CN204958489U - Pipeline formula flocculating reaction ware - Google Patents
Pipeline formula flocculating reaction ware Download PDFInfo
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- CN204958489U CN204958489U CN201520505936.XU CN201520505936U CN204958489U CN 204958489 U CN204958489 U CN 204958489U CN 201520505936 U CN201520505936 U CN 201520505936U CN 204958489 U CN204958489 U CN 204958489U
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Abstract
The utility model discloses a pipeline formula flocculating reaction ware wholly is horizontal pipeline structure, and horizontal both ends are water inlet and delivery port respectively, the one end of being close to the water inlet, and one side sets up the flocculating agent filling opening, and the opposite side sets up the coagulant aid filling opening, and the one end of being close to the delivery port sets up the baffling board of two sets of wrong cloth perpendicularly, and two sets of baffling boards are separated by and are arranged, and a set of baffling board sets up the passageway that link up in the centre, and another group's baffling board and reactor both ends form the passageway that runs through, it hangs down, need not the characteristics that the agitated vessel energy consumption is low, non -maintaining to have the reaction efficiency height, take up an area of little, investment.
Description
Technical field
The utility model belongs to technical field of sewage, is specifically related to a kind of duct type flocculation reactor.
Background technology
Flocculation reaction mode conventional in current sewage disposal has following several:
Dividing plate flocculation basin: be usually applicable to large and medium-sized water factory, but because of the water yield too small time, clapboard spacing cross narrow inconvenience construction and maintenance.Simple structure, convenient management.But the large person's flocculating effect of fluctuations in discharge is unstable, compared with flap and grid type flocculation basin, because flow condition is not satisfactory, the inactive portion large percentage in energy expenditure (i.e. head loss), therefore need longer flocculation time, pond volume is larger;
Folded plate flocculator: current Tortuous flow or contract between different setback plate, release dynamic and successively, so that form numerous little whirlpools, improve particle collision flocculating effect, close to push flowing between same setback plate.Compared with dividing plate flocculation basin, flow condition improves greatly, that is in total flow energy consumes, useful energy this consumption ratio improves, therefore required flocculation time can shorten, and pond volume reduces;
Mechanical stirring flocculation basin: simple structure, easy construction, but cost is high, and operation expense is high.
Flocculation agent is settling stability and the polymerization stability that can reduce or eliminate disperse particles in water, disperse particles is condensed, flocculates into aggregate and the class material that removes.Flocculation agent, in the means of sewage treatment area as strengthening solid-liquid separation, can be used for the secondary sedimentation after the primary deposition of enhanced sewage, flotation process and activated sludge process, also can be used for tertiary sewage treatment or advanced treatment.
Therefore flocculation reaction unit is processing unit conventional in sewage disposal.Under the effect of coagulating agent, make the colloid in waste water and fine suspension be condensed into flocs unit, be then separated the water treating method of removing.The application of coagulant sedimentation in water treatment is very widely, and it both can reduce the sense index of the water quality such as turbidity, colourity of former water, can remove multiple hazardous contaminant again.Flocculation reaction mode conventional at present has dividing plate flocculation basin, folded plate flocculator and mechanical flocculation basin, but all there is different shortcomings.
In the last few years, along with coagulation the reach of science, relevant flocculation basic theory and the research of efficient flocculating reaction technology all achieve impressive progress, but how to improve coagulation apparatus efficiency, the further research and extension process scope needs of reduction energy consumption.
Traditional flocculation reaction equipment generally adopts carbon steel grooved pond or reinforced concrete water pond, concrete basin is adopted when the process water yield is larger, and the water yield few time can adopt carbon steel grooved pond, but above 2 kinds of modes all need whipping device, have that floor space is large, consume energy problem that is high, maintenance workload.
Utility model content
The utility model provides a kind of duct type flocculation reactor, have reaction efficiency high, take up an area little, invest low, without the need to low, the non-maintaining feature of whipping device energy consumption.
The utility model solves the technical scheme that its technical problem adopts: duct type flocculation reactor of the present utility model, entirety is horizontal pipeline structure, horizontal two ends are respectively water-in and water outlet, near one end of water-in, side arranges flocculation agent inlet, opposite side arranges coagulant aids inlet, the traverse baffle of two groups of wrong cloth is vertically set near one end of water outlet, two groups of traverse baffles are separated by layout, one group of traverse baffle arranges through passage in centre, and another group traverse baffle and reactor two ends form the passage run through.
Often group comprises 2 traverse baffles.
Water-in, water outlet and traverse baffle center-aisle are in line.
This reactor reaction process forms mixing effect by the change of flow-shape and meets flocculation reaction condition in pipeline, does not need to increase mechanical stirring again and arranges.
This reactor is after inlet end forms injection, ambient air is taken away, form partial vacuum condition, add flocculation agent and coagulant aids herein, reacting by spraying fully to mix with sewage rapidly, then through overdraft diffusion reaction district and traverse baffle, forming flco and stablizing gradually, then enter follow-up precipitation or filtering unit, carry out mud-water separation.
Duct type flocculation reactor of the present utility model have reaction efficiency high, take up an area little, invest low, without the need to low, the non-maintaining feature of whipping device energy consumption.
Accompanying drawing explanation
Fig. 1 is duct type flocculation reactor plan structure schematic diagram of the present utility model.
In figure: 1. water-in; 2. water outlet; 3. flocculation agent inlet; 4. coagulant aids inlet; 5. traverse baffle; 6. jet reaction district; 7. compress diffusion reaction district.
Embodiment
Below in conjunction with drawings and Examples, the utility model is described in further detail.
Embodiment 1
See Fig. 1, duct type flocculation reactor of the present utility model, entirety is horizontal pipeline structure, and horizontal two ends are respectively water-in 1 and water outlet 2, near one end of water-in 1, side arranges flocculation agent inlet 3, opposite side arranges coagulant aids inlet 4, and traverse baffle 5, the two groups of traverse baffles 5 vertically arranging two groups of wrong cloth near one end of water outlet 2 are separated by layout, one group of traverse baffle 5 arranges through passage in centre, and another group traverse baffle 5 forms with reactor two ends the passage run through.
Often group comprises 2 traverse baffles 5.
Water-in 1, water outlet 2 and traverse baffle 5 center-aisle are in line.
This reactor reaction process forms mixing effect by the change of flow-shape and meets flocculation reaction condition in pipeline, does not need to increase mechanical stirring again and arranges.
This reactor is after water-in 1 end forms injection, in jet reaction district 6, ambient air is taken away, form partial vacuum condition, add flocculation agent and coagulant aids herein, reacting by spraying fully to mix with sewage rapidly, then through overdraft diffusion reaction district 7 and traverse baffle 5, forming flco and stablizing gradually, then enter follow-up precipitation or filtering unit, carry out mud-water separation.
Duct type flocculation reactor of the present utility model have reaction efficiency high, take up an area little, invest low, without the need to low, the non-maintaining feature of whipping device energy consumption.
Claims (3)
1. a duct type flocculation reactor, it is characterized in that: overall is horizontal pipeline structure, horizontal two ends are respectively water-in and water outlet, near one end of water-in, side arranges flocculation agent inlet, and opposite side arranges coagulant aids inlet, the traverse baffle of two groups of wrong cloth is vertically set near one end of water outlet, two groups of traverse baffles are separated by layout, and one group of traverse baffle arranges through passage in centre, and another group traverse baffle and reactor two ends form the passage run through.
2. duct type flocculation reactor according to claim 1, is characterized in that: often group comprises 2 traverse baffles.
3. duct type flocculation reactor according to claim 1, is characterized in that: water-in, water outlet and traverse baffle center-aisle are in line.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520505936.XU CN204958489U (en) | 2015-07-13 | 2015-07-13 | Pipeline formula flocculating reaction ware |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520505936.XU CN204958489U (en) | 2015-07-13 | 2015-07-13 | Pipeline formula flocculating reaction ware |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204958489U true CN204958489U (en) | 2016-01-13 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520505936.XU Expired - Fee Related CN204958489U (en) | 2015-07-13 | 2015-07-13 | Pipeline formula flocculating reaction ware |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204958489U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105776478A (en) * | 2016-05-13 | 2016-07-20 | 福建工程学院 | Flocculating reaction device |
| CN106277713A (en) * | 2016-10-21 | 2017-01-04 | 吴云萍 | A kind of efficiently bobbin carriage coagulator |
| CN114409041A (en) * | 2022-01-18 | 2022-04-29 | 广东新会中集特种运输设备有限公司 | Water treatment device |
-
2015
- 2015-07-13 CN CN201520505936.XU patent/CN204958489U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105776478A (en) * | 2016-05-13 | 2016-07-20 | 福建工程学院 | Flocculating reaction device |
| CN106277713A (en) * | 2016-10-21 | 2017-01-04 | 吴云萍 | A kind of efficiently bobbin carriage coagulator |
| CN106277713B (en) * | 2016-10-21 | 2022-12-06 | 安尼康（福建）环保设备有限公司 | High-efficient pipe case coagulation ware |
| CN114409041A (en) * | 2022-01-18 | 2022-04-29 | 广东新会中集特种运输设备有限公司 | Water treatment device |
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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: 20160113 Termination date: 20210713 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |