Regeneration method of SCR (selective catalytic reduction) catalyst
A kind of SCR catalyst and catalyst technology, applied in the direction of chemical instruments and methods, separation methods, adipic acid production, etc., can solve the problem of affecting catalyst activity recovery, poor cleaning effect of alkaline and alkaline earth metals, unfavorable uniform loading of active components, etc. problems, to achieve the effect of saving dosage, high recovery rate and reducing the loss of active substances
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Embodiment 1
[0035] Embodiment 1 A kind of regeneration method of SCR catalyst, specifically as follows:
[0036] Using the deactivated catalyst of a denitrification catalyst in a power plant after 3 years of operation, the denitrification efficiency is 60%, and the SO 2 converted to SO 3The oxidation rate is 0.47%. After physical and mechanical ash removal, soak in deionized water at 50°C for 30 minutes to remove ash deposits in the micropores; 3wt% sodium dodecylbenzenesulfonate solution with a concentration of 0.1wt%, soaked at 50°C for 20min; The concentration of sodium benzenesulfonate is 0.1wt% solution, soaking at 50°C for 30min. After cleaning, immerse in the deionized water prepared by the concentration of ammonium metavanadate of 0.5wt%, the concentration of ammonium paratungstate is 5wt%, the concentration of ammonium paramolybdate is 3wt%, the concentration of oxalic acid is 5.5wt% in the activation solution Active material loading was carried out for 10 min.
[0037] The ...
Embodiment 2
[0038] Embodiment 2 A kind of regeneration method of SCR catalyst, specifically as follows:
[0039] The deactivated catalyst after 4 years of denitrification catalyst in a power plant has a denitrification efficiency of 68%, SO 2 converted to SO 3 The oxidation rate is 0.42%. After physical and mechanical ash removal, soak in deionized water at 80°C for 30 minutes to remove ash deposits in the micropores; then immerse in deionized water prepared by sodium diamine tetraacetate 2wt%, sodium carbonate concentration of 0.2wt %, sodium dodecylbenzenesulfonate concentration of 0.05wt% solution, soaked at 80 ℃ for 40min; finally immersed in adipic acid prepared by deionized water concentration of 5wt%, dodecylbenzenesulfonate Sodium acid concentration is 0.05wt% solution, soaked at 80 ℃ for 40min. After the cleaning is completed, immerse in an activation solution prepared by deionized water with a concentration of 0.8wt% ammonium metavanadate, 3wt% ammonium paratungstate, 4wt% am...
Embodiment 3
[0041] Embodiment 3 A kind of regeneration method of SCR catalyst, specifically as follows:
[0042] The deactivated catalyst of a denitrification catalyst in a power plant after 3 years of operation has a denitrification efficiency of 58%, SO 2 converted to SO 3 The oxidation rate is 0.38%. After physical and mechanical ash removal, soak in deionized water at 60°C for 30 minutes to remove ash deposits in the micropores; 5wt% sodium dodecylbenzenesulfonate solution with a concentration of 0.2wt%, soaking at 60°C for 20min; Concentration of 0.2wt% solution, soaking at 60°C for 20min. After cleaning, immerse in the deionized water prepared by the concentration of ammonium metavanadate 2wt%, the concentration of ammonium paratungstate is 3.9wt%, the concentration of ammonium paramolybdate is 0.1wt%, the concentration of oxalic acid is 5wt% in the activation solution Carry out active material loading for 20min.
[0043] The results showed that the denitrification activity rec...
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