Method for preprocessing neopentyl glycol industrial wastewater by catalytic oxidation
A technology for the production of neopentyl glycol and wastewater, applied in the direction of oxidized water/sewage treatment, chemical instruments and methods, molecular sieve catalysts, etc., to achieve the effects of reducing organic loads, low cost, and broad prospects for engineering applications
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Embodiment 1
[0021] Take 2.0 grams of copper nitrate to make a copper nitrate solution with a mass fraction of 2.0%; then weigh 20.0 grams of γ-Al 2 o 3 Added to 2.0% copper nitrate solution, the catalyst active component, that is, copper nitrate, was evenly distributed in the γ-Al by equal volume impregnation method. 2 o 3 The catalyst was impregnated for 2 hours, dried at a constant temperature of 100°C for 8 hours, and calcined at 300°C for 3 hours.
Embodiment 2
[0023] Take 1.0 gram of ferric nitrate and make it into a 1.0% ferric nitrate solution; then weigh 20.0 grams of γ-Al 2 o 3 Added to 1.0% ferric nitrate solution, the active component of the catalyst, namely copper nitrate, was evenly distributed in the γ-Al 2 o 3 The catalyst was soaked for 1 hour, then dried at 80°C for 9 hours, and calcined at 200°C for 4 hours.
Embodiment 3
[0025] Take 6.0 grams of copper nitrate to make a copper nitrate solution with a mass fraction of 6.0%; then weigh 20.0 grams of γ-Al 2 o 3 Added to 6.0% copper nitrate solution, the catalyst active component, that is, copper nitrate, was evenly distributed in the γ-Al 2 o 3 The catalyst was impregnated for 2 hours, dried at a constant temperature of 100°C for 8 hours, and calcined at 300°C for 3 hours.
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