Medium/low temperature SCR (Selective Catalytic Reduction) denitration catalyst with gamma-Al2O3 as carrier and preparation method thereof
A technology of aluminum oxide and denitrification catalyst, which is applied in the field of formula composition and preparation of medium and low temperature selective catalytic reduction denitrification catalyst, which can solve the problems of high cost, poor water resistance and sulfur resistance, complex preparation process, etc., and achieve high utilization rate , stable performance and simple preparation process
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Embodiment 1
[0040] 1. The γ-Al of the present invention 2 o 3 Medium and low temperature SCR denitrification catalyst as carrier and its preparation:
[0041] (1) Using γ-Al 2 o 3 As a carrier, it is characterized by: 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 diameter is 12nm.
[0042] (2) The preparation method of the composite impregnation solution: add manganese acetate, lanthanum nitrate, and iron nitrate to the water to prepare the composite impregnation solution. The composite impregnation solution is composed of the following components in mass percentage:
[0043] Manganese acetate 7%,
[0044] Lanthanum nitrate 4%,
[0045] Iron 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 3-15 hours, take it out, dry it at room temperature (20°C), and then calcinate at 350-600°C for 1-6 ho...
Embodiment 2
[0055] The preparation method and product are the same as in Example 1, only the composition of the simulated flue gas is changed, and the application is as follows:
[0056] Taking 0.50g of the catalyst of the present invention as the experimental object, within the temperature range of 200-350°C, 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, the balance gas is N 2 , its denitrification efficiency is 77.12% at 200°C and 88.32% at 300°C. Usually, SO in flue gas 2 and H 2 O can cause catalyst poisoning, thereby reducing its denitrification efficiency. As can be seen from the above, the catalyst of the present invention has better anti-SO 2 and H 2 O performance, its denitrification efficiency is still at a high level, which is higher than that of existing products under the same conditions (about 70%).
Embodiment 3
[0058] 1. The γ-Al of the present invention 2 o 3 Medium and low temperature SCR denitrification catalyst as carrier and its preparation:
[0059] (1) Using γ-Al 2 o 3 As a carrier, it is characterized by: 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 diameter is 12nm.
[0060] (2) The preparation method of the composite impregnation solution: add manganese acetate, lanthanum nitrate, and iron nitrate to the water to prepare the composite impregnation solution. The composite impregnation solution is composed of the following components in mass percentage:
[0061] Manganese acetate 5%,
[0062] Lanthanum nitrate 3%,
[0063] Iron 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 3-15 hours, take it out, dry it at room temperature (20°C), and then calcinate at 350-600°C for 1-6 ho...
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