CN203678024U - Transverse shunt type solid-liquid separation purification device and sedimentation tank with purification device - Google Patents
Transverse shunt type solid-liquid separation purification device and sedimentation tank with purification device Download PDFInfo
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- CN203678024U CN203678024U CN201320722253.0U CN201320722253U CN203678024U CN 203678024 U CN203678024 U CN 203678024U CN 201320722253 U CN201320722253 U CN 201320722253U CN 203678024 U CN203678024 U CN 203678024U
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- wing plate
- plate body
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- sediment
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- 239000007788 liquid Substances 0.000 title claims abstract description 30
- 238000004062 sedimentation Methods 0.000 title claims abstract description 18
- 238000000926 separation method Methods 0.000 title claims abstract description 12
- 238000000746 purification Methods 0.000 title abstract description 16
- 239000013049 sediment Substances 0.000 claims abstract description 40
- 239000012530 fluid Substances 0.000 claims abstract description 39
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 24
- 238000001556 precipitation Methods 0.000 claims description 16
- 239000002244 precipitate Substances 0.000 claims description 11
- 239000007787 solid Substances 0.000 claims description 10
- 230000008676 import Effects 0.000 claims description 6
- 238000009991 scouring Methods 0.000 claims description 4
- 238000007599 discharging Methods 0.000 claims description 2
- 230000002706 hydrostatic effect Effects 0.000 abstract 2
- 230000000903 blocking effect Effects 0.000 abstract 1
- 238000000034 method Methods 0.000 description 5
- 239000010865 sewage Substances 0.000 description 4
- 230000008901 benefit Effects 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 1
- 210000002421 cell wall Anatomy 0.000 description 1
- 238000005352 clarification Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000001746 injection moulding Methods 0.000 description 1
- 238000009428 plumbing Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
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Abstract
The utility model discloses a transverse shunt type solid-liquid separation purification device and a sedimentation tank with the purification device. The purification device is formed by combining at least one group of sedimentation parts, wherein the sedimentation parts comprise a guide plate and multiple flanges; the flanges are divided into a first flange body and a second flange body along the fluid flow direction; a first baffle and a second baffle used for blocking fluid flush are respectively arranged at an inlet end and an outlet end of the first flange body; a hydrostatic area in which sediments are settled is formed between the first baffle and the second baffle; a discharge channel through which the sediments flow downwards is formed in a position, which is positioned in the hydrostatic area, on the first flange body; the first flange body and the second flange body have inclination through which the sediments conveniently flow into the discharge channel. According to the purification device, a medium flow direction is changed into a horizontal direction, the water flow is layered and purified through the flanges, the cost is saved, and the purification efficiency is improved.
Description
Technical field
The utility model relates to plumbing field, especially relates to a kind of horizontal shunting Separation of Solid and Liquid purifier and has the settling tank of 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 drain outlet, and cleaning water is low.
Utility model content
The utility model is in order to overcome the deficiencies in the prior art, provides that a kind of cleaning water is high, the measured horizontal shunting Separation of Solid and Liquid purifier of matter and have the settling tank of this purifier.
To achieve these goals, the utility model by the following technical solutions: a kind of laterally shunting Separation of Solid and Liquid 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 component combination; 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 blowdown 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 blowdown drain outlet.
Further, described deflector is connected away from a side of quiet liquid zone with on the second wing plate body.
Further again, described deflector has sedimentary second gradient of discharging from blowdown drain outlet for catching.
As preferably, between described the first wing plate body and deflector, be provided with interval to form described drain outlet.
As preferably, described the first wing plate body is provided with through hole to form described drain outlet.
The present invention also provides another technical scheme: a kind of laterally shunting 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, this purifier is formed by least one group precipitation component combination, the multi-disc wing plate that described precipitation parts comprise deflector and arrange along fluid circulating direction; 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 blowdown drain outlet of circulation downwards, and the first wing plate body and the second wing plate body have the inclination of being convenient to sediment and flowing into described blowdown drain outlet.
Further, described exit is along being provided with water leg perpendicular to fluid circulating direction.
Further, 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, by wing plate is set, current layering is purified, when MEDIA FLOW is after one deck wing plate wherein, its precipitum can be entered to settling zone, 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 Facad structure schematic diagram of the another 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-.
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 laterally shunting Separation of Solid and Liquid purifier, is arranged in order and is formed by least one group precipitation parts 9, certainly, according to environment for use difference, also can have other building forms, 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, wing plate 2 is located on deflector, and arrange along fluid circulating direction, and fluid circulating direction is horizontal direction in the present invention, 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 being connected with deflector, another part is for sedimentary the first wing plate body 21 of drainage, 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 the first wing plate body 21 respectively with the second flow-stopping plate 4, 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 the first wing plate body 21, between the first flow-stopping plate 3 and the second flow-stopping plate 4 threes, 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.
As in Figure 2-4, shown the structural representation of single group of sedimentation parts, it is by injection machine integrated injection molding; In the time only adopting one group of structure in settling tank, the side of the first flow-stopping plate of sedimentation parts, the second flow-stopping plate and pond body sidewall need to be close to; And in the time adopting combination as shown in Figure 1, the deflector of rear one group of sedimentation parts is just located at before the drain outlet of last group, between deflector, front and back two flow-stopping plates and the first wing plate body, form quiet liquid zone 71, fluid in this quiet liquid zone is almost static not to flow, and sediment well precipitates and enters drain outlet 11 in quiet liquid zone; On the first wing plate body 21, be positioned at quiet liquid zone and 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; And the first wing plate body and the second wing plate body all have the gradient of being convenient to sediment inflow drain outlet 11; Concrete, if when the first wing plate body and the second wing plate body are structure as a whole, wing plate 2 entirety have downward gradient, as shown in Figure 2,3; In the time that current are flowed through wing plate 2, sediment 88 can successfully flow to drain outlet 11 naturally, and as preferably, in the present embodiment, the tilt angle alpha of described wing plate is 60 °.
In the present embodiment, described wing plate 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; 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 3 has stopped the water flow impact pressure on the first 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, and it protrudes from the second flow-stopping plate 4 and arranges, and is exposed to stopping in scope of the second flow-stopping plate 4; And in the time that current are flowed through precipitation 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 88 is progressively precipitated, along the first wing plate body to drain outlet landing.
Fig. 1, 4, in 5, arrow represents fluid circulating direction, when fluid is as water to be clean, while flowing to from import department, the precipitation of flowing through parts, the second wing plate body 22 on every layer of wing plate carries out layering water conservancy diversion to current, water on the second wing plate body in mobile process its sediment along the first wing plate direction of flow drain outlet 11, 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 on the second wing plate body.
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, 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 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 β can be 80 °; As shown in Figure 2, the deflector of latter a group just can be caught the sediment 88 of the drain outlet discharge of last group of sedimentation parts, and sediment 88 is slowly discharged downwards along deflector again; The setting of gradient, 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.
Embodiment bis-
As shown in Figure 5, a kind of laterally shunting 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 3 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 (7)
1. a horizontal shunting Separation of Solid and Liquid purifier, is formed by least one group precipitation component combination, 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 blowdown 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 blowdown drain outlet.
2. horizontal shunting Separation of Solid and Liquid purifier according to claim 1, is characterized in that: described deflector (1) is connected away from a side of quiet liquid zone (71) with the second wing plate body (22) is upper.
3. horizontal shunting Separation of Solid and Liquid purifier according to claim 2, is characterized in that: described deflector (1) has sedimentary second gradient of discharging from blowdown drain outlet (11) for catching.
4. horizontal shunting Separation of Solid and Liquid purifier according to claim 1, is characterized in that: between described the first wing plate body (21) and deflector, be provided with interval to form described drain outlet (11).
5. horizontal shunting Separation of Solid and Liquid 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).
6. a horizontal shunting 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 least one group precipitation component combination the multi-disc wing plate (2) that 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 blowdown 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 blowdown drain outlet.
Horizontal shunting inclined plate sedimentation according to claim 6 pond, is characterized in that: described outlet (54) is located along being provided with water leg (55) perpendicular to fluid circulating direction.
7. horizontal shunting inclined plate sedimentation according to claim 6 pond, is characterized in that: described settling zone has funnel-form outlet (531).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320722253.0U CN203678024U (en) | 2013-11-17 | 2013-11-17 | Transverse shunt type solid-liquid separation purification device and sedimentation tank with purification device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320722253.0U CN203678024U (en) | 2013-11-17 | 2013-11-17 | Transverse shunt type solid-liquid separation purification device and sedimentation tank with purification device |
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| Publication Number | Publication Date |
|---|---|
| CN203678024U true CN203678024U (en) | 2014-07-02 |
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|---|---|---|---|
| CN201320722253.0U Expired - Lifetime CN203678024U (en) | 2013-11-17 | 2013-11-17 | Transverse shunt type solid-liquid separation purification device and sedimentation tank with purification device |
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| CN (1) | CN203678024U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107789864A (en) * | 2017-11-13 | 2018-03-13 | 重庆洁邦电器有限公司 | A kind of self-cleaning cycle water tank |
| CN108144330A (en) * | 2018-01-01 | 2018-06-12 | 浙江联池水务设备股份有限公司 | A kind of solid inclined plate purifier and the sedimentation basin with the purifier |
| CN110344488A (en) * | 2018-04-02 | 2019-10-18 | 玖龙纸业（太仓）有限公司 | A kind of novel pipeline blowdown apparatus |
-
2013
- 2013-11-17 CN CN201320722253.0U patent/CN203678024U/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107789864A (en) * | 2017-11-13 | 2018-03-13 | 重庆洁邦电器有限公司 | A kind of self-cleaning cycle water tank |
| CN108144330A (en) * | 2018-01-01 | 2018-06-12 | 浙江联池水务设备股份有限公司 | A kind of solid inclined plate purifier and the sedimentation basin with the purifier |
| CN110344488A (en) * | 2018-04-02 | 2019-10-18 | 玖龙纸业（太仓）有限公司 | A kind of novel pipeline blowdown apparatus |
| CN110344488B (en) * | 2018-04-02 | 2024-02-02 | 玖龙纸业（太仓）有限公司 | Novel pipeline blowdown device |
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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: 20141217 |
|
| 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: 20141217 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 |
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| C56 | Change in the name or address of the patentee | ||
| CP01 | Change in the name or title of a patent holder |
Address after: Yuhang District, Hangzhou City, Zhejiang Province, 310000 West No. 1500 Building 2 room 413 Patentee after: ZHEJIANG LIANCHI WATER EQUIPMENT STOCK Co.,Ltd. Address before: Yuhang District, Hangzhou City, Zhejiang Province, 310000 West No. 1500 Building 2 room 413 Patentee before: ZHEJIANG LIANCHI WATER EQUIPMENT Co.,Ltd. |
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| 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 | ||
| CX01 | Expiry of patent term |
Granted publication date: 20140702 |
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| CX01 | Expiry of patent term |