Treatment method for dephosphorizing and denitrifying sewage
A treatment method and technology for sewage, applied in water/sewage treatment, biological water/sewage treatment, neutralized water/sewage treatment, etc., can solve the problems of difficult separation of solid and liquid, high cost, low treatment cost, etc., and achieve adsorption effect The effect of improving and reducing processing costs and reducing dosage
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Embodiment 1
[0036] A treatment method for dephosphorization and denitrification of sewage, characterized in that it comprises the following steps:
[0037] (1) After the industrial wastewater passes through the grid, it enters the grit chamber, and the sewage separated from sand and water enters the primary sedimentation tank, and passes through the primary sedimentation tank. Facilitate the buoyancy of oil in wastewater , to reduce the content of suspended solids;
[0038] (2) Preparation of physical adsorbent
[0039] Mix according to the mass ratio of forsterite powder, shell powder, perlite powder, and pore-forming agent at a mass ratio of 4:1:2:3, stir evenly, place in a granulator, and add 22-25% (weight) of the mixture of water, granulated to obtain particles with a particle size of 3-5mm spherical Green body; drying at 100°C for 20 hours, and calcining at 1100°C for 1 hour to obtain a physical adsorbent.
[0040] (3) The wastewater treated by the primary sedimentation tank ent...
Embodiment 2
[0057] A treatment method for dephosphorization and denitrification of sewage, characterized in that it comprises the following steps:
[0058] (1) After the industrial wastewater passes through the grid, it enters the grit chamber, and the sewage separated from sand and water enters the primary sedimentation tank, and passes through the primary sedimentation tank. Facilitate the buoyancy of oil in wastewater , to reduce the content of suspended solids;
[0059] (2) Preparation of physical adsorbent
[0060] Mix according to the mass ratio of forsterite powder, shell powder, perlite powder, and pore-forming agent at a mass ratio of 4:1:2:3, stir evenly, place in a granulator, and add 22-25% (weight) of the mixture of water, granulated to obtain particles with a particle size of 3-5mm spherical Green body; drying at 100°C for 20 hours, and calcining at 1100°C for 1 hour to obtain a physical adsorbent.
[0061] (3) The wastewater treated by the primary sedimentation tank ent...
Embodiment 3
[0076] Embodiment 3 Treatment example of waste water effect
[0077] The factory sewage is entered into the sewage treatment system according to the method of embodiment 1-2 respectively, and the bottom material of the kettle is sampled and measured for COD, phosphorus, and ammonia nitrogen data;
[0078] Compared with Example 1, control group 1 does not add physical adsorbent; compared with Example 1, control group 2 does not add composite microbial preparation. Sampling and determination of COD, ammonia nitrogen, SS, and clarity test data are shown in Table 1:
[0079] Table 1
[0080] COD removal rate Ammonia nitrogen removal rate Phosphorus removal rate Phosphorus content in effluent Clarity control group 1 43.2% 47.8% 50.3% >0.5mg / L 10cm control group 2 47.7% 61.5% 63.8% >0.5mg / L 9cm Example 1 group 98.9% 99.1% 99.4% 26cm Example 2 group 99.1% 99.3% 99.5% 26cm
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