A microbial treatment method for uranium-contaminated water that can effectively resist re-oxidation of u(iv)
A technology for microbial treatment and uranium pollution, which is applied in the field of uranium-contaminated water treatment, low-level uranium-containing wastewater and uranium-contaminated groundwater. Satisfies the effect of long-term stable operation, fast processing speed, and reduced reaction conditions
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Embodiment 1
[0046] The simulated uranium-containing wastewater contains various major and trace elements. After passing it through a 0.45 μm (pore size) filter membrane, UO is added to the filtrate 2 SO 4 To U(VI) =10 mg / L, adjust pH=7, and add NaHCO 3 to 1 g / L, the initial dissolved oxygen = 8.99 mg / L, and the simulated uranium-containing wastewater in an oxidizing environment was obtained.
[0047] Add anaerobic granular sludge (starch wastewater cultivation, particle size 1-2 mm) to 3 g VSS / L, and glycerol phosphate to 30 mmol / L to the simulated uranium-containing wastewater in the aforementioned oxidative environment to obtain a reaction mixture liquid. Place the obtained reaction mixture in an anaerobic reaction device (the volume ratio of the reaction mixture in the anaerobic reaction device is 50-60%), seal it, do not need to fill with nitrogen, and the reaction temperature is 25 o C, the stirring speed was 300 rpm, and the reaction was carried out for 14 days. It has been dete...
Embodiment 2
[0050] The simulated uranium-containing wastewater contains various major and trace elements. After the solution passes through a 0.45 μm filter membrane, UO is added to the filtrate 2 SO 4 To U(VI) =10 mg / L, adjust pH=7, add NaHCO 3 to 1 g / L, initial dissolved oxygen = 9.03 mg / L, and uranium-containing wastewater to be treated is obtained.
[0051] Add anaerobic granular sludge (starch wastewater culture, particle size 1-2 mm) to 3 gVSS / L, and add glycerophosphate to 50 mM to the aforementioned wastewater containing uranium to obtain a reaction mixture. The resulting reaction mixture is placed in an anaerobic reaction device, sealed, without nitrogen, and the reaction temperature is 25 o C, the stirring speed was 300 rpm, and the reaction was carried out for 14 days.
[0052] It has been determined that the removal rate of U(VI) in water in this embodiment is 95.3%.
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