Process for the production of CLA triglycerides
View Patent ↗The invention concerns a novel process for the production of glycerol esters of polyunsaturated fatty acids, in particular of C18:2 conjugated fatty acids, by converting the polyunsaturated fatty acids with glycerol in the presence of a mixed catalyst comprising a combination of a food grade salt of a strong base and a weak acid and a soap of an organic acid with 2-26 C-atoms, preferably 10-20 C-atoms.
1. Process for the production of glycerol esters of conjugated polyunsaturated fatty acids with 18 to 24 carbon atoms and 2 to 5 double bonds by converting the conjugated polyunsaturated fatty acids with glycerol in the presence of a mixed catalyst comprising a combination of a food grade salt of a strong base and a weak acid and a soap of an organic acid with 2-26 C-atoms.
2. Process according to claim 1 wherein the weight ratio of the soap to the conjugated polyunsaturated fatty acids is between 0.01:1 and 0.6:1.
3. Process according to claim 1 or 2 wherein the weight ratio of the food grade salt to the soap is between 0.005:1 and 0.6:1.
4. Process according to claim 1 or 2 , wherein the mixed catalyst comprises a food grade salt derived from a strong base selected from the group consisting of potassium hydroxide, sodium hydroxide, ammonium hydroxide and a weak acid selected from the group consisting of carbonic acid, acetic acid, phosphoric acid.
5. Process according to claims 1 or 2 , wherein the soap is selected from the group consisting of sodium and potassium soaps of saturated and/or unsaturated fatty acids.
6. Process according to claim 1 wherein the process is carried out at a temperature of less than 175° C.
7. Process according to claim 1 wherein a molar ratio of glycerol to conjugated polyunsaturated fatty acids of between 1:1 to 1:15 is applied.
8. Process according to claim 1 wherein the soap is derived from the fatty acid applied for the conversion of the glycerol.
9. Process for the preparation of glycerol fatty acids from conjugated polyunsaturated fatty acids with 18 to 24 carbon atoms and 2 to 5 double bonds involving the steps of:
i) making a soap solution of a fatty acid by stirring of a solution of a mixture of a fatty acid and a base at 80° C.;
ii) concentrating the soap solution by eliminating water under vacuum;
iii) adding a food grade salt of a strong base and a weak acid, as well as glycerol and a conjugated polyunsaturated fatty acid with 18 to 24 carbon atoms and 2 to 5 double bonds to the soap solution and heating the mixture progressively to a temperature from 60° C. to 150° C. at less than atmospheric pressure for 0.5-5 days;
iv) cooling of the reaction mixture obtained to 50-60° C.;
v) adding concentrated strong acid to convert the soap to fatty acid;
vi) removing free fatty acids left by short path distillation.
10. Catalytic system comprising a food grade salt of a strong base, and a weak acid, and a soap of a conjugated fatty acid with 18-24 C-atoms and 2 to 5 double bonds, in weight ratio of 0.01:1 to 0.6:1 [−] soap to conjugated fatty acid.
11. The process according to claim 1 , wherein the polyunsaturated fatty acids are C18:2 conjugated fatty acids.
12. The process according to claim 1 , wherein the soap is a soap of an organic acid with 10-20 C-atoms.
13. The process according to claim 1 , wherein the weight ratio of the soap to the conjugated polyunsaturated fatty acids is between 0.02:1 and 0.15:1.
14. The process according to claim 1 or 2 , wherein the weight ratio of the food grade salt to the soap is between 0.02:1 and 0.1:1.
15. The process according to claim 1 or 2 , wherein the mixed catalyst comprises a food grade salt selected from the group consisting or alkali metal carbonate, hydrogencarbonates, acetates and phosphate.
16. The process according to claim 1 or 2 , wherein the mixed catalyst comprises a food grade salt selected from the group consisting of sodium or potassium salts from carbonates or hydrogencarbonates.
17. The process according to claim 1 , wherein the process is carried out at a temperature of between 100 and 140°C.
18. The process according to claim 1 , wherein a molar ratio of glycerol to conjugated polyunsaturated fatty acids of between 1:3 to 1:9 is applied.
19. The process according to claim 9 , wherein the base is potassium hydroxide or sodium hydroxide.
20. The process according to claim 9 , wherein the strong acid is H 2 SO 4 or HCl.
21. The catalytic system according to claim 10 , wherein the strong base is NaOH or KOH.
22. The catalytic system according to claim 10 , wherein the weak acid is carbonic acid.
23. The catalytic system according to claim 10 , wherein the conjugated fatty acid is conjugated linoleic acid.