Landfill leachate stock solution pretreatment method and system for disc tube type reverse osmosis treatment
A disc-tube reverse osmosis and landfill leachate technology, which is applied in filtration treatment, water/sewage treatment, water treatment parameter control, etc., can solve the problems affecting the disc-tube reverse osmosis treatment of landfill leachate raw water, etc. effect of use
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Embodiment 1
[0029] Adopt the present invention to treat the leachate raw water of a landfill site, COD=6000~8000mg / L, NH 3 -N=1500~2000mg / L, SS=500~1000mg / L; After the waste water passes through the sodium hypochlorite treatment unit, adjust the dosage of sodium hypochlorite to control the [·Cl] in the raw water of landfill leachate ≥ 0.3mg / L; The effluent passes through the PAC coagulation treatment unit (the dosage of PAC is 50-200g / m 3 , reaction time ≈20min), PAM flocculation treatment unit (1‰~5‰PAM dosage is controlled at 0.5~1L / m 3 , reaction time ≈20min), the SS in the effluent drops to ≤50mg / L, and the raw liquid of the landfill leachate becomes clearer; after passing through a sand filter with a particle size of quartz sand generally 0.5-1.0mm (the sand filter system is backwashed every 10d One time), the raw water of landfill leachate in the effluent SS<30mg / L enters the disc-type reverse osmosis system; the treated landfill leachate raw water enters the disc-type reverse osmo...
Embodiment 2
[0031] Adopt the method of the present invention to treat the leachate raw water of a landfill site, COD=4000~6000mg / L, NH 3 -N=1000~1500mg / L, SS=500~700mg / L, containing black colloidal substances; after the waste water is oxidized by sodium hypochlorite treatment unit, the black colloidal substances are oxidized and removed, and the raw water of landfill leachate is controlled [·Cl] ≈0.5mg / L; the effluent passes through the PAC coagulation treatment unit (the dosage of PAC is 50~100g / m 3 , reaction time ≈15min), PAM flocculation treatment unit (1‰~5‰PAM dosage is controlled at 0.5~0.8L / m 3 , reaction time ≈15min), the SS in the effluent is reduced to ≤40mg / L, after passing through the sand filter, the SS of the landfill leachate raw water is less than 25mg / L, and the water quality is clear; the landfill leachate raw water enters the disc tube after pretreatment Reverse osmosis system, the system is stable and normal operation, the water production rate of the system is incre...
Embodiment 3
[0033] Adopt the method of the present invention to process the leachate stoste of a landfill site, COD=7500~10000mg / L, NH 3 -N=1500~3000mg / L, SS=700~1500mg / L; After the raw water of landfill leachate is oxidized by sodium hypochlorite treatment unit, the odor in the raw water will be removed to a certain extent, and the [·Cl]≈0.5 in the landfill leachate stock solution will be maintained. mg / L, NH in raw water 3 -N drops to 1300~2500mg / L; the effluent of the sodium hypochlorite treatment unit passes through the PAC coagulation treatment unit (the dosage of PAC is 100~200g / m 3 , reaction time ≈30min), PAM flocculation treatment unit (1‰~5‰PAM dosage is controlled at 1.0~2.0L / m 3 , reaction time ≈30min), the SS in the effluent is reduced to ≤60mg / L, after passing through the sand filter, the SS of the landfill leachate raw water is less than 30mg / L; the landfill leachate raw water is pretreated and enters the disc tube reverse osmosis system , the system runs stably and norma...
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