CN103908862A - Stacked type electrostatic fabric filter - Google Patents
Stacked type electrostatic fabric filter Download PDFInfo
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- CN103908862A CN103908862A CN201410132895.4A CN201410132895A CN103908862A CN 103908862 A CN103908862 A CN 103908862A CN 201410132895 A CN201410132895 A CN 201410132895A CN 103908862 A CN103908862 A CN 103908862A
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- dust removing
- filter bag
- dust
- removing system
- purifying chamber
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- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
The invention discloses a stacked type electrostatic fabric filter. The stacked type electrostatic fabric filter comprises a box body, an ash hopper, an electric dust removing system and a filtering-bag dust removing system, wherein the ash hopper is arranged at the lower end of the box body; a gas purifying chamber is arranged at the inner and upper part of the box body; the bottom part of the gas purifying chamber is a pattern plate; the electric dust removing system and the filtering-bag dust removing system are positioned in the box body; the filtering-bag dust removing system is arranged on the pattern plate; the box body comprises an air inlet and an air outlet; the electric dust removing system comprises a cathode frame, an insulating suspension device, a cathode row and an anode row; the filtering-bag dust removing system comprises a filtering-bag dust removing unit which consists of a plurality of filtering bags; the electric dust removing system is positioned under the filtering-bag dust removing system; the insulated suspension device of the electric dust removing system is arranged in the gas purifying chamber; the cathode frame of the electric dust removing system penetrates through the space for the filtering-bag dust removing system, and is connected with the insulated suspension device positioned in the gas purifying chamber; and the air inlet of the box body is positioned at the lower part of the front end surface of the box body, and the air outlet of the box body is positioned on the rear end surface of the gas purifying chamber.
Description
Technical field
The present invention relates to a kind of cleaner technical field for smoke gas treatment, relate to specifically a kind of superposing type electric-bag complex dust collector.
Background technology
Existing a kind of electric-bag complex dust collector, its front portion is that electric dust removing system, rear portion are filter bag dust pelletizing system.Between electric dust removing system and filter bag dust pelletizing system, be provided with choke apparatus, the Main Function of this choke apparatus is the air-flow that electric dust removing system is flowed out, and enters in it, carry out dedusting from filter bag dust pelletizing system below.Because said structure can cause the bottom wind speed of electric dust removing system too high, thereby the efficiency of dust collection of electric dust removing system is declined.While, local filter bag was subject to washing away of high velocity air, easily produces broken bag, has therefore shortened the service life of filter bag because the flue gas flow of the front and rear portions of filter bag dust pelletizing system is inhomogeneous.In addition, for large-scale deduster, positive plate can be accomplished the height of 16 meters, can only reach 8 meters and filter bag is the longest, if adopt existing electricity bag composite construction, floor space is larger.
Summary of the invention
Technical problem to be solved by this invention is to provide a kind of superposing type electric-bag complex dust collector, and not only efficiency of dust collection is high for this superposing type electric-bag complex dust collector, and life of bag filter is long, and floor space is little.
For solving the problems of the technologies described above, a kind of superposing type electric-bag complex dust collector of the present invention, contain casing, ash bucket, electric dust removing system and filter bag dust pelletizing system, ash bucket is arranged on the lower end of casing, the internal upper part of casing is provided with air-purifying chamber, the bottom of this air-purifying chamber is card, electric dust removing system and filter bag dust pelletizing system are positioned at casing, filter bag dust pelletizing system is arranged on card, casing contains air inlet and air outlet, electric dust removing system comprises cathode frame, insulating suspension, negative electrode row and anode row, filter bag dust pelletizing system comprises the filter bag dust removing units being made up of several filter bags, described electric dust removing system is positioned at the below of filter bag dust pelletizing system, the insulating suspension of described electric dust removing system is arranged in described air-purifying chamber, the cathode frame of described electric dust removing system is through the space at filter bag dust pelletizing system place, and be connected with the insulating suspension that is positioned at air-purifying chamber, the air inlet of described casing is positioned at the bottom of casing front end face, the air outlet of described casing is positioned on the rear end face of described air-purifying chamber.
The both sides of the filter bag dust removing units in described filter bag dust pelletizing system are provided with deep bead.
The described bottom that is arranged on the insulating suspension in air-purifying chamber is provided with dust proof tube, and the upper end of this dust proof tube is connected with the sealed bottom of insulating suspension, and the lower end of this dust proof tube is fixedly connected with described air-purifying chamber bottom card.
Center line between the anode row of described electric dust removing system and adjacent negative electrode row, with the filter bag centerline in described filter bag dust pelletizing system in same plane.
Distance between the anode row of described electric dust removing system and adjacent negative electrode row, and distance between adjacent filter bag in described filter bag dust pelletizing system equates, this distance is 160mm-300mm.
Above-mentioned superposing type electric-bag complex dust collector, because electricity is positioned at the space of filter bag of dust collector dust pelletizing system bottom except dust pelletizing system, therefore floor space is little.Be positioned at the bottom of casing front end face due to air inlet simultaneously, air outlet is positioned on the rear end face of described air-purifying chamber, therefore first ash-laden gas enters electric dust removing system from air inlet and carries out dedusting, gas after electric precipitation enters in the filter bag dust pelletizing system in upper space again and carries out dedusting, thereby not only overcome the deficiency that prior art adopts choke apparatus to cause wind speed efficiency of dust collection too high and that cause in electric dust removing system bottom to decline, and overcome prior art filter bag dust pelletizing system before, the flue gas flow at rear portion is inhomogeneous, local filter bag is subject to high velocity air and washes away the generation of easy generation broken bag phenomenon.
Brief description of the drawings
Fig. 1 is the structural representation of superposing type electric-bag complex dust collector of the present invention.
Fig. 2 is the structure enlarged diagram of insulating suspension installation site in Fig. 1.
Fig. 3 is the arrangement position structure enlarged diagram of filter bag and negative electrode row and anode row in Fig. 1.
Detailed description of the invention
In Fig. 1, a kind of superposing type electric-bag complex dust collector, contains casing 2, ash bucket 5, electric dust removing system 3 and filter bag dust pelletizing system 4.Ash bucket 5 is arranged on the lower end of casing 2, and the internal upper part of casing 2 is provided with air-purifying chamber 6, and the bottom of this air-purifying chamber 6 is card 12.Electric dust removing system 3 and filter bag dust pelletizing system 4 are positioned at casing 2, and filter bag dust pelletizing system 4 is arranged on card 12, and casing 2 contains air inlet 1 and air outlet 7.Electric dust removing system 3 comprises cathode frame, insulating suspension 8, negative electrode row 14 and anode row 13.Filter bag dust pelletizing system 4 comprises the filter bag dust removing units being made up of several filter bags.Described electric dust removing system 3 is positioned at the below of filter bag dust pelletizing system 4.The insulating suspension 8 of described electric dust removing system 3 is arranged in described air-purifying chamber 6, the cathode frame of described electric dust removing system 3 is through the space at filter bag dust pelletizing system 4 places, and be connected with the insulating suspension 8 that is positioned at air-purifying chamber 6, the air inlet 1 of described casing 2 is positioned at the bottom of casing 2 front end faces, and the air outlet 7 of described casing 2 is positioned on the rear end face of described air-purifying chamber 6.In order to make ash-laden gas first carry out dedusting through electric dust removing system 3, then enter filter bag dust pelletizing system 4 and carry out dedusting, be beneficial to improve efficiency of dust collection, the both sides of the filter bag dust removing units in described filter bag dust pelletizing system 4 are provided with deep bead 9.For preventing leaking out between air-purifying chamber 6 and filter bag dust pelletizing system 4, the described bottom that is arranged on the insulating suspension 8 in air-purifying chamber 6 is provided with dust proof tube 11, the bottom 10 of the upper end of this dust proof tube 11 and insulating suspension 8 is tightly connected, and the lower end of this dust proof tube 11 is fixedly connected with described air-purifying chamber 6 bottom cards 12.During for guarantee filter bag ash removal, the passage of dirt cake between negative electrode row 14, anode row 13, land, reduce dirt cake and negative electrode row 14, anode row 13 to collide and produce reentrainment of dust, center line between the anode row 13 of described electric dust removing system 3 and adjacent negative electrode row 14, with the filter bag centerline in described filter bag dust pelletizing system 4 in same plane.Distance between the anode row 13 of described electric dust removing system 3 and adjacent negative electrode row 14, and distance between adjacent filter bag in described filter bag dust pelletizing system 4 can equate, this distance is 160mm-300mm.Above-mentioned superposing type electric-bag complex dust collector, because electricity is positioned at the space of filter bag of dust collector dust pelletizing system 4 bottoms except dust pelletizing system 3, therefore floor space is little.Be positioned at the bottom of casing 2 front end faces due to air inlet 1 simultaneously, air outlet 7 is positioned on the rear end face of described air-purifying chamber 6, therefore first ash-laden gas enters electric dust removing system 3 from air inlet 1 and carries out dedusting, gas after electric precipitation enters in the filter bag dust pelletizing system 4 in upper space again and carries out dedusting, thereby not only overcome the deficiency that prior art adopts electric dust removing system that choke apparatus causes 3 bottom wind speed efficiency of dust collection too high and that cause to decline, and overcome prior art filter bag dust pelletizing system 4 before, the flue gas flow at rear portion is inhomogeneous, local filter bag is subject to high velocity air and washes away the generation of easy generation broken bag phenomenon.In above-mentioned superposing type electric-bag complex dust collector, be positioned at the electricity of filter bag dust pelletizing system 4 belows except dust pelletizing system 3, both dedustings and charged in advance in advance also can play water conservancy diversion current-sharing simultaneously; Meanwhile, pre-charged dust directly enters filter bag dust pelletizing system 4 from electric dust removing system 3, has avoided existing electric-bag complex dust collector dust to subdue at the electric charge producing through zero potential member.Facts have proved, the dust after charged is rule and distributes on filter bag surface, can produce new high-performance filter course, and the effect of jetting deashing is also better than not charged dust.
Claims (5)
1. a superposing type electric-bag complex dust collector, contain casing, ash bucket, electric dust removing system and filter bag dust pelletizing system, ash bucket is arranged on the lower end of casing, the internal upper part of casing is provided with air-purifying chamber, the bottom of this air-purifying chamber is card, electric dust removing system and filter bag dust pelletizing system are positioned at casing, filter bag dust pelletizing system is arranged on card, casing contains air inlet and air outlet, electric dust removing system comprises cathode frame, insulating suspension, negative electrode row and anode row, filter bag dust pelletizing system comprises the filter bag dust removing units being made up of several filter bags, it is characterized in that: described electric dust removing system is positioned at the below of filter bag dust pelletizing system, the insulating suspension of described electric dust removing system is arranged in described air-purifying chamber, the cathode frame of described electric dust removing system is through the space at filter bag dust pelletizing system place, and be connected with the insulating suspension that is positioned at air-purifying chamber, the air inlet of described casing is positioned at the bottom of casing front end face, the air outlet of described casing is positioned on the rear end face of described air-purifying chamber.
2. a kind of superposing type electric-bag complex dust collector according to claim 1, is characterized in that: the both sides of the filter bag dust removing units in described filter bag dust pelletizing system are provided with deep bead.
3. a kind of superposing type electric-bag complex dust collector according to claim 1, it is characterized in that: described in be arranged on the insulating suspension in air-purifying chamber bottom be provided with dust proof tube, the upper end of this dust proof tube is connected with the sealed bottom of insulating suspension, and the lower end of this dust proof tube is fixedly connected with described air-purifying chamber bottom card.
4. a kind of superposing type electric-bag complex dust collector according to claim 3, is characterized in that: the center line between the anode row of described electric dust removing system and adjacent negative electrode row, with the filter bag centerline in described filter bag dust pelletizing system in same plane.
5. a kind of superposing type electric-bag complex dust collector according to claim 1, it is characterized in that: the distance between the anode row of described electric dust removing system and adjacent negative electrode row, and the distance between the adjacent filter bag in described filter bag dust pelletizing system equates, this distance is 160mm-300mm.
Priority Applications (1)
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CN201410132895.4A CN103908862A (en) | 2014-04-03 | 2014-04-03 | Stacked type electrostatic fabric filter |
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CN201410132895.4A CN103908862A (en) | 2014-04-03 | 2014-04-03 | Stacked type electrostatic fabric filter |
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CN201410132895.4A Pending CN103908862A (en) | 2014-04-03 | 2014-04-03 | Stacked type electrostatic fabric filter |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105148670A (en) * | 2015-09-17 | 2015-12-16 | 合肥中亚环保科技有限公司 | Bag-wet combined electrical dust remover |
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JP2000135411A (en) * | 1998-10-29 | 2000-05-16 | Tanabe Kogyo Kk | Exhaust gas treatment device and its manufacture |
US6152988A (en) * | 1997-10-22 | 2000-11-28 | The United States Of America As Represented By The Administrator Of The Environmental Protection Agency | Enhancement of electrostatic precipitation with precharged particles and electrostatic field augmented fabric filtration |
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CN101607164A (en) * | 2008-06-16 | 2009-12-23 | 福建龙净环保股份有限公司 | Vertical electrostatic fabric filter |
CN201529470U (en) * | 2009-05-27 | 2010-07-21 | 湖南湘达环保工程有限公司 | Vertical curved surface electric filter bag combined dust remover |
WO2011141827A1 (en) * | 2010-05-11 | 2011-11-17 | Flsmidth A/S | Method and plant for dedusting a stream of dust-laden gases in a hybrid filter installation |
CN102327724A (en) * | 2011-09-14 | 2012-01-25 | 福建龙净环保股份有限公司 | Electric-bag composite dust collector |
CN103203156A (en) * | 2013-05-07 | 2013-07-17 | 福建东源环保有限公司 | Embedded type electric bag compound dust remover |
CN203816432U (en) * | 2014-04-03 | 2014-09-10 | 江苏天洁环境工程有限公司 | Stacked electrostatic fabric filter |
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2014
- 2014-04-03 CN CN201410132895.4A patent/CN103908862A/en active Pending
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US6152988A (en) * | 1997-10-22 | 2000-11-28 | The United States Of America As Represented By The Administrator Of The Environmental Protection Agency | Enhancement of electrostatic precipitation with precharged particles and electrostatic field augmented fabric filtration |
JP2000135411A (en) * | 1998-10-29 | 2000-05-16 | Tanabe Kogyo Kk | Exhaust gas treatment device and its manufacture |
CN201186199Y (en) * | 2008-03-28 | 2009-01-28 | 赵璐 | Combined electric precipitator and bag precipitator |
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CN101607164A (en) * | 2008-06-16 | 2009-12-23 | 福建龙净环保股份有限公司 | Vertical electrostatic fabric filter |
CN201529470U (en) * | 2009-05-27 | 2010-07-21 | 湖南湘达环保工程有限公司 | Vertical curved surface electric filter bag combined dust remover |
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CN102327724A (en) * | 2011-09-14 | 2012-01-25 | 福建龙净环保股份有限公司 | Electric-bag composite dust collector |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN105148670A (en) * | 2015-09-17 | 2015-12-16 | 合肥中亚环保科技有限公司 | Bag-wet combined electrical dust remover |
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