CN204219842U - A kind of potassium permanganate composites - Google Patents
A kind of potassium permanganate composites Download PDFInfo
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- CN204219842U CN204219842U CN201420594551.0U CN201420594551U CN204219842U CN 204219842 U CN204219842 U CN 204219842U CN 201420594551 U CN201420594551 U CN 201420594551U CN 204219842 U CN204219842 U CN 204219842U
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- overfall
- district
- overflow launder
- preliminary sedimentation
- potassium permanganate
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Abstract
The utility model relates to a kind of potassium permanganate composites, belongs to sewage treatment process facility technology field.The utility model comprises coagulating district, flocculation reaction district, preliminary sedimentation district, sloping plate deposition district, preliminary sedimentation district side wall upper part is provided with overfall, overfall is provided with overflow launder, overflow launder overhead height is not less than overfall overhead height, overflow launder is fixedly connected on preliminary sedimentation district side wall upper part, overflow launder is provided with discharge pipeline, and discharge pipeline has valve.The utility model, by arranging overfall at preliminary sedimentation district sidewall, utilizes principle of overflow, floating sludge is drained into overflow launder, then enters neighbouring sludge concentration tank by discharge pipeline, thus solves the Mud up-floating problem of potassium permanganate composites, improves outlet effect.
Description
Technical field
The utility model relates to a kind of potassium permanganate composites, belongs to sewage treatment process facility technology field.
Background technology
Potassium permanganate composites be a kind of compact, efficiently, Novel sewage treatment process flexibly, every field can be widely used in, can be used for process industry and sanitary sewage, drinking water, rainwater and three grades of waste water, this new wastewater treatment method is very popular in European and American developed countries.
Potassium permanganate composites is primarily of coagulating district, flocculation reaction district, preliminary sedimentation district, sloping plate deposition district composition, and mud is discharged by bottom.But in application process, floating often appears in potassium permanganate composites mud, and especially in preliminary sedimentation district, a large amount of floating sludge is accumulated in more than the liquid level in preliminary sedimentation district, after reaching certain thickness, will affect the effect of final outflow water.
Utility model content
Technical problem to be solved in the utility model is: provide a kind of potassium permanganate composites, solves mud scum problem, improves outlet effect.
The technical scheme adopted for solving the problems of the technologies described above the utility model is: a kind of potassium permanganate composites, comprise coagulating district, flocculation reaction district, preliminary sedimentation district, sloping plate deposition district, preliminary sedimentation district side wall upper part is provided with overfall, overfall is provided with overflow launder, overflow launder overhead height is not less than overfall overhead height, overflow launder is fixedly connected on preliminary sedimentation district side wall upper part, and overflow launder is provided with discharge pipeline, and discharge pipeline has valve.
Further: overfall end face is plane, and overfall end face and preliminary sedimentation district top spacing are 500mm ~ 600mm, and overfall height is 300mm ~ 400mm.
Further: overfall length is identical with the preliminary sedimentation district side wall length of its side.
Further: overflow launder bottom surface is back taper, and overflow launder bottom center is located at by discharge pipeline, and discharge pipeline is arranged perpendicular to horizontal plane.
Further: preliminary sedimentation district is also provided with water pipe at the opposite side relative to overfall.
The beneficial effects of the utility model are: by arranging overfall at preliminary sedimentation district sidewall, utilize principle of overflow, floating sludge is drained into overflow launder, then enter neighbouring sludge concentration tank by discharge pipeline, thus solve the Mud up-floating problem of potassium permanganate composites, improve outlet effect.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Fig. 2 is top view of the present utility model.
Parts, position and numbering in figure: 1-coagulating district, 2-flocculation reaction district, 3-preliminary sedimentation district, 4-sloping plate deposition district, 31-overfall, 32-overflow launder, 33-discharge pipeline, 34-valve, 35-water pipe.
Detailed description of the invention
Below in conjunction with accompanying drawing, the utility model is described in further detail.
As shown in Figure 1 and Figure 2, the utility model comprises coagulating district 1, flocculation reaction district 2, preliminary sedimentation district 3, sloping plate deposition district 4, preliminary sedimentation district 3 side wall upper part is provided with overfall 31, overfall 31 is provided with overflow launder 32, overflow launder 32 overhead height is not less than overfall 31 overhead height, overflow launder 32 is fixedly connected on preliminary sedimentation district 3 side wall upper part, and overflow launder 32 is provided with discharge pipeline 33, and discharge pipeline 33 has valve 34.
The utility model is by arranging overfall 31 at preliminary sedimentation district 3 sidewall, utilize principle of overflow, floating sludge is drained into overflow launder 32, then enter neighbouring sludge concentration tank by discharge pipeline 33, thus solve the Mud up-floating problem of potassium permanganate composites, improve outlet effect.
As an improvement of the present utility model, overfall 31 end face is plane, and overfall 31 end face and preliminary sedimentation district 3 top spacing are 500mm ~ 600mm.During normal work, preliminary sedimentation district 3 water surface is positioned at and is about 300mm apart from top, overfall 31 end face and preliminary sedimentation district 3 top spacing are 500mm ~ 600mm, overfall 31 is highly 300mm ~ 400mm, can make, while mud scum effect is got rid of in guarantee, at utmost to utilize the sewage treatment capacity of potassium permanganate composites.Overfall 31 end face is plane, has best eliminating mud scum effect.
Improve as another item of the present utility model, overfall 31 length is identical with preliminary sedimentation district 3 side wall length of its side, flushing effect can be utilized and maximize.
Improve as another item of the present utility model, overflow launder 32 bottom surface is back taper, and overflow launder 32 bottom center is located at by discharge pipeline 33, and discharge pipeline 33 is arranged perpendicular to horizontal plane, utilizes gravity flow effect, namely has good sludge discharge effects.In addition, valve 34 is arranged near ground place on discharge pipeline 33, handled easily.
Improve as another item of the present utility model, preliminary sedimentation district 3 is also provided with water pipe 35 at the opposite side relative to overfall 31.When floating sludge mobility is poor, water pipe 35 can be opened, adopt hydraulic blow effect, the mud of floating is drained in overflow launder 32.
Claims (5)
1. a potassium permanganate composites, comprise coagulating district (1), flocculation reaction district (2), preliminary sedimentation district (3), sloping plate deposition district (4), it is characterized in that: described preliminary sedimentation district (3) side wall upper part is provided with overfall (31), described overfall (31) is provided with overflow launder (32), described overflow launder (32) overhead height is not less than described overfall (31) overhead height, described overflow launder (32) is fixedly connected on described preliminary sedimentation district (3) side wall upper part, described overflow launder (32) is provided with discharge pipeline (33), described discharge pipeline (33) has valve (34).
2. a kind of potassium permanganate composites as claimed in claim 1, it is characterized in that: described overfall (31) end face is plane, and overfall (31) end face and preliminary sedimentation district (3) top spacing are 500mm ~ 600mm, overfall (31) is highly 300mm ~ 400mm.
3. a kind of potassium permanganate composites as claimed in claim 1, is characterized in that: described overfall (31) length is identical with preliminary sedimentation district (3) side wall length of its side.
4. a kind of potassium permanganate composites as claimed in claim 1, it is characterized in that: described overflow launder (32) bottom surface is back taper, described overflow launder (32) bottom center is located at by described discharge pipeline (33), and discharge pipeline (33) is arranged perpendicular to horizontal plane.
5. a kind of potassium permanganate composites as claimed in claim 1, is characterized in that: described preliminary sedimentation district (3) is also provided with water pipe (35) at the opposite side relative to overfall (31).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420594551.0U CN204219842U (en) | 2014-10-14 | 2014-10-14 | A kind of potassium permanganate composites |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420594551.0U CN204219842U (en) | 2014-10-14 | 2014-10-14 | A kind of potassium permanganate composites |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204219842U true CN204219842U (en) | 2015-03-25 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
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| CN201420594551.0U Active CN204219842U (en) | 2014-10-14 | 2014-10-14 | A kind of potassium permanganate composites |
Country Status (1)
| Country | Link |
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| CN (1) | CN204219842U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113893608A (en) * | 2021-10-14 | 2022-01-07 | 中机国际工程设计研究院有限责任公司 | Suspension quick filter device |
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2014
- 2014-10-14 CN CN201420594551.0U patent/CN204219842U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113893608A (en) * | 2021-10-14 | 2022-01-07 | 中机国际工程设计研究院有限责任公司 | Suspension quick filter device |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |