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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

Pending Publication Date: 2021-09-24
GUIZHOU UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

A 2 The / O-MBR combination process is widely used in upgrading and upgrading projects of sewage treatment plants due to its advantages of small footprint, high pollutant removal efficiency, good effluent quality, and low residual sludge yield. However, the process itself has two problems. Big problem: One is the contradiction between nitrifying bacteria and phosphorus accumulating bacteria on sludge age. Nitrifying bacteria are autotrophic obligate aerobic bacteria, which are characterized by slow reproduction speed and long generation time. In order to improve the nitrification performance of the system, It is necessary to maintain a long sludge age; phosphorus accumulating bacteria are heterotrophic bacteria with a fast value-added rate, and the removal of phosphorus mainly depends on the discharge of excess sludge. In order to ensure the effect of biological phosphorus removal in the system, it is necessary to maintain a short sludge age
The second is that it is difficult to further improve the efficiency of nitrogen and phosphorus removal. Both denitrifying bacteria and phosphorus accumulating bacteria are heterotrophic functional bacteria and have a high demand for carbon sources. However, the organic matter content in urban sewage in my country is generally low, and the organic matter in the influent water is given priority Utilized by heterotrophic bacteria such as phosphorus accumulating bacteria in the anaerobic tank, it is difficult for the denitrifying bacteria in the anoxic tank to obtain sufficient carbon sources, which in turn affects the denitrification effect of the system
[0003] for A 2 / O-MBR combination process in the treatment of low-carbon urban sewage, Wang Yingying et al. (Wang Yingying, Yu Haiqin, Zhao Gang, et al. Inverted A 2 Study on the nitrogen and phosphorus removal effect of low-carbon source sewage treated by / O-MBR process[J].Water Treatment Technology,2013,39(6):77-79.) using inverted A 2 The / O-MBR process was used to test the nitrogen and phosphorus removal of domestic sewage in a certain town in the north. The results showed that the process's removal effect on nitrogen and phosphorus was still not ideal, and the total nitrogen concentration in the effluent was as high as 25mg·L -1 , the total phosphorus concentration in the effluent is as high as 2.2mg·L -1 , the main reason for this result is that the influent carbon source is insufficient. In order to improve the effect of nitrogen and phosphorus removal, carbon sources are often added to the device, resulting in an increase in operating costs.

Method used

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  • A2/O-MBR combined process and device for improving low-carbon source town sewage
  • A2/O-MBR combined process and device for improving low-carbon source town sewage
  • A2/O-MBR combined process and device for improving low-carbon source town sewage

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Experimental program
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Effect test

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.

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Abstract

The invention discloses an A2 / O-MBR combined process for improving low-carbon source town sewage and a device thereof. According to the combined process, sewage is treated by an anaerobic tank, a first anoxic tank, a second anoxic tank, an aerobic tank and a membrane tank in sequence and then is discharged; sewage in the second anoxic tank flows back to the anaerobic tank, sewage in the aerobic tank flows back to the first anoxic tank, and sludge in the membrane tank flows back to the anaerobic tank. Aiming at the problems of low nitrogen and phosphorus removal efficiency and matrix competition when the conventional A2 / O process is used for treating low-carbon-nitrogen-ratio town sewage, the anoxic tank is divided into two parts, the reflux of anoxic mixed liquid is increased, the nitrogen removal efficiency is improved by 11.5%, and the phosphorus removal efficiency is improved by 12.2%; according to the process, the average removal rates of COD, ammonia nitrogen, total nitrogen, total phosphorus and SS are 91.7 percent, 98.5 percent, 47.5 percent, 84.2 percent and 98.9 percent respectively; and under the condition that a carbon source is not added, the nitrogen and phosphorus removal effect can be greatly improved.

Description

technical field [0001] The invention belongs to the field of urban sewage treatment, in particular to a low-carbon source urban sewage improvement A 2 / O-MBR combination process and its device. Background technique [0002] In recent years, as pollutant discharge requirements have become more and more stringent, many sewage plants are facing upgrades. A 2 The / O-MBR combination process is widely used in upgrading and upgrading projects of sewage treatment plants due to its advantages of small footprint, high pollutant removal efficiency, good effluent quality, and low residual sludge yield. However, the process itself has two problems. Big problem: One is the contradiction between nitrifying bacteria and phosphorus accumulating bacteria on sludge age. Nitrifying bacteria are autotrophic obligate aerobic bacteria, which are characterized by slow reproduction speed and long generation time. In order to improve the nitrification performance of the system, It is necessary to ...

Claims

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Application Information

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IPC IPC(8): C02F3/30
CPCC02F3/308C02F2203/006C02F2301/046C02F2301/08C02F2209/08C02F2209/14C02F2209/16C02F2209/10C02F2303/14
Inventor 周少奇何春求郑可
Owner GUIZHOU UNIV