Polluted underground water deep purification combined denitrification system and process method
A deep purification and groundwater technology, applied in chemical instruments and methods, aerobic process treatment, water/sewage multi-stage treatment, etc.
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Embodiment 1
[0026] Example 1 Contaminated groundwater deep purification combined denitrification system
[0027] Such as figure 1 with figure 2 As shown, in a preferred embodiment of the present invention, the combined system for advanced purification of polluted groundwater mainly includes aerated biological fluidization tank 1 , primary subsurface flow wetland 2 and secondary subsurface flow wetland 3 connected in sequence.
[0028] The aerated biological fluidization tank 1 is a brick-concrete structure with a specification of 12m×1.0m×1.5m (length×width×depth). A microporous aeration system is installed at the bottom of the aerated biological fluidization tank. The filling specific gravity in the pool is 0.8g / cm 3 ~0.95g / cm 3 porous polymer fillers as microbial carriers. This system can use the microbial carrier materials commonly used in aerated biological fluidized tanks, as long as it is a polymer material with a spatial network structure, and has active groups such as amino,...
Embodiment 2
[0031] Example 2 Contaminated groundwater purification test
[0032] The polluted water source is the groundwater near a waste landfill in Beijing area. The ammonia nitrogen concentration in the raw water is 21.5mg / L~30.5mg / L. The system described in Example 1 is used to treat the sewage, and the polluted groundwater is lifted by the lifting pump and sent to the aeration plant. Materialization tank, the hydraulic retention time is 2.4h, the volume load is 0.5kgTN / (m 3 d) The gas-water ratio is 5:1, and the ammonia nitrogen concentration is reduced to 4.2mg / L-5.5mg / L after treatment.
[0033] Afterwards, the sewage enters the first-level subsurface flow wetland from the outlet of the aerated biological fluidization tank, the hydraulic retention time is 25h, and the surface load is 0.45m 3 / (m 3 d) After treatment, the concentration of ammonia nitrogen is reduced to 0.5mg / L-1.2mg / L.
[0034] The sewage treated by the primary subsurface wetland enters the secondary subsurface ...
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