Method for producing mono-hydrogen peroxide diisopropylbenzene
A technology of dicumyl hydrogen peroxide and dicumyl benzene is applied in the field of producing dicumyl hydrogen peroxide, can solve the problems of low product yield and high cost of additives, and achieves improving product yield and reducing additives. cost, and the effect of increasing the oxidation reaction rate
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Embodiment 1
[0011] 5% by weight of hydrochloric acid was used as a pH adjuster to adjust the pH of the reaction material to 1.60, the reaction pressure in the oxidation reactor was 1.2 MPa, the reaction temperature was 200° C., and the mass ratio of dicumyl to air was 3.33. Dicumyl and air are oxidized in the oxidation reactor to produce dicumyl hydroperoxide MHP.
[0012] The residence time is 24.0 hours, the product yield is 20.40% by weight, and the cost of the added pH regulator is 33.0 yuan / kg of MHP.
Embodiment 2
[0014] Same as [Example 1], except that the pH regulator used is 10% by weight of sulfuric acid to adjust the pH of the reaction material to 1.40.
[0015] The residence time is 24.0 hours, the product yield is 21.25% by weight, and the cost of the added pH regulator is 33.9 yuan / kg of MHP.
Embodiment 3
[0017] Same as [Example 1], except that the pH regulator used is 10% by weight of NaOH, and the pH of the reaction material is adjusted to 11.68.
[0018] The residence time is 24.0 hours, the product yield is 18.12% by weight, and the cost of the added pH regulator is 32.1 yuan / kg MHP.
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