Stable lycopene concentrates and process for their preparation

• US 5,965,183 A
• Filed: 04/30/1997
• Issued: 10/12/1999
• Est. Priority Date: 10/31/1994
• Status: Expired due to Term

• Current Assignee: Lycored Limited (ADAMA Ltd.)
• Original Assignee: Abraham Wolf, Dov Hartal, Yigal Raveh
• Inventors: Hartal, Dov, Wolf, Abraham, Raveh, Yigal
• Primary Examiner(s): CANO, MILTON I
• Application Number:
  US08/817,889
• Time in Patent Office: 895 Days
• Field of Search: 426/250, 426/262, 426/270, 426/302, 426/540, 426/481, 426/478, 426/651, 426/489
• US Class Current: 426/250
• CPC Class Codes: A23L 5/44 using carotenoids or xanthophylls

Abstract

A process for a preparing stable lycopene concentrate in an essentially non-dissolving liquid and uses thereof is described.

Claims

1. A process for the preparation of a stable lycopene concentrate which comprises placing lycopene crystals in a liquid medium which does not substantially dissolve lycopene;

and grinding the lycopene crystals to an average particle size of below about 5 μ

m.

2. A process according to claim 1, wherein the liquid medium is selected from the group consisting of glycerol, propylene glycol, ethanol, water, a water soluble liquid, a water miscible liquid, or mixtures thereof.

3. A process according to claim 2, wherein the lycopene crystals are ground to an average particle size of about 1-3 μ

m.

4. A process according to claim 1 wherein the lycopene crystals are ground to an average particle size of about 1-3 μ

m.

5. A process according to claim 1 wherein the liquid medium further comprises antioxidant, a preservative or a combination thereof.

6. A stable lycopene concentrate comprising lycopene crystals suspended in a food compatible or cosmetically or pharmaceutically acceptable liquid which does not substantially dissolve lycopene, wherein the lycopene crystals have an average particle size below about 5 μ

m.

7. A concentrate according to claim 6, wherein the liquid in which the lycopene crystals are suspended is a food-compatible or cosmetically- or pharmaceutically-acceptable liquid.

8. A concentrate according to claim 6, wherein the liquid is selected from the group consisting of glycerol, propylene glycol, ethanol, water or water soluble or water miscible liquid or mixtures thereof.

9. A concentrate according to claim 8, wherein the lycopene crystals have an average particle size of about 1-3 μ

m.

10. A concentrate according to claim 9, wherein the lycopene crystals have an average particle size of about 1-3 μ

m.

11. A concentrate according to claim 8 wherein the liquid medium further comprises an antioxidant, a preservative and mixtures thereof.

12. A concentrate according to claim 6, further composing one or more additional carotenoids.

13. A concentrate according to claim 12, wherein the additional carotenoids comprise β

-carotene.

31. A method of coloring a water-based product;

which comprises dissolving in the product a coloring-effective amount of a lycopene concentrate of claim 6 alone or together with additives and/or preservatives.

32. A method according to claim 31, wherein the water-based product is a food product or a cosmetic product or a pharmaceutical product.

14. A process for the preparation of a crystalline lycopene composition, comprising mixing a lycopene-containing oleoresin with a solvent or solvent mixture which dissolves the lipid phase of the oleoresin and which does not substantially dissolve lycopene crystals, to remove therefrom a major part of the oleoresin lipids.

15. A process according to claim 14, wherein the oleoresin is a tomato or watermelon oleoresin.

16. A process according to claim 14, wherein the solvent mixture is an acetone/ethyl acetate mixture.

17. A process according to claim 16, wherein the oleoresin contains about 2-10% lycopene, and the volumetric ratio between the oleoresin and the solvent mixture is between 1:

10 and 1;

2.

18. A process according to claim 17, wherein the ratio between acetone and ethyl acetate in the solvent mixture is about 2:

3 (v/v).

19. A process according to claim 14, wherein the oleoresin is kept in contact with the solvent mixture at a temperature of about 10°

C.

20. A process according to claim 19, wherein the temperature is about 50°

C.

21. A process according to claim 14, further comprising contacting crude lycopene-containing oleoresin with an acetone/ethyl acetate solvent mixture for a period of time and at a temperature sufficient to dissolve a substantial part of the lipid fraction in the solvent mixture, filtering the mixture to remove the fraction poor in lycopene, thereby leaving an enriched lycopene fraction, rinsing the enriched lycopene fraction with hot acetone to remove the acetone soluble materials thereby leaving a crude crystalline lycopene product.

22. A process according to claim 21, which is carried out in all stages at a temperature of about 50°

C.

23. A process according to claim 21 wherein a 1:

10 (v/v) oleoresin/solvent mixture ratio is employed, and a fraction containing more than 90 weight % crystalline lycopene is obtained.

24. A process according to claim 21 wherein a 1:

3 (v/v) oleoresin/solvent mixture ratio is employed, and a reaction containing more than 70 weight % lycopene is obtained.

25. A process according to claim 14 wherein the solvent is selected from the group consisting of ethanol, ethyl acetate, hexane, acetone, isopropanol and mixtures thereof.

26. A process for the preparation of a stable lycopene concentrate, comprising the steps of:

a) contacting crude lycopene-containing oleoresin with an acetone/ethyl acetate solvent mixture for a period of time and at a temperature sufficient to dissolve a substantial part of a lipid fraction in the solvent mixture;

b) separating the mixture to remove a substantial part of the lipid fraction thereby leaving an enriched lycopene fraction;

c) rinsing the enriched lycopene fraction with hot acetone to remove the acetone soluble materials thereby leaving, after filtration, a crystalline lycopene fraction;

d) dispersing the crystalline lycopene fraction so obtained in a food-compatible liquid which dissolve does not substantially dissolve lycopene; and

e) size-reducing the lycopene crystals in the food-compatible liquid.

27. A process according to claim 26, wherein the food-compatible liquid is selected from the group consisting of glycerol, propylene glycol, ethanol and their mixtures, or mixtures thereof.

28. A process according to claim 27, wherein the liquid is glycerol.

29. A process according to claim 27, wherein size-reduction of the lycopene crystals is effected by wet grinding.

30. A process according to claim 26, wherein the mixture is separated by filtration or centrifugation or decantation, or by a combination of two or more of such methods.