Technological method for controlling disinfection by-product and pathogenic microorganism risk of drinking water
A technology of pathogenic microorganisms and disinfection by-products, applied in chemical instruments and methods, adsorption water/sewage treatment, oxidized water/sewage treatment, etc., can solve the problem that the safety of microorganisms in the effluent cannot be guaranteed, and the removal effect of virus-like microorganisms is not good Ideal, the increase of effluent chemical health risks and other problems, to achieve the effect of overcoming disinfection by-products, improving removal performance, and good flocculation effect
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Embodiment 1
[0039] Experimental research is carried out on the process method of the present invention, the slightly polluted raw water enters the biological pretreatment tank, and the influent flow rate is controlled by a constant flow pump to 0.4 m 3 / d, the aeration air-water ratio in the tank is 1:1; the effluent enters the pre-ozone contact tank, the pre-ozone dosage is 0.5 mg / L, and the contact time is 10 min; the effluent enters the folding plate flocculation tank before adding polysulfide aluminum chloride , dosage 8.9 mg / L (as Al 2 o 3 After 15 minutes of effective flocculation, the effluent enters the inclined tube sedimentation tank, and the effective sedimentation time is 106 minutes; then enters the sand filter and enters the main ozone contact tank after filtration, the main ozone dosage is 2.5 mg / L, and the contact time is 20 minutes ; Then it enters the disinfection pool after being filtered by the activated carbon filter. The amount of chlorine added is 1.5~2.5 mg / L acco...
Embodiment 2
[0043] Experimental research is carried out on the process method of the present invention, the slightly polluted raw water enters the biological pretreatment tank, and the influent flow rate is controlled by a constant flow pump to 0.6 m 3 / d, the aeration air-water ratio in the tank is 1:1; the effluent enters the pre-ozone contact tank, the pre-ozone dosage is 0.5 mg / L, and the contact time is 10 min; the effluent enters the folding plate flocculation tank before adding polysulfide aluminum chloride , dosage 8.9 mg / L (as Al 2 o 3 After 15 minutes of effective flocculation, the effluent enters the inclined tube sedimentation tank, and the effective sedimentation time is 106 minutes; then enters the sand filter and enters the main ozone contact tank after filtration, the main ozone dosage is 2.5 mg / L, and the contact time is 20 minutes ; Then it enters the disinfection pool after being filtered by the activated carbon filter. The amount of chlorine added is 1.5~2.5 mg / L acco...
Embodiment 3
[0047] Experimental research is carried out on the process method of the present invention, the slightly polluted raw water enters the biological pretreatment tank, and the influent flow rate is controlled by a constant flow pump to 0.8 m 3 / d, the aeration air-water ratio in the tank is 1:1; the effluent enters the pre-ozone contact tank, the pre-ozone dosage is 0.5 mg / L, and the contact time is 10 min; the effluent enters the folding plate flocculation tank before adding polysulfide aluminum chloride , dosage 8.9 mg / L (as Al 2 o 3 After 15 minutes of effective flocculation, the effluent enters the inclined tube sedimentation tank, and the effective sedimentation time is 106 minutes; then enters the sand filter and enters the main ozone contact tank after filtration, the main ozone dosage is 2.5 mg / L, and the contact time is 20 minutes ; Then it enters the disinfection pool after being filtered by the activated carbon filter. The amount of chlorine added is 1.5~2.5 mg / L acco...
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