CN107859510A - A kind of aqueous vapor well atomizing spray component - Google Patents
A kind of aqueous vapor well atomizing spray component Download PDFInfo
- Publication number
- CN107859510A CN107859510A CN201710983385.1A CN201710983385A CN107859510A CN 107859510 A CN107859510 A CN 107859510A CN 201710983385 A CN201710983385 A CN 201710983385A CN 107859510 A CN107859510 A CN 107859510A
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- CN
- China
- Prior art keywords
- gas
- hole
- core body
- housing
- liquid
- Prior art date
- 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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- 239000007921 spray Substances 0.000 title claims abstract description 17
- 239000007788 liquid Substances 0.000 claims abstract description 88
- 238000009792 diffusion process Methods 0.000 claims description 9
- 238000005452 bending Methods 0.000 claims description 4
- 230000005514 two-phase flow Effects 0.000 claims description 3
- 239000000203 mixture Substances 0.000 abstract description 33
- 239000012530 fluid Substances 0.000 abstract description 13
- 230000006835 compression Effects 0.000 abstract description 3
- 238000007906 compression Methods 0.000 abstract description 3
- 230000015572 biosynthetic process Effects 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 description 5
- 238000000926 separation method Methods 0.000 description 5
- 238000000889 atomisation Methods 0.000 description 3
- 230000008859 change Effects 0.000 description 3
- 230000003993 interaction Effects 0.000 description 3
- 230000009471 action Effects 0.000 description 2
- 230000002776 aggregation Effects 0.000 description 2
- 238000004220 aggregation Methods 0.000 description 2
- 230000009194 climbing Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000005855 radiation Effects 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 241000521257 Hydrops Species 0.000 description 1
- 206010030113 Oedema Diseases 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
Classifications
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
- E21B43/34—Arrangements for separating materials produced by the well
- E21B43/38—Arrangements for separating materials produced by the well in the well
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Geology (AREA)
- Mining & Mineral Resources (AREA)
- Physics & Mathematics (AREA)
- Environmental & Geological Engineering (AREA)
- Fluid Mechanics (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Nozzles (AREA)
Abstract
The invention discloses a kind of aqueous vapor well atomizing spray component, including core body and housing, the end of housing is provided with spurt hole, the inwall formation air inlet cavity of internal conical surface, internal conical surface and housing is set in core body one end, and the core body other end is provided with the through hole of face spurt hole, multiple swirl vanes are installed on through-hole wall, the inwall of through hole and core body forms eddy flow cavity, and portion is provided with the convective tank of annular in the core, and two stomatas are symmetricly set on the both ends of convective tank.When the gas-fluid two-phase mixture in gas well is begun to ramp up under the promotion of borehole pressure, gas-liquid mixture enters in inlet chamber body and carries out volume compression to it by internal conical surface excessively, and then improve the flowing velocity of gas-liquid mixture, when gas-liquid mixture enters eddy flow cavity, fluid contacts with each other with swirl vane, fluid driven is rotated by swirl vane, finally thrown away from spurt hole gas-liquid mixture using centrifugal force caused by rotation.
Description
Technical field
The present invention relates to underground gas production field, in particular to a kind of aqueous vapor well atomizing spray component.
Background technology
The liquid that gas well shaft bottom just starts to occur during a small amount of hydrops in pit shaft can utilize the climbing power band of itself by gas
Go out pit shaft, gas well can also be produced normally, and at this moment the most stream flow velocity of gas well air-flow is referred to as gas well and takes liquid critical flow velocity, corresponding gas
Flow is referred to as gas well and takes liquid critical flow;When the actual flow velocity of gas in pit shaft is less than critical flow velocity, air-flow cannot be by well
Interior liquid takes well head out of using the climbing power of itself.And in the prior art, generally use emple hole, liquid obtains after over pressurizeed
Larger kinetic energy is obtained, liquid will be ejected with very big speed after nozzle, be hindered in surface tension of liquid, viscosity and air
Under power interaction, liquid by drippage, smooth flow, it is wavy flow to spray flow and gradually change, finally conveniently realize the two-phase of gas-liquid
Separation;But because the current discharged in emple hole have surface tension, therefore during liquid is changed into spray flow,
Need constantly to meet that when ejecting with very high speed with surrounding air friction occurs for liquid and separates to underground pressurization
Atomization, then the air pressure of underground is higher, and the safety reliability faced during gas production is lower, easily triggers security incident.
The content of the invention
It is an object of the invention to provide a kind of aqueous vapor well atomizing spray component, reaches and improves gas production safety reliability
Purpose.
The purpose of the present invention is achieved through the following technical solutions:
A kind of aqueous vapor well atomizing spray component, including core body and the housing that is set in outside core body, the end of housing is set
There is spurt hole, internal conical surface is set in described core body one end, and the inwall of the internal conical surface and housing forms air inlet cavity, core
The body other end is provided with the through hole of face spurt hole, and multiple swirl vanes, and the inwall of through hole and core body are provided with through-hole wall
Form eddy flow cavity;Also include two to be staggered the two of core body axis through housing and the stomata of core body, two stomatas
Side, and the outlet side of the stomata is in the opposite direction bending of the gas liquid two-phase flow along core body.Nozzle is fixed on going out for gas well
Gas end, when the gas-fluid two-phase mixture in gas well is begun to ramp up under the promotion of borehole pressure, gas-liquid mixture enters air inlet
Volume compression is carried out to it by internal conical surface after in cavity, and then improves the flowing velocity of gas-liquid mixture, in gas-liquid mixed
When thing enters eddy flow cavity, fluid contacts with each other with swirl vane, is rotated fluid driven by swirl vane, finally utilizes rotation
Centrifugal force caused by turning throws away gas-liquid mixture from spurt hole;
When the flow very little of gas-liquid mixture, when centrifugal force is more than surface tension of liquid, it is by what is thrown away in spurt hole
Larger-size big drop, now liquid directly split into drop;When flow increases, liquid is more into quantity by rotary splitter
Thread jet, the fluidised form of liquid is extremely unstable, liquid leave rotating vane end and by spurt hole spray a segment distance after, directly
Connect and rubbing action occurs and is separated into droplet with air, form mitoschisis drop, when flow continues increase, brin is mutual
Connect into liquid film, as liquid film is outwards extended to thinner liquid film, and so that friction occurs for the air of very high speed and surrounding and
Separation atomization, drop is split into by film-form so that vaporific gas-liquid mixture is sprayed in spurt hole, while in normal use
The gas-liquid two-phase in gas well is extracted under operating pressure, to facilitate the gas-liquid separation process in later stage;
Wherein by injecting steam to stomata, the steam poured into enters vortex chamber as working media along the inwall of stomata
In body, and bent in the end of stomata to the direction that gas-liquid mixture moves, i.e. steam is relatively moved with gas-liquid two-phase, is steamed
The surface tension of resistance caused by vapour and gas-liquid mixture, viscous interaction, swiftly flowing steam and relatively low speed
The gas-liquid mixture or liquid film of motion mutually produce vibrations, friction so that liquid is sprayed by drippage, smooth flow, wavy flow direction
Stream gradually transformation, final liquid crushing is tiny liquid;Then rise rapidly by the CENTRIFUGAL ACCELERATING of swirl vane again, it is convenient
Gas-liquid quickly independently rises outside discharge well, while reaches the purpose for improving gas production safety reliability.
Further, the end of the core body is provided with annular groove, and the eddy flow cavity passes through circular hole and annular groove
Connection.Annular space is formed between annular groove and the inwall of housing, gas-liquid mixture passes through circular hole when that will pass through swirl vane
Enter in annular space, reduce gas-liquid mixture to a certain extent and move speed close to the fluid layer of its inner wall section in eddy flow cavity
Degree, avoids gas-liquid mixture from directly being impacted to swirl vane, prevents the rotation of influence fluid after swirl vane Local Damaged,
Improve the atomizing effect of gas-liquid mixture in spurt hole.Also include the diffusion hole for being opened in shell end, the diffusion hole and spray
The outlet side connection of discharge orifice.The misty liquid droplets range of scatter projected by spurt hole is larger, is unfavorable on well operation to misty liquid droplets
Collection, the diffusion hole connected with spurt hole can to radiation spray misty liquid droplets carry out gathering aggregation, be allowed to be directly entered well
In accommodating chamber in upper device.
The present invention compared with prior art, has the following advantages and advantages:
1st, the present invention when flow continue increase when, brin is interconnected to liquid film, with liquid film be outwards extended to it is thinner
Liquid film, and friction is occurred with the air of surrounding with very high speed and separates atomization, drop is split into by film-form so that spraying
Discharge orifice sprays vaporific gas-liquid mixture, while extracts the gas-liquid two-phase in gas well under the operating pressure of normal use,
To facilitate the gas-liquid separation process in later stage.
Brief description of the drawings
Accompanying drawing described herein is used for providing further understanding the embodiment of the present invention, forms one of the application
Point, do not form the restriction to the embodiment of the present invention.In the accompanying drawings:
Fig. 1 is schematic structural view of the invention;
Fig. 2 is the structural representation of housing;
Fig. 3 is the structural representation of core body;
Mark and corresponding parts title in accompanying drawing:
1- housings, 2- air inlets cavity, 3- internal conical surfaces, 4- core bodys, 5- eddy flows cavity, 6- annular grooves, 7- swirl vanes,
8- spurt holes, 9- diffusion holes, 10- stomatas.
Embodiment
For the object, technical solutions and advantages of the present invention are more clearly understood, with reference to embodiment and accompanying drawing, to this
Invention is described in further detail, and exemplary embodiment of the invention and its explanation are only used for explaining the present invention, do not make
For limitation of the invention.
Embodiment 1
As shown in Figures 1 to 3, the present embodiment includes core body 4 and the housing 1 being set in outside core body 4, and the end of housing 1 is set
There is spurt hole 8, internal conical surface 3 is set in described one end of core body 4, and the inwall of the internal conical surface 3 and housing 1 forms inlet chamber
Body 2, the other end of core body 4 are provided with the through hole of face spurt hole 8, and multiple swirl vanes 7, and through hole and core are provided with through-hole wall
The inwall of body 4 forms eddy flow cavity 5;Also include two staggeredly to set through housing 1 and the stomata 10 of core body 4, two stomatas 10
Put in the both sides of the axis of core body 4, and the outlet side of the stomata 10 is in the opposite direction bending of the gas liquid two-phase flow along core body 4.
Nozzle is fixed on to the outlet side of gas well, when the gas-fluid two-phase mixture in gas well is opened under the promotion of borehole pressure
Begin to rise, gas-liquid mixture by internal conical surface 3 carries out it volume compression after entering in air inlet cavity 2, and then improves gas
The flowing velocity of liquid mixture, when gas-liquid mixture enters eddy flow cavity 5, fluid contacts with each other with swirl vane 7, passes through rotation
Stream blade 7 rotates fluid driven, is finally thrown away from spurt hole 8 gas-liquid mixture using centrifugal force caused by rotation;When
During the flow very little of gas-liquid mixture, when centrifugal force is more than surface tension of liquid, by being thrown away in spurt hole 8 to be larger-size
Big drop, now liquid directly split into drop;When flow increases, liquid thread is penetrated by rotary splitter into a fairly large number of
Stream, the fluidised form of liquid is extremely unstable, after liquid leaves rotating vane end and sprays a segment distance by spurt hole 8, directly with sky
Gas occurs rubbing action and is separated into droplet, forms mitoschisis drop, and when flow continues increase, brin is interconnected to
Liquid film, as liquid film is outwards extended to thinner liquid film, and friction is occurred with the air of surrounding with very high speed and separates mist
Change, drop is split into by film-form so that vaporific gas-liquid mixture is sprayed in spurt hole 8, while in the work of normal use
The gas-liquid two-phase in gas well is extracted under pressure, to facilitate the gas-liquid separation process in later stage;By injecting steam to stomata 10,
The steam poured into is entered in eddy flow cavity 5 as inwall of the working media along stomata 10, and in the end of stomata 10 to gas-liquid
The direction bending of mixture movement, i.e., steam is relatively moved with gas-liquid two-phase, resistance caused by steam and gas-liquid mixture
Surface tension, viscous interaction, the gas-liquid mixture or liquid film of the motion of swiftly flowing steam and relatively low speed
Mutually produce vibrations, friction so that liquid by drippage, smooth flow, it is wavy flow to spray flow and gradually change, final liquid crushing is
Tiny liquid;Then rise rapidly by the CENTRIFUGAL ACCELERATING of swirl vane 7 again, facilitate gas-liquid quickly independently to rise discharge well
Outside, at the same reach improve gas production safety reliability purpose.
Wherein, the end of the core body 4 is provided with annular groove 6, and the eddy flow cavity 5 passes through circular hole and annular groove 6
Connection.Form annular space between the inwall of annular groove 6 and housing 1, gas-liquid mixture is will be by swirl vane 7 when by circle
Hole is entered in annular space, is reduced gas-liquid mixture to a certain extent and is transported in eddy flow cavity 5 close to the fluid layer of its inner wall section
Dynamic speed, avoids gas-liquid mixture from directly being impacted to swirl vane 7, influences fluid after preventing the Local Damaged of swirl vane 7
Rotation, improve spurt hole 8 in gas-liquid mixture atomizing effect.
Also include the diffusion hole 9 for being opened in the end of housing 1, the diffusion hole 9 connects with the outlet side of spurt hole 8.By spraying
The misty liquid droplets range of scatter that discharge orifice 8 projects is larger, is unfavorable for collection of the operation to misty liquid droplets on well, is connected with spurt hole 8
Diffusion hole 9 can to radiation spray misty liquid droplets carry out gathering aggregation, be allowed to be directly entered in the accommodating chamber on well in device.
Above-described embodiment, the purpose of the present invention, technical scheme and beneficial effect are carried out further
Describe in detail, should be understood that the embodiment that the foregoing is only the present invention, be not intended to limit the present invention
Protection domain, within the spirit and principles of the invention, any modification, equivalent substitution and improvements done etc., all should include
Within protection scope of the present invention.
Claims (2)
1. a kind of aqueous vapor well atomizing spray component, including core body (4) and it is set in the housing (1) of core body (4) outside, housing
(1) end is provided with spurt hole (8), it is characterised in that:Internal conical surface (3), and the inner circle are set in the core body (4) one end
The inwall of the conical surface (3) and housing (1) forms air inlet cavity (2), and core body (4) other end is provided with the through hole of face spurt hole (8), leads to
Multiple swirl vanes (7) are installed, and the inwall of through hole and core body (4) forms eddy flow cavity (5) on the inwall of hole;Also include two
Through housing (1) and the stomata (10) of core body (4), two stomatas (10) are staggered in the both sides of core body (4) axis, and institute
The outlet side of stomata (10) is stated in the opposite direction bending along core body (4) interior gas liquid two-phase flow.
A kind of 2. aqueous vapor well atomizing spray component according to claim 1, it is characterised in that:The end of the core body (4)
Portion is provided with annular groove (6), and the eddy flow cavity (5) is connected by circular hole with annular groove (6);Also include being opened in housing
(1) diffusion hole (9) of end, the diffusion hole (9) connect with the outlet side of spurt hole (8).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710983385.1A CN107859510A (en) | 2017-10-20 | 2017-10-20 | A kind of aqueous vapor well atomizing spray component |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710983385.1A CN107859510A (en) | 2017-10-20 | 2017-10-20 | A kind of aqueous vapor well atomizing spray component |
Publications (1)
Publication Number | Publication Date |
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CN107859510A true CN107859510A (en) | 2018-03-30 |
Family
ID=61696764
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CN201710983385.1A Withdrawn CN107859510A (en) | 2017-10-20 | 2017-10-20 | A kind of aqueous vapor well atomizing spray component |
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CN (1) | CN107859510A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111844401A (en) * | 2020-07-26 | 2020-10-30 | 广东绿富域资源再生科技有限公司 | Brick making curing device and curing method for household garbage incinerator slag |
-
2017
- 2017-10-20 CN CN201710983385.1A patent/CN107859510A/en not_active Withdrawn
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111844401A (en) * | 2020-07-26 | 2020-10-30 | 广东绿富域资源再生科技有限公司 | Brick making curing device and curing method for household garbage incinerator slag |
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Application publication date: 20180330 |