CN205360687U - Flat counter -current swash plate purifier and have this purifier's settling basin - Google Patents
Flat counter -current swash plate purifier and have this purifier's settling basin Download PDFInfo
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- CN205360687U CN205360687U CN201521007271.6U CN201521007271U CN205360687U CN 205360687 U CN205360687 U CN 205360687U CN 201521007271 U CN201521007271 U CN 201521007271U CN 205360687 U CN205360687 U CN 205360687U
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Abstract
The utility model discloses a flat counter -current swash plate purifier and have this purifier's settling basin, including at least two sets of sedimentation part of transverse arrangement, form the passageway that supplies the precipitate whereabouts between the adjacent sedimentation part, sedimentation part parallel arrangement's about the multi -disc that is used for the drainage precipitate is the type of falling V pterygoid lamina forms the rivers passageway between the adjacent type of the falling V pterygoid lamina, the entry end of passageway is equipped with the drainage part, and this drainage part guides the rivers passageway to the adjacent sedimentation part on respectively with rivers, the drainage part links to each other with adjacent sedimentation part respectively, encloses the quiet liquid zone of establishing into the circulation of confession precipitate, the settling basin includes the cell body, is equipped with into shui qu, the water purification area who supplies fluid and precipitate separation and play pool in the cell body, is equipped with flat counter -current swash plate purifier in the water purification area. The utility model discloses simple structure, it is convenient to install, and resistance to motion is little, and water purification efficiency is high, and the water purification is effectual.
Description
Technical field
This utility model belongs to plumbing field, especially relates to a kind of putting down to stream swash plate purifier and the Sedimentation tank with this purifier.
Background technology
In traditional purifying water process technical matters, in order to make in water containing tiny particle as early as possible, effective sinking realization is separated from water, prior art is settlement separate for adding Particle Acceleration in flood, improve the density of hydraulic surface loading and mud granule, often adopt and in clarification or sedimentation tank, fill the measure separating inclined tube or swash plate to form the clarification of anisotropic flow mud-water separation or to accelerate precipitation, improve water treatment efficiency, reduce floor space, reduce the way of construction investment.This settler is widely used in sedimentation pond for water treatment and settling apparatus, it is adopt in Water and Waste Water Engineering the most at present and maturation water treatment facilities device, it is applied widely, suitable in water inlet desanding, general industry and domestic water precipitation, settlement of sewage, oil removal and Tailing thickening etc. process, and are particularly suited for water factory and sewage treatment project.
And the wastewater inlet in existing tube settler pond is in below inclined tube, by downward up flow process settles some mud and precipitate, water after purification is flowed out by the water leg being located at above inclined tube, the method current rising flow direction is contrary with particle sinking traffic direction, such precipitate suspended particles process is necessarily subject to ascending current impulsive disturbance and causes pulsation, impact sinks to separating and subsidence velocity, affects mud-water separation；And the inclined tube device of this structure to filter the time that water needs longer, it is necessary to waiting medium to flow through whole inclined tube passage can discharge, and cleaning water is low.
For the problems referred to above, Chinese patent CN103495292 discloses one " horizontal shunting swash plate purifier and have the Sedimentation tank of this purifier ", this transverse direction shunting swash plate purifier is formed by many group precipitations arrangement of parts, and settlement section includes deflector, the multi-disc wing plate, the first flow-stopping plate being located at both sides before and after deflector and the second flow-stopping plate that arrange along fluid circulating direction.This Sedimentation tank has the purifier being arranged in order in the horizontal direction by many group precipitations parts.The circulating direction of medium is changed into horizontal direction flowing by above-mentioned purifier, improves the purification efficiency of process, improves depuration quality.But foregoing invention there are disadvantages that, its each group precipitation parts are designed with the passage for precipitate circulation, and construction cost is higher, and take up an area space relatively greatly, decrease effective usable floor area, furthermore its whole machine balancing is poor, and adaptability is narrower.
Chinese patent CN203264351 discloses one " the lateral/horizontal stream muddy water based on tiny flocculation effect taps A type swash plate ", its cross section is the swash plate of A type, equipped with the rib of regular distribution on swash plate, during solid-liquid separation, heavy mud glides along swash plate, flocculation unit after constituting between two pieces of adjacent swash plates with adjacent two ribs.This device can avoid interfering between muddy water, but rib is while the trickle particle that helps to flocculate, it also blocks passing through of current, current are caused a bigger resistance, add the energy consumption of operation, and mud is easily accumulated in the junction of rib and swash plate, affect flocculating effect, and adhere to superincumbent mud and be difficult to be cleaned by, long-time use affects separating effect, also without mentioning spoil disposal passage in this utility model, floc sedimentation still can be disperseed by water impact, also without the concrete method for supporting mentioning swash plate, whole technical scheme is imperfect.
Chinese patent CN103182202 discloses one " v-shaped tube sedimentation tank device ", it includes spaced many group parallel risers of I shape and the reverse V-shaped dividing plate being located between adjacent riser, riser includes central plate and both sides transverse slat, forming sedimentary sliding channel, left transverse slat and right transverse slat between central plate and reverse V-shaped dividing plate makes left and right sliding channel closed at both ends form hydrostatic district.The parallel riser of I shape can also replace with rectangle flute profile riser, and flute profile riser hollow forms fluting above sliding channel, reverse V-shaped dividing plate both sides and rectangular flute profile riser intersection and forms mud discharging mouth.The I shape riser of this device is not easily processed and installs, sliding channel is separated into two sliding channels in left and right by central plate, thus the circulation passage of mud narrows, and mud is liable to stick on central plate, and mud phenomenon is hung in generation, not easy cleaning, easily it is piled into bulk, sliding channel can be blocked after long-time use, affect the properly functioning of whole device.Rectangular flute profile riser processing technique is complicated, it needs when installing to be connected reverse V-shaped dividing plate along water (flow) direction and the bottom surface of fluting are all identical, slightly error is positioned once install, V-type dividing plate is connected on the sidewall of the rectangular flute profile riser being slightly less than fluting bottom surface, then easily pile up precipitate in junction, affect sedimentary separation.And above two design arranges part flow arrangement all without the front end at sliding channel, current easily clash into the transverse slat of riser or the antetheca of rectangular flute profile riser, and current cause bigger resistance, also the easily sedimentary separation of disturbance water currents.
Utility model content
In order to overcome the deficiencies in the prior art, this utility model provides a kind of simple in construction, and water-flow equation is uniform, and cleaning water is high, and what purifying water effect was good puts down to stream swash plate purifier and the Sedimentation tank with this purifier.
This utility model solves the technical scheme is that one of its technical problem and puts down to stream swash plate purifier, including at least two transversely arranged group precipitation parts, the passage fallen for precipitate is formed between adjacent settlement section, described settlement section includes for the sedimentary multi-disc of drain in the reverse V-shaped wing plate be arrangeding in parallel up and down, water stream channel is formed between adjacent reverse V-shaped wing plate, the arrival end of described passage is provided with drainage component, and current are separately directed to the water stream channel on adjacent settlement section by this drainage component；Described drainage component is connected with adjacent settlement section respectively, encloses the hydrostatic district being set as precipitate circulation.Uniform fluid flow is drained to each group precipitation parts by drainage component so that the current that each group precipitation parts process are equalized distribution, and drainage component avoids current are caused bigger resistance.
Further, described drainage component is V-baffle structure, and its both sides are connected with the arrival end of adjacent settlement section respectively.Avoid drainage component to be stopped by water stream channel, current are caused bigger running resistance.
Further, the port of export of described passage is provided with flow-stopping plate.Avoid the precipitate in passage to be continued to wash away by current, affect sedimentation effect.
Further, described flow-stopping plate is for by the V-structure flow-stopping plate of water stream.Uniform fluid flow is made to flow to exhalant region.
Further, the both sides of described reverse V-shaped wing plate extend to form the first deflector and the second deflector separately down.Be conducive to guiding precipitate slide downward to fall into passage.
Further, described first deflector and water (flow) direction are vertically arranged.
The invention also discloses one and put down to stream inclined plate sedimentation pond, including cell body, the clean water area be provided with inhalant region in cell body, supplying fluid to separate with precipitate and exhalant region, in described clean water area, be provided with above-mentioned purifier.
As preferably, being provided with the cloth wet part for dispersed fluid in described inhalant region.The flow velocity of stationary flow, so as to uniformly flow to exhalant region.
As preferably, described cloth wet part is the slab construction being evenly equipped with multiple through hole.Simple in construction, it is convenient to install.
The beneficial effects of the utility model are, 1) the same passage fallen for precipitate is shared between adjacent settlement section, not only sludge discharge effects is good, and settlement section quantity decreases the quantity of passage when identical, save construction material accordingly, and save space, make use of usable floor area to greatest extent, and then reduce construction and use cost；2) both sides of reverse V-shaped wing plate are formed for the sedimentary region of drain respectively, it is achieved that short distance deposit seed, multiaspect solid-liquid separation technology, improve the purification efficiency of purifier, be increased to more than 6 times of prior art；3) settlement section can use integrated V-shape sheet material, it is not necessary to welding, simplifies processing technique, more energy-conserving and environment-protective；4) when fluid is by settlement section, whole machine balancing is better, and the volume that fluid passes through is relatively large；5) separate existence between settlement section, plays connection and supporting role by drainage component and flow-stopping plate, and therefore reverse V-shaped wing plate need not use thicker material plate, saves manufacture material；6) width of settlement section can be adjusted in relatively large scope, and the scope of application is wider；7) V-type flow-stopping plate plays shunting action, thus the current flowing into adjacent settlement section are more uniform, and avoids it that current cause bigger resistance.
Accompanying drawing explanation
Fig. 1 is the structural representation of this utility model settlement section.
Fig. 2 is the cross-sectional view one of this utility model settlement section.
Fig. 3 is the cross-sectional view two of this utility model settlement section.
Fig. 4 is many group precipitations unit construction status architecture schematic diagram.
Fig. 5 is the structural representation of Sedimentation tank.
Detailed description of the invention
In order to make those skilled in the art be better understood from this utility model scheme, below in conjunction with the accompanying drawing in this utility model embodiment, technical scheme in utility model embodiment is carried out clear, complete description, obviously, described embodiment is only a part of embodiment of the present utility model, rather than whole embodiments.Based on the embodiment in this utility model, the every other embodiment that those of ordinary skill in the art obtain under not making creative work premise, all should belong to the scope of this utility model protection.
With reference to shown in Fig. 1-4, one is put down to stream swash plate purifier, including at least two transversely arranged group precipitation parts, the passage 1 fallen for precipitate is formed between adjacent settlement section, every group precipitation parts include the reverse V-shaped wing plate 2 that multi-disc be arranged in parallel up and down, form water stream channel 3 between adjacent reverse V-shaped wing plate 2.The arrival end of passage 1 is provided with drainage component 4, and the right side of the left side of this drainage component 4 wing plate 2 reverse V-shaped with each of settlement section is connected, and the right side of this drainage component 4 is connected with the left side of each reverse V-shaped wing plate 2 of adjacent group precipitation parts.The left side of drainage component 4 can also be connected with the front side wall of each reverse V-shaped wing plate 2, wall thickness part is only sheltered from by it, the right side of drainage component 4 can also be connected with the front side wall of each reverse V-shaped wing plate 2 of adjacent group precipitation parts, and wall thickness part is only sheltered from by it.The rear wall of settlement section two groups adjacent and drainage component 4 encloses and sets the hydrostatic district formed for precipitate circulation.
The top of reverse V-shaped wing plate 2 can have certain radian, namely can be adjusted according to design needs in the inverted U structure with flared section, its v-angle angle and width.Drainage component 4 and water (flow) direction are vertically standing in the arrival end of fluid, the V-shaped structure of its cross section.The port of export of passage 1 and water (flow) direction have vertically erect flow-stopping plate 31, and in order to increase the circulation area of current, on the left of it, the right side of wing plate 2 reverse V-shaped with each of settlement section is connected, and right side is connected with the left side of each reverse V-shaped wing plate 2 of adjacent group precipitation parts.The left side of flow-stopping plate 31 can also be connected with the rear wall of each reverse V-shaped wing plate 2, wall thickness part is only sheltered from by it, the right side of flow-stopping plate 31 can also be connected with the rear wall of each reverse V-shaped wing plate 2 of adjacent group precipitation parts, and wall thickness part is only sheltered from by it.Flow-stopping plate 31 can be the plate-like structure erect, it is also possible to being the V-structure vertically erect with water (flow) direction, the current of the port of export can be tapped by it so that it is uniformly flows to exhalant region.Thus defining a hydrostatic district for precipitate circulation between the front side wall of the rear wall of drainage component 4, flow-stopping plate 31 and adjacent settlement section.
Successfully passage 1 is fallen into along the both sides of reverse V-shaped wing plate 2 for the ease of precipitate, the first deflector 21 and the second deflector 22 can be extended to form separately down in the both sides of reverse V-shaped wing plate 2, first deflector the 21, second deflector 22 can be vertically arranged with fluid circulating direction, can also arrange with the angle of inclination that the both sides of reverse V-shaped wing plate 2 are certain, precipitate flows to the upper surface of next layer of reverse V-shaped wing plate 2 by the first deflector 21, continue towards the reverse V-shaped wing plate 2 of next layer again through the deflector of next layer of reverse V-shaped wing plate, after, fall into hydrostatic district through passage 1.Corresponding second deflector 22 is also arranged with above-mentioned form.Drainage component 4 is connected with the first deflector sidewall of the second deflector 22 and adjacent settlement section respectively.
The height of first deflector the 21, second deflector 22 can be made adjustment accordingly according to the concentration difference of the medium that need to purify, when concentration of medium to be clean is higher, the height of deflector can respective design must be less, thus the gap between settlement section is relatively big up and down, namely bigger by the space of flow channel 1 for precipitate；When concentration of medium to be clean is relatively low, the height of deflector can respective design must be bigger, thus the gap between settlement section is less up and down, namely less by the space of flow channel 1 for precipitate.
The reverse V-shaped wing plate 2 of multi-disc is arranged up and down abreast along being perpendicular to fluid circulating direction, leave the gap passed through for precipitate between neighbouring reverse V-shaped wing plate 2, namely ensure to leave the gap naturally passed through for precipitate between the bottom surface of the deflector of reverse V-shaped wing plate 2 above and the end face of reverse V-shaped wing plate 2 being positioned below.One is put down and is included many group precipitations parts to stream swash plate purifier, lays side by side about each group precipitation parts, leaves space and form the passage 1 fallen for precipitate between adjacent settlement section.The arrival end of this passage 1 is provided with drainage component 4, and the port of export of passage 1 is provided with flow-stopping plate 31, all V-shaped structure of the cross section of drainage component 4 and flow-stopping plate 31, vertically erects setting with water (flow) direction.
In figure, arrow represents fluid circulating direction, i.e. horizontal direction, during operation, medium is by the arrival end each group precipitation parts of traverse, medium is tapped and stops by drainage component 4, adds action of gravity, by the second deflector 22, precipitate is drained to passage 1 with the right side wing plate of the reverse V-shaped wing plate 2 that water (flow) direction is certain angle of inclination, same, precipitate is drained to same passage 1 also by the first deflector by the left side wing plate of the reverse V-shaped wing plate 2 of adjacent group precipitation parts.Owing between two group precipitation parts, drainage component 4 and flow-stopping plate 31 block the impulsive force of fluid, it is to avoid continue to wash away to fluid flow direction by precipitate, precipitate will not again be broken up by current but accumulate in hydrostatic district.The water being cleaned successfully flows to exit along settlement section, and in flow process, precipitate is progressively precipitated, via passage 1 landing to hydrostatic district, without influence on the clarity of current in reverse V-shaped wing plate 2.
This utility model is perpendicular to water (flow) direction and is provided with the reverse V-shaped wing plate 2 of multi-disc, current are divided into multilamellar and carry out flowing precipitation purification, every reverse V-shaped wing plate 2 is symmetrical set, precipitate in the current of each layer only need to just complete isolation of purified from reverse V-shaped wing plate 2 both sides landing, substantially reduce sedimentary precipitation distance, and achieve the efficient technology of multiaspect solid-liquid separation, significantly improve purification efficiency.The V-shaped design of drainage component 4 and flow-stopping plate 31 cross section, has also functioned to shunting action so that be with sedimentary uniform fluid flow to drain into each group precipitation parts and be easily separated purification.
nullWith reference to shown in Fig. 5，One is put down to stream inclined plate sedimentation pond，Including cell body 5，It is provided with inhalant region in cell body 5、The clean water area 51 separated with precipitate for fluid and exhalant region，Aforesaid purifier it is provided with in clean water area 51，Volume according to cell body 5 and size，Can superposition up and down、Front and back superposition or left and right lay many group precipitations parts side by side，Cloth wet part 52 it is provided with in inhalant region，For medium is disperseed so as to uniformly flow into each group precipitation parts，And then improve treatment effect，Concrete，In the present embodiment，Cloth wet part 52 is slab construction vertically disposed with fluid circulating direction，Its integrated formed structure for being made up of plastic material or metal material or concrete，This cloth wet part 52 uniformly offers the through hole 521 of multiple circle，Concrete perforate designs than the water yield handled by sedimentation tank and water quality.Accordingly, in order to improve outlet effect and effluent quality, same cloth wet part 52 is set at exhalant region.The bottom of clean water area 51 is provided with mean for the funnel-form mud discharging mouth 53 that precipitate is discharged.Therefore needing the current purified to pass sequentially through inhalant region and enter clean water area 51, the separated bottom that is deposited on of precipitate is discharged by mud discharging mouth 53, and the water being cleaned is flowed out by exhalant region.
Above-mentioned detailed description of the invention is used for illustrating this utility model; rather than this utility model is limited; in spirit of the present utility model and scope of the claims, any amendment that this utility model is made and change, both fall within protection domain of the present utility model.
Claims (9)
1. put down to stream swash plate purifier for one kind, including at least two transversely arranged group precipitation parts, the passage (1) fallen for precipitate is formed between adjacent settlement section, described settlement section includes for the sedimentary multi-disc of drain in the reverse V-shaped wing plate (2) be arrangeding in parallel up and down, water stream channel (3) is formed between adjacent reverse V-shaped wing plate (2), it is characterized in that: the arrival end of described passage (1) is provided with drainage component (4), current are separately directed to the water stream channel (3) on adjacent settlement section by this drainage component (4)；Described drainage component (4) is connected with adjacent settlement section respectively, encloses the hydrostatic district being set as precipitate circulation.
2. purifier according to claim 1, it is characterised in that: described drainage component (4) is V-baffle structure, and its both sides are connected with the arrival end of adjacent settlement section respectively.
3. purifier according to claim 1, it is characterised in that: the port of export of described passage (1) is provided with flow-stopping plate (11).
4. purifier according to claim 3, it is characterised in that: described flow-stopping plate (31) is for by the V-structure flow-stopping plate of water stream.
5. purifier according to claim 1, it is characterised in that: the both sides of described reverse V-shaped wing plate (2) extend to form the first deflector (21) and the second deflector (22) separately down.
6. purifier according to claim 5, it is characterised in that: described first deflector (21) and water (flow) direction are vertically arranged.
7. put down to stream inclined plate sedimentation pond for one kind, including cell body (5), the clean water area (51) be provided with inhalant region in cell body (5), supplying fluid to separate with precipitate and exhalant region, it is characterised in that: described clean water area is provided with the purifier as according to any one of claim 1-6 in (51).
8. Sedimentation tank according to claim 7, it is characterised in that: it is provided with the cloth wet part (52) for dispersed fluid in described inhalant region.
9. Sedimentation tank according to claim 8, it is characterised in that: described cloth wet part (52) is the slab construction being evenly equipped with multiple through hole (521).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521007271.6U CN205360687U (en) | 2015-12-08 | 2015-12-08 | Flat counter -current swash plate purifier and have this purifier's settling basin |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521007271.6U CN205360687U (en) | 2015-12-08 | 2015-12-08 | Flat counter -current swash plate purifier and have this purifier's settling basin |
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| CN205360687U true CN205360687U (en) | 2016-07-06 |
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| CN201521007271.6U Active CN205360687U (en) | 2015-12-08 | 2015-12-08 | Flat counter -current swash plate purifier and have this purifier's settling basin |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105289056A (en) * | 2015-12-08 | 2016-02-03 | 浙江联池水务设备有限公司 | Flat flow inclined plate purification device and sedimentation tank with purification device |
| CN108553947A (en) * | 2018-06-21 | 2018-09-21 | 盐城工学院 | A kind of novel flat flow inclined-plate clarifying basin |
| CN110422920A (en) * | 2019-08-30 | 2019-11-08 | 河南蔚蓝水处理技术有限公司 | Level stream settling apparatus and its level stream inclined plate module |
-
2015
- 2015-12-08 CN CN201521007271.6U patent/CN205360687U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105289056A (en) * | 2015-12-08 | 2016-02-03 | 浙江联池水务设备有限公司 | Flat flow inclined plate purification device and sedimentation tank with purification device |
| CN108553947A (en) * | 2018-06-21 | 2018-09-21 | 盐城工学院 | A kind of novel flat flow inclined-plate clarifying basin |
| CN110422920A (en) * | 2019-08-30 | 2019-11-08 | 河南蔚蓝水处理技术有限公司 | Level stream settling apparatus and its level stream inclined plate module |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee | ||
| CP03 | Change of name, title or address |
Address after: Yuhang District, Hangzhou City, Zhejiang Province, 310000 West No. 1500 Building 2 room 413 Patentee after: Zhejiang pool water equipment Limited by Share Ltd Address before: Yuhang District, Hangzhou City, Zhejiang Province, 311121 West No. 1500 Building 2 room 413 Patentee before: Zhejiang Lianchi Water Equipment Co., Ltd. |
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| CB03 | Change of inventor or designer information |
Inventor after: Sheng Jinwen Inventor after: Chi Wanqing Inventor after: Zhu Haitao Inventor after: Meng Fanping Inventor after: Liu Hongyuan Inventor after: Hua Guoqiang Inventor before: Sheng Jinwen Inventor before: Chi Wanqing Inventor before: Zhu Haitao Inventor before: Meng Fanping Inventor before: Liu Hongyuan Inventor before: Hua Guoqiang |
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| COR | Change of bibliographic data | ||
| CP02 | Change in the address of a patent holder |
Address after: Room 407, building 18, No. 998, Wenyi West Road, Yuhang District, Hangzhou City, Zhejiang Province 310000 Patentee 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 Patentee before: ZHEJIANG LIANCHI WATER EQUIPMENT STOCK Co.,Ltd. |
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| CP02 | Change in the address of a patent holder |