CN106139804A - Pyrophillite crushing system dust arrester - Google Patents
Pyrophillite crushing system dust arrester Download PDFInfo
- Publication number
- CN106139804A CN106139804A CN201610665735.5A CN201610665735A CN106139804A CN 106139804 A CN106139804 A CN 106139804A CN 201610665735 A CN201610665735 A CN 201610665735A CN 106139804 A CN106139804 A CN 106139804A
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- dust
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- pyrophillite
- pipe
- arrester
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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
- B01D50/40—Combinations of devices covered by groups B01D45/00 and B01D47/00
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- Chemical Kinetics & Catalysis (AREA)
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Abstract
The invention provides pyrophillite crushing system dust arrester, it is intended to solving in prior art in pyrophillite shattering process, the dust of generation affects the problem of air quality.Pyrophillite crushing system dust arrester, including dust arrester, escape pipe, air-introduced machine and water deduster；Dust arrester includes body, dust collecting trough and connecting tube, basis is the most internal is provided with spiral passage, is arranged with dust discharge road bottom the inwall of passage, and lower end, each dust discharge road is all connected with dust flue, every dust flue lower end is all connected with dust collecting trough, and dust collecting trough is looped around on the lateral wall of body lower end.Under the influence of centrifugal force; the dust granule that density is bigger than air can be thrown on the sidewall of passage; under the effect of sidewall friction resistance; dust falls in the bottom of passage, and when dust slowly moves to dust discharge road along bottom, dust falls in dust discharge road; fall into the dust in dust discharge road; can be in dust flue fall into dust collecting trough, dusty gas processes through multiple dust discharge roads, is purified.
Description
Technical field
The present invention relates to pyrophillite crushing system dust arrester.
Background technology
At present, during pulverizing pyrophillite with disintegrating machine, a large amount of dust can be produced, cause air pollution, serious shadow
Ring working environment, staff is produced huge injury.
The dust produced during in order to remove broken, some producer uses sack cleaner to carry out dedusting at present, but this
Cleaner unit uses for a long time and is susceptible to blocking, affects dust removing effects；Additionally, the patent Shen of Application No. 201020254127.3
Please disclose a kind of diamond synthesis block crushing dust collection device, by the gas with dust through cyclone dust extractor dedusting, dedusting
Dust in device ash bucket, through tank, utilizes water to absorb dust；But adopt and collect the device of dust, cyclone dust removal in this way
Device and tank are all the parts separated, and are connected by pipeline, capture space big, and cost is high；Additionally, water produces the speed of mud
Comparatively fast, and to remove mud cumbersome.
Summary of the invention
The invention provides pyrophillite crushing system dust arrester, it is intended to solve prior art crushed at pyrophillite
Cheng Zhong, the dust of generation affects the problem of air quality in working environment.
In order to solve above technical problem, the present invention is achieved through the following technical solutions: pyrophillite crushing system dedusting
Device, including dust arrester, escape pipe, air-introduced machine and water deduster, described escape pipe is connected between water deduster and dust arrester,
Air-introduced machine is arranged on escape pipe；
Dust arrester includes body, dust collecting trough and connecting tube, and basis is the most internal is provided with spiral passage, arranges bottom the inwall of passage
Showing the dust discharge road communicated with passage, lower end, each dust discharge road is all connected with dust flue, every dust flue lower end all with dust collecting trough phase
Even, dust collecting trough is looped around on the lateral wall of body lower end；
Passage is provided with air inlet and gas outlet, and connecting tube two ends are respectively gas transmission end and for absorbing the gas collection end of dust,
The gas transmission end of connecting tube is connected with the air inlet of passage, and the gas collection end of connecting tube is towards blanking port, the gas outlet of passage with go out
Trachea is connected.
Further, body is up-small and down-big tubaeform, and passage is cone spiral type, and body lower end, towards blanking port, connects
The gas collection end of pipe is sealedly connected on body upper end；The gas outlet of passage is arranged on the upper end, lateral wall of body, and air inlet is arranged on
The lower end, lateral wall of body.Body is arranged to horn-like, dust gathering arrester can be substituted and play the effect collecting dust, be equivalent to gas
The circulating device of body and the collection device of gas are wholely set, and make overall structure be reduced, save work space, save
Manufacturing cost.
Further, water deduster includes tank and preserve pipe, and escape pipe leads in tank, the bottom surface of tank be upper big under
Little taper surface, preserves pipe and is connected to the minimum point of tank bottom surface, preserves the upper and lower of pipe and is equipped with one and preserves pipe
Valve.Using water good dedusting effect, the bottom of tank is the concentration of taper surface, beneficially mud, it is simple to discharge.
Further, preserve pipe and be provided with the container of fusiformis.It is easy to store more mud, improves the effect discharging mud；
Use fusiformis can reduce resistance when mud flows.
Further, body is cylindrical, and air inlet is arranged on the lower end, lateral wall of body, and gas outlet is arranged on the upper of body
End face, the gas collection end of connecting tube is connected with dust gathering arrester, and dust gathering arrester is towards blanking port.
Further, this internal cavity being provided with opening upwards, water deduster includes collection slurry pipe and the water being arranged in cavity；
Collection slurry pipe is arranged on the bottom of body and communicates with cavity, and the upper and lower of collection slurry pipe is equipped with a plasma discharge valve, gives vent to anger
Pipe leads in water.Body is provided with the cavity for being filled with water, and can play with the effect of Water warfare air, be equivalent to following of gas
Loop device is wholely set with the purifier of gas, makes overall structure be reduced, saves work space, has saved and be manufactured into
This.
Further, the bottom angled of cavity is arranged, and collection slurry pipe is arranged on the minimum point of body bottom portion.Incline in the bottom of tank
Tiltedly, the concentration of beneficially mud, it is simple to the discharge of mud.
Compared with prior art the invention have the advantage that
1, the present invention is provided with dust arrester and water deduster；Dust arrester is provided with spiral passage, and the inwall of passage is arranged
Showing dust discharge road, dust rises at passage internal coiling, and under the influence of centrifugal force, the dust granule that density is bigger than air can be got rid of
On the sidewall of passage, under the effect of sidewall friction resistance, dust falls in the bottom of passage, and dust slowly moves along bottom
During to dust discharge road, dust falls in dust discharge road, falls into the dust in dust discharge road, can be in dust flue falls into dust collecting trough, ash-laden gas
Body processes through multiple dust discharge roads, is purified.
2, dusty gas is circulated up flowing along passage, dust can be made from lower end to enter dust discharge road, can flow smoothly
Enter dust discharge road；If flowed downward, then dust crosses dust discharge road under wind-force effect, thus reduces the effect of dedusting.
3, the dust collection in dust collecting trough can be utilized, provide cost savings.
4, using hydrotreater air less to dustiness to process further, water makes air be fully purified, and reduces
The consumption of water.
5, use air-introduced machine to absorb dust, improve the circulation rate of air so as to get absorb in time, it is to avoid dust flows to
Air.
Accompanying drawing explanation
The invention will be further described below in conjunction with the accompanying drawings:
Fig. 1 is the structural representation of the present invention in embodiment one；
Fig. 2 is the structural representation of dust arrester in embodiment one；
Fig. 3 is the structural representation of the present invention in embodiment two；
Fig. 4 is the structural representation of dust arrester in embodiment two.
Detailed description of the invention
Embodiment one:
Refering to Fig. 1, pyrophillite crushing system dust arrester, including dust arrester, escape pipe 2, air-introduced machine 4 and water dedusting
Device, air-introduced machine 4 is arranged on escape pipe 2.
Refering to Fig. 1 and Fig. 2, dust arrester includes that body 11, dust collecting trough 16 and connecting tube 15, body 11 are up-small and down-big loudspeaker
Shape, is provided with the spiral passage 12 of cone, is arranged with the dust discharge road communicated with passage 12 bottom the inwall of passage 12 in body 11
13, lower end, each dust discharge road 13 is all connected with dust flue 14, and every dust flue 14 lower end is all connected with dust collecting trough 16, dust collecting trough 16 ring
It is wound on the lateral wall of body 11 lower end.
Refering to Fig. 1, water deduster includes tank 34 and preserves pipe 35, and the bottom surface of tank 34 is up big and down small taper
Face, preserves pipe 35 and is connected to the minimum point of tank 34 bottom surface, preserves the upper and lower of pipe 35 and is equipped with one and preserves pipe valve
Door 36；In order to increase the capacity preserving pipe 35, preserving the container 37 that a fusiformis is set on pipe 35.
The upper end, lateral wall of body 11 is provided with the air inlet of passage 12, and the lower end, lateral wall of body 11 is provided with going out of passage 12
QI KOU, connecting tube 15 two ends are respectively gas transmission end and for absorbing the gas collection end of dust, and body 11 lower end, towards blanking port, connects
The gas transmission end of pipe 15 is connected with the air inlet of passage 12, and the gas collection end of connecting tube 15 is sealedly connected on the upper end of body 11, i.e.
Connecting tube 15 passes through body 11 towards blanking port；One end of escape pipe 2 is connected with the gas outlet of passage 12, another of escape pipe 2
End leads in tank 34.
During work, making body 11 be directed at blanking port, start air-introduced machine 4, the air of band dust is entered by body 11 and connects
Pipe 15, enters passage 12 by connecting tube 15, and dust rises at passage 12 internal coiling, and under the influence of centrifugal force, density is than sky
The dust granule that gas is big can be thrown on the sidewall of passage 12, and under the effect of sidewall friction resistance, dust falls at passage 12
Bottom, when dust slowly moves to dust discharge road 13 along bottom, dust falls in dust discharge road 13, falls into the dust in dust discharge road 13,
Can be in dust flue 14 fall into dust collecting trough 16, the air after passage 12 dedusting for the first time is entered by the gas outlet of passage 12
Entering escape pipe 2, enter in tank 34 by escape pipe 2, gas obtains dust-free air through the process of water, the dust in gas
It is only absorbed by the water, when dust reaches a certain amount in water, mud can be formed, be deposited in bottom of gullet, when mud reaches certain
During amount, open preserve pipe 35 top preserve tube valve 36, make mud enter into and preserve in pipe 35, in preserving pipe 35, fill up silt
During mud, close preserve pipe 35 top preserve tube valve 36, open preserve pipe 35 bottom preserve tube valve 36, thus by mud
Discharge.
In the present embodiment, in order to be taken out by the dust in dust collecting trough 16, it is provided with multiple dust discharge in the bottom of dust collecting trough 16
Valve.
Embodiment two:
Refering to Fig. 3 and Fig. 4, pyrophillite crushing system dust arrester, remove including dust arrester, escape pipe 2, air-introduced machine 4, water
Dirt device and dust gathering arrester 5, air-introduced machine 4 is arranged on escape pipe 2；
Refering to Fig. 3 and Fig. 4, dust arrester includes body 11, dust collecting trough 16 and connecting tube 15, and body 11 is for cylinder and offers
There is the cavity 111 of opening upwards, be provided with the passage 12 of cylindrical screw shape in body 11, the inwall of passage 12 is arranged with and passage
The dust discharge road 13 that 12 communicate, lower end, each dust discharge road 13 is all connected with dust flue 14, every dust flue 14 lower end all with dust collecting trough 16
Being connected, dust collecting trough 16 is looped around on the lateral wall of body 11 lower end；
Refering to Fig. 3, passage 12 is provided with air inlet and gas outlet, and air inlet is arranged on the lower end, lateral wall of body 11, gives vent to anger
Mouth is arranged on the upper end of body 11；Connecting tube 15 two ends are respectively gas transmission end and for absorbing the gas collection end of dust, connecting tube 15
Gas transmission end be connected with the air inlet of passage 12, the gas collection end of connecting tube 15 is connected with dust gathering arrester 5, and connecting tube 15 passes through dust gathering arrester
5 towards blanking port.
Refering to Fig. 3, water deduster includes collection slurry pipe 31 and the water 32 being arranged in cavity 111；Collection slurry pipe 31 is arranged on this
The bottom of body 11 and communicating with cavity 111, the upper and lower of collection slurry pipe 31 is equipped with a plasma discharge valve 33；Cavity 111
Bottom angled is arranged, and collection slurry pipe 31 is arranged on the minimum point bottom body 11.
Escape pipe 2 one end is connected with the gas outlet of passage 12, and the other end of escape pipe 2 leads in water 32.
During work, making dust gathering arrester 5 be directed at blanking port, start air-introduced machine 4, the air of band dust is entered even by dust gathering arrester 5
Adapter 15, enters passage 12 by connecting tube 15, and dust rises at passage 12 internal coiling, under the influence of centrifugal force, and density ratio
The dust granule that air is big can be thrown on the sidewall of passage 12, and under the effect of sidewall friction resistance, dust falls at passage 12
Bottom, when dust slowly moves the entrance to dust discharge road 13 along bottom, dust falls in dust discharge road 13, falls into dust discharge road 13
Dust, can be in dust flue 14 falls into dust collecting trough 16, the air after passage 12 for the first time dedusting is by passage 12
Gas outlet enters escape pipe 2, enters in water 32 by escape pipe 2, and gas obtains dust-free air, in gas through the process of water
Dust be only absorbed by the water, when dust reaches a certain amount in water, mud can be formed, be deposited in bottom of gullet, when mud reaches
To time a certain amount of, open the plasma discharge valve 33 on collection slurry pipe 31 top, make mud enter in collection slurry pipe 31, when filling out in collection slurry pipe 31
During full mud, close the plasma discharge valve 33 on closed set slurry pipe 31 top, open the plasma discharge valve 33 of collection slurry pipe 31 bottom, thus by mud
Discharge.
In the present embodiment, in order to be taken out by the dust in dust collecting trough 16, it is provided with multiple dust discharge in the bottom of dust collecting trough 16
Valve.Air-introduced machine 4 is fixed on the upper end of body 11.
Blanking port in above-mentioned two embodiment refers to pyrophillite and drops into the position of disintegrating machine, it is also possible to replace with brokenly
The charging aperture of broken machine, the most alternative above-mentioned blanking port in position of a large amount of dust of i.e. emerging in shattering process.
The present invention is not only applicable to the broken of pyrophillite, and the broken of other Ore is also contained in protection scope of the present invention
Within.
These are only the specific embodiment of the present invention, but the technical characteristic of the present invention is not limited thereto, any this area
Technical staff in the field of the invention, made change or modify all contain among the scope of the claims of the present invention.
Claims (7)
1. pyrophillite crushing system dust arrester, is characterized in that: include that dust arrester, escape pipe (2), air-introduced machine (4) and water remove
Dirt device, described escape pipe (2) is connected between water deduster and dust arrester, and air-introduced machine (4) is arranged on escape pipe (2)；
Described dust arrester includes body (11), dust collecting trough (16) and connecting tube (15), and body is provided with spiral passage in (11)
(12), being arranged with the dust discharge road (13) communicated with passage (12) bottom the inwall of passage (12), each dust discharge road (13) lower end is equal
Being connected with dust flue (14), every dust flue (14) lower end is all connected with dust collecting trough (16), and dust collecting trough (16) is looped around body (11)
On the lateral wall of lower end；
Passage (12) is provided with air inlet and gas outlet, and connecting tube (15) two ends are respectively gas transmission end and for absorbing the gas collection of dust
End, the gas transmission end of connecting tube (15) is connected with the air inlet of passage (12), and the gas collection end of connecting tube (15) is towards blanking port, logical
The gas outlet in road (12) is connected with escape pipe (2).
Pyrophillite crushing system dust arrester the most according to claim 1, is characterized in that: described body (11) is upper little
The biggest is tubaeform, and passage (12) is cone spiral type, and body lower end is tightly connected towards blanking port, the gas collection end of described connecting tube
In body (11) upper end；The gas outlet of passage (12) is arranged on the upper end, lateral wall of body (11), and air inlet is arranged on body
(11) lower end, lateral wall.
Pyrophillite crushing system dust arrester the most according to claim 1 and 2, is characterized in that: described water deduster bag
Including tank (34) and preserve pipe (35), escape pipe (2) leads in tank (34), and the bottom surface of tank (34) is up big and down small cone
Shape face, preserves pipe (35) and is connected to the minimum point of tank (34) bottom surface, and the upper and lower preserving pipe (35) is equipped with one
Preserve tube valve (36).
Pyrophillite crushing system dust arrester the most according to claim 3, is characterized in that: described in preserve and set on pipe (35)
There is the container (37) of fusiformis.
Pyrophillite crushing system dust arrester the most according to claim 1, is characterized in that: described body (11) is cylinder
Shape, air inlet is arranged on the lower end, lateral wall of body (11), and gas outlet is arranged on the upper surface of body (11), described connecting tube
(15) gas collection end is connected with dust gathering arrester (5), and dust gathering arrester (5) is towards blanking port.
Pyrophillite crushing system dust arrester the most according to claim 5, is characterized in that: described body is provided with in (11)
The cavity (111) of opening upwards, described water deduster includes collection slurry pipe (31) and the water (32) being arranged in cavity (111)；Collection
Slurry pipe (31) is arranged on the bottom of body (11) and communicates with cavity (111), and the upper and lower of collection slurry pipe (31) is equipped with one
Individual plasma discharge valve (33), escape pipe (2) leads in water (32).
Pyrophillite crushing system dust arrester the most according to claim 6, is characterized in that: the end of described cavity (111)
Portion is obliquely installed, and collection slurry pipe (31) is arranged on the minimum point of body (11) bottom.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610665735.5A CN106139804B (en) | 2016-08-12 | 2016-08-12 | Pyrophillite crushing system dust-extraction unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610665735.5A CN106139804B (en) | 2016-08-12 | 2016-08-12 | Pyrophillite crushing system dust-extraction unit |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106139804A true CN106139804A (en) | 2016-11-23 |
| CN106139804B CN106139804B (en) | 2019-10-25 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610665735.5A Active CN106139804B (en) | 2016-08-12 | 2016-08-12 | Pyrophillite crushing system dust-extraction unit |
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Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100629438B1 (en) * | 2004-12-22 | 2006-09-27 | 성안산업개발 주식회사 | Dsut collector system for sand and gravel manufacture |
| CN101391165A (en) * | 2008-10-22 | 2009-03-25 | 广州大学 | Spiral type gas-solid separation device |
| CN204208424U (en) * | 2014-10-15 | 2015-03-18 | 林慧敏 | High effect dust cleaner |
| CN204933068U (en) * | 2015-08-14 | 2016-01-06 | 重庆市青蓝机械制造有限公司 | Smoke eliminating equipment |
| CN205850515U (en) * | 2016-08-12 | 2017-01-04 | 温州统利机械科技有限公司 | A kind of pyrophillite crushing system dust arrester |
-
2016
- 2016-08-12 CN CN201610665735.5A patent/CN106139804B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100629438B1 (en) * | 2004-12-22 | 2006-09-27 | 성안산업개발 주식회사 | Dsut collector system for sand and gravel manufacture |
| CN101391165A (en) * | 2008-10-22 | 2009-03-25 | 广州大学 | Spiral type gas-solid separation device |
| CN204208424U (en) * | 2014-10-15 | 2015-03-18 | 林慧敏 | High effect dust cleaner |
| CN204933068U (en) * | 2015-08-14 | 2016-01-06 | 重庆市青蓝机械制造有限公司 | Smoke eliminating equipment |
| CN205850515U (en) * | 2016-08-12 | 2017-01-04 | 温州统利机械科技有限公司 | A kind of pyrophillite crushing system dust arrester |
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| Publication number | Publication date |
|---|---|
| CN106139804B (en) | 2019-10-25 |
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Effective date of registration: 20190930 Address after: 317299 Fuxing Lane 5-2, Fuxi Street, Tiantai County, Taizhou City, Zhejiang Province Applicant after: Fan Dong Ting Address before: 325024 coastal Zhejiang Province Economic Development Zone Wenzhou city two Road No. 944 building 7 Room 405 Ruifeng Jinyuan East first Applicant before: Wenzhou Tongli Machinery Technology Co., Ltd. |
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Effective date of registration: 20200512 Address after: 422000 Jianghu neighborhood committee, Wuyi North Road, Shuangqing District, Shaoyang City, Hunan Province (original city food factory) Patentee after: Shaoyang Dongsheng Superhard Material Co., Ltd Address before: 317299 Fuxing Lane 5-2, Fuxi Street, Tiantai County, Taizhou City, Zhejiang Province Patentee before: Fan Dongting |