Method for the fractionation of phospho-lipids from phospholipid-containing material

Patent metadata

Field	Value
Publication number	US-9567356-B2
Application number	US-201314437711-A
Country	US
Kind code	B2
Filing date	Oct 24, 2013
Priority date	Oct 24, 2012
Publication date	Feb 14, 2017
Grant date	Feb 14, 2017

Abstract

The present invention relates to a counter-current extraction process involving a plurality of mixing and separation stages for fractionating a phospholipid-containing feed material into two or more fractions enriched in one or more phospholipids, comprising (a) contacting the phospholipid-containing starting material under agitation with an extractant comprising an aliphatic alcohol selected from C1 to C3 alcohols; (b) separating the obtained emulsion into a phospholipid-enriched extract from a residual raffinate.

First claim

The invention claimed is:

1. A counter-current extraction process involving a plurality of mixing and separation stages for fractionating a phospholipid-containing starting material into two or more fractions enriched in one or more phospholipids, comprising the following steps:
(a) contacting the phospholipid-containing starting material under agitation with an extractant comprising an aliphatic alcohol selected from C 1 to C 3 alcohols and combinations thereof for a period of time sufficient to effectuate the transfer of at least a fraction of the phospholipids into the extractant to obtain a mixture;
(b) separating the obtained mixture into a phospholipid-enriched extract from a residual raffinate by a process comprising applying centrifugal forces, wherein the phospholipid-enriched extract from each separation stage is at least in part returned to a previous, or further upstream mixing stage, and wherein a final phospholipid-enriched extract is separated from a first residual raffinate, and wherein a final raffinate phase is obtained having between 55 and 75 wt % of Acetone Insolubles (AI).

2. A process according to claim 1 , wherein in step (a) the phospholipid-containing starting material is contacted with the extractant in a co-current or counter-current mixing operation.

3. A process according to claim 1 , wherein the extracted phospholipids comprise one or more of phosphatidyl choline (PC), phosphatidyl ethanolamine (PE), phosphatidyl Inositol (PI) and/or phosphatidic acid (PA).

4. A process according to claim 1 , wherein the final raffinate phase comprises less than 12% by weight of phosphatidyl choline (PC).

5. A process according to claim 1 , wherein the final phospholipid-enriched extract comprises at least 25% by weight of phosphatidyl choline (PC).

6. A process according to claim 1 , wherein the aliphatic alcohol is ethanol.

7. A process according to claim 1 , wherein the aliphatic alcohol has a water concentration that is in the range of from 0 to 10% by weight.

8. A process according to claim 1 , wherein steps (a) and (b) are executed at least in part in a multistage extraction apparatus comprising for each stage:
i) a rotor,
ii) a mixing chamber connected to the rotor, and wherein two liquid streams are mixed, and wherein the mixing chamber comprises
iia) a stationary agitator placed in the mixing chamber, and
iib) a settling chamber in which the liquid streams are separated by the centrifugal force generated by the mixing chamber.

9. A process according to claim 8 , wherein the stationary agitator comprises a stationary disc, and wherein the mixing is achieved through speed differentials between the stationary disc and the rotating mixing chamber.

10. A process according to claim 1 , comprising at least two extraction and separation stages, wherein the respective extractant is added to the respective raffinate at one or more stages in a counter-current or co-current manner.

11. A process according to claim 1 , wherein the final phospholipid-enriched extract and the final raffinate phase are in a weight ratio that is in the range of from 1 to 5, wherein the phospholipid-enriched extract comprises water in an amount of from 1 to 10% by weight, wherein the extractant phase has a temperature of from 25° C. to 70° C., and wherein from 2 to 10 extraction stages are employed using of from 2 to 20.000 g for the separation step.

12. The process according to claim 1 , wherein the phospholipid-containing feed comprises lecithin.

13. The process according to claim 12 , wherein the lecithin is selected from the group consisting of soybean lecithin, corn lecithin, rapeseed lecithin, rice oil lecithin, sunflower lecithin, cotton seed lecithin, palm oil lecithin, marine oil lecithin, biomass lecithin, peanut lecithin, egg yolk lecithin, milk lecithin and/or brain lecithin.

14. The process according to claim 1 , further comprising isolating at least part of the phospholipids from the raffinate and/or extract phase.

Assignees

• Cargill Inc

Inventors

• Bruecher Tobias
• Demey Johan
• Katte Matthias
• Molnar Jeff
• Tirok Susanne

Classifications

• B01D11/048

  Mixing by counter-current streams provoked by centrifugal force, in rotating coils or in other rotating spaces · CPC title

• A23D9/013

  Other fatty acid esters, e.g. phosphatides · CPC title

• C07F9/103 Primary

  Extraction or purification by physical or chemical treatment of natural phosphatides; Preparation of compositions containing phosphatides of unknown structure · CPC title

• A21D2/32

  Phosphatides · CPC title

• A23D9/04

  Working-up · CPC title