[go: up one dir, main page]

CN102091496A - Double-effect dust remover with long service life - Google Patents

Double-effect dust remover with long service life Download PDF

Info

Publication number
CN102091496A
CN102091496A CN 201110008987 CN201110008987A CN102091496A CN 102091496 A CN102091496 A CN 102091496A CN 201110008987 CN201110008987 CN 201110008987 CN 201110008987 A CN201110008987 A CN 201110008987A CN 102091496 A CN102091496 A CN 102091496A
Authority
CN
China
Prior art keywords
dust
bag
air inlet
double
filter cylinder
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
Application number
CN 201110008987
Other languages
Chinese (zh)
Inventor
陈迅
刘佳佳
倪春伟
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.)
NANTONG HUANGPU MACHINERY MANUFACTURE CO Ltd
Original Assignee
NANTONG HUANGPU MACHINERY MANUFACTURE 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 NANTONG HUANGPU MACHINERY MANUFACTURE CO Ltd filed Critical NANTONG HUANGPU MACHINERY MANUFACTURE CO Ltd
Priority to CN 201110008987 priority Critical patent/CN102091496A/en
Publication of CN102091496A publication Critical patent/CN102091496A/en
Pending legal-status Critical Current

Links

Landscapes

  • Filtering Of Dispersed Particles In Gases (AREA)

Abstract

The invention discloses a double-effect dust remover with long service life, which comprises a filter drum, wherein a helical air inlet channel is arranged on the outer wall of the filter drum, the upper end of the helical air inlet channel is provided with an air inlet, the lower end of the helical air inlet channel is communicated with the lower part of the filter drum, and a cloth bag dust-removing device is arranged in the filter drum. The double-effect dust remover has the advantages of reasonable structure, low emission concentration and high dust-removing efficiency; when airflow rotates, dust particles in the airflow are separated from the airflow under the action of an eccentric force, thus the advantages of two dust-removing principles are integrated by combining the dust-removing effect with two dust-removing principles of achieving the dust-removing purpose through filtration of a filter bag.

Description

Economic benefits and social benefits long-life type deduster
Technical field
The present invention relates to a kind of deduster.
Background technology
Industrial dedusting equipment is the equipment of udst separation industrial gasses, and it is one of important component part of environment protection equipment.Present domestic deduster principle mainly contains and 1. relies on the gravity effect to make that the particle natural subsidence reaches the dedusting purpose in the dusty gas.The cleaner characteristics of this principle be simple structure, cost low, be convenient to maintenance management and can handle high-temperature gas, resistance is generally 50~150Pa, efficiency of dust collection is lower, generally can only remove the bulky grain greater than 40~50 microns.2. air-flow is when rotating, and the dust granules in the air-flow can reach dust removing effects because separated by action of centrifugal force from air-flow.Utilize the deduster of this principle simple in structure, make to install easily and maintenance management is convenient, the cost running cost is low, 3. efficiency of dust collection is relatively lower filters by filter bag, reach the dedusting purpose, this uses dust collection method efficiency of dust collection height, the pressure loss is about 800~1500Pa, filtration meets higher dusty gas and drop or the liquid film of 4. utilizing, the device structure of this dust collection method is simple, purification efficiency is high, movement-less part own, fault are few, be fit to high temperature does the humid gas dedusting, but the handling problem and the equipment corrosion problem of water are arranged after the dedusting.When 5. the dust grit is by the high-voltage electrostatic field in the flue gas; bump and charged (or charged in the ions diffusion motion) with interelectrode negative ions and electronics; with the grit of going up electronics and ion anisotropy electrode movement under the effect of electric field force and long-pending being attached on the different in nature electrode; make the dust on the electrode fall into the collection ash bucket by modes such as rappings; flue gas by electric cleaner is purified; reach the protection atmosphere, the purpose of protection environment.This dust collection method can be handled the high-temperature gas up to 500 ℃, can the catch liquid droplet; Resistance is little, and running expense is low, overhauls cumbersomely, and efficiency of dust collection is lower than bag-type dust.
Summary of the invention
The object of the present invention is to provide a kind of rational in infrastructure, the economic benefits and social benefits long-life type deduster that concentration of emission is low, efficiency of dust collection is high.
Technical solution of the present invention is:
A kind of economic benefits and social benefits long-life type deduster is characterized in that: comprise filter cylinder, the spirality air intake passage is set on the cartridge exine, the upper end of spirality air intake passage is provided with air inlet, and the lower end of spirality air intake passage communicates with the filter cylinder bottom, and bag-type dust collector is set in the filter cylinder.
The bottom of filter cylinder is the cone form.
Bag-type dust collector comprises dust-removal cloth-bag, and the dust-removal cloth-bag upper end communicates with the winding-up pipe, and the winding-up pipe is connected with blast pipe.
The present invention is rational in infrastructure; concentration of emission is low, efficiency of dust collection is high; with air-flow when rotating; dust granules in the air-flow can be because be separated from air-flow by action of centrifugal force; reach dust removing effects and filter by filter bag; two kinds of dust-cleaning principles that reach the dedusting purpose combine, the advantage of two kinds of dust-cleaning principles of set.
The present invention compares efficiency of dust collection with common cyclone dust collectors and has improved, common cyclone dust collectors efficiency of dust collection is between 50%~90%, efficiency of dust collection of the present invention is up to 99.9%, because the whirlwind bag dust collector is earlier through cyclone dust removal, big dust granules separates under centrifugal force and gravity effect, dust granularity when advancing filter bag is less, has prolonged the service life of filter bag.Can prevent " the again absorption " of filter cylinder outer surface laying dust behind deashing; Filter area in the unit are is big, is applicable to indoor installation, and can be placed on the roof and outdoor; Behind big-and-middle-sized whirlwind filter bag configuring pipes and blower fan, the chimney, can form a complete dust pelletizing system.Behind small-sized the configuration caster and power line, can be used as portable unit and use.
Description of drawings
The invention will be further described below in conjunction with drawings and Examples.
Fig. 1 is the structural representation of one embodiment of the invention.
Fig. 2 is Fig. 1 embodiment external structure figure.
The specific embodiment
A kind of economic benefits and social benefits long-life type deduster comprises filter cylinder 1, and spirality air intake passage 2 is set on the cartridge exine, and the upper end of spirality air intake passage is provided with rotation air inlet 3, and the lower end of spirality air intake passage communicates with the filter cylinder bottom, and bag-type dust collector is set in the filter cylinder.The bottom of filter cylinder is cone 7 forms.
Bag-type dust collector comprises dust-removal cloth-bag 4, and the dust-removal cloth-bag upper end communicates with winding-up pipe 5, and the winding-up pipe is connected with blast pipe 6.
When the present invention worked, dusty gas was entered by air inlet, did from top to bottom rotatablely moving earlier along rotating channel, and this motion is called outer eddy flow.In the air-flow rotary course, form very big centrifugal force, big grit is under action of centrifugal force, be thrown toward outer wall gradually, and in gravity effect lower edge outside wall surface rotation whereabouts, separate with flue gas, until the storage ash bin, remaining dusty gas is toward rising, by the comprehensive effects such as inertia, collision, sieve worry, interception and static on filter bag surface, make dust settling on the filter bag surface and form dust layer, purified gas by blast pipe row to atmosphere.

Claims (3)

1. economic benefits and social benefits long-life type deduster, it is characterized in that: comprise filter cylinder, the spirality air intake passage is set on the cartridge exine, the upper end of spirality air intake passage is provided with air inlet, the lower end of spirality air intake passage communicates with the filter cylinder bottom, and bag-type dust collector is set in the filter cylinder.
2. economic benefits and social benefits long-life type deduster according to claim 1, it is characterized in that: the bottom of filter cylinder is the cone form.
3. economic benefits and social benefits long-life type deduster according to claim 1 and 2, it is characterized in that: bag-type dust collector comprises dust-removal cloth-bag, and the dust-removal cloth-bag upper end communicates with the winding-up pipe, and the winding-up pipe is connected with blast pipe.
CN 201110008987 2011-01-17 2011-01-17 Double-effect dust remover with long service life Pending CN102091496A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201110008987 CN102091496A (en) 2011-01-17 2011-01-17 Double-effect dust remover with long service life

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201110008987 CN102091496A (en) 2011-01-17 2011-01-17 Double-effect dust remover with long service life

Publications (1)

Publication Number Publication Date
CN102091496A true CN102091496A (en) 2011-06-15

Family

ID=44124871

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201110008987 Pending CN102091496A (en) 2011-01-17 2011-01-17 Double-effect dust remover with long service life

Country Status (1)

Country Link
CN (1) CN102091496A (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103331070A (en) * 2013-06-13 2013-10-02 张玉伟 Cyclic wet filtration dust remover
CN103432856A (en) * 2013-09-10 2013-12-11 苏州新区枫桥净化设备厂 Centrifugal dust collector
CN103706152A (en) * 2014-01-20 2014-04-09 青岛啤酒股份有限公司 Waste kieselguhr collecting equipment and method for treating waste kieselguhr by using same
CN105564008A (en) * 2016-03-09 2016-05-11 苏州华策纺织科技有限公司 Modified dust removal device of rotary screen printing machine
CN106178791A (en) * 2016-08-29 2016-12-07 合肥合意环保科技工程有限公司 A kind of dust removing device for refuse incineration
CN106215556A (en) * 2016-08-29 2016-12-14 合肥合意环保科技工程有限公司 A kind of shaft kiln glass cleaner
CN110652830A (en) * 2019-11-18 2020-01-07 秦皇岛中青冶金阀门有限公司 Multi-pipe cyclone dust collector and dust collection method
CN111905537A (en) * 2020-07-10 2020-11-10 司昊源 Tail gas desulfurization device
CN114522494A (en) * 2020-11-03 2022-05-24 张云轩 Powder flow separator

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1033163A (en) * 1987-11-18 1989-05-31 南京工学院 Bag-type whirlwind dust remover
CN2055064U (en) * 1989-08-09 1990-03-28 陆莹 Purifier
CN201997218U (en) * 2011-01-17 2011-10-05 南通市煌埔机械制造有限公司 Double-effect long-service-life type dust remover

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1033163A (en) * 1987-11-18 1989-05-31 南京工学院 Bag-type whirlwind dust remover
CN2055064U (en) * 1989-08-09 1990-03-28 陆莹 Purifier
CN201997218U (en) * 2011-01-17 2011-10-05 南通市煌埔机械制造有限公司 Double-effect long-service-life type dust remover

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103331070A (en) * 2013-06-13 2013-10-02 张玉伟 Cyclic wet filtration dust remover
CN103432856A (en) * 2013-09-10 2013-12-11 苏州新区枫桥净化设备厂 Centrifugal dust collector
CN103706152A (en) * 2014-01-20 2014-04-09 青岛啤酒股份有限公司 Waste kieselguhr collecting equipment and method for treating waste kieselguhr by using same
CN103706152B (en) * 2014-01-20 2015-04-29 青岛啤酒股份有限公司 Waste kieselguhr collecting equipment and method for treating waste kieselguhr by using same
CN105564008A (en) * 2016-03-09 2016-05-11 苏州华策纺织科技有限公司 Modified dust removal device of rotary screen printing machine
CN106178791A (en) * 2016-08-29 2016-12-07 合肥合意环保科技工程有限公司 A kind of dust removing device for refuse incineration
CN106215556A (en) * 2016-08-29 2016-12-14 合肥合意环保科技工程有限公司 A kind of shaft kiln glass cleaner
CN110652830A (en) * 2019-11-18 2020-01-07 秦皇岛中青冶金阀门有限公司 Multi-pipe cyclone dust collector and dust collection method
CN111905537A (en) * 2020-07-10 2020-11-10 司昊源 Tail gas desulfurization device
CN114522494A (en) * 2020-11-03 2022-05-24 张云轩 Powder flow separator

Similar Documents

Publication Publication Date Title
CN102091496A (en) Double-effect dust remover with long service life
CN102553382B (en) Double-row filter bag embedded type electric bag compound dust catcher with electric field area at front stage
CN106237745A (en) Rotary grate automatic dust removing apparatus
CN107224828B (en) High speed smoke processing system
CN107648975B (en) Dust removal method and device for ultralow emission of dust-containing gas
CN107096309B (en) A kind of filtering cartridge combined dust-remover
CN202844811U (en) Electric-bag combined dust collection device
CN103252146B (en) A kind of vertical electrostatic precipitator integrating gravity, cyclone dust collection
CN102600994B (en) Electric spraying cyclone dust collector and application thereof
CN106422666A (en) Coal-fired power plant smoke gas circulating adsorbent demercuration device and demercuration method
CN204051328U (en) A kind of airflow uniform distribution type embedded-type electric bag compound dust-collection device
CN201389414Y (en) A high-efficiency electric bag dust collector
CN206355790U (en) A kind of coal-fired plant flue gas circulation absorption agent mercury removal device
CN202146697U (en) High temperature flue gas foam ceramic rotary dust collector
CN201997218U (en) Double-effect long-service-life type dust remover
CN203540269U (en) Composite dust remover
CN203540242U (en) Separating pulse dust remover of high concentration dust
CN205699984U (en) A kind of orientation dust removal machine
CN203315950U (en) Efficient pretreatment device for smoke gas of industrial silicon '75 ferrosilicon' ore smelting furnace
CN201988305U (en) Three-level serially-connected dust collection device
CN202490694U (en) Electric spray dust collector
CN203342569U (en) Dust collector provided with air box and pulse bags
CN103752121A (en) Combined dust remover applied to high-concentration dust
CN108126453A (en) A kind of NEW TYPE OF COMPOSITE dedusting takes off mist device
CN202683001U (en) Grading dedusting system

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C12 Rejection of a patent application after its publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20110615