Abstract: Food products containing legume products, as well as processes for producing the food products are disclosed.

Abstract: Processes for obtaining lignan extracts from plant materials are disclosed. Compositions including lignan extracts as well as uses of the lignan extracts are also disclosed.

Abstract: This invention pertains to the preparation of a sterol ester-enriched food ingredient utilizing a base-catalyzed tranesterification of free sterol with fatty acyl glyceride. Phytosterols are subject to transesterification with fatty acyl glyceride from vegetable oils in the presence of an alkali catalyst. The reaction is performed under vacuum in the range of 0.01-1 Torr. Following an initial period of transesterification, the reaction mixture is distilled to remove glycerol to enhance the formation of sterol esters. A sterol ester-rich fraction can be isolated from the reaction mixture using organic solvents in combination with aqueous washes.

Abstract: The temperature sensitive differential of solubilities of various isoflavone fractions is used to initially separate the fractions, preferably by heating an aqueous soy molasses or soy whey feed stream. The temperature of the feed stream is selected according to the temperature at which a desired isoflavone fraction or fractions become soluble. Then, the heated feed stream is passed through an ultrafiltration membrane in order to concentrate the isoflavones. The feed stream is put through a resin adsorption process. The isoflavone fractions are treated with either reverse osmosis or ultrafiltration (or both) to complete a solvent removal and to achieve a higher isoflavone concentration in the end product. Then, the feed stream is dried, preferably by spray drying, to produce dry particles.

Abstract: This invention pertains to the preparation of a sterol ester-enriched food ingredient utilizing a base-catalyzed tranesterification of free sterol with fatty acyl glyceride. Phytosterols are subject to transesterification with fatty acyl glyceride from vegetable oils in the presence of an alkali catalyst. The reaction is performed under vacuum in the range of 0.01-1 Torr. Following an initial period of transesterification, the reaction mixture is distilled to remove glycerol to enhance the formation of sterol esters. A sterol ester-rich fraction can be isolated from the reaction mixture using organic solvents in combination with aqueous washes.

Abstract: The temperature sensitive differential of the solubilities of various isoflavone fractions is used to initially separate the fractions by heating an aqueous soy molasses or soy whey feed stream. The temperature of the feed stream is selected according to the temperature at which a desired isoflavone fraction or fractions become soluble. Then, the heated feed stream is passed through an ultrafiltration membrane or reverse osmosis in order to concentrate the solids. The resulting permeate is put through a resin adsorption process carried out in at least one liquid chromatography column to further separate the desired isoflavone fractions. Various processes are described for drying and crystallizing the isoflavone fractions to a powder. A solvent is then added to the isoflavone fraction to dissolve impurities and rehydrate the dry powder. Usually, the rehydrated isoflavone is used as an ingredient in a food ingredient or food product.