Abstract: The present invention relates to gel capsules comprising sterol and solubilizer for use as food supplement or as pharmaceutical.

Abstract: The present invention relates to gel capsules comprising sterol and solubilizer for use as food supplement or as pharmaceutical.

Abstract: A powder containing particles, which particles include gum arabic and at least one polyunsaturated fatty acid (PUFA) ester, where the ratio by weight of the quantity of gum arabic present in the particles to the quantity of the polyunsaturated fatty acid ester present in the particles is from about 1:1.4 to about 1:0.25, is provided. A process for the production of the particles is also provided.

Abstract: Compositions in powder form of sterols or stanol esters, and milk powder and/or proteins are disclosed. A process of making the compositions is also disclosed. The suitability of incorporation of the compositions in powder form in food products, for example beverages and milk products, is also disclosed.

Abstract: The invention relates to aqueous dispersions containing (a) 5 to 50% by weight of sterols and/or stanols; and (b) 0.5 to 20% by weight of citric acid esters of mono- and/or diglycerides, based on the total weight of the dispersion, wherein the citric acid esters of mono- and/or diglycerides are partially neutralised; and to a process for the production of an aqueous sterol/stanol-containing dispersion, which process comprises (a) dissolving citric acid esters of mono- and/or diglycerides that are partly neutralised, in water; (b) dispersing sterols and/or stanols in the emulsifier solution to form a pre-dispersion; and (c) grinding the pre-dispersion in a ball-mill until the dispersion has a particle mass diameter, d90, of less than 5 ?m. Optionally, this dispersion is spray-dried.

Abstract: The present invention relates to a composition comprising at least one lipid suitable for human consumption, at least one water soluble sweetener, and at least one solubilizer, wherein water soluble sweetener means that at least 2 g sweetener are soluble in 1 l of water at a temperature of 20° C.

Abstract: The invention relates to aqueous dispersions containing (a) 5 to 50% by weight of sterols and/or stanols; and (b) 0.5 to 20% by weight of citric acid esters of mono- and/or diglycerides, based on the total weight of the dispersion, wherein the citric acid esters of mono- and/or diglycerides are partially neutralised; and to a process for the production of an aqueous sterol/stanol-containing dispersion, which process comprises (a) dissolving citric acid esters of mono- and/or diglycerides that are partly neutralised, in water; (b) dispersing sterols and/or stanols in the emulsifier solution to form a pre-dispersion; and (c) grinding the pre-dispersion in a ball-mill until the dispersion has a particle mass diameter, d90, of less than 5 ?m. Optionally, this dispersion is spray-dried.

Abstract: A powder containing particles, which particles include gum arabic and at least one polyunsaturated fatty acid (PUFA) ester, where the ratio by weight of the quantity of gum arabic present in the particles to the quantity of the polyunsaturated fatty acid ester present in the particles is from about 1:1.4 to about 1:0.25, is provided. A process for the production of the particles is also provided.

Abstract: Processes for preparing conjugated fatty acid glycerides comprising: (a) isomerizing a fatty acid lower alkyl ester corresponding to the general formula (I) in the presence of a basic catalyst at a temperature of from 100 to 160° C., to form a conjugated fatty acid lower alkyl ester: R1CO—OR2??(I) wherein R1CO represents an acyl radical having from 16 to 22 carbon atoms and at least two carbon-carbon unsaturations and R2 represents an alkyl radical having from 1 to 4 carbon atoms; and (b) transesterifying the conjugated fatty acid lower alkyl ester with glycerol to form a conjugated fatty acid glyceride, wherein a lower alkanol corresponding to the general formula R2OH is formed, wherein R2 is as defined above, and the lower alkanol is continuously removed from the transesterification reaction; are described.

Abstract: The disclosed invention relates to emulsions containing, based on the total weight of the emulsion, a) 0.1 to 50% by weight of a conjugated linoleic acid or derivative thereof, b) 0.1 to 30% by weight of a vegetable lecithin mixture, c) 0 to 20% by weight of a co-emulsifier, d) 0 to 70% by weight of a polyol, e) 0 to 70% by weight of a carbohydrate, f) 0 to 1% by weight of an antioxidant, and g) 20 to 99% by weight of an aqueous phase, with the proviso that the emulsion contains no other oils and fats except for the triglycerides of components a), b) and/or c) optionally present. The emulsions may be directly processed in foods, more particularly beverages, and show high stability in storage.

Abstract: Processes for preparing conjugated fatty acid glycerides comprising: (a) isomerizing a fatty acid lower alkyl ester corresponding to the general formula (I) in the presence of a basic catalyst at a temperature of from 100 to 160° C., to form a conjugated fatty acid lower alkyl ester: R1CO—OR2??(I) wherein R1CO represents an acyl radical having from 16 to 22 carbon atoms and at least two carbon-carbon unsaturations and R2 represents an alkyl radical having from 1 to 4 carbon atoms; and (b) transesterifying the conjugated fatty acid lower alkyl ester with glycerol to form a conjugated fatty acid glyceride, wherein a lower alkanol corresponding to the general formula R2OH is formed, wherein R2 is as defined above, and the lower alkanol is continuously removed from the transesterification reaction; are described.

Abstract: A process for making synthetic triglycerides involving: (a) providing a reaction component selected from the group consisting of glycerol, a triglyceride, and mixtures thereof; (b) providing a fatty acid mixture containing at least 50% by weight, based on the weight of the fatty acid mixture, of conjugated linoleic acid; (c) providing an inert gas atmosphere; (d) combining the reaction component with the fatty acid mixture, in the inert atmosphere, to form a reaction mixture; and (e) heating the reaction mixture to a temperature of from 180 to 240° C., at a heating rate of from 0.5 to 3 K per minute, thus forming the synthetic triglyceride.