Method for forcibly removing nitrogen and phosphorus by means of in-situ enrichment of nitrifying bacteria coupled with sludge hydrolysis

An in-situ enrichment, nitrogen and phosphorus removal technology, applied in chemical instruments and methods, water/sludge/sewage treatment, biological water/sewage treatment, etc., can solve the problem of difficult control, high chemical consumption, and unsustainable issues such as advanced green technology to achieve the effect of reducing demand and reducing TN load

Active Publication Date: 2014-11-19
四川发展环境科学技术研究院有限公司
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] The internal factors that affect the effect of simultaneous nitrogen and phosphorus removal are mainly restricted by two factors. One is the influence of sludge age (SRT). For a specific water temperature, nitrifying bacteria require a theoretical minimum SRT min , the activated sludge system requires the actual operating SRT ≥ SRT in order to satisfy sufficient nitrification min , the lower the water temperature, the longer the SRT is required; and the phosphorus removal process requires the shorter the SRT, the shorter the SRT often means the discharge of more excess sludge (WAS), therefore, for the same sewage treatment system, the existing It is often difficult to find a relatively reliable SRT in operation practice, which can not only meet the requirements of nitrification, but also efficiently remove phosphorus, and take into account the effect of nitrogen and phosphorus removal. It is often in a dilemma
[0004] There are similar lateral flow sludge bioaugmentation technologies in foreign countries, such as process, AT-3 process, etc., the main purpose is to strengthen the nitrification process, but the operating conditions and control of these processes are relatively cumbersome, such as The water temperature of the process operation needs to be controlled at 25-30°C, and the intermittent operation mode (water intake, mixing, aeration, sedimentation, decanting) is adopted, and the effect is difficult to control
[0005] At the same time, another important factor affecting the effect of nitrogen and phosphorus removal is the problem of influent water quality. As we all know, the main problems faced by China's sewage plants are insufficient carbon sources in influent water and poor nitrogen and phosphorus removal effects. This is because denitrification Both biological processes of nitrogen removal and anaerobic phosphorus release require sufficient dissolved readily biodegradable organic matter (SCOD), especially low molecular weight volatile fatty acids (VFAs) in wastewater, in order to achieve reliable enhanced biological phosphorus removal (EBPR ), often requires VFAs / TP≥10, which means that for a sewage plant with influent TP=4mg / L, the VFA concentration in the influent water must reach at least 40mg / L to achieve reliable EBPR. However, many sewage plants in my country Plant influent VFAs is less than 10mg / L
In order to make full use of activated sludge carbon sources, some technologies have been developed in recent years, such as ultrasonic cracking, alkaline sludge hydrolysis technology, etc., but these technologies have shortcomings such as high energy consumption, high chemical consumption, and destruction of sludge biological activity. Not a sustainable green process, difficult to apply on a large scale in production practice

Method used

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  • Method for forcibly removing nitrogen and phosphorus by means of in-situ enrichment of nitrifying bacteria coupled with sludge hydrolysis
  • Method for forcibly removing nitrogen and phosphorus by means of in-situ enrichment of nitrifying bacteria coupled with sludge hydrolysis
  • Method for forcibly removing nitrogen and phosphorus by means of in-situ enrichment of nitrifying bacteria coupled with sludge hydrolysis

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Experimental program
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Effect test

Embodiment 1

[0043] The original design treatment capacity of a certain sewage plant is 60,000 m3 / d, and the designed effluent water quality standard is GB18918-2002 Class I B. After four years of operation, the influent water quality of the plant has exceeded the original design standard, and it is planned to implement Class I A standard for the plant According to the actual operation conditions, the plant is mainly due to insufficient nitrification capacity, and the effluent NH 3 -N, TN, TP cannot reach the standard stably. However, the actual situation at the site is that the plant is located in the old city, and the expansion site is limited, so it is not allowed to expand the new biological pool capacity. For this reason, adopt the scheme of the present invention to carry out process design.

[0044] The specific plan is: in the case of keeping the original process hydraulic process unchanged, keep the original biological pool capacity unchanged, use a biological pool abandoned in th...

Embodiment 2

[0047] The concentration standard of influent pollutants remains unchanged and the hydraulic load is increased. Example: The original design treatment capacity of a sewage plant is 100,000 m3 / d. After two years of operation, the influent water volume has far exceeded the treatment capacity, but the influent concentration meets the design requirements. For this reason, it is planned to carry out expansion and upgrading, and the processing capacity is required to reach 130,000 m 3 / d, while meeting the original design effluent standards, but the sewage plant faces factors such as limited expansion sites, and cannot build a new bio-pool capacity. For this reason, adopt the scheme of the present invention to carry out process design, adopt flow chart to see figure 1 , the specific plan is:

[0048] In the case of keeping the original process flow unchanged, according to the process calculation, the design parameters are as follows: 25% of the pool volume at the front end of the o...

Embodiment 3

[0051] The hydraulic load remains unchanged and the concentration of pollutants increases. Example: The original design treatment capacity of a sewage plant is 100,000 m3 / d, but the current influent water quality of the plant has far exceeded the original design standard by 20-30%, and the effluent cannot meet the standard stably. , it is planned to carry out expansion and standard upgrading, and it is required that the effluent can reach the standard stably under the condition that the treated water volume remains unchanged. However, the sewage plant is facing factors such as limited expansion site and cannot build a new biological pool capacity.

[0052] For this reason, adopt the scheme of the present invention to carry out process design, adopt flow chart to see figure 2 , the specific plan is: in the case of keeping the original process hydraulic flow unchanged, keep the volume of the original biological pool unchanged, transform the original biological pool, and separate...

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Abstract

The invention discloses a method for forcibly removing nitrogen and phosphorus from a sewage plant by means of in-situ enrichment of nitrifying bacteria coupled with sludge hydrolysis, and belongs to the field of sewage treatment. Specific to the defects of the conventional mainstream nitrogen and phosphorus removing process, two independent serial or parallel reaction tanks namely, an S-NDN tank and an S-HY tank, are arranged on a sludge return line; sludge returning from a sludge return pump room is shunted into the S-NDN tank and the S-HY tank respectively; the other part of return sludge directly returns into a main biological tank; a nitrogen-rich supernatant generated on a sludge treatment segment of the sewage plant is introduced into the S-NDN tank for serving as a nitrogen source for use in a nitration process, and is applied to in-situ enrichment culture of the nitrifying bacteria; active sludge in the S-HY tank undergoes anaerobic hydrolysis and generates soluble chemical oxygen demand (SCOD); and a mud-water mixed solution which is subjected to the biochemical process in the two reaction tanks returns into a main biological tank respectively. By adopting the method, the nitrogen and phosphorus removing efficiencies can be increased remarkably, and sludge reduction can be realized.

Description

technical field [0001] The invention relates to a sewage treatment method, which belongs to the field of environmental protection, in particular to a method for in-situ enrichment of nitrifying bacteria coupled with sludge hydrolysis to strengthen nitrogen and phosphorus removal in sewage plants. Background technique [0002] At present, China's environmental problems are frequent, surface water eutrophication is serious, and the water quality of some waters even loses the function of drinking water source. Strengthening nitrogen and phosphorus removal will become an important task for a long time in the future. At the same time, the existing conventional treatment processes, such as the deformation process of various activated sludge methods, AAO, oxidation ditch, SBR, etc., are affected by factors such as influent water quality and sludge age control, and have poor nitrogen and phosphorus removal effects. Stability issues, the effluent nitrogen and phosphorus indicators ar...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F3/34
Inventor 李娜
Owner 四川发展环境科学技术研究院有限公司
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