CN104759365B - A kind of quick air collecting pipe of drainage underground - Google Patents

A kind of quick air collecting pipe of drainage underground Download PDF

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Publication number
CN104759365B
CN104759365B CN201510132909.7A CN201510132909A CN104759365B CN 104759365 B CN104759365 B CN 104759365B CN 201510132909 A CN201510132909 A CN 201510132909A CN 104759365 B CN104759365 B CN 104759365B
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CN
China
Prior art keywords
hole
gas
inner core
nozzle
nozzle inner
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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.)
Expired - Fee Related
Application number
CN201510132909.7A
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Chinese (zh)
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CN104759365A (en
Inventor
谭正怀
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Chengdu Zhirong Zhichuang Intellectual Property Operation Co ltd
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Chengdu Laibao Petroleum Equipment Co Ltd
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Priority to CN201510132909.7A priority Critical patent/CN104759365B/en
Publication of CN104759365A publication Critical patent/CN104759365A/en
Application granted granted Critical
Publication of CN104759365B publication Critical patent/CN104759365B/en
Expired - Fee Related legal-status Critical Current
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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05BSPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B3/00Spraying or sprinkling apparatus with moving outlet elements or moving deflecting elements
    • B05B3/02Spraying or sprinkling apparatus with moving outlet elements or moving deflecting elements with rotating elements
    • B05B3/10Spraying or sprinkling apparatus with moving outlet elements or moving deflecting elements with rotating elements discharging over substantially the whole periphery of the rotating member, i.e. the spraying being effected by centrifugal forces
    • B05B3/1007Spraying or sprinkling apparatus with moving outlet elements or moving deflecting elements with rotating elements discharging over substantially the whole periphery of the rotating member, i.e. the spraying being effected by centrifugal forces characterised by the rotating member
    • 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

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  • 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)
  • Manufacturing Of Tubular Articles Or Embedded Moulded Articles (AREA)
  • Nozzles (AREA)

Abstract

The invention discloses a kind of quick air collecting pipe of drainage underground, including nozzle inner core and nozzle housing, the end of nozzle housing is equipped with spurt hole, in nozzle inner core one end, internal conical surface is set, the inner wall of internal conical surface and nozzle housing forms air inlet cavity, the nozzle inner core other end is provided with the through hole of face spurt hole, multiple swirl vanes are installed on through-hole wall, the inner wall of through hole and nozzle inner core forms eddy flow cavity, the convective tank of annular is provided with the middle part of nozzle inner 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, the centrifugal force finally produced using rotation is thrown away gas-liquid mixture from spurt hole.

Description

A kind of quick air collecting pipe of drainage underground
Technical field
The present invention relates to underground gas production field, in particular to a kind of quick air collecting pipe of drainage underground.
Background technology
At home all can be in various degree in most gas wells there is ponding in shaft bottom, for there are the gas of bottom water or side water Well, liquid-gas ratio will gradually increase in recovery process, if adjustment liquid-gas ratio or shaft bottom hydrops exclude well not in time not in time Mouthful, this can cause the normal production of gas well, or even gas well is drowned and causes to stop production, therefore correctly predicted gas well is different degrees of Jacking capacity under liquid content selects the water drainage-gas recovery technology of suitable gas well to have important reality according to the actual conditions of gas well Meaning.
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 known as gas well and takes liquid critical flow velocity, corresponding gas Flow is known 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 being overpressurized 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 the current due to being discharged in emple hole have surface tension, 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 that when gas production is faced is lower, easily triggers security incident.
The content of the invention
It is an object of the invention to provide a kind of quick air collecting pipe of drainage underground, facilitates gas-liquid quickly independently to rise discharge Outside well, while achieve the purpose that to improve gas production safety reliability.
The purpose of the present invention is achieved through the following technical solutions:
A kind of quick air collecting pipe of drainage underground, including nozzle inner core and the nozzle housing that is set in outside nozzle inner core, spray The end of mouth shell is equipped with spurt hole, and internal conical surface is set in described nozzle inner core one end, and outside the internal conical surface and nozzle The inner wall of shell forms air inlet cavity, and the nozzle inner core other end is provided with the through hole of face spurt hole, is provided with through-hole wall multiple Swirl vane, and the inner wall of through hole and nozzle inner core forms eddy flow cavity;Two are further included in nozzle housing and nozzle The stomata of core, is provided with the convective tank of annular in the middle part of nozzle inner core, and two stomatas are symmetricly set on the both ends of convective tank, and institute State the outlet side internal diameter of stomata and successively decrease being radially directed towards along nozzle inner core on the direction in axle center.Nozzle is fixed on to the outlet of gas well 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 inlet chamber Volume compression is carried out to it by internal conical surface after in vivo, and then improves the flowing velocity of gas-liquid mixture, in gas-liquid mixture During into eddy flow cavity, fluid contacts with each other with swirl vane, is rotated fluid driven by swirl vane, finally utilizes rotation The centrifugal force of generation 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, at this time liquid directly split into drop;When flow increases, liquid is more into quantity by rotary splitter Filamentous jet stream, the fluidised form of liquid is extremely unstable, after liquid leaves rotating vane end and sprays a distance by spurt hole, 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 with 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;
The convective tank of annular is wherein provided with the middle part of nozzle inner core, injects air to stomata, the air poured into is in stomata End is compressed, i.e., further increases the jet velocity of air, and stomata is symmetrical arranged along the convective tank of annular, and then has two gas The air stream that hole sprays mutually liquidates, and can be carried out in convective tank a period of time, the gas-liquid mixed of flowing in vortex chamber body Thing mixes under the cylindrical environment that convective tank is formed with air, swiftly flowing air and the gas-liquid of relatively low speed movement Mixture or liquid film mutually produce vibrations, friction so that liquid crushing is tiny liquid;Then again by swirl vane CENTRIFUGAL ACCELERATING rises rapidly, facilitates gas-liquid quickly independently to rise outside discharge well, while reach and improve gas production safety reliability Purpose.
Further, the end of the nozzle inner core is equipped with annular groove, and the eddy flow cavity passes through circular hole and annular Groove connects.Annular space is formed between annular groove and the inner wall of nozzle housing, gas-liquid mixture is when that will pass through swirl vane Entered by circular hole in annular space, reduce stream of the gas-liquid mixture in eddy flow cavity close to its inner wall section to a certain extent Layer movement velocity, avoids gas-liquid mixture from directly causing to impact to swirl vane, influences stream after preventing swirl vane Local Damaged The rotation of body, improves the atomizing effect of gas-liquid mixture in spurt hole.
Further, the diffusion hole for being opened in nozzle housing end, the outlet side of the diffusion hole and spurt hole are further included Connection.The misty liquid droplets range of scatter projected by spurt hole is larger, is unfavorable for collection of the operation to misty liquid droplets on well, with jet flow The misty liquid droplets that the diffusion hole of hole connection can spray radiation carry out gathering aggregation, are allowed to be directly entered the receiving in device on well In chamber.
Compared with prior art, the present invention have 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;
2nd, annular space is formed between annular groove of the invention and the inner wall of nozzle housing, gas-liquid mixture will pass through rotation Entered when flowing blade by circular hole in annular space, reduce gas-liquid mixture to a certain extent in eddy flow cavity close to its inner wall Partial fluid layer movement velocity, avoids gas-liquid mixture from directly causing to impact to swirl vane, prevents swirl vane Local Damaged The rotation of fluid is influenced afterwards, improves the atomizing effect of gas-liquid mixture in spurt hole.
Brief description of the drawings
Attached 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 structure diagram of nozzle housing;
Fig. 3 is the structure diagram of nozzle inner core;
Mark and corresponding parts title in attached drawing:
1- nozzle housings, 2- air inlets cavity, 3- internal conical surfaces, 4- nozzles inner core, 5- eddy flows cavity, 6- annular grooves, 7- Swirl vane, 8- spurt holes, 9- diffusion holes, 10- convective tanks, 11- stomatas.
Embodiment
For the object, technical solutions and advantages of the present invention are more clearly understood, with reference to embodiment and attached 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 Fig. 1 ~ 3, the present embodiment includes nozzle inner core 4 and the nozzle housing 1 being set in outside nozzle inner core 4, spray The end of mouth shell 1 is equipped with spurt hole 8, and internal conical surface 3, and the internal conical surface 3 and spray are set in described 4 one end of nozzle inner core The inner wall of mouth shell 1 forms air inlet cavity 2, and 4 other end of nozzle inner core is provided with the through hole of face spurt hole 8, pacifies on through-hole wall Inner wall equipped with multiple swirl vanes 7, and through hole and nozzle inner core 4 forms eddy flow cavity 5;Further include two and run through nozzle housing 1 and the stomata 11 of nozzle inner core 4, the middle part of nozzle inner core 4 is provided with the convective tank 10 of annular, two stomatas 11 are symmetrical arranged At the both ends of convective tank 10, and the outlet side internal diameter of the stomata 11 is passed being radially directed towards along nozzle inner core 4 on the direction in axle center Subtract.
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, and the centrifugal force finally produced using rotation is thrown away gas-liquid mixture from spurt hole 8;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, at this time liquid directly split into drop;When flow increases, liquid is penetrated by rotary splitter into a fairly large number of filiform Stream, the fluidised form of liquid is extremely unstable, after liquid leaves rotating vane end and sprays a 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 occurs friction 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;Wherein opened at the middle part of nozzle inner core 4 There is the convective tank 10 of annular, inject air to stomata 11, the air poured into is compressed in the end of stomata 11, i.e., further increase is empty The jet velocity of gas, and stomata 11 is symmetrical arranged along the convective tank 10 of annular, and then the air stream phase for thering are two stomatas 11 to spray Mutually liquidate, and can be carried out in convective tank 10 a period of time, the gas-liquid mixture of flowing is in the institute of convective tank 10 in eddy flow cavity 5 Mixed under the cylindrical environment of formation with air, swiftly flowing air and the gas-liquid mixture or liquid of the movement of relatively low speed Film mutually produces vibrations, friction so that liquid crushing is tiny liquid;Then it is fast by the CENTRIFUGAL ACCELERATING of swirl vane 7 again Speed rises, and facilitates gas-liquid quickly independently to rise outside discharge well, while achievees the purpose that to improve gas production safety reliability.
Wherein, the end of the nozzle inner core 4 is equipped with annular groove 6, and the eddy flow cavity 5 is recessed with annular by circular hole Groove 6 connects.Annular space is formed between the inner wall of annular groove 6 and nozzle housing 1, gas-liquid mixture will pass through swirl vane 7 When entered by circular hole in annular space, reduce gas-liquid mixture to a certain extent in eddy flow cavity 5 close to its inner wall section Fluid layer movement velocity, avoid gas-liquid mixture from directly causing to impact to swirl vane 7, after preventing 7 Local Damaged of swirl vane The rotation of fluid is influenced, improves the atomizing effect of gas-liquid mixture in spurt hole 8.
The diffusion hole 9 for being opened in 1 end of nozzle housing is further included, the diffusion hole 9 is connected with the outlet side of spurt hole 8. The misty liquid droplets range of scatter projected by spurt hole 8 is larger, is unfavorable for collection of the operation to misty liquid droplets on well, with spurt hole 8 The misty liquid droplets that the diffusion hole 9 of connection can spray radiation carry out gathering aggregation, are allowed to be directly entered the receiving in device on well In chamber.
Above-described embodiment, has carried out the purpose of the present invention, technical solution and beneficial effect further Describe in detail, it should be understood that the foregoing is merely the embodiment of 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, improvement and etc. done, should all include Within protection scope of the present invention.

Claims (1)

1. a kind of quick air collecting pipe of drainage underground, including nozzle inner core (4) and it is set in the nozzle housing of nozzle inner core (4) outside (1), the end of nozzle housing (1) is equipped with spurt hole (8), it is characterised in that:In described nozzle inner core (4) one end, female cone is set Face (3), and the internal conical surface (3) and the inner wall of nozzle housing (1) form air inlet cavity (2), nozzle inner core (4) other end is opened There is the through hole of face spurt hole (8), three swirl vanes (7) are installed on through-hole wall, and through hole and nozzle inner core (4) is interior Wall forms eddy flow cavity (5);Two are further included through nozzle housing (1) and the stomata (11) of nozzle inner core (4), in nozzle The convective tank (10) of annular is provided with the middle part of core (4), two stomatas (11) are symmetricly set on the both ends of convective tank (10), and described The outlet side internal diameter of stomata (11) successively decreases being radially directed towards along nozzle inner core (4) on the direction in axle center;The nozzle inner core (4) End is equipped with annular groove (6), and the eddy flow cavity (5) is connected by circular hole with annular groove (6);Further include and be opened in spray The diffusion hole (9) of mouth shell (1) end, the diffusion hole (9) connect with the outlet side of spurt hole (8).
CN201510132909.7A 2015-03-26 2015-03-26 A kind of quick air collecting pipe of drainage underground Expired - Fee Related CN104759365B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510132909.7A CN104759365B (en) 2015-03-26 2015-03-26 A kind of quick air collecting pipe of drainage underground

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Application Number Priority Date Filing Date Title
CN201510132909.7A CN104759365B (en) 2015-03-26 2015-03-26 A kind of quick air collecting pipe of drainage underground

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CN104759365A CN104759365A (en) 2015-07-08
CN104759365B true CN104759365B (en) 2018-04-13

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Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104989277A (en) * 2015-07-22 2015-10-21 成都来宝石油设备有限公司 Spray nozzle for improving target oil reservoir pore permeability parameter
CN106761608B (en) * 2017-01-11 2022-11-18 山东科技大学 Liquid drainage and gas production device and method for natural gas underground gas storage
CN109806988B (en) * 2019-04-13 2023-10-03 江苏华威机械制造有限公司 Molten metal jet deposition atomizer capable of preventing nodulation and nozzle blockage

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201671603U (en) * 2010-05-10 2010-12-15 中国石油天然气股份有限公司 Gas well self-lifting dewatering gas producing device
CN201988465U (en) * 2011-02-21 2011-09-28 青岛欧卡玛环保科技有限公司 Spray sprinkler
CN202212297U (en) * 2011-08-15 2012-05-09 上海守望者喷雾智能系统有限公司 Nozzle of external-mixing spray gun
CN204620258U (en) * 2015-03-26 2015-09-09 成都来宝石油设备有限公司 Drainage underground gas production nozzle

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201671603U (en) * 2010-05-10 2010-12-15 中国石油天然气股份有限公司 Gas well self-lifting dewatering gas producing device
CN201988465U (en) * 2011-02-21 2011-09-28 青岛欧卡玛环保科技有限公司 Spray sprinkler
CN202212297U (en) * 2011-08-15 2012-05-09 上海守望者喷雾智能系统有限公司 Nozzle of external-mixing spray gun
CN204620258U (en) * 2015-03-26 2015-09-09 成都来宝石油设备有限公司 Drainage underground gas production nozzle

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Effective date of registration: 20180711

Address after: 610000 Rong Ou, 144 Qingbaijiang Road, Chengdu, Sichuan.

Patentee after: Chengdu Zhirong Zhichuang Intellectual Property Operation Co.,Ltd.

Address before: 610000 1 Zhongli Road, Nordic knowledge city, 3G, Xinzhi Town, Xindu District, Chengdu, Sichuan, 2 floor 13, No. 10,

Patentee before: CHENGDU LAIBAO PETROLEUM EQUIPMENT Co.,Ltd.

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Granted publication date: 20180413

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