PROCESS FOR DEGUMMING OILS

• US 20160108338A1
• Filed: 10/15/2014
• Published: 04/21/2016
• Est. Priority Date: 10/15/2014
• Status: Active Grant

• Current Assignee: Archer Daniels Midland Company
• Original Assignee: Arisdyne Systems Incorporated
• Inventors: Kozyuk, Oleg, Reimers, Peter, Reinking, Paul A.
• Granted Patent: US 9,453,180 B2
• Time in Patent Office: Days
• US Class Current: 1/1
• CPC Class Codes: C11B 3/001 by a combination of two or more of the means hereafter
• CPC Class Codes: C11B 3/04 with acids
• CPC Class Codes: C11B 3/06 with bases
• CPC Class Codes: C11B 3/16 by mechanical means
• CPC Class Codes: G11B 3/06 Determining or indicating positions of head

Abstract

A multi-stage agitation system is used for degumming vegetable oil to increase yield and reduce phosphatides. A high-shear mixing phase, that can include multiple stages, subjects an oil mixed with acid and base to a shear rate of greater than 15,000 s⁻¹ to form a neutralized oil mixture. A low-shear mixing phase is further used to disperse water into the neutralized oil mixture. A separation step can be used to remove the phosphatides from the treated oil to form a degummed oil product.

Claims

1. A process for degumming oil, comprising:

adding an acid to an oil to form an acid-oil mixture;

mixing an aqueous base with the acid-oil mixture at high shear with an agitation mixer, the mixing being at a shear rate of greater than 15,000 s<sup>−

1</sup> to form a neutralized oil mixture;

adding 0.2 to 4 weight percent of water to the neutralized oil mixture, the water measured by the total weight of the oil in the neutralized oil mixture;

mixing the water added neutralized oil mixture in an agitation mixer at a transitional state flow measuring a Reynolds number (N_Re) in the range of from 10 to 1000 to disperse the water in neutralized oil mixture;

separating a portion of the water in the neutralized oil mixture to obtain a degummed oil.

2. The process of claim 1, wherein the agitation mixer operating at a shear rate of greater than 15,000 s⁻

1 is selected from a group consisting of high-speed pumps, colloid mills, high-pressure jet nozzles, static mixers, high-pressure valve type homogenizers, turbine type rotor-rotor and rotor-stator homogenizers, hydrodynamic cavitation reactors and ultrasonic cavitation devices.

3. The process of claim 1, wherein the oil is a vegetable oil and the vegetable oil is a crude oil or water-degummed oil.

4. The process of claim 1, wherein the acid is selected from the group consisting of phosphoric acid, hydrochloric acid, sulfuric acid, ascorbic acid, acetic acid, citric acid, fumaric acid, maleic acid, tartaric acid, succinic acid, glycolic acid, or a combination thereof.

5. The process of claim 1, wherein the base of the aqueous base is selected from the group consisting of sodium hydroxide, potassium hydroxide, sodium silicate, sodium carbonate, calcium carbonate, or a combination thereof.

6. The process of claim 1, wherein the Reynolds number is in the range of 100 to 600.

7. The process of claim 1, wherein the phosphatide content of the degummed oil is at least 90 weight percent less than the phosphatide content of the oil used to form the acid-oil mixture.

8. The process of claim 1, wherein the phosphatide content of the degummed oil is at least 95 weight percent less than the phosphatide content of the oil used to form the acid-oil mixture.

9. The process of claim 1, the oil used to form the acid-oil mixture having a phosphatide content greater than 200 ppm and the degummed oil having a phosphatide content of less than 50 ppm.

10. The process of claim 1, the oil used to form the acid-oil mixture having a phosphatide content greater than 500 ppm and the degummed oil having a phosphatide content of less than 50 ppm.

11. A process for the degumming oil, comprising:

adding an acid to an oil to form an acid-oil mixture;

mixing an aqueous base with the acid-oil mixture, and subjecting the acid-oil mixture containing the aqueous base to a multi-stage agitation to form a neutralized oil mixture, wherein each stage of the multi-stage agitation mixes the aqueous base and the acid-oil mixture at a shear rate of greater than 15,000 s<sup>−

1</sup>;

adding 0.2 to 4 weight percent of water to the neutralized oil mixture, the water measured by the total weight of the oil in the neutralized oil mixture;

mixing the neutralized oil mixture in an agitation mixer at a transitional state flow measuring a Reynolds number (N_Re) in the range of from 10 to 1000 to disperse the water in neutralized oil mixture;

separating a portion of the water in the neutralized oil mixture to obtain a degummed oil.

12. The process of claim 11, wherein each stage of the multi-stage agitation mixes the acid-oil mixture and the aqueous base at a shear rate of greater than 20,000 s⁻

1.

13. The process of claim 11, the multi-stage agitation having at least two stages.

14. The process of claim 11, the multi-stage agitation having at least three stages.

15. The process of claim 11, the multi-stage agitation having at least four stages.

16. The process of claim 11, the multi-stage agitation having one stage that mixes the acid-oil mixture and the aqueous base at a shear rate of greater than 50,000 s⁻

1.

17. The process of claim 16, the multi-stage agitation having one stage that mixes the acid-oil mixture and the aqueous base at a shear rate of greater than 100,000 s⁻

1.

18. The process of claim 16, wherein the phosphatide content of the degummed oil is at least 90 weight percent less than the phosphatide content of the oil used to form the acid-oil mixture.

19. The process of claim 16, the oil used to form the acid-treated oil having a phosphatide content greater than 200 ppm and the degummed oil having a phosphatide content of less than 50 ppm.

20. The process of claim 11, the multi-stage agitation having a series of at least three orifices, wherein the first orifice in the series mixes the acid-oil mixture and the aqueous base at a shear rate of greater than 100,000 s⁻

1 and the second orifice and the third orifice in the series mixes the acid-oil mixture and the aqueous base at a shear rate of greater than 50,000 s<sup>−

1</sup>.