Process for purifying solanesol from tobacco leaf extract
A technology of solanesol and tobacco leaves, which is applied to the field of purifying solanesol from tobacco leaf extract and the preparation of intermediates, and can solve the problems of product purity and quality failing to meet requirements, complicated process, and insignificant purity improvement.
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Embodiment 1
[0028] Weigh 100kg of tobacco leaf extract with a solanesol content of 14.5% and add it to the saponification tank, start the agitator, add 100kg of 20% lye at an even speed within 30 minutes, keep warm at 60°C for three hours, and add 500kg of n-hexane after saponification The alkane was stirred and extracted three times, and the n-hexane layer was collected under reduced pressure to recover the n-hexane to obtain 71kg of n-hexane extract. The liquid extract was kept at 40°C and the flow rate was controlled at 0.5 liters / min. The concentration is controlled below 1-10 Pa to obtain 38kg of light phase transparent tobacco leaf absolute and heavy phase solanesol. Solanesol is dissolved in n-hexane and added to a silica gel chromatographic column. : 20 ratio for mobile phase elution, collect the high-purity solanesol segment, and desolventize to obtain 9.1kg of high-purity solanesol, keep the high-purity solanesol at 40°C and control the flow rate to 0.1 liter / min and pour it into...
Embodiment 2
[0030] Weigh 100kg of Yinye extract with a content of 16.7% into the saponification tank, start the agitator, add 100kg of 15% lye at an even speed within 30 minutes, keep warm at 55°C for three hours, and add 500kg after saponification The n-pentane was stirred and extracted three times, and the n-pentane layer was collected under reduced pressure to recover the n-pentane to obtain 75kg of n-pentane extract. The liquid extract was kept at 40°C and the flow rate was controlled at 0.5 liters / min. The temperature is 150°C, the vacuum degree is controlled below 1-10 Pa, and the light phase transparent tobacco leaf absolute and the heavy phase solanesol 43kg are obtained, and the solanesol is dissolved in n-pentane and added to a silica gel column, and n-pentane and acetone The mixed solvent was used as mobile phase elution at a ratio of 100:15, and the high-purity solanesol segment was collected and desolvated to obtain 9.6kg of high-purity solanesol. The high-purity solanesol was...
Embodiment 3
[0032] Weigh 100kg of tobacco leaf extract with a solanesol content of 13.2% and add it to the saponification tank, start the agitator, add 100kg of 25% lye at an even speed within 30 minutes, keep warm at 65°C for three hours, and add 500kg of petroleum oil after saponification The ether was stirred and extracted three times, and the petroleum ether layer was collected under reduced pressure to recover the petroleum ether to obtain 65 kg of petroleum ether extract. The liquid extract was kept at 40°C and the flow rate was controlled at 0.5 liters / min. The concentration is controlled below 1-10 Pa to obtain 39kg of light phase transparent tobacco leaf absolute and heavy phase solanesol. Solanesol is dissolved in petroleum ether and added to a silica gel chromatographic column, and the mixed solvent of petroleum ether and methanol is used at a ratio of 100:8. The proportion is used for mobile phase elution, and the high-purity solanesol segment is collected and desolvated to obt...
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