CN208482204U - A kind of gas-liquid separation mechanism - Google Patents
A kind of gas-liquid separation mechanism Download PDFInfo
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- CN208482204U CN208482204U CN201820917501.XU CN201820917501U CN208482204U CN 208482204 U CN208482204 U CN 208482204U CN 201820917501 U CN201820917501 U CN 201820917501U CN 208482204 U CN208482204 U CN 208482204U
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- gas
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- tube body
- cover
- liquid separation
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Abstract
The utility model discloses a kind of gas-liquid separation mechanisms, in tube body, for separating 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 includes blower, lime set plate, the spirally-guided channel between the inside circumference and lime set plate of tube body, the isolation cover in tube body in the 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 in spirally-guided channel and first outlet, the through-hole being opened on cover, set on the outside of cover circumference for stopping gas to enter along the hand of spiral in spirally-guided channel the block piece in through-hole.The utility model gas-liquid separation mechanism separating rate is very fast, separative efficiency is higher.
Description
Technical field
The utility model relates to a kind of gas-liquid separation mechanisms.
Background technique
In plant produced, such as lathe process, electric discharge machining, laser welding, plasma cut, coolant liquid spraying
Deng often generating some gases containing liquid, if be directly discharged into atmosphere, the harmful components in gas containing liquid can pollute air.
Meanwhile liquid therein is discharged into air there are also the value recycled and will cause the waste of resource, increase life
Produce the cost of processing.
Utility model content
The purpose of the utility model is to provide a kind of gas-liquid separation mechanisms, can efficiently carry out the gas-liquid point of the gas containing liquid
From structure is simple, and separating rate is very fast, separative efficiency is higher.
In order to achieve the above objectives, the technical solution adopted in the utility model is:
A kind of gas-liquid separation mechanism is set in tube body, and for separating gas containing liquid, the tube body includes being set to its lower end
For being passed through the first outlet of the entrance of the gas containing liquid, the gas isolated for pass-out for being provided thereon end, being set to it
The second outlet for the liquid of lower end isolated for pass-out, the gas-liquid separation mechanism include:
The blower 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 blower of the tube body, the lime set plate include plate body, open up
In the micropore of the inside circumference for the gas containing liquid to be oriented to the tube body on the plate body；
Spirally-guided channel between the inside circumference and the lime set plate of the tube body；The spirally-guided channel
Upper end be connected to the first outlet, the lower end in the spirally-guided channel is connected to the second outlet；The spiral is led
It supports and is set on the lime set plate to the inside circumference in channel, the outside circumference in the spirally-guided channel is supported set on the tube body
Inside circumference；
Isolation cover in the tube body, the isolation cover include for separating the spirally-guided channel and described
One outlet cover, be opened on the cover through-hole, on the outside of the cover circumference block piece, the block piece,
For stopping the gas to enter in the through-hole along the hand of spiral in the spirally-guided channel.
Preferably, the spirally-guided channel is the spring that elastic telescopic direction is distributed along the vertical direction.
Preferably, the lower end of the cover is set on the blower, and the cover in the upward direction gradually open by taper.
Preferably, successively contact two of the hand of spiral of the block piece by the gas along the spirally-guided channel
It is connected on the cover with the second side, the block piece by first side when being respectively first, the second side position
In side of the through-hole far from the cover.
Preferably, the blower is set in the middle part of the tube body, and the gas-liquid separation mechanism further includes being set on the blower
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 blower.
It is highly preferred that the blocking cover in the upward direction gradually shrink by 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 coated on the poly- oil coating of polywater on the lime set plate.
Due to the application of the above technical scheme, the utility model has the advantage that this is practical new compared with prior art
A kind of gas-liquid separation mechanism of type, when gas containing liquid passes through lime set plate, can effectively be agglomerated big absolutely out by the way that lime set plate is arranged
Partially liq；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, and also
The gas isolated can be made to flow up and down along the hand of spiral, gas during spiral and spiral decline,
Further the liquid that do not isolate can be separated due to the effect of centrifugal force, the liquid isolated is logical with spirally-guided
Road is that carrier continues to flow downward；By setting isolation cover and block piece, gas can be stopped along the spiral in spirally-guided channel
Direction is directly entered in through-hole, enters gas reverse flow after accumulation in through-hole, increases what gas was flowed around isolation cover
Time improves the effect of gas-liquid separation.
Detailed description of the invention
Attached drawing 1 is the structural schematic diagram of utility model device；
Attached drawing 2 is the structural schematic diagram of isolation cover.
Wherein: 1, tube body；2, entrance；3, blower；4, first outlet；5, second outlet；6, lime set plate；7, spirally-guided is logical
Road；8, isolation cover；81, cover；82, through-hole；83, block piece；84, the first side；85, the second side；9, barrier plate；10, stop cover.
Specific embodiment
The technical solution of the utility model is further elaborated with reference to the accompanying drawing.
Referring to shown in Fig. 1-2, a kind of above-mentioned gas-liquid separation mechanism is used to separate gas containing liquid.The gas-liquid separation mechanism is set
In the tube body 1 being distributed along the vertical direction, 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 in tube body 1
Machine 3, the lime set plate 6 between the inside circumference and blower 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, uses
It is oriented to its another side from plate body one side in liquid gas will be contained, i.e., for liquid gas will to be contained from plate body close to the side of blower 3
Face is oriented to plate body close to the another side in 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 cream
Glue.
The upper end in the spirally-guided channel 7 is connected to first outlet 4, and the lower end in spirally-guided channel 7 and second outlet 5 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
Spring between portion and the outside circumference of cylinder-shaped lime set plate 6, the elastic telescopic direction of the spring is distributed along the vertical direction, passes through
The spring is set, the path length in spirally-guided channel under identical height can be adjusted, to correspond to regulating gas and liquid 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 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 separated, the liquid isolated with spirally-guided channel 7 be carrier continue to flow downward, separating rate compared with
Fastly, separative efficiency is higher.
The gas-liquid separation mechanism further includes the isolation cover 8 in tube body 1, and isolation cover 8 includes for separating spirally-guided
The cover 81 of channel 7 and first outlet 4, the through-hole 82 being opened on cover 81, set on the block piece 83 of 81 outside circumference of cover,
Block piece 83 is for stopping gas to enter in through-hole 82 along the hand of spiral in spirally-guided channel 7, 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 81 is set
In on blower 3, cover 81 in the upward direction gradually open by taper.Block piece 83 is by gas along the spiral in spirally-guided channel 7
Direction successively contact two when being respectively first 84 and second side 85, block piece 83 cover 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 81.It is arranged by this, 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 returning 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
Biggish 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.
Blower 3 is set to 1 middle part of tube body, and gas-liquid separation mechanism further includes set on 3 top of blower for stopping 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 blower in tube body 1, stops cover 10
Gradually taper is shunk in the upward direction.By the way that the barrier plate 9 is arranged, it enter gas containing liquid can only from the side of blower 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:
It is passed through in tube body 1 firstly, liquid gas will be contained from entrance 2, under the centrifugal action of blower 3, gas containing liquid enters solidifying
In liquid plate 6, most of liquid out is agglomerated by micropore, penetration by liquid micropore enters in spirally-guided channel 7, along spirally-guided
Channel 7 flows downward；Gas then penetrates micropore and flows upward or downward along spirally-guided channel 7, since lower part is blocked cover
10 stop, and the gas after bottoming out can also be flowed up along spirally-guided channel 7, and gas is in flow process, due to centrifugal force
Effect further the liquid that do not isolate can be separated, wait gases rise to top after, in the counterclockwise direction around
Isolation cover 8 flow, due to the presence of block piece 83, gas be cannot be introduced into through-hole 82, when gas always in the counterclockwise direction
After flowing to accumulation, biggish buffer brake is generated at accumulation, gas is again along clockwise direction under buffer brake effect
It is flowed around isolation cover 8, into through-hole 82, then enters first outlet 4 from through-hole 82 and be passed through in external environment；It isolates
Liquid is then recycled from second outlet 5.
The above embodiments are only for explaining the technical ideas and features of the present invention, and its object is to allow be familiar with technique
Personage can understand the content of the utility model and be implemented, do not limit the protection scope of the present invention,
All equivalent change or modifications according to made by the spirit of the present invention essence, should all cover in the protection scope of the utility model
It is interior.
Claims (8)
1. a kind of gas-liquid separation mechanism is set in tube body, for separating 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 blower 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 blower 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, be opened on the cover through-hole, on the outside of the cover circumference block piece, the block piece is used for
The gas is stopped to enter in the through-hole along the hand of spiral in the spirally-guided channel.
2. a kind of gas-liquid separation mechanism according to claim 1, it is characterised in that: stretched for elasticity in the spirally-guided channel
The spring that contracting direction is distributed along the vertical direction.
3. a kind of gas-liquid separation mechanism according to claim 1, it is characterised in that: the lower end of the cover is set to the wind
On machine, the cover in the upward direction gradually open by 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 successively contacts 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, second side is located at side of the through-hole far from the cover.
5. a kind of gas-liquid separation mechanism according to claim 1, it is characterised in that: the blower is set in the tube body
Portion, the gas-liquid separation mechanism further include above the blower for stopping the blocking of the upward pass-out of the gas containing liquid
Plate is used for the blocking cover for preventing the gas from pass-out below the blower 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 |
|---|---|---|---|
| CN201820917501.XU CN208482204U (en) | 2018-06-13 | 2018-06-13 | A kind of gas-liquid separation mechanism |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820917501.XU CN208482204U (en) | 2018-06-13 | 2018-06-13 | A kind of gas-liquid separation mechanism |
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| Publication Number | Publication Date |
|---|---|
| CN208482204U true CN208482204U (en) | 2019-02-12 |
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ID=65251491
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820917501.XU Active CN208482204U (en) | 2018-06-13 | 2018-06-13 | A kind of gas-liquid separation mechanism |
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| Country | Link |
|---|---|
| CN (1) | CN208482204U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110886601A (en) * | 2019-12-09 | 2020-03-17 | 哈尔滨工程大学 | Spring type liquid level self-adaptive gas-liquid separator |
-
2018
- 2018-06-13 CN CN201820917501.XU patent/CN208482204U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110886601A (en) * | 2019-12-09 | 2020-03-17 | 哈尔滨工程大学 | Spring type liquid level self-adaptive gas-liquid separator |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20221011 Address after: Nanovia (Jiangsu) Intelligent Equipment Co., Ltd., No. 23-1, Chenyang Road, Yangshe Town, Zhangjiagang City, Suzhou City, Jiangsu Province, 215600 Patentee after: NANOVIA (JIANGSU) INTELLIGENT EQUIPMENT Co.,Ltd. Address before: 215637 Zhangjiagang Economic Development Zone, Suzhou City, Jiangsu Province (POADEC, No. 25, Renmin Road, Chenyang) Patentee before: SUZHOU PALDEK FILTRATION SCIENCE & TECHNOLOGY CO.,LTD. |