TiO-supported vanadium-tungsten composite oxide monolithic catalyst for flue gas denitrification
A composite oxide and monolithic technology, which is applied in the control of catalytic selective reduction of nitrogen oxides, the preparation of the above-mentioned catalyst, the above-mentioned catalyst, and the field of fixed source or mobile source denitrification, which can solve the problem of huge equipment, high operating cost, and waste water generation. and other issues, to achieve the effect of good stability, strong moisture resistance and wide operating temperature
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Example Embodiment
[0028] Example one
[0029] Monolithic catalyst for denitration with varying active composition.
[0030] 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, dissolve it with a certain concentration of nitric acid solution, stir evenly, and then ball mill for 1-5 hours to obtain a certain concentration of γ-Al 2 O 3 Slurry. Immerse the pre-treated cordierite honeycomb ceramics in the prepared γ-Al 2 O 3 After immersing in the slurry for 1 to 5 minutes, take it out, blow out the remaining liquid in the pores, dry in the shade at 80-130°C for 2-10 hours, and then calcinate at 500°C for 2-8 hours to obtain a load of 10% γ-Al 2 O 3 Of cordierite honeycomb ceramic samples.
[0031] Load γ-Al 2 O 3 And TiO 2 Preparation of cordierite honeycomb ceramics. Dissolve a certain amount of tetrabutyl titanate or titanium ethylate in absolute ethanol, stir for 1-30 minutes, add a certain amount of conce...
Example Embodiment
[0035] Example two
[0036] 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 is varied within the range of 5-15 wt% and 5-10 wt%, and the TVW content of the monolithic destocking catalyst is 15%, and the molar ratio of V / Ti is 0.15.
[0037] The catalytic activity test is the same as in Example 1. The results show that the content changes of the two supports have little effect on the overall catalytic performance.
Example Embodiment
[0038] Example three
[0039] 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-TW is adjusted to 10wt%, the content of the monolithic out-of-stock catalyst V-TW is 15wt%, and the molar ratio of V / Ti is 0.15.
[0040] The catalytic activity test was the same as in Example 1, and the reaction temperature was 150°C. Concentration of reaction tail gas: 35ppTiO, 0ppTi 2 O and 365ppTi 2 .
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