CN202223979U - Integrated inclined-tube settling tank - Google Patents
Integrated inclined-tube settling tank Download PDFInfo
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- CN202223979U CN202223979U CN 201120325452 CN201120325452U CN202223979U CN 202223979 U CN202223979 U CN 202223979U CN 201120325452 CN201120325452 CN 201120325452 CN 201120325452 U CN201120325452 U CN 201120325452U CN 202223979 U CN202223979 U CN 202223979U
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Abstract
The utility model relates to an integrated inclined-tube settling tank, and aims to provide the integrated inclined-tube settling tank, which integrates the functions of water distribution, coagulation, settlement, filtration and the like, so as to enhance the load impact resistance, improve the sewage disposal efficiency and ensure that the concentration of emersed suspended matters can meet the design requirements. The technical scheme adopted by the utility model is that the integrated inclined-tube settling tank comprises a tank body, as well as a water inlet pipe and a water outlet pipe which are respectively mounted at the upper parts of two opposite side walls of the tank body in the horizontal direction. The integrated inclined-tube settling tank is characterized in that two baffles are arranged in the tank body in the water flowing direction and sequentially divide the tank body into a reaction area, a separation area and a filtration area, the bottom ends of the baffles extend to the bottom of the tank and are higher than the bottom of the tank. The integrated inclined-tube settling tank is suitable for removing impurities and suspended matters in sewage.
Description
Technical field
The utility model relates to a kind of sedimentation basin, especially a kind of integrated tube settler.Be applicable to impurity and the suspension removed in the sewage.
Background technology
In mining ore dressing, boiler dusting, sandstone aggregate manual work such as produce at process, usually can produce the high-turbidity sewage that contains a large amount of suspended particulate substances.When adopting the common inclined-tube sedimentation basin to handle such sewage, for improving treatment effeciency, often need adopt the mode of ad hoc dispensing pond or pipeline dispensing to add flocculant, and be the fine particle thing of further removing in the sewage, also need behind tube settler, to increase filtering ponds.Not only floor space is big to adopt this independent mode that is provided with, and increase construction investment, and tube settler is relatively poor to the adaptive capacity that water quantity and quality changes, and in actual engineering, is difficult to guarantee that its water outlet concentration of suspension can reach designing requirement.
Summary of the invention
The technical problem that the utility model will solve is: to the problem of above-mentioned existence; Provide that a kind of to collect functions such as water distribution, coagulation, deposition and filtration be the integrated tube settler of one; Can strengthen its anti-load impact ability; Improve sewage treating efficiency, guarantee that the concentration of suspension of water outlet can reach designing requirement.
The technical scheme that the utility model adopted is: integrated tube settler; Comprise the pond body; And the level that is contained in relative two side wall upper part of pond body respectively to water inlet pipe and drainpipe it is characterized in that: along water (flow) direction two baffle plates are set in the body of pond; The pond body is divided into reaction zone, Disengagement zone and filtering area successively, and said baffle plate bottom extends at the bottom of the pond and is higher than at the bottom of the pond.
Said reaction zone top is vertically installed with drug tube and mixer.
Be provided with the perforated baffle at the bottom of the connection pool in the said Disengagement zone, evenly arrange some circular holes on this perforated baffle.
Said filtering area middle and lower part is the settling zone, and the top, settling zone is provided with the inclined tube filler, is the fibrous nodules filtering layer above the inclined tube filler; It above the fibrous nodules filtering layer clear water zone; The clear water zone top is the weir notch that is positioned at filtering area top, and weir notch is communicated with drainpipe, and the bottom of filtering area is the mud district.
Said fibrous nodules filtering layer is pricked knot by filament and is formed the about 200 ~ 500mm of the thickness of filtering layer.
Said inclined tube filler below is provided with the flushing tracheae, the external high-pressure pump of this flushing tracheae one end connection pool, and said flushing TD is 50 ~ 80mm.
Said pond body bottom margin is 50 ° ~ 60 ° to the inclination angle at center.
In the said settling zone, base fabric is established sludge pipe along the pond, this sludge pipe one end extends center at the bottom of the pond, and the other end stretches out the pond body.
The beneficial effect of the utility model is: said pond body adds flocculant and mixer is set and stirs in the water inlet, make waste water fully contact, mix with medicament, has improved sedimentation effect, and utilizes the overcurrent speed of baffle plate reduction sewage, cancellation part kinetic energy; Simultaneously, the fibre-ball filtration layer is set on the inclined tube filler, makes the remaining tiny suspended particulate substance that contains in the waste water after precipitation process be able to further removal.
Therefore, it is one that the utility model can collect functions such as water distribution, coagulation, deposition and filtration, and the effect and the effect in many ponds played in a pond, and floor space is little, has reduced construction investment, and has improved the adaptive capacity that sewage treating efficiency and sedimentation basin change water quantity and quality.
Description of drawings
Fig. 1 is the structural plan of the utility model.
The specific embodiment
As shown in Figure 1, present embodiment comprises pond body 1, and body 1 relative two side wall upper part levels are to arranging water inlet pipe 2 and drainpipe 3 in the pond.The pond body is infundibulate at the bottom of 1 pond, and pond body bottom margin is 50 ° ~ 60 ° to the inclination angle at center.Along water (flow) direction two baffle plates 4 are set in the said pond body 1, pond body 1 is divided into reaction zone 5, Disengagement zone 6 and filtering area successively.Baffle plate 4 extends at the bottom of pond body 1 pond and does not contact with at the bottom of the pond, and sewage can circulate from baffle plate 4 belows.
Said reaction zone 5 tops are vertically installed with drug tube 9 and mixer 10.
Said Disengagement zone 6 is built-in with perforated baffle 11, at the bottom of this perforated baffle connection pool, evenly has some circular hole 11-1 on it.Sewage can circulate from the top of perforated baffle 11 and circular hole 11-1, and perforated baffle plays and stops and the energy dissipating effect.
Said filtering area accounts for about half of pond body 1, and the middle and lower part of this filtering area is settling zone 7, and 7 tops, said settling zone are provided with inclined tube filler 12, fibrous nodules filtering layer 14, clear water zone 15 and weir notch 16 successively, and said drainpipe 3 is connected with weir notch 16.Below inclined tube filler 12, be provided with flushing tracheae 17, the high-pressure pump outside the flushing tracheae 17 1 end connection pool bodies 1, this flushing tracheae 17 can regularly wash inclined tube filler 12 and fibrous nodules filtering layer 14, avoids occurring stopping up.The bottom of filtering area is mud district 8.
Filtering area bottom is provided with sludge pipe 13, and these sludge pipe 13 1 ends feed mud district 8 (be pond at the bottom of center), and the other end stretches out pond body 1.
The processing mode of the utility model is: sewage gets in the reaction zone 5 from water inlet pipe 2, and sewage fully contacts, mixes with flocculant under the effect of mixer 10.The sewage that flows out from reaction zone 5 bottoms gets into Disengagement zone 6, and overcurrent speed decreases under perforated baffle 11 barrier effects, and cancellation part kinetic energy, part suspended particulate are able to remove.7 tops, settling zone are provided with inclined tube filler 12, utilize the different of water and particle speed difference, and suspended particulate begins from sewage, to separate, and get into mud district 8, and external through sludge pipe 13 discharge ponds.Fibrous nodules filtering layer 14 is arranged at the top of inclined tube filler 12, through effects such as interception, absorption, sievings fine particle remaining in the waste water is further removed.Water in clear water zone 15 reach a certain height, and is discharged by drainpipe 3 through weir notch 16.
Claims (8)
1. integrated tube settler; Comprise pond body (1); And the level that is contained in relative two side wall upper part of pond body (1) respectively to water inlet pipe (2) and drainpipe (3); It is characterized in that: along water (flow) direction two baffle plates (4) are set in the pond body (1), pond body (1) is divided into reaction zone (5), Disengagement zone (6) and filtering area successively, said baffle plate (4) bottom extends at the bottom of the pond and is higher than at the bottom of the pond.
2. integrated tube settler according to claim 1 is characterized in that: said reaction zone (5) top is vertically installed with drug tube (9) and mixer (10).
3. integrated tube settler according to claim 1 is characterized in that: be provided with the perforated baffle (11) at the bottom of the connection pool in said Disengagement zone (6), evenly arrange some circular holes (11-1) on this perforated baffle.
4. integrated tube settler according to claim 1; It is characterized in that: said filtering area middle and lower part is settling zone (7), and the top, settling zone is provided with inclined tube filler (12), is fibrous nodules filtering layer (14) above the inclined tube filler (12); Above the fibrous nodules filtering layer (14) is clear water zone (15); The clear water zone top is the weir notch (16) that is positioned at filtering area top, and weir notch is communicated with drainpipe (3), and the bottom of filtering area is mud district (8).
5. a kind of integrated tube settler according to claim 4 is characterized in that: said fibrous nodules filtering layer (14) is pricked knot by filament and is formed the about 200 ~ 500mm of the thickness of filtering layer.
6. integrated tube settler according to claim 4; It is characterized in that: said inclined tube filler (12) below is provided with flushing tracheae (17); The outer high-pressure pump of this flushing tracheae one end connection pool body (1), said flushing tracheae (17) diameter is 50 ~ 80mm.
7. integrated tube settler according to claim 1 is characterized in that: said pond body (1) bottom margin is 50 ° ~ 60 ° to the inclination angle at center.
8. integrated tube settler according to claim 4 is characterized in that: in said settling zone (7), base fabric is established sludge pipe (13) along the pond, this sludge pipe one end extends center at the bottom of the pond, and the other end stretches out pond body (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201120325452 CN202223979U (en) | 2011-09-01 | 2011-09-01 | Integrated inclined-tube settling tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201120325452 CN202223979U (en) | 2011-09-01 | 2011-09-01 | Integrated inclined-tube settling tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202223979U true CN202223979U (en) | 2012-05-23 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201120325452 Expired - Lifetime CN202223979U (en) | 2011-09-01 | 2011-09-01 | Integrated inclined-tube settling tank |
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| CN (1) | CN202223979U (en) |
Cited By (19)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103285661A (en) * | 2013-06-18 | 2013-09-11 | 浙江大学 | Solid-liquid separation device for waste water suspended matters |
| CN103432819A (en) * | 2013-09-04 | 2013-12-11 | 大连力达环境工程有限公司 | Upward-flow-direction filtering tank connected with common water treatment device |
| CN104355478A (en) * | 2014-10-14 | 2015-02-18 | 浙江钱江纺织印染有限公司 | Printing and dyeing sewage treatment system |
| CN104628229A (en) * | 2015-02-05 | 2015-05-20 | 四川立新瑞德水处理有限责任公司 | Deep chemical wastewater treatment system and process |
| CN104857769A (en) * | 2014-02-26 | 2015-08-26 | 上海清浥环保科技有限公司 | Light filter material combined suspension tank |
| CN105233566A (en) * | 2015-10-22 | 2016-01-13 | 安尼康（福建）环保设备有限公司 | Flocculation concentration device with grille structure bodies and filtrate recycling tank with grille structure bodies |
| CN105461180A (en) * | 2016-01-12 | 2016-04-06 | 浙江大学 | Water quality purification integrated device and method for eutrophic water |
| CN105771337A (en) * | 2015-12-28 | 2016-07-20 | 张春辉 | High-efficiency solid-liquid separation device and application thereof |
| CN105999842A (en) * | 2016-07-21 | 2016-10-12 | 江苏展宏环保科技有限公司 | Coal wastewater purifier |
| CN106242170A (en) * | 2016-08-23 | 2016-12-21 | 徐州工程学院 | A kind of integrated flocculation sediment equipment being applicable to micro-pollution algae removal |
| CN107050953A (en) * | 2016-12-12 | 2017-08-18 | 东莞市鸿捷环保科技有限公司 | Intellectuality backwash filter tank and its back-flushing method |
| CN107129077A (en) * | 2017-07-11 | 2017-09-05 | 佛山市银禾企业管理咨询有限公司 | A kind of process for treating industrial waste water |
| CN107754446A (en) * | 2017-11-01 | 2018-03-06 | 安徽舜禹水务股份有限公司 | A kind of sedimentation basin and filtering ponds compound sewage processing unit |
| CN109179813A (en) * | 2018-11-13 | 2019-01-11 | 安徽理工大学 | A kind of filtering settling pond |
| CN109467174A (en) * | 2018-12-25 | 2019-03-15 | 欧基（上海）环保科技有限公司 | A kind of gas return-air washes inclined plate inclined tube-type settler |
| CN113443741A (en) * | 2021-07-01 | 2021-09-28 | 重庆市梁平排水有限公司 | Follow-on high-density pond |
| CN113622994A (en) * | 2021-08-17 | 2021-11-09 | 安徽理工大学 | Drainage device for mining industry |
| CN113695077A (en) * | 2020-05-22 | 2021-11-26 | 中国科学院青海盐湖研究所 | Filtering tank for removing magnetic impurities from fluid and filtering method thereof |
| CN113979605A (en) * | 2021-11-30 | 2022-01-28 | 产学研(广州)环境服务有限公司 | High-efficient preprocessing device of pharmacy waste water |
-
2011
- 2011-09-01 CN CN 201120325452 patent/CN202223979U/en not_active Expired - Lifetime
Cited By (23)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103285661B (en) * | 2013-06-18 | 2015-12-09 | 浙江大学 | The equipment for separating liquid from solid of waste water suspension |
| CN103285661A (en) * | 2013-06-18 | 2013-09-11 | 浙江大学 | Solid-liquid separation device for waste water suspended matters |
| CN103432819A (en) * | 2013-09-04 | 2013-12-11 | 大连力达环境工程有限公司 | Upward-flow-direction filtering tank connected with common water treatment device |
| CN104857769A (en) * | 2014-02-26 | 2015-08-26 | 上海清浥环保科技有限公司 | Light filter material combined suspension tank |
| CN104355478A (en) * | 2014-10-14 | 2015-02-18 | 浙江钱江纺织印染有限公司 | Printing and dyeing sewage treatment system |
| CN104355478B (en) * | 2014-10-14 | 2016-07-13 | 浙江钱江纺织印染有限公司 | A kind of dyeing and printing sewage processes system |
| CN104628229A (en) * | 2015-02-05 | 2015-05-20 | 四川立新瑞德水处理有限责任公司 | Deep chemical wastewater treatment system and process |
| CN105233566A (en) * | 2015-10-22 | 2016-01-13 | 安尼康（福建）环保设备有限公司 | Flocculation concentration device with grille structure bodies and filtrate recycling tank with grille structure bodies |
| CN105771337B (en) * | 2015-12-28 | 2018-01-30 | 张春辉 | A kind of efficient equipment for separating liquid from solid and its application |
| CN105771337A (en) * | 2015-12-28 | 2016-07-20 | 张春辉 | High-efficiency solid-liquid separation device and application thereof |
| CN105461180A (en) * | 2016-01-12 | 2016-04-06 | 浙江大学 | Water quality purification integrated device and method for eutrophic water |
| CN105999842A (en) * | 2016-07-21 | 2016-10-12 | 江苏展宏环保科技有限公司 | Coal wastewater purifier |
| CN106242170A (en) * | 2016-08-23 | 2016-12-21 | 徐州工程学院 | A kind of integrated flocculation sediment equipment being applicable to micro-pollution algae removal |
| CN107050953A (en) * | 2016-12-12 | 2017-08-18 | 东莞市鸿捷环保科技有限公司 | Intellectuality backwash filter tank and its back-flushing method |
| CN107129077A (en) * | 2017-07-11 | 2017-09-05 | 佛山市银禾企业管理咨询有限公司 | A kind of process for treating industrial waste water |
| CN107754446A (en) * | 2017-11-01 | 2018-03-06 | 安徽舜禹水务股份有限公司 | A kind of sedimentation basin and filtering ponds compound sewage processing unit |
| CN109179813A (en) * | 2018-11-13 | 2019-01-11 | 安徽理工大学 | A kind of filtering settling pond |
| CN109467174A (en) * | 2018-12-25 | 2019-03-15 | 欧基（上海）环保科技有限公司 | A kind of gas return-air washes inclined plate inclined tube-type settler |
| CN113695077A (en) * | 2020-05-22 | 2021-11-26 | 中国科学院青海盐湖研究所 | Filtering tank for removing magnetic impurities from fluid and filtering method thereof |
| CN113443741A (en) * | 2021-07-01 | 2021-09-28 | 重庆市梁平排水有限公司 | Follow-on high-density pond |
| CN113443741B (en) * | 2021-07-01 | 2023-09-12 | 重庆市梁平排水有限公司 | Improved high-density pool |
| CN113622994A (en) * | 2021-08-17 | 2021-11-09 | 安徽理工大学 | Drainage device for mining industry |
| CN113979605A (en) * | 2021-11-30 | 2022-01-28 | 产学研(广州)环境服务有限公司 | High-efficient preprocessing device of pharmacy waste water |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20120523 |
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| CX01 | Expiry of patent term |