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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Embodiment 1
[0020] 1. Vegetable oil deodorization distillate 3000kg, the raw material of the present invention contains about 4% β-sitosterol, in addition contains 80% fatty acid, about 5% natural VE, about 3% other sterols and a small amount of triglyceride etc. For other ingredients, put in 5m 3 Add 1200kg of methanol (at normal temperature) to the enamel reactor, start stirring, add 210kg of concentrated sulfuric acid, and at a temperature of 80°C, the esterification reaction uses acid as a catalyst and lower alcohol as a reaction solvent to carry out the esterification reaction After 4 hours, 80% of the fatty acid was esterified into fatty acid methyl ester, so as to be separated from the raw material. The end of the reaction in the esterification process is based on an acid value less than 2. Stand to separate methanol and sulfuric acid mixture.
[0021] 2. Add 450kg of methanol into the enamel reactor with 3000kg of esterified oil, start stirring, add 45kg of NaOH, and carry out a...
Embodiment 2
[0027] 1. Take 500kg of vegetable oil deodorized distillate (containing about 7% β-sitosterol), 3 Add 150kg of ethanol to the reactor, stir to dissolve, add 30kg of phosphoric acid, reflux and stir at 70°C for 3 hours, let stand, and separate ethanol and phosphoric acid.
[0028] 2. Add 100kg of ethanol to the kettle, start stirring, add 5kg of KOH, and stir at 70°C for 1 hour under reflux.
[0029] 3. Add 70kg of water at 80°C to wash the oily reaction material, wash 3 times until pH=7.
[0030] 4. Put the washed oil into the short-path distillation device, at 150°C and 50Pa, feed 4 liters per minute, and 200kg of fatty acid methyl ester can be separated.
[0031] 5. About 300kg of the heavy component enters the filter press for filtration at 70°C to obtain about 290kg of filtrate. At 70°C, 12kg of regulator is added. The regulator is 10% sulfuric acid and water in a weight ratio of 1:2.5. Gradually lower the temperature and cool down to 30°C, filter to obtain about 60kg of...
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