CN108273293A - A kind of difunctional heavy sliding purifier of cross type and the sedimentation basin with the purifier - Google Patents
A kind of difunctional heavy sliding purifier of cross type and the sedimentation basin with the purifier Download PDFInfo
- Publication number
- CN108273293A CN108273293A CN201810000298.4A CN201810000298A CN108273293A CN 108273293 A CN108273293 A CN 108273293A CN 201810000298 A CN201810000298 A CN 201810000298A CN 108273293 A CN108273293 A CN 108273293A
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- Prior art keywords
- purifier
- difunctional
- cross type
- sediment
- deflector
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Links
- 238000004062 sedimentation Methods 0.000 title claims abstract description 20
- 239000013049 sediment Substances 0.000 claims abstract description 41
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 39
- 239000012530 fluid Substances 0.000 claims abstract description 15
- 229910001220 stainless steel Inorganic materials 0.000 claims description 6
- 239000010935 stainless steel Substances 0.000 claims description 6
- 230000006641 stabilisation Effects 0.000 claims description 5
- 238000011105 stabilization Methods 0.000 claims description 5
- 241000276425 Xiphophorus maculatus Species 0.000 claims description 4
- 239000004744 fabric Substances 0.000 claims description 4
- 238000004080 punching Methods 0.000 claims description 4
- 238000000926 separation method Methods 0.000 claims description 4
- 230000037431 insertion Effects 0.000 claims 1
- 238000003780 insertion Methods 0.000 claims 1
- 238000000746 purification Methods 0.000 abstract description 15
- 239000002245 particle Substances 0.000 abstract description 8
- 230000000694 effects Effects 0.000 description 18
- 230000015572 biosynthetic process Effects 0.000 description 9
- 238000001556 precipitation Methods 0.000 description 8
- 239000002244 precipitate Substances 0.000 description 6
- 238000005189 flocculation Methods 0.000 description 5
- 230000016615 flocculation Effects 0.000 description 5
- 230000002265 prevention Effects 0.000 description 5
- 230000002776 aggregation Effects 0.000 description 4
- 238000004220 aggregation Methods 0.000 description 4
- 238000010276 construction Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000004140 cleaning Methods 0.000 description 3
- 239000004567 concrete Substances 0.000 description 3
- 238000000151 deposition Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 239000010802 sludge Substances 0.000 description 3
- 238000005352 clarification Methods 0.000 description 2
- 230000008021 deposition Effects 0.000 description 2
- 230000002706 hydrostatic effect Effects 0.000 description 2
- 230000013011 mating Effects 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 238000001226 reprecipitation Methods 0.000 description 2
- 238000007790 scraping Methods 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 229920002472 Starch Polymers 0.000 description 1
- 230000001133 acceleration Effects 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 230000008719 thickening Effects 0.000 description 1
- 235000012773 waffles Nutrition 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/02—Settling tanks with single outlets for the separated liquid
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/0003—Making of sedimentation devices, structural details thereof, e.g. prefabricated parts
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/0015—Controlling the inclination of settling devices
Abstract
It the invention discloses a kind of difunctional heavy sliding purifier of cross type and with the sedimentation basin of the purifier, is arranged by multigroup settlement section, the settlement section includes deflector and the multi-disc wing plate set up and down for draining sediment；It states deflector and is equipped with the whirlpool area being formed between multiple protrusions that water (flow) direction is intervally arranged, adjacent projection for making fluid form vortex.Sediment coacervating large particle sediment can be accelerated purification efficiency, improves purification efficiency, at least improve to 3 times or more of the prior art by the vortex that flow can be formed in whirlpool area in the present invention.
Description
Technical field
The invention belongs to technical field of water purification, more particularly, to a kind of difunctional heavy sliding purifier of cross type and with this
The sedimentation basin of purifier.
Background technology
In traditional purifying water process technical matters, in order to make in water containing tiny suspended particulate as early as possible, effectively under
Heavy realization is separated from water, and the prior art is to increase Particle Acceleration sedimentation separation in water, improves hydraulic surface loading and sludge
The density of grain often forms anisotropic flow mud-water separation using the measure of filling separation inclined tube or inclined plate in clarification or sedimentation basin
Clarification accelerates precipitation, improves water treatment efficiency, reduces floor space, reduce the method for construction investment.The settler is extensive
Applied in sedimentation pond for water treatment and settling apparatus, be at present in Water and Waste Water Engineering use most extensive and ripe one
Water treatment facilities device, it is applied widely, it is suitable for water inlet desanding, general industry and domestic water precipitate, settlement of sewage,
The processing such as oil removal and Tailing thickening, are particularly suitable for water factory and sewage treatment project.
Chinese patent CN103585798B discloses one kind《Eddy current type solid-liquid diversion purifier and have the purifier
Settling tank》, for the purifier by the way that vortex region is arranged on wing plate, the formation vortex on wing plate accelerates the precipitation to flow.
Due to being arranged on wing plate when vortex region, to which vortex will be respectively formed on every layer of wing plate under this kind of structure, thus
When precipitation, multiple vortex easy to produce the situation for influencing each other, and then turbulent flow occur, influence sedimentation effect, cleaning water is poor.
Invention content
The present invention for overcome the deficiencies in the prior art, it is difunctional to provide a kind of cross type that purifying water effect is good, efficient
Heavy sliding purifier and the sedimentation basin with the purifier.
To achieve the goals above, the present invention uses following technical scheme：A kind of difunctional heavy sliding purifier of cross type,
It is arranged by multigroup settlement section, the settlement section includes deflector and the multi-disc for draining sediment is in setting up and down
Wing plate；State deflector be equipped be formed between multiple protrusions that water (flow) direction is intervally arranged, adjacent projection for making stream
Body forms the whirlpool area of vortex.Protrusion of the present invention is set up directly on deflector, to be formed by rotation between adjacent projection
Whirlpool area is the whole vortex region by being formed on deflector length direction, is inside formed by as the vortex of an entirety；It compares
Be not in the situation of turbulent flow for the case where traditional layering forms vortex, the vortex of formation remains unified direction,
Accelerate the flocculation of sediment, promotes cleaning water；And vortex region is formed between adjacent two protrusion, to which flow is caused in protrusion
Certain barrier effect avoids opposite jet flow from hitting to vortex region, is in hydrostatic to which vortex region maintains hydrostatic state always
The micro- vortex formed under state, compared to traditional for the case where vortex area is set on wing plate, be not in vortex by
To the situation of flow disorder, ensure that sedimentation effect is good.
By the formation in whirlpool area, the passive precipitation of sediment can be adjusted to actively to precipitate, flow can be in whirlpool area
Interior formation vortex, and then will coacervating large particle sediment be reinforced by the sediment slid on wing plate, accelerate purification efficiency, carries
High purification efficiency, is at least improved to 3 times or more of the prior art；And vortex formation will also can originally be difficult to precipitate it is tiny
Sediment force aggregation flocculation at can by the particle sediment from reprecipitation, enhance sedimentation effect, substantially improve water purification matter
Amount；Secondly, the dosage for reducing flocculant of high degree is gone back in the formation of vortex, achievees the effect that energy-saving consumption-reducing；Precipitation portion
Part can be directly realized by spoil disposal by whirlpool area, or quick spoil disposal, high degree can be realized in the spoil disposal channel for only needing setting smaller
Save space, reduce land area, improve land utilization ratio, the cost for thereby reducing construction and using.
Further, the deflector is one-time formed stainless steel wave plate；Integrally formed structure is very simple, does not deposit
The mutual splicing the case where, scrape that mud is existing, and later period maintenance, cleaning are more convenient to be less prone to；And due to entire
Deflector one-pass molding intersects traditional layer so that vortex region is the whole vortex by settlement section upper end to lower end
To for the mode of vortex, sedimentation effect is more preferable.
Further, the deflector is one time punching molded.
Further, the deflector, which corresponds to influent side, has the drainage face being obliquely installed；Drainage is played to flow
Effect, avoids the side wall in protrusion from the phenomenon that scraping mud occur.
Further, the protrusion is connected with the wing plate by connector, so as to be formed for heavy between protrusion and wing plate
The drain outlet that starch circulates downwards；The protrusion is connected with the wing plate by connector, so that shape between protrusion and wing plate
At the drain outlet circulated downwards for sediment；Ensure that the sediment for depositing and sliding on wing plate can be downward by drain outlet
Circulation, avoids the occurrence of precipitate bulk and occurs the case where scraping mud on protrusion and the junction or protrusion of wing plate, is convenient for the later stage
It repairs and clears up.
Preferably, the connector is platy structure；Be not in hang on the position of platy structure setting guarantee connector
The case where mud.
Preferably, the connector is equipped with the throughbore for circulating for fluid；Reduce connector to cause with flow
Resistance, secondly also can avoid connector on occur hang mud the phenomenon that.
Preferably, the wing plate has the first gradient slid downwards convenient for sediment；Sediment can be along inclination
Degree quickly slides downwards and then is expelled in the storage mud sump of bottom, accelerates deposition efficiency.
Further preferably, the deflector has the second gradient slid downwards convenient for sediment；Sediment can be along inclining
Gradient quickly slides downwards and then is expelled in the storage mud sump of bottom, accelerates deposition efficiency.
Further, be intervally arranged the plug division for having and being inserted into for the wing plate along its length on the connector；It realizes
Mating between wing plate and connector, easy to process, wing plate is convenient for disassembly and assembly with connector, and installation effectiveness is high.
Further, the disconnecting prevention structure for being limited to connector is equipped between the connector and the protrusion；
Connector is avoided to be detached from from protrusion, failure rate is low, and service life is long.
Further, the disconnecting prevention structure includes being set to the Connection protrusion on the connector, being set on the protrusion for being somebody's turn to do
The connection opening and the anti-falling piece in the Connection protrusion that Connection protrusion passes through；By the way that Connection protrusion is inserted into connection opening
In, then anti-falling piece is connected with Connection protrusion, deviate from outward in avoiding Connection protrusion from being open by connection, anticreep good positioning effect,
And simple in structure, easy to process and assembly.
The invention also discloses a kind of difunctional sedimentation basin of cross type, including pond body, it is equipped with inhalant region in the pond body, supplies
The purifying area and exhalant region that fluid is detached with sediment, the purifying area is interior to be equipped with above-mentioned purifier；Purifier is by more
Group precipitation arrangement of parts forms, and the settlement section includes deflector and the multi-disc wing set up and down for draining sediment
Plate；State deflector be equipped be formed between multiple protrusions that water (flow) direction is intervally arranged, adjacent projection for making fluid shape
At the whirlpool area of vortex.The passive precipitation of sediment can be adjusted to actively to precipitate, flow by the present invention by the formation in whirlpool area
Vortex can be formed in whirlpool area, and then will coacervating large particle sediment be reinforced by the sediment slid on wing plate, added
Fast purification efficiency improves purification efficiency, at least improves to 3 times or more of the prior art；And vortex formation can also will originally
Be difficult to the fine precipitates precipitated force aggregation flocculation at can by the particle sediment from reprecipitation, enhance sedimentation effect,
Substantially improve water purification quality；Secondly, the dosage for reducing flocculant of high degree is gone back in the formation of vortex, reaches energy-saving consumption-reducing
Effect；Settlement section can be directly realized by spoil disposal by whirlpool area, or the spoil disposal channel for only needing setting smaller can be realized quickly
Spoil disposal, high degree save space, reduce land area, improve land utilization ratio, thereby reduce construction and use
Cost.
Further, it is equipped with the cloth wet part for evenly dispersed fluid in the inhalant region, is equipped in the exhalant region
Current stabilization component for evenly dispersed fluid；By the setting of cloth wet part and current stabilization component, the flow velocity of stationary flow and uniformly
Water outlet status ensures that flow carries out uniformly water inlet and uniformly water outlet.
In conclusion the present invention has the following advantages：1, the vortex that flow is formed in whirlpool area can agglomerate sediment
At bulky grain sediment, accelerates purification efficiency, improve purification efficiency, at least improve to 3 times or more of the prior art；2, for
Aggregation flocculation can be forced into particle sediment by being difficult to the fine precipitates precipitated also, enhanced sedimentation effect, substantially improved water purification
Quality；3, the dosage for reducing flocculant, achievees the effect that energy-saving consumption-reducing；4, space is saved, land area is reduced, improves soil
Ground utilization rate, the cost for thereby reducing construction and using.
Description of the drawings
Fig. 1 is the structural diagram of the present invention.
Fig. 2 is the structural schematic diagram of settlement section in the present invention.
Fig. 3 is the vertical view of the present invention.
Fig. 4 is the sectional view of settlement section of the present invention.
Fig. 5 is the structural schematic diagram of sedimentation basin in the present invention.
Specific implementation mode
In order to make those skilled in the art be better understood from the present invention program, below in conjunction in the embodiment of the present invention
Attached drawing, technical solution in the embodiment of the present invention carry out clear, complete description.
As shown in Figs. 1-5, the difunctional heavy sliding purifier of a kind of cross type, is arranged in order by multigroup settlement section,
According to use environment difference, such as can vertically be arranged, or arrange along its length there are many building form；It is described
Settlement section includes deflector 1 and the multi-disc wing plate 2 set up and down for draining sediment；Deflector 1 is stainless steel plate,
For guiding sediment to flow downward, the wing plate 2 is also stainless steel plate, and wing plate 2 is arranged along the flow direction of fluid, Yu Benfa
In bright, the flow direction of fluid is horizontal direction, so wing plate is also horizontally disposed；The deflector 1 is equipped with edge
Multiple protrusions 11 that water (flow) direction is intervally arranged, and the whirlpool area for making fluid form vortex is formed between adjacent projection 11
12；Specifically, the protrusion is integrally formed with deflector and is made, it is convex by forming this after the direct punching press of deflector or bending
Portion；The protrusion 11 can be half hexagon, semicircle, triangle etc. so that deflector is shaped to honeycomb duct, corrugated sheet, semicircle
The structures such as shape corrugated sheet, triangular waveform plate, the part that certain above-mentioned shape is at least enumerated, not to the limit of protection domain
Fixed, specific structure is depending on actual conditions；Due to the vortex that flow can be formed in whirlpool area, sediment can be agglomerated
At bulky grain sediment, accelerates purification efficiency, improve purification efficiency；And the fine precipitates for being difficult to precipitate also can be strong
System aggregation flocculation enhances sedimentation effect, substantially improves water purification quality at particle sediment；Meanwhile the setting in whirlpool area is also reduced
The dosage of flocculant, achievees the effect that energy-saving consumption-reducing.
The deflector 1 is one-time formed stainless steel wave plate, specifically, the deflector 1 is one time punching molded, specifically
Principle is the prior art；The deflector 1, which corresponds to influent side, has the drainage face 13 being obliquely installed, and the drainage face 13 is by water conservancy diversion
The front end of plate is bent to form to side.
Preferably, the wing plate 2 has the first gradient inclined from top to bottom slid downwards convenient for sediment,
First gradient may be configured as 60 °, i.e. angle between wing plate and deflector is 60 °；It is described to lead in order to promote sludge discharge effects
Flowing plate 1 is whole to be also configured as tilting so that deflector has slid downwards convenient for sediment inclined from top to bottom second to incline
Gradient, second gradient may be configured as 60 °, i.e. angle between the axis and vertical line of deflector is 60 °；Certainly, Yu Qi
In his embodiment, deflector can be set to vertical state, only setting wing plate to opposite flow plate tilts；It also can be only by water conservancy diversion
Plate is set as tilting, and wing plate can achieve the effect that good drainage sediment relative to being arranged perpendicular to deflector.
Further, the protrusion 11 is connected with the wing plate 2 by connector 3, and the connector 3 is platy structure,
Specifically, the connector 3 is the longitudinally disposed stainless steel plate along protrusion, which is connected with protrusion, side and
Wing plate is connected；To between wing plate bottom side and protrusion by with certain gap, to form the row to circulate downwards for sediment
Dirty channel 4；Specifically, being intervally arranged along its length on the connector 3 has multiple plug divisions 32, which is and the wing
The corresponding open slot of thickness of plate, the wing plate 2 are inserted into the open slot, are realized mating with connector；Grafting
The angle of inclination of slot is not specifically limited herein depending on the angle of wing plate actual setting；Preferably, the connector 3
On it is upper along its length it is evenly spaced multiple throughbores 31 are distributed with, which can be to be arranged on connector
Round, rectangular, elliptical openings can directly be circulated by these throughbores 31 to which flow is in circulation, avoid water backward
Stream is by excessive resistance.
As shown in Figure 3-4, it is equipped with disconnecting prevention structure between the connector 3 and the protrusion 11, passes through the disconnecting prevention structure pair
Connector is limited, and connector is avoided to be disengaged from protrusion；Specifically, the disconnecting prevention structure includes along the length side of connector
To the multiple Connection protrusions 51 being spaced apart, the company is open and is set to for the connection that the Connection protrusion passes through on the protrusion
The anti-falling piece 53 on protrusion is connect, the Connection protrusion 51 is directed out by the side of the connector and extended to form, and the connection is opened
The shape size of mouth is set as matching with the Connection protrusion；The anti-falling piece 53 is a bolt, when Connection protrusion 51 passes through institute
State connection opening after, bolt can be connected to Connection protrusion 51 be pierced by connection opening position on, avoid Connection protrusion 51 by even
It connects in opening.
The direction of arrow is water (flow) direction in Fig. 1 and Fig. 5, and flow flows through settlement section, wing plate pair by arrival end when operation
Flow carries out layering water conservancy diversion, in precipitate to wing plate upper surface, and is slid downwards along wing plate；Meanwhile flow flows through whirlpool
Whirlpool area simultaneously forms vortex in whirlpool area, and the tiny suspended particulate in the sediment slid on wing plate and flow is forced to be condensed into
Bulky grain sediment is precipitated to downwards whirlpool area bottom later.
A kind of difunctional sedimentation basin of cross type is equipped with inhalant region 61, supplies as shown in figure 5, including pond body 6 in the pond body 6
The purifying area 62 and exhalant region 63 that fluid is detached with sediment, the purifying area 62 is interior to be equipped with above-mentioned purifier, herein not
Structure is repeated again；According to the volume and size of pond body 6, can be superimposed up and down, laying is more side by side for front and back superposition or left and right
Group precipitation component；Cloth wet part 7 is equipped in the inhalant region 61, which is made of plastics or metal or concrete
Water distributing plate 71 and the multiple water distributing pores 72 being distributed on the water distributing plate 71, disperse flow by the setting of through-hole,
Flow is uniformly flowed into settlement section, purifying water effect is promoted；Further, it also is provided in the exhalant region 63
Current stabilization component 8, the current stabilization component 8 are stabilier 81 made of plastics or metal or concrete and are distributed in the stabilier 81
On multiple through-holes 82 flow of water outlet is disperseed by the setting of through-hole 82 so that water outlet is uniform；The purifying area
Bottom be equipped with holder 91, which can be the concrete pier or waffle slab of strip, and settlement section can be placed on the holder,
Funnelform bucket 92 is equipped with below holder can continue to sink down into bucket after sediment is precipitated to whirlpool area bottom downwards,
Finally pass through sludge pipe to be discharged.
Obviously, described embodiment is only a part of the embodiment of the present invention, instead of all the embodiments.It is based on
Embodiment in the present invention, it is obtained by those of ordinary skill in the art without making creative efforts every other
Embodiment should all belong to the scope of protection of the invention.
Claims (10)
1. a kind of difunctional heavy sliding purifier of cross type, is arranged by multigroup settlement section, the settlement section includes leading
Flowing plate（1）With the multi-disc wing plate set up and down for draining sediment（2）；It is characterized in that：The deflector（1）On set
Have along multiple protrusions that water (flow) direction is intervally arranged（11）, adjacent projection（11）Between be formed with for make fluid formed vortex
Whirlpool area（12）.
2. the difunctional heavy sliding purifier of cross type according to claim 1, it is characterised in that：The deflector（1）For
One-time formed stainless steel wave plate.
3. the difunctional heavy sliding purifier of cross type according to claim 1, it is characterised in that：The deflector（1）For
It is one time punching molded.
4. the difunctional heavy sliding purifier of cross type according to claim 1, it is characterised in that：The deflector（1）It is right
There should be the drainage face being obliquely installed in influent side（13）.
5. the difunctional heavy sliding purifier of cross type according to claim 1, it is characterised in that：The protrusion（11）With institute
State wing plate（2）Pass through connector（3）It is connected, so that protrusion（11）With wing plate（2）Between form the row that circulates downwards for sediment
Dirty channel（4）.
6. the difunctional heavy sliding purifier of cross type according to claim 5, it is characterised in that：The connector（3）For
Platy structure.
7. the difunctional heavy sliding purifier of cross type according to claim 1, it is characterised in that：The connector（3）On
Equipped with the throughbore for circulating for fluid（31）.
8. the difunctional heavy sliding purifier of cross type according to claim 1, it is characterised in that：The connector（3）On
Being intervally arranged along its length has for the wing plate（2）The plug division of insertion（32）.
9. a kind of difunctional sedimentation basin of cross type, including pond body（6）, the pond body（6）It is interior to be equipped with inhalant region（61）, for fluid with
The purifying area of sediment separation（62）And exhalant region（63）, it is characterised in that：The purifying area（62）It is interior to be equipped with such as claim
Purifier described in any one of 1-8.
10. the difunctional sedimentation basin of cross type according to claim 9, it is characterised in that：The inhalant region（61）Inside it is equipped with
Cloth wet part for evenly dispersed fluid（7）, the exhalant region（63）The interior current stabilization component being equipped with for evenly dispersed fluid
（8）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810000298.4A CN108273293A (en) | 2018-01-01 | 2018-01-01 | A kind of difunctional heavy sliding purifier of cross type and the sedimentation basin with the purifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810000298.4A CN108273293A (en) | 2018-01-01 | 2018-01-01 | A kind of difunctional heavy sliding purifier of cross type and the sedimentation basin with the purifier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108273293A true CN108273293A (en) | 2018-07-13 |
Family
ID=62802877
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810000298.4A Pending CN108273293A (en) | 2018-01-01 | 2018-01-01 | A kind of difunctional heavy sliding purifier of cross type and the sedimentation basin with the purifier |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108273293A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111499088A (en) * | 2020-06-29 | 2020-08-07 | 北京图腾猎技科技有限公司 | Efficient coal chemical wastewater treatment device and method |
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|---|---|---|---|---|
| CN101843992A (en) * | 2009-03-23 | 2010-09-29 | 甘肃金桥给水排水设计与工程(集团)有限公司 | Vortex settling pond |
| CN202052360U (en) * | 2011-01-31 | 2011-11-30 | 章雪峰 | Horizontal-flow honeycomb cell type sedimentation device |
| CN103301658A (en) * | 2013-04-27 | 2013-09-18 | 江苏中超环保有限公司 | Efficient micro-resistance pulsating vortex sedimentation device |
| CN103585798A (en) * | 2013-11-17 | 2014-02-19 | 池万青 | Vortex type solid-liquid diversion purification device and sedimentation tank provided with same |
| CN206103424U (en) * | 2016-06-02 | 2017-04-19 | 浙江联池水务设备股份有限公司 | Compound sedimentation tank of high strength |
| CN208356184U (en) * | 2018-01-01 | 2019-01-11 | 浙江联池水务设备股份有限公司 | The difunctional heavy sliding purification device of cross type and the sedimentation basin with the purification device |
-
2018
- 2018-01-01 CN CN201810000298.4A patent/CN108273293A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101843992A (en) * | 2009-03-23 | 2010-09-29 | 甘肃金桥给水排水设计与工程(集团)有限公司 | Vortex settling pond |
| CN202052360U (en) * | 2011-01-31 | 2011-11-30 | 章雪峰 | Horizontal-flow honeycomb cell type sedimentation device |
| CN103301658A (en) * | 2013-04-27 | 2013-09-18 | 江苏中超环保有限公司 | Efficient micro-resistance pulsating vortex sedimentation device |
| CN103585798A (en) * | 2013-11-17 | 2014-02-19 | 池万青 | Vortex type solid-liquid diversion purification device and sedimentation tank provided with same |
| CN206103424U (en) * | 2016-06-02 | 2017-04-19 | 浙江联池水务设备股份有限公司 | Compound sedimentation tank of high strength |
| CN208356184U (en) * | 2018-01-01 | 2019-01-11 | 浙江联池水务设备股份有限公司 | The difunctional heavy sliding purification device of cross type and the sedimentation basin with the purification device |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111499088A (en) * | 2020-06-29 | 2020-08-07 | 北京图腾猎技科技有限公司 | Efficient coal chemical wastewater treatment device and method |
| CN111499088B (en) * | 2020-06-29 | 2021-04-16 | 呼伦贝尔金新化工有限公司 | Efficient coal chemical wastewater treatment device and method |
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Address after: Room 407, building 18, No. 998, Wenyi West Road, Yuhang District, Hangzhou City, Zhejiang Province 310000 Applicant after: ZHEJIANG LIANCHI WATER EQUIPMENT STOCK Co.,Ltd. Address before: Room 413, building 2, 1500 Wenyi West Road, Yuhang District, Hangzhou City, Zhejiang Province 310000 Applicant before: ZHEJIANG LIANCHI WATER EQUIPMENT STOCK Co.,Ltd. |
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Application publication date: 20180713 |