Landfill leachate treatment process
A technology for landfill leachate and treatment process, which is applied in the field of non-membrane treatment technology of landfill leachate, can solve the problems of aggravating the load of membrane modules, high replacement frequency, difficult re-cultivation, etc., so as to improve the impact resistance and improve the removal effect. , the effect of reducing secondary pollution
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Embodiment 1
[0028] Treatment of landfill leachate in a Nanjing landfill:
[0029] The processing capacity of the embodiment of the present invention is designed according to 0.5t / h, and the regulating pool is 24m 3 ;
[0030] The landfill leachate is subjected to physical and chemical pretreatment first, and the physical and chemical pretreatment adopts Fenton oxidation, and the Fenton oxidation (mass concentration is 30%) hydrogen peroxide dosage is 0.5‰ (mass percent) of the waste water quality, and n[Fe 2+ ]: n[H 2 o 2 ]=1:20, adjust the pH to be 2, and the residence time to be 4h;
[0031]Physicochemical effluent undergoes another biochemical treatment: anaerobic, anoxic, and aerobic processes are adopted in sequence; the anaerobic redox potential is -300mV, the residence time is 4d, the dissolved oxygen is 0.01mg / L; the anoxic dissolved oxygen is 0.2mg / L, The residence time is 5d; the aerobic residence time is 4d, and the dissolved oxygen is 4mg / L. In the aerobic process, polyet...
Embodiment 2
[0039] Landfill leachate from a landfill in Wuxi:
[0040] The processing capacity of the embodiment of the present invention is designed according to 0.5t / h, and the regulating pool is 24m 3 ;
[0041] The landfill leachate is first subjected to physical and chemical pretreatment, and the physical and chemical pretreatment is oxidized by sodium hypochlorite. The dosage of sodium hypochlorite [available chlorine 10% (mass percentage)] is 2‰ (mass percentage) of the waste water quality, the pH is adjusted to 6, and the residence time is 0.5h;
[0042] Physicochemical effluent undergoes a biochemical treatment: the primary biochemical process adopts anaerobic, anoxic and aerobic processes; the anaerobic dissolved oxygen is 0.19mg / L, the redox potential is -500mV, and the residence time is 5d; the anoxic dissolved oxygen is 0.4mg / L , The residence time is 4d; the aerobic dissolved oxygen is 3.0mg / L, and the residence time is 9d. In the aerobic process, polypropylene suspension...
Embodiment 3
[0050] Landfill leachate from a landfill in Changzhou:
[0051] The processing capacity of the embodiment of the present invention is designed according to 0.5t / h, and the regulating pool is 24m 3 ;
[0052] Landfill leachate is subjected to physical and chemical pretreatment first, and the dosage of ozone oxidation is 50mg / L, the pH is adjusted to 5, and the residence time is 0.1h;
[0053] Physicochemical effluent undergoes another biochemical treatment: the primary biochemical process adopts anaerobic, anoxic, and aerobic processes; the anaerobic dissolved oxygen is 0.01mg / L, the redox potential is -400mV, and the residence time is 8d; the anoxic dissolved oxygen is 0.4mg / L , The residence time is 3d; the aerobic dissolved oxygen is 3.0mg / L, and the residence time is 9d. In the aerobic process, polyethylene suspension filler is added, and the filler density is 0.95g / cm 3 , the effective specific surface area is 200m 2 / m 3 , The filler dosage is 25% ((volume percentage...
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