CN203750230U - Tilted plate settling device - Google Patents
Tilted plate settling device Download PDFInfo
- Publication number
- CN203750230U CN203750230U CN201420099033.1U CN201420099033U CN203750230U CN 203750230 U CN203750230 U CN 203750230U CN 201420099033 U CN201420099033 U CN 201420099033U CN 203750230 U CN203750230 U CN 203750230U
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- Prior art keywords
- zone
- basin body
- main flow
- settling
- tilted plate
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Abstract
The utility model discloses a tilted plate settling device which comprises a settling basin body, a sludge bucket and a support frame, wherein the settling basin body consists of a coagu-flocculation reaction zone, a main flow zone, a transition zone, a tilted plate zone and a clear water zone, wherein the coagu-flocculation reaction zone is vertically positioned on the inner side of the settling basin body and communicated with the main flow zone, the transition zone is positioned above the main flow zone, the tilted plate zone is positioned above the transition zone, the clear water zone is positioned above the tilted plate zone, the sludge bucket is arranged below the main flow zone, and the support frame is arranged at the bottom of the settling tank body. According to the tilted plate settling device, the coagu-flocculation reaction zone, the main flow zone, the transition zone, the tilted plate zone and the clear water zone are arranged in the settling basin body, two partitions are arranged in the coagu-flocculation zone, so that the flowing distance of water flow can be increased, the particle settling distance can be shortened through cooperation of a plurality of areas, the settling time length can be shortened, the settling removal rate can be improved, a sawtoothed overflow weir is more easily processed compared with the common horizontal weir, and the uniform effluent water is more easily guaranteed.
Description
[technical field]
The utility model relates to the technical field of the technical field of settling vessel, particularly tilted plate separator.
[background technology]
Tube settler refers to the sedimentation basin that is provided with inclined tube in settling zone.In the settling zone of flat flow or vertical sedimentation basin, utilize the parallel pipe or the parallelpiped (sometimes can utilize honeycomb filler) that tilt to be divided into a series of shallow layer precipitating layers, processed mutually moves and separates in each precipitation shallow-layer with the heavy mud of sedimentation.Be divided into contrary (different) to stream, concurrent and three kinds of different separate modes of reverse flow according to its mutual direction of motion.Between every two inclined paralled plates, (or in parallel pipe) is equivalent to a very shallow sedimentation basin.The disposal ability of traditional inclined-plate clarifying basin is poor, particles settling distance, and the sedimentation time is long, and precipitation clearance has much room for improvement.
[utility model content]
The purpose of this utility model solves the problems of the prior art exactly, proposes a kind of tilted plate separator, can reduce particles settling distance, shortens the sedimentation time long, improves precipitation clearance.
For achieving the above object, the utility model proposes a kind of tilted plate separator, comprise sedimentation basin body, sludge bucket and bracing frame, described sedimentation basin body comprises coagulating district, main flow area, transition region, swash plate district, clear water zone, described coagulating district is vertically positioned at the inner side of sedimentation basin body, coagulating district is connected with main flow area, transition region is positioned at the top of main flow area, swash plate district is positioned at the top of transition region, clear water zone is positioned at the top in swash plate district, described sludge bucket is installed on the below of main flow area, and bracing frame is installed on the bottom of sedimentation basin body.
As preferably, described coagulating is provided with the first dividing plate and second partition in district, inner side, the upper end fixed installation of described the first dividing plate and sedimentation basin body, and the inner side, lower end of described second partition and sedimentation basin body fixedly mounts.
As preferably, the inclined tube of some equidistant distributions is installed in described swash plate district, the angle of inclination of inclined tube is 45 °, and the length of inclined tube is 1 meter, and the distance between two inclined tubes is 5cm.
As preferably, the top of described clear water zone is provided with zigzag downflow weir.
As preferably, the bottom of described sludge bucket is provided with delivery port.
The beneficial effects of the utility model: the utility model by arranging coagulating district, main flow area, transition region, swash plate district and clear water zone in sedimentation basin body, and in coagulating district, be provided with two dividing plates, increase the mobile distance of current, the common cooperation in multiple regions can reduce particles settling distance, shorten the sedimentation time long, improve precipitation clearance, zigzag downflow weir is more easily processed and is also more easily ensured that water outlet is even than common horizontal weir.
Feature of the present utility model and advantage will be elaborated by reference to the accompanying drawings by embodiment.
[brief description of the drawings]
Fig. 1 is the main TV structure schematic diagram of a kind of tilted plate separator of the utility model.
[detailed description of the invention]
Consult Fig. 1, a kind of tilted plate separator of the utility model, comprise sedimentation basin body 1, sludge bucket 2 and bracing frame 3, described sedimentation basin body 1 comprises coagulating district 11, main flow area 12, transition region 13, swash plate district 14, clear water zone 15, described coagulating district 11 is vertically positioned at the inner side of sedimentation basin body 1, coagulating district 11 is connected with main flow area 12, transition region 13 is positioned at the top of main flow area 12, swash plate district 14 is positioned at the top of transition region 13, clear water zone 15 is positioned at the top in swash plate district 14, described sludge bucket 2 is installed on the below of main flow area 12, bracing frame 3 is installed on the bottom of sedimentation basin body 1, the first dividing plate 111 and second partition 112 are installed in described coagulating district 11, described the first dividing plate 111 fixedly mounts with the inner side, upper end of sedimentation basin body 1, described second partition 112 fixedly mounts with the inner side, lower end of sedimentation basin body 1, the inclined tube 141 of some equidistant distributions is installed in described swash plate district 14, the angle of inclination of inclined tube 141 is 45 °, the length of inclined tube 141 is 1 meter, distance between two inclined tubes 141 is 5cm, the top of described clear water zone 15 is provided with zigzag downflow weir 16, the bottom of described sludge bucket 2 is provided with delivery port 21.
The utility model course of work:
A kind of tilted plate separator of the utility model in the course of the work, by in the interior coagulating district 11 that arranges of sedimentation basin body 1, main flow area 12, transition region 13, swash plate district 14 and clear water zone 15, and in coagulating district 11, be provided with two dividing plates, increase the mobile distance of current, the Main Function in coagulating district 11 is to pass through PAC, the effect of PAM is by the substance trapping that is difficult to sedimentation tiny in waste water, make it to become the alumen ustum compared with free settling, main flow area 12 is positioned at the flow region of sedimentation basin body 1 bottom, its Main Function is that transmission mixed liquor to be separated enters swash plate district 14, mud after precipitation enters again sludge bucket 2 from here, the effect of transition region 13 is energy dissipatings and adjusts fluidised form, prevent from turning on mud, ensure solid-liquid separation effect, simultaneously, it also has even water inlet and as functions such as sludge reflux passages, play a part transmitted in both directions, the common cooperation in multiple regions can reduce particles settling distance, shorten the sedimentation time long, improve precipitation clearance, zigzag downflow weir 16 is more easily processed and is also more easily ensured that water outlet is even than common horizontal weir.
Above-described embodiment is to explanation of the present utility model, is not to restriction of the present utility model, any scheme after the utility model simple transformation is all belonged to protection domain of the present utility model.
Claims (5)
1. a tilted plate separator, it is characterized in that: comprise sedimentation basin body (1), sludge bucket (2) and bracing frame (3), described sedimentation basin body (1) comprises coagulating district (11), main flow area (12), transition region (13), swash plate district (14), clear water zone (15), described coagulating district (11) is vertically positioned at the inner side of sedimentation basin body (1), coagulating district (11) is connected with main flow area (12), transition region (13) is positioned at the top of main flow area (12), swash plate district (14) is positioned at the top of transition region (13), clear water zone (15) is positioned at the top of swash plate district (14), described sludge bucket (2) is installed on the below of main flow area (12), bracing frame (3) is installed on the bottom of sedimentation basin body (1).
2. a kind of tilted plate separator as claimed in claim 1, it is characterized in that: the first dividing plate (111) and second partition (112) are installed in described coagulating district (11), described the first dividing plate (111) fixedly mounts with the inner side, upper end of sedimentation basin body (1), inner side, the lower end fixed installation of described second partition (112) and sedimentation basin body (1).
3. a kind of tilted plate separator as claimed in claim 1, it is characterized in that: the inclined tube (141) that some equidistant distributions are installed in described swash plate district (14), the angle of inclination of inclined tube (141) is 45 °, the length of inclined tube (141) is 1 meter, and the distance between two inclined tubes (141) is 5cm.
4. a kind of tilted plate separator as claimed in claim 1, is characterized in that: the top of described clear water zone (15) is provided with zigzag downflow weir (16).
5. a kind of tilted plate separator as described in any one in claim 1 to 4, is characterized in that: the bottom of described sludge bucket (2) is provided with delivery port (21).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420099033.1U CN203750230U (en) | 2014-03-05 | 2014-03-05 | Tilted plate settling device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420099033.1U CN203750230U (en) | 2014-03-05 | 2014-03-05 | Tilted plate settling device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203750230U true CN203750230U (en) | 2014-08-06 |
Family
ID=51245541
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420099033.1U Expired - Fee Related CN203750230U (en) | 2014-03-05 | 2014-03-05 | Tilted plate settling device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203750230U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105169764A (en) * | 2015-10-14 | 2015-12-23 | 攀钢集团成都钢钒有限公司 | Oil-containing sewage treatment device |
| CN107321009A (en) * | 2017-08-04 | 2017-11-07 | 南京河海环境研究院有限公司 | A kind of tube settler pond |
| CN112390426A (en) * | 2020-10-09 | 2021-02-23 | 武汉泾渭环境科技有限公司 | Landfill leachate ammonia nitrogen removal method |
-
2014
- 2014-03-05 CN CN201420099033.1U patent/CN203750230U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105169764A (en) * | 2015-10-14 | 2015-12-23 | 攀钢集团成都钢钒有限公司 | Oil-containing sewage treatment device |
| CN107321009A (en) * | 2017-08-04 | 2017-11-07 | 南京河海环境研究院有限公司 | A kind of tube settler pond |
| CN112390426A (en) * | 2020-10-09 | 2021-02-23 | 武汉泾渭环境科技有限公司 | Landfill leachate ammonia nitrogen removal method |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140806 |