Method and catalyst for low-temperature catalytic combustion elimination of polychlorinated aromatic hydrocarbons
A low-temperature catalysis, aromatic hydrocarbon technology, applied in combustion methods, physical/chemical process catalysts, chemical instruments and methods, etc., to achieve the effects of strong chlorine poisoning resistance, convenient and practical technical route, and long service life
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Embodiment 1
[0028] Dissolve commercially available 12.7g of sodium carbonate in 100ml of water to form a sodium carbonate solution as solution A; dissolve commercially available 7.3g of cobalt nitrate hexahydrate in 50ml of water to form a solution of cobalt nitrate as solution B; in an oil bath at 80°C , under the condition of stirring, add the A solution drop by drop to the B solution to form a precipitate, and let it stand in the air at room temperature for 12 hours; filter the filter cake, wash the filter cake to about PH=7, and dry it in an oven at 110°C for 12 hours. Take it out and grind it into powder, then move it to the muffle furnace for roasting. The calcination process is as follows: start heating at 50°C, program temperature increase at a heating rate of 1°C / min, raise the temperature to 500°C, and keep at 500°C for 4 hours to obtain pure tricobalt tetroxide catalyst.
Embodiment 2
[0030] Dissolve commercially available 12.72g of sodium carbonate in 100ml of water to form a sodium carbonate solution as solution A; dissolve commercially available 7.28g of cobalt nitrate hexahydrate in 50ml of water to form a cobalt nitrate solution, and then add 0.813g of 50% cobalt nitrate to the cobalt nitrate solution manganese nitrate solution to form a mixed solution of cobalt nitrate and manganese nitrate as solution B; in an oil bath at 80°C, under the condition of stirring, add solution A drop by drop to solution B to form a precipitate. Stand in the middle for 12 hours; filter to get the filter cake, wash the filter cake to about PH = 7, dry in an oven at 110°C for 12 hours, take it out and grind it into powder, then move it to a muffle furnace for roasting. The calcination process was the same as in Example 1 to obtain a manganese-doped tricobalt tetroxide catalyst with a molar ratio of cobalt to manganese of 11:1, which was designated as Co11Mn1 catalyst.
Embodiment 3
[0032] According to the method of Example 2, a cobalt-manganese composite oxide catalyst with a cobalt-manganese molar ratio of 9:1 was prepared, which was referred to as Co9Mn1 catalyst.
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