CN205347020U - Deposit and filter integrated reactor - Google Patents
Deposit and filter integrated reactor Download PDFInfo
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- CN205347020U CN205347020U CN201521002881.7U CN201521002881U CN205347020U CN 205347020 U CN205347020 U CN 205347020U CN 201521002881 U CN201521002881 U CN 201521002881U CN 205347020 U CN205347020 U CN 205347020U
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- cell body
- sedimentation
- reaction district
- filtration
- flocculation
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Abstract
The utility model relates to a deposit and filter integrated reactor, include: the cell body, flocculating reaction district and filtering area, flocculation and precipitation system. The device that is located the flocculating reaction district includes the mixing drum of cell body central authorities and the reaction cylinder of cell body both sides to and be located and add medicine mouth and water inlet on the mixing drum, the filtering area is located the both sides in flocculating reaction district, packs with filtering including the bearing board, the flocculation and precipitation system includes reflecting plate, sludge bucket and mud pipe, and the reflecting plate is fixed in the lower part in flocculating reaction district, is connected with the flocculating reaction district of both sides, sludge bucket is located the bottom of cell body, is to leak hopper -shaped, the mud pipe is opened by the valve control along the installation of the sludge bucket slope. The utility model discloses increase flocculating reaction district and filtering area on original vertical -flow sedimentation tank basis for the efficiency of getting rid of suspended solid increases substantially, than the surface load improvement one time of original sedimentation tank. Besides, the utility model discloses still shorten water conservancy dwell time, reduce the area of sedimentation tank, reduce investment cost.
Description
Technical field
This utility model relates to a kind of sewage disposal device, is specifically related to a kind of sedimentation and filtration integratedization reactor.
Background technology
The effect of sedimentation tank is that the solid suspension that sewage Midst density is bigger is carried out precipitate and separate, to alleviate the load of subsequent treatment structures.By adding flocculant in sedimentation tank, micelle in sewage is de-steady under its influence or is adsorbed cohering, but after general sedimentation tank adds flocculant wherein, the floccule body that small part volume is bigger quickly deposits to bottom bucket, also have significant component of floccule body less due to particle diameter, it is difficult in sedimentation tank and precipitates, deposition efficiency is low, so causing sedimentation tank sedimentation effect poor, the sedimentation time is long, causing that required floor space is big, cost of investment is high.
In the prior art, number of patent application 201210062468.4, denomination of invention is: a kind of integrated water treatment purifier, including the housing containing inner chamber, housing upper connects outlet pipe, bottom connects discharge pipeline, housing cavity has flocculation reaction device, flocculation reaction device includes water inlet segment and reactor body, reactor body inner chamber has flocculation filler, reactor body upper conical air guide arranged below, type sloping plate component is had outside reactor body periphery, this type sloping plate component makes housing cavity form cavity of resorption, for concentrating mud collection area bottom cavity of resorption, type sloping plate component is arranged above with filter course, filter course makes housing cavity form lumen and epicoele, epicoele communicates with outlet pipe.This water purifier Collecting flocculation, precipitation, filtration and concentration integrate mud, and each functional areas do not interfere with each other, simple in construction, compact, take up an area less, are conducive to improving effluent quality.But this patent application only arranges reactor body on structure is arranged, lack sewage hybrid junctions component, thus sewage can not be sufficiently mixed in hybrid junctions component, is unfavorable for flocculation and the precipitation of water purifier.
Summary of the invention
This utility model provides a kind of sedimentation and filtration integratedization reactor, solves existing conventional precipitation pond sedimentation effect poor, and the sedimentation time is long, takes up an area and invests big problem.
For achieving the above object, this utility model adopts the following technical scheme that:
A kind of sedimentation and filtration integratedization reactor, including: cell body, flocculation reaction district and filtering area, flocculation sedimentation system.Wherein,
Described flocculation reaction district includes being positioned at the mixing drum of cell body central authorities and being positioned at the reaction tube of cell body both sides, and is positioned at the dosing mouth on mixing drum and water inlet.Described flocculation reaction district is arranged on the middle and upper part of cell body, is positioned at the top of described flocculation sedimentation system.
Described filtering area includes the supporting plate and the filter packing floor that are positioned at both sides, flocculation reaction district.
Described flocculation sedimentation system includes reflecting plate, sludge bucket and discharge pipeline.Wherein, reflecting plate is fixed on the bottom in flocculation reaction district, is connected with the flocculation reaction district of both sides；The bottom of cell body it is positioned in funnelform sludge bucket；Discharge pipeline is arranged along the sludge bucket gradient, by the unlatching of Valve controlling discharge pipeline.
Further, described cell body is circular or square, and the material of cell body is mechanical wound fiberglass-reinforced plastic or concrete or carbon steel, adopts buried or is placed directly on ground.
Further, described cell body top is the effluent weir of indented endless, and the effluent weir both sides of indented endless communicate with outlet and backwash water inlet and are fixed on the internal face of cell body.
Further, top, described flocculation reaction district exceeds liquid level 200～300mm.
Further, the device in described flocculation reaction district adopts fixed support and cell body to fix.
Further, the height of described filtering area is 300～400mm.
Further, the filter packing of described filter packing layer is quartz sand or activated carbon, and size is 1～2mm.
Further, described discharge pipeline arranges multiple 45 ° of holes down.
Further, described reactor also includes the inspection shaft for overhauling that is positioned at cell body top.
Compared with prior art, reactor described in the utility model has the advantages that
Described reactor increases flocculation reaction district and filtering area on the basis of original vertical sedimentation basin so that the efficiency removing suspended solid increases substantially, and doubles than the surface loading of existing sedimentation tank.In addition, this utility model also has the advantage shortening hydraulic detention time, the floor space of minimizing sedimentation tank, reduction cost of investment.
Accompanying drawing explanation
Fig. 1 is the profile of reactor described in the utility model；
Fig. 2 is the top view of reactor described in the utility model.
In figure: 1-inspection shaft, 2-cell body, 3-backwash water inlet, 4-dosing mouth, 5-effluent weir, 6-outlet, 7-fixed support, 8-water inlet, 9-sludge bucket, 10-filter packing layer, 11-supporting plate, 12-mixing drum, 13-reaction tube, 14-reflecting plate, 15-discharge pipeline.
Detailed description of the invention
Below in conjunction with drawings and Examples, this utility model is described further.
A kind of sedimentation and filtration integrated reactor, its structural representation as shown in Figure 1 and Figure 2, including cell body 2, is positioned at the inspection shaft 1 for overhauling at cell body 2 top, flocculation reaction district and filtering area, flocculation sedimentation system.Wherein, cell body 2 is circular or square, and the material of cell body 2 is mechanical wound fiberglass-reinforced plastic or concrete or carbon steel, adopts buried or is placed directly on ground.Cell body 2 top is the effluent weir 5 of indented endless, and effluent weir 5 both sides communicate with outlet 6 and backwash water inlet 3, are fixed on the internal face of cell body 2.The material of effluent weir 5 is fiberglass.
Flocculation reaction district includes the mixing drum 12 being positioned at cell body 2 central authorities and the reaction tube 13 being positioned at cell body 2 both sides, and it is positioned at the dosing mouth 4 on mixing drum 12 and water inlet 8, flocculation reaction district is arranged on the middle and upper part of cell body 2, being positioned at the top of flocculation sedimentation system, the top in flocculation reaction district exceeds liquid level 200-300mm.Described mixing drum 12, reaction tube 13 adopt fixed support 7 to fix with cell body 2.After medicament and sewage add from dosing mouth 4 and water inlet 8, first mix in mixing drum 12, react with the float in sewage in the reaction tube 13 flowing into both sides afterwards, form floccule body.
Filtering area is made up of supporting plate 11 and the filter packing layer 10 being positioned on supporting plate 11, and supporting plate 11 is fixed on the internal face of cell body 2, is highly 300-400mm.In filter packing layer 10, the filter packing of filling is quartz sand or activated carbon.Can be adulterated in sewage after reflecting plate 14 the tiny particle without precipitation and floccule body, when, after filter packing layer 10, tiny particle and floccule body are intercepted, and clear water flows out from filtering area.
Flocculation sedimentation system is made up of reflecting plate 14, sludge bucket 9 and discharge pipeline 15.Wherein, reflecting plate 14 is fixed on reaction container 13 bottom of cell body 2 both sides；The bottom of cell body 2 it is positioned in funnelform sludge bucket 9；Discharge pipeline 15 is installed along the gradient of sludge bucket 9, valve (not shown) control the unlatching of discharge pipeline 15 spoil disposal.Mud discharge pipeline 15 arranges multiple 45 ° of holes down, so that can uniformly be discharged without dead angle in cell body 2.The sewage flowed out from flocculation reaction district is distributed to surrounding through the obstruction of reflecting plate 14, slowly flows up on whole horizontal section.Sedimentation velocity sinks in sludge bucket 9 more than the particle of the current rate of climb and bigger floccule body, when, after valve opening, the mud in sludge bucket 9 is adopted gravity sludge discharge way to discharge cell body 2 by discharge pipeline 15.
Adopt described reactor, sewage enters from water inlet 8, after mixing with the coagulant added, flow through mixing drum 12 and reaction tube 13 forms floccule body with the colloid reaction in sewage, sewage separates under the effect of reflecting plate 14 for the first time with the big floccule body in sewage, granule, mud sinks in sludge bucket 9, and the mud of smaller particle is intercepted under the effect of described filter packing, and clear water flows out from top through effluent weir 5.The mud entered in sludge bucket 9 is adopted gravity sludge discharge way to be discharged to outside cell body 2 by discharge pipeline 15.
This utility model is not limited to above-mentioned embodiment, made above-mentioned embodiment is any conspicuously improved of those skilled in the art or change, all without the protection domain beyond the design of the present invention and claims.
Claims (9)
1. a sedimentation and filtration integratedization reactor, it is characterised in that including: cell body (2), flocculation reaction district and filtering area, flocculation sedimentation system；Wherein, described flocculation reaction district includes being arranged at the mixing drum (12) of described cell body (2) central authorities and being positioned at the reaction tube (13) of described cell body (2) inner side, and is positioned at the dosing mouth (4) on described mixing drum (12) and water inlet (8)；Described mixing drum (12) and reaction tube (13) are positioned at the top of described flocculation sedimentation system；The described filtering area being positioned at mixing drum (12) and reaction tube (13) both sides includes supporting plate (11) and filter packing layer (10)；Described flocculation sedimentation system includes reflecting plate (14), sludge bucket (9) and discharge pipeline (15)；Wherein, described reflecting plate (14) is fixed on the bottom in described flocculation reaction district and is connected with reaction tube (13)；The bottom of described cell body (2) it is positioned in funnelform sludge bucket (9)；The described discharge pipeline (15) opened by Valve controlling is installed along described sludge bucket (9) gradient.
2. sedimentation and filtration integratedization reactor according to claim 1, it is characterised in that described cell body (2) is for circular or square.
3. sedimentation and filtration integratedization reactor according to claim 1, it is characterized in that, described cell body (2) top is the effluent weir (5) of jagged annular, described effluent weir (5) both sides communicate with outlet (6) and backwash water inlet (3), are fixed on the internal face of cell body (2) described in described outlet (6) lower end.
4. sedimentation and filtration integratedization reactor according to claim 1, it is characterised in that top, described flocculation reaction district exceeds liquid level 200～300mm.
5. sedimentation and filtration integratedization reactor according to claim 1, it is characterised in that the device in described flocculation reaction district adopts fixed support (7) to fix with described cell body (2).
6. sedimentation and filtration integratedization reactor according to claim 1, it is characterised in that the height of described filtering area is 300～400mm.
7. sedimentation and filtration integratedization reactor according to claim 1, it is characterised in that the filler of described filter packing layer (10) is quartz sand or activated carbon, and size is 1～2mm.
8. sedimentation and filtration integratedization reactor according to claim 1, it is characterised in that multiple 45 ° of holes down are set on described discharge pipeline (15).
9. sedimentation and filtration integratedization reactor according to claim 1, it is characterised in that described reactor also includes the inspection shaft (1) for overhauling being positioned at cell body (2) top.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521002881.7U CN205347020U (en) | 2015-12-07 | 2015-12-07 | Deposit and filter integrated reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521002881.7U CN205347020U (en) | 2015-12-07 | 2015-12-07 | Deposit and filter integrated reactor |
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| Publication Number | Publication Date |
|---|---|
| CN205347020U true CN205347020U (en) | 2016-06-29 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521002881.7U Active CN205347020U (en) | 2015-12-07 | 2015-12-07 | Deposit and filter integrated reactor |
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| CN (1) | CN205347020U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107055871A (en) * | 2017-05-03 | 2017-08-18 | 北京师范大学 | A kind of new coagulating sedimentation retention filtering air-water backwashing integrated high-efficiency filter tank |
| CN110272150A (en) * | 2019-07-19 | 2019-09-24 | 湖南科技大学 | A kind of sewage disposal device for the cyclone sediment filtering integral that flocculates |
| CN112616622A (en) * | 2020-12-08 | 2021-04-09 | 东莞市园林绿化工程有限公司 | Environment-friendly automatic water storage irrigation system and irrigation method |
| CN115215485A (en) * | 2022-08-11 | 2022-10-21 | 北京市生态环境保护科学研究院 | High-speed solid-liquid separation integrated device |
-
2015
- 2015-12-07 CN CN201521002881.7U patent/CN205347020U/en active Active
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107055871A (en) * | 2017-05-03 | 2017-08-18 | 北京师范大学 | A kind of new coagulating sedimentation retention filtering air-water backwashing integrated high-efficiency filter tank |
| CN107055871B (en) * | 2017-05-03 | 2020-12-01 | 北京师范大学 | Novel coagulating sedimentation interception and filtration air-water backwashing integrated high-efficiency filter tank |
| CN110272150A (en) * | 2019-07-19 | 2019-09-24 | 湖南科技大学 | A kind of sewage disposal device for the cyclone sediment filtering integral that flocculates |
| CN112616622A (en) * | 2020-12-08 | 2021-04-09 | 东莞市园林绿化工程有限公司 | Environment-friendly automatic water storage irrigation system and irrigation method |
| CN115215485A (en) * | 2022-08-11 | 2022-10-21 | 北京市生态环境保护科学研究院 | High-speed solid-liquid separation integrated device |
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Address after: 101304 Shunyi District, Beijing, Mu Lin Town, 500 square meters east village committee Patentee after: Beijing Chaobai environmental Polytron Technologies Inc Address before: 101304 Shunyi District, Beijing, Mu Lin Town, 500 square meters east village committee Patentee before: Huang Yubao |