CN205815431U - Novel gas-liquid separation tray - Google Patents
Novel gas-liquid separation tray Download PDFInfo
- Publication number
- CN205815431U CN205815431U CN201620658843.5U CN201620658843U CN205815431U CN 205815431 U CN205815431 U CN 205815431U CN 201620658843 U CN201620658843 U CN 201620658843U CN 205815431 U CN205815431 U CN 205815431U
- Authority
- CN
- China
- Prior art keywords
- gas
- stopping plate
- tower
- guiding cylinder
- flow
- 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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Abstract
The utility model discloses a kind of novel gas-liquid separation tray, tower tray it is provided with in the middle part of tower body, tower tray is provided with gas flow guiding cylinder, it is provided with demister in gas flow guiding cylinder, being provided with demister bottom gas flow guiding cylinder to support, gas flow guiding cylinder top is provided with multiple flow-stopping plate, and flow-stopping plate is connected by flow-stopping plate support and fixture are fixing with tower body, tower body top is provided with spray head, and tower body sidewall is provided with leakage fluid dram.When desulfurization fume gas passes through the flow-stopping plate on gas flow guiding cylinder and top, gas flow guiding cylinder eliminates the drop carried secretly in gas, and gas can also be evenly distributed in absorption tower by flow-stopping plate, and the circulation fluid that beneficially spray equipment in tower falls contacts with gas secondary.This utility model can eliminate the phenomenon of gas entrained drip, plays except mist effect, allows gas to uniformly arrange again, can be effectively improved desulfurization absorption efficiency.
Description
Technical field
This utility model belongs to the technical field of flue gas desulfurization gas, is specifically related to a kind of in desulfuration spray tower, to up and down
Have no effect on during the partition of two sections of different liquids gas normal through novel gas-liquid separation tray.
Background technology
Using multi-layer multi-stage hollow-spraying-tower absorption techniques in wet desulfurizing process at present, every one-level has one or more
Spraying layer.The liquid spraying layer arranging multistage different medium in desulfurizing tower tower carries out Gas-Liquid Absorption to flue gas, and tower tray is in two
Planting the separating surface of different medium environment, tower tray should ensure the unimpeded of gas, makes gas so few that to carry front level segment secretly as far as possible again
Liquid enter next stage.Owing to traditional tower tray does not has the function of gas-liquid separation to prime gas, cause the liquid of previous stage
Taken to rear stage by gas, affect the treatment effect of system；And when using common tray structure when multi-stage column structure is set, also can
Forming flow velocity and the skewness of gas, space structure is big, it is impossible to eliminates gas and carries prime drop secretly, the use of confining device
Effect and efficiency.
Summary of the invention
The purpose of this utility model is to provide a kind of novel gas-liquid separation tray, when passing the gas through this tower tray, can carry out
Effective gas-liquid partition, gas-liquid separation and gas are the most uniform, and strengthen contact assimilation effect and the equipment efficiency of usage of rear class.
For achieving the above object, this utility model following structure of employing: a kind of novel gas-liquid separation tray, including tower tray
(1), demister support (2), gas flow guiding cylinder (3), demister (4), flow-stopping plate support (5), flow-stopping plate (6), fixture (7),
Tower body (8), tower body (8) middle part is provided with tower tray (1), and tower tray (1) is provided with gas flow guiding cylinder (3), and gas flow guiding cylinder is provided with in (3)
Demister (4), gas flow guiding cylinder (3) bottom is provided with demister and supports (2), and gas flow guiding cylinder (3) top is provided with multiple flow-stopping plate
(6), flow-stopping plate (6) is connected by flow-stopping plate support (5) and fixture (7) are fixing with tower body (8), and tower body (8) top is provided with spray
Drenching head (9), tower body (8) sidewall is provided with leakage fluid dram (10).
The cross sectional shape of flow-stopping plate (6) is S type, and flow-stopping plate (6) and tower body (8) horizontal tilt angle are 0-15 °.
When desulfurization fume gas passes through the flow-stopping plate on gas flow guiding cylinder and top, gas flow guiding cylinder eliminates in gas to be carried secretly
Drop, gas can also be evenly distributed in absorption tower by flow-stopping plate, the circulation fluid that beneficially spray equipment in tower falls with
Gas secondary contacts.This utility model can eliminate the phenomenon of gas entrained drip, plays except mist effect, allows gas to cloth the most again
Put, desulfurization absorption efficiency can be effectively improved.
Accompanying drawing explanation
Fig. 1 is this utility model structural representation.
Fig. 2 is the A-A sectional view of Fig. 1.
Fig. 3 is the I enlarged diagram in Fig. 1.
Fig. 4 is the II enlarged diagram in Fig. 2.
Detailed description of the invention:
In conjunction with accompanying drawing novel gas-liquid separation tray of the present utility model done following description:
As it can be seen, a kind of novel gas-liquid separation tray, support 2 including tower tray 1, demister, gas flow guiding cylinder 3, except mist
Device 4, flow-stopping plate support 5, flow-stopping plate 6, fixture 7, tower body 8, be provided with tower tray 1, tower tray 1 and tower body 8 surrounding seamless in the middle part of tower body 8
Welding, tower tray 1 is provided with gas flow guiding cylinder 3, places demister 4, be provided with and remove bottom gas flow guiding cylinder 3 in gas flow guiding cylinder 3
Day with fog supports 2, and gas flow guiding cylinder 3 top is provided with multiple flow-stopping plate 6, and flow-stopping plate 6 and tower body 8 support 5 and admittedly by flow-stopping plate
Locking member 7 is fixing to be connected, and flow-stopping plate supports 5 and is connected with tower body 8, is fixed on Ta Bishang.The cross sectional shape of flow-stopping plate 6 is S type, gear
Stream plate 6 is about 0-15 ° with tower body 8 horizontal tilt angle, it is simple to liquid fast guiding.Tower body 8 top is provided with spray head 9, tower body 8
Sidewall is provided with leakage fluid dram 10.
Operation principle: the wet flue gas after desulfurization, from bottom to top by the gas flow guiding cylinder 3 on tower tray 1, flue gas is at body water conservancy diversion
In cylinder 3, drop is retained by demister 4, and gas is from bottom to top by flow-stopping plate 6 time, and gas is uniformly distributed again, top
Spray liquid body drop is the most diversed on flow-stopping plate 6 to be collected on tower tray 1, and the liquid of collection is discharged outside tower through leakage fluid dram 10.
Claims (2)
1. a novel gas-liquid separation tray, including tower tray (1), demister support (2), gas flow guiding cylinder (3), demister (4),
Flow-stopping plate supports (5), flow-stopping plate (6), fixture (7), tower body (8), it is characterised in that: tower body (8) middle part is provided with tower tray (1),
Tower tray (1) is provided with gas flow guiding cylinder (3), is provided with demister (4) in gas flow guiding cylinder (3), and gas flow guiding cylinder (3) bottom is provided with
Demister supports (2), and gas flow guiding cylinder (3) top is provided with multiple flow-stopping plate (6), and flow-stopping plate (6) and tower body (8) pass through flow-stopping plate
Supporting (5) and the fixing connection of fixture (7), tower body (8) top is provided with spray head (9), and tower body (8) sidewall is provided with leakage fluid dram
(10)。
2. a kind of novel gas-liquid separation tray as claimed in claim 1, it is characterised in that: the cross sectional shape of flow-stopping plate (6) is S
Type, flow-stopping plate (6) and tower body (8) horizontal tilt angle are 0-15 °.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620658843.5U CN205815431U (en) | 2016-06-28 | 2016-06-28 | Novel gas-liquid separation tray |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620658843.5U CN205815431U (en) | 2016-06-28 | 2016-06-28 | Novel gas-liquid separation tray |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205815431U true CN205815431U (en) | 2016-12-21 |
Family
ID=57566352
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620658843.5U Expired - Fee Related CN205815431U (en) | 2016-06-28 | 2016-06-28 | Novel gas-liquid separation tray |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205815431U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107335332A (en) * | 2017-06-14 | 2017-11-10 | 大唐环境产业集团股份有限公司 | A kind of fold-line-shaped gas-liquid part flow arrangement with collecting tank |
-
2016
- 2016-06-28 CN CN201620658843.5U patent/CN205815431U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107335332A (en) * | 2017-06-14 | 2017-11-10 | 大唐环境产业集团股份有限公司 | A kind of fold-line-shaped gas-liquid part flow arrangement with collecting tank |
| CN107335332B (en) * | 2017-06-14 | 2023-08-04 | 大唐环境产业集团股份有限公司 | Fold-line-shaped gas-liquid flow dividing device with collecting tank |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20161221 Termination date: 20200628 |