CN201085969Y - Resistance bag-type dust remover - Google Patents

Resistance bag-type dust remover Download PDF

Info

Publication number
CN201085969Y
CN201085969Y CNU2007200322246U CN200720032224U CN201085969Y CN 201085969 Y CN201085969 Y CN 201085969Y CN U2007200322246 U CNU2007200322246 U CN U2007200322246U CN 200720032224 U CN200720032224 U CN 200720032224U CN 201085969 Y CN201085969 Y CN 201085969Y
Authority
CN
China
Prior art keywords
air
chamber
bag
purifying chamber
filtering
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
CNU2007200322246U
Other languages
Chinese (zh)
Inventor
刘江
毛少祥
王敏
贾东东
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.)
SHANXI HUAXIANG ENGINEERING EQUIPMENT Co Ltd
Original Assignee
SHANXI HUAXIANG ENGINEERING EQUIPMENT Co 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 SHANXI HUAXIANG ENGINEERING EQUIPMENT Co Ltd filed Critical SHANXI HUAXIANG ENGINEERING EQUIPMENT Co Ltd
Priority to CNU2007200322246U priority Critical patent/CN201085969Y/en
Application granted granted Critical
Publication of CN201085969Y publication Critical patent/CN201085969Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Filtering Of Dispersed Particles In Gases (AREA)

Abstract

A low-resistance bag type duster comprises a filtering chamber and an air purifying chamber communicated with the filtering chamber, wherein an air distributor and a rectifying passage are disposed inside an air inlet port, a rectifying partitioning plate is disposed inside the filtering chamber, the air purifying chamber is isolated from the filtering chamber via a tube sheet opened with a plurality of pores, a bag cage and a filtering bag positioned inside the filtering chamber are fixed on the tube sheet, an inner blowing tube with a diversion spray nozzle is disposed at the upper end of the tube plate inn the air purifying chamber, blowing holes are opened at the side wall of the air purifying chamber, the inner blowing tube is communicated with an outer blowing tube via the blowing holes, and the outer blowing tube is connected with an air bag. By the utility model, the dusty air is passed through the air distributor and the rectifying passage from the air inlet port, horizontally introduced into the filtering chamber, and filtered by the filtering bag, and the purified flue gas is introduced into the air purifying chamber from the filtering bag and horizontally ducted out of the duster from the air outlet port. The horizontal air inlet/outlet manner has the advantages of short flow path, and smooth and gentle flowing; and is helpful for reducing the structural resistance and running resistance of the bag type duster and reducing energy consumption of air flowing.

Description

A kind of lower resistance sack cleaner
Technical field
The utility model relates to a kind of sack cleaner, is specifically related to a kind of lower resistance sack cleaner that big air quantity ash-laden gas purifies that is used for.
Background technology
Along with the further raising of national environmental standard with to SO 2The increasing once more of control dynamics, and expense and requirement that pollutant emission is imposed are more and more higher, cause many efficiency of dust collections in the electrostatic precipitator of using as a servant not reach environmental requirement.Some electrostatic precipitator manufactories have dropped into sizable energy, have taked a lot of measures, join, change power supply etc. as increase electric field, the change utmost point, try hard to electrostatic precipitator equipment is carried out omnibearing transformation, but it are little to take effect; And in flue gas, add NH 3Improve the mode of dust removing effects, can produce very sticking deposit again, cause the vibration dust-cleaning mis-behave; Wash and can cause the corrosion of ESP shell and pole plate with water.In the case, transform electric cleaner as sack cleaner successively.
The influence that the filtration mechanism of sack cleaner has determined it changed by the exhaust gas dust physical property is very little, has efficient and reliable and stable separating power, can satisfy the environmental protection standard requirement of increasingly stringent; Sack cleaner belongs to dry-type dedusting equipment, does not exist wet scrubber mud to silt up and troublesome problem such as water treatment; Along with high temperature resistant, corrosion-resistant, the static that disappears, the exploitation refusing profit, resistance to oxidation, remove specific function filtrates such as gas, and the raising of the design of sack cleaner integral body and accessory, manufacture level, the advantage of sack cleaner appears gradually, and application just constantly enlarges.
Yet, the intake method of sack cleaner and air current composition are still permanent problem, running resistance and life-span of the filter bag that it directly has influence on sack cleaner are that equipment is realized one of long-life key of lower resistance, also whether influence the key factor of the operation of unit.
Summary of the invention
The purpose of this utility model is to overcome the shortcoming of above-mentioned prior art, provide that a kind of resistance is little, volume is little, simple in structure, the operation maintenance is convenient, off-line ash-clearing can be applicable to the lower resistance sack cleaner that big air quantity ash-laden gas purifies.
For achieving the above object, the technical solution adopted in the utility model is: comprise the filter chamber that is provided with air inlet and ash bucket and the air-purifying chamber that is connected with the filter chamber, on air-purifying chamber, offer the gas outlet, be provided with gas distributor and rectification passage in the air inlet, be provided with Partition for realigning water flow in the filter chamber, air-purifying chamber and filter chamber isolate by the card that offers some apertures, the bag cage and the filter bag that are positioned at the filter chamber are fixed on the card, the upper end that is positioned at card in air-purifying chamber is provided with the winding-up pipe that has drainage nozzles, offer injection hole on the sidewall of air-purifying chamber, interior winding-up pipe is connected with outer winding-up pipe by injection hole, and the outer pipe of jetting also links to each other with gas bag.
Also be provided with pulse dust cleaning valve and protective cover on the gas bag of the present utility model; Offer the purging mouth on the sidewall of ash bucket and break the arch mouth, break the arch mouth and be connected with Arch-Breaking Device by the broken ball valve that encircles; Be installed with the location channel-section steel on the air-purifying chamber inwall, interior winding-up pipe is fixedlyed connected with the location channel-section steel by locating piece; Also offer manhole in the filter chamber.
Because the whole filter chamber of the utility model adopts single cell structure, the filter bag grouping is arranged in the filter chamber, dusty gas from air inlet through gas distributor, rectification passage level enters the filter chamber, filter by filter bag, clean coal gas rises up into air-purifying chamber in filter bag, and level flows out deduster from the gas outlet.The gas flow pattern of this level turnover shows short, smooth and easy, the mild characteristics that flow of flow process, is of value to and reduces sack cleaner structural drag and running resistance, reduces the gas flow energy consumption.By gas distributor being set and the rectification passage is reintegrated distribution to air-flow, gas flow rate is slowed down in the multi-faceted filter bag space that enters, and effectively avoids air-flow directly to wash away filter bag, causes regional area filter bag load excessive and erosive wear is serious.
Description of drawings
Fig. 1 is an overall structure schematic diagram of the present utility model;
Fig. 2 is a side view of the present utility model;
Fig. 3 is the structure chart of filter chamber of the present utility model;
Fig. 4 is the partial enlarged drawing of the utility model Fig. 2.
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. 1,2,3,4, the utility model comprises and is provided with air inlet 1, the filter chamber 2 of manhole 14 and ash bucket 15 and the air-purifying chamber 9 that is connected with filter chamber 2, whole filter chamber 2 adopts single chamber, on air-purifying chamber, offer gas outlet 10, offer purging mouth 16 and broken arch mouth 17 on the sidewall of ash bucket 15, broken arch mouth 17 is connected with Arch-Breaking Device 18 by broken arch ball valve 19, be provided with gas distributor 20 and rectification passage 21 in the air inlet 1, be provided with Partition for realigning water flow 22 in the filter chamber 2, air-purifying chamber 9 and filter chamber 2 isolate by the card 13 that offers some apertures, the bag cage 7 and the filter bag 8 that are positioned at filter chamber 2 are fixed on the card 13, the upper end that is positioned at card 13 in air-purifying chamber 9 is provided with winding-up pipe 12, be installed with location channel-section steel 27 on air-purifying chamber 2 inwalls, locating piece 23 be decided to be channel-section steel 27 and be connected by bolt 25, nut 24 lockings, bolt 26 holds out against; Interior winding-up pipe 12 is fixedlyed connected with the location channel-section steel by locating piece 23, offer injection hole 11 on the sidewall of air-purifying chamber 9, the interior pipe 12 of jetting is managed 3 by injection hole 11 with outer winding-up and is connected, and winding-up pipe 3 also links to each other with gas bag 4 outward, also is provided with pulse dust cleaning valve 5 and protective cover 6 on the gas bag 4.
Workflow of the present utility model is as follows:
Dusty gas from air inlet 1 through gas distributor 20, level enters filter chamber 2 after 21 rectifications of rectification passage, hang on the filtration of filter bag 8 in the filter chamber 2 by grouping, clean flue gas rises up into air-purifying chamber 9 in filter bag 8, gathers the back level and 10 flows out dedusters from the gas outlet.Dust is then stayed filter bag 8 outer surfaces; Gas in the pulse dust cleaning valve 5 injection gas bags 4 enters the interior winding-up pipe 12 that is attached thereto by outer winding-up pipe 3, by the drainage nozzles on the winding-up pipe 12 in being arranged on, produce high flow rate and spray to filter bag 8, cause filter bag 8 shake and formation blowback air-flow effect from inside to outside comprehensively, removing is attached to the dust of filter bag 8 outer surfaces, and dust falls into ash bucket 15 lower ends.Arch-Breaking Device 18 links to each other by broken arch ball valve 19 and broken arch mouthfuls 17, and following time does not work dust stratification is broken arch clearly at ash bucket dust stratification knot arch.

Claims (5)

1. lower resistance sack cleaner, comprise the filter chamber (2) that is provided with air inlet (1) and ash bucket (15) and the air-purifying chamber (9) that is connected with filter chamber (2), on air-purifying chamber, offer gas outlet (10), it is characterized in that: be provided with gas distributor (20) and rectification passage (21) in the air inlet (1), be provided with Partition for realigning water flow (22) in the filter chamber (2), air-purifying chamber (9) and filter chamber (2) isolate by the card (13) that offers some apertures, the bag cage (7) and the filter bag (8) that are positioned at filter chamber (2) are fixed on the card (13), the upper end that is positioned at card (13) in air-purifying chamber (9) is provided with the winding-up pipe (12) that has drainage nozzles, offer injection hole (11) on the sidewall of air-purifying chamber (9), interior winding-up pipe (12) is managed (3) by injection hole (11) with outer winding-up and is connected, and outer winding-up pipe (3) also links to each other with gas bag (4).
2. lower resistance sack cleaner according to claim 1 is characterized in that: also be provided with pulse dust cleaning valve (5) and protective cover (6) on the said gas bag (4).
3. lower resistance sack cleaner according to claim 1 is characterized in that: offer on the sidewall of said ash bucket (15) and purge mouthful (16) and broken arch mouthful (17), broken arch mouthful (17) is connected with Arch-Breaking Device (18) by broken arch ball valve (19).
4. lower resistance sack cleaner according to claim 1 is characterized in that: be installed with location channel-section steel (27) on said air-purifying chamber (2) inwall, interior winding-up pipe (12) is fixedlyed connected with the location channel-section steel by locating piece (23).
5. lower resistance sack cleaner according to claim 1 is characterized in that: also offer manhole (14) on said filter chamber (2).
CNU2007200322246U 2007-07-10 2007-07-10 Resistance bag-type dust remover Expired - Fee Related CN201085969Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNU2007200322246U CN201085969Y (en) 2007-07-10 2007-07-10 Resistance bag-type dust remover

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNU2007200322246U CN201085969Y (en) 2007-07-10 2007-07-10 Resistance bag-type dust remover

Publications (1)

Publication Number Publication Date
CN201085969Y true CN201085969Y (en) 2008-07-16

Family

ID=39633558

Family Applications (1)

Application Number Title Priority Date Filing Date
CNU2007200322246U Expired - Fee Related CN201085969Y (en) 2007-07-10 2007-07-10 Resistance bag-type dust remover

Country Status (1)

Country Link
CN (1) CN201085969Y (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102553360A (en) * 2010-06-30 2012-07-11 广州迪森热能技术股份有限公司 Biomass ash bag deduster
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
CN108310878A (en) * 2017-08-19 2018-07-24 山东联西建环境科技有限公司 A kind of metallurgy blast furnace cast house gas cleaning sack cleaner

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102553360A (en) * 2010-06-30 2012-07-11 广州迪森热能技术股份有限公司 Biomass ash bag deduster
CN102553360B (en) * 2010-06-30 2014-05-28 广州迪森热能技术股份有限公司 Biomass ash bag deduster
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
CN108310878A (en) * 2017-08-19 2018-07-24 山东联西建环境科技有限公司 A kind of metallurgy blast furnace cast house gas cleaning sack cleaner

Similar Documents

Publication Publication Date Title
CN204919443U (en) Sweeping machine dust pelletizing system and have its sweeping machine
CN214319573U (en) Dust remover miropowder system of recycling
CN102698529B (en) Gas phase impulse back-flushing internal filtering type bag dust collector for blast furnace gas
CN201389413Y (en) Single-chamber electric bag composite dust remover
CN201085969Y (en) Resistance bag-type dust remover
CN111672254A (en) Chemical dust removal device
CN206468408U (en) A kind of diesel engine back flushing type smoke discharging and purifying device
CN207805265U (en) A kind of pulse type filter drum dust collector
CN112870899A (en) Bag type dust collector with built-in cyclone and working method thereof
CN106823641A (en) A kind of high protein fuel boiler tail gas dust cleaning apparatus
CN202715320U (en) Bag-type dust collector
CN201120228Y (en) Improved impulse bag-type dust remover
CN203829817U (en) Pulse dust cleaning bag type dust collector
CN207203771U (en) Pulse bag formula precipitron
CN102350158A (en) Device for filtering, purifying and dedusting of wind, water and mist matching to drying device
CN205613229U (en) High efficiency environmental protection dust collector
CN204530574U (en) Sweeping machine and dust pelletizing system thereof
CN202136899U (en) Wind water mist filtering, purifying and dust-removing equipment used with drying equipment
CN209885425U (en) Bag type dust collector
CN106268135A (en) One faces formula pulse bag-type dust-removing device directly
CN207119226U (en) A kind of multiple high-efficiency dust arrester
CN201320443Y (en) Water bath dust catcher
CN2865828Y (en) Pulse spraying bag-type dust collector with dispersion overflow tubesheet
CN204522558U (en) A kind of separate type sack cleaner
CN206325359U (en) A kind of twin-stage Water-bath silk net efficiency dust catcher

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: 20080716

Termination date: 20130710