Process for the production of an emulsifier based on lecithin and product thereof

Claim 2

A process for producing an emulsifier from lecithin base by solvent extraction, comprising treating a phospholipid mixture which contains phosphatidylcholine (Pc) and phosphatidylethanolamine (Pe) dissolved in alcohol with sufficient water to cause the partial precipitation of undissolved components of the phospholipid mixture whereafter said components are separated and dried.

Claim 3

A process as claimed in claim 1, wherein the amount of water added is so selected that the ratio between Pc and Pe in the separated undissolved proportion is between 7:3 and 6:1, and that the Pc content is at least 5% higher than in the phospholipid starting mixture.

Claim 4

A process as in claim 1 wherein the maximum fat content of the phospholipid starting mixture is 2% and the maximum fat content of the phospholipid fraction obtained is 3%, preferably 2%.

Claim 5

A process as claimed in claim 1 wherein the separation of the phospholipid fraction which is undissolved after the addition of water is effected by filtration, preferably ultrafiltration such that the undissolved proportions remain in the material retained by the filter or the retent.

Claim 6

A process as claimed in claim 1 wherein the separation from the solution of the phospholipid fraction which is undissolved after the addition of water is effected by gravity.

Claim 7

A process as in claim 1 wherein drying is effected in vacuum, excluding oxygen, preferably by freeze-drying.

Claim 8

A process as in claim 1, wherein egg lecithin dissolved in alcohol is mixed with water in an amount of approximately 35 to 65%, based on the resulting solvent mixture, and the undissolved phospholipid fraction thus precipitated is recovered and dried.

Claim 9

A process as in claim 1, wherein soybean lecithin dissolved in alcohol is mixed with water in an amount of from 65 to 96%, based on the resulting solvent mixture, and the undissolved phospholipid fraction thus precipitated is recovered and dried.

Claim 10

A process as in claim 1 wherein there is added from 5 to 65% of water, based on the resulting solvent mixture, to the alcoholic solution of egg lecithin and recovering by precipitation the fraction after a period of about 12 to 24 hours.

Claim 11

A process as in claim 1 wherein there is added from 5 to 55% of water, based on the resulting solvent mixture, to soybean lecithin dissolved in alcohol, and recovering by precipitation the undissolved phospholipid fraction after a period of about 12 to 24 hours.

Claim 12

A process as in claim 1, wherein the alcohol employed is an aliphatic C 1 to C 4 alcohol, preferably ethanol or isopropanol.

Claim 13

An emulsifier having the following physico-chemical parameters: (1) ratio between Pc and Pe from 7:3 to 6:1, preferably 4:1, (2) Pc content from 65 to 85% by weight, preferably from 75 to 80% by weight, (3) residual fat content less than 2%, (4) pyrogen-free in the rabbit test according to the European Pharmacopoeia (1975) vol. 2, page 56 et seqq., (5) clearly soluble in ethanol at 5% concentration, (6) clearly soluble in chloroform at 10% concentration, (7) maximum water content 2.5%, preferred maximum 1%, (8) maximum peroxide number 5, preferred maximum 1 (determined according to the DGF standard method F-1 3b (68).

Claim 14

An emulsifier having the following physico-chemical parameters: (1) ratio between Pc and Pe from 7:3 to 6:1, preferably 4:1, (2) Pc content from 65 to 85% by weight, preferably from 75 to 80% by weight, (3) residual fat content less than 2%, (4) pyrogen-free in the rabbit test according to the European Pharmacopoeia (1975) vol. 2, page 56 et seqq., (5) clearly soluble in ethanol at 5% concentration, (6) clearly soluble in chloroform at 10% concentration, (7) maximum water content 2.5%, preferred maximum 1%, (8) maximum peroxide number 5, preferred maximum 1 (determined according to the DGF standard method F-1 3b (68).