Integrated powder-loading enhanced biochemical water treatment device
A water treatment device and attached technology, applied in biological water/sewage treatment, water/sludge/sewage treatment, aerobic and anaerobic process treatment, etc. Low efficiency and other problems, to achieve good sewage treatment effect, high volume load, and good settlement performance
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Embodiment 1
[0032] Such as Figure 1-2 As shown, it is a longitudinal sectional view of an integrated powder-loaded enhanced biochemical water treatment device provided in this embodiment. The device is cylindrical and includes a central cylindrical central aerobic zone 3 and anoxic / Precipitation zone 31, anoxic / precipitation zone 31 includes anoxic zone 1 with water inlet 11, precipitation zone 2 located on the upper part of anoxic zone 1, and the device also includes a bottom flow connecting anoxic zone 1 and aerobic zone 3 Hole 14, returning the nitrifying liquid in the aerobic zone 3 to the return system 13 in the anoxic zone 1; the aerobic zone 3 and the anoxic / precipitation zone 31 are inclined 55° to the outside of the central axis of the device through the upper partition 34 of the partition The sliding mud plate 19, the partition partition plate 18 inclined 60° to the inside of the central axis of the device is separated from the partition lower partition tube 35, and the slidin...
Embodiment 2
[0046] The difference between this embodiment and embodiment 1 is that the volume ratio of the anoxic zone 1 to the aerobic zone 3 is 1:3.5, and the surface load of the precipitation zone 2 is 1.3m 3 / m 2 h, the volume load of the device is 1.2kg BOD when denitrification / nitrification biological denitrification 5 / m 3 d. The inclination angle of the sliding mud plate 19 to the outside of the central axis of the device is 65°, and the inclination angle of the partition partition 18 to the inboard of the central axis of the device is 65°.
[0047] The plug flow velocity of the plug flow mixer 12 is 0.32m / s, and the velocity of the mixed sewage in the device passing through the bottom flow hole 14 is 0.6m / s.
Embodiment 3
[0049] The difference between this embodiment and embodiment 1 and embodiment 2 is that the volume ratio of the anoxic zone 1 to the aerobic zone 3 is 1:5, and the surface load of the precipitation zone 2 is 2.6m 3 / m 2 h, the volume load of the device is 2.4kgBOD when denitrification / nitrification biological denitrification 5 / m 3 d. The inclination angle of the sliding mud plate 19 to the outside of the central axis of the device is 60°, and the inclination angle of the partition partition 18 to the inside of the central axis of the device is 55°.
[0050] The plug flow velocity of the plug flow mixer 12 is 0.4m / s, and the velocity of the mixed sewage in the device passing through the bottom flow hole 14 is 0.8m / s.
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