CN205627345U - Binary channels combination formula gas -liquid separation tower - Google Patents
Binary channels combination formula gas -liquid separation tower Download PDFInfo
- Publication number
- CN205627345U CN205627345U CN201620327656.9U CN201620327656U CN205627345U CN 205627345 U CN205627345 U CN 205627345U CN 201620327656 U CN201620327656 U CN 201620327656U CN 205627345 U CN205627345 U CN 205627345U
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- CN
- China
- Prior art keywords
- air inlet
- gas
- liquid separation
- post core
- separation tower
- 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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- Separation By Low-Temperature Treatments (AREA)
- Separating Particles In Gases By Inertia (AREA)
Abstract
The utility model discloses a binary channels combination formula gas -liquid separation tower, including the tube -shape casing, the air inlet has been seted up to the side of casing, be provided with vapour and liquid separator in the casing, vapour and liquid separator includes the post core, post core side is provided with a plurality of vertical baffles of arranging, leaves the space between baffle and the shells inner wall, the upside of baffle extends the post core, the top of a plurality of baffles is provided with the circumferential butt, cyclic annular cover connection casing, the air inlet is towards the baffle, inlet set has two, two air inlets set up relatively, the length of a plurality of baffle is crescent by department in the middle of air inlet to two air inlets, the utility model discloses simple structure, behind the gas -liquid separation, gas is no longer smugglied liquid secretly and is moved jointly, can handle large -capacity.
Description
Technical field
This utility model belongs to gas-liquid separation tower, a kind of dual pathways combination type gas-liquid separation tower.
Background technology
Commercial production produce waste gas purified after, gas-liquid separation need to be carried out through gas-liquid separation tower, water content in the gas of discharge is made to reach standard, the most conventional usually gravitational settling separates with deflection plate, during gravity settling separation, gas from bottom to top moves, liquid is when flowing with the gases, liquid can be affected by gravity, produce a downward speed, and gas is still towards original direction flowing, but along with continuous continuous print gas moves upward, the liquid of sedimentation will be carried secretly by gas again, separating effect is undesirable, deflection plate self structure is complicated, and need to periodically clear up, the complex trouble of scale removal process.
Utility model content
For the deficiencies in the prior art, this utility model provides a kind of simple in construction, after gas-liquid separation, gas no longer entrained liquids associated movement, it is possible to process the dual pathways combination type gas-liquid separation tower of atm number.
For achieving the above object, this utility model provides following technical scheme: a kind of dual pathways combination type gas-liquid separation tower, including tubular shell, the side opening of described housing is provided with air inlet, it is provided with gas-liquid separator in described housing, described gas-liquid separator includes post core, described post core side is provided with the baffle plate of some vertical layouts, space is left between baffle plate and inner walls, post core is extended in the upside of described baffle plate, the top of described some baffle plates is provided with circumferential butt, and described circumferential butt connects housing, and described air inlet is towards baffle plate.
Preferred described air inlet is provided with two, and said two air inlet is oppositely arranged.
The length of several baffle plates the most described is gradually increased to two air inlet middles by air inlet.
It is provided with initial distribution plate at preferred described post core correspondence air inlet.
Compared with prior art, the beneficial effects of the utility model are: corresponding with the air inlet of housing by the baffle plate of some vertical layouts, gas will be stopped by post core and baffle plate after being entered housing by air inlet, portion gas is walked around baffle plate and is moved along housing barrel circumferencial direction, when gas touches baffle plate, the liquid wherein carried secretly will be captured, liquid will flow downward along baffle plate, and its flow trace and gas motion track irrelevant, can avoid liquid again by gas entrained with, the gas removing liquid will rise on the space between baffle plate and barrel, last by cover plate, the passage formed between baffle plate and post core moves upward discharge；And the setting that several baffle length differ so that at circumferencial direction, any one is all distributed more uniform gas, improves treating capacity, and due to without bending part, it is not necessary to cleaning, impurity can move downwardly to housing bottom along baffle plate vertical direction is without hindrance.
Accompanying drawing explanation
Fig. 1 is the structural representation of this utility model dual pathways combination type gas-liquid separation tower；
Fig. 2 is the three-dimensional structure diagram of gas-liquid separator in this utility model；
Fig. 3 is the front view of gas-liquid separator in this utility model.
Reference: 1, housing；16, air inlet；2, passage；61, post core；62, baffle plate；63, cover plate；65, initial distribution plate.
Detailed description of the invention
Referring to figs. 1 through Fig. 3, the embodiment of this utility model dual pathways combination type gas-liquid separation tower is described further.
nullA kind of dual pathways combination type gas-liquid separation tower，Including tubular shell 1，The side opening of described housing 1 is provided with air inlet 16，It is provided with gas-liquid separator in described housing 1，Described gas-liquid separator includes post core 61，Described post core 61 side is provided with the baffle plate 62 of some vertical layouts，Space is left between baffle plate 62 and housing 1 inwall，Post core 61 is extended in the upside of described baffle plate 62，The top of described some baffle plates 62 is provided with circumferential butt 63，Described circumferential butt 63 connects housing 1，Described air inlet 16 is towards baffle plate 62，All extend a distance into by air inlet 16 above-below direction at this utility model center pillar core 61，Same baffle plate 62 is coextensive in company with post core 61，Ensure that the gas that air inlet 16 enters can be stopped by post core 61，Gas is made along the circumferential direction to move，Every piece of baffle plate 62 all can play the effect catching liquid.
Further, as it is shown in figure 1, described air inlet 16 is provided with two, said two air inlet 16 is oppositely arranged, the length of several baffle plates 62 described is gradually increased by air inlet 16 to two air inlet 16 middle, is provided with initial distribution plate 65 at the corresponding air inlet 16 of described post core 61.
Gas through air inlet 16 enter after just along figure the direction of arrow along the inwall circular motion of housing 1, as shown in Figure 1, make every piece of baffle plate 62 all can contact gas and catch liquid, two air inlets 16 increase air inflow, and the setting being gradually increased due to some baffle plate 62 length, bigger air inflow also can be by gas-liquid separation, and wherein initial distribution plate 65 then carries out water conservancy diversion to gas；Being distributed between post core 61 and housing 1 and will be risen by the gas except liquid, the passage 2 being made up of cover plate 63, baffle plate 62 and post core 61 is discharged, and the liquid being captured will flow downwardly to the bottom of housing 1 along baffle plate 62.
The above is only preferred implementation of the present utility model, and protection domain of the present utility model is not limited merely to above-described embodiment, and all technical schemes belonged under this utility model thinking belong to protection domain of the present utility model.It should be pointed out that, for those skilled in the art, without departing from the some improvements and modifications under this utility model principle premise, these improvements and modifications also should be regarded as protection domain of the present utility model.
Claims (4)
1. a dual pathways combination type gas-liquid separation tower, including tubular shell, it is characterized in that: the side opening of described housing is provided with air inlet, being provided with gas-liquid separator in described housing, described gas-liquid separator includes post core, described post core side is provided with the baffle plate of some vertical layouts, leaving space between baffle plate and inner walls, post core is extended in the upside of described baffle plate, and the top of described some baffle plates is provided with circumferential butt, described circumferential butt connects housing, and described air inlet is towards baffle plate.
Dual pathways combination type gas-liquid separation tower the most according to claim 1, it is characterised in that: described air inlet is provided with two, and said two air inlet is oppositely arranged.
Dual pathways combination type gas-liquid separation tower the most according to claim 2, it is characterised in that: the length of several baffle plates described is gradually increased to two air inlet middles by air inlet.
Dual pathways combination type gas-liquid separation tower the most according to claim 3, it is characterised in that: it is provided with initial distribution plate at described post core correspondence air inlet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620327656.9U CN205627345U (en) | 2016-04-16 | 2016-04-16 | Binary channels combination formula gas -liquid separation tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620327656.9U CN205627345U (en) | 2016-04-16 | 2016-04-16 | Binary channels combination formula gas -liquid separation tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205627345U true CN205627345U (en) | 2016-10-12 |
Family
ID=57064482
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620327656.9U Expired - Fee Related CN205627345U (en) | 2016-04-16 | 2016-04-16 | Binary channels combination formula gas -liquid separation tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205627345U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106861590A (en) * | 2017-02-20 | 2017-06-20 | 北京石油化工工程有限公司 | Aromatic hydrocarbons conversion reactor |
| CN113457186A (en) * | 2020-03-30 | 2021-10-01 | 中石油吉林化工工程有限公司 | Method for improving separation effect of crude MMA (methyl methacrylate) separation tower |
-
2016
- 2016-04-16 CN CN201620327656.9U patent/CN205627345U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106861590A (en) * | 2017-02-20 | 2017-06-20 | 北京石油化工工程有限公司 | Aromatic hydrocarbons conversion reactor |
| CN106861590B (en) * | 2017-02-20 | 2023-05-19 | 北京石油化工工程有限公司 | Aromatic hydrocarbon conversion reactor |
| CN113457186A (en) * | 2020-03-30 | 2021-10-01 | 中石油吉林化工工程有限公司 | Method for improving separation effect of crude MMA (methyl methacrylate) separation tower |
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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: 20161012 Termination date: 20170416 |