CN201543268U - Oil-water separating trap - Google Patents
Oil-water separating trap Download PDFInfo
- Publication number
- CN201543268U CN201543268U CN2009202366676U CN200920236667U CN201543268U CN 201543268 U CN201543268 U CN 201543268U CN 2009202366676 U CN2009202366676 U CN 2009202366676U CN 200920236667 U CN200920236667 U CN 200920236667U CN 201543268 U CN201543268 U CN 201543268U
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- chamber
- water
- clarifying
- organic
- oil
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Abstract
An oil-water separating trap of the utility model comprises a submarine chamber, a mixing chamber and a clarifying chamber, wherein the submarine chamber is communicated with the mixing chamber and is separated from the clarifying chamber by a spacer plate, and the mixing chamber is communicated with the clarifying chamber. Two sides of the submarine chamber are respectively provided with a trapping agent interface and a water tank interface. The controlled flow ratio of the trapping agent interface and the water tank interface is 1: (10-20000). The clarifying chamber is provided with an oil-removing water tank interface, and the clarifying chamber comprises at least two communicated compartments. The volume ratio of the submarine chamber, mixing chamber and the clarifying chamber is 1: (5-20): (15-100). The oil-water separating trap of the utility model effectively reduces the organic entraining of water phase, and the trapped organic trapping agent can be used for preparing organic extraction for product line after reaching a certain level in the clarifying chamber. The trapped water phase can reach an organic content of less than 10mg/L and an organic removing rate of more than 90%.
Description
Technical field
The utility model relates to a kind of separation and collection device, is specifically related to a kind of water-oil separating trap.
Background technology
To carry secretly organic be a very headachy thing to water in the lyometallurgy, generally more than 100mg/L.The one, cause organic waste, moreover also polluted product.For addressing this problem, used a lot of methods: the ultrasonic wave oil removing, active carbon adsorption, clarification or the like all each has pluses and minuses separately naturally.The ultrasonic wave deoiling effect is relatively good, but equipment investment is big, the operating cost height.Active carbon adsorption and natural clarification equipment are simple, but inefficiency, and the occupancy of material is higher.
The utility model content
For overcoming above-mentioned technological deficiency, the purpose of this utility model provides a kind of water-oil separating trap.
For achieving the above object, adopt following technical scheme:
Water-oil separating trap of the present utility model comprises latent chamber, mixing chamber and clarifying chamber, and the chamber of diving is communicated with mixing chamber, and both connections can realize by aperture on the dividing plate of two Room or crack.Latent chamber and clarifying chamber separate by dividing plate.Mixing chamber and clarifying chamber are communicated with, and the connection of mixing chamber and clarifying chamber can realize by aperture on the dividing plate of two Room or crack.
The both sides of latent chamber are respectively equipped with trapping agent interface and water-tank hole.The control flow ratio of trapping agent interface and water-tank hole is 1: (10～20000).The clarifying chamber is provided with the oil removing water-tank hole.The clarifying chamber is made up of the compartment of a plurality of connections.The volume ratio of latent chamber, mixing chamber and clarifying chamber is 1: (5～20): (15～100).
What water-oil separating trap of the present utility model used is that one-level is mixed clarification formula extraction tank, diluent with the preparation extractant, as sulfonated kerosene, as trapping agent, carry out once to organic extraction carrying organic water secretly, after the clarifying chamber flows through the multi-compartment chamber, make that having captured organic trapping agent separates well with water, obtains clean oil removing water.
Compared with prior art, the principle of water-oil separating trap utilization extraction of the present utility model with organic extraction that trapping agent is carried secretly aqueous phase, has reduced the organic of water effectively and has carried secretly, reaches good separating effect.Having captured organic trapping agent, can to pull the extraction that is used to prepare on the production line after the clarifying chamber is enriched to a certain degree out organic.Aqueous phase organic content after the capture can be less than the 10mg/L level.Organic clearance reaches more than 90%.
Description of drawings
Fig. 1 is the side view of a preferred embodiment of water-oil separating trap of the present utility model;
Fig. 2 is the vertical view of water-oil separating trap among Fig. 1.
The specific embodiment
For making the utility model easier to understand,, further set forth the utility model below in conjunction with specific embodiment.Should be understood that these embodiment only to be used to the utility model is described and be not used in the restriction scope of the present utility model.
Fig. 1 is the side view of a preferred embodiment of water-oil separating trap of the present utility model, and Fig. 2 is the vertical view of water-oil separating trap among Fig. 1.Two figure are combined, and this water-oil separating trap comprises dive chamber 1, mixing chamber 2 and clarifying chamber 3, and the chamber 1 of diving is communicated with mixing chamber 2, and both connections can realize by aperture on the dividing plate of two Room or crack.Dive chamber 1 and clarifying chamber 3 separates by dividing plate.Mixing chamber 2 and clarifying chamber 3 are communicated with, and the connection of mixing chamber 2 and clarifying chamber 3 can realize by aperture on the dividing plate of two Room or crack.The both sides of latent chamber 1 are respectively equipped with trapping agent interface 11 and water-tank hole 12.The control flow ratio of trapping agent interface 11 and water-tank hole 12 is 1: (20000～10).Clarifying chamber 3 is provided with oil removing water-tank hole 31.Clarifying chamber 3 is made up of the compartment 32 of a plurality of connections.The volume ratio of latent chamber 1, mixing chamber 2 and clarifying chamber 3 is divided into 1: (5～20): (15～100).Trapping agent carries out once organic extraction carrying organic water secretly, after clarifying chamber 3 flows through multi-compartment chamber 32, makes that having captured organic trapping agent separates well with water, obtains clean oil removing water.Trapping agent forms supernatant liquid in the water-oil separating trap, be trapping agent crystallizing field 33.
Last institute should be noted that; above embodiment is only in order to the explanation the technical solution of the utility model but not to the restriction of the utility model protection domain; although the utility model has been done detailed description with reference to preferred embodiment; those of ordinary skill in the art is to be understood that; can make amendment or be equal to replacement the technical solution of the utility model, and not break away from the essence and the scope of technical solutions of the utility model.
Claims (6)
1. a water-oil separating trap is characterized in that, comprises latent chamber, mixing chamber and clarifying chamber, and described latent chamber is communicated with described mixing chamber, and described latent chamber and described clarifying chamber separate by dividing plate; Described mixing chamber and described clarifying chamber are communicated with.
2. water-oil separating trap according to claim 1 is characterized in that the both sides of described latent chamber are respectively equipped with trapping agent interface and water-tank hole.
3. water-oil separating trap according to claim 2 is characterized in that, the control flow ratio of described trapping agent interface and described water-tank hole is 1: (10～20000).
4. water-oil separating trap according to claim 1 is characterized in that described clarifying chamber is provided with the oil removing water-tank hole.
5. water-oil separating trap according to claim 1 is characterized in that described clarifying chamber is made up of the compartment of two connections at least.
6. water-oil separating trap according to claim 1 is characterized in that, the volume ratio of described latent chamber, described mixing chamber and described clarifying chamber is 1: (5～20): (15～100).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009202366676U CN201543268U (en) | 2009-09-29 | 2009-09-29 | Oil-water separating trap |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009202366676U CN201543268U (en) | 2009-09-29 | 2009-09-29 | Oil-water separating trap |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201543268U true CN201543268U (en) | 2010-08-11 |
Family
ID=42598425
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009202366676U Expired - Fee Related CN201543268U (en) | 2009-09-29 | 2009-09-29 | Oil-water separating trap |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201543268U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108434866A (en) * | 2017-02-16 | 2018-08-24 | 松下知识产权经营株式会社 | Separator |
-
2009
- 2009-09-29 CN CN2009202366676U patent/CN201543268U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108434866A (en) * | 2017-02-16 | 2018-08-24 | 松下知识产权经营株式会社 | Separator |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100811 Termination date: 20120929 |