Anaerobic ammonia oxidation-based low-carbon nitrogen ratio urban sewage denitrification system and treatment process
A technology of anaerobic ammonium oxidation and urban sewage, applied in the field of sewage biological treatment, can solve the problems of high energy consumption and material consumption in operation, large surplus sludge output, and consumption of organic carbon sources, etc. The effect of low throughput and short start-up time
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Embodiment 1
[0033] Embodiment one: a kind of low carbon nitrogen ratio urban sewage denitrification treatment process based on anaerobic ammonium oxidation, comprises the following steps:
[0034] a. After pretreatment (thick and fine grid, grit chamber), the urban sewage enters the aeration tank 1 through the urban sewage inlet pipe 7, and in the aeration tank 1, the return sludge from the sedimentation tank 2 is used to treat the urban sewage Most of the organic matter undergoes biosorption, the treatment time is 20 minutes, and the sludge reflux ratio is 20%; the mud-water mixture discharged from the aeration tank 1 enters the sedimentation tank 2 for mud-water separation, and the treatment time is 1.5 hours; the MLSS of the aeration tank 1 ( Mixed liquor sludge concentration) is 1.5g / L, DO (dissolved oxygen) concentration is 0.2mg / L;
[0035] b. The urban sewage discharged from the sedimentation tank 2 is mixed with the reflux liquid of the nitrosation tank 4 and enters the anammox ta...
Embodiment 2
[0039] Embodiment two: a kind of low carbon nitrogen ratio urban sewage denitrification treatment process based on anaerobic ammonium oxidation, comprises the following steps:
[0040] a. After pretreatment (thick and fine grid, grit chamber), the urban sewage enters the aeration tank 1 through the urban sewage inlet pipe 7, and in the aeration tank 1, the return sludge from the sedimentation tank 2 is used to treat the urban sewage Most of the organic matter undergoes biosorption, the treatment time is 40 minutes, and the sludge reflux ratio is 50%; the mud-water mixture discharged from the aeration tank 1 enters the sedimentation tank 2 for mud-water separation, and the treatment time is 2 hours; the MLSS of the aeration tank 1 ( Mixed liquor sludge concentration) is 2.0g / L, DO (dissolved oxygen) concentration is 0.4mg / L;
[0041] b. The urban sewage discharged from the sedimentation tank 2 is mixed with the reflux liquid of the nitrosation tank 4 and enters the anammox tank...
Embodiment 3
[0045] Embodiment three: a kind of low carbon nitrogen ratio urban sewage denitrification treatment process based on anaerobic ammonium oxidation, comprises the following steps:
[0046] a. After pretreatment (thick and fine grid, grit chamber), the urban sewage enters the aeration tank 1 through the urban sewage inlet pipe 7, and in the aeration tank 1, the return sludge from the sedimentation tank 2 is used to treat the urban sewage Most of the organic matter undergoes biosorption, the treatment time is 30min, and the sludge reflux ratio is 30%; the mud-water mixture discharged from the aeration tank 1 enters the sedimentation tank 2 for mud-water separation, and the treatment time is 2 hours; the MLSS of the aeration tank 1 ( Mixed liquor sludge concentration) is 2g / L, DO (dissolved oxygen) concentration is 0.3mg / L;
[0047] b. The urban sewage discharged from the sedimentation tank 2 is mixed with the reflux liquid of the nitrosation tank 4 and enters the anammox tank 3 to...
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