CN203678025U - Eddy current type solid-liquid separating and purifying device and sedimentation tank provided with same - Google Patents
Eddy current type solid-liquid separating and purifying device and sedimentation tank provided with same Download PDFInfo
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- CN203678025U CN203678025U CN201320722254.5U CN201320722254U CN203678025U CN 203678025 U CN203678025 U CN 203678025U CN 201320722254 U CN201320722254 U CN 201320722254U CN 203678025 U CN203678025 U CN 203678025U
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Abstract
The utility model discloses an eddy current type solid-liquid separating and purifying device and a sedimentation tank provided with the same. The eddy current type solid-liquid separating and purifying device is formed by at least one group of sedimentation components, wherein each sedimentation component comprises a deflector and multiple wing plates; along the circulating direction of fluid, each wing plate is divided into a first wing plate body used for guiding sediment and a second wing plate body used for guiding the fluid; a first baffle and a second baffle which are used for stopping washing of the fluid are arranged at the inlet end and the outlet end of the first wing plate body, respectively, and a liquid standing region is formed between the first baffle and the second baffle; a drainage channel is formed in the liquid standing region on the first wing plate body, and the first wing plate body and the second wing plate body have inclinations facilitating flowing of the sediment into the drainage channel; an eddy region used for causing the fluid to form an eddy is formed along the circulating direction of the fluid on the second wing plate body, and a fluid collecting channel used for circulating the fluid is formed between the eddy region and the liquid standing region. The eddy current type solid-liquid shunting purifying device has the advantages that purification efficiency and purification water quality are greatly improved and cost is greatly reduced.
Description
Technical field
The utility model relates to plumbing field, especially relates to the settling tank that a kind of horizontal shunting purifies sloping plate unit and has this purifier.
Background technology
Inclined tube filler is development settler out on shallow pool theory, is widely used in sedimentation pond for water treatment and settling apparatus.In Water and Waste Water Engineering, to adopt at present a general and ripe water treatment facilities device of factory.The advantages such as it is applied widely, treatment effect is high, floor space is little.Be suitable for water inlet desanding general industry and domestic water precipitation, settlement of sewage, the processing such as oil removal and mine tailing are concentrated, is particularly useful for water factory and sewage treatment project.
And the sewage import of existing inclined tube settling tank is to be positioned at inclined tube below, by some mud of sedimentation and sediment in downward online flow process, the water after purification flows out by the water leg of being located at inclined tube top; The time that water of inclined tube device filtration of this structure needs is longer, need to wait MEDIA FLOW can discharge through whole inclined tube passage, and cleaning water is low.
Utility model content
The utility model is in order to overcome the deficiencies in the prior art, the eddy current type solid-liquid shunting purifier that a kind of water purification quality is good, efficiency is high is provided and has the settling tank of this purifier.
To achieve these goals, the utility model by the following technical solutions: a kind of eddy current type solid-liquid shunting purifier, is formed the multi-disc wing plate that described precipitation parts comprise deflector and arrange along fluid circulating direction by least one group precipitation arrangement of parts; Wing plate is divided into for sedimentary the first wing plate body of drainage with for the second wing plate body of drain fluids along fluid circulating direction; The entrance point of the first wing plate body and the port of export are respectively equipped with the first flow-stopping plate and the second flow-stopping plate for stopping fluid scouring, form the quiet liquid zone for precipitate between this first flow-stopping plate and the second flow-stopping plate; On the first wing plate body, be positioned at quiet liquid zone and be provided with for the sediment drain outlet of circulation downwards, and the first wing plate body and the second wing plate body have the gradient of being convenient to sediment and flowing into described drain outlet; On the second wing plate body, be provided with for making fluid form the vortex region of eddy current along fluid circulating direction, between Yu Jing liquid zone, vortex region, be formed with the collection flow channels for fluid circulation.
Further, described vortex region comprises the impeller circulating for blocking fluid being intervally arranged along fluid circulating direction, passes through mobile formation one vortex chamber of fluid self between adjacent impeller.
Further, described deflector has sedimentary second gradient of discharging from drain outlet for catching.
Described impeller has the 3rd gradient tilting along fluid circulating direction.
As preferably, between described the first wing plate body and deflector, be provided with interval to form described drain outlet.
Or described the first wing plate body is provided with through hole to form described drain outlet.
The utility model also provides a kind of eddy current type inclined plate sedimentation pond, comprise pond body, the outlet that is provided with the import flowing into for medium, the Disengagement zone separating with sediment for fluid, the settling zone that supplies precipitate in the body of pond and supplies fluid to flow out, in described Disengagement zone, be provided with purifier, described purifier is formed by many group precipitations arrangement of parts, described precipitation parts comprise deflector, along the multi-disc wing plate of fluid circulating direction setting, be located at the first flow-stopping plate and second flow-stopping plate of both sides before and after deflector; Wing plate is divided into for sedimentary the first wing plate body of drainage with for the second wing plate body of drain fluids along fluid circulating direction; The entrance point of the first wing plate body is connected with the first flow-stopping plate, and the port of export is connected with the second flow-stopping plate, forms the quiet liquid zone for precipitate between the first flow-stopping plate and the second flow-stopping plate; On the first wing plate body, be positioned at quiet liquid zone and be provided with for the sediment drain outlet of circulation downwards, and the first wing plate body and the second wing plate body have the gradient of being convenient to sediment and flowing into described drain outlet; On the second wing plate body, be provided with for making fluid form the vortex region of eddy current along fluid circulating direction, between Yu Jing liquid zone, vortex region, be formed with the collection flow channels for fluid circulation.
As preferably, described exit is along being provided with water leg perpendicular to fluid circulating direction.
Described settling zone has funnel-form outlet.
In sum, the utlity model has following advantage: the utility model purifier changes the circulating direction of medium into horizontal direction and flows, and when dielectric stratifying purifies, after one deck wing plate of flowing through wherein, its precipitum can be entered to settling zone; Set up vortex region, passive sedimentation is changed into initiatively and being carried out, forced suspension to be transformed into bulky grain, accelerated purification efficiency, thereby: the cost of investment that 1, has greatly reduced engineering construction; 2, reduced the dosage of purified treatment flocculant; 3, improve the purification efficiency of processing, be increased to the more than 3 times of prior art; 4, greatly improved depuration quality; 5, there is obvious effect of energy and obvious social benefit.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model embodiment mono-.
Fig. 2 is the Facad structure schematic diagram of a kind of single group sedimentation parts of the utility model embodiment mono-.
Fig. 3 is the overlooking surface structural representation of a kind of single group sedimentation parts of the utility model embodiment mono-.
Fig. 4 is the perspective view of single group sedimentation parts of the utility model embodiment mono-.
Fig. 5 is the structural representation of the utility model embodiment bis-.
Fig. 6 is the perspective view of the another kind of single group sedimentation parts of the utility model embodiment mono-.
The specific embodiment
In order to make those skilled in the art person better understand the utility model scheme, below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the utility model embodiment is carried out to clear, complete description.
Embodiment mono-
As shown in Figure 1, a kind of eddy current type solid-liquid shunting purifier, is arranged and is formed by least one group precipitation parts 9, according to environment for use difference, can have multiple building form, as vertically arranged, or arranges along its length, described precipitation parts comprise deflector 1, multi-disc wing plate 2, the first flow-stopping plate 3 and the second flow-stopping plate 4, deflector 1 is for guiding sediment to flow downward, wing plate arranges along fluid circulating direction, and fluid circulating direction is horizontal direction in the utility model, so wing plate 2 is also along continuous straight runs setting, wing plate is divided into two parts along fluid circulating direction, a part is the second wing plate body 22 for drain fluids, and another part is the first wing plate body 21 for drainage sediment 88, and described sediment 88 comprises and is deposited on the first wing plate body and the second wing plate body from sediment with it, as preferably, the first flow-stopping plate 3 is connected with the both sides, front and back of deflector 1 respectively with the second flow-stopping plate 4, two flow-stopping plates and a U-shaped like frame of deflector composition, concrete, the first flow-stopping plate 3 and the second flow-stopping plate 4 all arrange perpendicular to fluid circulating direction, the first flow-stopping plate 3 gears are located at the entrance point of the first wing plate body 21, the second flow-stopping plate 4 gears are located at the port of export of the second wing plate body 22, so deflector 1, between the first flow-stopping plate 3 and the second flow-stopping plate 4, form the quiet liquid zone 71 for precipitate, the first flow-stopping plate prevents that fluid from washing away the sediment in quiet liquid zone, the second flow-stopping plate is taken away the sediment in quiet liquid zone for block fluid flow by journey, the sediment that effectively guarantees whole quiet liquid zone precipitates fast, also guaranteed to be deposited in sediment on the second wing plate body flows to after the second wing plate body not can be by current scour and again floating.
In the present embodiment, described wing plate 2 has the first wing plate body 21 and the second wing plate body 22 that circulation area equates, i.e. the first wing plate body 21 and the second wing plate body 22 mean allocation, and between both wings plate body, be integrally formed the wing plate 2 of structure, obviously, also the split of both wings plate body can be arranged, arrange as staggered up and down etc., also fall into protection domain of the present utility model; In Fig. 2, dotted portion is the first wing plate body 21, and its entirety is positioned at the scope that stops of the second flow-stopping plate 4, when current are flowed through precipitation parts, the first flow-stopping plate has stopped the water flow impact pressure on the second wing plate body, and the second flow-stopping plate has stopped that water flow impact pressure washes away sediment backward; Solid line part is the second wing plate body, it protrudes from the second flow-stopping plate 4 and arranges, be exposed to stopping in scope of the second flow-stopping plate 4, be that current are flowed through while precipitating parts, current can not stopped by the first flow-stopping plate and the second flow-stopping plate, can be successfully along the second wing plate body to exit diffluence, in flow process, sediment is progressively precipitated, and breaks away to deflector one along the first wing plate body; On the first wing plate body 21, between a side of close deflector 1 and deflector 1, be provided with the drain outlet 11 for sediment circulation, this drain outlet 11 can be also the through hole being opened on the first wing plate body 21, and sediment is discharged downwards by these through holes; Wing plate 2 has the gradient of being convenient to sediment inflow drain outlet 11, concrete, wing plate 2 entirety have downward gradient, in the time that current are flowed through wing plate, sediment can successfully flow to drain outlet 11 naturally, as preferably, in the present embodiment, the gradient of described wing plate is 30 °, and the angle α between wing plate 2 upper surfaces and horizontal direction is 30 °.
On the second wing plate body 22, be provided with for making fluid form the vortex region 72 of eddy current along fluid circulating direction, between Yu Jing liquid zone, vortex region 71, be formed with the collection flow channels 73 for fluid circulation; Concrete, in the present embodiment, described vortex region comprises the impeller 721 circulating for blocking fluid being intervally arranged along fluid circulating direction, between adjacent impeller 721, pass through mobile formation one vortex chamber 722 of fluid self, in each vortex chamber, form a vortex, current in vortex are mandatory under centrifugal action forms bulky grain by the suspended impurity in fluid rapidly, is then deposited on the second wing plate body, discharged to drain outlet.Through overtesting, when fluid is flowed through the 6th vortex chamber, suspended impurity just similar precipitation is good, and purification efficiency promotes fairly obvious; And in order to improve the flow velocity of fluid, reduce drag, and do not affect in the situation of swirling action, impeller 721 can be arranged to the 3rd gradient tilting along fluid circulating direction, the 3rd gradient is preferably 80 degree.
As shown in Fig. 4,6, show the structural representation of two kinds single kind group sedimentation parts, these two groups all by injection machine integrated injection molding; What in the present embodiment, adopt is the structure shown in Fig. 4, in the time that sedimentation parts only have one group to use, the lateral wall of the second wing plate body 22 and sedimentation pool wall adhesive fabric need to be put, and the outside of the outside second wing plate body 22 of impeller 721 flushes; In the time that sedimentation parts are organized arrangement use more, can be horizontal direction, can be also longitudinal arrangement, as shown in Figure 1; And in the time adopting separately structure shown in Fig. 6, its deflector 1 is connected with the lateral wall of all the second wing plate bodies 22, the second wing plate body 22 is located on deflector 1, and the lateral wall of impeller 721 is also arranged with the sidewall laminating of deflector 1 simultaneously; When use, the inwall laminating of the first flow-stopping plate and the second flow-stopping plate and settling tank is arranged; And in the time of many group sedimentation component combinations, the deflector of rear one group of sedimentation parts is just located at before the drain outlet of last group, in the time that gradient is set, the deflector of latter a group just can be caught the sediment that discharge last group of sedimentation parts drain outlet.Two groups of structures all can reach identical result of use, and described in Fig. 6, structure is processed more for convenience.
Compared to the inclined tube-type purifier of prior art, purification efficiency of the present utility model improves greatly, the multilayer wing plate that along continuous straight runs layering arranges, current are divided into the multilayer precipitation that flows, and sediment in the current of every one deck only need to flow down from the first wing plate body, just complete purification, greatly dwindle sedimentary precipitation distance; Tradition inclined tube-type purifier, the sediment of purification need to be precipitated to bottom from the upper end of each root inclined tube just can flow to settling zone, and the clarification time has extended more than 3 times compared with the utility model; And in the utility model, be also provided with especially vortex, vortex is enforceable to be become suspended particulate into bulky grain and carries out sedimentation, has changed traditional passive type pattern, initiative suspended particulate is carried out to sedimentation, increase substantially again purification efficiency.
And the concentration of the fluid that need to purify at some is when higher, we can be arranged to deflector to have the second gradient, and this second gradient can be 80 °, between deflector lower surface and horizontal plane, forms 80 °; When deflector has after this second gradient, can catch the sediment falling down on wing plate, can avoid sediment directly to drop to polluting in the process of settling zone a layer fluid below; And the sediment that every one deck has precipitated all flows to after deflector upper surface, then flow to settling zone discharge through deflector, further shortened mobile distance, improved purification efficiency.
As Fig. 1, shown in 3, in figure, arrow represents fluid circulating direction, when fluid is as water to be clean, while flowing to from import department, the many group precipitations parts 9 of flowing through, the second wing plate body 22 carries out layering water conservancy diversion to current, due to the drag effect of impeller, impel current in mobile process, to form vortex on the second wing plate body, each vortex chamber all forms an independent vortex, under the centrifugal action of current, the granule that suspends in water is run to rapidly vortex region, by coacervating large particle forcibly, and the clean water of removing after suspended particulate confluxes to the port of export by collection flow channels 73, oarse-grained precipitate is to bottom, vortex region, along the first wing plate direction of flow drain outlet 11, thereby reach the effect of purification, the setting of the first flow-stopping plate and the second flow-stopping plate, can effectively prevent from flow process, the sediments such as the mud having precipitated on the first wing plate body 21 being washed away, the a part of water having purified just continues to circulate to Way out by the second wing plate body 22, the sediment having precipitated does not just flow into drain outlet 11 not disturbedly smoothly, can not affect the clarity of the current in collection flow channels.
Embodiment bis-
As shown in Figure 5, a kind of eddy current type inclined plate sedimentation pond, comprise pond body 5, body 5 right sides in pond are provided with the import 51 flowing into for medium, in the body of pond, be provided with the Disengagement zone 52 separating with sediment for fluid, the settling zone 53 that supplies precipitate, body left side, pond is provided with the outlet 54 of flowing out for fluid, outlet 54 connects one along being provided with water leg 55 perpendicular to fluid circulating direction, concrete, water leg is strip, along the left side edge setting of pond body, the through hole passing through on water leg cell wall having purified flows into water leg, then flows out by outlet 54; As preferably, described settling zone has funnel-form outlet 531, is convenient to sediment and discharges; In described Disengagement zone, be provided with the purifier in embodiment 1, in concrete structure the present embodiment of purifier, repeat no more, this purifier is for lying in a horizontal plane in Disengagement zone, conventionally in Disengagement zone, can be provided with grid for placing purifier or block of wood of strip, sewage to be clean flows into from import 51, precipitate purification through Disengagement zone, the impurity such as sediment flow in settling zone and discharge.
This settling tank is simple in structure, and cost is low, and compared with onesize existing pond body, purification efficiency has improved at least 6 times, and the quality of purification also improves greatly, and the sediment undergoes washing on purifier is convenient, saves energy consumption, environmental protection low-carbon (LC).
Obviously, described embodiment is only a part of embodiment of the present utility model, rather than whole embodiment.Based on the embodiment in the utility model, those of ordinary skills are not making the every other embodiment obtaining under creative work prerequisite, all should belong to the scope of the utility model protection.
Claims (9)
1. an eddy current type solid-liquid shunting purifier, is formed by least one group precipitation arrangement of parts, it is characterized in that: the multi-disc wing plate (2) that described precipitation parts comprise deflector (1) and arrange along fluid circulating direction; Wing plate is divided into for sedimentary the first wing plate body (21) of drainage with for the second wing plate body (22) of drain fluids along fluid circulating direction; The entrance point of the first wing plate body (21) and the port of export are respectively equipped with the first flow-stopping plate (3) and the second flow-stopping plate (4) for stopping fluid scouring, form the quiet liquid zone (71) for precipitate between this first flow-stopping plate (3) and the second flow-stopping plate (4); On the first wing plate body (21), be positioned at quiet liquid zone (71) and be provided with for the sediment drain outlet (11) of circulation downwards, and the first wing plate body (21) and the second wing plate body (22) have the gradient of being convenient to sediment and flowing into described drain outlet; The second wing plate body (22) is upper to be provided with for making fluid form the vortex region (72) of eddy current along fluid circulating direction, is formed with the collection flow channels (73) for fluid circulation between Yu Jing liquid zone, vortex region.
2. eddy current type solid-liquid shunting purifier according to claim 1, it is characterized in that: described vortex region comprises the impeller (721) circulating for blocking fluid being intervally arranged along fluid circulating direction, between adjacent impeller (721), pass through mobile formation one vortex chamber (722) of fluid self.
3. eddy current type solid-liquid shunting purifier according to claim 1, is characterized in that: described deflector (1) has for catching sedimentary the second gradient that discharge (11) from drain outlet.
4. eddy current type solid-liquid shunting purifier according to claim 2, is characterized in that: described impeller (721) has the 3rd gradient tilting along fluid circulating direction.
5. eddy current type solid-liquid according to claim 1 shunting purifier, is characterized in that: between described the first wing plate body (21) and deflector, be provided with interval to form described drain outlet (11).
6. eddy current type solid-liquid shunting purifier according to claim 1, is characterized in that: described the first wing plate body (21) is provided with through hole to form described drain outlet (11).
7. an eddy current type inclined plate sedimentation pond, comprise pond body (5), the outlet (54) that is provided with the import (51) flowing into for medium, the Disengagement zone (52) separating with sediment for fluid, the settling zone (53) that supplies precipitate in pond body (5) and supplies fluid to flow out, in described Disengagement zone, be provided with purifier, it is characterized in that: described purifier is formed by many group precipitations arrangement of parts multi-disc wing plate (2), the first flow-stopping plate (3) and the second flow-stopping plate (4) that described precipitation parts comprise deflector (1), arrange along fluid circulating direction; Wing plate is divided into for sedimentary the first wing plate body (21) of drainage with for the second wing plate body (22) of drain fluids along fluid circulating direction; The entrance point of the first wing plate body (21) is connected with the first flow-stopping plate (3), and the port of export is connected with the second flow-stopping plate (4), forms the quiet liquid zone (71) for precipitate between the first flow-stopping plate (3) and the second flow-stopping plate (4); On the first wing plate body (21), be positioned at quiet liquid zone (71) and be provided with for the sediment drain outlet (11) of circulation downwards, and the first wing plate body (21) and the second wing plate body (22) have the gradient of being convenient to sediment and flowing into described drain outlet; The second wing plate body (22) is upper to be provided with for making fluid form the vortex region (72) of eddy current along fluid circulating direction, is formed with the collection flow channels (73) for fluid circulation between Yu Jing liquid zone, vortex region.
8. horizontal shunting inclined plate sedimentation according to claim 7 pond, is characterized in that: described outlet (54) is located along being provided with water leg (55) perpendicular to fluid circulating direction.
9. horizontal shunting inclined plate sedimentation according to claim 7 pond, is characterized in that: described settling zone has funnel-form outlet (531).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320722254.5U CN203678025U (en) | 2013-11-17 | 2013-11-17 | Eddy current type solid-liquid separating and purifying device and sedimentation tank provided with same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320722254.5U CN203678025U (en) | 2013-11-17 | 2013-11-17 | Eddy current type solid-liquid separating and purifying device and sedimentation tank provided with same |
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| Publication Number | Publication Date |
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| CN203678025U true CN203678025U (en) | 2014-07-02 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320722254.5U Withdrawn - After Issue CN203678025U (en) | 2013-11-17 | 2013-11-17 | Eddy current type solid-liquid separating and purifying device and sedimentation tank provided with same |
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| CN (1) | CN203678025U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103585798A (en) * | 2013-11-17 | 2014-02-19 | 池万青 | Vortex type solid-liquid diversion purification device and sedimentation tank provided with same |
-
2013
- 2013-11-17 CN CN201320722254.5U patent/CN203678025U/en not_active Withdrawn - After Issue
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103585798A (en) * | 2013-11-17 | 2014-02-19 | 池万青 | Vortex type solid-liquid diversion purification device and sedimentation tank provided with same |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: ZHEJIANG LIANCHI WATER EQUIPMENT CO., LTD. Free format text: FORMER OWNER: CHI WANQING Effective date: 20141215 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 317600 TAIZHOU, ZHEJIANG PROVINCE TO: 310000 HANGZHOU, ZHEJIANG PROVINCE |
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| TR01 | Transfer of patent right |
Effective date of registration: 20141215 Address after: Yuhang District, Hangzhou City, Zhejiang Province, 310000 West No. 1500 Building 2 room 413 Patentee after: Zhejiang Lianchi Water Equipment Co., Ltd. Address before: Taizhou City, Zhejiang province 317600 Ring Road No. 20-3 Truman town of Yuhuan County Patentee before: Chi Wanqing |
|
| AV01 | Patent right actively abandoned |
Granted publication date: 20140702 Effective date of abandoning: 20160127 |
|
| C25 | Abandonment of patent right or utility model to avoid double patenting |