Catalyst of reaction for removing oxynitrides by methane and preparation method thereof
A technology of nitrogen oxides and catalysts, which is applied in the field of catalysts for removing nitrogen oxides from methane and its preparation, can solve the problems of narrow active temperature range, complicated preparation methods, and low catalyst activity, and achieve good water and sulfur resistance, The preparation method is simple and the effect of improving the removal efficiency
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Embodiment 1
[0017] With 29.1g tetraethylammonium bromide, 29ml ammonia water, 3.45g sodium metaaluminate (41wt.%Al 2 o 3 , 35wt.% Na 2 (2) and 1.88g sodium hydroxide are dissolved in 50ml water, then add 83.5ml silica sol (29wt.%), after crystallization 200 hours under 413K, add 2.75g sodium metaaluminate and 1.2g sodium hydroxide again, in 443K crystallization for 24 hours to obtain Na-Beta / Mordenite double microporous molecular sieve; 4 NO 3 Exchanged for 24 hours, and then calcined at 823K for 5 hours to obtain H-Beta / Mordenite double microporous molecular sieves. Put 1g of H-Beta / Mordenite double microporous molecular sieve into 30ml of 0.015mol / L cobalt acetate solution, exchange at 80°C for 24h, dry at 110°C for 12 hours, and finally bake at 550°C for 4 hours to obtain the cobalt content 2.5% Co-HBeta / Mordenite catalyst. The catalyst was ground and pressed into tablets, broken into 40-60 mesh particles, 0.5 g was taken and placed in a quartz tube reactor, and the reaction activ...
Embodiment 2
[0029]The preparation of the carrier H-Beta / Mordenite, the preparation of the Co-HBeta / Mordenite catalyst and the activity evaluation method are the same as in Example 1, except that the concentration of cobalt acetate solution used for ion exchange is 0.01mol / L, and the cobalt content is 1.6%. . The reaction results showed that when the reaction temperatures were 400, 450, 500, 550, 600, and 650°C, the conversion rates of NO were 51.2, 73.3, 91.6, 85.1, 78.5, and 65.3%, respectively.
Embodiment 3
[0031] The preparation of the carrier H-Beta / Mordenite, the preparation of the Co-HBeta / Mordenite catalyst and the activity evaluation method are the same as in Example 1, except that the concentration of cobalt acetate solution used for ion exchange is 0.005mol / L, and the cobalt content is 1.0% . The reaction results showed that when the reaction temperatures were 400, 450, 500, 550, 600, 650°C, the conversion rates of NO were 45.8, 67.9, 86.8, 82.5, 74.4, 63.9%, respectively.
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