Urban sewage treatment of anaerobic biological-low voltage electric field oxidizing coupling system
An urban sewage and oxidation coupling technology, applied in anaerobic digestion treatment, magnetic field/electric field water/sewage treatment, electrochemical water/sewage treatment, etc., can solve the problem of long hydraulic retention time, insufficient flexibility, and high aeration power consumption To achieve the effect of increasing the rising flow rate and stirring, increasing the mass transfer rate, and improving the removal efficiency
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Embodiment 1
[0022] The urban sewage from a certain place enters the EGSB reactor through the water distributor after being pretreated by grille and grit, and contacts with the highly active anaerobic sludge in the reactor from bottom to top, and the anaerobic sludge is produced by fermentative bacteria , Hydrogen-producing acetogenic bacteria, methanogenic bacteria, sulfate-reducing bacteria and other microorganisms, they degrade organic pollutants in urban sewage into CH 4 , CO 2 、H 2 O and other final products. Under the action of sulfate-reducing bacteria, SO in urban sewage 4 2- for H 2 S, the hydraulic retention time of the anaerobic reactor is 3 hours. At the same time, the supernatant from the upper three-phase separator was refluxed to the bottom of the reactor at a ratio of 1:1 to increase the rising flow rate and stirring. During the whole year of operation, about 80% of the time the ammonia nitrogen concentration in the effluent from the EGSB reactor is less than 25mg / L (...
Embodiment 2
[0025] The urban sewage from a certain place enters the EGSB reactor through the water distributor after being pretreated by grille and sand settling, and contacts with the highly active anaerobic sludge in the reactor from bottom to top, and the anaerobic sludge is produced by fermentative bacteria , Hydrogen-producing acetogenic bacteria, methanogenic bacteria, sulfate-reducing bacteria and other microorganisms, they degrade organic pollutants in urban sewage into CH 4 , CO 2 、H 2 O and other final products. Under the action of sulfate-reducing bacteria, SO in urban sewage 4 2- for H 2S, the hydraulic retention time of the anaerobic reactor is 4 hours. At the same time, the supernatant from the upper three-phase separator was refluxed to the bottom of the reactor at a ratio of 1:2 to increase the rising flow rate and stirring. During the whole year of operation, about 85% of the time the ammonia nitrogen concentration in the effluent from the EGSB reactor is less than ...
Embodiment 3
[0028] The urban sewage from a certain place enters the EGSB reactor through the water distributor after being pretreated by grille and grit, and contacts with the highly active anaerobic sludge in the reactor from bottom to top, and the anaerobic sludge is produced by fermentative bacteria , Hydrogen-producing acetogenic bacteria, methanogenic bacteria, sulfate-reducing bacteria and other microorganisms, they degrade organic pollutants in urban sewage into CH 4 , CO 2 、H 2 O and other final products. Under the action of sulfate-reducing bacteria, SO in urban sewage 4 2- for H 2 S, the hydraulic retention time of the anaerobic reactor is 6 hours. At the same time, the supernatant from the upper three-phase separator was refluxed to the bottom of the reactor at a ratio of 1:5 to increase the rising flow rate and stirring. During the whole operation of one year and three months, about 90% of the time the concentration of ammonia nitrogen in the effluent from the EGSB react...
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