CN207379703U - The separation screening device of wind-tunnel trace particle - Google Patents

The separation screening device of wind-tunnel trace particle Download PDF

Info

Publication number
CN207379703U
CN207379703U CN201721267419.9U CN201721267419U CN207379703U CN 207379703 U CN207379703 U CN 207379703U CN 201721267419 U CN201721267419 U CN 201721267419U CN 207379703 U CN207379703 U CN 207379703U
Authority
CN
China
Prior art keywords
separation screening
trace particle
wind
barrel
pipe road
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.)
Expired - Fee Related
Application number
CN201721267419.9U
Other languages
Chinese (zh)
Inventor
赵维明
李昱
朱本华
岳廷瑞
马军
梁磊
段丕轩
尹熹伟
姜德龙
刘垒
左承林
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.)
Low Speed Aerodynamics Institute of China Aerodynamics Research and Development Center
Original Assignee
Low Speed Aerodynamics Institute of China Aerodynamics Research and Development Center
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 Low Speed Aerodynamics Institute of China Aerodynamics Research and Development Center filed Critical Low Speed Aerodynamics Institute of China Aerodynamics Research and Development Center
Priority to CN201721267419.9U priority Critical patent/CN207379703U/en
Application granted granted Critical
Publication of CN207379703U publication Critical patent/CN207379703U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Separating Particles In Gases By Inertia (AREA)
  • Aerodynamic Tests, Hydrodynamic Tests, Wind Tunnels, And Water Tanks (AREA)

Abstract

The utility model discloses a kind of separation screening device of wind-tunnel trace particle, including centrifugal blower, gas mixing pipe road and separation screening storehouse;Separation screening storehouse includes:Barrel, head cover, bottom cover, arranged on the mixed gas input port of barrel bottom, the trace particle delivery outlet on head cover and the liquids recovery mouth on bottom cover;The mixed gas input port in separation screening storehouse is connected by gas mixing pipe road with the output terminal of centrifugal blower, and gas mixing pipe road and the barrel in separation screening storehouse are tangent;Gas mixing pipe road is equipped with tracer vapor inlet port.The separation screening device of the utility model wind-tunnel trace particle, it can screen the trace particle of droplet morphology, big droplet particles are intercepted, the uniform droplet particle of output size, exclude interference of the different size particle to detection image, ensure the uniform and stability in flow field, improve the accuracy of result of calculation, big drop can also be avoided to be condensed at camera lens, laser exit.

Description

The separation screening device of wind-tunnel trace particle
Technical field
The utility model is related to the separation screening devices of wind-tunnel trace particle.
Background technology
PIV(Particle Image Velocimetry particle image velocimetries)Technology is to grow up the end of the seventies A kind of transient state, multiple spot, non-contacting hydrodynamics speed-measuring method, can synchronization record space velocity profile information, Flow field space structure and flow behavior are measured, is to solve complex flowfield to show and the important means of analysis of flow characteristics.In wind-tunnel Middle application PIV technologies, it is glitch-free in stream field, invisible complicated or even microcosmic flow phenomenon becomes For visual flow image or animation, it can not only qualitatively observe flow field situation, and can quantitatively provide fluid field pressure, speed The air force knowledge in Flight Vehicle Design is grasped and solved to the characteristics such as degree to recognizing the essence and flow mechanism of flow phenomenon, Topic plays an important roll.
Representative of the trace particle as fluid velocity, it is the key that one of PIV technologies to generate and launch.Drop is common Trace particle form, i.e. trace particle enters flow field with drops, but if the droplet particles size into flow field cannot Uniformity can influence the uniform and stability in flow field, can generate interference to detection image, can influence the accurate of result of calculation Degree, and big drop easily condenses at camera lens, laser exit.
Utility model content
The purpose of this utility model is to provide a kind of separation screening devices of wind-tunnel trace particle, can be to drop shape The trace particle of state is screened, and big droplet particles is intercepted, the uniform droplet particle of output size, is excluded different Interference of the sized particles to detection image ensures the uniform and stability in flow field, improves the accuracy of result of calculation, can also avoid Big drop condenses at camera lens, laser exit.
To achieve the above object, the technical solution of the utility model is to design a kind of separation screening of wind-tunnel trace particle Device, including centrifugal blower, gas mixing pipe road and separation screening storehouse;
The separation screening storehouse includes:Cylindric barrel is vertically arranged, by the horizontal head cover of barrel top closure, by barrel bottom The horizontal bottom cover of closing, arranged on the mixed gas input port of barrel bottom, the trace particle delivery outlet on head cover, Yi Jishe In the liquids recovery mouth on bottom cover;The trace particle delivery outlet heart coaxial with barrel;
The gas mixing pipe road is horizontal square tube type, and separation screening storehouse and centrifugal blower are divided into gas mixing pipe road both ends, is separated The mixed gas input port in screening storehouse is connected by gas mixing pipe road with the output terminal of centrifugal blower, and gas mixing pipe road and separation screening The barrel in storehouse is tangent;Gas mixing pipe road is equipped with tracer vapor inlet port.
Preferably, the gas mixing pipe road is vertically arranged side plate by horizontal bottom plate, horizontal top plate and a pair and surrounds;This is to side plate bag It includes:The first tangent side plate and second side plate parallel with the first side plate with separation screening storehouse barrel;Plate top surface is with separating The top surface of screening orlop lid maintains an equal level, and tracer vapor inlet port is arranged on bottom plate;The spacing of bottom plate and top plate is not more than bolter Select the half of storehouse barrel height;The spacing of first side plate and the second side plate is not more than the radius of separation screening storehouse barrel.
Preferably, the internal diameter of the trace particle delivery outlet is a quarter of barrel internal diameter.
Preferably, the trace particle delivery outlet is circumscribed with trace particle efferent duct.
Preferably, the liquids recovery mouth is circumscribed with liquid recovery tube.
Preferably, the tracer vapor inlet port is circumscribed with tracer steam pipeline.
Preferably, the trace particle delivery outlet is to be vertically arranged circular tube shaped.
Preferably, the liquids recovery mouth is equipped with strainer.
Preferably, the centrifugal blower, gas mixing pipe road and separation screening storehouse are fixed on same supporting structure.
Preferably, the centrifugal blower, gas mixing pipe road and separation screening storehouse are fixed on a horizontal support plate.
The advantages of the utility model and advantageous effect are:A kind of separation screening device of wind-tunnel trace particle is provided, It can screen the trace particle of droplet morphology, big droplet particles be intercepted, the uniform droplet of output size Particle excludes interference of the different size particle to detection image, ensures the uniform and stability in flow field, improves the standard of result of calculation Exactness can also avoid big drop from being condensed at camera lens, laser exit.
Tracer steam is generated by evaporator, and tracer steam enters gas mixing pipe road by tracer vapor inlet port, meanwhile, Air is blasted gas mixing pipe road by centrifugal blower, and tracer steam is mixed with air in gas mixing pipe road, and edge is tangent with barrel By mixed gas input port, into separation screening storehouse, mixed gas is rotated at a high speed in separation screening storehouse, collided, and is mixed in direction The tracer closed in gas is condensed into droplet morphology, and big droplet particles are intercepted in separation screening storehouse, uniform in size consistent Droplet particle is discharged by trace particle delivery outlet, defeated by liquids recovery mouth after the big droplet particles aggregation in separation screening storehouse Go out.
Description of the drawings
Fig. 1 is the schematic diagram of the utility model.
Specific embodiment
With reference to the accompanying drawings and examples, specific embodiment of the present utility model is further described.Implement below Example is only used for clearly illustrating the technical solution of the utility model, and the protection model of the utility model cannot be limited with this It encloses.
The utility model specific implementation technical solution be:
As shown in Figure 1, a kind of separation screening device of wind-tunnel trace particle, including centrifugal blower 1,2 and of gas mixing pipe road Separation screening storehouse 3;
The separation screening storehouse 3 includes:Cylindric barrel is vertically arranged, by the horizontal head cover of barrel top closure, by barrel bottom The horizontal bottom cover that end seal is closed, arranged on the mixed gas input port of barrel bottom, the trace particle delivery outlet 4 on head cover, with And the liquids recovery mouth on bottom cover;The heart coaxial with barrel of trace particle delivery outlet 4;
The gas mixing pipe road 2 is horizontal square tube type, and separation screening storehouse 3 and centrifugal blower 1 are divided into 2 both ends of gas mixing pipe road, The mixed gas input port in separation screening storehouse 3 is connected by gas mixing pipe road 2 with the output terminal of centrifugal blower 1, and gas mixing pipe road 2 with The barrel in separation screening storehouse 3 is tangent;Gas mixing pipe road 2 is equipped with tracer vapor inlet port.
Preferably, the gas mixing pipe road 2 is vertically arranged side plate by horizontal bottom plate, horizontal top plate and a pair and surrounds;This is to side plate Including:The first tangent side plate and second side plate parallel with the first side plate with 3 barrel of separation screening storehouse;Plate top surface with The top surface of 3 bottom cover of separation screening storehouse maintains an equal level, and tracer vapor inlet port is arranged on bottom plate;The spacing of bottom plate and top plate, which is not more than, divides Half from screening 3 barrel height of storehouse;The spacing of first side plate and the second side plate is not more than the radius of 3 barrel of separation screening storehouse.
Preferably, the internal diameter of the trace particle delivery outlet 4 is a quarter of barrel internal diameter.
Preferably, the trace particle delivery outlet 4 is circumscribed with trace particle efferent duct 5.
Preferably, the liquids recovery mouth is circumscribed with liquid recovery tube 6.
Preferably, the tracer vapor inlet port is circumscribed with tracer steam pipeline 7.
Preferably, the trace particle delivery outlet 4 is to be vertically arranged circular tube shaped.
Preferably, the liquids recovery mouth is equipped with strainer.
Preferably, same supporting structure is fixed in the centrifugal blower 1, gas mixing pipe road 2 and separation screening storehouse 3(Such as horizontal Support plate)On.
Tracer steam is generated by evaporator, and tracer steam enters gas mixing pipe road 2 by tracer vapor inlet port, together When, air is blasted gas mixing pipe road 2 by centrifugal blower 1, and tracer steam is mixed with air in gas mixing pipe road 2, and edge and barrel Tangent direction is by mixed gas input port, into separation screening storehouse 3, mixed gas in separation screening storehouse 3 at a high speed rotation, It collides, the tracer in mixed gas is condensed into droplet morphology, and big droplet particles are intercepted in separation screening storehouse 3, and size is equal Even consistent droplet particle is discharged by trace particle delivery outlet 4, by liquid after the big droplet particles aggregation in separation screening storehouse 3 Body recovery port exports.
The separation screening device of the utility model wind-tunnel trace particle can sieve the trace particle of droplet morphology Big droplet particles are intercepted, the uniform droplet particle of output size by choosing, exclude different size particle to detection image Interference, ensure the uniform and stability in flow field, improve the accuracy of result of calculation, can also avoid big drop camera lens, It is condensed at laser exit.
The above is only the preferred embodiment of the utility model, it is noted that for the common skill of the art For art personnel, on the premise of the utility model technical principle is not departed from, several improvements and modifications can also be made, these change The scope of protection of the utility model is also should be regarded as into retouching.

Claims (10)

1. the separation screening device of wind-tunnel trace particle, which is characterized in that including centrifugal blower, gas mixing pipe road and separation screening Storehouse;
The separation screening storehouse includes:Cylindric barrel is vertically arranged, by the horizontal head cover of barrel top closure, by barrel bottom end closure Horizontal bottom cover, arranged on the mixed gas input port of barrel bottom, trace particle delivery outlet on the head cover and bottom of arranged on The liquids recovery mouth covered;The trace particle delivery outlet heart coaxial with barrel;
The gas mixing pipe road is horizontal square tube type, and separation screening storehouse and centrifugal blower are divided into gas mixing pipe road both ends, separation screening The mixed gas input port in storehouse is connected by gas mixing pipe road with the output terminal of centrifugal blower, and gas mixing pipe road and separation screening storehouse Barrel is tangent;Gas mixing pipe road is equipped with tracer vapor inlet port.
2. the separation screening device of wind-tunnel trace particle according to claim 1, which is characterized in that the gas mixing pipe road Side plate is vertically arranged by horizontal bottom plate, horizontal top plate and a pair to surround;This includes side plate:Tangent with separation screening storehouse barrel Side plate and second side plate parallel with the first side plate;The top surface of plate top surface and separation screening orlop lid maintains an equal level, tracer Vapor inlet port is arranged on bottom plate;The spacing of bottom plate and top plate is not more than the half of separation screening storehouse barrel height;First side plate It is not more than the radius of separation screening storehouse barrel with the spacing of the second side plate.
3. the separation screening device of wind-tunnel trace particle according to claim 2, which is characterized in that the trace particle The internal diameter of delivery outlet is a quarter of barrel internal diameter.
4. the separation screening device of wind-tunnel trace particle according to claim 3, which is characterized in that the trace particle Delivery outlet is circumscribed with trace particle efferent duct.
5. the separation screening device of wind-tunnel trace particle according to claim 4, which is characterized in that the liquids recovery Mouth is circumscribed with liquid recovery tube.
6. the separation screening device of wind-tunnel trace particle according to claim 5, which is characterized in that the tracer steams Vapour input port is circumscribed with tracer steam pipeline.
7. the separation screening device of wind-tunnel trace particle according to claim 6, which is characterized in that the trace particle Delivery outlet is to be vertically arranged circular tube shaped.
8. the separation screening device of wind-tunnel trace particle according to claim 7, which is characterized in that the liquids recovery Mouth is equipped with strainer.
9. the separation screening device of wind-tunnel trace particle according to claim 8, which is characterized in that the centrifugation wind Machine, gas mixing pipe road and separation screening storehouse are fixed on same supporting structure.
10. the separation screening device of wind-tunnel trace particle according to claim 9, which is characterized in that the centrifugation wind Machine, gas mixing pipe road and separation screening storehouse are fixed on a horizontal support plate.
CN201721267419.9U 2017-09-29 2017-09-29 The separation screening device of wind-tunnel trace particle Expired - Fee Related CN207379703U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201721267419.9U CN207379703U (en) 2017-09-29 2017-09-29 The separation screening device of wind-tunnel trace particle

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201721267419.9U CN207379703U (en) 2017-09-29 2017-09-29 The separation screening device of wind-tunnel trace particle

Publications (1)

Publication Number Publication Date
CN207379703U true CN207379703U (en) 2018-05-18

Family

ID=62337687

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201721267419.9U Expired - Fee Related CN207379703U (en) 2017-09-29 2017-09-29 The separation screening device of wind-tunnel trace particle

Country Status (1)

Country Link
CN (1) CN207379703U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111077339A (en) * 2019-12-26 2020-04-28 哈尔滨工程大学 PIV particle recovery unit
CN111721495A (en) * 2020-06-16 2020-09-29 中国人民解放军国防科技大学 Novel particle of nano particle plane laser scattering experiment generates device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111077339A (en) * 2019-12-26 2020-04-28 哈尔滨工程大学 PIV particle recovery unit
CN111077339B (en) * 2019-12-26 2022-02-22 哈尔滨工程大学 PIV particle recovery unit
CN111721495A (en) * 2020-06-16 2020-09-29 中国人民解放军国防科技大学 Novel particle of nano particle plane laser scattering experiment generates device

Similar Documents

Publication Publication Date Title
CN207379703U (en) The separation screening device of wind-tunnel trace particle
CN104353310B (en) A kind of gas-liquid separator applied in hydrogenation plant
CN110031046A (en) A kind of gas-liquid two-phase flow measuring system
CN207379704U (en) The generating means of wind-tunnel trace particle
CN104128047A (en) Fine particulate matter removal device and method with combined action of acoustic agglomeration and cyclone separation
Morimoto et al. Classification of ultra fine powder by a new pneumatic type classifier
US10663429B2 (en) Device for collecting semi-volatile or non-volatile substrate
CN102680203A (en) Micro-channel gas-liquid two-phase flow voidage measuring device and method
CN107764702A (en) Trace particle screening plant
CN109506724A (en) A kind of gas-liquid two-phase flow metering device and method
CN105709509A (en) Steam-water separation device
Gustavsson A tutorial review of the basic theory for and practical aspects of aerosol chambers
CN207114272U (en) A kind of air particle comprehensively sampling device
JP5427141B2 (en) Apparatus and method for measuring particles in liquid
CN107748053A (en) Trace displaying particle generator
CN105854330A (en) Cyclone atomizing vertical sieve plate
CN209094553U (en) A kind of horizontal atomizer of 3D printing metal powder production
CN209387075U (en) Based on the natural gas moisture measuring device for being mutually separated in pipe with mutually separating
Lim et al. Collection efficiency and particle loss of virtual impactors with different methods of increasing pressure drop
CN205613164U (en) Steam and water separator
CN202155115U (en) Baffle type vapor-liquid separator
CN218524424U (en) Particulate matter removing device
US2875823A (en) Apparatus for converting liquids, solutions, emulsions, suspensions, and the like int dry powders
RAVILEVNA NUMERICAL STUDY OF DRIP ENTRAINMENT IN BUBBLING APPARATUSES
CN107281825A (en) A kind of whirlpool formula demister

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20180518

Termination date: 20180929