A kind of preparation method of propylene oxide
A technology of propylene oxide and epoxidation reaction, which is applied in the field of propylene oxide, can solve the problems of increased TBHP content, hidden dangers of incineration and other safety hazards, and achieve the effect of increasing the reaction rate
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[0039] The preparation method of the present invention will be described in further detail below with reference to specific examples. It should be understood that the following examples are only for illustrating and explaining the present invention, and should not be construed as limiting the protection scope of the present invention. All technologies implemented based on the above content of the present invention are covered within the intended protection scope of the present invention.
[0040] The experimental methods used in the following examples are conventional methods unless otherwise specified; the reagents, materials, etc. used in the following examples can be obtained from commercial sources unless otherwise specified.
Embodiment 1
[0047] 150.00g of the primary epoxidation product tower bottom heavy component in Comparative Example 1 was added to the rectifying tower, and concentrated by vacuum rectification. A total of 34.8 g of TBA and some impurities are extracted from the top of the tower, of which the content of acetone is 0.88 wt % and the content of water is 0.98 wt %. The tower still produced 115.0 g of heavy components in the tower still, wherein the content of TBHP was 7.46 wt %, the content of acetone was 0.017 wt %, and the content of water was 0.20 wt %.
[0048] Add 115.00g of the above-mentioned tower reactor components to a 1L stainless steel reaction kettle, then add 25.12g of propylene, heat up to control the reaction temperature at 134°C, and react for 34 minutes. The content of TBHP is 0.23wt% and the content of PO is 3.59wt% by sampling and analysis. .
[0049] After calculation, the conversion rate of the secondary epoxidation reaction TBHP was 96.2%, and the selectivity of PO was ...
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