CN2258099Y - Multi-ring plate cyclone flocculation separator - Google Patents
Multi-ring plate cyclone flocculation separator Download PDFInfo
- Publication number
- CN2258099Y CN2258099Y CN 96231204 CN96231204U CN2258099Y CN 2258099 Y CN2258099 Y CN 2258099Y CN 96231204 CN96231204 CN 96231204 CN 96231204 U CN96231204 U CN 96231204U CN 2258099 Y CN2258099 Y CN 2258099Y
- Authority
- CN
- China
- Prior art keywords
- housing
- overflow pipe
- concentric ring
- eddy flow
- flocculation
- 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
- 238000005189 flocculation Methods 0.000 title claims abstract description 22
- 230000016615 flocculation Effects 0.000 title claims abstract description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 27
- 238000000926 separation method Methods 0.000 claims abstract description 13
- 238000007599 discharging Methods 0.000 claims description 7
- 238000006243 chemical reaction Methods 0.000 abstract description 9
- 230000000694 effects Effects 0.000 abstract description 7
- 239000008187 granular material Substances 0.000 abstract description 5
- 238000006073 displacement reaction Methods 0.000 abstract 1
- 239000010802 sludge Substances 0.000 abstract 1
- 239000002245 particle Substances 0.000 description 9
- 238000004062 sedimentation Methods 0.000 description 5
- 239000000463 material Substances 0.000 description 2
- 239000003814 drug Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
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- Cyclones (AREA)
Abstract
A multi-ring plate cyclone flocculation separator comprises a plurality of concentric ring plates and an overflow pipe, wherein the concentric ring plates and the overflow pipe are arranged inside the cyclone flocculation separator, the lower end of the overflow pipe extends out of a shell, an overflow groove is formed in the upper side of each concentric ring plate, one end of the overflow groove is communicated with the upper end of the overflow pipe, a tangential water inlet is formed in a barrel body of the shell, and a sludge discharge hole is formed in the bottom of a cone of the. This separator has adopted a plurality of concentric ring shaped plates, and the granule through flocculation reaction is fast and the radial displacement distance is short under the effect of hydraulic cyclone centrifugal force to make flocculation separation time greatly shorten, equipment is small, and the treatment effeciency is high. Has good treatment effect on water with suspended matters of any concentration.
Description
The utility model relates to a kind of device of water treatment, a kind of multi-annular plate eddy flow flocculation separation device that is used for water treatment of more specifically saying so.
At present, the capital equipment of water treatment has three kinds: 1. hydraulic cyclone sedimentation basin, and utilize tangential water inlet to cause hydraulic cyclone, remove bigger or heavier particle in the water with the centrifugal force that eddy flow forms.But when removing less or lighter particle, poor effect.Even if when the adding flocculant carried out water treatment, effect was also very poor.2. inclined-plate clarifying basin, utilize the parallel tilting flat board of polylith to shorten the sedimentation time of particle, to containing less or when handling than the water of light grains thing, flocculation reaction is carried out in adding by flocculant, reacted water feeds inclined-plate clarifying basin again, because flocculation reaction equipment is subjected to the restriction of technology, and be difficult to be combined into one with sedimentation basin, therefore, the overall device volume is big, many with material, and floor space is bigger, when handling the low concentrations of particulates thing, because granule density is low, flocculation reaction is incomplete, poor processing effect.3. circulatior clarifier, particle and water inlet that the jet action suction that utilizes water inlet to form has precipitated are mixed together, thereby have strengthened the granule density of flocculation reaction, make flocculation reaction more complete.But because the separation of particle relies on gravity, therefore, the sedimentation time is longer, and equipment volume is bigger.
The utility model purpose provides the efficient multi-annular plate eddy flow flocculation separation device that a kind of volume is little, material is economized, cost is low, treatment effect is good.
The purpose of this utility model can realize in the following manner: a kind of eddy flow flocculation separation device that is used for water treatment, including top is housing cylindric, that the bottom is inverted cone shape, overflow pipe is arranged on the housing middle part, and housing is stretched out in the lower end, several concentric ring-shaped being arranged in the housing top, at concentric ring-shaped upside, be provided with the spilling water groove that is no less than, and an end communicates with overflow pipe, the sidewall of housing is provided with tangential water inlet, the cone base of housing is provided with mud discharging mouth, the housing stent support.
The utility model compared with prior art has following effect: contain the water of suspended particulate, behind the adding flocculant, tangentially sent in the housing through water inlet by the pump pressurization, form hydraulic cyclone.Under the acting in conjunction of medicament and centrifugal force field, particle increases gradually, to the annular slab enrichment, and further contact-impact, form the bulky grain floc sedimentation, glide along the plate face, fall conical base, discharge from tangential mud discharging mouth.
In eddy flow flocculation reaction process, sink to the part particle of cone, upwards reflux along the center once more at the eddy flow enrichment region, and mix, thereby strengthen the granule density that participates in reaction with water inlet.
In whole water treatment procedure,, react more complete owing to participate in the granule density height of reaction, under action of centrifugal force, the particle translational speed is fast, and the annular slab spacing is little, it is short that particle moves radially distance, thereby the flocculation separation time is shortened dramatically, and reduced equipment volume.
Description of drawings:
Accompanying drawing 1 is a structure cutaway view of the present utility model.
Accompanying drawing 2 is structure vertical views of the present utility model.
The utility model is described in further detail with reference to the accompanying drawings:
Shown in accompanying drawing 1,2: a kind of multi-annular plate eddy flow flocculation separation device, include thin wall shape housing 3, top is cylindric, and the bottom is reverse taper, and overflow pipe 4 is arranged on the middle part of housing 3, and housing 3 is stretched out in its lower end.In the top of housing 3, be provided with several concentric ring-shaped 2, described concentric ring flat-plate 2 is concentric with housing 3, upside concentric ring-shaped 2 is provided with at least one spilling water groove 1, and an end of spilling water groove 1 communicates with overflow pipe 4, and the water in the spilling water groove 1 is discharged through overflow pipe 4.Described overflow pipe 4 is concentric with housing 3.Be arranged at least one tangential water inlet 5 in the cylinder bottom of housing 3, the cone base of housing 3 is provided with mud discharging mouth 6.Described mud discharging mouth 6 tangentially is provided with.Housing 3 usefulness supports 7 are propped.
Claims (5)
1. multi-annular plate eddy flow flocculation separation device that is used for water treatment, it is characterized in that: it is cylindric including top, the bottom is the housing (3) of inverted cone shape, overflow pipe (4) is arranged on housing (3) middle part, and housing (3) is stretched out in the lower end, several concentric ring-shaped (2) are arranged in housing (3) top, upside in concentric ring-shaped (2), be provided with and be no less than a spilling water groove (1), and an end communicates with overflow pipe (4), the sidewall of housing (3) is provided with tangential water inlet (5), the cone base of housing (3) is provided with mud discharging mouth (6), and housing (3) supports with support (7).
2. eddy flow flocculation separation device according to claim 1 is characterized in that: described concentric ring-shaped (2) are concentric with housing (3).
3. eddy flow flocculation separation device according to claim 1 and 2 is characterized in that: described overflow pipe (4) is concentric with housing (3).
4. eddy flow flocculation separation device according to claim 1 and 2 is characterized in that: described mud discharging mouth (6) is tangential to be provided with.
5. eddy flow flocculation separation device according to claim 3 is characterized in that: described mud discharging mouth (6) is tangential to be provided with.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 96231204 CN2258099Y (en) | 1996-01-31 | 1996-01-31 | Multi-ring plate cyclone flocculation separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 96231204 CN2258099Y (en) | 1996-01-31 | 1996-01-31 | Multi-ring plate cyclone flocculation separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2258099Y true CN2258099Y (en) | 1997-07-23 |
Family
ID=33908442
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 96231204 Expired - Fee Related CN2258099Y (en) | 1996-01-31 | 1996-01-31 | Multi-ring plate cyclone flocculation separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2258099Y (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102886164A (en) * | 2012-10-23 | 2013-01-23 | 曹会勋 | Aquaculture water processing device and method |
| CN106044944A (en) * | 2016-07-14 | 2016-10-26 | 宣尧杭 | Mud-water separator |
| CN107032463A (en) * | 2017-04-25 | 2017-08-11 | 煤科集团杭州环保研究院有限公司 | A kind of municipal treatment device for overflow sewage and method |
| 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 |
| CN111111270A (en) * | 2020-01-06 | 2020-05-08 | 中国矿业大学 | Novel flocculating agent and ore pulp stirring and mixing process and device |
-
1996
- 1996-01-31 CN CN 96231204 patent/CN2258099Y/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102886164A (en) * | 2012-10-23 | 2013-01-23 | 曹会勋 | Aquaculture water processing device and method |
| CN102886164B (en) * | 2012-10-23 | 2014-12-03 | 曹会勋 | Aquaculture water processing device and method |
| CN106044944A (en) * | 2016-07-14 | 2016-10-26 | 宣尧杭 | Mud-water separator |
| CN106044944B (en) * | 2016-07-14 | 2022-05-10 | 宣尧杭 | Mud-water separator |
| CN107032463A (en) * | 2017-04-25 | 2017-08-11 | 煤科集团杭州环保研究院有限公司 | A kind of municipal treatment device for overflow sewage and method |
| CN107032463B (en) * | 2017-04-25 | 2019-05-10 | 煤科集团杭州环保研究院有限公司 | A kind of municipal administration treatment device for overflow sewage and method |
| 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 |
| CN111111270A (en) * | 2020-01-06 | 2020-05-08 | 中国矿业大学 | Novel flocculating agent and ore pulp stirring and mixing process and device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |