Automatic strengthening system and process for preparing hydrogen peroxide based on anthraquinone method
A technology of hydrogen peroxide and anthraquinone method, applied in peroxide/peroxy hydrate/peroxyacid/superoxide/ozonide, inorganic chemistry, chemical instruments and methods, etc., can solve the problem of low system reaction efficiency
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Embodiment 1
[0107] Use above-mentioned system and process to carry out anthraquinone method to prepare hydrogen peroxide, wherein:
[0108] Hydrogenation reaction: In the process, a palladium catalyst is added to the hydrogenation tower, and an anthraquinone derivative-containing working solution composed of 2-ethylanthraquinone (EAQ), heavy aromatics (AR) and trioctyl phosphate is introduced, wherein EAQ The concentration is 110g / L, the reaction temperature is 35°C, the reaction pressure is 0.10MPa, and the gas-liquid ratio in the micro-interface generator is 400:1.
[0109] Oxidation reaction: The reaction temperature in the hydrogenation tower in the process is 38°C, the reaction pressure is 0.15MPa, and the gas-liquid ratio in the micro-interface generator is 600:1.
Embodiment 2
[0111] Use above-mentioned system and process to carry out anthraquinone method to prepare hydrogen peroxide, wherein:
[0112] Hydrogenation reaction: In the process, a palladium catalyst is added to the hydrogenation tower, and an anthraquinone derivative-containing working solution composed of 2-ethylanthraquinone (EAQ), heavy aromatics (AR) and trioctyl phosphate is introduced, wherein EAQ The concentration is 120g / L, the reaction temperature is 37°C, the reaction pressure is 0.13MPa, and the gas-liquid ratio in the micro-interface generator is 500:1.
[0113] Oxidation reaction: In the process, the reaction temperature in the hydrogenation tower is 40°C, the reaction pressure is 0.17MPa, and the gas-liquid ratio in the micro-interface generator is 700:1.
Embodiment 3
[0115] Use above-mentioned system and process to carry out anthraquinone method to prepare hydrogen peroxide, wherein:
[0116] Hydrogenation reaction: In the process, a palladium catalyst is added to the hydrogenation tower, and an anthraquinone derivative-containing working solution composed of 2-ethylanthraquinone (EAQ), heavy aromatics (AR) and trioctyl phosphate is introduced, wherein EAQ The concentration is 125g / L, the reaction temperature is 39°C, the reaction pressure is 0.14MPa, and the gas-liquid ratio in the micro-interface generator is 600:1.
[0117] Oxidation reaction: In the process, the reaction temperature in the hydrogenation tower is 42°C, the reaction pressure is 0.19MPa, and the gas-liquid ratio in the micro-interface generator is 750:1.
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