[go: up one dir, main page]

CN202237791U - Organic gas plasma catalytic converter - Google Patents

Organic gas plasma catalytic converter Download PDF

Info

Publication number
CN202237791U
CN202237791U CN201120151093XU CN201120151093U CN202237791U CN 202237791 U CN202237791 U CN 202237791U CN 201120151093X U CN201120151093X U CN 201120151093XU CN 201120151093 U CN201120151093 U CN 201120151093U CN 202237791 U CN202237791 U CN 202237791U
Authority
CN
China
Prior art keywords
electric field
catalyst
shell
negative electrode
honeycomb carrier
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201120151093XU
Other languages
Chinese (zh)
Inventor
魏飞
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to CN201120151093XU priority Critical patent/CN202237791U/en
Application granted granted Critical
Publication of CN202237791U publication Critical patent/CN202237791U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

Landscapes

  • Physical Or Chemical Processes And Apparatus (AREA)
  • Catalysts (AREA)

Abstract

The utility model relates to an organic gas plasma catalytic converter, it includes a shell, parallelly connected or a plurality of electric fields of establishing ties in the shell, the electric field comprises negative electrode and positive electrode, all coats high dielectric constant material layer and electricity respectively connect to a high-voltage pulse power just, negative pole on just, the negative electrode, place the electric field catalyst honeycomb carrier that several porous ceramics made in the electric field, the difference packing load is TiO catalyst honeycomb carrier in2And AL2O3A first catalyst of (2), supported by V2O5And TiO2The second catalyst is connected with a section of non-electric field catalyst honeycomb carrier in series close to the electric field after the electric field, and the filling load is MnO2The third catalyst of (1). The utility model discloses can improve energy utilization efficiency and reduce the CO emission by a wide margin.

Description

一种有机气体等离子催化器An organic gas plasma catalyst

技术领域 technical field

本实用新型涉及一种在常温状态等离子体环境下催化降解有机气体的反应装置。  The utility model relates to a reaction device for catalyzing and degrading organic gas in a plasma environment at normal temperature. the

背景技术Background technique

目前,环保领域有机气体的净化方法分为分离法和降解法。分离法有溶剂吸收、吸附脱附分离、冷凝法、膜分离法,降解法有燃烧、催化燃烧、生物降解、等离子消除法。  At present, the purification methods of organic gases in the field of environmental protection are divided into separation methods and degradation methods. Separation methods include solvent absorption, adsorption-desorption separation, condensation, and membrane separation, and degradation methods include combustion, catalytic combustion, biodegradation, and plasma elimination. the

目前的等离子反应器结构如图1所示:通过直流高压电源90向外壳91内的与外壳91电连接的第一电极92和第二电极93供电,第二电极93通过尖刺的放电极94向第一电极92放电,从而在外壳91空间内产生等离子体。含有有机气体的气流沿着图中C所示的方向流动,在等离子体中有机气体被部分分解产生CO2、H2O、CO、及其中间产物CxHyOz,这种结构不仅降解率低,而且能量利用率低,最重要的是产生可观的CO,带来更严重的污染。  The current plasma reactor structure is as shown in Figure 1: the first electrode 92 and the second electrode 93 electrically connected to the shell 91 in the shell 91 are powered by a direct current high voltage power supply 90, and the second electrode 93 passes through the discharge electrode 94 of the spike. A discharge is made to the first electrode 92 to generate plasma in the space of the housing 91 . The gas flow containing organic gas flows along the direction shown by C in the figure. In the plasma, the organic gas is partially decomposed to produce CO 2 , H 2 O, CO, and its intermediate product C x H y O z . This structure not only The degradation rate is low, and the energy utilization rate is low, and the most important thing is to produce considerable CO, which brings more serious pollution.

发明内容Contents of the invention

本实用新型所要解决的技术问题是提高气体等离子催化器的能量利用效率。  The technical problem to be solved by the utility model is to improve the energy utilization efficiency of the gas plasma catalytic converter. the

本实用新型所要解决的另一个技术问题是减少CO产生量。  Another technical problem to be solved by the utility model is to reduce the amount of CO produced. the

为了解决上述技术问题,本发明提供有一种有机气体等离子催化器,其包括一个外壳,外壳中并联或串联多个电场,电场由作为负电极的外壳和正电极组成,正、负电极上均涂覆高介电常数材料层并各自电连接至一个高压脉冲电源的正、负极,在电场中放置由数个多孔陶瓷制成的电场催化剂蜂窝载体,催化剂蜂窝载体内分别填充第一催化剂、第二催化剂,在电场之后紧邻电场串联一段非电场催化剂蜂窝载体,填充第三催化剂。  In order to solve the above-mentioned technical problems, the present invention provides an organic gas plasma catalytic converter, which includes a casing, in which a plurality of electric fields are connected in parallel or in series, and the electric field is composed of a casing as a negative electrode and a positive electrode, and the positive and negative electrodes are coated with The high dielectric constant material layer is electrically connected to the positive and negative poles of a high-voltage pulse power supply, and an electric field catalyst honeycomb carrier made of several porous ceramics is placed in the electric field, and the catalyst honeycomb carrier is filled with the first catalyst and the second catalyst respectively. , a section of non-electric field catalyst honeycomb carrier is connected in series next to the electric field, and filled with the third catalyst. the

本实用新型所带来的有益效果是由于采用高压脉冲电源而不是直流高压电源,绝大部分的电能都是用来产生高能电子而不是用来加热气体,所以催化效率和能量利用率大为提高。另外,电场之后的第三催化剂能够将CO彻底氧化成CO2,所以等离子催化器的CO产生量可以得到大幅降低。  The beneficial effect brought by the utility model is that because the high-voltage pulse power supply is used instead of the DC high-voltage power supply, most of the electric energy is used to generate high-energy electrons instead of heating gas, so the catalytic efficiency and energy utilization rate are greatly improved. . In addition, the third catalyst behind the electric field can completely oxidize CO into CO 2 , so the amount of CO produced by the plasma catalyst can be greatly reduced.

附图说明Description of drawings

图1是目前等离子反应器的结构示意图。  Figure 1 is a schematic diagram of the structure of the current plasma reactor. the

图2是本实用新型一种催化剂能带示意图。  Fig. 2 is a schematic diagram of energy bands of a catalyst of the present invention. the

图3是本实用新型反应机理示意图。  Fig. 3 is a schematic diagram of the reaction mechanism of the utility model. the

图4是本实用新型的一个剖视示意图。  Fig. 4 is a schematic sectional view of the utility model. the

图5是本实用新型图4中A-A方向的剖视示意图。  Fig. 5 is a schematic cross-sectional view of the A-A direction in Fig. 4 of the present invention. the

具体实施方式 Detailed ways

如图4、5所示,本实用新型的有机气体等离子催化器包括一个外壳10,外壳10中并联或串联多个电场20,电场20由作为负电极的外壳10和正电极21组成,正、负电极21、10上均涂覆高介电常数材料层22,正、负电极21、10各自电连接至一个高压脉冲电源23的正、负极,从而在电场20内发生介质阻挡层放电。在电场20中放置由数个多孔陶瓷制成的电场催化剂蜂窝载体30,催化剂蜂窝载体30内分别填充负载为TiO2和Al2O3的第一催化剂31、负载为V2O5和TiO2的第二催化剂32。在电场20之后紧邻电场20串联一段非电场催化剂蜂窝载体40,填充负载为MnO2的第三催化剂41。  As shown in Figures 4 and 5, the organic gas plasma catalytic converter of the present utility model comprises a shell 10, and a plurality of electric fields 20 are connected in parallel or in series in the shell 10, and the electric field 20 is made up of shell 10 and positive electrode 21 as negative electrode, positive and negative The electrodes 21, 10 are coated with a high dielectric constant material layer 22, and the positive and negative electrodes 21, 10 are electrically connected to the positive and negative electrodes of a high-voltage pulse power supply 23, so that dielectric barrier discharge occurs in the electric field 20. The electric field catalyst honeycomb carrier 30 made of several porous ceramics is placed in the electric field 20, and the catalyst honeycomb carrier 30 is filled with the first catalyst 31 loaded with TiO 2 and Al 2 O 3 and loaded with V 2 O 5 and TiO 2 The second catalyst 32. Immediately after the electric field 20, a section of non-electric field catalyst honeycomb carrier 40 is connected in series, filled with a third catalyst 41 loaded with MnO 2 .

等离子净化污染物的机理是,尖刺脉冲通过无声放电(高介电常数材料阻挡放电)激发出大量高能电子、丰富的紫外线、少量射线,处于这种环境中的物质原子与高能电子发生非弹性碰撞,引起气体原子外层电子振荡,脱离原子束缚,这个过程会导致化学键断裂,生成活性很高的激发态离子。同时,高能电子和射线的能量被空气分子吸收,会产生强氧化剂O3,活性很高的HO2,OH自由基和准分子O。所有这些激发态离子、强氧化剂、自由基和准分子自身的能量大于有机物的分子键能,从而打开了有机物的化学键发生化学反应。高能电子激发活性物质的化学式:H2O+e-→H*+HO*+e-  H*+O3→OH*+O2 HO*+O3→HO2*+O2HO2*+O3→HO*+2O2。  The mechanism of plasma purification of pollutants is that the spike pulse excites a large number of high-energy electrons, abundant ultraviolet rays, and a small amount of rays through silent discharge (high dielectric constant material blocking discharge), and the material atoms in this environment are inelastic to high-energy electrons. The collision causes the electrons in the outer layer of the gas atoms to oscillate and escape from the bondage of the atoms. This process will cause the chemical bonds to break and generate highly active excited state ions. At the same time, the energy of high-energy electrons and rays is absorbed by air molecules, which will produce strong oxidant O 3 , highly active HO 2 , OH free radicals and excimer O. The energy of all these excited state ions, strong oxidants, free radicals and excimers is greater than the molecular bond energy of organic matter, thus opening the chemical bonds of organic matter to undergo chemical reactions. The chemical formula of high-energy electron-excited active substances: H 2 O+e - →H*+HO*+e - H*+O 3 →OH*+O 2 HO*+O 3 →HO 2 *+O 2 HO 2 *+ O 3 →HO*+2O 2 .

催化剂蜂窝载体选用具有优良吸附性能和高介电常数的多孔陶瓷体,对于有机物有优先的吸附性,因而能够将有机物在其体内富集,待有机物完全降解后再将降解产物脱附;多孔陶瓷体还能富集短寿命的活性物质如自由基、准分子,这样就意味着有机物和活性物质被富集在特定区域从而增加了有机物降解的机率;高介电常数的多孔陶瓷体在电子和射线轰击下多孔表面被激发成活性中心,利于有机物的降解。  The catalyst honeycomb carrier is a porous ceramic body with excellent adsorption performance and high dielectric constant, which has preferential adsorption for organic matter, so it can enrich organic matter in its body, and desorb the degradation products after the organic matter is completely degraded; porous ceramics The body can also enrich short-lived active substances such as free radicals and excimers, which means that organic matter and active substances are enriched in specific areas, thereby increasing the probability of organic matter degradation; porous ceramic bodies with high dielectric constant are in the electronic and Under the radiation bombardment, the porous surface is excited into active centers, which is beneficial to the degradation of organic matter. the

AL2O3和V2O5作为常规催化剂,可以显著提升有机物降解的速度,并且使反应向希望的氧化还原方向进行。MnO2的作用是加速O3→O2+O*,并且利用O*降解有机物。TiO2是一种N型半导体,用作催化剂的TiO2粒子的能带是不连续的,其能带结构由一个充满电子的低能价带(VB)和一个空的高能导带(CB)构成,电子在价带和导带中是非定域化的,可以自由移动。在理想TiO2半导体中,价带顶和导带底之间带隙不存在电子状态,这种带隙称为禁带,禁带宽度用Eg表示。  AL 2 O 3 and V 2 O 5 as conventional catalysts can significantly increase the degradation rate of organic matter and make the reaction proceed in the desired redox direction. The role of MnO 2 is to accelerate O 3 →O 2 +O*, and use O* to degrade organic matter. TiO2 is an N-type semiconductor. The energy band of TiO2 particles used as a catalyst is discontinuous, and its energy band structure consists of a low-energy valence band (VB) full of electrons and an empty high-energy conduction band (CB). , electrons are delocalized in the valence and conduction bands and can move freely. In an ideal TiO2 semiconductor, there is no electronic state in the band gap between the top of the valence band and the bottom of the conduction band. This band gap is called the forbidden band, and the forbidden band width is represented by Eg.

实际的TiO2半导体由于其中不可避免地存在杂质和各种陷阱,使电子和空穴 束缚在其周围,成为捕获电子和空穴的陷阱,产生局域化电子态,在禁带中引入相应电子态能级。如图2所示,以粒子晶体中点缺陷为例,在正电中心,负离子空位和间隙中的正离子都是正电中心,正电中心束缚一个电子,这个被束缚的电子很容易挣脱而成为导带中的自由电子。如图3所示,纳米尺寸的TiO2吸收能量大于等于Eg的光子和高能电子能量,将发生电子由价带向导带的跃迁,从而在价带生成空穴h+,在导带生成电子e-,在反应器电场的驱动下,电子和空穴迁移到粒子表面的不同位置,它们能在电场作用或通过扩散与吸附在催化剂粒子表面上的物质发生氧化还原反应,或者直接复合。如图3所示,TiO2等离子催化反应主要步骤中,①TiO2受高能电子和紫外线激发后产生电子-空穴对;②电子-空穴对之间发生复合反应,并以热能或光能的形式释放能量;③由价带空穴诱发的氧化反应;④有导带电子诱发的还原反应;⑤发生进一步催化反应;⑥捕获导带电子生成Ti3+;⑦捕获价带空穴生成Titanol基团。反应④形成的超氧自由基具有很强的氧化能力,对整个有机物的降解起了决速的作用。在没有电场的情况下,反应②的发生概率是主要的,但是由于TiO2催化剂被置于高压脉冲电场中之后,能迫使激发的电子向电场正电极移动,从而显著削弱反应②,使得所需要的反应③④⑤得到明显增强。  Due to the inevitable existence of impurities and various traps in the actual TiO2 semiconductor, electrons and holes are bound around it, becoming traps for capturing electrons and holes, resulting in localized electronic states, and introducing corresponding electrons in the forbidden band state energy level. As shown in Figure 2, taking the point defect in the particle crystal as an example, in the positive center, the negative ion vacancies and the positive ions in the gap are all positive centers. The positive center binds an electron, and the bound electron is easy to break free and become Free electrons in the conduction band. As shown in Figure 3, nanometer-sized TiO2 absorbs photons and high-energy electrons with energy greater than or equal to Eg, and electrons will transition from the valence band to the conduction band, thereby generating holes h+ in the valence band and electrons e- in the conduction band. , driven by the electric field of the reactor, the electrons and holes migrate to different positions on the surface of the particle, and they can undergo redox reactions with the substances adsorbed on the surface of the catalyst particle under the action of the electric field or through diffusion, or directly recombine. As shown in Figure 3, in the main steps of the TiO 2 plasma catalytic reaction, ① TiO 2 is excited by high-energy electrons and ultraviolet rays to generate electron-hole pairs; ③Oxidation reaction induced by valence band holes; ④Reduction reaction induced by conduction band electrons; ⑤Further catalytic reaction occurs; group. The superoxide free radical formed in reaction ④ has a strong oxidizing ability and plays a speed-determining role in the degradation of the entire organic matter. In the absence of an electric field, the occurrence probability of reaction ② is the main one, but after the TiO 2 catalyst is placed in a high-voltage pulsed electric field, it can force the excited electrons to move to the positive electrode of the electric field, thereby significantly weakening the reaction ②, making the required The responses of ③④⑤ were significantly enhanced.

如本技术领域的人所知,本实用新型的附图和实施例仅为说明本实用新型的功能、结构和原理而不应当成为对发明创造理解上的限制;同时,本实用新型的目的均已经实现。上述实施例可能在不脱离本实用新型原理的情况下有所变更,故此,本实用新型的保护应以权利要求书中所描述的范围为准。  As known to those skilled in the art, the accompanying drawings and embodiments of the present utility model only illustrate the function, structure and principle of the present utility model and should not be limitations on the understanding of the invention; meanwhile, the purpose of the utility model is has been achieved. The above embodiments may be changed without departing from the principle of the utility model, therefore, the protection of the utility model shall be based on the scope described in the claims. the

Claims (1)

1. organic gas plasma catalytic device; It is characterized in that comprising a shell (10); The parallel connection or a plurality of electric fields (20) of connecting in the shell (10); Electric field (20) is made up of shell (10) and positive electrode (21) as negative electrode; All apply high dielectric constant material layer (22) on the positive and negative electrode (21,10) and be electrically connected to the positive and negative electrode of a high-voltage pulse power source (23) separately, the electric field catalysis agent honeycomb substrate (30) that placement is processed by several porous ceramics in electric field (20) is filled first catalyst (31), second catalyst (32) respectively in the catalyst monolith carrier (30); Be close to electric field series connection one section non-electric field catalyst monolith carrier (40) afterwards at electric field (20), fill the 3rd catalyst (41).
CN201120151093XU 2011-05-12 2011-05-12 Organic gas plasma catalytic converter Expired - Fee Related CN202237791U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201120151093XU CN202237791U (en) 2011-05-12 2011-05-12 Organic gas plasma catalytic converter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201120151093XU CN202237791U (en) 2011-05-12 2011-05-12 Organic gas plasma catalytic converter

Publications (1)

Publication Number Publication Date
CN202237791U true CN202237791U (en) 2012-05-30

Family

ID=46099096

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201120151093XU Expired - Fee Related CN202237791U (en) 2011-05-12 2011-05-12 Organic gas plasma catalytic converter

Country Status (1)

Country Link
CN (1) CN202237791U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102773007A (en) * 2011-05-12 2012-11-14 魏飞 Organic gas plasma catalyzing device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102773007A (en) * 2011-05-12 2012-11-14 魏飞 Organic gas plasma catalyzing device

Similar Documents

Publication Publication Date Title
US8791354B2 (en) Photoelectrochemical cell
CN104069722B (en) A kind of Trinity industrial source peculiar smell emission-control equipment and method
CN101785971A (en) Photoelectrocatalysis device used for degrading gaseous-phase organic pollutant
CN102695353B (en) High voltage is utilized to produce gas plasma electric discharge elementary cell and reactor
CN105521705A (en) Method for treating organic waste gas through low-temperature plasma concerted catalysis
CN104437040B (en) Removal of nitrogen oxide device based on dielectric barrier discharge reactor and removal methods thereof
CN101107062A (en) Solid carbon decomposition type ceramic chemical reaction device
CN204082267U (en) A kind of device of the vehicle maintenance service based on low temperature plasma
CN104179552A (en) Automobile tail gas treatment device and method based on low-temperature plasma
CN112156647A (en) High-voltage auxiliary photocatalytic purification module, purification device and method
CN102230410A (en) Automobile exhaust gas purification device realizing photocatalysis based on plasmas
JP4719073B2 (en) Electrochemical reactor
CN203916426U (en) A kind of Trinity industrial source peculiar smell emission-control equipment
CN205760514U (en) Low temperature spiral corona plasma VOCsemission-control equipment
CN102773007A (en) Organic gas plasma catalyzing device
CN102836639A (en) Automotive exhaust purification apparatus based on composition of titanium dioxide photocatalysis and plasma device
CN107176654A (en) A kind of utilization solar energy cooperates with the set composite of processing sewage with photoelectrocatalysis
CN202237791U (en) Organic gas plasma catalytic converter
ES2795975T3 (en) Device for treating a compound comprising a photocatalyst element activated by a plasmon generated by a buried activation element, and in particular activated with a plasma
CN108355486B (en) Low temperature plasma synergistic catalytic device
CN206823546U (en) A kind of plasma-catalytic purification gas processing unit
CN106268223A (en) A kind of method of low-temperature plasma synergistic catalyst of transition metal oxide oxidation mercury in flue gas
CN202724994U (en) Device for governing waste gas by plasma catalysis
CN103994499A (en) Plasma synergy bismuth molybdate thin film catalyzing air purification device
CN207576103U (en) A kind of compartment low-temperature plasma generator for filling ozone-decomposing agent

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20120530

Termination date: 20130512