CN103008109B - The hollow polar plate electrostatic precipitation device and method that a kind of porous media material is formed - Google Patents

The hollow polar plate electrostatic precipitation device and method that a kind of porous media material is formed Download PDF

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CN103008109B
CN103008109B CN201210553549.4A CN201210553549A CN103008109B CN 103008109 B CN103008109 B CN 103008109B CN 201210553549 A CN201210553549 A CN 201210553549A CN 103008109 B CN103008109 B CN 103008109B
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pole plate
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由长福
王晓华
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Tsinghua University
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Abstract

一种多孔介质材料构成的中空极板静电除尘装置及方法,属于除尘技术领域。本发明特征在于采用了多孔介质材料构成的中空极板,通入水后,水穿过多孔介质材料在极板表面形成水膜,捕集由静电场作用沉积于极板表面的颗粒物,当极板表面有较多难以清除的颗粒物沉积时,向极板内部通入气体,气体穿过多孔介质材料在极板表面形成短暂气膜,清除颗粒物。进水与供气交替进行。本发明可有效降低湿式除尘的耗水量,保证收尘极板的水膜覆盖完整以实现高效脱除颗粒物的目的。采用本装置的静电除尘系统具有结构紧凑、少水高效、易于大型化应用的优势。

The invention relates to a hollow polar plate electrostatic precipitator and method composed of a porous medium material, belonging to the technical field of dedusting. The present invention is characterized in that a hollow pole plate made of a porous medium material is adopted. After water is passed through, the water passes through the porous medium material to form a water film on the surface of the pole plate to trap particles deposited on the surface of the pole plate by the action of an electrostatic field. When the pole plate When there are many particles deposited on the surface that are difficult to remove, the gas is introduced into the inside of the plate, and the gas passes through the porous medium material to form a short gas film on the surface of the plate to remove the particles. Water intake and air supply are carried out alternately. The invention can effectively reduce the water consumption of the wet dust removal, and ensure the complete coverage of the water film of the dust collection plate to realize the purpose of efficient removal of particulate matter. The electrostatic dust removal system using the device has the advantages of compact structure, less water and high efficiency, and easy large-scale application.

Description

一种多孔介质材料构成的中空极板静电除尘装置及方法Hollow plate electrostatic precipitator and method made of porous dielectric material

技术领域technical field

本发明涉及一种多孔介质材料构成的中空极板静电除尘装置及方法,属于除尘技术领域。The invention relates to a hollow plate electrostatic dust removal device and method made of a porous medium material, belonging to the field of dust removal technology.

背景技术Background technique

人类活动所产生的大量气态污染物和颗粒物正威胁着人类所赖于生存的基本物质——洁净的空气。可吸入颗粒物(PM10)特别是细颗粒物(PM2.5)污染已成为突出的大气环境问题,并日益引起世界各国的高度重视。人们已经认识到大气颗粒物(特别是其中的细颗粒物)是导致人类死亡率上升的主要原因。同时,大气颗粒物也是导致大气能见度降低、酸雨、全球气候变化和臭氧层破坏等重大大气污染问题的主要原因。控制细颗粒物的污染是全球节能减排战略的重大需求。在相当长的时期内,细颗粒物作为我国大气污染的首要污染物的基本状况不会改变。目前,我国大气PM2.5浓度比发达国家高数倍,已对人体健康和经济社会发展造成很大的威胁,细颗粒物的排放控制已是迫在眉睫。A large number of gaseous pollutants and particulate matter produced by human activities are threatening the basic substance that human beings rely on for survival - clean air. Inhalable particulate matter (PM 10 ), especially fine particulate matter (PM 2.5 ) pollution has become a prominent atmospheric environmental problem, and has increasingly attracted great attention from all over the world. Atmospheric particulate matter (especially fine particulate matter) has been recognized as the main cause of increased human mortality. At the same time, atmospheric particulate matter is also the main cause of major air pollution problems such as reduced atmospheric visibility, acid rain, global climate change, and ozone layer destruction. Controlling the pollution of fine particles is a major requirement of the global energy conservation and emission reduction strategy. In a fairly long period of time, the basic situation of fine particulate matter as the primary pollutant of air pollution in my country will not change. At present, China's atmospheric PM 2.5 concentration is several times higher than that of developed countries, which has posed a great threat to human health and economic and social development. The emission control of fine particulate matter is imminent.

目前,国际上总颗粒物控制技术虽然可以达到很高的水平,但对于细颗粒的捕获率却很低,造成数量巨大的细颗粒物进入环境大气中。以燃煤电站为例,虽然现有除尘装置的除尘效率可高达99%以上,但这些除尘器对细颗粒物的捕获率较低。这部分飞灰以粒径小于2.5微米甚至亚微米级的细颗粒为主,以颗粒的数量计可达到颗粒物总数的90%以上。这也是我国在大气中总悬浮颗粒物(TSP)呈逐年下降趋势,颗粒物排放总量也下降的情况下,PM2.5却呈上升趋势的原因,因此,颗粒物控制的重点在于细颗粒物,必须寻求更有效和更有针对性的技术发展途径。At present, although the total particle control technology in the world can reach a very high level, the capture rate of fine particles is very low, resulting in a huge amount of fine particles entering the ambient atmosphere. Taking coal-fired power stations as an example, although the dust removal efficiency of existing dust collectors can be as high as 99%, the capture rate of these dust collectors for fine particles is low. This part of fly ash is dominated by fine particles with a particle size of less than 2.5 microns or even submicrons, which can reach more than 90% of the total number of particles in terms of the number of particles. This is also the reason why China's total suspended particulate matter (TSP) in the atmosphere is declining year by year, and the total amount of particulate matter emissions is also decreasing, but PM 2.5 is on the rise. and a more targeted approach to technological development.

国内外致力于提高和优化传统污染物控制设备脱除细颗粒物捕捉能力的研究逐渐增多。例如在传统袋式除尘设备基础上改进滤袋的纤维材料和结构,在传统静电除尘设备基础上通过增加中间高能电极等方法。在更加严格的细颗粒物排放标准下,采用任何单一脱除技术都无法满足需求,因此发展不同控制方式协同脱除技术日益迫切。There are more and more researches at home and abroad devoted to improving and optimizing the ability of traditional pollutant control equipment to remove fine particles. For example, improving the fiber material and structure of the filter bag on the basis of traditional bag-type dust removal equipment, and adding intermediate high-energy electrodes on the basis of traditional electrostatic dust removal equipment. Under the more stringent fine particle emission standards, no single removal technology can meet the demand, so it is increasingly urgent to develop collaborative removal technologies with different control methods.

以静电场为脱除机理的静电除尘器作为目前常用的烟气除尘装置,在电力企业与水泥行业得到很普遍的应用。利用静电场脱除颗粒物在工业上的应用主要是将静电力直接施加到颗粒物上,使颗粒荷电,并运动到异性电极上,从而实现脱除。实际操作中,多以高压直流电在两极间产生电晕放电,含尘气流通过两电极间电场时,颗粒物被强制荷电,荷电的颗粒在静电力的作用下向极性相反的极板运动并被极板捕集。The electrostatic precipitator, which uses electrostatic field as the removal mechanism, is a commonly used flue gas dust removal device at present, and is widely used in electric power enterprises and cement industries. The industrial application of using an electrostatic field to remove particles is mainly to apply electrostatic force directly to the particles to charge the particles and move them to the opposite electrode to achieve removal. In actual operation, high-voltage direct current is often used to generate corona discharge between the two electrodes. When the dust-laden airflow passes through the electric field between the two electrodes, the particles are forcibly charged, and the charged particles move to the polar plate with the opposite polarity under the action of electrostatic force. and is captured by the plates.

电除尘器对于大粒径颗粒物有很好的脱除效果,但对于小颗粒尤其是细颗粒物的脱除效率并不高。为了更好地脱除细颗粒物,在实际工程应用中往往设置多级电场,以尽可能地提高对颗粒物的脱除效率。但是利用这种方法,对除尘效率的提高并不明显。造成这种现象的一个重要原因就是该粒径范围的细颗粒物易于跟随烟气流动,横向扩散弱,以及可能发生二次扬尘。如何增强静电场横向作用依旧是提高细颗粒物捕集效率的重要发展方向。目前已经工业化的湿式静电除尘装置均采用极板施加水膜技术,诸如中国专利02222513.7、00215471.4、200410058967.1等。施加水膜的方法均采用向极板表面喷水的方式进行,为避免极板表面局部形成干区或水膜不完整所造成的收尘极板腐蚀以及除尘效率低,需要喷入大量的水维持系统的正常运行,这样势必导致耗水量的增加。中国专利20111048292.7提出了一种湿式静电除尘器的收尘极液膜的测试装置,可监测极板表面是否出现干区问题。The electrostatic precipitator has a good removal effect on large-size particles, but the removal efficiency of small particles, especially fine particles, is not high. In order to better remove fine particles, multi-level electric fields are often set in practical engineering applications to improve the removal efficiency of particles as much as possible. But using this method, the improvement of dust removal efficiency is not obvious. An important reason for this phenomenon is that the fine particles in this particle size range are easy to follow the flue gas flow, the lateral diffusion is weak, and secondary dust may occur. How to enhance the lateral action of the electrostatic field is still an important development direction to improve the capture efficiency of fine particles. At present, the wet electrostatic precipitators that have been industrialized all adopt the technology of applying water film on the polar plate, such as Chinese patents 02222513.7, 00215471.4, 200410058967.1 and so on. The methods of applying water film are all carried out by spraying water on the surface of the plate. In order to avoid the corrosion of the dust collection plate caused by the formation of dry areas on the surface of the plate or the incomplete water film and the low efficiency of dust removal, a large amount of water needs to be sprayed. Maintaining the normal operation of the system will inevitably lead to an increase in water consumption. Chinese patent 20111048292.7 proposes a test device for the dust collecting electrode liquid film of a wet electrostatic precipitator, which can monitor whether there is a dry area problem on the surface of the electrode plate.

综上所述,如何提供一种有效保证极板液膜覆盖完整的湿式静电除尘装置,实现高效脱除颗粒物的同时降低水的消耗,是目前本领域技术人员亟待解决的问题。To sum up, how to provide a wet electrostatic precipitator that can effectively ensure the complete coverage of the liquid film on the plate, realize efficient removal of particulate matter and reduce water consumption is an urgent problem to be solved by those skilled in the art.

发明内容Contents of the invention

本发明的目的是提供一种低耗水、高效率的多孔介质材料构成的中空极板静电除尘装置及方法。The object of the present invention is to provide a hollow plate electrostatic precipitator and method made of porous medium material with low water consumption and high efficiency.

本发明的目的是通过如下技术方案实现的:The purpose of the present invention is achieved through the following technical solutions:

一种多孔介质材料构成的中空极板静电除尘装置,该装置包括多个收尘单元和粉尘收集器,每个收尘单元包括收尘极板和极线,其特征在于:收尘极板为中空极板,其内部腔室为六面体结构;中空极板表面由多孔介质材料构成;在中空极板上分别通过管道与进水阀门和供气阀门连接。A hollow plate electrostatic precipitator made of porous media material, the device includes a plurality of dust collection units and dust collectors, each dust collection unit includes a dust collection plate and a pole line, characterized in that: the dust collection plate is The hollow plate has a hexahedral internal chamber; the surface of the hollow plate is made of porous medium material; the hollow plate is connected to the water inlet valve and the gas supply valve through pipes.

本发明所述的多孔介质材料构成的中空极板静电除尘装置,其特征在于:所述的多孔介质材料采用金属、金属合金、陶瓷、高分子化合物、碳、玻璃、树脂或棉麻。The hollow plate electrostatic precipitator made of porous medium material according to the present invention is characterized in that the porous medium material is made of metal, metal alloy, ceramic, polymer compound, carbon, glass, resin or cotton.

本发明所述的多孔介质材料构成的中空极板静电除尘装置,其特征在于:所述的多孔介质材料的孔隙率为0.3~0.9,平均孔径为0.1~100μm。The hollow plate electrostatic precipitator made of porous media material according to the present invention is characterized in that: the porosity of the porous media material is 0.3-0.9, and the average pore diameter is 0.1-100 μm.

本发明所述的多孔介质材料构成的中空极板静电除尘装置,其特征在于:中空极板与两侧极线相对的表面内部间距为10~50mm。The hollow plate electrostatic precipitator made of porous medium material according to the present invention is characterized in that: the internal distance between the surface of the hollow plate and the polar lines on both sides is 10-50 mm.

本发明提供的一种多孔介质材料构成的中空极板静电除尘方法,其特征在于该方法包括如下步骤:The present invention provides a method for electrostatic dust removal of a hollow plate made of a porous dielectric material, which is characterized in that the method comprises the following steps:

1)供气阀门关闭时,进水阀门开启,水进入中空极板并充满整个腔室,水从多孔介质材料孔隙流出并在中空极板外表面形成水膜,捕集由静电场作用沉积于收尘极板表面的颗粒物,并流入静电除尘器的粉尘收集器;1) When the air supply valve is closed, the water inlet valve is opened, water enters the hollow plate and fills the entire chamber, water flows out from the pores of the porous medium material and forms a water film on the outer surface of the hollow plate, and is captured by the electrostatic field and deposited on the Collect the particles on the surface of the dust plate and flow into the dust collector of the electrostatic precipitator;

2)进水阀门关闭时,待中空极板腔室内水分排出后,供气阀门开启,通入的气体从多孔介质材料孔隙穿过,并将中空极板外表面沉积颗粒物清除;2) When the water inlet valve is closed, after the water in the hollow plate chamber is discharged, the gas supply valve is opened, and the gas introduced passes through the pores of the porous medium material, and the deposited particles on the outer surface of the hollow plate are removed;

3)重复步骤1)和2)。3) Repeat steps 1) and 2).

本发明所述的一种多孔介质材料构成的中空极板静电除尘方法,,其特征在于:系统运行过程中,供气时中空极板表面单位面积通入的气体平均流量为0.005~1m3/s,通气时间为1~10s。The electrostatic dust removal method for hollow plates made of porous media materials according to the present invention is characterized in that: during the operation of the system, the average gas flow per unit area of the surface of the hollow plates is 0.005-1m 3 / s, the ventilation time is 1-10s.

本发明所述的一种多孔介质材料构成的中空极板静电除尘方法,,其特征在于:通入气体时中空极板腔室内水体积小于腔室体积的1/3。The electrostatic dust removal method for a hollow electrode plate made of a porous medium material according to the present invention is characterized in that the volume of water in the cavity of the hollow electrode plate is less than 1/3 of the volume of the cavity when gas is introduced.

本发明与现有技术相比,具有以下优点及突出性效果:①在对常规静电除尘器设计不进行较大改动的前提下,通过更换现有收尘极板并连接进水和供气的管道和阀门即可实施,可方便用于现有静电除尘设备的设计升级与装置改造;②由于采用了供水管道给中空极板供水,水从多孔介质流出并在中空极板外表面形成水膜,以脱除颗粒物,无需专门设置外部喷嘴清洗极板表面颗粒物,与现有常规湿式静电除尘器相比,可降低系统费用;③采用多孔介质材料后,收尘极板表面水膜覆盖完整,可保证较高的收尘效率;气体供入中空极板后,在中空极板多孔介质材料表面所形成的气膜可有效去除粘附于表面的颗粒,保证清灰的效果,且可减少水的消耗。Compared with the prior art, the present invention has the following advantages and outstanding effects: ① On the premise of not making major changes to the design of the conventional electrostatic precipitator, by replacing the existing dust collecting plate and connecting the water inlet and air supply Pipes and valves can be implemented, which can be conveniently used for design upgrades and device transformations of existing electrostatic precipitators; ②Due to the use of water supply pipes to supply water to the hollow plates, water flows out from the porous media and forms a water film on the outer surface of the hollow plates , to remove particulate matter, no need to set up external nozzles to clean the particulate matter on the surface of the plate, compared with the existing conventional wet electrostatic precipitator, it can reduce the system cost; ③After using porous media materials, the water film on the surface of the dust collecting plate is completely covered, It can ensure a high dust collection efficiency; after the gas is fed into the hollow plate, the gas film formed on the surface of the hollow plate porous medium material can effectively remove the particles adhering to the surface, ensure the effect of dust removal, and reduce water pollution. consumption.

附图说明Description of drawings

图1为本发明提供的多孔介质材料构成的中空极板与供气阀门和进水阀门的结构示意图。Fig. 1 is a structural schematic diagram of a hollow plate made of a porous medium material, an air supply valve and a water inlet valve provided by the present invention.

图2为中空极板表面施加水膜时的中空极板和极线布置简图。Fig. 2 is a schematic diagram of the arrangement of the hollow pole plate and the pole line when a water film is applied on the surface of the hollow pole plate.

图3为中空极板表面施加气膜时的中空极板和极线布置简图。Fig. 3 is a schematic diagram of the arrangement of hollow pole plates and polar lines when a gas film is applied on the surface of the hollow pole plates.

图中:1-中空极板,2-极线,3-进水阀门,4-供气阀门,5-水膜。In the figure: 1-hollow polar plate, 2-polar line, 3-water inlet valve, 4-gas supply valve, 5-water film.

具体实施方式detailed description

下面结合附图对本发明的原理、结构和工作过程做进一步的说明。The principle, structure and working process of the present invention will be further described below in conjunction with the accompanying drawings.

本发明提供的一种多孔介质材料构成的中空极板静电除尘装置,该装置包括多个收尘单元和粉尘收集器,每个收尘单元包括收尘极板和极线2,收尘极板采用中空极板1,其内部腔室为六面体结构;中空极板表面由多孔介质材料构成;在中空极板1上分别通过管道与进水阀门3和供气阀门4连接。中空极板静电除尘装置所采用的多孔介质材料采用金属、金属合金、陶瓷、高分子化合物、碳、玻璃、树脂或棉麻。当采用柔性材料时,如棉麻、碳纤维布或玻璃纤维布,需要设置金属框架结构,以维持中空极板1的形状。多孔介质材料的孔隙率为0.3~0.9,平均孔径为0.1~100μm。中空极板与两侧极线相对的表面内部间距为10~50mm。The invention provides a hollow plate electrostatic precipitator made of porous media material, the device includes a plurality of dust collection units and dust collectors, each dust collection unit includes a dust collection pole plate and a pole line 2, and the dust collection pole plate The hollow pole plate 1 is adopted, and its inner chamber is a hexahedral structure; the surface of the hollow pole plate is made of porous medium material; the hollow pole plate 1 is respectively connected with the water inlet valve 3 and the gas supply valve 4 through pipelines. The porous medium material used in the hollow plate electrostatic precipitator is metal, metal alloy, ceramics, polymer compound, carbon, glass, resin or cotton. When flexible materials are used, such as cotton, carbon fiber cloth or glass fiber cloth, a metal frame structure is required to maintain the shape of the hollow electrode plate 1 . The porosity of the porous medium material is 0.3-0.9, and the average pore diameter is 0.1-100 μm. The internal distance between the surface of the hollow pole plate and the polar lines on both sides is 10-50mm.

本发明所提出的收尘单元在组装静电除尘器整体系统时,末端收尘单元只设置供水管道,不设置供气管道。主要是避免供气所导致的扬尘后期不能被捕集的问题。When the dust collection unit proposed by the present invention is assembled into the overall system of the electrostatic precipitator, the dust collection unit at the end is only provided with a water supply pipe, and no air supply pipe is provided. The main purpose is to avoid the problem that the dust caused by the air supply cannot be captured in the later stage.

本发明的工作过程如下:Working process of the present invention is as follows:

1)供气阀门4关闭时,进水阀门3开启,水进入中空极板1并充满整个腔室,水从多孔介质材料孔隙流出并在中空极板1外表面形成水膜5,捕集由静电场作用沉积于收尘极板表面的颗粒物,并流入静电除尘器的粉尘收集器;1) When the gas supply valve 4 is closed, the water inlet valve 3 is opened, water enters the hollow plate 1 and fills the entire chamber, water flows out from the pores of the porous medium material and forms a water film 5 on the outer surface of the hollow plate 1, and is captured by The electrostatic field acts on the particles deposited on the surface of the dust collecting plate, and flows into the dust collector of the electrostatic precipitator;

2)进水阀门3关闭时,待中空极板1腔室内水分排出后,供气阀门4开启,通入的气体从多孔介质材料孔隙穿过,并将中空极板1外表面沉积颗粒物清除;2) When the water inlet valve 3 is closed, after the water in the cavity of the hollow plate 1 is discharged, the gas supply valve 4 is opened, and the gas passed through through the pores of the porous medium material, and the deposited particles on the outer surface of the hollow plate 1 are removed;

3)重复步骤1)和2)。3) Repeat steps 1) and 2).

系统运行过程中,供气时中空极板表面单位面积通入的气体平均流量一般为0.005~1m3/s,通气时间为1~10s。During the operation of the system, the average gas flow per unit area of the surface of the hollow plate is generally 0.005-1m 3 /s, and the ventilation time is 1-10s.

通入气体时中空极板腔室内水体积小于腔室体积的1/3。The volume of water in the cavity of the hollow plate is less than 1/3 of the volume of the cavity when gas is introduced.

在静电除尘器控制系统设计时,除常规静电除尘器控制策略外,还需要考虑如下策略:供气阀门的开启频率设定需要依据中空极板表面所粘附颗粒物的性质决定。如果出现极板腐蚀,极板表面存在破损问题时,停止进水阀门的开启,采用间断供气方式进行清灰。In the design of the electrostatic precipitator control system, in addition to the conventional electrostatic precipitator control strategy, the following strategies also need to be considered: the opening frequency setting of the gas supply valve needs to be determined according to the nature of the particles adhered to the surface of the hollow plate. If the plate is corroded or the surface of the plate is damaged, stop opening the water inlet valve, and use intermittent air supply to clean the dust.

Claims (7)

1. the hollow polar plate electrostatic precipitation device of a porous media material formation, this device comprises multiple unit and dust collection of gathering dust, each unit that gathers dust comprises dust collecting pole plate and polar curve (2), it is characterized in that: dust collecting pole plate adopts hollow pole plate (1), and its internal chamber is hexahedron structure; Hollow polar board surface is made up of porous media material; Hollow pole plate is connected with inlet valve (3) and air-supplying valve (4) respectively by pipeline.
2. according to the hollow polar plate electrostatic precipitation device that porous media material according to claim 1 is formed, it is characterized in that: described porous media material adopts metal, metal alloy, pottery, macromolecular compound, carbon or glass.
3. according to the hollow polar plate electrostatic precipitation device that porous media material according to claim 1 is formed, it is characterized in that: the porosity of described porous media material is 0.3 ~ 0.9, and average pore size is 0.1 ~ 100mm.
4. according to the hollow polar plate electrostatic precipitation device that porous media material according to claim 1 is formed, it is characterized in that: the interior surface spacing that hollow pole plate is relative with both sides polar curve is 10 ~ 50mm.
5. adopt a hollow polar plate electrostatic precipitation method for device as claimed in claim 1, it is characterized in that the method comprises the steps:
1) when air-supplying valve (4) is closed, inlet valve (3) is opened, water enters hollow pole plate (1) and is full of whole chamber, water flows out from porous media material hole and forms moisture film (5) at hollow pole plate (1) outer surface, trapping is deposited on the particle on dust collecting pole plate surface by electrostatic field, and flows into the dust collection of electrostatic precipitator;
2) when inlet valve (3) is closed, after moisture in hollow pole plate (1) chamber is discharged, air-supplying valve (4) is opened, and the gas passed into passes from porous media material hole, and is removed by hollow pole plate (1) outside deposition particle;
3) step 1 is repeated) and 2).
6. according to hollow polar plate electrostatic precipitation method according to claim 5, it is characterized in that: in system operation, the gas average discharge that during air feed, hollow polar board surface unit are passes into is 0.005 ~ 1m 3/ s, duration of ventilation is 1 ~ 10s.
7. according to hollow polar plate electrostatic precipitation method according to claim 5, it is characterized in that: when passing into gas, hollow pole plate chamber inner volume is less than 1/3 of chamber volume.
CN201210553549.4A 2012-12-18 2012-12-18 The hollow polar plate electrostatic precipitation device and method that a kind of porous media material is formed Expired - Fee Related CN103008109B (en)

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Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103272697B (en) * 2013-05-06 2016-01-13 清华大学 A kind of wet static dedusting chamber structure dust collecting pole plate
CN103341409B (en) * 2013-06-28 2016-08-10 中节环立为(武汉)能源技术有限公司 The dust collecting pole plate of wet type moisture film electrostatic precipitator
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CN111229466A (en) * 2019-12-13 2020-06-05 深圳宾萃环保科技有限公司 Water film electrostatic purification treatment system and method thereof
CN111111923A (en) * 2020-03-02 2020-05-08 国电科学技术研究院有限公司 Dust collecting polar plate for wet electric dust collector
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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62136255A (en) * 1985-12-11 1987-06-19 Miyahara Isao Dust collector
JP2001046907A (en) * 1999-08-06 2001-02-20 Mitsubishi Heavy Ind Ltd Electric dust collector
CN201625582U (en) * 2010-02-23 2010-11-10 曹婷婷 Electrostatic precipitator plate
CN201644221U (en) * 2010-05-17 2010-11-24 山东电力研究院 Wet and dry hybrid electrostatic precipitator
CN202590955U (en) * 2011-12-28 2012-12-12 宝山钢铁股份有限公司 Three-area electric coagulation dust catcher
CN203253532U (en) * 2012-12-18 2013-10-30 清华大学 Hollow pole plate electrostatic dust removing apparatus formed from porous dielectric material

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62136255A (en) * 1985-12-11 1987-06-19 Miyahara Isao Dust collector
JP2001046907A (en) * 1999-08-06 2001-02-20 Mitsubishi Heavy Ind Ltd Electric dust collector
CN201625582U (en) * 2010-02-23 2010-11-10 曹婷婷 Electrostatic precipitator plate
CN201644221U (en) * 2010-05-17 2010-11-24 山东电力研究院 Wet and dry hybrid electrostatic precipitator
CN202590955U (en) * 2011-12-28 2012-12-12 宝山钢铁股份有限公司 Three-area electric coagulation dust catcher
CN203253532U (en) * 2012-12-18 2013-10-30 清华大学 Hollow pole plate electrostatic dust removing apparatus formed from porous dielectric material

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