The present invention relates to ready-to-drink cocoa milk beverage products. In particular, the invention is concerned with a protein system induced by controlled aggregation of milk proteins which imparts outstanding sensory attributes and improved physical stability of the beverage products, in particular when containing low fat and/or low sugar. A method of 5 producing such beverage and the products obtainable from the method are also part of the present invention.

The present invention relates to ready-to-drink cocoa milk beverage products. In particular, the invention is concerned with a protein system induced by controlled aggregation of milk proteins which imparts outstanding sensory attributes and improved physical stability of the beverage products, in particular when containing low fat and/or low sugar. A method of 5 producing such beverage and the products obtainable from the method are also part of the present invention.

This disclosure provides beverage compositions comprising a pectin, a first xanthan gum, optionally a second xanthan gum, and a non-nutritive sweetener, such as steviol glycosides and blends thereof. These beverage compositions have improved mouthfeel properties.

This disclosure provides beverage compositions comprising a pectin, a first xanthan gum, optionally a second xanthan gum, and a non-nutritive sweetener, such as steviol glycosides and blends thereof. These beverage compositions have improved mouthfeel properties.

The invention relates to separated, decompacted, cellulose-based fibres acquired from a vegetable raw material, wherein the separated, decompacted, cellulose-based fibres have an aspect ratio after soaking in water of longitudinal diameter to transverse diameter of 1:1 to 1000:1 and a water-binding capacity of >200 wt. % and a water retention capacity of >50%, and a method for acquiring and producing these separated, decompacted cellulose-based fibres. The purification method involves incubation of the vegetable material with an aqueous decomposition solution containing at least one dissolved amino acid and/or peptide with 2-50 amino acids to decompose the compacted cellulose-based fibres.

The invention relates to separated, decompacted, cellulose-based fibres acquired from a vegetable raw material, wherein the separated, decompacted, cellulose-based fibres have an aspect ratio after soaking in water of longitudinal diameter to transverse diameter of 1:1 to 1000:1 and a water-binding capacity of >200 wt. % and a water retention capacity of >50%, and a method for acquiring and producing these separated, decompacted cellulose-based fibres. The purification method involves incubation of the vegetable material with an aqueous decomposition solution containing at least one dissolved amino acid and/or peptide with 2-50 amino acids to decompose the compacted cellulose-based fibres.

Described herein is the method of using a complex coacervate system including Gum Arabic and chitosan as lubricating agents. Also described herein are consumer products including the complex coacervate system.

Described herein is the method of using a complex coacervate system including Gum Arabic and chitosan as lubricating agents. Also described herein are consumer products including the complex coacervate system.

The present invention facilitates the elimination of foam generated in an acidic liquid seasoning containing plant-derived crushed materials after the seasoning is mixed by stirring/shaking. This acidic liquid seasoning contains plant-derived crushed materials, gums, a cold water swellable starch, and a vinegar, wherein (A) the viscosity at 20 C. is 500 to 10,000 mPa.Math.s, and (B) the dissociated acetic acid concentration is 0.15 mass % or less.

The present invention facilitates the elimination of foam generated in an acidic liquid seasoning containing plant-derived crushed materials after the seasoning is mixed by stirring/shaking. This acidic liquid seasoning contains plant-derived crushed materials, gums, a cold water swellable starch, and a vinegar, wherein (A) the viscosity at 20 C. is 500 to 10,000 mPa.Math.s, and (B) the dissociated acetic acid concentration is 0.15 mass % or less.