Drinking water purification device for simultaneously removing organic matter and ammonia nitrogen and method
A water purification and organic matter technology, applied in chemical instruments and methods, water/sewage treatment, water/sewage multi-stage treatment, etc., can solve the problems of incomplete degradation, poor adsorption effect, etc., achieve reasonable duration and improve water output effect , good removal effect
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Embodiment 1
[0030] Such as figure 1 As shown, a drinking water purification device that removes organic matter and ammonia nitrogen at the same time includes a mixing tank, a flocculation tank, a sedimentation tank, a concentration tank and a degradation tank that are connected end to end in sequence. The coagulant dosing pipeline, the concentration tank is provided with a mud discharge pipeline, the degradation tank is provided with an aeration pipeline, the degradation tank and the mixing tank are connected by a carbon mud return pipeline, and the flocculation tank is provided with a mixer. The mixing tank includes a static mixer or a mechanically agitated mixing tank.
[0031] A drinking water purification method for simultaneously removing organic matter and ammonia nitrogen, comprising the following steps:
[0032] a) The raw water enters the mixing tank and is quickly mixed with carbon mud, coagulant and newly added powdered activated carbon;
[0033] b) The mixed water enters the...
Embodiment 2
[0048] The difference between this embodiment and embodiment 1 is only:
[0049] a) The dosage of coagulant in the step is 40mg / L.
[0050] The hydraulic retention time in the flocculation tank is 35min.
[0051] The hydraulic retention time in the concentration tank is 10h.
[0052] The aeration time of the degradation pond is 7 hours, and the aeration rate is 1:80.
[0053] In this embodiment, using this purification method, the carbon mud is degraded by concentration and aeration, and then flows back into the mixing tank. The turbidity of raw water before treatment is about 6.21NTU, UV 254 about 0.054 cm -1 、COD Mn It is about 3.04mg / L, ammonia nitrogen is about 1.12mg / L, and the initial carbon input amount is 2000mg / L. After three weeks of stable operation, the sludge concentration in the degradation tank is about 3400mg / L; the turbidity of the effluent is about 1.23NTU, UV 254 about 0.034 cm -1 , COD Mn About 1.67mg / L, ammonia nitrogen is about 0.61mg / L.
[0054...
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