CN201324539Y - Monomer separating device - Google Patents
Monomer separating device Download PDFInfo
- Publication number
- CN201324539Y CN201324539Y CNU2008201435231U CN200820143523U CN201324539Y CN 201324539 Y CN201324539 Y CN 201324539Y CN U2008201435231 U CNU2008201435231 U CN U2008201435231U CN 200820143523 U CN200820143523 U CN 200820143523U CN 201324539 Y CN201324539 Y CN 201324539Y
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- China
- Prior art keywords
- slurry
- monomer
- outlet
- inlet
- cooling water
- Prior art date
- 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.)
- Expired - Fee Related
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
A monomer separating device comprises a tower body (1), trays (2), a slurry inlet (3), a slurry outlet (5),a monomer outlet (4), a steam inlet (7), and a cooling water inlet (6), wherein, a plurality of trays (2) are arranged in the middle of the tower body (1) in a staggered manner; the monomer outlet (4) and the slurry outlet (5) are respectively formed at the top and the bottom of the tower body; the slurry inlet (3) and the steam inlet (7) are respectively formed at the upper part and the lower part of the trays (2); and the cooling water inlet (6) higher than the slurry inlet (3) is formed below the monomer outlet (4).
Description
Affiliated technical field
The utility model relates to a kind of separator, relates in particular to a kind of monomer separation stripper.
Background technology
The stripper that industry is at present used mostly is by steam slurry to be heated, and makes the gas componant in the slurry obtain separating.But the adding of steam often makes the gas componant that extracts contain a large amount of steam, also needs to enter the further cooling of other operations and removes moisture, and this has not only prolonged production procedure, makes complex process, and has increased production cost.
Summary of the invention
The utility model provides a kind of monomer separation device, it can make the gas componant that extracts obtain cooling, go out the moisture that wherein contains, in order to achieve the above object, the technical solution adopted in the utility model is, a kind of monomer separation device, comprise tower body, tower tray, the slurry inlet, slurry outlet, the monomer outlet, the steam inlet, the cooling water inlet, be staggeredly equipped with the multilayer tower tray in the middle of the described tower body, its top and bottom are respectively equipped with monomer outlet and slurry outlet, described tower tray upper and lower is respectively equipped with slurry inlet and steam inlet, is provided with the cooling water inlet in monomer outlet bottom, and is higher than the slurry inlet.
When slurry runs into high-temperature steam along tower tray is descending, contained gaseous monomer composition is deviate from the slurry, up with remaining steam, the cooling water that when arriving monomer outlet position and cooling water inlet sprays into meets, make the steam cooling get back to tower body, discharge from slurry outlet with the slurry after the degassing, the gaseous monomer composition that is suggested is discharged from the monomer outlet.
The utility model has solved the problem that the gaseous monomer that is suggested contains steam effectively, has reduced technology, has saved cost, and satisfactory for result.
Description of drawings
The utility model is described in further detail below in conjunction with accompanying drawing.
Fig. 1 is the utility model structural representation.
The specific embodiment
By accompanying drawing as can be known, the utility model comprises tower body 1, tower tray 2, slurry inlet 3, slurry outlet 5, monomer outlet 4, steam inlet 7, cooling water inlet 6, be staggeredly equipped with multilayer tower tray 2 in the middle of the described tower body 1, its top and bottom are respectively equipped with monomer outlet 4 and slurry outlet 5, described tower tray 2 upper and lowers are respectively equipped with slurry inlet 3 and steam inlet 7, export 4 bottoms at monomer and be provided with cooling water inlet 6, and be higher than slurry inlet 3.
When slurry runs into high-temperature steam along tower tray 2 is descending, contained gaseous monomer composition is deviate from the slurry, up with remaining steam, the cooling water that when the arrival monomer exports 4 positions and cooling water inlet 6 sprays into meets, make the steam cooling get back to tower body, discharge from slurry outlet 5 with the slurry after the degassing, the gaseous monomer composition that is suggested is discharged from monomer outlet 4.
Claims (2)
1, a kind of monomer separation device, comprise tower body (1), tower tray (2), slurry inlet (3), slurry outlet (5), monomer outlet (4), steam inlet (7), cooling water inlet (6), it is characterized in that: be staggeredly equipped with multilayer tower tray (2) in the middle of the described tower body (1), its top and bottom are respectively equipped with monomer outlet (4) and slurry outlet (5), described tower tray (2) upper and lower is respectively equipped with slurry inlet (3) and steam inlet (7), is provided with cooling water inlet (6) in monomer outlet (4) bottom.
2, according to the described monomer separation device of claim 1, it is characterized in that: described cooling water inlet (6) are higher than slurry inlet (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008201435231U CN201324539Y (en) | 2008-11-26 | 2008-11-26 | Monomer separating device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008201435231U CN201324539Y (en) | 2008-11-26 | 2008-11-26 | Monomer separating device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201324539Y true CN201324539Y (en) | 2009-10-14 |
Family
ID=41176514
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2008201435231U Expired - Fee Related CN201324539Y (en) | 2008-11-26 | 2008-11-26 | Monomer separating device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201324539Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102335520A (en) * | 2010-07-22 | 2012-02-01 | 天津科技大学 | Multilayer fluidized solid continuous distillation column |
| CN112708441A (en) * | 2019-10-24 | 2021-04-27 | 中国石化工程建设有限公司 | Tray for catalytic slurry oil separation and catalytic slurry oil separation tower |
-
2008
- 2008-11-26 CN CNU2008201435231U patent/CN201324539Y/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102335520A (en) * | 2010-07-22 | 2012-02-01 | 天津科技大学 | Multilayer fluidized solid continuous distillation column |
| CN112708441A (en) * | 2019-10-24 | 2021-04-27 | 中国石化工程建设有限公司 | Tray for catalytic slurry oil separation and catalytic slurry oil separation tower |
| CN112708441B (en) * | 2019-10-24 | 2022-10-28 | 中国石化工程建设有限公司 | Tray for catalytic slurry oil separation and catalytic slurry oil separation tower |
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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: 20091014 Termination date: 20101126 |