Formula for coal-fired flue gas denitrification catalyst activity regeneration
A denitration catalyst, coal-fired flue gas technology, applied in catalyst regeneration/reactivation, physical/chemical process catalysts, chemical instruments and methods, etc. Influence and other problems, to achieve the effect of solving toxic effects
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Embodiment 1
[0020] Take a piece of honeycomb-type monolithic catalyst that has been running for more than 15000 h, with a volume of 122.5 cm 3 , after removing the dust from the surface, place it in the regeneration solution. The regeneration solution consists of (NH 4 ) 2 SO 4 (0.1~10 mol / L), EDTA (0.01~0.2 wt %), OP~(n) (n=10, 0.1~5 wt %), penetrant JFC (0.1~5 wt %), flat plus O (0.1~5 wt %), and using oxalic acid as solvent, adding ammonium metavanadate (0.5~10 wt %), ammonium paratungstate (0.5~10 wt %). During the regeneration process, the bottom aeration is used for auxiliary cleaning to remove the sediment in the internal pores of the catalyst. Drying and high-temperature calcination are carried out after the regeneration to remove the residual (NH 4 ) 2 SO 4 solid. The activity of the catalyst after regeneration was 96%, which was 35.7% higher than that before regeneration; the specific surface area of the catalyst increased by 22.0%.
Embodiment 2
[0022] Take a honeycomb-type monolithic catalyst with a volume of 122.5 cm 3 , after cleaning the surface dust, put it in the regeneration solution. The regeneration solution consists of (NH 4 ) 2 SO 4 (0.1~10 mol / L), EDTA (0.01~0.2 wt %), OP~(n) (n=10, 0.1~5 wt %), penetrant JFC (0.1~5 wt %), flat plus O (0.1~5 wt %), and using oxalic acid as solvent, adding ammonium metavanadate (0.5~10 wt %), ammonium paratungstate (0.5~10 wt %). During the regeneration process, the bottom aeration is used for auxiliary cleaning to remove the sediment in the internal pores of the catalyst. Drying and high-temperature calcination are carried out after the regeneration to remove the residual (NH 4 ) 2 SO 4 solid. The activity of the catalyst after regeneration is 94%, which is 66.7% higher than that before regeneration; the specific surface area of the catalyst is increased by 25.1%.
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