Cerium oxide/HZSM-5 molecular sieve composite catalytic material, preparation method, and application thereof in decomposing carbon tetrafluoride
A catalytic material, carbon tetrafluoride technology, applied in molecular sieve catalysts, separation methods, chemical instruments and methods, etc., can solve problems such as low activity and poor stability, and achieve high catalytic activity, stable catalytic performance, and preparation process. simple effect
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Embodiment 1
[0051] Analytical pure cerium nitrate (Ce(NO 3 ) 3 ·6H 2 O) added to deionized water to make Ce 3+ A colorless solution with a concentration of 0.015 to 0.15 mol / L, the resulting solution is denoted as A; the HZSM-5 molecular sieve (Si / Al=18) was heated to 550°C at a heating rate of 2°C / min and kept for 5 hours to remove the commercial HZSM- 5 The template agent remaining in the molecular sieve was used to obtain solid A; 3 g of solid A was added to 30 mL of solution A, stirred at 500 rpm / min for 3 h, and the solution obtained by ultrasonic treatment for 3 h was recorded as B; the solution B was left to stand for 12 h, and placed in an oven at 80 ° C Dry to obtain sample C; place sample C in a tube furnace at 700°C, and roast it under a nitrogen atmosphere for 4 hours, with a heating rate of 5°C / min; after roasting, it is naturally cooled to room temperature under a nitrogen atmosphere, and taken out from the roasting tube. Obtain white cerium oxide / HZSM-5 molecular sieve c...
Embodiment 2
[0053] The commercial HZSM-5 molecular sieve (Si / Al=18) was heated to 550°C at a heating rate of 2°C / min and kept for 5 hours to remove the template agent remaining in the commercial HZSM-5 molecular sieve to obtain a solid HZSM-5 molecular sieve. The experiment was carried out in a fixed-bed reactor, the filling capacity of HZSM-5 molecular sieve was 1g, and nitrogen was used as CF 4 Carrier gas, control its flow rate to 2.5mL / min (10000ppm), another path of nitrogen as a balance gas to control its flow rate to 30ml / min (60vol%), and the flow rate of water vapor after vaporization to 17.5ml / min (35vol%), Keep the total gas flow rate at 50mL / min, and the experimental temperature at 550°C. After flue gas treatment, the catalyst treatment efficiency was recorded after the concentration of carbon tetrafluoride reached a stable level. The result is as figure 2 shown, from figure 2 It can be seen that the use of a single HZSM-5 molecular sieve for CF 4 The catalytic conversio...
Embodiment 3
[0055] Analytical pure cobalt nitrate (Ce(NO 3 ) 3 ·6H 2 O) Put it into a crucible and place it in a tube furnace for roasting at 650-750° C. to obtain pure cerium oxide solid. The experiment was carried out in a fixed-bed reactor with a filling capacity of 1 g of pure cerium oxide, and nitrogen was used as CF 4 Carrier gas, control its flow rate to 2.5mL / min (10000ppm), another path of nitrogen is used as a balance gas to control its flow rate to 30ml / min (60vol%), and the flow rate of water vapor after vaporization is 17.5ml / min (35vol%), Keep the total gas flow rate at 50mL / min, and the experimental temperature at 550°C. After flue gas treatment, the catalyst treatment efficiency was recorded after the concentration of carbon tetrafluoride reached a stable level. The result is as image 3 shown, from image 3 It can be seen that using a single cerium oxide for CF 4 The catalytic conversion rate is only about 7%.
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