CN108514798A - A kind of gas-liquid separation mechanism - Google Patents
A kind of gas-liquid separation mechanism Download PDFInfo
- Publication number
- CN108514798A CN108514798A CN201810608309.7A CN201810608309A CN108514798A CN 108514798 A CN108514798 A CN 108514798A CN 201810608309 A CN201810608309 A CN 201810608309A CN 108514798 A CN108514798 A CN 108514798A
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- Prior art keywords
- gas
- spirally
- tube body
- liquid separation
- separation mechanism
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- 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.)
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- 239000007788 liquid Substances 0.000 title claims abstract description 82
- 238000000926 separation method Methods 0.000 title claims abstract description 33
- 230000007246 mechanism Effects 0.000 title claims abstract description 27
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims abstract description 32
- 235000011941 Tilia x europaea Nutrition 0.000 claims abstract description 32
- 239000004571 lime Substances 0.000 claims abstract description 32
- 238000002955 isolation Methods 0.000 claims abstract description 16
- 230000000903 blocking effect Effects 0.000 claims description 9
- 239000011248 coating agent Substances 0.000 claims description 5
- 238000000576 coating method Methods 0.000 claims description 5
- 239000007789 gas Substances 0.000 description 51
- 238000009825 accumulation Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 230000004888 barrier function Effects 0.000 description 4
- 230000007423 decrease Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 210000000481 breast Anatomy 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 230000001976 improved effect Effects 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 238000003754 machining Methods 0.000 description 1
- 230000003340 mental effect Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 239000004810 polytetrafluoroethylene Substances 0.000 description 1
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 230000000007 visual effect Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/12—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/12—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces
- B01D45/16—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces generated by the winding course of the gas stream, the centrifugal forces being generated solely or partly by mechanical means, e.g. fixed swirl vanes
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separating Particles In Gases By Inertia (AREA)
- Gas Separation By Absorption (AREA)
Abstract
The invention discloses a kind of gas-liquid separation mechanisms, in tube body, for detaching gas containing liquid, tube body include for being passed through the entrance of the gas containing liquid, for the first outlet of vent, for the second outlet of pass-out liquid, gas-liquid separation mechanism include be set to tube body in wind turbine, lime set plate, the spirally-guided channel between the inside circumference and lime set plate of tube body, the isolation cover in tube body；The micropore that lime set plate includes plate body, is opened on plate body；The top and bottom in spirally-guided channel are connected to first outlet and second outlet respectively；The inside circumference and outside circumference in spirally-guided channel support the inside circumference set on lime set plate and tube body respectively；Isolation cover include for separate the cover body in spirally-guided channel and first outlet, the through-hole being opened on cover body, set on the outside of cover body circumference for stopping that the hand of spiral of the gas along spirally-guided channel enters the block piece in through-hole.Gas-liquid separation mechanism of the present invention separating rate is very fast, separative efficiency is higher.
Description
Technical field
The present invention relates to a kind of gas-liquid separation mechanisms.
Background technology
In plant produced, such as lathe process, electric discharge machining, laser welding, plasma cut, coolant liquid spraying
Deng often will produce some gases containing liquid, if be directly discharged into air, the harmful components in gas containing liquid can pollute air.
Meanwhile liquid therein also has the value recycled, the waste of resource can be caused by being discharged into air, increase life
Produce the cost of processing.
Invention content
The object of the present invention is to provide a kind of gas-liquid separation mechanisms, can efficiently carry out the gas-liquid separation of the gas containing liquid,
Simple in structure, separating rate is very fast, separative efficiency is higher.
In order to achieve the above objectives, the technical solution adopted by the present invention is：
A kind of gas-liquid separation mechanism is set in tube body, and for detaching gas containing liquid, the tube body includes being used for set on its lower end
It is passed through the entrance of the gas containing liquid, the first outlet for the gas isolated for pass-out for being provided thereon end, set on its lower end
The liquid isolated for pass-out second outlet, the gas-liquid separation mechanism includes：
The wind turbine of the inside circumference for the gas containing liquid to be blowed to the tube body in the tube body；
Lime set plate between the inside circumference and the wind turbine of the tube body, the lime set plate include plate body, are opened in institute
State the micropore of the inside circumference for the gas containing liquid to be oriented to the tube body on plate body；
Spirally-guided channel between the inside circumference and the lime set plate of the tube body；The spirally-guided channel it is upper
End is connected to the first outlet, and the lower end in the spirally-guided channel is connected to the second outlet；The spirally-guided is logical
The inside circumference in road, which is supported, to be set on the lime set plate, and the outside circumference in the spirally-guided channel is supported set on the inside of the tube body
Circumference；
Isolation cover in the tube body, the isolation cover include going out for separating the spirally-guided channel and described first
Mouthful cover body, be opened on the cover body through-hole, on the outside of the cover body circumference block piece, the block piece is used for
Stop that the hand of spiral of the gas along the spirally-guided channel enters in the through-hole.
Preferably, the spirally-guided channel is the spring that elastic telescopic direction is vertically distributed.
Preferably, the lower end of the cover body is set on the wind turbine, and the cover body in the upward direction open by gradual taper.
Preferably, contact successively two of the hand of spiral of the block piece by the gas along the spirally-guided channel
It is connected on the cover body by first side with the second side, the block piece when being respectively first, the second side position
In side of the through-hole far from the cover body.
Preferably, the wind turbine is set in the middle part of the tube body, and the gas-liquid separation mechanism further includes being set on the wind turbine
The barrier plate for stopping the upward pass-out of the gas containing liquid of side is used to prevent the gas from institute in the tube body
State the blocking cover of pass-out below wind turbine.
It is highly preferred that the blocking cover in the upward direction shrink by gradual taper.
Preferably, the lime set plate is cylindrical, and the lime set plate, the spirally-guided channel, the tube body coaxially divide
Cloth.
Preferably, the gas-liquid separation mechanism further includes the poly- oil coating of polywater being coated on the lime set plate.
Due to the application of the above technical scheme, the present invention has following advantages compared with prior art：A kind of gas of the present invention
Liquid separator structure effectively can agglomerate most liquid by the way that lime set plate is arranged when gas containing liquid is by lime set plate
Body；By the way that spirally-guided channel is arranged, the liquid isolated can not only be made to flow downward convergence along the hand of spiral, additionally it is possible to make
The gas isolated flows up and down along the hand of spiral, gas during spiral and spiral decline, due to from
The effect of mental and physical efforts can further detach the liquid that do not isolate, and the liquid isolated is to carry with spirally-guided channel
Body continues to flow downward；By the way that isolation cover and block piece is arranged, it can stop that the hand of spiral of the gas along spirally-guided channel is straight
It taps into through-hole, gas reverse flow after accumulation is made to enter in through-hole, increase the time that gas is flowed around isolation cover, carry
The high effect of gas-liquid separation.
Description of the drawings
Attached drawing 1 is the structural schematic diagram of apparatus of the present invention；
Attached drawing 2 is the structural schematic diagram of isolation cover.
Wherein：1, tube body；2, entrance；3, wind turbine；4, first outlet；5, second outlet；6, lime set plate；7, spirally-guided is logical
Road；8, isolation cover；81, cover body；82, through-hole；83, block piece；84, the first side；85, the second side；9, barrier plate；10, blocking cover.
Specific implementation mode
The technical solution of the present invention will be further described below with reference to the accompanying drawings.
Shown in Fig. 1-2, above-mentioned a kind of gas-liquid separation mechanism, for detaching gas containing liquid.The gas-liquid separation mechanism is set
In the tube body 1 being vertically distributed, tube body 1 includes set on the entrance 2 for being passed through the gas containing liquid of its lower end, set on it
The first outlet 4 for the gas of upper end isolated for pass-out, be used for the liquid that pass-out is isolated second set on its lower end
Outlet 5.
The gas-liquid separation mechanism includes the wind for blowing to the inside circumference of tube body 1 for that will contain liquid gas being set in tube body 1
Machine 3, the lime set plate 6 between the inside circumference and wind turbine 3 of tube body 1, between the inside circumference and lime set plate 6 of tube body 1
Spirally-guided channel 7.
The lime set plate 6 include plate body, be opened on plate body for will contain liquid gas guide pipe body 1 inside circumference it is micro-
Hole, coated on the poly- oil coating of polywater on lime set plate 6.In this embodiment, which has multiple, and path is in irregular shape, is used
It is oriented to its another side from plate body one side in liquid gas will be contained, that is, is used to that liquid gas will to be contained from plate body close to the side of wind turbine 3
Face is oriented to another side of the plate body close to spirally-guided channel 7.Gas containing liquid in micropore by when, liquid condensation at drop,
With gas initial gross separation.The lime set plate 6 is cylindrical, with the coaxial distribution of tube body 1.By the way that the poly- oil coating of polywater is arranged, further
The ability for improving 6 agglomeration liquid of lime set plate improves the efficiency of gas-liquid separation.The poly- oil coating of the polywater can be PTFE breasts
Glue.
The upper end in the spirally-guided channel 7 is connected to first outlet 4, and lower end and the second outlet 5 in spirally-guided channel 7 connect
It is logical.Spirally-guided channel 7 and the coaxial distribution of tube body 1.In the present embodiment, spirally-guided channel 7 is set on the inside of tube body 1 week
The elastic telescopic direction of spring between portion and the outside circumference of cylindrical shape lime set plate 6, the spring is vertically distributed, and is passed through
The spring is set, the path length in spirally-guided channel under identical height can be adjusted, with corresponding gas and the liquid of adjusting in spiral shell
The path length flowed on rotation guide channel, that is, adjust the speed of gas-liquid separation.The inside circumference in spirally-guided channel 7 is supported and is set to
The outside circumference of lime set plate 6, the outside circumference in spirally-guided channel 7 are supported the inside circumference set on tube body 1, are arranged by this,
The liquid agglomerated in micropore can be made to flow directly into spirally-guided channel 7.Spirally-guided channel 7 is in the counterclockwise direction（Referring to
Fig. 1, the spirally-guided channel 7 from coming from the vertical view visual angle of Fig. 1）Spiral.By the way that the spirally-guided channel 7 is arranged, no
The liquid isolated can be only set to flow downward convergence along the hand of spiral, additionally it is possible to keep the gas isolated upward along the hand of spiral
With flow downward, gas, due to the effect of centrifugal force can further will not during spiral and spiral decline
The liquid isolated is detached, the liquid isolated with spirally-guided channel 7 be carrier continue to flow downward, separating rate compared with
Soon, separative efficiency is higher.
The gas-liquid separation mechanism further includes the isolation cover 8 being set in tube body 1, and isolation cover 8 includes for separating spirally-guided
The cover body 81 of channel 7 and first outlet 4, the through-hole 82 being opened on cover body 81, set on the block piece 83 of 81 outside circumference of cover body,
Block piece 83 is for stopping that gas enters along the hand of spiral in spirally-guided channel 7 in through-hole 82, since spirally-guided channel 7 is pasted
On lime set plate 6, which is set between lime set plate 6 and first outlet 4.In the present embodiment, the lower end of cover body 81 is set
In on wind turbine 3, cover body 81 in the upward direction open by gradual taper.Block piece 83 is by gas along the spiral in spirally-guided channel 7
Direction contact successively two when being respectively first 84 and second side 85, block piece 83 cover body 81 is connected to by the first side 84
On, the second side 85 is then located at side of the through-hole 82 far from cover body 81.By this setting, gas is formed in spirally-guided channel
The eddy flow rotated in an anti-clockwise direction flows, due to block piece in the counterclockwise direction after being returned in micropore around isolation cover 8
83 setting, gas cannot directly enter in through-hole 82.After gas flows to accumulation in the counterclockwise direction always, at accumulation
Larger buffer brake is generated, gas is flowed around isolation cover 8 along clockwise direction again under buffer brake effect, into logical
In hole 82, then from through-hole 82 enter first outlet 4；The time that gas is flowed around isolation cover 8 is increased, gas-liquid separation is improved
Effect.
Wind turbine 3 is set to 1 middle part of tube body, and gas-liquid separation mechanism further includes being set to above wind turbine 3 to be used to stop gas containing liquid
The barrier plate 9 of upward pass-out is used to prevent gas from the blocking cover 10 of 3 lower section pass-out of wind turbine, blocking cover 10 in tube body 1
Gradual taper is shunk in the upward direction.By the way that the barrier plate 9 is arranged, make gas containing liquid that can only enter from the side of wind turbine 3 solidifying
In liquid plate 6；By the way that the blocking cover 10 is arranged, when gas flows downward along spirally-guided channel 7, again along spiral after bottoming out
Guide channel 7 flows up.
The course of work of lower the present embodiment is illustrated in detail below：
First, liquid gas will be contained to be passed through in tube body 1 from entrance 2, under the centrifugal action of wind turbine 3, gas containing liquid enters lime set plate 6
In, agglomerate most of liquid by micropore, penetration by liquid micropore enters in spirally-guided channel 7, along spirally-guided channel 7
It flows downward；Gas is then flowed through micropore along spirally-guided channel 7 upward or downward, is hindered since lower part is blocked cover 10
Gear, the gas after bottoming out can also be flowed up along spirally-guided channel 7, and gas is in flow process, due to the work of centrifugal force
With further the liquid that do not isolate can be detached, wait gases rise to top after, in the counterclockwise direction around every
It is flowed from cover 8, due to the presence of block piece 83, gas cannot be introduced into through-hole 82, when gas flows always in the counterclockwise direction
To accumulation, larger buffer brake is generated at accumulation, the buffer brake effect under gas again along clockwise direction around
Isolation cover 8 flows, and into through-hole 82, then enters first outlet 4 from through-hole 82 and is passed through in external environment；The liquid isolated
Then recycled from second outlet 5.
The above embodiments merely illustrate the technical concept and features of the present invention, and its object is to allow person skilled in the art
Scholar can understand present disclosure and be implemented, and it is not intended to limit the scope of the present invention, all according to the present invention
Equivalent change or modification made by Spirit Essence should all cover within the scope of the present invention.
Claims (8)
1. a kind of gas-liquid separation mechanism is set in tube body, for detaching gas containing liquid, the tube body includes the use set on its lower end
The entrance of the gas containing liquid described in being passed through, is set under it the first outlet for being used for the gas that pass-out is isolated for being provided thereon end
The second outlet of the liquid isolated for pass-out at end, it is characterised in that：The gas-liquid separation mechanism includes：
The wind turbine of the inside circumference for the gas containing liquid to be blowed to the tube body in the tube body；
Lime set plate between the inside circumference and the wind turbine of the tube body, the lime set plate include plate body, are opened in institute
State the micropore of the inside circumference for the gas containing liquid to be oriented to the tube body on plate body；
Spirally-guided channel between the inside circumference and the lime set plate of the tube body；The spirally-guided channel it is upper
End is connected to the first outlet, and the lower end in the spirally-guided channel is connected to the second outlet；The spirally-guided is logical
The inside circumference in road, which is supported, to be set on the lime set plate, and the outside circumference in the spirally-guided channel is supported set on the inside of the tube body
Circumference；
Isolation cover in the tube body, the isolation cover include going out for separating the spirally-guided channel and described first
Mouthful cover body, be opened on the cover body through-hole, on the outside of the cover body circumference block piece, the block piece is used for
Stop that the hand of spiral of the gas along the spirally-guided channel enters in the through-hole.
2. a kind of gas-liquid separation mechanism according to claim 1, it is characterised in that：It is stretched for elasticity in the spirally-guided channel
The spring that contracting direction is vertically distributed.
3. a kind of gas-liquid separation mechanism according to claim 1, it is characterised in that：The lower end of the cover body is set to the wind
On machine, the cover body in the upward direction open by gradual taper.
4. a kind of gas-liquid separation mechanism according to claim 1, it is characterised in that：The block piece is by the gas along institute
State that the hand of spiral in spirally-guided channel contacts successively two when being respectively first and the second side, the block piece pass through institute
It states the first side to be connected on the cover body, second side is located at side of the through-hole far from the cover body.
5. a kind of gas-liquid separation mechanism according to claim 1, it is characterised in that：The wind turbine is set in the tube body
Portion, the gas-liquid separation mechanism further include the blocking for stopping the upward pass-out of the gas containing liquid being set to above the wind turbine
Plate is used for the blocking cover for preventing the gas from pass-out below the wind turbine in the tube body.
6. a kind of gas-liquid separation mechanism according to claim 5, it is characterised in that：Blocking cover in the upward direction by
Gradually taper is shunk.
7. a kind of gas-liquid separation mechanism according to claim 1, it is characterised in that：The lime set plate is cylindrical, described
Lime set plate, the spirally-guided channel, the tube body are coaxially distributed.
8. a kind of gas-liquid separation mechanism according to claim 1, it is characterised in that：The gas-liquid separation mechanism further includes applying
The poly- oil coating of polywater being overlying on the lime set plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810608309.7A CN108514798B (en) | 2018-06-13 | 2018-06-13 | Gas-liquid separation mechanism |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810608309.7A CN108514798B (en) | 2018-06-13 | 2018-06-13 | Gas-liquid separation mechanism |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN108514798A true CN108514798A (en) | 2018-09-11 |
| CN108514798B CN108514798B (en) | 2023-12-22 |
Family
ID=63427509
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810608309.7A Active CN108514798B (en) | 2018-06-13 | 2018-06-13 | Gas-liquid separation mechanism |
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| Country | Link |
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| CN (1) | CN108514798B (en) |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5431228A (en) * | 1993-04-27 | 1995-07-11 | Atlantic Richfield Company | Downhole gas-liquid separator for wells |
| CN101949380A (en) * | 2010-10-11 | 2011-01-19 | 吉首大学 | Foam remover of compressor separator |
| CN202173849U (en) * | 2011-07-26 | 2012-03-28 | 杭州潜阳科技有限公司 | Gas-liquid separator |
| CN102961940A (en) * | 2012-11-20 | 2013-03-13 | 邢学军 | Gas-liquid separator combining centrifugal separation, baffle plate and filter |
| CN203908141U (en) * | 2014-06-19 | 2014-10-29 | 烟台顿汉布什工业有限公司 | Gas-liquid separation mechanism of flooded evaporator |
| CN207048763U (en) * | 2017-06-20 | 2018-02-27 | 中国石油化工股份有限公司 | Spiral separation gas bag |
| CN208482203U (en) * | 2018-06-13 | 2019-02-12 | 苏州颇澳德克过滤系统科技有限公司 | A kind of gas-liquid separation device |
-
2018
- 2018-06-13 CN CN201810608309.7A patent/CN108514798B/en active Active
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5431228A (en) * | 1993-04-27 | 1995-07-11 | Atlantic Richfield Company | Downhole gas-liquid separator for wells |
| CN101949380A (en) * | 2010-10-11 | 2011-01-19 | 吉首大学 | Foam remover of compressor separator |
| CN202173849U (en) * | 2011-07-26 | 2012-03-28 | 杭州潜阳科技有限公司 | Gas-liquid separator |
| CN102961940A (en) * | 2012-11-20 | 2013-03-13 | 邢学军 | Gas-liquid separator combining centrifugal separation, baffle plate and filter |
| CN203908141U (en) * | 2014-06-19 | 2014-10-29 | 烟台顿汉布什工业有限公司 | Gas-liquid separation mechanism of flooded evaporator |
| CN207048763U (en) * | 2017-06-20 | 2018-02-27 | 中国石油化工股份有限公司 | Spiral separation gas bag |
| CN208482203U (en) * | 2018-06-13 | 2019-02-12 | 苏州颇澳德克过滤系统科技有限公司 | A kind of gas-liquid separation device |
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| Publication number | Publication date |
|---|---|
| CN108514798B (en) | 2023-12-22 |
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Effective date of registration: 20231201 Address after: 215000, 3rd Floor, Building B, Leyu Technology Entrepreneurship Park, No. 8 Lekun Road, Leyu Town, Zhangjiagang City, Suzhou City, Jiangsu Province Applicant after: Antler automation equipment (Suzhou) Co.,Ltd. Address before: 215637 Zhangjiagang Economic Development Zone, Suzhou City, Jiangsu Province (POADEC, No. 25, Renmin Road, Chenyang) Applicant before: SUZHOU PALDEK FILTRATION SCIENCE & TECHNOLOGY CO.,LTD. |
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