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CN203060977U - Bag-type dust collector - Google Patents

Bag-type dust collector Download PDF

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Publication number
CN203060977U
CN203060977U CN 201220756451 CN201220756451U CN203060977U CN 203060977 U CN203060977 U CN 203060977U CN 201220756451 CN201220756451 CN 201220756451 CN 201220756451 U CN201220756451 U CN 201220756451U CN 203060977 U CN203060977 U CN 203060977U
Authority
CN
China
Prior art keywords
dust collector
bag
collector shell
air
deduster
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
CN 201220756451
Other languages
Chinese (zh)
Inventor
汪宗永
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.)
MAANSHAN JIAYUAN ENVIRONMENTAL PROTECTION TECHNOLOGY Co Ltd
Original Assignee
MAANSHAN JIAYUAN ENVIRONMENTAL PROTECTION TECHNOLOGY 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 MAANSHAN JIAYUAN ENVIRONMENTAL PROTECTION TECHNOLOGY Co Ltd filed Critical MAANSHAN JIAYUAN ENVIRONMENTAL PROTECTION TECHNOLOGY Co Ltd
Priority to CN 201220756451 priority Critical patent/CN203060977U/en
Application granted granted Critical
Publication of CN203060977U publication Critical patent/CN203060977U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Filtering Of Dispersed Particles In Gases (AREA)

Abstract

The utility model discloses a bag-type dust collector, belongs to the field of bag-type dust collectors and aims at providing a bag-type dust collector which is simple in structure, is wide in application range, is high in dedusting efficiency, can desulfurize high-temperature flue gases and the like. The technical scheme is as follows: the bag-type dust collector comprises a dust collector shell, a filter bag, a back blowing fan, a draught fan, an air intake pipe, an air exhaust pipe and the like; dust collector shell is fixed on the ground; the filter bag is arranged in the dust collector shell; the air intake pipe is positioned on the middle part of the dust collector shell; the draught fan and the air exhaust pipe are positioned on the upper part of the dust collector shell; the back blowing fan is positioned on the top of the dust collector shell; the draught fan is connected with the air exhaust pipe; the air intake pipe is provided with an adder funnel and a cold air blowing system; a planetary feeder is arranged between the air intake pipe and the adder funnel; a dust hopper is positioned on the lower part of the dust collector shell; and a dual-stage reversing turning plate material discharge device is positioned at the lower part of the dust hopper.

Description

Sack cleaner
Technical field
The utility model relates to a kind of deduster, is specifically related to a kind of sack cleaner.
Background technology
At present, domestic existing rotary counter-blowing sack cleaner, great majority are applicable to the normal temperature dedusting, udst separation for high temperature flue gases such as fuel boiler, kiln, spray drying towers, be easy to stick with paste the phenomenon of bag, coking, corrosion filter bag, and exist filter efficiency low, not easy-to-clean ash, high-temperature flue gas can not desulfurization etc. defective, therefore be subjected to very big restriction in the use.
Summary of the invention
The purpose of this utility model is to overcome weak point of the prior art, provides a kind of simple in structure, wide accommodation, and the efficiency of dust collection height, and can be to the sack cleaner of high-temperature flue gas desulfurization.
For achieving the above object, the utility model is by the following technical solutions: sack cleaner, comprise: the deduster housing, filter bag, back blowing machine, air-introduced machine, blast pipe, discharge pipe etc., the deduster housing fixes by support and ground, filter bag is in the deduster housing, blast pipe is positioned at the middle part of deduster housing, air-introduced machine, discharge pipe is positioned at the top of deduster housing, back blowing machine is positioned at the top of deduster housing, air-introduced machine links to each other with discharge pipe, and the adder funnel is housed on the blast pipe, quenching system is provided with the planet dispenser between blast pipe and adder funnel, dust hopper is positioned at the deduster lower housing portion, and twin-stage turnover panel discharger is positioned at the bottom of dust hopper.
The beneficial effects of the utility model are, have simple in structure, applied widely, efficiency of dust collection height, and advantages such as pair high-temperature flue gas desulfurization are arranged.
Description of drawings
Fig. 1 is structural representation of the present utility model.
Among the figure: 1, quenching system; 2, blast pipe; 3, planet dispenser; 4, adder funnel; 5, deduster housing; 6, filter bag; 7, back blowing machine; 8, discharge pipe; 9, air-introduced machine; 10, dust hopper; 11, twin-stage turnover panel discharger; 12, support
Specific implementation method
Among the embodiment shown in Figure 1, a kind of sack cleaner, comprise: deduster housing 5, filter bag 6, back blowing machine 7, air-introduced machine 9, blast pipe 2, discharge pipe 8 etc., deduster housing 5 fixes by support 12 and ground, filter bag 6 is in deduster housing 5, blast pipe 2 is positioned at the middle part of deduster housing 5, air-introduced machine 9, discharge pipe 8 is positioned at the top of deduster housing 5, back blowing machine 7 is positioned at the top of deduster housing 5, air-introduced machine 9 links to each other with discharge pipe 8, adder funnel 4 is housed on the blast pipe 2, quenching system 1,4 in blast pipe 2 and adder funnel are provided with planet dispenser 3, dust hopper 10 is positioned at deduster housing 5 bottoms, and twin-stage turnover panel discharger 11 is positioned at the bottom of dust hopper 10.Operation principle of the present utility model is, flue gas enters deduster housing 5 by blast pipe 2, when deduster housing 5 internal resistances rise to 1200Pa, back blowing machine 7 carries out reverse gas cleaning, when deduster housing 5 internal resistances drop to 800Pa, stop blowback, filter aid in the adder funnel 4 is under the effect of planet dispenser 3 simultaneously, be mixed in the deduster housing 5 by blast pipe 2 and flue gas by some cycles, the filter aid composition is that silicate material (has flyash, calcium oxide, talcum powder mixes by a certain percentage, granularity requirements is below 0.5mm), the addition of filter aid can arbitrarily be adjusted according to the content of smoke dust, the filter bag 6 surface formation that filter aid is adsorbed on behind the deashing help filtering layer, help filtering layer to form back planet dispenser 3 and stop to add filter aid, dust in the high-temperature flue gas is helping filtering layer to adsorb, filter, part pernicious gas wherein is (as sulphur, acid, alkali etc.) also chemical reaction can take place with filter aid, efficiency of dust collection is improved, the filtering layer that helps that filter bag 6 surfaces form can effectively prevent from sticking with paste bag, coking, and can reduce corrosion to filter bag 6, improve the service life of filter bag 6, dust falls into dust hopper 10 behind the deashing, by being positioned at twin-stage turnover panel discharger 11 emptyings of dust collecting opening 10 bottoms, when deduster continuous operation in high-temperature flue gas, temperature in the deduster housing 5 can constantly increase, will inevitably influence dust removing effects, and reduced the service life of filter bag 6, thereby the quenching system on the blast pipe 21 can be sent into cold wind by blast pipe 2 according to variation of temperature in the deduster housing 5 in trend deduster housing 5, so that the temperature in the deduster housing 5 keeps stable, to guarantee the service life of efficiency of dust collection and equipment.This use new structure is simple, and the scope of application is wide, the efficiency of dust collection height, and advantage such as pair high-temperature flue gas desulfurization is arranged, be the desirable substitute products of existing sack cleaner.

Claims (1)

1. sack cleaner, comprise sack cleaner, it is characterized in that: described deduster housing fixes by support and ground, filter bag is in the deduster housing, blast pipe is positioned at the middle part of deduster housing, air-introduced machine, discharge pipe are positioned at the top of deduster housing, back blowing machine is positioned at the top of deduster housing, air-introduced machine links to each other with discharge pipe, adder funnel, quenching system are housed on the blast pipe, be provided with the planet dispenser between blast pipe and adder funnel, dust hopper is positioned at the deduster lower housing portion, and twin-stage turnover panel discharger is positioned at the bottom of dust hopper.
CN 201220756451 2012-12-22 2012-12-22 Bag-type dust collector Expired - Fee Related CN203060977U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201220756451 CN203060977U (en) 2012-12-22 2012-12-22 Bag-type dust collector

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201220756451 CN203060977U (en) 2012-12-22 2012-12-22 Bag-type dust collector

Publications (1)

Publication Number Publication Date
CN203060977U true CN203060977U (en) 2013-07-17

Family

ID=48759807

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201220756451 Expired - Fee Related CN203060977U (en) 2012-12-22 2012-12-22 Bag-type dust collector

Country Status (1)

Country Link
CN (1) CN203060977U (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104607038A (en) * 2015-01-20 2015-05-13 山东环冠科技有限公司 Dedusting and denitrification integrated equipment and production technology of component of dedusting and denitrification integrated equipment
CN104984605A (en) * 2015-06-30 2015-10-21 成都市新都区鑫悦空气净化设备厂 Woodworking central dust remover
CN108771922A (en) * 2018-07-02 2018-11-09 黑龙江兰德超声科技股份有限公司 Industrial waste gas processing dust accumulation recycle device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104607038A (en) * 2015-01-20 2015-05-13 山东环冠科技有限公司 Dedusting and denitrification integrated equipment and production technology of component of dedusting and denitrification integrated equipment
CN104984605A (en) * 2015-06-30 2015-10-21 成都市新都区鑫悦空气净化设备厂 Woodworking central dust remover
CN108771922A (en) * 2018-07-02 2018-11-09 黑龙江兰德超声科技股份有限公司 Industrial waste gas processing dust accumulation recycle device

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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: 20130717

Termination date: 20131222