Biochemical tail water deep nitrogen and phosphorus removal method based on magnetic coagulation-adsorption coupling
A deep denitrification and magnetic coagulation technology, applied in chemical instruments and methods, magnetic field/electric field water/sewage treatment, water pollutants, etc., can solve problems such as reducing TN concentration, and achieve reasonable steps and excellent deep denitrification and removal. Phosphorus, efficient removal effect
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Embodiment 1
[0050] The biochemical effluent from the secondary sedimentation tank of a sewage treatment plant has a TN of 22.6mg / L and a TP concentration of 1.04mg / L.
[0051] (A): Import the biochemical effluent from the secondary sedimentation tank into the mixing tank 1, and add PAC solution with a mass concentration of 10%, and the dosage is 3L / m 3 For the biochemical tail water, the average velocity gradient (G value) of the mixed liquid is 600 / S when stirred by the first stirrer 101, and the mixed reaction is 1.5 min;
[0052] (B): The mixed solution is introduced into the coagulation reaction tank 2, and the average velocity gradient (G value) of the mixed solution is 120 / S when being stirred by the second agitator 201, and the time control of the coagulation reaction is 6 minutes;
[0053] (C): The mixed solution of the coagulation reaction tank 2 is introduced into the adsorption reaction tank 3, and at the same time, the selectively adsorbed nitrate-type magnetic powder (either ...
Embodiment 2
[0058] The biochemical effluent from the secondary sedimentation tank of a sewage treatment plant has a TN of 28.3mg / L and a TP concentration of 1.42mg / L.
[0059] (A): Lead the biochemical effluent from the secondary sedimentation tank into the mixing tank 1, and add PAC solution with a mass concentration of 20%, and the dosage is 2L / m 3 For the biochemical tail water, the average velocity gradient (G value) of the mixed solution is 900 / S when being stirred by the first agitator 101, and the mixing reaction is 2 minutes;
[0060] (B): The mixed solution is introduced into the coagulation reaction tank 2, and the average velocity gradient (G value) of the mixed solution is 180 / S when being stirred by the second agitator 201, and the time control of the coagulation reaction is 8 min;
[0061] (C): The mixed solution of the coagulation reaction tank 2 is introduced into the adsorption reaction tank 3, and at the same time, the selectively adsorbed nitrate-type magnetic powder (e...
Embodiment 3
[0066] The biochemical effluent from the secondary sedimentation tank of a sewage treatment plant has a TN of 15.8mg / L and a TP concentration of 0.76mg / L.
[0067] (A): Lead the biochemical effluent from the secondary sedimentation tank into the mixing tank 1, and add PAC solution with a mass concentration of 15%, and the dosage is 1.5L / m 3 For the biochemical tail water, the average velocity gradient (G value) of the mixed solution is 700 / S when stirred by the first stirrer 101, and the mixed reaction is 1 min;
[0068] (B): The mixed solution is introduced into the coagulation reaction tank 2, and the average velocity gradient (G value) of the mixed solution is 150 / S when stirred by the second agitator 201, and the time of the coagulation reaction is controlled to be 10min;
[0069] (C): The mixed solution of the coagulation reaction tank 2 is introduced into the adsorption reaction tank 3, and at the same time, the selective adsorption nitrate-type magnetic powder (either e...
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