CN106512632A - Folded gathering unit and agglomeration gathering device of sintering flue gas fine particles - Google Patents

Folded gathering unit and agglomeration gathering device of sintering flue gas fine particles Download PDF

Info

Publication number
CN106512632A
CN106512632A CN201611077977.9A CN201611077977A CN106512632A CN 106512632 A CN106512632 A CN 106512632A CN 201611077977 A CN201611077977 A CN 201611077977A CN 106512632 A CN106512632 A CN 106512632A
Authority
CN
China
Prior art keywords
flue gas
unit
agglomeration
turning back
particulate matter
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.)
Granted
Application number
CN201611077977.9A
Other languages
Chinese (zh)
Other versions
CN106512632B (en
Inventor
春铁军
王欢
音正元
许伟
薛凡
王松
宁超
龙红明
王平
孟庆民
狄瞻霞
余正伟
魏汝飞
王臻
李东升
穆固天
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.)
Anhui University of Technology AHUT
Original Assignee
Anhui University of Technology AHUT
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 Anhui University of Technology AHUT filed Critical Anhui University of Technology AHUT
Priority to CN201811621271.3A priority Critical patent/CN109569169B/en
Priority to CN201611077977.9A priority patent/CN106512632B/en
Publication of CN106512632A publication Critical patent/CN106512632A/en
Application granted granted Critical
Publication of CN106512632B publication Critical patent/CN106512632B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D51/00Auxiliary pretreatment of gases or vapours to be cleaned
    • B01D51/02Amassing the particles, e.g. by flocculation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D45/00Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
    • B01D45/02Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising gravity
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D45/00Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
    • B01D45/04Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia
    • B01D45/08Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia by impingement against baffle separators
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D50/00Combinations of methods or devices for separating particles from gases or vapours
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2258/00Sources of waste gases
    • B01D2258/02Other waste gases
    • B01D2258/025Other waste gases from metallurgy plants
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2258/00Sources of waste gases
    • B01D2258/02Other waste gases
    • B01D2258/0283Flue gases

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Treating Waste Gases (AREA)
  • Electrostatic Separation (AREA)

Abstract

The invention discloses a folded gathering unit and an agglomeration gathering device of sintering flue gas fine particles and belongs to the field of management of iron ore sintering flue gas. According to a particle agglomeration unit and the folded gathering unit, the particle agglomeration unit is internally provided with an agglomeration agent nozzle; the folded gathering unit comprises a storage part, a gas inlet bent pipe and a gas outlet bent pipe; bottoms of the gas inlet bent pipe and the gas outlet bent pipe are communicated to form a folded bent pipe; the storage part is obliquely arranged on the gas outlet bent pipe, and particles are deposited in the folded bent pipe and are stored in the storage part; the particle agglomeration unit is arranged at the upper part of the folded gathering unit; and the bottom of the agglomeration gathering unit is connected with the gas inlet bent pipe of the folded gathering unit. According to the agglomeration gathering device disclosed by the invention, the particle agglomeration unit and the folded gathering unit are arranged, so that the fine particles are firstly agglomerated, then are gathered through the folded gathering unit and are stored in the storage part, and furthermore, the removing efficiency of the flue gas particles is improved.

Description

A kind of sintering flue gas fine particulate matter is turned back capture unit and reunion capturing device
Technical field
The present invention relates to agglomeration for iron mine gas pollution control field, more particularly, it relates to a kind of sintering flue gas fine Grain thing is turned back capture unit and reunion capturing device.
Background technology
Agglomeration for iron mine operation is requisite link in Production Processes In Steel Industry, while and being that steel and iron industry is maximum PM10And PM2.5Emission source, accounts for 40% of its total release or so.Dedusting method traditional at present is difficult to effective control PM2.5Row Put, fine particle groups can be made to be polymerized to larger grain by physics or chemical action so pretreatment stage is arranged before deduster The particle in footpath such that it is able to which being removed by traditional deduster becomes a kind of new dust collection method.
At present sintering plant is mainly using deduster come the particulate matter in purifying sintering flue gas, deduster to flue gas in thick Grain thing removal effect is preferable, but the fine particle (PM for particle diameter less than 10 μm10And PM2.5), as its particle diameter is little, Ratio resistance is high, charge capacity is poor.General dust collection method is difficult to effectively remove fine particle, and urgent need develops a kind of burning The processing equipment of knot flue gas fine particulate matter, so as to be effectively treated to sintering the fine particle in flue gas.
Jing is retrieved, Chinese Patent Application No.:201620055887.9, authorized announcement date is on June 29th, 2016, invents wound A kind of entitled flue gas dust collecting system is made, this application case discloses a kind of flue gas dust collecting system, the dust pelletizing system includes that gravity sinks Drop room, inertia dust-removing device, cyclone dust collector and Wet type electric dust-removing device;Wherein inertia dust-removing device is arranged at gravitational settling Smoke outlet that is indoor and being located at gravity settling chamber, the smoke outlet of gravity settling chamber are entered with the flue gas of cyclone dust collector Mouth end is connected;Wet type electric dust-removing device is arranged at the smoke outlet of cyclone dust collector.This application case is relative to existing Wet type electric dust-removing device improves efficiency of dust collection to a certain extent, but its be disadvantageous in that using cleaner species compared with Many, crushing is big, and high energy consumption, equipment investment cost are higher.
In addition, Chinese Patent Application No.:201610288719.9, the applying date be on April 28th, 2016, invention and created name For a kind of agglomeration for iron mine flue gas PM10And PM2.5Discharge-reducing method, this application case discloses Ore Sintering Process fine particle Emission-reducing system, in Ore Sintering Process, sprays into reunion liquid in the exhaust gases passes of sintering flue gas, sinters the subparticle in flue gas Thing is reunited in the presence of reunion liquid and is grown up, and removes the fine particle grown up of reuniting, described reunion using dust arrester Agent includes aluminium polychloride, sodium carboxymethylcellulose, polyacrylamide and solid additive.Subject application causes to be adsorbed with fine The reunion liquid mist of particulate matter drops in nucleation under low voltage situations, collides, grows up, the bulky grain aggregate of formation, and is filled using dedusting Put and remove the fine particle grown up of reuniting.Fine particle reunion during this application case proposes a kind of new agglomeration for iron mine flue gas subtracts The method of row, the agglomerating effect for improving fine particle in agglomeration for iron mine flue gas realize the reduction of discharging of fine particle, but the Shen The trapping that particulate matter after reuniting such as please will be improved in case also needs to the more efficient capturing device of cooperation.
The content of the invention
1. invention technical problem to be solved
It is an object of the invention in overcoming prior art, Ore Sintering Process fine particle is difficult to asking for effective removal Topic, there is provided a kind of sintering flue gas fine particulate matter is turned back capture unit and reunion capturing device, a kind of flue gas particles therein Capture unit of turning back, the removal efficiency of flue gas particles is improve by the reservoir block being obliquely installed;A kind of iron therein Ore deposit sinters flue gas fine particulate matter reunion capturing device so that the fine particle in flue gas first carries out reunion and grows up, then is inclined The reservoir block trapping for tiltedly arranging, improves the removal efficiency of fine particle in flue gas.
2. technical scheme
To reach above-mentioned purpose, the technical scheme that the present invention is provided is:
A kind of capture unit of turning back of flue gas particles of the present invention, including reservoir block, intake elbow and outlet bend pipe, Described intake elbow is connected with the bottom of outlet bend pipe and constitutes bend pipe of turning back, and described reservoir block is inclined to be arranged at On outlet bend pipe, particulate matter in bend pipe of turning back is settled and is stored in reservoir block.
Preferably, described intake elbow and outlet bend pipe are connected with flue by shaking bellows.
Preferably, described reservoir block and the inclination angle of vertical direction are 10-30 °, and reservoir block porch is arranged There is waterfog head.
Preferably, electromagnetic shaker is provided with described capture unit of turning back.
A kind of agglomeration for iron mine flue gas fine particulate matter reunion capturing device of the present invention, including
Particle agglomeration unit, is provided with agglomerator shower nozzle in the particle agglomeration unit;
Turn back capture unit, the capture unit of turning back that capture unit is preceding claim of turning back;
Described particle agglomeration unit is arranged at the top of capture unit of turning back, and the bottom of particle agglomeration unit is caught with turning back The intake elbow of collection unit is connected.
Preferably, described particle agglomeration unit includes agglomerator shower nozzle, turbulence columns and particle agglomeration room, described reunion Agent shower nozzle and turbulence columns are arranged at the inside of particle agglomeration room, and agglomerator shower nozzle is located at the top of turbulence columns.
Preferably, the injection direction of described agglomerator shower nozzle is contrary with the flow direction of flue gas;Described turbulence columns Shape of cross section is isosceles triangle.
Preferably, the bottom of described particle agglomeration room is provided with Contraction Ducts, the cross-sectional area of the Contraction Ducts along Vertically downward direction is gradually reduced, and particle agglomeration room is connected with intake elbow by Contraction Ducts.
Preferably, also including electrostatic precipitation unit, the electrostatic precipitation unit includes corona electrode, collection electrode and power supply Part, described corona electrode are arranged in particle agglomeration unit, and collection electrode is arranged on the outlet bend pipe of capture unit of turning back, Described corona electrode, collection electrode are connected with the negative and positive electrode of power supply part respectively.
Preferably, described corona electrode is arranged at the bottom of turbulence columns, and described collection electrode is arranged at reservoir block Above porch.
3. beneficial effect
The technical scheme provided using the present invention, compared with existing known technology, with following remarkable result:
(1) capture unit of turning back of a kind of flue gas particles of the invention, intake elbow are connected with the bottom of outlet bend pipe Lead to and constitute bend pipe of turning back, reservoir block is inclined to be arranged on outlet bend pipe, and reservoir block is inclined to be arranged at outlet bend pipe Bottom, under the collective effect of the inertia force in gravity and particle motion process, particle is deposited in the bottom of bend pipe of turning back, and And the bottom of outlet bend pipe is mainly gathered in, and as the upper end open of reservoir block and the angle of horizontal plane are 10-30 °, particle In the bottom infall process of outlet bend pipe, can directly by the upper end open first motion of reservoir block into reservoir block, Directly trapped by reservoir block so as to promote particulate matter, improve the removal efficiency of flue gas particles;
(2) capture unit of turning back of a kind of flue gas particles of the invention, the flue gas at the top of intake elbow flow into end and pass through Concussion bellows is connected with the flue on top, and the flue gas outflow end at the top of outlet bend pipe is by shaking bellows with top Flue is connected, that is, bend pipe of turning back can make the vibrations of vertical direction relative to flue, during vibrations in flue gas Fine particle simultaneously occurs to disturb in bend pipe of turning back with flue gas, touch in bend pipe of turning back so as to promote particulate matter Hit, and promote fine particle to reunite and grow up, improve the removal efficiency of flue gas particles;
(3) a kind of agglomeration for iron mine flue gas fine particulate matter reunion capturing device of the invention, agglomerator shower nozzle and turbulence columns It is arranged at the inside of particle agglomeration room, agglomerator shower nozzle is located at the top of turbulence columns, the flow direction phase of injection direction and flue gas Instead, the agglomerator droplet touch opportunity increase that fine particle is head-on sprayed with agglomerator shower nozzle in flue gas, promotes particulate matter Quick reunion;
(4) a kind of agglomeration for iron mine flue gas fine particulate matter reunion capturing device of the invention, corona electrode and power supply part Negative pole be connected, collection electrode is connected with the positive pole of power supply part, bottom quilt of the particulate matter in flue gas in particle agglomeration unit Negative electrical charge on load, then into electrostatic precipitation unit, locates above reservoir block porch, carries the particulate matter quilt of negative electrical charge Collection electrode is trapped, and bend pipe of turning back can make the vibrations of vertical direction relative to particle agglomeration unit, is shaken and is produced phase Mutual collision, increases the contact probability of particulate matter and collection electrode, so as to promote particulate matter on reservoir block porch Square place is trapped by collection electrode, and is deposited in reservoir block.
Description of the drawings
Fig. 1 is a kind of overall structure diagram of agglomeration for iron mine flue gas fine particulate matter reunion capturing device of the present invention;
Fig. 2 is the structural representation of the reservoir block of the present invention.
Label declaration in schematic diagram:
100th, particle agglomeration unit;101st, agglomerator shower nozzle;102nd, turbulence columns;103rd, Contraction Ducts;104th, particle agglomeration Room;105th, expansion line;
200th, turn back capture unit;201st, shake bellows;202nd, electromagnetic shaker;210th, reservoir block;211st, dust flow-disturbing Plate;212nd, waterfog head;213rd, unload dirt valve;214th, dust bellows;220th, intake elbow;221st, flue gas flows into end;230th, go out Gas bend pipe;231st, flue gas outflow end;
300th, electrostatic precipitation unit;301st, corona electrode;302nd, collection electrode;303rd, power supply part.
Specific embodiment
Accompanying drawing with reference to the detailed description of the exemplary embodiment of the present invention hereafter, the accompanying drawing forms of description Point, show enforceable exemplary embodiment of the invention in the figure as an example.Although these exemplary embodiment quilts Fully describe in detail so that those skilled in the art can implement the present invention, it is to be understood that be capable of achieving other embodiment and Can without departing from the spirit and scope of the present invention to the present invention various changes can be made.Hereafter to embodiments of the invention More detailed description is not limited to required the scope of the present invention, and just to being illustrated and not limiting right The characteristics of of the invention and the description of feature, to propose to perform the best mode of the present invention, and are sufficient so that those skilled in the art The present invention can be implemented.Therefore, the scope of the invention is only defined by the appended claims.
Hereafter detailed description of the present invention and example embodiment can combine accompanying drawing to more fully understand, wherein the present invention Element and feature are identified by reference.
Embodiment 1
With reference to Fig. 1, a kind of capture unit of turning back of flue gas particles of the present embodiment, including reservoir block 210, intake elbow 220 and outlet bend pipe 230, described intake elbow 220 is connected with the bottom of outlet bend pipe 230 and constitutes bend pipe of turning back, institute The reservoir block 210 stated is inclined to be arranged on outlet bend pipe 230, and reservoir block 210 is inclined to be arranged at outlet bend pipe 230 Bottom, as shown in figure 1, reservoir block 210 is arranged at bend pipe bottom side to the right of turning back, described reservoir block 210 is set to circle It is spherical so that fine particle after into reservoir block 210 once be difficult to be flown out by reservoir block 210, it is therefore prevented that reservoir portion There is reentrainment of dust in the particle in part 210.
Particulate matter in bend pipe of turning back is settled and is stored in reservoir block 210, and reservoir block 210 and vertical direction Inclination angle is δ for the inclination angle of 10-30 °, the i.e. geometric center lines of reservoir block 210 and vertical direction, δ=10-30 °, that is, is stored up Integrate the upper end open of part 210 with the angle of horizontal plane as 10-30 °, preferably 20 ° of the present embodiment.When flue gas and particulate matter are in folding When bending pipe is moved, under the collective effect of gravity and inertia force, the particulate matter in flue gas can be deposited in bend pipe of turning back to particulate matter, And the bottom of outlet bend pipe 230 is mainly gathered in, as the upper end open of reservoir block 210 and the angle of horizontal plane are 10- 30 °, particle, can directly by the upper end open first motion of reservoir block 210 in the bottom infall process of outlet bend pipe 230 Into reservoir block 210.
It is worth further illustrating, the minimum position of bend pipe radius of curvature of turning back is located at the bottommost of bend pipe of turning back, and The reservoir block 210 of the present invention is not arranged at the minimum position of bend pipe radius of curvature of turning back, but inclined is arranged at outlet On bend pipe 230, the position is not the minimum position of radius of curvature, and reservoir block 210 is obliquely installed, has broken the formula of turning back and gathered dust Device capturing device is arranged on turn back bend pipe curvature minimum at or vertical lowest point inertial thinking, on the contrary particulate matter is had Preferably trap and trap effect.Its reason is probably, on the basis of the original initial velocity of the particle in flue gas, in gravity and particle Under the collective effect of the inertia force in motion process, it is more easy to be gathered near the bottom of outlet bend pipe 230, the setting causes particle Thing is easier in bend pipe of turning back to settle and be stored in reservoir block 210.
Above-mentioned 210 porch of reservoir block is additionally provided with waterfog head 212, and particulate matter is being stored up after water smoke moistening Secondary agglomeration is carried out in collection part 210 so that fine particle carries out reunion and grows up, increases weight, it is to avoid be deposited in reservoir portion The particulate matter of 210 bottom of part is flown in outlet bend pipe 230 again.And, it is provided with 210 bottom of reservoir block and unloads dirt valve 213, After a part of particle thing has been preserved in reservoir block 210, can open and unload dirt valve 213, will accumulate in reservoir block 210 Grain thing is discharged.
Above-mentioned intake elbow 220 and outlet bend pipe 230 are connected with flue by shaking bellows 201, i.e. air inlet Flue gas at the top of bend pipe 220 is flowed into end 221 and is connected with the flue on top by shaking bellows 201, and outlet bend pipe 230 is pushed up The flue gas outflow end 231 in portion is connected with the flue on top by shaking bellows 201, that is, bend pipe of turning back can be relative to flue gas Pipeline makees the vibrations of vertical direction, and the fine particle during vibrations in flue gas is sent out in bend pipe of turning back with flue gas simultaneously Raw disturbance, collides in bend pipe of turning back so as to promote particulate matter, and promotes fine particle generation reunion to grow up, this Rolled over bending pipe increases the complexity that particle is moved in bend pipe of turning back during vibrations simultaneously, promotes particulate matter more Among easily entering reservoir block 210.Electromagnetic shaker 202 is provided with capture unit of turning back 200, electromagnetic shaker 202 can promote to roll over There are vibrations in bending pipe.
Embodiment 2
A kind of agglomeration for iron mine flue gas fine particulate matter reunion capturing device of the present embodiment, including 100 He of particle agglomeration unit Agglomerator shower nozzle 101 is provided with capture unit of turning back 200, wherein particle agglomeration unit 100;Capture unit of turning back 200 is upper The capture unit 200 of turning back stated;Particle agglomeration unit 100 is arranged at the top of capture unit 200 of turning back, particle agglomeration unit 100 bottom is connected with the intake elbow 220 of capture unit 200 of turning back, and particulate matter is reunited in particle agglomeration unit 100 and grown up, And capture unit 200 of being turned back is trapped, the arresting efficiency of particulate matter in flue gas is improve.
Particle agglomeration unit 100 is arranged at the top of capture unit 200 of turning back, bottom and the folding of particle agglomeration unit 100 Turn capture unit 200 intake elbow 220 be connected, particle agglomeration unit 100 include agglomerator shower nozzle 101, turbulence columns 102 and Grain reunion room 104, described agglomerator shower nozzle 101 and turbulence columns 102 are arranged at the inside of particle agglomeration room 104, agglomerator spray 101 tops for being located at turbulence columns 102, the flow direction of injection direction and flue gas conversely, in flue gas fine particle with reunite The agglomerator droplet touch opportunity increase that agent shower nozzle 101 head-on sprays, so as to improve agglomerating effect.
What deserves to be explained is the diameter with diameter greater than flue of particle agglomeration room 104, above particle agglomeration room 104 Pipeline is provided with an expansion line 105, and flue is connected by expansion line 105 with particle agglomeration room 104, and flue gas is in extension Preliminary turbulent flow is produced at pipeline 105, while reducing flue gas speed.Flue gas enters particle agglomeration room 104 by the flue on top Afterwards, flue gas flow rate slows down so that fine particle is contacted with agglomerator droplet more fully, be conducive to particulate matter in flue gas with Agglomerator mixes;The shape of cross section of turbulence columns 102 is isosceles triangle, and triangle base is perpendicular to flow of flue gas direction, top Angle pointing direction is relative with flow of flue gas direction, flue gas turbulization when turbulence columns 102, by rotation and mutually collision, It is fully contacted between fine particle and agglomerator droplet and between other particles, strengthens agglomerating effect, promote fine Particulate matter is reunited and is grown up, so as to increase particle size, beneficial to being trapped by ensuing capture unit 200 of turning back.
The bottom of particle agglomeration room 104 is provided with Contraction Ducts 103, and the cross-sectional area of the Contraction Ducts 103 is along vertical Downwardly direction is gradually reduced, and particle agglomeration room 104 is connected with intake elbow 220 by Contraction Ducts 103, increases gas velocity Rate so that flue gas is entered higher initial velocity in capture unit 200 of turning back, produces larger inertia force, is conducive to particulate matter There is sedimentation in capture unit 200 of turning back.
Flue gas at the top of intake elbow 220 flows into end 221 by shaking 103 phase of Contraction Ducts of bellows 201 and top Even, the flue gas outflow end 231 at the top of outlet bend pipe 230 is connected with the flue on top by shaking bellows 201, that is, turn back Bend pipe can make the vibrations of vertical direction relative to particle agglomeration unit 100.
Embodiment 3
The substance of the present embodiment with embodiment 2, difference is:Also include electrostatic precipitation unit 300, electrostatic is removed Dirt unit 300 includes corona electrode 301, collection electrode 302 and power supply part 303, and described corona electrode 301 is arranged at particle The bottom of agglomeration unit 100, in sintering flue gas, fine particle speed after the reunion of 102 flow-disturbing of turbulence columns is reduced, therefore Jing Cross corona electrode 301 to take longer for, it is charged more abundant, and also subparticle is in 104 top of particle agglomeration room reunion length Greatly so that the particle that reunion is grown up can be preferably charged by corona electrode 301;Collection electrode 302 is arranged at reservoir block 210 and enters Top at mouthful, the particulate matter of the trapping of collection electrode 302 are fallen in reservoir block 210.Corona electrode 301 in the present embodiment, gather dust Electrode 302 is connected with the negative and positive electrode of power supply part 303 respectively, i.e., corona electrode 301 is connected with the negative pole of power supply part 303, Collection electrode 302 is connected with the positive pole of power supply part 303.
In the case that corona electrode 301 discharges, the particulate matter in flue gas is in the bottom of particle agglomeration unit 100 by load Negative electrical charge, then into electrostatic precipitation unit 300, locates above 210 porch of reservoir block, carries the particulate matter quilt of negative electrical charge Collection electrode 302 is trapped, and bend pipe of turning back can make the vibrations of vertical direction relative to particle agglomeration unit 100, vibrations and Mutual collision is produced, the contact probability of particulate matter and collection electrode 302 is increased.So as to promote particulate matter in reservoir block 210 places above porch are trapped by collection electrode 302, and the particulate matter of collection electrode 302 is deposited in storage during vibrations In collection part 210.
Embodiment 4
The substance of the present embodiment with embodiment 2, difference is:The present embodiment is turned back in capture unit 200 Electromagnetic shaker 202 is provided with, capture unit of entirely turning back 200 can all produce vibrations, particulate matter reaches receipts above reservoir block 210 Before dirt electrode 302, vibrations and produce mutual collision, be more easy to be trapped by collection electrode 302, reach after collection electrode 302 because Increase particulate matter and 302 contact probability of collection electrode for vibrations, collection electrode 302 is ejected in the particulate matter vibrations after neutralization, and is fallen Enter in reservoir block 210, capture, trap more particulate matters.Intake elbow 220 and outlet bend pipe 230 are by shaking ripple Pipe 201 is connected with flue, and, during vibrations, the particle agglomeration unit 100 on top can't for capture unit of turning back 200 Generation shakes, and reduces during capture unit 200 of turning back is trapped for 100 aggregation procedure of particle agglomeration unit affects.
Embodiment 5
As shown in Fig. 2 the substance of the present embodiment is with embodiment 2, difference is:Reservoir block 210 is by collection Dirt bellows 214 is connected with bend pipe of turning back, it is to avoid bend pipe of turning back vibrations cause 210 airborne dust of reservoir block;Enter in reservoir block 210 Dust spoiler 211 is additionally provided with mouthful, its effect is to reduce the speed after particulate matter enters reservoir block 210, coordinates water smoke Shower nozzle 212, makes particulate matter better through water smoke secondary agglomeration, it is to avoid 210 endoparticle thing of reservoir block is raised out.
The present invention reduction of discharging step be:
Step one, fine particle are reunited
Flue gas enters reunion capturing device, sprays into agglomerator in reunion capturing device in flue gas, fine particle with Agglomerator is sufficiently mixed, and agglomerator droplet is sufficiently mixed with flue gas and is reunited grows up;Describe in detail as follows:
A, flue gas enter particle agglomeration room 104, spray into agglomerator droplet at the top of particle agglomeration room 104 in flue gas, And the flow direction of the injection direction of agglomerator droplet and flue gas is conversely, flue gas is under the effect of 102 flow-disturbing of turbulence columns, subparticle There is the motion of irregular direction in thing, the particulate matter in agglomerator droplet and flue gas is sufficiently mixed and reunites grows up;
After B, particulate matter reunion are grown up, corona electrode 301 carries out corona discharge to particulate matter, makes electricity is taken on particulate matter Lotus, and corona electrode 301 is connected with the negative pole of power supply part 303, so that negative electrical charge on particulate matter band.
Step 2, trap particulate matter
Fine particle reunite grow up after enter reunion capturing device and turning back in bend pipe, in the steering of bend pipe bottom of turning back The change gas flow rapidly of position flue gas, the particulate matter in flue gas are separated with flue gas in the presence of gravity and inertia force, folding Bending pipe is inclined to arrange reservoir block 210, and particulate matter is trapped and stored by reservoir block 210;Describe in detail as follows:
Particulate matter in A, flue gas grows up Jing reuniting, capture unit 200 of turning back is entered after corona discharge, and particulate matter is with flue gas Move along in bend pipe of turning back, particulate matter is settled under the collective effect of gravity and Particle Inertia power, is captured under bend pipe of turning back In the reservoir block 210 in portion;
B, power supply part 303 are powered for collection electrode 302 so that collection electrode 302 takes the electric charge different with particulate matter, The particle not settled is trapped by collection electrode 302, Jing after vibrations is stored in reservoir block 210;Wherein collection electrode 302 and power supply The positive pole of part 303 is connected, and is adsorbed by collection electrode 302 by the particulate matter of negative electricity on 301 load of corona electrode, in vibrations During the particulate matter that adsorbs in collection electrode 302 fall in reservoir block 210, and trapped by reservoir block 210.
The present invention is described in detail above in conjunction with specific exemplary embodiment.It is understood, however, that can not take off Various modifications and variations are carried out in the case of the scope of the present invention being defined by the following claims.Detailed description and drawings Should be to be considered only as it is illustrative and not restrictive, if there is any such modification and modification, then they all incite somebody to action Fall in the scope of the present invention described here.Additionally, background technology is intended to illustrate the Development Status and meaning of this technology, It is not intended to limit the application of the present invention or the application and the present invention.
Although more specifically, here has been described with the exemplary embodiment of the present invention, the invention is not limited in These embodiments, but including those skilled in the art according to above detailed description it can be appreciated that it is modified, omit, Any and whole embodiments of (such as between each embodiment) combination, adaptive change and/or replacement.In claim Restriction can be widely explained according to the language used in claim, and is not limited in foregoing detailed description or in reality The example described during applying this application, these examples are considered as nonexcludability.For example, in the present invention, term is " preferred Ground " not exclusively, preferably, here it means that " but be not restricted to that ".Where method or process claims in office In any step for the enumerating order that can perform in any order and propose in being not limited to claim.Therefore, the present invention Scope only should be determined by claims and its legal equivalents, rather than by descriptions and examples given above come It is determined that.

Claims (10)

1. the capture unit of turning back of a kind of flue gas particles, it is characterised in that:Including reservoir block (210), intake elbow (220) With outlet bend pipe (230), described intake elbow (220) is connected with the bottom of outlet bend pipe (230) and constitutes bend pipe of turning back, Described reservoir block (210) is inclined to be arranged on outlet bend pipe (230), and particulate matter in bend pipe of turning back is settled and is stored in In reservoir block (210).
2. the capture unit of turning back of a kind of flue gas fine particulate matter according to claim 1, it is characterised in that:Described enters Gas bend pipe (220) and outlet bend pipe (230) are connected with flue by shaking bellows (201).
3. the capture unit of turning back of a kind of flue gas fine particulate matter according to claim 2, it is characterised in that:Described storage The inclination angle for integrating part (210) with vertical direction is as 10-30 °, and reservoir block (210) porch is provided with waterfog head (212)。
4. the capture unit of turning back of a kind of flue gas particles according to any one of claim 1-3, it is characterised in that:It is described Capture unit of turning back (200) on be provided with electromagnetic shaker (202).
5. a kind of agglomeration for iron mine flue gas fine particulate matter reunion capturing device, it is characterised in that:Including
Agglomerator shower nozzle (101) is provided with particle agglomeration unit (100), the particle agglomeration unit (100);
Capture unit of turning back (200), turn back trapping of the capture unit of turning back (200) described in any one of claim 1-4 are single Unit;
Described particle agglomeration unit (100) is arranged at the top of capture unit of turning back (200), particle agglomeration unit (100) Bottom is connected with the intake elbow (220) of capture unit of turning back (200).
6. a kind of agglomeration for iron mine flue gas fine particulate matter reunion capturing device according to claim 5, it is characterised in that:Institute The particle agglomeration unit (100) stated includes agglomerator shower nozzle (101), turbulence columns (102) and particle agglomeration room (104), described Agglomerator shower nozzle (101) and turbulence columns (102) are arranged at the inside of particle agglomeration room (104), and agglomerator shower nozzle (101) is located at The top of turbulence columns (102).
7. a kind of agglomeration for iron mine flue gas fine particulate matter reunion capturing device according to claim 6, it is characterised in that:Institute The injection direction of the agglomerator shower nozzle (101) stated is contrary with the flow direction of flue gas;The cross section shape of described turbulence columns (102) Shape is isosceles triangle.
8. a kind of agglomeration for iron mine flue gas fine particulate matter reunion capturing device according to claim 6 or 7, its feature exist In:The bottom of described particle agglomeration room (104) is provided with Contraction Ducts (103), the cross-sectional area edge of the Contraction Ducts (103) Vertically downward direction to be gradually reduced, particle agglomeration room (104) are connected with intake elbow (220) by Contraction Ducts (103).
9. a kind of agglomeration for iron mine flue gas fine particulate matter reunion capturing device according to claim 8, it is characterised in that:Also Including electrostatic precipitation unit (300), the electrostatic precipitation unit (300) is including corona electrode (301), collection electrode (302) and supplies Electric part (303), described corona electrode (301) are arranged in particle agglomeration unit (100), and collection electrode (302) is arranged at On the outlet bend pipe (230) of capture unit of turning back (200), described corona electrode (301), collection electrode (302) respectively with confession The negative and positive electrode of electric part (303) is connected.
10. a kind of agglomeration for iron mine flue gas fine particulate matter reunion capturing device according to claim 9, it is characterised in that: Described corona electrode (301) is arranged at the bottom of turbulence columns (102), and described collection electrode (302) is arranged at reservoir block (210) above porch.
CN201611077977.9A 2016-11-30 2016-11-30 A kind of sintering flue gas fine particle is turned back capture unit Active CN106512632B (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
CN201811621271.3A CN109569169B (en) 2016-11-30 2016-11-30 Device and method for capturing fine particles of sintering flue gas
CN201611077977.9A CN106512632B (en) 2016-11-30 2016-11-30 A kind of sintering flue gas fine particle is turned back capture unit

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201611077977.9A CN106512632B (en) 2016-11-30 2016-11-30 A kind of sintering flue gas fine particle is turned back capture unit

Related Child Applications (1)

Application Number Title Priority Date Filing Date
CN201811621271.3A Division CN109569169B (en) 2016-11-30 2016-11-30 Device and method for capturing fine particles of sintering flue gas

Publications (2)

Publication Number Publication Date
CN106512632A true CN106512632A (en) 2017-03-22
CN106512632B CN106512632B (en) 2018-12-14

Family

ID=58353521

Family Applications (2)

Application Number Title Priority Date Filing Date
CN201611077977.9A Active CN106512632B (en) 2016-11-30 2016-11-30 A kind of sintering flue gas fine particle is turned back capture unit
CN201811621271.3A Active CN109569169B (en) 2016-11-30 2016-11-30 Device and method for capturing fine particles of sintering flue gas

Family Applications After (1)

Application Number Title Priority Date Filing Date
CN201811621271.3A Active CN109569169B (en) 2016-11-30 2016-11-30 Device and method for capturing fine particles of sintering flue gas

Country Status (1)

Country Link
CN (2) CN106512632B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111672238A (en) * 2020-06-11 2020-09-18 安徽天顺环保设备股份有限公司 Nozzle anti-blocking device and method of submerged arc furnace flue gas spray dust remover

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB373661A (en) * 1931-02-02 1932-06-02 George Henry Clifford Corner Improvements in or relating to the separation of liquid particles from steam and other gases and apparatus therefor
CN102784536A (en) * 2012-07-18 2012-11-21 樊荣 Spiral pipe gas-water separator
CN102814098A (en) * 2012-09-19 2012-12-12 巨锋 Multilevel combined waste gas purifying equipment
CN103920354A (en) * 2013-01-15 2014-07-16 宝山钢铁股份有限公司 Multi-level spray tower type dust removal device for processing and discharging steelmaking roller slag
CN104888571A (en) * 2015-06-25 2015-09-09 山东钢铁股份有限公司 Industrial flue gas dust removal device
CN204745985U (en) * 2015-06-10 2015-11-11 长春职业技术学院(长春市职业技术教育中心长春市财政学校) Electrified dust collector
CN205095600U (en) * 2015-10-30 2016-03-23 施可丰泸州化工有限公司 Monoammonium phosphate tail gas two -stage dust purification device
CN205235644U (en) * 2015-12-25 2016-05-18 天津市维海环保工程设备有限公司 Foam dust -removing device
CN206355783U (en) * 2016-11-30 2017-07-28 安徽工业大学 One kind sintering flue gas fine particulate matter is turned back capture unit and reunion capturing device

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3609853A1 (en) * 1986-03-22 1987-09-24 Bosch Gmbh Robert Device for removing solid or liquid particles from a gas stream
DE4112455A1 (en) * 1991-04-12 1992-10-15 Ver Energiewerke Ag Dust removal from flue gas - by gas flow diversion and electrostatic pptn.
SE527104C2 (en) * 2004-05-21 2005-12-20 Alstom Technology Ltd Method and apparatus for separating dust particles
JP2007107399A (en) * 2005-10-11 2007-04-26 Denso Corp Exhaust emission control device for internal combustion engine
CN101664623A (en) * 2009-09-25 2010-03-10 合肥工业大学 Ultrafine particle deduster
KR101265497B1 (en) * 2012-10-30 2013-05-20 한국지질자원연구원 Duct for ventilating air of mining with dust collecting structue by controlling air flow
CN103768886B (en) * 2014-01-24 2015-07-08 浙江大学 Efficient multi-field-coordination fine particulate matter removal device and method
CN104801420B (en) * 2015-05-13 2017-05-10 东南大学 Device and method for increasing grain size of PM2.5 (particulate matter2.5) through turbulent flow and chemical agglomeration coupling
CN105597477B (en) * 2016-03-23 2017-12-01 河北工业大学 Remove the device and method of superfine particulate matter in fire coal boiler fume
CN105854500B (en) * 2016-04-28 2018-02-13 河北工业大学 Turbulent flow reunion room and the method for application reunion room removing superfine particulate matter
CN105797531B (en) * 2016-04-28 2018-12-04 安徽工业大学 A kind of method that agglomeration process inhibits the discharge of Ore Sintering Process fine particle

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB373661A (en) * 1931-02-02 1932-06-02 George Henry Clifford Corner Improvements in or relating to the separation of liquid particles from steam and other gases and apparatus therefor
CN102784536A (en) * 2012-07-18 2012-11-21 樊荣 Spiral pipe gas-water separator
CN102814098A (en) * 2012-09-19 2012-12-12 巨锋 Multilevel combined waste gas purifying equipment
CN103920354A (en) * 2013-01-15 2014-07-16 宝山钢铁股份有限公司 Multi-level spray tower type dust removal device for processing and discharging steelmaking roller slag
CN204745985U (en) * 2015-06-10 2015-11-11 长春职业技术学院(长春市职业技术教育中心长春市财政学校) Electrified dust collector
CN104888571A (en) * 2015-06-25 2015-09-09 山东钢铁股份有限公司 Industrial flue gas dust removal device
CN205095600U (en) * 2015-10-30 2016-03-23 施可丰泸州化工有限公司 Monoammonium phosphate tail gas two -stage dust purification device
CN205235644U (en) * 2015-12-25 2016-05-18 天津市维海环保工程设备有限公司 Foam dust -removing device
CN206355783U (en) * 2016-11-30 2017-07-28 安徽工业大学 One kind sintering flue gas fine particulate matter is turned back capture unit and reunion capturing device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111672238A (en) * 2020-06-11 2020-09-18 安徽天顺环保设备股份有限公司 Nozzle anti-blocking device and method of submerged arc furnace flue gas spray dust remover

Also Published As

Publication number Publication date
CN109569169B (en) 2023-09-19
CN106512632B (en) 2018-12-14
CN109569169A (en) 2019-04-05

Similar Documents

Publication Publication Date Title
CN106440840B (en) A kind of Ore Sintering Process flue gas PM10/2.5Selective emission-reducing system
CN102179125A (en) Method and device for removing dust in flue gas
CN103495322B (en) The apparatus and method of a kind of dedusting demercuration integration
CN104324805A (en) Method for capturing PM2.5 fine particles through water mist charged coagulation for electric precipitation
CN105797524A (en) Heteropolar electric charge fogdrop coalescence dust-removing device and method thereof
CN206222955U (en) A kind of selective emission-reducing system of Ore Sintering Process flue gas PM10/2.5
CN106693593A (en) Double-ejection type angle type ultrafine particle coagulation tank
CN107648975A (en) A kind of dust removal method and device of dusty gas minimum discharge
CN104069712A (en) Chemical coagulation-based 'electricity-bag' integrated compound dust removing process
CN101745284A (en) Ultrasonic atomizing bag type dust removing device and dust removing method
CN106512563B (en) A kind of reunion trapping of sintering flue gas subparticle and discharge-reducing method
CN104069713B (en) A kind of electricity-bag dust collecting process strengthening coalescence
CN106731434A (en) A kind of combined ultra-fine grain coalescence case
CN206343044U (en) A kind of agglomeration for iron mine flue gas fine particulate matter magnetic field reunion capturing device
CN105561726B (en) One kind carrying acting type wet static dedusting demister
CN106215538B (en) One kind is used to sinter/pelletizing wet desulfurization flue gas deep treatment system
CN206355783U (en) One kind sintering flue gas fine particulate matter is turned back capture unit and reunion capturing device
CN106583042B (en) A method of sintering flue gas fine particle is removed based on pulsed discharge
CN106731437A (en) The horizontal anchor type ultra-fine grain coalescence case of double jet type
CN106512632A (en) Folded gathering unit and agglomeration gathering device of sintering flue gas fine particles
CN106693592A (en) Double-jet type streamlined ultra-fine particle coagulation box
CN204247379U (en) A kind of vertical wide-space wet electrical dust precipitator
CN206746199U (en) Double filter screen electrocoagulation fine particle cleaning equipment
CN106694225A (en) Device for removing fine particulate matter of sintering flue gas by pulse corona charge
CN206382119U (en) A kind of device of pulse corona charge removing sintering flue gas fine particulate matter

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant