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High-load artificial wetland system with enhanced nitrogen and phosphorus removal function

A constructed wetland system, nitrogen and phosphorus removal technology, applied in the field of enhanced nitrogen and phosphorus removal high-load constructed wetland system, can solve the problems of high labor intensity, depletion, and exceeding the standard of the project, to avoid hydraulic short circuit, ensure treatment effect, prolong The effect of migration path

Active Publication Date: 2019-02-26
GUANGZHOU INST OF GEOCHEMISTRY - CHINESE ACAD OF SCI +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

These supplementary methods of organic carbon sources have effectively improved the effect of denitrification and denitrification, but there are still some problems: the hydrolysis of solid carbon sources takes time, the release of carbon sources is unstable, the organic carbon sources in the filler will be exhausted soon, and the duration of efficient denitrification Short; adding hydrolyzate requires artificial regular addition of plants for hydrolysis, which is labor-intensive for large-scale projects, and plant hydrolysis residues need to be disposed of; it is most economical and convenient to use raw sewage organic carbon sources, but raw sewage will also be brought into NH 3 -N, in the denitrification section is anoxic environment, the NH 3 -N removal ability is weak, easy to lead to water NH 3 -N exceeds the standard
It can be seen that efficient, continuous, and low-cost denitrification is a difficult problem faced by sewage treatment technology, which makes it difficult to discharge TN in the effluent.
[0004] In addition, the effluent of the secondary aerobic unit usually contains a relatively high concentration of total phosphorus. Adding a flocculant to remove phosphorus can achieve a good phosphorus removal effect, but the cost is high, and it is more difficult to implement in the practice of decentralized domestic sewage in villages and towns.

Method used

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  • High-load artificial wetland system with enhanced nitrogen and phosphorus removal function

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0040] The hydraulic load of this embodiment is 0.40m3 / (m 2 d). The structure of the high-load constructed wetland system for enhanced nitrogen and phosphorus removal is as follows: figure 1 shown. In this embodiment, the area ratio of wetland I and wetland II is 1:1, wetland I is downward flow, and wetland II is upward flow. The pool body of the artificial wetland system is a brick-concrete structure, and the bottom and the pool wall are treated with anti-seepage. The water collecting and distributing pipe 8 collects the sewage treated in the wetland I and evenly distributes it in the wetland II. Wherein the water collecting and distributing pipe 8 is connected to an emptying pipe 11 with a ball valve leading to the outside of the pool, which is used for emptying the wetland or discharging mud. The bottom of the fourth packing layer 6 is provided with a water collection and drainage pipe 9 for discharging the treated sewage out of the system. The water collection and dr...

Embodiment 2

[0045] The hydraulic load of this embodiment is 1.20m 3 / (m 2 d). The structure of the high-load constructed wetland system for enhanced nitrogen and phosphorus removal is as follows: figure 1 shown. The arrangement sequence of the packing layers in this example is basically the same as that in Example 1, the main difference is that the area ratio of wetland I and wetland II is 2:1, and the composition and thickness of each packing layer are also different. The first packing layer 1 and the fourth packing layer 6 both have a thickness of 35 cm, and the fillers are mixed fillers of zeolite and crushed stone (volume ratio 2:1), and the particle size ranges from 0.4 to 0.8 cm. The thickness of the second packing layer 2 and the third packing layer 5 are both 80cm, and the fillers are mixed fillers of steel slag, gravel and pyrite (the mixing ratio is 4:2:1), and the particle size ranges from 0.5 to 1.2cm. The first crushed stone layer 3 and the second crushed stone layer 4 bo...

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Abstract

The invention discloses a high-load artificial wetland system with an enhanced nitrogen and phosphorus removal function. The system comprises a wetland I and a wetland II which are communicated at thebottom, wherein the wetland I comprises water sprinkling devices, a first packing layer, a second packing layer and a first broken rubble layer which are laid from top to bottom; the wetland II comprises a second broken rubble layer, a third packing layer and a fourth packing layer which are laid from bottom to top; the artificial wetland system further comprises a water collecting and distributing pipe and a drain pipe, the water collecting and distributing pipe is arranged in the first broken rubble layer and the second broken rubble layer and used for communicating the bottoms of the wetlands on the left side and the right side; the water collecting and distributing pipe is connected with the drain pipe; a water collecting and draining pipe is arranged at the bottom of the fourth packing layer of the wetland II and provided with an electrically operated valve which is used for controlling draining time of the system. The system is simple in structure, high in integration level, high in hydraulic loading, good in nitrogen and phosphorus removal effect and lower in investment and operating cost, consumes no energy during oxygen supply and is not prone to blocking.

Description

technical field [0001] The invention belongs to the technical field of sewage treatment in environmental engineering, and in particular relates to a high-load constructed wetland system for strengthening denitrification and dephosphorization. Background technique [0002] In order to protect the ecological environment and reduce water eutrophication, my country's sewage discharge standards are becoming increasingly strict, which requires deep nitrogen and phosphorus removal of the effluent from the secondary aerobic unit (the tail water of the sewage treatment plant). Microbial aerobic nitrification and anoxic denitrification are considered to be the most important ways of wastewater denitrification. However, in the aerobic removal of NH 3 -N at the same time, the organic carbon in the sewage is basically removed, so that the post-denitrification unit is severely inhibited due to the lack of organic carbon sources. [0003] Therefore, it is necessary to add an organic carb...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F3/30C02F3/32C02F101/16C02F101/10
CPCC02F3/301C02F3/302C02F3/32C02F2101/105C02F2101/16
Inventor 杨永强张玲玲高丽英吴世军陈繁荣
Owner GUANGZHOU INST OF GEOCHEMISTRY - CHINESE ACAD OF SCI
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