A2/O-MBR combined process and device for improving low-carbon source town sewage
A technology of urban sewage and combined process, which is applied in the direction of biological treatment devices, biological water/sewage treatment, water/sludge/sewage treatment, etc. Unsatisfactory effect and other problems, to achieve the effect of improving the total phosphorus removal effect, improving the removal efficiency, and simple transformation
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Embodiment 1
[0050] Improved A 2 / O-MBR processing device:
[0051] Improved A 2 The floor plan of the / O-MBR processing device is shown in figure 2 As shown, the pilot test device is made of steel plates. The internal partition of the device is made of 4mm steel plate, the outer plate is made of 6mm steel plate, and the bottom plate is made of 8mm steel plate. leakage. The length, width and height of the boundary of the reactor are 6.0, 2.5 and 2.5m respectively, the effective water depth is 2.0m, and the total volume is 37.5m 3 . The main supporting equipment of the device includes: ① 2 sets of submerged mixers with a power of 1.5kw, 1 set of anaerobic tank and 1 set of anoxic tank, which are used to keep the sludge in suspension; 2) 4 electromagnetic flowmeters, respectively located at the water inlet, Nitrifying liquid backflow, anoxic mixed liquor backflow and sludge backflow; ③2 gas flowmeters with a measuring range of 25m respectively 3 h -1 and 50m 3 h -1 , to measure the...
Embodiment 2
[0058] Improvement A using Example 1 2 / O-MBR treatment device, cancel the reflux of anoxic mixed solution, other processes are according to the sewage treatment process of embodiment 1, adjust the influent flow rate to 2.08m 3 h -1 , the corresponding hydraulic retention time is 14h, and the investigation on COD, NH 4 + - Removal effect of N, TN, TP and SS.
Embodiment 3
[0060] Improvement A using Example 1 2 / O-MBR treatment device, cancel the reflux of the anoxic mixed solution, other processes are according to the sewage treatment process of embodiment 1, adjust the influent flow rate to be 2.65m 3 h -1 , the corresponding hydraulic retention time is 11h. 4 + - Removal effect of N, TN, TP and SS.
PUM
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