CN205461575U - Dust recovery plant - Google Patents

Dust recovery plant Download PDF

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Publication number
CN205461575U
CN205461575U CN201620072785.8U CN201620072785U CN205461575U CN 205461575 U CN205461575 U CN 205461575U CN 201620072785 U CN201620072785 U CN 201620072785U CN 205461575 U CN205461575 U CN 205461575U
Authority
CN
China
Prior art keywords
cylindrical shell
cyclone
separator
dust
micropowder
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
Application number
CN201620072785.8U
Other languages
Chinese (zh)
Inventor
胡杰
徐海荣
王强
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Deqing Zhejiang Mei Shile Pigment Science And Technology Ltd
Original Assignee
Deqing Zhejiang Mei Shile Pigment Science And Technology Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Deqing Zhejiang Mei Shile Pigment Science And Technology Ltd filed Critical Deqing Zhejiang Mei Shile Pigment Science And Technology Ltd
Priority to CN201620072785.8U priority Critical patent/CN205461575U/en
Application granted granted Critical
Publication of CN205461575U publication Critical patent/CN205461575U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model relates to a dust recovery plant belongs to pigment production technical field. A dust recovery plant, includes consecutive primary cyclone, secondary cyclone, tertiary cyclone, terminal filtering separator and air extraction equipment. This dust recovery plant can retrieve the pigment dust of collecting in order to be applicable to different pigment processing in grades.

Description

A kind of dust reclaimer
Technical field
This utility model relates to pigment production technical field, is 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.
Utility model content
The purpose of this utility model, is to solve the problems referred to above, it is provided that a kind of pigment in dusty gas carries out classification the dust reclaimer reclaimed completely.
The technical scheme that this utility model solves the problems referred to above is as follows:
A kind of dust reclaimer, including the primary cyclone being sequentially connected, secondary cyclone, three-stage cyclone separator, end-filtration separator and air-extractor, described primary cyclone, described secondary cyclone and described three-stage cyclone separator by cylindrical shell, be positioned at described cylindrical shell top the air inlet being tangentially connected with described cylindrical shell, two ends lay respectively at that described cylindrical shell is internal and the outlet pipe on top and aggregate bin are constituted;Described primary cyclone, described secondary cyclone, the internal diameter of cylindrical shell of described three-stage cyclone separator increase successively, increase the most 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 uses 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 micropowder catcher.
Preferred as technique scheme, the internal diameter of the cylindrical shell of described primary cyclone, described secondary cyclone and described three-stage cyclone separator is respectively 20cm, 50cm and 125cm;Accordingly, the height of the cylindrical shell of described primary cyclone, described secondary cyclone and described three-stage cyclone separator is respectively 50cm, 110cm and 235cm.
Preferred as technique scheme, described micropowder catcher is internally provided with micropowder collecting chamber, is provided with collection liquid in described micropowder collecting chamber.
Preferred as technique scheme, is provided with tapered portion, described tapered portion is provided with device for discharging between described aggregate bin and described cylindrical shell.
Preferred as technique scheme, described device for discharging includes the star dump skip on top and is positioned at the valve below described star dump skip.
Preferred as technique scheme, is provided with fan in described tapered portion, described fan makes air-flow flow downward when rotating.
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 includes vibration motor and the vibrating plate of described concussion driven by motor, and described vibrating plate crosses described tapered portion.
When described primary cyclone, described secondary cyclone and described three-stage cyclone separator inner accumulated have granules of pigments to be difficult to, open vibration motor and drive oscillator plate vibrations or mobile, drive or rub the vibrations of described tapered portion, the granules of pigments being difficult to drop is shaken off, plays the effect cleaning described cyclone separator.
In sum, this utility model has the advantage that
The pigment dust classification collected can be reclaimed to be applicable to different pigment processing by a kind of dust reclaimer described in the utility model.
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-micropowder catcher, 411-micropowder collecting chamber, 5-recoil gas circuit, 51-air compressor machine, 52-pressurized tank, 53-electromagnetic valve, a-cylindrical shell, b-air inlet, c-outlet pipe, d-aggregate bin, e-tapered portion, e1-fan.
Detailed description of the invention
Technical scheme in this utility model embodiment will be clearly and completely described below, it is clear that described embodiment is only a part of embodiment of this utility model rather than whole embodiments.Embodiment in this utility model, all other embodiments that those of ordinary skill in the art are obtained under not doing creative work premise, broadly fall into the scope of this utility model protection.
With embodiment, this utility model is described in detail below in conjunction with the accompanying drawings.
Embodiment 1: a kind of dust reclaimer, including the primary cyclone 1 being sequentially connected, 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 by cylindrical shell a, be positioned at described cylindrical shell a top the air inlet b being tangentially connected with described cylindrical shell a, two ends lay respectively at described cylindrical shell a internal and top outlet pipe c and aggregate bin d and are constituted;Described primary cyclone 1, described secondary cyclone 2, the internal diameter of cylindrical shell a of described three-stage cyclone separator 3 increase successively, respectively 10cm, 35cm, 75cm;Increase the most successively, respectively 20cm, 50cm, 100cm;Described end-filtration separator 4 uses 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 micropowder catcher 41.
Described micropowder catcher 41 is internally provided with micropowder collecting chamber 411, is provided with collection liquid in described micropowder collecting chamber 411.
It is provided with tapered portion e between described aggregate bin d and described cylindrical shell a, it is provided with device for discharging in described tapered portion e, described device for discharging includes the star dump skip on top and is positioned at the valve below described star dump skip, fan e1 it is additionally 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 includes air compressor machine 51, pressurized tank 52 and the electromagnetic valve 53 being sequentially connected.
Embodiment 2: a kind of dust reclaimer, including the primary cyclone 1 being sequentially connected, 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 by cylindrical shell a, be positioned at described cylindrical shell a top the air inlet b being tangentially connected with described cylindrical shell a, two ends lay respectively at described cylindrical shell a internal and top outlet pipe c and aggregate bin d and are constituted;Described primary cyclone 1, described secondary cyclone 2, the internal diameter of cylindrical shell a of described three-stage cyclone separator 3 increase successively, respectively 50cm, 100cm, 200cm;Increase the most successively, respectively 100cm, 180cm, 275cm;Described end-filtration separator 4 uses 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 micropowder catcher 41.
Described micropowder catcher 41 is internally provided with micropowder collecting chamber 411, is provided with collection liquid in described micropowder collecting chamber 411.
It is provided with tapered portion e between described aggregate bin d and described cylindrical shell a, it is provided with device for discharging in described tapered portion e, described device for discharging includes the star dump skip on top and is positioned at the valve below described star dump skip, fan e1 it is additionally 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 includes air compressor machine 51, pressurized tank 52 and the electromagnetic valve 53 being sequentially connected.
Embodiment 3: a kind of dust reclaimer, including the primary cyclone 1 being sequentially connected, 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 by cylindrical shell a, be positioned at described cylindrical shell a top the air inlet b being tangentially connected with described cylindrical shell a, two ends lay respectively at described cylindrical shell a internal and top outlet pipe c and aggregate bin d and are constituted;Described primary cyclone 1, described secondary cyclone 2, the internal diameter of cylindrical shell a of described three-stage cyclone separator 3 increase successively, respectively 20cm, 50cm, 125cm;Increase the most successively, respectively 50cm, 110cm, 235cm;Described end-filtration separator 4 uses 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 micropowder catcher 41.
Described micropowder catcher 41 is internally provided with micropowder collecting chamber 411, is provided with collection liquid in described micropowder collecting chamber 411.
It is provided with tapered portion e between described aggregate bin d and described cylindrical shell a, it is provided with device for discharging in described tapered portion e, described device for discharging includes the star dump skip on top and is positioned at the valve below described star dump skip, fan e1 it is additionally 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 includes air compressor machine 51, pressurized tank 52 and the electromagnetic valve 53 being sequentially connected.

Claims (8)

1. a dust reclaimer, it is characterized in that: include the primary cyclone (1) being sequentially connected, 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), it is positioned at described cylindrical shell (a) top the air inlet (b) being tangentially connected with described cylindrical shell (a), two ends lay respectively at described cylindrical shell (a) inside and the outlet pipe (c) on top and aggregate bin (d) is constituted;Described primary cyclone (1), described secondary cyclone (2), the internal diameter of cylindrical shell (a) of described three-stage cyclone separator (3) increase successively, increase the most 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) uses 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 micropowder catcher (41).
A kind of dust reclaimer the most according to claim 1, it is characterised in that: the internal diameter of the cylindrical shell (a) of described primary cyclone (1), described secondary cyclone (2) and described three-stage cyclone separator (3) is respectively 20cm, 50cm and 125cm;Accordingly, the height of the cylindrical shell (a) of described primary cyclone (1), described secondary cyclone (2) and described three-stage cyclone separator (3) is respectively 50cm, 110cm and 235cm.
A kind of dust reclaimer the most according to claim 1, it is characterised in that: described micropowder catcher (41) is internally provided with micropowder collecting chamber (411), is provided with collection liquid in described micropowder collecting chamber (411).
A kind of dust reclaimer the most according to claim 1, it is characterised in that: it is 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.
A kind of dust reclaimer the most according to claim 4, it is characterised in that: described device for discharging includes the star dump skip on top and is positioned at the valve below described star dump skip.
A kind of dust reclaimer the most according to claim 4, it is characterised in that: being provided with fan (e1) in described tapered portion (e), described fan (e1) makes air-flow flow downward when rotating.
A kind of dust reclaimer the most according to claim 6, it is characterised in that: it is provided with absorption fine hair on the flabellum of described fan (e1).
A kind of dust reclaimer the most according to claim 1, it is characterised in that: described recoil gas circuit (5) includes air compressor machine (51), pressurized tank (52) and the electromagnetic valve (53) being sequentially connected.
CN201620072785.8U 2016-01-26 2016-01-26 Dust recovery plant Expired - Fee Related CN205461575U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620072785.8U CN205461575U (en) 2016-01-26 2016-01-26 Dust recovery plant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620072785.8U CN205461575U (en) 2016-01-26 2016-01-26 Dust recovery plant

Publications (1)

Publication Number Publication Date
CN205461575U true CN205461575U (en) 2016-08-17

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Family Applications (1)

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CN201620072785.8U Expired - Fee Related CN205461575U (en) 2016-01-26 2016-01-26 Dust recovery plant

Country Status (1)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105477971A (en) * 2016-01-26 2016-04-13 浙江德清美史乐颜料科技有限公司 Dust recovery equipment

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105477971A (en) * 2016-01-26 2016-04-13 浙江德清美史乐颜料科技有限公司 Dust recovery equipment

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C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20160817

Termination date: 20220126