CN209451482U - A kind of rotary blowing smoke duster - Google Patents

A kind of rotary blowing smoke duster Download PDF

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Publication number
CN209451482U
CN209451482U CN201821831765.XU CN201821831765U CN209451482U CN 209451482 U CN209451482 U CN 209451482U CN 201821831765 U CN201821831765 U CN 201821831765U CN 209451482 U CN209451482 U CN 209451482U
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China
Prior art keywords
cylindrical shell
flue gas
gas inlet
inlet tube
rotary blowing
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CN201821831765.XU
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Chinese (zh)
Inventor
陈作锋
汪建营
纪律律
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Tongji University
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Tongji University
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Priority to CN201821831765.XU priority Critical patent/CN209451482U/en
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Abstract

The utility model relates to a kind of rotary blowing smoke dusters, including cylindrical shell (1), ash bucket (2), flue gas inlet tube (3) and smoke outlet tube (5), the ash bucket (2) is connected to the lower section of cylindrical shell (1), the smoke outlet tube (5) is located at the top of cylindrical shell (1), the flue gas inlet tube (3) is set on the side wall of cylindrical shell (1), the flue gas inlet tube (3) along the tangential access cylindrical shell (1) of cylindrical shell (1) radial section side wall, helical ring is wound with wind deflector (4) on described cylindrical shell (1) inner wall, the wind deflector (4) is vertically arranged with cylindrical shell (1) inner wall, leak hole (41) are offered on the wind deflector (4).Compared with prior art, the utility model has many advantages, such as that eddy flow effect is good, separating effect is excellent and saves the device space.

Description

A kind of rotary blowing smoke duster
Technical field
The utility model relates to a kind of cleaners, more particularly, to a kind of rotary blowing smoke duster.
Background technique
Currently, the smoke inlet of smoke duster largely uses top to be arranged vertically or horizontally disposed, by spray, quiet The method of electric precipitation or cyclonic separation reduces the amount of dust in flue gas, but sprays or the equipment of electrostatic precipitation is usually larger, and And energy consumption is higher.And the ash bucket that current cyclonic separation cleaner includes shell and is arranged on the downside of shell, blast pipe from On the upside of shell in the chamber of access shell, discharge pipe access chamber and extends to cavity bottom on the upside of shell, flue gas from Blast pipe enters chamber top, is formed after certain eddy flow and enters discharge pipe, flue gas shape from the discharge pipe nozzle of chamber lower portion When at eddy flow, larger particles are thrown toward cavity wall because of the effect of centrifugal force in flue gas, are finally discharged from the ash port of ash bucket lower end, but In existing fume dust remover, the effect of eddy flow is unobvious, results in the serious disorder stream of chamber interior, causes dust removing effects not It is ideal.
Patent CN201610457931.3 discloses a kind of Industrial Boiler smoke duster, comprising: bracket, cabinet, ash bucket, Shake cinder-discharging port, clean room, ceramic dust removing tube, ceramic guider, dusty gas import and purified gas outlet, the bracket Top be provided with cabinet, lower part is provided with ash bucket, and the bottom of the ash bucket is provided with vibration cinder-discharging port, in the cabinet It is disposed with the clean room and ceramic dust removing tube from top to bottom, the bottom of the ceramic dust removing tube is provided with ceramics and leads To device, the side of the lower box is provided with dusty gas import.Guider is disclosed in the utility model, but is not limited Fixed specific flue gas guiding, does not illustrate the structure of guiding parts yet.
Summary of the invention
The purpose of this utility model is exactly to provide a kind of rotary blowing to overcome the problems of the above-mentioned prior art Smoke duster.
The purpose of this utility model can be achieved through the following technical solutions:
A kind of rotary blowing smoke duster, including cylindrical shell, ash bucket, flue gas inlet tube and smoke outlet tube, it is described Ash bucket be connected to the lower section of cylindrical shell, the smoke outlet tube is located at the top of cylindrical shell, and the flue gas inlet tube is set In on the side wall of cylindrical shell, the flue gas inlet tube along the tangential access cylindrical shell of cylindrical shell radial section side Wall, helical ring is wound with wind deflector on the cylindrical shell inner wall, and the wind deflector is vertically arranged with cylindrical shell inner wall, institute Leak hole is offered on the wind deflector stated, adjacent wind deflector forms wind guide tank, and flue gas is tangentially entered by flue gas inlet tube, flue gas In wind guide tank inside spin uplink, wind guide tank plays good guiding role close to cylindrical shell part circulation to flue gas, the part Circulation is according to hand of spiral uplink, and the guiding role that the circulation far from cylindrical shell inner wall is subject to is less, therefore spiral Trend it is relatively slow, so that circulation and close the circulation layering rising from cylindrical shell inner wall far from cylindrical shell inner wall, It is referred to as inside circulation and outside circulation, the dust granule in the circulation of inside in this way can collide in contact zone, after collision The momentum of dust reduce, can be sunk by leak hole, in sinking watching can and the dust granule of lower layer continue to collide so that its His dust granule momentum reduces, and declines dust granule successively by leak hole, eventually enters into ash bucket, final to realize Flue dust of flue gas during spiral uplink gradually is detached from, and the flue gas after dedusting is discharged by the smoke outlet tube at top.
Further, the spacing of the two adjacent ring wind deflectors is 0.4~0.8 times of cylindrical shell internal diameter, the model Spacing in enclosing can be supplied to the enough spiral spaces of flue gas.
Further, the width of the wind deflector is 0.1~0.3 times of cylindrical shell internal diameter.
Further, the width of the wind deflector is 0.15 times of cylindrical shell internal diameter.
Further, the leak hole is round hole, and leak hole internal diameter is 0.3~0.7 times of the width of wind deflector.
Further, the axial length of the flue gas inlet tube is 0.5~2 times of cylindrical shell internal diameter, gas inlet Pipe is connect with flue dust delivery outlet to be processed, thus flue gas inlet tube need enough length come to the direction of motion of flue gas into Row guiding makes flue gas when entering flue gas inlet tube along section tangential direction.In addition, wind can be added before flue gas inlet tube Machine promotes the kinetic energy of flue gas with this.
Further, the axial length of the flue gas inlet tube is 1.1 times of cylindrical shell internal diameter.
Further, the reducer pipe that the flue gas inlet tube can be gradually increased for diameter uniform straight tube or diameter.
Further, on-position height of the flue gas inlet tube on cylindrical shell is the 1/ of cylindrical shell height At 10~1/2.
Further, on-position height of the flue gas inlet tube on cylindrical shell is the 1/ of cylindrical shell height At 5, be conducive to the effect of rotating separation and sedimentation close to the on-position of cylindrical shell bottom end.
Further, the ash bucket is reverse frustoconic shell, and the big diametral plane of ash bucket is communicated with the lower end of cylindrical shell.
Compared with prior art, it is hardened to joined wind-guiding on the basis of original Cyclonic separating apparatus for the utility model Structure, so which produces the collisions between the flue gas particle of two sides inside and outside the flue gas of upper rotation receives guiding role and be divided into, and Declined by leak hole, form layer-by-layer sedimentation separation, enhance the effect of eddy flow, overcome internal disorder stream, improve Isolated efficiency saves the occupied space of separation equipment.
Detailed description of the invention
Fig. 1 is the overall structure diagram of rotary blowing smoke duster in the utility model;
Fig. 2 is the structural schematic diagram of wind deflector in the utility model.
In figure: 1, cylindrical shell, 2, ash bucket, 3, flue gas inlet tube, 4, wind deflector, 5, smoke outlet tube, 41, leak hole.
Specific embodiment
The utility model is described in detail in the following with reference to the drawings and specific embodiments.
Embodiment
Rotary blowing smoke duster includes cylindrical shell 1, ash bucket 2, flue gas inlet tube 3 and smoke outlet tube 5, referring to figure 1, the ash bucket 2 is connected to the lower section of cylindrical shell 1, and the smoke outlet tube 5 is located at 1 top of cylindrical shell, and feature exists In the flue gas inlet tube 3 is set on the side wall of cylindrical shell 1, and the flue gas inlet tube 3 is radial along cylindrical shell 1 The side wall of the tangential access cylindrical shell 1 in section, helical ring is wound with wind deflector 4 on 1 inner wall of cylindrical shell, referring to fig. 2, The wind deflector 4 is vertically arranged with 1 inner wall of cylindrical shell, offers leak hole 41 on the wind deflector 4.Described is adjacent The spacing of two ring wind deflectors 4 is 0.4~0.8 times of 1 internal diameter of cylindrical shell.The width of the wind deflector 4 is in cylindrical shell 1 0.1~0.3 times of diameter.The leak hole 41 is round hole, and 41 internal diameter of leak hole is 0.3~0.7 times of the width of wind deflector 4.Institute The axial length for the flue gas inlet tube 3 stated is 0.5~2 times of 1 internal diameter of cylindrical shell.The axial direction of the flue gas inlet tube 3 is long Degree is 1.1 times of 1 internal diameter of cylindrical shell.The flue gas inlet tube 3 is that diameter uniform straight tube or diameter are gradually increased Reducer pipe.On-position height of the flue gas inlet tube 3 on cylindrical shell 1 is the 1/10~1/2 of 1 height of cylindrical shell Place.The flue gas inlet tube 3 is at 1/5 that the on-position height on cylindrical shell 1 is 1 height of cylindrical shell.Described Ash bucket 2 is reverse frustoconic shell, and the big diametral plane of ash bucket 2 is communicated with the lower end of cylindrical shell 1.
During carrying out practically, the flue gas to dedusting is passed through blower by pipeline, later by flue gas inlet tube 3 with cylinder The direction of 1 section tangent line of shell is passed through, and flue gas is in wind guide tank inside spin uplink, and wind guide tank is to flue gas close to 1 part of cylindrical shell Circulation plays good guiding role, the part circulation according to hand of spiral uplink, and far from 1 inner wall of cylindrical shell circulation by The guiding role arrived is less, therefore spiralling trend is relatively slow, so that circulation far from 1 inner wall of cylindrical shell with it is close Circulation sealing from 1 inner wall of cylindrical shell rises, and is referred to as inside circulation and outside circulation, the in this way dust in the circulation of inside Particle can collide in contact zone, and the momentum of the dust after collision reduces, and can be sunk by leak hole 41, the meeting in sinking watching Continue to collide with the dust granule of lower layer, so that other dust granule momentum reduce, just makes dust granule pass through leakage in this way Hole 41 successively declines, and eventually enters into ash bucket 2, final to realize that the flue dust of flue gas during spiral uplink gradually is detached from, and removes Flue gas after dirt is discharged by the smoke outlet tube 5 at top.

Claims (10)

1. a kind of rotary blowing smoke duster, including cylindrical shell (1), ash bucket (2), flue gas inlet tube (3) and exhanst gas outlet It manages (5), the ash bucket (2) is connected to the lower section of cylindrical shell (1), and the smoke outlet tube (5) is located at cylindrical shell (1) top Portion, which is characterized in that the flue gas inlet tube (3) is set on the side wall of cylindrical shell (1), the flue gas inlet tube (3) Along the side wall of the tangential access cylindrical shell (1) of cylindrical shell (1) radial section, spiral shell on the cylindrical shell (1) inner wall Rotation is surrounded with wind deflector (4), and the wind deflector (4) is vertically arranged with cylindrical shell (1) inner wall, on the wind deflector (4) Offer leak hole (41).
2. a kind of rotary blowing smoke duster according to claim 1, which is characterized in that led described in two adjacent rings The spacing of aerofoil (4) is 0.4~0.8 times of cylindrical shell (1) internal diameter.
3. a kind of rotary blowing smoke duster according to claim 1, which is characterized in that the wind deflector (4) Width is 0.1~0.3 times of cylindrical shell (1) internal diameter.
4. a kind of rotary blowing smoke duster according to claim 3, which is characterized in that the leak hole (41) is circle Shape hole, leak hole (41) internal diameter are 0.3~0.7 times of the width of wind deflector (4).
5. a kind of rotary blowing smoke duster according to claim 1, which is characterized in that the flue gas inlet tube (3) axial length is 0.5~2 times of cylindrical shell (1) internal diameter.
6. a kind of rotary blowing smoke duster according to claim 5, which is characterized in that the flue gas inlet tube (3) axial length is 1.1 times of cylindrical shell (1) internal diameter.
7. a kind of rotary blowing smoke duster according to claim 1, which is characterized in that the flue gas inlet tube (3) reducer pipe being gradually increased for diameter uniform straight tube or diameter.
8. a kind of rotary blowing smoke duster according to claim 1, which is characterized in that the flue gas inlet tube (3) at 1/10~1/2 that the on-position height on cylindrical shell (1) is cylindrical shell (1) height.
9. a kind of rotary blowing smoke duster according to claim 8, which is characterized in that the flue gas inlet tube (3) at 1/5 that the on-position height on cylindrical shell (1) is cylindrical shell (1) height.
10. a kind of rotary blowing smoke duster according to claim 1, which is characterized in that the ash bucket (2) is to fall The big diametral plane of truncated cone-shaped shell, ash bucket (2) is communicated with the lower end of cylindrical shell (1).
CN201821831765.XU 2018-11-06 2018-11-06 A kind of rotary blowing smoke duster Active CN209451482U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201821831765.XU CN209451482U (en) 2018-11-06 2018-11-06 A kind of rotary blowing smoke duster

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201821831765.XU CN209451482U (en) 2018-11-06 2018-11-06 A kind of rotary blowing smoke duster

Publications (1)

Publication Number Publication Date
CN209451482U true CN209451482U (en) 2019-10-01

Family

ID=68037902

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201821831765.XU Active CN209451482U (en) 2018-11-06 2018-11-06 A kind of rotary blowing smoke duster

Country Status (1)

Country Link
CN (1) CN209451482U (en)

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