A method of producing microparticles by spray drying comprises the steps of providing a spray-drying feedstock solution comprising water, a volatile divalent metal salt, weak acid, 5-15% dairy or vegetable protein (w/v) and 1-20% active agent (w/v). The feedstock solution is adjusted to have a pH at which the volatile divalent metal salt is substantially insoluble. The feedstock solution is then spray-dried at an elevated temperature to provide atomised droplets, whereby the volatile divalent metal salt disassociates at the elevated temperature to release divalent metal ions which crosslink and aggregate the protein in the atomised droplets to produce microparticles having a crosslinked aggregated protein matrix and active agent dispersed throughout the matrix.

The disclosure relates to a beverage additive that contains a complexing agent, a thickening agent, and a preservative and methods of using the beverage additive to prevent teeth staining.

The disclosure relates to a beverage additive that contains a complexing agent, a thickening agent, and a preservative and methods of using the beverage additive to prevent teeth staining.

A method for forming encapsulated sweetener granules (ESGs) may include heating a first mixture to form a molten mixture, the first mixture includes one or more polyols and one or more hydrocolloids; cooling the molten mixture to a first temperature to form a cooled molten mixture; adding one or more high-intensity sweeteners to the cooled molten mixture to form a second mixture; cooling the second mixture to a second temperature to form one or more sheets, the second temperature being different from the first temperature; and fragmenting the one or more sheets to form a plurality of encapsulated sweetener granules. The first temperature may be between about 120° C. and about 200° C. The second temperature may be below a glass transition temperature (T.sub.g) of the one or more polyols and the one or more hydrocolloids. For example, the second temperature may be between about 65° C. and about 200° C.

A method for forming encapsulated sweetener granules (ESGs) may include heating a first mixture to form a molten mixture, the first mixture includes one or more polyols and one or more hydrocolloids; cooling the molten mixture to a first temperature to form a cooled molten mixture; adding one or more high-intensity sweeteners to the cooled molten mixture to form a second mixture; cooling the second mixture to a second temperature to form one or more sheets, the second temperature being different from the first temperature; and fragmenting the one or more sheets to form a plurality of encapsulated sweetener granules. The first temperature may be between about 120° C. and about 200° C. The second temperature may be below a glass transition temperature (T.sub.g) of the one or more polyols and the one or more hydrocolloids. For example, the second temperature may be between about 65° C. and about 200° C.

The invention relates to a structured fat system for use in food applications. The invention also relates to the use of a structured fat system for reducing the trans- and saturated fat content of a food product.

The invention relates to a structured fat system for use in food applications. The invention also relates to the use of a structured fat system for reducing the trans- and saturated fat content of a food product.

This disclosure relates generally to whippable food products and methods for making the whippable food products and for making whipped food products therefrom. In one embodiment, a whippable food product has less than 5% by weight fat and includes about 0.5% to about 30% by weight of a dietary fiber; about 50% to about 95% by weight of water; up to about 5% by weight of a protein; up to about 5% by weight of a food starch; up to about 5% by weight of an emulsifier; and up to about 5% by weight of a hydrocolloid. The total amount of the protein, food starch, emulsifier, and hydrocolloid is within the range of about 0.25% to about 20% by weight. In certain embodiments, the whippable food product is substantially free of emulsifier. Such a whippable food product can be capable of being aerated, for example, to a stable foam having an overrun in the range of 100%-700%.

This disclosure relates generally to whippable food products and methods for making the whippable food products and for making whipped food products therefrom. In one embodiment, a whippable food product has less than 5% by weight fat and includes about 0.5% to about 30% by weight of a dietary fiber; about 50% to about 95% by weight of water; up to about 5% by weight of a protein; up to about 5% by weight of a food starch; up to about 5% by weight of an emulsifier; and up to about 5% by weight of a hydrocolloid. The total amount of the protein, food starch, emulsifier, and hydrocolloid is within the range of about 0.25% to about 20% by weight. In certain embodiments, the whippable food product is substantially free of emulsifier. Such a whippable food product can be capable of being aerated, for example, to a stable foam having an overrun in the range of 100%-700%.

This invention relates to an alginate composition for coating food products, in particular cooked meat products such as sausages and a method for producing the alginate composition. Furthermore, the invention relates to a method for producing coated food products with the use of the alginate composition of the invention.