CN206652344U - A kind of modularization dust pelletizing system - Google Patents
A kind of modularization dust pelletizing system Download PDFInfo
- Publication number
- CN206652344U CN206652344U CN201720286459.1U CN201720286459U CN206652344U CN 206652344 U CN206652344 U CN 206652344U CN 201720286459 U CN201720286459 U CN 201720286459U CN 206652344 U CN206652344 U CN 206652344U
- Authority
- CN
- China
- Prior art keywords
- interface channel
- dust removing
- removing units
- dust
- air inlet
- 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.)
- Active
Links
Landscapes
- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
The utility model discloses a kind of modularization dust pelletizing system, including air inlet/outlet passage to be connected with two of air inlet/outlet passage both sides or the dust removing units of more than two, each dust removing units are laid in using dismountable interface channel with the air inlet/outlet passage.Using unit-modularized design, when enterprise produces, substantial amounts of dust removing units can first be produced and carry out standby deposit, need to assemble the dust removing units of varying number further according to client, both it had been easy to the production management and control of enterprise, production difficulty and production equipment cost are reduced again, ETCD estimated time of commencing discharging and efficiency can be gone out with effective guarantee product simultaneously, and easily facilitate logistics delivery, when equipment is installed, only need to be connected dust removing units with air inlet/outlet passage by interface channel, when some dust removing units needs repair and maintenance, only need that the dust removing units are shut down or dismantled, the operating of other equipment is not influenceed, mutual backup can also be formed between each dust removing units, ensure the normal production requirement of enterprise.
Description
Technical field
Technical field of dust removal equipment is the utility model is related to, more particularly to a kind of modularization dust pelletizing system.
Background technology
At present, it is to adopt in the wide variety of sack cleaner in the fields such as mine, metallurgy, machinery, building materials, chemical industry, its principle
The filter bag made of the filter cloth of weaving or nonwoven felt, is filtered to dusty gas, when the gas containing dust by except
During filter bag in dirt device, a gas permeation is gone, and dust is delayed on filter bag surface, reaches dedusting purpose, with other dedustings
Device is compared, and advantage is filter efficiency height, seldom from the gas dust-laden of deduster discharge typically more than 99.99%, can effectively be expired
The requirement of sufficient environmental emission standard, therefore obtain being widely recognized as market.
But bag-type dust removal system traditional at present is mostly integral solder assembling structure, difficulty is on the one hand manufactured, to life
Production. art and equipment working condition require higher, on the other hand transport inconvenience and cost is high, welding structure, can not disassemble, easily by
Ultra-wide superelevation limits, meanwhile, installation maintenance is inconvenient, and needs to use ultra-large type hanging device during installation, due to cloth bag quantity
It is big and be consumable accessory, it is necessary to which overall shutdown, greatly affected production efficiency during repair and maintenance.
Utility model content
In view of the deficienciess of the prior art, technical problem to be solved in the utility model be to provide it is a kind of modular
Dust pelletizing system, its convenient disassembly, it is easy to produce, transport, install and safeguard, and according to production needs assembling can be selected to remove
Dirt unit is how much, has both been easy to production management and the depot spare part of enterprise, again can with the time of delivery of effective guarantee product and efficiency,
Reduce enterprise's production and operation cost.
In order to solve the above-mentioned technical problem, the utility model is to realize by the following technical solutions, a kind of modularization
Dust pelletizing system, including air inlet/outlet passage and the dust removing units of more than two for being laid in air inlet/outlet passage both sides, each dedusting list
Member is connected using dismountable interface channel with the air inlet/outlet passage.
The dust removing units include body of deduster and are arranged on the ash bucket of body lower end, and ash bucket side passes through first
Interface channel connects with the air intake part of the air inlet/outlet passage, tilting in ash bucket to have matrix vortex airflow uniform distribution plate, institute
It is concordant with the top of the passway of first interface channel to state matrix form airflow uniform distribution plate upper end, lower end extends to dust stratification obliquely
The opposite side of first interface channel on bucket, and it is corresponding with the extension line of the first interface channel passway lower end.
The matrix form airflow uniform distribution plate include multiple stringer boards parallel with the airflow direction of first interface channel and
Some transverse slats vertical with the airflow direction of first interface channel on the stringer board are laid in, the transverse slat is set in vertical shape
Put on the stringer board.
The transverse slat is identical height dimension, and the transverse slat height for the 1/2-2/3 that mutually misplaces up and down successively.
Section of the transverse slat on stringer board direction be " I " shape, serpentine, "（" shape, the one or more in " > " shape.
The second interface channel is provided with the top of the body of deduster, second interface channel at least bottom surface is planar junction
Structure, passway is provided with the bottom surface of second interface channel and is connected with the air-outlet part of the air inlet/outlet passage.
The dust pelletizing system also includes pulse backblowing module, and the pulse backblowing module includes high pressure tank and setting
Pulse backblowing unit on the second interface channel of each dust removing units, the high pressure tank pass through high voltage charge and laying
High pressure branch on high voltage charge is connected with each pulse backblowing unit respectively, is provided with each high pressure branch high voltage-controlled
Valve processed.
The pulse backblowing unit includes being arranged on pulse gassing mechanism and the passway at the top of second interface channel
Plugging mechanism.
The pulse gassing mechanism includes the high-pressure nozzle being connected with the high pressure branch and is arranged on the high-pressure nozzle
On impulse electromagnetic valve, the spout end of the high-pressure nozzle is extended to inside second interface channel.
The plugging mechanism includes being arranged on the telescopic cylinder above the second interface channel, and the expansion link of cylinder extends into institute
State inside the second interface channel, and have closure cover plate in its end set.
Sealing ring is provided between the expansion link and the second interface channel roof or the expansion link overcoat is provided with
Seal bellows, the both ends of bellows are tightly connected with the roof of the closure cover plate and second interface channel respectively.
The bottom of the closure cover plate is provided with flexible rubber dam pad.
The pulse backblowing unit is arranged on the top of the body of deduster, the high-pressure nozzle and the telescopic cylinder
On the top plate that may be contained within the body of deduster, the expansion link of high-pressure nozzle and telescopic cylinder extends into the deduster sheet
One pulse backblowing plate of connection, pulse backblowing intralamellar part are cavity structure in vivo, its bottom be laid with the body of deduster
The corresponding some high pressure nozzles of filter bag.
The utility model is relative to positive beneficial effect possessed by prior art：
1. dust pelletizing system of the present utility model uses unit-modularized design, led to by the way that dust removing units are laid in into air inlet/outlet
Road both sides, and connected by dismountable interface channel, so as to effectively realize the removable unloading functions of each unit module, enterprise's production
When, it can first produce substantial amounts of dust removing units and carry out the standby dust removing units deposited, assembling varying number is needed further according to client, both just
In the production management and control of enterprise, production difficulty and production equipment cost are reduced again, while can be with effective guarantee product
Go out ETCD estimated time of commencing discharging and efficiency, and easily facilitate logistics delivery, equipment install when, it is only necessary to by interface channel by dust removing units with
Air inlet/outlet passage connects, when some dust removing units needs repair and maintenance, it is only necessary to which the dust removing units are shut down or dismantled i.e.
Can, the operating of other equipment is not influenceed, mutual backup can also be formed between each dust removing units, and ensureing the normal production of enterprise needs
Ask.
2. single dust removing units are by the tilting matrix form airflow uniform distribution plate in the ash bucket of body of deduster lower end, thereon
End is concordant with the passway of the first interface channel top, and lower end extends to the relative of the first interface channel on ash bucket obliquely
Side, and it is corresponding with the extension line of the first interface channel passway lower end, it is stepped to forming one so as to come in dust-contained airflow
The uniform barricade of wind stream, when the dust-contained airflow of high speed is entered inside ash bucket along the first interface channel, ash-laden gas
Stream is formed and met successively with stepped matrix form airflow uniform distribution plate by different level from top to bottom, on the one hand, airflow uniform distribution plate pair
Dust-contained airflow carries out abundant air-flow and turned to uniformly, and lower stream of airflow will not be caused excessive and produce the phenomenon of reentrainment of dust, and made
Filter bag lower end space of planes air flow method is uniform, on the other hand, while turning to uniform, certain resistance is formed to dust-contained airflow
Keep off, the big dust particle in dust-contained airflow bumps against with uniform board, and kinetic energy reduces, and speed declines, and falls under gravity into dust stratification
Struggle against bottom, so as to effectively stop that big dust particle is up, realize one-level bulky grain dedusting, the 3rd, dust-contained airflow is by matrix
During formula airflow uniform distribution plate, after uniform board forms effectively stop, the air pressure of rear side is relatively low, and air-flow is when flowing through herein, shape
Into being vortexed one by one, matrix form is integrally formed and is vortexed, effect of the part smaller particle dust in dust-contained airflow in vortex cyclone device
Under, reduce speed uplink, and form reuniting effect, finally fall on ash bucket bottom under gravity, so as to stop portions compared with
Little particle dust is up, realizes second part smaller particle dedusting, and then is combined with filter bag, deduster is effectively realized overall three
The effect of level dedusting, improves efficiency of dust collection and dust removing effects, also, avoids shock of the big dust particle to filter bag, effectively carries
High filter bag security reliability and service life.
3. using the stringer board and transverse slat of multiple crisscross layings, matrix type structure is formed, transverse slat is vertically arranged, to gas
After flow resistance gear, side forms vortex behind, and stringer board forms significant interval, a vortex is formed in each interval, realizes square
Configuration is distributed, and on the one hand makes vortex more stable, on the other hand makes the separating effect of smaller particle dust more preferable.Transverse slat is using identical
Height dimension and successively mutually up and down dislocation 1/2-2/3 transverse slat height, effective windbreak is formed in direction windward
On the basis of, the separative efficiency of one-level big dust particle and second part smaller particle dust effectively can be further improved, optimization removes
Dirt effect.
4. at least bottom surface is used as the second interface channel of planar structure and going out for air inlet/outlet passage at the top of body of deduster
Wind part connects, and on the one hand convenient combination installation and demolition and maintenance, on the other hand facilitate the plugging mechanism of pulse backblowing module to adopt
Passway is blocked with closure cover plate quickness and high efficiency.
5. pulse backblowing module matches with dust removing units, unit-modularized design, high pressure is set on each high pressure branch
Control valve, the control respectively to each pulse backblowing unit can be effectively realized, and voltage stabilizing control is realized entirely through high pressure tank
System, blowback effect is improved, ensure that the dust on filter bag is effectively blown off.High-pressure nozzle is arranged on the second interface channel, a side
Face makes the structure of body of deduster simpler, is easy to processing and manufacturing and repair and maintenance, another aspect high-pressure nozzle anti-here
Blow, during blowback, the air-out passage mouth closure of the second interface channel, gases at high pressure are quickly filled with and produced in the second interface channel
One kinetic energy to the lateral movement of body of deduster one, it is easy to gases at high pressure to be covered with the top of body of deduster, deduster top rapidly
Portion the overall action for producing a downward blowback filter bag, makes all filter bags can be in the effect of high pressure draught by cover closure
Under, blowback is shaken dust stratification, simple, convenient, efficient.
6. by setting sealing ring between expansion link and the second interface channel roof or setting and block in expansion link overcoat
The seal bellows that the roof of cover plate and the second interface channel is tightly connected, and flexible rubber dam is set in the bottom of cover plate
Pad, the air-tightness of equipment can be effectively improved, avoid gas leakage, ensure high pressure effect during blowback, the stabilization for improving reverse gas cleaning can
By property.
7. the utility model is simple in construction, production, transport, installation, repair and maintenance are convenient, and efficiency of dust collection is high, dust removing effects
Good, life of bag filter length, pulse backblowing is reliable and stable, practical, and should be widely promoted utilization.
Brief description of the drawings
The utility model is further described below in conjunction with the accompanying drawings：
Fig. 1 is the overlooking the structure diagram of the utility model embodiment one；
Fig. 2 is the main structure diagram of the utility model embodiment one；
Fig. 3 is the partial structural diagram of ash bucket part in Fig. 2；
Fig. 4 is Fig. 3 overlooking the structure diagram；
Fig. 5 is the main structure diagram of the utility model embodiment two；
Fig. 6 is the overlooking the structure diagram of the utility model embodiment three；
Fig. 7 is the overlooking the structure diagram of the utility model embodiment four.
Embodiment
With reference to embodiment, the utility model is expanded on further.
As Figure 1-4：A kind of modularization dust pelletizing system, including air inlet/outlet passage 1 and it is laid in the both sides of air inlet/outlet passage 1
The dust removing units 2 of more than two, the present embodiment illustrates with 2 dust removing units, and each dust removing units 2 are using detachable
Interface channel connected with the air inlet/outlet passage 1, referring to Fig. 1 and 2.Dust pelletizing system uses unit-modularized design, each unit
Module is composable and dismantles, and when enterprise produces, can first produce substantial amounts of dust removing units 2 and for depositing, needed further according to client,
The dust removing units 2 of varying number are assembled on air inlet/outlet passage 1, enterprise production management is easy, production difficulty and cost are able to
Reducing, production efficiency and time are secure, and logistics transportation avoids the limitation such as superelevation ultra-wide, and cost of transportation effectively reduces, installation,
Overhaul, be easy to maintenance, enterprise's production is secure.
Referring to Fig. 2, the dust removing units 2 include body of deduster 2-1 and are arranged on the ash bucket 2-2 of body 2-1 lower ends,
Ash bucket 2-2 sides are connected by the first interface channel 3-1 with the air intake part 1-1 of the air inlet/outlet passage 1, ash bucket 2-2
It is interior it is tilting have a matrix vortex airflow uniform distribution plate 2-3, the matrix form airflow uniform distribution plate 2-3 upper ends and first interface channel
Concordant at the top of 3-1 passway, lower end extends to the opposite side of the first interface channel 3-1 on ash bucket 2-2 obliquely, and
It is corresponding with the extension line of the first interface channel 3-1 passways lower end.It is stair-stepping to forming one so as to come in dust-contained airflow
The uniform barricade of wind stream, when the dust-contained airflow of high speed is entered inside ash bucket 2-2 along the first interface channel 3-1, contain
Dust and gas stream is formed and met successively with stepped matrix form airflow uniform distribution plate by different level from top to bottom, and dust-contained airflow is filled
Point air-flow turns to uniform, while turning to uniform, forms certain stop to dust-contained airflow, the bulky grain powder in dust-contained airflow
Dirt bumps against with uniform board, and kinetic energy reduces, and speed declines, and falls under gravity into ash bucket bottom, so as to effectively stop big
Grain dust is up, and the air pressure on rear side of uniform board is relatively low, and when flowing through herein, formation is vortexed air-flow one by one, is integrally formed
Matrix form is vortexed, and the part smaller particle dust in dust-contained airflow reduces speed uplink, finally existed in the presence of vortex cyclone device
Ash bucket bottom is fallen under Action of Gravity Field, realizes second part smaller particle dedusting, and then is combined with filter bag, makes deduster effective
The effect of overall 3-stage dust-removal is realized, improves efficiency of dust collection and dust removing effects, also, avoid big dust particle and filter bag is hit
Hit, effectively improve filter bag security reliability and service life.
Referring to Fig. 3 and 4, the matrix form airflow uniform distribution plate 2-3 includes the multiple and air-flow of the first interface channel 3-1
The parallel stringer board 2-3-1 in direction and it is laid in vertical with the airflow direction of the first interface channel 3-1 on the stringer board 2-3-1
Some transverse slat 2-3-2, the transverse slat 2-3-2 is arranged on the stringer board 2-3-1 in vertical shape.The transverse slat 2-3-2 is
Identical height dimension, and mutually highly, the transverse slat 2-3-2 in the present embodiment is used dislocation 1/2-2/3 transverse slat up and down successively
" I " shape structure, the transverse slat 2-3-2 and stringer board 2-3-1 are woven into fenestral fabric, have both improved matrix vortex airflow uniform distribution
Plate 2-3 bulk strength, cause each small vortex is independent to produce again, do not interfere with each other, improve the separation to smaller particle dust
Effect.The section of matrix vortex airflow uniform distribution plate 2-3 of the present utility model, its transverse slat 2-3-2 on stringer board 2-3-1 directions is also
Can use serpentine, "（" shape, any one structure in " > " shape or various structures combination, applicant applied for title on the same day
For the utility model patent of " a kind of airflow uniform distribution device for producing matrix vortex ", will not be repeated here.
Referring to Fig. 2, the second interface channel 3-2, the second interface channel 3- is provided with the top of the body of deduster 2-1
2 bottom surface is planar structure, and passway and the air inlet/outlet passage 1 are provided with the bottom surface of the second interface channel 3-2
Air-outlet part 1-2 is connected.The dust pelletizing system also includes pulse backblowing module, and the pulse backblowing module includes high-pressure gas
Tank and the pulse backblowing unit being arranged on the second interface channel 3-2 of each dust removing units 2, the high pressure tank pass through height
Pressure supervisor 4 and the high pressure branch 5 being laid on high voltage charge 4 are connected with each pulse backblowing unit respectively, each high pressure branch 5
On be provided with high pressure control valve 6, the work of the pulse backblowing unit on each dust removing units 2 is controlled by high pressure control valve 6
Whether, the pulse backblowing unit includes being arranged on pulse gassing mechanism and the passway at the top of the second interface channel 3-2
Plugging mechanism, the pulse gassing mechanism include the high-pressure nozzle 8 being connected with the high pressure branch 5 and are arranged on the high pressure spray
Impulse electromagnetic valve 7 on pipe 8, the spout end of the high-pressure nozzle 8 are extended to inside the second interface channel 3-2.The envelope
Stifled mechanism includes being arranged on the telescopic cylinder 9 above the second interface channel 3-2, and cylinder 9 is connected with the high pressure branch 5, passed through
High pressure branch 5 provides power gas source, and the expansion link of cylinder 9 is extended into inside the second interface channel 3-2, and is set in its end
Closure cover plate 10 is equipped with, the bottom of the closure cover plate 10 is provided with flexible rubber dam pad.The expansion link and described second
Sealing ring is provided between interface channel 3-2 roofs or the expansion link overcoat is provided with seal bellows, the both ends point of bellows
It is not tightly connected with the closure cover plate 12 and the second interface channel 3-2 roof, above-mentioned sealing structure can effectively improve
The air-tightness of equipment, gas leakage is avoided, ensure high pressure effect during blowback, improve the reliability of reverse gas cleaning.
During pulse backblowing, the driving closure cover plate 12 of cylinder 9 is descending, passway is blocked, impulse electromagnetic valve 7 is controlled to second
Impulse jet gases at high pressure in interface channel 3-2, gases at high pressure quickly filled with the second interface channel 3-2 and produce one to
The kinetic energy of body of deduster 2-1 directions motion, makes gases at high pressure be covered with dust remover roof, meanwhile, it is overall to produce one downwards instead
The action of filter bag is blown, makes all filter bags can be in the presence of high pressure draught, blowback is shaken dust stratification.
Embodiment two
Referring to Fig. 5, the present embodiment and the difference of embodiment one are：The matrix vortex airflow uniform distribution plate 2-3
Transverse slat 2-3-2 use serpentine structure, the pulse backblowing unit is arranged on the top of the body of deduster 2-1, the height
Pressure jet pipe 8 and the telescopic cylinder 9 may be contained within the top plate of the body of deduster 2-1, high-pressure nozzle 8 and telescopic cylinder 9
Expansion link extend into one pulse backblowing plate 13 of connection in the body of deduster 2-1, the inside of pulse backblowing plate 13 is cavity
Structure, its bottom are laid with some high pressure nozzles 14 corresponding with filter bag in the body of deduster 2-1, high-pressure nozzle 8 with
The internal cavity structures connection of pulse backblowing plate 13, the expansion link lower end of telescopic cylinder 9 and the top of pulse backblowing plate 13 are solid
Fixed connection.High-pressure nozzle 8 can use the stretching structure with good sealing property or can bear high pressure and be beneficial to the high pressure of bending
Flexible pipe, so as to effectively realize the lifting that pulse backblowing plate 13 is controlled by telescopic cylinder 9, during blowback, the driving pulse of telescopic cylinder 9
Blowback plate 13 is descending, and high pressure nozzle 14 is inserted at the top of filter bag, and is closed to forming lid press seal at the top of filter bag, the gases at high pressure of blowback
Filter bag is directly entered, so as to effectively improve the high-pressure pulse back-blowing effect to filter bag.
Embodiment three
Referring to Fig. 6, the present embodiment and the difference of embodiment one are：The both sides difference cloth of the air inlet/outlet passage 1
Provided with 2 dust removing units 2, in the case of other conditions identical, efficiency of dust collection can be effectively improved more than twice compared with embodiment one.
Example IV
Referring to Fig. 7, the present embodiment and the difference of embodiment one are：The both sides difference cloth of the air inlet/outlet passage 1
Provided with 3 dust removing units 2, in the case of other conditions identical, can be effectively improved more than efficiency of dust collection three times compared with embodiment one.
Dust removing units 2 of the present utility model can also use asymmetric design, and quantity can freely add and subtract combination, can also
According to enterprise's place situation, only dust removing units 2 are laid in the side of air inlet/outlet passage 1.
The technical solution of the utility model is not restricted in the range of embodiment described in the utility model, for ability
For the those of ordinary skill in domain, it is possible to understand that can be to these in the case where not departing from principle of the present utility model and spirit
Embodiment carries out a variety of change, modification, replacement and modification, and the scope of protection of the utility model is defined by claims, this reality
Technology contents with new not detailed description are known technology.
Claims (7)
1. a kind of modularization dust pelletizing system, it is characterised in that including air inlet/outlet passage and be laid in two of air inlet/outlet passage both sides
Dust removing units above, each dust removing units are connected using dismountable interface channel with the air inlet/outlet passage, described to remove
Dirt unit includes body of deduster and is arranged on the ash bucket of body lower end, ash bucket side by the first interface channel with it is described
The air intake part connection of air inlet/outlet passage, tilting in ash bucket to have a matrix vortex airflow uniform distribution plate, the matrix form air-flow is equal
Fabric swatch upper end is concordant with the top of the passway of first interface channel, and lower end extends to first company on ash bucket obliquely
Connect the opposite side in road, and, the matrix form airflow uniform distribution plate corresponding with the extension line of the first interface channel passway lower end
Including multiple stringer boards parallel with the airflow direction of first interface channel and it is laid on the stringer board and the described first company
The vertical some transverse slats of the airflow direction in road are connected, the transverse slat is arranged on the stringer board in vertical shape, the deduster sheet
It is provided with the second interface channel at the top of body, second interface channel at least bottom surface is planar structure, second interface channel
Bottom surface on be provided with passway and connected with the air-outlet part of the air inlet/outlet passage.
2. dust pelletizing system as claimed in claim 1, it is characterised in that：The dust pelletizing system also includes pulse backblowing module,
The pulse backblowing module includes high pressure tank and the pulse backblowing being arranged on the second interface channel of each dust removing units
Unit, the high pressure tank by high voltage charge and the high pressure branch being laid on high voltage charge respectively with each pulse backblowing
Unit is connected, and high pressure control valve is provided with each high pressure branch.
3. dust pelletizing system as claimed in claim 2, it is characterised in that：The pulse backblowing unit includes being arranged on described second
Pulse gassing mechanism and passway plugging mechanism at the top of interface channel.
4. dust pelletizing system as claimed in claim 3, it is characterised in that：The pulse gassing mechanism includes and the high pressure branch
The high-pressure nozzle of connection and the impulse electromagnetic valve being arranged on the high-pressure nozzle, the spout end of the high-pressure nozzle extends to institute
State inside the second interface channel.
5. dust pelletizing system as claimed in claim 4, it is characterised in that：The plugging mechanism includes being arranged on the second interface channel
The telescopic cylinder of top, the expansion link of cylinder is extended into inside second interface channel, and has capping in its end set
Plate.
6. dust pelletizing system as claimed in claim 5, it is characterised in that：Between the expansion link and the second interface channel roof
Be provided with sealing ring or the expansion link overcoat be provided with seal bellows, the both ends of bellows respectively with the closure cover plate and
The roof of second interface channel is tightly connected.
7. dust pelletizing system as claimed in claim 5, it is characterised in that：The pulse backblowing unit is arranged on the deduster sheet
The top of body, the high-pressure nozzle and the telescopic cylinder may be contained within the top plate of the body of deduster, high-pressure nozzle and
The expansion link of telescopic cylinder extends into one pulse backblowing plate of connection in the body of deduster, and pulse backblowing intralamellar part is cavity
Structure, its bottom are laid with some high pressure nozzles corresponding with filter bag in the body of deduster.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720286459.1U CN206652344U (en) | 2017-03-23 | 2017-03-23 | A kind of modularization dust pelletizing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720286459.1U CN206652344U (en) | 2017-03-23 | 2017-03-23 | A kind of modularization dust pelletizing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206652344U true CN206652344U (en) | 2017-11-21 |
Family
ID=60315625
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720286459.1U Active CN206652344U (en) | 2017-03-23 | 2017-03-23 | A kind of modularization dust pelletizing system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206652344U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110115880A (en) * | 2019-04-06 | 2019-08-13 | 南阳盛易德环保科技有限公司 | Integrated Environmental-protecting dust-removing system and its control system and control method suitable for mixing station |
-
2017
- 2017-03-23 CN CN201720286459.1U patent/CN206652344U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110115880A (en) * | 2019-04-06 | 2019-08-13 | 南阳盛易德环保科技有限公司 | Integrated Environmental-protecting dust-removing system and its control system and control method suitable for mixing station |
| CN110115880B (en) * | 2019-04-06 | 2023-05-30 | 南阳盛易德环保科技有限公司 | Integrated dust removal system suitable for mixing station, and control system and control method thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201082376Y (en) | Dust remover | |
| CN207899141U (en) | A kind of injection pulse bag type dust collector | |
| CN101884873A (en) | Process and facility for dedusting and removing exhaust gas | |
| CN102059026A (en) | High-efficiency pre-separation pulse bag-type dust collector | |
| CN107866121A (en) | Calcination, fluidization stove dust arrester | |
| CN202876590U (en) | Combined cleaning device of thermoelectric coal conveying system | |
| CN206652319U (en) | A kind of sack cleaner | |
| CN206652344U (en) | A kind of modularization dust pelletizing system | |
| CN209796937U (en) | Dust collector of cement clinker canopy unloading system | |
| CN205516954U (en) | High temperature bag dust removal exhaust gas cleaner | |
| CN203043755U (en) | Pulse bag type dust collector with denitration catalyst function | |
| CN105999910B (en) | A kind of fly-ash filter dust arrester | |
| CN205598785U (en) | Low -pressure pulse bag type dust collector | |
| CN207576043U (en) | Calcination, fluidization stove dust-extraction unit | |
| CN203002126U (en) | Low-pressure jet-pulse bag type dust collector | |
| CN213467129U (en) | Pulse cyclone bag dust collector | |
| CN102755790A (en) | Ammonium polyorthovanadate powder collector | |
| CN207805266U (en) | A kind of filter drum type precipitator | |
| CN208018313U (en) | A kind of filter drum type precipitator | |
| CN103587981B (en) | Powder bin and concrete preparation equipment | |
| CN206762572U (en) | A kind of electric-bag complex dust collector | |
| CN205627386U (en) | Long bag low pressure pulse dust remover | |
| CN207899164U (en) | A kind of hydrofilter | |
| CN207324390U (en) | One kind sintering electrostatic dust collection equipment | |
| CN205699855U (en) | A kind of Novel bag-type dust remover |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |