The present invention concerns a method for preparing dehydrated avocados, a method for preparing an unsaponifiable-rich avocado oil, a method for preparing an avocado cake rich in sugars and proteins, and a method for preparing an unsaponifiable fraction; these methods all comprising a step of drying avocado slices by means of microwaves until dehydrated avocados are obtained having residual moisture less than or equal to 5%; during this step, the water evaporated under the action of the microwaves being eliminated by a warm air stream with a temperature less than or equal to 80° C. and/or by air extraction.

The present invention relates to a fixed bed decolorization process for an polyunsaturated fatty acid, comprising a polyunsaturated fatty acid or a polyunsaturated fatty acid solution is either passed directly through a filler of the fixed bed or recycled in a filler of the fixed bed, a colorless or light-colored polyunsaturated fatty acid product is ultimately produced, at the same time, other than the color, other qualities of the polyunsaturated fatty acid remain unaffected. The decolorization process allows continuous operation or intermittent operation. The filler of the fixed bed comprises one or a mixture of activated carbon, diatomite, carclazyte, silicone and an ion-exchange resin. An upper or a middle or a bottom or a combination thereof is employed to feed a polyunsaturated fatty acid feedstock or a polyunsaturated fatty acid solution. The filler in the fixed bed can be used repeatedly. The filler can be reused after being washed when decolorization effects thereof become deteriorated or ineffective.

Methods for producing oil from fats and oils having high free fatty acid content are provided. In the method, fats and oils are treated with a mixture including an alcohol to result in a low-free fatty acid oily phase and an alcohol phase. The mixture may also include an alkali. The alcohol may be a monohydric alcohol and an aqueous alcohol, such as an aqueous alcohol having a concentration of at least about 15% alcohol-by-weight. The low-free fatty acid phase may include oil and at least one impurity. The low-free fatty acid phase may be cooled, and the oil may be separated from the at least one impurity. Fats and oils amenable to such a method may include, but are not limited to, waste fats, waste oils, high acid grease, high acid tallow, sorghum heat oil, and corn oil, such as corn oil produced at an ethanol production plant.

Methods for producing oil from fats and oils having high free fatty acid content are provided. In the method, fats and oils are treated with a mixture including an alcohol to result in a low-free fatty acid oily phase and an alcohol phase. The mixture may also include an alkali. The alcohol may be a monohydric alcohol and an aqueous alcohol, such as an aqueous alcohol having a concentration of at least about 15% alcohol-by-weight. The low-free fatty acid phase may include oil and at least one impurity. The low-free fatty acid phase may be cooled, and the oil may be separated from the at least one impurity. Fats and oils amenable to such a method may include, but are not limited to, waste fats, waste oils, high acid grease, high acid tallow, sorghum heat oil, and corn oil, such as corn oil produced at an ethanol production plant.

The disclosure discloses an enzymatic method for preparation of lecithin polyunsaturated fatty acids (PUFAs), and belongs to the technical field of separation and application of enzyme. A heat treatment procedure is added after a reaction substrate is in contact with an enzyme to adjust the ratio of sn-1 lysophospholipid PUFAs to sn-2 lysophospholipid PUFAs in a reaction product and to promote the production of sn-2 lysophospholipid PUFAs, thereby promoting the production of lecithin PUFAs, which greatly increases the production efficiency of lecithin PUFAs and the lecithin PUFA content in the product. With simple operations and high reaction rate, the method can significantly increase the content of lecithin PUFAs in the product, can effectively avoid the oxidation of PUFA, and has high economic benefits and promising industrial application prospects.

The present technology provides a process of reducing, removing or eliminating organohalo, glycidol, and oxirane species from carboxylic acid esters streams and crude and refined triglyceride oils to provide a carboxylic acid ester stream or triglyceride oil with reduced levels or essentially free of organohalo, glycidyl or other oxirane species. The process includes adding to the carboxylic acid ester stream or triglyceride oil an amount of a carboxylate anion and a cation counterion sufficient to react with the organohalo, glycidyl and oxirane species present.

Rice-bran oil of superior quality can be obtained from rice bran in high yields, and defatted rice bran of superior quality can be obtained as well. The process of the invention comprises a first processing step of bringing overheated steam in contact with fresh rice bran obtained just after rice polishing to deactivate enzymes, a second processing step of extracting rice-bran oil from the rice bran obtained in the first processing step, and a third processing step of isolating and obtaining defatted rice bran. Preferably in the first processing step, overheated steam of 250° C. to 650° C. is brought in contact with rice bran for 0.5 to 60 seconds. The extracted rice-bran oil has a low acid number, and the obtained defatted rice bran is free of bacteria and nasty smells, providing a meal of superior edible quality.

Rice-bran oil of superior quality can be obtained from rice bran in high yields, and defatted rice bran of superior quality can be obtained as well. The process of the invention comprises a first processing step of bringing overheated steam in contact with fresh rice bran obtained just after rice polishing to deactivate enzymes, a second processing step of extracting rice-bran oil from the rice bran obtained in the first processing step, and a third processing step of isolating and obtaining defatted rice bran. Preferably in the first processing step, overheated steam of 250° C. to 650° C. is brought in contact with rice bran for 0.5 to 60 seconds. The extracted rice-bran oil has a low acid number, and the obtained defatted rice bran is free of bacteria and nasty smells, providing a meal of superior edible quality.

A method for producing hemp oil, comprising decarboxylation of CBDA in hemp oil; short-path evaporation of CBD from the decarboxylated hemp oil to produce CBD oil; selective THC to CBN conversion performed on the decarboxylated hemp oil.

A method for producing hemp oil, comprising decarboxylation of CBDA in hemp oil; short-path evaporation of CBD from the decarboxylated hemp oil to produce CBD oil; selective THC to CBN conversion performed on the decarboxylated hemp oil.