A method and device for separating benzaldehyde, phenylpropionaldehyde, cinnamaldehyde, cinnamyl acetate and o-methoxycinnamaldehyde from cinnamon oil
A technology of cinnamon acetate and cinnamon oil, which is applied in chemical instruments and methods, fat oil/fat refining, separation/purification of carbonyl compounds, etc., can solve the problems of high cost, waste of resources, high energy consumption, etc., and reduce production costs , improve the yield, and the effect of high-efficiency separation
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Embodiment 1
[0026] Add 500.0 g of cinnamon oil containing 1.2% benzaldehyde, 0.7% phenylpropanal, 85% cinnamaldehyde, 0.7% acetate cinnamaldehyde and 4.5% o-methoxycinnamaldehyde. Water sodium sulfate for dehydration, put the processed cinnamon oil into material tank 1, control the rectifying column temperature at 75℃, evaporation temperature at 45℃, total reflux for 30min, reflux ratio of 1.5 and vacuum degree of 200 Pa, and collect the components in this section Obtain 3.2g of benzaldehyde with a purity of 63.2%; increase the rectifying column temperature to 85°C, evaporation temperature 55°C, total reflux for 40min, reflux ratio of 2.5 and vacuum degree of 130Pa, collect the components in this section, and obtain 1.8g with a purity of 51.4 % Phenylpropanal; keep the distillation column temperature 85℃, increase and control the evaporation temperature 80℃, total reflux 40 min, reflux ratio 3 and vacuum degree 50 Pa, collect 370.0g cinnamon with 99.5% purity in this section Aldehydes; inc...
Embodiment 2
[0028] Add 500.0 g of cinnamon oil containing 1.2% benzaldehyde, 0.7% phenylpropanal, 85% cinnamaldehyde, 0.7% acetic acid cinnamon fat, and 4.5% o-methoxycinnamaldehyde. The water sodium sulfate is dehydrated, the processed cinnamon oil is put into the material tank 1, and the material tank 1 of the molecular distillation and rectification coupling device is added to control the temperature of the rectifying column, the evaporation temperature, the reflux ratio and the vacuum degree, and the rectification conditions As follows: distillation column temperature 78℃, evaporation temperature 40℃, total reflux 35min, reflux ratio 2 and vacuum degree 220Pa. Collect the components in this section to obtain 3.1g of benzaldehyde with a purity of 61.7%; increase the distillation column temperature by 82 ℃, evaporating temperature 60℃, total reflux 48min, reflux ratio 3 and vacuum degree 120Pa, collect the components in this section, obtain 1.92g phenylpropanal with a purity of 53.2%; inc...
Embodiment 3
[0030] Add 500.0g of cinnamon oil with 1.2% benzaldehyde content, 0.7% phenylpropanal content, 85% cinnamaldehyde content, 0.7% acetate cinnamaldehyde content, and 4.5% o-methoxycinnamaldehyde content. The water sodium sulfate is dehydrated, the processed cinnamon oil is put into the material tank 1, and the material tank 1 of the molecular distillation and rectification coupling device is added to control the temperature of the rectifying column, the evaporation temperature, the reflux ratio and the vacuum degree, and the rectification conditions As follows: distillation column temperature 80℃, evaporation temperature 50℃, total reflux 40 min, reflux ratio 1.5 and vacuum degree 180 Pa. Collect the components in this section to obtain 3.6g of benzaldehyde with a purity of 66.0%; raise the distillation column Temperature 88℃, evaporating temperature 68℃, total reflux 40 min, reflux ratio 3 and vacuum degree 110Pa, collect the components in this section, obtain 2.06g phenylpropana...
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