CN202538426U - Multilayer parallel-vane micro-vortex skew-plate set for water treatment - Google Patents
Multilayer parallel-vane micro-vortex skew-plate set for water treatment Download PDFInfo
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- CN202538426U CN202538426U CN2012200350957U CN201220035095U CN202538426U CN 202538426 U CN202538426 U CN 202538426U CN 2012200350957 U CN2012200350957 U CN 2012200350957U CN 201220035095 U CN201220035095 U CN 201220035095U CN 202538426 U CN202538426 U CN 202538426U
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Abstract
The utility model provides a multilayer parallel-vane micro-vortex skew-plate set for water treatment. The multilayer parallel-vane micro-vortex skew-plate set for water treatment comprises micro-vortex skew plate units. Each micro-vortex skew plate unit is composed of a plastic plate, a plurality of parallel ribs and vanes. The parallel ribs are arranged on the back of the plastic plate, the parallel vanes in multiple layers are disposed on the lower portion of each rib, and the vanes are integrally connected with the ribs on the plastic plate at a connecting angle of 30-90 degrees. The ribs are added to the micro-vortex skew plates, water passing the skew plates can generate micro vortexes at the rears of the vanes, and accordingly flocculating effect is enhanced. By the micro vortexes of the water, alum floc particles are further flocculated, contact collision and rubbing are generated, the particles grow big and compact further, and sedimentation is better. By contact floc action, small floc particle difficult or unavailable to sedimentate can be removed effectively, effluent effect is guaranteed effectively, and sedimentation efficiency of the skew plate set is improved greatly.
Description
Technical field
A kind of water treatment of the utility model is used for the water treatment of water suspended substance sedimentation with the parallel fin microvovtex of multilayer swash plate, is particularly useful for the precipitation process of former water pretreatment, clean water treatment, advanced treatment of wastewater, belongs to the water treatment facilities technical field.
Background technology
At present; The efficient precipitation form that water treatment field is generally acknowledged has tube settler and inclined-plate clarifying basin, ties up to inclined tube or swash plate equipment are installed in the pond, makes when the water that contains suspension passes through inclined tube (plate); Suspended solid obtains sedimentation and removes; Be the guidance and the practical application of water treatment field PRECIPITATION MECHANISM and shallow pool theory, for horizontal sedimentation tank, deposition efficiency increases.But the inclined tube of common form (plate) intensity difference, the life-span is low, deposition efficiency is also general on the whole.Usually compressive resistance is at 490KN/m
2In, very easily damaged or cave in, in 3 years service life.
Through swash plate, between plate, flowing is approximately laminar condition in inclined tube (plate) bottom for the different orientation flowing oblique tube of traditional form (plate), current; Suppress the pulsation of current in swash plate, according to PRECIPITATION MECHANISM, the alumen ustum after the flocculation is under the self gravitation effect as far as possible; Overcome and go up the surface that its jacking force is deposited in swash plate to current; But because it is a lot of that flocculate and bad to get into the alumen ustum of swash plate, cause particle very tiny, can not precipitate; Be easy to got into water leg to the current jacking, thereby influence effluent quality by last.
In addition, along with the raising of living standards of the people, water consumption also constantly increases, and the required soil of engineering of water treatment also climbs up and up, and in order to save limited land resources, we will adopt floor space littler, the swash plate equipment that deposition efficiency is higher.
To sum up, and though existing swash plate on the compressive resistance, on the water outlet effect, or on deposition efficiency, all need further to improve, this has just proposed higher improvement requirement to it.
Summary of the invention
The utility model provides a kind of water treatment with the parallel fin microvovtex of multilayer swash plate, has solved traditional inclined tube swash plate intensity difference, the life-span is low and water outlet weak effect, problem that deposition efficiency is low.
The technology solution case of the utility model is following:
Constitute microvovtex swash plate unit by plastic plate, rib, fin, the formation water treatment system is vertically arranged in several microvovtex swash plate unit; In microvovtex swash plate unit, if the back side of plastic plate is provided with many parallel ribs, in the Lower Half of every rib the parallel fin of multilayer is set, and fin is connected as a whole with the rib of plastic plate, and connection angle is 30-90 °;
Described fin be positioned at rib bottom 500mm with height, the fin width is 1-10mm, the fin spacing is at 50-200mm.
Because plastic plate has laterally increased the fin reinforcing, has improved swash plate intensity, compressive resistance reaches more than the 980KN/m2, has strengthened the stability of swash plate, and has prolonged service life, can reach more than 8 years.
The utility model good effect is: set up bead structures on the microvovtex swash plate, when current pass through swash plate, can produce the micro-vortex fluidised form at the rear portion of fin; Strengthened flocculating effect; Utilize the micro-vortex fluidised form of current, alumina blossom particles further flocculates, and comes in contact to collide and rub; Particle is further grown up with closely knit, and sedimentation function is better.Through this contact flocculation effect, sedimentation difficulty or granule alumen ustum that can't sedimentation can effectively be removed, and can effectively guarantee the water outlet effect, and improve sloping plate deposition efficient greatly.
The utlity model has good stability, do not have distortion basically, be more than 2 times of traditional swash plate service life.Make the more traditional swash plate technology of this treatment process save pharmaceutical quantities more than 20%, greatly reduce processing cost.Under equal effluent quality required, the more traditional swash plate of the deposition hydraulic load (upflow velocity) of high density microvovtex swash plate improved more than 40%, reaches more than the 3.0mm/s (10.8m3/m2h).Deposition efficiency is high, and floor space is little, and occupation of land is about 70% of traditional swash plate.
Description of drawings
Fig. 1 is the utility model front organigram;
Fig. 2 is the utility model vertical section organigram;
Waterpower schematic diagram when Fig. 3 works for the utility model;
Among the figure 1, fin; 2, plastic plate; 3, rib; 4, deposit seed; L representes enhanced flocculation district height.
The specific embodiment
According to shown in Figure 1, constitute microvovtex swash plate unit by plastic plate 2, rib 3, fin 1, the formation water treatment system is vertically arranged in several microvovtex swash plate unit; In microvovtex swash plate unit, if the back side of plastic plate 2 is provided with many parallel ribs 3, in the Lower Half of every rib 3 the parallel fin of multilayer 1 is set, and fin 1 is connected as a whole with the rib 3 of plastic plate 2.
With reference to Fig. 2, fin 1 be positioned at rib 3 bottom 500mm with height, between parallel fin 1, form the enhanced flocculation district, the flocculation zone height is L, fin 1 width is 1-10mm, fin 1 spacing is at 50-200mm.
In Fig. 3, according to the difference of handling water quantity and quality, current are got into by bottom, swash plate unit, the fin 1 front and rear part current generation micro-vortex fluidised form in the enhanced flocculation district, and particle 4 comes in contact flocculation, and absorption granule floccule body improves deposition efficiency.
Claims (2)
1. a water treatment is with the parallel fin microvovtex of multilayer swash plate; It is characterized in that: the back side of plastic plate is provided with some parallel ribs; Lower Half at every rib is provided with the parallel fin of multilayer, and fin is connected as a whole with the rib of plastic plate, and connection angle is 30-90 °.
2. water treatment according to claim 1 is characterized in that with the parallel fin microvovtex of multilayer swash plate: fin be positioned at rib bottom 500mm with height, the fin width is 1-10mm, the fin spacing is at 50-200mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012200350957U CN202538426U (en) | 2012-02-06 | 2012-02-06 | Multilayer parallel-vane micro-vortex skew-plate set for water treatment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012200350957U CN202538426U (en) | 2012-02-06 | 2012-02-06 | Multilayer parallel-vane micro-vortex skew-plate set for water treatment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202538426U true CN202538426U (en) | 2012-11-21 |
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ID=47159120
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012200350957U Expired - Fee Related CN202538426U (en) | 2012-02-06 | 2012-02-06 | Multilayer parallel-vane micro-vortex skew-plate set for water treatment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202538426U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103301658A (en) * | 2013-04-27 | 2013-09-18 | 江苏中超环保有限公司 | Efficient micro-resistance pulsating vortex sedimentation device |
| CN103585798A (en) * | 2013-11-17 | 2014-02-19 | 池万青 | Vortex type solid-liquid diversion purification device and sedimentation tank provided with same |
| CN105999778A (en) * | 2014-10-14 | 2016-10-12 | 刘伟 | Clarification treatment device and environmental protection device |
-
2012
- 2012-02-06 CN CN2012200350957U patent/CN202538426U/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103301658A (en) * | 2013-04-27 | 2013-09-18 | 江苏中超环保有限公司 | Efficient micro-resistance pulsating vortex sedimentation device |
| CN103301658B (en) * | 2013-04-27 | 2015-07-22 | 江苏中超环保有限公司 | Efficient micro-resistance pulsating vortex sedimentation device |
| CN103585798A (en) * | 2013-11-17 | 2014-02-19 | 池万青 | Vortex type solid-liquid diversion purification device and sedimentation tank provided with same |
| CN105999778A (en) * | 2014-10-14 | 2016-10-12 | 刘伟 | Clarification treatment device and environmental protection device |
| CN106039777A (en) * | 2014-10-14 | 2016-10-26 | 刘伟 | Sewage sediment device for protecting environment |
| CN106039778A (en) * | 2014-10-14 | 2016-10-26 | 刘伟 | Water clarification treatment device capable of being applied to water plant, environmental protection device and water processing plant |
| CN106039777B (en) * | 2014-10-14 | 2017-12-29 | 惠州市合新科技有限公司 | Sewage precipitation device for environmental protection |
| CN106039778B (en) * | 2014-10-14 | 2018-06-22 | 中山公用水务有限公司 | Available for the clarification of water processing unit of water factory, environmental protecting device, water processing factory |
| CN105999778B (en) * | 2014-10-14 | 2018-07-31 | 葛礼双 | Apparatus for clarifying, environmental protecting device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20121121 Termination date: 20140206 |