A kind of circulating egsb reaction device and sewage treatment method based on the device
A sewage treatment method and reaction device technology, applied in the field of circulating EGSB reaction device, can solve the problems affecting the long-term stability of denitrification performance, slow growth of anaerobic ammonium oxidizing bacteria, sludge accumulation, etc., to increase the effective working biomass , increase the effective collision probability, and improve the effect of denitrification efficiency
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0038] like figure 1 Shown is a circulating EGSB reaction device, which includes a reaction unit, a gas separation unit and a sewage water inlet unit. The reaction unit includes a reactor housing 11 and a sludge collection mechanism arranged in the reactor housing 11. The gas The separation unit includes a separator 10 arranged outside the reactor shell 11 and communicated with the sludge collection mechanism. The bottom of the separator 10 communicates with the bottom of the reactor shell 11, and an exhaust port is opened on the top, and the sewage enters The water unit communicates with the separator 10 .
[0039] Wherein, the reactor housing 11 includes a rectifying section 1101, a reaction section 1102, an expanding section 1103 and a drainage section 1104 connected in sequence from bottom to top. The bottom of the separator 10 communicates with the rectification section 1101 . A circulation pump 5 is provided between the bottom of the separator 10 and the rectifying sec...
Embodiment 2
[0047] A kind of sewage treatment method based on the circulating EGSB reaction device in embodiment 1 is: the sewage to be treated in the sewage water inlet unit enters the reactor shell 11 through the separator 10, and in the reactor shell 11 from bottom to bottom At the same time, the anammox sludge in the reactor shell 11 is denitrified; part of the denitrified sewage is discharged from the reactor shell 11, and the other part is mixed with anammox sludge , and enter the separator 10 through the sludge collection mechanism, and mix with the sewage to be treated in the separator 10; the gas in the separator 10 is discharged from the exhaust port.
[0048] Wherein, in the reactor shell 11, the volatile sludge concentration of the anammox sludge is ≥3000mg / L, the ascending flow rate of the liquid flow is 4m / h, the hydraulic retention time is 20h, and the reaction temperature is 30°C.
Embodiment 3
[0050] In this embodiment, in the reactor shell 11, the volatile sludge concentration of the anaerobic ammonium oxidation sludge is 3000mg / L, the ascending velocity of the liquid flow is 5m / h, the hydraulic retention time is 15h, and the reaction temperature is 35°C , all the other are with embodiment 2.
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 


