A low-temperature flue gas denitration catalyst using CO to selectively reduce NOx and its application
A denitration catalyst, low temperature flue gas technology, applied in molecular sieve catalysts, physical/chemical process catalysts, chemical instruments and methods, etc., can solve the problems of reduced NO removal rate, unsuitable catalyst preparation, and low specific surface area.
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Embodiment 1
[0032] The low-temperature flue gas denitration catalyst using CO to selectively reduce NOx of the present embodiment is prepared according to the following steps:
[0033] A. Add Cu(NO) to the 5L stirred tank 3 ) 2 0.20mol / L, Mn(NO 3 ) 2 2.0L of 0.20mol / L aqueous solution (quality 2110g), pH 3.5; start stirring, heat up to 90°C, add 1280g of newly prepared ammonium type SSZ-13 molecular sieve water-containing suction filter cake (550g in terms of solids), control The temperature was 85°C for 1.5h for ion exchange, suction filtration, rinsing and suction filtration with 2400g water three times, the filter cake was dried at 120°C for 5h, calcined at 570°C for 6h in an air-conditioned muffle furnace, and pulverized to -600 mesh to obtain Cu -Mn / SSZ-13 molecular sieve calcined powder; the Cu-Mn / SSZ-13 molecular sieve calcined powder obtained by testing, in terms of oxide mass content, contains CuO2.6% and MnO1.7%; ammonium type SSZ-13 is prepared The sodium type SSZ-13 molecu...
Embodiment 2
[0038] The steps A-C of Example 1 were basically repeated to prepare the low-temperature flue gas denitration catalyst using CO to selectively reduce NOx in this example. The difference was that in step B, the amount of basic copper carbonate was 160 g, and the aluminum phosphate sol-pseudoboehmite composite glue was used. The consumption of the liquid is 1300g, and the water absorption rate of the obtained roasted bar is 0.42ml / g; in step C, 84ml of acetic acid aqueous solution with a mass concentration of 75% is sprinkled.
[0039] It is estimated that the mass percentage of each main component in the low-temperature flue gas denitration catalyst of this embodiment is about 37.7% of SSZ-13 molecular sieve in hydrogen form, 9.5% of copper in CuO, and 5.0% of manganese in MnO.
Embodiment 3
[0041] Basically repeat the steps A-C of Example 2 to prepare the low-temperature flue gas denitration catalyst using CO to selectively reduce NOx in this example, the difference is that the amount of basic manganese carbonate in step B is 180g, the aluminum phosphate sol-pseudoboehmite composite glue The consumption of the liquid is 1400g, and the water absorption rate of the obtained roasted bar is 0.43ml / g; in step C, 86ml of acetic acid aqueous solution with a mass concentration of 80% is sprinkled.
[0042] It is estimated that the mass percentage of each main component in the low-temperature flue gas denitration catalyst of this embodiment is about 36.0% of SSZ-13 molecular sieve in hydrogen form, 10.0% of copper in CuO, and 8.0% of manganese in MnO.
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Abstract
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Application Information
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