CN201389413Y - Single-chamber electric bag composite dust remover - Google Patents
Single-chamber electric bag composite dust remover Download PDFInfo
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- CN201389413Y CN201389413Y CN200820228349U CN200820228349U CN201389413Y CN 201389413 Y CN201389413 Y CN 201389413Y CN 200820228349 U CN200820228349 U CN 200820228349U CN 200820228349 U CN200820228349 U CN 200820228349U CN 201389413 Y CN201389413 Y CN 201389413Y
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Abstract
A single-chamber electric bag composite dust remover comprises a filter chamber electric field area and a filter chamber filter bag area communicated therewith, the filter chamber filter bag area therein is provided with a plurality of filter bags, the gas outlet of the filter chamber filter bag area is communicated with a gas purification chamber, the lower ends of the filter chamber electric field area and the filter chamber filter bag area are respectively provided with an ash bucket, a ring beam and a tube nest are arranged between the gas purification chamber and the filter chamber filter bag area, a keel and the filter bags are fixed on the tube nest, and the gas purification chamber thereon is provided with a pulse blowing system. As the whole filter chamber adopts a single-chamber structure, dust-containing gas enters the filter chamber electric field area so as to pre-remove dust and pre-charge the dust-containing flue gas with a high concentration, the filter bags are arranged in the filter chamber filter bag area in groups, clean coal gas enters the gas purification chamber from the filter bags through the filtration of the filter bags and then horizontally flows out from the dust remover from the gas outlet, so as to improve dust collection performance, deduce system resistance, greatly reduce the dust removal load of the filter bag area and prolong the service life of the filter bags, without hazard caused by high specific resistance.
Description
Technical field
The utility model relates to a kind of electric-bag complex dust collector, is used for the single chamber electric-bag complex dust collector of big dust content gas cleaning in particularly a kind of environmental protection field.
Background technology
Up to now, the purification of China's coal fired thermal power plant and cement rotary kiln kiln tail flue dust, basically adopt electric precipitation, past is in order to save construction investment, efficiency of dust collection requires on the low side, lectotype selection is less than normal, along with national environmental standard requires to improve constantly, expense that pollutant emission is imposed and requirement are more and more higher, the concentration of emission of most of electric cleaners can not satisfy new environmental requirement, also is a new problem to effective capture of subparticle dust, and electric cleaner has been taked a lot of corrective measures from design, as increase electric field, change the utmost point and join or the like, but produce little effect.For this reason, electric cleaner is transformed into bag dust collector, slowly become a kind of developing direction.But new problem produces again thereupon.Shortcomings such as equipment volume is big, running resistance is high, maintaining is frequent become a big drawback of sack cleaner.At these problems, a kind of single chamber electric-bag complex dust collector arises at the historic moment, and promptly prime is gathered dust and is electric precipitation, and the back level is the filter bag dedusting.
In newly-built coal fired thermal power plant and cement rotary kiln kiln tail clarifying smoke scheme, as adopt conventional electric cleaner scheme,, can only increase specification of equipment, just increased investment unavoidably greatly for adapting to new environmental protection standard; As simple employing bag dust collector, load is big, resistance is big, life of bag filter is low, and frequent replacing filter bag is a unavoidable problem, thus adopt this electric-bag complex dust collector, more than both advantage just be able to complementation technically.
The deduster of this pattern is specially adapted to go into operation not up to standard, the electric cleaner transformation that the place is restricted, modification scheme keeps first electric field of former electric cleaner generally speaking, utilize back level space alteration to be the bag dedusting, not only investment cost is little, the transformation cycle short for this forms of modification, and technical performance is very superior.
Summary of the invention
The purpose of this utility model is to overcome the shortcoming of above-mentioned prior art, provide a kind of efficiency of dust collection height, long service life, simple in structure, the operation maintenance is convenient, online independent deashing can be applicable to the single chamber electric-bag complex dust collector of big dust content gas cleaning.
For achieving the above object, the technical solution adopted in the utility model is: comprise filter chamber's electric field region that has the air inlet loudspeaker and the filter bag district, filter chamber that is connected with this filter chamber's electric field region, the filter chamber is provided with several filter bags in the filter bag district, the gas vent in filter bag district, filter chamber with the air-purifying chamber that exports loudspeaker that has be connected, the lower end in filter chamber's electric field region and filter chamber's filter bag district is respectively arranged with ash bucket, be provided with the collar tie beam and the card of buffer action between air-purifying chamber and filter chamber's filter bag district, the cage bone and the filter bag that are positioned at filter bag district, filter chamber are fixed on the card; The pulse jet system is set on air-purifying chamber.
Be equipped with on the sidewall of ash bucket of the present utility model and purge mouthful and broken arch mouthful, broken arch mouthful links to each other with Arch-Breaking Device by broken arch ball valve; Be provided with gas distributor in the air inlet loudspeaker; Filter chamber's electric field region is made up of positive plate that is connected with high-voltage rectifier power source and cathode line, and is respectively arranged with anode vibrated system and cathode rapping system on positive plate and cathode line; The pulse jet system comprises the interior winding-up pipe of the band drainage nozzles that is arranged on the card upper end, and the inlet of interior winding-up pipe is connected with gas bag by pulse valve, offers the injection hole that is connected with interior winding-up pipe on the sidewall of air-purifying chamber; Filter chamber's electric field region and bottom, filter chamber's filter bag district are equipped with manhole.
Because the whole filter chamber of the utility model adopts single cell structure, dusty gas enters filter chamber's electric field region from the air inlet loudspeaker, filter chamber's electric field region of compact conformation is realized the pre-dedusting of big concentration ash-laden gas and charged in advance, the filter bag grouping is arranged on filter bag district, filter chamber, filter by filter bag, clean coal gas rises up into air-purifying chamber in filter bag, level flows out deduster from the gas outlet.Because the pre-dedusting and the pre-charged effect of filter chamber's electric field region, enter the filter bag district after making on the grit band electric charge and the carrying capacity that reaches capacity, caught by the filtering surface of filter bag.Be deposited on the dust on filter bag surface, assemble electric charge and increase particle diameter and static repulsion force by the static aggegation, realize the non-dense set degree on filter bag surface, improved dust collection performance, reduced SR, do not have the harm that high specific resistance brings again, alleviated the dedusting burden in filter bag district significantly, prolonged the service life of filter bag.
Description of drawings
Fig. 1 is an overall structure schematic diagram of the present utility model;
Fig. 2 is the left view of Fig. 1;
The vertical view of Fig. 3 Fig. 1.
The specific embodiment
Below in conjunction with accompanying drawing structural principle of the present utility model and operation principle are described in further detail.
Referring to Fig. 1,2,3, the utility model comprises filter chamber's electric field region 2 that has air inlet loudspeaker 1 and the filter bag district, filter chamber 3 that is connected with this filter chamber's electric field region 2, be provided with gas distributor 15 in the air inlet loudspeaker 1, filter chamber's electric field region 2 is made up of positive plate 22 that is connected with high-voltage rectifier power source 20 and cathode line 23, and on positive plate 22 and cathode line 23, be respectively arranged with anode vibrated system 14 and cathode rapping system 21, be provided with several filter bags 7 in the filter bag district, filter chamber 3, the gas vent in filter bag district, filter chamber 3 with the air-purifying chamber 4 that exports loudspeaker 5 that has be connected, the lower end in filter chamber's electric field region 2 and filter chamber's filter bag district 3 is respectively arranged with establishes manhole 8 and ash bucket 9, the manhole 8 that is provided with makes things convenient for the people to enter deduster from the bottom, overhauls.Purging mouth 10 and broken arch mouth 11 are installed on the sidewall of ash bucket 9, broken arch mouth 11 links to each other with Arch-Breaking Device 12 by broken arch ball valve 13, be provided with the collar tie beam 6 and the card 16 of buffer action between air-purifying chamber 4 and filter chamber's filter bag district 3, the cage bone and the filter bag 7 that are positioned at filter bag district, filter chamber 3 are fixed on the card 16; The pulse jet system is set on air-purifying chamber 4, the pulse jet system comprises the interior winding-up pipe 17 of the band drainage nozzles that is arranged on card 16 upper ends, the inlet of interior winding-up pipe 17 is connected with gas bag 18 by pulse valve 19, offers the injection hole that is connected with interior winding-up pipe 17 on the sidewall of air-purifying chamber 4.
Workflow of the present utility model is as follows:
Dusty gas enters filter chamber's electric field region 2 from air inlet loudspeaker 1 level behind gas distributor 15, pre-filtering by the electric field passage, part dust is attracted on the positive plate 22, by the rapping of anode vibrated system 14 and cathode rapping system 21 dust on the pole plate polar curve is shaken to fall into ash bucket 9 lower ends; Enter filter bag district 3 again, hang in the filter bag 7 on the card 16 by grouping and rise up into air-purifying chamber 4, gather the back level and flow out dedusters from outlet loudspeaker 5.Dust is then stayed filter bag 7 outer surfaces; The drainage nozzles on 17 is managed by the pulse dust cleaning system by jetting in being arranged on, produce high flow rate and spray to filter bag, and the initiation filter bag is shaken and formation blowback air-flow effect from inside to outside comprehensively, removes the dust attached to filter bag 7 outer surfaces, and dust falls into ash bucket 9 lower ends.Arch-Breaking Device 12 links to each other by ball valve 13 and broken arch mouthfuls 11, and following time does not work dust stratification is broken arch clearly at ash bucket dust stratification knot arch.
Claims (6)
1, a kind of single chamber electric-bag complex dust collector, it is characterized in that: comprise filter chamber's electric field region (2) that has air inlet loudspeaker (1) and the filter bag district, filter chamber (3) that is connected with this filter chamber's electric field region (2), be provided with several filter bags (7) in the filter bag district, filter chamber (3), the gas vent in filter bag district, filter chamber (3) with have the outlet loudspeaker (5) air-purifying chamber (4) be connected, the lower end in filter chamber's electric field region (2) and filter chamber's filter bag district (3) is respectively arranged with ash bucket (9), be provided with the collar tie beam (6) and the card (16) of buffer action between air-purifying chamber (4) and filter chamber's filter bag district (3), the cage bone and the filter bag (7) that are positioned at filter bag district, filter chamber (3) are fixed on the card (16); On air-purifying chamber (4), the pulse jet system is set.
2, single chamber electric-bag complex dust collector according to claim 1 is characterized in that: be equipped with on the sidewall of said ash bucket (9) and purge mouthful (10) and broken arch mouthful (11), broken arch mouthful (11) links to each other with Arch-Breaking Device (12) by broken arch ball valve (13).
3, single chamber electric-bag complex dust collector according to claim 1 is characterized in that: be provided with gas distributor (15) in the said air inlet loudspeaker (1).
4, single chamber electric-bag complex dust collector according to claim 1, it is characterized in that: said filter chamber electric field region (2) is made up of positive plate (22) that is connected with high-voltage rectifier power source (20) and cathode line (23), and is respectively arranged with anode vibrated system (14) and cathode rapping system (21) on positive plate (22) and cathode line (23).
5, single chamber electric-bag complex dust collector according to claim 1, it is characterized in that: said pulse jet system comprises the interior winding-up pipe (17) of the band drainage nozzles that is arranged on card (16) upper end, the inlet of interior winding-up pipe (17) is connected with gas bag (18) by pulse valve (19), offers the injection hole that is connected with interior winding-up pipe (17) on the sidewall of air-purifying chamber (4).
6, single chamber electric-bag complex dust collector according to claim 1 is characterized in that: said filter chamber electric field region (2) and bottom, filter chamber's filter bag district (3) are equipped with manhole (8).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200820228349U CN201389413Y (en) | 2008-12-17 | 2008-12-17 | Single-chamber electric bag composite dust remover |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200820228349U CN201389413Y (en) | 2008-12-17 | 2008-12-17 | Single-chamber electric bag composite dust remover |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201389413Y true CN201389413Y (en) | 2010-01-27 |
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ID=41596231
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN200820228349U Expired - Fee Related CN201389413Y (en) | 2008-12-17 | 2008-12-17 | Single-chamber electric bag composite dust remover |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201389413Y (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102641630A (en) * | 2012-04-19 | 2012-08-22 | 江苏康洁环境工程有限公司 | Bag type deduster with arch breaking device |
| CN102908837A (en) * | 2012-11-20 | 2013-02-06 | 黄山加佳荧光材料有限公司 | Superfine powdery fluorescent pigment collector |
| CN105709550A (en) * | 2016-03-07 | 2016-06-29 | 苏州保酚环境科技有限公司 | Combined dust remover |
| CN109908688A (en) * | 2017-12-13 | 2019-06-21 | 山东盛华投资有限责任公司 | A kind of sack cleaner assembly |
| CN111359777A (en) * | 2019-11-19 | 2020-07-03 | 北京铝能清新环境技术有限公司 | Alumina roasting furnace flue gas composite dust remover and dust removing method thereof |
| CN111389118A (en) * | 2020-05-12 | 2020-07-10 | 福建龙净环保股份有限公司 | Filter bag device and dust remover |
-
2008
- 2008-12-17 CN CN200820228349U patent/CN201389413Y/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102641630A (en) * | 2012-04-19 | 2012-08-22 | 江苏康洁环境工程有限公司 | Bag type deduster with arch breaking device |
| CN102641630B (en) * | 2012-04-19 | 2014-10-15 | 江苏康洁环境工程有限公司 | Bag type deduster with arch breaking device |
| CN102908837A (en) * | 2012-11-20 | 2013-02-06 | 黄山加佳荧光材料有限公司 | Superfine powdery fluorescent pigment collector |
| CN105709550A (en) * | 2016-03-07 | 2016-06-29 | 苏州保酚环境科技有限公司 | Combined dust remover |
| CN109908688A (en) * | 2017-12-13 | 2019-06-21 | 山东盛华投资有限责任公司 | A kind of sack cleaner assembly |
| CN111359777A (en) * | 2019-11-19 | 2020-07-03 | 北京铝能清新环境技术有限公司 | Alumina roasting furnace flue gas composite dust remover and dust removing method thereof |
| CN111389118A (en) * | 2020-05-12 | 2020-07-10 | 福建龙净环保股份有限公司 | Filter bag device and dust remover |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100127 Termination date: 20131217 |