Producto alimenticio saludable que contiene ésteres etílicos de ácidos grasos de aceite de linaza, y procedimiento de obtención del mismo

Un producto alimenticio saludable que contiene ésteres etílicos de ácidos grasos de aceite de linaza, caracterizado porque está constituido por microcápsulas en forma de polvo, que contiene, en una matriz de proteínas y carbohidratos, un nutracéutico con ésteres etílicos bioactivos de ácidos ALA (ácido a-linolénico) y LA (ácido linoleico) en forma de gotas de diámetro inferior a 2 mm, con no más de 4 por ciento en peso adicional de etanol basado en al menos 99,8% de etanol farmacéutico anhidro, en el que en la matriz de proteína-carbohidrato como proteínas se utilizan concentrados de proteína láctea con concentración de lactosa disminuida, que contiene un mínimo del 30 por ciento en peso de proteínas y/o concentrados de proteínas vegetales, en el que en la matriz de proteína-carbohidrato como carbohidrato se utiliza maltodextrina de baja sacarificación con índice DE no superior a 13. The subject of invention is the health-giving foodstuff containing ethyl esters of fatty acids of linen oil or linen oil and fish oil, characterised in that it constitutes of microcapsules in form of powder, which contains, in a protein-carbohydrate matrix, a nutraceutical with bioactive ethyl esters of acids ALA, LA or ALA, LA, DHA, EPA with not more than 4 percent by weight addition of ethanol, based on at least 99.8% anhydrous pharmaceutical ethanol, in form of drops of diameter less than 21.1m. The nature of the invention is also a method for obtaining of the health-giving foodstuff containing ethyl esters of fatty acids, namely of linen oil or linen oil and fish oil, by mixing of ingredients, their homogenisation, drying, characterised by that after obtaining liquid protein-carbohydrate matrix, a nutraceutical containing bioactive ethyl esters of acids ALA, LA or ALA, LA, DHA, EPA is introduced into it, followed by carrying out of dispergation of ester phase by mechanical agitation until stable form of emulsion is obtained, which is then treated with two-steps and two-stages pressure homogenisation: in 1st stage-at pressure of at least 20 MPa on the 1st step and 4 MPa at the 2nd step, and in 2nd stage-at pressure of at least 30 MPa on the 1st step and 10 MPa at the 2nd step, whilst homogenisation during the 1st stage is carried out in process coupled with thermal processing of the emulsion, which is then spray dried in atmosphere of temperature 160-190° C. in the inlet of to drying cabinet and the powder is dispensed in neutral gas atmosphere.