Deacidfieation method of high-acid-value vegetable oil
A deacidification method and vegetable oil technology, applied in the direction of fat oil/fat refining, fat production, etc., can solve the problems of high pretreatment requirements of crude oil, price restrictions on wide application, lack of selectivity in reaction, etc., to achieve solvent recovery and recycling, price Inexpensive, highly selective effects
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Embodiment 1
[0029] The batch enzyme reaction is carried out in a batch-type stirred tank reactor. The free fatty acid and monoethanolamine in the high acid value rice bran oil are in a molar ratio of 1:4 (the acid value of the high acid value rice bran oil is 38.29mgKOH / g), and the added The ratio of vegetable oil to n-hexane is 1:0.5 (w / v), add high acid value vegetable oil and 12% calcium oxide of the total mass of monoethanolamine, stir and react at 60°C under normal pressure for 6 hours, after the reaction, the reaction product is settled by centrifugation Remove the catalyst, add 4% hydrochloric acid to the clear liquid for pickling, wash off the reaction product of hydrochloric acid and monoethanolamine and unreacted hydrochloric acid and monoethanolamine with deionized water, then add 8 times the volume of n-hexane, and heat up To 50 ℃ until the reaction product is completely dissolved, the fatty acid ethanolamide is removed by cooling and crystallization, and the solvent is removed...
Embodiment 2
[0031] The batch enzyme reaction is carried out in a batch-type stirred tank reactor, and the free fatty acid and monoethanolamine in the high acid value wheat germ oil are in a molar ratio of 1:2 (the acid value of the high acid value wheat germ oil is 21.87mgKOH / g), The ratio of added vegetable oil to methanol is 1:2.5 (w / v), add 10% egg shells, stir and react at normal pressure 50°C for 10 hours, after the reaction is over, the reaction product is removed by centrifugal sedimentation, and the concentration is added to the clear liquid Pickling with 2% hydrochloric acid, and then washing away the reaction product of hydrochloric acid and monoethanolamine and unreacted hydrochloric acid and monoethanolamine with deionized water, then adding 10 times the volume of n-hexane, and raising the temperature to 60°C until the reaction product is completely dissolved. The fatty acid ethanolamide was removed by cooling and crystallization, and the solvent was removed by rotary evaporati...
Embodiment 3
[0033] The batch enzyme reaction is carried out in a batch-type stirred tank reactor. The free fatty acid and monoethanolamine in the high acid value rice bran oil are in a molar ratio of 1:6 (the acid value of the high acid value rice bran oil is 33.59mgKOH / g), and the added The ratio of vegetable oil to n-hexane is 1:3 (w / v), add 8% crab shells, stir and react at 60°C under normal pressure for 12 hours, after the reaction, the reaction product is removed by centrifugal sedimentation to remove the catalyst, washed with water to remove unreacted monoethanolamine , and then add 5 times the volume of n-hexane, raise the temperature to 70°C until the reaction product is completely dissolved, cool down and crystallize to remove fatty acid ethanolamide, and remove the solvent by rotary evaporation to obtain a low-acid value vegetable oil with an acid value of 13.28 mgKOH / g.
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