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CN206597461U - The emission-control equipment of array plasma catalyst synergy - Google Patents

The emission-control equipment of array plasma catalyst synergy Download PDF

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CN206597461U
CN206597461U CN201720275589.5U CN201720275589U CN206597461U CN 206597461 U CN206597461 U CN 206597461U CN 201720275589 U CN201720275589 U CN 201720275589U CN 206597461 U CN206597461 U CN 206597461U
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plasma
electrode
catalyst
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electrodes
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刘克富
肖泽铧
郝春静
徐迪
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Fudan University
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Abstract

本实用新型属于环保技术领域,具体为阵列式等离子体‑催化剂协同作用的废气处理装置。本实用新型装置包括:脉冲电源、金属电极、绝缘介质管、催化剂模块及壳体;金属电极插在绝缘介质管中,作为等离子体发生电极,等离子体发生电极以几何阵列的形式排列,同一列电极中高压电极与地电极相间排布;催化剂模块插在相邻两列等离子体发生电极之间;等离子体产生于同列电极之间的气隙之中,可以通过调节电极的行数、列数,以满足不同种类、浓度、空速的废气治理需求。催化剂模块置于相邻两列电极之间,紧靠在等离子体放电区域之后,使废气依次通过多层等离子体与催化剂,既可避免催化剂结构遭等离子体破坏,又可使等离子体放电产生的活性粒子与催化剂充分接触,使其达到高效的协同作用。

The utility model belongs to the technical field of environmental protection, in particular to an array type plasma-catalyst synergistic exhaust gas treatment device. The utility model device comprises: a pulse power supply, a metal electrode, an insulating medium tube, a catalyst module and a casing; the metal electrode is inserted into the insulating medium tube as a plasma generating electrode, and the plasma generating electrodes are arranged in a geometric array, and the same row Among the electrodes, the high-voltage electrodes and the ground electrodes are arranged alternately; the catalyst module is inserted between two adjacent columns of plasma generating electrodes; the plasma is generated in the air gap between the electrodes in the same column, and the number of rows and columns of electrodes can be adjusted To meet the needs of exhaust gas treatment of different types, concentrations, and space velocities. The catalyst module is placed between two adjacent rows of electrodes, close to the plasma discharge area, so that the exhaust gas passes through the multi-layer plasma and the catalyst in sequence, which can not only prevent the catalyst structure from being damaged by the plasma, but also make the plasma discharge The active particles are in full contact with the catalyst to achieve efficient synergy.

Description

阵列式等离子体-催化剂协同作用的废气处理装置Array type plasma-catalyst synergistic exhaust gas treatment device

技术领域technical field

本实用新型属于环保技术领域,具体涉及阵列式等离子体-催化剂协同作用的废气处理装置。The utility model belongs to the technical field of environmental protection, and in particular relates to an array type plasma-catalyst synergistic waste gas treatment device.

背景技术Background technique

经济建设带来的大气污染问题已成为最严重的环境问题之一,工业废气中含有挥发性有机化合物(volatile organic compounds,简称VOCs)、二氧化硫、氮氧化物等诸多有毒有害性气体,不但严重危害人体生命健康,而且对地球生态环境有着巨大的危害。传统的废气处理技术如焚烧法、吸附法、冷凝法等,存在着净化效率低、投入成本高、易产生二次污染等弊端,难以满足现代工业社会的需求。The air pollution caused by economic construction has become one of the most serious environmental problems. Industrial waste gas contains many toxic and harmful gases such as volatile organic compounds (VOCs), sulfur dioxide, nitrogen oxides, etc., which not only seriously harm the Human life is healthy, and it has great harm to the earth's ecological environment. Traditional waste gas treatment technologies such as incineration, adsorption, condensation, etc., have disadvantages such as low purification efficiency, high input cost, and easy to produce secondary pollution, making it difficult to meet the needs of modern industrial society.

等离子体是由离子、电子、中性粒子组成的整体呈电中性的物质集合,是不同于固体、液体、气体的物质第四态,其中非热力学平衡等离子体在宏观上的温度接近常温,被称为低温等离子体,广泛应用于材料、电子等领域,并在环保领域备受关注。利用介质阻挡放电技术能在大气压下产生大面积的低温等离子体,等离子体中存在着大量的高能电子,与废气中的背景气体分子发生非弹性碰撞,通过能量传递产生种类繁多的激发态物种、正负离子、自由基等活性粒子,其中臭氧、激发态氧原子、羟基自由基等组分则有着很强的氧化性,能将废气中的有毒有害成分氧化降解,转化成无毒无害或是低毒低害的物质。介质阻挡放电处理废气可在常温常压下进行,运行方便、操作简单、处理效率高且二次污染小,有着广阔的应用前景。Plasma is a collection of electrically neutral substances composed of ions, electrons, and neutral particles. It is the fourth state of matter different from solids, liquids, and gases. Known as low-temperature plasma, it is widely used in materials, electronics and other fields, and has attracted much attention in the field of environmental protection. The use of dielectric barrier discharge technology can generate a large area of low-temperature plasma under atmospheric pressure. There are a large number of high-energy electrons in the plasma, which inelastically collide with the background gas molecules in the exhaust gas, and generate a wide variety of excited state species through energy transfer. Positive and negative ions, free radicals and other active particles, among which components such as ozone, excited oxygen atoms, and hydroxyl radicals have strong oxidizing properties, which can oxidize and degrade toxic and harmful components in the exhaust gas, and convert them into non-toxic and harmless or Substances with low toxicity and low harm. Dielectric barrier discharge treatment of waste gas can be carried out at normal temperature and pressure, with convenient operation, simple operation, high treatment efficiency and low secondary pollution, and has broad application prospects.

低温等离子体技术处理废气存在能耗较高、易产生多种副产物的缺陷,为了解决这一问题,等离子体-催化协同技术成为了研究热点。利用等离子体高反应活性的优点,结合活性催化剂,在室温下即可显著提高废气降解的能量效率,减少副产物的生成,提高有毒有害气体的转化率和矿化率。传统的催化剂填充方式分为一段式和二段式:一段式是将催化剂置于等离子体反应器内部,这种结构可以充分利用等离子体中产生的短寿命活性物质,对废气分子进行催化氧化,缺点是催化剂长时间置于等离子体中可能会遭到破坏;二段式是将催化剂置于等离子体反应器之后,这种结构可以防止催化剂结构被等离子体破坏,缺点是只有长寿命的活性物质才可到达催化剂层,且催化剂吸附饱和后需要再生或更换。Low-temperature plasma technology has the disadvantages of high energy consumption and easy production of various by-products in the treatment of waste gas. In order to solve this problem, plasma-catalysis synergistic technology has become a research hotspot. Utilizing the advantages of high plasma reactivity, combined with active catalysts, the energy efficiency of waste gas degradation can be significantly improved at room temperature, the generation of by-products can be reduced, and the conversion rate and mineralization rate of toxic and harmful gases can be improved. The traditional catalyst filling method is divided into one-stage and two-stage: one-stage is to place the catalyst inside the plasma reactor. This structure can make full use of the short-lived active substances generated in the plasma to catalyze the oxidation of exhaust gas molecules. The disadvantage is that the catalyst may be damaged if it is placed in the plasma for a long time; the two-stage type is to place the catalyst after the plasma reactor. This structure can prevent the catalyst structure from being damaged by the plasma. The disadvantage is that there are only long-lived active substances The catalyst layer can only be reached, and the catalyst needs to be regenerated or replaced after the adsorption is saturated.

现有的介质阻挡放电装置通常存在形状受限制、处理气体量少、电极难以更换等不足,难以满足不同种类、浓度和空速的废气治理需求,后期维护困难,这些因素都限制了等离子体装置在工业废气治理领域的广泛应用。Existing dielectric barrier discharge devices usually have shortcomings such as limited shape, small amount of processing gas, and difficult to replace electrodes. It is difficult to meet the needs of exhaust gas treatment of different types, concentrations, and space velocities, and it is difficult to maintain in the later stage. These factors limit the plasma device. It is widely used in the field of industrial waste gas treatment.

发明内容Contents of the invention

本实用新型提供了一种等离子体-催化协同作用的工业废气处理装置,目的在于解决等离子体发生器处理气量小、难以维护,以及传统催化剂填充方式难以与等离子体有效结合的问题。The utility model provides a plasma-catalysis synergistic industrial waste gas treatment device, aiming to solve the problems that the plasma generator has a small processing gas volume, is difficult to maintain, and the traditional catalyst filling method is difficult to effectively combine with the plasma.

本实用新型提出的等离子体-催化协同作用的工业废气处理装置,其构成如图1和图2所示,包括:脉冲电源、金属电极、绝缘介质管、催化剂模块及壳体;其中,一根金属电极插在一个绝缘介质管中,作为等离子体发生电极,绝缘介质管呈柱状的长条型,一端封闭,另一端开口以引出金属电极;绝缘介质管以几何阵列的形式排列,且同一列中绝缘介质管的端封闭和开口端方向相间排列,一个方向引出的金属电极接脉冲电源的高压输出,成为高压电极,另一方向引出的金属电极接大地,成为地电极;这样使等离子体发生电极以几何阵列的形式排列,同一列电极中高压电极与地电极相间排布(即交叉分布),当电源输出电压达到击穿电压时,相邻的高压电极与地电极之间将产生等离子体;催化剂模块插在相邻两列等离子体发生电极之间,与等离子体协同处理有害气体;整个电极阵列安装在壳体内。The industrial waste gas treatment device with plasma-catalysis synergy proposed by the utility model is composed as shown in Figure 1 and Figure 2, including: pulse power supply, metal electrode, insulating medium tube, catalyst module and housing; wherein, a The metal electrode is inserted in an insulating dielectric tube as a plasma generating electrode. The insulating dielectric tube is a long columnar shape with one end closed and the other end open to lead out the metal electrode; the insulating dielectric tubes are arranged in a geometric array, and the same row The closed end and the open end of the medium insulating medium tube are arranged alternately. The metal electrode drawn in one direction is connected to the high-voltage output of the pulse power supply to become a high-voltage electrode, and the metal electrode drawn in the other direction is connected to the earth to become a ground electrode; in this way, the plasma is generated. The electrodes are arranged in a geometric array. In the same row of electrodes, the high-voltage electrodes and the ground electrodes are arranged alternately (that is, cross-distributed). When the output voltage of the power supply reaches the breakdown voltage, plasma will be generated between the adjacent high-voltage electrodes and the ground electrodes. ; The catalyst module is inserted between two adjacent rows of plasma generation electrodes, and the harmful gas is treated in cooperation with the plasma; the entire electrode array is installed in the casing.

本实用新型中,为防止高压电极与壳体之间打火,在绝缘介质管封闭端留出一段1-2cm长的真空区域或是介质层,其余部分填充金属电极;同一列等离子体发生电极中,交叉排列的高压电极与地电极之间间距与脉冲电源输出电压相匹配,可在1-10mm间进行调节。In the utility model, in order to prevent ignition between the high-voltage electrode and the housing, a 1-2cm long vacuum area or medium layer is reserved at the closed end of the insulating medium tube, and the remaining part is filled with metal electrodes; the same row of plasma generating electrodes Among them, the distance between the cross-arranged high-voltage electrodes and the ground electrodes matches the output voltage of the pulse power supply, and can be adjusted between 1-10mm.

本实用新型中,所述绝缘介质管的尺寸可根据实际情况调节,例如,外径为2-5mm,内径为1-3mm,长度80mm -300mm。In the present invention, the size of the insulating medium pipe can be adjusted according to the actual situation, for example, the outer diameter is 2-5mm, the inner diameter is 1-3mm, and the length is 80mm-300mm.

本实用新型中,所述绝缘介质管为耐高压非极性绝缘材料,可选石英玻璃、陶瓷(如氧化铝、氧化锆、氮化硅)、环氧树脂、聚四氟乙烯等,以石英玻璃、陶瓷为佳;所述金属电极为导电性良好的金属材料,可选金、银、铜、铁、铝、锌、钨、铂、钯、铱、不锈钢等,可以是金属棒、金属粉末,若是金属粉末则在填充入绝缘介质管后需引出一根导线,与外界电源相连。In the utility model, the insulating medium tube is a high-voltage non-polar insulating material, which can be quartz glass, ceramics (such as alumina, zirconia, silicon nitride), epoxy resin, polytetrafluoroethylene, etc., and quartz Glass and ceramics are preferred; the metal electrode is a metal material with good conductivity, which can be gold, silver, copper, iron, aluminum, zinc, tungsten, platinum, palladium, iridium, stainless steel, etc., and can be a metal rod or metal powder If it is metal powder, it needs to lead out a wire after filling it into the insulating medium tube, and connect it to the external power supply.

本实用新型中,所述高压电极与地电极从相对的两个侧面分别引出并通过金属板(金属条)连接在一起,使得高压电极与地电极各自保持电势相等;所述等离子体发生电极与壳体、金属板(金属条)之间通过螺丝、卡扣等可拆卸部件相连接,方便更换电极。In the utility model, the high-voltage electrode and the ground electrode are respectively drawn from two opposite sides and connected together through a metal plate (metal strip), so that the high-voltage electrode and the ground electrode maintain equal potentials; the plasma generating electrode and the The housing and the metal plate (metal strip) are connected by removable parts such as screws and buckles, which is convenient for electrode replacement.

本实用新型中,所述装置壳体为易加工抗腐蚀绝缘材料,可以是有机玻璃、聚四氟乙烯、环氧等。In the utility model, the housing of the device is an easy-to-process and anti-corrosion insulating material, which can be plexiglass, polytetrafluoroethylene, epoxy and the like.

本实用新型中,所述等离子体发生电极的长度、每列电极的根数、同列电极之间距离以及电极的列数均可调节。当废气空速一定时,改变电极长度、每列电极根数或同列电极之间距离可改变产生的等离子体的横截面积,从而改变废气的停留时间;改变电极列数则可改变废气流动方向上的等离子体区域长度,同样可改变废气的停留时间。因此,对于确定的某一工业废气,在保证足够的停留时间使其达到所需的降解效果时,可以通过增加等离子体发生电极的长度、每列电极的根数、同列电极之间距离以及电极的列数来增大废气空速,增加装置处理气体的气量。In the present invention, the length of the plasma generating electrodes, the number of electrodes in each row, the distance between electrodes in the same row and the number of rows of electrodes can all be adjusted. When the air velocity of the exhaust gas is constant, changing the electrode length, the number of electrodes in each column or the distance between electrodes in the same column can change the cross-sectional area of the generated plasma, thereby changing the residence time of the exhaust gas; changing the number of electrode columns can change the flow direction of the exhaust gas The length of the plasma region above can also change the residence time of the exhaust gas. Therefore, for a certain industrial waste gas, when ensuring sufficient residence time to achieve the desired degradation effect, the length of the plasma generation electrode, the number of electrodes in each column, the distance between electrodes in the same column and the distance between electrodes can be increased. The number of columns to increase the exhaust gas space velocity and increase the gas volume of the device to process the gas.

本实用新型中,相邻两列等离子体发生电极之间距离可调。催化剂的一段式填充方式可能会使催化剂结构遭破坏,二段式填充方式会减弱活性粒子与催化剂的协同作用,将催化剂填充在相邻两列电极之间则既可避免催化剂结构遭破坏,又可使催化剂紧靠等离子体放电区域,使得等离子体放电产生的活性粒子与催化剂充分接触,产生协同作用。通过改变相邻两列电极之间距离可调节等离子体放电区域与催化剂模块之间的距离,从而经过系列实验来找到催化剂最适宜的填充位,提高系统效能。In the utility model, the distance between two adjacent rows of plasma generating electrodes is adjustable. The one-stage filling method of the catalyst may damage the catalyst structure, and the two-stage filling method will weaken the synergy between the active particles and the catalyst. Filling the catalyst between two adjacent rows of electrodes can not only avoid the destruction of the catalyst structure, but also The catalyst can be close to the plasma discharge area, so that the active particles generated by the plasma discharge can fully contact with the catalyst to produce a synergistic effect. By changing the distance between two adjacent rows of electrodes, the distance between the plasma discharge area and the catalyst module can be adjusted, so that a series of experiments can be performed to find the most suitable filling position of the catalyst and improve the system performance.

本实用新型中,所述脉冲电源施加于等离子体发生电极上产生的脉冲电压为1-100kV,频率为0-10kHz。相比于传统的交流电源,脉冲电源功率更小、放电气体温度更低、产生的活性粒子种类更多、臭氧量更大,处理废气的效果更好、成本更低。In the utility model, the pulse voltage generated by the pulse power supply applied to the plasma generating electrode is 1-100kV, and the frequency is 0-10kHz. Compared with the traditional AC power supply, the pulse power supply has smaller power, lower discharge gas temperature, more types of active particles, larger amount of ozone, better waste gas treatment effect and lower cost.

本实用新型中,催化剂模块可以压制成片的形式直接插入等离子体阵列之间,也可以用耐压、耐温、耐腐蚀材料(聚四氟乙烯)所制成的网状盒子,将催化剂填充在盒中;填充型催化剂可以是粉末状、颗粒状、块状等。网状盒子,以让废气气体通过。聚四氟乙烯有着良好的电绝缘性、抗腐蚀性、抗老化与抗高温耐力,对人体无毒,是良好的封装材料。In the utility model, the catalyst module can be directly inserted between the plasma arrays in the form of pressing into sheets, or a mesh box made of pressure-resistant, temperature-resistant, and corrosion-resistant materials (polytetrafluoroethylene) can be used to fill the catalyst In the box; packed catalyst can be powder, granular, block and so on. Mesh box to allow exhaust gases to pass through. PTFE has good electrical insulation, corrosion resistance, anti-aging and high temperature resistance, non-toxic to the human body, and is a good packaging material.

本实用新型中,气体源可以是混合了工业废气的空气、氦气、氩气、氮气等,气体压力、温度、湿度、流速等在一定范围内可根据要求做不同选择。In the utility model, the gas source can be air mixed with industrial waste gas, helium, argon, nitrogen, etc., and the gas pressure, temperature, humidity, flow rate, etc. can be selected according to requirements within a certain range.

本实用新型可以产生大面积的等离子体,可通过调节等离子体发生电极的长度、数量、间距来满足不同种类、浓度与空速的工业废气处理需求;电极可拆卸,维护方便;催化剂与等离子体放电区域交替分布,弥补了催化剂一段式、二段式填充方式的不足,能充分发挥出等离子体-催化剂的协同作用;使用脉冲电源作为等离子体发生源,可产生接近室温的等离子体,能量效率高、运行成本低。The utility model can generate large-area plasma, and can meet the industrial waste gas treatment requirements of different types, concentrations and space velocities by adjusting the length, quantity and spacing of the plasma generating electrodes; the electrodes are detachable and easy to maintain; the catalyst and plasma The discharge area is distributed alternately, which makes up for the deficiency of the one-stage and two-stage filling methods of the catalyst, and can give full play to the synergistic effect of the plasma-catalyst; using the pulse power supply as the plasma generation source, it can generate plasma close to room temperature, with high energy efficiency. High, low operating costs.

附图说明Description of drawings

图1为本实用新型原理结构的俯视图。Fig. 1 is the plan view of the principle structure of the utility model.

图2为本实用新型原理结构的左视图。Fig. 2 is the left view of the principle structure of the utility model.

具体实施方式detailed description

图1、图2分别为本实用新型原理结构的俯视图、左视图,包括高压电极1、地电极2、绝缘介质管3、高压金属板4、接地金属板5、催化剂模块6和脉冲电源7。本实施例中等离子体发生电极有3列×6行共18根,所有高压电极1与高压金属板4通过接线柱相连,高压金属板与脉冲电源7的高压输出相连;所有地电极2与接地金属板4通过接线柱相连,并与大地相连;高压电极1与地电极2置于绝缘介质管3中,分别组成一根等离子体发生电极;催化剂模块6置于相邻的两列等离子体发生电极之间。Fig. 1 and Fig. 2 are respectively the top view and the left view of the principle structure of the utility model, including a high voltage electrode 1, a ground electrode 2, an insulating medium pipe 3, a high voltage metal plate 4, a grounding metal plate 5, a catalyst module 6 and a pulse power supply 7. In this embodiment, there are 18 plasma generating electrodes in 3 columns×6 rows, all high-voltage electrodes 1 are connected to high-voltage metal plates 4 through terminal posts, and high-voltage metal plates are connected to the high-voltage output of pulse power supply 7; all ground electrodes 2 are connected to the ground The metal plate 4 is connected to the ground through a terminal; the high-voltage electrode 1 and the ground electrode 2 are placed in the insulating medium tube 3 to form a plasma generating electrode; the catalyst module 6 is placed in two adjacent columns of plasma generating electrodes. between the electrodes.

工业废气流动方向如图1中风向所示,废气交替通过等离子体放电区域和催化剂模块。等离子体放电区域中有大量的高能电子和强氧化性活性粒子,与废气中的有害气体分子产生碰撞、裂解、氧化等物理化学反应,未被彻底转化成无害物质的废气再进入后续的催化剂模块,经过吸附、催化氧化,大大提高有害气体的转化率,如是经过多层放电区域与催化剂模块,使得废气被彻底净化,达到排放标准。The flow direction of industrial waste gas is shown in the wind direction in Figure 1, and the waste gas alternately passes through the plasma discharge area and the catalyst module. There are a large number of high-energy electrons and strong oxidizing active particles in the plasma discharge area, which have physical and chemical reactions such as collision, cracking, and oxidation with harmful gas molecules in the exhaust gas, and the exhaust gas that has not been completely converted into harmless substances enters the subsequent catalyst The module, through adsorption and catalytic oxidation, greatly improves the conversion rate of harmful gases. If it passes through the multi-layer discharge area and the catalyst module, the exhaust gas is completely purified and meets the emission standard.

本实施例装置中,高压电极1、地电极2为铜棒,长220mm,外径2mm;绝缘介质管3为石英玻璃管,长200mm,外径4mm,内径2mm,电极插入介质管中在顶端留有10mm空隙,对高压尖端起到绝缘保护的作用。In the device of this embodiment, the high-voltage electrode 1 and the ground electrode 2 are copper rods with a length of 220 mm and an outer diameter of 2 mm; the insulating dielectric tube 3 is a quartz glass tube with a length of 200 mm, an outer diameter of 4 mm, and an inner diameter of 2 mm. The electrodes are inserted into the dielectric tube at the top A 10mm gap is left to provide insulation protection for the high voltage tip.

上述装置中,同列电极间气隙间隔为4mm,相邻两列电极之间气隙间隔20mm,选用分子筛为催化剂,填充在聚四氟乙烯制成的长方体网盒中,插入相邻电极之间。In the above device, the air gap interval between electrodes in the same row is 4mm, and the air gap interval between two adjacent rows of electrodes is 20mm. Molecular sieve is used as the catalyst, filled in a rectangular parallelepiped net box made of polytetrafluoroethylene, and inserted between adjacent electrodes. .

上述装置中,脉冲电源7为高频高压单极性脉冲电源,频率0~10kHz可调,电压0~30kV可调。In the above device, the pulse power supply 7 is a high-frequency high-voltage unipolar pulse power supply, the frequency is adjustable from 0 to 10 kHz, and the voltage is adjustable from 0 to 30 kV.

选用浓度200ppm、空速10L/min的二甲苯模拟废气作为实验样品气体,在25℃室温环境下,通过调节脉冲电源输出电压与催化剂的填充量,可使二甲苯的转化率达到95%以上,二氧化碳选择性在60%以上。The xylene simulated exhaust gas with a concentration of 200ppm and a space velocity of 10L/min was selected as the experimental sample gas. At a room temperature of 25°C, by adjusting the output voltage of the pulse power supply and the filling amount of the catalyst, the conversion rate of xylene can reach more than 95%. Carbon dioxide selectivity is above 60%.

对于实际废气,催化剂的种类、填量须视情况而定。对于低浓度、小气量的易处理气体,可不添加催化剂模块,仅用等离子体进行处理;对于高浓度、大气量的工业废气,依次添加催化剂,探究处理结果达标所需的催化剂量,以降低装置成本。For the actual exhaust gas, the type and filling amount of the catalyst shall depend on the situation. For low-concentration and small-volume easy-to-treat gases, the catalyst module may not be added, and only plasma can be used for treatment; for high-concentration and large-volume industrial waste gases, catalysts are added in sequence to explore the amount of catalyst required for the treatment results to meet the standard, so as to reduce the cost of the device. cost.

在实际应用中,等离子体发生电极的列数、行数及长度根据实际情况可大幅改变,以满足不同种类、浓度、空速的工业废气治理需求;电极间行距可在适当范围内调节,与脉冲电源相匹配;电极间列距、催化剂模块层数、催化剂模块与电极间距离应根据实际情况决定,使系统的效率达到最高。In practical applications, the number of columns, rows and lengths of plasma generating electrodes can be greatly changed according to actual conditions to meet the needs of industrial waste gas treatment of different types, concentrations, and space velocities; the row spacing between electrodes can be adjusted within an appropriate range, and The pulse power supply should be matched; the distance between the electrodes, the number of layers of the catalyst module, and the distance between the catalyst module and the electrodes should be determined according to the actual situation to maximize the efficiency of the system.

Claims (9)

1. a kind of emission-control equipment of array Plasma catalyst synergy, it is characterised in that including:Pulse electricity Source, metal electrode, insulated dielectric tube, catalyst module and housing;Wherein, a metal electrode is inserted in an insulated dielectric tube In, as plasma-generating electrode, the long strip type that insulated dielectric tube is in the form of a column, one end closing, another end opening is to draw gold Belong to electrode;Insulated dielectric tube is arranged in the form of geometric array, and in same row insulated dielectric tube end seal closing and opening mouthful end side To spaced, the metal electrode that side direction is drawn connects the High voltage output of the pulse power, as high-field electrode, opposite side direction The metal electrode of extraction connects the earth, as ground electrode;Plasma-generating electrode is so set to be arranged in the form of geometric array, together One row electrode mesohigh electrode and ground electrode interphase distribution;Catalyst module be inserted in adjacent two row plasma-generating electrode it Between;Whole electrod-array is arranged in housing.
2. the emission-control equipment of array Plasma catalyst synergy according to claim 1, its feature exists In the blind end of the insulated dielectric tube reserves the vacuum area of one section of 1-2cm length, or filled media layer, remainder filling Metal electrode;In same row plasma-generating electrode, spacing and pulse electricity between the high-field electrode and ground electrode of cross arrangement Source output voltage matches, and spacing is adjusted between 1-10mm.
3. the emission-control equipment of array Plasma catalyst synergy according to claim 1 or 2, it is special Levy and be, the insulated dielectric tube is high pressure resistant nonpolar insulating materials, selected from quartz glass, ceramics, epoxy resin, polytetrafluoro Ethene;The metal electrode is metal material with good conductivity, selected from gold, silver, copper, iron, aluminium, zinc, tungsten, platinum, palladium, iridium, no Become rusty steel, and its form is metal bar or metal dust, if metal dust then needs extraction one to lead after insulated dielectric tube is packed into Line, is connected with extraneous power supply or ground.
4. the emission-control equipment of array Plasma catalyst synergy according to claim 3, its feature exists In the high-field electrode is drawn and linked together by metallic plate respectively with ground electrode from two relative sides, makes high pressure Electrode is equal with each self-sustaining potential of ground electrode.
5. the emission-control equipment of the array Plasma catalyst synergy according to claim 1,2 or 4, its It is characterised by, is connected between plasma-generating electrode and housing, metallic plate by detachable blocks such as screw, buckles.
6. the emission-control equipment of array Plasma catalyst synergy according to claim 5, its feature exists The columns of distance and electrode is equal between the length of, the plasma-generating electrode, the radical of each column electrode, same column electrode It is adjustable.
7. the emission-control equipment of the array Plasma catalyst synergy according to claim 1,2,4 or 6, Characterized in that, it is 1-100kV that the pulse power, which puts on the pulse voltage produced on plasma-generating electrode, frequency is 0-10kHz。
8. the emission-control equipment of array Plasma catalyst synergy according to claim 7, its feature exists In, catalyst module is inserted directly between plasma array in tabletted form, or catalyst be filled in it is netted In box, between catalyst box insertion plasma array.
9. the emission-control equipment of array Plasma catalyst synergy according to claim 1, its feature exists In gas source is air, helium, argon gas or the nitrogen for being mixed with industrial waste gas.
CN201720275589.5U 2017-03-21 2017-03-21 The emission-control equipment of array plasma catalyst synergy Expired - Fee Related CN206597461U (en)

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CN109772111A (en) * 2019-02-01 2019-05-21 广州尚洁环保科技有限公司 One kind being based on Electronics Factory workshop organic exhaust gas micro discharge processing unit
CN110127624A (en) * 2018-02-09 2019-08-16 中国石油化工股份有限公司 The method of grating type high throughput plasma reactor and decomposing hydrogen sulfide
CN113727509A (en) * 2021-09-02 2021-11-30 南通三信塑胶装备科技股份有限公司 Discharge generating structure and planar plasma discharge generating device based on same
CN113893650A (en) * 2021-10-29 2022-01-07 杭州壹鼎工贸有限公司 Plasma ozone deodorization waste gas treatment equipment
CN116282408A (en) * 2023-05-04 2023-06-23 珠海格力电器股份有限公司 Purification device, preparation method of catalytic structure and wastewater treatment equipment

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110127624A (en) * 2018-02-09 2019-08-16 中国石油化工股份有限公司 The method of grating type high throughput plasma reactor and decomposing hydrogen sulfide
CN110127624B (en) * 2018-02-09 2023-08-15 中国石油化工股份有限公司 Grid type high flux plasma reactor and method for decomposing hydrogen sulfide
CN109772111A (en) * 2019-02-01 2019-05-21 广州尚洁环保科技有限公司 One kind being based on Electronics Factory workshop organic exhaust gas micro discharge processing unit
CN109772111B (en) * 2019-02-01 2022-02-22 广州尚洁环保科技有限公司 Based on little discharge treatment device of electron factory workshop organic waste gas
CN113727509A (en) * 2021-09-02 2021-11-30 南通三信塑胶装备科技股份有限公司 Discharge generating structure and planar plasma discharge generating device based on same
CN113727509B (en) * 2021-09-02 2023-08-18 南通三信塑胶装备科技股份有限公司 Discharge generating structure and planar plasma discharge generating device based on same
CN113893650A (en) * 2021-10-29 2022-01-07 杭州壹鼎工贸有限公司 Plasma ozone deodorization waste gas treatment equipment
CN116282408A (en) * 2023-05-04 2023-06-23 珠海格力电器股份有限公司 Purification device, preparation method of catalytic structure and wastewater treatment equipment

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