CN202410537U - Atomizing gas mixing and refining device - Google Patents

Atomizing gas mixing and refining device Download PDF

Info

Publication number
CN202410537U
CN202410537U CN2011204804812U CN201120480481U CN202410537U CN 202410537 U CN202410537 U CN 202410537U CN 2011204804812 U CN2011204804812 U CN 2011204804812U CN 201120480481 U CN201120480481 U CN 201120480481U CN 202410537 U CN202410537 U CN 202410537U
Authority
CN
China
Prior art keywords
input channel
atomization gas
passage
lodicule
conical shell
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
CN2011204804812U
Other languages
Chinese (zh)
Inventor
吴国清
梁婷
吴振宇
吴超章
刘艳朝
顾进
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.)
CHEMICAL DEFENSE COLLEGE OF PLA
Beihang University
Original Assignee
CHEMICAL DEFENSE COLLEGE OF PLA
Beihang University
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 CHEMICAL DEFENSE COLLEGE OF PLA, Beihang University filed Critical CHEMICAL DEFENSE COLLEGE OF PLA
Priority to CN2011204804812U priority Critical patent/CN202410537U/en
Application granted granted Critical
Publication of CN202410537U publication Critical patent/CN202410537U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Nozzles (AREA)

Abstract

The utility model discloses an atomizing gas mixing and refining device which comprises a pressure reducing cylinder, a main cylinder body, a pressurizing cylinder and a movable propeller blade, wherein the pressure reducing cylinder comprises an atomizing gas input channel, two auxiliary gas injection channels and a conical cylinder body, the atomizing gas input channel and the two auxiliary gas injection channels are fixed on the conical cylinder body, the auxiliary gas injection channels are arranged at the two ends of the atomizing gas input channel, and a space angle of 60 degrees is formed among the axis of the atomizing gas input channel and the axes of the two auxiliary gas injection channels; the main cylinder body is composed of a shell, a plurality of cutting blades and a third auxiliary gas injection channel; the movable propeller blade is composed of a blade, a blade shaft and fixed links, and the blade is fixed on the blade shaft; and the two ends of the blade shaft are respectively restrained in middle holes at the middle parts of the fixed links at the two ends of the main cylinder body, and keep rotating freely. The atomizing gas mixing and refining device disclosed by the utility model can achieve an effect of refining atomizing gas particles, thereby achieving the dual purposes of gas mixing and refining.

Description

A kind of atomization gas mixing device for thinning
Technical field
The utility model relates to a kind of atomization gas mixing device for thinning, is mainly used in the further refinement of the mixing of atomization gas and other gas, atomization gas.
Background technology
Blender mainly is to let fluid pass through specific passage, and the flow regime that changes fluid of the design through device in passage and the passage reaches the purpose of mixing, can be divided into two kinds of static mixer and dynamic mixers.Itself does not have moving component static mixer, relies on the special construction and the fluid motion of unit, and immiscible fluid is disperseed separately, is mixed with each other, and is usually used in gas gas, gas-liquid, the mixing between the liquid liquid.Multiple motions such as dynamic mixer then has outer power to participate in, and imposes stirring, and rotation is sprayed, and is reciprocal, heterogeneous mixing such as complex structure is mainly used in gas-liquid, and is solid, liquid-solid.Release tens kinds of blenders both at home and abroad, and be widely used in fields such as oil, chemical industry, light industry, traffic, the energy.In fact, when gas gas mixed, people often not only expected to realize the abundant mixing of two kinds of gases, also hope in this process, can carry out further refinement to the droplet particulate of a certain atomization gas.In atomization gas and process that other gas mixes; If the principle that can utilize air-flow to pulverize; Can realize of impact, collision or the friction of high pressure air-flow through the pressure differential of two kinds of air-flows, thereby realize pulverizing and refinement the atomization gas particle to low-pressure air-flow (atomization gas) particle.
The utility model content
The technology of the utility model is dealt with problems: a kind of atomization gas mixing device for thinning is provided; Realization is cut, shears, is rotated and mix again with two strands of other gases or a plurality of fluids atomization gas; When mixing; Realization reaches the dual purpose of mixing gas and refinement to the refinement of atomization gas.
The technical solution of the utility model: a kind of atomization gas mixing device for thinning comprises: decompression tube, main cylinder, pressurization cylinder, movable spiral lodicule; Said decompression tube comprises that atomization gas input channel, two assist gas inject passage and conical shell; The passage of injecting of atomization gas input channel and two assist gas is fixed on the conical shell; Wherein assist gas is injected the both sides that passage is positioned at the atomization gas input channel; The axis of atomization gas input channel becomes 60 ° of angles, space with the axis that two assist gas are injected passage, the thin end of conical shell is connected with the atomization gas input channel, and the conical shell butt end is connected with main cylinder; Said main cylinder by housing, be fixed on multi-disc cutting blade, the 3rd assist gas that the line in the shape of a spiral of main cylinder madial wall distributes and inject passage and form; Said the 3rd assist gas injected passage and is positioned on the housing, and its axis and housing are tangent; Said movable spiral lodicule is made up of lodicule, lodicule axle and fixed bar, and said lodicule is fixed on the said lodicule axle; Said lodicule axle two ends constrain in the interstitial hole of the fixed bar center that is positioned at the main cylinder two ends respectively, and keep freely rotating; Said pressurization cylinder is a conical shell, and its butt end is connected with main cylinder, and thin end is connected with the output channel of gaseous mixture.
The utility model advantage compared with prior art: the utility model is when mixing two or more gases; Reach cutting, shearing, rotation and mix again through the cross rotary impact of the movable spiral lodicule of centrifugal impact and center that impact, tangential gas flow combine with cutting blade of space air-flow, reach the further refinement of atomization gas particulate and the dual purpose of mixing with other gas to atomization gas.
Description of drawings
Fig. 1 is the structure chart of the utility model;
Fig. 2 is the distributed architecture sketch map of cutting blade in the utility model;
Fig. 3 injects the relation structure diagram of passage and housing for the 3rd assist gas in the utility model.
The specific embodiment
Like Fig. 1, shown in 2, the utility model comprises: decompression tube, main cylinder, pressurization cylinder 211, movable spiral lodicule; What wherein decompression tube comprised atomization gas input channel 201, two assist gas injects passage 202 and conical shell 203; The passage 202 of injecting of atomization gas input channel 201 and two assist gas is fixed on the conical shell 203; Two assist gas are injected the both sides that passage 202 is positioned at atomization gas input channel 201; The axis of atomization gas input channel 201 becomes 60 ° of angles, space with the axis that two assist gas are injected passage 202; And the axis extended line of injecting passage 202 of atomization gas input channel 201 and two assist gas meets at 1: 212, and is as shown in Figure 1.Conical shell 203 thin ends are connected with atomization gas input channel 201, and conical shell 203 butt ends are connected with main cylinder.Atomization gas input channel 201 extends into conical shell 203, and the length in conical shell 203 equals atomization gas input channel 201 inwalls and accessory channel 202 inwall extending line intersection points to the distance of conical shell 203 with atomization gas input channel 201 intersection points.
Main cylinder by housing 204, be fixed on multi-disc cutting blade 205, the 3rd assist gas that the line in the shape of a spiral of main cylinder madial wall distributes and inject passage 206 and form; The 3rd assist gas injected passage 206 and is positioned on the housing 204, and axis and housing 204 inwalls that the 3rd assist gas injected passage 206 are tangent, as shown in Figure 3; And the 3rd assist gas original position of injecting passage 206 and multi-disc cutting blade 205 over against, as shown in Figure 2.The multi-disc cutting blade 205 that line in the shape of a spiral in the utility model distributes can be one or more groups, can be distribution of left-hand screw line and right-hand helix respectively and distribute, and also or simultaneously is that the left-hand screw line distributes and right-hand helix distributes.Among Fig. 2 be two, be distribution of left-hand screw line and right-hand helix respectively and distribute.
Movable spiral lodicule is made up of lodicule 207, lodicule axle 208 and fixed bar 209; Lodicule 207 is fixed on the lodicule axle 208, and lodicule 207 can be for a plurality of, straggly at an angle arranging; Lodicule axle 208 two ends constrain in the interstitial hole 210 of fixed bar 209 centers that are positioned at the main cylinder two ends respectively, and keep freely rotating.
Pressurization cylinder 211 is a conical shell, and its butt end is connected with main cylinder, and thin end is connected with the output channel of gaseous mixture.
The course of work of the utility model: atomization gas is got into by atomization gas input channel 201; Being injected the assist gas that passage 202 got into by two assist gas impacts, mixes; Mixed airflow on the axial direction by a plurality of lodicule 207, sidewall in the shape of a spiral the multi-disc cutting blade 205 that distributes of line cut apart and stop; The 3rd the auxiliary assist gas of injecting passage 206 entering on the main body cylinder is to mixed air-flow secondary pulse; Quicken the cutting, shearing, rotation of mixed gas and mixed process again, mix gas after the refinement through pressurization cylinder 211 outputs.

Claims (7)

1. an atomization gas mixing device for thinning is characterized in that comprising: decompression tube, main cylinder, pressurization cylinder (211), movable spiral lodicule; Said decompression tube comprises that atomization gas input channel (201), two assist gas inject passage (202) and conical shell (203); The passage (202) of injecting of atomization gas input channel (201) and two assist gas is fixed on the conical shell (203); Wherein two assist gas are injected the both sides that passage (202) lays respectively at atomization gas input channel (201); The axis of atomization gas input channel (201) becomes the space certain angle with the axis that two assist gas are injected passage (202); Atomization gas input channel (201) is connected with the thin end of conical shell (203), and extends into conical shell (203) certain-length, and conical shell (203) butt end is connected with main cylinder; Said main cylinder by housing (204), be fixed on multi-disc cutting blade (205), the 3rd assist gas that the line in the shape of a spiral of main cylinder madial wall distributes and inject passage (206) and form; Said the 3rd assist gas injected passage (206) and is positioned on the housing (204), and its axis and housing (204) are tangent; Said movable spiral lodicule is made up of lodicule (207), lodicule axle (208) and fixed bar (209), and said lodicule (207) is fixed on the said lodicule axle (208); Said lodicule axle (208) two ends constrain in the interstitial hole (210) of fixed bar (209) center that is positioned at the main cylinder two ends respectively, and keep freely rotating; Said pressurization cylinder (211) is a conical shell, and its butt end is connected with main cylinder, and thin end is connected with the output channel of gaseous mixture.
2. atomization gas mixing device for thinning according to claim 1 is characterized in that: the axis of said atomization gas input channel (201) becomes 60 ° of angles, space with the axis that two assist gas are injected passage (202).
3. atomization gas mixing device for thinning according to claim 1; It is characterized in that: said atomization gas input channel (201) extends into conical shell (203), and the length in conical shell (203) equals atomization gas input channel (201) inwall and accessory channel (202) inwall extending line intersection point to the distance of conical shell (203) with atomization gas input channel (201) intersection point.
4. atomization gas mixing device for thinning according to claim 1 is characterized in that: the original position that said the 3rd assist gas injected the multi-disc cutting blade (205) that passage (206) and line in the shape of a spiral distribute over against.
5. atomization gas mixing device for thinning according to claim 1 is characterized in that: the axis extended line of injecting passage (202) of said atomization gas input channel (201) and two assist gas meets at a bit.
6. atomization gas mixing device for thinning according to claim 1 is characterized in that: the multi-disc cutting blade (205) that said line in the shape of a spiral distributes is the distribution of left-hand screw line or right-hand helix distributes, or is that the left-hand screw line distributes and right-hand helix distributes simultaneously.
7. atomization gas mixing device for thinning according to claim 1 is characterized in that: said lodicule (207) is a plurality of, straggly at an angle arranging.
CN2011204804812U 2011-11-28 2011-11-28 Atomizing gas mixing and refining device Expired - Fee Related CN202410537U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011204804812U CN202410537U (en) 2011-11-28 2011-11-28 Atomizing gas mixing and refining device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011204804812U CN202410537U (en) 2011-11-28 2011-11-28 Atomizing gas mixing and refining device

Publications (1)

Publication Number Publication Date
CN202410537U true CN202410537U (en) 2012-09-05

Family

ID=46735336

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2011204804812U Expired - Fee Related CN202410537U (en) 2011-11-28 2011-11-28 Atomizing gas mixing and refining device

Country Status (1)

Country Link
CN (1) CN202410537U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109200952A (en) * 2018-11-15 2019-01-15 中石化炼化工程(集团)股份有限公司 A kind of gas-liquid mixed component and the catalyst bed structure for reactor
CN111036103A (en) * 2019-12-27 2020-04-21 安徽海德化工科技有限公司 N-butane and air mixing device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109200952A (en) * 2018-11-15 2019-01-15 中石化炼化工程(集团)股份有限公司 A kind of gas-liquid mixed component and the catalyst bed structure for reactor
CN109200952B (en) * 2018-11-15 2021-04-27 中石化炼化工程(集团)股份有限公司 Gas-liquid mixing assembly and catalyst bed layer structure for reactor
CN111036103A (en) * 2019-12-27 2020-04-21 安徽海德化工科技有限公司 N-butane and air mixing device

Similar Documents

Publication Publication Date Title
CN206730896U (en) A kind of high pressure homogenizer
CN202410537U (en) Atomizing gas mixing and refining device
CN203990338U (en) A kind of static mixer
WO2008084776A1 (en) Apparatus for production of microfluid mixed liquid fuel
CN102309932A (en) Gas liquid mixing apparatus and application method thereof
CN201871349U (en) Foam generator
CN205517470U (en) Tubular blender for chemical industry
CN103446902A (en) Spiral jet mixer
CN104492299A (en) Powder mixing dispersing machine
CN101601980B (en) Liquid nano-shearing machine
CN203540393U (en) High-speed mixer
CN205925486U (en) Assembled stirring rod
CN204138622U (en) A kind of list reflection super-gravity device of continuous production methanol emulsified diesel
CN104232192B (en) A kind of list reflection super-gravity device of continuous production methanol emulsified diesel and technique
CN203577677U (en) Cutting emulsification device with premixing device
CN202191860U (en) Homogenizer for powder material
CN202876729U (en) Emulsification cavity device of high-voltage homogeneous emulsifying equipment for nano-crystallization preparation
CN201906579U (en) Multi-stage emulsification device for blended fuel
CN202668789U (en) Phenolic aldehyde mixing and shearing gun head
CN104226178A (en) III-shaped supergravity device and process for continuously preparing methanol emulsified diesel fuel
CN201632200U (en) Straight-pipe-type cyclone mixer
CN210356723U (en) Multiphase mixer
CN205288163U (en) Developments mixing pump
CN202516491U (en) Four-rotation mixer
US20160207013A1 (en) Device For Mixing Fluids

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20120905

Termination date: 20141128

EXPY Termination of patent right or utility model