CN106268136A - A kind of unit pulse bag-type dust-removing device - Google Patents
A kind of unit pulse bag-type dust-removing device Download PDFInfo
- Publication number
- CN106268136A CN106268136A CN201610769903.5A CN201610769903A CN106268136A CN 106268136 A CN106268136 A CN 106268136A CN 201610769903 A CN201610769903 A CN 201610769903A CN 106268136 A CN106268136 A CN 106268136A
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- China
- Prior art keywords
- bag
- filter
- filter bag
- removing device
- type dust
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
- B01D50/20—Combinations of devices covered by groups B01D45/00 and B01D46/00
-
- 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
- B01D46/0027—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions
- B01D46/0028—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions provided with antibacterial or antifungal means
-
- 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
- B01D46/0027—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions
- B01D46/0036—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions by adsorption or absorption
-
- 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
- B01D46/0027—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions
- B01D46/0038—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions with means for influencing the odor, e.g. deodorizing substances
-
- 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
- B01D46/42—Auxiliary equipment or operation thereof
-
- 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
- B01D46/66—Regeneration of the filtering material or filter elements inside the filter
- B01D46/70—Regeneration of the filtering material or filter elements inside the filter by acting counter-currently on the filtering surface, e.g. by flushing on the non-cake side of the filter
- B01D46/71—Regeneration of the filtering material or filter elements inside the filter by acting counter-currently on the filtering surface, e.g. by flushing on the non-cake side of the filter with pressurised gas, e.g. pulsed air
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
- B01D2253/10—Inorganic adsorbents
- B01D2253/102—Carbon
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
The invention discloses a kind of unit pulse bag-type dust-removing device, including upper box and lower box；Upper box is separated by filter with lower box；It is provided with air outlet and maintenance door on upper box, is internally provided with soot cleaning system and defecator；Being provided with air inlet on lower box, lower section is provided with ash bucket；Being provided with the gravitational precipitator being connected with air inlet in lower box, be provided with dust-exhausting port bottom gravitational precipitator, top is provided with gas outlet.The present invention arranges filter bag by horizontal tilt, on the one hand can improve the filter effect of dusty gas, is on the other hand easy to the heavy grain so that filter bag surface from the landing of filter bag surface, it is to avoid filter bag surface is sunk grain blocking；The aperture of the filter bag being layered setting from down to up is sequentially reduced, make filter bag can retain the granule of different-grain diameter, improve filter effect, after making to purify, gas meets state environmental emissioning standard, simultaneously in deashing process, the granule that upper strata filter bag blows off can enter ash bucket through lower floor's large aperture filter bag.
Description
Technical field
The present invention relates to exhaust dust device with bag field, particularly relate to a kind of unit pulse bag-type dust-removing device.
Background technology
Unit bag pulse dedusting device is a kind of purge mode using pulse jet, automatic ash removing monomer dedusting
Equipment, it has, and ash-removal effect is good, purification efficiency is high, it is big to process air quantity, life-span of the filter bag length, maintenance load are little, run safety
The advantage such as reliable, at cement, breeze, the industrial and mining establishment such as mining, metallurgy, building materials, machinery, chemical industry, grain processing are widely used.But
It is, existing unit pulsed jet cloth filter to also exist that ash-removal effect is undesirable, purification efficiency is low, so that after Jing Huaing
Gas can not reach discharging standards.
Summary of the invention
In view of this, the present invention provides a kind of unit pulsed jet cloth filter, it is possible to after dusty gas is purified, meet
State environmental emissioning standard.
The technical scheme is that and be achieved in that:
A kind of unit pulse bag-type dust-removing device, including upper box and lower box；Described upper box and described lower box by
Filter separates；
It is provided with air outlet and maintenance door on described upper box, is internally provided with soot cleaning system and defecator；Described clearly
Ash system includes air accumulator, escape pipe tank connected with described gas storage, the some pulse valves being arranged on described escape pipe, if with
The injection tube that dry described pulse valve connects, and the pulse control instrument being connected with described pulse valve signal；
The filter bag in described defecator includes bag cage and is fixed on described bag cage and matched with described bag cage type shape, institute
The quantity stating bag cage is identical with the quantity of described filter bag, is 3～6；Described bag cage is from top to bottom stratified and set on described
In casing；Each described equal horizontal tilt of bag cage is fixed in described upper box；It is layered the described filter bag of setting from down to up
Aperture is sequentially reduced；It is provided with described injection tube above each described bag cage；Described injection tube bottom is provided with some winding-ups
Mouth；
Described lower box side is provided with air inlet, and lower section is provided with ash bucket；Be provided with in described lower box with described enter
The gravitational precipitator that air port connects, is provided with dust-exhausting port bottom described gravitational precipitator, top is provided with gas outlet.
Preferably, described filter bag surface-coated has super-hydrophobic coat.
Preferably, described super-hydrophobic coat is made up of the silicon dioxide that Kaolin and silicon fluoride are modified, described Kaolin and
The mass ratio of the silicon dioxide that described silicon fluoride is modified is 92～96:3～5.
Preferably, described silicon fluoride is tridecafluoro-n-octyltriethoxysilane, trifluoromethyl trimethylsilane, 17 fluorine last of the ten Heavenly stems
One or more in ethyl triethoxy silicane alkane.
Preferably, the horizontal tilt angle of described filter bag is 10～30 °.
Preferably, described air outlet is provided with purifier, is provided with chalk dust removing plate, except antibacterial plate in described purifier
With degasification taste plate.
Preferably, described air inlet is provided with gas flow homogenization device.
Preferably, the surface of described filter is provided with activated carbon adsorption layer, and the aperture of described filter is more than all described filter bags
Aperture.
Preferably, the top surface of described upper box is umbrella parabola.
Preferably, described winding-up mouth presents the trapezoidal of short lower length, and described winding-up gonys portion is provided with porous plate.
The invention have the benefit that
A kind of unit pulse bag-type dust-removing device that the present invention provides, the setting of gravitational precipitator, it is possible to make quality big
Granule sink, thus improve the clean-up effect of dusty gas；Filter bag horizontal tilt in bag cage is arranged, and on the one hand can improve
The filter effect of dusty gas, is on the other hand easy to the heavy grain so that filter bag surface from the landing of filter bag surface, it is to avoid filter bag surface
Blocked by heavy grain；The aperture of the filter bag being layered setting from down to up is sequentially reduced so that filter bag can retain different-grain diameter
Grain, improves filter effect so that purified gas meets state environmental emissioning standard, simultaneously in deashing process, and upper metafiltration
The granule that bag blows off can enter ash bucket through lower floor's large aperture filter bag；By being provided above injection tube at bag cage so that winding-up
Winding-up mouth below pipe can directly blow off the heavy grain on filter bag surface so that the heavy grain of a part can be between bag cage and filter bag
Space falls into ash bucket, and another part enters ash bucket through lower floor's large aperture filter bag；
Accompanying drawing explanation
In order to be illustrated more clearly that the embodiment of the present invention or technical scheme of the prior art, below will be to embodiment or existing
In having technology to describe, the required accompanying drawing used is briefly described, it should be apparent that, the accompanying drawing in describing below is only this
Some embodiments of invention, for those of ordinary skill in the art, on the premise of not paying creative work, it is also possible to
Other accompanying drawing is obtained according to these accompanying drawings.
Fig. 1 is the structural representation of unit pulse bag-type dust-removing device of the present invention.
In figure:
1 upper box；2 lower boxes；3 filter bags；4 gravitational precipitators；401 dust-exhausting ports；402 gas outlets；5—
Air outlet；6 air inlets；7 air accumulators；8 escape pipes；9 pulse valves；10 pulse control instruments；11 injection tubes；12—
Winding-up mouth；13 ash buckets；14 filters.
Detailed description of the invention
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clear, complete
Describe, it is clear that described embodiment is only a part of embodiment of the present invention rather than whole embodiments wholely.Based on
Embodiment in the present invention, it is every other that those of ordinary skill in the art are obtained under not making creative work premise
Embodiment, broadly falls into the scope of protection of the invention.
As it is shown in figure 1, a kind of unit pulse bag-type dust-removing device that the present invention provides, including upper box 1 and lower box 2；
Upper box 1 and lower box 2 are separated by filter 14；It is provided with air outlet 5 and maintenance door on upper box 1, is internally provided with deashing system
System and defecator；Soot cleaning system includes air accumulator 7, the escape pipe 8 being connected with air accumulator 7, and be arranged on escape pipe 8 is some
Pulse valve 9, the injection tube 11 being connected with some pulse valves 9, and the pulse control instrument 10 being connected with pulse valve 9 signal；Filter
Device includes bag cage and the filter bag 3 being fixed in bag cage and matching with bag cage type shape, the quantity phase of the quantity of bag cage and filter bag 3
With, it is 3～6；Bag cage is from top to bottom stratified and set in upper box 1；The each bag of equal horizontal tilt of cage is fixed on upper box 1
In；The aperture of the filter bag 3 being layered setting from down to up is sequentially reduced；It is provided with injection tube 11 above each bag of cage；Injection tube
11 bottoms are provided with some winding-up mouths 12；Lower box 2 side is provided with air inlet 6, and lower section is provided with ash bucket 13；In lower box 2
Being provided with the gravitational precipitator 4 being connected with air inlet 6, be provided with dust-exhausting port 401 bottom gravitational precipitator 4, top is provided with out
QI KOU 402.
In technique scheme, filter bag 3 horizontal tilt in bag cage is arranged, and on the one hand can improve the filtration of dusty gas
On the other hand effect, is easy to the heavy grain so that filter bag 3 surface from filter bag 3 surface landing, it is to avoid filter bag 3 surface is sunk grain blocking；
The aperture of the filter bag 3 being layered setting from down to up is sequentially reduced so that filter bag 3 can retain the granule of different-grain diameter, improved
Filter effect, simultaneously in deashing process, the granule that upper strata filter bag 3 blows off can enter ash bucket 13 through lower floor's large aperture filter bag 3；
By being provided above injection tube 11 at bag cage so that the winding-up mouth 12 below injection tube 11 can directly blow off filter bag 3 surface
Heavy grain so that the heavy grain of a part falls into ash bucket 13 from the space between bag cage and filter bag 3, another part is through lower floor's large aperture filter
Bag 3 enters ash bucket 13；Enter the setting of gravitational precipitator 4, it is possible to sunk by granule big for quality, thus improve the clean of dusty gas
Change effect.
In the present embodiment, in order to improve further ash-removal effect and the service life of filter bag 3, filter bag 3 surface-coated
Super-hydrophobic coat.Wherein, on the one hand in order to reduce cost, the strongest with the bonding of filter bag 3 in order to improve super-hydrophobic coat
Degree, it is to avoid breakage to super-hydrophobic coat in compressed air deashing process, super-hydrophobic coat is by Kaolin and silicon fluoride modified
Silicon dioxide is constituted, and the mass ratio of the silicon dioxide of Kaolin and silicon fluoride modification is (92～96): (3～5), and this coating is in filter
The contact angle on bag 3 surfaces is 158.3 °, and roll angle is 3.8 °.
In the present embodiment, silicon fluoride be tridecafluoro-n-octyltriethoxysilane, trifluoromethyl trimethylsilane, 17
One or more in fluorine decyl triethoxysilane.
In the present embodiment, for the ease of clearing up the dust on filter bag 3 surface, ensure that again filter effect, filter simultaneously
The horizontal tilt angle of bag 3 is 10～30 °.
In the present embodiment, in order to remove the harmful gas in dusty gas, cross the filter 14 active charcoal of surface configuration
Adsorption layer, the aperture of filter 14 is more than the aperture of all filter bags 3.
In the present embodiment, for the ease of clearing up the dust of filter bag 3 surfaces externally and internally, ensure that the most again filtration effect
Really, the horizontal tilt angle of filter bag 3 is 10～30 °.
In the present embodiment, in order to avoid filter bag 3 is damaged, affect filter effect, in filter bag 3, be provided with broken bag detection
Instrument, is used for detecting whether filter bag 3 damaged condition occurs.
In the present embodiment, during in order to avoid outdoor placement and rainfall, upper box 1 top surface hydrops, cause filter bag 3
Soaking, affect efficiency of dust collection, the top surface of upper box 1 is umbrella parabola.
It should be noted that in order to purify air further, air outlet 5 is provided with purifier, purifier
Inside it is provided with chalk dust removing plate, except antibacterial plate and degasification taste plate.
The operation principle of a kind of unit pulse bag-type dust-removing device that the present invention provides is described in conjunction with Fig. 1:
Dusty gas is entered in gravitational precipitator 4 by air inlet 6, after settlement section bulky grain, enters the filter chamber of filter bag 3
In, and by filter bag 3, dusty gas is filtered, after filter bag 3 purifies, gas is discharged to external environment by air outlet 5, the gas of discharge
Body meets state environmental emissioning standard.Along with the increase of filtration time, the dust of gravitational precipitator 4 and filter bag 3 surface attachment is not
Disconnected increase, gravitational precipitator 4, the filter efficiency of filter bag 3 decrease, when dust arrester resistance rises to a setting value, for protecting
Card dust arrester works on, and needs to carry out deashing.Bulky grain in gravitational precipitator 4 is discharged from dust-exhausting port 401；Pulse Width Control
Instrument 10 sends instruction, makes pulse valve 9 discharge compressed air, and compressed air passes through the winding-up mouth 12 in injection tube 11 just to filter bag 3
Aperture at a high speed pour filter bag 3, while it pours filter bag 3 inside, will accumulate in the heavy grain of filter bag 3 outer surface from filter bag 3
On come off, heavy grain can through between lower floor's large aperture filter bag 3 and/or filter bag 3 and bag cage space enter ash bucket 13.
The foregoing is only presently preferred embodiments of the present invention, not in order to limit the present invention, all essences in the present invention
Within god and principle, any modification, equivalent substitution and improvement etc. made, should be included within the scope of the present invention.
Claims (10)
1. a unit pulse bag-type dust-removing device, it is characterised in that include upper box (1) and lower box (2)；Described upper box
(1) separate by filter (14) with described lower box (2)；
It is provided with air outlet (5) and maintenance door on described upper box (1), is internally provided with soot cleaning system and defecator；Described
Soot cleaning system includes air accumulator (7), the escape pipe (8) being connected with described air accumulator (7), is arranged on described escape pipe (8)
Some pulse valves (9), the injection tube (11) being connected with some described pulse valves (9), and be connected with described pulse valve (9) signal
Pulse control instrument (10)；
The filter bag (3) in described defecator includes bag cage and is fixed on described bag cage and matched with described bag cage type shape, institute
The quantity stating bag cage is identical with the quantity of described filter bag (3), is 3～6；Described bag cage is from top to bottom stratified and set on described
In upper box (1)；Each described equal horizontal tilt of bag cage is fixed in described upper box (1)；It is layered the institute of setting from down to up
The aperture stating filter bag (3) is sequentially reduced；It is provided with described injection tube (11) above each described bag cage；Described injection tube (11)
Bottom is provided with some winding-up mouths (12)；
Described lower box (2) side is provided with air inlet (6), and lower section is provided with ash bucket (13)；Described lower box is provided with in (2)
The gravitational precipitator (4) being connected with described air inlet (6), described gravitational precipitator (4) bottom is provided with dust-exhausting port (401), top
Portion is provided with gas outlet (402).
2. unit pulse bag-type dust-removing device as claimed in claim 1, it is characterised in that described filter bag (3) surface-coated has
Super-hydrophobic coat.
3. unit pulse bag-type dust-removing device as claimed in claim 2, it is characterised in that described super-hydrophobic coat is by Kaolin
The silicon dioxide modified with silicon fluoride is constituted, and the mass ratio of the silicon dioxide of described Kaolin and the modification of described silicon fluoride is (92
～96): (3～5).
4. unit pulse bag-type dust-removing device as claimed in claim 3, it is characterised in that described silicon fluoride is ten trifluoro octyl groups
One or more in triethoxysilane, trifluoromethyl trimethylsilane, 17 fluorine decyl triethoxysilanes.
5. unit pulse bag-type dust-removing device as claimed in claim 1, it is characterised in that the horizontal tilt of described filter bag (3)
Angle is 10～30 °.
6. unit pulse bag-type dust-removing device as claimed in claim 1, it is characterised in that described air outlet (5) is provided with only
Gasifying device, is provided with chalk dust removing plate, except antibacterial plate and degasification taste plate in described purifier.
7. unit pulse bag-type dust-removing device as claimed in claim 1, it is characterised in that described air inlet (6) is provided with gas
Stream homogenizer.
8. unit pulse bag-type dust-removing device as claimed in claim 1, it is characterised in that the surface of described filter (14) is provided with
Activated carbon adsorption layer, the aperture of described filter (14) is more than the aperture of all described filter bags (3).
9. unit pulse bag-type dust-removing device as claimed in claim 1, it is characterised in that the top table of described upper box (1)
Face is umbrella parabola.
10. unit pulse bag-type dust-removing device as claimed in claim 1, it is characterised in that described winding-up mouth (12) is presented short
Lower length trapezoidal, described winding-up mouth (12) bottom is provided with porous plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610769903.5A CN106268136A (en) | 2016-08-29 | 2016-08-29 | A kind of unit pulse bag-type dust-removing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610769903.5A CN106268136A (en) | 2016-08-29 | 2016-08-29 | A kind of unit pulse bag-type dust-removing device |
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| Publication Number | Publication Date |
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| CN106268136A true CN106268136A (en) | 2017-01-04 |
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ID=57675966
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610769903.5A Pending CN106268136A (en) | 2016-08-29 | 2016-08-29 | A kind of unit pulse bag-type dust-removing device |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108993037A (en) * | 2018-08-17 | 2018-12-14 | 南通艾迈特机械有限公司 | A kind of pulsed stand-alone sack cleaner |
Citations (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201108786Y (en) * | 2007-11-19 | 2008-09-03 | 北京博鹏北科科技有限公司 | Pocket type collector |
| CN101476007A (en) * | 2008-11-18 | 2009-07-08 | 无锡红旗除尘设备有限公司 | Dry dust collection method and apparatus for blast furnace gas |
| CN202202888U (en) * | 2011-08-19 | 2012-04-25 | 天津赛瑞机器设备有限公司 | Horizontal dry method filter bag dust collector for mine |
| CN102728153A (en) * | 2012-07-22 | 2012-10-17 | 解波 | Dust collection device |
| CN202538522U (en) * | 2012-03-15 | 2012-11-21 | 南昌航空大学 | Louvered bent plate gravity dust collector |
| CN102908857A (en) * | 2012-11-09 | 2013-02-06 | 昆明中铁大型养路机械集团有限公司 | Dirt collecting device integrating gravity and bag type dust collection |
| CN202762233U (en) * | 2012-12-15 | 2013-03-06 | 解波 | Dust collection device |
| CN103252152A (en) * | 2013-05-30 | 2013-08-21 | 华南理工大学 | Horizontal type electrostatic fabric filter |
| CN103305122A (en) * | 2013-07-03 | 2013-09-18 | 华北电力大学 | Montmorillonite-silicon dioxide super-hydrophobic coating and preparation method thereof |
| CN103372361A (en) * | 2013-08-09 | 2013-10-30 | 张家港市盛港绿色防火建材有限公司 | Single pulse bag type dust collector |
| KR20130125041A (en) * | 2012-05-08 | 2013-11-18 | 한국에너지기술연구원 | Bagfilter dust collector equiped with highly efficient filter-cleaning device and operation procedure of the same |
| CN103933794A (en) * | 2014-05-15 | 2014-07-23 | 海安县晋全电工器材有限公司 | High-efficiency horizontal-type dust remover |
| CN104548784A (en) * | 2014-12-04 | 2015-04-29 | 江西凯天环保科技有限公司 | Inner-filtering inner-blowing type bag type dust collector and ash removal method thereof |
| CN204428997U (en) * | 2015-01-09 | 2015-07-01 | 陈苹 | A kind of flat bag pulse bag type dust collector |
| CN205287913U (en) * | 2016-01-26 | 2016-06-08 | 浙江蓝威环保科技设备有限公司 | Horizontal distribution pulse bag dust collector |
-
2016
- 2016-08-29 CN CN201610769903.5A patent/CN106268136A/en active Pending
Patent Citations (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201108786Y (en) * | 2007-11-19 | 2008-09-03 | 北京博鹏北科科技有限公司 | Pocket type collector |
| CN101476007A (en) * | 2008-11-18 | 2009-07-08 | 无锡红旗除尘设备有限公司 | Dry dust collection method and apparatus for blast furnace gas |
| CN202202888U (en) * | 2011-08-19 | 2012-04-25 | 天津赛瑞机器设备有限公司 | Horizontal dry method filter bag dust collector for mine |
| CN202538522U (en) * | 2012-03-15 | 2012-11-21 | 南昌航空大学 | Louvered bent plate gravity dust collector |
| KR20130125041A (en) * | 2012-05-08 | 2013-11-18 | 한국에너지기술연구원 | Bagfilter dust collector equiped with highly efficient filter-cleaning device and operation procedure of the same |
| CN102728153A (en) * | 2012-07-22 | 2012-10-17 | 解波 | Dust collection device |
| CN102908857A (en) * | 2012-11-09 | 2013-02-06 | 昆明中铁大型养路机械集团有限公司 | Dirt collecting device integrating gravity and bag type dust collection |
| CN202762233U (en) * | 2012-12-15 | 2013-03-06 | 解波 | Dust collection device |
| CN103252152A (en) * | 2013-05-30 | 2013-08-21 | 华南理工大学 | Horizontal type electrostatic fabric filter |
| CN103305122A (en) * | 2013-07-03 | 2013-09-18 | 华北电力大学 | Montmorillonite-silicon dioxide super-hydrophobic coating and preparation method thereof |
| CN103372361A (en) * | 2013-08-09 | 2013-10-30 | 张家港市盛港绿色防火建材有限公司 | Single pulse bag type dust collector |
| CN103933794A (en) * | 2014-05-15 | 2014-07-23 | 海安县晋全电工器材有限公司 | High-efficiency horizontal-type dust remover |
| CN104548784A (en) * | 2014-12-04 | 2015-04-29 | 江西凯天环保科技有限公司 | Inner-filtering inner-blowing type bag type dust collector and ash removal method thereof |
| CN204428997U (en) * | 2015-01-09 | 2015-07-01 | 陈苹 | A kind of flat bag pulse bag type dust collector |
| CN205287913U (en) * | 2016-01-26 | 2016-06-08 | 浙江蓝威环保科技设备有限公司 | Horizontal distribution pulse bag dust collector |
Non-Patent Citations (3)
| Title |
|---|
| 王文才主编: "《粉尘与有害气体防止技术》", 31 August 2012, 内蒙古大学出版社 * |
| 王永忠，宋七棣编著: "《电炉炼钢除尘》", 30 September 2003, 冶金工业出版社 * |
| 郭庆中等: "氟烷基改性的二氧化硅纳米球的制备与应用研究", 《有机硅材料》 * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108993037A (en) * | 2018-08-17 | 2018-12-14 | 南通艾迈特机械有限公司 | A kind of pulsed stand-alone sack cleaner |
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