Novel supported catalyst, preparation method therefor and use of novel supported catalyst
A supported catalyst, ozone catalytic oxidation technology, applied in chemical instruments and methods, physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, etc., can solve the problem of low production efficiency and non-repeatability of ozone generators Utilization, short service life and other problems, to achieve the effect of being conducive to industrial application, good effect of advanced treatment, and reducing production cost
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Embodiment 1
[0025] With 2-4mm alumina as the carrier, after activation treatment, Cd(NO 3 ) 2 As the precursor of Cd, after configuring it into an aqueous solution with a mass fraction of 3%, the Cd(NO 3 ) 2 Loaded on the carrier, calcined, and after activation and reduction, the supported catalyst AODO with a mass fraction of 2% is obtained; the percentage refers to the percentage of the active component in the total mass of the supported catalyst; wherein, the activated carrier The time is 2 minutes; the temperature for the activation of the carrier is 400°C; the time for the calcination is 1 hour; the temperature for the calcination is 500°C. The specific surface area of the finally prepared supported catalyst AODO is 230m 2 / g, the pore volume is 0.36mL / g, and the pore diameter is 6.80nm (measured by X-ray fluorescence spectrometer).
Embodiment 2
[0027] Use 2-4mm alumina as the carrier, after activation treatment, use ZnCl 2 As the precursor of Zn, after configuring it into an aqueous solution with a mass fraction of 2%, the ZnCl 2 Loaded on the carrier, calcined, after activation and reduction, the supported catalyst AODO with a mass fraction of 4% is obtained; the percentage refers to the percentage of the active component in the total mass of the supported catalyst; wherein, the activated carrier The time is 15 minutes; the temperature for the activation of the carrier is 500°C; the time for the calcination is 2 hours; the temperature for the calcination is 540°C. The specific surface area of the finally prepared supported catalyst AODO is 240m 2 / g, the pore volume is 0.38mL / g, and the pore diameter is 7.10nm (measured by X-ray fluorescence spectrometer).
Embodiment 3
[0029] With 2-4mm alumina as the carrier, after activation treatment, Ni(NO 3 ) 2 ·6H 2 O is used as the precursor of Ni. After configuring it into an aqueous solution with a mass fraction of 2%, the Ni(NO 3 ) 2 Loaded on the carrier, calcined, after activation and reduction, the supported catalyst AODO with a mass fraction of 4% is obtained; the percentage refers to the percentage of the active component in the total mass of the supported catalyst; wherein, the activated carrier The time is 10 minutes; the temperature for the activation of the carrier is 450°C; the time for the calcination is 2 hours; the temperature for the calcination is 550°C. The specific surface area of the finally prepared supported catalyst AODO is 246m 2 / g, the pore volume is 0.42mL / g, and the pore diameter is 6.92nm (measured by X-ray fluorescence spectrometer).
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