Method for removing dissolvent residual from lycopene oleoresin
A technology of lycopene oil and resin, which is applied in the direction of organic chemistry, distillation purification/separation, etc., can solve the problems that organic solvent residues cannot be fully removed, limit the wide application of lycopene, and cannot completely remove solvent residues, etc., to achieve easy operation, Enhanced activity and high product quality
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Embodiment 1
[0016] A method for removing solvent residues in lycopene oleoresin, using lycopene oleoresin as raw material, wherein the content of lycopene is 7.23%, the content of n-hexane is 2%, and the content of ethyl acetate is 0.8%. The steps are as follows:
[0017] (1) Add 50ml of lycopene oleoresin extract to be treated in the material bottle;
[0018] (2) After checking and confirming that the system is airtight, turn on the vacuum pump to degas the material. After the vacuum degree is stable, the degassing process is completed;
[0019] (3) Set the scraper speed to 96r / min, feed rate to 10ml / min, molecular distillation pressure to 6.5Pa, distillation temperature to 85°C, water circulation cooling, condensation temperature to 40°C, open the material valve, and the material flows into the distillation body for molecular distillation. Distillation, the impurities contained in the oleoresin enter the distillate component, and the remaining residue component is collected as the purif...
Embodiment 2
[0022] A method for removing solvent residues in lycopene oleoresin, using lycopene oleoresin as raw material, wherein the content of lycopene is 5.69%, the content of ethanol is 0.6%, and the content of ethyl acetate is 0.4%. The steps are as follows:
[0023] (1) Add 50ml of lycopene oleoresin extract to be treated in the material bottle;
[0024] (2) After checking and confirming that the system is airtight, turn on the vacuum pump to degas the material. After the vacuum degree is stable, the degassing process is completed;
[0025] (3) Set the scraper speed to 96r / min, feed rate to 12ml / min, molecular distillation pressure to 2.5Pa, distillation temperature to 100°C, water circulation cooling, condensation temperature to 40°C, open the material valve, and the material flows into the distillation body for molecular distillation. Distillation, the impurities contained in the oleoresin enter the distillate component, and the remaining residue component is collected as the pur...
Embodiment 3
[0028] A method for removing solvent residues in lycopene oleoresin, using lycopene oleoresin as raw material, wherein the content of lycopene is 6.14%, the content of ethanol is 1%, and the content of ethyl acetate is 0.9%. The steps are as follows:
[0029] (1) Add 50ml of lycopene oleoresin extract to be treated in the material bottle;
[0030] (2) After checking and confirming that the system is airtight, turn on the vacuum pump to degas the material. After the vacuum degree is stable, the degassing process is completed;
[0031] (3) Set the scraper speed to 110r / min, feed rate to 15ml / min, molecular distillation pressure to 0.5Pa, distillation temperature to 85°C, water circulation cooling, condensation temperature to 40°C, open the material valve, and the material flows into the distillation body for molecular distillation. Distillation, the impurities contained in the oleoresin enter the distillate component, and the remaining residue component is collected as the purif...
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