Method and device for separating high-purity sabinene from cinnamomum longepaniculatum oil
A separation and high-purity technology, applied in distillation purification/separation, organic chemistry, etc., can solve problems such as the difficulty of further improving the purity of sabinene, environmental safety hazards, and the reduction of sabinene content
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Embodiment 1
[0031]One embodiment of the present invention is a method of separating high purity thyene from the oil oil, comprising the step of: step a, refining the oil branch leaf, distilled with water vapor, condenses, and the oil is separated. Ethen oil; this mode of operation is performed by existing essential oil refining equipment, and its operation is a conventional manner, and then dried and pulverized and pulverized, and mixed with aqueous solution of sodium chloride. The existing water vapor distillation apparatus is distilled, continuously heated, is condensed by a condensing apparatus to obtain a liquid, and then a layer of oily material is taken, and the amount of anhydrous sodium sulfate is added to obtain an oil. It is to be noted that the oil fuel is usually within 1.5 hours of extraction time, and there is an increase in the extraction time with the increase of the extraction time, and the extraction time increases with the increase of extraction time. The reason why the gas t...
Embodiment 2
[0039]Based on the above embodiment, another embodiment of the present invention is that the second condenser is condensed when it is condensed against the light phase gas, and the content of more than 85% is stored in the material receiving tank by the optometry. The volatiles produced during the working process are output to the buffer tank through fine hydrazine, and the camrhyl liquid in the wafer is trapped, and the fine hydrazine is trapped to the abether liquid through the optometry to the material receiving tank. Its second condenser output of the extract is trapped to the thyristor liquid, and its form is transparent. Since the process is in a vacuum environment, there is a negative pressure flow in the gas phase flow, and the volatile material is prevented by the buffer tank and the fine hydrazine from flowing to the negative pressure device, and the gas phase output by the condenser can be subjected to a secondary separation of hot hydrazine. The liquid separated liquid c...
Embodiment 3
[0041]Based on the above embodiment, another embodiment of the present invention is that the pressure of 4000 Pa in the rectification column is 4000Pa, and the rectification column temperature in the rectification column is 70 degrees Celsius, the evaporation temperature of the column is 80 degrees Celsius, and the reflow ratio controller The reflow ratio is 5 to 1, the distillation time is 1 hour, the obtained liquid, the content of the thye is 70%; since the oil fuel is usually within 1 hour, within 1.5 hours, if the fine When the distillation time is less than 1 hour, the tamamob oil does not meet the relevant requirements in the extraction rate. The molecular distiller is a scraper film molecular distiller, and the scraper rotation speed is 400 r / min, since the film speed has a certain effect on the product yield, if the speed is less than 400R / min, the thickness of the formed film is large, the heat transfer is uneven, Efficiency and yield will decrease. Among them, the fee...
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