A comprehensive treatment method and device for selenium-containing wastewater
A comprehensive treatment and wastewater technology, applied in water/sewage treatment, water treatment parameter control, water/sewage multi-stage treatment, etc., can solve the trouble of choosing chemicals, can not handle selenium-containing wastewater, limited anaerobic biological tolerance, etc. problems, achieve the effects of reduced processing load, improved economic benefits, and reduced toxicity
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Embodiment 1
[0032] The process flow of the invention is adopted to treat the selenium-containing wastewater. The water quality of the wastewater is: pH is 7.3, and the selenate ion (SeO2) in the wastewater is determined by single column ion chromatography. 4 2- ) concentration is 3263.2μg / L, selenite ion (SeO 3 2- ) concentration was 2697.3μg / L, COD was 633mg / L, and ammonia nitrogen was 52.4 mg / L. The concentration of sulfur dioxide in the flue gas is 3170mg / m³.
[0033] A two-stage gas-liquid contact reaction tower is adopted, the selenium-containing wastewater first enters the second reactor, and the liquid-gas volume ratio is controlled to be 5L / m 3 , remove sulfur dioxide in the flue gas, and discharge the purified gas; the effluent from the second reactor enters the anaerobic reactor, and uses a biological contact tower to inoculate the deselenium sludge from the selenium-containing environment. The temperature is controlled at 30°C and the pH is 7- 8. The treatment time is 8 ho...
Embodiment 2
[0036] The method of the invention is used to treat the selenium-containing wastewater. Wastewater water quality: pH is 6.7, utilizes single-column ion chromatography to measure wherein selenate ion (SeO 4 2- ) concentration is 21228.3μg / L, selenite ion (SeO 3 2- ) concentration was 12757.7μg / L, COD: 682mg / L, ammonia nitrogen: 73.3 mg / L. The concentration of sulfur dioxide in the flue gas is 8630mg / m³.
[0037] A two-stage gas-liquid contact reaction tower is adopted, the selenium-containing wastewater first enters the second reactor, and the liquid-gas volume ratio is controlled to be 25L / m 3 , remove sulfur dioxide in the flue gas, and discharge the purified gas; the effluent from the second reactor enters the anaerobic reactor, and uses a biological contact tower to inoculate the deselenium sludge from the selenium-containing environment. The temperature is controlled at 30°C and the pH is 7 -8, the treatment time is 12 hours, and 51% of the selenate ions in the wastew...
Embodiment 3
[0040] The anaerobic activated sludge taken from the selenium-containing environment was used for domestication as follows: (1) Nutrient salts ammonium chloride and potassium dihydrogen phosphate were added to the original selenium-containing wastewater in advance so that the concentrations were 1mg / L and 0.2mg / L, respectively. L, and add a certain concentration of methanol as a hydrogen source; (2) Adopt continuous water inflow operation mode to control the SeO in inflow water 4 2- The concentration is 400μg / L, and the hydraulic retention time is controlled to be 8h. When the SeO in the effluent 4 2- When the concentration is lower than 100μg / L, the SeO 4 2- Anaerobic sludge with specific reducing ability; (3) Adopt intermittent water inflow operation mode, gradually increase SeO in influent water according to 100μg / L 4 2- The concentration of SeO in anaerobic sludge 4 2- Bacteria with strong processing ability proliferate in large quantities; when SeO 4 2- The conce...
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