CN206823452U - A kind of dust pelletizing system - Google Patents
A kind of dust pelletizing system Download PDFInfo
- Publication number
- CN206823452U CN206823452U CN201720748529.0U CN201720748529U CN206823452U CN 206823452 U CN206823452 U CN 206823452U CN 201720748529 U CN201720748529 U CN 201720748529U CN 206823452 U CN206823452 U CN 206823452U
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- CN
- China
- Prior art keywords
- dust
- conduit
- cyclonic
- level cyclone
- pipe
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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Abstract
The utility model discloses a kind of dust pelletizing system, including two one cyclonic dust arresters being connected by air inlet pipe, first conduit, blower fan, humidify conduit, two level cyclone dust collector, blast pipe, atomized steam separator box and dust conveyer belt, the one cyclonic dust arrester, first conduit, blower fan, humidify conduit, two level cyclone dust collector passes sequentially through flange with blast pipe and connected, inside wherein described blast pipe end insertion atomized water gas separator box, the dust conveyer belt is located at the underface of one cyclonic dust arrester and two level cyclone dust collector, the utility model is reasonable in design, flue gas drives dust of the water in Whirlwind cyclone internal rotation absorbs flue gas by forming whirlwind after two one cyclonic dust arresters, being introduced into for water dedusting is introduced into effectively raise dust removing effects and reduce dirt content in tail gas.
Description
Technical field
The utility model belongs to tails dedusting equipment technical field, more particularly to a kind of dust pelletizing system.
Background technology
The problem of environmental problem be that current all trades and professions all suffer from one is serious, dust is dirty in numerous pollution types
Contaminate it is especially prominent, especially mine development utilize and construction material manufacturing in problem of environmental pollution it is more prominent, therefore
Targetedly design a set of dust pollution dust pelletizing system to be necessary, current dedusting method has water dedusting, vortex to remove
The dedusting methods such as dirt, wherein vortex deduster principle be essentially all rotated using air-flow in circular shell so as to
Dust rotary motion is driven, dust hits housing under the influence of centrifugal force during dust and air-flow rotate together with motion
So as to which most is captured by housing, the part dust of the enclosure interior of this dedusting method may in the presence of swirling eddy
It can be rotated together the problem of causing secondary pollution with air-flow again, it is most absolutely for the such secondary pollution problem of customer service at present
Number dust pelletizing system is used tail gas by being discharged after the elite of pond, although the dedusting of deduster also greatly reduces in such mode
Effect, but high velocity air can still contain substantial amounts of dust by pond marquis and dirty effect and not up to preferable effect drop in steam dedusting
Fruit.
The content of the invention
Technical assignment of the present utility model is to provide a kind of cyclone centrifugal duster for above prior art deficiency.
It is a kind of dust pelletizing system that the utility model, which solves technical scheme used by its technical problem, including two by entering
The connected one cyclonic dust arrester of tracheae, the first conduit, blower fan, humidification conduit, two level cyclone dust collector, blast pipe, mist
Change steam separator box and dust conveyer belt, the one cyclonic dust arrester, the first conduit, blower fan, humidification conduit, two level whirlwind
Dust arrester passes sequentially through flange with blast pipe and connected, wherein inside blast pipe end insertion atomized water gas separator box, institute
State the underface that dust conveyer belt is located at one cyclonic dust arrester and two level cyclone dust collector.
Further, the one cyclonic dust arrester and two level cyclone dust collector include gas outlet, escape pipe, shunting
Room, cyclone dustproof pipe and laying dust room, wherein the escape pipe is set is located at diffluence room with the top of diffluence room and the escape pipe
The length of internal body is the 2/3 of diffluence room's height, and the side wall of the diffluence room is provided with air inlet flange-interface.
Further, opening position of the humidification conduit close to lower end is provided with atomization water inlet pipe, centre is provided with rotor.
Further, the atomized steam separator box includes casing, filter screen and discharge outlet, and the casing top is open, and institute
The top half for stating box house is provided with filter screen.
Originally the beneficial effect for being utility model is：The deduster does rotation fortune at a high speed using air-flow in primary dust removing device
It is dynamic most dust is lost the inertia of rotation with dust arrester inwall under the influence of centrifugal force and is fallen into dust arrester
Discharged in the laying dust room of bottom；Residual gas stir by adding atomization aqueous vapor through rotor cause dust and steam be sufficiently mixed into
Enter the further dedusting in two-stage dust removal room；Finally the wet gas containing a small amount of dust carries out last into atomized steam separator box
Dedusting is walked, and the suitable clean gas discharge of aridity is obtained by the filter screen condensation water removal in atomized steam separator box, should
System dust removing positive effect.
Brief description of the drawings
Fig. 1 is the utility model overall structure diagram.
Fig. 2 is the structural representation of the utility model primary dust removing cyclone dust collector and two level cyclone dust collector.
Embodiment
Workflow of the present utility model is described below with reference to Figure of description：
A kind of dust pelletizing system as shown in Figure 1, including two one cyclonic dust arresters 1, first being connected by air inlet pipe 8
Conduit 13, blower fan 2, humidification conduit, two level cyclone dust collector 3, blast pipe 5, atomized steam separator box 6 and dust conveyer belt 9,
The one cyclonic dust arrester 1, the first conduit 13, blower fan 2, humidification conduit, two level cyclone dust collector 3 and blast pipe 5 according to
Secondary to be connected by flange, wherein inside the end of the blast pipe 5 insertion atomized water gas separator box 6, the dust conveyer belt 9 is located at
The underface of one cyclonic dust arrester 1 and two level cyclone dust collector 3.
Further, the one cyclonic dust arrester 1 and two level cyclone dust collector 3 include gas outlet 16, escape pipe
17th, diffluence room 15, cyclone dustproof pipe 14 and laying dust room 7, wherein the escape pipe 17 is set and the top of diffluence room 15 and described
The length that escape pipe 17 is located at the body inside diffluence room 15 is the 2/3 of the height of diffluence room 15, in the side wall of the diffluence room 15
Provided with the flange-interface of air inlet 16.
Further, opening position of the humidification conduit close to lower end is provided with atomization water inlet pipe 4, centre is provided with rotor 12.
Further, the atomized steam separator box 6 includes casing, filter screen 11 and discharge outlet 10, and the casing top is open,
And the top half of the box house is provided with filter screen 11.
System operation is as follows：Open system outer gas stream is removed under the drive of blower fan by air inlet pipe 8 into one cyclonic
Dirt device 1 completes first time dedusting, and adding the well mixed two-stage dust removal device 3 that enters of atomization aqueous vapor by humidifying conduit carries out the
Final dusting, wet gas finally containing micro dust are removed water by atomized steam, can directly arranged such as air after dedusting；Simultaneously
The dust that the rotational conveyance of dust conveyer belt 9 is isolated.
Claims (4)
1. a kind of dust pelletizing system, including two the one cyclonic dust arresters (1) being connected by air inlet pipe (8), the first conduits
(13), blower fan (2), humidification conduit, two level cyclone dust collector (3), blast pipe (5), atomized steam separator box (6) and dust are defeated
Send band (9), it is characterised in that：The one cyclonic dust arrester (1), the first conduit (13), blower fan (2), humidification conduit, two level
Cyclone dust collector (3) passes sequentially through flange with blast pipe (5) and connected, wherein the blast pipe (5) end insertion atomization aqueous vapor
Separator box (6) is internal, and the dust conveyer belt (9) is located at one cyclonic dust arrester (1) and two level cyclone dust collector (3)
Underface.
A kind of 2. dust pelletizing system according to claim 1, it is characterised in that：The one cyclonic dust arrester (1) and two
Level cyclone dust collector (3) includes gas outlet (16), escape pipe (17), diffluence room (15), cyclone dustproof pipe (14) and laying dust
Room (7), wherein the escape pipe (17) is set is located at diffluence room (15) with the top of diffluence room (15) and the escape pipe (17)
The length of internal body is the 2/3 of diffluence room (15) height, and the side wall of the diffluence room (15) is provided with air inlet (16) method
Blue interface.
A kind of 3. dust pelletizing system according to claim 1, it is characterised in that：Opening position of the humidification conduit close to lower end
Rotor (12) is provided with provided with atomization water inlet pipe (4), centre.
A kind of 4. dust pelletizing system according to claim 1, it is characterised in that：The atomized steam separator box (6) includes case
Body, filter screen (11) and discharge outlet (10), the casing top is open, and the top half of the box house is provided with filter screen
(11)。
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720748529.0U CN206823452U (en) | 2017-06-26 | 2017-06-26 | A kind of dust pelletizing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720748529.0U CN206823452U (en) | 2017-06-26 | 2017-06-26 | A kind of dust pelletizing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206823452U true CN206823452U (en) | 2018-01-02 |
Family
ID=60777566
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720748529.0U Expired - Fee Related CN206823452U (en) | 2017-06-26 | 2017-06-26 | A kind of dust pelletizing system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206823452U (en) |
-
2017
- 2017-06-26 CN CN201720748529.0U patent/CN206823452U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180102 Termination date: 20180626 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |