Coal chemical wastewater biological treatment system based on sludge catalytic ozonation and treatment method thereof
A technology of ozone catalytic oxidation and coal chemical wastewater, applied in the direction of oxidized water/sewage treatment, water/sludge/sewage treatment, anaerobic digestion treatment, etc. Low-efficiency problems, to achieve the effect of low-cost sludge digestion promotion, conducive to reduction, and thorough sludge digestion
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Embodiment 1
[0093] This embodiment provides a biological treatment system for coal chemical wastewater, which includes a first-stage pre-denitrification anoxic / aerobic biological treatment system, a sludge ozone catalytic oxidation multi-phase reaction system and a second-stage anoxic denitrification / Aerobic biological treatment system;
[0094] Among them, the first-stage sedimentation tank in the anoxic / aerobic biological treatment system with pre-denitrification and the sludge ozone catalytic oxidation reactor in the sludge ozone catalytic oxidation multiphase reaction system are connected through sludge pipelines, and the sludge The clear liquid outlet of the ozone catalytic oxidation reactor in the ozone catalytic oxidation multiphase reaction system and the sewage discharge outlet of the primary sedimentation tank in the anoxic / aerobic biological treatment system of primary pre-denitrification are simultaneously connected with the secondary The liquid inlet of the secondary anoxic...
Embodiment 2
[0101] In this embodiment, the coal chemical wastewater biological treatment system described in Example 1 is used to treat the coal chemical wastewater. The COD content in the coal chemical wastewater to be treated is 3000-8000 mg / L, and the ammonia nitrogen content is 50-300 mg / L.
[0102] The coal chemical wastewater to be treated enters the anoxic / aerobic biological treatment system of the first-level pre-denitrification for the first-level anoxic treatment, the first-level aerobic treatment and the first-level sedimentation treatment. Among them, the first-level anoxic treatment adopts biological Membrane method, the primary aerobic treatment adopts the activated sludge method, the hydraulic retention time in the primary anoxic reactor is 25-30h, the hydraulic retention time in the primary aerobic reactor is 60-70h, and the primary The total hydraulic retention time of the denitrification anoxic / aerobic biological treatment unit is 100-120h.
[0103] The concentration of ...
Embodiment 3
[0108] In this example, the coal chemical wastewater biological treatment system described in Example 1 is used to treat coal chemical wastewater. Except that the hydraulic retention time in the primary anoxic reactor is 40-45h, the hydraulic retention time in the primary aerobic reactor is The residence time is 80-90h, and the total hydraulic retention time of the anoxic / aerobic biological treatment unit of the first-stage pre-denitrification is 130-140h; the flow ratio of the sludge used for backflow and the sludge used for ozone catalytic digestion is 10:1; the ozone generator produces ozone with a concentration of 10-12%, and the dosage of ozone in the sludge ozone catalytic oxidation reactor is 0.05-0.06O 3 / MLSS(g / g), the ozone catalytic digestion time is 20-30min; the hydraulic retention time of the secondary anoxic treatment is 15-20h, and the hydraulic retention time of the secondary aerobic treatment is 10-15h, other operating steps All the same as in Example 2.
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