Denitrification treatment method for organic wastewater
A technology of organic wastewater and treatment methods, applied in biological water/sewage treatment, water/sludge/sewage treatment, chemical instruments and methods, etc., can solve problems such as low total nitrogen removal efficiency, and reduce equipment footprint. , the effect of reducing operating costs
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Embodiment 1
[0083] Integrated denitrification reactor such as figure 2 As shown, it includes an outlet weir 1, a ceramsite layer 2, a cobblestone layer 3, a water distributor 4, an intermittent air inlet pipeline 5, an intermittent water inlet pipeline 6, and a reaction chamber 7.
[0084] The reaction chamber 7 is made of plexiglass, cylindrical in appearance, with a height of 1.25m and a diameter of 0.1m. There is 5L ceramsite filter material inside. The ceramsite diameter is 3-5mm and the density is 1.75g / cm 3 , with a specific surface area of about 4m 2 / g.
[0085] (1) Biofilm treatment stage:
[0086] Soak the ceramsite in the reaction chamber with a starch aqueous solution with a COD value of 300mg / L, and continuously feed air into the reaction chamber, and the intake rate of the air is 30L / min;
[0087] After 24 hours, the COD value of the aqueous sugar solution soaked in ceramsite was determined to be 250mg / L;
[0088] Remove the aqueous carbohydrate solution in the reacti...
Embodiment 2
[0105] (1) biofilm processing stage, same as embodiment 1;
[0106] (2) Denitrification stage:
[0107] The organic waste water produced in the production process of the thin film transistor liquid crystal display with a carbon-to-nitrogen ratio of 4:1 is passed into the reaction chamber after the biofilm treatment, and after 0.5 hours,
[0108] After stopping the introduction of the organic waste water to be treated, aerate the reaction chamber;
[0109] After aeration for 0.5 hours, stop the aeration and continue to feed the organic wastewater;
[0110] The process of feeding organic wastewater and aeration is carried out alternately; the process of feeding organic wastewater and aeration is performed once, and the air-water ratio is 4:1.
[0111] Maintain the hydraulic retention time of the organic wastewater to be treated at 8 hours, and run for 4 to 7 days.
[0112] The organic waste water produced in the production process of the thin-film transistor liquid crystal di...
Embodiment 3
[0129] (1) biofilm processing stage, same as embodiment 1;
[0130] (2) Denitrification stage:
[0131] The organic waste water produced in the production process of the thin-film transistor liquid crystal display with a carbon-to-nitrogen ratio of 4:1 is passed into the reaction chamber after the biofilm treatment, and after 1 hour,
[0132] After stopping the introduction of the organic waste water to be treated, aerate the reaction chamber;
[0133] After 1 hour of aeration, stop the aeration and continue to introduce organic wastewater;
[0134] The process of feeding organic wastewater and aeration is carried out alternately; the process of feeding organic wastewater and aeration is performed once, and the air-water ratio is 4:1.
[0135] The hydraulic retention time (HRT) of the organic wastewater to be treated is maintained at 8 hours, and the operation days are 5 days.
[0136] The organic waste water produced in the production process of the thin-film transistor li...
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