CN202951301U - Rotational flow clearing reactor - Google Patents
Rotational flow clearing reactor Download PDFInfo
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- CN202951301U CN202951301U CN 201220688842 CN201220688842U CN202951301U CN 202951301 U CN202951301 U CN 202951301U CN 201220688842 CN201220688842 CN 201220688842 CN 201220688842 U CN201220688842 U CN 201220688842U CN 202951301 U CN202951301 U CN 202951301U
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- cylinder
- rotational flow
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Abstract
The utility model relates to a rotational flow clearing reactor which comprises a cylinder body (1), wherein the top end of the cylinder body is of an open structure, a water outlet pipe (5) is arranged at the upper end of the cylinder body, an overflow cylinder (3) the top end of which is of a sawtooth structure is arranged inside the cylinder body, a flanging (10) welded together with the cylinder body is arranged at the bottom end of the overflow cylinder and is positioned at the lower end of the water outlet pipe, at least three support pipes (6) vertical to the cylinder body are arranged at the inner wall of the cylinder body, a rotational flow pipe (4) is arranged at the axle wire of the cylinder body and is fixed by the support pipes, a water inlet pipe (2) is arranged at the lower end of the water outlet pipe and is communicated with the rotational flow pipe tangently after penetrating through the cylinder body, support legs (8) are arranged at the lower end of the cylinder body, the bottom end of the cylinder body is connected with a cylinder bottom, and a blowdown pipe (9) is connected to the bottom end of the cylinder bottom. The rotational flow clearing reactor provided by the utility model is smaller in size, convenient to install and maintain and higher in clearing speed, and is used for carrying out rapid solid-liquid separation on wastewater containing high-suspended solids through a rotational flow centrifugal function.
Description
Technical field
The utility model relates to water-treatment technology field, particularly a kind of cyclone clarification reactor.
Background technology
The method of utilizing tube settler to carry out water treatment is a kind of method commonly used in the Treatment of Industrial Water technology.Tube settler is parallel pipe or the parallel-plate that inclination is set in the precipitation zone of flat flow or vertical sedimentation basin, utilize the parallel pipe or the parallel-plate that tilt that precipitation zone is divided into to a series of shallow layer precipitating layers, the impurity of the water in waste water and processed or sedimentation or heavy mud mutually move and separate in each beds of precipitation.Tube settler realizes that the separating rate of water and impurity is not high, by the volume that increases each beds of precipitation, can improve separating rate, but the structure of corresponding tube settler also increases.In addition, inclined tube is also inconvenient in the installation of precipitation zone.
The utility model content
The purpose of this utility model is: the slow-footed deficiency of utilizing tube settler to carry out water treatment existed for prior art, a kind of cyclone clarification reactor is provided, and utilize the eddy flow centrifugal principle to realize the quick Separation of Solid and Liquid to high suspended matter waste water.
To achieve these goals, the technical solution adopted in the utility model is:
A kind of cyclone clarification reactor, comprise the cylindrical shell that top is unenclosed construction, the upper end of described cylindrical shell is provided with outlet pipe, inner barrel is provided with the overflow cylinder that top is broached-tooth design, the bottom of described overflow cylinder is provided with the flanging with barrel soldering, described flanging and barrel soldering and be positioned at the lower end of outlet pipe, cylinder inboard wall is provided with at least 3 stay pipes perpendicular to cylindrical shell, the position, axis of cylindrical shell is provided with cyclone pipe, described cyclone pipe is fixed by described stay pipe, the lower end of outlet pipe is provided with water inlet pipe, described water inlet pipe is communicated with the cyclone pipe tangent line through after cylindrical shell, the lower end of cylindrical shell is provided with supporting leg, at the bottom of the bottom of cylindrical shell is connected with tin, the bottom at the described cylinder end is connected with blow-off pipe.
Preferably, the described cylinder end and cylindrical shell connect as one.
Preferably, the described cylinder end is shaped as taper shape or square taper.
In sum, owing to having adopted technique scheme, the beneficial effects of the utility model are: the new cyclone clarification reactor of this practicality, by the eddy flow centrifugal action, realize the quick Separation of Solid and Liquid to high suspended matter waste water, with tube settler, compare, clarifying speed is faster, its settling time is approximately half of tube settler of equal volume, and volume is less, is convenient to I&M.
The accompanying drawing explanation
Fig. 1 is structural representation.
Fig. 2 is top view of the present utility model.
Fig. 3 is the structural representation of overflow cylinder.
Mark in figure: the 1-cylindrical shell, the 2-water inlet pipe, the 3-overflow cylinder, the 4-cyclone pipe, the 5-outlet pipe, the 6-stay pipe, at the bottom of the 7-conically shaped, 8-supporting leg, 9-blow-off pipe, 10-flanging.
The specific embodiment
Below in conjunction with accompanying drawing, the utility model is described in detail.
In order to make the purpose of this utility model, technical scheme and advantage clearer, below in conjunction with drawings and Examples, the utility model is further elaborated.Should be appreciated that specific embodiment described herein is only in order to explain the utility model, and be not used in restriction the utility model.
With reference to figure 1, Fig. 2, Fig. 3, a kind of cyclone clarification reactor that the present embodiment is enumerated, comprise cylindrical shell 1, it is circular or square that the shape of cylindrical shell 1 can be, the upper end of cylindrical shell 1 is unenclosed construction, at the bottom of the lower end of cylindrical shell 1 is connected with conically shaped 7 and conically shaped at the bottom of 7 with cylindrical shell 1, connect as one, at the bottom of conically shaped, 7 is conical or square taper, at the bottom of conically shaped, 7 bottom is connected with blow-off pipe 9, and the lower end of cylindrical shell 1 is provided with supporting leg 8, for supporting cylindrical shell 1.The top sidewall of cylindrical shell 1 is provided with outlet pipe 5, cylindrical shell 1 inside is provided with the overflow cylinder 3 that top is broached-tooth design, the bottom of described overflow cylinder 3 is provided with the flanging 10 with cylindrical shell 1 welding, described flanging 10 is positioned at the lower end of outlet pipe 5, the axis of cylindrical shell 1 is provided with cyclone pipe 4, the outer wall of cyclone pipe 4 is fixed by stay pipe 6 and cylindrical shell 1 inwall, and the quantity of stay pipe 6 is at least three, to guarantee cyclone pipe 4, remains on the axis vertical line position of cylindrical shell 1 under hydraulic blow.The lower end of outlet pipe 5 is provided with water inlet pipe 2, and water inlet pipe 2 is communicated with cyclone pipe 4 tangent lines through cylindrical shell 1 is rear.
Operation principle: the waste water that contains suspending sundries (as the high concentration suspended matter waste water after electric flocculation treatment) is under the effect of water pump and other impressed pressures, enter the rear High Rotation Speed of cyclone pipe 4 by water inlet pipe 2 with tangential direction, under the effect of centrifugal force, the solid particle foreign material are thrown to wall, and drop at the bottom of conically shaped in 7 with eddy flow, and discharge by blow-off pipe 9.Water after clarification is from the outside rising of cyclone pipe 4, entered in the overflow launder formed between overflow cylinder 3 and cylindrical shell 1 by the broached-tooth design overflow of overflow cylinder 3 upper ends, and flows out the rear dependence Action of Gravity Field of water pipe 5 outflow reactor.
Claims (3)
1. a cyclone clarification reactor, it is characterized in that, comprise the cylindrical shell (1) that top is unenclosed construction, the upper end of described cylindrical shell (1) is provided with outlet pipe (5), cylindrical shell (1) inside is provided with the overflow cylinder (3) that top is broached-tooth design, the bottom of described overflow cylinder (3) is provided with the flanging (10) with cylindrical shell (1) welding, described flanging (10) is positioned at the lower end of outlet pipe (5), cylindrical shell (1) inwall is provided with at least 3 stay pipes perpendicular to cylindrical shell (1) (6), the position, axis of cylindrical shell (1) is provided with cyclone pipe (4), described cyclone pipe (4) is fixing by described stay pipe (6), the lower end of overflow cylinder (3) is provided with water inlet pipe (2), described water inlet pipe (2) is communicated with cyclone pipe (4) tangent line through after cylindrical shell (1), the lower end of cylindrical shell (1) is provided with supporting leg (8), at the bottom of the bottom of cylindrical shell (1) is connected with tin, the bottom of described cylinder is connected with blow-off pipe (9).
2. cyclone clarification reactor according to claim 1, is characterized in that, the described cylinder end and cylindrical shell connect as one.
3. cyclone clarification reactor according to claim 1 and 2, is characterized in that, the described cylinder end be shaped as taper shape or square taper.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220688842 CN202951301U (en) | 2012-12-13 | 2012-12-13 | Rotational flow clearing reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220688842 CN202951301U (en) | 2012-12-13 | 2012-12-13 | Rotational flow clearing reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202951301U true CN202951301U (en) | 2013-05-29 |
Family
ID=48456894
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220688842 Expired - Fee Related CN202951301U (en) | 2012-12-13 | 2012-12-13 | Rotational flow clearing reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202951301U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104623934A (en) * | 2013-11-08 | 2015-05-20 | 中冶长天国际工程有限责任公司 | Pre-grading thickener |
| CN107335284A (en) * | 2017-08-29 | 2017-11-10 | 中国建筑设计院有限公司 | A kind of rubbish from cooking equipment for separating liquid from solid |
| CN109020003A (en) * | 2018-10-17 | 2018-12-18 | 成都飞创科技有限公司 | A kind of wastewater efficient flocculation clarifier |
| CN110642462A (en) * | 2019-09-24 | 2020-01-03 | 广东东荣金属制品有限公司 | Ultra-large floating body runoff separator suitable for large water body circulation culture system |
-
2012
- 2012-12-13 CN CN 201220688842 patent/CN202951301U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104623934A (en) * | 2013-11-08 | 2015-05-20 | 中冶长天国际工程有限责任公司 | Pre-grading thickener |
| CN104623934B (en) * | 2013-11-08 | 2017-02-01 | 中冶长天国际工程有限责任公司 | Pre-grading thickener |
| CN107335284A (en) * | 2017-08-29 | 2017-11-10 | 中国建筑设计院有限公司 | A kind of rubbish from cooking equipment for separating liquid from solid |
| CN107335284B (en) * | 2017-08-29 | 2023-03-31 | 中国建筑设计研究院有限公司 | Kitchen garbage solid-liquid separation device |
| CN109020003A (en) * | 2018-10-17 | 2018-12-18 | 成都飞创科技有限公司 | A kind of wastewater efficient flocculation clarifier |
| CN110642462A (en) * | 2019-09-24 | 2020-01-03 | 广东东荣金属制品有限公司 | Ultra-large floating body runoff separator suitable for large water body circulation culture system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130529 Termination date: 20151213 |
|
| EXPY | Termination of patent right or utility model |