'Main-auxiliary' activated sludge method for coupling deodorization and strengthening nitrogen and phosphorus removal

A technology for activated sludge, nitrogen and phosphorus removal, applied in chemical instruments and methods, water/sludge/sewage treatment, water pollutants, etc. Microbial activity and other problems, to achieve the effect of strengthening the biological phosphorus removal effect of the system, overcoming the instability of phosphorus removal effect, and increasing the content of nitrifying bacteria

Pending Publication Date: 2019-01-25
李达
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] At the same time, many areas of our country suffer from severe shortage of carbon sources for sewage plants. Existing conventional treatment processes, such as deformation processes of various activated sludge methods, AAO and its variant processes, oxidation ditch, MBR, SBR and Its various variant processes mainly rely on the traditional phosphorus removal bacteria Accumulibacter to achieve EBPR (Enhanced Biological Phosphorus Removal), while Accumulibacter can only rely on the ingestion of VFA in the influent, and there is also substrate competition between PAO and GAO; in addition, the reflux of nitrate and DO Interference with the anaerobic zone makes it difficult to control the ORP below -150mv in the anaerobic zone, which is not an ideal anaerobic environment for biological phosphorus removal. Many of the above factors lead to unstable biological phosphorus removal effects of traditional mainstream treatment processes
In addition, the high pollution load caused by the high ammonia nitrogen reflux of the sludge dewatering liquid in the sludge treatment section, the low water temperature season and other factors lead to insufficient nitrification capacity and the ammonia nitrogen in the effluent does not meet the standard. The above factors make it difficult for the traditional process to remove nitrogen and phosphorus. For further improvement, standard upgrading often has to choose to transform the original aeration tank into the IFAS process, or add a third-level biochemical treatment unit (such as BAF, deep-bed denitrification filter), which greatly increases the project investment. At the same time, it also increases the operating cost during the operation period, and the greenhouse gases released by the environment also increase exponentially with the prolongation of the process. The lengthy upgrading and transformation process is generally unsustainable
[0004] After more than a hundred years of development, the activated sludge process is still the most economical and effective method for sewage treatment. However, the traditional mainstream activated sludge process is vulnerable to external disturbances (water quantity, water quality, and water temperature changes). From the perspective of the control of the bacterial flora structure, because the traditional mainstream activated sludge process only has the activated sludge process on the "main line", although anaerobic, anoxic and aerobic environments are set, the above environments are affected by various factors (influent water quality water fluctuations, internal backflow and external backflow), and the removal of different pollutants must be taken into account, but the ecological niches of different microorganisms are very different, so it is difficult to take into account the habitat conditions of different functional flora under the process control conditions, and it is difficult to realize the removal of active pollutants. The optimization and regulation of the structure of the mud flora makes it more difficult to achieve directional transformation and control
[0005] In response to the above problems, the current technical route solutions often use "multiple methods" and "separate solutions". The process is becoming more and more complicated, but systematic and collaborative consideration is not achieved, and nutrients are often solved through the superposition of lengthy process routes. However, the deodorization problem is still not resolved, and it is still necessary to increase the deodorization measures along the whole process along with the extension of the sewage treatment process, resulting in high investment and operating costs for the deodorization system.
Some deodorization technologies commonly used at present ...

Method used

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  • 'Main-auxiliary' activated sludge method for coupling deodorization and strengthening nitrogen and phosphorus removal
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  • 'Main-auxiliary' activated sludge method for coupling deodorization and strengthening nitrogen and phosphorus removal

Examples

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Effect test

Embodiment 1

[0055] Take a certain 50,000 m 3 / d Sewage plant upgrading and upgrading as an example, the discharge standard of upgrading and upgrading is upgraded from Class A standard to "quasi-four category".

[0056] Removal rate table of pollutants in and out of a sewage treatment plant

[0057]

[0058] For this reason, the technological process of this transformation plan is as follows: figure 1 , select the "S2HBR-S2ASH process" involved in the present invention, build a new group of side flow "S2HBR-S2ASH", respectively adopt two rectangular reaction tanks and connect them in series, and return the pump room sludge to 105m 3 / h after being filtered by two micro-sieves with a filtration precision of 250 microns, it flows through the side flow S2 pool sequentially, and the remaining RAS is directly returned to the anaerobic pool. Among them, the S2HBR pool is equipped with 12 microbial culture tanks, and the upper and lower layers of biological culture beds in the tank are pre-f...

Embodiment 2

[0060] Due to the increase in the concentration of influent pollutants, the A sewage treatment plant in a certain city cannot meet the standards stably, and the air pollution to the surrounding environment is relatively large, causing complaints from nearby residents. Upgrading and upgrading and adding deodorization measures, the scale of the plant is 120,000 m 3 / d, using the Carrousel 2000 oxidation ditch process. The process flow of this transformation plan is as follows: figure 2 , transforming the original 4 grid series anaerobic pools into S2HBR pools (the first 3 grids) and S2ASH pools (the last 1 grid), in which 24 microbial culture tanks are placed in the S2HBR pools, and the tanks are filled with two layers of fillers, S and F, and Increase the aeration device, design the main biological MLSS to be 4000mg / L, control the frequency conversion of the total return flow at 33%-40%, control the actual return sludge concentration at 12000-14000mg / L, and return the total a...

Embodiment 3

[0062] A certain 60,000 m 3 / d Sewage plant, raised from Grade B to "quasi-four" standard, requiring COD=40mg / L, TN=10mg / L, TP=0.3mg / L, NH3-N=2mg / L. The primary organism pool is the Aubert Oxidation Ditch. The process flow of this transformation plan is as follows: image 3 , the original selection tank was transformed into a side-flow S2ASH tank, and a new S2HBR tank was built, in which 18 microbial culture tanks were placed in the S2HBR tank (two layers of S and F fillers were filled in the tank), and the two side-flow tanks were operated in parallel mode. The MLSS of the main organism is 4.5g / L, the reflux ratio is controlled by frequency conversion speed regulation to 33%-45%, the concentration of the reflux sludge is controlled at 14500-18000mg / L, and the sludge is drawn from the sludge reflux pump room for 135m 3 / h, after being filtered by two 300 micron micro-sieves, it is sent to the S2 pool, and the return sludge is 60m 3 / h to the S2HBR pool, the residence time o...

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Abstract

The invention relates to a 'main-auxiliary' activated sludge method for coupling deodorization and strengthening nitrogen and phosphorus removal. A main line adopts traditional activated sludge and adeformation process thereof, and in an 'auxiliary' line, a sludge micro-screen filter, a side-flow sludge biological culture tank (S2HBR) filled with a strain culture tank (SBIO-A) and a side-flow activated sludge anaerobic hydrolysis tank (S2ASH) reactor are arranged in an activated sludge return line; an auxiliary line reaction tank S2HBR and S2ASH tank can be connected in parallel or in series.The method can directionally enrich, and significantly improve and optimize a flora structure of the activated sludge, 'main-auxiliary' reactor combination achieves the directed cultivation of specific microorganisms through a side-flow reactor on the 'auxiliary' line and conducts functional microbial inoculation on a main biochemical system on the 'main line', and the 'main-auxiliary' reactor configuration can achieve deep denitrification and dephosphorization of the biochemical system, and significantly improve the deodorization effect of the whole process, while saving commercial carbon sources and achieving activated sludge In situ process reduction.

Description

technical field [0001] The invention belongs to the field of sewage treatment and water environment treatment, and in particular relates to a "main-auxiliary" activated sludge method that couples the whole process of deodorization and strengthens the functions of nitrogen and phosphorus removal. Background technique [0002] At present, China's water environment problems are frequent, surface water eutrophication is serious, and the water quality of some water areas even loses the function of drinking water source. important long-term tasks. At the same time, due to historical reasons, many urban sewage plants are built in urban areas. The process of sewage collection and treatment releases a large amount of volatile odorous gases (such as hydrogen sulfide, ammonia, etc.), which seriously interferes and affects the ambient air quality of surrounding cities. The avoidance effect becomes more prominent. Stable water quality compliance and odor control are common problems fac...

Claims

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Application Information

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IPC IPC(8): C02F3/30
CPCC02F3/302C02F2101/16C02F2101/105
Inventor 李娜唐怡
Owner 李达
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