CN206566623U - A kind of sinter-plate precipitator - Google Patents
A kind of sinter-plate precipitator Download PDFInfo
- Publication number
- CN206566623U CN206566623U CN201720283637.5U CN201720283637U CN206566623U CN 206566623 U CN206566623 U CN 206566623U CN 201720283637 U CN201720283637 U CN 201720283637U CN 206566623 U CN206566623 U CN 206566623U
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- plate
- dust
- filter core
- shell
- dust remover
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Abstract
The utility model provides a kind of sinter-plate precipitator, belong to industrial dedusting equipment technical field, its structure includes shell of dust remover, sintered plate filter core, high pressure gas bag and blower fan, sintered plate filter core has the gas exchanges room of closing, sintered plate filter core surrounds dirt pocket with shell of dust remover, the outlet side of high pressure gas bag is provided with pulse valve, and the outlet side of high pressure gas bag stretches into shell of dust remover with the air intake of blower fan and connects the gas exchanges room of sintered plate filter core separately down.To improve dust removing effects, the bottom of shell of dust remover offers dust mouth, and the bottom side of shell of dust remover is disposed with into dirt pipe；Enter inside one end insertion shell of dust remover of dirt pipe and be connected with dedusting dividing plate, dedusting dividing plate is located between sintered plate filter core and dust mouth and dirt pocket is divided into the two dedusting chamber units connected up and down, final dusting, reduction cleaning or the frequency for changing sintered plate filter core are realized by dedusting dividing plate.The utility model especially handles the dust containing hot gas and moisture.
Description
Technical field
The utility model is related to industrial dedusting equipment technical field, specifically a kind of sinter-plate precipitator.
Background technology
At present, domestic air cleaning technology industry uses fiber bag precipitator or sinter-plate precipitator dedusting, cloth bag mostly
The easy bad cloth bag of formula deduster, filtering accuracy be not high, deduster volume is big.Sinter-plate precipitator has selected the wave modeling of uniqueness
Plate filter core substitution conventional cloth bag is burnt, because sintered plate filter core is rigid structure, will not be deformed, and exoskeletal abrasion, so using
Long lifespan, along with advanced treating is passed through on sintered plate surface, aperture fine uniform, with hydrophobicity, not easy-adhesion water content compared with
High dust, so sinter-plate precipitator is optimal selection when handling higher water content and fibre dust.Further, since modeling
The high-precision technique manufacture for burning plate maintains uniform micron order aperture, so ultrafine dust and high concentration powder can also be handled
Dirt, the entrance concentration of bagroom is generally less than 20 grams ms 3, and sinter-plate precipitator entrance is dense up to 500 grams ms 3.It
Two grades can be simplified gather dust and be gathered dust for one-level, not only technique is convenient, can also reduce cost energy consumption and reduce floor space and space pipe
Road.Therefore, the application of sinter-plate precipitator at present is wide.
But, it can handle that water content is higher and fibrous dust based on sinter-plate precipitator, especially in commercial Application
In, the dust containing moisture can be adsorbed largely in the outer surface of sintered plate filter core when entering sinter-plate precipitator, although high pressure gas
The gas that bag sprays can make the dust for being attached to sintered plate filter core outer surface drop, after prolonged dust removal and filtration, sintered plate
The dust removal performance of filter core can still be affected, serious to also need to frequently change or clean sintered plate filter core, directly improve
The use cost of industrial dedusting.
The content of the invention
Technical assignment of the present utility model is that there is provided a kind of sinter-plate precipitator for solution the deficiencies in the prior art.
The utility model solves the technical scheme that its technical problem used：
A kind of sinter-plate precipitator, its structure includes shell of dust remover, the sintered plate being arranged in inside shell of dust remover filter
Core, the high pressure gas bag being arranged in outside shell of dust remover and blower fan, sintered plate filter core have the gas exchanges room of closing, sintered plate
Filter core also surrounds dirt pocket between shell of dust remover, and the outlet side of high pressure gas bag is provided with pulse valve, the outlet of high pressure gas bag
End stretches into shell of dust remover with the air intake of blower fan and connects the gas exchanges room of sintered plate filter core separately down.In order to realize more
Good dust removing effects, the bottom of shell of dust remover offers dust mouth, and the bottom side of shell of dust remover is disposed with into dirt pipe；Enter
One end of dirt pipe be located at shell of dust remover on the outside of, enter dirt pipe the other end insertion shell of dust remover inside and be connected with dedusting every
Plate, dedusting dividing plate is located between sintered plate filter core and dust mouth, and dedusting dividing plate surrounds sintered plate filter core and shell of dust remover
Dirt pocket is divided into the two dedusting chamber units connected up and down, can so to enter the fraction steam and dust into dirt pipe
Dedusting baffle surface is attached to, bypasses after dedusting dividing plate and is adsorbed by sintered plate filter core into remaining steam and dust for entering dirt pipe,
Final dusting is realized by dedusting dividing plate, cleaning is reduced or changes the frequency of sintered plate filter core.
On the basis of said structure, adsorb for convenience in the dust whereabouts of sintered plate filter core outer surface, dedusting dividing plate can
To be the arcuate structure that Open Side Down, wherein one end of dedusting dividing plate is fixedly connected with dust removing tube, and the other end of dedusting dividing plate is to remote
Direction from dust removing tube extends.
On the basis of said structure, adsorb for convenience in the dust whereabouts of sintered plate filter core outer surface, dedusting dividing plate is also
Can be the v-shaped structure that Open Side Down, wherein one end of dedusting dividing plate is fixedly connected with dust removing tube, the other end of dedusting dividing plate is to remote
Direction from dust removing tube extends.
On the basis of said structure, involved sintered plate filter core includes sintered plate body, is arranged in sintered plate body top
The top plate in portion, the bottom plate for being arranged in sintered plate body bottom.Sintered plate body is integrally connected by the V-arrangement corrugated plating of two panels symmetrical structure
Composition is connect, the gas exchanges room of at least one closing, two panels V is also surrounded after the connection of two panels V-arrangement corrugated plating jointly with top plate, bottom plate
Shape corrugated plating outer surface even spread polytetrafluorethylecoatings coatings, polytetrafluorethylecoatings coatings have hydrophobicity, can be by dirt pocket
Water segregation can allow the gas of dirt pocket to enter gas exchanges room outside gas exchanges room.Top plate and bottom plate are fixed on dedusting
Device shell inner surface；Top plate embeds at least one injection tube, and the lateral cross-sectional area of injection tube is equal to or slightly less than gas exchanges room
Lateral cross-sectional area, at least one injection tube is relative one by one with least one above-mentioned gas exchanges room, and injection tube is connected downwards
Gas exchanges room, injection tube connects the outlet side of above-mentioned high pressure gas bag upwards.
On the basis of said structure, preferably the bottom of injection tube, which coordinates, inserts sintered plate body interior, and injection tube
Outer surface coordinates with the inner surface of sintered plate body contacts realization sealing, and the top of injection tube is higher by top plate, and injection tube upwards
Lateral cross section be rectangle or ellipse.
On the basis of said structure, preferably the quantity of sintered plate filter core is at least two, at least two sintered plate filter cores
It is arranged in parallel inside shell of dust remover.
Produced beneficial effect is a kind of sinter-plate precipitator of the present utility model compared with prior art：
1）The utility model is simple in construction, reasonable in design, on the architecture basics of existing sinter-plate precipitator, will enter dirt pipe
Be arranged on the sidepiece of shell of dust remover, meanwhile, enter dirt pipe stretch into shell of dust remover part connect dedusting dividing plate, pass through dedusting
Dividing plate to enter shell of dust remover dust handled for the first time, with reduce sintered plate filter core dedusting burden, dedusting dividing plate without
The steam and dust of method processing are then adsorbed in sintered plate filter core, and dust removing effects are good, and service life is long, can especially realize in dust
The separation of moisture and hot gas；
2）On the other hand, injection tube is embedded on top plate of the present utility model, and the lateral cross-sectional area of injection tube is equal to or omited
Less than the lateral cross-sectional area of gas exchanges room, to increase the contact area of gas and sintered plate filter core internal gas switch room,
During high pressure gas bag jet, drop speed of the absorption in the dust of sintered plate filter core outer surface is improved, accelerates moisture and heat in dust
The separation of gas.
Brief description of the drawings
Accompanying drawing 1 is structural representation of the present utility model；
Accompanying drawing 2 is that Fig. 1 removes the A-A after blower fan to structure for amplifying sectional view；
Accompanying drawing 3 is the structure diagram of sintered plate filter core in the utility model；
Accompanying drawing 4 is Fig. 3 structure for amplifying top view；
Accompanying drawing 5 is Fig. 3 B-B direction structure for amplifying sectional view.
Each label is represented in figure：
10th, shell of dust remover, 20, sintered plate filter core, 30, high pressure gas bag, 40, blower fan；
11st, dust mouth, 12, enter dirt pipe, 13, dedusting dividing plate, 14, dirt pocket；
21st, sintered plate body, 22, top plate, 23, injection tube, 24, bottom plate, 25, gas exchanges room；
31st, outlet side, 32, pulse valve.
Embodiment
1-5, is described in detail below to a kind of sinter-plate precipitator of the present utility model below in conjunction with the accompanying drawings.
As shown in accompanying drawing 1,2, a kind of sinter-plate precipitator of the present utility model, its structure includes shell of dust remover 10, put down
The capable multiple sintered plate filter cores 20 being arranged in inside shell of dust remover 10, the high pressure gas bag 30 being arranged in outside shell of dust remover 10
With blower fan 40, sintered plate filter core 20 has a gas exchanges room 25 of closing, multiple sintered plate filter cores 20 and shell of dust remover 10 it
Between surround dirt pocket 14, the outlet side 31 of high pressure gas bag 30 is provided with pulse valve 32, the outlet side 31 of high pressure gas bag 30 and blower fan
40 air intake stretches into shell of dust remover 10 and connects the gas exchanges room 25 of sintered plate filter core 20 separately down.In order to realize more
Good dust removing effects, the bottom of shell of dust remover 10 offers dust mouth 11, the bottom side of shell of dust remover 10 be disposed with into
Dirt pipe 12；The one end for entering dirt pipe 12 is located at the outside of shell of dust remover 10, enters in the other end insertion shell of dust remover 10 of dirt pipe 12
Portion is simultaneously connected with dedusting dividing plate 13, and dedusting dividing plate 13 is located between sintered plate filter core 20 and dust mouth 11, and dedusting dividing plate 13 will be moulded
Burn plate filter core 20 and be divided into connect up and down two units of dirt pocket 14 with the dirt pocket 14 that shell of dust remover 10 is surrounded, so may be used
To cause the fraction steam and dust that enter into dirt pipe 12 to be attached to the surface of dedusting dividing plate 13, into remaining water for entering dirt pipe 12
Vapour and dust are bypassed after dedusting dividing plate 13 and adsorbed by sintered plate filter core 20, and final dusting is realized by dedusting dividing plate 13, are reduced
Cleaning or the frequency for changing sintered plate filter core 20.
Adsorb for convenience in the dust whereabouts of the outer surface of sintered plate filter core 20, dedusting dividing plate 13 can be that Open Side Down
Arcuate structure, wherein one end of dedusting dividing plate 13 is fixedly connected with dust removing tube, and the other end of dedusting dividing plate 13 is to away from dust removing tube
Direction extends.Like this, the surface of dedusting dividing plate 13 is attached to by entering steam and dust fractions that dirt pipe 12 enters at the beginning, separately
A part bypasses dedusting dividing plate 13 and up in dirt pocket 14, and then is attached to the sintered plate filter core 20 of the top of dedusting dividing plate 13
Surface, when high pressure 30 jet of gas bag, gases at high pressure enter the gas exchanges room 25 of sintered plate filter core 20, based on sintered plate filter core
20 structure, gases at high pressure are attached to the steam and dust on the surface of sintered plate filter core 20, powder through sintered plate filter core 20 and injection
Dirt declines naturally under self gravitation, during decline, dust may directly under drop down onto dust mouth 11, it is also possible to land first
In the upper surface of dedusting dividing plate 13, based on the arcuate structure of dedusting dividing plate 13, the dust for dropping to the upper surface of dedusting dividing plate 13 enters one
Step drops down onto dust mouth 11 along under the curved surfaces of dedusting dividing plate 13.
In conjunction with accompanying drawing 3, sintered plate filter core 20 includes sintered plate body 21, is arranged in the top plate at the top of sintered plate body 21
22nd, it is arranged in the bottom plate 24 of the bottom of sintered plate body 21.Sintered plate body 21 is integrally connected by the V-arrangement corrugated plating of two panels symmetrical structure
Composition is connect, the gas exchanges room of nine independences and closing is also surrounded after the connection of two panels V-arrangement corrugated plating jointly with top plate 22, bottom plate 24
25, two panels V-arrangement corrugated plating outer surface even spread polytetrafluorethylecoatings coatings, polytetrafluorethylecoatings coatings have hydrophobicity, can be by
The water segregation of dirt pocket 14 can allow the gas of dirt pocket 14 to enter gas exchanges room 25 outside gas exchanges room 25.Top plate
22 and bottom plate 24 be fixed on the inner surface of shell of dust remover 10.In order to improve the injection efficiency of high pressure gas bag 30, top plate 22 embedded nine
Individual injection tube 23, the lateral cross-sectional area of injection tube 23 is equal to or slightly less than the lateral cross-sectional area of gas exchanges room 25, nine injections
Pipe 23 and above-mentioned nine gas exchanges rooms 25 are relative one by one, and the connection gas exchanges room 25 downwards of injection tube 23, injection tube 23 to
The outlet side 31 of the upper above-mentioned high pressure gas bag 30 of connection.
With reference to accompanying drawing 4,5, the bottom of injection tube 23 coordinates inside insertion sintered plate body 21, and the outer surface of injection tube 23
Coordinate with the inner surface of sintered plate body 21 and contact realization sealing, the top of injection tube 23 is higher by top plate 22, and injection tube upwards
23 lateral cross section is rectangle or ellipse, and this is the optimum structure of injection tube 23, the gases at high pressure that high pressure gas bag 30 is blown
Can within the most short time filling gas switch room 25, then, to being attached to the table of sintered plate body 21 within the most short time
The dust in face is blown, efficiently cleaning sintered plate body 21, it is to avoid attachment causes to be difficult to clear up dust for a long time.
The utility model, which is arranged on, to be needed on the industrial equipment of dedusting, is contained in the dust that especially industrial equipment is produced
There are a large amount of hot gas and moisture.
The course of work of utility model works：
1）Dust containing hot gas and moisture is entered by entering dirt pipe 12, and part dust is attached to the surface of dedusting dividing plate 13, its
Remaining dust bypasses dedusting dividing plate 13 and up in dirt pocket 14, and then is attached to the sintered plate filter core 20 of the top of dedusting dividing plate 13
Surface；
2）Based on the performance of sintered plate filter core 20, the moisture contained in dust can not be passed through in sintered plate filter core 20, dust
Hot gas then through sintered plate filter core 20 and enter gas exchanges room 25, this part hot gas by connection gas exchanges room 25 blower fan
40 absorb and outer row；
3）High pressure gas bag 30 works, in the presence of pulse valve 32, when the outlet side 31 of high pressure gas bag 30 is spaced certain
Between section be the jet of gas exchanges room 25 to sintered plate filter core 20, the gases at high pressure of gas exchanges room 25 pass through sintered plate filter core 20
And spray to fall to be attached to the dust of sintered plate filter core 20, dust declines naturally under self gravitation, during decline, and dust may
Dust mouth 11 is dropped down onto under directly, it is also possible to drop to the upper surface of dedusting dividing plate 13 first, based on the arcuate structure of dedusting dividing plate 13,
The dust of the upper surface of dedusting dividing plate 13 is dropped to further along dropping down onto dust mouth 11 under the curved surfaces of dedusting dividing plate 13；
4）Step 2）With step 3）Constantly repeat, realization, which is known clearly, discharges the purification of dust to industrial equipment, it is ensured that
Staff's is healthy.
Require supplementation with explanation is adsorbed for convenience in the dust whereabouts of the outer surface of sintered plate filter core 20, dedusting
Dividing plate 13 can also be the v-shaped structure that Open Side Down, and wherein one end of dedusting dividing plate 13 is fixedly connected with dust removing tube, dedusting dividing plate 13
The other end to away from dust removing tube direction extend.Like this, at the beginning by entering steam and dust fractions that dirt pipe 12 enters
The surface of dedusting dividing plate 13 is attached to, another part bypasses dedusting dividing plate 13 and up in dirt pocket 14, and then is attached to dedusting
The surface of sintered plate filter core 20 of the top of dividing plate 13, when high pressure 30 jet of gas bag, gases at high pressure enter the gas of sintered plate filter core 20
Body switch room 25, based on the structure of sintered plate filter core 20, gases at high pressure are through sintered plate filter core 20 and injection is attached to sintered plate
The steam and dust on the surface of filter core 20, dust declines naturally under self gravitation, during decline, and dust may directly fall
To dust mouth 11, it is also possible to drop to the upper surface of dedusting dividing plate 13 first, based on the v-shaped structure of dedusting dividing plate 13, drop to and remove
The dust of the upper surface of dirt dividing plate 13 under the V-arrangement surface of dedusting dividing plate 13 further along dropping down onto dust mouth 11.
Also need to supplementary notes is a little that the utility model is based primarily upon the existing structure of sintered plate filter core 20, due to
Had the advantage that using the dust removal device of sintered plate filter core 20：1）The dust size effectively filtered is less than 0.1um, and concentration of emission
It can reach much smaller than 1mg/Nm3；2）High Inlet dust concentration is suitable for, the running resistance and deduster of industrial equipment are not influenceed
Filter efficiency it is stable；3）It is lightweight, the 1/3 of small volume, only conventional cloth bag deduster volume；4）Sintered plate filter core 20 is used
Exoskeletal rigid structure, antistatic, acid and alkali-resistance is pressure-resistant, impact resistance, high temperature resistant, and filtering accuracy is high, deashing compressed air consumption
It is low；5）Using the jet performance and the permeable watertight performance of sintered plate filter core 20 of high pressure gas bag 30, sintered plate filter core 20 is realized
Timely cleaning, increase the service life.On this basis, in order to further improve the property of the deduster using sintered plate filter core 20
Can, the enter position of dirt pipe 12 and the jet position of deduster are improved, to improve the dust removing effects of dedusting, secondary remove is realized
Dirt, improves the cleaning effect of deduster, extends the service life of deduster.
Finally it should be noted that above content is only illustrating the technical solution of the utility model, rather than to this practicality
The limitation of novel protected scope, although the embodiment part is explained to the utility model, this area
It is to be appreciated by one skilled in the art that the technical solution of the utility model can be modified or equivalent substitution, without departing from
The spirit and scope of technical solutions of the utility model.
Claims (6)
1. a kind of sinter-plate precipitator, its structure include shell of dust remover, the sintered plate filter core being arranged in inside shell of dust remover,
High pressure gas bag and blower fan outside shell of dust remover are arranged in, the sintered plate filter core has the gas exchanges room of closing, and modeling is burnt
Plate filter core also surrounds dirt pocket between shell of dust remover, and the outlet side of the high pressure gas bag is provided with pulse valve, high pressure gas bag
Outlet side stretch into shell of dust remover separately down with the air intake of blower fan and connect the gas exchanges room of sintered plate filter core, it is special
Levy and be, the bottom of the shell of dust remover offers dust mouth, and the bottom side of shell of dust remover is disposed with into dirt pipe；It is described
Enter dirt pipe one end be located at shell of dust remover on the outside of, enter dirt pipe the other end insertion shell of dust remover inside and be connected with dedusting every
Plate, the dedusting dividing plate is located between sintered plate filter core and dust mouth, and dedusting dividing plate encloses sintered plate filter core and shell of dust remover
Into dirt pocket be divided into two dedusting chamber units connecting up and down.
2. a kind of sinter-plate precipitator according to claim 1, it is characterised in that the dedusting dividing plate is what Open Side Down
Arcuate structure, wherein one end of dedusting dividing plate is fixedly connected with dust removing tube, and the other end of dedusting dividing plate is to the direction away from dust removing tube
Extension.
3. a kind of sinter-plate precipitator according to claim 1, it is characterised in that the dedusting dividing plate is what Open Side Down
V-shaped structure, wherein one end of dedusting dividing plate is fixedly connected with dust removing tube, and the other end of dedusting dividing plate prolongs to the direction away from dust removing tube
Stretch.
4. a kind of sinter-plate precipitator according to claim 1 or 2 or 3, it is characterised in that the sintered plate filter core includes
Sintered plate body, the top plate for being arranged in sintered plate bodies top, the bottom plate for being arranged in sintered plate body bottom, the sintered plate sheet
Body is made up of the V-arrangement corrugated plating integrally connected of two panels symmetrical structure, also common with top plate, bottom plate after the connection of two panels V-arrangement corrugated plating
Surround the gas exchanges room of at least one closing, two panels V-arrangement corrugated plating outer surface even spread polytetrafluorethylecoatings coatings；
The top plate and bottom plate are fixed on shell of dust remover inner surface；The top plate embeds at least one injection tube, the injection
The lateral cross-sectional area of pipe be equal to or slightly less than gas exchanges room lateral cross-sectional area, at least one injection tube with it is above-mentioned at least one
Gas exchanges room is relative one by one, and injection tube connects downwards gas exchanges room, and injection tube connects going out for above-mentioned high pressure gas bag upwards
Gas end.
5. a kind of sinter-plate precipitator according to claim 4, it is characterised in that the bottom of the injection tube coordinates insertion
Sintered plate body interior, and the inner surface of outer surface and the sintered plate body of injection tube coordinates and contacts, the top of injection tube is upward
Top plate is higher by, and the lateral cross section of injection tube is rectangle or ellipse.
6. a kind of sinter-plate precipitator according to claim 1 or 3 or 5, it is characterised in that the number of the sintered plate filter core
Measure as at least two, at least two sintered plate filter cores are arranged in parallel inside shell of dust remover.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720283637.5U CN206566623U (en) | 2017-03-22 | 2017-03-22 | A kind of sinter-plate precipitator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720283637.5U CN206566623U (en) | 2017-03-22 | 2017-03-22 | A kind of sinter-plate precipitator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206566623U true CN206566623U (en) | 2017-10-20 |
Family
ID=60054909
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720283637.5U Expired - Fee Related CN206566623U (en) | 2017-03-22 | 2017-03-22 | A kind of sinter-plate precipitator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206566623U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115999262A (en) * | 2023-02-03 | 2023-04-25 | 江苏耀先环境设备有限公司 | Control system of plastic-sintered plate dust remover, plastic-sintered plate dust remover and processing technology of plastic-sintered plate dust remover |
| CN116889773A (en) * | 2023-09-08 | 2023-10-17 | 张家港市金帆环保科技有限公司 | Plastic plate dust remover |
-
2017
- 2017-03-22 CN CN201720283637.5U patent/CN206566623U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115999262A (en) * | 2023-02-03 | 2023-04-25 | 江苏耀先环境设备有限公司 | Control system of plastic-sintered plate dust remover, plastic-sintered plate dust remover and processing technology of plastic-sintered plate dust remover |
| CN115999262B (en) * | 2023-02-03 | 2024-04-12 | 江苏耀先环境设备有限公司 | Control system of plastic-sintered plate dust remover, plastic-sintered plate dust remover and processing technology of plastic-sintered plate dust remover |
| CN116889773A (en) * | 2023-09-08 | 2023-10-17 | 张家港市金帆环保科技有限公司 | Plastic plate dust remover |
| CN116889773B (en) * | 2023-09-08 | 2023-11-21 | 张家港市金帆环保科技有限公司 | Plastic plate dust remover |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
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Granted publication date: 20171020 Termination date: 20180322 |