CN202191738U - Double-inclined-plate type efficient sediment device - Google Patents
Double-inclined-plate type efficient sediment device Download PDFInfo
- Publication number
- CN202191738U CN202191738U CN2011202906281U CN201120290628U CN202191738U CN 202191738 U CN202191738 U CN 202191738U CN 2011202906281 U CN2011202906281 U CN 2011202906281U CN 201120290628 U CN201120290628 U CN 201120290628U CN 202191738 U CN202191738 U CN 202191738U
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- Prior art keywords
- swash plate
- inclined plate
- double
- reaction
- utility
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Abstract
The utility model discloses a double-inclined-plate type efficient sediment device. The efficient sediment device consists of a reaction area, a sediment area which are connected in series; a mixing motor is arranged at the top of the reaction area and drives a mixing blade at the lower part of a mixing shaft to rotate; two layers of inclined plate filler are arranged in the sediment area; a lower inclined plate and an upper inclined plate are arranged above a sludge collecting hopper; and the lower inclined plate is opposite to the upper inclined plate in inclined direction to form a certain included angle. According to the utility model, the folded plate reaction of the reaction area is changed into mechanical mixing reaction, the sediment area is provided with the two layers of inclined plate (tube) filler, and the upper inclined plate and the lower inclined plate are arranged in a crossed way, so that the large-flow, efficient and high-quality sewage treatment effect can be achieved, and the overall treatment capacity is increased by 2-5 times.
Description
Technical field
The utility model relates to the sewage disposal device field, the efficient settler of especially double-deck ramp type.
Background technology
Existing swash plate (pipe) sedimentation basin is applied to low turbidity waste sewage, water purifying processing systems such as municipal sewage, river water cleaning, and as shown in Figure 1, swash plate (pipe) sedimentation basin is made up of two parts usually, and leading portion is a reaction zone 1, and the rear end is settling zone 2.Reaction zone adopts the flap reaction formation usually, reaches the hybrid reaction of medicament and sewage thereby utilize current between each lattice flap, to flow back and forth, increases the time of contact of medicament and sewage, and this regional reaction time is 20～25 minutes.Settling zone 2 is made up of two parts up and down; Top is swash plate (pipe) packing area 2-2, and the bottom is sludge hopper district 2-1, and the sewage that reacts completely gets into from swash plate (pipe) filler bottom and upwards flows; Suspension, particle flow along water (flow) direction and run into swash plate (pipe) and hinder its rising; Fall into sludge hopper along swash plate (pipe), thereby reach the effect of deposition, this zone design surface loading is 2～4m
3/ m
2.h.But the sedimentation basin of this structure processing cycle is longer, and treatment effeciency is lower, and the reaction zone reaction time is longer, and the settling zone surface loading is less, and therefore required volume is bigger, and equipment investment cost is higher.
The utility model content
The applicant is longer to above-mentioned existing swash plate (pipe) the sedimentation basin processing cycle; Shortcomings such as treatment effeciency is lower; A kind of efficient settler of double-deck ramp type of compactness rational in infrastructure is provided, thereby can purifies coal mine sewage efficiently, satisfy the water treatment requirement.
The technical scheme that the utility model adopted is following:
The efficient settler of a kind of double-deck ramp type is composed in series by reaction zone, settling zone, and the top of reaction zone is provided with stirring motor, and stirring motor drives the stirring vane rotation of shaft bottom; Double-deck swash plate filler is set in the settling zone, above sludge hopper, is provided with lower floor's swash plate and upper strata swash plate, and the incline direction of lower floor's swash plate and upper strata swash plate forms an angle on the contrary.
It is further characterized in that: the aperture of said lower floor swash plate is greater than the aperture of upper strata swash plate.
Angle between said lower floor swash plate and the upper strata swash plate is 60～120 degree.
The beneficial effect of the utility model is following:
The utility model changes the flap reaction of reaction zone into the mechanical agitation reaction; And be provided with double-deck swash plate (pipe) filler in the settling zone; Two-layer up and down swash plate is arranged in a crossed manner, therefore can reach big flow, high efficiency, high-quality wastewater treatment efficiency, and the overall process ability has improved 2～5 times.
Description of drawings
Fig. 1 is the structural representation of existing swash plate (pipe) sedimentation basin.
Fig. 2 is the structural representation of the utility model.
Fig. 3 is the vertical view of Fig. 2.
Fig. 4 is the left view of Fig. 2.
The specific embodiment
Below in conjunction with accompanying drawing, the specific embodiment of the utility model is described.
Extremely shown in Figure 4 like Fig. 2; The utility model is made up of reaction zone 1 and settling zone 2, has cancelled folded structure in the reaction zone 1 of the utility model, and has adopted the mechanical agitation structure; Center of top at reaction zone is provided with stirring motor 101; Stirring motor 101 drives stirring vane 103 rotations of shaft 102 bottoms, sewage and the flocculation medicament that gets into reaction zone 1 from water inlet 104 is mixed, thereby quicken the hybrid reaction of medicament and sewage; Reduced the reaction time, the mechanical agitation reaction time generally only needs 5～10 minutes.
The utility model is provided with double-deck swash plate (pipe) filler in settling zone 2, above sludge hopper 203, be provided with lower floor's swash plate 201 and upper strata swash plate 202, and the aperture of lower floor's swash plate 201 is that the aperture of 50mm, upper strata swash plate 202 is 35mm; And lower floor's swash plate 201 is opposite with the incline direction of upper strata swash plate 202; Lower floor as shown in Figure 2 swash plate is horizontal by oblique upper left 45 degree, and the upper strata swash plate is horizontal by oblique upper right 45 degree, and promptly the angle between lower floor's swash plate and the upper strata swash plate is 90 degree; Certainly; This angle value also can be set to 60～120 degree, and 2 opposite sides in the settling zone are provided with delivery port 204.During real work, got into from swash plate (pipe) filler bottom and upwards flowed by the sewage behind the confection of flow export 105 entering settling zones 2, suspension, particle flow along water (flow) direction and run into swash plate (pipe) and hinder its rising; Fall into sludge hopper along swash plate (pipe); Thereby the deposition of realization, the utility model is provided with double-deck swash plate (pipe) filler, and arranged in a crossed manner; Increase the frequency of exposure of suspension and filler greatly, improved sedimentation effect; From the microcosmic angle analysis; If for traditional individual layer swash plate filler; Need increase the unit interval treating capacity, must accelerate the flow velocity of sewage, and the blocking effect of individual layer swash plate be limited; Velocity potential must make the lighter dirt particle of part break through the packing area faster, causes the reduction of final outflow water quality.And lower floor's swash plate of double-deck swash plate can stop and the dirt of the larger particles that capture velocity is slower; And rapid speed than the dirt of granule through behind this layer swash plate; Speed slows down greatly, to be stopped and intercept and capture by the upper strata swash plate, thereby can obtain effluent characteristics preferably.Therefore the utility model can be accelerated the flow velocity of sewage greatly; Thereby improve the treating capacity of unit interval; Also can under same treating capacity requires, effectively reduce the volume of settling zone, show that according to the actual tests data surface loading of double-deck swash plate (pipe) is 7～8m
3/ m
2.h, disposal ability has improved 2～4 times.
More than describing is the explanation to the utility model, is not the qualification to utility model, and the utility model institute restricted portion is referring to claim, and under the situation of the utility model spirit, the utility model can be done any type of modification.
Claims (3)
1. efficient settler of double-deck ramp type, it is characterized in that: be composed in series by reaction zone, settling zone, the top of reaction zone is provided with stirring motor, and stirring motor drives the stirring vane rotation of shaft bottom; Double-deck swash plate filler is set in the settling zone, above sludge hopper, is provided with lower floor's swash plate and upper strata swash plate, and the incline direction of lower floor's swash plate and upper strata swash plate forms an angle on the contrary.
2. according to the efficient settler of the described double-deck ramp type of claim 1, it is characterized in that: the aperture of said lower floor swash plate is greater than the aperture of upper strata swash plate.
3. according to the efficient settler of the described double-deck ramp type of claim 1, it is characterized in that: the angle between said lower floor swash plate and the upper strata swash plate is 60～120 degree.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011202906281U CN202191738U (en) | 2011-08-11 | 2011-08-11 | Double-inclined-plate type efficient sediment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011202906281U CN202191738U (en) | 2011-08-11 | 2011-08-11 | Double-inclined-plate type efficient sediment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202191738U true CN202191738U (en) | 2012-04-18 |
Family
ID=45946670
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011202906281U Expired - Lifetime CN202191738U (en) | 2011-08-11 | 2011-08-11 | Double-inclined-plate type efficient sediment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202191738U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103848487A (en) * | 2012-11-30 | 2014-06-11 | 南通京源水工自动化设备有限公司 | Grid stirring flocculation reaction device |
| CN111420433A (en) * | 2020-04-09 | 2020-07-17 | 杭州鼎辉环保科技有限公司 | SS double-layer mixed flow precipitation and concentration integrated equipment and precipitation method thereof |
-
2011
- 2011-08-11 CN CN2011202906281U patent/CN202191738U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103848487A (en) * | 2012-11-30 | 2014-06-11 | 南通京源水工自动化设备有限公司 | Grid stirring flocculation reaction device |
| CN111420433A (en) * | 2020-04-09 | 2020-07-17 | 杭州鼎辉环保科技有限公司 | SS double-layer mixed flow precipitation and concentration integrated equipment and precipitation method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee |
Owner name: JIANGSU XINYU TIANCHENG ENVIRONMENTAL PROTECTION E Free format text: FORMER NAME: JIANGSU XINYU TIANCHENG ENVIRONMENTAL PROTECTION ENGINEERING CO., LTD. |
|
| CP01 | Change in the name or title of a patent holder |
Address after: 214214 3-4-5, 39 international environmental protection city, Wuxi, Jiangsu, Yixing Patentee after: JIANGSU XINYU TIANCHENG ENVIRONMENTAL PROTECTION ENGINEERING CO., LTD. Address before: 214214 3-4-5, 39 international environmental protection city, Wuxi, Jiangsu, Yixing Patentee before: Jiangsu Xinyu Tiancheng Environmental Protection Engineering Co., Ltd. |
|
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 214214 3-4-5, 39 international environmental protection city, Wuxi, Jiangsu, Yixing Patentee after: Jiangsu Xinyu Tiancheng environmental protection Co. Ltd. Address before: 214214 3-4-5, 39 international environmental protection city, Wuxi, Jiangsu, Yixing Patentee before: JIANGSU XINYU TIANCHENG ENVIRONMENTAL PROTECTION ENGINEERING CO., LTD. |
|
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20120418 |