Embodiments of the present invention provide a method, comprising obtaining a lecithin-containing material, in some aspects derived from a crude refining stream, comprising 20-80 wt % acetone insoluble matter, 1-30 wt % free fatty acid, and less than 10 wt % water, adding a fatty acid or carboxylic source to the lecithin-containing material to obtain a lecithin fatty acid blend or lecithin carboxylic acid blend and incorporating the blend into asphalt or oil field applications.

The present application provides a phosphatidylcholine product represented by formula (I) and a fatty acid composition containing same. In formula (I), R.sub.1 and R.sub.2 are each independently selected from residues of saturated or unsaturated fatty acids having more than 12 carbon atoms; and R.sub.1 and R.sub.2 comprise an EPA residue and a DHA residue. The phosphatidylcholine product represented by formula (I) and fatty acid composition provided by the present application can improve damage of IBD model animal colon tissues to a certain extent, have certain anti IBD activity, and are superior to the first-line drug, sulfasalazine.

The present invention relates to a high-LPI lysolecithin and methods related to the same. The high-LPI product is produced through the reaction of lecithin with a unique method using solvent, buffer/water, and phospholipase. Using the current production method, LPI content increased from 1.4% to 3.2-13.1% using regular soy lecithin as the starting material and LPC, LPE and LPA contents also increased from 5.1%, 2.0%, 1.0% to 15.8%, 14.6% and 4.4% respectively.

Embodiments of the present invention provide a method, comprising obtaining a lecithin-containing material, in some aspects derived from a crude refining stream, comprising 20-80 wt % acetone insoluble matter, 1-30 wt % free fatty acid, and less than 10 wt % water, adding a fatty acid or carboxylic source to the lecithin-containing material to obtain a lecithin fatty acid blend or lecithin carboxylic acid blend and incorporating the blend into asphalt or oil field applications.

Aspects of the present invention provide methods of drying lecithin in a batch reaction, comprising the steps of obtaining a lecithin-containing material (derived from a crude refining stream) comprising 15-50% water, 10-30% acetone insoluble matter, and 10-20% free fatty acid; adding a fatty acid source (also derived from a crude refining stream) to the lecithin-containing material composition to obtain a lecithin/fatty acid reaction mixture; and blowing dry gas through the gum/fatty acid reaction mixture to obtain a resultant dried lecithin fatty acid blend having a water content of less than 2%. The resultant dried lecithin fatty acid blend may be used in asphalt or oil field applications.

Embodiments of the present invention provide a method, comprising obtaining a lecithin-containing material, in some aspects derived from a crude refining stream, comprising 20-80 wt % acetone insoluble matter, 1-30 wt % free fatty acid, and less than 10 wt % water, adding a fatty acid or carboxylic source to the lecithin-containing material to obtain a lecithin fatty acid blend or lecithin carboxylic acid blend and incorporating the blend into asphalt or oil field applications.

The invention belongs to the technical field of phospholipid processing, in particular to a self-aggregating hydrous phospholipid and a preparation method thereof. The self-aggregating hydrous phospholipid, the main components of the self-aggregating hydrous phospholipid are phospholipids, oil and water, the water content is 70-80 g/100 g, and the acetone-insoluble content on a dry basis is 92.5-95.5 g/100 g. Preferably, the self-aggregating hydrous phospholipid is a brown translucent fluid. The present invention is used to overcome the defects of low acetone-insoluble content of the hydrous phospholipid prepared by the existing method and the long-term dependence of the industry on the solvent method to prepare powder phospholipid, and to solve the technical problem that the hydration method powder phospholipid cannot realize industrial production.

The invention belongs to the technical field of phospholipid processing, in particular to a low-iron hydrous phospholipid and a method for separating low-iron hydrous phospholipids from soybean oil sediments. The main components of low-iron water-containing phospholipids are phospholipids, oil and water; its water content is 70-80 g/100 g; on a dry basis, the content of acetone-insoluble matter is 92.5-95.5 g/100 g; in terms of acetone-insoluble matter, the iron content is less than or equal to 18 mg/kg. The low-iron water-containing phospholipid of the present invention is prepared from soybean oil by a hydration method, and is used to solve the defects of low acetone-insoluble content of the water-containing phospholipid, inability to remove iron ions and the industry's long-term dependence on the solvent method to prepare the powdered phospholipid; At the same time, the method solves the technical problem that “the preparation of powder phospholipid by hydration method cannot realize industrial production”.

A liposome composition having a lipid bilayer membrane, made of a crude or de-oiled lecithin, at least one triglyceride, a non-triglyceride active agent, and conditioned water. The liposome composition may be utilized for purposes and treatments including increased plant growth, insecticide or insect repellant, inhibiting fruit decay, forensic labeling of plants, wound treatment, and cosmetic applications.

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.