Method for removing thallium in wastewater
A waste water and ceramic material technology, applied in chemical instruments and methods, water pollutants, water/sewage treatment, etc., can solve problems such as inconvenient waste water recycling, difficulty in reaching standards, and increasing waste water salinity, and achieves suitable for large-scale applications, The process is simple and controllable, and the effect of reducing the amount of use
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Embodiment 1
[0031] 1. Ozone oxidation is introduced into the thallium-containing wastewater with a thallium content of 4.5mg / L, and the oxidation-reduction potential is controlled at 400-450mV during oxidation.
[0032] 2. Add mixed flocculant, in the mixed flocculant, the mass ratio of sodium hydroxide, sodium sulfide, polyferric sulfate, and sodium polystyrene sulfonate is: 3.2:1.8:4.5:0.5; during the flocculation process, the pH is controlled at 9- 10.
[0033] Sodium hydroxide, sodium sulfide, polyferric sulfate, and sodium polystyrene sulfonate are mixed and slowly dissolved in water at 55°C before use.
[0034] Add 20mL of mixed flocculant to every 500mL of waste water.
[0035] 3. Solid-liquid separation, adding a pore size of 10-22nm to the liquid part, using a carboxyl-modified ceramic material for adsorption, and keeping it in contact with wastewater for 10 minutes.
[0036] 4. Use deionized water to clean the ceramic material adsorbing thallium, and the contact time with deio...
Embodiment 2
[0039] 1. When the thallium-containing wastewater with a thallium content of 15.3mg / L is passed through ozone for oxidation, the oxidation-reduction potential is controlled to be 415mV during oxidation.
[0040] 2. Add the mixed flocculant, in the mixed flocculant, the mass ratio of sodium hydroxide, sodium sulfide, polyferric sulfate, and sodium polystyrene sulfonate in the mixed flocculant is: 3.1:1.9:4.3:0.7; during the flocculation process Control the pH to 9.5.
[0041] Add 24mL of mixed flocculant to every 500mL of waste water.
[0042] 3. Solid-liquid separation, adding pore size of 15-35nm to the liquid part, using hydroxyl-modified ceramic material for adsorption, and keeping it in contact with wastewater for 10.5 minutes.
[0043] 4. Use deionized water to clean the ceramic material adsorbing thallium, and the contact time with deionized water is 6.3 minutes.
[0044] In the wastewater after adsorption, the content of thallium is 0.00025mg / L.
Embodiment 3
[0046] 1. Ozone oxidation is introduced into the thallium-containing wastewater with a thallium content of 50.66mg / L, and the oxidation-reduction potential is controlled to be 435mV during oxidation.
[0047] 2. Add mixed flocculant, in the mixed flocculant, the mass ratio of sodium hydroxide, sodium sulfide, polyferric sulfate, and sodium polystyrene sulfonate is: 3.3:1.7:4.2:0.8; control the pH to 10 during the flocculation process.
[0048] Sodium hydroxide, sodium sulfide, polyferric sulfate, and sodium polystyrene sulfonate are mixed and slowly dissolved in water at 55°C before use.
[0049] Add 30mL of mixed flocculant to every 500mL of waste water.
[0050] 3. Solid-liquid separation, adding a pore size of 12-20nm to the liquid part, using a siloxane-based modified ceramic material for adsorption, and keeping it in contact with the wastewater for 14 minutes.
[0051] 4. Use deionized water to clean the ceramic material adsorbing thallium, and the contact time with deio...
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