CN203874903U - Wet-type electric filtration device with high gas speed and high efficiency for deeply treating PM2.5 - Google Patents
Wet-type electric filtration device with high gas speed and high efficiency for deeply treating PM2.5 Download PDFInfo
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- CN203874903U CN203874903U CN201420093328.8U CN201420093328U CN203874903U CN 203874903 U CN203874903 U CN 203874903U CN 201420093328 U CN201420093328 U CN 201420093328U CN 203874903 U CN203874903 U CN 203874903U
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- 238000001914 filtration Methods 0.000 title claims abstract description 7
- 239000007789 gas Substances 0.000 claims abstract description 42
- 238000009826 distribution Methods 0.000 claims abstract description 15
- 239000002131 composite material Substances 0.000 claims abstract description 14
- 238000000926 separation method Methods 0.000 claims abstract description 11
- 239000002912 waste gas Substances 0.000 claims abstract description 8
- 239000010865 sewage Substances 0.000 claims description 5
- 239000007921 spray Substances 0.000 claims description 2
- 239000000428 dust Substances 0.000 abstract description 21
- 239000000443 aerosol Substances 0.000 abstract description 5
- 230000000694 effects Effects 0.000 abstract description 5
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 abstract description 2
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- 239000003344 environmental pollutant Substances 0.000 description 5
- 239000010419 fine particle Substances 0.000 description 5
- 239000003546 flue gas Substances 0.000 description 5
- 238000009413 insulation Methods 0.000 description 5
- 231100000719 pollutant Toxicity 0.000 description 5
- 239000002253 acid Substances 0.000 description 4
- 230000009286 beneficial effect Effects 0.000 description 3
- 150000002500 ions Chemical class 0.000 description 3
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- 238000006477 desulfuration reaction Methods 0.000 description 2
- 230000023556 desulfurization Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 229910001385 heavy metal Inorganic materials 0.000 description 2
- 238000000034 method Methods 0.000 description 2
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- 239000012717 electrostatic precipitator Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 239000003574 free electron Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
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- 238000005272 metallurgy Methods 0.000 description 1
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- 239000004753 textile Substances 0.000 description 1
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Abstract
Description
技术领域 technical field
本实用新型涉及电除尘设备技术领域,尤其是一种PM2.5深度治理高气速高效湿式电滤装备。 The utility model relates to the technical field of electric dust removal equipment, in particular to high-gas-velocity and high-efficiency wet electric filter equipment for PM2.5 deep treatment. the
背景技术 Background technique
“中国目前是世界PM2.5污染最严重的地区之一”,历史上空气污染最严重的伦敦的PM2.5指标约在10至20微克/立方米,而北京在高峰期达到了90微克/立方米左右,广州等城市也达到了50微克/立方米左右。PM2.5细颗粒,是病毒、细菌、有害物质的携带体,人体生理结构决定了对PM2.5没有任何过滤、阻拦能力。石油、化工、电力、冶金、水泥、纺织、生物、医药等行业脱硫脱硝后湿烟气中含有大量的细微粉尘、气溶胶、酸雾、重金属等细颗粒污染物(PM2.5),为防治雾霾,需要一种除尘效果好的环保技术装备。 "China is currently one of the areas with the most serious PM2.5 pollution in the world." The PM2.5 index of London, which has the worst air pollution in history, is about 10 to 20 micrograms per cubic meter, while Beijing reached 90 micrograms per cubic meter at its peak. About 50 micrograms per cubic meter in Guangzhou and other cities. PM2.5 fine particles are carriers of viruses, bacteria, and harmful substances. The physiological structure of the human body determines that there is no ability to filter or block PM2.5. After desulfurization and denitrification in petroleum, chemical, electric power, metallurgy, cement, textile, biology, medicine and other industries, the wet flue gas contains a large amount of fine dust, aerosol, acid mist, heavy metal and other fine particle pollutants (PM2.5). Smog requires a kind of environmental protection technology and equipment with good dust removal effect. the
国内目前捕捉燃烧源颗粒物的除尘设备主要有:机械除尘器、布袋除尘器、电除尘器、电袋复合除尘器等。但这些设备只能去除的最小粒径为40-50μm的污染物,粒径小于40μm的液滴以及微细粉尘、气溶胶粒子等无法去除。也就是对PM2.5的细颗粒物没有效果或效果不佳。 At present, the domestic dust removal equipment for capturing combustion source particles mainly includes: mechanical dust collector, bag dust collector, electrostatic precipitator, electric bag composite dust collector, etc. However, these devices can only remove pollutants with a minimum particle size of 40-50 μm, and liquid droplets with a particle size of less than 40 μm, fine dust, and aerosol particles cannot be removed. That is, it has no effect or poor effect on PM2.5 fine particles. the
实用新型内容 Utility model content
本实用新型要解决的技术问题是:克服现有技术中难以去除细颗粒污染物且现有技术中的绝缘箱有热烟气及细微粉尘、雾滴进入,绝缘箱的可靠性受到影响,产生“污闪”现象的技术问题,提供一种PM2.5深度治理高气速高效湿式电滤装备,有效、高效去除细颗粒污染物。 The technical problem to be solved by the utility model is: to overcome the difficulty in removing fine particle pollutants in the prior art and the insulation box in the prior art has hot smoke, fine dust, and mist entering, and the reliability of the insulation box is affected, resulting in The technical problem of the "pollution flashover" phenomenon provides a PM2.5 deep treatment high-speed and high-efficiency wet electric filtration equipment, which can effectively and efficiently remove fine particle pollutants. the
本实用新型解决其技术问题所采用的技术方案是:一种PM2.5深度治理高 气速高效湿式电滤装备,包括主壳体和设置于主壳体内的电极分离装置,所述的主壳体的下部设有下气室、上部设有上气室,所述的下气室上开设有废气进口和排污口,下气室与主壳体的连接处设有气体分布装置,所述的上气室的顶部具有排气口;所述的电极分离装置包括阴极装置、阳极装置和供电装置;所述的阳极装置为蜂窝式导电复合材料管束;所述的阴极装置包括位于上气室内的阴极连接板和悬挂于阴极连接板上的若干阴极导线,所述的阴极导线一一对应穿设于蜂窝式导电复合材料管束中,每个阴极导线的下端连接一个重锤;所述的供电装置包括位于上气室顶部的绝缘箱,所述的绝缘箱内设有电能引入装置,所述的电能引入装置与阴极连接板通过导线连接。所述的绝缘箱上设有向绝缘箱内部鼓入热风的正压保护装置。阻止热烟气及细微粉尘、雾滴进入,保证箱体绝缘性更可靠,有效避免“污闪”现象的发生。 The technical solution adopted by the utility model to solve the technical problems is: a kind of PM2.5 deep control high gas velocity high-efficiency wet electric filter equipment, including the main casing and the electrode separation device arranged in the main casing, the main casing The lower part of the body is provided with a lower air chamber, and the upper part is provided with an upper air chamber. The lower air chamber is provided with a waste gas inlet and a sewage outlet. The connection between the lower air chamber and the main shell is provided with a gas distribution device. The top of the upper air chamber has an exhaust port; the electrode separation device includes a cathode device, an anode device and a power supply device; the anode device is a honeycomb conductive composite tube bundle; the cathode device includes a a cathode connection plate and a plurality of cathode wires suspended on the cathode connection plate, the cathode wires are arranged in the honeycomb conductive composite tube bundle one by one, and a weight is connected to the lower end of each cathode wire; the power supply device It includes an insulating box located on the top of the upper air chamber, and an electric energy introduction device is arranged inside the insulating box, and the electric energy introduction device is connected with the cathode connection plate through wires. The insulating box is provided with a positive pressure protection device that blows hot air into the insulating box. Prevent hot smoke, fine dust, and mist from entering, ensure more reliable insulation of the cabinet, and effectively avoid the occurrence of "pollution flashover". the
进一步的,所述的上气室中还设有用于提高主壳体内导电性的喷雾装置。有利于增加烟气流中的湿气和增强导电性,加速电晕区粉尘颗粒向阳极的迁移速度。 Further, the upper air chamber is also provided with a spraying device for improving the electrical conductivity in the main casing. It is beneficial to increase the moisture in the flue gas flow and enhance the conductivity, and accelerate the migration speed of dust particles in the corona area to the anode. the
进一步的,为使气体更均匀的穿过电极分离装置,所述的气体分布装置包括气体导流板和气体分布板,所述的气体分布板位于气体导流板的上部。 Further, in order to make the gas pass through the electrode separation device more uniformly, the gas distribution device includes a gas guide plate and a gas distribution plate, and the gas distribution plate is located on the upper part of the gas guide plate. the
进一步的,为防止重锤晃动,所述的重锤之间设有固定装置。避免阴极导线因高气速气流的冲洗而出现晃动导致除尘效率的降低。 Further, in order to prevent the weights from shaking, a fixing device is provided between the weights. Avoid the shaking of the cathode wire due to the flushing of the high-velocity air flow, resulting in a reduction in dust removal efficiency. the
本实用新型的有益效果是,本实用新型的PM2.5深度治理高气速高效湿式电滤装备,对微细/粘性/高电阻比PM2.5粉尘、气溶胶、细小的金属颗粒及二恶英等有非常理想的捕集效果;具有耐高温、导电性强、除雾效率高、阻燃性能好、加工制造安装周期短、结构紧凑、性能稳定、使用寿命长等优点。 The beneficial effect of the utility model is that the PM2.5 deep treatment of the utility model with high gas velocity and high-efficiency wet electric filter equipment is effective for fine/viscous/high resistance ratio PM2.5 dust, aerosol, fine metal particles and dioxin It has a very ideal collection effect; it has the advantages of high temperature resistance, strong conductivity, high defogging efficiency, good flame retardancy, short processing, manufacturing and installation cycle, compact structure, stable performance, and long service life. the
附图说明 Description of drawings
下面结合附图和实施例对本实用新型进一步说明。 Below in conjunction with accompanying drawing and embodiment the utility model is further described. the
图1是本实用新型的PM2.5深度治理高气速高效湿式电滤装备优选实施例的半剖图; Fig. 1 is a semi-sectional view of a preferred embodiment of PM2.5 deep control high-gas velocity and high-efficiency wet-type electric filtration equipment of the present utility model;
图2是蜂窝式导电复合材料管束与阴极导线的结构图。 Fig. 2 is a structural diagram of a honeycomb conductive composite material tube bundle and a cathode wire. the
图中:1.主壳体,2.下气室,21.废气进口,22.排污口,3.上气室,31.排气口,4.气体分布装置,41.气体导流板,42.气体分布板,5.电极分离装置,51.蜂窝式导电复合材料管束,52.阴极连接板,53.阴极导线,54.重锤,6.绝缘箱。 In the figure: 1. Main shell, 2. Lower air chamber, 21. Waste gas inlet, 22. Sewage outlet, 3. Upper air chamber, 31. Exhaust port, 4. Gas distribution device, 41. Gas deflector, 42. Gas distribution plate, 5. Electrode separation device, 51. Honeycomb conductive composite tube bundle, 52. Cathode connection plate, 53. Cathode wire, 54. Weight, 6. Insulation box. the
具体实施方式 Detailed ways
现在结合附图对本实用新型作进一步详细的说明。这些附图均为简化的示意图,仅以示意方式说明本实用新型的基本结构,因此其仅显示与本实用新型有关的构成。 Now in conjunction with accompanying drawing, the utility model is described in further detail. These drawings are all simplified schematic diagrams, and only schematically illustrate the basic structure of the utility model, so they only show the configurations related to the utility model. the
如图1和图2所示,本实用新型的一种PM2.5深度治理高气速高效湿式电滤装备,包括主壳体1和设置于主壳体1内的电极分离装置5,所述的主壳体1的下部设有下气室2、上部设有上气室3,所述的下气室2上开设有废气进口21和排污口22,下气室2与主壳体1的连接处设有气体分布装置4,所述的上气室3的顶部具有排气口31;所述的电极分离装置5包括阴极装置、阳极装置和供电装置;所述的阳极装置为蜂窝式导电复合材料管束51;所述的阴极装置包括位于上气室内的阴极连接板52和悬挂于阴极连接板52上的若干阴极导线53,所述的阴极导线53一一对应穿设于蜂窝式导电复合材料管束51中,每个阴极导线53的下端连接一个重锤54;所述的供电装置包括位于上气室3顶部的绝缘箱6,所述的绝缘箱6内设有电能引入装置,所述的电能引入装置与阴极连接板 52通过导线连接。所述的绝缘箱6上设有向绝缘箱内部鼓入热风的正压保护装置。阻止热烟气及细微粉尘、雾滴进入,保证箱体绝缘性更可靠,有效避免“污闪”现象的发生。 As shown in Figures 1 and 2, a high-efficiency wet-type electric filter equipment for PM2.5 deep treatment of the present utility model includes a main casing 1 and an electrode separation device 5 arranged in the main casing 1. The lower part of the main housing 1 is provided with a lower air chamber 2, and the upper part is provided with an upper air chamber 3. The lower air chamber 2 is provided with a waste gas inlet 21 and a sewage outlet 22. The lower air chamber 2 and the main housing 1 A gas distribution device 4 is provided at the connection, and the top of the upper gas chamber 3 has an exhaust port 31; the electrode separation device 5 includes a cathode device, an anode device and a power supply device; the anode device is a honeycomb conductive Composite material tube bundle 51; the cathode device includes a cathode connection plate 52 located in the upper air chamber and a number of cathode wires 53 suspended on the cathode connection plate 52, and the cathode wires 53 are arranged in the honeycomb conductive composite In the material tube bundle 51, a weight 54 is connected to the lower end of each cathode wire 53; the power supply device includes an insulating box 6 located on the top of the upper air chamber 3, and an electric energy introduction device is arranged in the insulating box 6, and the The electric energy introducing device is connected with the cathode connecting plate 52 by wire. The insulating box 6 is provided with a positive pressure protection device that blows hot air into the insulating box. Prevent hot smoke, fine dust, and mist from entering, ensure more reliable insulation of the cabinet, and effectively avoid the occurrence of "pollution flashover". the
进一步的,所述的上气室3中还设有用于提高主壳体1内导电性的喷雾装置7。有利于增加烟气流中的湿气和增强导电性,加速电晕区粉尘颗粒向阳极的迁移速度。 Further, the upper air chamber 3 is also provided with a spray device 7 for improving the electrical conductivity in the main casing 1 . It is beneficial to increase the moisture in the flue gas flow and enhance the conductivity, and accelerate the migration speed of dust particles in the corona area to the anode. the
进一步的,为使气体更均匀的穿过电极分离装置5,所述的气体分布装置4包括气体导流板41和气体分布板42,所述的气体分布板42位于气体导流板41的上部。 Further, in order to make the gas pass through the electrode separation device 5 more uniformly, the gas distribution device 4 includes a gas guide plate 41 and a gas distribution plate 42, and the gas distribution plate 42 is located on the upper part of the gas guide plate 41 . the
进一步的,为防止重锤54带动阴极导线53晃动,所述的重锤54之间设有固定装置。避免阴极导线53因高气速气流的冲洗而出现晃动导致除尘效率的降低。 Further, in order to prevent the weight 54 from driving the cathode wire 53 to shake, a fixing device is provided between the weights 54 . To prevent the cathode wire 53 from shaking due to the washing of the high-velocity air flow, resulting in a reduction in dust removal efficiency. the
以下结合具体使用介绍本实用新型,将废气从废气进口21引入下气室2;接着,废气向上流动进入蜂窝式导电复合材料管束51中;然后,将55-72千伏的高压直流电通过电能引入器引到阴线导线53上,使其产生电晕放电,维持一个足以使气体电离的电场,把阴极导线53和蜂窝式导电复合材料管束51之间的气体电离成负离子和自由电子,尘、酸雾等颗粒碰到电子而产生荷电,按照同性相斥、异性相吸的原理,荷电后尘、酸雾雾滴应向电极性相反的电极移动,正离子向电晕极移动,负离子和电子则移向蜂窝式导电复合材料管束51的内壁上,靠自重顺壁而下,落入电滤装备的下气室2内从排污口22排出,使废气得到净化;最后净化后的废气进入上气室,从排气口流出。 The utility model is introduced below in conjunction with specific use, waste gas is introduced into the lower air chamber 2 from the waste gas inlet 21; then, the waste gas flows upwards into the honeycomb conductive composite tube bundle 51; then, the high-voltage direct current of 55-72 kV is introduced through electric energy lead to the cathode wire 53 to generate corona discharge, maintain an electric field sufficient to ionize the gas, and ionize the gas between the cathode wire 53 and the honeycomb conductive composite tube bundle 51 into negative ions and free electrons, dust, acid Fog and other particles encounter electrons and generate charges. According to the principle of same-sex repulsion and opposite-sex attraction, charged dust and acid mist droplets should move to electrodes with opposite polarities, positive ions move to corona electrodes, negative ions and electrons Then move to the inner wall of the honeycomb conductive composite material tube bundle 51, fall down along the wall by its own weight, fall into the lower air chamber 2 of the electric filter equipment and discharge from the sewage outlet 22, so that the exhaust gas is purified; finally the purified exhaust gas enters the upper The air chamber, which flows from the exhaust port. the
本实用新型应用于大烟气量、高气速1.6-3.2m/s的湿法脱硫脱硝工艺,用于细微粉尘、气溶胶、酸雾、重金属等污染物(PM2.5)的综合治理,除尘效率大 于95%、烟气出口浓度小于20mg/Nm3。 The utility model is applied to the wet desulfurization and denitrification process with large flue gas volume and high gas velocity of 1.6-3.2m/s, and is used for the comprehensive treatment of fine dust, aerosol, acid mist, heavy metals and other pollutants (PM2.5). The dust removal efficiency is greater than 95%, and the flue gas outlet concentration is less than 20mg/Nm 3 .
以上述依据本实用新型的理想实施例为启示,通过上述的说明内容,相关工作人员完全可以在不偏离本项实用新型技术思想的范围内,进行多样的变更以及修改。本项实用新型的技术性范围并不局限于说明书上的内容,必须要根据权利要求范围来确定其技术性范围。 Inspired by the above ideal embodiment according to the utility model, through the above description content, relevant staff can completely make various changes and modifications within the scope of not deviating from the technical idea of the utility model. The technical scope of this utility model is not limited to the content in the description, but must be determined according to the scope of the claims. the
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103817004A (en) * | 2014-03-03 | 2014-05-28 | 江苏中兴化工设备有限公司 | High gas speed and high efficiency wet-type electrofiltration device for deep treatment of PM2.5 |
| CN107297113A (en) * | 2017-07-06 | 2017-10-27 | 常州大学 | A kind of waste gas residual heat is reclaimed and pollutant integrated conduct method and system |
| CN117643795A (en) * | 2023-11-07 | 2024-03-05 | 石家庄凤山化工有限公司 | Nitrate tail gas treatment device |
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2014
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103817004A (en) * | 2014-03-03 | 2014-05-28 | 江苏中兴化工设备有限公司 | High gas speed and high efficiency wet-type electrofiltration device for deep treatment of PM2.5 |
| CN107297113A (en) * | 2017-07-06 | 2017-10-27 | 常州大学 | A kind of waste gas residual heat is reclaimed and pollutant integrated conduct method and system |
| CN117643795A (en) * | 2023-11-07 | 2024-03-05 | 石家庄凤山化工有限公司 | Nitrate tail gas treatment device |
| CN117643795B (en) * | 2023-11-07 | 2024-06-07 | 石家庄凤山化工有限公司 | A nitrate tail gas treatment device |
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