CN203591665U - Gas-liquid separation mechanism for spiral tube - Google Patents
Gas-liquid separation mechanism for spiral tube Download PDFInfo
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- CN203591665U CN203591665U CN201320769363.2U CN201320769363U CN203591665U CN 203591665 U CN203591665 U CN 203591665U CN 201320769363 U CN201320769363 U CN 201320769363U CN 203591665 U CN203591665 U CN 203591665U
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- gas
- helix tube
- cylindrical shell
- liquid
- liquid separation
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Abstract
The utility model discloses a gas-liquid separation mechanism for a spiral tube. The gas-liquid separation mechanism comprises a cylinder body, wherein the spiral tube is mounted in the cylinder body; the spiral tube is coaxial with the cylinder body; a mixed gas-liquid inlet is formed in the cylinder body; an air outlet is formed in the top of the cylinder body; a liquid outlet is formed in one side of the bottom end of the cylinder body; the upper end of the spiral tube is connected with the mixed gas-liquid inlet; the lower end of the spiral tube is connected with a divider; the rotating radius of the spiral tube is 150-200 mm; apertures are formed in the inner upper side of the spiral tube; the gas-liquid separation mechanism further comprises a baffle plate; the baffle plate is mounted right above the spiral tube and connected with the inner wall of the cylinder body; a through hole is formed in the baffle plate; the through hole directly faces to the air outlet; a demisting mechanism is further mounted on the through hole. According to the gas-liquid separation mechanism, the rotating radius of the spiral tube is relatively small, so that the gas-liquid separation effect is effectively improved; the rotating radius of the spiral tube is set to be 150-200 mm, so that the separation effect is enabled to be best.
Description
Technical field
The utility model relates to a kind of gas-liquid separation mechanism, specifically refers to a kind of helix tube gas-liquid separation mechanism.
Background technology
Prepare natural gas or coal gas in petrochemical plant time, these gases are normally made gas-liquid under cryogenic conditions, and conventionally contain the impurity such as oil, water in the gas-liquid of preparation, thereby need to use gas and these impurity that gas-liquid separator is prepared needs to separate, make the gas purity that makes higher.But the not only complex structure of gas-liquid separator using in the market, is not easy to maintenance; And cost is higher, need to injects capital into more, thereby make troubles to user.
Utility model content
The purpose of this utility model is to overcome the not only complex structure of gas-liquid separator using in the market, is not easy to maintenance; And cost is higher, need to inject capital into more, thereby the defect of making troubles to user provides one not only simple in structure, is convenient to install and use, and gas-liquid separator with low cost.
The utility model is achieved through the following technical solutions:
A kind of helix tube gas-liquid separation of the utility model mechanism, comprise cylindrical shell, in described cylindrical shell, helix tube is installed, described helix tube is coaxial with cylindrical shell, on cylindrical shell, be provided with gas-liquid mixed import, top at cylindrical shell has venthole, in a side of cylindrical shell bottom, have liquid outlet, the upper end of described helix tube is connected with gas-liquid mixed import, lower end at helix tube is connected with current divider, the radius of turn of described helix tube is 150 ~ 200 ㎜, in described helix tube, upside has aperture, also comprise flow-stopping plate, described flow-stopping plate be arranged on helix tube directly over and be connected with cylinder inboard wall, on flow-stopping plate, have through hole, described through hole is just to venthole, demist mechanism is also installed on described through hole.The utility model adopts Gravity Separation with the dual separate mode of centrifugation, gas to be separated, and has improved separative efficiency, when work, gas-liquid mixture fluid enters into helix tube by gas-liquid mixed import, in helix tube, produce centrifugal acceleration, make fluid under the acting in conjunction of centrifugal force and gravity, the liquid that relative density is larger is assembled at the outer downside of helix tube, the gas that relative density is less is assembled at the interior upside of helix tube, most of gas of assembling flows out helix tube by the aperture of offering on helix tube, gas utilizes the effect of inertia after CENTRIFUGAL ACCELERATING, enter the demist mechanism on through hole, by demist mechanism, residual droplets in gas is removed, guarantee the purity of gas in venthole, the liquid flowing out in helix tube starts sedimentation under the shunting action of current divider, and in infall process, liquid, because gravity reason starts to sink down into cylinder body bottom, is discharged by liquid outlet, wherein, the radius of turn that reduces helix tube can effectively improve the separating effect of gas-liquid, and the radius of turn of helix tube is set to 150 ~ 200 ㎜, can make separating effect reach best, when the radius of turn of helix tube is during higher than 200 ㎜, the separating effect of gas-liquid is reduced gradually, when the radius of turn of helix tube is during lower than 150 ㎜, the time of staying of gas-liquid in helix tube shortens, and then causes the loss of an internal drop to increase, and the separating effect of gas-liquid reduces equally.
Described demist mechanism comprises corrugated sheet, support rail and the screen pack that multiple tile verticallies arrange, and the middle part of described corrugated sheet is tiltedly installed with side plate, and corrugated sheet is fixed on support rail, and screen pack is fixedly mounted on corrugated sheet.After centrifugation, the drop of the residual small part of meeting in effluent air from helix tube, under the double filtration of screen pack and corrugated sheet, drop is attached on corrugated sheet, has guaranteed the purity of effluent air from gas outlet.
Bottom at described cylindrical shell has sewage draining exit, on described sewage draining exit, is provided with check-valves.After long separation circuit, cylinder body bottom has accumulated more liquid residue, and by being arranged on the check-valves on sewage draining exit, staff can clear up inner barrel fast, to improve the job stability of separating mechanism.
The angle that described side plate becomes with corrugated sheet is 35 °～40 °.The side plate that the middle part of corrugated sheet arranges can be strengthened the cleaning to drop residual in gas, gas during by corrugated sheet side plate can stop it, after meeting with obstruction, can continue to flow by cut-through thing gas, drop residual in gas is adhered in skirt walls, drop finally falls into cylinder body bottom along skirt walls, and then completes the cleaning to residual drop; The angle that side plate becomes with corrugated sheet is 35 °～40 °, can guarantee the barrier effectiveness to drop, and don't can affect the circulation of gas.
The height of described helix tube is 450～550 ㎜.The height of helix tube can affect the efficiency of gas-liquid in centrifugation, highly be arranged between 450～550 ㎜, can make gas flow out helix tube by aperture in former circles of helix tube, reduce the residual quantity of gas in separator, greatly improve the effect of gas-liquid separation.
The utility model compared with prior art, has the following advantages and beneficial effect:
1, a kind of helix tube gas-liquid separation of the utility model mechanism, comprise cylindrical shell, in described cylindrical shell, helix tube is installed, described helix tube is coaxial with cylindrical shell, on cylindrical shell, be provided with gas-liquid mixed import, top at cylindrical shell has venthole, in a side of cylindrical shell bottom, have liquid outlet, the upper end of described helix tube is connected with gas-liquid mixed import, lower end at helix tube is connected with current divider, the radius of turn of described helix tube is 150 ~ 200 ㎜, in described helix tube, upside has aperture, also comprise flow-stopping plate, described flow-stopping plate be arranged on helix tube directly over and be connected with cylinder inboard wall, on flow-stopping plate, have through hole, described through hole is just to venthole, demist mechanism is also installed on described through hole, the radius of turn that reduces helix tube can effectively improve the separating effect of gas-liquid, the radius of turn of helix tube is set to 150 ~ 200 ㎜, can make separating effect reach best, when the radius of turn of helix tube is during higher than 200 ㎜, the separating effect of gas-liquid be reduced gradually, when the radius of turn of helix tube is during lower than 150 ㎜, the time of staying of gas-liquid in helix tube shortens, and then causes the loss of an internal drop to increase, and the separating effect of gas-liquid reduces equally.
2, a kind of helix tube gas-liquid separation of the utility model mechanism, after centrifugation, the drop of the residual small part of meeting in effluent air from helix tube, under the double filtration of screen pack and corrugated sheet, drop is attached on corrugated sheet, has guaranteed the purity of effluent air from gas outlet.
3, a kind of helix tube gas-liquid separation of the utility model mechanism, drop residual in gas is adhered in skirt walls, and drop finally falls into cylinder body bottom along skirt walls, and then completes the cleaning to residual drop; The angle that side plate becomes with corrugated sheet is 35 °～40 °, can guarantee the barrier effectiveness to drop, and don't can affect the circulation of gas.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Fig. 2 is the structural representation of demist mechanism;
Wherein, the parts title that Reference numeral is corresponding is as follows:
1-cylindrical shell, 2-helix tube, the import of 3-gas-liquid mixed, 4-venthole, 5-liquid outlet, 6-current divider, 7-aperture, 8-flow-stopping plate, 9-through hole, 10-demist mechanism, 11-sewage draining exit, 12-check-valves, 13-screen pack, 14-support rail, 15-corrugated sheet, 16-side plate.
The specific embodiment
Below in conjunction with embodiment, the utility model is described in further detail, but embodiment of the present utility model is not limited to this.
Embodiment
As Fig. 1, shown in 2, the utility model comprises cylindrical shell 1, in described cylindrical shell 1, helix tube 2 is installed, described helix tube 2 is coaxial with cylindrical shell 1, on cylindrical shell 1, be provided with gas-liquid mixed import 3, have venthole 4 at the top of cylindrical shell 1, in a side of cylindrical shell 1 bottom, have liquid outlet 5, the upper end of described helix tube 2 is connected with gas-liquid mixed import 3, be connected with current divider 6 in the lower end of helix tube 2, the radius of turn of described helix tube 2 is 150 ~ 200 ㎜, the interior upside of described helix tube 2 has aperture 7, also comprise flow-stopping plate 8, described flow-stopping plate 8 be arranged on helix tube 2 directly over and be connected with cylindrical shell 1 inwall, on flow-stopping plate 8, have through hole 9, described through hole 9 is just to venthole 4, on described through hole 9, demist mechanism 10 is also installed, described demist mechanism 10 comprises corrugated sheet 15, support rail 14 and the screen pack 13 that multiple tile verticallies arrange, and the middle part of described corrugated sheet 15 is tiltedly installed with side plate 16, and corrugated sheet 15 is fixed on support rail 14, and screen pack 13 is fixedly mounted on corrugated sheet 15, described side plate 16 is 35 °～40 ° with the angle of 15 one-tenth of corrugated sheets, the height of described helix tube 2 is 450～550 ㎜.
The utility model adopts Gravity Separation with the dual separate mode of centrifugation, gas to be separated, and has improved separative efficiency, when work, gas-liquid mixture fluid enters into helix tube 2 by gas-liquid mixed import 3, in helix tube 2, produce centrifugal acceleration, make fluid under the acting in conjunction of centrifugal force and gravity, the liquid that relative density is larger is assembled at the outer downside of helix tube 2, the gas that relative density is less is assembled at the interior upside of helix tube 2, most of gas of assembling flows out helix tube 2 by the aperture 5 of offering on helix tube 2, gas utilizes the effect of inertia after CENTRIFUGAL ACCELERATING, enter the demist mechanism 10 on through hole 9, by demist mechanism 10, residual droplets in gas is removed, guarantee the purity of gas in venthole 4, the liquid flowing out in helix tube 2 starts sedimentation under the shunting action of current divider 6, and in infall process, liquid, because gravity reason starts to sink down into cylindrical shell 1 bottom, is discharged by liquid outlet 5, wherein, the radius of turn that reduces helix tube 2 can effectively improve the separating effect of gas-liquid, and the radius of turn of helix tube 2 is set to 150 ~ 200 ㎜, can make separating effect reach best, when the radius of turn of helix tube 2 is during higher than 200 ㎜, the separating effect of gas-liquid is reduced gradually, when the radius of turn of helix tube 2 is during lower than 150 ㎜, the time of staying of gas-liquid in helix tube 2 shortens, and then causes the loss of an internal drop to increase, and the separating effect of gas-liquid reduces equally.
After centrifugation, the drop of the residual small part of meeting in effluent air from helix tube 2, under the double filtration of screen pack and corrugated sheet 15, drop is attached on corrugated sheet 15, has guaranteed the purity of effluent air from gas outlet 4; The side plate 16 that the middle part of corrugated sheet 15 arranges can be strengthened the cleaning to drop residual in gas, gas during by corrugated sheet 15 side plate 16 can stop it, after meeting with obstruction, can continue to flow by cut-through thing gas, in gas, residual drop is adhered on side plate 16 walls, drop finally falls into cylindrical shell 1 bottom along side plate 16 walls, and then completes the cleaning to residual drop; Side plate 16 is 35 °～40 ° with the angle of 15 one-tenth of corrugated sheets, can guarantee the barrier effectiveness to drop, and don't can affect the circulation of gas.
Have sewage draining exit 11 in the bottom of described cylindrical shell 1, on described sewage draining exit 11, be provided with check-valves 12.After long separation circuit, cylindrical shell 1 bottom has accumulated more liquid residue, and by being arranged on the check-valves 12 on sewage draining exit 11, staff can clear up cylindrical shell 1 inside fast, to improve the job stability of separating mechanism; Wherein, the height of helix tube 2 can affect the efficiency of gas-liquid in centrifugation, is highly arranged between 450～550 ㎜, can make gas flow out helix tube 2 by aperture 7 in former circles of helix tube 2, reduce the residual quantity of gas in separator, greatly improved the effect of gas-liquid separation.
As mentioned above, just can realize preferably the utility model.
Claims (5)
1. a helix tube gas-liquid separation mechanism, comprise cylindrical shell (1), helix tube (2) is installed in described cylindrical shell (1), described helix tube (2) is coaxial with cylindrical shell (1), on cylindrical shell (1), be provided with gas-liquid mixed import (3), have venthole (4) at the top of cylindrical shell (1), in a side of cylindrical shell (1) bottom, have liquid outlet (5), it is characterized in that: the upper end of described helix tube (2) is connected with gas-liquid mixed import (3), be connected with current divider (6) in the lower end of helix tube (2), the radius of turn of described helix tube (2) is 150 ~ 200 ㎜, the interior upside of described helix tube (2) has aperture (7), also comprise flow-stopping plate (8), described flow-stopping plate (8) be arranged on helix tube (2) directly over and be connected with cylindrical shell (1) inwall, on flow-stopping plate (8), have through hole (9), described through hole (9) is just to venthole (4), demist mechanism (10) is also installed on described through hole (9).
2. a kind of helix tube gas-liquid separation according to claim 1 mechanism, it is characterized in that: described demist mechanism (10) comprises corrugated sheet (15), support rail (14) and the screen pack (13) that multiple tile verticallies arrange, the middle part of described corrugated sheet (15) is tiltedly installed with side plate (16), it is upper that corrugated sheet (15) is fixed on support rail (14), and screen pack (13) is fixedly mounted on corrugated sheet (15).
3. a kind of helix tube gas-liquid separation according to claim 1 mechanism, is characterized in that: have sewage draining exit (11) in the bottom of described cylindrical shell (1), be provided with check-valves (12) on described sewage draining exit (11).
4. a kind of helix tube gas-liquid separation according to claim 2 mechanism, is characterized in that: the angle that described side plate (16) becomes with corrugated sheet (15) is 35 °～40 °.
5. according to a kind of helix tube gas-liquid separation mechanism described in claim 1～4 any one, it is characterized in that: the height of described helix tube (2) is 450～550 ㎜.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320769363.2U CN203591665U (en) | 2013-11-30 | 2013-11-30 | Gas-liquid separation mechanism for spiral tube |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320769363.2U CN203591665U (en) | 2013-11-30 | 2013-11-30 | Gas-liquid separation mechanism for spiral tube |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203591665U true CN203591665U (en) | 2014-05-14 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320769363.2U Expired - Fee Related CN203591665U (en) | 2013-11-30 | 2013-11-30 | Gas-liquid separation mechanism for spiral tube |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203591665U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103657313A (en) * | 2013-11-30 | 2014-03-26 | 成都科盛石油科技有限公司 | Gas-liquid separator |
| CN104043317A (en) * | 2014-07-08 | 2014-09-17 | 徐挺 | Filter pipe |
| CN105056639A (en) * | 2015-07-31 | 2015-11-18 | 四川金锋建设有限公司 | Spiral pipe gas-liquid separation method |
| CN111569581A (en) * | 2020-04-13 | 2020-08-25 | 北京空间飞行器总体设计部 | Gas-liquid separation device and separation method suitable for lunar gravity environment |
-
2013
- 2013-11-30 CN CN201320769363.2U patent/CN203591665U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103657313A (en) * | 2013-11-30 | 2014-03-26 | 成都科盛石油科技有限公司 | Gas-liquid separator |
| CN104043317A (en) * | 2014-07-08 | 2014-09-17 | 徐挺 | Filter pipe |
| CN104043317B (en) * | 2014-07-08 | 2016-02-03 | 徐挺 | Screen pipe |
| CN105056639A (en) * | 2015-07-31 | 2015-11-18 | 四川金锋建设有限公司 | Spiral pipe gas-liquid separation method |
| CN111569581A (en) * | 2020-04-13 | 2020-08-25 | 北京空间飞行器总体设计部 | Gas-liquid separation device and separation method suitable for lunar gravity environment |
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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 |
Granted publication date: 20140514 Termination date: 20141130 |
|
| EXPY | Termination of patent right or utility model |