Method for performing Fenton treatment on 6-nitro-1-diazo-2-naphthol-4-sulfonic acid wastewater and coproducing sodium sulfate
A technology of acid oxygen body and sodium sulfate, which is applied in filtration treatment, multi-stage water treatment, water/sewage treatment, etc., can solve the problems of incomplete oxidation, low removal rate of organic matter, and low utilization rate, so as to improve efficiency and The effect of equipment utilization, improvement of wastewater treatment efficiency, and ease of recycling
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Embodiment 1
[0031] Put 200ml of 6-nitro-1,2,4-acid oxygen body reduction transposition wastewater into a beaker, adjust the pH to 2.5 with sodium carbonate, add 0.3g of activated carbon and 1mmol of FeSO at 35°C 4 , and then slowly add 3ml mass percent concentration of 28% H 2 o 2 , keep the temperature constant, let the reaction stand for 2h, adjust the pH to 10 with 25% aqueous sodium hydroxide solution in mass percentage, slowly add 10% Al in mass fraction under stirring 2 (SO 4 ) 3 solution, adjust the pH to 6.2, and then let it stand for 0.5h. Filter the turbid liquid after standing and settling. Repeat the process of oxidation, sedimentation and filtration for 3 times, the filtrate meets the treatment requirements, and after evaporation, concentration and drying, industrial grade sodium sulfate is obtained, with a content of more than 98%.
Embodiment 2
[0033] Put 200ml of 6-nitro-1,2,4-acid oxygen body acid precipitation wastewater into a beaker, adjust the pH to 2.0 with sodium carbonate, add 0.4g of activated carbon and 2mmol of FeSO at 45°C 4 , and then slowly add 4ml mass percent concentration of 28% H 2 o 2 , keep the temperature constant, let it stand for 1.5h, adjust the pH to 9.5 with 35% aqueous sodium hydroxide solution, slowly add 30% Al with mass fraction under stirring 2 (SO 4 ) 3 solution, adjust the pH to 6.5, and then let it stand for 1h. Filter the turbid liquid after standing and settling. The process of oxidation, sedimentation and filtration is repeated twice, and the filtrate meets the treatment requirements. After evaporation, concentration and drying, industrial grade sodium sulfate is obtained, with a content of more than 98%.
Embodiment 3
[0035] Put 100ml of 6-nitro-1,2,4-acid oxygen body reduction translocation and acid precipitation wastewater into a beaker, adjust the pH to 2.8 with 30% sodium hydroxide, add 0.1g of activated carbon at 25°C, 0.5 mmol FeSO 4 , and then slowly add 2ml mass percent concentration of 28% H 2 o 2 , keep the temperature constant, let the reaction stand for 1.5h, adjust the pH to 9.3 with 30% aqueous sodium hydroxide solution, slowly add Al with a mass fraction of 20% under stirring 2 (SO 4 ) 3solution, adjust the pH to 6.5, and then let it stand for 0.5h. Filter the turbid liquid after standing and settling. Repeat the process of oxidation, sedimentation and filtration for 4 times, and the filtrate meets the processing requirements. After evaporation, concentration and drying, industrial grade sodium sulfate is obtained, with a content of more than 98%.
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