CN204224366U - Efficient full automatic water purifier - Google Patents
Efficient full automatic water purifier Download PDFInfo
- Publication number
- CN204224366U CN204224366U CN201420693953.6U CN201420693953U CN204224366U CN 204224366 U CN204224366 U CN 204224366U CN 201420693953 U CN201420693953 U CN 201420693953U CN 204224366 U CN204224366 U CN 204224366U
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- CN
- China
- Prior art keywords
- flocculation zone
- pipe
- water
- reduction
- inlet pipe
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- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
Efficient full automatic water purifier.Providing one is not reducing in water intake velocity situation, and flocculating effect is good, and filter effect is good, reduces the efficient full automatic water purifier of production cost.Comprise the water inlet pipe connected successively, flocculation zone, transition water reserve, inclined-pipe settler, settling region, filtering cabin, clean water basin and rising pipe, bottom, described flocculation zone is provided with shore pipe, exit near described water inlet pipe in described flocculation zone is provided with speed decreasing mechanism, described speed decreasing mechanism comprises reduction of speed plate, turning axle and motor, the outside of described flocculation zone is located at by described motor, described turning axle one end connects the output shaft of described motor, the other end of described turning axle is fed through described reduction of speed plate, described inclined-pipe settler comprises some sediments tube, the cross section of described sediment tube is that continuous print is stepped, the junction of described flocculation zone and transition water reserve is provided with screen plate.The utility model plays reduction flow velocity, extends the reaction times, improves spoil disposal efficiency.
Description
Technical field
The utility model relates to sewage treatment area, particularly relates to efficient full automatic water purifier.
Background technology
Sewage disposal needs usually through operations such as flocculation, filtration, precipitations, and the most standard compliant water outwards discharges.Wherein in flocculation and filtration two procedures, usually in flocculation basin, add flocculation agent, suspended particulates in water or liquid are gathered and becomes large, or form floc sedimentation, thus add the coagulation of fast particle, reach the object of solid-liquid separation.But because water inlet pipe is in flocculation basin during water filling, because water intake velocity is fast, cause sewage and the flocculation agent reaction times short, flocculating effect is poor; If reduction water intake velocity, then cause whole sewage treating efficiency low.
Utility model content
The utility model is for above problem, and provide one and do not reducing in water intake velocity situation, flocculating effect is good, and filter effect is good, reduces the efficient full automatic water purifier of production cost.
The technical solution of the utility model is: comprise the water inlet pipe connected successively, flocculation zone, transition water reserve, inclined-pipe settler, settling region, filtering cabin, clean water basin and rising pipe, bottom, described flocculation zone is provided with shore pipe, the top of described flocculation zone is communicated with described transition water reserve, described transition water reserve and settling region lay respectively at above and below described inclined-pipe settler, described filtering cabin is located at the side of described settling region, the top of described filtering cabin is located at by described clean water basin, described transition water reserve is provided with filtered water inlet pipe and is communicated in described filtering cabin, described rising pipe connects described clean water basin,
Exit near described water inlet pipe in described flocculation zone is provided with speed decreasing mechanism, described speed decreasing mechanism comprises reduction of speed plate, turning axle and motor, the outside of described flocculation zone is located at by described motor, described turning axle one end connects the output shaft of described motor, the other end of described turning axle is fed through described reduction of speed plate, and described reduction of speed plate is wavy towards the one side of described water inlet pipe;
Described inclined-pipe settler comprises some oblique settings and the sediment tube be parallel to each other, and the cross section of described sediment tube is that continuous print is stepped;
The junction of described flocculation zone and transition water reserve is provided with screen plate.
Described screen plate be provided with some trumpet-shaped filter pore and the opening small end of trumpet-shaped described filter pore towards described flocculation zone.
The angle of described reduction of speed plate and described water inlet pipe is 30 degree-75 and spends.
The angle of inclination of the utility model reduction of speed plate according to the flow of water inlet and speed setting, plays reduction flow velocity, guarantees that the flocculation agent in sewage and flocculation zone fully reacts.Because reduction of speed plate is wavy towards the one side of water inlet pipe, after making sewage enter flocculation zone, also can the wave path of rising in certain rising space, extend the reaction times.Reduction of speed plate also plays guide effect simultaneously, and impurity agglomerating for the flocculation fallen is collected to shore pipe place, improves spoil disposal efficiency.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model,
Fig. 2 is the left view of Fig. 1,
Fig. 3 is the structural representation of sediment tube in Fig. 1,
Fig. 4 is I place close-up schematic view in Fig. 1;
In figure, 1 is water inlet pipe, and 2 is flocculation zones, and 3 is transition water reserves, 31 is filtered water inlet pipes, and 4 is inclined-pipe settlers, and 41 is sediments tube, 5 is settling regions, and 6 is filtering cabins, and 7 is clean water basin, 8 is rising pipes, and 9 is shore pipes, and 10 is speed decreasing mechanisms, 101 is reduction of speed plates, and 102 is turning axles, and 103 is motors, 11 is screen plates, and 111 is filter pore.
Embodiment
The utility model as Figure 1-4, comprise the water inlet pipe 1 connected successively, flocculation zone 2, transition water reserve 3, inclined-pipe settler 4, settling region 5, filtering cabin 6, clean water basin 7 and rising pipe 8, bottom, described flocculation zone 2 is provided with shore pipe 9, the top of described flocculation zone 2 is communicated with described transition water reserve 3, described transition water reserve 3 and settling region 5 lay respectively at above and below described inclined-pipe settler 41, described filtering cabin 6 is located at the side of described settling region 5, the top of described filtering cabin 6 is located at by described clean water basin 7, described transition water reserve 3 is provided with filtered water inlet pipe 31 and is communicated in described filtering cabin 6, described rising pipe 8 connects described clean water basin 7.
Speed decreasing mechanism 10 is provided with near the exit of described water inlet pipe 1 in described flocculation zone 2, described speed decreasing mechanism 10 comprises reduction of speed plate 101, turning axle 102 and motor 103, the outside of described flocculation zone 2 is located at by described motor 103, described turning axle 102 one end connects the output shaft of described motor 103, the other end of described turning axle 102 is fed through described reduction of speed plate 101, and described reduction of speed plate 101 is wavy towards the one side of described water inlet pipe 1.
Described inclined-pipe settler 4 comprises some oblique settings and the sediment tube 41 be parallel to each other, and the cross section of described sediment tube 41 is that continuous print is stepped, when making sewage enter described sediment tube 41, by extending conduct path, improves sedimentation effect.Meanwhile, because the cross section of described sediment tube 41 is stepped, make the impurity in sewage strike the tube wall of described sediment tube 41, thus glide until precipitation along the tube wall of sediment tube 41, thus promote sedimentation effect further.
Described flocculation zone 2 is provided with screen plate 11 with the junction of transition water reserve 3, described screen plate 11 be provided with some trumpet-shaped filter pore 111 and the opening small end of trumpet-shaped described filter pore 111 towards described flocculation zone 2.
Described reduction of speed plate 101 is 30 degree-75 with the angle of described water inlet pipe 1 and spends.
In the utility model, according to the flow of intaking and speed setting, the angle of inclination of reduction of speed plate, plays reduction flow velocity, guarantees that the flocculation agent in sewage and flocculation zone fully reacts.Because reduction of speed plate is wavy towards the one side of water inlet pipe, after making sewage enter flocculation zone, also can the wave path of rising in certain rising space, extend the reaction times.Reduction of speed plate also plays guide effect simultaneously, and impurity agglomerating for the flocculation fallen is collected to shore pipe place, improves spoil disposal efficiency.
Claims (3)
1. efficient full automatic water purifier, comprise the water inlet pipe connected successively, flocculation zone, transition water reserve, inclined-pipe settler, settling region, filtering cabin, clean water basin and rising pipe, bottom, described flocculation zone is provided with shore pipe, the top of described flocculation zone is communicated with described transition water reserve, described transition water reserve and settling region lay respectively at above and below described inclined-pipe settler, described filtering cabin is located at the side of described settling region, the top of described filtering cabin is located at by described clean water basin, described transition water reserve is provided with filtered water inlet pipe and is communicated in described filtering cabin, described rising pipe connects described clean water basin, it is characterized in that,
Exit near described water inlet pipe in described flocculation zone is provided with speed decreasing mechanism, described speed decreasing mechanism comprises reduction of speed plate, turning axle and motor, the outside of described flocculation zone is located at by described motor, described turning axle one end connects the output shaft of described motor, the other end of described turning axle is fed through described reduction of speed plate, and described reduction of speed plate is wavy towards the one side of described water inlet pipe;
Described inclined-pipe settler comprises some oblique settings and the sediment tube be parallel to each other, and the cross section of described sediment tube is that continuous print is stepped;
The junction of described flocculation zone and transition water reserve is provided with screen plate.
2. efficient full automatic water purifier according to claim 1, is characterized in that, described screen plate be provided with some trumpet-shaped filter pore and the opening small end of trumpet-shaped described filter pore towards described flocculation zone.
3. efficient full automatic water purifier according to claim 1, is characterized in that, the angle of described reduction of speed plate and described water inlet pipe is 30 degree-75 and spends.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201420693953.6U CN204224366U (en) | 2014-11-18 | 2014-11-18 | Efficient full automatic water purifier |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201420693953.6U CN204224366U (en) | 2014-11-18 | 2014-11-18 | Efficient full automatic water purifier |
Publications (1)
Publication Number | Publication Date |
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CN204224366U true CN204224366U (en) | 2015-03-25 |
Family
ID=52922484
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201420693953.6U Expired - Fee Related CN204224366U (en) | 2014-11-18 | 2014-11-18 | Efficient full automatic water purifier |
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CN (1) | CN204224366U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111494995A (en) * | 2020-04-24 | 2020-08-07 | 淮北市中芬矿山机器有限责任公司 | Efficient steady-flow uniform distributing device of central transmission thickener |
-
2014
- 2014-11-18 CN CN201420693953.6U patent/CN204224366U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111494995A (en) * | 2020-04-24 | 2020-08-07 | 淮北市中芬矿山机器有限责任公司 | Efficient steady-flow uniform distributing device of central transmission thickener |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150325 Termination date: 20181118 |
|
CF01 | Termination of patent right due to non-payment of annual fee |