CN207446545U - A kind of gas-liquid two-phase multistage atomizing nozzle - Google Patents
A kind of gas-liquid two-phase multistage atomizing nozzle Download PDFInfo
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- CN207446545U CN207446545U CN201721323171.3U CN201721323171U CN207446545U CN 207446545 U CN207446545 U CN 207446545U CN 201721323171 U CN201721323171 U CN 201721323171U CN 207446545 U CN207446545 U CN 207446545U
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- gas
- nozzle
- liquid
- atomization core
- inner cavity
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Abstract
The utility model belongs to atomising device technical field, refer specifically to a kind of gas-liquid two-phase multistage atomizing nozzle, nozzle housing including being equipped with inner cavity, the inner cavity is cylinder, air inlet and dispersive nozzle are respectively equipped at the top and bottom of the nozzle housing, it is characterized in that, further includes atomization core and the collection chamber being coaxially disposed in the lumen.Gas-liquid two-phase multistage atomizing nozzle described in the utility model contains three-level atomization mechanism, and atomizing principles at different levels differ, and the atomization that can make liquid is more abundant；In addition structure is also relatively simple, and the shape of each building block is more regular, easy to manufacture.
Description
Technical field
The utility model belongs to atomising device technical field, refers specifically to a kind of gas-liquid two-phase multistage atomizing nozzle.
Background technology
The atomization mechanism of gas-liquid two-phase atomizer is mainly membranaceous division, when gas-liquid mixed stream at a relatively high speed from
When pressure nozzle sprays, the film-form droplet group of gas-in-liquid can be formed, gas expansion makes liquid-sheet disintegration mist formation, increases air pressure,
It reduces liquid measure and can further improve atomizing effect.There are two types of patterns for gas-liquid two-phase atomizer：Ejection type and gas-liquid collision type.Its
In, gas-liquid collision type nozzle generates atomization mainly by the alternate high velocity impact of gas-liquid, has preferable atomization stability.It is existing
Gas-liquid collision type nozzle mainly considers to be atomized using the alternate high velocity impact of gas-liquid in design, without utilizing gas-liquid two
Further atomization is realized in the impact rotary-cut effect that shearing force between mutually flowing generates, it is therefore necessary to be further improved nozzle
Internal structure sets multistage atomizing mechanism, the shearing force between biphase gas and liquid flow preferably to be utilized to promote atomizing effect.
The content of the invention
The utility model for deficiency of the prior art devise it is a kind of can be preferably using between biphase gas and liquid flow
The gas-liquid two-phase multistage atomizing nozzle for the atomizing that shearing force generates.
Gas-liquid two-phase multistage atomizing nozzle described in the utility model includes the nozzle housing equipped with inner cavity, and the inner cavity is in circle
Cylindricality is respectively equipped with air inlet and dispersive nozzle at the top and bottom of the nozzle housing, is characterized in that, further includes same
Axis sets atomization core and collection chamber in the lumen.
The atomization core includes the atomization core body equipped with spray chamber and the inlet tube positioned at atomization core body top.It is described
Spray chamber is equipped with the atomisation outlet for connecting and being located above dispersive nozzle with inner cavity.The atomization core body is in the form of a column, and top is set
Have a delivery hole that multiple both ends connect respectively with spray chamber and inlet tube, side wall be equipped with multiple both ends respectively with inner cavity and atomization
The gas port of room connection, the atomization core body bottom are equipped with annulus in rounding mesa-shaped and between the bottom inside of nozzle housing
The tube wall of inlet tube described in gap is fixedly connected with nozzle housing and inlet is located at outside nozzle housing top.The collection chamber includes
Be set in inlet tube is outer and upper end is connected with nozzle housing inside top isolating cylinder, inside edge and outer ledge respectively with into
The annular partition that liquid pipe outer wall is connected with isolating cylinder bottom is provided with venthole on the side wall of the isolating cylinder.
The width at the most narrow place in the annulus is less than atomization core outer body and the spacing on the inside of nozzle housing.
The bottom of the spray chamber is the diversion cavity of a reverse frustoconic.
Multiple spiral helicine guide vanes are equipped at intervals on the inner wall of the diversion chamber.
The venthole is respectively to be tangentially disposed in isolating cylinder positioned at the opposite sides and venthole of inlet tube with air inlet
Side wall on.
Multiple gas ports are round taper hole.
Multiple gas ports are set for multilayer, and every layer of gas port is the side wall for being radially arranged in atomization core body
On.
Gas-liquid two-phase multistage atomizing nozzle described in the utility model contains three-level atomization mechanism, and atomizing principles at different levels are equal
It differs, the atomization that can make liquid is more abundant；In addition structure is also relatively simple, and the shape of each building block is more regular,
It is easy to manufacture.
Description of the drawings
Fig. 1 is the structure diagram of the utility model；
Fig. 2 is the A-A schematic cross-sectional views of Fig. 1；
Fig. 3 is the B-B schematic cross-sectional views of Fig. 1.
Wherein：1- nozzle housings (11- inner cavities, 12- air inlets, 13- dispersive nozzles), 2- atomization cores (21- atomization core sheets
Body, 211- spray chambers, 2111- atomisation outlets, 2112- diversion cavities, 212- delivery holes, 213- gas ports, 214- guide vanes,
22- inlet tubes), 3- collection chambers (31- isolating cylinders, 311- ventholes, 32- annular partitions), 4- annulus.
Specific embodiment
Gas-liquid two-phase multistage atomizing nozzle described in the utility model is made into one in the following with reference to the drawings and specific embodiments
Walk explanation.
As shown in Figures 1 to 3, gas-liquid two-phase multistage atomizing nozzle described in the utility model is included outside the nozzle equipped with inner cavity 11
Shell 1, inner cavity 11 is cylinder, and the top and bottom of nozzle housing 1 are respectively equipped with air inlet 12 and dispersive nozzle 13, it is special it
It is in further including the atomization core 2 being co-axially located in inner cavity 11 and collection chamber 3.
Atomization core 2 includes the atomization core body 21 equipped with spray chamber 211 and the inlet tube positioned at 21 top of atomization core body
22.Spray chamber 211, which is equipped with, to be connected with inner cavity 11 and positioned at the atomisation outlet 2111 of 13 top of dispersive nozzle.Atomization core body 21 is in
Column, top are equipped with the delivery hole 212 that multiple both ends connect respectively with spray chamber 211 and inlet tube 22, and side wall is equipped with multiple
The gas port 213 that both ends connect respectively with inner cavity 11 and spray chamber 211,21 bottom of atomization core body are in rounding mesa-shaped and and nozzle
Annulus 4 is equipped between the bottom inside of shell 1.The tube wall of inlet tube 22 is fixedly connected with nozzle housing 1 and inlet is located at
1 top of nozzle housing is outer.Collection chamber 3 include being set in inlet tube 22 is outer and upper end is connected with 1 inside top of nozzle housing every
From the annular partition 32 that cylinder 31, inside edge and outer ledge are connected respectively with 22 outer wall of inlet tube and 31 bottom of isolating cylinder, every
Venthole 311 is provided on side wall from cylinder 31.
The width at the most narrow place in annulus 4 is less than the spacing in 21 outside of atomization core body and 1 inside of nozzle housing.
Above-mentioned atomizer is from top air inlet and feed liquor, and inside changes the flowing side of gas with the collection chamber 3 set
To, so as to the air intake structure from setting complexity in 1 side of nozzle body, help to simplify the external structure of nozzle body 1, and
Convenient for the transport and installation of atomizer.The narrow throat of Laval nozzle is equivalent at the relatively narrow annulus 4 of nozzle interior, is had
Help accelerate the air-flow near dispersive nozzle 13 and promote atomizing effect.
Rear portion is discharged through venthole 311 enter spray chamber 211 through gas port 213 into the air-flow in collection chamber 3, after
It is discharged from 211 bottom of spray chamber, another part is then via gap of 21 outside of atomization core body with 1 inside of nozzle body and annular
Gap 4 crosses with discharging the gas of spray chamber 211, then discharges nozzle housing 1 through dispersive nozzle 13 together.In inlet tube 22
Liquid to be atomized enters spray chamber 211 and the suction function inside spray chamber 211 via multiple more elongated delivery holes 212
Lower realization is atomized for the first time, and the droplet of generation via gas stream make impact of the gas port 213 into spray chamber 211 with realizing second
Secondary atomization finally flows through the air-flow at annulus 4 and impact rotary-cut is further carried out to the droplet for discharging spray chamber 211 so as to reality
Now third time is atomized.Above-mentioned atomizer contains three-level atomization mechanism, and atomizing principles at different levels differ, and can make liquid
Atomization is more abundant.In addition the structure of atomizer is relatively simple, and the shape of each building block is more regular, system easy to process
Make.
The bottom of spray chamber 211 is the diversion cavity 2112 of a reverse frustoconic.Narrowed diversion cavity 2112 contributes to droplet
Accelerating Removal spray chamber 211 acts on its impact rotary-cut so as to aggravate air-flow at annulus 4.
Multiple spiral helicine guide vanes 214 are equipped at intervals on the inner wall of diversion cavity 2112.Flow through the mist of diversion cavity 2112
Acceleration can be further rotated by, which dropping under the action of guide vane 214, goes out spray chamber 211, aggravates itself and air-flow at annulus 4
Rotary-cut impact, and then promoted atomizing effect.
Venthole 311 is respectively to be tangentially disposed in positioned at the opposite sides and venthole 311 of inlet tube 22 with air inlet 12
On the side wall of isolating cylinder 31.So air-flow can be through tangential discharge of the venthole 311 along isolating cylinder 31, so as to reduce air-flow to nozzle
The impact of 1 inner wall of shell is conducive to maintain the stabilization of air-flow.
Multiple gas ports 213 are round taper hole, and conical gas port 213 is helped speed up into spray chamber 211
Air-flow velocity aggravates the mutual collision of air-flow and drop, promotes atomizing effect.
Multiple gas ports 213 are set for multilayer, and every layer of gas port 213 is the side wall for being radially arranged in atomization core body 21
On, so contribute to the abundant effect of air-flow and drop.
Claims (6)
1. a kind of gas-liquid two-phase multistage atomizing nozzle, the nozzle housing (1) including being equipped with inner cavity (11), the inner cavity (11) is in circle
Cylindricality is respectively equipped with air inlet (12) and dispersive nozzle (13) at the top and bottom of the nozzle housing (1), which is characterized in that
Further include the atomization core (2) being co-axially located in inner cavity (11) and collection chamber (3)；
The atomization core (2) includes being equipped with the atomization core body (21) of spray chamber (211) and positioned at atomization core body (21) top
Inlet tube (22), the spray chamber (211) is equipped with the atomization for connect with inner cavity (11) and being located above dispersive nozzle (13) and goes out
Mouthful (2111), the atomization core body (21) are in the form of a column, top be equipped with multiple both ends respectively with spray chamber (211) and inlet tube
(22) delivery hole (212) of connection, side wall are equipped with the air guide that multiple both ends connect respectively with inner cavity (11) and spray chamber (211)
Hole (213), atomization core body (21) bottom are equipped with annulus in rounding mesa-shaped and between the bottom inside of nozzle housing (1)
Gap (4), the tube wall of the inlet tube (22) is fixedly connected with nozzle housing (1) and inlet is located at outside nozzle housing (1) top,
The collection chamber (3) includes the isolating cylinder for being set in inlet tube (22) outside and upper end is connected with nozzle housing (1) inside top
(31), the annular partition that inside edge and outer ledge are connected respectively with inlet tube (22) outer wall and isolating cylinder (31) bottom
(32), it is provided with venthole (311) on the side wall of the isolating cylinder (31)；
The width at the most narrow place of annulus (4) is less than on the outside of atomization core body (21) and the spacing on the inside of nozzle housing (1).
2. gas-liquid two-phase multistage atomizing nozzle as described in claim 1, which is characterized in that the bottom of the spray chamber (211)
For the diversion cavity (2112) of a reverse frustoconic.
3. gas-liquid two-phase multistage atomizing nozzle as claimed in claim 2, which is characterized in that the inner wall of the diversion cavity (2112)
On be equipped at intervals with multiple spiral helicine guide vanes (214).
4. gas-liquid two-phase multistage atomizing nozzle as claimed in claim 3, which is characterized in that the venthole (311) and air inlet
Mouth (12) is respectively to be tangentially disposed in the side wall of isolating cylinder (31) positioned at the opposite sides and venthole (311) of inlet tube (22)
On.
5. gas-liquid two-phase multistage atomizing nozzle as claimed in claim 4, which is characterized in that multiple gas ports (213) are equal
For round taper hole.
6. gas-liquid two-phase multistage atomizing nozzle as claimed in claim 5, which is characterized in that multiple gas ports (213) are
Multilayer is set, and every layer of gas port (213) is to be radially arranged on the side wall of atomization core body (21).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721323171.3U CN207446545U (en) | 2017-10-09 | 2017-10-09 | A kind of gas-liquid two-phase multistage atomizing nozzle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721323171.3U CN207446545U (en) | 2017-10-09 | 2017-10-09 | A kind of gas-liquid two-phase multistage atomizing nozzle |
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| Publication Number | Publication Date |
|---|---|
| CN207446545U true CN207446545U (en) | 2018-06-05 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721323171.3U Expired - Fee Related CN207446545U (en) | 2017-10-09 | 2017-10-09 | A kind of gas-liquid two-phase multistage atomizing nozzle |
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| CN (1) | CN207446545U (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108534419A (en) * | 2018-06-12 | 2018-09-14 | 中联信达（天津）科技发展有限公司 | A kind of artificial snow-making nucleon gas spraying device |
| CN109396454A (en) * | 2018-12-24 | 2019-03-01 | 南通金源智能技术有限公司 | A kind of 3D printing twin-stage aerosolization nozzle |
| CN109482380A (en) * | 2018-12-24 | 2019-03-19 | 亿川科技(成都)有限责任公司 | A kind of mixed-flow multistage steam atomizer |
| CN110065150A (en) * | 2019-05-24 | 2019-07-30 | 刘文斌 | It is a kind of to apply color device for ceramic surface synergy |
| CN110757240A (en) * | 2019-11-04 | 2020-02-07 | 深圳市普林司顿模具塑胶有限公司 | Emulsion spray cooling processing technology of mould and processing machine tool thereof |
| CN112808476A (en) * | 2019-11-15 | 2021-05-18 | 中国石油天然气集团有限公司 | Nozzle atomization effect strengthening device and nozzle |
| CN113522177A (en) * | 2021-06-30 | 2021-10-22 | 江苏新化化工有限公司 | Reactor for improving hydration reaction effect of propylene |
| CN113522178A (en) * | 2021-06-30 | 2021-10-22 | 江苏新化化工有限公司 | System for propylene hydration reaction prepares isopropanol |
| CN114308822A (en) * | 2021-12-28 | 2022-04-12 | 西安奕斯伟材料科技有限公司 | Two-fluid nozzle and cleaning device |
-
2017
- 2017-10-09 CN CN201721323171.3U patent/CN207446545U/en not_active Expired - Fee Related
Cited By (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108534419A (en) * | 2018-06-12 | 2018-09-14 | 中联信达（天津）科技发展有限公司 | A kind of artificial snow-making nucleon gas spraying device |
| CN108534419B (en) * | 2018-06-12 | 2023-12-26 | 中联信达（天津）科技发展有限公司 | Nuclear air spraying device for snow making |
| CN109482380B (en) * | 2018-12-24 | 2023-11-21 | 亿川科技(成都)有限责任公司 | Mixed-flow type multistage steam atomizing nozzle |
| CN109396454A (en) * | 2018-12-24 | 2019-03-01 | 南通金源智能技术有限公司 | A kind of 3D printing twin-stage aerosolization nozzle |
| CN109482380A (en) * | 2018-12-24 | 2019-03-19 | 亿川科技(成都)有限责任公司 | A kind of mixed-flow multistage steam atomizer |
| CN110065150A (en) * | 2019-05-24 | 2019-07-30 | 刘文斌 | It is a kind of to apply color device for ceramic surface synergy |
| CN110757240A (en) * | 2019-11-04 | 2020-02-07 | 深圳市普林司顿模具塑胶有限公司 | Emulsion spray cooling processing technology of mould and processing machine tool thereof |
| CN110757240B (en) * | 2019-11-04 | 2022-03-22 | 深圳市普林司顿模具塑胶有限公司 | Emulsion spray cooling processing technology of mould and processing machine tool thereof |
| CN112808476A (en) * | 2019-11-15 | 2021-05-18 | 中国石油天然气集团有限公司 | Nozzle atomization effect strengthening device and nozzle |
| CN113522177A (en) * | 2021-06-30 | 2021-10-22 | 江苏新化化工有限公司 | Reactor for improving hydration reaction effect of propylene |
| CN113522178B (en) * | 2021-06-30 | 2022-06-17 | 江苏新化化工有限公司 | System for propylene hydration reaction prepares isopropanol |
| CN113522177B (en) * | 2021-06-30 | 2022-08-16 | 江苏新化化工有限公司 | Reactor for improving hydration reaction effect of propylene |
| CN113522178A (en) * | 2021-06-30 | 2021-10-22 | 江苏新化化工有限公司 | System for propylene hydration reaction prepares isopropanol |
| CN114308822A (en) * | 2021-12-28 | 2022-04-12 | 西安奕斯伟材料科技有限公司 | Two-fluid nozzle and cleaning device |
| CN114308822B (en) * | 2021-12-28 | 2024-02-13 | 西安奕斯伟材料科技股份有限公司 | Two-fluid nozzle and cleaning device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180605 Termination date: 20181009 |
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| CF01 | Termination of patent right due to non-payment of annual fee |