Anaerobic molysite biological nitrogen removal process
A biological denitrification and iron salt technology, applied in the field of anaerobic iron salt biological denitrification process, to achieve sustainable development and full utilization
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Embodiment 1
[0012] In the ferric salt biological denitrification reactor, the enriched culture of denitrifying bacteria was used as the biocatalyst, and the molar ratio of nitrate to ferrous salt concentration was 1:2 in the simulated wastewater to run the ferric salt biological denitrification reactor. The main process conditions controlled are: the concentration of nitrate and ferrous salt is 100 mg N / L and 800 mg Fe / L respectively, the concentration of dissolved oxygen is 0.4 mg / L, the reaction temperature is 32 ℃, and the initial pH value is 7.0 , and the hydraulic retention time is 0.5 d. The process can remove nitrate and ferrous salt at the same time, and the removal rates of nitrate and ferrous salt in the effluent reached 95.97 % and 96.22 %, respectively.
Embodiment 2
[0014] In the ferric salt biological denitrification reactor, the ferric salt biological denitrification reactor is operated with the enriched culture of denitrifying bacteria as the biocatalyst and the simulated wastewater with the molar ratio of nitrate and ferrous salt concentration being 1:5. The main process conditions controlled are: the concentration of nitrate and ferrous salt is 100 mg N / L and 2000 mg Fe / L respectively, the concentration of dissolved oxygen is 0.3 mg / L, the reaction temperature is 30 ℃, and the initial pH value is 7.3 , and the hydraulic retention time is 0.5 d. The process can remove nitrate and ferrous salt at the same time, and the volume removal load of nitrate and ferrous salt in the effluent reaches 0.18 kg N / (m 3 d) and 2.60 kg Fe / (m 3 d).
Embodiment 3
[0016] In the ferric salt biological denitrification reactor, the enriched culture of denitrifying bacteria was used as the biocatalyst, and the molar ratio of nitrate to ferrous salt concentration was 1:2 in the simulated wastewater to run the ferric salt biological denitrification reactor. The main process conditions controlled are: the concentration of nitrate and ferrous salt is 100 mg N / L and 800 mg Fe / L respectively, the concentration of dissolved oxygen is 0.4 mg / L, the reaction temperature is 28 ℃, and the initial pH value is 8.0 , and the hydraulic retention time is 0.5 d. The process can remove nitrate and ferrous salt at the same time, and the removal rate of nitrate and ferrous salt in the effluent reaches 0.17 kg N / (m 3 d) and 1.58 kg Fe / (m 3 d).
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