Deep purification treatment process based on landfill leachate membrane
A landfill leachate and deep purification technology, which is applied in the direction of contaminated groundwater/leachate treatment, anaerobic digestion treatment, special compound water treatment, etc., can solve the problems of ecological environment and human health risks, and is beneficial to removal, cost reduction effect
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Embodiment 1
[0024] Embodiment 1: (1) Landfill leachate influent COD is 250mg / L, and ammonia nitrogen is 30mg / L, plant ash adjusts pH to be 7, and landfill leachate is input in activated sludge, carries out microbial degradation landfill leachate under aerobic conditions The organic matter in the reaction for 2 hours, the energy generated is used to synthesize new activated sludge cells, and at the same time obtain the primary treatment liquid;
[0025] (2) plant ash to adjust the pH of the primary treatment solution to 7, heat the leachate to 30° C., transport it into the aerobic MBR membrane tank, and carry out oxidation reaction with ammonia. The reaction time is 0.5 hours to obtain the secondary treatment solution containing nitrate;
[0026] (3) The secondary treatment solution is injected into the anoxic reaction tank, carbon source is added, and reacted for 0.5 hours. The nitrate is denitrified to generate ammonia gas, and the tertiary treatment solution is obtained. At the same time...
Embodiment 2
[0030] Embodiment 2: (1) Landfill leachate influent COD is 300mg / L, and ammonia nitrogen is 50mg / L, plant ash adjusts pH to be 7.5, and landfill leachate is input in activated sludge, carries out microbial degradation landfill leachate under aerobic conditions The organic matter in the reaction for 2 hours, the energy generated is used to synthesize new activated sludge cells, and at the same time obtain the primary treatment liquid;
[0031] (2) plant ash to adjust the pH of the primary treatment solution to 7.5, heat the leachate to 35° C., transport it into the aerobic MBR membrane tank, and carry out the oxidation reaction of ammonia. The reaction time is 0.5 hours to obtain the secondary treatment solution containing nitrate;
[0032] (3) The secondary treatment solution is injected into the anoxic reaction tank, carbon source is added, and reacted for 1 hour. The nitrate denitrification produces ammonia gas, and the tertiary treatment solution is obtained. At the same tim...
Embodiment 3
[0036] Embodiment 3: (1) landfill leachate influent COD is 320mg / L, and ammonia nitrogen is 35mg / L, plant ash adjusts pH to be 8, and landfill leachate is input in activated sludge, carries out microbial degradation landfill leachate under aerobic conditions The organic matter in the reaction for 2.5 hours, the energy generated is used to synthesize new activated sludge cells, and at the same time obtain the primary treatment liquid;
[0037] (2) plant ash to adjust the pH of the primary treatment solution to be 8, heat the leachate to 40° C., transport it into the aerobic MBR membrane tank, and carry out oxidation reaction with ammonia. The reaction time is 1.2 hours to obtain the secondary treatment solution containing nitrate;
[0038] (3) The secondary treatment solution is injected into the anoxic reaction tank, carbon source is added, and reacted for 1.5 hours. The nitrate is denitrified to generate ammonia gas, and the tertiary treatment solution is obtained. At the same...
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