Method for utilizing cycloalkanol in eucalyptol separation water solution and application of cycloalkanol
A technology of cycloalkanol and eucalyptol, which is applied in the field of cycloalkanol, can solve problems such as difficult and effective separation of cycloalkanol, failure to achieve separation, waste of cycloalkanol, etc., and achieves beneficial recycling, excellent extraction effect, and reduced The effect of content
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Embodiment 1
[0030] An aqueous solution containing cyclohexanol at a concentration of 10,000 ppm was passed through a grid to remove impurities. Take eucalyptol and cyclohexanol aqueous solution and place them in an extraction vessel at a volume ratio of 0.5:1. Under the condition of 10°C, the rotating speed of the magnetic stirrer is 500rpm, stirring for 10min, and standing for 1h in a constant temperature bath at a temperature of 10°C. After standing, the solution is divided into upper and lower phases, and the lower raffinate phase is separated, and the content of cyclohexanol in the raffinate phase is 70 ppm by gas chromatography.
Embodiment 2
[0032] An aqueous solution containing cyclohexanol at a concentration of 20,000 ppm was passed through a grid to remove impurities. Take eucalyptol and cyclohexanol aqueous solution and put them in the extraction container according to the volume ratio of 1:1. Under the condition of 25°C, the rotating speed of the magnetic stirrer is 500rpm, stirring for 10min, and standing in a constant temperature bath at 25°C for 1h. After standing, the solution is divided into upper and lower phases, and the lower raffinate phase is separated, and the content of cyclohexanol in the raffinate phase is 110 ppm by gas chromatography.
Embodiment 3
[0034] An aqueous solution containing cyclohexanol at a concentration of 30,000 ppm was passed through a grid to remove impurities. Take eucalyptol and cyclohexanol aqueous solution and put them in the extraction container according to the volume ratio of 1:1. Under the condition of 25°C, the rotating speed of the magnetic stirrer is 500rpm, stirring for 10min, and standing in a constant temperature bath at 25°C for 1h. After standing, the solution is divided into upper and lower phases, and the lower raffinate phase is separated, and the content of cyclohexanol in the raffinate phase is 120 ppm by gas chromatography.
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