CN204751394U - Coal breaker dust suppression device - Google Patents
Coal breaker dust suppression device Download PDFInfo
- Publication number
- CN204751394U CN204751394U CN201520454361.3U CN201520454361U CN204751394U CN 204751394 U CN204751394 U CN 204751394U CN 201520454361 U CN201520454361 U CN 201520454361U CN 204751394 U CN204751394 U CN 204751394U
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- CN
- China
- Prior art keywords
- dust
- material blanking
- blanking tube
- chamber
- deflector chute
- 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.)
- Withdrawn - After Issue
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- 239000000428 dust Substances 0.000 title claims abstract description 106
- 239000003245 coal Substances 0.000 title claims abstract description 50
- 230000001629 suppression Effects 0.000 title abstract description 6
- 238000001179 sorption measurement Methods 0.000 claims abstract description 42
- 238000000926 separation method Methods 0.000 claims abstract description 24
- 239000000463 material Substances 0.000 claims description 71
- 229920001971 elastomer Polymers 0.000 claims description 7
- 229920002635 polyurethane Polymers 0.000 claims description 7
- 239000004814 polyurethane Substances 0.000 claims description 7
- 229910000831 Steel Inorganic materials 0.000 claims description 3
- 238000005299 abrasion Methods 0.000 claims description 3
- 230000006835 compression Effects 0.000 claims description 3
- 238000007906 compression Methods 0.000 claims description 3
- 239000010959 steel Substances 0.000 claims description 3
- LENZDBCJOHFCAS-UHFFFAOYSA-N tris Chemical compound OCC(N)(CO)CO LENZDBCJOHFCAS-UHFFFAOYSA-N 0.000 claims description 3
- 230000000694 effects Effects 0.000 description 6
- 238000007667 floating Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 239000002245 particle Substances 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000000151 deposition Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000032258 transport Effects 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000000763 evoking effect Effects 0.000 description 1
- 231100000616 occupational exposure limit Toxicity 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
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- Auxiliary Methods And Devices For Loading And Unloading (AREA)
Abstract
The utility model provides a coal breaker dust suppression device, sets up on the baffle box, including vortex chamber, circulation chamber, circulation pipe, dirt gas sinker, circulation pipe manhole cover, dust shunt, micronic dust adsorption separation system, a tail curtain, manhole door, vortex chamber combines as an organic wholely with blanking pipe, baffle box intercommunication between two blanking pipes, on the baffle box, the circulation chamber sets up on the next door that the first blanking that is close to the baffle box front end was managed, manages the lower part intercommunication with first blanking, and as an organic whole with first blanking pipe and the combination of baffle box intercommunication, first blanking is managed upper portion and is the coal breaker to the upper portion in circulation chamber is passed through circulation pipe and is connected with the coal breaker, the circulation chamber is separated into the main ring by built -in baffle and is flowed chamber and secondary ring stream chamber. The utility model discloses can solve the problem of broken coal unit room transfer post raise dust well, press down the dirt dust fall effectively, make the workplace dust concentration of broken coal unit room transfer post department accord with national standard. Both prevent the dust pollution environment, ensured post workman's vital interests again.
Description
Technical field
The utility model relates to the environmental protecting device of a kind of coal crusher house transfer point dust suppression, particularly coal crushes dust-arrest device.
Background technology
Coal crushes is a kind of conventional lump coal breaking equipment, lump coal breaking can be become nut coal or fine coal by it, coal crushes has the advantages such as crushing efficiency is high, stable, but can produce a large amount of induced airs when coal crushes transhipment, induced air takes up a large amount of dust, makes the transfer point below coal crushes be formed and flies upward dust in a large number, the disorderly air stream evoked by induced air makes fine dusts elegant everywhere, become main dust source, cause dust from flying, contaminated environment.
At present, have the way of various dedusting for coal crusher house transfer point, wet type as negative pressure-induced process of cleaning, dry fog process of cleaning ... dry type as duct cyclone, flat bag filter, electric dust collector ...These dedusting technologies can receive certain dust removing effects after implementing in a short time, but constantly decline after running a period of time, to such an extent as to finally lie idle.So all fail to solve well the problem of coal crusher house transfer point airborne dust.
Summary of the invention
The purpose of this utility model provides a kind of coal crushes dust-arrest device, suppresses the dust that coal crusher house transfer point produces, and solves the problem of coal crusher house transfer point airborne dust well.
For achieving the above object, the technical solution of the utility model is:
A kind of coal crushes dust-arrest device, be arranged on deflector chute, comprise vortex cavity, circulation chamber, circulating pipe, dirt gas sinker, circulating pipe manhole cover, dust diverter, micronic dust adsorption separation system, tail envelope curtain, manhole door, described vortex cavity, between two material blanking tubes, on deflector chute, is communicated with material blanking tube, deflector chute and is combined as a whole; Described circulation chamber is arranged on the side of the first material blanking tube near deflector chute front end, be communicated with the first material blanking tube bottom, to be communicated with deflector chute with the first material blanking tube and to be combined as a whole, first material blanking tube top is coal crushes, and the top in circulation chamber is connected with coal crushes by circulating pipe, described circulation chamber is separated into main ring stream chamber and inner loop stream chamber by inner division plate, and described dirt gas sinker is arranged in vortex cavity, main ring stream chamber, inner loop stream chamber; Described dust diverter, micronic dust adsorption separation system, tail envelope curtain is all fixed in deflector chute, described micronic dust adsorption separation system is arranged on deflector chute leading portion, described tail envelope curtain is arranged on deflector chute tail end, and described dust diverter is arranged in the deflector chute below the first material blanking tube and circulation chamber.
Described micronic dust adsorption separation system comprises seal cover cap, micronic dust adsorption bar, fixed mount, and described seal cover cap and deflector chute upper cover are combined as a whole; Described micronic dust adsorption bar is fixed on fixed mount, described micronic dust adsorption bar is cubic strip structure, wherein, two leptoprosopy are " W " shape, all the other two wide is plane, the width of described micronic dust adsorption separation system is a little large than the width in deflector chute, and described micronic dust adsorption bar is no less than four layers, and micronic dust adsorption bar is between layers staggered to be stacked.
By counterweight rubber plate, industrial canvas, polyurethane sheet, described dust diverter arranges that compression forms successively, meeting charge level is two blocks of abrasion resistant polyurethane plates, is then the industrial canvas of a monoblock, is finally one block of counterweight rubber plate that at least 10mm is thick.
Described vortex cavity, main ring stream chamber, inner loop stream chamber are all identical with the width of material blanking tube, material blanking tube removes with the part steel plate at the main ring stream chamber place of combining with the vortex cavity place of combining and material blanking tube, makes vortex cavity, main ring stream chamber and material blanking tube form a large cavity.
Have three groups of dirt gas sinkers in described vortex cavity, be arranged at equably between two material blanking tubes.
Have three groups of dirt gas sinkers in described main ring stream chamber, be arranged between dividing plate and the first material blanking tube.
Described inner loop stream chamber is provided with manhole door, has one group of dirt gas sinker, be arranged between dividing plate and manhole door in it.
Described circulating pipe is terminated on the non-working surface of coal crushes supplied materials material blanking tube, under be terminated on main ring stream chamber and inner loop stream chamber.
The width of described dust diverter, micronic dust adsorption separation system, tail envelope curtain is a bit larger tham the inner width of deflector chute, dust diverter, micronic dust adsorption separation system, tail envelope curtain bottom and conveyer belt Elastic Contact.
The beneficial effects of the utility model
The utility model can solve the problem of coal crusher house transfer point airborne dust well, dust suppression depositing dust effectively, makes the working space dust concentration at coal crusher house transfer point place meet the requirement of standard GB/T Z2.1-2007 " workplace harmful factors occupational exposure limit section 1 ".Both prevent dust polluting environment, ensure again the vital interests of post workman.
Accompanying drawing explanation
Fig. 1 is the front elevation of the utility model one embodiment.
Fig. 2 is the structural representation of dust diverter of the present utility model.
Fig. 3 is the structural representation of micronic dust adsorption separation system of the present utility model.
Fig. 4 is the structural representation of micronic dust adsorption bar of the present utility model.
Fig. 5 is dust suppression principle schematic of the present utility model.
In figure: 1, tail envelope curtain; 21, the first material blanking tube; 22, the second material blanking tube; 3, dirt gas sinker; 4, vortex cavity; 5, coal crushes; 6, circulating pipe manhole cover; 7, circulating pipe; 8, main ring stream chamber; 9, inner loop stream chamber; 10, dust diverter; 101, counterweight rubber plate; 102, industrial canvas; 103, polyurethane sheet; 11, deflector chute; 12, micronic dust adsorption separation system; 121, seal cover cap; 122, micronic dust adsorption bar; 123, fixed mount; 13, belt; 14, manhole door; 15, dividing plate.
Detailed description of the invention
See Fig. 1, coal crushes dust-arrest device of the present utility model, is arranged on the deflector chute 11 in material blanking tube front (be front with belt speed direction, reversing sense is rear); Described vortex cavity 4 is between the first material blanking tube 21 and the second material blanking tube 22, on deflector chute, be communicated with material blanking tube, deflector chute and be combined as a whole; Described circulation chamber is arranged on the side of the first material blanking tube 21 near deflector chute front end, be communicated with the first material blanking tube bottom, to be communicated with deflector chute with the first material blanking tube and to be combined as a whole, first material blanking tube top is coal crushes 5, and the top in circulation chamber is connected with coal crushes by circulating pipe, described circulation chamber is separated into main ring stream chamber 8 and inner loop stream chamber 9 by inner division plate 15, and described dirt gas sinker 3 is arranged in vortex cavity 4, main ring stream chamber 8, inner loop stream chamber 9; Described dust diverter 10, micronic dust adsorption separation system 12, tail envelope curtain 1 is all fixed in deflector chute, described micronic dust adsorption separation system 12 is arranged on deflector chute leading portion, described tail envelope curtain 1 is arranged on deflector chute tail end, and described dust diverter 10 is arranged in the deflector chute below the first material blanking tube 21 and circulation chamber.
As Figure 3-Figure 4, described micronic dust adsorption separation system 12 comprises seal cover cap 121, micronic dust adsorption bar 122, fixed mount 123, and described seal cover cap and deflector chute upper cover are combined as a whole; Described micronic dust adsorption bar is fixed on fixed mount, described micronic dust adsorption bar is cubic strip structure, wherein, two leptoprosopy are " W " shape, all the other two wide is plane, the width of described micronic dust adsorption separation system is a little large than the width in deflector chute, and described micronic dust adsorption bar is no less than four layers, and micronic dust adsorption bar is between layers staggered to be stacked.
By counterweight rubber plate 101, industrial canvas 102, polyurethane sheet 103, described dust diverter 10 arranges that compression forms successively as shown in Figure 2, meeting charge level is two blocks of abrasion resistant polyurethane plates, then being the industrial canvas of a monoblock, is finally one block of counterweight rubber plate that at least 10mm is thick.
In the present embodiment, vortex cavity 4, main ring stream chamber 8, inner loop stream chamber 9 are all identical with the width of material blanking tube 2, material blanking tube 2 removes with the part steel plate at main ring stream chamber 8 place of combining with vortex cavity 4 place of combining and material blanking tube 2, makes vortex cavity 4, main ring stream chamber 8 and material blanking tube 2 form a large cavity.
In the present embodiment, vortex cavity 4 has three groups of dirt gas sinkers 3, is arranged at equably between material blanking tube 2.
In the present embodiment, main ring stream chamber 8 has three groups of dirt gas sinkers 3, is arranged between dividing plate 15 and material blanking tube 2.
In the present embodiment, described inner loop stream chamber is provided with manhole door 14, has one group of dirt gas sinker, be arranged between dividing plate and manhole door in it.
In addition, circulating pipe 7 described in the utility model is terminated on the non-working surface of coal crushes 5 supplied materials material blanking tube, under be terminated on main ring stream chamber 8 and inner loop stream chamber 9.
When making dust diverter 10, micronic dust adsorption separation system 12, tail envelope curtain 1, their width must be made to be a bit larger tham the inner width of deflector chute 11, such energy sealing is tight, ensure the filter effect of dirt gas, when dust diverter 10, micronic dust adsorption separation system 12, tail envelope curtain 1 are installed, this three bottom and conveyer belt 13 Elastic Contact.
As shown in Figure 5, working process: when coal crushes runs, when material is transported to next belt from coal crushes by material blanking tube, the disorderly air stream that evokes because material falls, makes the material with dust be formed at belt feeder discharging place and flies upward dust in a large number.Belt travels forward and take up induced air in deflector chute, dirt gas in deflector chute along with induced air moves forward.When dirt gas runs into dust diverter, dust is separated into two parts; The larger dust of major part particle enters in eddy current cavity with dirt gas upward movement, and the trickle dust of sub-fraction can pass through dust diverter, along with the continuation of belt induced air forward.
Material blanking tube place material constantly falls, and air is constantly drained with the whereabouts of material, and therefore form negative pressure and produce suction, the dirt gas entering vortex cavity, under aerodynamic driving, moves to material blanking tube direction; In the process, under the effect of dirt gas sinker, the kinetic energy of dirt gas is consumed in a large number; According to aerodynamic principle, most dust settles down because kinetic energy is not enough to provide it to continue floating aerial power, falls above belt, transports with material; Fraction dust can be less because of its particle, and quality is less, and remaining aerodynamic force is still enough to make it in atmosphere floating and continues to the motion of material blanking tube direction, and dirt gas that is last and material blanking tube merges together, and participates in the motion cycle of next round
Major and minor circulation cavity is by circulating pipe and material blanking tube UNICOM, separated by dividing plate between major and minor circulation cavity, according to aerodynamic principle, when having material to pass through in coal crushes running, material blanking tube, take away most of air in material blanking tube, circulating pipe and material blanking tube will produce pressure reduction, and the air in circulating pipe will flow to material blanking tube; Under aerodynamic effect, gas in major and minor circulation cavity constantly upwards flows to material blanking tube by circulating pipe, form air-flow winding, therefore after a large amount of dust that coal crushes produces enter within the scope of circulation cavity by material blanking tube, by aerodynamic effect upwards and the shunting action of dust diverter, major part dust enters in main ring stream cavity, fraction dust enters in main ring stream cavity, dust will by dirt gas sinker, under the effect of dirt gas sinker, the kinetic energy of dirt gas is consumed in a large number; According to aerodynamic principle, most of dust settles down because kinetic energy is not enough to provide it to continue floating aerial power, falls above belt, transports with material.
Part dust can be less because of its particle, quality is less, aerodynamic force is still enough to make it in atmosphere floating, and continue through circulating pipe to material blanking tube direction and move, dirt gas that is last and material blanking tube merges together, and participates in the motion cycle of next round ... be arranged on the micronic dust adsorption separation system of deflector chute front end, energy of adsorption is by extremely trickle a small amount of dust of twice dust diverter, it is separated from air, thus ensures that deflector chute prosopyle end does not have dust loss out.Deflector chute tail end is provided with tail envelope room, ensure that deflector chute tail end does not have dust loss out.
After the utility model is implemented, solve the problem of coal crusher house transfer point airborne dust well, dust suppression depositing dust, decreases aerial contamination effectively, improves the working environment of post workman.
Claims (9)
1. a coal crushes dust-arrest device, be arranged on deflector chute, it is characterized in that, comprise vortex cavity, circulation chamber, circulating pipe, dirt gas sinker, circulating pipe manhole cover, dust diverter, micronic dust adsorption separation system, tail envelope curtain, manhole door, described vortex cavity, between two material blanking tubes, on deflector chute, is communicated with material blanking tube, deflector chute and is combined as a whole; Described circulation chamber is arranged on the side of the first material blanking tube near deflector chute front end, be communicated with the first material blanking tube bottom, to be communicated with deflector chute with the first material blanking tube and to be combined as a whole, first material blanking tube top is coal crushes, and the top in circulation chamber is connected with coal crushes by circulating pipe, described circulation chamber is separated into main ring stream chamber and inner loop stream chamber by inner division plate, and described dirt gas sinker is arranged in vortex cavity, main ring stream chamber, inner loop stream chamber; Described dust diverter, micronic dust adsorption separation system, tail envelope curtain is all fixed in deflector chute, described micronic dust adsorption separation system is arranged on deflector chute leading portion, described tail envelope curtain is arranged on deflector chute tail end, and described dust diverter is arranged in the deflector chute below the first material blanking tube and circulation chamber.
2. coal crushes dust-arrest device as claimed in claim 1, it is characterized in that, described micronic dust adsorption separation system comprises seal cover cap, micronic dust adsorption bar, fixed mount, and described seal cover cap and deflector chute upper cover are combined as a whole; Described micronic dust adsorption bar is fixed on fixed mount, described micronic dust adsorption bar is cubic strip structure, wherein, two leptoprosopy are " W " shape, all the other two wide is plane, the width of described micronic dust adsorption separation system is a little large than the width in deflector chute, and described micronic dust adsorption bar is no less than four layers, and micronic dust adsorption bar is between layers staggered to be stacked.
3. coal crushes dust-arrest device as claimed in claim 1, it is characterized in that, by counterweight rubber plate, industrial canvas, polyurethane sheet, described dust diverter arranges that compression forms successively, meeting charge level is two blocks of abrasion resistant polyurethane plates, then being the industrial canvas of a monoblock, is finally one block of counterweight rubber plate that at least 10mm is thick.
4. coal crushes dust-arrest device as claimed in claim 2 or claim 3, it is characterized in that, vortex cavity, main ring stream chamber, inner loop stream chamber are all identical with the width of material blanking tube, material blanking tube removes with the part steel plate at the main ring stream chamber place of combining with the vortex cavity place of combining and material blanking tube, makes vortex cavity, main ring stream chamber and material blanking tube form a large cavity.
5. coal crushes dust-arrest device as claimed in claim 4, it is characterized in that, described vortex cavity has three groups of dirt gas sinkers, is arranged at equably between two material blanking tubes.
6. coal crushes dust-arrest device as claimed in claim 4, it is characterized in that, described main ring stream chamber has three groups of dirt gas sinkers, is arranged between dividing plate and the first material blanking tube.
7. coal crushes dust-arrest device as claimed in claim 4, it is characterized in that, described inner loop stream chamber is provided with manhole door, has one group of dirt gas sinker, be arranged between dividing plate and manhole door in it.
8. coal crushes dust-arrest device as claimed in claim 4, is characterized in that, described circulating pipe is terminated on the non-working surface of coal crushes supplied materials material blanking tube, under be terminated on main ring stream chamber and inner loop stream chamber.
9. coal crushes dust-arrest device as claimed in claim 4, it is characterized in that, the width of described dust diverter, micronic dust adsorption separation system, tail envelope curtain is a bit larger tham the inner width of deflector chute, dust diverter, micronic dust adsorption separation system, tail envelope curtain bottom and conveyer belt Elastic Contact.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520454361.3U CN204751394U (en) | 2015-06-19 | 2015-06-19 | Coal breaker dust suppression device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520454361.3U CN204751394U (en) | 2015-06-19 | 2015-06-19 | Coal breaker dust suppression device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204751394U true CN204751394U (en) | 2015-11-11 |
Family
ID=54466124
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520454361.3U Withdrawn - After Issue CN204751394U (en) | 2015-06-19 | 2015-06-19 | Coal breaker dust suppression device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204751394U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104960879A (en) * | 2015-06-19 | 2015-10-07 | 李文玉 | Dust suppression device for coal crusher |
| CN107215611A (en) * | 2017-06-28 | 2017-09-29 | 张玉伟 | The dustless material blanking tube of material-transporting system transfer station |
-
2015
- 2015-06-19 CN CN201520454361.3U patent/CN204751394U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104960879A (en) * | 2015-06-19 | 2015-10-07 | 李文玉 | Dust suppression device for coal crusher |
| CN107215611A (en) * | 2017-06-28 | 2017-09-29 | 张玉伟 | The dustless material blanking tube of material-transporting system transfer station |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20160408 Address after: Tian Dawa County 124010 Liaoning province Panjin City District office headquarters town garden district A building 2-11-1 Patentee after: Liaoning Jinfu Dust Suppression Technology Co., Ltd. Address before: 124010 Liaoning province Panjin city Xinglongtai District No. 101 Street Huibin room 210 Patentee before: Li Wenyu |
|
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20151111 Effective date of abandoning: 20170623 |