Production method of high-content beta-sitosterin
A production method and technology for sitosterol are applied in the production field of high-content β-sitosterol, can solve problems such as trivial details, difficulty in separation, no production method for β-sitosterol, etc., achieve full utilization of resources, improve purity and yield , the effect of large-scale industrial production value and social benefits
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Example Embodiment
[0019] Example one:
[0020] 1. 3000kg of vegetable oil deodorized distillate. The raw material of the present invention contains about 4% β-sitosterol, in addition to 80% fatty acid, 5% natural VE, about 3% other sterols and a small amount of triglycerides, etc. Other ingredients, put in 5m 3 In the enamel reactor, put 1200kg of methanol (input at room temperature) to start stirring, add 210kg of concentrated sulfuric acid, and at a temperature of 80℃, the esterification reaction uses acid as a catalyst and lower alcohol as the reaction solvent to carry out the esterification reaction. In 4 hours, the fatty acid containing 80% is esterified into fatty acid methyl ester to facilitate separation from the raw material. The end of the reaction of the esterification process takes the acid value less than 2 as the indicator. Set aside to separate the methanol and sulfuric acid mixture.
[0021] 2. Add 450kg of methanol to the enamel reactor containing 3000kg of esterified oil, start st...
Example Embodiment
[0026] Embodiment two:
[0027] 1. Take 500kg of vegetable oil deodorized distillate (containing about 7% of β-sitosterol), 3 Add 150kg of ethanol to the reaction kettle, stir to dissolve, add 30kg of phosphoric acid, reflux and stir at 70°C for 3 hours, stand still to separate ethanol and phosphoric acid.
[0028] 2. Add 100 kg of ethanol to the kettle, start stirring, add 5 kg of KOH, and stir at 70°C under reflux for 1 hour.
[0029] 3. Add 70kg, 80°C water to wash the oily reaction material, wash 3 times, to PH=7.
[0030] 4. Put the water-washed oil into the short-path distillation unit, and feed 4 liters per minute at 150°C and 50 Pa, and 200kg of fatty acid methyl esters can be separated.
[0031] 5. About 300kg of the reconstituted portion enters the filter press to filter at 70°C to obtain about 290kg of filtrate. At 70°C, 12kg of regulator is added, and the regulator is 10% sulfuric acid and water in a weight ratio of 1:2.5. Gradually reduce the temperature and cool to 3...
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