CN107875788A - A kind of sack cleaner - Google Patents
A kind of sack cleaner Download PDFInfo
- Publication number
- CN107875788A CN107875788A CN201711274489.1A CN201711274489A CN107875788A CN 107875788 A CN107875788 A CN 107875788A CN 201711274489 A CN201711274489 A CN 201711274489A CN 107875788 A CN107875788 A CN 107875788A
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- Prior art keywords
- bag
- fixed plate
- electric
- dust
- type dust
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Classifications
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- 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
-
- 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
- B01D46/42—Auxiliary equipment or operation thereof
- B01D46/48—Removing dust other than cleaning filters, e.g. by using collecting trays
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/34—Constructional details or accessories or operation thereof
- B03C3/74—Cleaning the electrodes
- B03C3/76—Cleaning the electrodes by using a mechanical vibrator, e.g. rapping gear ; by using impact
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/34—Constructional details or accessories or operation thereof
- B03C3/74—Cleaning the electrodes
- B03C3/80—Cleaning the electrodes by gas or solid particle blasting
-
- 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
- B01D2258/0283—Flue gases
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
A kind of sack cleaner,Including mainframe,Demarcation strip,Water dedusting cooling system,Apply electric dust collector,Bag-type dust removal system,Flue gas heat-exchange unit and condenser system,The water dedusting cooling system,Apply electric dust collector,Bag-type dust removal system,Flue gas heat-exchange unit and condenser system are prolonged flue gas direction of advance and are successively set in mainframe,The demarcation strip is eight,Eight demarcation strips are successively set in mainframe,Mainframe is divided into water dirt pocket by eight demarcation strips,First exhaust gases passes,Apply electric precipitation room,Second exhaust gases passes,Bag-type dust room,3rd exhaust gases passes,Regenerator volume,4th exhaust gases passes and condensation chamber,Water dedusting cooling system is arranged in water dirt pocket,Apply electric dust collector and be arranged on and apply in electric precipitation room,Bag-type dust removal system is arranged in bag-type dust room,Flue gas heat-exchange unit is arranged in regenerator volume,Condenser system is arranged in condensation chamber.
Description
Technical field
The present invention relates to dry type dust filtration device, more particularly to a kind of sack cleaner.
Background technology
Sack cleaner is dry type dust filtration device, for fume treatment caused by all kinds of boilers of processing, incinerator burning
Capital equipment.Suitable for trapping tiny, dry, non-fiber dust.Filter bag using weaving filter cloth or nonwoven felt into,
Dusty gas is filtered using the filtration of fabric, after dusty gas enters sack cleaner, particle is big, ratio
Great dust, because the effect of gravity settles down, fall into ash bucket, the gas containing relatively fine dust when passing through filtrate,
Dust is purified gas by detention.Sack cleaner general structure is upper box body, middle part casing, lower part box (ash
Bucket), soot cleaning system and ash exhauster etc..With the extension of sack cleaner usage time, the thickness of dust layer is gradual on cloth bag
Thickening, dedusting resistance gradually increases, and bathroom needs to carry out deashing to deduster.Soot cleaning system plays to the performance of sack cleaner
Conclusive effect.Therefore, soot cleaning system is to discriminate between one of characteristic of sack cleaner, and During Operation of Bag Dust Filter is important
A ring.
And all non-high-temperature gas of flue gas caused by the burning of all kinds of boilers, incinerator, in order to prevent high-temperature gas to cloth
Bag cause damage so as to reduce service life the occurrence of, it is necessary to be carried out before flue gas is by cloth bag to flue gas at cooling
Reason.
Meanwhile the efficiency of dust collection of simple sack cleaner is not high, it is necessary to improve the efficiency of dust collection of sack cleaner.
The content of the invention
It is an object of the invention to provide a kind of manhole fastening bolt component simple in construction, easy for installation, not easy to be lost.
In order to solve the above technical problems, the present invention provides a kind of sack cleaner, including mainframe, demarcation strip, water dedusting
Cooling system, electric dust collector, bag-type dust removal system, flue gas heat-exchange unit and condenser system are applied, the water dedusting cooling system, applied
Electric dust collector, bag-type dust removal system, flue gas heat-exchange unit and condenser system are prolonged flue gas direction of advance and are successively set in mainframe,
The demarcation strip is eight, and eight demarcation strips are successively set in mainframe, and mainframe is divided into water dedusting by eight demarcation strips
Room, the first exhaust gases passes, apply electric precipitation room, the second exhaust gases passes, bag-type dust room, the 3rd exhaust gases passes, regenerator volume, the 4th
Exhaust gases passes and condensation chamber, water dedusting cooling system are arranged in water dirt pocket, are applied electric dust collector and are arranged on and apply electric precipitation room
Interior, bag-type dust removal system is arranged in bag-type dust room, and flue gas heat-exchange unit is arranged in regenerator volume, and condenser system is arranged on cold
Solidifying interior, the electric dust collector of applying include the first fixed plate, the first blowing device, electric rotating machine, electric cleaner and rubber bar,
First fixed plate, which is arranged on, to be applied in electric precipitation room, and the first fixed plate is provided with several first through hole, the first blowing device
It is arranged on the first fixed plate upper surface, the injection mouth of the first blowing device is corresponding with first through hole, and electric rotating machine is arranged on
On first fixed plate bottom surface, electric cleaner is arranged on electric rotating machine, electric cleaner can under the drive of electric rotating machine
Apply in electric precipitation room and rotate, the rubber bar is several, and straggly be arranged on of several rubber bars is applied in electric precipitation chamber interior walls, rubber
The length of glue stick is slightly larger than electric cleaner and applies the beeline between electric precipitation chamber interior walls, and rubber bar top can be with electric precipitation
Device is in contact.
In order to improve the dust-removal cloth-bag life-span and be easy to deashing, the bag-type dust removal system includes the second fixed plate, the second spray
Blowing apparatus, motor, rotating device, connecting plate and dust-removal cloth-bag, second fixed plate are arranged in bag-type dust room, the
Two fixed plates adapt to chamber in bag-type dust room, and bag-type dust room is separated into waste gas chamber and net air cavity, waste gas by the second fixed plate
Chamber is arranged on below the second fixed plate, and net air cavity is arranged on above the second fixed plate, and the second blowing device is arranged on the second fixation
On plate, rotating device is arranged on the second fixed plate lower surface, is provided with gas channel in rotating device, the second fixed plate is provided with
Second through hole, the injection mouth of the second blowing device are connected with the second through hole, and the second through hole is connected with gas channel, driving electricity
Machine is arranged in the second fixed plate, and motor is arranged in the second fixed plate, and motor is connected with rotating device, rotation
Device can be rotated by motor, and the connecting plate is set on the spinning device, and connecting plate adapts to cloth bag and removed
Chamber in dirt room, connecting plate periphery are provided with bristle, and bag-type dust chamber interior walls are provided with a circle expansion slot, and bristle is arranged on expansion slot
Interior, dust-removal cloth-bag is several, and several dust-removal cloth-bags are arranged on connecting plate, and connecting plate is provided with several third through-holes,
Several third through-holes correspond with several dust-removal cloth-bags.
In order to improve water dedusting cooling efficiency, in addition to total air inlet and oblique deflector, total air inlet is taper, always
Air inlet is arranged on mainframe, and total air inlet is connected with water dirt pocket, and oblique deflector is several, several oblique deflectors
It is uniformly arranged in total air inlet, inlet channel is formed between adjacent oblique deflector.
Preferably, the rubber bar is soft, wear-resistant rubber bar.
For the ease of collection ash, in addition to water dedusting ash bucket, the water dedusting ash bucket is arranged on below water dirt pocket.
For the ease of collection ash, the electric precipitation ash bucket, which is arranged on, to be applied below electric precipitation room.
For the ease of collection ash, in addition to bag-type dust ash bucket, the bag-type dust ash bucket is arranged on below bag-type dust room.
Beneficial effects of the present invention are:The sack cleaner, simple in construction, attended operation is convenient, handles the scope of air quantity
Extensively, small only 1min numbers cubic metre, the big tens thousand of cubic meters of reachable 1min, for the flue gas ash removal of industrial furnace, air is reduced
The discharge of pollutant, efficiency of dust collection is high, and typically more than 99%, exit gas dust content is within tens of mg/m3, to sub-micro
The thin dirt in grain of rice footpath has higher classification efficiency, insensitive to the characteristic of dust, is not influenceed by dust and resistance, steel,
During nonferrous metallurgy, building materials, the furnace flue gas of chemical industry purify, the various complex environments and unfavorable factor that run into, all by one by one
Overcome, the application field of the sack cleaner constantly expands;The sack cleaner uses several oblique deflectors by total air inlet
Be separated into several inlet channels, flue gas enters from total air inlet, successively by several inlet channels enter water dirt pocket with
Whole water dedusting cooling system fully contacts, and improves contact area, improves water dedusting cooling efficiency, flue gas is entered comprehensively
Water-filling dedusting cools;The motor and rotating device set up, can be while dust-removal cloth-bag carries out dedusting, motor band
Dynamic rotating device rotation, rotating device drive connecting plate rotation, and connecting plate drives dust-removal cloth-bag rotation thereon, so as to change in real time
Become the position of several dust-removal cloth-bags so that dust-removal cloth-bag fully can be in contact with flue gas, prevent because smoke distribution is uneven and
Cause the excess load running of the dust-removal cloth-bag that has and the occurrence of substantially untapped some dust-removal cloth-bags, so as to add
The service life of dust-removal cloth-bag, lower the deashing frequency of dust-removal cloth-bag, strengthen operating efficiency;Second fixed plate, connecting plate and brush
The setting of hair, can avoid exhaust gas leakage to net air cavity, so as to ensure that flue gas with the barrier of double shield waste gas chamber and net air cavity
Degree of purification and efficiency;Being equipped with for electric rotating machine and rubber bar, can be the dust for being not easy to be blowed on electric cleaner
Shaken off, ensure that electric cleaner deashing is fairly perfect, extend the service life of electric cleaner.
Brief description of the drawings
Accompanying drawing 1 is the structural representation of the sack cleaner of the present invention;
Label declaration:1- mainframes;2- demarcation strips;3- water dedusting cooling systems;4- applies electric dust collector;401- first is solid
Fixed board;4011- first through hole;The blowing devices of 402- first;403- electric rotating machines;404- electric cleaners;405- rubber bars;5- cloth
Bag dust pelletizing system;The fixed plates of 501- second;The through holes of 5011- second;The blowing devices of 502- second;503- motors;504- revolves
Rotary device;5041- gas channels;505- connecting plates;5051- bristles;5052- third through-holes;506- dust-removal cloth-bags;6- flue gases change
Hot device;7- condenser systems;8- water dirt pockets;The exhaust gases passes of 9- first;10- applies electric precipitation room;The exhaust gases passes of 11- second;12- cloth
Bag dirt pocket;1201- waste gas chambers;The net air cavitys of 1202-;1203- expansion slot;The exhaust gases passes of 13- the 3rd;14- regenerator volume;15-
4th exhaust gases passes;16- condensation chambers;The total air inlets of 17-;The oblique deflectors of 18-;1801- inlet channels;19- water dedusting ash buckets;
20- electric precipitation ash buckets;21- bag-type dust ash buckets;
Embodiment
To describe the technology contents of the present invention, construction feature, the objects and the effects in detail, below in conjunction with embodiment
And accompanying drawing is coordinated to be explained in detail.
Referring to the drawings 1, the present invention provides a kind of sack cleaner, including mainframe 1, demarcation strip 2, water dedusting cooling system
3rd, electric dust collector 4, bag-type dust removal system 5, flue gas heat-exchange unit 6 and condenser system 7 are applied, the water dedusting cooling system 3, applies electricity
Dust arrester 4, bag-type dust removal system 5, flue gas heat-exchange unit 6 and condenser system 7 prolong flue gas direction of advance and are successively set on mainframe 1
Interior, the demarcation strip 2 is eight, and eight demarcation strips 2 are successively set in mainframe 1, and mainframe 1 is split by eight demarcation strips 2
Into water dirt pocket 8, the first exhaust gases passes 9, apply electric precipitation room 10, the second exhaust gases passes 11, bag-type dust room 12, the 3rd flue gas lead to
Road 13, regenerator volume 14, the 4th exhaust gases passes 15 and condensation chamber 16, water dedusting cooling system 3 are arranged in water dirt pocket 8, applied
Electric dust collector 4, which is arranged on, to be applied in electric precipitation room 10, and bag-type dust removal system 5 is arranged in bag-type dust room 12, flue gas heat-exchange unit 6
It is arranged in regenerator volume 14, condenser system 7 is arranged in condensation chamber 16, and the electric dust collector 4 of applying includes the first fixed plate
401st, the first blowing device 402, electric rotating machine 403, electric cleaner 404 and rubber slab 405, first fixed plate 401 are set
Applying in electric precipitation room 10, the first fixed plate 401 is provided with several first through hole 4011, and the first blowing device 402 is arranged on
On the upper surface of first fixed plate 401, the injection mouth of the first blowing device 402 is corresponding with first through hole 4011, electric rotating machine 403
It is arranged on the bottom surface of the first fixed plate 401, electric cleaner 404 is arranged on electric rotating machine 403, and electric cleaner 404 can be
Rotation in electric precipitation room 10 is being applied under the drive of electric rotating machine 403, the rubber slab 405 is several, several rubber slabs 405
Straggly be arranged on is applied on the inwall of electric precipitation room 10, and the length of rubber slab 405 slightly larger than electric cleaner 404 and is applied in electric precipitation room 10
Beeline between wall, the top of rubber slab 405 can be in contact with electric cleaner 404.
In the present embodiment, the bag-type dust removal system 5 includes the second fixed plate 501, the second blowing device 502, driving electricity
Machine 503, rotating device 504, connecting plate 505 and dust-removal cloth-bag 506, second fixed plate 501 are arranged on bag-type dust room 12
Interior, the second fixed plate 501 adapts to the inner chamber of bag-type dust room 12, and bag-type dust room 12 is separated into waste gas by the second fixed plate 501
Chamber 1201 and net air cavity 1202, waste gas chamber 1201 are arranged on the lower section of the second fixed plate 501, and net air cavity 1202 is arranged on the second fixation
The top of plate 501, the second blowing device 502 are arranged in the second fixed plate 501, and rotating device 504 is arranged on the second fixed plate 501
On lower surface, gas channel 5041 is provided with rotating device 504, the second fixed plate 501 is provided with the second through hole 5011, the second spray
The injection mouth of blowing apparatus 502 is connected with the second through hole 5011, and the second through hole 5011 is connected with gas channel 5041, driving electricity
Machine 503 is arranged in the second fixed plate 501, and motor 503 is arranged in the second fixed plate 501, motor 503 and rotation
Device 504 is connected, and rotating device 504 can be rotated by motor 503, and the connecting plate 505 is arranged on rotation
On rotary device 504, connecting plate 505 adapts to the inner chamber of bag-type dust room 12, and the periphery of connecting plate 505 is provided with bristle 5051, and cloth bag removes
The inwall of dirt room 12 is provided with a circle expansion slot 1203, and bristle 5051 is arranged in expansion slot 1203, and dust-removal cloth-bag 506 is some
Individual, several dust-removal cloth-bags 506 are arranged on connecting plate 505, and connecting plate 505 is provided with several third through-holes 5052, some
Individual third through-hole 5052 corresponds with several dust-removal cloth-bags 506.
The sack cleaner, in addition to total air inlet 17 and oblique deflector 18, total air inlet 17 are taper, total air inlet
Mouth 17 is arranged on mainframe 1, and total air inlet 17 is connected with water dirt pocket 8, and oblique deflector 18 is several, and several are tiltedly led
Flowing plate 18 is uniformly arranged in total air inlet 17, and inlet channel 1801 is formed between adjacent oblique deflector 18.
In the present embodiment, the rubber slab 405 is soft, wear-resistant rubber slab 405.
The sack cleaner, in addition to water dedusting ash bucket 19, the water dedusting ash bucket 19 are arranged on the lower section of water dirt pocket 8.
The sack cleaner, in addition to electric precipitation ash bucket 20, the electric precipitation ash bucket 20, which is arranged on, to be applied under electric precipitation room 10
Side.
The sack cleaner, in addition to bag-type dust ash bucket 21, the bag-type dust ash bucket 21 are arranged on bag-type dust room
12 lower sections.
The sack cleaner, when in use, flue gas enter from total air inlet 17, successively by several inlet channels 1801
Fully contacted with whole water dedusting cooling system 3 into water dirt pocket 8, improve contact area, improve water dedusting cooling effect
Rate, flue gas is set to enter water-filling dedusting cooling comprehensively;Flue gas is applied electricity by the entrance of the first exhaust gases passes 9 after water dedusting cooling and removed
Dirt room 10, electric cleaner 404 proceed by absorption dedusting, and the dust flue gas not adsorbed completely passes through the second exhaust gases passes 11
Into bag-type dust room 12;Flue gas enters behind bag-type dust room 12 after by bag-type dust, by the third through-hole of connecting plate 505
5052 gas channels 5041 entered in rotating device 504, finally enter net air cavity 1202, in dedusting via the second through hole 5011
While cloth bag 506 carries out dedusting, motor 503 drives rotating device 504 to rotate, and rotating device 504 drives connecting plate 505
Rotation, connecting plate 505 drive dust-removal cloth-bag 506 thereon to rotate, so as to change the position of several dust-removal cloth-bags 506 in real time,
Dust-removal cloth-bag 506 is fully in contact with flue gas, prevents from having caused the dust-removal cloth-bag 506 having because smoke distribution is uneven
Through excess load running the occurrence of substantially untapped some dust-removal cloth-bags 506;Flue gas removes again by dust-removal cloth-bag 506
Dirt, flue gas enter regenerator volume 14 after third dedusting by the 3rd exhaust gases passes 13, flue gas after third dedusting with
Former flue gas is exchanged heat, and reduces the temperature of former flue gas, while the flue-gas temperature after third dedusting is reached on dew point,
So as to improve the diffusance of pollutant, flue gas enters condensation chamber 16 by the 4th exhaust gases passes 15 after heat exchanger, most passed through afterwards
Sufficiently cleaned up fume emission is crossed into air;The dust accumulation on electric cleaner 404 to a certain extent after, electric cleaner
404 start ash discharge, start the first blowing device 402, and the first blowing device 402 starts blowing gas and sprayed by first through hole 4011
Blow on electric cleaner 404, dust thereon is blown off in a dedusting ash bucket, while start electric rotating machine 403, electric rotating machine
403 drive electric cleaners 404 rotate, and electric cleaner 404 is beaten in rotation process and shaken by rubber slab 405, so that will not
The dust shake being easily blowed is dropped in electric precipitation ash bucket 20, so as to ensure that the deashing of electric cleaner 404 is fairly perfect, extends electricity
The service life of deduster 404;After dust accumulation to a certain extent on dust-removal cloth-bag 506, dust-removal cloth-bag 506 starts clearly
Ash, now starts the second blowing device 502, and the second training beats device and starts the gas of injection is led to by the second through hole 5011, air-flow
Blowback is carried out to dust-removal cloth-bag 506 behind road 5041 and third through-hole 5052, the dust accumulated on cloth bag is blown off into bag-type dust
In ash bucket 21.
The sack cleaner, simple in construction, attended operation is convenient, handles that the scope of air quantity is wide, small only 1min numbers cube
Rice, the big tens thousand of cubic meters of reachable 1min, for the flue gas ash removal of industrial furnace, reduce the discharge of atmosphere pollution, dedusting effect
Rate is high, and typically more than 99%, exit gas dust content has higher within tens of mg/m3 to the thin dirt of sub-micron particle diameter
Classification efficiency, it is insensitive to the characteristic of dust, do not influenceed by dust and resistance, in steel, nonferrous metallurgy, building materials, chemical industry
In the furnace flue gas purification of industry, the various complex environments and unfavorable factor that run into, all overcome one by one, the sack cleaner
Application field constantly expands;Total air inlet 17 is separated into several air inlets by the sack cleaner using several oblique deflectors 18
Passage 1801, flue gas enter from total air inlet 17, enter water dirt pocket 8 and whole water by several inlet channels 1801 successively
Dedusting cooling system 3 fully contacts, and improves contact area, improves water dedusting cooling efficiency, flue gas is entered water-filling comprehensively
Dedusting cools;The motor 503 and rotating device 504 set up, can be while dust-removal cloth-bag 506 carries out dedusting, driving
Motor 503 drives rotating device 504 to rotate, and rotating device 504 drives connecting plate 505 to rotate, and connecting plate 505 drives removing thereon
Dirt cloth bag 506 rotates, so as to change the positions of several dust-removal cloth-bags 506 in real time so that dust-removal cloth-bag 506 can fully and cigarette
Gas phase contacts, and excess load operates and some dust-removal cloth-bags the dust-removal cloth-bag 506 for preventing from causing to have because smoke distribution is uneven
506 it is substantially untapped the occurrence of, so as to add the service life of dust-removal cloth-bag 506, lower the clear of dust-removal cloth-bag 506
Grey frequency, strengthen operating efficiency;The setting of second fixed plate 501, connecting plate 505 and bristle 5051, can be with double shield waste gas
The barrier of chamber 1201 and net air cavity 1202, exhaust gas leakage is avoided to net air cavity 1202, so as to ensure that gas cleaning degree and effect
Rate;Electric rotating machine 403 is equipped with rubber slab 405, can be that the dust for being not easy to be blowed on electric cleaner 404 is shaken
Fall, ensure that the deashing of electric cleaner 404 is fairly perfect, extend the service life of electric cleaner 404.
Embodiments of the invention are the foregoing is only, are not intended to limit the scope of the invention, it is every to utilize this hair
The equivalent structure or equivalent flow conversion that bright specification and accompanying drawing content are made, or directly or indirectly it is used in other related skills
Art field, is included within the scope of the present invention.
Claims (7)
- A kind of 1. sack cleaner, it is characterised in that including mainframe, demarcation strip, water dedusting cooling system, apply electric precipitation dress Put, bag-type dust removal system, flue gas heat-exchange unit and condenser system, the water dedusting cooling system, apply electric dust collector, bag-type dust System, flue gas heat-exchange unit and condenser system are prolonged flue gas direction of advance and are successively set in mainframe, the demarcation strip be eight, eight Individual demarcation strip is successively set in mainframe, and mainframe is divided into water dirt pocket, the first exhaust gases passes by eight demarcation strips, applies electricity Dirt pocket, the second exhaust gases passes, bag-type dust room, the 3rd exhaust gases passes, regenerator volume, the 4th exhaust gases passes and condensation chamber, water Dedusting cooling system is arranged in water dirt pocket, is applied electric dust collector and is arranged on and applies in electric precipitation room, and bag-type dust removal system is set In bag-type dust room, flue gas heat-exchange unit is arranged in regenerator volume, and condenser system is arranged in condensation chamber, described to apply electric precipitation Device includes the first fixed plate, the first blowing device, electric rotating machine, electric cleaner and rubber bar, and first fixed plate is set Applying in electric precipitation room, the first fixed plate is provided with several first through hole, and the first blowing device is arranged in the first fixed plate On surface, the injection mouth of the first blowing device is corresponding with first through hole, and electric rotating machine is arranged on the first fixed plate bottom surface, Electric cleaner is arranged on electric rotating machine, and electric cleaner can be rotated applying in electric precipitation room under the drive of electric rotating machine, institute It is several to state rubber bar, and straggly be arranged on of several rubber bars is applied in electric precipitation chamber interior walls, and the length of rubber bar is slightly larger than electricity Deduster and the beeline between electric precipitation chamber interior walls is applied, rubber bar top can be in contact with electric cleaner.
- 2. sack cleaner according to claim 1, it is characterised in that the bag-type dust removal system, which includes second, to be fixed Plate, the second blowing device, motor, rotating device, connecting plate and dust-removal cloth-bag, second fixed plate are arranged on cloth bag and removed In dirt room, the second fixed plate adapts to chamber in bag-type dust room, and bag-type dust room is separated into waste gas chamber and net by the second fixed plate Air cavity, waste gas chamber are arranged on below the second fixed plate, and net air cavity is arranged on above the second fixed plate, and the second blowing device is arranged on In second fixed plate, rotating device is arranged on the second fixed plate lower surface, and gas channel is provided with rotating device, and second fixes Plate is provided with the second through hole, and the injection mouth of the second blowing device is connected with the second through hole, and the second through hole is connected with gas channel Logical, motor is arranged in the second fixed plate, and motor is arranged in the second fixed plate, motor and rotating device phase Connection, rotating device can be rotated by motor, and the connecting plate is set on the spinning device, connecting plate adaptation In chamber in bag-type dust room, connecting plate periphery is provided with bristle, and bag-type dust chamber interior walls are provided with a circle expansion slot, and bristle is arranged on In expansion slot, dust-removal cloth-bag is several, and several dust-removal cloth-bags are arranged on connecting plate, connecting plate be provided with several the 3rd Through hole, several third through-holes correspond with several dust-removal cloth-bags.
- 3. sack cleaner according to claim 1 or 2, it is characterised in that also including total air inlet and oblique deflector, institute It is taper to state total air inlet, and total air inlet is arranged on mainframe, and total air inlet is connected with water dirt pocket, if oblique deflector is Dry, several oblique deflectors are uniformly arranged in total air inlet, and inlet channel is formed between adjacent oblique deflector.
- 4. sack cleaner according to claim 1 or 2, it is characterised in that the rubber bar is soft, wear-resistant rubber bar.
- 5. sack cleaner according to claim 1 or 2, it is characterised in that also including water dedusting ash bucket, the water dedusting Ash bucket is arranged on below water dirt pocket.
- 6. sack cleaner according to claim 1 or 2, it is characterised in that, in addition to electric precipitation ash bucket, the electricity remove Dirt ash bucket, which is arranged on, to be applied below electric precipitation room.
- 7. sack cleaner according to claim 1 or 2, it is characterised in that also including bag-type dust ash bucket, the cloth bag Dedusting ash bucket is arranged on below bag-type dust room.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201711274489.1A CN107875788A (en) | 2017-12-06 | 2017-12-06 | A kind of sack cleaner |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201711274489.1A CN107875788A (en) | 2017-12-06 | 2017-12-06 | A kind of sack cleaner |
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Publication Number | Publication Date |
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CN107875788A true CN107875788A (en) | 2018-04-06 |
Family
ID=61773120
Family Applications (1)
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CN201711274489.1A Pending CN107875788A (en) | 2017-12-06 | 2017-12-06 | A kind of sack cleaner |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111646252A (en) * | 2020-07-15 | 2020-09-11 | 北京中电国核节能环保科技股份有限公司 | High-efficiency energy-saving dust removing equipment for belt conveyor |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN204710020U (en) * | 2015-05-04 | 2015-10-21 | 中起重工(大连)有限公司 | A kind of electric-bag complex dust collector of improvement |
CN205627465U (en) * | 2016-04-15 | 2016-10-12 | 盐城永悦新材料有限公司 | Bag -type dust remover |
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2017
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CN204710020U (en) * | 2015-05-04 | 2015-10-21 | 中起重工(大连)有限公司 | A kind of electric-bag complex dust collector of improvement |
CN205627465U (en) * | 2016-04-15 | 2016-10-12 | 盐城永悦新材料有限公司 | Bag -type dust remover |
CN106310813A (en) * | 2016-10-20 | 2017-01-11 | 广西金邦泰科技有限公司 | Bag-type dust remover with high stability for chemical engineering |
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CN111646252A (en) * | 2020-07-15 | 2020-09-11 | 北京中电国核节能环保科技股份有限公司 | High-efficiency energy-saving dust removing equipment for belt conveyor |
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