IP Library Granted Patent US 12,011,012
Granted Patent B2
US 12,011,012 · App. 17/629,682 · Granted Jun 18, 2024

Method and system for directly heating a protein-enriched milk product by introducing steam into said milk product

Inventors: Dennis Glinke (Hannover, DE); Ulrich Rolle (Everswinkel, DE); Jurgen Gehling (Stadtlohn, DE); Ludger Tacke (Velen, DE); Hubert Assing (Ahaus, DE)
Assignee: GEA TDS GmbH
A23C3/037A23C3/005A23C3/045
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Quick Facts
Patent No.
US 12,011,012
App. No.
17/629,682
Granted
Jun 18, 2024
Kind
B2
Abstract

Directly heating a protein-enriched milk product occurs by introducing steam, the direct heating taking the form of an infusion or injection method. The described technique significantly extends service time, ensuring a content of non-denatured whey proteins in the treated protein-enriched milk product greater than that obtained in the prior art. The milk product, which is preheated and kept at temperature is indirectly cooled before direct heating by a recuperative cooling step from the preheating temperature to a cool-down temperature with a temperature difference ranging from 5 K to 10 K. The direct heating from the cool-down temperature to the high pasteurization temperature is controlled by direct heating setting parameters which are known per se. Finally, the milk product is cooled by flash cooling from the high pasteurization temperature to a necessarily required exit temperature.

Claims (26)

1. A method for directly heating a protein-enriched milk product by introducing steam into the protein-enriched milk product, wherein:

(a) during direct heating, the steam heats the protein-enriched milk product to produce a high-temperature pasteurized protein-enriched milk product by means of direct high-temperature pasteurization to a high pasteurization temperature,

(b) before the direct heating, the protein-enriched milk product is preheated indirectly to a preheating temperature and, following on from the preheating when viewed in a direction of flow of the protein-enriched milk product, a first instance of keeping the protein-enriched milk product at the preheating temperature is carried out for a defined and controlled first dwell time,

(c) following on from the direct heating to the high pasteurization temperature when viewed in the direction of flow of the protein-enriched milk product, a second instance of keeping the protein-enriched milk product at the preheating temperature is carried out for a defined and controlled second dwell time,

(d) flash cooling the protein-enriched milk product by means of decompression of the steam from a first pressure to a lower pressure, and removal of water from the high-temperature pasteurized protein-enriched milk product in an amount corresponding to that of the steam supplied to the high-temperature pasteurized protein-enriched milk product that has been kept at the preheating temperature,

the protein-enriched milk product that is preheated indirectly and kept at the high pasteurization temperature is indirectly cooled before the direct heating by means of a recuperative cooling step so that a temperature difference between the preheating temperature and a cool-down temperature is in a range from 5 K to 10 K,

the direct heating from the cool-down temperature to the high pasteurization temperature is controlled by means of adjusting direct heating setting parameters, and

in accordance with the feature (d), the protein-enriched milk product is cooled by flash cooling from the high pasteurization temperature to an exit temperature.

2. The method according to claim 1 , wherein:

the temperature difference is 10 K.

3. The method according to claim 1 , wherein:

the direct heating setting parameters are pressure, temperature, and a duration of action of the steam.

4. The method according to claim 1 , wherein:

the direct heating is achieved by means of an infusion method.

5. The method according to claim 1 , wherein:

the direct heating is achieved by means of an injection method.

6. The method according to claim 2 , wherein:

the direct heating setting parameters are pressure, temperature, and a duration of action of the steam.

7. The method according to claim 6 , wherein:

the direct heating is achieved by an infusion method.

8. The method according to claim 2 , wherein:

the direct heating is achieved by an injection method.

9. The method according to claim 3 , wherein:

the direct heating is achieved by an infusion method.

10. The method according to claim 3 , wherein:

the direct heating is achieved by an injection method.

Assignments (3)
MERGER AND CHANGE OF NAME Recorded Apr 30, 2026
From: GEA TDS GMBH; GEA BREWERY SYSTEMS GMBH
To: GEA BREWERY SYSTEMS GMBH
Reel/Frame 075494/0666 →
MERGER AND CHANGE OF NAME Recorded Apr 30, 2026
From: GEA BREWERY SYSTEMS GMBH; GEA LIQUID TECHNOLOGIES GERMANY GMBH
To: GEA LIQUID TECHNOLOGIES GERMANY GMBH
Reel/Frame 075372/0934 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 16, 2022
From: GLINKE, DENNIS; ROLLE, ULRICH; GEHLING, JURGEN; TACKE, LUDGER; ASSING, HUBERT
To: GEA TDS GMBH
Reel/Frame 059283/0265 →
Priority Claims (1)
DE 10 2019 005 133.5 · Jul 24, 2019 · national
Continuity (1)
Related Publication 20220378057A1 · Dec 1, 2022