A method for preparing high-content conjugated linoleic acid (CLA) through purification of vegetable oil includes alcoholysis, purification and isomerization of vegetable oil. Alcoholysis is for preparing corresponding methyl ester or ethyl ester with glyceride; purification of methyl ester or ethyl ester is for obtaining methyl linoleate or ethyl linoleate of content over 85% through silver-based silica gel column chromatography; high-content CLA is obtained after alkali-catalyzed conjugation of methyl linoleate or ethyl linoleate, and CLA products are prepared as needed. This invention changes the status quo of preparing high-content CLA with safflower oil alone, expands sources of CLA, and develops an efficient technology for separation and purification of linoleic acid. The CLA obtained is of high purity and meets applications in pharmaceutical, health care products and other industries.

A method of producing a composition comprising a high concentration of very long chain polyunsaturated fatty acids (VLCPUFAs) from natural oils such as fish oil, squid oil, algal oil and krill oil. In addition, a composition comprising a high concentration of very long chain polyunsaturated fatty acids isolated from such natural sources; as well as to a process for isolating separate fractions of very long chain polyunsaturated fatty acids having identical chain lengths but different degrees of unsaturation from such highly concentrated compositions is disclosed.

The present invention relates to a process for winterizing crude fish oil by an improved winterization process, wherein a solubilizing agent is added to the fish oil prior to the winterization. The solubilizing agent is preferably a fat-soluble edible organic compound, such as fatty acids or fatty acid mixtures. The invention further relates to compositions obtainable by the process.

[PROBLEM TO BE SOLVED] To provide a method for producing ether phospholipids of high purity by an easy process. [SOLUTION] This production method comprises: (A) a step of extracting total lipids from organisms with non-polar organic solvent and branched alcohol mixture; and (B) a step of reacting the total lipids obtained by the step (A) with phospholipase A1 to decompose mixed diacyl-glycerophospholipids. This makes it possible to produce plasmalogen-type glycerophospholipids or ether phospholipids of high purity by an easy process.

Lipid compositions derived from a solvent-extracted distillers oil of a dry grind ethanol process and lipid compositions included in cosmetic products, personal care products, skin care products, nutraceuticals, bio fuels, bio-lubricants, oleo chemicals, nutritional products, other bio-products, and animal feed compositions. Concentrations of lipid components.

One or more techniques are disclosed for a process of preparing stearic acid from animal and/or plant sources may comprise: 1) deodorizing and distilling a fat; 2) concentrating fatty acids of the fat; and 3) hydrogenating the fatty acid to provide stearic acid. The process may include the use of co-products from plant and/or animal sources. The process may also include distilling the stearic acid to provide palmitic acid and/or fully hydrogenated fatty acid. Tallow fatty acid, vegetable fatty acid, stearic acid, and palmitic acid prepared from the process described are also disclosed.

A method for increasing oil yield from a whole stillage byproduct produced in a corn dry-milling process for making alcohol (e.g., ethanol) and/or other biofuels/biochemicals and a system therefor is disclosed. In one embodiment, the method includes separating the whole stillage byproduct into an insoluble solids portion and a thin stillage portion. Thereafter, the thin stillage portion can be separated into a water-soluble solids portion, which includes oil, and a protein portion. Oil can be recovered from the water-soluble solids portion. In one example, to break oil in water emulsions in the water-soluble solids portion and increase the oil yield, a treated portion of the recovered oil, which may be heated, may be re-introduced/recycled to the water-soluble solids portion prior to the oil recovery.

The present disclosure relates methods and systems for refining grain oil compositions using water, and related compositions produced therefrom. The present disclosure also relates to methods of using grain oil derived from a fermentation product in an anti-foam composition and/or feedstock to make diesel.

Provided herein are systems and methods for the facile extraction and purification of oils from plant material, including cannabis and hemp. The systems and methods herein are versatile, and may utilize a wide range of solvents to extract oils from a variety of plant-based material. Further, the provided systems and methods are closed loop, reducing the loss solvent and decreasing the risk of safety concerns such as human exposure to solvent chemicals or explosion of volatiles. In some embodiments, the systems and methods remove impurities from the extracted oils, for example waxes or other precipitates, and provide a higher purity and higher quality extract.

A method of producing fatty alcohols comprises: introducing a fatty alcohol feedstock stream to a distillation column; forming a light outlet stream and a heavy outlet stream; condensing at least a portion of the light outlet stream to form a reflux stream; returning the reflux stream to a reflux inlet of the distillation column at a reflux ratio of greater than or equal to 2; and recovering a fatty alcohol product stream from an outlet of the distillation column, wherein the fatty alcohol product stream comprises a first mass percentage of the first fatty alcohol species (M), and a second mass percentage of the second fatty alcohol species (M2), and wherein a fatty alcohol mass ratio (M.sub.1/M.sub.2) of the fatty alcohol product stream is the first mass percentage divided by the second mass percentage, and wherein the fatty alcohol mass ratio is greater than or equal to 2.0.