IP Library › Granted Patent US 9,468,896
Granted Patent B2
US 9,468,896 · App. 14/437,669 · Granted Oct 18, 2016

Phospholipid-containing emulsifier composition

Inventors: Arnulf Schoeppe (Hamburg, DE); Daniel Steiger (Pinneberg, DE); Susanne Tirok (Hamburg, DE)
Assignee: CARGILL, INCORPORATED
B01F17/0092A21D2/32A23D7/011A23D7/013A23G3/40A23J7/00A23K20/158A23L1/035A23L1/24A61K8/553A61K47/24C11B11/00A61K2800/10
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Quick Facts
Patent No.
US 9,468,896
App. No.
14/437,669
Granted
Oct 18, 2016
Kind
B2
Abstract

The present invention relates to a novel phospholipid emulsifier composition allowing stabilizing water-in-oil emulsions, and to a novel process for the preparation of such emulsions involving 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.

Claims (58)

1. A phospholipid emulsifier composition comprising Phosphatidyl Choline (PC), Lyso Phosphatidyl Choline (ITC), Phosphatidyl Inositol (PI), Phosphatidyl Ethanolamine (PE) and Phosphatidic Acid (PA), and having a phospholipid ratio R 1 :R 2 in the range of from 1:1 to 1.7:1,

wherein R 1 is defined as a weight ratio of phospholipid components according to general formula I:

R

1

=

PC

+

LPC

+

PI

+

PA

PE

,

(

I

)

and wherein R 2 is defined as a weight ratio of phospholipid components according to general formula II:

R

2

=

PC

+

LPC

+

PI

PE

+

PA

.

(

II

)

2. An emulsifier according to claim 1 , having an Acetone Insoluble content of at least 60 weight %, and a Phosphatidyl Choline content of at most 20 weight %.

3. A water-in-oil emulsion comprising the emulsifier composition of claim 1 .

4. A water-in-oil-in-water emulsion comprising an emulsion according to claim 3 .

5. An emulsion according to claim 3 , further comprising one or more texturing agents, and/or a calcium salt.

6. A counter-current extraction process for the preparation of the emulsifier according to claim 1 , comprising:

(a) contacting a 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 phospholipids in the phospholipid-containing starting material 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 stages, and wherein a final phospholipid-enriched extract comprising the emulsifier is separated from a first residual raffinate, and

(c) isolating at least part of the phospholipids from the raffinate to obtain the emulsifier.

7. A process according to claim 6 , wherein in step (a) the phospholipid-containing starting material is contacted with the extractant in a co-current or counter-current mixing operation.

8. A process according to claim 6 , wherein in the aliphatic alcohol has a water concentration in the range of from 0 to 10% by weight.

9. A process according to claim 6 , 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 centrifugal force generated by the mixing chamber.

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

11. The process according to claim 6 , wherein the phospholipid-containing starting material comprises lecithin, 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.

12. The process according to claim 6 , further comprising isolating at least part of the phospholipids from the raffinate and/or extract phase.

13. A process for the preparation of an water-in-oil emulsion, comprising

(i) contacting a lipid composition with a suitable amount of an emulsifier according to claim 1 to obtain an emulsion stabilized lipid composition, and

(ii) contacting the emulsion stabilized lipid composition with an first aqueous phase to form a water-in-oil emulsion.

14. A process according to claim 13 , further comprising dispersing the water-in oil emulsion in a second aqueous phase to obtain an oil-in-water-in oil emulsion.

15. A process according to claim 14 , wherein the oil-in-water-in oil emulsion is prepared using a cross-flow membrane with suitable pore size.

16. An emulsifier according to claim 2 , wherein the Phosphatidyl Choline content is at most 12 weight %.

17. A process according to claim 6 , wherein the aliphatic alcohol has a water concentration in the range of from 0 to 5% by weight.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 21, 2015
From: SCHOEPPE, ARNULF; STEIGER, DANIEL; TIROK, SUSANNE
To: CARGILL, INCORPORATED
Reel/Frame 037337/0653 →
Priority Claims (1)
EP 12007324 · Oct 24, 2012 · regional
Continuity (1)
Related Publication 20150298084A1 · Oct 22, 2015