IP Library Granted Patent US 9,353,331
Granted Patent B2
US 9,353,331 · App. 14/079,059 · Granted May 31, 2016

Method to recover free fatty acids from fats and oils

Inventors: Mohan Prasad A. Dasari (West Des Moines, IA); Kidron Joel Knox (Ankeny, IA)
Assignee: RRIP, LLC
C11B3/04C11B3/00C11B7/0008C11B7/0066
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Quick Facts
Patent No.
US 9,353,331
App. No.
14/079,059
Granted
May 31, 2016
Kind
B2
Abstract

Methods for recovering free fatty acids from fats and oils having high free fatty acid content are provided. In the method, fats and oils are treated with a mixture having an alcohol to result in a low-free fatty acid oily phase and an alcohol phase. The mixture may also include an alkali. The alcohol may be a monohydric alcohol and an aqueous alcohol, such as an aqueous alcohol having a concentration of at least about 15% alcohol by weight. The alcohol phase may be treated with an acid to form an aqueous alcohol phase and a lipid alcohol phase, wherein the lipid alcohol phase includes free fatty acids, which may be recovered. Fats and oils amenable to such a method may include, but are not limited to, waste fats, waste oils, high acid grease, high acid tallow, and corn oil, such as corn oil produced at an ethanol production plant.

Claims (49)

1. A method to recover free fatty acids from fats and oils comprising:

treating fats and oils having a high free fatty acid content with a mixture comprising a monohydric alcohol to form a low-free fatty acid oily phase and an alcohol phase wherein said monohydric alcohol is a solvent;

said monohydric alcohol having a concentration of at least about 15% alcohol by weight;

treating said alcohol phase with an acid to form an aqueous alcohol phase and a lipid alcohol phase, wherein said lipid alcohol phase comprises free fatty acids; and

recovering fatty acids from said lipid alcohol phase.

2. The method of claim 1 wherein said mixture comprising a monohydric alcohol further comprises an alkali.

3. The method of claim 2 wherein said low-free fatty acid oily phase is further treated with at least one of a monohydric alcohol, aqueous monohydric alcohol, water, acid, or a combination thereof.

4. The method of claim 2 wherein said monohydric alcohol is selected from the group consisting of methanol, aqueous methanol, ethanol, aqueous ethanol, propanol, aqueous propanol, isopropanol, aqueous isopropanol, butanol, aqueous butanol, isobutanol, aqueous isobutanol, pentanol, aqueous pentanol, and combinations thereof.

5. The method of claim 4 wherein said alcohol is an aqueous alcohol comprising about 15% to 55% ethanol by weight.

6. The method of claim 2 wherein said the step of treating said fats and oils with a mixture comprising an alcohol and an alkali to form a low-free fatty acid oily phase and an alcohol phase is carried out at about 25 to 75 degrees Celsius and about atmospheric pressure.

7. The method of claim 6 wherein the step of treating said fats and oils with a mixture comprising an alcohol and an alkali to form a low-free fatty acid oily phase and an alcohol phase is carried out at about 65 degrees Celsius.

8. The method of claim 2 wherein said acid is selected from the group consisting of carbonic acid formed by treating said alcohol phase with carbon dioxide, sulfuric acid, hydrochloric acid, phosphoric acid, citric acid, oxalic acid, and combinations thereof.

9. The method of claim 2 wherein said fats and oils are selected from the group consisting of waste fats, waste oils, high acid grease, high acid tallow, corn oil, used cooking oil and combinations thereof.

10. The method of claim 2 wherein said fats and oils are first treated with a mixture comprising an alcohol and an acid.

11. The method of claim 2 wherein said fatty acids are recovered by using a process selected from the group consisting of drying, evaporation, distillation, and combinations thereof.

12. The method of claim 2 wherein said acid is added to said alcohol phase until the pH of said alcohol phase is at least 6.

13. The method of claim 2 wherein said acid is added to said alcohol phase until the pH of said alcohol phase is 2.

14. The method of claim 2 wherein said fats and oils have a free fatty acid content of at least 4%.

15. The method of claim 2 wherein the neutral oil loss of the process is less than 10%.

16. The method of claim 15 wherein the neutral oil loss of the process is less than 3%.

17. The method of claim 2 wherein the ratio of aqueous monohydric alcohol to oil is about 0.4-0.75.

18. A method to recover free fatty acids from fats and oils comprising:

treating fats and oils having a high free fatty acid content with a mixture consisting essentially of an aqueous alcohol and an alkali to form a low-free fatty acid oily phase and an alcohol phase and wherein said aqueous alcohol is a solvent;

treating said alcohol phase with an acid to form an aqueous alcohol phase and a lipid alcohol phase, wherein said lipid alcohol phase comprises free fatty acids; and

recovering fatty acids from said lipid alcohol phase;

wherein said aqueous alcohol has a concentration of at least about 15% alcohol by weight.

19. A method to recover free fatty acids from corn oil comprising:

said corn oil having a free fatty acid content of at least 4%;

treating said corn oil with a mixture comprising an aqueous alcohol and an alkali to form a low-free fatty acid oily phase and an alcohol phase and wherein

said aqueous alcohol is a solvent;

treating said alcohol phase with an acid to form an aqueous alcohol phase and a lipid alcohol phase, wherein said lipid alcohol phase comprises free fatty acids; and

recovering fatty acids from said lipid alcohol phase;

wherein said aqueous alcohol is selected from the group consisting of aqueous methanol, aqueous ethanol, aqueous propanol, aqueous isopropanol, aqueous butanol, aqueous isobutanol, aqueous pentanol, and combinations thereof; and

wherein said aqueous alcohol has a concentration comprising at least about 15% alcohol by weight.

20. The method of claim 19 wherein said aqueous alcohol is an aqueous ethanol comprising about 15% to 55% ethanol by weight.

21. The method of claim 19 wherein said alkali is selected from the group consisting of sodium hydroxide, potassium hydroxide, magnesium hydroxide, calcium hydroxide, lithium hydroxide, sodium amide, ammonia, and combinations thereof.

22. The method of claim 19 wherein said acid is selected from the group consisting of sulfuric acid, hydrochloric acid, phosphoric acid, citric acid, oxalic acid, carbonic acid produced by treating said alcohol phase with carbon dioxide, and combinations thereof.

23. A method to recover free fatty acids from corn oil produced in an ethanol production facility comprising:

collecting corn oil produced in an ethanol production facility, said corn oil having a free fatty acid content of at least 4%;

treating said corn oil with a mixture comprising an aqueous ethanol having a concentration of at least about 1.5% percent ethanol by weight and an alkali to form a low-free fatty acid oily phase and an alcohol phase and wherein said aqueous alcohol is a solvent;

said alcohol phase comprising free fatty acid soaps;

treating said alcohol phase with an acid to form an aqueous alcohol phase and a lipid alcohol phase, said lipid alcohol phase comprising free fatty acids; and

recovering said free fatty acids.

24. A method to recover free fatty acids from corn oil produced in an ethanol production facility comprising:

collecting corn oil produced in an ethanol production facility, said corn oil having a free fatty acid content of at least 4%;

treating said corn oil with a mixture comprising an aqueous ethanol having a concentration of about at least 15% percent ethanol by weight and an alkali to form a low-free fatty acid oily phase and an alcohol phase and wherein said aqueous alcohol is a solvent;

said alcohol phase comprising free fatty acid soaps;

treating said alcohol phase with carbon dioxide to form an aqueous alcohol phase and a lipid alcohol phase, said lipid alcohol phase comprising free fatty acids; and

recovering said free fatty acids.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 21, 2015
From: RIVERHEAD RESOURCES
To: RRIP, LLC
Reel/Frame 035458/0134 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 4, 2014
From: DASARI, MOHAN PRASAD A.; KNOX, KIDRON JOEL
To: RIVERHEAD RESOURCES, L.L.C.
Reel/Frame 033457/0477 →
Continuity (3)
Provisional Application 61725598 · Nov 13, 2012
Provisional Application 61793727 · Mar 15, 2013
Related Publication 20140135515A1 · May 15, 2014