CN202415224U - Emulsion treatment device - Google Patents
Emulsion treatment device Download PDFInfo
- Publication number
- CN202415224U CN202415224U CN2011205791237U CN201120579123U CN202415224U CN 202415224 U CN202415224 U CN 202415224U CN 2011205791237 U CN2011205791237 U CN 2011205791237U CN 201120579123 U CN201120579123 U CN 201120579123U CN 202415224 U CN202415224 U CN 202415224U
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- chamber
- emulsion
- water
- gas
- air floatation
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Abstract
The utility model discloses an emulsion treatment device, belonging to the field of industrial sewage treatment. The emulsion treatment device mainly comprises a current stabilization chamber, an air floatation chamber, a separation chamber and a water collection chamber, and is characterized by further comprising an electrolytic oxidizer formed by multiple electrode plates, and the electrode plates are externally connected with a direct current power supply; the water collection disc at the lower end of the electrolytic oxidizer is communicated with the current stabilization chamber; the lower part of the current stabilization chamber is communicated with the air floatation chamber, the air floatation chamber is externally connected with a pressure container provided with an air compressor and a water pump; the upper part of the air floatation chamber is communicated with the separation chamber, and a mud scraping board is arranged on the upper end of the separation chamber. Homogeneous condensation and heterogeneous condensation are formed through electrolysis, and separation is carried out through the air floatation manner, impurities in the emulsion can be effectively scraped to purify the sewage, and the emulsion treatment device has the effects of large sewage treatment quantity and high impurity removal rate.
Description
Technical field
The utility model belongs to sewage treatment area, particularly industrial sewage is carried out the isolated plant of separating treatment.
Background technology
Activated sludge process or stabilizing sugar method are generally adopted in the existing WWT of China, but because concentration of wastewater is high, water quality and quantity changes greatly, particularly the content of impurity such as nitrogen, phosphorus is higher in the industrial sewage; Emulsion like the steel industry generation; Contain a large amount of MO and impurity, directly discharging causes severe environmental pollution, adopts common treatment process; Control expense is high, and processing rate is low.
Summary of the invention
The purpose of the utility model is to provide a kind of Emulsion treatment unit that is used to handle industrial sewage.
The utility model is achieved in that
The emulsion treatment unit; Mainly comprise the tank body that is used to handle emulsion sewage; Be provided with plenum chamber, gas-floating chamber, separate chamber and collecting chamber in this tank body, collecting chamber is provided with mud mouth and water outlet, it is characterized in that: also be provided with an electrolytic oxidation device of being made up of a plurality of battery lead plates; This electrolytic oxidation device lower end is provided with water-collecting tray, and this water-collecting tray is communicated with plenum chamber; The battery lead plate external direct current power supply; The plenum chamber bottom communicates with gas-floating chamber, the external pressure vessel of this gas-floating chamber, and pressure vessel connects air and water pump; Gas-floating chamber top communicates with the separate chamber, and the upper end in this separate chamber is provided with cleaning shoe, and this cleaning shoe is arranged on the rotating band by driven by motor; Separate chamber's connected set hydroecium.
After the utility model adopts said structure; In emulsion sewage, form cohesion and flocculation through electrolysis; Separate through the air supporting mode again, can effectively strike off the impurity in the emulsion, reach the purpose of purifying treatment sewage; Have the effect that sewage load is big, removal of impurity is high, be suitable for the purifying treatment of various industrial emulsion liquid sewage.
Description of drawings
Accompanying drawing is a kind of structural representation of the utility model.
In the accompanying drawing, 1 is that plenum chamber, 2 is that gas-floating chamber, 3 is that separate chamber, 4 is that collecting chamber, 5 is that mud mouth, 6 is that water outlet, 7 is that battery lead plate, 8 is that water-collecting tray, 9 is that pressure vessel, 10 is that air, 11 is that water pump, 12 is that cleaning shoe, 13 is that rotating band, 14 is a liberation port.
Embodiment
Embodiment to the utility model elaborates below in conjunction with accompanying drawing.
Shown in accompanying drawing, the utility model is a kind of device that is exclusively used in the WWT of industrial emulsion liquid, mainly comprises electrolytic oxidation device and tank body, and the electrolytic oxidation device mainly is made up of the battery lead plate 7 of a plurality of vertical arrangements, battery lead plate 7 external direct current power supplies.Emulsion sewage is through battery lead plate 7, and ionization emulsion sewage produces homogeneity coacervation and heterogeneous flocculation, and rapid aggegation of the suspended substance in the sewage and deposition are until forming suspended solid.Electrolytic oxidation device lower end is provided with a water-collecting tray 8, and the emulsion sewage after the ionization is collected by water-collecting tray 8.Be provided with plenum chamber 1, gas-floating chamber 2, separate chamber 3 and collecting chamber 4 in the said tank body, water-collecting tray 8 is communicated with plenum chamber 1.Emulsion sewage gets into plenum chamber 1 through water-collecting tray 8, and plenum chamber 1 is the consume water energy of flow effectively, improves steady flow result, and the air supporting of being convenient to postorder is handled.Plenum chamber 1 bottom communicates with gas-floating chamber 2, gas-floating chamber 2 external pressure vessels 9, and the pipe that goes out of pressure vessel 9 stretches in the gas-floating chamber 2, in gas-floating chamber 2, is provided with liberation port 14.Pressure vessel 9 connects air 10 and water pump 11 respectively, and air 10 provides high pressure gas; Water pump 11 external water sources provide high pressure water; High pressure gas and high pressure water form the high pressure air water in pressure vessel 9, inject gas-floating chamber 2 through going out pipe by liberation port 14, with the emulsion sewage thorough mixing after the flocculation, form the air supporting effect, and the flocculation piece fully contacts and rise to the sewage surface with micro-bubble.Gas-floating chamber 2 tops communicate with separate chamber 3, and the upper end in the separate chamber 3 is provided with cleaning shoe 12, and this cleaning shoe 12 is arranged on the rotating band 13, and rotating band 13 is by driven by motor; Cleaning shoe 12 was scraped on emulsion sewage surface, struck off the flocculation matter sludge.Separate chamber 3 communicates with collecting chamber 4, and collecting chamber 4 is provided with mud mouth 5 and water outlet 6; Mud mouth 5 is positioned at the rearward end of rotating band 13, and the flocculation matter sludge that strikes off is discharged by mud mouth 5; Water after the purification is discharged by water outlet 6.
For reducing water consumption, said water pump 11 connected set hydroeciums 4 utilize the water after purifying in the collecting chamber 4 to carry out recycle.
During use, emulsion sewage is at first through the electrolytic oxidation device, and ionization sewage forms aggregation.Get into gas-floating chamber 2 through plenum chamber 1 again, form the air supporting effect through the high pressure air water that injects, flocculation piece and micro-bubble evenly rise to the sewage surface; Strike off by cleaning shoe 12; Discharged by mud mouth 5 at last, the water part after the purification is by water pump 11 reuses, and another part is then discharged by water outlet 6.
Claims (3)
1. emulsion treatment unit; Mainly comprise the tank body that is used to handle emulsion sewage; Be provided with plenum chamber (1), gas-floating chamber (2), separate chamber (3) and collecting chamber (4) in this jar, collecting chamber (4) is provided with mud mouth (5) and water outlet (6), it is characterized in that: also be provided with an electrolytic oxidation device of being made up of a plurality of battery lead plates (7); This electrolytic oxidation device lower end is provided with water-collecting tray (8), and water-collecting tray (8) is communicated with plenum chamber (1); Battery lead plate (7) external direct current power supply; Plenum chamber (1) bottom communicates with gas-floating chamber (2), the external pressure vessel of this gas-floating chamber (2) (9), and pressure vessel (9) connects air (10) and water pump (11); Gas-floating chamber (2) top communicates with separate chamber (3), and the upper end in this separate chamber (3) is provided with cleaning shoe (12), and cleaning shoe (12) is arranged on the rotating band (13) by driven by motor; Separate chamber (3) connected set hydroecium (4).
2. emulsion treatment unit according to claim 1 is characterized in that: said water pump (11) connected set hydroecium (4).
3. emulsion treatment unit according to claim 1 and 2 is characterized in that: said mud mouth (5) is positioned at the rearward end of rotating band (13).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011205791237U CN202415224U (en) | 2011-12-31 | 2011-12-31 | Emulsion treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011205791237U CN202415224U (en) | 2011-12-31 | 2011-12-31 | Emulsion treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202415224U true CN202415224U (en) | 2012-09-05 |
Family
ID=46740007
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011205791237U Expired - Fee Related CN202415224U (en) | 2011-12-31 | 2011-12-31 | Emulsion treatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202415224U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104563056A (en) * | 2013-10-23 | 2015-04-29 | 宋在洪 | Removal method of marine sediments using micro-air bubbles |
| CN105217709A (en) * | 2014-06-14 | 2016-01-06 | 周春江 | A kind of heterogeneous catalytic oxidation air-floating apparatus |
| CN106335973A (en) * | 2016-11-04 | 2017-01-18 | 中海油天津化工研究设计院有限公司 | Stepped low-pressure electrochemical assisted polymer-bearing wastewater demulsification treatment process method |
-
2011
- 2011-12-31 CN CN2011205791237U patent/CN202415224U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104563056A (en) * | 2013-10-23 | 2015-04-29 | 宋在洪 | Removal method of marine sediments using micro-air bubbles |
| CN105217709A (en) * | 2014-06-14 | 2016-01-06 | 周春江 | A kind of heterogeneous catalytic oxidation air-floating apparatus |
| CN105217709B (en) * | 2014-06-14 | 2018-01-30 | 周春江 | A kind of heterogeneous catalytic oxidation air-floating apparatus |
| CN106335973A (en) * | 2016-11-04 | 2017-01-18 | 中海油天津化工研究设计院有限公司 | Stepped low-pressure electrochemical assisted polymer-bearing wastewater demulsification treatment process method |
| CN106335973B (en) * | 2016-11-04 | 2019-05-28 | 中海油天津化工研究设计院有限公司 | A kind of auxiliary demulsification processing of ladder low pressure electrochemistry contains poly- waster water process method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: SHANDONG LIAOCHENG SANYANG ENVIRONMENTAL PROTECTION INDUSTRY CO., LTD. Assignor: Li Lianqing Contract record no.: 2014370000204 Denomination of utility model: Waste emulsion treatment device Granted publication date: 20120905 License type: Exclusive License Record date: 20141224 |
|
| LICC | Enforcement, change and cancellation of record of contracts on the licence for exploitation of a patent or utility model | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120905 Termination date: 20191231 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |