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CN103586135B - Formation mode of dust collection pole plate and ash removal water film of wet-type electric precipitator - Google Patents

Formation mode of dust collection pole plate and ash removal water film of wet-type electric precipitator Download PDF

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CN103586135B
CN103586135B CN201310528825.6A CN201310528825A CN103586135B CN 103586135 B CN103586135 B CN 103586135B CN 201310528825 A CN201310528825 A CN 201310528825A CN 103586135 B CN103586135 B CN 103586135B
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dust
plate
water
pole plate
film
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CN103586135A (en
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齐立强
崔少平
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North China Electric Power University
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North China Electric Power University
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Abstract

本发明为一种湿式电除尘器收尘极板及其清灰水膜形成方式。其方法为:采用耐高温、耐腐蚀材料制成的收尘极板,布水管路设置在极板内部,保证极板的运行可靠稳定及向极板表面均匀布水;极板表面贴伏有纤维编织薄膜,利用毛细作用,在极板表面形成完整均匀的清灰水膜,避免二次扬尘,同时提高了对颗粒物特别是细微颗粒物的捕集效率。The invention relates to a dust-collecting pole plate of a wet-type electric dust collector and a method for forming a dust-cleaning water film thereof. The method is as follows: use a dust collection plate made of high temperature resistant and corrosion resistant materials, and set the water distribution pipeline inside the plate to ensure reliable and stable operation of the plate and evenly distribute water to the surface of the plate; The fiber woven film uses capillary action to form a complete and uniform dust-removing water film on the surface of the plate, avoiding secondary dust and improving the collection efficiency of particulate matter, especially fine particulate matter.

Description

一种湿式电除尘器收尘极板及其清灰水膜形成方式A dust-collecting pole plate of a wet electrostatic precipitator and its formation method of ash-cleaning water film

所属技术领域Technical field

本发明属于环境保护设备,尤其涉及一种湿式电除尘器收尘极板及其清灰水膜形成方式。The invention belongs to environmental protection equipment, in particular to a dust-collecting pole plate of a wet-type electric dust collector and a method for forming a dust-cleaning water film thereof.

背景技术Background technique

湿式电除尘器是利用其在收尘极板上形成的一层水膜向下流动时清洗被捕集在极板上的粉尘的。与干式电除尘器相比:湿式电除尘器不需要振打装置,从而避免了振打引起的二次扬尘,还防止了气流和电晕风引起的二次扬尘;由于极板上始终分布着向下流动的水膜,被捕集到极板上的粉尘立即被水膜冲洗掉,因而对于高比电阻粉尘,不会发生反电晕,避免了由此引起的二次扬尘;对于低比电阻粉尘,不会发生被捕集的颗粒逃离极板,再次返回气流的现象。由于上述优点,湿式电除尘器具有非常高的除尘效率,可以适应各种比电阻的粉尘。The wet electrostatic precipitator uses a layer of water film formed on the dust collecting plate to clean the dust collected on the plate when it flows downward. Compared with the dry electrostatic precipitator: the wet electrostatic precipitator does not need a rapping device, thereby avoiding the secondary dust caused by the rapping, and also preventing the secondary dust caused by the air flow and corona wind; because the electrode plate is always distributed With the downward flowing water film, the dust trapped on the electrode plate is immediately washed away by the water film, so for high specific resistance dust, there will be no back corona, avoiding the secondary dust caused by it; for low For specific resistance dust, the trapped particles will not escape from the plate and return to the airflow again. Due to the above advantages, the wet electrostatic precipitator has a very high dust removal efficiency and can adapt to dust with various specific resistances.

现有的湿式电除尘器收尘极多为板式或圆筒式。由于湿式电除尘器中水膜在极板上依靠重力自行向下流动,若遇到阻碍或极板表面的几何变化,就会改变流向,发生“汇流”、“岔流”等现象,在极板下方不能形成完整均匀的清灰水膜,捕集的粉尘不能及时清理掉,越积越厚,导致电晕极对堆积粉尘放电,甚至会影响电除尘器供电,造成除尘器无法正常运行。当前燃煤发电机组往往较大,对除尘器处理烟气量也提出了更大的要求,这也导致相应的湿式电除尘器的设计尺寸比较大,十多米甚至二十多米的极板高度将使极板上水膜的均匀分布更加困难。传统的湿式电除尘器使用钢制收尘极板,成本较高,且湿式的收尘环境对普通钢制极板会造成腐蚀,使用特种钢制极板或对极板进行防腐化处理也是一笔不小的投资。另外,湿式电除尘器为了能够将捕集的粉尘收集起来,往往需要大量的清灰水,这也不能满足对水资源的集约化利用的要求,而且会产生大量清灰水,对环境造成二次污染,也不利于粉煤灰的综合利用。Most of the existing wet electrostatic precipitators are plate type or cylinder type. Since the water film in the wet electrostatic precipitator flows downward on the pole plate by gravity, if it encounters obstacles or geometric changes on the surface of the pole plate, the flow direction will be changed, and phenomena such as "convergence" and "fork flow" will occur. A complete and uniform dust-removing water film cannot be formed under the plate, and the collected dust cannot be cleaned up in time, and it will accumulate and become thicker, which will cause the corona electrode to discharge the accumulated dust, and even affect the power supply of the electrostatic precipitator, causing the precipitator to fail to operate normally. The current coal-fired power generation units are often large, which also puts forward greater requirements on the amount of flue gas treated by the dust collector, which also leads to a relatively large design size of the corresponding wet electrostatic precipitator, with a plate length of more than ten meters or even more than twenty meters. The height will make it more difficult to evenly distribute the water film on the plates. Traditional wet electrostatic precipitators use steel dust-collecting pole plates, which are expensive, and the wet dust-collecting environment will cause corrosion to ordinary steel pole plates. Using special steel pole plates or anti-corrosion treatment on the pole plates is also a Not a small investment. In addition, wet electrostatic precipitators often need a large amount of ash cleaning water in order to collect the collected dust, which cannot meet the requirements for intensive utilization of water resources, and will produce a large amount of ash cleaning water, causing secondary pollution to the environment. Secondary pollution is also not conducive to the comprehensive utilization of fly ash.

发明内容Contents of the invention

本发明的目的就是为了解决湿式电除尘器收尘极板上无法形成完整均匀的水膜的问题,使湿式电除尘器能够在燃煤电厂稳定运行,提供一种能够减少投资成本、减少腐蚀、节约用水量的湿 式电除尘器收尘极板以及清灰水膜形成方法。The purpose of the present invention is to solve the problem that a complete and uniform water film cannot be formed on the dust collecting plate of the wet electrostatic precipitator, so that the wet electrostatic precipitator can run stably in a coal-fired power plant, and provide a method that can reduce investment costs, reduce corrosion, The invention discloses a dust-collecting plate of a wet-type electrostatic precipitator which saves water consumption and a method for forming a dust-cleaning water film.

为实现上述目的,本发明采用下述技术方案:To achieve the above object, the present invention adopts the following technical solutions:

一种湿式除尘器收尘极板,主体使用耐热塑料、陶瓷材料等材料,具有能够耐受电除尘器内高温、腐蚀的环境,极板表面光滑平整,而且具有一定的刚性和机械强度,满足电除尘器内吊挂、运行的性能要求。湿式电除尘器收尘极板布水管路位于极板内部,沿烟气流动方向依次排列,在收尘极板底部有一条主供水管路将各条布水管路相连接,并通过内部布水管路由下向上供水。布水管路一直通向收尘极板顶部,在极板顶部相应位置开有布水孔,通过溢流的形式向极板布水。A dust collecting pole plate of a wet dust collector. The main body is made of heat-resistant plastic, ceramic materials and other materials, which can withstand the high temperature and corrosion environment in the electric dust collector. The surface of the pole plate is smooth and flat, and it has certain rigidity and mechanical strength. Meet the performance requirements of hanging and running in the electrostatic precipitator. The water distribution pipes of the dust collection plate of the wet electrostatic precipitator are located inside the plate and arranged in sequence along the flow direction of the flue gas. There is a main water supply pipe at the bottom of the dust collection plate to connect the various water distribution pipes, and through the internal water distribution pipe Route down-up water supply. The water distribution pipeline leads all the way to the top of the dust collection plate, and there are water distribution holes at the corresponding positions on the top of the plate, and water is distributed to the plate through overflow.

所述收尘极板上布水孔向收尘极板均衡供水,沿气流方向极板上方各点水流向下流动的初始压力、流速和流量都相同。The water distribution holes on the dust-collecting pole plate supply water to the dust-collecting pole plate in a balanced manner, and the initial pressure, flow velocity and flow rate of the water flowing downward at each point above the pole plate along the airflow direction are the same.

所述收尘极板一般为两片相同的结构板材贴合而成,两片板材上的沟槽在拼接后形成输水管路。为维护和更换方便,整块收尘极板由若干块竖条状的收尘极板条拼接而成。The dust-collecting plate is generally formed by laminating two identical structural plates, and the grooves on the two plates form a water delivery pipeline after splicing. For the convenience of maintenance and replacement, the entire dust collection plate is spliced by several vertical dust collection plates.

一种湿式电除尘器清灰水膜形成方法,收尘极板上悬挂覆盖有纤维编织薄膜,薄膜贴伏于极板表面,利于均匀水膜的形成。A method for forming a dust-cleaning water film of a wet electrostatic precipitator, in which a fiber woven film is suspended and covered on a dust collecting pole plate, and the film is attached to the surface of the pole plate, which is beneficial to the formation of a uniform water film.

所述纤维编织薄膜一般为碳纤维、硅纤维、丙纶或涤纶等类型,具有较好的毛细作用和布水特性。利用编织纤维的毛细作用可使得清灰水膜能够更加均匀稳定地分布于收尘极板表面。The fiber woven film is generally carbon fiber, silicon fiber, polypropylene or polyester, and has good capillary action and water distribution characteristics. Utilizing the capillary action of the braided fibers can make the dust-cleaning water film more evenly and stably distributed on the surface of the dust-collecting plate.

为了保证在极板上形成良好的水膜,在极板上覆盖纤维编织薄膜之前要对极板进行脱脂处理,去除表面油污。In order to ensure a good water film is formed on the pole plate, the pole plate should be degreased before covering the pole plate with a fiber woven film to remove surface oil.

本发明的有益效果是:The beneficial effects of the present invention are:

(1)采用本发明的收尘极板,利用均匀分布于极板内部的布水管路,以及极板表面覆盖的纤维编织薄膜的毛细作用,可以有效解决湿式电除尘器极板表面清灰水膜均匀分布的问题。(1) Adopt the dust-collecting plate of the present invention, utilize the water distribution pipeline evenly distributed inside the plate, and the capillary action of the fiber woven film covered on the surface of the plate, can effectively solve the problem of cleaning water on the surface of the plate surface of the wet electrostatic precipitator The problem of uniform distribution of the film.

(2)清灰水膜均匀完整,清灰效果好,极板上不会形成清灰死角,不会形成影响水膜完整的粉尘块,因而不会发生电晕线对积灰放电现象,确保供电稳定,确保电除尘器正常工作。(2) The dust removal water film is uniform and complete, and the dust removal effect is good. There will be no dead spots for dust removal on the plate, and no dust blocks that will affect the integrity of the water film. Therefore, there will be no discharge phenomenon of corona wires to dust accumulation, ensuring The power supply is stable to ensure the normal operation of the electrostatic precipitator.

(3)节约成本,采用新型材料的收尘极板相对于传统的湿式电除尘器钢制极板成本更加低廉,也大大降低了在防止腐蚀方面的资金投入。(3) Cost saving. Compared with the traditional wet electrostatic precipitator steel plate, the cost of the dust collection plate using new materials is lower, and the capital investment in corrosion prevention is also greatly reduced.

(4)节约用水,采用均匀分布的管路进行供水,并通过纤维编织薄膜的毛细特性进行布水, 形成均匀水膜,可以有效减少保持均匀水膜所用水量。随着用水量的减少带来的是清灰水循环利用设备规模的减少,以及清灰水处理量的减少,反过来又降低了设备的投资和运行费用。(4) Save water, use evenly distributed pipelines for water supply, and distribute water through the capillary characteristics of the fiber woven film to form a uniform water film, which can effectively reduce the amount of water used to maintain a uniform water film. With the reduction of water consumption, the scale of cleaning water recycling equipment is reduced, and the amount of cleaning water treatment is reduced, which in turn reduces the investment and operation costs of equipment.

(5)安装及维修方便,新型材料的收尘极板相对于传统的湿式电除尘器钢制极板质量更轻,安装维护更加方便。采用收尘极板条拼接的形式,使得在极板维修时只要拆除相应的极板条进行更换维护即可。(5) Easy installation and maintenance. Compared with the traditional wet electrostatic precipitator steel plate, the dust collection plate made of new material is lighter, and the installation and maintenance are more convenient. The form of splicing of dust-collecting pole plates is adopted, so that only the corresponding pole plates need to be removed for replacement and maintenance during pole plate maintenance.

附图说明Description of drawings

图1为湿式电除尘器收尘极板正视图。图中,1为极板表面覆盖的纤维编织薄膜;4为收尘极板供水管道;5为供水管道水量控制阀门。Figure 1 is a front view of the dust collecting plate of the wet electrostatic precipitator. In the figure, 1 is the fiber woven film covered on the surface of the pole plate; 4 is the water supply pipe for the dust collector plate; 5 is the water volume control valve of the water supply pipe.

图2为湿式电除尘器收尘极板全剖视图。图中,1为极板表面覆盖的纤维编织薄膜;2为电除尘器收尘极板;3为收尘极板内部布水管路;4为收尘极板供水管道;5为供水管道水量控制阀门。Fig. 2 is a full sectional view of the dust collecting plate of the wet electrostatic precipitator. In the figure, 1 is the fiber woven film covered on the surface of the plate; 2 is the dust collection plate of the electrostatic precipitator; 3 is the water distribution pipeline inside the dust collection plate; 4 is the water supply pipe for the dust collection plate; 5 is the water volume control of the water supply pipe valve.

图3为湿式电除尘器收尘极板A-A垂直断面剖视图。图中,1为极板表面覆盖的纤维编织薄膜;2为电除尘器收尘极板;3为收尘极板内部布水管路;4为收尘极板供水管道。Fig. 3 is a vertical cross-sectional view of A-A of the dust collecting pole plate of the wet electrostatic precipitator. In the figure, 1 is the fiber woven film covered on the surface of the plate; 2 is the dust collection plate of the electrostatic precipitator; 3 is the water distribution pipeline inside the dust collection plate; 4 is the water supply pipe for the dust collection plate.

图4为湿式电除尘器收尘极板B-B水平断面剖视图。Fig. 4 is a horizontal cross-sectional view of B-B of the dust collecting pole plate of the wet electrostatic precipitator.

图5为湿式电除尘器单个极板片示意图及其C-C水平断面剖视图。Fig. 5 is a schematic diagram of a single electrode plate of a wet electrostatic precipitator and its C-C horizontal section view.

具体实施方式detailed description

实施例:如图1、图2和图3所示,主要有:1、纤维编织薄膜;2、电除尘器收尘极板;3、收尘极板内部布水管路;4、收尘极板供水管路组成,在收尘极板供水管路上设置有供水管道水量控制阀门5。纤维编织薄膜1贴覆固定于收尘极板2表面,如图3所示。收尘极板供水管路4将各条收尘极板内部布水管路3相连接,以向其供应冲灰水,如图2所示。电除尘器收尘极板2一般由两片相同的如图5所示的单个收尘极板片相对贴合组装而成,效果可见图4。电除尘器收尘极板2悬挂于湿式电除尘器壳体内部,下部接地。Embodiment: As shown in Fig. 1, Fig. 2 and Fig. 3, it mainly includes: 1. Fiber woven film; 2. Dust collecting plate of electrostatic precipitator; 3. Water distribution pipeline inside the dust collecting plate; 4. Dust collecting pole The plate water supply pipeline is formed, and the water supply pipeline water volume control valve 5 is arranged on the dust collection plate water supply pipeline. The fiber woven film 1 is pasted and fixed on the surface of the dust collecting pole plate 2, as shown in FIG. 3 . The water supply pipeline 4 of the dust collection plate connects the internal water distribution pipeline 3 of each dust collection plate to supply gray flushing water thereto, as shown in FIG. 2 . The dust collector plate 2 of the electrostatic precipitator is generally assembled by two identical single dust collector plates as shown in FIG. 5 , and the effect can be seen in FIG. 4 . The dust collecting pole plate 2 of the electrostatic precipitator is suspended inside the shell of the wet electrostatic precipitator, and the lower part is grounded.

在运行过程中,含尘气体进入除尘部分,并被荷电。在电场力的驱动下,荷电尘粒运动至收尘极板上的纤维编织薄膜1。清灰水在输水泵的驱动下进入收尘极板供水管路4,并由其输送至各个收尘极板内部布水管路3中,清灰水的流量由管道水量控制阀门5调节。清灰水被输送至电除尘器收尘极板2顶部,通过溢流的方式分布至收尘极板表面的纤维编织薄膜1中。纤维编织薄膜1 中的清灰水在重力的作用下向下流动,将薄膜表面的尘粒冲刷下来。清灰水一般进入相应的清灰水循环利用系统,经处理循环使用。During operation, the dust-containing gas enters the dust removal part and is charged. Driven by the force of the electric field, the charged dust particles move to the fiber woven film 1 on the dust collecting plate. The ash removal water enters the dust collection plate water supply pipeline 4 driven by the water transfer pump, and is transported by it to the internal water distribution pipeline 3 of each dust collection plate. The flow of the ash removal water is regulated by the pipeline water volume control valve 5. The cleaning water is transported to the top of the dust collection plate 2 of the electrostatic precipitator, and is distributed to the fiber woven film 1 on the surface of the dust collection plate by way of overflow. The dedusting water in the fiber woven film 1 flows downward under the action of gravity to wash down the dust particles on the surface of the film. The ash removal water generally enters the corresponding ash removal water recycling system and is recycled after treatment.

Claims (3)

1.一种湿式电除尘器收尘极板,其特征是,主体由两片相同结构的、具有一定刚性和机械强度的耐热塑料或陶瓷材料贴合而成,表面贴伏有纤维编织薄膜,两片极板上的沟槽在贴合后形成布水管路,布水管路位于极板内部,沿烟气流动方向依次竖直排列,在收尘极板底部有一条主供水管路将各条布水管路相连接,并通过内部布水管路由下向上供水,布水管路一直通向收尘极板顶部,在极板顶部相应位置开有布水孔,通过溢流的形式向极板布水。1. A dust-collecting pole plate of a wet electrostatic precipitator, characterized in that the main body is made of two heat-resistant plastic or ceramic materials with the same structure and certain rigidity and mechanical strength, and a fiber woven film is attached to the surface , the grooves on the two pole plates form a water distribution pipeline after they are bonded together. The water distribution pipeline is located inside the pole plate and arranged vertically along the flue gas flow direction. There is a main water supply pipeline at the bottom of the dust collecting pole plate to connect each The water distribution pipelines are connected together, and the water is supplied from the bottom to the top through the internal water distribution pipeline. The water distribution pipeline leads to the top of the dust collecting plate. There are water distribution holes at the corresponding position on the top of the plate, and the water is distributed to the plate through the form of overflow. water. 2.根据权利要求1所述的湿式电除尘器收尘极板,其特征在于所述的极板由两片相同结构的板材贴合而成,两片极板上的沟槽在贴合后形成布水管路,布水管路沿烟气流动方向均匀排布,保证在极板上方向极板均匀供水,沿烟气方向极板顶部各布水孔水流向下流动的初始压力、流速、流量都相同。2. The dust collecting pole plate of the wet electrostatic precipitator according to claim 1, characterized in that the pole plate is formed by laminating two plates of the same structure, and the grooves on the two pole plates are formed after lamination. The water distribution pipeline is formed, and the water distribution pipeline is evenly arranged along the flow direction of the flue gas to ensure uniform water supply to the pole plate in the direction of the pole plate. all the same. 3.一种权利要求1所述的湿式电除尘器收尘极板的清灰水膜形成方法,其特征是,对具有一定刚性和机械强度的收尘极板进行脱脂处理后,在其表面贴伏纤维编织薄膜,利用纤维编织薄膜的毛细作用,使清灰水均匀、快速地分布于薄膜表面。3. a method for forming a dust-cleaning water film of the dust-collecting pole plate of a wet-type electrostatic precipitator as claimed in claim 1, characterized in that, after degreasing the dust-collecting pole plate with certain rigidity and mechanical strength, on its surface Lay fiber woven film, use the capillary action of fiber woven film to distribute the cleaning water evenly and quickly on the surface of the film.
CN201310528825.6A 2013-10-23 2013-10-23 Formation mode of dust collection pole plate and ash removal water film of wet-type electric precipitator Expired - Fee Related CN103586135B (en)

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