CN1463928A - Water treatment clarification apparatus - Google Patents
Water treatment clarification apparatus Download PDFInfo
- Publication number
- CN1463928A CN1463928A CN 02112114 CN02112114A CN1463928A CN 1463928 A CN1463928 A CN 1463928A CN 02112114 CN02112114 CN 02112114 CN 02112114 A CN02112114 A CN 02112114A CN 1463928 A CN1463928 A CN 1463928A
- Authority
- CN
- China
- Prior art keywords
- air
- water
- dissolving
- chamber
- water treatment
- 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.)
- Pending
Links
Images
Landscapes
- Physical Water Treatments (AREA)
Abstract
The present invention is water clarifying treatment apparatus and relates to water treating apparatus to eliminate water insoluble matter, such as suspended matter and oil. The present invention consists of gravitational deposit chamber, air dissolving and air floating separation chamber, water collector and water level controller. The gravitational deposit chamber and the air dissolving and air floating separation chamber are integrated to make the present invention has compact and reasonable structure and small volume. Compared with available single gravitational deposit chamber and air dissolving and air floating separation apparatus, the present invention has higher efficiency of eliminating water insoluble matter.
Description
Technical field
A kind of water treatment clarifying plant relates to the water treatment clarification technique, especially relates to the water treatment device that is used for removing water insoluble material, as: the water treatment device of removing suspended matter and oils.
Background technology
In existing water treatment, adopt make a return journey insoluble substance in dewatering of single gravitational settling method or dissolved air flotation usually, as: suspended matter and oils.For example, the settling tank of conventional municipal sewage plant is with regard to make a return journey suspended solids in dewatering of the method that is based on gravitational settling.This class settling tank can be removed heavier suspended solids (density is much larger than the solid of 1 grams per milliliter) soon, yet, for the less and little suspended solids of density or oils (density less than or approach the insoluble substance of 1 grams per milliliter), just be difficult to maybe can not remove with settling tank.As everyone knows, contain usually in water and the waste water the different insoluble substance of density (from less than 1 grams per milliliter to greater than 1 grams per milliliter).Because the bigger insoluble substance of density can at first sedimentation in settling tank, the just more and more difficult sedimentation of remaining insoluble substance, the speed that the total insoluble substance of water treatment is removed can be in time more and more lower, therefore, single intermediate processing is only adopted in water treatment, it is only effective to removing heavier insoluble substance, and can not effectively remove all insoluble substances, especially the less insoluble substance of those density.
Adopt the insoluble substance in the dissolved air flotation removal water, this method needs the high density dissolved air water is imported in institute's water to be processed continuously, enters the dissolved air flotation pond after mixing.Because the gas in the high density dissolved air water can discharge gradually with the form of microbubble after decompression, these microbubbles can be attached on the surface of insoluble substance (suspended solids and elaioleucite), make the insoluble substance come-up and are retained in the surface of dissolved air flotation pool inner water.The air supporting mud of having assembled (being scum silica frost) is removed by overflow or with slag scraper usually, thereby makes water to be processed obtain clarification.Dissolved air flotation can be removed less suspended solids and the oils of density in the water well.Yet, owing to contain the insoluble substance of different densities in the water, even the bigger suspended solids of some density can not float under the help of micro bubble, but can be with sink to the pond than original slower speed at the bottom of; Some was easy to the material removed through free setting originally, became on the contrary under the effect of micro bubble and can not precipitate and can not float, and therefore can be retained in the water outlet.That is to say that dissolved air flotation has hindered the removal of the bigger insoluble substance of density.Therefore, water treatment adopts single dissolved-air air-float method can not remove all insoluble substances effectively, the bigger insoluble substance of those density especially, and it can only effectively remove less suspended solids of density and oils.
Summary of the invention
Usually contain the different insoluble substance of multiple density in water and the waste water, in the ideal case, the solid that density is big needs to remove with the precipitator method, and less suspended solids and the oils of density needs remove with dissolved air flotation.Yet, in existing engineering practice, only adopt single method usually, or adopt the insoluble substance in gravitational settling method or the employing dissolved air flotation removal water.In order to overcome the deficiency of existing treatment process to the water that contains suspended solids and oils, the present invention proposes and a kind ofly gravitational settling is removed in the water insoluble substance and air-dissolving air-float remove that insoluble substance organically combines in the water, make full use of precipitation and pneumatically supported effect, with more effective and remove the suspended solids in the water and the water treatment clarifying plant of oils apace.
The present invention is by a gravity settling chamber that is used to remove the bigger suspended solids of density, an air-dissolving air-float separate chamber that is used to remove less suspended solids of density and/or oils, and and air-dissolving apparatus, captation and water-level control apparatus constitute together.Water inlet pipe is located at gravity settling chamber's sidepiece, and the water-in of water inlet pipe can be located at an indoor middle part of gravitational settling or a side.At the indoor snubber assembly that is provided with of gravitational settling, passed through aquaporin between gravity settling chamber and the air-dissolving air-float separate chamber and be communicated with, cross and in the aquaporin mixing apparatus can be set or directly will cross aquaporin and make and promote gas, the mixed structure of water.Captation is communicated with air-dissolving apparatus and water-level control apparatus respectively by pipe connecting; The water-in of air-dissolving apparatus is communicated with captation, and from captation water inlet, the water outlet of air-dissolving apparatus is communicated with the aquaporin of crossing between gravity settling chamber and the air-dissolving air-float separate chamber by pipe connecting, to aquaporin water outlet excessively.In water treatment procedure, the water that contains suspended solids and/or oils at first enters the settling chamber, through reducing the turbulent fluctuation degree of water inlet behind the snubber assembly, makes the bigger solid of density sink at the bottom of the pond in a short period of time rapidly and is excluded.In the top tiltable of the indoor water-in of gravitational settling or flow deflector or thrust-augmenting nozzle vertically are set, the turbulent fluctuation degree with further reduction water inlet improves removal effect.The high density dissolved air water that is produced by air-dissolving apparatus imports crossing in the aquaporin between connection gravity settling chamber and the air-dissolving air-float separate chamber, contact, mix with the water that contains less suspended solids of density and/or oils after the process precipitation process, enter the gas-floating chamber separation then and carry out solid-liquid separation.Gas in dissolved air water form with microbubble after being decompressed to normal pressure discharges, these microbubbles are attached on the surface of suspended solids and olesome, make suspended solids and oils the come-up or stably rest on the water surface of gas-floating chamber, form air supporting sludge blanket (scum silica frost), after being accumulated to a certain degree, these air supporting mud are discharged automatically or are struck off by the mechanical curettage device via the scum silica frost outlet.Be provided with in water-level control apparatus and regulate weir plate and rising pipe, be used to control the indoor water level of dissolved air flotation, treated water is collected after water-level control apparatus is discharged from rising pipe via captation.
If in water treatment procedure, need add chemical agent such as coagulating agent and/or flocculation agent, on the water inlet pipe of apparatus of the present invention, a motionless mixer can be installed, chemical agent filling at the front end of motionless mixer so that mixed fully at the mixer place with water, entering device of the present invention then clarifies, in this case, the gravity settling chamber has the function of flocculating chamber simultaneously concurrently, can further improve the effect of water treatment.
Characteristics of the present invention are: the water treatment clarifying plant is by the gravity settling chamber of removing the big suspended solids of density and remove the little suspended solids of density and/or the air flotation separating chamber organic combination of oils is integral, and and air-dissolving apparatus, captation, water-level control apparatus constitutes together, its compact construction, rationally, volume is little, it not only given full play to gravitational settling and air-dissolving air-float water treatment effect and can replenish mutually, therefore, water treatment device of the present invention carries out water treatment than single gravitational settling method of existing employing or dissolved-air air-float method, can more effectively remove the insoluble material in the water.Because air flotation separating chamber of the present invention only is used for less suspended solids of partition density and/or oils, solid therefore needed gas/lower than understanding, thus reduced the energy consumption that is used to make the high density dissolved air water.In device of the present invention, heavy solid can be removed rapidly in the gravity settling chamber, and simultaneously light solid and/or oils can be removed rapidly in gas-floating chamber, and therefore total treatment time of water is less than traditional settling tank or air flotation pool, and water treatment is effective.
Description of drawings
Accompanying drawing is two kinds of embodiment synoptic diagram in the embodiment of the invention, and it does not limit enforcement of the present invention, wherein:
Fig. 1. be that a kind of water inlet of the present invention is located at the structural representation in the device,
Fig. 2. be that a kind of water inlet of the present invention is located at device one side and is provided with the structural representation of slag scraper,
Fig. 3. be the structural representation that the present invention adopts another rainwater catchment.
Embodiment
According to above-mentioned accompanying drawing, the present invention is further illustrated: the present invention is integral by gravity settling chamber 13, air-dissolving air-float separate chamber 17 organic combinations, and air-dissolving air-float separate chamber 17 is positioned at the top of gravity settling chamber 13, is equipped with sludge outlet 1 at its top.Water inlet pipe 14 is located at a side of gravity settling chamber 13, its water-in is located at middle part in the gravity settling chamber 13, be fixedly equipped with snubber assembly 12 in the water inlet of water inlet pipe 14, water inlet is run into behind the snubber assembly 12 can reduce the turbulent fluctuation degree, makes density is bigger in the water solid sink at the bottom of the device in a short period of time rapidly and is excluded.The top tiltable of the water-in in gravity settling chamber 13 or flow deflector 9 vertically is set, the turbulent fluctuation degree with further reduction water inlet improves removal effect.The bottom of gravity settling chamber 13 is a bucket 11, and bucket 11 is connected with mud discharging pipe 10, handles the heavy solid that is deposited in the device bottom bucket 11 through gravitational settling and discharges from mud discharging pipe 10.Captation 8 is arranged on the bottom in the air-dissolving air-float separate chamber 17, be communicated with water-level control apparatus 4 by pipe connecting 5 or water exit 5 by pipe connecting air-dissolving apparatus 15 connected sums outer respectively with being located at clarifying plant, in water-level control apparatus 4, be provided with and regulate weir plate 2 and rising pipe 3, regulate weir plate 2 in order to regulate the water level in the air-dissolving air-float separate chamber 17.Gravity settling chamber 13 was provided with water channel 7 with 17 of air-dissolving air-float separate chambers is communicated with them.Cross mixing apparatus 6 is set in the water channel 7.One end of pipe connecting 16 is communicated with air-dissolving apparatus 15, and the other end is communicated with the bottom of crossing water channel 7.Water in the air-dissolving air-float separate chamber 17 is collected by captation 8, behind air-dissolving apparatus 15, become the high pressure dissolved air water, entering in the water channel 7 water after handling through gravitational settling through pipe connecting 16 is blended into mixed liquid by mixing apparatus 6 and enters and carry out dissolved air flotation in the air-dissolving air-float separate chamber 17, dissolved gas after reducing pressure in the dissolved air water discharges and is attached on the surface of suspended solids and olesome with the form of microbubble under normal pressure, make suspended solids and oils the come-up or stably rest on the water surface of air-dissolving air-float separate chamber 17, form one deck sludge blanket, after waiting to be accumulated to a certain degree, these air supporting mud are discharged automatically via scum silica frost outlet 1 or are scraped into scum silica frost outlet 1 removal by removing device 18, treated water then by captation 8 through pipe connecting 5 to water-level control apparatus 4, discharge through rising pipe 3 then.
Claims (7)
1. water treatment clarifying plant, it is characterized in that: clarifying plant is made of gravity settling chamber (13), air-dissolving air-float separate chamber (17), air-dissolving apparatus (15), captation (8), water-level control apparatus (4), air-dissolving air-float separate chamber (17) is positioned at the top of gravity settling chamber (13), and organic combination is integral, and is equipped with sludge outlet (1) at its top; Water inlet pipe (14) is located at a side of gravity settling chamber (13), and its water-in can be located at an indoor middle part of gravitational settling or a side, and the bottom of gravity settling chamber (13) is bucket (11), and bucket (11) is connected with mud discharging pipe (10); Be provided with aquaporin (7) between gravity settling chamber (13) and air-dissolving air-float separate chamber (17); Captation (8) is arranged on the bottom in the air-dissolving air-float separate chamber (17), be communicated with air-dissolving apparatus (15) by pipe connecting with water-level control apparatus (4) connected sum by pipe connecting (5) respectively, air-dissolving apparatus (15) is communicated with the Lower Half of crossing aquaporin (7) by pipe connecting (16).
2. water treatment clarifying plant according to claim 1 is characterized in that: the water inlet of water inlet pipe (14) is provided with snubber assembly (12) in gravity settling chamber (13).
3. water treatment clarifying plant according to claim 1 is characterized in that: tilt in gravity settling chamber (13) or flow deflector or thrust-augmenting nozzle (9) vertically are set.
4. water treatment clarifying plant according to claim 1 is characterized in that: contain the mud removing device (18) that strikes off the interior mud scum in air-dissolving air-float separate chamber (17).
5. water treatment clarifying plant according to claim 1 is characterized in that: mixed device (6) is being set or will making the structure that promotes that gas, water mix at mistake aquaporin (7) in the aquaporin (7) excessively.
6. water treatment clarifying plant according to claim 1 is characterized in that: be provided with the rising pipe (3) of regulating weir plate (2) in the water-level control apparatus (4).
7. water treatment clarifying plant according to claim 1 is characterized in that: on water inlet pipe (14) static mixing apparatus can be set.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 02112114 CN1463928A (en) | 2002-06-18 | 2002-06-18 | Water treatment clarification apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 02112114 CN1463928A (en) | 2002-06-18 | 2002-06-18 | Water treatment clarification apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN1463928A true CN1463928A (en) | 2003-12-31 |
Family
ID=29742044
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 02112114 Pending CN1463928A (en) | 2002-06-18 | 2002-06-18 | Water treatment clarification apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1463928A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101195499B (en) * | 2006-12-08 | 2011-08-10 | 深圳市清泉水业股份有限公司 | Automatic equalization method and structure of water load of upward flow water filtering pool |
| CN102198993A (en) * | 2011-04-29 | 2011-09-28 | 周先锋 | Diffuser board |
| CN104291497A (en) * | 2014-11-03 | 2015-01-21 | 山东建筑大学 | Copolymerization pond integrating functions of air flotation and clarification |
| CN107445327A (en) * | 2016-05-30 | 2017-12-08 | 上海京明环境科技有限公司 | A kind of integrated apparatus and method of waterpower collaboration flotation processing sewage |
-
2002
- 2002-06-18 CN CN 02112114 patent/CN1463928A/en active Pending
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101195499B (en) * | 2006-12-08 | 2011-08-10 | 深圳市清泉水业股份有限公司 | Automatic equalization method and structure of water load of upward flow water filtering pool |
| CN102198993A (en) * | 2011-04-29 | 2011-09-28 | 周先锋 | Diffuser board |
| CN104291497A (en) * | 2014-11-03 | 2015-01-21 | 山东建筑大学 | Copolymerization pond integrating functions of air flotation and clarification |
| CN104291497B (en) * | 2014-11-03 | 2015-12-02 | 山东建筑大学 | A kind of copolymerizing and air-float settling pond |
| CN107445327A (en) * | 2016-05-30 | 2017-12-08 | 上海京明环境科技有限公司 | A kind of integrated apparatus and method of waterpower collaboration flotation processing sewage |
| CN107445327B (en) * | 2016-05-30 | 2020-11-17 | 上海京明环境科技有限公司 | Integrated device and method for treating sewage through hydraulic collaborative flotation |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205774033U (en) | A kind of compound efficient depositing reservoir | |
| CN202529925U (en) | Air-flotation filtering integrated processing device | |
| CN107337263B (en) | Vertical flow type coagulating sedimentation and air flotation dual-purpose tank | |
| CN106904680A (en) | A kind of air floatation machine | |
| CN201334406Y (en) | Integrated water treatment device for surface water and sewage treatment | |
| CN208250006U (en) | A kind of high efficient aeration sedimentation integrated device | |
| CN209853876U (en) | Integrated grease separation water purifier | |
| CN2786096Y (en) | Dissolved-air floatation unit | |
| CN109293079B (en) | Low-energy-consumption aeration circulation clarification tank | |
| CN1463928A (en) | Water treatment clarification apparatus | |
| CN115608009A (en) | Assembled secondary sedimentation tank and sewage treatment equipment | |
| JP2000185279A (en) | Sewage treatment method and apparatus | |
| CN2194357Y (en) | Waste water comprehensive purifying treatment equipment | |
| JP2000354858A (en) | Sewage treatment method and device therefor | |
| CN1312226A (en) | Counter-current air floating water-treating method and apparatus | |
| KR20020068311A (en) | Apparatus for clarifying water and wastewater | |
| CN205999234U (en) | Sludge in sewage effectively can be carried out the sewage disposal system of precipitation and separation | |
| CN220034257U (en) | Device for separating sediment from sewage | |
| CN109354234A (en) | A kind of method and its construction substituting biochemical method sewage treatment secondary settling tank | |
| CN204981223U (en) | Novel cavitation air supporting machine | |
| CN212799721U (en) | Air floatation device | |
| CN2410286Y (en) | Waste water treater by jet-flow air floation | |
| CN2437664Y (en) | Airfloat sewage treating apparatus | |
| JP2766881B2 (en) | Water treatment equipment | |
| CN219929709U (en) | Separating device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C12 | Rejection of a patent application after its publication | ||
| RJ01 | Rejection of invention patent application after publication |