CN105477971A - Dust recovery equipment - Google Patents
Dust recovery equipment Download PDFInfo
- Publication number
- CN105477971A CN105477971A CN201610050163.XA CN201610050163A CN105477971A CN 105477971 A CN105477971 A CN 105477971A CN 201610050163 A CN201610050163 A CN 201610050163A CN 105477971 A CN105477971 A CN 105477971A
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- China
- Prior art keywords
- cylindrical shell
- cyclone
- separator
- cyclone separator
- micro mist
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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
- B01D50/20—Combinations of devices covered by groups B01D45/00 and B01D46/00
Abstract
The invention relates to dust recovery equipment, and belongs to the technical field of pigment production. The dust recovery equipment comprises a first-stage cyclone separator, a second-stage cyclone separator, a third-stage cyclone separator, a terminal filter separator and exhaust equipment which are connected in sequence. The dust recovery equipment can recycle collected pigment dust in a classified mode to be suitable for processing different pigments.
Description
Technical field
The present invention relates to pigment production technical field, be specifically related to a kind of dust reclaimer.
Background technology
In pigment manufacturing process, can produce pigment dust, one pollutes production environment, and two cause part pigment to waste, need a kind of can the retracting device of effective recycling pigment dust.
Summary of the invention
Object of the present invention is to solve the problem, and provides a kind of and carries out classification and the dust reclaimer reclaimed completely to the pigment in dusty gas.
The technical scheme that the present invention solves the problem is as follows:
A kind of dust reclaimer, comprise the primary cyclone, secondary cyclone, three-stage cyclone separator, end-filtration separator and the air-extractor that are connected successively, described primary cyclone, described secondary cyclone and described three-stage cyclone separator by cylindrical shell, be positioned at described cylindrical shell top and the air inlet be tangentially connected with described cylindrical shell, two ends lay respectively at the outlet pipe on the inner and top of described cylindrical shell and aggregate bin formed; The internal diameter of the cylindrical shell of described primary cyclone, described secondary cyclone, described three-stage cyclone separator increases successively, increases highly successively; The internal diameter of the cylindrical shell of described primary cyclone is 10-50cm, and the internal diameter of the cylindrical shell of described secondary cyclone is 35-100cm, and the internal diameter of the cylindrical shell of described three-stage cyclone separator is 75-200cm; The height of the cylindrical shell of described primary cyclone is 20-100cm, and the height of the cylindrical shell of described primary cyclone is 50-180cm, and the height of the cylindrical shell of described primary cyclone is 100-275cm; Described end-filtration separator adopts HEPA to be filter medium, and described end-filtration separator is outside equipped with recoil gas circuit, and described end-filtration separator lower end is provided with micro mist collector.
Preferred as technique scheme, the internal diameter of the cylindrical shell of described first cyclone separator, described second cyclone separator and described 3rd cyclone separator is respectively 20cm, 50cm and 125cm; Accordingly, the height of the cylindrical shell of described first cyclone separator, described second cyclone separator and described 3rd cyclone separator is respectively 50cm, 110cm and 235cm.
Preferred as technique scheme, described micro mist collector inside is provided with micro mist collecting chamber, is provided with collection liquid in described micro mist collecting chamber.
Preferred as technique scheme, is provided with tapered portion between described aggregate bin and described cylindrical shell, described tapered portion is provided with device for discharging.
Preferred as technique scheme, the star dump skip that described device for discharging comprises top and the valve be positioned at below described star dump skip.
Preferred as technique scheme, is provided with fan in described tapered portion, makes air-flow flow downward during described fan turns.
Preferred as technique scheme, the flabellum of described fan is provided with absorption fine hair.
Preferred as technique scheme, described tapered portion is provided with oscillation device, and described oscillation device comprises the vibrating plate of vibration motor and described concussion driven by motor, and described vibrating plate crosses described tapered portion.
When described first cyclone separator, described second cyclone separator and described 3rd cyclone separator inner accumulated have granules of pigments not easily to fall, open vibration motor and drive oscillator plate vibrations or mobile, drive or rub the vibrations of described tapered portion, the granules of pigments not easily dropped is shaken off, plays the effect of clean described cyclone separator.
In sum, tool of the present invention has the following advantages:
The pigment dust classification of collecting can be reclaimed to be applicable to different pigment processing by a kind of dust reclaimer of the present invention.
Accompanying drawing explanation
Fig. 1 is a kind of dust reclaimer structural representation;
Fig. 2 is the A district enlarged drawing of Fig. 1;
In figure, 1-primary cyclone, 2-secondary cyclone, 3-three-stage cyclone separator, 4-end-filtration separator, 41-micro mist collector, 411-micro mist collecting chamber, 5-recoil gas circuit, 51-air compressor machine, 52-pressurized tank, 53-magnetic valve, a-cylindrical shell, b-air inlet, c-outlet pipe, d-aggregate bin, e-tapered portion, e1-fan.
Detailed description of the invention
Be clearly and completely described to the technical scheme in the embodiment of the present invention below, obviously, described embodiment is only the present invention's part embodiment, instead of whole embodiments.Embodiment in the present invention, those of ordinary skill in the art, not doing other embodiments all obtained under creative work prerequisite, belong to the scope of protection of the invention.
Below in conjunction with accompanying drawing, with embodiment, the present invention is described in detail.
Embodiment 1: a kind of dust reclaimer, comprise the primary cyclone 1, secondary cyclone 2, three-stage cyclone separator 3, end-filtration separator 4 and the air-extractor that are connected successively, described primary cyclone 1, described secondary cyclone 2 and described three-stage cyclone separator 3 by cylindrical shell a, be positioned at described cylindrical shell a top and the air inlet b be tangentially connected with described cylindrical shell a, two ends lay respectively at the outlet pipe c on the inner and top of described cylindrical shell a and aggregate bin d formed; The internal diameter of the cylindrical shell a of described primary cyclone 1, described secondary cyclone 2, described three-stage cyclone separator 3 increases successively, is respectively 10cm, 35cm, 75cm; Increase highly successively, be respectively 20cm, 50cm, 100cm; Described end-filtration separator 4 adopts HEPA to be filter medium, and described end-filtration separator 4 is outside equipped with recoil gas circuit 5, and described end-filtration separator 4 lower end is provided with micro mist collector 41.
Described micro mist collector 41 inside is provided with micro mist collecting chamber 411, is provided with collection liquid in described micro mist collecting chamber 411.
Tapered portion e is provided with between described aggregate bin d and described cylindrical shell a, described tapered portion e is provided with device for discharging, the star dump skip that described device for discharging comprises top and the valve be positioned at below described star dump skip, fan e1 is also provided with in described tapered portion e, described fan e1 makes air-flow flow downward when rotating, and the flabellum of described fan e1 is provided with absorption fine hair.
Described recoil gas circuit 5 comprises the air compressor machine 51, pressurized tank 52 and the magnetic valve 53 that are connected successively.
Embodiment 2: a kind of dust reclaimer, comprise the primary cyclone 1, secondary cyclone 2, three-stage cyclone separator 3, end-filtration separator 4 and the air-extractor that are connected successively, described primary cyclone 1, described secondary cyclone 2 and described three-stage cyclone separator 3 by cylindrical shell a, be positioned at described cylindrical shell a top and the air inlet b be tangentially connected with described cylindrical shell a, two ends lay respectively at the outlet pipe c on the inner and top of described cylindrical shell a and aggregate bin d formed; The internal diameter of the cylindrical shell a of described primary cyclone 1, described secondary cyclone 2, described three-stage cyclone separator 3 increases successively, is respectively 50cm, 100cm, 200cm; Increase highly successively, be respectively 100cm, 180cm, 275cm; Described end-filtration separator 4 adopts HEPA to be filter medium, and described end-filtration separator 4 is outside equipped with recoil gas circuit 5, and described end-filtration separator 4 lower end is provided with micro mist collector 41.
Described micro mist collector 41 inside is provided with micro mist collecting chamber 411, is provided with collection liquid in described micro mist collecting chamber 411.
Tapered portion e is provided with between described aggregate bin d and described cylindrical shell a, described tapered portion e is provided with device for discharging, the star dump skip that described device for discharging comprises top and the valve be positioned at below described star dump skip, fan e1 is also provided with in described tapered portion e, described fan e1 makes air-flow flow downward when rotating, and the flabellum of described fan e1 is provided with absorption fine hair.
Described recoil gas circuit 5 comprises the air compressor machine 51, pressurized tank 52 and the magnetic valve 53 that are connected successively.
Embodiment 3: a kind of dust reclaimer, comprise the primary cyclone 1, secondary cyclone 2, three-stage cyclone separator 3, end-filtration separator 4 and the air-extractor that are connected successively, described primary cyclone 1, described secondary cyclone 2 and described three-stage cyclone separator 3 by cylindrical shell a, be positioned at described cylindrical shell a top and the air inlet b be tangentially connected with described cylindrical shell a, two ends lay respectively at the outlet pipe c on the inner and top of described cylindrical shell a and aggregate bin d formed; The internal diameter of the cylindrical shell a of described primary cyclone 1, described secondary cyclone 2, described three-stage cyclone separator 3 increases successively, is respectively 20cm, 50cm, 125cm; Increase highly successively, be respectively 50cm, 110cm, 235cm; Described end-filtration separator 4 adopts HEPA to be filter medium, and described end-filtration separator 4 is outside equipped with recoil gas circuit 5, and described end-filtration separator 4 lower end is provided with micro mist collector 41.
Described micro mist collector 41 inside is provided with micro mist collecting chamber 411, is provided with collection liquid in described micro mist collecting chamber 411.
Tapered portion e is provided with between described aggregate bin d and described cylindrical shell a, described tapered portion e is provided with device for discharging, the star dump skip that described device for discharging comprises top and the valve be positioned at below described star dump skip, fan e1 is also provided with in described tapered portion e, described fan e1 makes air-flow flow downward when rotating, and the flabellum of described fan e1 is provided with absorption fine hair.
Described recoil gas circuit 5 comprises the air compressor machine 51, pressurized tank 52 and the magnetic valve 53 that are connected successively.
Claims (8)
1. a dust reclaimer, it is characterized in that: comprise the primary cyclone (1) be connected successively, secondary cyclone (2), three-stage cyclone separator (3), end-filtration separator (4) and air-extractor, described primary cyclone (1), described secondary cyclone (2) and described three-stage cyclone separator (3) are by cylindrical shell (a), be positioned at described cylindrical shell (a) top and the air inlet (b) be tangentially connected with described cylindrical shell (a), two ends lay respectively at the outlet pipe (c) on the inner and top of described cylindrical shell (a) and aggregate bin (d) formed, the internal diameter of the cylindrical shell (a) of described primary cyclone (1), described secondary cyclone (2), described three-stage cyclone separator (3) increases successively, increases highly successively, the internal diameter of the cylindrical shell (a) of described primary cyclone (1) is 10-50cm, the internal diameter of the cylindrical shell (a) of described secondary cyclone (2) is 35-100cm, and the internal diameter of the cylindrical shell (a) of described three-stage cyclone separator (3) is 75-200cm, the height of the cylindrical shell (a) of described primary cyclone (1) is 20-100cm, the height of the cylindrical shell (a) of described secondary cyclone (2) is 50-180cm, and the height of the cylindrical shell (a) of described three-stage cyclone separator (3) is 100-275cm, described end-filtration separator (4) adopts HEPA to be filter medium, and described end-filtration separator (4) is outside equipped with recoil gas circuit (5), and described end-filtration separator (4) lower end is provided with micro mist collector (41).
2. a kind of dust reclaimer according to claim 1, is characterized in that: the internal diameter of the cylindrical shell (a) of described first cyclone separator (1), described second cyclone separator (2) and described 3rd cyclone separator (3) is respectively 20cm, 50cm and 125cm; Accordingly, the height of the cylindrical shell (a) of described first cyclone separator (1), described second cyclone separator (2) and described 3rd cyclone separator (3) is respectively 50cm, 110cm and 235cm.
3. a kind of dust reclaimer according to claim 1, is characterized in that: described micro mist collector (41) inside is provided with micro mist collecting chamber (411), is provided with collection liquid in described micro mist collecting chamber (411).
4. a kind of dust reclaimer according to claim 1, is characterized in that: be provided with tapered portion (e) between described aggregate bin (d) and described cylindrical shell (a), described tapered portion (e) is provided with device for discharging.
5. a kind of dust reclaimer according to claim 4, is characterized in that: the star dump skip that described device for discharging comprises top and the valve be positioned at below described star dump skip.
6. a kind of dust reclaimer according to claim 4, is characterized in that: be provided with fan (e1) in described tapered portion (e), when described fan (e1) rotates, air-flow is flowed downward.
7. a kind of dust reclaimer according to claim 6, is characterized in that: the flabellum of described fan (e1) is provided with absorption fine hair.
8. a kind of dust reclaimer according to claim 1, is characterized in that: described recoil gas circuit (5) comprises the air compressor machine (51), pressurized tank (52) and the magnetic valve (53) that are connected successively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610050163.XA CN105477971A (en) | 2016-01-26 | 2016-01-26 | Dust recovery equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610050163.XA CN105477971A (en) | 2016-01-26 | 2016-01-26 | Dust recovery equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105477971A true CN105477971A (en) | 2016-04-13 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610050163.XA Pending CN105477971A (en) | 2016-01-26 | 2016-01-26 | Dust recovery equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105477971A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106119943A (en) * | 2016-08-31 | 2016-11-16 | 扬中市宏飞镀业有限公司 | A kind of plating recycling equipment dust collection defecator |
| CN106191979A (en) * | 2016-08-31 | 2016-12-07 | 扬中市宏飞镀业有限公司 | A kind of plating recycling equipment |
| CN110997159A (en) * | 2017-08-10 | 2020-04-10 | 东丽工程株式会社 | Coating device and coating method |
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| DE2042744A1 (en) * | 1970-08-28 | 1972-03-02 | Polysius Ag | Process for dedusting hot gases |
| CN201073615Y (en) * | 2007-07-27 | 2008-06-18 | 潘劭华 | Double graininess segment high-efficiency superfine raymond mill |
| CN201179475Y (en) * | 2008-04-16 | 2009-01-14 | 昆明理工大学 | Centrifugal separation device for aluminium foil scrap papers with dry method |
| CN203342962U (en) * | 2013-06-07 | 2013-12-18 | 亚普汽车部件股份有限公司 | Dust removal system for ground materials |
| CN203750321U (en) * | 2014-03-24 | 2014-08-06 | 贵溪大三元实业（集团）股份有限公司 | Fume and dust collector |
| CN204503371U (en) * | 2015-03-18 | 2015-07-29 | 昆山青烽精细化工有限公司 | With the air-flow vortex flour mill that deduster duplex is gathered materials |
| CN204953154U (en) * | 2015-08-14 | 2016-01-13 | 木林森活性炭江苏有限公司 | Multistage whirlwind branch stone device of leaving away |
| CN205461575U (en) * | 2016-01-26 | 2016-08-17 | 浙江德清美史乐颜料科技有限公司 | Dust recovery plant |
-
2016
- 2016-01-26 CN CN201610050163.XA patent/CN105477971A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2042744A1 (en) * | 1970-08-28 | 1972-03-02 | Polysius Ag | Process for dedusting hot gases |
| CN201073615Y (en) * | 2007-07-27 | 2008-06-18 | 潘劭华 | Double graininess segment high-efficiency superfine raymond mill |
| CN201179475Y (en) * | 2008-04-16 | 2009-01-14 | 昆明理工大学 | Centrifugal separation device for aluminium foil scrap papers with dry method |
| CN203342962U (en) * | 2013-06-07 | 2013-12-18 | 亚普汽车部件股份有限公司 | Dust removal system for ground materials |
| CN203750321U (en) * | 2014-03-24 | 2014-08-06 | 贵溪大三元实业（集团）股份有限公司 | Fume and dust collector |
| CN204503371U (en) * | 2015-03-18 | 2015-07-29 | 昆山青烽精细化工有限公司 | With the air-flow vortex flour mill that deduster duplex is gathered materials |
| CN204953154U (en) * | 2015-08-14 | 2016-01-13 | 木林森活性炭江苏有限公司 | Multistage whirlwind branch stone device of leaving away |
| CN205461575U (en) * | 2016-01-26 | 2016-08-17 | 浙江德清美史乐颜料科技有限公司 | Dust recovery plant |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106119943A (en) * | 2016-08-31 | 2016-11-16 | 扬中市宏飞镀业有限公司 | A kind of plating recycling equipment dust collection defecator |
| CN106191979A (en) * | 2016-08-31 | 2016-12-07 | 扬中市宏飞镀业有限公司 | A kind of plating recycling equipment |
| CN106191979B (en) * | 2016-08-31 | 2019-03-29 | 扬中市宏飞镀业有限公司 | A kind of plating recycling equipment |
| CN110997159A (en) * | 2017-08-10 | 2020-04-10 | 东丽工程株式会社 | Coating device and coating method |
| CN110997159B (en) * | 2017-08-10 | 2022-05-03 | 东丽工程株式会社 | Coating device and coating method |
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| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20160413 |
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| RJ01 | Rejection of invention patent application after publication |