MnMe/molecular sieve series catalysts and preparation and application thereof
A technology of catalysts and molecular sieves, which is applied in molecular sieve catalysts, physical/chemical process catalysts, chemical instruments and methods, etc., can solve the problems of poor anti-sintering ability of active components, insufficient low-temperature activity, and unsatisfactory selectivity, etc., to achieve increased Effective surface area, low activation temperature, and improved low-temperature activity
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Embodiment 1
[0024] Take manganese nitrate (Mn(NO 3 ) 2 ·6H 2 O)977.2g and copper nitrate (Cu(NO 3 ) 2 ·3H 2 (2) 38.0g, respectively dissolved in water and made into a mixed solution, then put the molecular sieve carrier RPSA 1000g into the aqueous solution to impregnate, stir constantly, evaporate the water to dryness at 30°C under vacuum conditions to obtain the catalyst precursor, and the above catalyst precursor Body was roasted at 800 DEG C for 2 hours to obtain the catalyst of the present invention. Taking the molecular sieve carrier quality as a benchmark, the loading of the catalyst Mn was 30%, and the loading of Cu was 1%. The catalyst made was: Mn(30)Cu( 1) / PSRY.
[0025] This series of catalysts is used for NH 3 Selective reduction of NOx in flue gas, reducing agent NH 3The molar ratio to NOx is 1.1:1.0, and the concentration of NOx in the flue gas is 100ppm. Reaction temperature T corresponding to NO removal rate of 50%, 85% and 95% 50 , T 85 and T 95 They are: 140°...
Embodiment 2
[0027] Get manganese nitrate 488.6g and lanthanum nitrate (La(NO 3 ) 3 ·6H 2 (2) 155.9g, respectively dissolved in water and made into a mixed solution, then 1000 grams of molecular sieve carrier HZSM-5 was immersed in the aqueous solution, stirred constantly, evaporated to dryness at a temperature of 50°C under vacuum conditions to obtain a catalyst precursor, and Above-mentioned catalyst precursor is calcined at 300 ℃ for 10 hours, obtains the catalyst of the present invention, is based on molecular sieve carrier mass, and the loading capacity of this catalyst Mn is 15%, and the loading capacity of La is 5%, is recorded as: Mn(15)La( 5) / HZSM-5.
[0028] This series of catalysts is used for NH 3 In the selective reduction of NOx, the reducing agent NH 3 The molar ratio to NOx is 1.0:1.0, and the concentration of NOx in the flue gas is 1000ppm. Reaction temperature T corresponding to NO removal rate of 50%, 85% and 95% 50 , T 85 and T 95 They are: 140°C, 200°C and 245°...
Embodiment 3
[0030] Weigh manganese nitrate 162.9g, cerium nitrate (Ce(NO 3 ) 3 ·6H 2 O)247.9g and ferric nitrate (Fe(NO 3 ) 2 9H 2 O) 144.7g, respectively dissolved in water and made into a mixed solution, 1000g NH 4 The Y molecular sieve carrier is immersed in an aqueous solution, stirred continuously, evaporated to dryness at a temperature of 70°C under vacuum conditions to obtain a catalyst precursor, and roasting the above catalyst precursor at 300°C for 5 hours to obtain the catalyst of the present invention. The mass of the molecular sieve carrier is Benchmark, the load of this catalyst Mn is 5%, the load of Ce is 8%, the load of Fe is 2%, is recorded as: Mn(15)Ce(5)Fe(2) / NH 4 Y.
[0031] This series of catalysts is used for NH 3 In the selective reduction of NOx, the reducing agent NH 3 The molar ratio to NOx is 0.8:1.0, and the concentration of NOx in the flue gas is 600ppm. Reaction temperature T corresponding to NO removal rate of 50%, 85% and 95% 50 , T 85 and T 95 ...
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