IP Library Granted Patent US 11,419,346
Granted Patent B2
US 11,419,346 · App. 15/518,631 · Granted Aug 23, 2022

Edible aerated water-in-oil emulsions

Inventors: Renate Gemma Jacobine Maria Jacobs (Delft, NL); Sergey Michailovich Melnikov (Hamburg, DE); Theodorus Stam (Vlaardingen, NL)
Assignee: UPFIELD EUROPE B.V.
A23D7/013A23D7/0056A23D7/02
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Quick Facts
Patent No.
US 11,419,346
App. No.
15/518,631
Granted
Aug 23, 2022
Kind
B2
Abstract

Process to manufacture edible aerated water-in-oil emulsion comprising: from 0.5 to 50 wt. % of micronized fat powder comprising hardstock fat; from 10 to 85 wt. % of liquid oil; from 10 to 85 wt. % of water-phase; from 2 to 100 vol. % of gas-phase; wherein the gas has an average solubility in water at 20 degrees Celsius and at 1 bar of pressure of at most 0.75 gram gas per kg water; and wherein the gas has an average solubility in sunflower oil at 20 degrees Celsius and at 1 bar of pressure of at most 0.75 gram gas per kg oil; comprising the step of: mixing the fat powder, the liquid oil, the water-phase and the gas-phase to provide the edible aerated water-in-oil emulsion.

Claims (50)

1. A process for manufacturing an edible aerated water-in-oil emulsion comprising:

from 0.5 to 50 wt. % of a micronized fat powder comprising hardstock fat;

from 10 to 85 wt. % of a liquid oil;

from 10 to 85 wt. % of a water-phase;

from 2 to 100 vol. % of a gas-phase; wherein the gas-phase comprises a gas having (i) an average solubility in water at 20 degrees Celsius and at 1 bar of pressure of at most 0.75 gram gas per kg water; (ii) an average solubility in sunflower oil at 20 degrees Celsius and at 1 bar of pressure of at most 0.75 gram gas per kg oil; and (iii) wherein the gas-phase comprises at least 50 vol. % of nitrogen, oxygen, helium, neon, argon, krypton, xenon, or a mixture thereof, based on the total volume of the gas-phase;

comprising the following steps:

a) forming an emulsion by mixing the liquid oil, and the water-phase; and

b) introducing the gas-phase by post-aeration of the emulsion; and

c) adding the micronized fat powder to the aerated emulsion, wherein the micronized fat powder is not subjected to temperatures at which the hardstock substantially melts;

to provide the edible aerated water-in-oil emulsion.

2. The process of claim 1 , wherein the micronized fat powder is produced by supercritical melt micronisation.

3. The process of claim 1 , wherein the amount of micronized fat powder comprising hardstock fat is from 1 to 20 wt. %.

4. The process of claim 1 , wherein the hardstock fat comprised by the fat powder has a solid fat content profile of:

N10 from 50 to 100,

N20 from 26 to 95, and

N35 from 5 to 60.

5. The process of claim 1 , wherein the amount of gas-phase is from 3 to 70 vol. %.

6. The process of claim 1 , wherein the amount of liquid oil is from 15 to 70 wt. %.

7. The process of claim 1 , wherein a combination comprising

a) a monoglyceride, a diglyceride, or a polyglycerol ester of fatty acids, or a combination thereof; and

b) lecithin are added as ingredients.

8. The process of claim 1 , wherein the micronized fat powder comprising hardstock fat is subjected to at least partial vacuum.

9. An edible aerated water-in-oil emulsion manufactured by the process of claim 1 .

10. The emulsion of claim 9 , wherein the emulsion is an aerated liquid margarine, an aerated wrapper or an aerated tub-spread.

11. The emulsion of claim 10 , wherein the mixing in step a) is performed using one or more C-units, A-units, Trefa-mixers or a combination thereof.

12. The process of claim 1 , wherein the amount of gas-phase is at least 50 vol. %.

13. The process of claim 1 , wherein the amount of gas-phase is at least 66.7 vol. %.

14. The process of claim 1 , wherein the amount of gas-phase is from 50 to 70 vol. %.

15. The process of claim 1 , wherein the micronized fat powder is added to the emulsion in step c) after the emulsion is fully aerated, and the amount of gas-phase is at least 33.3 vol. %.

16. The process of claim 1 , wherein the micronized fat powder is added to the emulsion in step c) after the emulsion is fully aerated, and the amount of gas-phase is at least 50 vol. %.

17. A process for manufacturing an edible aerated water-in-oil emulsion comprising:

from 0.5 to 50 wt. % of a micronized fat powder comprising hardstock fat;

from 10 to 85 wt. % of a liquid oil;

from 10 to 85 wt. % of a water-phase;

at least 33.3 vol. % of a gas-phase; wherein the gas-phase comprises a gas having (i) an average solubility in water at 20 degrees Celsius and at 1 bar of pressure of at most 0.75 gram gas per kg water; and (ii) an average solubility in sunflower oil at 20 degrees Celsius and at 1 bar of pressure of at most 0.75 gram gas per kg oil;

comprising the following steps:

a) forming an emulsion by mixing the liquid oil, and the water-phase; and

b) introducing the gas-phase by post-aeration of the emulsion; and

c) adding the micronized fat powder to the aerated emulsion, wherein the micronized fat powder is not subjected to temperatures at which the hardstock substantially melts;

to provide the edible aerated water-in-oil emulsion.

18. A process for manufacturing an edible aerated water-in-oil emulsion comprising:

from 0.5 to 50 wt. % of a micronized fat powder comprising hardstock fat;

from 10 to 85 wt. % of a liquid oil;

from 10 to 85 wt. % of a water-phase;

at least 33.3 vol. % of a gas-phase;

comprising the following steps:

a) forming an emulsion by mixing the liquid oil, and the water-phase; and

b) introducing the gas-phase by post-aeration of the emulsion; and

c) adding the micronized fat powder to the aerated emulsion, wherein the micronized fat powder is not subjected to temperatures at which the hardstock substantially melts;

to provide the edible aerated water-in-oil emulsion.

Assignments (5)
CHANGE OF NAME Recorded Jan 15, 2025
From: UPFIELD EUROPE B.V.
To: FLORA FOOD GLOBAL PRINCIPAL B.V.
Reel/Frame 069928/0125 →
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 Jun 8, 2018
From: CONOPCO, INC., D/B/A UNILEVER
To: UNILEVER BCS US, INC.
Reel/Frame 046026/0451 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 21, 2017
From: JACOBS, RENATE GEMMA JACOBINE MARIA; MELNIKOV, SERGEY MICHAILOVICH; STAM, THEODORUS
To: CONOPCO, INC., D/B/A UNILEVER
Reel/Frame 042088/0196 →
Priority Claims (1)
EP 14189337 · Oct 17, 2014 · regional
Continuity (1)
Related Publication 20170231242A1 · Aug 17, 2017