CN104771961A - Horizontal impinging stream gas-water separator - Google Patents
Horizontal impinging stream gas-water separator Download PDFInfo
- Publication number
- CN104771961A CN104771961A CN201510134656.7A CN201510134656A CN104771961A CN 104771961 A CN104771961 A CN 104771961A CN 201510134656 A CN201510134656 A CN 201510134656A CN 104771961 A CN104771961 A CN 104771961A
- Authority
- CN
- China
- Prior art keywords
- tank body
- baffle plate
- water
- gas
- knockout drum
- 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.)
- Granted
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 29
- 239000007788 liquid Substances 0.000 claims abstract description 24
- 238000000926 separation method Methods 0.000 claims abstract description 8
- 230000005514 two-phase flow Effects 0.000 claims description 11
- 238000009527 percussion Methods 0.000 claims description 6
- 229910000831 Steel Inorganic materials 0.000 claims description 4
- 239000007792 gaseous phase Substances 0.000 claims description 4
- 239000007791 liquid phase Substances 0.000 claims description 4
- 239000010959 steel Substances 0.000 claims description 4
- 238000005259 measurement Methods 0.000 abstract 1
- 238000003466 welding Methods 0.000 abstract 1
- 238000005516 engineering process Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 230000008676 import Effects 0.000 description 2
- 238000003889 chemical engineering Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 238000005476 soldering Methods 0.000 description 1
Landscapes
- Separating Particles In Gases By Inertia (AREA)
- Measuring Volume Flow (AREA)
Abstract
The invention relates to a horizontal impinging stream gas-water separator. The horizontal impinging stream gas-water separator comprises a separation tank body (1), a backflow baffle plate (2) is arranged in the separation tank body (1), one side of the backflow baffle plate (2) is a rectification zone (3), the other side of the backflow baffle plate (2) is an impinging zone (4), the rectification zone (3) is provided with a gas outlet (10), an overflow opening (5), a liquidometer (6) and a liquid outlet (7); and the impinging zone (4) is provided with two gas and water outlets (8), and the welding openings of the gas and water outlets (8) are welded with gas inlet tubes (9). The body of the horizontal impinging stream gas-water separator adopts an elliptical tank body structure. The horizontal impinging stream gas-water separator overcomes the disadvantage of large occupied area of original devices, greatly reduces the gas and liquid fluctuation of the rectification zone, and makes liquid drops difficultly fly out, and the measurement of the liquidometer is accurate.
Description
Technical field
The present invention relates to the energy, Chemical Engineering Technology research field, is more particularly a kind of horizontal percussion flow moisture trap.
Background technology
At engineering field, moisture trap is often designed to the vertical tank body of single admission.The problems such as it is large that the type moisture trap exists floor space, and separating effect is not good, and liquid is easily gone out, and tank level fluctuation is large.
Vertical tank body import form is single, and the necessary lateral arrangement of air water inlet pipeline, tank body floor space is comparatively large, limits entire system compact layout.
Unidirectional import causes knockout drum flow field extremely uneven, and liquid fluctuating is comparatively large, and level gauging is forbidden.
Partial design has set up baffle plate in tank body, but the setting of this baffle plate result in the further increase of flow resistance, and gas-water separation carries effect limited extent.
Summary of the invention
The object of the invention is to the deficiency overcoming above-mentioned background technology, and propose horizontal percussion flow moisture trap.
The object of the invention is to be reached by following measure: it comprises knockout drum tank body 1, is provided with refluence baffle plate 2 in described knockout drum tank body 1; The side of refluence baffle plate 2 is commutating zone 3, and opposite side is impingement region 4; Described commutating zone 3 is provided with gaseous phase outlet 10, overfall 5, liquid level gauge 6 and liquid-phase outlet 7; Described impingement region 4 is provided with two air-water two phase flow outlets 8, exports 8 places at described air-water two phase flow and be welded with air inlet pipe 9; The opening of the air-water two phase flow outlet 8 described in two is oppositely arranged; Have water in described knockout drum tank body 1, the horizontal plane of described water is positioned at below described knockout drum tank body 1 center line; Described refluence baffle plate 2 welded top, on separation tank body 1, has interval bottom the bottom of described refluence baffle plate 2 and knockout drum tank body 1; Described refluence baffle plate 2 is divided into two sections, and epimere is airflow layer, and described airflow layer is cavernous structure 2-1, and hypomere is anti-ripple layer, and described anti-ripple layer is steel plate structure 2-2; The bottom of described anti-ripple layer is positioned at below described horizontal plane, and the top of described anti-ripple layer is positioned at above described horizontal plane; Described horizontal plane is positioned at the below of described center line.
Tool of the present invention has the following advantages: 1. the two-part subregion in the present invention and flow apron design, greatly reduces the gas-liquid fluctuation of commutating zone, drop is not easily gone out, and liquid level gauge is measured more accurate; 2. the top that vacuum pump body is arranged in cooler is close to by knockout drum of the present invention, vavuum pump low in energy consumption; 3. vavuum pump integrated size is little, saves space and floor space, equipment conveying and arrangement convenience.
Accompanying drawing explanation
Fig. 1 is traditional vertical steam-water separator schematic diagram.
Fig. 2 is structural representation of the present invention.
Fig. 3 is that Fig. 1 flows backwards the structural representation of baffle plate.
Fig. 4 is A-A profile in Fig. 1.
Fig. 5 is air water two-phase concrete structure detail drawing.
In figure: knockout drum tank body 1, refluence baffle plate 2, cavernous structure 2-1, steel plate structure 2-2, commutating zone 3, impingement region 4, overfall 5, liquid level gauge 6, liquid-phase outlet 7, air-water two phase flow outlet 8, air inlet pipe 9, gaseous phase outlet 10.
Detailed description of the invention
Describe performance of the present invention in detail below in conjunction with accompanying drawing, but they do not form limitation of the invention, only for example; To become clearly and easy understand advantage of the present invention by illustrating simultaneously.
With reference to shown in Fig. 1: traditional vertical steam-water separator kinetic energy after biphase gas and liquid flow enters tank body cannot be offset, impact comparatively large to tank body, after gas-liquid separation, the total tank body lower part outlet of liquid is flowed out, and for preventing lower liquid from spilling, part knockout drum is provided with baffle plate.But in actual moving process, the knockout drum of traditional design has occurred that such as floor space is large, and not easy of integration, overhead-liquid easily spills, and liquid fluctuating is comparatively large, and liquid level gauge is measured and easily occurred the problems such as relatively large deviation.
With reference to shown in Fig. 2: the horizontal percussion flow moisture trap of the present invention, it comprises knockout drum tank body 1, refluence baffle plate 2 is provided with in described knockout drum tank body 1, the side of refluence baffle plate 2 is commutating zone 3, opposite side is impingement region 4, described commutating zone 3 is provided with gaseous phase outlet 10, overfall 5, liquid level gauge 6 and liquid-phase outlet 7; Described impingement region 4 is provided with two air-water two phase flow outlets 8, is welded with air inlet pipe 9 at the soldering opening place of described air-water two phase flow outlet 8; The opening of the air-water two phase flow outlet 8 described in two is arranged in correspondence with each other; Described knockout drum tank body 1 has some water in advance, and the horizontal plane of described water is positioned at below described knockout drum tank body 1 center line; Described refluence baffle plate 2 welded top is on separation tank body 1, and the bottom of described refluence baffle plate 2 does not separate bottom tank 1; Described refluence baffle plate 2 is divided into two sections, and epimere is airflow layer, and described airflow layer is cavernous structure 2-1, and hypomere is anti-ripple layer, and described anti-ripple layer is steel plate structure 2-2; The bottom of described anti-ripple layer is positioned at below described horizontal plane, and the top of described anti-ripple layer is positioned at above described horizontal plane; Described horizontal plane is positioned at the below of described center line.
And the two-part subregion of horizontal percussion flow moisture trap disclosed in this patent and the design of special flow apron 2 can solve the problem preferably: when gas-liquid two-phase flows through after air inlet pipe 9 enters tank body, fluid dynamic energy is discharged owing to mutually clashing into; Flow apron 2 bottom is inserted in liquid level, makes gas-water separation upper back gas flow in commutating zone 3 by deflector 2, and the liquid after being separated then keeps liquid level consistent by bottom UNICOM with commutating zone 3.
Two-part subregion and the special flow apron 2 of knockout drum of the present invention design, and greatly reduce the gas-liquid fluctuation of commutating zone 3, drop is not easily gone out, and liquid level gauge 6 are measured more accurate.The top that vacuum pump body is arranged in cooler is close to by knockout drum of the present invention, vavuum pump low in energy consumption, and vavuum pump integrated size is little, saves space and floor space, equipment conveying and arrangement convenience.
Other unspecified part is prior art.
Claims (1)
1. horizontal percussion flow moisture trap, is characterized in that: it comprises knockout drum tank body (1), is provided with refluence baffle plate (2) in described knockout drum tank body (1); The side of refluence baffle plate (2) is commutating zone (3), and opposite side is impingement region (4); Described commutating zone (3) is provided with gaseous phase outlet (10), overfall (5), liquid level gauge (6) and liquid-phase outlet (7); Described impingement region (4) is provided with two air-water two phase flows outlet (8), in the outlet of described air-water two phase flow, (8) place is welded with air inlet pipe (9); The opening of air-water two phase flow outlet (8) described in two is oppositely arranged; Have water in described knockout drum tank body (1), the horizontal plane of described water is positioned at below described knockout drum tank body (1) center line; Described refluence baffle plate (2) welded top is in separation tank body (1), and interval is arranged at the bottom of described refluence baffle plate (2) and knockout drum tank body (1) bottom; Described refluence baffle plate (2) is divided into two sections, and epimere is airflow layer, and described airflow layer is cavernous structure (2-1), and hypomere is anti-ripple layer, and described anti-ripple layer is steel plate structure (2-2); The bottom of described anti-ripple layer is positioned at below described horizontal plane, and the top of described anti-ripple layer is positioned at above described horizontal plane; Described horizontal plane is positioned at the below of described center line.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510134656.7A CN104771961B (en) | 2015-03-26 | 2015-03-26 | Horizontal percussion flow air water separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510134656.7A CN104771961B (en) | 2015-03-26 | 2015-03-26 | Horizontal percussion flow air water separator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104771961A true CN104771961A (en) | 2015-07-15 |
| CN104771961B CN104771961B (en) | 2016-06-15 |
Family
ID=53613919
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510134656.7A Active CN104771961B (en) | 2015-03-26 | 2015-03-26 | Horizontal percussion flow air water separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104771961B (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107741777A (en) * | 2017-11-02 | 2018-02-27 | 曙光节能技术（北京）股份有限公司 | Cooling system and liquid cooled server for server |
| CN108097177A (en) * | 2016-11-25 | 2018-06-01 | 中国石油化工股份有限公司 | It is a kind of that there is subtracting for incrustation sediment function to rush equal flow table |
| CN112322344A (en) * | 2020-10-22 | 2021-02-05 | 青岛理工大学 | Pipe network rod electrode squirrel cage array three-stage degassing and dehydration device |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2648068Y (en) * | 2003-10-03 | 2004-10-13 | 胜利油田胜利工程设计咨询有限责任公司 | High efficiency three phase separating device |
| CN1569663A (en) * | 2004-05-12 | 2005-01-26 | 胜利油田胜利工程设计咨询有限责任公司 | Integrated device for separation of oil-field production liquid and treatment of sewage |
| CN102120103A (en) * | 2011-01-27 | 2011-07-13 | 宁波威瑞泰默赛多相流仪器设备有限公司 | Gas-oil-water three-phase separator |
| CN102872617A (en) * | 2012-09-24 | 2013-01-16 | 森松(江苏)海油工程装备有限公司 | Demountable rectifying device of horizontal triphase separator |
| CN203577476U (en) * | 2013-10-29 | 2014-05-07 | 中国石油化工集团公司 | Hydrogen sulfide-resistant and acid corrosion-resistant water diversion separator |
| CN203763912U (en) * | 2014-03-31 | 2014-08-13 | 华东理工大学 | Three-phase separation device |
| CN204502586U (en) * | 2015-03-26 | 2015-07-29 | 中国电力工程顾问集团中南电力设计院有限公司 | Horizontal percussion flow moisture trap |
-
2015
- 2015-03-26 CN CN201510134656.7A patent/CN104771961B/en active Active
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2648068Y (en) * | 2003-10-03 | 2004-10-13 | 胜利油田胜利工程设计咨询有限责任公司 | High efficiency three phase separating device |
| CN1569663A (en) * | 2004-05-12 | 2005-01-26 | 胜利油田胜利工程设计咨询有限责任公司 | Integrated device for separation of oil-field production liquid and treatment of sewage |
| CN102120103A (en) * | 2011-01-27 | 2011-07-13 | 宁波威瑞泰默赛多相流仪器设备有限公司 | Gas-oil-water three-phase separator |
| CN102872617A (en) * | 2012-09-24 | 2013-01-16 | 森松(江苏)海油工程装备有限公司 | Demountable rectifying device of horizontal triphase separator |
| CN203577476U (en) * | 2013-10-29 | 2014-05-07 | 中国石油化工集团公司 | Hydrogen sulfide-resistant and acid corrosion-resistant water diversion separator |
| CN203763912U (en) * | 2014-03-31 | 2014-08-13 | 华东理工大学 | Three-phase separation device |
| CN204502586U (en) * | 2015-03-26 | 2015-07-29 | 中国电力工程顾问集团中南电力设计院有限公司 | Horizontal percussion flow moisture trap |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108097177A (en) * | 2016-11-25 | 2018-06-01 | 中国石油化工股份有限公司 | It is a kind of that there is subtracting for incrustation sediment function to rush equal flow table |
| CN107741777A (en) * | 2017-11-02 | 2018-02-27 | 曙光节能技术（北京）股份有限公司 | Cooling system and liquid cooled server for server |
| CN112322344A (en) * | 2020-10-22 | 2021-02-05 | 青岛理工大学 | Pipe network rod electrode squirrel cage array three-stage degassing and dehydration device |
Also Published As
| Publication number | Publication date |
|---|---|
| CN104771961B (en) | 2016-06-15 |
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