CN102115236B - Maze eddy folded plate flocculation pool - Google Patents
Maze eddy folded plate flocculation pool Download PDFInfo
- Publication number
- CN102115236B CN102115236B CN 201010017239 CN201010017239A CN102115236B CN 102115236 B CN102115236 B CN 102115236B CN 201010017239 CN201010017239 CN 201010017239 CN 201010017239 A CN201010017239 A CN 201010017239A CN 102115236 B CN102115236 B CN 102115236B
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- Prior art keywords
- reaction tank
- reaction
- flap
- folded plate
- eddy
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- 238000005189 flocculation Methods 0.000 title claims abstract description 28
- 230000016615 flocculation Effects 0.000 title claims abstract description 25
- 238000006243 chemical reaction Methods 0.000 claims abstract description 52
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 13
- 230000000694 effects Effects 0.000 abstract description 10
- 230000036632 reaction speed Effects 0.000 abstract description 4
- 239000003814 drug Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 230000035484 reaction time Effects 0.000 description 3
- 101001017827 Mus musculus Leucine-rich repeat flightless-interacting protein 1 Proteins 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000003541 multi-stage reaction Methods 0.000 description 2
- 230000008649 adaptation response Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
Images
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- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The invention relates to a maze eddy folded plate flocculation pool, belonging to the field of water treatment equipment. The maze eddy folded plate flocculation pool comprises a reaction tank and multiple groups of folded plates, wherein the multiple groups of folded plates are arranged in the reaction tank; each folded plate is provided with ribs; speed controllers or V-shaped guide plates are arranged among the folded plates; and the speed controllers or V-shaped guide plates can lead water current to form controllable reaction speed gradients in the folded plates, and simultaneously a large amount of eddy is formed through the turbulent flow of the ribs. By combination of high speed and low speed, the collision probability of a flocculation reaction is increased, and the effect of theflocculation reaction is improved.
Description
Technical field
The invention belongs to the water treatment facilities field, refer in particular to a kind of labyrinth eddy current folded plate flocculation reaction tank.
Background technology
In water treatment procedures such as running water purification, recycle-water processing, flocculation reaction is one of most important cell process.Flocculation process reaction efficiency and completeness directly influence engineering construction investment and engineering operation cost, directly have influence on the treatment effect of subsequent technique simultaneously, finally have influence on the technology effluent quality.Common folded plate flocculation reaction tank is the conventional flap of design in reaction tank, this traditional flocculation process is only paid attention to macroscopical hydraulics of heterogeneous fluid, and it is very few to flow velocity fine setting control and micro-structure of turbulence utilization, cause that flocculation efficiency is low, the reaction time is long, effect is not ideal enough, simultaneously medicine is caused a large amount of wastes, strengthened the burden of user's operating cost.Occurred a kind of improved folded plate flocculation reaction tank on the market, the folding in the reaction tank is pulled and fin is set reaching flow velocity fine setting effect, but this fine setting effect is limited, and the current between flap still are more stable, influence the hybrid reaction effect of medicament and water.
Summary of the invention
In order to address the above problem, the invention provides a kind of change reaction flow velocity that passes through to improve the labyrinth eddy current folded plate flocculation reaction tank of flocculation efficiency, main innovation is to arrange speed regulator or V-type deflector between the reaction tank flap.Specifically implement like this: labyrinth eddy current folded plate flocculation reaction tank, comprise reaction tank, some groups of flaps in the reaction tank are equipped with fin on the flap, it is characterized in that being provided with between flap speed regulator or V-type deflector.The speed regulator and the V-type deflector that are used for the governing speed gradient have formed the labyrinth to current, this equipment utilization flocculation rate gradient principle and principle of dynamics, when making current in flap, form macroscopical turbulence, pass through speed regulator or V-type deflector reaction speed gradient, to form controlled reaction speed gradient, form a large amount of eddy current by the fin flow-disturbing simultaneously, at a high speed with the combination of low velocity, increase the collision probability of flocculation reaction, improved the flocculation reaction effect.In order to reach velocity gradient regulating effect preferably, speed regulator is designed to the polygon speed regulator.
According to actual needs, this reaction tank can be applied to separately in the engineering, also can be used in combination, and the flap in the reaction tank can be arranged by symmetric form, also can arrange by parallel type.The reaction tank governing speed of band speed regulator is powerful, generally is placed on the foremost in composite reaction pond, for the last steady water outlet requirement of adaptive response, can also add one at last in the composite reaction pond only with the popular response pond of flap.
The present invention can make current form controlled reaction speed gradient in flap, forms a large amount of eddy current by the fin flow-disturbing simultaneously, at a high speed with the combination of low velocity, has increased the collision probability of flocculation reaction, has improved the flocculation reaction effect.
Description of drawings
Fig. 1 is flap A type structural representation;
Fig. 2 analyses plate Type B structural representation;
Fig. 3 analyses plate C type structural representation;
Fig. 4 is combined flocculation reaction tank structural representation.
The specific embodiment:
Some groups of flaps 1 in the C type labyrinth eddy current folded plate flocculation reaction tank, reaction tank are arranged in parallel.
Some groups of flaps 1 symmetric form in the A type labyrinth eddy current folded plate flocculation reaction tank, reaction tank is arranged, is equipped with fin 2 on the flap 1, is provided with polygon speed regulator 3 between flap.
Some groups of flaps 1 symmetric form in the Type B labyrinth eddy current folded plate flocculation reaction tank, reaction tank is arranged, is equipped with fin 2 on the flap 1, is provided with V-type deflector 4 between flap.
The arrangement of flap also can change as required, is not limited to above-mentioned three kinds.
Be applied in the engineering, single reaction tank can use separately, in most cases, for reaching reaction effect preferably, can be that wherein two or more combination serial connection is used (identical or different reaction tank).Preferable a kind of compound mode is: A type, Type B, C type are connected in series successively, current are by flap the time, earlier change flow rate of water flow with speed regulator, utilize the guide functions of fin simultaneously, at the vortex of a large amount of high speeds of the inner formation of reaction tank with low speed, form high-intensity eddy current, medicament and water generates are rubbed in a large number, increase particle collision probability in the water, carry and do reaction efficiency, the enhanced flocculation effect; Along with the carrying out of reaction, slow down the decline rate of current, namely allow current enter the Type B reaction tank, change water velocity by the V-type deflector; Before reaction finished, because going out water sedimentation current more stably, C type reaction tank just satisfied the demands.Successively decreasing of this combination is length according to the reaction time, the requirement of course of reaction designs, so the traditional flocculation process of this labyrinth eddy current folded plate flocculation reaction tank and common flap reaction tank or other relatively, generally can shorten reaction time 40% or more, save capital expenditure about 30%, saving operating cost more than 30%.
Claims (1)
1. labyrinth eddy current folded plate flocculation reaction tank, it is composed in series successively by A type reaction tank, Type B reaction tank and C type reaction tank, wherein:
Have some groups of flaps (1) in the A type reaction tank, the flap symmetric arrangement is equipped with fin (2) on the flap, be provided with speed regulator (3) between flap;
Have some groups of flaps (1) in the Type B reaction tank, the flap symmetric arrangement is equipped with fin (2) on the flap, be provided with V-type deflector (4) between flap;
Have some groups of flaps (1) in the C type reaction tank, flap be arranged in parallel and flap on do not establish fin.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201010017239 CN102115236B (en) | 2010-01-05 | 2010-01-05 | Maze eddy folded plate flocculation pool |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201010017239 CN102115236B (en) | 2010-01-05 | 2010-01-05 | Maze eddy folded plate flocculation pool |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102115236A CN102115236A (en) | 2011-07-06 |
| CN102115236B true CN102115236B (en) | 2013-09-18 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201010017239 Expired - Fee Related CN102115236B (en) | 2010-01-05 | 2010-01-05 | Maze eddy folded plate flocculation pool |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102115236B (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103848488B (en) * | 2014-02-25 | 2015-06-10 | 宜兴市海博环保科技有限公司 | Flocculation reaction pool of maze turbulent folded plate |
| CN105170312B (en) * | 2015-08-14 | 2017-09-22 | 昆明理工大学 | A kind of mine tailing is classified ore drawing device |
| CN105244145B (en) * | 2015-10-30 | 2017-06-06 | 国家电网公司 | A kind of liquid cooling apparatus based on oil-immersed type transformer radiator |
| CN105600900B (en) * | 2015-11-10 | 2018-05-15 | 山东建筑大学 | Utilize the device and method of gamma-polyglutamic acid Adsorption industrial wastewater ion |
| CN111072185A (en) * | 2020-01-09 | 2020-04-28 | 伟通工业设备（江苏）有限公司 | Classified sewage flocculation device and working method thereof |
| CN114634233B (en) * | 2022-03-31 | 2023-04-11 | 哈尔滨理工大学 | Folded plate flocculation tank with central turbulence column and structure optimization method thereof |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2540406Y (en) * | 2002-04-17 | 2003-03-19 | 徐立群 | Flocculation pond with fin division plate |
| CN2560633Y (en) * | 2002-07-25 | 2003-07-16 | 长春联创水务有限责任公司 | Microvortex folded plate floculating reaction tank |
| CN201235237Y (en) * | 2008-03-14 | 2009-05-13 | 王鹤名 | Y shaped fin piece flocculation apparatus |
| CN201701790U (en) * | 2010-01-05 | 2011-01-12 | 宜兴市海博环保科技有限公司 | Labyrinth vortex folded-plate flocculation reaction tank |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7717275B2 (en) * | 2008-05-27 | 2010-05-18 | Hany Zarif Gerges | Integrated perforated flocculating baffle system |
-
2010
- 2010-01-05 CN CN 201010017239 patent/CN102115236B/en not_active Expired - Fee Related
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2540406Y (en) * | 2002-04-17 | 2003-03-19 | 徐立群 | Flocculation pond with fin division plate |
| CN2560633Y (en) * | 2002-07-25 | 2003-07-16 | 长春联创水务有限责任公司 | Microvortex folded plate floculating reaction tank |
| CN201235237Y (en) * | 2008-03-14 | 2009-05-13 | 王鹤名 | Y shaped fin piece flocculation apparatus |
| CN201701790U (en) * | 2010-01-05 | 2011-01-12 | 宜兴市海博环保科技有限公司 | Labyrinth vortex folded-plate flocculation reaction tank |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102115236A (en) | 2011-07-06 |
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| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
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| 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: 20130918 |