CN202265435U - Oil-water separator - Google Patents
Oil-water separator Download PDFInfo
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- CN202265435U CN202265435U CN2011202457687U CN201120245768U CN202265435U CN 202265435 U CN202265435 U CN 202265435U CN 2011202457687 U CN2011202457687 U CN 2011202457687U CN 201120245768 U CN201120245768 U CN 201120245768U CN 202265435 U CN202265435 U CN 202265435U
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- oil
- water
- separation cell
- separating
- level control
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Abstract
The utility model discloses an oil-water separator, to which a cavitation air flotation technology and a special filtering material are applied. A main body of the device comprises a separating pond, wherein the head end of the separating pond is provided with a water inlet pipe for injecting oil-containing sewage; a sundry separating frame is arranged at a position close to a water inlet pipe orifice in the separating pond; the sundry separating frame is used for separating and filtering large-particle impurities in the oil-containing sewage; a cavitation air flotation aerator is arranged in the separating pond; the cavitation air flotation aerator adheres to the periphery of oil drop particles through a large quantity of superfine bubbles generated in the oil-containing sewage, so that oil drops rapidly float upwards to a liquid level; a sloping plate oil removing device for shortening the rising distance of oil slick is arranged in the separating pond; an oil collecting groove for accommodating rising oil slick is formed inside the separating pond; a drain pipe with a filter core is arranged at the tail end of the separating pond, and is connected with a liquid level control device; and the liquid level control device comprises a control valve for controlling the water yield and water delivery height of the drain pipe.
Description
Technical field:
The utility model relates to a kind of oily-water seperating equipment, particularly a kind of water-and-oil separator of using cavitation air flotation technology and special filtrate.
Background technology:
As everyone knows, existing water-and-oil separator just is employed in installs several dividing plates in square or the round pond, play grease and the isolated effect of water.There is following shortcoming in these water-and-oil separators:
At first, the separation efficiency of existing water-and-oil separator is low, and the water outlet oil-contg is still higher, generally can only reach three grades of emission standards to be<100mg/L.Secondly, what existing installation adopted is with low content of technology, just adds several roads dividing plate simply, easily by imitated.In addition, the existing installation oil extraction is cumbersome, needs the labor cleaning.
The utility model content:
In view of above-mentioned technical problem, the utility model provides a kind of water-and-oil separator of using cavitation air flotation technology and special filtrate.This device just can be realized functions such as air-breathing automatically, dissolving, release, absorption through installing a cavitation aerator additional, does not need equipment such as conventional dissolving, reflux pump, reliever.In addition, special filter core of this equipment band and automatic oil draining device can be realized automatic oil draining, save manpower, improve the efficient of oily water separation simultaneously.
The concrete technical scheme of the utility model is following:
Water-and-oil separator, this device main body comprises a separation cell, said separation cell head end is provided with the water inlet pipe that is used for injecting oily(waste)water; Near the said foreign material discrete blocks that in separation cell, is provided with the water inlet pipe mouth, this is stated the foreign material discrete blocks and is used for the large granular impurity in the separating and filtering oily(waste)water; The said cavitation air flotation aerator that in separation cell, is mounted with, this is stated the cavitation air flotation aerator and is attached on through a large amount of micro bubbles that in oily(waste)water, charge into and oil droplet is floated to liquid level around the olesome rapidly; Also be provided with swash plate oil removal plant in the said separation cell into the distance that shortens the oil slick rising; Said separation cell inside is provided with the oil trap that is used for holding the rising oil slick; Said end at separation cell is provided with the water shoot of a band filter core; Said water shoot connects a fluid level control device, this fluid level control device comprise one be used for controlling water shoot aquifer yield and freeboard level control valve.
In the such scheme, oil trap one side is provided with oil outlet pipe in the said separation cell.
In the such scheme, said level control valve is placed on the water shoot.
In the such scheme, said device also be provided with one can cover whole separation cell cover plate.
In the such scheme, saidly be provided with electric heating tube in the oil trap bottom.
In the such scheme, said separation cell the bottom be provided with a plurality of blow-down pipes.
The above technological water-and-oil separator of the application of the utility model indication, its beneficial effect is following:
1, the existing same category of device of comparing, the utility model equipment has improved the efficient of oily water separation, can make the content<10mg/L of oil in the water outlet.
2, the utility model equipment can be realized automatic oil draining.Through adjusting mouth of a river liquid level, can realize automatic oil draining, save manpower and running cost, improve the efficient of oily water separation simultaneously.
3, in order to reduce the volume of equipment, the utility model equipment adopts special swash plate oil removal plant, and this swash plate can shorten the distance that oil slick rises, thereby reduces the residence time of water and oil.
4, in order to prevent that cold district oil content in winter viscosity from increasing, mobile poor, the oil extraction difficulty, the utility model design is established electric heating tube in the oil trap bottom, so that oil extraction is smooth and easy.
5, the utility model is owing to adopt cavitation air flotation principle, shallow pond sedimentation theory and incorgruous flow point from principle and turbulent boundary layer principle; Improved the release surface that the unit pond holds; The effect of oily water separation is improved widely; Shorten retention time of sewage, reduced volume of equipment greatly, saved floor space and cost.
6, the utility model equipment work is reliable, and work-ing life is extremely long, need not add any reagent and medicine, non-secondary pollution.
7, the installation and maintenance of the utility model equipment are simple and convenient: just can use as long as connect water inlet pipe, rising pipe, need not special messenger's during-operation service, a regular oil extraction of need gets final product.
8, the utility model equipment is applicable to all oil kinds; Oil-feed concentration is unrestricted: can be widely used among the waste water treatment engineering that contains natural oil and petroleum products, tar and tar fraction, vegetable and animals oils and yolk etc., be specially adapted to the processing of catering oily(waste)water.
Description of drawings:
Further specify the utility model below in conjunction with accompanying drawing and embodiment.
Fig. 1 is the sectional structure chart of the said water-and-oil separator of the utility model.
Fig. 2 is the plan structure figure of the said water-and-oil separator of the utility model.
Embodiment:
For technique means, creation characteristic that the utility model is realized, reach purpose and be easy to understand understanding with effect, below in conjunction with concrete diagram, further set forth the utility model.
As depicted in figs. 1 and 2, the described water-and-oil separator of the utility model, this device main body comprises a separation cell 1, is provided with the water inlet pipe 2 that is used for injecting oily(waste)water at the separation cell head end; In separation cell, be provided with foreign material discrete blocks 3 near 2 mouthfuls of the water inlet pipes, this is stated foreign material discrete blocks 3 and is used for the large granular impurity in the separating and filtering oily(waste)water; In separation cell, be mounted with cavitation air flotation aerator 4, this is stated cavitation air flotation aerator 4 and is attached on through a large amount of micro bubbles that in oily(waste)water, produce and oil droplet is floated to liquid level around the olesome rapidly.
Also be provided with swash plate oil removal plant 5 in the separation cell 1 into the distance that shortens the oil slick rising; Be close in the not far separation cell of swash plate oil removal plant 5 and be provided with the oil trap 6 that is used for holding the rising oil slick, this oil trap one side is provided with oil outlet pipe 7, and the oil trap bottom is provided with electric heating tube 8.
Be provided with the water shoot 9 of a band filter core 10 at the end of separation cell 1, this water shoot 9 connects a fluid level control device 11, this fluid level control device 11 comprise one be used for controlling the water shoot aquifer yield level control valve 12, this level control valve 12 is placed on the water shoot 9.
Need particularly point out be the water-and-oil separator of the utility model also be provided with one can cover whole separation cell 1 cover plate 13.Simultaneously separation cell the bottom be provided with several blow-down pipes (14a, 14b, 14c, 14d).
Below be the concrete operational process of the utility model equipment:
At first, make the water inlet pipe access arrangement of oily(waste)water, through the foreign material discrete blocks, oarse-grained impurity is separated then at this from separation cell.Then get into the cavitation air flotation stage, around a large amount of micro bubbles that produce under the effect of cavitation air flotation aerator are attached on olesome, make oil droplet under the lifting effect of microbubble, reduce its proportion; And float rapidly to liquid level; When treating that the liquid level oil slick reaches certain thickness, close or turn down the valve of automatic control of liquid device, liquid level is raise; Add the effect of swash plate oil removal plant, sewage gets into the swash plate disengaging zone from the cavitation air flotation district makes oil slick rapidly increase to liquid level.And the oil slick that floats on the liquid level can flow into oil trap automatically, and is recycled to oil storage barrel through oil outlet pipe.
In addition; In order further to strengthen the oil removal efficiency of water outlet; End at separation cell is placed the filter core that adopts special filtrate to be made into; This filtrate has the selection adsorptivity to oil, can an oil suction not absorb water, and makes remaining micro-oil droplet particle be adsorbed onto that water then drains into the equipment rising pipe through filter core on the filtering material.
Facts have proved, but the utility model can the oil slick more than the particle diameter 60um be removed more than 90%, the content of externally discharged waste water vegetable and animals oils is lower than " integrated wastewater discharge standard " primary standard (10mg/L) in (GB8978-1996).
Following table is the main technical details effect of the utility model equipment:
Project | Technical parameter | Remarks |
The water inlet oil concentration | Unrestricted | |
The water outlet oil concentration | Reach first discharge standard | Petroleum-type 5mg/l, vegetable and animals oils 10mg/l |
The clearance of oil | >90% | But for oil slick |
Working temperature | More than 0 ℃ | |
WP | Normal pressure | |
The proportion of separable oil | <1 | |
The particle diameter of separable minimum oil droplet | 60um | |
The oil droplet ascent rate | >0.2mm/s |
More than show and described ultimate principle of the utility model and the advantage of principal character and the utility model.The technician of the industry should understand; The utility model is not restricted to the described embodiments; The principle of describing in the foregoing description and the specification sheets that the utility model just is described; Under the prerequisite that does not break away from the utility model spirit and scope, the utility model also has various changes and modifications, and these variations and improvement all fall in the utility model scope that requires protection.The utility model requires protection domain to be defined by appending claims and equivalent thereof.
Claims (6)
1. water-and-oil separator, this device main body comprises a separation cell, it is characterized in that, said separation cell head end is provided with the water inlet pipe that is used for injecting oily(waste)water; Near the said foreign material discrete blocks that in separation cell, is provided with the water inlet pipe mouth, this is stated the foreign material discrete blocks and is used for the large granular impurity in the separating and filtering oily(waste)water; The said cavitation air flotation aerator that in separation cell, is mounted with, this state the cavitation air flotation aerator through in oily(waste)water, charge into a large amount of micro bubbles be attached on and oil droplet floated to liquid level around the olesome rapidly; Also be provided with swash plate oil removal plant in the said separation cell into the distance that shortens the oil slick rising; Said separation cell inside is provided with the oil trap that is used for holding the rising oil slick; Said end at separation cell is provided with the water shoot of a band filter core; Said water shoot connects a fluid level control device, this fluid level control device comprise one be used for controlling water shoot aquifer yield and freeboard level control valve.
2. according to the water-and-oil separator of claim 1, it is characterized in that oil trap one side is provided with oil outlet pipe in the said separation cell.
3. according to the water-and-oil separator of claim 1, it is characterized in that said level control valve is placed on the water shoot.
4. according to the water-and-oil separator of claim 1, it is characterized in that, said device also be provided with one can cover whole separation cell cover plate.
5. according to the water-and-oil separator of claim 1, it is characterized in that, saidly be provided with electric heating tube in the oil trap bottom.
6. according to the water-and-oil separator of claim 1, it is characterized in that, said separation cell the bottom be provided with a plurality of blow-down pipes.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011202457687U CN202265435U (en) | 2011-07-13 | 2011-07-13 | Oil-water separator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011202457687U CN202265435U (en) | 2011-07-13 | 2011-07-13 | Oil-water separator |
Publications (1)
Publication Number | Publication Date |
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CN202265435U true CN202265435U (en) | 2012-06-06 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN2011202457687U Expired - Fee Related CN202265435U (en) | 2011-07-13 | 2011-07-13 | Oil-water separator |
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Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102259950A (en) * | 2011-07-13 | 2011-11-30 | 济南鲁发环保科技有限公司 | Oil-water separator |
CN102923818A (en) * | 2012-11-15 | 2013-02-13 | 南京奥脉工程设备有限公司 | Integral closed oil separator |
CN102976442A (en) * | 2012-12-12 | 2013-03-20 | 张家港市远腾机械模具有限公司 | Oil slick recovery plant |
CN103435207A (en) * | 2013-08-19 | 2013-12-11 | 宋汶芸 | Improved oil-water separator |
CN104341068A (en) * | 2013-07-30 | 2015-02-11 | 麦王环境技术股份有限公司 | Combined cavitation air flotation apparatus and technology thereof |
CN108675473A (en) * | 2018-06-07 | 2018-10-19 | 苏州赛易特环保科技有限公司 | A kind of oil water separator adapting to low temperature environment |
-
2011
- 2011-07-13 CN CN2011202457687U patent/CN202265435U/en not_active Expired - Fee Related
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102259950A (en) * | 2011-07-13 | 2011-11-30 | 济南鲁发环保科技有限公司 | Oil-water separator |
CN102923818A (en) * | 2012-11-15 | 2013-02-13 | 南京奥脉工程设备有限公司 | Integral closed oil separator |
CN102923818B (en) * | 2012-11-15 | 2014-08-27 | 南京奥脉工程设备有限公司 | Integral closed oil separator |
CN102976442A (en) * | 2012-12-12 | 2013-03-20 | 张家港市远腾机械模具有限公司 | Oil slick recovery plant |
CN104341068A (en) * | 2013-07-30 | 2015-02-11 | 麦王环境技术股份有限公司 | Combined cavitation air flotation apparatus and technology thereof |
CN103435207A (en) * | 2013-08-19 | 2013-12-11 | 宋汶芸 | Improved oil-water separator |
CN108675473A (en) * | 2018-06-07 | 2018-10-19 | 苏州赛易特环保科技有限公司 | A kind of oil water separator adapting to low temperature environment |
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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: 20120606 Termination date: 20150713 |
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EXPY | Termination of patent right or utility model |