Sewage treatment system capable of intensifying biological denitrification and chemical dephosphorization and technical method
A sewage treatment device and denitrification chemical technology, applied in the direction of biological water/sewage treatment, chemical instruments and methods, water/sewage multi-stage treatment, etc., to achieve the effects of easy dehydration, easy production implementation, and simple control
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Embodiment 1
[0030] The influent water quality of a city sewage plant is as follows: COD C 268mg / L, NH + 4 -N is 30.1mg / L, NO 3 - -N was 1.1 mg / L, TN was 35.5 mg / L, and TP was 4.52 mg / L. Adopting the technological method of the present invention to carry out biological denitrification and chemical phosphorus removal, the specific implementation is as follows:
[0031] (1) The main parameters of the biological treatment system of the present invention are as follows: anaerobic, anoxic and aerobic residence times are respectively 1.5h, 2.0h and 4.0h; the dissolved oxygen concentration in the aerobic tank is 2mg / L; the sludge in the aerobic tank The concentration is 2800mg / L; the reflux ratio of sludge is 0.8, and the reflux ratio of nitrification solution is 2.0; the induced crystallization liquid is refluxed to the anoxic tank; the sludge age is 14 days, and intermittent sludge is discharged twice a day. Mud time is 0.5h.
[0032] (2) control parameter of surplus sludge oxidative deco...
Embodiment 2
[0040] The influent water quality of a city sewage plant in the rainy season is as follows: COD C 158mg / L, NH + 4 -N is 20.5mg / L, NO 3 - -N was 0.9 mg / L, TN was 25.9 mg / L, and TP was 4.8 mg / L. Adopt technological method of the present invention to carry out enhanced biological phosphorus removal, the specific implementation mode is:
[0041] (1) The main parameters of the biological treatment system of the present invention are as follows: anaerobic, anoxic and aerobic residence times are respectively 1.5h, 2.0h and 4.0h; the dissolved oxygen concentration in the aerobic tank is 1.5mg / L; The sludge concentration is 2100mg / L; the reflux ratio of sludge is 0.8, and the reflux ratio of nitrification solution is 1.5; the induced crystallization liquid is refluxed to the anaerobic tank; The mud discharge time is 0.5h.
[0042] (2) control parameter of surplus sludge oxidative decomposition system of the present invention is as follows: enter mud (dosing) and reaction time alt...
Embodiment 3
[0050] The influent water of a city sewage plant contains some industrial wastewater, and its influent water quality is as follows: COD C 358.8mg / L, NH + 4 -N is 45.0mg / L, NO 3 - -N is 1.5 mg / L, TN is 62.0 mg / L, and TP is 5.5 mg / L. Adopting the technological method of the present invention to strengthen biological denitrification and chemical phosphorus removal, the specific implementation method is:
[0051] (1) The main parameters of the biological treatment system of the present invention are as follows: anaerobic, anoxic and aerobic residence times are respectively 2.0h, 2.5h and 6.0h; the dissolved oxygen concentration in the aerobic pond is 2.5mg / L; The sludge concentration is 3500mg / L; the sludge reflux ratio is 0.8, and the nitrifying liquid reflux ratio is 2.0; the induced crystallization liquid is refluxed to the anoxic tank; the sludge age is 15 days, and intermittent sludge discharge is adopted, and the sludge is discharged twice a day, each time The mud disch...
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