Abstract: The invention relates to a liquid nutritional composition comprising (a) 2-25% by weight of a calcium-depleted milk protein concentrate (MPC) that has undergone a heat treatment to at least 80° C. and has between 15-45% by weight of the calcium removed; (b) 0-30% by weight fat; (c) 5-45% by weight carbohydrate; wherein the nutritional composition has a viscosity of less than 200 cP at a temperature of 20° C. and shear rate of 100 s?1, and has an energy density of at least 0.5 kcal/ml, and wherein protein provides 10-40% of the total energy content of the composition. Also provided is a powdered composition dispersible in water to form the liquid composition.

Abstract: The disclosure relates to a method of making a beverage comprising a milk protein concentrate (MPC), a beverage comprising an MPC, an MPC or use of a MPC. More particularly, this disclosure relates to treatment of an MPC to allow for heat homogenisation of a beverage containing the MPC, while reducing occurrence of malodour and/or egg-type or sulphur-type smell and/or taste.

Abstract: Heat-treated, shelf-stable liquid nutritional compositions comprising whey protein and non-whey protein, and methods of producing and using these compositions. The compositions have a pH of from about 6.0 to about 8.0, a total protein content of at least about 6 g per 100 mL of the composition. The whey protein comprises or is provided by an ingredient that comprises heat-denaturable protein of which at least about 55% is present in a denatured state, and the non-whey protein comprises or consists of casein, or one or more non-dairy proteins, or casein and one or more non-dairy proteins.

Abstract: The invention relates to a liquid nutritional composition comprising (a) 2-25% by weight of a calcium-depleted milk protein concentrate (MPC) that has undergone a heat treatment to at least 80° C. and has between 15-45% by weight of the calcium removed; (b) 0-30% by weight fat; (c) 5-45% by weight carbohydrate; wherein the nutritional composition has a viscosity of less than 200 cP at a temperature of 20° C. and shear rate of 100s?1, and has an energy density of at least 0.5 kcal/ml, and wherein protein provides 10-40% of the total energy content of the composition. Also provided is a powdered composition dispersible in water to form the liquid composition.

Abstract: The invention relates to a liquid nutritional composition comprising (a) 2-25% by weight of a calcium-depleted milk protein concentrate (MPC) that has undergone a heat treatment to at least 80.degree. C. and has between 15-45% by weight of the calcium removed; (b) 0-30% by weight fat; (c) 5-45% by weight carbohydrate; wherein the nutritional composition has a viscosity of less than 200 cP at a temperature of 20.degree. C. and shear rate of 100 s.sup.?1, and has an energy density of at least 0.5 kcal/ml, and wherein protein provides 10-40% of the total energy content of the composition. Also provided is a powdered composition dispersible in water to form the liquid composition.

Abstract: The invention relates to a liquid nutritional composition comprising (a) 2-25% by weight of a calcium-depleted milk protein concentrate (MPC) that has undergone a heat treatment to at least 80° C. and has between 15-45% by weight of the calcium removed; (b) 0-30% by weight fat; (c) 5-45% by weight carbohydrate; wherein the nutritional composition has a viscosity of less than 200 cP at a temperature of 20° C. and shear rate of 100 s?1, and has an energy density of at least 0.5 kcal/ml, and wherein protein provides 10-40% of the total energy content of the composition. Also provided is a powdered composition dispersible in water to form the liquid composition.

Abstract: The invention provides a process for preparing a dried modified whey protein concentrate. A whey protein solution is used having less than 5% total solids and a combined calcium and magnesium concentration of less than 70 mmol/kg on a dry basis and a pH of 6.0-7.5. It is heated to greater than 70° C. for up to 60 minutes to denature the whey protein. The solution is then cooled to 40° C.-60° C.; and subsequently spray dried. Alternatively a higher initial concentration of total solids may be used in an embodiment where the heating is carried out on a scraped surface heat exchanger.