Preparation method of supported rare earth doped manganese dioxide (MnO2) used in ozone catalyst
A rare earth doping and catalyst technology is applied in the field of ozone decomposition catalyst and its preparation, which can solve the problems of high equipment requirements, high energy consumption, reduced particle dispersion and the like, and achieves the effects of broad application prospects and simple preparation process.
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Embodiment 1
[0016] (1) Weigh 1mmol of MnSO 4 ·H 2 O was dissolved in 10 mL of deionized water, and then 40 mL of isopropanol was added to prepare solution A;
[0017] (2) Add 5g of γ-Al in solution A obtained in step (1) 2 o 3 , heated to 65°C after stirring for 120 minutes;
[0018] (3) Weigh 1 mmol of KMnO 4 , dissolved in 10mL deionized water, then added to the mixed solution prepared in step 2, and stopped the reaction after reacting for 2 hours;
[0019] (4) Filter, wash and dry the product obtained in step 3 to obtain the modified γ-Al 2 o 3 sample.
[0020] The sample prepared in this example was used for ozone catalytic oxidation treatment of printing and dyeing wastewater. When the residence time was 60 minutes, the COD of import and export printing and dyeing wastewater was measured after the reaction was stable. The removal rate of COD was 81.2%, and the effluent was colorless and odorless.
Embodiment 2
[0022] (1) Weigh 1mmol of MnCl 2 4H 2 O and 0.1mmol La(NO 3 ) 3 ·6H 2 O. Dissolve in 10mL deionized water, then add 40mL isopropanol to prepare solution A;
[0023] (2) Add 5g of γ-Al in solution A obtained in step (1) 2 o 3 , heated to 75°C after stirring for 120min;
[0024] (3) Weigh 1 mmol of KMnO 4 , dissolved in 10mL of deionized water, then added to the mixed solution prepared in step 2, and stopped the reaction after reacting for 4 hours;
[0025] (4) Filter, wash and dry the product obtained in step 3 to obtain the modified γ-Al 2 o 3 sample.
[0026] The sample prepared in this example was used for ozone catalytic oxidation treatment of printing and dyeing wastewater. When the residence time was 60 minutes, the COD of import and export printing and dyeing wastewater was measured after the reaction was stable. The removal rate of COD was 99.6%, and the effluent was colorless and odorless.
Embodiment 3
[0028] (1) Weigh 1mmol of MnCl 2 4H 2 O and 0.1mmol Ga(NO 3 ) 3 ·6H 2 O. Dissolve in 10mL deionized water, then add 40mL isopropanol to prepare solution A;
[0029] (2) Add 5g of γ-Al in solution A obtained in step (1) 2 o 3 , heated to 75°C after stirring for 120min;
[0030] (3) Weigh 1mmol of KMnO 4 , dissolved in 10mL of deionized water, then added to the mixed solution prepared in step 2, and stopped the reaction after reacting for 4 hours;
[0031] (4) Filter, wash and dry the product obtained in step 3 to obtain the modified γ-Al 2 o 3 sample.
[0032] The sample prepared in this example was used for ozone catalytic oxidation treatment of printing and dyeing wastewater. When the residence time was 60 minutes, the COD of import and export printing and dyeing wastewater was measured after the reaction was stable. The removal rate of COD was 92.3%, and the effluent was colorless and odorless.
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