Polyunsaturated fatty acids from fish oils

Claim 2

A process for the concentration of polyunsaturated acids present as their glycerides in a fish oil containing relatively low proportions of saturated and mono-unsaturated fatty acids, also present as their glycerides, of the same chain length as the polyunsaturated fatty acids to be concentrated, consisting essentially of transesterifying said glycerides with a lower alkanol to form a mixture of lower alkyl fatty acid esters, and extracting said esters with carbon dioxide under supercritical conditons.

Claim 3

A process according to claim 1, wherein the esters are methyl esters.

Claim 4

A process according to claim 1, wherein lower molecular weight acid esters are extracted to leave a residue.

Claim 5

A process according to claim 3, wherein higher molecular weight polyunsaturated acid esters are recovered from the residue.

Claim 6

A process according to claim 1, wherein the mixture of lower alkyl fatty acid esters is extracted with successive portions of carbon dioxide.

Claim 7

A process according to claim 5, wherein the successive portions of carbon dioxide contain enhanced concentrations of higher molecular weight acid esters.

Claim 8

A process according to claim 1 wherein the carbon dioxide is at a pressure of about 2000-3500 psi.

Claim 9

A process according to claim 7, wherein the temperature of extraction is between about 24°-80° C.

Claim 10

A process according to claim 1, wherein the fish oil is menhaden, Peruvian sardine, sea bass, albacore tuna, skipjack tuna or yellowfin tuna oil.

Claim 11

A process according to claim 1, wherein the fish oil contains less than 3% of 20:1 and less than 3% of 22:1 fatty acid glycerides.

Claim 12

A process for the concentration of polyunsaturated fatty acids present as their glycerides in a fish oil containing relatively low proportions of saturated and mono-unsaturated fatty acids, also present as their glycerides, of the same chain length as the polyunsaturated fatty acids to be concentrated, consisting essentially of hydrolyzing said glycerides to form a mixture of fatty acids, and extracting said acids with carbon dioxide under supercritical conditions.

Claim 13

A process for the concentration of polyunsaturated fatty acids present as their glycerides in a fish oil containing relatively low proportions of saturated and mono-unsaturated fatty acids, also present as their glycerides, of the same chain length as the polyunsaturated fatty acids to be concentrated, consisting essentially of hydrolyzing said glycerides to form a mixture of fatty acids, and extracting said acids with carbon dioxide under supercritical conditions.

Claim 14

A process according to claim 11, wherein lower molecular weight acids are extracted to leave a residue.

Claim 15

A process according to claim 11, wherein higher molecular weight polyunsaturated acids are recovered from the residue.

Claim 16

A process according to claim 11, wherein the mixture of fatty acids is extracted with successive portions of carbon dioxide.

Claim 17

A process according to claim 14, wherein the successive portions of carbon dioxide contain enhanced concentrations of higher molecular weight acids.

Claim 18

A process according to claim 11, wherein the fish oil is menhaden, Peruvian sardine, sea bass, albacore tuna, skipjack tuna or yellowfin tuna oil.

Claim 19

A process according to claim 11, wherein the fish oil contains less than 3% of 20:1 and less than 3% of 22:1 fatty acid glycerides.

Claim 20

A process for the concentration of polyunsaturated acids present as their glycerides in a fish oil containing relatively low proportions of saturated and monounsaturated fatty acids, also present as their glycerides, of the same chain length as the polyunsaturated fatty acids to be concentrated, consisting essentially of trasnesterifying said glycerides with a lower alkanol to a form a mixture of lower alkyl fatty acid esters, pretreating said mixture of lower alkyl fatty acid esters to remove unsaturated and mono-unsaturated fatty esters, and extracting said esters with carbon diode under spercritical conditions.

Claim 21

A process for the concentration of polyunsaturated acids present as their glycerides in a fish oil containing relatively low proportions of saturated and monounsaturated fatty acids, also present as their glycerides, of the same chain length as the polyunsaturated fatty acids to be concentrated, consisting essentially of trasnesterifying said glycerides with a lower alkanol to a form a mixture of lower alkyl fatty acid esters, pretreating said mixture of lower alkyl fatty acid esters to remove unsaturated and mono-unsaturated fatty esters, and extracting said esters with carbon diode under spercritical conditions.

Claim 22

A process for the concentration of polyunsaturated fatty acids present as their glycerides in a fish oil containing relatively low proportions of saturated and mono-unsaturated fatty acids, also present as their glycerides, of the same chain length as the polyunsaturated fatty acids to be concentrated, consisting essentially of hydrolyzing said glycerides to form a mixture of fatty acids, pretreating said mixture of fatty acids to remove unsaturated and mono-unsaturated fatty acids, and extracting said acids with carbon diodide under supercritical conditions.

Claim 23

A process for the concentration of polyunsaturated fatty acids present as their glycerides in a fish oil containing relatively low proportions of saturated and mono-unsaturated fatty acids, also present as their glycerides, of the same chain length as the polyunsaturated fatty acids to be concentrated, consisting essentially of hydrolyzing said glycerides to form a mixture of fatty acids, pretreating said mixture of fatty acids to remove unsaturated and mono-unsaturated fatty acids, and extracting said acids with carbon diodide under supercritical conditions.