CN204952365U - A subsider for water treatment solid -liquid separation - Google Patents
A subsider for water treatment solid -liquid separation Download PDFInfo
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- CN204952365U CN204952365U CN201520545176.5U CN201520545176U CN204952365U CN 204952365 U CN204952365 U CN 204952365U CN 201520545176 U CN201520545176 U CN 201520545176U CN 204952365 U CN204952365 U CN 204952365U
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Abstract
本装置所述箱体从进水口到出水口依次设有搅拌区、沉降区和污泥室,所述箱体的进水口设置在搅拌区的上方,搅拌区内设有搅拌装置的搅拌部件,所述沉降区通过水平设置的多孔隔板和支撑板分隔为上区、中区和下区,所述上区、中区和下区垂直排列,所述上区内排列有斜板或斜管作为沉降加速装置,所述斜板或斜管固定在支撑板上方,所述搅拌区的出口与沉降区的下区入口连接,所述沉降区的中区通过溢流口与污泥室连通,所述沉降区的上区与污泥室连通,所述箱体在污泥室的上方的侧壁上设有箱体的出水口,所述箱体在污泥室的底部的侧壁上设有污泥室排泥口。本实用新型结构紧凑,提高水中悬浮物的沉降性能、降低出水中悬浮物。
The box body of this device is provided with a stirring area, a settling area and a sludge chamber in sequence from the water inlet to the water outlet. The settling zone is divided into an upper zone, a middle zone and a lower zone by horizontally arranged porous partitions and support plates, the upper zone, the middle zone and the lower zone are vertically arranged, and inclined plates or inclined tubes are arranged in the upper zone As a settling acceleration device, the inclined plate or inclined tube is fixed above the support plate, the outlet of the stirring zone is connected to the entrance of the lower zone of the settling zone, and the middle zone of the settling zone communicates with the sludge chamber through the overflow port, The upper area of the settling area communicates with the sludge chamber, and the box is provided with a water outlet on the side wall above the sludge chamber, and the box is provided with a water outlet on the side wall at the bottom of the sludge chamber. There is a sludge discharge port in the sludge chamber. The utility model has a compact structure, improves the settling performance of the suspended matter in the water, and reduces the suspended matter in the effluent.
Description
技术领域 technical field
本实用新型涉及一种用于水处理固液分离的沉降槽。 The utility model relates to a settling tank used for solid-liquid separation in water treatment.
背景技术 Background technique
带有斜板或斜管的沉淀设备是给水排水处理中广泛用于固液分离的设备,利用浅层沉降原理,将水中比重比水大的悬浮物分离出来,从而使水的浊度降低,具有结构简单,无易损件,经久耐用,维护简单的优点。但对于某些水质或由于水中悬浮物的絮凝性能不好,导致水中的悬浮物很细小,或悬浮物絮体疏松比重小,则在斜板或斜管沉淀区分离时,由于悬浮物沉淀速度很慢,以致于悬浮物分离不干净,导致出水浊度较高。 Sedimentation equipment with inclined plates or inclined tubes is widely used for solid-liquid separation in water supply and drainage treatment. It uses the principle of shallow sedimentation to separate suspended solids in water whose specific gravity is larger than that of water, thereby reducing the turbidity of water. It has the advantages of simple structure, no wearing parts, durable and easy maintenance. However, for some water quality or due to the poor flocculation performance of suspended solids in water, the suspended solids in water are very small, or the loose specific gravity of suspended solid flocs is small. Very slow, so that the suspended solids are not separated cleanly, resulting in high turbidity of the effluent.
实用新型内容 Utility model content
本实用新型的目的在于克服现有技术的不足而提供一种结构紧凑,提高水中悬浮物的沉降性能、降低出水中悬浮物的用于水处理固液分离的沉降槽。 The purpose of the utility model is to overcome the deficiencies of the prior art and provide a settling tank for solid-liquid separation of water treatment which has a compact structure, improves the settling performance of suspended matter in water, and reduces suspended matter in effluent water.
为了实现上述目的,本实用新型所采用的技术方案是: In order to achieve the above object, the technical solution adopted in the utility model is:
一种用于水处理固液分离的沉降槽,包括箱体,所述箱体从进水口到出水口依次设有搅拌区、沉降区和污泥室,所述箱体的进水口设置在搅拌区的上方,搅拌区内设有搅拌装置的搅拌部件,所述沉降区通过水平设置的多孔隔板和支撑板分隔为上区、中区和下区,所述上区、中区和下区垂直排列,所述上区内排列有斜板或斜管作为沉降加速装置,所述斜板或斜管固定在支撑板上方,所述搅拌区的出口与沉降区的下区入口连接,所述沉降区的中区通过溢流口与污泥室连通,所述沉降区的上区与污泥室连通,所述箱体在污泥室的上方的侧壁上设有箱体的出水口,所述箱体在污泥室的底部的侧壁上设有污泥室排泥口,所述箱体在沉降区的底部设有沉降区排泥口。 A settling tank for solid-liquid separation in water treatment, comprising a box, the box is sequentially provided with a stirring zone, a settling zone and a sludge chamber from a water inlet to a water outlet, and the water inlet of the box is set at the stirring Above the zone, the stirring part of the stirring device is arranged in the stirring zone, and the settling zone is divided into an upper zone, a middle zone and a lower zone by a horizontally arranged porous partition and a support plate, and the upper zone, the middle zone and the lower zone Arranged vertically, the upper area is arranged with inclined plates or inclined tubes as a settling acceleration device, the inclined plates or inclined tubes are fixed above the support plate, the outlet of the stirring area is connected with the entrance of the lower area of the settling area, and the The middle area of the settling area communicates with the sludge chamber through the overflow port, the upper area of the settling area communicates with the sludge chamber, and the box body is provided with a water outlet of the box body on the side wall above the sludge room, The box body is provided with a sludge chamber sludge outlet on the side wall of the bottom of the sludge chamber, and the box body is provided with a sedimentation area mud outlet at the bottom of the sedimentation area.
所述多孔隔板上布满透水孔,所述透水孔的直径为5-20mm。 The porous separator is covered with permeable holes, and the diameter of the permeable holes is 5-20mm.
所述搅拌区和沉降区的下区形成“L”形。 The stirring zone and the lower zone of the settling zone form an "L" shape.
所述搅拌区上设有絮凝剂投放口。 The stirring area is provided with a flocculant feeding port.
由于采用上述方案,本实用新型通过设置在沉降区的多孔隔板,污水通过搅拌装置的搅拌后进入斜板或斜管需要穿过多孔隔板,而由于在投放絮凝剂后,多孔隔板上就会积聚有大量的污泥,形成污泥床,因此含有悬浮物的水穿过污泥床时,由于同相絮凝的作用,高浓度的污泥床迅速加快了进水中是悬浮颗粒的凝聚速度,同时也由于微粒捕获的作用,将水中细小的颗粒物聚集到了大絮团了。这样,当颗粒物穿过污泥床后,所有的颗粒物都变大了,这样,水中的悬浮物的沉淀速度变大了,有利于在后续斜板或斜管上的沉降,将大大降低出水中悬浮物的含量,使得出水更加清澈,由于大大提高了水中悬浮物的沉降性能,斜板或斜管沉淀的占地面积将大为减少,设备也更加紧凑。 Due to the adoption of the above scheme, the utility model uses the porous partition arranged in the settlement area. After the sewage is stirred by the stirring device, it needs to pass through the porous partition when it enters the inclined plate or the inclined pipe. A large amount of sludge will accumulate to form a sludge bed. Therefore, when water containing suspended matter passes through the sludge bed, due to the same-phase flocculation, the high-concentration sludge bed quickly accelerates the agglomeration of suspended particles in the influent. At the same time, due to the effect of particle capture, the fine particles in the water are gathered into large flocs. In this way, when the particles pass through the sludge bed, all the particles become larger, so that the sedimentation velocity of the suspended solids in the water becomes larger, which is conducive to the settlement on the subsequent inclined plate or inclined tube, which will greatly reduce the amount of water in the effluent. The content of suspended solids makes the effluent clearer. Since the settling performance of suspended solids in water is greatly improved, the occupied area of inclined plate or inclined tube sedimentation will be greatly reduced, and the equipment will be more compact.
附图说明 Description of drawings
图1为本实用新型的结构示意图。 Fig. 1 is the structural representation of the utility model.
图2为本实用新型的俯视图。 Fig. 2 is a top view of the utility model.
图中,1、进水口;2、搅拌装置;3、多孔隔板;4、斜板或斜管;5、支撑板;6、溢流口;7、出水口;8、污泥室排泥口;9、沉降区排泥口;10、箱体;11、透水孔。 In the figure, 1. Water inlet; 2. Stirring device; 3. Porous partition; 4. Inclined plate or inclined pipe; 5. Support plate; 6. Overflow port; 7. Water outlet; 8. Sludge chamber discharge Mouth; 9, sedimentation zone mud outlet; 10, box; 11, permeable hole.
具体实施方式 detailed description
下面结合附图,进一步详细说明本专利的具体实施方式。 Below in conjunction with accompanying drawing, the specific implementation manner of this patent is described in further detail.
如图1、2所示,一种用于水处理固液分离的沉降槽,包括箱体10,所述箱体10从进水口1到出水口7依次设有搅拌区、沉降区和污泥室,所述箱体10的进水口1设置在搅拌区的上方,搅拌区内设有搅拌装置2的搅拌部件,所述沉降区通过水平设置的多孔隔板3和支撑板5分隔为上区、中区和下区,所述上区、中区和下区垂直排列,所述多孔隔板3上布满透水孔11,所述透水孔11的直径为5-20mm,所述上区内排列有斜板或斜管4作为沉降加速装置,所述斜板或斜管4固定在多孔隔板上方的支撑板5上,所述搅拌区的出口与沉降区的下区入口连接,所述沉降区的中区通过溢流口6与污泥室连通,所述沉降区的上区与污泥室连通,所述箱体10在污泥室的上方的侧壁上设有箱体的出水口7,所述箱体10在污泥室的底部的侧壁上设有污泥室排泥口8,所述箱体10在沉降区的底部设有沉降区排泥口9。所述搅拌区上设有絮凝剂投放口。 As shown in Figures 1 and 2, a settling tank for solid-liquid separation in water treatment includes a box body 10, and the box body 10 is sequentially provided with a stirring zone, a settling zone and a sludge tank from the water inlet 1 to the water outlet 7 chamber, the water inlet 1 of the box 10 is set above the stirring zone, the stirring part of the stirring device 2 is arranged in the stirring zone, and the settling zone is divided into an upper zone by a horizontally arranged porous partition 3 and a support plate 5 , the middle area and the lower area, the upper area, the middle area and the lower area are vertically arranged, and the porous separator 3 is covered with water-permeable holes 11, and the diameter of the water-permeable holes 11 is 5-20mm. An inclined plate or inclined tube 4 is arranged as a settling acceleration device, and the inclined plate or inclined tube 4 is fixed on the support plate 5 above the porous partition, and the outlet of the stirring zone is connected with the lower zone inlet of the settling zone, and the The middle area of the settling area communicates with the sludge chamber through the overflow port 6, the upper area of the settling area communicates with the sludge chamber, and the box body 10 is provided with an outlet of the box body on the side wall above the sludge room. Water outlet 7, the box body 10 is provided with a sludge chamber sludge outlet 8 on the side wall of the bottom of the sludge chamber, and the box body 10 is provided with a sedimentation area mud outlet 9 at the bottom of the settlement area. The stirring area is provided with a flocculant feeding port.
本装置的原理如下: The principle of this device is as follows:
当处理水从进水口1进入斜板或斜管4沉淀池,通过投加絮凝剂,通过搅拌装置2的搅拌后,进入到穿过多孔隔板3,由于在多孔隔板3积聚有大量的污泥,形成污泥床,当含有悬浮物的水穿过污泥床时,由于絮凝剂的作用,高浓度的污泥床迅速加快了进水中是悬浮颗粒的凝聚速度,同时也由于微粒捕获的作用,将水中细小的颗粒物聚集到了大絮团了。这样,当颗粒物穿过污泥床后,所有的颗粒物都变大了,这样,水中的悬浮物的沉淀速度变大了,有利于在后续斜板或斜管上的沉降。 When the treated water enters the inclined plate or inclined tube 4 sedimentation tank from the water inlet 1, after being stirred by the stirring device 2 by adding flocculant, it enters through the porous partition 3, because a large amount of water is accumulated in the porous partition 3 Sludge forms a sludge bed. When water containing suspended matter passes through the sludge bed, due to the action of flocculants, the high-concentration sludge bed rapidly accelerates the agglomeration speed of suspended particles in the influent, and at the same time due to the The effect of capture is to gather the fine particles in the water into large flocs. In this way, when the particles pass through the sludge bed, all the particles become larger, so that the sedimentation speed of the suspended solids in the water becomes larger, which is conducive to the settlement on the subsequent inclined plate or inclined tube.
当斜板或斜管沉降池中污泥床的污泥很多时,高过溢流口6的高度,则自动溢流到右侧的室中,定期打开污泥室排泥口8将污泥及时排除。为了避免污泥长期在多孔隔板3下部的室体中沉积堵塞流道,需定期打开沉降区排泥口9将部分污泥及时排出。通过斜板或斜管沉降后的水变成了清液,则自流水出口7排出。 When there is a lot of sludge in the sludge bed in the inclined plate or inclined tube settling tank, which is higher than the height of the overflow port 6, it will automatically overflow into the chamber on the right, and the sludge chamber discharge port 8 will be opened regularly to discharge the sludge. Get rid of it in time. In order to avoid the long-term deposition of sludge in the lower chamber of the porous partition 3 to block the flow channel, it is necessary to periodically open the sludge discharge port 9 in the settling area to discharge part of the sludge in time. The water settled by the sloping plate or the inclined tube becomes clear liquid, which is then discharged from the running water outlet 7.
Claims (5)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520545176.5U CN204952365U (en) | 2015-07-24 | 2015-07-24 | A subsider for water treatment solid -liquid separation |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520545176.5U CN204952365U (en) | 2015-07-24 | 2015-07-24 | A subsider for water treatment solid -liquid separation |
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| Publication Number | Publication Date |
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| CN204952365U true CN204952365U (en) | 2016-01-13 |
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| CN201520545176.5U Expired - Lifetime CN204952365U (en) | 2015-07-24 | 2015-07-24 | A subsider for water treatment solid -liquid separation |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109607843A (en) * | 2018-12-29 | 2019-04-12 | 江苏金梓环境科技股份有限公司 | Detachable construction project slurry treatment device |
| CN110369366A (en) * | 2019-07-24 | 2019-10-25 | 苏州工业职业技术学院 | A workpiece production line, a workpiece cleaning machine, and a workpiece cleaning tank |
-
2015
- 2015-07-24 CN CN201520545176.5U patent/CN204952365U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109607843A (en) * | 2018-12-29 | 2019-04-12 | 江苏金梓环境科技股份有限公司 | Detachable construction project slurry treatment device |
| CN110369366A (en) * | 2019-07-24 | 2019-10-25 | 苏州工业职业技术学院 | A workpiece production line, a workpiece cleaning machine, and a workpiece cleaning tank |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
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| CX01 | Expiry of patent term |
Granted publication date: 20160113 |