Efficient denitrified integral catalyst of stationary source
An integral, fixed-source technology, applied in the field of fixed-source denitrification, can solve the problem of catalyst low temperature and other problems, and achieve the effects of good stability, strong sulfur resistance, and wide operating temperature
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Embodiment 1
[0030] Monolithic catalyst for stationary source denitrification with varying active composition.
[0031] Contains γ-Al 2 o 3 Preparation of cordierite honeycomb ceramics. Weigh a certain amount of diaspore, add a certain proportion of urea or ammonia water, dissolve it with a certain concentration of nitric acid solution, stir it evenly, and ball mill it for 1 to 5 hours to obtain a certain concentration of γ-Al 2 o 3 slurry. The pre-treated cordierite honeycomb ceramics were impregnated in the prepared γ-Al 2 o 3 In the slurry, take it out after immersing for 1-5 minutes, blow off the residual liquid in the channel, dry in the shade and dry at 80-130°C for 2-10 hours, and then bake at 500°C for 2-8 hours to obtain 10% γ-Al loading 2 o 3 cordierite honeycomb ceramic samples.
[0032] Loaded γ-Al 2 o 3and TiO 2 Preparation of cordierite honeycomb ceramics. Dissolve a certain amount of tetrabutyl titanate or titanium ethoxide in absolute ethanol, stir for 1 to 30 m...
Embodiment 2
[0037] The preparation method of the catalyst is the same as in Example 1. γ-Al 2 o 3 and TiO 2 The content of V-OMS varies in the range of 5-15wt% and 5-10wt%, respectively, and the content of V-OMS in the monolithic de-sales catalyst is 15%, and the molar ratio of V / Mn is 0.15.
[0038] The catalytic activity test is the same as in Example 1. The results showed that the content changes of the two supports had little effect on the overall catalytic performance.
Embodiment 3
[0040] The preparation method of the catalyst is the same as in Example 1. γ-Al 2 o 3 and TiO 2 The content of V-OMS is adjusted to 10wt%, the content of V-OMS is 15wt%, and the molar ratio of V / Mn is 0.15.
[0041] The catalytic activity test was the same as in Example 1, and the reaction temperature was 150°C. Concentration of reaction tail gas: 35ppmNO, 0ppmN 2 O and 365ppmN 2 .
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