CN201524509U - Zincum powder dust collecting device - Google Patents
Zincum powder dust collecting device Download PDFInfo
- Publication number
- CN201524509U CN201524509U CN2009202170942U CN200920217094U CN201524509U CN 201524509 U CN201524509 U CN 201524509U CN 2009202170942 U CN2009202170942 U CN 2009202170942U CN 200920217094 U CN200920217094 U CN 200920217094U CN 201524509 U CN201524509 U CN 201524509U
- Authority
- CN
- China
- Prior art keywords
- air
- zinc powder
- cyclone separator
- sack cleaner
- powder dust
- 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 - Lifetime
Links
Images
Landscapes
- Cyclones (AREA)
Abstract
The utility model discloses a zincum powder dust collecting device with simple structure, high dust collecting efficiency and completely dedusting function. The zincum powder dust collecting device comprises an air intake pipe (1), a cyclone separator (3), a pocket type dust remover (5) and a draft fan (6); wherein the air intake pipe (1) is connected with upper and lower rows of suction openings (2); the air intake pipe (1) is communicated with the cyclone separator (3); the cyclone separator (3) is communicated with the pocket type dust remover (5) through an air flow pipe (4); and air flow outlet of the pocket type dust remover (5) is externally connected with the draft fan (6). The utility mode can realize two-stage dedusting, has high zincum powder collecting efficiency, recovers the originally lost zincum powder particles and benefits to worker health.
Description
Technical field
The utility model relates to a kind of equipment of eliminating dust, a kind of zinc powder dust arrester installation that is applied in zinc powder processing factory of saying so more specifically.
Background technology
The equipment of the existing particle separation in the technology has cyclone separator, hydrofilter, electrostatic precipitator and filtration dust catcher etc. usually at present.Usually the dust-laden thing of high concentration is generally taked the mode of multistage dedusting, the general form of all taking primary cyclone or multi-cyclone, perhaps affix sack cleaner, but this scheme, the long flow path of system, equipment is many, the operating cost height, and the floor space of whole system is bigger, is unfavorable for very much industrial production.
In existing zinc powder processing factory, because the thinner dust of zinc powder work in-process particle is easy to fly upward, cause the air ambient of workplace contaminated, the threat workman's is healthy, the a large amount of losses and the waste of zinc powder have also been caused, what employing was more at present is to utilize sack cleaner to collect zinc powder, but its efficient is not high, dedusting is not thorough, service life is not long yet, what take usually in the collecting device to the zinc powder dust is the flat bag dust collector of rotary counter-blowing, but this mode will be provided with a cover blowback wind system and a rotary system specially, and volume is big like this, the energy consumption height, maintenance and manufacturing expense are higher, and such gathering dust, the dust separation of middle granularity is not come out, and has strengthened the filtration load of filter bag, the requirement that does not reach large-scale processing factory required collection zinc powder equipment.
In the prior art, Chinese patent ZL00248215.0 " the flat bag compound type dust remover of efficient cyclone rotary counter-blowing " has disclosed the dust arrester of a kind of compound cyclone separator and sack cleaner, but the efficient of its cyclonic separation is not high, bigger dust is still filtered by filter bag, filter bag ash removal is frequent, service life is short, so and be not suitable for doing the dust arrester installation of field of metallurgy, in other Chinese patent ZL93217194.X, disclosed a kind of whirlwind bag dust collector, taked the mode of downflow type, elementary dedusting is arranged on the outside, and taked the mode of vibrating motor vibration cleaning, strengthened the effect of primary separation, but this equipment only is that the primary separation of dust is strengthened, and follow-up gathering dust do not had significant effect, in the seizure of metallurgy industry especially zinc powder is collected, be easy to miss gathering dust of intermediate grain, so this method collection efficiency is not high, dedusting is not thorough.
The utility model content
Technical problem to be solved in the utility model is to overcome the deficiencies in the prior art, provide a kind of simple in structure, collection efficiency is high, dedusting zinc powder dust arrester installation completely.
The technical scheme that the utility model adopted is: the utility model comprises blast pipe, cyclone separator, sack cleaner and air-introduced machine, described blast pipe is connected with the two rows inlet scoop, described blast pipe is communicated with described cyclone separator, described cyclone separator is communicated with described sack cleaner by gas flow tube, and the air stream outlet of described sack cleaner is circumscribed with air-introduced machine.
Described sack cleaner comprises air-purifying chamber and filter bag chamber, is provided with the porous card between described air-purifying chamber and the filter bag chamber, and described porous card is provided with the filter dirt cloth bag that several inlets are provided with Venturi tube; The winding-up pipe also is housed above described porous card, on the described winding-up pipe plurality of nozzles is arranged, described nozzle is corresponding with the filter dirt cloth bag of below.
Below described filter bag chamber, be provided with collection powder bucket.
Standard ash bucket type or unlimited flange form are adopted in described inlet scoop.
The beneficial effects of the utility model are: because the utility model comprises blast pipe, cyclone separator, sack cleaner and air-introduced machine, described blast pipe is connected with the two rows inlet scoop, described blast pipe is communicated with described cyclone separator, described cyclone separator is communicated with described sack cleaner by gas flow tube, the air stream outlet of described sack cleaner is circumscribed with air-introduced machine, the omnibearing absorption of energy has the dusty gas of zinc powder, the efficient height that purifies air, dusty gas is through cyclone separator and sack cleaner twice dedusting operation, and dedusting is more thorough; Because described sack cleaner comprises air-purifying chamber and filter bag chamber, is provided with the porous card between described air-purifying chamber and the filter bag chamber, described porous card is provided with the filter dirt cloth bag that several inlets are provided with Venturi tube; The winding-up pipe also is housed above described porous card, on the described winding-up pipe plurality of nozzles is arranged, described nozzle is corresponding with the filter dirt cloth bag of below, by the nozzle on the winding-up pipe zinc powder on the filter dirt cloth bag is come off, take off dirt efficient height, prolong the service life of sack cleaner, also improved the dust-collecting efficiency of zinc powder accordingly.
Description of drawings
With reference to respective drawings, in conjunction with preferred implementation, other purposes of the present utility model, details, feature and advantage will become more clear, and described embodiment only is exemplary introduction and unconfined intention, wherein:
Fig. 1 is a structural representation of the present utility model;
Fig. 2 is the structural representation of sack cleaner in the utility model.
The specific embodiment
As shown in Figure 1, the utility model comprises blast pipe 1, cyclone separator 3, sack cleaner 5 and air-introduced machine 6, described blast pipe 1 is connected with two rows inlet scoop 2, ash bucket or unlimited flange can be adopted in described inlet scoop 2, described blast pipe 1 is communicated with described cyclone separator 3, described cyclone separator 3 is communicated with described sack cleaner 5 by gas flow tube 4, the air stream outlet of described sack cleaner 5 is circumscribed with air-introduced machine 6, is provided with the ash bucket of collecting zinc powder below described sack cleaner 5 and cyclone separator 3; Under the effect of air-introduced machine 6, dust-laden (zinc powder) gas enters from several inlet scoops 2 on the working face, arrive cyclone separator 3 through blast pipe 1, carry out primary dust removing and collect zinc powder, the gas of handling continues to enter sack cleaner 5 by gas flow tube 4, realize two-stage dust removal, zinc powder is collected in the ash bucket of below.
As shown in Figure 2, above-mentioned sack cleaner 5 comprises air-purifying chamber 12 and filter bag chamber 8, be provided with porous card 13 between described air-purifying chamber 12 and the filter bag chamber 8, be provided with collection powder bucket 7 below described filter bag chamber 8, described porous card 13 is provided with the filter dirt cloth bag 9 that several inlets are provided with Venturi tube; Winding-up pipe 11 also is housed above described porous card 13, on the described winding-up pipe 11 plurality of nozzles 10 is arranged, described nozzle 10 is corresponding with the filter dirt cloth bag 9 of below.Dust-laden (zinc powder) gas enters filter bag chamber 8, and by filter dirt cloth bag 9, zinc powder is adsorbed on filter dirt cloth bag 9 surfaces, and purified gas enters air-purifying chamber 12, discharges through the outlet of air-introduced machine 6; Because it is more and more to be accumulated in the zinc powder on filter dirt cloth bag 9 surfaces, constantly increase, the resistance of deduster is constantly risen, at this moment need open impulse electromagnetic valve, high velocity air feeds winding-up pipe 11, because nozzle 10 is aimed at Venturi tube, high velocity air is through nozzle 10 ejections, filter dirt cloth bag 9 is expanded and vibration, the zinc powder on surface is shaken off down, be collected in the collection powder bucket 7.
Though in conjunction with specific embodiments the utility model has been done detailed description; but it is evident that; this does not constitute any limitation this; those of ordinary skill in the art can replace all technical equivalents things and their combinations according to the knowledge of being grasped, and these all fall within the scope of the utility model protection.
Claims (5)
1. zinc powder dust arrester installation, it is characterized in that: it comprises blast pipe (1), cyclone separator (3), sack cleaner (5) and air-introduced machine (6), described blast pipe (1) is connected with two rows inlet scoop (2), described blast pipe (1) is communicated with described cyclone separator (3), described cyclone separator (3) is communicated with described sack cleaner (5) by gas flow tube (4), and the air stream outlet of described sack cleaner (5) is circumscribed with air-introduced machine (6).
2. according to the described zinc powder dust arrester installation of claim 1, it is characterized in that: described sack cleaner (5) comprises air-purifying chamber (12) and filter bag chamber (8), be provided with porous card (13) between described air-purifying chamber (12) and filter bag chamber (8), described porous card (13) is provided with the filter dirt cloth bag (9) that several inlets are provided with Venturi tube; In the top of described porous card (13) winding-up pipe (11) is housed also, plurality of nozzles (10) is arranged on the described winding-up pipe (11), described nozzle (10) is corresponding with the filter dirt cloth bag (9) of below.
3. according to the described zinc powder dust arrester installation of claim 2, it is characterized in that: be provided with collection powder bucket (7) in the below of described filter bag chamber (8).
4. according to claim 1 or 2 or 3 arbitrary described zinc powder dust arrester installations, it is characterized in that: described inlet scoop (2) employing standard ash bucket type.
5. according to claim 1 or 2 or 3 arbitrary described zinc powder dust arrester installations, it is characterized in that: described inlet scoop (2) are adopted and are opened wide flange form.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009202170942U CN201524509U (en) | 2009-09-28 | 2009-09-28 | Zincum powder dust collecting device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009202170942U CN201524509U (en) | 2009-09-28 | 2009-09-28 | Zincum powder dust collecting device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201524509U true CN201524509U (en) | 2010-07-14 |
Family
ID=42515809
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009202170942U Expired - Lifetime CN201524509U (en) | 2009-09-28 | 2009-09-28 | Zincum powder dust collecting device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201524509U (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102935321A (en) * | 2012-11-30 | 2013-02-20 | 海宁洁宇环保设备有限公司 | Vacuum sweeping dust sucking device |
| CN104353318A (en) * | 2014-11-17 | 2015-02-18 | 浙江九川竹木有限公司 | Dust purification device and method |
| CN104552004A (en) * | 2014-12-19 | 2015-04-29 | 广西大学 | Fiberboard sanding dust recycling machine capable of automatically separating sand grains and recycling method |
| CN105598094A (en) * | 2016-02-26 | 2016-05-25 | 西安交通大学 | Water-free cleaning device for waste plastic film |
| CN105797492A (en) * | 2016-03-17 | 2016-07-27 | 北京展铭科技发展有限公司 | Dust removal and purification system |
| CN107198921A (en) * | 2016-03-17 | 2017-09-26 | 天津宝丽杰涂料有限公司 | A kind of powdery paints separates dust arrester |
| CN107262485A (en) * | 2017-05-15 | 2017-10-20 | 滁州亿扬零部件制造有限公司 | A kind of job shop dust arrester |
-
2009
- 2009-09-28 CN CN2009202170942U patent/CN201524509U/en not_active Expired - Lifetime
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102935321A (en) * | 2012-11-30 | 2013-02-20 | 海宁洁宇环保设备有限公司 | Vacuum sweeping dust sucking device |
| CN104353318A (en) * | 2014-11-17 | 2015-02-18 | 浙江九川竹木有限公司 | Dust purification device and method |
| CN104552004A (en) * | 2014-12-19 | 2015-04-29 | 广西大学 | Fiberboard sanding dust recycling machine capable of automatically separating sand grains and recycling method |
| CN105598094A (en) * | 2016-02-26 | 2016-05-25 | 西安交通大学 | Water-free cleaning device for waste plastic film |
| CN105797492A (en) * | 2016-03-17 | 2016-07-27 | 北京展铭科技发展有限公司 | Dust removal and purification system |
| CN107198921A (en) * | 2016-03-17 | 2017-09-26 | 天津宝丽杰涂料有限公司 | A kind of powdery paints separates dust arrester |
| CN107262485A (en) * | 2017-05-15 | 2017-10-20 | 滁州亿扬零部件制造有限公司 | A kind of job shop dust arrester |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201524509U (en) | Zincum powder dust collecting device | |
| CN102553382B (en) | Double-row filter bag embedded type electric bag compound dust catcher with electric field area at front stage | |
| CN107648975B (en) | Dust removal method and device for ultralow emission of dust-containing gas | |
| CN201776059U (en) | Cyclonic filtration type composite dust collector | |
| CN201179393Y (en) | Electrostatic reinforced low-voltage impulse bag-type dust-collector | |
| CN2920362Y (en) | Pulse reversed spray blow bag type dust collector | |
| CN204996274U (en) | Circulating fluidized bed boiler is with two bag dust removers of two electricity | |
| CN2781203Y (en) | Multiple cyclone static compound dust separator | |
| CN201676610U (en) | Inner-filter type big-bag dust collector | |
| CN207533010U (en) | A kind of Novel dust collection device | |
| CN203540269U (en) | Composite dust remover | |
| CN201613080U (en) | Dust catcher | |
| CN2815474Y (en) | Compartment-jet pulse bag type duster | |
| CN2561492Y (en) | Rotating flap dust collector | |
| CN208959515U (en) | A kind of polishing class dust pulse dust collector | |
| CN201880459U (en) | Impulse type filter-barrel dust collector | |
| CN201791436U (en) | Straight through type low-resistance and wear-resistant large dust-removing bagged dust remover | |
| CN207287017U (en) | Three-stage kiln tail gas dust cleaning device | |
| CN201061795Y (en) | Industry suction cleaner | |
| CN203342569U (en) | Dust collector provided with air box and pulse bags | |
| CN2633405Y (en) | Novel dust remover | |
| CN209485074U (en) | A kind of intermediate frequency furnace removing dust and clearing ash device | |
| CN207356837U (en) | A kind of deduster for carrying two trace gather apparatus for ash | |
| CN201519537U (en) | Cyclone-bag composite dust collector | |
| CN201445888U (en) | Three-level dust removing set |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: YEJIAN NEW MATERIAL CO., LTD. Free format text: FORMER OWNER: JIANGSU YEJIAN CORROSION PROTECTION MATERIAL CO., LTD. |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20110901 Address after: 213331, Gaoqiao Road, Town Industrial Zone, 9, Dai Town, Jiangsu, Liyang Co-patentee after: YEJIAN NEW MATERIAL CO., LTD. Patentee after: Jiangsu Yejian Zincum Industry Co., Ltd. Address before: 213331, Gaoqiao Road, Town Industrial Zone, 9, Dai Town, Jiangsu, Liyang Co-patentee before: Jiangsu Yejian Anti-corrosion Material Co., Ltd. Patentee before: Jiangsu Yejian Zincum Industry Co., Ltd. |
|
| CX01 | Expiry of patent term |
Granted publication date: 20100714 |
|
| CX01 | Expiry of patent term |