CN113731091A - Asymmetric electrostatic enhancement electric bag coupling dust remover - Google Patents

Asymmetric electrostatic enhancement electric bag coupling dust remover Download PDF

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Publication number
CN113731091A
CN113731091A CN202111071370.0A CN202111071370A CN113731091A CN 113731091 A CN113731091 A CN 113731091A CN 202111071370 A CN202111071370 A CN 202111071370A CN 113731091 A CN113731091 A CN 113731091A
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China
Prior art keywords
electric field
cloth bag
anode plate
ash
folded
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CN202111071370.0A
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CN113731091B (en
Inventor
卓建坤
李海龙
吴逸凡
李水清
姚强
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Tsinghua University
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Tsinghua University
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D50/00Combinations of methods or devices for separating particles from gases or vapours

Abstract

The invention discloses an asymmetric static enhanced electric bag coupling dust remover which comprises an inlet flue, a shell, an ash bucket, a gas purifying chamber and an outlet flue. At least two electric field channels and a cloth bag area are arranged in the shell, and the inlet flue is communicated with the electric field channels and the cloth bag area in sequence. The electric field channel comprises a non-porous anode plate for generating an electric field, a folded anode plate and a cathode wire frame arranged in the folded anode plate, and the cloth bag region is arranged between the two electric field channels. The folded anode plate is arranged according to the electric field channel and the cloth bag area. The folding anode plate is provided with a plurality of folding slits which can communicate the electric field channel with the cloth bag area, so that the airflow can pass through the folding slits in a streaming mode. The bag area is provided with a plurality of filter bags, and the bottom is provided with a separating hopper. The separating hopper is positioned at the top of the ash hopper, an ash discharging channel is formed at the bottom of the separating hopper and communicated with the ash hopper, and a star-shaped ash discharger or a middle partition plate is arranged at the upper part of the ash discharging channel. The invention has the advantages of high dust removal efficiency, reduced cloth bag load, prolonged cloth bag service life, etc.

Description

Asymmetric electrostatic enhancement electric bag coupling dust remover
Technical Field
The invention relates to an asymmetric electrostatic enhancement electrostatic bag coupling dust remover, and belongs to the technical field of dust removal.
Background
In recent years, with the continuous advance of the country in deep removal of atmospheric pollutants, the composite electric bag dust removal technology has the characteristics of long service life of a cloth bag, high efficiency and the like, and becomes one of main technical routes for realizing ultralow emission of smoke dust. The embedded compact composite electrostatic bag technology realizes the coupling of the electrostatic region and the cloth bag region by utilizing the staggered arrangement of the electrostatic region and the cloth bag region, thereby realizing the operation with high filtering wind speed, low resistance and high efficiency. In order to improve the dust removal efficiency of the electrostatic area, the prior art respectively adopts methods of a preposed electrostatic dust removal area without an opening, an additional hood for the opening of the dust collection plate, or a single preposed electrostatic dust removal area. However, the effect is not good in practical operation, and firstly, the electric field area is short-circuited with the airflow at the bottom of the cloth bag area; secondly, the dust collecting plate is provided with holes, so that the problems of insufficient charge of particles, over-small dust collecting area and the like of the structure are caused, the dust collecting efficiency of an electrostatic region cannot be effectively improved, the filtering load of a cloth bag is increased, the resistance is increased, and the dust collecting efficiency is finally influenced.
Disclosure of Invention
The invention aims to provide an asymmetric electrostatic enhancement electric bag coupling dust remover, which forms a non-uniform flow charge electric field by adopting a charge channel in an asymmetric arrangement form of an anode plate and a folded anode plate, further improves charge efficiency and dust collection area, and realizes high-efficiency removal of fine particles.
The invention is realized by the following technical scheme:
the asymmetric electrostatic enhancement electric bag coupling dust collector comprises an inlet flue, a shell, an ash bucket, an air purifying chamber and an outlet flue, wherein the inlet flue is arranged at the front end of the shell, the air purifying chamber and the outlet flue are arranged above the shell, the ash bucket is arranged at the bottom of the shell, at least two electric field channels and a cloth bag area are arranged in the shell, and the inlet flue is sequentially communicated with the electric field channels and the cloth bag area.
The electric field channel comprises a non-porous anode plate for generating an electric field, a folded anode plate and a cathode wire frame arranged between the non-porous anode plate and the folded anode plate, and the non-porous anode plate and the folded anode plate are arranged on two sides of the electric field channel in parallel; the cloth bag area is arranged between the two electric field channels, the folded anode plate is arranged in a partition mode shared by the electric field channels and the cloth bag area, and a plurality of folding slits capable of communicating the electric field channels and the cloth bag area are formed in the folded anode plate, so that air flow can pass through the folding slits in a streaming mode.
The bag area is internally provided with a plurality of filter bags, the bottom of the bag area is provided with a plurality of baffles which are obliquely arranged in opposite directions to form a separation hopper; the separating hopper is positioned at the top of the ash hopper, an ash discharging channel is formed at the bottom of the separating hopper and communicated with the ash hopper, and a star-shaped ash discharger or a middle partition plate is arranged at the upper part of the ash discharging channel.
Furthermore, when more than two cloth bag zones are arranged, an electric field channel is arranged between every two adjacent cloth bag zones, the electric field channel at least comprises a non-porous anode plate and two folded anode plates, and a cathode wire frame is arranged between the non-porous anode plate and the folded anode plates.
Further, the folding gap comprises a gap and a folding baffle arranged on the surface of the gap; the folding baffle is obliquely arranged towards one side of the electric field channel and is arranged at an acute angle with the folding anode plate along the air flow.
Furthermore, the angle alpha between the folding baffle plate and the folding anode plate is 0< alpha is less than or equal to 30 degrees, and the width of the folding baffle plate is greater than or equal to the width of the gap.
Furthermore, a pre-dedusting area is arranged at the front part of the cloth bag area.
Furthermore, the middle partition board is an inverted V-shaped board.
Furthermore, a uniform distribution plate is arranged in the inlet flue.
Compared with the prior art, the invention has the following advantages and beneficial effects:
the sampling folded anode plate replaces a porous anode plate used by a conventional coupling electric bag, so that the effective dust collecting area of the anode plate is increased while the effective flow area is ensured; the dust-containing flue gas flows around the folding slit to form a vortex region, so that the inertial separation of large-particle dust is facilitated, and the removal efficiency of the charged dust in the electric field region is improved; the arrangement of the separating hopper effectively avoids the short circuit of the air flow of the high-dust-content flue gas at the bottom of the electric field area and the cloth bag area, avoids the increase of the cloth bag filtering load, can reduce the cloth bag dust removing frequency, and effectively prolongs the service life of the cloth bag.
Drawings
Fig. 1 is a schematic diagram of the internal structure of an asymmetric electrostatic enhanced electrostatic bag coupled dust collector according to the present invention.
Fig. 2 is a schematic top view of an asymmetric electrostatic enhancement electrostatic bag coupled dust collector according to the present invention.
Fig. 3 is a schematic structural diagram of a folded anode plate of the asymmetric electrostatic enhanced electrostatic bag coupling dust collector according to the invention.
Fig. 4 is a schematic flow diagram of an asymmetric electrostatically enhanced electrostatic precipitator with an electrically coupled precipitator according to the present invention.
Fig. 5 is a schematic view of a folded seam structure of the folded anode plate according to the present invention.
Fig. 6 is a schematic structural view of a separating hopper according to one embodiment of the present invention.
Fig. 7 is a schematic view of a structure of a partitioned bucket according to another embodiment of the present invention.
In the figure: 1-a housing; 2-electric field channel; 21-folding the anode plate; 211-a nip; 212-folding flaps; 22-non-porous anode plate; 23-cathode wire frame; 3-a cloth bag area; 31-a filter bag; 4-separating bucket; 41-star-type ash discharger; 42-a median septum; 5-ash bucket; 6-inlet flue; 61-uniform distribution plate; 7-air purifying chamber; 8-outlet flue.
Detailed Description
The following describes the embodiments and operation of the present invention with reference to the accompanying drawings. While exemplary embodiments of the invention are shown in the drawings, it should be understood that the invention can be embodied in various forms and should not be limited to the embodiments set forth herein. Rather, these embodiments are provided so that this disclosure will be thorough and complete, and will fully convey the scope of the invention to those skilled in the art.
The terms of orientation such as up, down, left, right, front, and rear in the present specification are established based on the positional relationship shown in the drawings. The corresponding positional relationship may also vary depending on the drawings, and therefore, should not be construed as limiting the scope of protection. Furthermore, the terms "first", "second", etc. are used for descriptive purposes only and are not to be construed as indicating or implying relative importance or implicitly indicating the number of technical features indicated. In the description of the following examples, "plurality" means two or more unless specifically limited otherwise.
The invention provides an asymmetric electrostatic enhancement electric bag coupling dust remover, which is an embedded electric bag composite dust remover and comprises an electric field area and a cloth bag area which are relatively independent. As shown in figures 1 and 2, the asymmetric electrostatic enhancement electrostatic bag coupling dust remover comprises an inlet flue 6, a shell 1, an ash bucket 5, a gas purifying chamber 7 and an outlet flue 8. The inlet flue 6 is arranged at the front end of the shell 1, when the flue gas enters the inlet flue 6, in order to achieve uniform gas distribution, the inlet flue 6 is arranged according to the bell mouth, and is internally provided with the uniform distribution plate 61, preferably, two layers of uniform distribution plates are arranged, and the inlet flue comprises a first uniform distribution plate and a second uniform distribution plate. In one embodiment, the first uniform distribution plate has an aperture ratio of 40% to 50% and the second uniform distribution plate has an aperture ratio of 30% to 45%.
The outlet flue 8 is arranged above the shell 1, a gas purifying chamber 7 is usually arranged above the shell 1, and the flue gas after electrostatic dust collection in the electric field area enters the cloth bag area, penetrates through the filter bag, is subjected to bag type dust collection, is converged to the gas purifying chamber from the central area of the filter bag, and is discharged out of the dust collector from the outlet flue. The ash hopper 5 is arranged at the bottom of the shell 1. The working mode of the bag-type area (bag-type dust remover) can be understood and imagined by a person skilled in the art, and is not described in detail herein.
At least two electric field channels 2 and a cloth bag area 3 are arranged in the shell, the electric field channels 2 are communicated with an inlet flue 6, and flue gas is uniformly distributed and shunted to each electric field channel through uniform distribution plates. The electric field channel comprises a non-porous anode plate 22, a folded anode plate 21, and a cathode wire frame 23 disposed intermediate the non-porous anode plate and the folded anode plate. The non-porous anode plate and the folded anode plate are arranged on two sides of the electric field channel in parallel. An asymmetric electric field is generated between the anode plate (comprising the non-porous anode plate and the folded anode plate) and the cathode wire frame. The cloth bag area is arranged between the two electric field channels, the folded anode plate is arranged on one side close to the cloth bag area and is arranged in a partition plate mode shared by the electric field channels and the cloth bag area. The folded anode plate is provided with a plurality of folded gaps which can communicate the electric field channel with the cloth bag area and are used as channels for smoke to enter the cloth bag area from the electric field channel (electric field area). The bag area is internally provided with a plurality of filter bags.
As shown in fig. 3, the folding nip includes a nip 211 and a folding flap 212 disposed on a surface of the nip. The opening of the folding baffle is obliquely arranged towards one side of the electric field channel, and the folding baffle and the folding anode plate are arranged in a straight-air acute angle manner, so that flue gas flow passes through the folding baffle from front to back in the electric field channel and then flows around to enter the cloth bag area through the folding gap, as shown in fig. 4. As a preferable technical scheme, the angle alpha between the folding baffle plate and the folding anode plate is 0< alpha < 30 degrees, and the width b of the folding baffle plate is more than or equal to the width of the gap, as shown in figure 5.
When the dust-containing flue gas to be dedusted flows through the electric field area, the dust in the flue gas is charged under the action of the electric field. On one hand, large particle dust in the flue gas is easily adsorbed on the surface layers of the non-porous anode plate and the folded anode plate, and most of dust load is removed. On the other hand, when the dust-containing smoke passes through the folding baffle, the smoke enters the cloth bag area through the folding gap in a streaming mode due to the action of inertia force, and large-particle dust which is not collected by an electric field is difficult to enter the cloth bag area in a reverse flow mode. The fine particle dust entering the cloth bag area along with the flue gas can form a loose and irregular filtering surface layer on the surface layer of the filter bag due to the same charge, so that the fine particle removal efficiency can be improved, the pressure loss of the filter bag can be reduced, and a better ventilation effect can be ensured.
In fact, the dust-containing flue gas can further form a vortex region through the folding baffle, thereby increasing the agglomeration and the residence time of the dust in an electric field region and being beneficial to high-efficiency dust removal. Meanwhile, the dust collecting area is not reduced by the folded anode plate, the shielding effect on the discharge sparks possibly generated by the cathode wire is achieved, and the firing problem of the cloth bag caused by the sparks is avoided.
The bottom of the cloth bag area is provided with a plurality of baffles, usually a group of 4 baffles, which are obliquely arranged in opposite directions to form a separation hopper. The separating hopper is positioned at the top of the ash hopper, and the mode of implementation which is often optimized is to arrange a plurality of separating hoppers. The arrangement of the separation hopper is mainly used for avoiding the short circuit of the flue gas caused by the flue gas entering the cloth bag area from the lower part of the electric field area. An ash discharge channel formed at the bottom of the separating hopper is communicated with the ash hopper, and a star-shaped ash discharger is arranged in the ash discharge channel, as shown in figure 6. Through the start-up of star ash discharger, can transfer the dirt that the sack district was collected to the ash bucket in, avoid the flue gas to go upward from here simultaneously. Another embodiment is as shown in fig. 7, a middle partition board is arranged in the ash discharging channel, the middle partition board selects an inverted V-shaped board, certain gaps are reserved on two sides of the inverted V-shaped board, when dust collected in a cloth bag area is accumulated to a certain degree, the dust can slide down into the ash bucket through the gaps under the action of gravity, meanwhile, the inverted V-shaped board greatly reduces the upward channel of air flow, the gap between the inverted V-shaped board and the ash discharging channel is blocked by the collected dust, and the upward channeling of flue gas is avoided.
Preferably, the front part of the cloth bag area is provided with a pre-dedusting area. As an optimized technical scheme, the folding anode plates at two sides of the pre-dust-removing area are provided with less or no folding seams, and the folding seams are intensively arranged in the area with the filter bag.
When the dust collector is provided with a plurality of cloth bag areas, correspondingly, the electric field channels are also increased, and the structure of one cloth bag area and two electric field channels is usually formed into a modular configuration. At this time, two electric field channels as described above are arranged between two adjacent cloth bag regions, that is, each electric field channel includes a non-porous anode plate, a folded anode plate, and a cathode wire frame arranged between the non-porous anode plate and the folded anode plate. And as mentioned above, the folded anode plate is arranged at one side close to the cloth bag area and is arranged in a partition mode shared by the electric field channel and the cloth bag area. Therefore, two adjacent electric field channels can be separated by a non-porous anode plate, and the electric field channel between two adjacent cloth bag regions can be called a double-electric-field channel.
An ash cleaning device is also arranged in the shell. The anode plate (comprising a non-porous anode plate and a folded anode plate) is provided with a dust cleaning device, preferably a mechanical rapping dust cleaning device. The filter bag is preferably a pulse ash removal device. The arrangement and operation of the ash removal device can be understood and envisioned by one of ordinary skill in the art and will not be described in detail herein.
The above description is only a preferred embodiment of the present invention and is not intended to limit the present invention, and various modifications and changes may be made by those skilled in the art. Any modification, equivalent replacement, or improvement made within the spirit and principle of the present invention should be included in the protection scope of the present invention.

Claims (7)

1. The asymmetric electrostatic enhancement electric bag coupling dust collector comprises an inlet flue, a shell, an ash bucket and an outlet flue, wherein the inlet flue is arranged at the front end of the shell, the outlet flue is arranged above the shell, and the ash bucket is arranged at the bottom of the shell;
the electric field channel comprises a non-porous anode plate for generating an electric field, a folded anode plate and a cathode wire frame arranged between the non-porous anode plate and the folded anode plate, and the non-porous anode plate and the folded anode plate are arranged on two sides of the electric field channel in parallel; the cloth bag area is arranged between the two electric field channels, the folded anode plate is arranged in a partition mode shared by the electric field channels and the cloth bag area, and a plurality of folded cracks capable of communicating the electric field channels and the cloth bag area are formed in the folded anode plate;
a plurality of filter bags are arranged in the cloth bag area, and a plurality of baffles which are arranged in an inclined mode are arranged at the bottom of the cloth bag area to form a separating hopper; the separating hopper is positioned at the top of the ash hopper, an ash discharging channel is formed at the bottom of the separating hopper and communicated with the ash hopper, and a star-shaped ash discharger or a middle partition plate is arranged in the ash discharging channel.
2. A precipitator in accordance with claim 1, wherein when there are more than two cloth bag zones, an electric field channel is provided between two adjacent cloth bag zones.
3. A precipitator in accordance with claim 1 or 2, wherein the folder nip comprises a nip and a folder baffle disposed at a surface of the nip; the folding baffle is obliquely arranged towards one side of the electric field channel and is arranged at an acute angle with the folding anode plate along the air flow.
4. A precipitator in accordance with claim 3, wherein the angle α between the folded baffle plate and the folded anode plate is 0< α ≦ 30 ° and the folded baffle plate width is equal to or greater than the nip width.
5. A precipitator in accordance with claim 1, wherein the median septum is an inverted "V" shaped plate.
6. A precipitator in accordance with claim 1, wherein a pre-dusting area is provided in front of the cloth bag area.
7. The precipitator of claim 1, wherein a uniform distribution plate is disposed within the inlet flue.
CN202111071370.0A 2021-09-13 2021-09-13 Asymmetric electrostatic enhancement electric bag coupling dust remover Active CN113731091B (en)

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* Cited by examiner, † Cited by third party
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WO2012016481A1 (en) * 2010-08-04 2012-02-09 Yuan Ye Combined electrostatic precipitator
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CN203264504U (en) * 2013-05-07 2013-11-06 福建东源环保有限公司 Improved embedded electric bag dust remover
CN103566695A (en) * 2013-11-12 2014-02-12 清华大学 Enhanced coupled-mode embedded type electrostatic-bag integrated dust collector
CN203935905U (en) * 2014-05-14 2014-11-12 彭伟明 Dust arrester
WO2016029333A1 (en) * 2013-05-07 2016-03-03 福建东源环保有限公司 Embedded-type electrified bag composite dust collector
CN106111337A (en) * 2015-11-29 2016-11-16 解标 A kind of gas-particle two-phase part flow arrangement of electric cleaner portion gas dust suppression
CN106552469A (en) * 2016-01-28 2017-04-05 福建龙净环保股份有限公司 Electric-bag complex dust collector
CN106861906A (en) * 2017-04-26 2017-06-20 福建龙净环保股份有限公司 A kind of electric cleaner
CN206935019U (en) * 2017-06-27 2018-01-30 北京中电隆达节能环保科技股份有限公司 Electric bag integrated dust collector
CN107684796A (en) * 2017-09-11 2018-02-13 宁波捷通环保工程有限公司 A kind of waste gas dedusting system

Patent Citations (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2156940Y (en) * 1992-11-24 1994-02-23 王子江 Electrostatic dust-collector
US6321869B1 (en) * 2000-02-22 2001-11-27 Il Sung International Co., Ltd. Speaker system for personal computers
US20100068111A1 (en) * 2008-08-12 2010-03-18 Walsh Jr William Arthur Joining the mixing and variable gas atomizing of reactive chemicals in flue gas cleaning systems for removal of sulfur oxides, nitrogen oxides and mercury
WO2012016481A1 (en) * 2010-08-04 2012-02-09 Yuan Ye Combined electrostatic precipitator
CN201949765U (en) * 2010-11-16 2011-08-31 武汉龙净环保科技有限公司 Electrostatic bag dust collector
CN201899959U (en) * 2010-12-18 2011-07-20 吕艳红 Integrated cyclone electric bag flue gas dedusting device
CN102553382A (en) * 2011-12-30 2012-07-11 福建龙净环保股份有限公司 Double-row filter bag embedded type electric bag compound dust catcher with electric field area at front stage
WO2016029333A1 (en) * 2013-05-07 2016-03-03 福建东源环保有限公司 Embedded-type electrified bag composite dust collector
CN203264504U (en) * 2013-05-07 2013-11-06 福建东源环保有限公司 Improved embedded electric bag dust remover
CN103566695A (en) * 2013-11-12 2014-02-12 清华大学 Enhanced coupled-mode embedded type electrostatic-bag integrated dust collector
CN203935905U (en) * 2014-05-14 2014-11-12 彭伟明 Dust arrester
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CN106861906A (en) * 2017-04-26 2017-06-20 福建龙净环保股份有限公司 A kind of electric cleaner
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CN107684796A (en) * 2017-09-11 2018-02-13 宁波捷通环保工程有限公司 A kind of waste gas dedusting system

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