CN204294066U - A kind of efficient cyclone utilizing cyclonic action to carry out gas-liquid separation - Google Patents
A kind of efficient cyclone utilizing cyclonic action to carry out gas-liquid separation Download PDFInfo
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- CN204294066U CN204294066U CN201420727948.2U CN201420727948U CN204294066U CN 204294066 U CN204294066 U CN 204294066U CN 201420727948 U CN201420727948 U CN 201420727948U CN 204294066 U CN204294066 U CN 204294066U
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- liquid
- gas
- liquid separation
- cyclonic action
- jet
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Abstract
The utility model provides a kind of efficient cyclone utilizing cyclonic action to carry out gas-liquid separation, comprise separator shell, Separate System of Water-jet and liquid separation system, it is inner that described Separate System of Water-jet and described liquid separation system are all included in described separator shell, described Separate System of Water-jet is connected with described liquid separation system, and described Separate System of Water-jet is positioned at the upper end of described liquid separation system.The beneficial effects of the utility model are the separation utilizing cyclonic action to realize gas-liquid; effectively improve the separative efficiency of gas-liquid; in addition liquid separating appts add the integration achieving gas-liquid separation and fluid separation applications; simplify the workflow of gas-liquid separation; effectively improve operating efficiency; solve and control liquid level difficulty, and often can cause the problem that gas circuit string oil or oil circuit are collaborated.
Description
Technical field
The utility model belongs to chemical materials process field, especially relates to a kind of efficient cyclone utilizing cyclonic action to carry out gas-liquid separation.
Background technology
In existing technology; common separator carries out gas-liquid separation by sedimentation; utilize the Action of Gravity Field of liquid; the separation of gas-liquid is carried out through long sedimentation; which results in the problem that container is larger, the processing time is long of separator; and common separator controls liquid level difficulty, the phenomenon such as often can cause that gas circuit string oil or oil circuit are collaborated.
Summary of the invention
The purpose of this utility model is to provide a kind of efficient cyclone utilizing cyclonic action to carry out gas-liquid separation, the eddy flow that this separator utilizes rotary body to produce, import gas liquid mixture with eddy flow tangential direction, realize being separated under cyclonic action, effectively improve the separative efficiency of gas-liquid.
For reaching above-mentioned purpose, the technical solution adopted in the utility model is: a kind of efficient cyclone utilizing cyclonic action to carry out gas-liquid separation, comprise separator shell, Separate System of Water-jet and liquid separation system, it is characterized in that: it is inner that described Separate System of Water-jet and described liquid separation system are all included in described separator shell, described Separate System of Water-jet is connected with described liquid separation system, described Separate System of Water-jet is positioned at the upper end of described liquid separation system, described separator shell comprises box hat, gas feed, inlet control valve, clean gas outlet, discharge control valve, light oil outlet, light oil control valve, impurity outlet and impurity discharge control valve, described gas feed is arranged on the position of the side, below of described box hat by described inlet control valve, described clean gas outlet is arranged on the top of described box hat by described discharge control valve, described light oil outlet is arranged on the side, bottom of described box hat by described light oil control valve, described impurity outlet discharges by described impurity the bottom opposite side that control valve is arranged on described box hat, described Separate System of Water-jet comprises pre-filtering chamber, filter chamber baffle plate, pre-filtering conduit, liquid backflow plate, second liquid refluxing opening, cyclonic action device, rotating shaft, drive motors, gas baffle and gas egress filtering core, described pre-filtering chamber is connected with described filter chamber baffle plate side, first liquid refluxing opening is provided with below described filter chamber baffle plate, described filter chamber baffle plate opposite side is connected with described pre-filtering conduit, described pre-filtering conduit stretches in described cyclonic action device through described liquid backflow plate, liquid collection storehouse is provided with below described cyclonic action device, described liquid collection storehouse surrounding is connected with described liquid backflow plate, lower end, described liquid collection storehouse is connected with described second liquid refluxing opening, described cyclonic action device is connected with described drive motors by described rotating shaft, described drive motors is fixed on described gas baffle, described gas baffle is provided with the first gas passage and the second gas passage, filter course is provided with above described gas baffle, described filter course side is provided with pressure detector, described gas vent filtration core is coated on described clean gas outlet, described Separate System of Water-jet is connected with described liquid separation system with described second liquid refluxing opening by described first liquid refluxing opening, described liquid separation system comprises fluid storage storehouse, first baffle plate and liquid height alarm, described fluid storage storehouse is connected with described first baffle plate side, described first baffle plate opposite side is provided with second baffle, spatial transition is formed in the middle of described first baffle plate and described second baffle, described spatial transition bottom is provided with Weight retainer, described liquid height alarm is arranged on top, described fluid storage storehouse, described liquid separation system is connected with described separator shell with described impurity outlet by described light oil outlet.
Further, described pre-filtering conduit is stretched in described cyclonic action device by the tangential direction of inclination angle pipeline upwards along special angle.
Further, described cyclonic action device rotates relative to described separator shell under the effect of described drive motors.
Particularly, described liquid backflow plate surface is the recess structure of rule, avoids separating liquid and described liquid backflow plate to adhere to.
Particularly, described filter course is fibrous glass filter course, described filter course filtration pore is from the bottom to top arranged from large to small, and liquid pearl is coalescent gradually in described filter course to grow up, and can split away off when drop reaches certain size because of the percussion of air-flow from inner surface.
The advantage that the utility model has and good effect are: owing to adopting technique scheme; utilize the effect of eddy flow by gas-liquid separation; with traditional gravity separator ratio; substantially increase separative efficiency; the adding of liquid separation system in addition; effectively light oil can be extracted from the liquid separated; eliminate the step that liquid is separated again; greatly reduce technological process; improve operating efficiency; solve and control liquid level difficulty, and often can cause the problem that gas circuit string oil or oil circuit are collaborated.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
In figure: 1, separator shell; 1-1, box hat; 1-2, gas feed; 1-3, inlet control valve; 1-4, clean gas outlet; 1-5, discharge control valve; 1-6, light oil outlet; 1-7, light oil control valve; 1-8, impurity outlet; 1-9 impurity discharges control valve; 2, Separate System of Water-jet; 2-1, pre-filtering chamber; 2-2, filter chamber baffle plate; 2-3, first liquid refluxing opening; 2-4, pre-filtering conduit; 2-5, liquid collection storehouse; 2-6, liquid backflow plate; 2-7, second liquid refluxing opening; 2-8, cyclonic action device; 2-9, rotating shaft; 2-10, drive motors; 2-11, gas baffle; 2-12, the first gas passage; 2-13, the second gas passage; 2-14, filter course; 2-15, pressure detector; 2-16, gas vent filtration core; 3, liquid separation system; 3-1, fluid storage storehouse; 3-2, the first baffle plate; 3-3, second baffle; 3-4, spatial transition; 3-5, Weight retainer; 3-6, liquid height alarm.
Detailed description of the invention
Contrast accompanying drawing below, by the description to embodiment, to detailed description of the invention of the present utility model, effect and operation principle etc. as the mutual alignment between the shape of involved each component, structure, each several part and annexation, each several part are described in further detail.
Embodiment one: as shown in Figure 1, the utility model provides a kind of efficient cyclone utilizing cyclonic action to carry out gas-liquid separation, comprise separator shell 1, Separate System of Water-jet 2 and liquid separation system 3, it is inner that Separate System of Water-jet 2 and liquid separation system 3 are all included in separator shell 1, Separate System of Water-jet 2 is connected with liquid separation system 3, Separate System of Water-jet 2 is positioned at the upper end of liquid separation system 3, separator shell 1 comprises box hat 1-1, gas feed 1-2, inlet control valve 1-3, clean gas outlet 1-4, discharge control valve 1-5, light oil outlet 1-6, light oil control valve 1-7, impurity outlet 1-8 and impurity discharge control valve 1-9, gas feed 1-2 is arranged on the position of the side, below of box hat 1-1 by inlet control valve 1-2, clean gas outlet 1-4 is arranged on the top of box hat 1-1 by discharge control valve 1-5, light oil outlet 1-6 is arranged on the side, bottom of box hat 1-1 by light oil control valve 1-7, impurity outlet 1-8 discharges by impurity the opposite side that control valve 1-9 is arranged on the bottom of box hat 1-1, Separate System of Water-jet 2 comprises pre-filtering chamber 2-1, filter chamber baffle plate 2-2, first liquid refluxing opening 2-3, pre-filtering conduit 2-4, liquid collection storehouse 2-5, liquid backflow plate 2-6, second liquid refluxing opening 2-7, cyclonic action device 2-8, rotating shaft 2-9, drive motors 2-10, gas baffle 2-11, first gas passage 2-12, second gas passage 2-13, filter course 2-14, pressure detector 2-15 and gas egress filtering core 2-16, pre-filtering chamber 2-1 is connected with filter chamber baffle plate 2-2 side, first liquid refluxing opening 2-3 is provided with below filter chamber baffle plate 2-2, filter chamber baffle plate 2-2 opposite side is connected with pre-filtering conduit 2-4, pre-filtering conduit 2-4 stretches in cyclonic action device 2-8 through liquid backflow plate 2-6, liquid collection storehouse 2-5 is provided with below cyclonic action device 2-8, liquid collection storehouse 2-5 surrounding is connected with liquid backflow plate 2-6, 2-5 lower end, liquid collection storehouse is connected with second liquid refluxing opening 2-7, cyclonic action device 2-8 is connected with drive motors 2-10 by rotating shaft 2-9, drive motors 2-10 is fixed on gas baffle 2-11, gas baffle 2-11 is provided with the first gas passage 2-12 and the second gas passage 2-13, filter course 2-14 is provided with above gas baffle 2-11, filter course 2-14 side is provided with pressure detector 2-15, gas vent filtration core 2-16 is coated on clean gas outlet 1-4, Separate System of Water-jet 2 is connected with liquid separation system 3 with second liquid refluxing opening 2-7 by first liquid refluxing opening 2-3, liquid separation system 3 comprises fluid storage storehouse 3-1, first baffle plate 3-2, second baffle 3-3, spatial transition 3-4, Weight retainer 3-5 and liquid height alarm 3-6, fluid storage storehouse 3-1 is connected with the first baffle plate 3-2 side, first baffle plate 3-2 opposite side is provided with second baffle 3-3, spatial transition 3-4 is formed in the middle of first baffle plate 3-2 and second baffle 3-3, spatial transition 3-4 bottom is provided with Weight retainer 3-5, liquid height alarm 3-6 is arranged on 3-1 top, fluid storage storehouse, liquid separation system 3 is connected with separator shell 1 with impurity outlet 1-8 by light oil outlet 1-6.Pre-filtering conduit 2-4 is stretched in cyclonic action device 2-8 by the tangential direction of inclination angle pipeline upwards along special angle.Cyclonic action device 2-8 relative separation device shell 1 under the effect of drive motors 2-10 rotates.Liquid backflow plate 2-6 surface is set to the recess structure of rule, avoids separating liquid and liquid backflow plate 2-6 to adhere to.Filter course 2-14 is fibrous glass filter course, and filter course 2-14 filtration pore is from the bottom to top more and more less, and liquid pearl is coalescent gradually in filter course 2-14 to grow up, and can split away off when drop reaches certain size because of the percussion of air-flow from inner surface.
The course of work of this example: gas liquid mixture enters into pre-filtering chamber 2-1 by gas feed 1-2, under the effect of filter chamber baffle plate 2-2, gas is stopped change circulating direction, a part of fluid separation applications out under gravity, after the 2-1 of pre-filtering chamber, by pre-filtering conduit 2-4, gas is sent in cyclonic action device 2-8 with eddy flow tangential direction, under cyclonic action, gas-liquid realizes being separated, liquid is beaten on cyclonic action device 2-8 sidewall, then fall in the 2-5 of liquid collection storehouse, be back in the 3-1 of fluid storage storehouse through second liquid refluxing opening 2-7, the first gas passage 2-12 of gas on gas baffle 2-11 be separated through cyclonic action device 2-8 and the second gas passage 2-13 discharges, the gas of discharging is in the filtration carrying out fine liquid molecule through filter course 2-14, gas after filtration completes whole gas-liquid separation through the effect of gas vent filtration core 2-16 again, and the liquid separated is back in the 3-1 of fluid storage storehouse through first liquid refluxing opening 2-3 and second liquid refluxing opening 2-7, under the effect of force density, liquid realizes layering, along with continuous accumulation and the layering of liquid, some light oils float on the surface, when light oil liquid level is more than the first baffle plate 3-2, light oil overflows across the first baffle plate 3-2 and enters in spatial transition 3-4, after spatial transition is filled up by light oil, light oil will overflow across second baffle 3-3, and then realize the separation again of liquid.
Above embodiment of the present utility model has been described in detail, but described content being only preferred embodiment of the present utility model, can not being considered to for limiting practical range of the present utility model.All equalizations done according to the utility model application range change and improve, and all should still belong within patent covering scope of the present utility model.
Claims (5)
1. the efficient cyclone utilizing cyclonic action to carry out gas-liquid separation, comprise separator shell, Separate System of Water-jet and liquid separation system, it is characterized in that: it is inner that described Separate System of Water-jet and described liquid separation system are all included in described separator shell, described Separate System of Water-jet is connected with described liquid separation system, described Separate System of Water-jet is positioned at the upper end of described liquid separation system, described separator shell comprises box hat, gas feed, inlet control valve, clean gas outlet, discharge control valve, light oil outlet, light oil control valve, impurity outlet and impurity discharge control valve, described gas feed is arranged on the position of the side, below of described box hat by described inlet control valve, described clean gas outlet is arranged on the top of described box hat by described discharge control valve, described light oil outlet is arranged on the side, bottom of described box hat by described light oil control valve, described impurity outlet discharges by described impurity the bottom opposite side that control valve is arranged on described box hat, described Separate System of Water-jet comprises pre-filtering chamber, filter chamber baffle plate, pre-filtering conduit, liquid backflow plate, second liquid refluxing opening, cyclonic action device, rotating shaft, drive motors, gas baffle and gas egress filtering core, described pre-filtering chamber is connected with described filter chamber baffle plate side, first liquid refluxing opening is provided with below described filter chamber baffle plate, described filter chamber baffle plate opposite side is connected with described pre-filtering conduit, described pre-filtering conduit stretches in described cyclonic action device through described liquid backflow plate, liquid collection storehouse is provided with below described cyclonic action device, described liquid collection storehouse surrounding is connected with described liquid backflow plate, lower end, described liquid collection storehouse is connected with described second liquid refluxing opening, described cyclonic action device is connected with described drive motors by described rotating shaft, described drive motors is fixed on described gas baffle, described gas baffle is provided with the first gas passage and the second gas passage, filter course is provided with above described gas baffle, described filter course side is provided with pressure detector, described gas vent filtration core is coated on described clean gas outlet, described Separate System of Water-jet is connected with described liquid separation system with described second liquid refluxing opening by described first liquid refluxing opening, described liquid separation system comprises fluid storage storehouse, first baffle plate and liquid height alarm, described fluid storage storehouse is connected with described first baffle plate side, described first baffle plate opposite side is provided with second baffle, spatial transition is formed in the middle of described first baffle plate and described second baffle, described spatial transition bottom is provided with Weight retainer, described liquid height alarm is arranged on top, described fluid storage storehouse, described liquid separation system is connected with described separator shell with described impurity outlet by described light oil outlet.
2. a kind of efficient cyclone utilizing cyclonic action to carry out gas-liquid separation according to claim 1, is characterized in that: described pre-filtering conduit is stretched in described cyclonic action device by the tangential direction of inclination angle pipeline upwards along special angle.
3. a kind of efficient cyclone utilizing cyclonic action to carry out gas-liquid separation according to claim 1, is characterized in that: described cyclonic action device rotates relative to described separator shell under the effect of described drive motors.
4. a kind of efficient cyclone utilizing cyclonic action to carry out gas-liquid separation according to claim 1, is characterized in that: described liquid backflow plate surface is the recess structure of rule.
5. a kind of efficient cyclone utilizing cyclonic action to carry out gas-liquid separation according to claim 1, is characterized in that: described filter course is fibrous glass filter course, and described filter course filtration pore is from the bottom to top arranged from large to small.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420727948.2U CN204294066U (en) | 2014-11-28 | 2014-11-28 | A kind of efficient cyclone utilizing cyclonic action to carry out gas-liquid separation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420727948.2U CN204294066U (en) | 2014-11-28 | 2014-11-28 | A kind of efficient cyclone utilizing cyclonic action to carry out gas-liquid separation |
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| Publication Number | Publication Date |
|---|---|
| CN204294066U true CN204294066U (en) | 2015-04-29 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420727948.2U Expired - Fee Related CN204294066U (en) | 2014-11-28 | 2014-11-28 | A kind of efficient cyclone utilizing cyclonic action to carry out gas-liquid separation |
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| CN (1) | CN204294066U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104888560A (en) * | 2015-04-23 | 2015-09-09 | 刘洋 | Efficient separator using swirling flow effect to carry out gas-liquid separation |
| CN106823474A (en) * | 2017-02-07 | 2017-06-13 | 重庆科技学院 | A kind of application method of blood shunt device |
-
2014
- 2014-11-28 CN CN201420727948.2U patent/CN204294066U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104888560A (en) * | 2015-04-23 | 2015-09-09 | 刘洋 | Efficient separator using swirling flow effect to carry out gas-liquid separation |
| CN106823474A (en) * | 2017-02-07 | 2017-06-13 | 重庆科技学院 | A kind of application method of blood shunt device |
| CN106823474B (en) * | 2017-02-07 | 2023-01-24 | 重庆科技学院 | Application method of blood shunt |
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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: 20150429 Termination date: 20151128 |