A preparation method of supported rare earth doped manganese oxide for ozone catalyst
A rare earth doping and catalyst technology, which is applied in the oxidation water/sewage treatment, textile industry wastewater treatment and other directions, can solve the problems of high equipment requirements, high energy consumption, reduced particle dispersion, etc., and achieves a simple preparation process and wide application. Foreground effect
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Embodiment 1
[0016] (1) Weigh 1 mmol 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 5 g of γ-Al to solution A obtained in step (1) 2 o 3 , heated to 65 °C after stirring for 120 min;
[0018] (3) Weigh 1mmol of KMnO 4 , dissolved in 10 mL of deionized water, then added to the mixed solution prepared in step 2, reacted for 2 h and stopped the reaction;
[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 min, 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 1 mmol 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 5 g of γ-Al to solution A obtained in step (1) 2 o 3 , heated to 75 °C after stirring for 120 min;
[0024] (3) Weigh 1mmol of KMnO 4 , dissolved in 10 mL of deionized water, then added to the mixed solution prepared in step 2, reacted for 4 h and stopped the reaction;
[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 min, 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 1 mmol 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 5 g of γ-Al to solution A obtained in step (1) 2 o 3 , heated to 75 °C after stirring for 120 min;
[0030] (3) Weigh 1mmol of KMnO 4 , dissolved in 10 mL of deionized water, then added to the mixed solution prepared in step 2, reacted for 4 h and stopped the reaction;
[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 min, 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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