CN1657136A - Dry type miropore filtering dust separator - Google Patents
Dry type miropore filtering dust separator Download PDFInfo
- Publication number
- CN1657136A CN1657136A CN 200410046991 CN200410046991A CN1657136A CN 1657136 A CN1657136 A CN 1657136A CN 200410046991 CN200410046991 CN 200410046991 CN 200410046991 A CN200410046991 A CN 200410046991A CN 1657136 A CN1657136 A CN 1657136A
- Authority
- CN
- China
- Prior art keywords
- filter mantle
- dry type
- type micro
- micro porous
- porous filtration
- 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.)
- Pending
Links
Images
Landscapes
- Filtering Of Dispersed Particles In Gases (AREA)
- Filtering Materials (AREA)
Abstract
A dry micropore-filtering duster is composed of top cover, the upper and middle case bodies, dust hopper and its supporter, dust discharging valve under dust hopper, the patterned plate with the uniformly arranged circular holes between upper and middle case bodies, and the micropore filtering ceramic tubes for said circular holes on patterned plate. It has high dusting effect and high mechanical strength.
Description
Technical field
The present invention relates to a kind of dry type micro porous filtration and remove the device of pernicious gases such as dust in flue gas, particle, belong to the cleaning equipment of boiler, kiln gas and the industrial waste gas of field of environment protection.
Background technology
The dry dust removal technology, cloth bag filtration method commonly used carries out dedusting, and its efficiency of dust collection height stable and reliable for performancely is widely used in dedusting.Filtrate is the core of sack cleaner, adopts strainability good usually, and chemical stability is good, the inorfil filtrate that price is low.The operation principle of sack cleaner is that dusty gas enters filter bag from the bottom, and when passing through the hole of filtrate, dust is caught to combine on the filtrate, and purified gas is discharged from exhaust outlet, thereby reaches the dedusting purpose.But along with practical application, adopt the weakness of fiber filtering also to come out, there are the shortcoming of stopping up, easily wearing out in its heatproof, wearability, corrosion-resistant, and can not wash with water in the process of deashing, have limitation, can not satisfy the requirement of dedusting.
Summary of the invention
Technical problem to be solved by this invention is the deficiency that overcomes existing dry collector, a kind of long service life, mechanical strength height, low price, efficiency of dust collection height, easy cleaning, heatproof, corrosion resistant dry type micro porous filtration deduster are provided, this device not only can adopt the traditional machinery rotation blowback or the method for pulse backblowing in the process of deashing, also can adopt the method for washing.
Solving the problems of the technologies described above the technical scheme that is adopted is: a kind of dry type micro porous filtration deduster, comprise top cover, upper box, middle casing, ash bucket, support, on, be provided with the uniform card that has circular hole on it between the middle casing, ash bucket has and unloads the dirt valve, ash bucket is by stent support, middle casing places on the ash bucket, the top of described ash bucket is provided with air inlet, upper box is provided with exhaust outlet, it is characterized in that described in the casing circular hole position on the corresponding card be provided with the upper shed hole ceramic filter tube that declines, the upper shed of filter mantle is communicated with the inner chamber of upper box inner chamber, and filter mantle seals the circular hole on the card.
Advantage of the present invention is, to dusty gas purification efficiency height, easy to use.Adopt porous ceramic filter material to determine device in the process of deashing, not only can adopt the traditional machinery rotation blowback or the method for pulse backblowing, also can adopt the method for washing.Thereby make this device long service life, mechanical strength height, low price, have the characteristics of efficiency of dust collection height, easy cleaning, heatproof, corrosion-resistant, easy to use, stable performance.
Description of drawings
The present invention is further described below in conjunction with drawings and Examples.
Fig. 1 is a front view of the present invention.
Fig. 2 is a vertical view of the present invention.
Fig. 3 is the structural representation of filter mantle.
Fig. 4 installs the structural representation of relation for expression filter mantle and card.
Each label is represented among the figure:
1, top cover 2, upper box 21, exhaust outlet 3, middle casing
4, ash bucket 41, air inlet 5, support 6, unload the dirt valve
7, card 8, filter mantle 81, upper shed 82, flange
9, asbestos cord sealing gasket
The specific embodiment:
Shown in Fig. 1～4, dry type micro porous filtration deduster of the present invention, comprise top cover 1, upper box 2, middle casing 3, ash bucket 4, support 5, on, middle casing 2, be provided with the card 7 that offers uniform circular hole on it between 3, ash bucket 4 has and unloads dirt valve 6, ash bucket 4 is supported by support 5, middle casing 3 places on the ash bucket 4, the top of ash bucket 4 is provided with air inlet 41, upper box 2 is provided with exhaust outlet 21, in in the casing 3 on the corresponding cards 7 the circular hole position be provided with the upper shed hole ceramic filter tube 8 that declines, the upper shed 81 of filter mantle 8 is communicated with the inner chamber of upper box 2, filter mantle 8 seals the circular hole on the card 7.In the embodiment that accompanying drawing 3,4 provides, upper shed 81 places of filter mantle 8 are provided with flange 82, and by this flange 82, under the gravity effect by filter mantle 8 self, filter mantle 8 places on the card 7.Be provided with asbestos cord sealing gasket 9 between filter mantle 8 and the card 7.Filter mantle 8 can strengthen filter mantle or be silica enhancing filter mantle or not siliceous extraordinary filter mantle for aluminium oxide.Its cross section can be circle or rectangle or ellipse, and its filtrate micro-pore diameter is 10～400um.
The course of work of the present invention is as follows: casing 3 during dusty gas is entered by air inlet 41, dust is caught to combine in filter mantle 8 in appearance when the filtrate micropore by filter mantle 8, fall into ash bucket 4 at effect of inertia, purified gas is discharged by the exhaust outlet 21 of upper box 2 through the filtrate micropore and the upper shed 81 of filter mantle.Because filtrate is a micropore ceramic tube among the present invention, both can adopt the method for machinery rotation blowback or pulse backblowing when deashing, also can adopt method for washing.
Claims (8)
1, a kind of dry type micro porous filtration deduster, comprise top cover (1), upper box (2), middle casing (3), ash bucket (4), support (5), on, middle casing (2), (3) be provided with the card (7) that has uniform circular hole on it between, ash bucket (4) has and unloads dirt valve (6), ash bucket (4) is supported by support (5), middle casing (3) places on the ash bucket (4), the top of described ash bucket (4) is provided with air inlet (41), upper box (2) is provided with exhaust outlet (21), it is characterized in that described in the casing (3) corresponding card (7) go up the circular hole position and be provided with the upper shed hole ceramic filter tube (8) that declines, the upper shed (81) of filter mantle (8) is communicated with the inner chamber of upper box (2), and filter mantle (8) seals the circular hole on the card (7).
2, dry type micro porous filtration deduster according to claim 1 is characterized in that the upper shed (81) of filter mantle (8) locates to be provided with flange (82), places on the card (7) by this flange (82) filter mantle (8).
3, dry type micro porous filtration deduster according to claim 2 is characterized in that being provided with asbestos cord sealing gasket (9) between filter mantle (8) and card (7).
4,, it is characterized in that described filter mantle (8) strengthens filter mantle for aluminium oxide according to claim 2 or 3 described dry type micro porous filtration dedusters.
5,, it is characterized in that described filter mantle (8) strengthens filter mantle for silica according to claim 2 or 3 described dry type micro porous filtration dedusters.
6,, it is characterized in that described filter mantle (8) is not siliceous extraordinary filter mantle according to claim 2 or 3 described dry type micro porous filtration dedusters.
7,, it is characterized in that described filter mantle (8) cross section is circle, rectangle or ellipse according to claim 2 or 3 described dry type micro porous filtration dedusters.
8, according to claim 2 or 3 described dry type micro porous filtration dedusters, it is characterized in that described filter mantle (8) filtrate micro-pore diameter is 10～400um.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200410046991 CN1657136A (en) | 2004-11-30 | 2004-11-30 | Dry type miropore filtering dust separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200410046991 CN1657136A (en) | 2004-11-30 | 2004-11-30 | Dry type miropore filtering dust separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN1657136A true CN1657136A (en) | 2005-08-24 |
Family
ID=35006959
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200410046991 Pending CN1657136A (en) | 2004-11-30 | 2004-11-30 | Dry type miropore filtering dust separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1657136A (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100393390C (en) * | 2006-05-17 | 2008-06-11 | 孙琦 | Combined filter tube element pulse dust-collector |
| CN106268097A (en) * | 2016-09-30 | 2017-01-04 | 中国恩菲工程技术有限公司 | Filtrating equipment of flue gas |
| CN106310830A (en) * | 2016-09-20 | 2017-01-11 | 派勒（天津）纳米技术有限公司 | Intelligent collector of dry ball-milling system |
| CN106582131A (en) * | 2016-12-30 | 2017-04-26 | 莱歇研磨机械制造(上海)有限公司 | Cabin structure of off-line ash-clearing ceramic filtering medium dust removal device |
| CN106731270A (en) * | 2016-12-30 | 2017-05-31 | 莱歇研磨机械制造(上海)有限公司 | A kind of off-line ash-clearing ceramic filter material dust arrester |
| CN107281848A (en) * | 2017-08-23 | 2017-10-24 | 萍乡市普天高科实业有限公司 | A kind of waste gas filter |
| CN109929962A (en) * | 2019-04-24 | 2019-06-25 | 广州华鑫工程技术有限公司 | The ultra-clean cleaner of high temperature resistant and dust removal method for coal gas of steel-smelting revolving furnace |
| CN110030841A (en) * | 2019-04-24 | 2019-07-19 | 广州华鑫工程技术有限公司 | Dedusting of EAF equipment and dust removal method |
-
2004
- 2004-11-30 CN CN 200410046991 patent/CN1657136A/en active Pending
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100393390C (en) * | 2006-05-17 | 2008-06-11 | 孙琦 | Combined filter tube element pulse dust-collector |
| CN106310830A (en) * | 2016-09-20 | 2017-01-11 | 派勒（天津）纳米技术有限公司 | Intelligent collector of dry ball-milling system |
| CN106268097A (en) * | 2016-09-30 | 2017-01-04 | 中国恩菲工程技术有限公司 | Filtrating equipment of flue gas |
| CN106582131A (en) * | 2016-12-30 | 2017-04-26 | 莱歇研磨机械制造(上海)有限公司 | Cabin structure of off-line ash-clearing ceramic filtering medium dust removal device |
| CN106731270A (en) * | 2016-12-30 | 2017-05-31 | 莱歇研磨机械制造(上海)有限公司 | A kind of off-line ash-clearing ceramic filter material dust arrester |
| CN107281848A (en) * | 2017-08-23 | 2017-10-24 | 萍乡市普天高科实业有限公司 | A kind of waste gas filter |
| CN109929962A (en) * | 2019-04-24 | 2019-06-25 | 广州华鑫工程技术有限公司 | The ultra-clean cleaner of high temperature resistant and dust removal method for coal gas of steel-smelting revolving furnace |
| CN110030841A (en) * | 2019-04-24 | 2019-07-19 | 广州华鑫工程技术有限公司 | Dedusting of EAF equipment and dust removal method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204841246U (en) | Bag -type dust collector | |
| CN208975368U (en) | A kind of bag-type dust collector | |
| CN207708721U (en) | A kind of self-cleaning type dry filter | |
| CN201524509U (en) | Zincum powder dust collecting device | |
| CN201085970Y (en) | Back flushing cloth bag dust-collecting equipment | |
| CN1657136A (en) | Dry type miropore filtering dust separator | |
| CN207805265U (en) | A kind of pulse type filter drum dust collector | |
| CN207533010U (en) | A kind of Novel dust collection device | |
| CN201346427Y (en) | Pulse dust remover with side-insert flat bag | |
| CN205598785U (en) | Low -pressure pulse bag type dust collector | |
| CN205095567U (en) | Pulse bag deduster | |
| CN106268068A (en) | A kind of novel environment friendly sack cleaner | |
| CN108015080A (en) | A kind of spinning and weaving workshop flying dust cleaning plant | |
| CN210356392U (en) | Mould board dust remover that burns | |
| CN2406716Y (en) | Dust collecting and purifying apparatus | |
| CN2752624Y (en) | Filtering dust cleaner | |
| CN204767912U (en) | From clear formula airsetting tape bag dust remover | |
| CN107252600A (en) | Dust bag-type dusting technique under a kind of unordered uneven state | |
| CN211864227U (en) | Dust settling device of bag type dust collector | |
| CN209485074U (en) | A kind of intermediate frequency furnace removing dust and clearing ash device | |
| CN103071345A (en) | Novel anti-frosting bag type dust collector | |
| CN211133315U (en) | Pulse dust collector | |
| CN2633405Y (en) | Novel dust remover | |
| CN2459066Y (en) | High-temp. high-efficient surface filter | |
| CN109603330A (en) | Automatically cleaning sack cleaner |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |