CN2520929Y - Cyclone mixing reaction settler - Google Patents
Cyclone mixing reaction settler Download PDFInfo
- Publication number
- CN2520929Y CN2520929Y CN 01245443 CN01245443U CN2520929Y CN 2520929 Y CN2520929 Y CN 2520929Y CN 01245443 CN01245443 CN 01245443 CN 01245443 U CN01245443 U CN 01245443U CN 2520929 Y CN2520929 Y CN 2520929Y
- Authority
- CN
- China
- Prior art keywords
- settler
- central reaction
- shaft
- chamber
- reaction
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 238000006243 chemical reaction Methods 0.000 title claims abstract description 43
- 238000002156 mixing Methods 0.000 title abstract description 10
- 230000001112 coagulating effect Effects 0.000 claims abstract description 24
- 238000003756 stirring Methods 0.000 claims abstract description 12
- 239000000126 substance Substances 0.000 claims description 10
- 239000000945 filler Substances 0.000 claims description 2
- 238000012856 packing Methods 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 30
- 230000015271 coagulation Effects 0.000 abstract description 4
- 238000005345 coagulation Methods 0.000 abstract description 4
- 238000000034 method Methods 0.000 abstract description 4
- 238000005192 partition Methods 0.000 abstract description 3
- 239000008394 flocculating agent Substances 0.000 abstract 1
- 230000003311 flocculating effect Effects 0.000 abstract 1
- 230000001376 precipitating effect Effects 0.000 abstract 1
- 239000003814 drug Substances 0.000 description 8
- 238000005189 flocculation Methods 0.000 description 5
- 230000016615 flocculation Effects 0.000 description 5
- 238000001556 precipitation Methods 0.000 description 3
- 241000208140 Acer Species 0.000 description 2
- 102000010637 Aquaporins Human genes 0.000 description 1
- 108010063290 Aquaporins Proteins 0.000 description 1
- 108091006146 Channels Proteins 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 238000012384 transportation and delivery Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Images
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
A cyclone mixing reaction settler belongs to the technical field of water treatment equipment. The settler is provided with an outer cylinder, a central reaction cylinder and a slip cone which are arranged in the outer cylinder, wherein the slip cone is arranged at the bottom of the central reaction cylinder, and an inclined plate and a water distributor are arranged in an annular cavity between the central reaction cylinder and the outer cylinder. The interior of the central reaction cylinder is divided into mutually independent coagulating chambers by partition plates, and a stirring mechanism consisting of a driving blade, a stirring shaft, a stirring blade, a stirring shaft support and the like is installed. Each relatively independent coagulation chamber is provided with a dosing port and a nozzle. The utility model realizes the process of water treatment such as adding, mixing, reacting, flocculating and precipitating of a plurality of flocculating agents in one device. The integrity is good, the occupied area is small, the energy is saved, and the water treatment efficiency and quality are improved.
Description
Technical field
The utility model relates to a kind of water treatment facilities, particularly realizes the water treatment facilities of multiple flocculation medicament delivery, mixing, reaction, flocculation, precipitation in an equipment.Belong to the water treatment facilities technical field.
Background technology
Coagulation is by add flocculant in former water, make former water-borne glue body take off steady and cohesion, this process is divided into two stages, at mix stages, requires flocculant to mix equably rapidly with former water, and arrived the stage of reaction, should make enough collision opportunity and good adsorption condition, allow flco that enough growth opportunities are arranged, prevent that again the little flco that generates is broken, therefore stirring intensity will reduce gradually, and the reaction time will be grown.Existingly in former water, add the equipment that flocculation medicament hybrid reaction is carried out water treatment, be generally separated type.Mixing apparatus has pulpboard formula machine maple mixing channel, split-flow baffles mixing channel, water pump to mix; Consersion unit has flat flow and vertical-flow partition plate reaction tank, swinging partition plate reaction tank, eddy current reaction tank, machine maple reaction tank.The available coagulation water treatment facilities exist globality poor, and volume is big, and area occupied is many, need additional power, and the coagulating process is long, and water treatment efficiency is low, of poor quality.
Summary of the invention
The purpose of this utility model is exactly the deficiency that exists at existing coagulation water treatment facilities, and a kind of eddy flow hybrid reaction settler of finishing dispensing, mixing, reaction, flocculation, precipitation process in an equipment is provided.
The purpose of this utility model is to realize like this, eddy flow hybrid reaction settler, it is characterized in that settler has central reaction tube (2), the slip awl (9) that is provided with in a urceolus (1) and the urceolus, the slip awl is arranged on the central reaction tube bottom, looping chamber between central reaction drum outer wall and the outer tube inner wall, swash plate (7), water-locator (8) are installed in the annular chamber, and central reaction tube inner-use clapboard (17) is separated into separate coagulating chamber, and rabbling mechanism is installed in the coagulating chamber.Said rabbling mechanism has active blade (14), shaft (13), stirring vane (15), shaft to prop up Cuo (12), and shaft props up in the Cuo coagulating chamber by shaft, and active blade, stirring vane are installed on the shaft.Said separate coagulating chamber is provided with chemical feed pipe (4) and nozzle (16), and the track of the emission direction of nozzle and active blade (14) rotation is tangent or crossing.Said swash plate (7) structure is multi-layer sheet filler and/or corrugated plate packing.Former water and first kind of medicament at first enter first coagulating chamber on central reaction tube top from water inlet pipe and chemical feed pipe, tangentially inject by nozzle, former water is injected on the active blade of rabbling mechanism, the rotation of promotion rabbling mechanism, utilize the effect of entrainmenting of jet and the stirring of rabbling mechanism, realize mixing of medicament and former water in the short period of time, reaction generates flco, forms one-level and handles former water.One-level is handled former water and second kind of medicament and is entered second coagulating chamber through nozzle and No. two chemical feed pipes and carry out hybrid reaction.The former water of two stage treatment after the abundant hybrid reaction of second coagulating chamber and the third medicament enter the further hybrid reaction of the 3rd coagulating chamber through nozzle and No. three chemical feed pipes.The former water that contains great quantity of floc after reaction is finished is discharged by the bottom of central reaction tube, and great quantity of floc is slipped to the urceolus inner bottom part by the slip awl.The former water that contains a small amount of flco returns through on the water-locator, than the silt of small particle diameter and suspension coalescent growing up when the swash plate, falls back to the urceolus inner bottom part.Purify waste water and discharged by the top drainpipe, the urceolus inner bottom part is heaped the silt that forms by flco and is discharged by discharge pipeline.
The utility model is rational in infrastructure simple, manufactures easily, and cost is low.Volume is little, good integrity, and area occupied is few, utilizes former hydrodynamic force to mix energy savings.The several separate coagulating chamber is set, realizes that in an equipment various medicaments adds according to certain order and ratio, finish abundant mixing, reaction, flocculation, the precipitation of medicament and former water simultaneously.The water treatment efficiency height, quality is good, and excellent popularization application market prospect is arranged.
Description of drawings
Accompanying drawing 1 is a structural representation of the present utility model, and 1 urceolus, 2 central reaction tubes, 3 water inlet pipes, No. 4 chemical feed pipes, 5 No. two chemical feed pipes, 6 No. three chemical feed pipes, 7 swash plates, 8 water-locators, 9 sliies awl, 10 discharge pipelines, 11 drainpipes, 12 shafts prop up Cuo, 13 shafts, 14 active blades, 15 stirring vanes, 16 nozzles, 17 dividing plates among the figure.
The specific embodiment
Narrate case study on implementation of the present utility model below in conjunction with accompanying drawing.
Central reaction tube and slip awl is set in urceolus, and the slip awl is arranged on the bottom of central reaction tube.In the annular chamber between urceolus and the central reaction tube, the bottom is provided with water-locator, and top is provided with swash plate.Central reaction tube inner-use clapboard is separated into three relatively independent coagulating chambers, from top to bottom, be provided with in first, second coagulating chamber by shaft and prop up the rabbling mechanism that Cuo, shaft, stirring vane, active blade constitute, the nozzle of jet flow from top to bottom is set between the adjacent coagulating chamber.The former water water inlet pipe mouth of first coagulating chamber is installed nozzle, and the track of the direction of nozzle ejection and active blade rotation is tangent or crossing, and the water of nozzle ejection is sprayed on the active blade, promotes rabbling mechanism and rotates.Each coagulating chamber is provided with the flocculant chemical feed pipe respectively, and the chemical feed pipe of first coagulating chamber is connected with water inlet pipe, and the dosing mouth of pipe correspondence of second, third coagulating chamber between one, two coagulating chambers and the nozzle that is provided with between two, three coagulating chambers.The top of urceolus is provided with drainpipe, and the bottom is provided with discharge pipeline.
Claims (4)
1, a kind of eddy flow hybrid reaction settler, it is characterized in that settler has central reaction tube (2), the slip awl (9) that is provided with in a urceolus (1) and the urceolus, the slip awl is arranged on the central reaction tube bottom, looping chamber between central reaction drum outer wall and the outer tube inner wall, swash plate (7), water-locator (8) are installed in the annular chamber, central reaction tube inner-use clapboard (17) is separated into separate coagulating chamber, and rabbling mechanism is installed in the coagulating chamber.
2, according to the said eddy flow hybrid reaction of claim 1 settler, it is characterized in that said rabbling mechanism has active blade (14), shaft (13), stirring vane (15), shaft to prop up Cuo (12), shaft props up in the Cuo coagulating chamber by shaft, and active blade, stirring vane are installed on the shaft.
3, according to the said eddy flow hybrid reaction of claim 1 settler, it is characterized in that said separate coagulating chamber is provided with chemical feed pipe (4) and nozzle (16), the track of the emission direction of nozzle and active blade (14) rotation is tangent or crossing.
4,, it is characterized in that said swash plate (7) structure is multi-layer sheet filler and/or corrugated plate packing according to the said eddy flow hybrid reaction of claim 1 settler.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 01245443 CN2520929Y (en) | 2001-08-20 | 2001-08-20 | Cyclone mixing reaction settler |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 01245443 CN2520929Y (en) | 2001-08-20 | 2001-08-20 | Cyclone mixing reaction settler |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2520929Y true CN2520929Y (en) | 2002-11-20 |
Family
ID=33656695
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 01245443 Expired - Fee Related CN2520929Y (en) | 2001-08-20 | 2001-08-20 | Cyclone mixing reaction settler |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2520929Y (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102580366A (en) * | 2012-03-09 | 2012-07-18 | 中国水电顾问集团成都勘测设计研究院 | High-concentration suspended matter wastewater treatment system and technology and flocculation inclined plate precipitation equipment |
| CN105540702A (en) * | 2016-02-22 | 2016-05-04 | 西安晨宇环境工程有限公司 | Multiphase vortex mixed water distributor |
| CN106495297A (en) * | 2016-11-25 | 2017-03-15 | 江苏鼎弘环境科技有限公司 | One-step method advanced waste treatment system |
| CN109133297A (en) * | 2017-12-05 | 2019-01-04 | 广州市地龙环保技术有限公司 | A kind of precipitation reaction pond |
| CN110090473A (en) * | 2018-01-31 | 2019-08-06 | 沈阳铝镁设计研究院有限公司 | A kind of separation of solid and liquid feeding device |
-
2001
- 2001-08-20 CN CN 01245443 patent/CN2520929Y/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102580366A (en) * | 2012-03-09 | 2012-07-18 | 中国水电顾问集团成都勘测设计研究院 | High-concentration suspended matter wastewater treatment system and technology and flocculation inclined plate precipitation equipment |
| CN105540702A (en) * | 2016-02-22 | 2016-05-04 | 西安晨宇环境工程有限公司 | Multiphase vortex mixed water distributor |
| CN105540702B (en) * | 2016-02-22 | 2018-03-30 | 西安晨宇环境工程有限公司 | A kind of multiphase eddy flow mixing water-locator |
| CN106495297A (en) * | 2016-11-25 | 2017-03-15 | 江苏鼎弘环境科技有限公司 | One-step method advanced waste treatment system |
| CN109133297A (en) * | 2017-12-05 | 2019-01-04 | 广州市地龙环保技术有限公司 | A kind of precipitation reaction pond |
| CN110090473A (en) * | 2018-01-31 | 2019-08-06 | 沈阳铝镁设计研究院有限公司 | A kind of separation of solid and liquid feeding device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20021120 Termination date: 20090921 |