A method for preparing high-content mixed tocopherols by extraction and separation of lyotropic liquid crystals
A technology of lyotropic liquid crystals and tocopherols, which is applied in the fields of chemical engineering and natural product separation, can solve problems such as the inability to separate high-content mixed tocopherols with high efficiency and low energy consumption, and achieve good application prospects, environmental friendliness, and high extraction capacity.
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Embodiment 1
[0047] The extraction agent is prepared by dissolving choline laurate in DMSO, wherein the molar fraction of choline laurate is 5%; take the deodorized distillate of vegetable oil after esterification (which contains 20% mixed tocopherols), dissolve it in n-hexane , and made into a 150mg / ml raw material solution. Under the condition that the liquid flow ratio of the extractant to the raw material is 1:0.5, after 4 stages of countercurrent extraction at 40°C, the extract phase is collected, 2 times the volume of acetonitrile and water are added thereto, back-extracted with 3 times the volume of n-hexane, and the Evaporation, washing, drying and other post-treatment steps to obtain mixed tocopherol products, the purity of which is 93%, and the yield is 98%.
Embodiment 2
[0049] Dissolve tetraethylquaternary ammonium laurate in DMSO to prepare extractant, wherein the molar fraction of tetraethylquaternary ammonium laurate is 10%; get the vegetable oil deodorization distillate after esterification (which contains mixed tocopherols 75%), dissolved in petroleum ether with a boiling range of 60-90°C, and made into a 100mg / ml raw material solution. Under the condition that the liquid flow ratio of extractant to raw material is 1:10, after 4 stages of countercurrent extraction at 30°C, the extract phase is collected, 3 times the volume of water and acetonitrile are added to it, and the boiling range is 60 Petroleum ether back-extraction at ~90°C, after evaporation, water washing, drying and other post-treatment steps, the mixed tocopherol product is obtained, with a purity of 92% and a yield of 90%.
Embodiment 3
[0051] The extraction agent is prepared by dissolving 1-ethyl-3-methylimidazole laurate in acetonitrile, wherein the molar fraction of 1-ethyl-3-methylimidazole laurate is 15%; take the vegetable oil after esterification The deodorized distillate (which contains 25% mixed tocopherols) is dissolved in petroleum ether with a boiling range of 90-120° C. to prepare a 125 mg / ml raw material solution. Under the condition that the liquid flow ratio of extractant, washing agent and raw material is 1:0.2:0.5, after three-stage fractional distillation extraction operation at 30°C, the extract phase is collected, and a certain amount of DMF and acetonitrile are added to it, and the boiling range is 90~ Back extraction with petroleum ether at 120°C, followed by evaporation, water washing, drying and other post-processing steps to obtain mixed tocopherol products with a purity of 95% and a yield of 99%.
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