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HEALTH-GIVING FOODSTUFF CONTAINING ETHYL ESTERS OF FATTY ACIDS OF LINSEED OIL, AND METHOD FOR OBTAINING THE SAME

机译:亚麻籽油脂肪酸乙酯的赋予健康的食物及其获得方法

摘要

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 stageat pressure of at least 20 MPa on the 1st step and 4 MPa at the 2nd step, and in 2nd stageat 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.
机译:本发明的主题是一种保健食品,其包含亚麻油或亚麻油和鱼油的脂肪酸乙酯,其特征在于它由粉末形式的微胶囊组成,其在蛋白质-碳水化合物基质中包含营养食品。含有酸ALA,LA或ALA,LA,DHA,EPA的生物活性乙酯,并以重量计小于21.1m的液滴形式添加不超过4%重量的乙醇(基于至少99.8%的无水药用乙醇)。本发明的本质还是一种通过成分混合,均质化,干燥来获得含有脂肪酸乙酯(亚麻油或亚麻油和鱼油)的保健食品的方法,其特征在于将液态蛋白质-碳水化合物基质,含有酸ALA,LA或ALA,LA,DHA,EPA的生物活性乙酯的营养食品引入其中,然后通过机械搅拌进行酯相的分散,直至获得稳定的乳液形式,然后进行两步和两阶段的压力均质处理:在第一阶段,第一步骤的压力至少为20 MPa,第二阶段的压力为4 MPa,第二阶段的第一步骤的压力至少为30 MPa在第二步和10 MPa的压力下进行,同时在第一步中进行均质化,同时进行乳液的热处理,然后将乳液在温度为160-190°C的空气中于D的入口进行喷雾干燥。干燥柜中,粉末在中性气体气氛中分配。

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