Urea supported carbon based denitration catalyst, preparation and application method thereof
A denitration catalyst and catalyst technology, applied in chemical instruments and methods, physical/chemical process catalysts, separation methods, etc., can solve problems such as difficulty in controlling the amount of ammonia added, easy leakage of ammonia, difficulties in operation and storage, etc.
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Embodiment 1
[0023] Weigh 0.5 g of F22 pitch-based spherical activated carbon (Shanghai Heda Carbon Co., Ltd.) with a particle size of 0.4-0.6 mm, and impregnate the pitch-based spherical activated carbon in urea aqueous solution (the concentration of urea is 0.049 g / ml) for 6h, followed by drying at 70°C for 6h, the catalyst can be prepared, wherein the loading of urea is 9%.
[0024] The prepared catalyst was installed in a fixed-bed reactor, and the temperature was raised to 30°C for ventilation. The simulated flue gas composition was: 500ppmNO, 21vol%O 2 , N 2 As balance gas, normal pressure operation, space velocity is 6000h -1 . The test result is: the stable conversion rate of NO is 61%, and the duration is 10h.
Embodiment 2
[0026] Weigh 0.5 g of F22 pitch-based spherical activated carbon with a particle size of 0.4-0.6 mm, and impregnate the pitch-based spherical activated carbon in urea aqueous solution (the concentration of urea is 0.068 g / ml) for 12 h by using an equal-volume impregnation method. After drying at ℃ for 12 hours, the catalyst can be prepared, and the loading amount of urea is 12%.
[0027] The prepared catalyst was installed in a fixed-bed reactor, and the temperature was raised to 30°C for ventilation. The simulated flue gas composition was: 500ppmNO, 21vol%O 2 , N 2 As balance gas, normal pressure operation, space velocity is 5000h -1 . The test result is: the stable conversion rate of NO is 53%, and the duration is 19h.
Embodiment 3
[0029] Weigh 0.5 g of F22 pitch-based spherical activated carbon with a particle size of 0.4-0.6 mm, and impregnate the pitch-based spherical activated carbon in urea aqueous solution (the concentration of urea is 0.026 g / ml) for 18 hours by using an equal-volume impregnation method. After drying at ℃ for 18 hours, the catalyst can be prepared, and the loading amount of urea is 5%.
[0030] The prepared catalyst was installed in a fixed-bed reactor, and the temperature was raised to 30°C for ventilation. The simulated flue gas composition was: 500ppmNO, 21vol%O 2 , N 2 As balance gas, normal pressure operation, space velocity is 6200h -1 . The test result is: the stable conversion rate of NO is 74%, and the duration is 5h.
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