Resource utilization method of acid wastewater
A technology for recycling acidic wastewater, applied in chemical instruments and methods, multi-stage water/sewage treatment, water/sludge/sewage treatment, etc., can solve the problems of no use value and low acid concentration, and achieve low treatment costs Effect
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Embodiment 1
[0041] Add sodium hydroxide solution to wastewater with sulfuric acid content of 0.9% and nitric acid content of 0.6% to make the pH of the wastewater = 6.5. After cooling the wastewater to 20°C, add PAM (polyacrylamide) flocculant to the wastewater. According to the addition of 0.5% in the waste water, after precipitation, the suspended solids in the waste water are removed by ultrafiltration through a fiber ball filter and two precision filters with a filter aperture of 5 μm, and then the waste water is treated with 2m 3 The flow rate of / h enters the electrodialysis treatment device. The salt content (including sodium sulfate and sodium nitrate) in the concentrated water after electrodialysis treatment is 10.8%, and the power consumption for treating 1 ton of wastewater is 4.0kwh. Then the waste water with a salt content of 10.8% was treated with 0.1m according to the method of patent number 201010570625.3. 3The flow rate of / h enters the multi-effect membrane distillation ...
Embodiment 2
[0044] Add potassium hydroxide solution to wastewater with a sulfuric acid content of 0.9% and a nitric acid content of 0.6% to make the pH of the wastewater = 6.4. After cooling the wastewater to 30°C, add PAM (polyacrylamide) flocculant to the wastewater. According to the addition of 0.5% in the waste water, after precipitation, the suspended solids in the waste water are removed by ultrafiltration through a fiber ball filter and two precision filters with a filter aperture of 5 μm, and then the waste water is treated with 2m 3 The flow rate of / h enters the electrodialysis treatment device. The salt content (including potassium sulfate and potassium nitrate) in the concentrated water after electrodialysis treatment is 10.1%, and the power consumption for treating 1 ton of wastewater is 4.1kwh. Then the waste water with a salt content of 10.1% was treated with 0.1m according to the method of Patent No. 201010570625.3. 3 The flow rate of / h enters the multi-effect membrane di...
Embodiment 3
[0047] Add sodium hydroxide solution to wastewater with sulfuric acid content of 0.9% and nitric acid content of 0.6% to make the pH of the wastewater = 6.0. After cooling the wastewater to 40°C, add PAM (polyacrylamide) flocculant to the wastewater. According to the addition of 0.5% in the waste water, after precipitation, the suspended solids in the waste water are removed by ultrafiltration through a fiber ball filter and two precision filters with a filter aperture of 5 μm, and then the waste water is treated with 2m 3 The flow rate of / h enters the electrodialysis treatment device. After the electrodialysis treatment, the salt content (including ammonium sulfate and ammonium nitrate) in the concentrated water is 10%, and the power consumption for treating 1 ton of wastewater is 3.8kwh. Then the waste water with a salt content of 10% was mixed with 0.1m according to the method of Patent No. 201010570625.3. 3 The flow rate of / h enters the multi-effect membrane distillation...
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