The invention relates to a fermented milk product includes angiogenin and/or angiogenin hydrolysate in an amount of 0.9 mg/100 g to 150 mg/100 g, and cystatin and/or cystatin hydrolysate in the mass ratio to the angiogenin and/or angiogenin hydrolysate of 0.006 to 1.7.

The invention relates to a drink includes angiogenin and/or angiogenin hydrolysate in an amount of more than 0.8 mg/100 ml and not more than 150 mg/100 ml, and lactoperoxidase and/or lactoperoxidase hydrolysate in the mass ratio to the angiogenin and/or angiogenin hydrolysate of 0.3 to 23.

The present invention relates to a method for separating at least one soluble protein fraction from an aggregated casein-containing material, the method comprises the steps of: (i) providing the aggregated casein-containing material; (ii) Contacting the aggregated casein-containing material with a chromatographic support allowing one or more soluble protein(s) present in the aggregated casein-containing material to be retained by the chromatographic support; (iii) Obtaining a permeate fraction from the chromatographic support comprising aggregated casein; (iv) Optionally washing the chromatographic support; (v) Subjecting the chromatographic support to at least one elution buffer obtaining at least one soluble protein fraction from the chromatographic support; and wherein the chromatographic support comprises one or more mixed-mode ligands capable of binding the soluble proteins from the aggregated casein-containing material.

The invention relates to a drink includes angiogenin and/or angiogenin hydrolysate in an amount of more than 0.8 mg/1.00 ml and not more than 150 mg/100 ml, and cystatin and/or cystatin hydrolysate in the mass ratio to the angiogenin and/or angiogenin hydrolysate of 0.006 to 1.7.

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 P1 and a retentate R1 containing casein and GMP in the process; (c) Subjecting the permeate P1 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.

Systems and methods for filtering dairy may filter milk with a wide-pore filter to produce a wide-pore retentate and a wide-pore permeate, wherein the wide-pore retentate may comprise casein and beta-lactoglobulin. The systems and methods may further ultra-filter the wide-pore permeate to produce an ultra-filtered retentate and an ultra-filtered permeate, wherein the ultra-filtered retentate comprises alpha-lactalbumin. The systems and methods may further nano-filter the ultra-filtered permeate to produce a nano-filtered retentate and a nano-filtered permeate, wherein the nano-filtered retentate comprises lactose. The systems and methods may further perform reverse osmosis (RO) on the nano-filtered permeate to produce a reverse osmosis retentate and a reverse osmosis permeate.

The present invention relates to compositions and methods for modulating or detecting allergy in a subject. The invention may be used to reduce allergenicity of compositions, such as food products, or to stimulate immunogenicity of products, such as vaccines by removal of cationic proteins resulting from transcription infidelity. The invention may be used in any mammal such as human.

The invention relates to a powdered milk product includes angiogenin and/or angiogenin hydrolysate in an amount of 1.4 to 24 mg/15 g, and cystatin and/or cystatin hydrolysate in the mass ratio to the angiogenin and/or angiogenin hydrolysate of 0.03 to 1.3.

The present invention relates to a method for providing an alpha-lactalbumin fraction and a beta-lactoglobulin fraction from a whey material obtained from milk, the method comprising the steps of: (i) providing the whey material; (ii) contacting the whey material with a chromatographic support allowing beta-lactoglobulin to be retained by the chromatographic support; (iii) obtaining a permeate fraction from the chromatographic support comprising the alpha-lactalbumin fraction; (iv) optionally washing the chromatographic support; and (v) obtaining a retentate fraction from the chromatographic support comprising the beta-lactoglobulin fraction; wherein the whey material provided in step (i) has been depleted, or substantially depleted from at least one whey protein, such as at least 2 whey proteins, e.g. at least 3 whey proteins.

Systems and methods for filtering dairy may filter milk with a wide-pore filter to produce a wide-pore retentate and a wide-pore permeate, wherein the wide-pore retentate may comprise casein and beta-lactoglobulin. The systems and methods may further ultra-filter the wide-pore permeate to produce an ultra-filtered retentate and an ultra-filtered permeate, wherein the ultra-filtered retentate comprises alpha-lactalbumin. The systems and methods may further nano-filter the ultra-filtered permeate to produce a nano-filtered retentate and a nano-filtered permeate, wherein the nano-filtered retentate comprises lactose. The systems and methods may further perform reverse osmosis (RO) on the nano-filtered permeate to produce a reverse osmosis retentate and a reverse osmosis permeate.