Denitrification filter combined packing and application thereof
A denitrification filter and combined packing technology, which is applied in the field of nitrogen-containing domestic sewage and industrial wastewater treatment, can solve the problems of no accumulation of nitrite nitrogen and high pH, so as to avoid sludge bulking and produce less sludge , cost reduction effect
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Embodiment 1
[0060] The low-carbon source in embodiment 1 adds the combined packing of high-efficiency denitrification filter, and is made up of iron-carbon filler, sulfur, porous material, wherein the mass ratio of each component of iron-carbon filler is reduced iron powder 45%, activated carbon 15% , copper powder 10%, calcium sulfate 20%, ammonium bicarbonate 5%, sodium bicarbonate 5%.
[0061] (1) Blend and mix the reduced iron powder, activated carbon, copper powder, calcium sulfate, ammonium bicarbonate and sodium bicarbonate, slowly add water with 20% of the raw material mass and mix to form a viscous mixture;
[0062] (2) Fill the mixture obtained in step (1) into a spherical mold with an inner diameter of 9mm, and dry it in a vacuum oven at 60°C for 8 hours;
[0063] (3) The product obtained after vacuum drying in step (2) was calcined at 400° C. for 2 hours under high-purity nitrogen to make iron-carbon filler.
[0064] (4) Static film-hanging stage: the combined filler is the i...
Embodiment 2
[0068] The low-carbon source in Example 2 is added with the combined filler of the high-efficiency denitrification filter. The combined filler in the reactor is iron-carbon filler, sulfur, oyster shell and volcanic rock from bottom to top, and its volume ratio is: iron-carbon filler: Sulfur: oyster shell: volcanic rock = 1:1:1:1, the combined filler accounts for 50% of the reactor volume, and the preparation method of the iron-carbon filler is the same as in Example 1.
[0069] Through the same static film-hanging stage as in Example 1, after the continuous culture stage and the stable operation stage, the average influent nitrate nitrogen concentration is 30 ± 5mg / L, C / N=1.5-2, and the influent dissolved oxygen DO= Under the conditions of 1.0-2.0mg / L and hydraulic retention time HRT=4h, the average concentration of nitrate nitrogen in the effluent is 1.8-3mg / L, the removal rate of nitrate nitrogen is 90-94%, and there is no ammonia nitrogen and nitrite nitrogen accumulation, ...
Embodiment 3
[0071] The low-carbon source in Example 3 is added with the combined filler of the high-efficiency denitrification filter. The combined filler in the reactor is iron-carbon filler, sulfur, medical stone and volcanic rock from bottom to top, and its volume ratio is: iron-carbon filler : sulfur: medical stone: volcanic rock=1:1:1:1, the combined filler accounts for 50% of the reactor volume, wherein the preparation method of the iron-carbon filler is the same as in Example 1.
[0072] Through the same static film-hanging stage as in Example 1, after the continuous culture stage and the stable operation stage, the average influent nitrate nitrogen concentration is 30 ± 5mg / L, C / N=1.5-2, and the influent dissolved oxygen DO= Under the conditions of 1.0-2.0mg / L and hydraulic retention time HRT=4h, the average concentration of nitrate nitrogen in the effluent is 2.3-3.2mg / L, the removal rate of nitrate nitrogen is 89-92%, and there is no ammonia nitrogen and nitrite The accumulation...
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