Process for extracting oleaginous seed materials particularly cottonseed with aqueous alcohol

• US 4,359,417 A
• Filed: 02/25/1981
• Issued: 11/16/1982
• Est. Priority Date: 02/25/1981
• Status: Expired due to Term

• Current Assignee: DAVY Mckee Corporation
• Original Assignee: Dravo Corporation
• Inventors: Karnofsky, George B., Hansotte, Roger J.
• Primary Examiner(s): SCHAIN, HOWARD
• Application Number:
  US06/238,034
• Time in Patent Office: 629 Days
• Field of Search: 260/123.5
• US Class Current: 530/377
• CPC Class Codes: C11B 1/108 after-treatment, e.g. of miscellae

Abstract

There is disclosed a process for extracting oleaginous seed material consisting in part of solubles comprising carbohydrates, fatty-acids, non-oil lipids and oils with a less concentrated aqueous solution of a monohydric alcohol selective for the extraction of the solubles other than the carbohydrates and oil followed by a contact of the resulting particulate solids with a concentrated aqueous solution of a monohydric alcohol for the extraction of oil.

Claims

1. In a process for forming residue meal by extracting oil from an oleaginous seed material consisting in part of components comprising carbohydrates, fatty acids, non-oil lipids and oil wherein the oil is extracted last by a concentrated aqueous solution of a monhydric alcohol, the improvement comprising first contacting said oleaginous seed material with an aqueous solution of said monohydric alcohol less concentrated than said concentrated aqueous solution thereof, and at a concentration to form a miscella by selectively extracting substantially all of said components other than said carbohydrates and oil from said oleaginous seed material with minimal extraction of said carbohydrates.

2. The process as defined in claim 1 wherein said monohydric alcohol is selected from the group consisting of methanol, ethanol, isopropanol and mixtures thereof.

3. The process as defined in claim 2 wherein said monohydric alcohol is ethanol.

4. The process as defined in claim 1 wherein oleaginous seed material is cottonseed or cottonseed press cake.

5. The process as defined in claim 4 wherein said cottonseed or cottonseed press cake includes gossypol as a component extractable by said less concentrated monohydric alcohol solution.

6. The process as defined in claim 5 wherein said contacting is effected at a temperature between 90°

to 150°

F.

7. The process as defined in claim 6 wherein said less concentrated monohydric alcohol solution is 80 to 90 weight percent ethanol.

8. The process as defined in claim 1 wherein aflatoxin is a component extractable by said less concentrated monohydric alcohol solution and the temperature of said contacting is 160°

to 180°

F.

9. The process as defined in claim 8 wherein said less concentrated monohydric alcohol solution is 80 to 90 weight percent ethanol.

10. The process as defined in claim 4 wherein said cottonseed or cottonseed press cake contains both gossypol and aflatoxin as components extractable by said less concentrated monohydric alcohol solution and said contacting is effected sequentially:

a first contacting, at a temperature between 90°

to 150°

F. to preferentially extract said gossypol; and

a second contacting, at a temperature between 160°

to 180°

F. to extract aflatoxin.

11. The process as defined in claim 10 wherein said less concentrated monohydric alcohol solution is 85 weight percent ethanol, the temperature of said first contacting is 110°

F. and the temperature of said second contacting is 175°

F.

12. The process as defined in claim 1 wherein said contacting is effected at a temperature above 110°

F. the process further comprising cooling said miscella to form an oil phase and recycling said oil phase to said contacting.

13. A process for extracting oil from oleaginous seed material consisting in part of components comprising carbohydrates, fatty acids, non-oil lipids and oil, which comprises:

(a) particulating said oleaginous seed material to form extractable particles;

(b) contacting said particles with a less concentrated aqueous solution of a monohydric alcohol to selectively extract all of said components othe than said carbohydrates and oil with minimal extraction of said carbohydrates an oil;

(c) separating a miscella from the particles of step (b);

(d) contacting said particles of step (c) with a concentrated aqueous solution of said monohydric alcohol at a temperature at or near the boiling point to displace said less concentrated aqueous solution of said monohydric alcohol therefrom;

(e) separating a miscella from the particles of step (d);

(f) contacting said particles of step (e) with a concentrated aqueous solution of said monohydric alcohol at a temperature at or near the boiling point to extract substantially all of said oil;

(g) separating an oil-enriched miscella from the particles of step (f);

(h) cooling said oil-enriched miscella of step (g) to separate a solvent phase from an oil phase;

(i) returning said solvent phase to step (f);

(j) withdrawing said oil phase from the process; and

(k) desolventizing the particles resulting from step (g) to yield a residue meal including unextracted carbohydrates.

14. The process as defined in claim 13 wherein said monohydric alcohol is selected from the group consisting of methanol, ethanol, isopropanol and mixtures thereof.

15. The process as defined in claim 14 wherein said monohydric alcohol is ethanol.

16. The process as defined in claim 13 wherein said oleaginous seed material is cottonseed or cottonseed press cake.

17. The process as defined in claim 16 wherein said cottonseed or cottonseed press cake includes gossypol as a component extractable by said less concentrated monohydric alcohol solution.

18. The process as defined in claim 17 wherein step (b) is effected at a temperature between 90°

to 150°

F.

19. The process as defined in claim 18 wherein said less concentrated aqueous solution of said monohydric alcohol is 80 to 90 weight percent ethanol.

20. The process as defined in claim 13 wherein aflatoxin is a component extractable by said less concentrated aqueous solution in step (b) and temperature of step (b) is 160°

to 180°

F.

21. The process as defined in claim 20 wherein said less concentrated aqueous solution of said monohydric alcohol is 80 to 90 weight percent ethanol.

22. The process as defined in claim 16 wherein said cottonseed or cottonseed press cake contains both gossypol and aflatoxin as components extractable by said less concentrated aqueous solution of said monohydric alcohol and step (b) is effected sequentially:

first, at a temperature between 90° and

150°

F. to preferentially extract said gossypol; and

second, at a temperature between 160° and

180°

F. to extract said aflatoxin.

23. The process as defined in claim 22 wherein said less concentrated aqueous solution of said monohydric alcohol is 85 weight percent ethanol and said sequential temperatures are 110°

F. and 175°

F.

24. The process as defined in claim 13 wherein step (b) is effected at a temperature above 110°

F. and the miscella of said components separated in step (c) is cooled to separate a solvent phase and an oil phase; and

said oil phase is recycled to step (b).

25. The process as defined in claim 13 wherein water is added to said miscella separated in step (e), the mixture comprising at least a portion of said less concentrated aqueous solution of said monohydric alcohol of step (b).

26. The process as defined in claim 25 wherein the remaining portion of said less concentrated aqueous solution of said monohydric alcohol comprises a distillate from the distillation of the miscella separated in step (c).

27. The process as defined in claim 26 wherein said miscella withdrawn from step (f) constitutes said concentrated aqueous solution of said monohydric alcohol of step (d).