Method for oxidizing cyclic ketone by utilizing zinc-supported Beta molecular sieve
A β-molecular sieve and cyclic ketone oxidation technology are applied in molecular sieve catalysts, chemical instruments and methods, and oxidative preparation of carboxylic acids, etc., which can solve the problems of non-compliance with the basic principles of green chemistry, unstable properties of heteropolyacid catalysts, and difficult purification. Achieve catalytic oxidation activity and catalytic activity stability, high catalytic oxidation activity and activity stability, and overcome the complex production process
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Embodiment 1
[0043] Take by weighing 2.3 grams of zinc-loaded acid-eluting aluminum nano-beta-molecular sieve catalyst (zinc oxide content 2.5wt%, aluminum oxide content 2.3wt%) and put it in a 100ml three-necked flask, then add a magnetic stirrer, 19.63 grams of ring Pentanone, 36 grams of dioxane and 23ml of 30% hydrogen peroxide, the molar ratio of cyclopentanone to hydrogen peroxide is 1:1. The three-necked flask is placed on a temperature-controlled magnetic stirrer, and the upper part of the three-necked flask is condensed and refluxed with a condenser, and the magnetic stirrer and heating device are started to start the reaction. The reaction temperature was controlled at about 64°C. After 3 hours of reaction, the conversion rate of cyclopentanone was 20.65%, the selectivity of generating δ-valerolactone was 96.45%, the selectivity of 5-hydroxyvaleric acid was 1.08%, and the selectivity of pentadiene Acid selectivity was 0.17%.
Embodiment 2
[0045] Take by weighing 2.44 grams of zinc-loaded acid-eluting aluminum nano-beta-molecular sieve catalyst (zinc oxide content 3.1wtwt%, aluminum oxide content is 1.8wt%) and be loaded in a 100ml three-necked flask, then add a magnetic stirrer, 19.63 grams of ring Pentanone, 6.4 grams of methanol and 23ml of 30% hydrogen peroxide, the molar ratio of cyclopentanone to hydrogen peroxide is 1:1. The three-necked flask is placed on a temperature-controlled magnetic stirrer, and the upper part of the three-necked flask is condensed and refluxed with a condenser, and the magnetic stirrer and heating device are started to start the reaction. The reaction temperature was controlled at about 70°C. After 5 hours of reaction, the conversion rate of cyclopentanone was 37.82%, the selectivity of generating δ-valerolactone was 28.65%, the selectivity of 5-hydroxyvaleric acid was 21.78%, and the selectivity of pentadiene Acid selectivity was 28.37%.
Embodiment 3
[0047] Take by weighing 2.65 grams of zinc-loaded acid-eluting aluminum nano-beta-molecular sieve catalyst (zinc oxide content 2.6wt%, aluminum oxide content is 2.2wt%) and be loaded in a 100ml three-necked flask, then add a magnetic stirrer, 19.63 grams of ring Pentanone, 18 grams of acetone and 46 ml of 30% hydrogen peroxide, the molar ratio of cyclopentanone to hydrogen peroxide is 1:2. The three-necked flask is placed on a temperature-controlled magnetic stirrer, and the upper part of the three-necked flask is condensed and refluxed with a condenser, and the magnetic stirrer and heating device are started to start the reaction. The reaction temperature was controlled at about 70°C. After 6 hours of reaction, the conversion rate of cyclopentanone was 68.57%, the selectivity of generating δ-valerolactone was 93.98%, the selectivity of 5-hydroxyvaleric acid was 3.28%, and the selectivity of pentadiene Acid selectivity was 1.57%.
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