Integrated sewage biochemical treatment device

A biochemical treatment device and sewage technology, applied in water/sewage treatment, biological water/sewage treatment, degassed water/sewage treatment, etc., can solve the problem of high construction and management costs, high construction investment, and rising management costs, etc. problems, to achieve the effect of improving the deep denitrification function, reducing the construction cost and operation cost, and reducing the area

Pending Publication Date: 2020-04-03
BEIJING BOHUITE ENVIRONMENTAL TECH CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

For the sake of insurance, some newly-built sewage plants have also followed the above-mentioned main process settings and adopted the main process flow of traditional biochemical process equipment + deep denitrification process equipment for construction, which not only resulted in high construction investment, but also a long process flow , more process devices will also lead to higher management costs
[0004] Especially some smaller ones, such as 500m 3 If the sewage treatment plants at the village and town level below / d still adopt the above-mentioned main technological process for construction by CCB, the construction cost and management cost will be very high and unbearable

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0046] An integrated sewage biochemical treatment device provided in this embodiment, such as figure 1 As shown, it includes the first treatment unit, the second treatment unit, the third treatment unit, the fourth treatment unit and a mud-water separation unit arranged along the sewage flow direction and allowing sewage circulation, the second treatment unit and the fourth treatment unit are side by side It is provided that the mud-water separation unit is sandwiched between the second treatment unit and the fourth treatment unit and is used to isolate the second treatment unit and the fourth treatment unit. The middle and lower parts of the mud-water separation unit near the fourth treatment unit are respectively It communicates with the fourth processing unit, and the inlet port of the second processing unit and the outlet port of the fourth processing unit are adjacent to the first processing unit, and the outlet port of the second processing unit and the inlet port of the ...

Embodiment 2

[0061] The difference between the present embodiment and embodiment one is that an anaerobic pool 11 is also provided in the first treatment unit, and the head end of the anaerobic pool 11 communicates with the end of the secondary aerobic pool 4, and the end of the anaerobic pool 11 is connected with the first-level aerobic pool. The anoxic pool 1 is connected, and a mixed liquid return device 41 is provided at the joint between the anaerobic pool 11 and the secondary aerobic pool 14 . The integrated sewage treatment device with the addition of anaerobic pool 11 can enable the integrated sewage treatment device to have sludge anaerobic phosphorus release function partitions, which provides a prerequisite for subsequent aerobic excess phosphorus uptake, and can effectively improve the integrated sewage treatment capacity. The biological phosphorus removal effect of the treatment unit.

Embodiment 3

[0063] The difference between this embodiment and Embodiment 2 is that: a pre-denitration pool 12 is also provided in the first treatment unit; The end of the pool 4 is connected, the end of the pre-denitration pool 12 is connected with the head end of the anaerobic pool 11, and the mixed liquid return device 41 is arranged at the joint between the pre-denitration pool 12 and the secondary aerobic pool 4. The integrated sewage treatment device of the pre-denitrification tank 12 is added, and the returned mixed solution first enters the pre-denitrative tank 12 for denitrification to remove nitrate nitrogen, which can further reduce the amount of mixed solution entering the anaerobic tank 11. The concentration is reduced inside the anaerobic tank 11 The competition for volatile fatty acid carbon sources provides a more ideal phosphorus release environment for the sludge phosphorus release in the anaerobic tank 11, thereby improving the effect of aerobic phosphorus uptake and f...

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Abstract

The invention discloses an integrated sewage biochemical treatment device, and belongs to the field of sewage treatment. According to the technical scheme, the integrated sewage biochemical treatmentdevice is characterized by comprising a first treatment unit, a second treatment unit, a third treatment unit and a fourth treatment unit which are arranged in the sewage circulation direction and allow sewage to circulate; the second treatment unit and the fourth treatment unit are arranged side by side, and a sedimentation tank for isolating the second treatment unit from the fourth treatment unit is arranged between the second treatment unit and the fourth treatment unit; wherein the first treatment unit comprises at least one first-stage anoxic tank, the second treatment unit comprises atleast one first-stage aerobic tank, the third treatment unit comprises at least one second-stage anoxic tank, and the fourth treatment unit comprises at least one second-stage aerobic tank; aeration pipes are arranged in the first-stage aerobic tank and the second-stage aerobic tank. The problem that small-scale sewage treatment plants are high in construction and operation cost is solved.

Description

technical field [0001] The invention relates to the field of sewage treatment, in particular to an integrated sewage biochemical treatment device. Background technique [0002] With the increasingly stringent environmental protection regulations in my country and the increasing demand for ecological environment, the control of COD, total nitrogen and total phosphorus in various large and small sewage treatment plants (stations) is also getting higher and higher, and some sensitive areas have begun to implement higher level A Stricter local and regional drainage standards, such as total nitrogen ≤ 10mg / L, COD ≤ 30mg / L, etc. [0003] Under the premise of the new standard requirements, some old factories have not only upgraded and upgraded the original biochemical devices, but also added deep denitrification process devices such as denitrification filters to ensure that the total nitrogen reaches the standard. , and achieved many successful cases. For the sake of insurance, so...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/14C02F101/10C02F101/16
CPCC02F1/00C02F1/20C02F1/32C02F3/302C02F9/00C02F2001/007C02F2101/105C02F2101/16C02F2209/16
Inventor 迟金宝张雷汪翠萍陈凯华潘建通张鹤
Owner BEIJING BOHUITE ENVIRONMENTAL TECH CO LTD
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