CN202569810U - Gas-liquid separation cylinder - Google Patents
Gas-liquid separation cylinder Download PDFInfo
- Publication number
- CN202569810U CN202569810U CN 201220112272 CN201220112272U CN202569810U CN 202569810 U CN202569810 U CN 202569810U CN 201220112272 CN201220112272 CN 201220112272 CN 201220112272 U CN201220112272 U CN 201220112272U CN 202569810 U CN202569810 U CN 202569810U
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- liquid
- gas
- liquid separation
- tube
- cylinder
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Abstract
The utility model relates to chemical equipment, in particular to a gas-liquid separation cylinder, and aims to provide a device which has a simple structure, is simple and convenient to operate and achieves the gas-liquid separation effect by utilizing the centrifugal force. The gas-liquid separation cylinder disclosed by the utility model comprises a barrel; the lower end of the barrel is connected with a liquid outlet pipe; the upper end of the barrel is provided with a gas outlet pipe; a liquid separation cylinder of which the upper and lower parts are open is arranged in the barrel; an inner cylinder is arranged in the liquid separation cylinder; a baffle is fixed on the inner wall of the liquid separation cylinder; the lower end of the inner cylinder is blocked by the baffle; the side wall of the lower end of the inner cylinder is provided with a gas outlet hole; liquid dropping holes are uniformly distributed in the baffle between the liquid separation cylinder and the inner cylinder; a gas liquid inlet pipe passes through the upper end of the barrel to be communicated with the inner cylinder; a rotational flow plate is arranged between the liquid separation cylinder and the inner cylinder; a spiral gas guide slot is formed by the rotational flow plate, the inner wall of the liquid separation cylinder and the inner cylinder; and the cylinder wall of the liquid separation cylinder is provided with a liquid collection hole communicated with the spiral gas guide slot. According to the utility model, the centrifugal force can be utilized to separate gas from liquid.
Description
Technical field
The utility model relates to a kind of chemical industry equipment, particularly relates to a kind of gas-liquid separation device.
Background technology
Gas-liquid separation device is one of chemical producing system process device commonly used; For the gas-liquid mixture that gets into container can effectively be separated; Normally used separator adopts first separation promptly to reduce the difference of flow velocity, gas-liquid density mostly and achieves the above object; So just make that device diameters and volume are big, the equipment investment expense is high, gas-liquid separation effect does not often reach designing requirement yet simultaneously, influences product quality.
The utility model content
The utility model provide a kind of simple in structure, easy and simple to handle, utilize centrifugal force to reach the device of gas-liquid separation.
The utility model gas-liquid separation tube comprises cylindrical shell, and said cylindrical shell lower end connects drain pipe; The upper end offers gas and goes out pipe, and the liquid separatnig tube of upper and lower opening is set in the said cylindrical shell, in the said liquid separatnig tube inner core is set; Baffle plate is fixed on the inwall of liquid separatnig tube; The said inner core of said baffle plate shutoff lower end, said inner core lower end sidewall is provided with venthole, even distribution dripping hole on the baffle plate between said liquid separatnig tube and the said inner core; The gas-liquid inlet tube passes said cylindrical shell upper end and said inner core is communicated with; Between said liquid separatnig tube and the said inner core eddy flow plate is set, said eddy flow plate and said liquid separatnig tube inwall and inner tank theca form the spiral air-conducting groove, and said liquid separatnig tube barrel is provided with the liquid collecting hole that is communicated with the spiral stream guidance groove.
Earlier be provided with the eddy flow plate than the utility model with prior art, the spiral stream guidance groove of eddy flow plate throws away droplet under action of centrifugal force when gas-liquid is rotated in groove from liquid collecting hole, reached the purpose of gas-liquid separation.
The utility model gas-liquid separation tube, wherein said shunting tube top and bottom respectively are fixed on the said cylinder inboard wall through three fixed blocks.Adopting this kind structure is for not only can economical with materials, and can make the liquid that throws away from liquid collecting hole flow to drain pipe from the space beyond the fixed block.
The utility model gas-liquid separation tube, wherein said cylindrical shell lower end is taper.Adopting this kind structure is for liquid is compiled in the cylindrical shell lower end more easily.
Be described further below in conjunction with the gas-liquid separation tube of accompanying drawing the utility model.
Description of drawings
Fig. 1 is the utility model gas-liquid separation tube cutaway view.
The specific embodiment
As shown in Figure 1, comprise cylindrical shell 1, cylindrical shell 1 lower end is a taper connection drain pipe 2; The upper end offers gas and goes out pipe 7, and the liquid separatnig tube 3 of upper and lower opening is set in the cylindrical shell 1, and shunting tube 3 top and bottom respectively are fixed on cylindrical shell 1 inwall through three fixed blocks 10; Inner core 4 is set in the liquid separatnig tube 3, and baffle plate 6 is fixed on the inwall of liquid separatnig tube 3, baffle plate 6 shutoff inner cores 4 lower ends; Inner core 4 lower end sidewalls are provided with venthole 11; Even distribution dripping hole 12 on the baffle plate 6 between liquid separatnig tube 3 and the inner core 4, gas-liquid inlet tube 5 pass cylindrical shell 1 upper end and inner core 4 is communicated with, and between liquid separatnig tube 3 and the inner core 4 eddy flow plate 8 is set; Eddy flow plate 8 forms the spiral air-conducting groove with liquid separatnig tube 3 inwalls and inner core 4 outer walls, and liquid separatnig tube 3 barrels are provided with the liquid collecting hole 9 that is communicated with the spiral stream guidance groove.The utility model gas-liquid mixture in use gets into inner core 4, gas-liquid chance baffle plate 6 change directions from venthole 11 outflows from the gas-liquid inlet tube; Few partially liq flows out through liquid drain pipe 2 along liquid separatnig tube 3 from baffle plate 6 dripping holes 12 are descending under the deadweight situation; Most of gas-liquid is up walked along eddy flow plate 8, gas-liquid in the spiral stream guidance groove under the centrifugal action liquid throw away from liquid collecting hole 9, gas goes out pipe 7 and discharges along eddy flow plate 8 directions from gas; Because fluid density is greater than gas density; Liquid flows out through drain pipe 2 from liquid collecting hole 9 outflows and descending along the space between cylindrical shell 1 and the liquid separatnig tube 3 of liquid separatnig tube 3, has reached the purpose of gas-liquid separation.
Above-described embodiment describes the preferred implementation of the utility model; Be not that scope to the utility model limits; Under the prerequisite that does not break away from the utility model design spirit; Various distortion and improvement that those of ordinary skills make the technical scheme of the utility model all should fall in the definite protection domain of the utility model claims.
Claims (3)
1. gas-liquid separation tube; Comprise cylindrical shell (1), said cylindrical shell (1) lower end connects drain pipe (2), and the upper end offers gas and goes out pipe (7); The liquid separatnig tube (3) of upper and lower opening is set in the said cylindrical shell (1); Inner core (4) is set in the said liquid separatnig tube (3), and baffle plate (6) is fixed on the inwall of liquid separatnig tube (3), the said inner core of said baffle plate (6) shutoff (4) lower end; Said inner core (4) lower end sidewall is provided with venthole (11); Baffle plate (6) between said liquid separatnig tube (3) and the said inner core (4) is gone up even distribution dripping hole (12), and gas-liquid inlet tube (5) passes said cylindrical shell (1) upper end and said inner core (4) is communicated with, and it is characterized in that: between said liquid separatnig tube (3) and the said inner core (4) eddy flow plate (8) is set; Said eddy flow plate (8) forms the spiral air-conducting groove with said liquid separatnig tube (3) inwall and inner core (4) outer wall, and said liquid separatnig tube (3) barrel is provided with the liquid collecting hole (9) that is communicated with the spiral stream guidance groove.
2. gas-liquid separation tube according to claim 1 is characterized in that: said shunting tube (3) top and bottom respectively are fixed on said cylindrical shell (1) inwall through three fixed blocks (10).
3. gas-liquid separation tube according to claim 2 is characterized in that: said cylindrical shell (1) lower end is taper.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220112272 CN202569810U (en) | 2012-03-22 | 2012-03-22 | Gas-liquid separation cylinder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220112272 CN202569810U (en) | 2012-03-22 | 2012-03-22 | Gas-liquid separation cylinder |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202569810U true CN202569810U (en) | 2012-12-05 |
Family
ID=47239267
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220112272 Expired - Fee Related CN202569810U (en) | 2012-03-22 | 2012-03-22 | Gas-liquid separation cylinder |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202569810U (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103285706A (en) * | 2013-06-28 | 2013-09-11 | 广西大学 | High-pressure separator for compression and liquefaction of supercritical carbon dioxide from methane |
| CN103691238A (en) * | 2013-12-17 | 2014-04-02 | 成都展望能源机械有限公司 | Spiral oil-gas separator for natural gas |
| CN103691232A (en) * | 2013-12-17 | 2014-04-02 | 成都展望能源机械有限公司 | Natural gas oil-gas separator with inverted circular truncated cone-shaped filter element |
| CN104107611A (en) * | 2013-04-16 | 2014-10-22 | 袁建华 | Screw expander oil and gas separator |
| CN105032101A (en) * | 2015-08-28 | 2015-11-11 | 湖南九鼎科技（集团）永州鼎立饲料有限公司 | Compressed air filter |
| CN107446625A (en) * | 2017-09-08 | 2017-12-08 | 新奥科技发展有限公司 | A kind of gasification furnace |
| CN108543385A (en) * | 2018-06-13 | 2018-09-18 | 苏州颇澳德克过滤系统科技有限公司 | A kind of gas-liquid separation device |
| CN108786282A (en) * | 2018-06-15 | 2018-11-13 | 淮阴工学院 | High temperature high pressure liquid recycles storage tank |
| CN110523095A (en) * | 2018-05-24 | 2019-12-03 | 中国石油化工集团有限公司 | Self weight eddy flow vapour liquid separator in vertical tube falling evaporator |
-
2012
- 2012-03-22 CN CN 201220112272 patent/CN202569810U/en not_active Expired - Fee Related
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104107611A (en) * | 2013-04-16 | 2014-10-22 | 袁建华 | Screw expander oil and gas separator |
| CN103285706B (en) * | 2013-06-28 | 2015-10-07 | 广西大学 | The high-pressure separator that biogas supercritical carbon dioxide compresses and liquefies |
| CN103285706A (en) * | 2013-06-28 | 2013-09-11 | 广西大学 | High-pressure separator for compression and liquefaction of supercritical carbon dioxide from methane |
| CN103691238B (en) * | 2013-12-17 | 2016-01-13 | 成都展望能源机械有限公司 | Spiral gas in natural gas separator |
| CN103691238A (en) * | 2013-12-17 | 2014-04-02 | 成都展望能源机械有限公司 | Spiral oil-gas separator for natural gas |
| CN103691232A (en) * | 2013-12-17 | 2014-04-02 | 成都展望能源机械有限公司 | Natural gas oil-gas separator with inverted circular truncated cone-shaped filter element |
| CN103691232B (en) * | 2013-12-17 | 2015-09-09 | 成都展望能源机械有限公司 | A kind of gas in natural gas separator with inverted round stage filter core |
| CN105032101A (en) * | 2015-08-28 | 2015-11-11 | 湖南九鼎科技（集团）永州鼎立饲料有限公司 | Compressed air filter |
| CN107446625A (en) * | 2017-09-08 | 2017-12-08 | 新奥科技发展有限公司 | A kind of gasification furnace |
| CN110523095A (en) * | 2018-05-24 | 2019-12-03 | 中国石油化工集团有限公司 | Self weight eddy flow vapour liquid separator in vertical tube falling evaporator |
| CN108543385A (en) * | 2018-06-13 | 2018-09-18 | 苏州颇澳德克过滤系统科技有限公司 | A kind of gas-liquid separation device |
| CN108543385B (en) * | 2018-06-13 | 2023-12-19 | 苏州颇澳德克过滤系统科技有限公司 | Gas-liquid separation device |
| CN108786282A (en) * | 2018-06-15 | 2018-11-13 | 淮阴工学院 | High temperature high pressure liquid recycles storage tank |
| CN108786282B (en) * | 2018-06-15 | 2021-05-11 | 淮阴工学院 | High-temperature high-pressure liquid recovery storage tank |
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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: 20121205 Termination date: 20130322 |