CN103127780A - High temperature bag dedusting exhaust gas purifier - Google Patents
High temperature bag dedusting exhaust gas purifier Download PDFInfo
- Publication number
- CN103127780A CN103127780A CN2011103892613A CN201110389261A CN103127780A CN 103127780 A CN103127780 A CN 103127780A CN 2011103892613 A CN2011103892613 A CN 2011103892613A CN 201110389261 A CN201110389261 A CN 201110389261A CN 103127780 A CN103127780 A CN 103127780A
- Authority
- CN
- China
- Prior art keywords
- bag
- air
- chamber
- high temperature
- communicated
- 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)
Abstract
The invention relates to an exhaust gas purifier, in particular to a high temperature bag dedusting exhaust gas purifier. The high temperature bag dedusting exhaust gas purifier comprises a base seat, a bag chamber is arranged above the base seat, a clean air chamber is arranged above the bag chamber, an air outlet and an air inlet are formed in the side face of the bag chamber, an ash bucket is arranged inside the base seat, the air outlet is communicated with the clean air chamber, and the air inlet is communicated with the ash bucket. The bag chamber is provided with a plurality of filter bags, the bottom portions of the filter bags are arranged above the ash bucket, a spiral conveyer is arranged on the bottom portion of the ash bucket, and the spiral conveyer is provided with a rotating discharger. The mouth portions of the filters are communicated with the clean air chamber, the mouth portion of each filter bag is communicated with a blowpipe through a communication pipe, and the blowpipe is connected with an air storage tank through a pulse valve. Lime and active carbon granules are arranged outside the filter bags. The high temperature bag dedusting exhaust gas purifier is simple and compact in structure, and not only can remove big granules in dust ahead of time, but also cannot lower the flow speed of air flow. Each filter bag can achieve independent ash removal, and cannot affect the normal work of other parts.
Description
Technical field
The present invention is a kind of catalytic converter, particularly a kind ofly is applicable to collect the flue gas aluminium powder, purifies the high temperature bag dust-removing waste gas clarifier of the blowing purification combination of the inorganic waste gases that aluminium metallurgy industry and various industry produce.
Background technology
Traditional catalytic converter is off-line ash-clearing, adopts compressed air blowback cloth bag, and the dust that cloth bag is outer blows off as far as possible, and its dedusting effect is not good enough, and use is inconvenient, and in waste gas, the inorganic pollution emission level can't purify, and does not reach environmental requirement.
Summary of the invention
The objective of the invention is to invent a kind of high temperature bag dust-removing waste gas clarifier that adopts online ash removal to use simultaneously compressed air blowback cloth bag in order to overcome the not good enough defective of using inconvenience of existing catalytic converter efficiency of dust collection.
The objective of the invention is to realize as follows: described high temperature bag dust-removing waste gas clarifier, comprise base, the base top is provided with a bag chamber, top, bag chamber is provided with air-purifying chamber, the side of bag chamber is provided with gas outlet and air inlet, be provided with ash bucket in base, the gas outlet is communicated with air-purifying chamber, and air inlet is communicated with ash bucket; Bag is indoor is provided with a plurality of filter bags, and the bottom of filter bag is positioned at the top of ash bucket, and the bottom of ash bucket is provided with conveying worm, and conveying worm is provided with the revolution discharger; The oral area of filter bag is communicated with air-purifying chamber, and by being communicated with injection tube a communicating pipe, injection tube is connected with air accumulator by pulse valve the oral area of each filter bag separately.
The top of described air-purifying chamber is provided with changes a bag access door.
Pressure gauge and blowoff valve are housed on described air accumulator.
The outside of described filter bag is provided with lime and activated carbon granule.
Described filter bag adopts terylene needled felt, Chopped Strand Mat or heat resisting film-coating filtrate to make.
Good effect of the present invention is as follows: the present invention is simple and compact for structure, and it can either remove particle larger in dust and fine particle in advance, can not reduce again the flow velocity of air-flow; Each filter bag can realize that independent pressure reduction ash is clear, and namely keeping cloth bag pressure is 1700Pa, and the cloth bag Pressure Drop gets off and quits work again when impulse electromagnetic valve is started working, and can not affect the normal operation of other parts; Can also thoroughly purify the inorganic waste gases that aluminium metallurgy industry and various industry produce, automaticity is high, and good dedusting effect operates very easy to use.
Description of drawings
Fig. 1 is structure chart of the present invention
In figure: 12 bags of bases chambers, 3 air-purifying chambers
4 gas outlet 5 air intake 6 ash buckets
7 filter bag 8 conveying worm 9 revolution dischargings
10 communicating pipes 11 injection tube 12 pulse valves
13 air accumulator 14 access doors
The specific embodiment
As shown in Figure 1, described high temperature bag dust-removing waste gas clarifier comprises base 1, base 1 top is provided with bag chamber 2, and bag 2 tops, chamber are provided with air-purifying chamber 3, and the side of bag chamber 2 is provided with gas outlet 4 and air inlet 5, be provided with ash bucket 6 in base 1, gas outlet 4 is communicated with air-purifying chamber 3, and air inlet 5 is communicated with ash bucket 6; Bag is provided with a plurality of filter bags 7 in chamber 2, and the bottom of filter bag 7 is positioned at the top of ash bucket 6, and the bottom of ash bucket 6 is provided with conveying worm 8, and conveying worm 8 is provided with revolution discharger 9; The oral area of filter bag 7 is communicated with air-purifying chamber 3, and by being communicated with injection tube 11 communicating pipe 10, injection tube 11 is connected with air accumulator 13 by pulse valve 12 oral area of each filter bag 7 separately.
The top of described air-purifying chamber 3 is provided with changes bag access door 14.Can change bag by access door repair apparatus and locellus in normal operation, not affect the cleaner normal operation.
On described air accumulator 13, Pressure gauge and blowoff valve are housed.Can get rid of ponding and dirt in air accumulator by blowoff valve.
The outside of described filter bag 6 is provided with lime and activated carbon granule.Lime and activated carbon granule are favourable for the inorganic wastes of removing in waste gas.
Described filter bag 6 adopts terylene needled felt to make.Terylene needled felt, Chopped Strand Mat or heat resisting film-coating filtrate are made.These materials allow filtration velocity high, and resistance is low, easy-to-clean ash, and the life-span is long.
Operation principle of the present invention is as follows: dusty gas enters a bag chamber from air inlet by ash bucket, crude particle dust in air-flow directly falls into ash bucket, play the effect of gathering dust in advance, then air-flow upwards passes through filter bag, make dust be trapped in the outer surface of filter bag, purified gas enters air-purifying chamber by filter bag, then discharges from the gas outlet.During to certain thickness, the pulse valve action makes compressed air stream enter injection tube when the dust accumulation of filter bag outside, and sprays into communicating pipe in each filter bag by one group, makes the dust releasing that is captured on the filter bag outer wall.The dust settling that comes off is drained into technique through screw reamer and revolution discharger in the ash bucket and returns in grey conveying equipment.
Claims (5)
1. high temperature bag dust-removing waste gas clarifier, it is characterized in that: it comprises base, the base top is provided with a bag chamber, top, bag chamber is provided with air-purifying chamber, and the side of bag chamber is provided with gas outlet and air inlet, is provided with ash bucket in base, the gas outlet is communicated with air-purifying chamber, and air inlet is communicated with ash bucket; Bag is indoor is provided with a plurality of filter bags, and the bottom of filter bag is positioned at the top of ash bucket, and the bottom of ash bucket is provided with conveying worm, and conveying worm is provided with the revolution discharger; The oral area of filter bag is communicated with air-purifying chamber, and by being communicated with injection tube a communicating pipe, injection tube is connected with air accumulator by pulse valve the oral area of each filter bag separately.
2. high temperature bag dust-removing waste gas clarifier according to claim 1, it is characterized in that: the top of described air-purifying chamber is provided with changes a bag access door.
3. high temperature bag dust-removing waste gas clarifier according to claim 1, is characterized in that: Pressure gauge and blowoff valve are housed on described air accumulator.
4. high temperature bag dust-removing waste gas clarifier according to claim 1, it is characterized in that: the outside of described filter bag is provided with lime and activated carbon granule.
5. high temperature bag dust-removing waste gas clarifier according to claim 1, is characterized in that: described filter bag employing terylene needled felt, Chopped Strand Mat or the making of heat resisting film-coating filtrate.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011103892613A CN103127780A (en) | 2011-11-30 | 2011-11-30 | High temperature bag dedusting exhaust gas purifier |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011103892613A CN103127780A (en) | 2011-11-30 | 2011-11-30 | High temperature bag dedusting exhaust gas purifier |
Publications (1)
Publication Number | Publication Date |
---|---|
CN103127780A true CN103127780A (en) | 2013-06-05 |
Family
ID=48488614
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2011103892613A Pending CN103127780A (en) | 2011-11-30 | 2011-11-30 | High temperature bag dedusting exhaust gas purifier |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN103127780A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107243195A (en) * | 2017-07-26 | 2017-10-13 | 荆门市吉光环保科技有限责任公司 | A kind of air box pulse dust remover |
CN112516691A (en) * | 2019-09-19 | 2021-03-19 | 苏州首泓信息科技有限公司 | Mining plant dust removal purifier for environmental protection equipment |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH06198111A (en) * | 1992-12-28 | 1994-07-19 | Plantec:Kk | Operation control method for precoat type bag filter device |
CN2531859Y (en) * | 2002-01-28 | 2003-01-22 | 驻马店市龙山通用机械有限公司 | Double-state dust collection chamber for bag type dust collector |
CN201287013Y (en) * | 2008-10-24 | 2009-08-12 | 余建军 | Air box type pulse bag dust collector |
CN201419061Y (en) * | 2009-06-04 | 2010-03-10 | 张继全 | Downstream pulse bag type dust collector |
-
2011
- 2011-11-30 CN CN2011103892613A patent/CN103127780A/en active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH06198111A (en) * | 1992-12-28 | 1994-07-19 | Plantec:Kk | Operation control method for precoat type bag filter device |
CN2531859Y (en) * | 2002-01-28 | 2003-01-22 | 驻马店市龙山通用机械有限公司 | Double-state dust collection chamber for bag type dust collector |
CN201287013Y (en) * | 2008-10-24 | 2009-08-12 | 余建军 | Air box type pulse bag dust collector |
CN201419061Y (en) * | 2009-06-04 | 2010-03-10 | 张继全 | Downstream pulse bag type dust collector |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107243195A (en) * | 2017-07-26 | 2017-10-13 | 荆门市吉光环保科技有限责任公司 | A kind of air box pulse dust remover |
CN112516691A (en) * | 2019-09-19 | 2021-03-19 | 苏州首泓信息科技有限公司 | Mining plant dust removal purifier for environmental protection equipment |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN201744255U (en) | Movable self-cleaning type welding smoke purifier | |
CN201157746Y (en) | Energy-saving cooking fume purifier | |
CN106390652A (en) | Wet type fine particle high-efficiency cyclone removal device | |
CN203017913U (en) | Welding fume purifying system and deduster thereof | |
CN206468408U (en) | A kind of diesel engine back flushing type smoke discharging and purifying device | |
CN103432844A (en) | Assembled transverse multi-filter-cartridge dust collector | |
CN200961246Y (en) | Dust remover of road sweeping lorry | |
CN204973383U (en) | Steam injection boiler unit sled seat weldment work station is with welding cigarette dust purification device | |
CN207591515U (en) | Suitable for the flue gas processing device of civil heating stove | |
CN212017255U (en) | Dust collector for SOx/NOx control | |
CN102580417A (en) | High-temperature smoke bag type dust remover of submerged arc furnace, dust removing process and dust removing system | |
CN103127780A (en) | High temperature bag dedusting exhaust gas purifier | |
WO2017080074A1 (en) | Plenum pulse dust collector | |
CN203507713U (en) | Integral welded type dust collector provided with multiple filter cartridges vertically arranged | |
CN206372641U (en) | The dust pelletizing system of flue gas produced by sludge high temperature processing | |
CN211274048U (en) | Tail flue gas dust remover of waste incineration boiler | |
CN106268135A (en) | One faces formula pulse bag-type dust-removing device directly | |
CN203507712U (en) | Assembling type dust collector provided with multiple transverse filter cartridges | |
CN202490514U (en) | Combined ash and dust removing machine | |
CN202427313U (en) | Smoke humidification composite type dust-removing and synergistic desulfurization and denitration device | |
CN2781204Y (en) | Desulfurization dust removing integral equipment | |
CN205760347U (en) | A kind of high efficiency gas wash tower | |
CN204522573U (en) | Novel dust removing equipment | |
CN109381991A (en) | A kind of low temperature SCR denitration dust removal integrated plant | |
CN214809290U (en) | Negative pressure pulse bag dust collector device of large ferrosilicon furnace |
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 |
Application publication date: 20130605 |