CN107859510A - A kind of aqueous vapor well atomizing spray component - Google Patents

A kind of aqueous vapor well atomizing spray component Download PDF

Info

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
Authority
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.)
Withdrawn
Application number
CN201710983385.1A
Other languages
Chinese (zh)
Inventor
陈磊
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to CN201710983385.1A priority Critical patent/CN107859510A/en
Publication of CN107859510A publication Critical patent/CN107859510A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • EFIXED CONSTRUCTIONS
    • E21EARTH OR ROCK DRILLING; MINING
    • E21BEARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/34Arrangements for separating materials produced by the well
    • E21B43/38Arrangements 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

A kind of aqueous vapor well atomizing spray component
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).
CN201710983385.1A 2017-10-20 2017-10-20 A kind of aqueous vapor well atomizing spray component Withdrawn CN107859510A (en)

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
CN107859510A true CN107859510A (en) 2018-03-30

Family

ID=61696764

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710983385.1A Withdrawn CN107859510A (en) 2017-10-20 2017-10-20 A kind of aqueous vapor well atomizing spray component

Country Status (1)

Country Link
CN (1) CN107859510A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
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

Cited By (1)

* Cited by examiner, † Cited by third party
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

Similar Documents

Publication Publication Date Title
CN104759369B (en) A kind of steam atomization nozzle
CN100478088C (en) Nozzle and method for washing gas turbine compressors
CN100496643C (en) Closed type middle and low pressure water mist sprayer with single spraying nozzle
US20220040722A1 (en) Air-assisted electrostatic ultrasonic atomization nozzle and method
JP5500475B2 (en) Two-fluid nozzle
CN204620263U (en) A kind of aqueous vapor well steam atomization injector
CN216094330U (en) Atomizing spray head for air purification site
CN104759365B (en) A kind of quick air collecting pipe of drainage underground
CN105855078A (en) Centrifugal nozzle with multihole cyclone wall and spray method
CN204620253U (en) A kind of down-hole gas production vortex atomizing nozzle
JP2008126200A (en) Nozzle device
CN204620258U (en) Drainage underground gas production nozzle
CN104759366B (en) A kind of rotational flow atomized spray injector
CN107859510A (en) A kind of aqueous vapor well atomizing spray component
CN106731356A (en) A kind of suppressing dust with dry mist equipment
CN107816338A (en) Gas reservoir gas production tubing string
CN104785392B (en) Gas reservoir exploitation drive nozzle
CN204627558U (en) Drainage underground gas production system
CN112774891A (en) Double-fluid nozzle
CN204627559U (en) A kind of pressure swirl water drainage gas production device
CN107630695A (en) Oil mining construction spray structure
CN204627557U (en) A kind of aqueous vapor well Fast Algorithm for Mining device
CN113464981B (en) Air atomizing nozzle for enhancing atomizing effect
JPH0434000B2 (en)
CN107587864A (en) A kind of gas well exploitation nozzle

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
WW01 Invention patent application withdrawn after publication
WW01 Invention patent application withdrawn after publication

Application publication date: 20180330