CN206027932U - Wet -type electrostatic dust collector - Google Patents
Wet -type electrostatic dust collector Download PDFInfo
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- CN206027932U CN206027932U CN201620906135.9U CN201620906135U CN206027932U CN 206027932 U CN206027932 U CN 206027932U CN 201620906135 U CN201620906135 U CN 201620906135U CN 206027932 U CN206027932 U CN 206027932U
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- 239000000428 dust Substances 0.000 title claims abstract description 87
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 50
- 238000009826 distribution Methods 0.000 claims abstract description 26
- 239000000835 fiber Substances 0.000 claims abstract description 26
- 239000003546 flue gas Substances 0.000 claims abstract description 17
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 15
- 239000011152 fibreglass Substances 0.000 claims abstract description 6
- 239000004744 fabric Substances 0.000 claims description 27
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 7
- 239000007789 gas Substances 0.000 claims description 6
- -1 polypropylene Polymers 0.000 claims description 6
- 239000004734 Polyphenylene sulfide Substances 0.000 claims description 4
- 239000004743 Polypropylene Substances 0.000 claims description 4
- 229920000069 polyphenylene sulfide Polymers 0.000 claims description 4
- 229920001155 polypropylene Polymers 0.000 claims description 4
- 239000000377 silicon dioxide Substances 0.000 claims description 4
- 239000002131 composite material Substances 0.000 claims description 3
- 239000000463 material Substances 0.000 claims description 3
- 229920001343 polytetrafluoroethylene Polymers 0.000 claims description 3
- 239000004810 polytetrafluoroethylene Substances 0.000 claims description 3
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims 1
- 239000012719 wet electrostatic precipitator Substances 0.000 abstract description 16
- 238000007789 sealing Methods 0.000 abstract description 10
- 239000010865 sewage Substances 0.000 abstract description 7
- 238000005260 corrosion Methods 0.000 abstract description 6
- 230000007797 corrosion Effects 0.000 abstract description 6
- 239000012212 insulator Substances 0.000 abstract description 5
- 238000005406 washing Methods 0.000 abstract description 2
- 230000005684 electric field Effects 0.000 description 11
- 238000006477 desulfuration reaction Methods 0.000 description 6
- 230000023556 desulfurization Effects 0.000 description 6
- 238000011010 flushing procedure Methods 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 239000000779 smoke Substances 0.000 description 6
- 239000002253 acid Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 239000012717 electrostatic precipitator Substances 0.000 description 3
- 239000007921 spray Substances 0.000 description 3
- 238000009825 accumulation Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000003595 mist Substances 0.000 description 2
- 239000013618 particulate matter Substances 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000000443 aerosol Substances 0.000 description 1
- 229910052785 arsenic Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008033 biological extinction Effects 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 150000002013 dioxins Chemical class 0.000 description 1
- 239000012718 dry electrostatic precipitator Substances 0.000 description 1
- 238000010892 electric spark Methods 0.000 description 1
- 230000005686 electrostatic field Effects 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 229910052602 gypsum Inorganic materials 0.000 description 1
- 239000010440 gypsum Substances 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 229910052753 mercury Inorganic materials 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 125000005575 polycyclic aromatic hydrocarbon group Chemical group 0.000 description 1
- 239000012716 precipitator Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229920006303 teflon fiber Polymers 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- 238000009827 uniform distribution Methods 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
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- Electrostatic Separation (AREA)
Abstract
本实用新型公开一种湿式静电除尘器,包括壳体、阴极线和收尘极管;阴极线固定于收尘极管的中心,阴极线外接高压电源,高压电源通过绝缘子室引入阴极线,壳体上设置有绝缘密封套,且绝缘密封套同时用于在上下两端固定收尘极管;收尘极管固定于壳体内部,收尘极管内壁覆盖用于实现均布水膜的纤维布,收尘极管上端设有用于实现均布水膜的布水器;壳体下部设置有烟气进口和污水出口,壳体上部设置有烟气出口。收尘极管为导电玻璃钢阳极管,收尘极管的截面呈倒圆角的正六边形,且在壳体内部呈蜂窝状排列。本实用新型能保障收尘极板上水流的均匀性、阴极线放电的可靠性、收尘极管的耐腐蚀性,并且能保证冲洗的效率和运行的稳定性,进而提高除尘效率。
The utility model discloses a wet electrostatic precipitator, which comprises a casing, a cathode line and a dust collection pole tube; the cathode line is fixed at the center of the dust collection pole tube, the cathode line is externally connected to a high-voltage power supply, and the high-voltage power supply is introduced into the cathode line through an insulator chamber. There is an insulating sealing sleeve on the body, and the insulating sealing sleeve is used to fix the dust collecting pole tube at the upper and lower ends; the dust collecting pole tube is fixed inside the shell, and the inner wall of the dust collecting pole tube is covered with fibers for uniform water film distribution The upper end of the dust collector tube is provided with a water distributor for uniform water film distribution; the lower part of the shell is provided with a flue gas inlet and a sewage outlet, and the upper part of the shell is provided with a flue gas outlet. The dust collection pole tube is a conductive glass fiber reinforced plastic anode tube, and the section of the dust collection pole tube is a regular hexagon with rounded corners, and is arranged in a honeycomb shape inside the shell. The utility model can guarantee the uniformity of the water flow on the dust collecting pole plate, the reliability of the discharge of the cathode line, the corrosion resistance of the dust collecting pole tube, and can ensure the efficiency of washing and the stability of operation, thereby improving the efficiency of dust removal.
Description
技术领域technical field
本实用新型属于环境保护技术领域,具体涉及一种湿式静电除尘器。The utility model belongs to the technical field of environmental protection, in particular to a wet electrostatic precipitator.
背景技术Background technique
近年来国内外环保要求越来越高,各种石化尾气、炉窑烟气均须经除尘脱硫后达标排放。目前,湿法除尘脱硫的工艺仍是一种可靠的主流工艺。然而,目前常用的湿法除尘脱硫处理后排放的烟气含湿、含尘和含沫较高,冒白烟和拖尾现象严重。为了降低烟囱冒白烟和拖尾现象,目前湿法除尘脱硫处理后的烟气要经电除雾器或湿式静电除尘器处理后再由烟囱排放。In recent years, environmental protection requirements at home and abroad have become higher and higher. All kinds of petrochemical tail gas and furnace flue gas must be discharged after dedusting and desulfurization. At present, the process of wet dedusting and desulfurization is still a reliable mainstream process. However, the currently commonly used wet dedusting and desulfurization treatment emits flue gas with high humidity, dust and foam content, white smoke and tailing phenomenon are serious. In order to reduce the phenomenon of white smoke and trailing from the chimney, the flue gas after wet dedusting and desulfurization treatment must be treated by an electrostatic precipitator or a wet electrostatic precipitator before being discharged from the chimney.
静电除尘器,是一种依靠静电力来收集上述粉尘的工业设备。它的工作包括如下过程:(1)来自高压电源的高电压施加到电晕线上,电晕线产生电晕放电,并形成电场;(2)流经电场的烟气中的粉尘,被电晕放电产生的离子荷电;(3)带电的粉尘,在电场力作用下,被收集到收尘极板上;(4)被收集到收尘极板上的粉尘,从极板上脱离。根据粉尘从极板上脱离的方式不同,静电除尘器分为干式和湿式两种形式。干式静电除尘器是以振打或旋转刷的方式使粉尘脱离,湿式静电除尘器是以流动水膜的方式使粉尘脱离。Electrostatic precipitator is an industrial equipment that relies on electrostatic force to collect the above-mentioned dust. Its work includes the following processes: (1) The high voltage from the high-voltage power supply is applied to the corona wire, and the corona wire generates corona discharge and forms an electric field; (2) The dust in the flue gas flowing through the electric field is charged by the electric field The ion charge generated by corona discharge; (3) The charged dust is collected on the dust collecting plate under the action of the electric field force; (4) The dust collected on the dust collecting plate is separated from the plate. According to the way the dust is separated from the plate, the electrostatic precipitator is divided into two types: dry type and wet type. The dry electrostatic precipitator removes the dust by vibrating or rotating the brush, and the wet electrostatic precipitator removes the dust by means of a flowing water film.
湿式静电除尘器作为一种终端净化设备,利用高压放电的方式使烟气中粉尘收集到极板上,采用布水膜的方式去除极板上所收集到的粉尘。对微细颗粒物(PM2.5粉尘、SO3酸雾、气溶胶)、重金属(Hg、As、Se、Pb、Cr)、有机污染物(多环芳烃、二恶英)等颗粒物有着非常好的去除效果,能够从源头上控制其排放,广泛应用于电力、钢铁、化工、纺织、水泥、陶瓷及玻璃等行业的废气治理,能够有效解决石膏雨、蓝烟羽或白烟问题,效果非常显著。As a terminal purification equipment, the wet electrostatic precipitator uses high-voltage discharge to collect the dust in the flue gas on the plate, and uses the water film to remove the dust collected on the plate. It has a very good removal effect on fine particulate matter (PM2.5 dust, SO3 acid mist, aerosol), heavy metals (Hg, As, Se, Pb, Cr), organic pollutants (polycyclic aromatic hydrocarbons, dioxins) and other particulate matter , can control its emission from the source, and is widely used in waste gas treatment in industries such as electric power, steel, chemical, textile, cement, ceramics and glass, and can effectively solve the problems of gypsum rain, blue smoke plume or white smoke, and the effect is very significant.
但传统的湿式静电除尘器有如下缺点:1.传统的板状电极,线状电极,杆状电极的电晕强度不够高,必须靠提高电压来获得高捕尘率和防止灭弧影响;2.通常酸性气体在被捕集后于极板和水膜间形成稀酸,稀酸会腐蚀设备,影响使用寿命;3.气流在各个电极间的分布不均匀,甚至有“死角”,降低了捕尘效率;4.传统的圆形电极管有难以准确保持同心的问题,使电场不均匀,易造成频繁电火花,影响整体捕尘效果;5.通常喷淋层的喷嘴只是设置在静电除尘组件上端,喷嘴位置的分布通常比较简单,容易产生喷淋死角。此外,喷嘴形成的冲洗水膜布在除尘极表面并不均匀,容易形成沟状水流和斑点污渍。污垢累积后会发生电极失效。由于冲洗水膜的不均匀,需在除尘组件下端设置烟气加湿喷雾,虽然弥补了水膜不均匀的问题,但容易形成电晕封闭的现象;而雾状喷嘴可实现较均匀的冲洗水膜,但容易形成导电的小液滴,导致电场短路。However, the traditional wet electrostatic precipitator has the following disadvantages: 1. The corona intensity of the traditional plate electrode, wire electrode and rod electrode is not high enough, and it is necessary to increase the voltage to obtain a high dust collection rate and prevent arc extinction; 2. .Usually the acid gas forms dilute acid between the plate and the water film after being captured. The dilute acid will corrode the equipment and affect the service life; 3. The distribution of the gas flow between the electrodes is uneven, and there are even "dead angles", which reduces the Dust collection efficiency; 4. The traditional circular electrode tube has the problem of being difficult to maintain accurate concentricity, which makes the electric field uneven, which easily causes frequent electric sparks and affects the overall dust collection effect; 5. Usually the nozzles of the spray layer are only set in the electrostatic dust On the upper end of the component, the distribution of the nozzle position is usually relatively simple, and it is easy to produce a spray dead angle. In addition, the rinse water film cloth formed by the nozzle is not uniform on the surface of the dust collector, and it is easy to form groove-like water flow and spot stains. Electrode failure occurs after fouling builds up. Due to the unevenness of the flushing water film, it is necessary to install the flue gas humidification spray at the lower end of the dust removal component. Although the problem of uneven water film is made up for, it is easy to form a phenomenon of corona sealing; and the mist nozzle can achieve a more uniform flushing water film , but it is easy to form conductive small droplets, resulting in a short circuit of the electric field.
因此,本领域技术人员亟需提供一种能保障收尘极管上水流的均匀性、阴极线放电可靠性、运行稳定性,进而提高除尘效率的湿式静电除尘器。Therefore, those skilled in the art urgently need to provide a wet electrostatic precipitator that can ensure the uniformity of the water flow on the dust collecting electrode tube, the reliability of the discharge of the cathode line, and the operation stability, thereby improving the dust removal efficiency.
实用新型内容Utility model content
针对上述现有技术中的不足,本实用新型提供了一种能保障收尘极管上水流的均匀性、阴极线放电可靠性、运行的稳定性,进而提高除尘效率的湿式静电除尘器。Aiming at the deficiencies in the above-mentioned prior art, the utility model provides a wet electrostatic precipitator which can ensure the uniformity of the water flow on the dust collecting electrode tube, the reliability of the discharge of the cathode line, and the stability of the operation, thereby improving the efficiency of dust removal.
为实现上述目的,本实用新型采用了以下技术方案:In order to achieve the above object, the utility model adopts the following technical solutions:
一种湿式静电除尘器,包括壳体、阴极线和收尘极管;所述阴极线固定于收尘极管的中心,阴极线外接高压电源,所述高压电源通过绝缘子室引入阴极线,所述壳体上设置有绝缘密封套,且绝缘密封套同时用于在上下两端固定收尘极管;所述收尘极管固定于壳体内部,所述收尘极管内壁覆盖用于实现均布水膜的纤维布,收尘极管上端设有用于实现均布水膜的布水器;所述壳体下部设置有烟气进口和污水出口,壳体上部设置有烟气出口。A wet electrostatic precipitator, comprising a housing, a cathode wire and a dust collection pole tube; the cathode line is fixed at the center of the dust collection pole tube, the cathode line is externally connected to a high-voltage power supply, and the high-voltage power supply is introduced into the cathode line through an insulator chamber. The casing is provided with an insulating sealing sleeve, and the insulating sealing sleeve is used to fix the dust collecting pole tube at the upper and lower ends at the same time; the dust collecting pole tube is fixed inside the housing, and the inner wall of the dust collecting pole tube is covered to realize The fiber cloth with uniform water film distribution, the upper end of the dust collector tube is provided with a water distributor for realizing uniform water film distribution; the lower part of the housing is provided with a smoke inlet and a sewage outlet, and the upper part of the housing is provided with a smoke outlet.
优选的,所述收尘极管为导电玻璃钢阳极管。Preferably, the dust collector tube is a conductive glass fiber reinforced plastic anode tube.
进一步的,所述收尘极管的截面呈倒圆角的正六边形,且收尘极管在壳体内部呈蜂窝状排列。Further, the section of the dust collection pole tube is a regular hexagon with rounded corners, and the dust collection pole tubes are arranged in a honeycomb shape inside the housing.
进一步的,所述壳体内的烟气进口处设有气流分布板。Further, an air flow distribution plate is provided at the flue gas inlet in the housing.
进一步的,所述气流分布板、收尘极管、绝缘密封套均采用玻璃钢复合耐腐蚀材质。Further, the airflow distribution plate, the dust collection pole tube, and the insulating sealing sleeve are all made of glass fiber reinforced plastic composite corrosion-resistant material.
优选的,在壳体内所述收尘极管的底部固设有格栅板,格栅板上设置有与每根极管内腔中心轴线相对应的格栅孔,且所述的阴极线下端穿过该格栅孔,阴极线末端定格于该格栅板上。Preferably, a grid plate is fixed at the bottom of the dust collection pole tube in the housing, and a grid hole corresponding to the central axis of each pole tube inner cavity is provided on the grid plate, and the lower end of the cathode wire passes through Through the grid hole, the end of the cathode wire is fixed on the grid plate.
优选的,所述阴极线采用RSB芒刺线。Preferably, the cathode wire is RSB barbed wire.
优选的,所述纤维布采用聚丙烯纤维织物或聚苯硫醚纤维织物或聚四氟乙烯纤维织物或高硅氧纤维织物。Preferably, the fiber cloth is made of polypropylene fiber fabric or polyphenylene sulfide fiber fabric or polytetrafluoroethylene fiber fabric or high silica fiber fabric.
优选的,所述布水器上连接有用于控制布水阀门调节布水量的PLC。Preferably, the water distributor is connected with a PLC for controlling the water distribution valve to adjust the water distribution amount.
本实用新型的有益效果在于:The beneficial effects of the utility model are:
本实用新型提供的湿式静电除尘器能保障收尘极板上水流的均匀性、阴极线放电的可靠性、收尘极管的耐腐蚀性,并且能保证冲洗的效率和运行的稳定性,进而提高除尘效率。The wet electrostatic precipitator provided by the utility model can ensure the uniformity of the water flow on the dust collection plate, the reliability of the discharge of the cathode line, the corrosion resistance of the dust collection pole tube, and can ensure the efficiency of washing and the stability of operation, thereby improving Dust removal efficiency.
附图说明Description of drawings
图1为本实用新型的结构简示图。Fig. 1 is a schematic diagram of the structure of the utility model.
图中标注符号的含义如下:The meanings of the marked symbols in the figure are as follows:
1-壳体 10-绝缘密封套 11-烟气进口 12-污水出口1-housing 10-insulation sealing sleeve 11-flue gas inlet 12-sewage outlet
13-烟气出口 14-气流分布板 2-阴极线 20-阴极框架线路13-Flue gas outlet 14-Air distribution plate 2-Cathode line 20-Cathode frame line
3-收尘极管 4-高压电源 5-绝缘子室 6-布水器3- Dust collector tube 4- High voltage power supply 5- Insulator chamber 6- Water distributor
60-布水阀门 61-布水管路 7-格栅板60-Water distribution valve 61-Water distribution pipeline 7-Grille
具体实施方式detailed description
下面将结合本实用新型实施例中的附图,对本实用新型中的技术方案进行清楚、完整地描述。以下实施例仅用于更加清楚地说明本实用新型的技术方案,而不能以此来限制本实用新型的保护范围。The technical solution in the utility model will be clearly and completely described below in combination with the drawings in the embodiments of the utility model. The following examples are only used to illustrate the technical solution of the utility model more clearly, but not to limit the protection scope of the utility model.
如图1所示,为一种湿式静电除尘器,包括壳体1、阴极线2和收尘极管3;阴极线2固定于收尘极管3的中心,阴极线2外接高压电源4,高压电源4通过绝缘子室5引入阴极线2,壳体1底部及顶部设置有绝缘密封套10,且绝缘密封套10用于在上下两端固定收尘极管3,并有效地防止气流逃逸,防止气流通过非电场区域,进入除尘器出口,从而影响湿式静电除尘器效率;收尘极管3固定于壳体1内部,收尘极管3内壁覆盖用于实现均布水膜的纤维布,收尘极管3上端设有用于实现均布水膜的布水器6;壳体1下部设置有烟气进口11和污水出口12,壳体1上部设置有烟气出口13。As shown in Figure 1, it is a wet electrostatic precipitator, including a housing 1, a cathode line 2 and a dust collecting pole tube 3; the cathode line 2 is fixed at the center of the dust collecting pole tube 3, and the cathode line 2 is externally connected to a high voltage power supply 4, The high-voltage power supply 4 is introduced into the cathode line 2 through the insulator chamber 5, and the bottom and top of the housing 1 are provided with insulating sealing sleeves 10, and the insulating sealing sleeves 10 are used to fix the dust collecting electrode tube 3 at the upper and lower ends, and effectively prevent the airflow from escaping. Prevent the air flow from passing through the non-electric field area and enter the outlet of the dust collector, thereby affecting the efficiency of the wet electrostatic precipitator; the dust collecting pole tube 3 is fixed inside the shell 1, and the inner wall of the dust collecting pole tube 3 is covered with fiber cloth for uniform water film distribution. The upper end of the dust collector tube 3 is provided with a water distributor 6 for uniform distribution of the water film;
其中,收尘极管3为导电玻璃钢阳极管,其重量轻、拉伸强度高、耐腐蚀,使用寿命长,导电性能优良,受温度影响的变形小,刚度好,极板边缘没有锐边、毛刺,不易产生局部放电现象。Among them, the dust collection pole tube 3 is a conductive glass fiber reinforced plastic anode tube, which has light weight, high tensile strength, corrosion resistance, long service life, excellent electrical conductivity, small deformation affected by temperature, good rigidity, and no sharp edge on the edge of the pole plate. Glitch, not easy to produce partial discharge phenomenon.
收尘极管3的截面呈倒圆角的正六边形,且收尘极管3在壳体1内部呈蜂窝状排列。收尘极管3的截面也可呈倒圆角的正方形或其它避免折角处积尘的形状。蜂巢型排列的正六边形收尘极管3相比板式收尘增大了湿式静电除尘器的除尘收尘面积,提高了效率。The cross-section of the dust collection pole tube 3 is a regular hexagon with rounded corners, and the dust collection pole tube 3 is arranged in a honeycomb shape inside the housing 1 . The cross section of the dust collector tube 3 can also be a square with rounded corners or other shapes to avoid dust accumulation at the corners. The regular hexagonal dust collection pole tubes 3 arranged in a honeycomb pattern increase the dust collection area of the wet electrostatic precipitator compared with the plate dust collection, and improve the efficiency.
壳体1内的烟气进口11处设有使气流均匀分布的气流分布板14,同时作为检修平台布置于除尘器内部。The flue gas inlet 11 in the casing 1 is provided with an air flow distribution plate 14 for evenly distributing the air flow, and it is also arranged inside the dust collector as an inspection platform.
由于处理烟气中含有酸性气体,为了防止湿式静电除尘器内构件腐蚀,除尘器内构件,如气流分布板14、收尘极管3、绝缘密封套10等均采用玻璃钢复合耐腐蚀材质。Due to the acid gas contained in the treated flue gas, in order to prevent corrosion of the internal components of the wet electrostatic precipitator, the internal components of the precipitator, such as the air flow distribution plate 14, the dust collection pole tube 3, and the insulating sealing sleeve 10, are all made of FRP composite corrosion-resistant materials.
在壳体1内收尘极管3的底部设置有格栅板7,格栅板7上设置有与每根极管内腔中心轴线相对应的格栅孔,且阴极线2下端穿过该格栅孔,阴极线2末端定格于该格栅板7上;能使得阴极线2的固定稳定可靠,从而减少摆动和震幅发生,防止局部短路,使其放电均匀、稳定,提高了脱除效率和用电效率。A grid plate 7 is provided at the bottom of the dust collection pole tube 3 in the housing 1, and a grid hole corresponding to the central axis of each pole tube cavity is provided on the grid plate 7, and the lower end of the cathode wire 2 passes through the grid. The grid hole, the end of the cathode line 2 is fixed on the grid plate 7; it can make the fixation of the cathode line 2 stable and reliable, thereby reducing the occurrence of swing and amplitude, preventing local short circuit, making the discharge uniform and stable, and improving the removal efficiency and power efficiency.
其中,阴极线2采用RSB芒刺线;不仅具有传统RS芒刺线所具有的不断线、不变形、刺尖上下不易积灰、放电强度大的优点,而且还克服了其放电均匀性差,平均电场强度弱的缺点,改善了电晕电流的密度的均匀性,放电方位多,避免了电晕死区,增强平均电流密度,可有效提高除尘效率,提高了运行的可靠性。Among them, the cathode line 2 adopts RSB barbed wire; it not only has the advantages of continuous line, no deformation, no dust accumulation on the top and bottom of the thorn tip, and high discharge intensity of the traditional RS barbed wire, but also overcomes its poor discharge uniformity, and the average The disadvantage of weak electric field strength improves the uniformity of the density of the corona current, and the discharge orientation is more, avoiding the corona dead zone and enhancing the average current density, which can effectively improve the dust removal efficiency and improve the reliability of operation.
纤维布采用聚丙烯纤维织物或聚苯硫醚纤维织物或聚四氟乙烯纤维织物或高硅氧纤维。可根据具体工作条件来选择,如聚丙烯纤维织物、聚苯硫醚纤维织物和聚四氟乙烯纤维织物的工作温度为110℃左右,而耐高温的高硅氧纤维可以保证设备在180℃状况时正常工作。收尘极管3的上端,水在重力作用向下流动,利用纤维毛细效应,向四周扩散渗透,在布水孔下部约300mm处,形成的均匀水膜以波纹状向下平铺至底端,纤维布收尘极管表面均匀水膜形成。Fiber cloth adopts polypropylene fiber fabric or polyphenylene sulfide fiber fabric or polytetrafluoroethylene fiber fabric or high silica fiber. It can be selected according to specific working conditions. For example, the working temperature of polypropylene fiber fabric, polyphenylene sulfide fiber fabric and Teflon fiber fabric is about 110°C, and the high temperature resistant high-silica fiber can ensure that the equipment is kept at 180°C. work normally. At the upper end of the dust collector tube 3, the water flows downward under the action of gravity, and diffuses and infiltrates to the surroundings by using the fiber capillary effect. At the lower part of the water distribution hole about 300mm, the formed uniform water film spreads down to the bottom in a corrugated shape. A uniform water film is formed on the surface of the fiber cloth dust collecting pole tube.
布水器6上连接有用于控制布水阀门60调节布水量的PLC。水膜厚度的大小可由PLC控制的布水阀门60实时调节冲洗水量及冲洗时间,从而可实现水膜厚度均匀。并且,本发明的设计对冲洗水量要求低、可间歇带电冲洗、脱除物呈片状脱落无二次污染、长期连续可靠运行。The water distributor 6 is connected with a PLC for controlling the water distribution valve 60 to adjust the water distribution volume. The thickness of the water film can be adjusted in real time by the PLC-controlled water distribution valve 60 to adjust the flushing water volume and flushing time, so that the thickness of the water film can be uniform. Moreover, the design of the present invention has low requirements on flushing water volume, can be charged intermittently, removes flakes and falls off without secondary pollution, and can operate continuously and reliably for a long time.
本实用新型湿式静电除尘器可竖直立式布置在脱硫塔顶部或脱硫塔后部。The wet electrostatic precipitator of the utility model can be arranged vertically on the top of the desulfurization tower or at the rear of the desulfurization tower.
下面结合附图对本实用新型的工作过程作出如下的详细说明。Below in conjunction with accompanying drawing, working process of the present utility model is described in detail as follows.
如图1所示,烟气经进气口11进入湿式静电除尘器内,经过气流分布板14进入电场,来自高压电源4的高电压通过绝缘子室5施加到阴极线2上,形成高压静电场。As shown in Figure 1, the flue gas enters the wet electrostatic precipitator through the air inlet 11, enters the electric field through the air distribution plate 14, and the high voltage from the high voltage power supply 4 is applied to the cathode line 2 through the insulator chamber 5 to form a high voltage electrostatic field .
气流经过电场,在电场力作用下粉尘被收集到收尘极板3的纤维布水膜上,由PLC控制的冲洗水经过布水器60、布水管路61流到收尘极管3内壁的纤维布上,向下流动形成均匀水膜。随着吸附过程的延长,在纤维布集尘极表面形成糊状层,且水膜厚度逐渐变薄、变干,因糊状层和纤维布表面张力和收缩比不同,糊状层积到一定程度后,呈片状断裂脱落,通过污水出口12排出;根据糊状层的厚度及脱落情况,由PLC控制的布水器6的布水阀门60调节布水量,再次形成水膜。净化后的烟气从上部烟气出口13排出,污水从下部污水出口12排出,流入污水处理系统。The air flow passes through the electric field, and the dust is collected on the fiber cloth water film of the dust collecting pole plate 3 under the action of the electric field force, and the flushing water controlled by PLC flows to the inner wall of the dust collecting pole pipe 3 through the water distributor 60 and the water distribution pipeline 61 On the fiber cloth, flow down to form a uniform water film. With the extension of the adsorption process, a paste layer is formed on the surface of the fiber cloth dust collector, and the thickness of the water film gradually becomes thinner and drier. After a certain degree, it breaks and falls off in flakes, and is discharged through the sewage outlet 12; according to the thickness and shedding of the paste layer, the water distribution valve 60 of the water distributor 6 controlled by PLC adjusts the water distribution to form a water film again. The purified flue gas is discharged from the upper flue gas outlet 13, and the sewage is discharged from the lower sewage outlet 12 and flows into the sewage treatment system.
高压电源4、阴极框架线路20、阴极线2等通电设备为阴极,收尘极管3束可靠接地为阳极。High-voltage power supply 4, cathode frame line 20, cathode line 2 and other energized equipment are cathodes, and 3 bundles of dust collecting pole tubes are reliably grounded as anodes.
以上所述仅是本实用新型的优选实施方式,应当指出,对于本技术领域的普通技术人员来说,在不脱离本实用新型技术原理的前提下,还可以做出若干改进和变形,这些改进和变形也应视为本实用新型的保护范围。The above is only the preferred embodiment of the utility model, it should be pointed out that for those of ordinary skill in the art, without departing from the technical principle of the utility model, some improvements and deformations can also be made. And deformation should also be regarded as the protection scope of the present utility model.
Claims (9)
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107149986A (en) * | 2017-07-03 | 2017-09-12 | 华美节能科技集团有限公司 | A kind of industrial waste-gas purifier |
| CN109569886A (en) * | 2019-01-07 | 2019-04-05 | 佛山绿语蓝天环保科技有限公司 | A kind of moisture film wet electrostatic flue gas removing device |
| CN109806975A (en) * | 2019-01-30 | 2019-05-28 | 浙江大学 | A kind of reinforcing Uniform Discharge device and method |
| CN112121572A (en) * | 2020-09-04 | 2020-12-25 | 襄阳九鼎昊天环保设备有限公司 | a plasma filter |
| JP2023154898A (en) * | 2022-04-08 | 2023-10-20 | 三菱重工業株式会社 | Dust collector and dust collection method |
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2016
- 2016-08-19 CN CN201620906135.9U patent/CN206027932U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107149986A (en) * | 2017-07-03 | 2017-09-12 | 华美节能科技集团有限公司 | A kind of industrial waste-gas purifier |
| CN109569886A (en) * | 2019-01-07 | 2019-04-05 | 佛山绿语蓝天环保科技有限公司 | A kind of moisture film wet electrostatic flue gas removing device |
| CN109806975A (en) * | 2019-01-30 | 2019-05-28 | 浙江大学 | A kind of reinforcing Uniform Discharge device and method |
| CN109806975B (en) * | 2019-01-30 | 2024-03-01 | 浙江大学 | A device and method for strengthening uniform discharge |
| CN112121572A (en) * | 2020-09-04 | 2020-12-25 | 襄阳九鼎昊天环保设备有限公司 | a plasma filter |
| JP2023154898A (en) * | 2022-04-08 | 2023-10-20 | 三菱重工業株式会社 | Dust collector and dust collection method |
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