CN204779170U - Remove look water purification unit - Google Patents
Remove look water purification unit Download PDFInfo
- Publication number
- CN204779170U CN204779170U CN201520461957.6U CN201520461957U CN204779170U CN 204779170 U CN204779170 U CN 204779170U CN 201520461957 U CN201520461957 U CN 201520461957U CN 204779170 U CN204779170 U CN 204779170U
- Authority
- CN
- China
- Prior art keywords
- water
- basin
- settling tank
- flocculation
- purifying plant
- 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.)
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 79
- 238000000746 purification Methods 0.000 title abstract description 4
- 238000005189 flocculation Methods 0.000 claims abstract description 37
- 230000016615 flocculation Effects 0.000 claims abstract description 37
- 238000001914 filtration Methods 0.000 claims abstract description 26
- 239000006004 Quartz sand Substances 0.000 claims abstract description 18
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 18
- 239000000463 material Substances 0.000 claims abstract description 10
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 6
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 6
- AZDRQVAHHNSJOQ-UHFFFAOYSA-N alumane Chemical class [AlH3] AZDRQVAHHNSJOQ-UHFFFAOYSA-N 0.000 claims description 5
- 230000000630 rising effect Effects 0.000 claims description 5
- 238000004891 communication Methods 0.000 claims description 4
- 238000002386 leaching Methods 0.000 claims description 4
- 239000007788 liquid Substances 0.000 claims description 4
- 230000001427 coherent effect Effects 0.000 claims description 3
- 230000001105 regulatory effect Effects 0.000 claims description 2
- 230000000694 effects Effects 0.000 abstract description 6
- 239000008394 flocculating agent Substances 0.000 abstract 4
- 238000004062 sedimentation Methods 0.000 abstract 4
- 159000000013 aluminium salts Chemical class 0.000 abstract 2
- 229910000329 aluminium sulfate Inorganic materials 0.000 abstract 2
- 230000002776 aggregation Effects 0.000 abstract 1
- 238000004220 aggregation Methods 0.000 abstract 1
- 238000002347 injection Methods 0.000 abstract 1
- 239000007924 injection Substances 0.000 abstract 1
- 238000000034 method Methods 0.000 description 7
- 238000002156 mixing Methods 0.000 description 7
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 description 6
- 238000001179 sorption measurement Methods 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 3
- 239000002352 surface water Substances 0.000 description 3
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000011010 flushing procedure Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000013618 particulate matter Substances 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 230000000717 retained effect Effects 0.000 description 2
- 238000011001 backwashing Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 230000003311 flocculating effect Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Water Treatment By Sorption (AREA)
Abstract
The utility model relates to a remove look water purification unit, remove look water purification unit includes flocculation basin, sedimentation tank and filtering ponds, the flocculation basin is connected with the pipeline that entries, the flocculation basin is equipped with the flocculation well that the several is linked together, the pipe chute is installed to the sedimentation tank, the quartz sand filter material is equipped with in the filtering ponds, it installs line mixer on the pipeline to entry, the last flocculating agent that is equipped with of line mixer is thrown with the mouth, and aluminium salt flocculating agent passes through the flocculating agent is thrown and is added a mouthful injection line mixer, be located the sedimentation tank middle part the pipe chute upside is equipped with the water catch bowl, the water catch bowl with be located the bypass channel of filtering ponds is linked together through the opening that is located the pool wall top, bypass channel is located quartz sand filter material top, quartz sand filter material downside is equipped with the active carbon filter material. The cooperation of aluminium salt flocculating agent and active carbon is used, guarantees higherly except that the look effect. Aggregation is played to the filth of deposit in the bottom in the V -arrangement groove of sedimentation tank bottom, and the blowdown is thorough, guarantees quality of water.
Description
Technical field
The utility model relates to water purifying plant, particularly relates to a kind of except look water purifying plant.
Background technology
Surface water can cause it to occur a kind of colourity due to decomposed leaves.Usually the method adopted this surface water with certain colourity carries out ion remaval method by magnetic resin.But for the surface water of this colourity, the water just after magnetic resin ion remaval is up to standard, places colourity after 12 hours and increase, more than more than 50 degree.After water after process places for some time, water quality is not up to standard.
Utility model CN201962154U discloses a kind of efficient adsorption integrative water purifying device, comprises flocculating chamber, settling chamber, filtration chamber, adsorption chamber four formants, has except look, the function that eliminates the unusual smell.Reservoir water and urban river water all can reach sanitary standard for drinking water after this device processes.But this efficient adsorption integrative water purifying device complex structure, only adopt gac, adsorption effect is undesirable.
Utility model content
Technical problem to be solved in the utility model is to provide a kind of high to earth's surface purificating raw water degree, except chromatic effect is good, compact construction except look water purifying plant.
For solving the problems of the technologies described above, the technical solution of the utility model is: a kind of except look water purifying plant, comprise flocculation basin, settling tank and filtering basin, described flocculation basin, settling tank and filtering basin are connected by the opening be positioned on pool wall successively, described flocculation basin is connected with water inlet pipe, described flocculation basin is provided with several flocculation well be connected, described settling tank is provided with inclined tube, described filtering basin are built with quartz sand filter media, it is characterized in that: described water inlet pipe is provided with line mixer, described line mixer is provided with flocculant concentration mouth, aluminum salt flocculant injects described line mixer by described flocculant concentration mouth, distribution reservoir is provided with between described flocculation basin and settling tank, water leg is provided with on the upside of the inclined tube being positioned at described settling tank middle part, described water leg and be positioned at the bypass channel of described filtering basin by being positioned at the opening in communication above pool wall, described bypass channel is positioned at above described quartz sand filter media, is provided with carbon leaching material on the downside of described quartz sand filter media.
As preferred technical scheme, described flocculation basin is provided with nine flocculation wells.
As preferred technical scheme, described flocculation basin, distribution reservoir, settling tank and filtering basin are equipped with blow-off pipe, and described blow-off pipe is provided with wash water valve.
As preferred technical scheme, bottom described settling tank, be provided with several coherent V-shaped groove.
As preferred technical scheme, described blow-off pipe position is corresponding with the bottom position of described V-shaped groove.
As preferred technical scheme, described rising pipe is provided with out water regulating valve.
As preferred technical scheme, described filtering basin are provided with liquidometer.
As preferred technical scheme, described liquid level counts ultrasonic level gage.
Owing to have employed technique scheme, aluminum salt flocculant and gac with the use of, eliminate the peculiar smell of water, particulate matter etc., adsorb chromatogenous material, ensure that the effect except look.Flocculation basin is divided into nine flocculation wells, and eddy flow is effective, and reaction thoroughly.The use of liquidometer ensure that the accurate operation of water purifying plant, ensures water quality.V-shaped groove bottom settling tank plays congregation to the dirt being deposited on bottom, and blowdown is thorough.Settling tank top is provided with water leg, stationary flow, and particle-removing thing is effective.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model embodiment;
Fig. 2 is the vertical view of Fig. 1.
Embodiment
As depicted in figs. 1 and 2, a kind of except look water purifying plant, comprise flocculation basin 4, distribution reservoir 5, settling tank 6 and filtering basin 11.Described flocculation basin 3, distribution reservoir 5, settling tank 6 and filtering basin 11 are successively by being positioned at the opening in communication on adjacent wall.Described flocculation basin is connected with water inlet pipe 1, and described water inlet pipe 1 is provided with line mixer 3, and described line mixer 3 is provided with flocculant concentration mouth 2, and aluminum salt flocculant injects described line mixer 3 by described flocculant concentration mouth 2.Described flocculation basin 4 is provided with several flocculation well be connected.Described settling tank 6 is provided with inclined tube 8, is provided with water leg 7 on the upside of described inclined tube 8.Described water leg 7 and bypass channel 9 are by being positioned at the opening in communication on described settling tank 6 and filtering basin 11 adjacent wall, described filtering basin 11 are built with quartz sand filter media 12, described bypass channel 9 is positioned at the top of described quartz sand filter media 12, and the downside of described quartz sand filter media 12 is provided with carbon leaching material 13.
Its implementation process is as follows:
1) former water enters line mixer 3 through water inlet pipe 1, adds flocculant of polymeric aluminium chloride at the flocculant concentration mouth 2 of line mixer 3.Flocculant of polymeric aluminium chloride fully mixes through line mixer 3 with former water, enters flocculation basin 4.
2) described flocculation basin 4 is provided with nine flocculation wells, the eddy flow of mixing water in flocculation basin 4 is effective, mixing is abundant, the material causing colourity to produce in flocculant of polymeric aluminium chloride and former water fully reacts, form alumen ustum, along with the carrying out of reaction, alumen ustum can be increasing, can form large alumen ustum below, then enter distribution reservoir 5 at flocculation basin 4.
3) mixing water after flocculation basin completes uniformly distributing in distribution reservoir 5, makes current uniform flow on the water inlet direction of settling tank 6.The mixing water of distributed uniform flows into settling tank 6.
4) mixing water after distribution reservoir 5 carries out uniformly distributing enters settling tank 6 by the bottom of settling tank 6.Mixing water is from bottom to top through inclined tube 8, the flowing of mixing water in inclined tube 8 is more stable, and some macrobead alumen ustum toward declining, can be gathered in the bottom of settling tank 6, the bottom of described settling tank 6 is provided with several coherent V-shaped groove, is provided with blow-off pipe 15 with the bottom position corresponding section of described V-shaped groove.Described V-shaped groove plays congregation to alumina blossom particles thing, and blow-off pipe 15 position is corresponding to the position of the bottom of described V-shaped groove, ensures that blowdown is more thorough.Clear water can be gathered in the top of settling tank, is catchmented by water leg 7, enters filtering basin 11.Water leg 7 plays the effect of current stabilization, and near water leg 7, alumina blossom particles can be stopped and precipitate to greatest extent.
5) water in water leg 7 is communicated with the bypass channel 9 in filtering basin 11 by the opening above pool wall.By point water effect of described bypass channel 9, on the quartz sand filter media 12 that being distributed to of uniform fluid flow is positioned at below described bypass channel 9.Some little flcos cannot removed by precipitation are removed after quartz sand filter media 12 filters.In order to improve water quality further, the water after filtering adsorbs through carbon leaching material 13 again, can remove some heavy metal ion in water simultaneously, eliminate the unusual smell.Water after having purified connects Outer Tube through rising pipe 14, and the water after purification can meet routine use.
After filtering basin 11 run for some time, quartz sand filter media 12 inside filter tank has retained the dirt in water, along with the dirt retained gets more and more, the filtration capacity of quartz sand filter media 12 declines, the liquid level in filter tank is caused to rise, when filter tank liquid level rises to certain altitude, liquidometer can trigger automatic control program, automatically carries out back flushing to quartz sand filter media.Back flushing is from clean water basin water intaking, completes water supply by backwashing pump.Oppositely intake by the rising pipe 14 in filter tank 11, rinse bottom filter tank 11 to quartz sand filter media, sewage is discharged by blow-off pipe 15.
Owing to have employed technique scheme, aluminum salt flocculant and gac with the use of, eliminate the peculiar smell of water, particulate matter etc., ensure higher colourity.Flocculation basin is divided into nine flocculation wells, and eddy flow is effective, and reaction thoroughly.The use of liquidometer ensure that the accurate operation of water purifying plant, ensures water quality.V-shaped groove bottom settling tank plays congregation to the dirt being deposited on bottom, and blowdown is thorough.Settling tank top is provided with water leg, stationary flow, and particle-removing thing is effective.
More than show and describe ultimate principle of the present utility model, principal character and advantage of the present utility model.The technician of the industry should understand; the utility model is not restricted to the described embodiments; what describe in above-described embodiment and specification sheets just illustrates principle of the present utility model; under the prerequisite not departing from the utility model spirit and scope; the utility model also has various changes and modifications, and these changes and improvements all fall within the scope of claimed the utility model.The claimed scope of the utility model is defined by appending claims and equivalent thereof.
Claims (8)
1. one kind is removed look water purifying plant, comprise flocculation basin, settling tank and filtering basin, described flocculation basin, settling tank and filtering basin are connected by the opening be positioned on adjacent pool wall successively, described flocculation basin is connected with water inlet pipe, described flocculation basin is provided with several flocculation well be connected, described settling tank is provided with inclined tube, described filtering basin are built with quartz sand filter media, it is characterized in that: described water inlet pipe is provided with line mixer, described line mixer is provided with flocculant concentration mouth, and aluminum salt flocculant injects described line mixer by described flocculant concentration mouth; Distribution reservoir is provided with between described flocculation basin and settling tank; Water leg is provided with on the upside of the inclined tube being positioned at described settling tank middle part; Described water leg and be positioned at the bypass channel of described filtering basin by being positioned at the opening in communication above pool wall; Described bypass channel is positioned at above described quartz sand filter media, is provided with carbon leaching material on the downside of described quartz sand filter media.
2. as claimed in claim 1 a kind of except look water purifying plant, it is characterized in that: described flocculation basin is provided with nine flocculation wells.
3. as claimed in claim 1 a kind of except look water purifying plant, it is characterized in that: described flocculation basin, distribution reservoir, settling tank and filtering basin are equipped with blow-off pipe, described blow-off pipe is provided with wash water valve.
4. as claimed in claim 3 a kind of except look water purifying plant, it is characterized in that: the bottom of described settling tank is provided with several coherent V-shaped groove.
5. as claimed in claim 4 a kind of except look water purifying plant, it is characterized in that: described blow-off pipe position is corresponding with the bottom position of described V-shaped groove.
6. as claimed in claim 1 a kind of except look water purifying plant, it is characterized in that: described filtering basin are connected with rising pipe, described rising pipe is provided with out water regulating valve.
7. as claimed in claim 1 a kind of except look water purifying plant, it is characterized in that: described filtering basin are provided with liquidometer.
8. as claimed in claim 7 a kind of except look water purifying plant, it is characterized in that: described liquid level counts ultrasonic level gage.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520461957.6U CN204779170U (en) | 2015-07-01 | 2015-07-01 | Remove look water purification unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520461957.6U CN204779170U (en) | 2015-07-01 | 2015-07-01 | Remove look water purification unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204779170U true CN204779170U (en) | 2015-11-18 |
Family
ID=54519262
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520461957.6U Active CN204779170U (en) | 2015-07-01 | 2015-07-01 | Remove look water purification unit |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204779170U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105384282A (en) * | 2015-12-14 | 2016-03-09 | 山东华通环境科技股份有限公司 | Modularized water purifier, manufacturing method of modularized water purifier and fast sludge discharge method |
| CN105540920A (en) * | 2015-12-18 | 2016-05-04 | 新昌中法供水有限公司 | Conventional water treatment strengthening filtering process |
| CN105565540A (en) * | 2015-12-14 | 2016-05-11 | 山东华通环境科技股份有限公司 | Modular water purification device with settling, sludge discharging and back flushing functions and quick sludge discharging method |
| CN110156204A (en) * | 2019-04-24 | 2019-08-23 | 昆明理工大学 | A kind of integrated water power waste water recycling processing unit |
-
2015
- 2015-07-01 CN CN201520461957.6U patent/CN204779170U/en active Active
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105384282A (en) * | 2015-12-14 | 2016-03-09 | 山东华通环境科技股份有限公司 | Modularized water purifier, manufacturing method of modularized water purifier and fast sludge discharge method |
| CN105565540A (en) * | 2015-12-14 | 2016-05-11 | 山东华通环境科技股份有限公司 | Modular water purification device with settling, sludge discharging and back flushing functions and quick sludge discharging method |
| CN105565540B (en) * | 2015-12-14 | 2019-05-07 | 山东华通环境科技股份有限公司 | Modularization purifier and quick sludge discharging method with precipitating spoil disposal counter-flush |
| CN105540920A (en) * | 2015-12-18 | 2016-05-04 | 新昌中法供水有限公司 | Conventional water treatment strengthening filtering process |
| CN110156204A (en) * | 2019-04-24 | 2019-08-23 | 昆明理工大学 | A kind of integrated water power waste water recycling processing unit |
| CN110156204B (en) * | 2019-04-24 | 2021-07-06 | 昆明理工大学 | Integrated hydrodynamic wastewater recycling treatment device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20161227 Address after: Shandong Yidu 262500 east city of Weifang province Qingzhou City, No. 4069 Patentee after: SHANDONG HOTONE ENVIRONMENT TECHNOLOGY CO., LTD. Address before: Donghai West Road 266000 Shandong city of Qingdao province No. 48, No. 6 Building 4 unit 401 Patentee before: Mao Yunming |