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Method for starting total biological phosphorus removal AOO process

A biological phosphorus removal, all-biological technology, applied in the field of urban sewage treatment and resource utilization, can solve the problems of difficulty in stabilization, complex process procedures, easy sludge expansion and difficulty in stabilization, etc., achieving stable operation, high startup success rate, and saving exposure. air volume effect

Active Publication Date: 2019-01-18
江苏孚璋生物技术有限公司
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  • Application Information

AI Technical Summary

Problems solved by technology

[0007] 2) The system is difficult to run stably under low load;
[0009] Under the condition of low load of 0.5CODg / g, the sludge of AO continuous flow biological phosphorus removal process is easy to expand and difficult to stabilize
[0010] 3) The system cannot start and operate at low temperature;
Under normal temperature from April to October, the anaerobic and aerobic AO continuous flow biological phosphorus removal reactor often has sludge bulking after running for about 3 months due to the low load and the accumulation of Thiobacillus, which is difficult to stabilize
[0015] 2) Double sludge anaerobic anoxic phosphorus removal-anaerobic aerobic nitrogen removal A 2 N continuous flow dual-sludge system, the process procedure is complex, need to be started separately and recombined, the ratio of influent nitrogen and phosphorus is relatively strict, and auxiliary chemical phosphorus removal is required;

Method used

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  • Method for starting total biological phosphorus removal AOO process

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0044] Such as figure 1 Shown: The reactor is in the form of a continuous flow baffle AO reactor, with agitator 1, water inlet 2, return pipe 3, testing equipment pH meter 4, testing equipment ORP meter 5, dissolved oxygen meter 6, testing equipment pollution Mud concentration meter 7, overflow port 8, anaerobic section 9, aerobic first section 10, aerobic middle section 11, aerobic final section 12, sedimentation tank 13; Microporous aeration heads are installed at the bottom of the middle section of the aerobic section, the middle section of the aerobic section, and the aeration volume is controlled by a gas flow meter.

[0045] The volume of the anaerobic section: the total volume of the reactor is 1:3.3; the volume of the first aerobic section: the total volume ratio of the aerobic section is 1:3.3.

[0046] The reaction temperature is low (14-18°C). First, the activated sludge retrieved from the sewage plant is inoculated in the continuous flow baffle AO reactor. The ini...

Embodiment 2

[0059] Influent water quality and reactor form are the same as above.

[0060] The reaction temperature is normal temperature (20-25° C.). Firstly, inoculate the inoculation sludge phosphorus removal activity of 40%-75% in the continuous flow baffle AO reactor, the inoculation volume is 60L, and the sludge concentration is 1500mg / L.

[0061] A kind of start-up method of whole biological phosphorus removal AOO process, comprises the following steps:

[0062] The first step: the domestication and enrichment stage before start-up, including:

[0063] (1) Sludge volume amplification and optimal aeration volume search stage: Fill the reactor containing domesticated sludge with actual domestic sewage, adopt anaerobic and aerobic internal reflux cycle, control volume load 2g / L, total The aeration rate is 30ml / min, and the dissolved oxygen concentration in each section is controlled at 2mg / L~4mg / L. After the sludge concentration in the reactor increases to 2000mg / L, the continuous wa...

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Abstract

The invention provides a method for starting a total biological phosphorus removal AOO process. The method comprises the following steps: 1, starting a domestication and enrichment stage before start,comprising (1) anaerobic contact of sludge; (2) high-aeration aerobic domestication of sludge; and (3) sludge amount enlargement and optimum aeration amount search; and 2, starting stage, namely (1)entering a reactor, and respectively setting an anaerobic zone, an aerobic first zone, an aerobic middle zone and an aerobic tail zone, wherein the hydraulic retention time in the anaerobic zone is consistent with that of the traditional AO process; and (2) controlling the dissolved oxygen concentration to be 0.3-0.7mg / L and the hydraulic retention time to be 0.7-1 hour at the aerobic first zone,controlling the dissolved oxygen concentration to be 1.0-1.6mg / L and the hydraulic retention time to be 1.5-2 hours at the aerobic middle zone and the aerobic tail zone, controlling the sludge age tobe 5-7 days, and controlling the reflux ratio to be 50-60%. The method disclosed by the invention is rapid in system startup and high in starting success rate, the operation is stable, and the aeration amount is saved.

Description

technical field [0001] The invention belongs to the field of urban sewage treatment and resource utilization, and relates to a start-up method of an all-biological phosphorus removal AOO process. Background technique [0002] Nitrogen and phosphorus are the main factors causing lake eutrophication. At present, the main goal of sewage treatment in my country is still COD, and insufficient attention has been paid to the removal of nitrogen and phosphorus. The concentration of ammonia nitrogen in the actual domestic sewage of the community is 50-70mg / L, and the concentration of phosphorus is 6 ~7mg / L, due to the different sludge ages of nitrifying bacteria and aerobic phosphorus accumulating bacteria, limited COD in sewage and other reasons, the removal of nitrogen and phosphorus cannot be taken into account. Sewage plants usually adopt biological denitrification, and phosphorus removal is a biological + chemical auxiliary method, which increases the cost of sewage treatment, an...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F3/34C02F3/30C02F101/10
CPCC02F3/30C02F3/308C02F3/34C02F2101/105C02F2001/007
Inventor 许达张浩宾王川
Owner 江苏孚璋生物技术有限公司
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