This invention provides a technique that is capable of suppressing variation in the amount of phospholipids obtained in each operation when a phospholipid concentrate is obtained by subjecting an ethanol extract concentrate of livestock or poultry tissue to a degumming step and collecting gum. More specifically, the invention provides a method for producing a phospholipid concentrate from livestock or poultry tissue, comprising step (A) of mixing an ethanol extract concentrate of livestock or poultry tissue with water, the water being in an amount of less than 7 parts by mass per 100 parts by mass of the concentrate, and step (B) of centrifuging the obtained liquid mixture at 2° C. or lower.

This disclosure provides compositions and methods for improving the dispersion of a hydrophobic amino acid entity in an aqueous suspension. This disclosure further provides compositions and methods for improving the stability of N-acetylcysteine in the presence of acetyl acceptors, e.g., carnitine.

It is provided a process for generating enriched phospholipid compositions from raw krill oil, where such processes may be batchwise, continuous, of include both batchwise steps and continuous steps. The present technology provides high quality enriched phospholipid compositions from such methods. Moreover, the continuous process provides a significantly higher throughput compared to a batch process while concurrently providing products of equal or greater quality.

This invention provides a technique that is capable of efficiently producing a phospholipid concentrate without using centrifugation and that is suitable for scaling up, the technique being for use in obtaining a phospholipid concentrate by subjecting an ethanol extract concentrate of bird breast meat to a degumming step and collecting gum. More specifically, the invention provides a method for producing a phospholipid concentrate, comprising a step of allowing a liquid mixture comprising an ethanol extract concentrate of bird breast meat and a 40 to 60 mass % aqueous ethanol solution in a mass ratio of 1:0.8 to 1.2 to stand at 40 to 60 C.

The method of producing a lipid composition comprises an extraction treatment step to extract a lipid comprised in a hydrated raw material by using an extraction solvent comprising a polar solvent and a nonpolar solvent, and a separation treatment step to separate an extract solution obtained in the extraction treatment step into a polar solvent phase comprising a first lipid fraction and a nonpolar solvent phase comprising a second lipid fraction.

The method of producing a lipid composition comprises an extraction treatment step to extract a lipid comprised in a hydrated raw material by using an extraction solvent comprising a polar solvent and a nonpolar solvent, and a separation treatment step to separate an extract solution obtained in the extraction treatment step into a polar solvent phase comprising a first lipid fraction and a nonpolar solvent phase comprising a second lipid fraction.

Use of an -lactalbumin enriched whey protein extract as a source of sphingomyelin in a synthetic nutritional composition for an infant or child wherein, the -lactalbumin enriched WPE is obtained by a process comprising: a. acidifying a whey protein product to pH 4 or below b. forming a low calcium whey protein product by concentrating the proteins in the acidified whey protein until the calcium to protein ratio is less than about 0.001 and, c. Precipitating -lactalbumin from the low-calcium whey protein product, wherein said precipitating step includes the sub-steps of: I. diluting the low-calcium whey protein product, II. adjusting the pH of the diluted low-calcium whey protein product to between 4 and 5 to form a precipitate and soluble proteins, and III. Separating the precipitate proteins from the soluble proteins.

The present invention relates to the field of the manufacture of food compounds derived from processing plant species, more specifically the process taught here provides products resulting from a process for obtaining compounds derived from vegetable raw material. The present invention describes the recovery of lecithin from the micelle/soy molasses, a residue obtained during the soy carrier concentrate (SPC) process. In a first aspect of the invention it describes a process for extracting phospholipids in conjunction with extraction of soluble sugars during the industrial process of obtaining (SPC). In a second aspect, the present invention describes an industrial process for recovering/removing such micelle phospholipids/soy molasses, cleaning and use for the production of soy lecithin.

The present invention relates to the field of the manufacture of food compounds derived from processing plant species, more specifically the process taught here provides products resulting from a process for obtaining compounds derived from vegetable raw material. The present invention describes the recovery of lecithin from the micelle/soy molasses, a residue obtained during the soy carrier concentrate (SPC) process. In a first aspect of the invention it describes a process for extracting phospholipids in conjunction with extraction of soluble sugars during the industrial process of obtaining (SPC). In a second aspect, the present invention describes an industrial process for recovering/removing such micelle phospholipids/soy molasses, cleaning and use for the production of soy lecithin.

The present invention relates to a low-fat water-in-oil (W/O) emulsion comprising a fat phase in an amount of at most 60 wt % relative to the total weight of the emulsion, an aqueous phase dispersed within the fat phase and an emulsifier composition, said emulsifier composition comprising an Acetone-insoluble (AI) component containing a Phosphatidyl Choline (PC), a Phosphatidyl Inositol (PI), a Phosphatidyl Ethanolamine (PE) and a Phosphatidic Acid (PA), wherein PC is in an amount of at most 15.5% relative to the total weight of the emulsifier composition and wherein the emulsifier composition is characterized by a weight ratio R of at most 65%, the ratio R being defined as (1) wherein PC+PI+PE+PA is the sum of the individual weights of the respective constituents of the AI component and AI is the total weight of the AI component.