CN2585852Y - Fully automatic integrated water purifier - Google Patents
Fully automatic integrated water purifier Download PDFInfo
- Publication number
- CN2585852Y CN2585852Y CN 02283212 CN02283212U CN2585852Y CN 2585852 Y CN2585852 Y CN 2585852Y CN 02283212 CN02283212 CN 02283212 CN 02283212 U CN02283212 U CN 02283212U CN 2585852 Y CN2585852 Y CN 2585852Y
- Authority
- CN
- China
- Prior art keywords
- water
- fully automatic
- flocculator
- siphon
- pipe
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Images
Abstract
The utility model relates to a fully automatic integrated water purifier, which belongs to the technical field of water purifiers. The fully automatic integrated water purifier comprises a raw water inlet pipe, a flocculating device, a sedimentation tank, a filter tank, a filtered water outlet pipe, a flocculating device, a sedimentation tank and a filter tank which are integrated into one body. The water inlet pipe is connected with the flocculating device. The flocculating device is arranged at the lower part of the sedimentation tank. A water outlet of the sedimentation tank is connected with the filter tank. An automatic sewage drainage device is arranged on the filter tank. The flocculating device, a sedimentation device and a filter device are integrated into one body by the utility model. The utility model is capable of integral and industrial bulk production. The utility model has the advantages of small occupation area and short site construction period. The utility model is additionally provided with the variable current flocculating device and the vertical current type parallel flap flocculating device to enhance a flocculating effect and the quality of the water outlet of the sedimentation tank, change the composition of the diameter of filtering material grain, and enhance the quality of the water outlet of the filtered water. The utility model adopts hydraulic full-automatic control without unattended operation and realizes the hydraulic full automation of the integrated water purifier.
Description
Technical field
The utility model belongs to the purifier technical field, relates to a kind of fully automatic integral purifier.
Background technology
The middle-size and small-size waterworks in cities and towns adopted the reinforced concrete water pond form as the main structures that purify more in the past, and big, the on-the-spot construction period of floor space is long.Existing integral water purifier on the market, the suspension contact is only adopted in flocculation, and it is insufficient to flocculate, and the delivery turbidity of settling tank can only be controlled at below the 10NTU.What the filtrate on the market in the existing integral water purifier adopted is the common quartz sand filter media of 0.6～1.2mm, and the delivery turbidity of filter back water can only be controlled at below the 3NTU.Existing integral water purifier is to adopt manually operation by rule of thumb on the market, can not move automatically.Because above factor, the construction of China middle-size and small-size water factory in cities and towns exists,, defectives such as effluent quality poor, operational administrative inconvenience long with big, the on-the-spot construction period of ground area.
Summary of the invention
Technical problem to be solved in the utility model is to overcome above defective of the prior art, impel the middle-size and small-size waterworks construction in cities and towns, provide little, the on-the-spot construction period of a kind of floor space short, effluent quality good, the fully automatic integral purifier of unattended, convenient management.
The technical scheme that solution the utility model technical problem is adopted is this fully automatic integral purifier, comprise water rising pipe after former water water inlet pipe, flocculator, settling tank, filtering basin, the filter, flocculator, settling tank, filtering basin are formed one, water inlet pipe is connected with flocculator, flocculator is in the bottom of settling tank, the rising pipe of settling tank is connected with filtering basin, and the automatic pollution discharge drainage facility is installed on the filtering basin.
The utility model is formed flocculation, precipitation and filtration facility integrated, can whole batch production produce by batch, and little, the on-the-spot construction period of floor space is short.Set up variable flow flocculator and vertical-flow parallel folded plate flocculation device, improve flocculating effect and effluent quality of sedimentation tank.Change particle diameter of filter medium and form, improve filter back water effluent quality.Adopt the waterpower full automatic control, unattended, realize the waterpower full-automation of integral water purifier.
Description of drawings
Below in conjunction with the embodiment accompanying drawing, the utility model is described in further detail.
Fig. 1 the utility model front view
Fig. 2 is the utility model vertical view
Fig. 3 is the A-A sectional view among Fig. 2
Fig. 4 is the B-B sectional view among Fig. 3
Fig. 5 is the C-C sectional view among Fig. 3
Fig. 6 is the D-D sectional view among Fig. 3
Fig. 7 is the E-E sectional view among Fig. 3
Among the figure: water outlet pipe 21-sedimentation basin and wall 22-filter tank, filter tank median septum 23-sedimentation basin centre housing 24-railing 25-steel cover manhole 27-inclined tube wallsten stent 28-pool wall water leg 29-two-sided water collecting groove 30-drain channel of sedimentation tank 31-washing strength regulator 32-water dispensing board 33-filter tank, 26-filter tank top manway 34-cover body 35-walkway board 36-syphon hood top board interface 37-external water source tube of marking time after the quartzy extra large sand filter blanket of grain 10-gathering ground, 11-intercommunicating pore, 12-flush box, the 13-siphon tedge 14-siphon destructing tube 15-exhaust tube 16-auxiliary siphon tube 17-siphon down-comer 18-siphon destructive bucket 19-gully 20-filter of 1-former water water inlet pipe 2-non-uniform flow flocculator 3-folded plate flocculation device 4-suspension contact layer 5-sludge hopper 6-tube settler 7-triangle water leg 8-U-shaped water sealing (sealing water) pipe 9-all
Embodiment
In the present embodiment, flocculator is variable flow flocculator (2), or is that variable flow flocculator (2) is combined with folded plate flocculation device (3).Settling tank is tube settler (6), suspension contact layer (4) is arranged between flocculator and the settling tank, the rising pipe of settling tank is a U type syphon trap (8), be connected with filtering basin, filtering basin adopt all grain quartzy extra large sand filter blankets (9), catchment area under the filtering basin (10) connects flush box (12) by communicating aperture (11), filter back water rising pipe (20) is connected on the flush box (12), to be a siphonal siphon upcast (13) be connected with the mouth of pipe on the filtering basin sealing cover automatic pollution discharge drainage facility of installing on the filtering basin, siphon downtake (17) inserts in drain well (19) water, siphon downtake (17) pipe end is carried out water seal, other has the pipe end of siphon destructing tube (14) to insert in the flush box (12), has the pipe end of an auxiliary siphon tube (16) to insert in the drain well (19); Siphon upcast (13) top has extraction pipe (15) to connect auxiliary siphon tube (16), the end of siphon downtake (17) has washing strength regulator (31), by regulating the spacing of washing strength regulator (31) and siphon downtake (17), regulate backwash rate.
During the utility model work, added the mixed former water of flocculation agent and entered purifier via former water water inlet pipe (1).Flocculation rate flocculates from fast to slow in variable flow flocculator (2), enters further enhanced flocculation effect of suspension contact layer (4) through parallel folded plate flocculation device (3) flocculation again.Through fully entering tube settler (6) after the flocculation, suspended substance cause mud-removing bucket (5) bottom under precipitation separation regularly is discharged into water drain, and clear water continues to rise to triangle water leg (7) and enters in the tank.Clear water through post precipitation inserts filtering basin by U type syphon trap (8).Water rises to flush box (12) via communicating aperture (11) and stores by entering the catchment area (10) of filtrate bottom after all the quartzy extra large sand filter blanket of grain (9) filters, and water tank (12) is full of after filter back water rising pipe (20) outflow and use for the user.Because all the quartzy extra large sand filter blanket of grain (9) is constantly held back suspended substance, cause equal grain quartzy extra large sand filter blanket (9) resistance constantly to increase, impel the water level in the siphon upcast (13) constantly to raise, when water level reaches auxiliary siphon tube (16) mouth of pipe, water falls in this pipe, so as to taking away the air in the siphon downtake (17), when vacuum tightness reaches certain value, syphonic effect just takes place by extraction pipe (15).At this moment, the filtering layer that passes through from bottom to top of the water in the water tank (12) carries out back flushing to the quartzy extra large sand filtering material of equal grain.When flush box (12) underwater dropped to siphon destructing tube (14) mouth of pipe, the air admission siphon pipe destroyed syphonic effect, and filter back washing finishes, and the filter tank enters the work of next cycle.The length that the absolute altitude control back flushing of siphon destructive bucket (18) lasts.
Effluent quality of sedimentation tank maintenance good premise is that the impurity in the requirement water can be formed blocky flock, and one of extraneous essential condition that blocky flock forms is to provide suitable waterpower collision opportunity to it.The utility model with variable flow flocculator (2) as the fs flocculation process.The variable flow flocculator is a two-fold inverted cone, and flocculation agent mixes the back and flowed into by the base cone place with water, and diffusion is risen and also descended, along with the cone water-carrying section constantly enlarges, the flocculation flow velocity also progressively from large to small, this variable flow flocculation help the wadding a quilt with cotton formation of grain.With vertical-flow parallel folded plate flocculation device (3) as second section flocculation process.Folded plate flocculation is to add the flow-disturbing unit to reach the desired turbulent state of flocculation on flow route, strengthens the particle collision chance, and energy is fully used, and improves flocculating effect.With suspension contact layer (4) as the phase III flocculation process.Keep a floss suspended layer in the bottom of settling tank, the still inadequate particle of flocculation is fully flocculated, also make the flocculation agent of input bring into play its pharmacy effect fully, and the macrobead flco is held back herein, alleviate the load of settling region at this.Because above measure strengthened flocculation process, make that impurity can form blocky flock in the water, for settling tank raising effluent quality provides the good premise condition.Head loss progressively increased when the utility model utilized water to pass through quartz sand filtration, the principle that required filtering cloth head improves constantly, a certain height at the back flushing water shoot is provided with place's extraction pipe (15), when bringing up to this position, filtering cloth head forms overflow, it is air in the siphon upcast (13) that overflow water is taken the back flushing water shoot away by the suction function of extraction pipe (15), form siphon, finish the back flushing in filter tank.At the back flushing water shoot is that the top of siphon upcast (13) is siphon destructing tube (14) when certain with small pipeline device siphon destructive bucket (18) links to each other, timing device is a water holding box, when the water of water holding box is backwashed that water shoot is pumped to a certain height and when causing the mouth of pipe of pipe connecting to expose to enter air, the siphon state of back flushing water shoot is destroyed and stop siphon drainage, next round normal filtration state is finished and entered automatically to backwash process, go round and begin again, realize full-automatic water purification process.
The flocculation that the utility model is adopted general ground water purification process, precipitation, three kinds of required independent structures of filtration three road master schedules assemble one, the vacant lot area that reduces the contact pipeline between the structures and take.Utilize the waterhead of settling tank and filtering basin, flocculator is arranged on the bottom of settling tank, made full use of the space, further reduced floor space, floor space has only 0.03m
2/ m
3.d.Water purifier adopts steel, can whole batch production produce by batch, and the field assembly debugging only needs 10 day time, has only 1/15 of the general construction period.Table 1 is the utility model technique effect synopsis compared with prior art.
Table 1
| Sequence number | Item compared | Prior art | The utility model | Technique effect |
| 1 | Floor space | 0.35m 2/m 3.d | 0.03m 2/m 3.d | Have only 1/12 |
| 2 | Construction period | 150 | 10 days | Have only 1/15 |
| 3 | Flocculation plant | The suspension contact, settling tank delivery turbidity＜10NTU | The variable flow flocculator adds vertical-flow parallel folding flocculator and the acting in conjunction of suspension contact, settling tank delivery turbidity＜5NTU | Effluent quality of sedimentation tank improves 1 |
| 4 | Filtrate | 0.6-1.2mm common quartz sand, filter back water delivery turbidity＜3NTU | 0.6-0.8mm all the quartzy extra large sand of grain is filtered back water delivery turbidity＜1NTU | Filter back effluent quality improves 2 grades |
| 5 | Control mode | Control manually | The waterpower full automatic control | Unmanned |
| 6 | Construction investment | 300-500 unit/m 3.d | 150-250 unit/m 3.d | Have only 50% |
Claims (10)
1, a kind of fully automatic integral purifier, comprise water rising pipe (20) after former water water inlet pipe (1), flocculator (2), settling tank, filtering basin, the filter, it is characterized in that flocculator (2), settling tank, filtering basin composition one, water inlet pipe (1) is connected with flocculator (2), flocculator is in the bottom of settling tank, the rising pipe of settling tank is connected with filtering basin, and the automatic pollution discharge drainage facility is installed on the filtering basin.
2, fully automatic integral purifier according to claim 1 is characterized in that flocculator is variable flow flocculator (2).
3, fully automatic integral purifier according to claim 1 is characterized in that flocculator is that variable flow flocculator (2) is combined with folded plate flocculation device (3).
4, fully automatic integral purifier according to claim 1 is characterized in that settling tank is tube settler (6).
5, fully automatic integral purifier according to claim 1 is characterized in that suspension contact layer (4) is arranged between flocculator and the settling tank.
6, fully automatic integral purifier according to claim 1, the rising pipe that it is characterized in that settling tank are U type syphon trap (8), and filtering basin adopt all grain quartzy extra large sand filter blankets (9).
7, fully automatic integral purifier according to claim 1 is characterized in that the catchment area (10) under the filtering basin connects flush box (12) by communicating aperture (11), and filter back water rising pipe (20) is connected on the flush box (12).
8, according to claim 1 or 7 described fully automatic integral purifiers, it is characterized in that the automatic pollution discharge drainage facility of installing on the filtering basin is a siphonal siphon upcast (13) and is connected with the mouth of pipe on the filtering basin sealing cover, siphon downtake (17) inserts in drain well (19) water, other has the pipe end of siphon destructing tube (14) to insert in the flush box (12), has the pipe end of an auxiliary siphon tube (16) to insert in the drain well (19).
9, fully automatic integral purifier according to claim 8 is characterized in that siphon upcast (13) top has extraction pipe (15) to connect siphon auxiliary (16).
10, fully automatic integral purifier according to claim 8 is characterized in that the end of siphon downtake (17) has washing strength regulator (31).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 02283212 CN2585852Y (en) | 2002-12-30 | 2002-12-30 | Fully automatic integrated water purifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 02283212 CN2585852Y (en) | 2002-12-30 | 2002-12-30 | Fully automatic integrated water purifier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2585852Y true CN2585852Y (en) | 2003-11-12 |
Family
ID=33745063
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 02283212 Expired - Fee Related CN2585852Y (en) | 2002-12-30 | 2002-12-30 | Fully automatic integrated water purifier |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2585852Y (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1868899B (en) * | 2006-06-08 | 2010-04-07 | 王超 | Method of automatic reusing sewage without discharging and its equipment |
| CN101121553B (en) * | 2006-10-07 | 2010-05-26 | 宋健瑞 | Water treatment technique and device for waterpower osmosis |
| CN101927109A (en) * | 2010-09-16 | 2010-12-29 | 江苏新龙鼎环保成套工程有限公司 | Uniform water supply full-automatic water purifying device |
| CN102442739A (en) * | 2011-09-28 | 2012-05-09 | 江苏金山环保科技股份有限公司 | Efficient chemical oil remover |
| CN110803802A (en) * | 2019-11-21 | 2020-02-18 | 湖南俊翔科技发展有限公司 | Automatic clean system of water works |
| CN110818134A (en) * | 2019-11-21 | 2020-02-21 | 湖南俊翔科技发展有限公司 | Automatic monitoring control system of water plant |
-
2002
- 2002-12-30 CN CN 02283212 patent/CN2585852Y/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1868899B (en) * | 2006-06-08 | 2010-04-07 | 王超 | Method of automatic reusing sewage without discharging and its equipment |
| CN101121553B (en) * | 2006-10-07 | 2010-05-26 | 宋健瑞 | Water treatment technique and device for waterpower osmosis |
| CN101927109A (en) * | 2010-09-16 | 2010-12-29 | 江苏新龙鼎环保成套工程有限公司 | Uniform water supply full-automatic water purifying device |
| CN102442739A (en) * | 2011-09-28 | 2012-05-09 | 江苏金山环保科技股份有限公司 | Efficient chemical oil remover |
| CN110803802A (en) * | 2019-11-21 | 2020-02-18 | 湖南俊翔科技发展有限公司 | Automatic clean system of water works |
| CN110818134A (en) * | 2019-11-21 | 2020-02-21 | 湖南俊翔科技发展有限公司 | Automatic monitoring control system of water plant |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN100366549C (en) | High-efficiency energy-saving water purification process and apparatus | |
| US20110155655A1 (en) | Modular integrated water-purifying device | |
| CN204973194U (en) | Circulation szyrt washes filter | |
| CN104193027A (en) | A gravity type integrated water purifier | |
| CN205275342U (en) | Modularization inner loop air supporting filter equipment | |
| CN207137521U (en) | A kind of sewage disposal device of precipitation and filtering integral | |
| CN206298424U (en) | Mixed liquor, sludge can automatic back flow small-sized integrated sewage-treatment plant | |
| CN2585852Y (en) | Fully automatic integrated water purifier | |
| CN206368078U (en) | A kind of coal yard wastewater recycling system with oil interceptor | |
| CN205475587U (en) | Regional burst rainwater reposition of redundant personnel processing system based on reposition of redundant personnel tubulation net | |
| CN204469383U (en) | The full-automatic self-cleaning wetting system of Non-energy-consumption | |
| CN104973711A (en) | Sewage impurity separation method | |
| CN106630249A (en) | Automatic tunnel wastewater treatment system | |
| CN207277526U (en) | A kind of rainwater depth-type filtration pond of modularization assembling and filtration apparatus | |
| CN205935044U (en) | Modular roof rainwater automatic collection purifies collection and holds system | |
| CN201981585U (en) | Integrated water saving device | |
| CN2482550Y (en) | Automatic water purifier | |
| CN106049621B (en) | A kind of multilayer public building water saving system of toilet | |
| CN201347579Y (en) | Novel reinforced concrete screen well | |
| CN2551641Y (en) | Fully-automatic water purifier | |
| CN210736421U (en) | Integrated advanced treatment device for small and medium-scale domestic sewage in villages and small towns | |
| CN212026534U (en) | Surface water recycling system | |
| CN209161774U (en) | The pond assembled A/O and assembled sewage disposal system | |
| CN202146674U (en) | Cheek type filter | |
| CN208394886U (en) | Automate country sewage integrated equipment for wastewater treatment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C53 | Correction of patent for invention or patent application | ||
| C56 | Change in the name or address of the patentee | ||
| CB03 | Change of inventor or designer information |
Designer after: Zhou Jian Designer after: Yang Qingshan Designer after: Chen Yuetang Designer after: Tan Jianjun Designer after: Liu Ying Designer before: Zhou Jian Designer before: Yang Qingshan Designer before: Tan Jianjun Designer before: Liu Ying |
|
| COR | Change of bibliographic data |
Free format text: CORRECT: DESIGNER; FROM: ZHOU JIAN YANG QINGSHAN TAN JIANJUN LIU YING TO: ZHOU JIAN YANG QINGSHAN CHEN YUETANG TAN JIANJUN LIU YING |
|
| CP03 | Change of name, title or address |
Address after: 410011 No. 140 Renmin Middle Road, Hunan, Changsha Co-patentee after: Yang Qingshan Patentee after: Zhou Jian Co-patentee after: Chen Yuetang Co-patentee after: Tan Jianjun Address before: 410011 No. 140 Renmin Middle Road, Hunan, Changsha Co-patentee before: Yang Qingshan Patentee before: Zhou Jian Co-patentee before: Tan Jianjun |
|
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |