Medium/low temperature SCR (Selective Catalytic Reduction) denitration catalyst with gamma-Al2O3 as carrier and preparation method thereof
A technology of aluminum oxide and denitration catalyst, which is applied in the field of formula composition and preparation of medium and low temperature selective catalytic reduction denitration catalyst, can solve the problems of high cost, poor water and sulfur resistance, complicated preparation process, etc., and achieves high utilization rate , stable performance and simple preparation process
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[0039] Example 1:
[0040] 1. The invention uses γ-Al 2 O 3 Supported medium and low temperature SCR denitration catalyst and its preparation:
[0041] (1) Using γ-Al 2 O 3 As a carrier, its characteristic is: γ-Al 2 O 3 The specific surface area is 142m 2 / g, the total pore volume is 0.43cm 3 / g, the average pore size is 12nm.
[0042] (2) Preparation method of composite impregnation solution: Add manganese acetate, lanthanum nitrate, and ferric nitrate to the water to prepare a composite impregnation solution. The composite impregnation solution is composed of the following components by mass percentage:
[0043] Manganese acetate 7%,
[0044] Lanthanum nitrate 4%,
[0045] Ferric nitrate 10%,
[0046] The rest is water.
[0047] (3) Loading of active components: the carrier γ-Al 2 O 3 Immerse in the composite impregnation solution prepared in step (2) for 3-15h, take it out and dry at room temperature (20℃), and then calcinate at 350-600℃ for 1-6h to prepare the γ-Al 2 O 3 The medium an...
Example Embodiment
[0054] Example 2:
[0055] The preparation method and product are the same as in Example 1, only the simulated smoke composition is changed, and the application is as follows:
[0056] Taking 0.50g of the catalyst of the present invention as the experimental object, in the temperature range of 200~350℃, the space velocity is 15,000 / h, and the simulated flue gas composition is: 1000ppm NO, NH 3 / NO=1.1, 5% O 2 , 400ppm SO 2 , 10% H 2 O, balance gas is N 2 , Its denitration efficiency is 77.12% at 200℃, and its denitration efficiency is 88.32% at 300℃. Generally, SO in flue gas 2 And H 2 O will cause catalyst poisoning, thereby reducing its denitration efficiency. It can be seen from the above that the catalyst of the present invention has better resistance to SO 2 And H 2 O performance, its denitration efficiency is still at a relatively high level, higher than the denitration efficiency of existing products under the same conditions (about 70%).
Example Embodiment
[0057] Example 3:
[0058] 1. The invention uses γ-Al 2 O 3 Supported medium and low temperature SCR denitration catalyst and its preparation:
[0059] (1) Using γ-Al 2 O 3 As a carrier, its characteristic is: γ-Al 2 O 3 The specific surface area is 142m 2 / g, the total pore volume is 0.43cm 3 / g, the average pore size is 12nm.
[0060] (2) Preparation method of composite impregnation solution: Add manganese acetate, lanthanum nitrate, and ferric nitrate to the water to prepare a composite impregnation solution. The composite impregnation solution is composed of the following components by mass percentage:
[0061] Manganese acetate 5%,
[0062] Lanthanum nitrate 3%,
[0063] Ferric nitrate 6%,
[0064] The rest is water.
[0065] (3) Loading of active components: the carrier γ-Al 2 O 3 Immerse in the composite impregnation solution prepared in step (2) for 3-15h, take it out and dry at room temperature (20℃), and then calcinate at 350-600℃ for 1-6h to prepare the γ-Al 2 O 3 The medium and...
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