IP Library Granted Patent US 9,125,425
Granted Patent B2
US 9,125,425 · App. 13/823,150 · Granted Sep 8, 2015

Edible fat continuous spreads

Inventors: Johannes Robert Bons (AT Vlaardingen, NL); Eckhard Flöter (Berlin, DE); Hindrik Huizinga (AT Vlaardingen, NL); Irene Erica Smit-Kingma (AT Vlaardingen, NL)
Assignee: Conopco, Inc.
A23D7/05A23D7/0056A23D7/013A23L1/3004A23L1/3006
View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 9,125,425
App. No.
13/823,150
Granted
Sep 8, 2015
Kind
B2
Abstract

The invention relates to a method of preparing an edible fat continuous spread comprising a dispersed aqueous phase and crystalline non-esterified plant sterol, said method comprising the steps of preparing a fat continuous emulsion and mixing said emulsion with fast re-crystallized non-esterified plant sterol.

Claims (26)

1. Method of preparing an edible fat continuous spread comprising a dispersed aqueous phase, 20 to 80 wt % fat and 0.1 to 20 wt % crystalline non-esterified plant sterol, said method comprising the steps of

a. providing an aqueous phase (A);

b. providing a fat phase (B);

c. preparing a fat continuous emulsion (C) comprising the step of mixing aqueous phase (A) and fat phase (B);

d. providing a fat slurry (D) comprising crystalline non-esterified plant sterol and vegetable oil;

e. mixing fat slurry (D) with fat continuous emulsion (C);

wherein fat slurry (D) comprises re-crystallized non-esterified plant sterol prepared by re-crystallizing the non-esterified plant sterol from a mixture comprising vegetable oil and heat dissolved non-esterified plant sterol by cooling said mixture at a cooling rate of at least 2.5 degrees Celsius per second and wherein the average particle size of the resulting crystalline non-esterified plant sterol is smaller than 20 micron.

2. Method according to claim 1 wherein the re-crystallized non-esterified plant sterol is prepared by re-crystallizing the non-esterified plant sterol from a mixture comprising vegetable oil and heat dissolved non-esterified plant sterol by cooling said mixture at a cooling rate of at least 3, degrees Celsius per second.

3. The method according to claim 2 wherein the cooling rate is 4 to 15 degrees Celsius per second.

4. The method according to claim 2 wherein the cooling rate is 5 to 10 degrees Celsius per second.

5. Method according to claim 1 wherein the re-crystallized non-esterified plant sterol is prepared by re-crystallizing the non-esterified plant sterol from a mixture comprising vegetable oil and heat dissolved non-esterified plant sterol by cooling said mixture, said mixture having a temperature of 100 to 150 degrees Celsius.

6. The method according to claim 5 wherein the temperature of the mixture is from 110 to 135 degrees Celsius.

7. Method according to claim 1 wherein the re-crystallized non-esterified plant sterol is prepared by re-crystallizing the non-esterified plant sterol from a mixture comprising vegetable oil and heat dissolved non-esterified plant sterol by cooling said mixture and the resulting mixture has a temperature of less than 60 degrees Celsius.

8. The method according to claim 7 wherein the temperature of the resulting mixture is from 20 to 60 degrees Celsius.

9. Method according to claim 1 wherein fat slurry (D) comprises non-esterified plant sterol and vegetable oil in a weight ratio of 1:1 to 1:10.

10. The method according to claim 9 wherein the fat slurry (D) comprises non-esterified plant sterol and vegetable oil in a weight ratio of 1:1.5 to 1:6.

11. Method according to claim 1 wherein the average particle size of the resulting crystalline non-esterified plant sterol is smaller than 15 micron.

12. The method according to claim 11 wherein the average particle size of the resulting crystalline non-esterified plant sterol is from 5 to 15 micron.

13. Method according to claim 1 wherein fat slurry (D) and fat continuous emulsion (C) are mixed in a weight ratio of 1:10 to 4:1.

14. The method according to claim 13 wherein fat slurry (D) and fat continuous emulsion (C) are mixed in a weight ratio of 1:5 to 2:1.

15. Method according to claim 1 wherein the edible fat continuous spread comprises 25 to 60 wt % fat.

16. The method according to claim 15 wherein the edible fat continuous spread comprises 30 to 50 wt % fat.

17. Method according to claim 1 wherein the edible fat continuous spread comprises 15 to 75 wt % water.

18. Method according to claim 1 wherein the edible fat continuous spread comprises 2 to 15 wt % crystalline non-esterified plant sterol.

19. The method according to claim 18 wherein the edible fat continuous spread comprises 4 to 10 wt % crystalline non-esterified plant sterol.

20. Method according to claim 1 wherein the edible fat continuous spread comprises less than 1 wt % of sweetener.

Assignments (4)
CHANGE OF NAME Recorded Jun 15, 2020
From: UPFIELD US INC.
To: UPFIELD EUROPE B.V.
Reel/Frame 052938/0715 →
CHANGE OF NAME Recorded Sep 27, 2018
From: UNILEVER BCS US INC.
To: UPFIELD US INC.
Reel/Frame 047158/0449 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 5, 2017
From: CONOPCO, INC., D/B/A UNILEVER
To: UNILEVER BCS US, INC.
Reel/Frame 042166/0596 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 3, 2013
From: BONS, JOHANNES ROBERT; FLOTER, ECKHARD; HUIZINGA, HINDRIK; SMIT-KINGMA, IRENE ERICA
To: CONOPCO, INC., D/B/A/ UNILEVER
Reel/Frame 030139/0289 →
Priority Claims (1)
EP 10178323 · Sep 22, 2010 · regional
Continuity (1)
Related Publication 20130171310A1 · Jul 4, 2013