Catalyst for volatile halocarbon catalytic combustion and its preparation method and use
A catalytic combustion and catalyst technology, applied in the direction of physical/chemical process catalysts, molecular sieve catalysts, chemical instruments and methods, etc., can solve the problems of low activity, high price, complicated production, etc., achieve low reaction temperature, low price, and easy collection Effect
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Embodiment 1
[0024] Dissolve 0.167g of commercially available copper nitrate trihydrate in 10mL of deionized water, add 10g of HSBA-15 zeolite molecular sieve into it, heat at 70°C in a water bath with magnetic stirring for 5h, and then place it in an oven at 100°C Dry overnight. Finally, it is roasted. The roasting process is: start heating at 30°C, raise the temperature to 600°C at a rate of 2°C / min, and keep it at this temperature for 4h. The obtained sample is a 0.5% Cu-loaded catalyst, marked as 0.005 Cu / HSBA-15.
[0025] Put the above catalyst 0.005Cu / HSBA-15 in a fixed bed reactor, pass through 20.3L / h of waste gas containing trichlorethylene and excess air, and the space velocity is 15000h -1 , the concentration of trichlorethylene in the exhaust gas is 300ppm, and the combustion reaction is carried out in a fixed-bed reactor at a combustion temperature of 100°C. Finally, the conversion rate of trichlorethylene is 20.4%, and the generated CO 2 、H 2 O and hydrogen halide are disc...
Embodiment 2
[0027] Dissolve 0.334g of commercially available copper nitrate trihydrate in 10mL of deionized water, add 10g of HSBA-15 zeolite molecular sieve to it, heat at 70°C in a water bath with magnetic stirring for 5h, and then place it in an oven at 100°C Dry overnight. Finally, it is roasted. The roasting process is: start heating at 30°C, raise the temperature to 400°C at a rate of 2°C / min, and keep it at this temperature for 6h. The obtained sample is a 1% Cu-loaded catalyst, marked as 0.01 Cu / HSBA-15.
[0028] Put the above catalyst 0.01Cu / HSBA-15 in a fixed bed reactor, pass through the exhaust gas containing trichlorethylene and excess air with a volume flow rate of 41.336L / h, and the space velocity is 15000h -1 , the concentration of trichlorethylene in the exhaust gas is 300ppm, and the combustion reaction is carried out in a fixed-bed reactor at a combustion temperature of 250°C. Finally, the conversion rate of trichlorethylene is 30.2%, and the generated CO 2 、H 2 O an...
Embodiment 3
[0030] Dissolve 1.07g of commercially available ferric nitrate in 10mL of deionized water, add 10g of HSBA-15 zeolite molecular sieve into it, heat at 70°C in a water bath with magnetic stirring for 5h, and then place it in an oven at 100°C overnight drying. Finally, it is roasted. The roasting process is as follows: start heating at 30°C, raise the temperature to 600°C at a rate of 2°C / min, and keep it at this temperature for 6h. The obtained sample is a catalyst loaded with 3% Fe, marked as 0.03 Fe / HSBA-15.
[0031] Put the above catalyst 0.03Fe / HSBA-15 in a fixed bed reactor, pass through the exhaust gas containing trichlorethylene and excess air with a volume flow rate of 276.75L / h, and the space velocity is 15000h -1 , the concentration of trichlorethylene in the exhaust gas is 2500ppm, and the combustion reaction is carried out in a fixed-bed reactor at a combustion temperature of 300°C. Finally, the conversion rate of trichlorethylene is 30.5%, and the generated CO2 、H...
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