IP Library › Granted Patent US 10,638,772
Granted Patent B2
US 10,638,772 · App. 15/472,773 · Granted May 5, 2020

Demineralized whey powders

Inventors: Sven-Rainer Döring (Zeven, DE); Thorben Oehlckers (Buchholz, DE); Torben Wiegers (Zeven, DE)
Assignee: DMK Deutsches Milchkontor GmbH
A23C9/1512A23C9/144A23C9/148A23C9/1422A23C9/1425A23C9/1427A23C9/1465A23C9/152A23C21/00A23J1/205A23L33/40
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Quick Facts
Patent No.
US 10,638,772
App. No.
15/472,773
Granted
May 5, 2020
Kind
B2
Abstract

A demineralised whey powder is suggested which is obtainable by: (a) Separating raw milk, removing the cream; (b) Subjecting the skimmed milk such obtained to microfiltration or microdiafiltration, obtaining a whey protein-rich permeate P 1 and a retentate R 1 containing casein and GMP in the process; (c) Subjecting the permeate P 1 to column chromatography separation, in which the lactoferrin contained therein remains on the column; (d) Subjecting the permeate, from which lactoferrin had been removed, to dialysis; and (e) Dehydrating the diluate such obtained.

Claims (17)

1. A process for the production of a demineralised whey powder, comprising the following steps:

(a) separating raw milk into skimmed milk and cream;

(b) microfiltrating or microdiafiltrating the skimmed milk with a membrane having a pore size in the range from about 0.1 to about 1 μm, obtaining a whey protein-rich permeate P 1 and a retentate R 1 containing casein and GMP;

(c) subjecting the permeate P 1 to column chromatography separation, in which lactoferrin contained therein remains on the column;

(d) subjecting the permeate P 1 , from which lactoferrin had been removed, to nanofiltration or reverse osmosis and retaining thus-obtained retentate R 2 which contains milk minerals, wherein the nanofiltration is performed with a membrane having a pore size in the range from about 150 to about 1,000 nm;

(e) dialysing thus-obtained permeate P 2 in step (d) from which lactoferrin had been removed by subjecting the permeate P 2 to electrodialysis;

(f) treating thus-obtained diluate with a cation exchanger; and

(g) drying the diluate, obtaining a product in powder form.

2. The process of claim 1 , wherein the raw milk is cold-separated.

3. The process of claim 2 , wherein the raw milk is separated at a temperature in the range from 8 to 15° C.

4. The process of claim 1 , wherein the lactoferrin of the column is eluated, salts are removed from the eluate, which is then dried, and the pure lactoferrin is subsequently added to the demineralised whey powder in defined amounts again.

5. The process of claim 1 , wherein the permeate P 1 , from which lactoferrin had been removed, is concentrated before dialysis by evaporation.

6. The process of claim 1 , wherein the diluate is subjected to pasteurisation and then dried.

7. The process of claim 1 , wherein the diluate is subjected to spray drying or freeze drying.

8. The process of claim 1 , comprising incorporating the demineralised whey powder into an infant formula.

9. The process of claim 6 , wherein the pasteurization is carried out by direct steam injection.

10. The process of claim 6 , wherein the pasteurization is carried out by steam infusion.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 23, 2017
From: DORING, SVEN-RANIER; OEHLCKERS, THORBEN; WIEGERS, TORBEN
To: DMK DEUTSCHES MILCHKONTOR GMBH
Reel/Frame 042479/0748 →
Priority Claims (1)
EP 16163027 · Mar 30, 2016 · regional
Continuity (1)
Related Publication 20170280738A1 · Oct 5, 2017