims (27)

1. A method of extracting oil from a byproduct stream of a bio-based ethanol production process under conditions in which there is an attraction between oil and oil sequestering components in the byproduct stream, the method comprising:

applying an oil concentrator to the byproduct stream of the bio-based ethanol production process with the byproduct stream at a pH between 3 and 7, wherein the oil concentrator is a surfactant compound having a hydrophilic group and a lipophilic group providing the oil concentrator a hydrophile-lipophile balance (HLB) of about 12 to about 18, wherein the lipophilic group is a fatty acid group and the hydrophilic group is a polyethylene oxide;

mixing the oil concentrator with the byproduct stream; and

separating the oil from the byproduct stream,

wherein said method is free of adding additional oil to the byproduct stream.

2. The method of extracting oil from the byproduct stream of the bio-based ethanol production process of claim 1 , wherein the hydrophile-lipophile balance (HLB) is about 14 to about 16.

3. The method of extracting oil from the byproduct stream of the bio-based ethanol production process of claim 1 , wherein the hydrophile-lipophile balance (HLB) is about 15.

4. The method of extracting oil from the byproduct stream of the bio-based ethanol production process of claim 1 , wherein the byproduct stream comprises an aqueous liquid byproduct stream with dissolved solids.

5. The method of extracting oil from the byproduct stream of the bio-based ethanol production process of claim 4 , wherein the byproduct stream comprises a thin stillage or syrup derived therefrom.

6. The method of extracting oil from the byproduct stream of the bio-based ethanol production process of claim 4 , wherein adding the oil concentrator into the aqueous liquid byproduct stream includes adding an amount of oil concentrator so that the oil concentrator concentration is below a critical micellar concentration for the oil concentrator in the aqueous liquid byproduct stream.

7. A method of extracting oil from a byproduct stream of a bio-based ethanol production process under conditions in which there is an attraction between oil and oil sequestering components in the byproduct stream, the method comprising:

applying an oil concentrator to the byproduct stream of the bio-based ethanol production process with the byproduct stream at a pH between 3 and 7, wherein the oil concentrator is a surfactant compound having a hydrophilic group and a lipophilic group providing the oil concentrator a hydrophile-lipophile balance (HLB) of about 14 to about 16 and wherein the oil concentrator is an FDA acceptable direct food additive for humans and animals, said food additive selected from the group consisting of polyoxyethylene (20) sorbitan monostearate (Polysorbate 60), polyoxyethylene (20) sorbitan tristearate (Polysorbate 65), and polyoxyethylene (20) sorbitan monooleate (Polysorbate 80);

mixing the oil concentrator with the byproduct stream;

applying centrifugal force after mixing the oil concentrator with the byproduct stream to enable the formation of a separable oil phase and aqueous phase, wherein the oil concentrator is distributed between the oil phase and the aqueous phase: and separating the oil from the byproduct stream.

8. A method of extracting oil from a byproduct stream of a bio-based ethanol production process under conditions in which there is an attraction between oil and oil sequestering components in the byproduct stream, the method comprising:

evaporating water from the byproduct stream;

subsequently applying an oil concentrator to the byproduct stream of the bio-based ethanol production process with the byproduct stream at a pH between 3 and 7, wherein the oil concentrator is a surfactant compound having a hydrophilic group and a lipophilic group providing the oil concentrator a hydrophile-lipophile balance (HLB) of about 14 to about 16 wherein the oil concentrator is an FDA acceptable direct food additive for humans and animals, said food additive selected from the group consisting of polyoxyethylene (20) sorbitan monostearate (Polysorbate 60), polyoxyethylene (20) sorbitan tristearate (Polysorbate 65), and polyoxyethylene (20) sorbitan monooleate (Polysorbate 80);

mixing the oil concentrator with the byproduct stream;

separating the oil from the byproduct stream;

and

drying the byproduct stream after said oil separating step to produce a distillers dried grains.

9. The method of extracting oil from the byproduct stream of the bio-based ethanol production process of claim 7 , wherein the byproduct stream comprises an aqueous liquid byproduct stream with dissolved solids.

10. The method of extracting oil from the byproduct stream of the bio-based ethanol production process of claim 9 , wherein the byproduct stream comprises a thin stillage or syrup derived therefrom.

11. The method of extracting oil from the byproduct stream of the bio-based ethanol production process of claim 9 , wherein adding the oil concentrator into the aqueous liquid byproduct stream includes adding an amount of oil concentrator so that the oil concentrator concentration is below a critical micellar concentration for the oil concentrator in the aqueous liquid byproduct stream.

12. The method of extracting oil from the byproduct stream of the bio-based ethanol production process of claim 8 , wherein the byproduct stream comprises an aqueous liquid byproduct stream with dissolved solids.

13. The method of extracting oil from the byproduct stream of the bio-based ethanol production process of claim 12 , wherein the byproduct stream comprises a thin stillage or syrup derived therefrom.

14. The method of extracting oil from the byproduct stream of the bio-based ethanol production process of claim 12 , wherein adding the oil concentrator into the aqueous liquid byproduct stream includes adding an amount of oil concentrator so that the oil concentrator concentration is below a critical micellar concentration for the oil concentrator in the aqueous stream.

Assignments (12)
SECURITY INTEREST Recorded Nov 14, 2025
From: CHEM-AQUA, INC.; DIVERSEY, INC.; DIVERSEY TASKI, INC.; INNOVATIVE WATER CARE, LLC; NCH CORPORATION; NCH LIFE SCIENCES LLC; SOLENIS TECHNOLOGIES, L.P.
To: THE BANK OF NEW YORK MELLON TRUST COMPANY, N.A., AS NOTES COLLATERAL AGENT
Reel/Frame 073570/0838 →
RELEASE OF SECURITY INTEREST Recorded Nov 14, 2025
From: THE BANK OF NEW YORK MELLON TRUST COMPANY, N.A., AS NOTES COLLATERAL AGENT
To: BIRKO CORPORATION; DIVERSEY, INC.; DIVERSEY TASKI, INC.; INNOVATIVE WATER CARE, LLC; SOLENIS TECHNOLOGIES, L.P.
Reel/Frame 073564/0864 →
RELEASE OF 2023 NOTES PATENT SECURITY INTERESTS Recorded Oct 10, 2025
From: THE BANK OF NEW YORK MELLON TRUST COMPANY, N.A.
To: BIRKO CORPORATION; DIVERSEY, INC.; DIVERSEY TASKI, INC.; INNOVATIVE WATER CARE, LLC; SOLENIS TECHNOLOGIES, L.P.
Reel/Frame 073074/0198 →
SECURITY AGREEMENT (NOTES) Recorded Oct 10, 2025
From: DIVERSEY, INC.; DIVERSEY TASKI, INC.; INNOVATIVE WATER CARE, LLC; SOLENIS TECHNOLOGIES, L.P.
To: THE BANK OF NEW YORK MELLON TRUST COMPANY, N.A., AS NOTES COLLATERAL AGENT
Reel/Frame 073061/0885 →
SECURITY AGREEMENT (2024 NOTES) Recorded Jun 24, 2024
From: BIRKO CORPORATION; DIVERSEY, INC.; DIVERSEY TASKI, INC.; INNOVATIVE WATER CARE, LLC; SOLENIS TECHNOLOGIES, L.P.
To: THE BANK OF NEW YORK MELLON TRUST COMPANY, N.A., AS NOTES COLLATERAL AGENT
Reel/Frame 067824/0278 →
2023 NOTES PATENT SECURITY AGREEMENT Recorded Jul 7, 2023
From: BIRKO CORPORATION; SOLENIS TECHNOLOGIES, L.P.; INNOVATIVE WATER CARE, LLC; DIVERSEY, INC.; DIVERSEY TASKI, INC.; INNOVATIVE WATER CARE GLOBAL CORPORATION
To: BANK OF NEW YORK MELLON TRUST COMPANY, N.A.
Reel/Frame 064225/0170 →
SECURITY AGREEMENT (NOTES) Recorded Sep 14, 2022
From: SOLENIS TECHNOLOGIES, L.P.; INNOVATIVE WATER CARE, LLC
To: THE BANK OF NEW YORK MELLON TRUST COMPANY, N.A. AS COLLATERAL AGENT
Reel/Frame 061432/0821 →
NOTES SECURITY AGREEMENT Recorded Nov 10, 2021
From: INNOVATIVE WATER CARE, LLC; SOLENIS TECHNOLOGIES, L.P.
To: THE BANK OF NEW YORK MELLON TRUST COMPANY, N.A.
Reel/Frame 058103/0066 →
TERM LOAN PATENT SECURITY AGREEMENT Recorded Nov 10, 2021
From: INNOVATIVE WATER CARE, LLC; SOLENIS TECHNOLOGIES, L.P.
To: GOLDMAN SACHS BANK USA
Reel/Frame 058102/0407 →
ABL PATENT SECURITY AGREEMENT Recorded Nov 10, 2021
From: INNOVATIVE WATER CARE, LLC; SOLENIS TECHNOLOGIES, L.P.
To: BANK OF AMERICA, N.A.
Reel/Frame 058102/0122 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 18, 2021
From: FRODERMAN, CHRISTOPHER S.; HILDEBRAND, WILLIAM C.
To: SUPERIOR OIL COMPANY INC.
Reel/Frame 055634/0160 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 18, 2021
From: SUPERIOR OIL COMPANY INC.
To: SOLENIS TECHNOLOGIES, L.P.
Reel/Frame 055634/0188 →
Continuity (3)
Continuation 14627618 · Feb 20, 2015
Continuation 13117301 · May 27, 2011
Related Publication 20180242626A1 · Aug 30, 2018