CN106621600A - Rotary type blowback bag dust collector - Google Patents
Rotary type blowback bag dust collector Download PDFInfo
- Publication number
- CN106621600A CN106621600A CN201611120398.8A CN201611120398A CN106621600A CN 106621600 A CN106621600 A CN 106621600A CN 201611120398 A CN201611120398 A CN 201611120398A CN 106621600 A CN106621600 A CN 106621600A
- Authority
- CN
- China
- Prior art keywords
- rotary type
- blowing
- dedusting
- type back
- settling pocket
- 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.)
- Pending
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/02—Particle separators, e.g. dust precipitators, having hollow filters made of flexible material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/02—Particle separators, e.g. dust precipitators, having hollow filters made of flexible material
- B01D46/023—Pockets filters, i.e. multiple bag filters mounted on a common frame
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/02—Particle separators, e.g. dust precipitators, having hollow filters made of flexible material
- B01D46/04—Cleaning filters
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/02—Particle separators, e.g. dust precipitators, having hollow filters made of flexible material
- B01D46/06—Particle separators, e.g. dust precipitators, having hollow filters made of flexible material with means keeping the working surfaces flat
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/42—Auxiliary equipment or operation thereof
- B01D46/4227—Manipulating filters or filter elements, e.g. handles or extracting tools
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/02—Other waste gases
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
The invention discloses a rotary type blowback bag dust collector, comprising a dust collector body and a dust removing mechanism, wherein the dust removing mechanism is arranged in the dust collector body; the dust collector body is sequentially provided with a top cover, an upper shell, a lower shell and an ash bucket from top to bottom; an air outlet is formed in the upper shell, and an air inlet is formed in the ash bucket; the ash bucket is connected with a vibrating apparatus; the rotary type blowback bag dust collector also comprises a blowback device; the blowback device is connected with an air inlet pipe and an air outlet pipe; the blowback device extends into the dust collector body by means of the air outlet pipe; the blowback device is connected with the dust removing mechanism. By utilizing a structural form of the blowback device and a pulse compensation device, the dust removal efficiency of the bag dust collector is improved, and the problem of 'burnt bag' is effectively improved; the rotary type blowback bag dust collector is simple in structure and convenient and fast in part replacement, and can enable flue gas dust removal to be continuously performed.
Description
Technical field
The present invention relates to a kind of industrial dust collector, particularly a kind of rotary type back-blowing sack cleaner.
Background technology
If industrial gases are directly discharged in air, serious pollution can be caused to environment, form acid rain, acid mist etc. and dislike
Bad weather, affects the mankind and other vegeto-animal healthy growths.Electric cleaner and sack cleaner capture current dedusting market
Dominant contribution.
Electric precipitation is to produce ionization phenomena in the electric field of some strength using gas, when grit is ionized sky through containing
During the space of gas ionization by collision son and it is charged, become charged corpuscle；Substantial amounts of charged corpuscle is in the presence of electric field force to gathering dust
Pole displacement simultaneously adsorbs on dust collection plate, the lasting strike dust collection plate of rapping apparatus, and the dirt block that substantial amounts of micronic dust is formed is in weight
Fall in dust arrester installation under power effect, complete the dust removal process of flue gas.
Sack cleaner is also referred to as filtration dust catcher, is a kind of dry type high efficiency rate cleaner unit, and it is worked out using fiber
The bag type filter elements that thing makes to trap dusty gas in solid particulate matter dust arrester, its action principle be grit around
It is intercepted because inertia force effect and fiber collide, rub when filtering measuring fiber, trickle grit then receives gas molecular impingement (cloth
Bright motion) constantly change the direction of motion, because interfibrous space is less than the free path of gas molecule Brownian movement, grit
Just it is separated with fiber making contact；Its course of work and cloth bag material, weaving method, the density of fiber and dust
The factor such as diffusion, inertia, quality and static characteristic and purge mode are relevant.
At present, in the high dusty gas of collection humidity, sack cleaner easily occurs causing " paste because flue dust condenses
The phenomenon of bag ", therefore bag-type dust gas has certain requirement to the humidity of gas；Although in addition sack cleaner can be prevented effectively from
Secondary fly-up, and efficiency of dust collection can be improved, but in actual use the efficiency of dust collection of sack cleaner also needs to continue perfect.
The content of the invention
The present invention goal of the invention be：For above-mentioned problem, there is provided a kind of rotary type back-blowing cloth bag is removed
Dirt device, by using back-blowing and the frame mode of impulse compensation device, improves the efficiency of dust collection of sack cleaner, and can have
Effect improves the problem of " paste bag ", and the rotary type back-blowing sack cleaner simple structure, replacing part is convenient, can guarantee that flue gas
Dedusting is persistently carried out.
The technical solution used in the present invention is as follows：
The rotary type back-blowing sack cleaner of the present invention, including cleaner unit body and dedusting mechanism；The cleaner unit body
Inside it is provided with dedusting mechanism；The cleaner unit body is sequentially provided with from top to bottom top cover, upper shell, lower house and ash bucket；On described
Housing is provided with air vent, and ash bucket is provided with air inlet；The ash bucket is also connected with rapping apparatus；Also include inverse blowing device；
The inverse blowing device is connected with blast pipe and discharge pipe, and it is internal that inverse blowing device stretches into cleaner unit sheet by discharge pipe；It is described
Inverse blowing device is connected with dedusting mechanism.
Due to adopting said structure, inverse blowing device and dedusting mechanism interconnection function, effectively flue gas shunting is processed, dropped
The pressure that low dedusting is processed fume centralized, decentralized processing load；Flue dust by inverse blowing device from top to bottom, dedusting it is same
When also by wind-force effect by the dust gathered on dedusting mechanism, with the wind band delivers to ash bucket, when reducing the work of the big device that shakes
Effect, reduces energy consumption, its simple structure, and efficiency of dust collection is high, it is ensured that the sustainability of fume treatment is carried out.
The rotary type back-blowing sack cleaner of the present invention, the dedusting mechanism includes some dedusting supports and dedusting
Bag；The two ends of the dedusting support are connected respectively by bearing with upper supporting plate and lower carrier plate；The lower end of the dedusting support connects
It is connected to rotating driving device；The upper supporting plate and lower carrier plate are set in parallel in cleaner unit sheet in vivo, on upper supporting plate and lower carrier plate
It is provided with through hole or reticulated cell；The dedusting support is arranged with dust settling pocket.
Due to adopting said structure, dedusting support that the turn of certain speed in the presence of rotating driving device, can be carried out,
The place to dust of dust settling pocket can be improve to a certain extent by the dust hanging fascia gathered on dust settling pocket fiber to ash bucket lower section
Reason efficiency, and during the turn of dedusting support, can effectively increase the flowing of dust settling pocket interior air-flow so that the temperature of air-flow and
Humidity is reduced, and can effectively improve the phenomenon that " paste bag " is caused because of flue dust condensation, extends the service life of dust settling pocket, is reduced
Use cost, while reducing the frequency for changing dust settling pocket, has saved labour cost.
The rotary type back-blowing sack cleaner of the present invention, the discharge pipe extends upper supporting plate top, and total with air-out
Pipe connects；The blast pipe is connected at air inlet by defecator；The discharge pipe is connected with blast pipe by back blowing machine
Connect.
Further, one end of the dust settling pocket is connected on air intake house steward by bridge piece, and the dust settling pocket other end leads to
Cross pendant weight body to be placed on lower carrier plate.
Due to adopting said structure, processed flue gas is branched to enter in some dust settling pockets by blowing machine by air-out house steward
Row is processed, dedusting bag filtration flue gas ash removal, substantially increases the dedusting effect of the rotary type back-blowing sack cleaner of the present invention
Rate.
The rotary type back-blowing sack cleaner of the present invention, is also associated with blast compensation dress on the cleaner unit body
Put；The blast compensation device includes pulse valve, injection tube and air bag；Pulse valve is connected with injection pipeline, and injection pipeline is stretched into
Cleaner unit sheet is internal；The pulse valve is connected with air bag, and pulse valve is by being electrically connected to controller；The injection pipeline and arteries and veins
The junction for rushing valve sets wind pressure sensor, and wind pressure sensor is connected to controller.
Due to adopting said structure, can effectively divide maintenance one efficient dedusting ambient pressure by blast compensation device,
Dust removing effects are improved, is processed by exterior airbag and inside smoke and is balanced Action of Wind pressure, pulse valve cycle operation so that whole
Individual dust pelletizing system voltage stabilizing dedusting, not only effectively reduces loss of each mechanism of dedusting under long term, moreover it is possible to ensure
The dedusting of whole device is carried out in order, greatly reduces maintenance and the probability keeped in repair.
The rotary type back-blowing sack cleaner of the present invention, the injection pipeline is also connected by isocon with dust settling pocket
Connect；The isocon is connected by bridge piece with dust settling pocket.
Due to adopting said structure, blast compensation device directly can carry out by the air-out house steward shunting being connected with dust settling pocket
Control, with nearest control point preferable pressure control effect is reached, and can effectively lower loss, realizes quick control Accommodation, is protected
Card dedusting speed.
The rotary type back-blowing sack cleaner of the present invention, the controller is also electric with temperature sensor and attemperating unit
Property connection；The temperature sensor is arranged on dedusting support, in dust settling pocket.
Due to adopting said structure, when too high into the intrinsic processed flue gas of cleaner unit, attemperating unit can be passed through
Control reduces the dedusting temperature inside dust settling pocket, dust removing effects is not only is it beneficial to, while the dedusting material of dust settling pocket can also be protected
Matter is not damaged because of high temperature action, extends the service life of dust settling pocket.
The rotary type back-blowing sack cleaner of the present invention, the top cover is provided with inspection socket and changes bag mouth；Under described
Housing is provided with inspection door and door to access；The ash bucket lower section is also associated with ash discharge valve；The cleaner unit body integral erection
On pedestal.
Due to adopting said structure, whole dust catcher device install convenient, and the work feelings of cleaner unit can easily be observed
Condition, overhauls and easy to maintenance, practical.
The control system of the rotary type back-blowing sack cleaner of the present invention, the control process of the control system is：
Wind pressure sensor detects wind pressure value, and when wind pressure value exceedes or during less than default wind pressure value, controller control impulse valve is opened
Conjunction degree, by air bag effect adjustment wind pressure value；When temperature sensor detects temperature value in dust settling pocket, and pass information to
Controller, controller is compared the temperature value for detecting and preset temperature value, when temperature is higher than preset temperature value, control
Device will start attemperating unit, reduce flue gas intake air temperature, it is to avoid damage dust settling pocket.
The default wind pressure value of the controller is 0.1-0.2MPa；The preset temperature value of the controller is 80 °C.
Due to using above-mentioned control system, leading in the rotary type back-blowing sack cleaner dust removal process of the present invention
Under crossing the collective effect of each control unit of controller and information gathering part, the good dedusting environment of cleaner unit is maintained, improved
Efficiency of dust collection, it is ensured that dedusting it is real-time controllable, ensure that plate invent cleaner unit dedusting order while, reduce people
The input of power work.
In sum, as a result of above-mentioned technical proposal, the invention has the beneficial effects as follows：
1st, rotary type back-blowing sack cleaner of the invention, smart structural design, exploitativeness is strong, is adapted to popularization and application；
2nd, by back-blowing and the collective effect of blast compensation device, the efficiency of dust collection of cleaner unit, cleaner unit can effectively be improved
Realize good dust removing effects；
3rd, by dedusting support can rotary structure design, with reference to the effect of control system, can effectively improve conventional bag
Cleaner unit occur " paste bag " phenomenon '
4th, rotary type back-blowing sack cleaner of the invention, can effectively improve the durability of each mechanism of cleaner unit,
Extend its service life, reduce the use cost and human cost caused because of frequent more exchange device.
Description of the drawings
Fig. 1 is the schematic diagram of the rotary type back-blowing sack cleaner of the present invention；
Fig. 2 is the internal structure simplified schematic diagram of the rotary type back-blowing sack cleaner of the present invention；
Labelling in figure：1- cleaner unit bodies, 2- upper shells, 3- lower houses, 31- inspection doors, 32- door to access, 4- top covers, 41- sees
Cha Kou, 42- change bag mouth, 5- ash buckets, 6- ash discharge valves, 7- air inlets, 8- air vents, 9- dedusting mechanisms, 91- dedusting supports, 92-
Dust settling pocket, 93- upper supporting plates, 94- lower carrier plates, 95- bearings, 10- back blowing machines, 11- discharge pipes, 12- blast pipes, 13- air-out is total
Pipe, 14- bridge pieces, 15- isocons, 16- pulse valves, 17- injection pipelines, 18- air bags, 19- controllers, 20- pedestals, 21-
Dust.
Specific embodiment
With reference to embodiment, the present invention is described in detail.
In order that the purpose of invention, technical scheme and advantage become more apparent, with reference to embodiments, the present invention is entered
Row is further described.It should be appreciated that specific embodiment described herein is not used to limit only to explain the present invention
The fixed present invention.
Embodiment 1
As shown in figure 1, a kind of rotary type back-blowing sack cleaner, including cleaner unit body 1 and dedusting mechanism 9；It is described to remove
Dedusting mechanism 9 is provided with dirt device body 1；The cleaner unit body 1 is sequentially provided with from top to bottom top cover 4, upper shell 2, lower house 3
With ash bucket 5；Top cover 4 is provided with inspection socket and changes bag mouth；The lower house 3 is provided with inspection door and door to access；Under the ash bucket 5
Side is also associated with ash discharge valve 6；The integral erection of cleaner unit body 1 is on pedestal 20；Upper shell 2 is provided with air vent 8, ash
Bucket 5 is provided with air inlet 7；The ash bucket 5 is also connected with rapping apparatus, it is characterised in that：Also include inverse blowing device；It is described anti-
Blowing device is connected with blast pipe 12 and discharge pipe 11, and inverse blowing device is stretched in cleaner unit body 1 by discharge pipe 11；It is described
Inverse blowing device is connected with dedusting mechanism 9.
As shown in Fig. 2 dedusting mechanism 9 includes some dedusting supports 91 and dust settling pocket 92；The two ends of the dedusting support 91
It is connected with upper supporting plate 93 and lower carrier plate 94 respectively by bearing 95；The lower end of the dedusting support 91 is respectively connected with rotation driving dress
Put；The upper supporting plate 93 and lower carrier plate 94 are set in parallel in cleaner unit body 1, are equipped with upper supporting plate 93 and lower carrier plate 94 logical
Hole or reticulated cell；The dedusting support 91 is arranged with dust settling pocket 92.Discharge pipe 11 extends the top of upper supporting plate 93, and and air-out
House steward 13 connects；The blast pipe 12 is connected at air inlet 7 by defecator；The discharge pipe 11 passes through with blast pipe 12
Back blowing machine 10 connects.One end of the dust settling pocket 92 is connected on air intake house steward by bridge piece 14, and dust settling pocket 92 is another
End is placed on lower carrier plate 94 by falling weight body.
A blast compensation device is also associated with the cleaner unit body 1 of the rotary type back-blowing sack cleaner；It is described
Blast compensation device includes pulse valve 16, injection tube and air bag 18；Pulse valve 16 is connected with injection pipeline 17, and injection pipeline 17 is stretched
Enter in cleaner unit body 1；The pulse valve 16 is connected with air bag 18, and pulse valve 16 is by being electrically connected to controller 19；It is described
Injection pipeline 17 sets wind pressure sensor with the junction of pulse valve 16, and wind pressure sensor is connected to controller 19.Injection pipeline 17
Also it is connected with dust settling pocket 92 by isocon 15；The isocon 15 is connected by bridge piece 14 with dust settling pocket 92.Controller
19 are also electrically connected with temperature sensor and attemperating unit；The temperature sensor is arranged on dedusting support 91, positioned at dedusting
In bag 92.
Based on the control system of the rotary type back-blowing sack cleaner, the control process of the control system is：
Wind pressure sensor detects wind pressure value, when wind pressure value exceedes or during less than default wind pressure value, controller control impulse valve
Folding degree, by air bag effect adjustment wind pressure value；When temperature sensor detects temperature value in dust settling pocket, and information is passed
Controller is passed, controller is compared the temperature value for detecting and preset temperature value, when temperature is higher than preset temperature value,
Controller will start attemperating unit, reduce flue gas intake air temperature, it is to avoid damage dust settling pocket；The default wind pressure value of controller is 0.1-
0.2MPa；The preset temperature value of the controller is 80 °C.
Presently preferred embodiments of the present invention is the foregoing is only, not to limit the present invention, all essences in the present invention
Any modification, equivalent and improvement made within god and principle etc., should be included within the scope of the present invention.
Claims (10)
1. a kind of rotary type back-blowing sack cleaner, including cleaner unit body（1）And dedusting mechanism（9）；The cleaner unit
Body（1）Inside it is provided with dedusting mechanism（9）；The cleaner unit body（1）Top cover is sequentially provided with from top to bottom（4）, upper shell（2）、
Lower house（3）And ash bucket（5）；The upper shell（2）It is provided with air vent（8）, ash bucket（5）It is provided with air inlet（7）；The ash
Bucket（5）Also it is connected with rapping apparatus, it is characterised in that：Also include inverse blowing device；The inverse blowing device is connected with blast pipe
（12）And discharge pipe（11）, inverse blowing device is by discharge pipe（11）Stretch into cleaner unit body（1）It is interior；The inverse blowing device with
Dedusting mechanism（9）Connection.
2. rotary type back-blowing sack cleaner according to claim 1, it is characterised in that：The dedusting mechanism（9）
Including some dedusting supports（91）And dust settling pocket（92）；The dedusting support（91）Two ends pass through bearing（95）Respectively with upper
Plate（93）And lower carrier plate（94）Connection；The dedusting support（91）Lower end be respectively connected with rotating driving device；The upper supporting plate
（93）And lower carrier plate（94）It is set in parallel in cleaner unit body（1）It is interior, upper supporting plate（93）And lower carrier plate（94）On be equipped with through hole
Or reticulated cell；The dedusting support（91）It is arranged with dust settling pocket（92）.
3. rotary type back-blowing sack cleaner according to claim 2, it is characterised in that：The discharge pipe（11）Stretch
To upper supporting plate（93）Top, and with air-out house steward（13）Connection；The blast pipe（12）Air inlet is connected to by defecator
（7）Place；The discharge pipe（11）With blast pipe（12）By back blowing machine（10）Connection.
4. rotary type back-blowing sack cleaner according to claim 3, it is characterised in that：The dust settling pocket（92）'s
One end passes through bridge piece（14）It is connected on air intake house steward, dust settling pocket（92）The other end is placed on lower carrier plate by pendant weight body
（94）On.
5. rotary type back-blowing sack cleaner according to claim 4, it is characterised in that：The cleaner unit body
（1）On be also associated with a blast compensation device；The blast compensation device includes pulse valve（16）, injection tube and air bag（18）；
Pulse valve（16）With injection pipeline（17）Connection, is blown pipeline（17）Stretch into cleaner unit body（1）It is interior；The pulse valve（16）With
Air bag（18）Connection, pulse valve（16）By being electrically connected to controller（19）；The injection pipeline（17）With pulse valve（16）
Junction set wind pressure sensor, wind pressure sensor is connected to controller（19）.
6. rotary type back-blowing sack cleaner according to claim 5, it is characterised in that：The injection pipeline（17）
Also pass through isocon（15）With dust settling pocket（92）Connection；The isocon（15）By bridge piece（14）With dust settling pocket（92）Even
Connect.
7. the rotary type back-blowing sack cleaner according to claim 5 or 6, it is characterised in that：The controller
（19）Also it is electrically connected with temperature sensor and attemperating unit；The temperature sensor is arranged on dedusting support（91）On, it is located at
Dust settling pocket（92）It is interior.
8. the rotary type back-blowing sack cleaner one of according to claim 1-6, it is characterised in that：The top cover
（4）It is provided with inspection socket and changes bag mouth；The lower house（3）It is provided with inspection door and door to access；The ash bucket（5）Lower section also connects
It is connected to ash discharge valve（6）；The cleaner unit body（1）Integral erection is in pedestal（20）On.
9. the control system of rotary type back-blowing sack cleaner according to claim 7, it is characterised in that the control
The control process of system processed is：Wind pressure sensor detects wind pressure value, when wind pressure value exceedes or during less than default wind pressure value, control
Device controls the folding degree of impulse valve, by air bag effect adjustment wind pressure value；When temperature sensor detects dust settling pocket interior temperature
Angle value, and controller is passed information to, controller is compared the temperature value for detecting and preset temperature value, when temperature height
When preset temperature value, controller will start attemperating unit, reduce flue gas intake air temperature, it is to avoid damage dust settling pocket.
10. the control system of rotary type back-blowing sack cleaner according to claim 9, it is characterised in that：It is described
The default wind pressure value of controller is 0.1-0.2MPa；The preset temperature value of the controller is 80 °C.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611120398.8A CN106621600A (en) | 2016-12-08 | 2016-12-08 | Rotary type blowback bag dust collector |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611120398.8A CN106621600A (en) | 2016-12-08 | 2016-12-08 | Rotary type blowback bag dust collector |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106621600A true CN106621600A (en) | 2017-05-10 |
Family
ID=58820009
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201611120398.8A Pending CN106621600A (en) | 2016-12-08 | 2016-12-08 | Rotary type blowback bag dust collector |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106621600A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115414736A (en) * | 2022-10-31 | 2022-12-02 | 徐州玉科工程机械有限公司 | Pulse dust collector is used in pitch stirring production |
| CN116313916A (en) * | 2023-03-28 | 2023-06-23 | 扬州和铵半导体有限公司 | Semiconductor component packaging equipment |
| CN116588695A (en) * | 2023-04-04 | 2023-08-15 | 湖北潜江江汉环保有限公司 | Circulating fluidization negative pressure dilute phase dust pneumatic ash conveying and discharging system |
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| CN2576316Y (en) * | 2002-10-28 | 2003-10-01 | 上海化工研究院 | Novel bag-type composite duster |
| CN201287012Y (en) * | 2008-10-24 | 2009-08-12 | 余建军 | Pulse bag type dust collector |
| CN201959668U (en) * | 2011-01-27 | 2011-09-07 | 泊头市科盛环保设备有限公司 | Rotating back-flushing flat-bag dust collector |
| WO2015032246A1 (en) * | 2013-09-09 | 2015-03-12 | 佛山市人居环保工程有限公司 | Continuous sorting dust remover with accumulation shelf layer having controllable thickness, and operation method therefor |
| CN104474807A (en) * | 2015-01-06 | 2015-04-01 | 广西南宁华国环境科技有限公司 | Filtering bag dust collector |
| CN204601856U (en) * | 2015-02-04 | 2015-09-02 | 林松彬 | A kind of Environmental-protecting dust-removing device |
| CN205391997U (en) * | 2016-02-23 | 2016-07-27 | 四川皇元集团有限公司 | Pulse dust removal device based on carry out accurate control to inside dust removal state |
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2016
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2576316Y (en) * | 2002-10-28 | 2003-10-01 | 上海化工研究院 | Novel bag-type composite duster |
| CN201287012Y (en) * | 2008-10-24 | 2009-08-12 | 余建军 | Pulse bag type dust collector |
| CN201959668U (en) * | 2011-01-27 | 2011-09-07 | 泊头市科盛环保设备有限公司 | Rotating back-flushing flat-bag dust collector |
| WO2015032246A1 (en) * | 2013-09-09 | 2015-03-12 | 佛山市人居环保工程有限公司 | Continuous sorting dust remover with accumulation shelf layer having controllable thickness, and operation method therefor |
| CN104474807A (en) * | 2015-01-06 | 2015-04-01 | 广西南宁华国环境科技有限公司 | Filtering bag dust collector |
| CN204601856U (en) * | 2015-02-04 | 2015-09-02 | 林松彬 | A kind of Environmental-protecting dust-removing device |
| CN205391997U (en) * | 2016-02-23 | 2016-07-27 | 四川皇元集团有限公司 | Pulse dust removal device based on carry out accurate control to inside dust removal state |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115414736A (en) * | 2022-10-31 | 2022-12-02 | 徐州玉科工程机械有限公司 | Pulse dust collector is used in pitch stirring production |
| CN116313916A (en) * | 2023-03-28 | 2023-06-23 | 扬州和铵半导体有限公司 | Semiconductor component packaging equipment |
| CN116313916B (en) * | 2023-03-28 | 2023-10-31 | 扬州和铵半导体有限公司 | Semiconductor component packaging equipment |
| CN116588695A (en) * | 2023-04-04 | 2023-08-15 | 湖北潜江江汉环保有限公司 | Circulating fluidization negative pressure dilute phase dust pneumatic ash conveying and discharging system |
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Application publication date: 20170510 |