Process for preparing high-purity decanediol by side-line vacuum distillation
A technology of vacuum distillation and decanediol, which is applied in the preparation of hydroxyl compounds, organic compounds, organic chemistry, etc., can solve the problems that there is no special description of the purification method of high-purity decanediol, so as to reduce production costs and energy The effect of low consumption and high product yield
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Embodiment 1
[0020] Side-line vacuum distillation process flow: the crude 1.10-decanediol is injected into the rectification tower through the feeding unit, and the rectification operation is carried out from the intermediate feed of the rectification tower, and the light components are extracted from the top of the rectification tower, Collect and process; extract the intermediate substance from the side discharge port of the rectification tower, and collect and process; the heavy component is extracted from the bottom of the rectification tower and collect and process, which is a high-purity 1.10-decanediol product.
Embodiment 2
[0022] The content of 1,10-decanediol in crude decanediol is 90%;
[0023] The operating conditions of rectification are: the vacuum degree is 0.0012MPa, the reflux ratio at the top of the rectification tower is 7:1, the temperature at the top of the tower is 132~143.5°C, the temperature at the side outlet is 158~162°C, and the temperature at the bottom of the tower is 170~183°C ℃; the purity of 1,10-decanediol prepared at the bottom of the tower is 99.95%.
Embodiment 3
[0025] The content of 1,10-decanediol in crude decanediol is 95%;
[0026] The rectification operating conditions are: the vacuum degree is 0.002MPa, the reflux ratio at the top of the rectification tower is 3:1, the temperature at the top of the tower is 132~138.5°C, the temperature at the side outlet is 155~158°C, and the temperature at the bottom of the tower is 172~190°C °C. The purity of 1,10-decanediol prepared at the bottom of the column was 99.8%.
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