CN204958550U - High -efficient oil removal breakdown of emulsion subsider - Google Patents
High -efficient oil removal breakdown of emulsion subsider Download PDFInfo
- Publication number
- CN204958550U CN204958550U CN201520439676.0U CN201520439676U CN204958550U CN 204958550 U CN204958550 U CN 204958550U CN 201520439676 U CN201520439676 U CN 201520439676U CN 204958550 U CN204958550 U CN 204958550U
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- cell body
- oil
- emulsion
- breakdown
- combustion chamber
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- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The utility model discloses a high -efficient oil removal breakdown of emulsion subsider, including the cell body, cell body left side bottom is equipped with the combustion chamber hopper, and the combustion chamber hopper top is equipped with fore -and -aft baffle, and the baffle left side sets up the collection oil pipe who has the horn mouth, and the flocculating reaction plate framework is installed in the position of combustion chamber hopper top to the baffle right lateral position, and the intussuseption of flocculating reaction plate framework is filled with the flocculating reaction board, the cell body top that is located flocculating reaction plate framework right side is provided with an album oiled -plate method, and collection oiled -plate method right side is connected with the oil trap, the cell body upper right side is provided with out the basin, the cell body outside is provided with water inlet, delivery port, row's sediment drain and oil -out. The utility model discloses compact structure, oil removal and breakdown of emulsion close as an organic wholely, have reduced area, because the inside flocculating reaction board that sets up need not to adopt the driving system stirring.
Description
Technical field
The utility model belongs to and relates to oily(waste)water abatement equipment technical field, specifically a kind of for the oil removal breaking device in oily(waste)water improvement.
Background technology
Oil removal emulsion breaking principle is by means of buoyancy of water, to make in water not solvent pollutent emerge, then with the water treatment method that machinery is struck off.
Oil removal breakdown of emulsion is strong and weak according to material dispersed wetting ability and density size, and the different treatment mechanism produced therefrom, and buoyancy method can be divided into: naturally floating upper method, air bubble buoyancy method and medicament flotation process three class.
It is 1, naturally floating that above method---the slightly material dispersed strong-hydrophobicity material being proportion and being less than l in-water, can rely on buoyancy of water to make it spontaneously float to the water surface.Be mainly used in the floated oil separating that particle diameter is greater than 50 ~ 60 μm, be thus often called oil removal.
2, air bubble buoyancy method----material dispersed be oil in water emulsion or slightly water-wet suspended substance, just need to produce fine gas bubbles in water, dispersed phase particles adhered on bubble and floats to the water surface together, be called for short air supporting.
3, medicament flotation process----material dispersed be strongly hydrophilic material, just first must add flotation reagent, the surface properties of particle is transformed into hydrophobic, and then be removed with By Bubble-floating Method, medicament flotation process that Here it is, be called for short flotation.
The technology that current oil removal breakdown of emulsion adopts is substantially all the technique adopting oil trap, air flotation pool and medicament flotation.Technique chooses the technique of oil removal, air supporting and flotation, have and choose treatment process that is single, that have selection to combine, singly from treatment process, select single technique, not that treatment effect is bad, be exactly working cost high (power and medicament), need to find a kind for the treatment of effect good for this reason, and the oil removal breaking device that working cost is low.
Summary of the invention
The purpose of this utility model is exactly will solve above-mentioned deficiency and propose a kind of efficient oil removal breakdown of emulsion subsider for oiliness sewage treatment, oleaginous materials in waste water is effectively removed by this efficient oil removal breakdown of emulsion subsider, and equipment is simple, easy and simple to handle, unpowered systems.
The utility model is achieved through the following technical solutions:
A kind of efficient oil removal breakdown of emulsion subsider, include cell body, it is characterized in that: cell body left bottom is provided with combustion chamber hopper, longitudinal dividing plate is provided with above combustion chamber hopper, bell-mouthed oil header is provided with on the left of dividing plate, the position be positioned on the right side of dividing plate above combustion chamber hopper is provided with flocculation reaction plate framework, is filled with flocculation reaction plate in flocculation reaction plate framework; Be positioned at above the cell body on the right side of flocculation reaction plate framework and be provided with oil collection plate, on the right side of oil collection plate, be connected with oil trap; Cell body upper right side is provided with effluent trough; Described cell body outer setting has water-in, water outlet, deslagging drain and oil outlet.
A kind of efficient oil removal breakdown of emulsion subsider, is characterized in that: be provided with brace rod bottom described cell body, is provided with diagonal brace muscle between cell body and effluent trough bottom land; Cell body ring wall is distributed with some stiffening webs.
Principle of work of the present utility model: according to the characteristic of oily(waste)water, rationally efficient oil removal breakdown of emulsion subsider is designed, first oily(waste)water flows into inlet area, add medicament in waste water simultaneously, first particle diameter in oily(waste)water is greater than 50 ~ 60 μm of oil slick removals by arranging bell-mouthed oil header, bottom arranges combustion chamber hopper, oily waste water impurities in water and large particle are removed at this, then waste water is by flocculation reaction region, at the special tectonic of conversion zone reflector, medicament and oily(waste)water fully react, waste water rises to oil collection plate, be separated the oil in waste water, a part enters oil partition tank, a part is flowed out by oil header, waste water flow to effluent trough certainly through water outlet weir plate, then discharge.The oily sludge thing centralized collection of efficient oil removal breakdown of emulsion subsider institute output, to oil collection barrel, regularly transports outward process.
Advantage of the present utility model:
The utility model compact construction, oil removal and breakdown of emulsion are integrated, and decrease floor space, due to the flocculation reaction plate that inside is arranged, stir without the need to adopting power system; Oil removing have employed hydraucone oil header and oil collection plate and oil trap facility, does not need configuration power removing equipment for oil, thus reduces construction cost and working cost.
accompanying drawing illustrates:
Fig. 1 is front view of the present utility model.
Fig. 2 is vertical view of the present utility model.
01-cell body, 02-combustion chamber hopper, 03-flocculation reaction plate, 04-with hydraucone oil header, 05-oil collection plate, 06-oil trap, 07-effluent trough, 08-brace rod, 09-diagonal brace muscle, 10-stiffening web, 11-flocculation reaction plate framework, 12-water-in, 13-water outlet, 14-deslagging drain, 15-oil outlet.
Embodiment
See accompanying drawing.
A kind of efficient oil removal breakdown of emulsion subsider, include cell body 1, cell body 1 left bottom is provided with combustion chamber hopper 2, longitudinal dividing plate is provided with above combustion chamber hopper 2, bell-mouthed oil header 4 is provided with on the left of dividing plate, the position be positioned on the right side of dividing plate above combustion chamber hopper 2 is provided with flocculation reaction plate framework 11, is filled with flocculation reaction plate 3 in flocculation reaction plate framework 11; Be positioned at above the cell body on the right side of flocculation reaction plate framework 11 and be provided with oil collection plate 5, on the right side of oil collection plate 5, be connected with oil trap 6; Cell body upper right side is provided with effluent trough 7; Described cell body 1 outer setting has water-in 12, water outlet 13, deslagging drain 14 and oil outlet 15.
Be provided with brace rod 8 bottom cell body 1, between cell body and effluent trough bottom land, be provided with diagonal brace muscle 9; Cell body ring wall is distributed with some stiffening webs 10.
The oily sludge thing produced when whole equipment runs, collects the oil collection barrel of configuration by oil outlet 15, cleaning of pledging love, and the mud of combustion chamber hopper 02 output is regularly discharged from deslagging drain 14, flows into the sewage sludge storage pond of specifying.
Claims (2)
1. an efficient oil removal breakdown of emulsion subsider, include cell body, it is characterized in that: cell body left bottom is provided with combustion chamber hopper, longitudinal dividing plate is provided with above combustion chamber hopper, bell-mouthed oil header is provided with on the left of dividing plate, the position be positioned on the right side of dividing plate above combustion chamber hopper is provided with flocculation reaction plate framework, is filled with flocculation reaction plate in flocculation reaction plate framework; Be positioned at above the cell body on the right side of flocculation reaction plate framework and be provided with oil collection plate, on the right side of oil collection plate, be connected with oil trap; Cell body upper right side is provided with effluent trough; Described cell body outer setting has water-in, water outlet, deslagging drain and oil outlet.
2. one according to claim 1 efficient oil removal breakdown of emulsion subsider, is characterized in that: be provided with brace rod bottom described cell body, is provided with diagonal brace muscle between cell body and effluent trough bottom land; Cell body ring wall is distributed with some stiffening webs.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520439676.0U CN204958550U (en) | 2015-06-24 | 2015-06-24 | High -efficient oil removal breakdown of emulsion subsider |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520439676.0U CN204958550U (en) | 2015-06-24 | 2015-06-24 | High -efficient oil removal breakdown of emulsion subsider |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204958550U true CN204958550U (en) | 2016-01-13 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520439676.0U Expired - Fee Related CN204958550U (en) | 2015-06-24 | 2015-06-24 | High -efficient oil removal breakdown of emulsion subsider |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204958550U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111825174A (en) * | 2019-04-23 | 2020-10-27 | 中国石油化工股份有限公司 | Demulsification device and method for oil-in-water emulsion |
-
2015
- 2015-06-24 CN CN201520439676.0U patent/CN204958550U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111825174A (en) * | 2019-04-23 | 2020-10-27 | 中国石油化工股份有限公司 | Demulsification device and method for oil-in-water emulsion |
| CN111825174B (en) * | 2019-04-23 | 2022-11-04 | 中国石油化工股份有限公司 | Demulsification device and method for oil-in-water emulsion |
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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: 20160113 Termination date: 20190624 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |