Methods of refining a grain oil composition

Patent metadata

Field	Value
Publication number	US-11530369-B2
Application number	US-202017026771-A
Country	US
Kind code	B2
Filing date	Sep 21, 2020
Priority date	Jun 11, 2018
Publication date	Dec 20, 2022
Grant date	Dec 20, 2022

Abstract

The present disclosure relates methods and systems for refining grain oil compositions using water, and related compositions produced therefrom. The present disclosure also relates to methods of using said compositions. The present disclosure also relates to methods of using grain oil derived from a fermentation product in an anti-foam composition.

First claim

What is claimed is:

1. A method of refining a grain oil composition feedstock to provide a grain oil product, wherein the method comprises:
combining the grain oil composition feedstock with water to form an oil-water mixture, wherein the grain oil composition comprises an impurity component, and wherein the oil-water mixture does not include chelating agent in an amount to aid in removal of metals and metal compounds from the grain oil composition feedstock;
exposing the oil-water mixture to a temperature in the range from 0° C. to 50° C. for a time period at least until the oil-water mixture forms at least an oil phase and an emulsion phase; and
separating at least a portion of the oil phase from the emulsion phase to form the grain oil product, wherein an amount of the impurity component in the emulsion phase is greater than an amount of the impurity component in the grain oil product.

2. The method of claim 1 , wherein the grain oil composition feedstock is derived from thin stillage by a method comprising:
optionally evaporating at least a portion of water from the thin stillage to condense the thin stillage into a syrup; and
separating the thin stillage or syrup into a first oil fraction and a first aqueous fraction, wherein the first oil fraction is the grain oil composition feedstock.

3. The method of claim 1 , wherein the grain oil composition feedstock is derived from thin stillage by a method comprising:
optionally evaporating at least a portion of water from the thin stillage to condense the thin stillage into a syrup;
separating the thin stillage or syrup into a first oil fraction and a first aqueous fraction, wherein the first oil fraction is an emulsion; and
breaking the emulsion to separate the first oil fraction into a second oil fraction and a second aqueous fraction, wherein the second oil fraction is the grain oil composition feedstock.

4. The method of claim 3 , wherein the emulsion is broken by adjusting the pH of the emulsion.

5. A method of refining a grain oil composition feedstock to provide a grain oil product, wherein the method comprises:
combining the grain oil composition feedstock with water to form an oil-water mixture having water in an amount of 3-40% based on the total volume of the oil-water mixture (v/v), wherein the grain oil composition comprises an impurity component, wherein the impurity component comprises an element component, wherein the element component comprises at least one element chosen from calcium, phosphorus, potassium, sodium, magnesium and combinations thereof; and wherein the oil-water mixture does not include chelating agent in an amount to aid in removal of metals and metal compounds from the grain oil composition feedstock,
exposing the oil-water mixture to a temperature for a time period at least until the oil-water mixture forms at least an oil phase and an emulsion phase; and
separating at least a portion of the oil phase from the emulsion phase to form the grain oil product, wherein an amount of the impurity component in the emulsion phase is greater than an amount of the impurity component in the grain oil product, wherein the grain oil product comprises element component in an amount from 0-20 ppm.

6. The method of claim 5 , wherein the grain oil product comprises element component in an amount from 0-10 ppm.

7. The method of claim 5 , wherein the grain oil product comprises element component in an amount from 0-5 ppm.

8. The method of claim 5 , further comprising mixing the oil-water mixture via one or more static mixers, shear mixers, and combinations thereof to disperse water in the grain oil composition, wherein mixing occurs for a time period from 5 minutes to 5 hours.

9. The method of claim 5 , wherein grain oil composition feedstock is derived from whole stillage by a method comprising:
separating whole stillage into thin stillage and wet cake;
optionally evaporating at least a portion of water from the thin stillage to condense the thin stillage into a syrup;
separating the thin stillage or syrup into an oil fraction and an aqueous fraction, wherein the oil fraction is the grain oil composition feedstock.

10. The method of claim 5 , wherein grain oil composition feedstock is derived from whole stillage by a method comprising:
separating whole stillage into thin stillage and wet cake;
optionally evaporating at least a portion of water from the thin stillage to condense the thin stillage into a syrup;
separating the thin stillage or syrup into a first oil fraction and a first aqueous fraction, wherein the first oil fraction is an emulsion; and
breaking the emulsion to separate the first oil fraction into a second oil fraction and a second aqueous fraction, wherein the second oil fraction is the grain oil composition feedstock.

11. A method of refining a grain oil composition feedstock to provide a grain oil product, wherein the method comprises:
combining the grain oil composition feedstock with water to form an oil-water mixture, wherein the grain oil composition comprises an impurity component, wherein the impurity component comprises an element component, wherein the element component comprises at least one element chosen from calcium, phosphorus, potassium, sodium, magnesium and combinations thereof; and wherein the oil-water mixture does not include chelating agent in an amount to aid in removal of metals and metal compounds from the grain oil composition feedstock;
forming at least an oil phase and an emulsion phase from the oil-water mixture;
separating at least a portion of the oil phase from the emulsion phase to form the grain oil product, wherein an amount of the impurity component in the emulsion phase is greater than an amount of the impurity component in the grain oil product; and
filtering the grain oil product to form a permeate comprising a filtered grain oil product, wherein the filter grain oil product comprises element component in an amount from 0-20 ppm.

12. The method of claim 11 , wherein filtering comprises passing the grain oil product through a filter chosen from a cylindrical cartridge filter, a pleated cartridge filter, a sock filter, and combinations thereof.

13. The method of claim 11 , wherein filtering comprises passing the grain oil product through a filter having a nominal opening size from 1 to 10 microns.

14. The method of claim 11 , wherein filtering comprises passing the grain oil product through a filter press.

15. The method of claim 11 , wherein the grain oil product comprises element component in an amount from 0-10 ppm.

16. The method of claim 11 , wherein the forming comprises mixing the oil-water mixture via one or more static mixers, shear mixers, and combinations thereof to disperse water in the grain oil composition and form at least the oil phase and the emulsion phase from the oil-water mixture.

17. The method of claim 16 , wherein mixing occurs for a time period from 5 minutes to 5 hours.

18. A method of refining a grain oil composition feedstock to provide a grain oil product, wherein the method comprises:
combining the grain oil composition feedstock with water to form an oil-water mixture, wherein the grain oil composition comprises an impurity component;
exposing the oil-water mixture to a temperature for a time period at least until the oil-water mixture forms at least an oil phase and an emulsion phase; and
filtering at least a portion of the oil phase from the emulsion phase to form a permeate comprising a filtered grain oil product, wherein an amount of the impurity component in the emulsion phase is gr

Assignees

• Poet Res Inc

Inventors

• Urban Shannon S
• Sarks Cory J
• Flittie Brett A
• Milbrandt Jacob A
• Bly Steven T
• Mccurdy Alex T

Classifications

• C11B1/14

  with hot water or aqueous solutions · CPC title

• C11B1/04

  of vegetable raw material {(C11B1/025 takes precedence)} · CPC title

• C11B3/00

  Refining fats or fatty oils · CPC title

• C11B13/00 Primary

  Recovery of fats, fatty oils or fatty acids from waste materials · CPC title

• C11B3/12

  by distillation · CPC title