CN204939031U - High separation rate oily-water seperating equipment - Google Patents
High separation rate oily-water seperating equipment Download PDFInfo
- Publication number
- CN204939031U CN204939031U CN201520693816.7U CN201520693816U CN204939031U CN 204939031 U CN204939031 U CN 204939031U CN 201520693816 U CN201520693816 U CN 201520693816U CN 204939031 U CN204939031 U CN 204939031U
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- China
- Prior art keywords
- sewage
- water
- water inlet
- tube
- vertical tube
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- 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.)
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Abstract
The utility model discloses high separation rate oily-water seperating equipment, it comprises open-topped water inlet vertical tube (1) and vertical drain (2), water inlet vertical tube is communicated with by U-shaped curved (3) with vertical drain, water inlet vertical tube sidewall is provided with water filling port (4), U-shaped curved interior adaptation has gate valve moving up and down (5), in water inlet vertical tube, below water filling port, adaptation has aeration tube (6), the water inlet vertical tube between water filling port and aeration tube is connected with horizontal filter screen (7).The beneficial effects of the utility model utilize gate valve to be isolated in by pending sewage in water vertical tube and maintain certain liquid level, the fluid in sewage is taken to sewage surface after the aeration of aeration tube for some time, open gate valve again, separated sewage enters vertical drain, then enters biochemical treatment workshop in vertical drain, ensure that being separated completely of fluid and sewage, and other molecule impurity can removed in sewage, oily water separation efficiency is high, and structure is simple, with low cost.
Description
Technical field
The utility model relates to tripping device, particularly relates to oily-water seperating equipment.
Background technology
Dehydration tower is a kind of device target solution being carried out to processed, be widely used in coke-oven plant, it is the portion of water removed by flash distillation in rich oil, in use, the a small amount of sewage produced in production can enter dehydration tower, is originally and allows sewage tower sewage out directly enter biochemical treatment workshop.If the sewage that mishandle enters biochemical treatment workshop will carry oil phase, increase material loss, add production cost, also bring certain pressure to sewage disposal.This carries out oily water separation operation with regard to needing to the sewage of discharging from sewage tower.
Utility model content
The technical problems to be solved in the utility model is that the sewage that existing sewage tower is discharged directly enters biochemical treatment workshop, strengthens material loss, adds production cost, also bring certain pressure to sewage disposal, provide a kind of high separation rate oily-water seperating equipment for this reason.
The technical solution of the utility model is: high separation rate oily-water seperating equipment, it comprises open-topped water inlet vertical tube and vertical drain, described water inlet vertical tube and vertical drain to be curvedly communicated with by U-shaped, described water inlet vertical tube sidewall is provided with water filling port, described U-shaped curved interior adaptation has gate valve moving up and down, in described water inlet vertical tube, below water filling port, adaptation has aeration tube, and the water inlet vertical tube between described water filling port and aeration tube is connected with horizontal filter screen.
Longitudinal filter screen is connected with between described U-shaped curved interior gate valve and vertical drain.
The beneficial effects of the utility model utilize gate valve to be isolated in by pending sewage in water vertical tube and maintain certain liquid level, the fluid in sewage is taken to sewage surface after the aeration of aeration tube for some time, open gate valve again, separated sewage enters vertical drain, then enters biochemical treatment workshop in vertical drain, ensure that being separated completely of fluid and sewage, and other molecule impurity can removed in sewage, oily water separation efficiency is high, and structure is simple, with low cost.
Accompanying drawing explanation
Fig. 1 is the utility model schematic diagram;
In figure, 1, water inlet vertical tube, 2, vertical drain, 3, U-shaped curved, 4, water filling port, 5, gate valve, 6, aeration tube, 7, horizontal filter screen, 8, longitudinal filter screen.
Embodiment
Below in conjunction with accompanying drawing, the utility model is described further.
As shown in Figure 1, the utility model comprises open-topped water inlet vertical tube 1 and vertical drain 2, described water inlet vertical tube is communicated with by U-shaped curved 3 with vertical drain, described water inlet vertical tube sidewall is provided with water filling port 4, described U-shaped curved interior adaptation has gate valve 5 moving up and down, in described water inlet vertical tube, below water filling port, adaptation has aeration tube 6, and the water inlet vertical tube between described water filling port and aeration tube is connected with horizontal filter screen 7.
When using the utility model, first inject pending sewage from water filling port, gate valve is closed and is cut off water inlet vertical tube and vertical drain, make constantly to raise into the liquid level in water vertical tube, after entering the sewage level in water vertical tube and exceeding aeration tube, aeration tube is started working, bubble is utilized to take liquid level to the fluid in sewage and molecule impurity, thus reach the effect of profit layering, make to enter after above horizontal filter screen into the sewage in water vertical tube and fluid and molecule separated from impurities after aeration tube work certain hour, open gate valve, because law of connected vessels makes sewage pour in vertical drain, the sewage entered in vertical drain is not containing fluid, directly can enter biochemical treatment workshop to process.
In order to ensure oily water separation rate, preventing micro-fluid from pouring in vertical drain, longitudinal filter screen 8 can be connected with between U-shaped curved interior gate valve and vertical drain, secondary filtration be carried out to the sewage of process, filters out fluid and oarse-grained impurity.
Claims (2)
1. high separation rate oily-water seperating equipment, it is characterized in that it comprises open-topped water inlet vertical tube (1) and vertical drain (2), described water inlet vertical tube is communicated with by U-shaped curved (3) with vertical drain, described water inlet vertical tube sidewall is provided with water filling port (4), described U-shaped curved interior adaptation has gate valve moving up and down (5), in described water inlet vertical tube, below water filling port, adaptation has aeration tube (6), the water inlet vertical tube between described water filling port and aeration tube is connected with horizontal filter screen (7).
2. high separation rate oily-water seperating equipment as claimed in claim 1, is characterized in that being connected with longitudinal filter screen (8) between described U-shaped curved interior gate valve and vertical drain.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520693816.7U CN204939031U (en) | 2015-09-09 | 2015-09-09 | High separation rate oily-water seperating equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520693816.7U CN204939031U (en) | 2015-09-09 | 2015-09-09 | High separation rate oily-water seperating equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204939031U true CN204939031U (en) | 2016-01-06 |
Family
ID=55006474
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520693816.7U Expired - Fee Related CN204939031U (en) | 2015-09-09 | 2015-09-09 | High separation rate oily-water seperating equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204939031U (en) |
-
2015
- 2015-09-09 CN CN201520693816.7U patent/CN204939031U/en not_active Expired - Fee Related
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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: 20160106 Termination date: 20180909 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |