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Domestic sewage biological denitrification method and system starting method

A technology for domestic sewage and biological denitrification, applied in biological water/sewage treatment, chemical instruments and methods, water/sludge/sewage treatment, etc. and other problems, to achieve the effect of easy upgrading, excellent denitrification effect and low start-up cost

Active Publication Date: 2021-07-02
BEIJING UNIVERSITY OF CIVIL ENGINEERING AND ARCHITECTURE
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AI Technical Summary

Problems solved by technology

On the one hand, the concentration range of ammonia nitrogen in domestic sewage is generally 30-50mg / L, and the concentration of ammonia nitrogen is low. Under the low concentration of ammonia nitrogen, it is difficult for free ammonia to reach the concentration level that can be suppressed, and the nitrosation process is difficult to stabilize, and the rapid proliferation of NOB will Destroy the reaction pathway of autotrophic denitrification and oxidize the NO obtained by AOB 2 - -N is directly converted to nitrate nitrogen (NO 3 - -N); on the other hand, lower temperature (10-28°C) and low substrate concentration are not conducive to the proliferation of fully autotrophic denitrification bacteria, especially AnAOB, and the overall denitrification efficiency will become worse
Therefore, it is particularly important to ensure the high efficiency and stability of AOB and AnAOB activities while also achieving effective inhibition of NOB, but the existing technology cannot achieve the above goals
[0005] At the same time, it is inevitable that a certain concentration of organic matter will remain in domestic sewage, and heterotrophic bacteria will inevitably appear in the water treatment system. More stable operation is also a problem to be solved

Method used

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specific Embodiment approach 1

[0019] Specific implementation mode 1: The biological denitrification method of domestic sewage in this embodiment: feed the domestic sewage into the activated domestic sewage biological denitrification treatment system for denitrification treatment; DO (dissolved oxygen) control <0.5mg during the denitrification treatment operation process / L.

[0020] In this embodiment, the domestic sewage biological denitrification treatment system selects a granular sludge expanded bed reactor for domestic sewage treatment. The granular sludge in the domestic sewage biological denitrification treatment system of this embodiment is enriched by AOB and AnAOB, wherein the outer layer of the granular sludge is AOB, and the inner layer of the granular sludge is AnAOB. ​​Due to the higher affinity of AOB to oxygen, It tends to accumulate in the outer layer of sludge to obtain oxygen, and after the consumption of surface AOB, the inner layer of sludge is an anaerobic zone, which is suitable for ...

specific Embodiment approach 2

[0021] Embodiment 2: The difference between this embodiment and Embodiment 1 is that the hydraulic retention time of the denitrification treatment is 2 to 6 hours. Other steps and parameters are the same as those in Embodiment 1.

specific Embodiment approach 3

[0022] Specific implementation mode three: the start-up method of the domestic sewage biological denitrification treatment system in this implementation mode:

[0023] 1. Put the denitrification granular sludge in the reaction zone of the EGSB reactor. 3 d)±0.01kgN(m 3 d) artificial water intake operation, DO (dissolved oxygen) control <0.3mg / L during operation, gradually increase NLR (nitrogen volume loading rate) in stages; until the effluent ammonia nitrogen removal rate and total nitrogen removal rate reach 90% respectively And more than 80%, and the ratio of ammonia nitrogen removal / total nitrogen removal is ≥0.88, the ratio of nitrate nitrogen production / ammonia nitrogen removal is ≤0.11, and the relative abundance of NOB is less than 1%;

[0024] 2. Into the EGSB reactor, the pH value is 7.8-8.0, and the NLR is 0.24kgN (m 3 d)±0.01kgN(m 3 ·D) simulated sewage operation, DO control <0.3mg / L during operation, if the nitrate nitrogen production / ammonia nitrogen removal ...

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Abstract

The invention discloses a domestic sewage biological denitrification method and a system starting method, and relates to a sewage treatment method and a system starting method. The denitrification method comprises the following steps: introducing domestic sewage into the started domestic sewage biological denitrification treatment system for denitrification treatment; wherein DO is controlled to be less than 0.5 mg / L in the denitrification operation process. The starting method comprises the following steps: 1, placing the denitrified granular sludge in a reaction zone of the EGSB reactor, introducing artificial water which is considered to be set for operation, and controlling DO to gradually increase NLR in stages; 2, introducing simulated sewage for operation until the NOB relative abundance is less than 1%; and 3, introducing actual domestic sewage to realize stable operation of the completely autotrophic nitrogen removal process. The domestic sewage biological denitrification method is low in operation cost, low in starting cost, convenient for upgrading and reconstruction of sewage plants and easier to realize. Moreover, the method disclosed by the invention is not influenced by temperature fluctuation of the domestic sewage, and also has an excellent denitrification effect at a relatively low temperature of 10-28 DEG C.

Description

technical field [0001] The invention relates to a sewage treatment method and a system starting method. Background technique [0002] For nitrogen source pollution in urban sewage, traditional biological denitrification processes based on nitrification and denitrification processes are currently used for treatment. These processes have been widely used in urban sewage treatment. However, with the improvement of wastewater discharge standards, the traditional denitrification process has also exposed its own shortcomings. For example: the infrastructure cost of multi-stage treatment system is high; the denitrification process needs to add a large amount of carbon source, which increases the operating cost of the water plant; the excess sludge output is high, which further increases the treatment cost; more greenhouses are generated in the denitrification process Gas, not conducive to sustainable development. [0003] Anammox (anammox) process means that under anaerobic condi...

Claims

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Application Information

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IPC IPC(8): C02F3/30
CPCC02F3/301C02F3/302C02F2209/22C02F2209/40
Inventor 高大文向韬
Owner BEIJING UNIVERSITY OF CIVIL ENGINEERING AND ARCHITECTURE
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