Integrated absorbent and catalyzer for removing SO2and NOx and preparation method thereof
A catalyst and absorbent technology, which is applied in the field of integrated absorbent and catalyst for removing SO2 and NOx and its preparation, can solve the problem of a certain distance between commercialization and popularization, and achieve good application prospects, good regeneration performance, and simplification. The effect of desulfurization equipment
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Embodiment 1
[0034] Preferred embodiment one, a SO removal 2 with NO x The preparation method of the integrated absorber and catalyst specifically comprises steps:
[0035] (1) Take 97.5 parts of Al 2 o 3 The powder is prepared with a BET surface area of 225m 2 / g, the BJH adsorption pore volume is 0.49ml / g, the bulk density is 0.73g / ml, and the particle size is about 20 mesh microspheres;
[0036] The BET surface area here refers to the sum of the total surface area of all particles per gram of substance, which can be detected by a special instrument, and data processing is carried out according to the BET theory.
[0037] (2) Activate the above-mentioned microspheres and impregnate them in 2.5 parts of Cu(NO 3 ) 2 Keep in an equal volume of solution for 40 minutes;
[0038] (3) heating the above solution to 150°C and drying for 12 hours to obtain the dried crude catalyst;
[0039] (4) Calcining the dried crude catalyst at 500° C. for 5 hours, and cooling to obtain the desired...
Embodiment 2
[0040] Preferred embodiment two, a SO removal 2 with NO x The preparation method of the integrated absorber and catalyst specifically comprises steps:
[0041] (1) Take 85 parts of Al 2 o 3 The powder is prepared with a BET surface area of 295m 2 / g, the BJH adsorption pore volume is 0.64ml / g, the bulk density is 0.47g / ml, and the particle size is about 30 mesh microspheres;
[0042] (2) Activate the above microspheres and impregnate them in Cu(NO 3 ) 2 and 1 part of Zn(NO 3 ) 2 Keep in the mixed equal volume solution for 50 minutes;
[0043] (3) heating the above solution to 150°C and drying for 10 hours to obtain the dried crude catalyst;
[0044] (4) Calcining the dried crude catalyst at 600° C. for 7 hours, and cooling to obtain the desired desulfurizing agent.
Embodiment 3
[0045] Preferred embodiment three, a SO removal 2 with NO x The preparation method of the integrated absorber and catalyst specifically comprises steps:
[0046] (1) Take 78.5 parts of Al 2 o 3 The powder is prepared with a BET surface area of 205m 2 / g, the BJH adsorption pore volume is 0.54ml / g, the bulk density is 0.69g / ml, and the particle size is about 30 mesh microspheres;
[0047] (2) Activate the above microspheres and impregnate them in 20 parts of Cu(NO 3 ) 2 and 1.5 parts of Zn(NO 3 ) 2 Keep in the mixed equal volume solution for 60 minutes;
[0048] (3) heating the above solution to 130°C and drying for 11 hours to obtain the dried crude catalyst;
[0049] (4) Calcining the dried crude catalyst at 500° C. for 8 hours, and cooling to obtain the desired desulfurizing agent.
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