The invention discloses a same-tank carbon and
nitrogen removal process which comprises the following steps: introducing
sewage into a low-dissolved-
oxygen area through a water inlet end of a BAE reactor, and monitoring the dissolved
oxygen concentration in the low-dissolved-
oxygen area in real time through a DO sensor a and a DO sensor b, when DO in the
low dissolved oxygen area is smaller than or equal to 0.2 mg / L, an
air blower is started to supply air, and the microporous
aeration device is used for
aeration; when the concentration is 1.0 mg / L, air supply of the
air blower is stopped, and the low-dissolved-oxygen-area water
impeller a and the low-dissolved-oxygen-area water
impeller b are started; according to the BAE reactor, anaerobic,
facultative, aerobic, water outlet,
backflow and other multifunctional areas are integrated into the same tank body, the
water flow speed of the
low dissolved oxygen area is controlled to be 0.25-0.9 m / s through partition wall division, the occupied area of a traditional multi-tank series connection technology is greatly reduced, through application of an inclined tube
sedimentation tank (the liquid level load is 0.5-1.5 m / (m.h)) or an MBR membrane (the
membrane flux is 8-15 L / (m.h)), the
solid-liquid separation efficiency is remarkably improved, and the
solid-liquid separation efficiency is greatly improved. The
settling area is reduced, and capital construction investment is saved.