Synchronous anaerobic denitrification and desulfurization process
A denitrification and process technology, applied in the field of synchronous anaerobic denitrification and desulfurization process, can solve problems such as consumption
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Embodiment 1
[0013] In the synchronous anaerobic denitrification and desulfurization reactor, the anaerobic digested sludge from the urban sewage treatment plant was used as the inoculum, and the simulated wastewater with a ratio of nitrite to sulfide (mol / mol) of about 2:3, Start the synchronous anaerobic denitrification and sulfur removal reactor. The main process conditions controlled are: hydraulic retention time is 2.0d, nitrite and sulfide (substrate) concentrations are 21mg N / L and 32mg S / L respectively, reaction temperature is 30°C, and pH is about 7. The process can remove sulfide and nitrite at the same time, the concentration of sulfide in the effluent is less than 1mgS / L, and the removal rates of sulfide and nitrite are 98.8% and 94.7% respectively.
Embodiment 2
[0015] Using the anaerobic digested sludge from the urban sewage treatment plant as the inoculum, the denitrification and desulfurization process was run with simulated wastewater with a ratio of nitrite to sulfide (mol / mol) of about 12:3. The main process conditions controlled: the hydraulic retention time is 1.0d, the concentration of nitrite and sulfide (matrix) is 3325mgN / L and 1900mgS / L, the reaction temperature is 35℃, and the pH value is about 7. The volumetric removal loads of sulfide and nitrite are up to 1.918kgS / (m 3 · d) and 2.03kg N / (m 3 d).
Embodiment 3
[0017] Using anaerobic digested sludge from urban sewage treatment plants as inoculum, sulfide and nitrite were removed simultaneously. The main process conditions controlled are: hydraulic retention time is 2.0d, nitrite and sulfide (substrate) concentrations are 2270mg N / L and 1920mg S / L respectively, reaction temperature is 30°C, and pH is about 9. The process can remove sulfide and nitrite at the same time, and the volumetric removal loads of sulfide and nitrite respectively reach 0.73kg S / (m 3 d) and 0.96kg N / (m 3 d).
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