CN210419416U - Vertical oxidation ditch - Google Patents

Vertical oxidation ditch Download PDF

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Publication number
CN210419416U
CN210419416U CN201920813112.7U CN201920813112U CN210419416U CN 210419416 U CN210419416 U CN 210419416U CN 201920813112 U CN201920813112 U CN 201920813112U CN 210419416 U CN210419416 U CN 210419416U
Authority
CN
China
Prior art keywords
oxidation ditch
ditch body
vertical
oxidation
glass fiber
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201920813112.7U
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Chinese (zh)
Inventor
姜文发
褚强
王清方
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hubei Dingyu Energy Saving And Environmental Protection Technology Co ltd
Original Assignee
Wujiang City Zhaoshun Frp Products Co ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Wujiang City Zhaoshun Frp Products Co ltd filed Critical Wujiang City Zhaoshun Frp Products Co ltd
Priority to CN201920813112.7U priority Critical patent/CN210419416U/en
Application granted granted Critical
Publication of CN210419416U publication Critical patent/CN210419416U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

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  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
  • Sewage (AREA)
  • Activated Sludge Processes (AREA)

Abstract

The utility model relates to a vertical oxidation ditch, its characterized in that: the oxidation ditch comprises a cylindrical frame and an oxidation ditch body arranged in the frame, wherein the oxidation ditch body is designed into a structure which is spirally downward and closed; a plurality of aeration heads are arranged at the downstream of the oxidation ditch body; the inner wall of the oxidation ditch body is provided with a flow deflector. The oxidation ditch body is designed into a structure which is spirally downward, so that sewage can move without arranging equipment such as a flow impeller and the like when entering the oxidation ditch body, the energy consumption is reduced, and the energy conservation and emission reduction are facilitated; meanwhile, the space in the vertical direction is expanded due to the downward spiral arrangement, and the occupied area is greatly reduced under the condition of the same flow compared with that of a conventional oxidation ditch; the oxidation ditch is made of glass fiber reinforced plastics, and the materials have the advantages of good chemical stability, corrosion resistance, high and low temperature resistance, non-conductivity, light weight, high strength and the like; the oxidation ditch adopting the material also has the advantages of high strength and light weight, so that the flexibility of building and applying the oxidation ditch is greatly increased.

Description

Vertical oxidation ditch
Technical Field
The utility model relates to a glass steel equipment field especially relates to a vertical oxidation ditch.
Background
The oxidation ditch is one of activated sludge methods in sewage treatment technology, and the constructed structure is in a ditch shape; the conventional oxidation ditch is usually constructed by reinforced concrete, so that the occupied area is large, and space limitation exists when a plurality of factories are reconstructed; moreover, the investment cost is high and is more or less permanent, so that the application difficulty is high and the application flexibility is poor; therefore, the utility model aims to solve the problem of providing an oxidation ditch which has small occupied area and flexible application.
Disclosure of Invention
The utility model overcomes the defects of the prior art and provides an oxidation ditch which occupies small area and is flexible to use.
In order to achieve the above purpose, the utility model adopts the technical scheme that: the vertical oxidation ditch is characterized in that: the oxidation ditch comprises a cylindrical frame and an oxidation ditch body arranged in the frame, wherein the oxidation ditch body is designed into a structure which is spirally downward and closed; a plurality of aeration heads are arranged at the downstream of the oxidation ditch body; and the inner wall of the oxidation ditch body is provided with a flow deflector.
Preferably, the cylindrical frame and the oxidation ditch are made of glass fiber reinforced plastics.
More preferably, the glass fiber reinforced plastic is epoxy resin-based glass fiber reinforced plastic.
Preferably, the oxidation ditch body is arranged to circle for three times, the track of each circle is the same, and the projection of the track on the horizontal plane is elliptical.
As a preferable scheme, the oxidation ditch body is connected with an environment-friendly defoaming agent dosing device through a pipeline.
As a more preferable scheme, the environment-friendly antifoaming agent is caramel ester.
As a preferable scheme, the inlet of the oxidation ditch body is positioned at the top of the spiral structure, and the outlet of the oxidation ditch body is positioned at the bottom of the spiral structure.
Preferably, the oxidation ditch body heating device.
The beneficial technical effects of the utility model mainly lie in: provides an oxidation ditch which occupies small area and is flexible to use. The oxidation ditch body is designed into a structure which is spirally downward and closed, an inlet of the oxidation ditch body is positioned at the top of the spiral structure, and an outlet of the oxidation ditch body is positioned at the top of the spiral structure; therefore, sewage entering the oxidation ditch body can flow downwards in a spiral mode under the action of gravity, and related equipment such as a flow impeller is not needed, so that the energy consumption is reduced, and the energy conservation and emission reduction are facilitated; meanwhile, the space in the vertical direction is expanded due to the downward spiral arrangement, and the occupied area is greatly reduced under the condition of the same flow compared with that of a conventional oxidation ditch; the oxidation ditch is made of glass fiber reinforced plastics, and compared with the traditional oxidation ditch material, the material has the advantages of good chemical stability, corrosion resistance, high and low temperature resistance, non-conductivity, light weight, high strength and the like; the oxidation ditch adopting the material also has the advantages of high strength and light weight, so that the flexibility of building and applying the oxidation ditch is greatly increased.
Drawings
The present invention will be further explained with reference to the drawings and examples.
Fig. 1 is a schematic structural view (front view) of a preferred embodiment of the present invention.
Fig. 2 is a schematic structural view (top view) of a preferred embodiment of the present invention.
Fig. 3 is a schematic structural view of an oxidation ditch body according to a preferred embodiment of the present invention.
Detailed Description
The invention will now be described in further detail with reference to the accompanying drawings, which are simplified schematic drawings and illustrate, by way of illustration only, the basic structure of the invention, and which therefore show only the constituents relevant to the invention. It should be noted that the terms "front," "back," "left," "right," "upper" and "lower" used in the following description refer to directions in the drawings, and the terms "inner" and "outer" refer to directions toward and away from, respectively, the geometric center of a particular component.
As shown in fig. 1-3, a vertical oxidation ditch comprises a cylindrical frame 1 and an oxidation ditch body 2 arranged in the frame 1, wherein the oxidation ditch body 2 is arranged in a downward spiral and closed structure, an oxidation ditch body inlet 21 is positioned at the top of the spiral structure, and an oxidation ditch body outlet 22 is positioned at the top of the spiral structure; therefore, the sewage can flow downwards in a spiral mode under the action of gravity after entering the oxidation ditch body 2, and related equipment such as a flow impeller and the like is not needed, so that the energy consumption is reduced, and the energy conservation and emission reduction are facilitated; meanwhile, the space in the vertical direction is expanded due to the downward spiral arrangement, and the occupied area is greatly reduced under the condition of the same flow compared with that of a conventional oxidation ditch.
The cylindrical frame 1 and the oxidation ditch body 2 are made of glass fiber reinforced plastics; glass Fiber Reinforced Plastic (FRP), i.e., fiber reinforced plastic, is a composite material of unsaturated polyester, epoxy resin and phenolic resin matrix reinforced by glass fiber; compared with the traditional oxidation ditch material, the material has the advantages of good chemical stability, corrosion resistance, high and low temperature resistance, non-conductivity, light weight, high strength and the like; the oxidation ditch adopting the material also has the advantages of high strength and light weight, so that the flexibility of building and applying the oxidation ditch is greatly increased. The glass fiber reinforced plastic adopted by the embodiment is epoxy resin-based glass fiber reinforced plastic, has higher hardness and stronger strength compared with other glass fiber reinforced plastics, and is more suitable for the oxidation ditch of a vertical structure.
In the embodiment, the oxidation ditch body 2 is arranged to circle for three circles, the tracks of the oxidation ditch body in each circle are the same, and the projections of the tracks on the horizontal plane are all oval. The reason for the oval shape is that the flow of the sewage is smoother and less affected by the centrifugal force than the circular or other shapes.
The oxidation ditch body 2 is provided with a plurality of aeration heads 23 at the lower two weeks, namely the downstream of the oxidation ditch body 2. Thus, an anaerobic zone is formed upstream of the oxidation ditch body 2 and an oxygen-rich zone is formed downstream thereof. By means of the anaerobic and aerobic combined mode, organic components and oil substances in the sewage can be removed more effectively, and the purification effect and the purification efficiency of the sewage are improved.
The oxidation ditch body 2 is connected with an environment-friendly defoaming agent dosing device 3 through a pipeline so as to solve the problem that the oxidation ditch process is easy to generate foam. The environment-friendly defoaming agent adopts the caramel ester, and has no pollution to the environment.
The inner wall of the oxidation ditch body 2 is provided with a flow deflector 4; the flow deflector 4 has an arc-shaped end part and dumps towards the direction of sewage flow direction, so that sewage flows forwards more smoothly, the treatment process is facilitated to be carried out smoothly, and the efficiency of sewage treatment is positively influenced.
The oxidation ditch body 2 is provided with a heating device 5, and the temperature of the sewage in the oxidation ditch body 2 is controlled to be 27-32 ℃, so that the biochemical reaction of the sewage is facilitated; not only can improve the efficiency of biochemical reaction, but also can improve the degree of biochemical reaction. Meanwhile, the oxidation ditch body 2 is of a closed structure, so that an anaerobic environment can be ensured, and the leakage of sewage and smell can be prevented.
In light of the foregoing, it is to be understood that various changes and modifications may be made by those skilled in the art without departing from the spirit and scope of the invention. The technical scope of the present invention is not limited to the content of the specification, and must be determined according to the scope of the claims.

Claims (8)

1. A vertical oxidation ditch is characterized in that: the oxidation ditch comprises a cylindrical frame and an oxidation ditch body arranged in the frame, wherein the oxidation ditch body is designed into a structure which is spirally downward and closed; a plurality of aeration heads are arranged at the downstream of the oxidation ditch body; and the inner wall of the oxidation ditch body is provided with a flow deflector.
2. The vertical oxidation ditch of claim 1, wherein: the cylindrical frame and the oxidation ditch body are made of glass fiber reinforced plastics.
3. The vertical oxidation ditch of claim 2, wherein: the glass fiber reinforced plastic is epoxy resin-based glass fiber reinforced plastic.
4. The vertical oxidation ditch of claim 1, wherein: the oxidation ditch body is arranged to be coiled for three circles, the tracks of every circle are the same, and the projections of the tracks on the horizontal plane are all oval.
5. The vertical oxidation ditch of claim 1, wherein: the oxidation ditch body is connected with an environment-friendly defoaming agent dosing device through a pipeline.
6. The vertical oxidation ditch of claim 5, wherein: the environment-friendly defoaming agent is caramel ester.
7. The vertical oxidation ditch of claim 1, wherein: the inlet of the oxidation ditch body is positioned at the top of the spiral structure, and the outlet of the oxidation ditch body is positioned at the bottom of the spiral structure.
8. The vertical oxidation ditch of claim 1, wherein: the oxidation ditch body heating device.
CN201920813112.7U 2019-05-31 2019-05-31 Vertical oxidation ditch Expired - Fee Related CN210419416U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201920813112.7U CN210419416U (en) 2019-05-31 2019-05-31 Vertical oxidation ditch

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201920813112.7U CN210419416U (en) 2019-05-31 2019-05-31 Vertical oxidation ditch

Publications (1)

Publication Number Publication Date
CN210419416U true CN210419416U (en) 2020-04-28

Family

ID=70373568

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201920813112.7U Expired - Fee Related CN210419416U (en) 2019-05-31 2019-05-31 Vertical oxidation ditch

Country Status (1)

Country Link
CN (1) CN210419416U (en)

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Date Code Title Description
GR01 Patent grant
GR01 Patent grant
CP03 Change of name, title or address
CP03 Change of name, title or address

Address after: 215200 Li Li Zhen Lu Xu Xin TA Lian Nan Lu, Wujiang District, Suzhou City, Jiangsu Province

Patentee after: Suzhou Xugong New Material Technology Co.,Ltd.

Address before: 215000 No. 3355 Linhu Avenue, FENHU Economic Development Zone, Wujiang District, Suzhou City, Jiangsu Province

Patentee before: WUJIANG CITY ZHAOSHUN FRP PRODUCTS CO.,LTD.

TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20220823

Address after: 432800 south side of North Yiheng Road, Qili Village, Dawu County Economic Development Zone, Xiaogan City, Hubei Province

Patentee after: HUBEI DINGYU ENERGY SAVING AND ENVIRONMENTAL PROTECTION TECHNOLOGY CO.,LTD.

Address before: 215200 Li Li Zhen Lu Xu Xin TA Lian Nan Lu, Wujiang District, Suzhou City, Jiangsu Province

Patentee before: Suzhou Xugong New Material Technology Co.,Ltd.

CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20200428