CN202113752U - Nonequilibrium state plasma purifier - Google Patents
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- 238000000746 purification Methods 0.000 claims abstract description 16
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 14
- 238000001179 sorption measurement Methods 0.000 claims abstract description 10
- 239000000758 substrate Substances 0.000 claims abstract description 9
- 239000007787 solid Substances 0.000 claims description 9
- 229910052751 metal Inorganic materials 0.000 claims description 8
- 239000002184 metal Substances 0.000 claims description 8
- 229910000831 Steel Inorganic materials 0.000 claims description 2
- 239000010959 steel Substances 0.000 claims description 2
- 239000007789 gas Substances 0.000 abstract description 38
- 239000002912 waste gas Substances 0.000 abstract description 6
- 238000003933 environmental pollution control Methods 0.000 abstract description 2
- 239000002245 particle Substances 0.000 description 13
- 238000005516 engineering process Methods 0.000 description 10
- 239000003344 environmental pollutant Substances 0.000 description 10
- 231100000719 pollutant Toxicity 0.000 description 10
- 230000000694 effects Effects 0.000 description 7
- 239000000428 dust Substances 0.000 description 5
- 239000012855 volatile organic compound Substances 0.000 description 5
- 241000282414 Homo sapiens Species 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- 230000001590 oxidative effect Effects 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 230000004888 barrier function Effects 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
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- 238000007667 floating Methods 0.000 description 2
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- 230000007246 mechanism Effects 0.000 description 2
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- 230000003068 static effect Effects 0.000 description 2
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical class [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000000443 aerosol Substances 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- JRPBQTZRNDNNOP-UHFFFAOYSA-N barium titanate Chemical class [Ba+2].[Ba+2].[O-][Ti]([O-])([O-])[O-] JRPBQTZRNDNNOP-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
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- 230000003197 catalytic effect Effects 0.000 description 1
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- 238000005260 corrosion Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000005281 excited state Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 238000009832 plasma treatment Methods 0.000 description 1
- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical class S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 description 1
- 229910052815 sulfur oxide Inorganic materials 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
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- 239000002699 waste material Substances 0.000 description 1
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Abstract
一种非平衡态等离子体净化器属于环境污染治理技术领域。包括电源、非平衡态等离子体反应器和尾气活性炭吸附净化器;在密闭非平衡态等离子体反应器内安装放电电极、接地电极,通过高压电线将电源与放电电极相连,接地电极通过接地线接地;放电电极垂直于接地电极,基盘平行接地电极布设于非平衡态等离子体反应器内;基盘面向接地电极一侧表面安装有放电电极,放电电极与基盘垂直;在反应器内靠近接地电极的一侧设有两个进气口,两个进气口上下对称分布;在反应器内靠近基盘的一侧上下对称布设两个出气口;两个出气口同时连接在尾气活性炭吸附净化器上。这种反应器形式很大程度上提高了废气的处理效率,而且结构简单,适用性强,运行费用低。
A non-equilibrium plasma purifier belongs to the technical field of environmental pollution control. Including power supply, non-equilibrium plasma reactor and exhaust activated carbon adsorption purifier; discharge electrode and ground electrode are installed in the closed non-equilibrium plasma reactor, and the power supply and discharge electrode are connected through high-voltage wires, and the ground electrode is grounded through the ground wire The discharge electrode is perpendicular to the ground electrode, and the substrate is arranged parallel to the ground electrode in the non-equilibrium plasma reactor; the discharge electrode is installed on the surface of the substrate facing the ground electrode, and the discharge electrode is perpendicular to the substrate; it is close to the ground in the reactor There are two gas inlets on one side of the electrode, and the two gas inlets are distributed symmetrically up and down; two gas outlets are arranged symmetrically up and down on the side close to the base plate in the reactor; the two gas outlets are connected to the activated carbon adsorption and purification of exhaust gas at the same time. device. This type of reactor greatly improves the treatment efficiency of waste gas, and has simple structure, strong applicability and low operating cost.
Description
技术领域 technical field
本实用新型是一种针对大气治理领域的污染物净化处理装置,尤其是一种逆流式非平衡等离子体反应装置,属于环境污染治理技术领域。The utility model relates to a pollutant purification treatment device aimed at the field of atmospheric control, in particular to a countercurrent non-equilibrium plasma reaction device, which belongs to the technical field of environmental pollution control.
背景技术 Background technique
随着人类生产活动和生活活动的不断扩大,排放到环境中的废气污染物成分既复杂,而且有毒有害物日益增加。不仅给生态环境造成了严重的破坏,也给人类自身带来不可估量的危害。传统的废物处理技术已不能适应需要,而非平衡等离子体技术由于其具有开发费用低、处理彻底、无二次污染等优点,正受到研究领域的广泛关注。With the continuous expansion of human production activities and living activities, the components of exhaust pollutants discharged into the environment are complex, and the number of toxic and harmful substances is increasing. Not only has it caused serious damage to the ecological environment, but it has also brought immeasurable harm to human beings. The traditional waste treatment technology can no longer meet the needs, and the non-equilibrium plasma technology is attracting extensive attention in the research field because of its advantages of low development cost, thorough treatment, and no secondary pollution.
废气中的主要成分有:总悬浮颗粒、飘尘、硫氧化物、氮氧化物、硫化氢、氨、碳氧化物和有机蒸气(VOCs)等。它们分别来自于生活污染源、工业污染源和交通污染源。通常的处理技术有:机械过滤、液体吸附、固体吸附、静电吸附、催化转化等。这些技术对废气的治理起着重要的作用。但随着废气成分的复杂化、浓度增大,这些技术的效率低、一次污染、腐蚀设备、工艺复杂、投资大、运行费用高等缺陷逐渐显露出来。日前最具活力的废气处理技术当数非平衡态等离子体技术。80年代末Masnda S.首次提出的脉冲放电脱硫脱硝技术,属于这一技术范畴。The main components in the exhaust gas are: total suspended particles, floating dust, sulfur oxides, nitrogen oxides, hydrogen sulfide, ammonia, carbon oxides and organic vapors (VOCs). They come from domestic pollution sources, industrial pollution sources and traffic pollution sources respectively. Common treatment technologies include: mechanical filtration, liquid adsorption, solid adsorption, electrostatic adsorption, catalytic conversion, etc. These technologies play an important role in the treatment of exhaust gas. However, with the complexity and concentration of exhaust gas components, the defects of these technologies, such as low efficiency, primary pollution, corrosion of equipment, complex process, large investment and high operating cost, are gradually revealed. The most dynamic exhaust gas treatment technology is the non-equilibrium plasma technology. The pulse discharge desulfurization and denitrification technology first proposed by Masnda S. in the late 1980s belongs to this technical category.
工业废气中悬浮颗粒和飘尘以气态和气溶胶态长期悬浮在空气中,对大气环境造成了严重的污染,其中粒径在0.1~5um之间的颗粒对人体危去最大。非平衡态等离子体技术可以有效地清除废气中的这些颗粒物。其处理机理是:通过非均匀放电(如电晕放电)产生的非平衡态等离子体,其中的电子和离子在梯度场的作用下和废气中的颗粒物相互碰撞并附着在这些粒子上,使之成为荷电粒子,进而被集尘极所收集。Suspended particles and floating dust in industrial waste gas are suspended in the air for a long time in gaseous state and aerosol state, causing serious pollution to the atmospheric environment. Among them, particles with a particle size between 0.1 and 5um are the most dangerous to the human body. Non-equilibrium plasma technology can effectively remove these particles in the exhaust gas. The treatment mechanism is: non-equilibrium plasma generated by non-uniform discharge (such as corona discharge), in which electrons and ions collide with particles in the exhaust gas under the action of gradient field and attach to these particles, making them Become charged particles, and then be collected by the dust collector.
对废气中的其它气态污染物的等离子体处理机理为:通过气体放电产生的等离子体中含有大量高能电子、离子、激发态粒子和具有很强氧化性的自由基,其中活性粒子的平均能量高于气体分子的键能。这些活性粒子和有害分子碰撞的结果是,一方面打开气体分子键生成一些单原子分子和固体微粒;另一方而产生大量·OH、·HO2、·O等自由基和氧化性极强的O3。由这些单原子分子、自由基和O3等组成的活性粒子所引起的化学反应,最终将废气中的有害物质变成无害物质。The plasma treatment mechanism for other gaseous pollutants in the exhaust gas is as follows: the plasma generated by gas discharge contains a large number of high-energy electrons, ions, excited state particles and free radicals with strong oxidative properties, and the average energy of active particles is high. The bond energy of gas molecules. As a result of the collision between these active particles and harmful molecules , on the one hand, the bonds of gas molecules are opened to generate some monatomic molecules and solid particles; 3 . The chemical reaction caused by the active particles composed of these single-atom molecules, free radicals and O3, etc., finally changes the harmful substances in the exhaust gas into harmless substances.
实用新型内容 Utility model content
本实用新型的目的在于提供一种新型的、有效的、低能耗的逆流针板式非平衡态等离子体净化装置。The purpose of the utility model is to provide a novel, effective and low energy consumption countercurrent needle plate type non-equilibrium plasma purification device.
本实用新型提供的废气处理装置,是将电晕放电和介质阻挡放电相结合产生非平衡态等离子体技术,反应器为类针-板式结构,采用污染物气流与非平衡态等离子体通道逆流接触的形式来降解废气。该装置具有结构简单,占地面积小,适用面广,处理效果好等优点。The waste gas treatment device provided by the utility model combines corona discharge and dielectric barrier discharge to generate non-equilibrium plasma technology. The reactor is a pin-plate structure, and the pollutant gas flow is used to contact the non-equilibrium plasma channel countercurrently. form to degrade exhaust gas. The device has the advantages of simple structure, small footprint, wide application range and good treatment effect.
本实用新型的一种非平衡态等离子体净化装置,其特征在于:一种非平衡态等离子体净化装置,其特征在于:包括电源5、非平衡态等离子体反应器6和尾气活性炭吸附净化器10;在非平衡态等离子体反应器6内安装放电电极1、接地电极2,通过高压电线8将电源5与放电电极1相连,接地电极2通过接地线9接地;放电电极1垂直于接地电极2,放电电极1为曲率半径<10mm的实心或空心针尖、实心或空心金属棒或金属管;基盘7为表面光滑的金属平板,基盘7和接地电极2均采用3~5mm厚钢板制作,孔径为40~60mm,开孔率为50%~65%;基盘7平行接地电极2布设于非平衡态等离子体反应器6内;基盘7面向接地电极2一侧表面安装有放电电极1,放电电极1与基盘7垂直;放电电极1与接地电极2之间的间距为1cm~12cm;在非平衡态等离子体反应器6内靠近接地电极2的一侧设有两个进气口3,两个进气口3上下对称分布,非平衡态等离子体反应器6整体结构密闭;在非平衡态等离子体反应器6内靠近基盘7的一侧上下对称布设两个出气口4;两个出气口4同时连接在尾气活性炭吸附净化器10上。A non-equilibrium plasma purification device of the present utility model is characterized in that: a non-equilibrium plasma purification device is characterized in that it includes a power supply 5, a non-equilibrium plasma reactor 6 and an exhaust activated carbon adsorption purifier 10. Install the
本实用新型所提供的一种非平衡态等离子体净化装置与现有的非平衡态等离子体净化装置相比明显的不同是:The obvious difference between the non-equilibrium plasma purification device provided by the utility model and the existing non-equilibrium plasma purification device is:
在放电电极1和接地电极2之间形成了非平衡态等离子体通道,进入反应器6的污染气体与非平衡态等离子体通道逆向接触,提高了等离子体通道中高能电子、强氧化性自由基及准中性分子的碰撞几率及碰撞速率,从而提高了等离子的利用率;非平衡态等离子体反应器6整体结构密封操作,利用了静压箱的原理,净化器内部压力均衡,有利于气态污染物气流及浓度稳定;采用了尾气净化器,来达到污染物废气彻底的无害化排放;同时,这种装置将电晕放电和介质阻挡放电相结合,在放电期间避免了电弧的产生,利于生成等离子体活性基团。A non-equilibrium plasma channel is formed between the
总之,这种反应器形式很大程度上提高了废气的处理效率,而且结构简单,适用性强,运行费用低。In short, this type of reactor greatly improves the efficiency of waste gas treatment, and has a simple structure, strong applicability, and low operating costs.
采用该净化装置净化VOCs气体,发现较一般的针-板式反应器对气态VOCs污染物净化效果提高了15%以上,除尘效果提高到99.99%以上。Using the purification device to purify VOCs gas, it is found that the purification effect of gaseous VOCs pollutants is increased by more than 15% compared with the general pin-plate reactor, and the dust removal effect is increased to more than 99.99%.
附图说明 Description of drawings
图1是本实用新型的工艺流程示意图。Fig. 1 is the technological process schematic diagram of the present utility model.
图2是本实用新型的针-板式电极结构示意图。Fig. 2 is a schematic diagram of the structure of the needle-plate electrode of the present invention.
图3是本实用新型的针管-板式电极结构示意图。Fig. 3 is a schematic diagram of the structure of the needle tube-plate electrode of the present invention.
图中,1.放电电极,2.接地电极;3.进气口,4.出气口,5.电源,6.非平衡态等离子体反应器,7.基盘,8.高压电线,9.接地电线,10.尾气净化器。In the figure, 1. Discharge electrode, 2. Ground electrode; 3. Air inlet, 4. Gas outlet, 5. Power supply, 6. Non-equilibrium plasma reactor, 7. Base plate, 8. High voltage wire, 9. Ground wire, 10. Exhaust gas purifier.
具体实施方式 Detailed ways
非平衡态等离子体反应器6整体结构密封操作,利用了静压箱的原理,净化器内部压力均衡,有利于气态污染物气流及浓度稳定;放电电极1、接地电极2为针板式,放电电极1垂直于接地电极2,针型放电电极1为曲率半径<10mm的实心或空心针尖、实心或空心金属棒或金属管,针型放电电极1安置于基盘7上;基盘7为表面光滑的金属平板,当放电电极1实心时,进入的废气与非平衡等离子体作用后,从基盘7上均匀分布孔排向净化装置6出气口4,最后由出气口4排出;当放电电极1空心时,基盘7上无孔,净化废气由放电电极1排出;针型放电电极1与板型接地电极2之间的间距为6cm;接地电极2接地,接地电阻≤4Ω。The overall structure of the non-equilibrium plasma reactor 6 is sealed and operated, using the principle of the static pressure box, and the internal pressure of the purifier is balanced, which is conducive to the stability of the gas flow and concentration of gaseous pollutants; the
电源5输出高压,施加在放电极1和接地电极2之间,调整放电电极1与接地电极2之间距离、电源5输出电压峰值,使放电电极1与接地电极2之间电场强度达到8kV/cm时,在电极1、电极2之间形成非平衡态等离子体通道,在通道中存在大量的高能电子、强氧化性基团及准中性分子;预处理的气态污染物由进气口3进入净化装置6,与等离子通道逆向接触,充分反应后,由净化装置6出气口4排放;排放气体在经过附加的尾气净化器10后排入大气。The power supply 5 outputs high voltage, which is applied between the
在电极表面附着一定量的催化剂。催化剂以改性钛酸钡Ba0.8Sr0.2Zr0.1Ti0.9O3为载体,载体表面负载MnO2/γ-Al2O3等金属氧化物作为活性组分。A certain amount of catalyst is attached to the surface of the electrode. The catalyst uses modified barium titanate Ba 0.8 Sr 0.2 Zr 0.1 Ti 0.9 O 3 as the carrier, and metal oxides such as MnO 2 /γ-Al 2 O 3 are loaded on the surface of the carrier as active components.
污染物废气经过等离子体净化后,再通过附加的尾气净化器10,达到彻底净化的目的。尾气净化器10采用活性炭吸附装置。After the pollutant exhaust gas is purified by plasma, it passes through the additional exhaust gas purifier 10 to achieve the purpose of thorough purification. The tail gas purifier 10 adopts an activated carbon adsorption device.
采用该净化装置净化VOCs气体,发现较一般的针-板式反应器对气态VOCs污染物净化效果提高了15%以上,除尘效果提高到99.99%以上。Using the purification device to purify VOCs gas, it is found that the purification effect of gaseous VOCs pollutants is increased by more than 15% compared with the general pin-plate reactor, and the dust removal effect is increased to more than 99.99%.
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
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CN108541124A (en) * | 2018-04-27 | 2018-09-14 | 浙江大维高新技术股份有限公司 | A kind of honeycomb low temperature plasma generating means and its application method |
CN109173591A (en) * | 2018-10-11 | 2019-01-11 | 中国矿业大学(北京) | A kind of recirculating fluidized bed VOCs adsorption and regeneration device and its operation method |
CN116963847A (en) * | 2021-12-30 | 2023-10-27 | 米凯·亚历山大维奇·米山尼诺夫 | Reactor of waste treatment device |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108541124A (en) * | 2018-04-27 | 2018-09-14 | 浙江大维高新技术股份有限公司 | A kind of honeycomb low temperature plasma generating means and its application method |
CN109173591A (en) * | 2018-10-11 | 2019-01-11 | 中国矿业大学(北京) | A kind of recirculating fluidized bed VOCs adsorption and regeneration device and its operation method |
CN116963847A (en) * | 2021-12-30 | 2023-10-27 | 米凯·亚历山大维奇·米山尼诺夫 | Reactor of waste treatment device |
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