IP Library Granted Patent US 6,909,021
Granted Patent B2
US 6,909,021 · App. 10/770,345 · Granted Jun 21, 2005

Method of extracting lutein from green plant materials

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Quick Facts
Patent No.
US 6,909,021
App. No.
10/770,345
Granted
Jun 21, 2005
Kind
B2
Abstract

The present invention provides a method for extracting carotenoids from green plant materials using supercritical fluid extraction. A first and second supercritical fluid extraction is performed on the green plant composition at two different pressures to obtain two extracts. The first extract includes substantial amounts of β-carotene. The second extract may have a controlled concentration of β-carotene, and includes substantial amounts of lutein.

Claims (51)

1. A method for obtaining lutein from green plant materials comprising:

performing a first supercritical fluid extraction of a green plant material at a first pressure and temperature to obtain a first extract;

performing a second supercritical fluid extraction of the green plant material at a second pressure and temperature to obtain a second extract that includes a higher concentration of lutein than the concentration of lutein in the first extract, and

separating the second extract from the supercritical fluid.

2. The method of claim 1 wherein the green plant material is derived from dried green plants or green plant fractions.

3. The method of claim 1 wherein the first extract comprises β-carotene, at least one fatty acid, or both.

4. The method of claim 1 wherein the first supercritical fluid extraction is performed to reduce the concentration of β-carotene, fatty acid, or both in the green plant material.

5. The method of claim 1 wherein the first supercritical fluid extraction is performed to reduce the concentration of coumesterol in the green plant material.

6. The method of claim 1 wherein the first supercritical fluid extraction is performed to reduce the concentration of chlorophyll in the green plant material.

7. The method of claim 1 wherein the first supercritical fluid extraction is performed to reduce the concentration of odor or flavor-producing compounds in the green plant material.

8. The method of claim 1 wherein the second extract comprises β-carotene.

9. The method of claim 1 wherein the second extract comprises between about 10 and about 60 weight percent β-carotene.

10. The method of claim 1 wherein the concentration of β-carotene in the second extract is loss than in the first extract.

11. The method of claim 1 wherein the second extract comprises at least one fatty acid.

12. The method of claim 11 wherein the second abstract comprises less than about 20 weight percent fatty acid.

13. The method of claim 1 wherein the second extract is free of hormones.

14. The method of claim 1 wherein the second extract is free of coumesterol.

15. The method of claim 1 wherein the second extract is substantially free of chlorophyll.

16. The method of claim 1 wherein the first and second pressures are between about 10 and about 120 MPa.

17. The method of claim 1 wherein the first pressure is lower than the second pressure.

18. The method of claim 1 wherein the first pressure is between about 10 and about 40 MPa.

19. The method of claim 1 wherein the second pressure is between about 41 and about 80 MPa.

20. The method of claim 1 wherein the first pressure is between about 15 and about 35 MPa and the second pressure is between about 55 and about 80 MPa.

21. The method of claim 1 wherein the first and second supercritical fluid extractions occur at between about 31° C. and about 100° C.

22. The method of claim 1 wherein the first temperature is lower than the second temperature.

23. The method of claim 1 wherein the first temperature is between about 31° C. and about 40° C., and the second temperature is between about 65° C. and about 75° C.

24. The method of claim 1 wherein the first and second supercritical fluid extractions occur at a substantially constant temperature.

25. The method of claim 1 wherein separating the second extract from the supercritical fluid comprises subjecting the second extract to a post-extraction pressure that is lower than the second pressure.

26. The method of claim 25 wherein the post-extraction pressure is between about 15 and about 45 MPa.

27. The method of claim 1 further comprising separating the first extract from the supercritical fluid.

28. The method of claim 27 comprising separating the first extract from the supercritical fluid by subjecting the first extract to a post-extraction pressure that is lower than the first pressure.

29. The method of claim 27 comprising combining the first and second extract.

30. The method of claim 1 comprising performing at least a third supercritical fluid extraction of the green plant material at a third pressure and temperature to obtain at least a third extract.

31. The method of claim 30 wherein the third pressure is lower or higher than the first and second pressures.

32. The method of claim 30 wherein the third pressure is higher than the first and second pressures.

33. The method of claim 30 wherein third extract comprises at least one saponin.

34. A method for obtaining a plurality of extracts from green plant material comprising

performing a first supercritical fluid extraction of the green plant material at a first pressure and temperature to obtain a first extract;

performing at least one additional supercritical fluid extraction of the green plant material at least one additional pressure and temperature to obtain at least one additional extract, wherein at least one of the additional extracts includes a higher concentration of lutein than in the first extract; and

separating at least one of the additional extracts from the supercritical fluid.

35. The method of claim 34 wherein at least one extract comprises β-carotene.

36. The method of claim 34 wherein at least one extract comprises alpha-carotene.

37. The method of claim 23 wherein at least one extract comprises at least one fatty acid.

38. The method of claim 37 wherein the green plant material is derived from alfalfa, and the fatty acid comprising linolenic acid, linoleic acid palmitic acid or oleic acid.

39. The method of claim 34 , wherein at least one extract comprises xanthophyll, zeaxanthin, astaxanthin, canthaxanthin, capsorubin, or cryptoxanthin.

40. The method of claim 34 wherein at least one of the extracts comprises coumesterol.

41. The method of claim 34 wherein at least one extract comprises a mixture of at least two nutrients.

42. The method of claim 34 wherein at least one of the additional extracts comprises a mixture of lutein and β-carotene.

43. The method of claim 43 wherein the additional extract comprises between about 20 and about 60 weight percent lutein and between about 20 and about 60 weight percent β-carotene.

44. The method of claim 42 wherein the additional extract further comprises at least one fatty acid.

45. The method of claim 44 further comprising between about 5 and about 20 weight percent of at least one fatty acid.

Assignments (5)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 11, 2007
From: ALFALFA AMERICA, INC.
To: PANDORA SELECT PARTNERS, L.P.; WHITEBOX HEDGED HIGH YIELD PARTNERS, L.P.
Reel/Frame 019805/0484 →
SECURITY AGREEMENT Recorded Jun 13, 2006
From: ALFALFA AMERICA, INC.
To: PANDORA SELECT PARTNERS L.P.; WHITEBOX HEDGED HIGH YIELD PARTNERS, L.P.
Reel/Frame 017766/0814 →
SECURITY AGREEMENT Recorded Apr 8, 2005
From: ALFALFA AMERICA, INC.
To: PANDORA SELECT PARTNERS, L.P.
Reel/Frame 015878/0028 →
CORRECTIVE ASSIGNMENT TO CORRECT THE ASSIGNEE ADDRESS PREVIOUSLY RECORDED ON REEL 015724 FRAME 0950. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNEE ADDRESS IS ALFALFA AMERICA, INC., 805 ENTERPRISE DRIVE, BELLE PLAINE, MN 56011. Recorded Mar 4, 2005
From: CROMBIE, LANCE B.
To: ALFALFA AMERICA, INC.
Reel/Frame 015729/0317 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 3, 2005
From: CROMBIE, LANCE B.
To: ALFALFA AMERICA, INC.
Reel/Frame 015724/0950 →