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CN103272696A - A method for particle diffusion charge thickening - Google Patents

A method for particle diffusion charge thickening Download PDF

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CN103272696A
CN103272696A CN2013102251739A CN201310225173A CN103272696A CN 103272696 A CN103272696 A CN 103272696A CN 2013102251739 A CN2013102251739 A CN 2013102251739A CN 201310225173 A CN201310225173 A CN 201310225173A CN 103272696 A CN103272696 A CN 103272696A
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白敏菂
毛首蕾
朱玉鹏
李超群
冷白羽
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Dalian Maritime University
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Abstract

A method for particle diffusion charge thickening belongs to the technical field of environmental engineering and the like. The method is characterized in that PM0.1 primary particles and unipolar ions are injected into a high-frequency high-voltage alternating electric field together, and the unipolar ions are carried out in the high-frequency high-voltage alternating electric field by 103~104The particles do secondary up-and-down reciprocating motion, each PM0.1 particle and unipolar ions generate collision charge thickening for tens of thousands of times, even tens of thousands of times, and further the particle size of the particles is increased by 10-103And then the mixture is condensed into primary particles with the particle size larger than 2 mu m. The invention has the advantages of providing an effective method for eliminating PM0.1 primary particle atmospheric pollutants, being also used for the diffusion, charge and condensation pretreatment of the ultrafine dust of a dust remover, greatly reducing the primary investment, the operation cost, the energy consumption and the like, and the like.

Description

一种颗粒物扩散荷电增粗的方法A method for particle diffusion charge thickening

技术领域technical field

本发明属于气体放电物理、等离子体技术及环境工程等技术领域,涉及一种粒径小于0.1μm一次颗粒物扩散荷电增粗的方法。The invention belongs to the technical fields of gas discharge physics, plasma technology and environmental engineering, and relates to a method for thickening primary particles with a particle diameter of less than 0.1 μm by diffusion charging.

背景技术Background technique

我国是正在崛起的经济大国,能源有三分之二来自煤炭,依赖度很高,仅2005年至2010年间煤炭消费量就增加44%,工业企业、发电厂燃煤、燃油锅炉燃烧过程产生超微细烟尘,即粒径≤0.1μm一次颗粒物PM0.1。由于其比表面积很大、活性强、吸附性强,致使PM0.1表面极易富集空气中重金属(As、Se、Pb、Cr等)和PAHs、VOCs等有机污染物;还易贴附SO2、NOx及其副产物硫酸、硝酸、硫酸盐、硝酸盐等污染物,这些污染物多为致癌物质或基因毒性诱变物质。这些微量污染物可在其表面进一步迁移和富集,其危害性极大。治理PM0.1大气污染已成为我国刻不容缓的重大民生问题。my country is a rising economic power. Two-thirds of energy comes from coal, which is highly dependent. From 2005 to 2010, coal consumption increased by 44%. Fine dust, that is, primary particulate matter PM0.1 with a particle size of ≤0.1 μm. Due to its large specific surface area, strong activity, and strong adsorption, the surface of PM0.1 is very easy to accumulate heavy metals (As, Se, Pb, Cr, etc.) in the air and organic pollutants such as PAHs and VOCs; it is also easy to attach SO 2. NOx and its by-products such as sulfuric acid, nitric acid, sulfate, nitrate and other pollutants, these pollutants are mostly carcinogens or genotoxic mutagenic substances. These trace pollutants can further migrate and accumulate on the surface, which is extremely harmful. Controlling PM0.1 air pollution has become an urgent and major livelihood issue in my country.

一次颗粒物荷电增粗通过气体电离后产生的单极性离子与其碰撞来实现,增粗机制分为两种,一种是电场荷电增粗,气体单极性离子在外加电场作用下沿电力线方向做有规则运动时与颗粒物碰撞荷电增粗;另一种扩散荷电增粗,气体做不规则运动时与颗粒物碰撞荷电增粗。一次颗粒物荷电增粗机制依其粒径不同而异。当粒径>1μm时以电场荷电增粗为主导;当粒径<0.1μm时则以扩散荷电增粗为主导。目前电除尘技术是以电场荷电增粗为主,主要捕集粒径>1μm的颗粒物。对PM0.1则无能为力。The charge thickening of primary particles is realized by the collision of unipolar ions generated after gas ionization. The thickening mechanism is divided into two types. One is the charge thickening of electric field, and the gas unipolar ions move along the electric force line When the gas moves in a regular direction, the charge becomes thicker when it collides with the particles; the other kind of diffusion charge becomes thicker, and when the gas moves irregularly, the charge becomes thicker when it collides with the particles. The charging and thickening mechanism of primary particulate matter varies with the particle size. When the particle size > 1 μm, the coarsening by electric field charging is dominant; when the particle size is < 0.1 μm, the coarsening by diffusion charging is dominant. At present, the electrostatic precipitator technology is mainly based on electric field charging to thicken, and mainly captures particles with a particle size > 1 μm. Nothing can be done about PM0.1.

发明内容Contents of the invention

本发明解决了现有捕集粒径小于0.1μm一次颗粒物存在的问题,提供一种粒径小于0.1μm一次颗粒物扩散荷电增粗的新方法。此法将含有PM0.1一次颗粒物的气体和高浓度单极性离子一并注入高频高压交变电场中,单极性离子以极高速度在高频高压交变电场中做103~104次上下往复运动,PM0.1一次颗粒物与单极性离子或带电PM0.1一次颗粒物扩散荷电增粗数万次,甚至数十万次;PM0.1一次颗粒物通过高频高压交变电场扩散荷电增粗后,粒径增大10~103倍,荷电凝聚成粒径>2μm一次颗粒物。为消除PM0.1一次颗粒物大气污染物提供一种有效的方法,且具有一次投资、运行成本、能耗等均大幅度的降低等优点。The invention solves the existing problem of collecting primary particles with a particle size of less than 0.1 μm, and provides a new method for thickening the primary particles with a particle size of less than 0.1 μm by diffusion charging. In this method, the gas containing PM0.1 primary particles and high-concentration unipolar ions are injected into the high-frequency and high-voltage alternating electric field, and the unipolar ions make 10 3 to 10 4 up and down reciprocating movements, PM0.1 primary particles and unipolar ions or charged PM0.1 primary particles diffuse and charge tens of thousands of times, or even hundreds of thousands of times; PM0.1 primary particles pass through high-frequency high-voltage alternating electric field After diffusion charging thickens, the particle size increases by 10 to 10 3 times, and the charge condenses into primary particles with a particle size > 2 μm. It provides an effective method for eliminating PM0.1 primary particulate air pollutants, and has the advantages of greatly reducing primary investment, operating costs, and energy consumption.

PM0.1一次颗粒物扩散荷电是作无规则热运动的离子与其碰撞而使之荷电。对于粒径<0.1μm尘粒的扩散荷电与其大小、荷电量及离子热运动强度、碰撞几率、运动速度和在电场中停留时间等多种因素有关。尘粒荷电过程及荷电量计算式推导都遵循气体分子运动的有关理论。The diffusion charging of PM0.1 primary particles is charged by the collision of ions in irregular thermal motion. The diffusion charging of dust particles with a particle size of <0.1 μm is related to various factors such as size, charge, ion thermal movement intensity, collision probability, movement speed and residence time in the electric field. The charging process of dust particles and the derivation of the calculation formula of the charging quantity follow the relevant theory of gas molecule motion.

设距尘粒相当远外,电场中单位体中的单极性离子数位N;紧靠尘粒周围的离子数为N1,根据气体分子运动理论,可得两者关系的表示式:Assume that the number of unipolar ions in the unit body in the electric field is quite far away from the dust particles, N; the number of ions close to the dust particles is N1. According to the theory of gas molecular motion, the expression of the relationship between the two can be obtained:

N1=N×exp(-eV/kT)式1N 1 =N×exp (-eV/kT) Formula 1

式中:e为离子的电荷量;V为尘粒所在之处的电位;k为波慈曼常数;T为气体温度;离子在单位时间内穿过尘粒单位外表面积的数目用N2表示时,则In the formula: e is the electric charge of the ion; V is the electric potential where the dust particle is located; k is Botzmann’s constant; T is the gas temperature; when

N 2 = N 1 kT 2 &pi;m 式2 N 2 = N 1 kT 2 &pi;m Formula 2

式中:m为离子的质量。根据高斯定理知,位于尘粒外围区域电场强度为In the formula: m is the mass of the ion. According to Gauss's theorem, the electric field strength in the peripheral area of dust particles is

E 2 = q p 4 &pi; &epsiv; 0 r 2 式3 E. 2 = q p 4 &pi; &epsiv; 0 r 2 Formula 3

式中:qp为一次颗粒物电荷量;E2为尘粒外围荷电量为qp时的电场场强;ε0为真空介质常数;r为颗粒物外围荷电半径。将式3的微分形式对r积分,则得尘粒荷电后在半径r处的电位In the formula: q p is the charge amount of the primary particle; E 2 is the electric field strength when the charge amount on the periphery of the dust particle is q p ; ε 0 is the vacuum dielectric constant; r is the charge radius on the periphery of the particle. Integrate the differential form of Equation 3 with respect to r, and then get the potential at the radius r after the dust particle is charged

V = q p 4 &pi; &epsiv; 0 r 式4 V = q p 4 &pi; &epsiv; 0 r Formula 4

将式4代入式1中,则Substituting Equation 4 into Equation 1, then

N 1 = N &times; exp ( - eq p 4 &pi; &epsiv; 0 kTr ) 式5 N 1 = N &times; exp ( - eq p 4 &pi; &epsiv; 0 kTr ) Formula 5

在尘粒外表面r=a处,单位体积中的离子数N1aAt r=a on the outer surface of the dust particle, the number of ions N 1a per unit volume is

N 1 a = N &times; exp ( - eq p 4 &pi; &epsiv; 0 kTa ) 式6 N 1 a = N &times; exp ( - eq p 4 &pi; &epsiv; 0 kT ) Formula 6

利用式6计算出颗粒物表面的荷电速率Calculate the charge rate on the particle surface by using Equation 6

dqdq pp dtdt == 44 &pi;e&pi;e NN 22 aa aa 22 == 44 &pi;ea&pi;ea 22 NN 11 aa kTkT 22 &pi;m&pi;m

== ee 88 &pi;kT&pi;kT mm aa 22 NexpNext (( -- eqeq pp 44 &pi;&pi; &epsiv;&epsiv; 00 kTakT ))

式7Formula 7

式中m为离子的质量。以t=0、qp=0的边界条件对式7进行积分则得PM0.1荷电量:where m is the mass of the ion. Integrating Equation 7 with the boundary conditions of t=0, qp =0, the charge of PM0.1 can be obtained:

q p = 2 &pi; &epsiv; 0 d p kT e 1 n ( 1 + d p Ne 2 t 2 &epsiv; 0 2 m&pi;kT ) 式8 q p = 2 &pi; &epsiv; 0 d p kT e 1 no ( 1 + d p Ne 2 t 2 &epsiv; 0 2 m&pi;kT ) Formula 8

如以离子平均速度

Figure BDA00003312951500036
代入上式,上式则改写为average velocity of ions
Figure BDA00003312951500036
Substituting into the above formula, the above formula can be rewritten as

q p = 2 &pi; &epsiv; 0 d p kT e 1 n ( 1 + d p u - Ne 2 t 8 &epsiv; 0 kT ) 式9 q p = 2 &pi; &epsiv; 0 d p kT e 1 no ( 1 + d p u - Ne 2 t 8 &epsiv; 0 kT ) Formula 9

式中:dp为PM0.1的直径;为离子平均速度。上式适用于粒径dp<0.1μm一次颗粒物的扩散荷电量计算。从式中可见,只有增加单极性离子数N、气体温度T、离子平均速度

Figure BDA00003312951500039
和一次颗粒物荷电时间t方可增加PM0.1荷电量。由于气体温度T、一次颗粒物荷电时间t增加量很有限,而单极性粒子数N及其平均速度可成
Figure BDA000033129515000310
数量级式增加,可采用增加单极性粒子数N和单极性离子平均速度方法
Figure BDA000033129515000311
来增加PM0.1一次颗粒物的电荷量。In the formula: dp is the diameter of PM0.1; is the average ion velocity. The above formula is applicable to the calculation of the diffusion charge of primary particles with a particle size d p <0.1 μm. It can be seen from the formula that only by increasing the number N of unipolar ions, the gas temperature T, and the average velocity of ions
Figure BDA00003312951500039
And the charging time t of the primary particulate matter can increase the charging capacity of PM0.1. Due to the limited increase in the gas temperature T and the charging time t of primary particles, the number N of unipolar particles and their average velocity can be
Figure BDA000033129515000310
The order of magnitude increases, and the method of increasing the number N of unipolar particles and the average velocity of unipolar ions can be used
Figure BDA000033129515000311
To increase the charge of PM0.1 primary particles.

以下详述PM0.1一次颗粒物的扩散荷电增粗方法。The method for thickening the PM0.1 primary particulate matter by diffusion charging will be described in detail below.

提高单极性离子数量及其运动速度是PM0.1一次颗粒物荷电增粗的关键。通过高频高压交变电源8输出电压施加到高压电极11上,高压电极11与接地极10之间形成高频高压荷电增粗交变电场3,电场强度为0.8kV~40kV。将浓度高达1010/cm3~1014/cm3的单极性离子1(负离子或正离子)和含有PM0.1一次颗粒物2的气体一并注入0.1m~4m长的高频高压荷电增粗交变电场3中,即每1cm3气体中单极性离子达到1010~1014个。单极性离子1在高频高压荷电增粗交变电场3中平均运动速度高达2km/s,并以2km/s的速度在高压电极11与接地极10之间的间隙作103~104次上下往复运动,其运动轨迹如图1中4所示。每个PM0.1一次颗粒物2每秒钟与单极性离子1碰撞荷电增粗机遇为数万次,甚至数十万次。M0.1一次颗粒物在交变电场中荷电增粗轨迹如图1中5所示。PM0.1一次颗粒物通过高频高压荷电增粗交变电场3扩散荷电增粗后,其粒径增大10~103倍,饱和荷电凝聚成粒径>2μm一次颗粒物7。Increasing the number of unipolar ions and their moving speed is the key to the charge thickening of PM0.1 primary particles. The output voltage of the high-frequency high-voltage alternating power source 8 is applied to the high-voltage electrode 11, and a high-frequency high-voltage charge-thickened alternating electric field 3 is formed between the high-voltage electrode 11 and the ground electrode 10, and the electric field strength is 0.8kV-40kV. Inject unipolar ions 1 (negative ions or positive ions) with a concentration as high as 10 10 /cm 3 to 10 14 /cm 3 and gas containing PM0.1 primary particulate matter 2 together into a 0.1m to 4m long high-frequency high-voltage charging In thickening the alternating electric field 3, the number of unipolar ions per 1 cm 3 of gas reaches 10 10 -10 14 . Unipolar ions 1 move at an average speed of 2 km/s in the high-frequency, high-voltage charged and thickened alternating electric field 3, and move 10 3 to 10 in the gap between the high-voltage electrode 11 and the ground electrode 10 at a speed of 2 km/s. 4 times of up and down reciprocating motion, its motion track is shown as 4 in Fig. 1. Every PM0.1 particle 2 collides with unipolar ions 1 every second for tens of thousands or even hundreds of thousands of times. The thickening trajectory of M0.1 primary particles in the alternating electric field is shown as 5 in Figure 1. After PM0.1 primary particles are thickened by high-frequency high-voltage charging and alternating electric field 3, the particle size increases by 10 to 10 3 times, and the saturated charge condenses into primary particles with a particle size > 2 μm7.

高频高压荷电增粗交变电场3包括Al2O3薄片9、接地极10、高压电极11,其间隙距离为10cm~60cm;接地极10、高压电极11均采用304不锈薄钢板加工而成的长方形极板。高频高压交变电源8频率范围为80Hz~12kHz,输出电压幅值范围为10kV~600kV。High-frequency high-voltage charged thickening alternating electric field 3 includes Al 2 O 3 sheet 9, grounding electrode 10, and high-voltage electrode 11, and the gap distance is 10 cm to 60 cm; grounding electrode 10 and high-voltage electrode 11 are all made of 304 stainless steel sheets formed rectangular plates. The frequency range of the high-frequency and high-voltage alternating power supply 8 is 80Hz-12kHz, and the range of the output voltage amplitude is 10kV-600kV.

本发明将PM0.1一次颗粒物通过高频高压交变电场完成一次颗粒物饱和荷电并凝聚增粗成粒径>2μm一次颗粒物。这解决了PM0.1一次颗粒物捕集净化难题,并为扩散荷电凝聚增粗提供了一种可行、有效的新方法。本发明也可以应用于电除尘器、布袋、沉降等除尘器的预处理中,经预先荷电凝聚成大粒径的一次颗粒物,将大幅度提高电除尘器、布袋、沉降等除尘器的净化效率。同时又可大幅度缩小除尘器体积,降低钢材用量,进而降低了一次投资和运行成本,又减少了能耗。In the present invention, the PM0.1 primary particles are saturated and charged through a high-frequency and high-voltage alternating electric field, and then condensed and thickened into primary particles with a particle diameter > 2 μm. This solves the problem of PM0.1 primary particle capture and purification, and provides a feasible and effective new method for diffusion charging and condensation thickening. The present invention can also be applied to the pretreatment of dust collectors such as electrostatic precipitators, cloth bags, and sedimentation. After pre-charging and condensing into primary particles with large particle diameters, the purification of dust collectors such as electrostatic precipitators, cloth bags, and sedimentation will be greatly improved. efficiency. At the same time, the volume of the dust collector can be greatly reduced, and the amount of steel used can be reduced, thereby reducing the primary investment and operating costs, and reducing energy consumption.

附图说明Description of drawings

下面结合附图和实施例对本发明作进一步说明。The present invention will be further described below in conjunction with drawings and embodiments.

图1是PM0.1一次颗粒物荷电增粗方法原理示意图。Figure 1 is a schematic diagram of the principle of charging thickening method for PM0.1 primary particulate matter.

图2是交变电场频率对粒径0.1μm一次颗粒物质量占有率影响曲线图。Figure 2 is a graph showing the influence of alternating electric field frequency on the mass occupancy rate of primary particles with a particle size of 0.1 μm.

图3是交变电场场强对粒径0.1μm一次颗粒物质量占有率影响曲线图。Figure 3 is a graph showing the influence of alternating electric field strength on the mass occupancy rate of primary particulate matter with a particle size of 0.1 μm.

图中:1单极性离子;2PM0.1一次颗粒物;3高频高压荷电增粗交变电场;4单极性离子运动轨迹;5PM0.1一次颗粒物在交变电场中荷电增粗轨迹;6荷电增粗一次颗粒物;7饱和荷电凝聚成粒径>2μm一次颗粒物;8高频高压交变电源;9Al2O3薄片;10接地极;11高压电极。In the figure: 1 unipolar ion; 2PM0.1 primary particulate matter; 3 high-frequency high-voltage charging thickening alternating electric field; 4 unipolar ion trajectory; 5PM0.1 primary particulate matter charging thickening trajectory in alternating electric field ; 6 Charged and thickened primary particles; 7 Saturated charge condenses into primary particles with a particle size > 2 μm; 8 High-frequency high-voltage alternating power supply; 9 Al 2 O 3 flakes; 10 Grounding electrode; 11 High-voltage electrode.

具体实施方式Detailed ways

下面结合技术方案和附图详细叙述本发明的实施例:Describe the embodiment of the present invention in detail below in conjunction with technical scheme and accompanying drawing:

本发明PM0.1一次颗粒物荷电增粗方法原理示意如图1所示。通过高频高压交变电源8输出电压施加到高压电极11上,高压电极11与接地极10之间形成高频高压荷电增粗交变电场3,将浓度高达1010/cm3~1014/cm3的单极性离子1和含有PM0.1一次颗粒物2的气体一并注入0.1m~4m长的高频高压荷电增粗交变电场3中,即每1cm3气体中单极性离子达到1010~1014个以上。单极性离子1在高频高压荷电增粗交变电场3中以2km/s的速度在高压电极11与接地极10之间的间隙作103~104次上下往复运动,每个PM0.1一次颗粒物2每秒钟与单极性离子1碰撞荷电增粗机遇为数万次,至数十万次。PM0.1一次颗粒物通过高频高压荷电增粗交变电场3经扩散荷电增粗后,其粒径增大10~103倍,饱和荷电凝聚成粒径>2μm一次颗粒物7。The schematic diagram of the method for charging and thickening PM0.1 primary particles of the present invention is shown in FIG. 1 . The output voltage of the high-frequency high-voltage alternating power supply 8 is applied to the high-voltage electrode 11, and a high-frequency high-voltage charge thickening alternating electric field 3 is formed between the high-voltage electrode 11 and the ground electrode 10, and the concentration is as high as 10 10 /cm 3 to 10 14 Unipolar ions 1/cm 3 and gas containing PM0.1 primary particulate matter 2 are injected into the 0.1m-4m long high-frequency high-voltage charge thickening alternating electric field 3, that is, the unipolar ion in every 1cm 3 of gas The number of ions reaches 10 10 to 10 14 or more. The unipolar ion 1 reciprocates 10 3 to 10 4 times up and down in the gap between the high-voltage electrode 11 and the ground electrode 10 at a speed of 2 km/s in the high-frequency high-voltage charging thickening alternating electric field 3 , and each PM0 .1 The opportunity for particle 2 to collide with unipolar ion 1 to charge and thicken is tens of thousands to hundreds of thousands of times per second. PM0.1 primary particles are thickened by high-frequency and high-voltage charging in alternating electric field 3 and thickened by diffusion charging, the particle size increases by 10 to 10 3 times, and the saturated charge condenses into primary particles with a particle size > 2 μm 7 .

本发明实施结果如图2、3所示。从图2交变电场频率对粒径0.1μm一次颗粒物质量占有率的影响曲线可知,在高频高压电场强度为5kV/cm的条件下,当交变电场频率为10kHz时,粒径为0.1μm一次颗粒物质量占有率约为28%,即有72%的粒径0.1μm一次颗粒物荷电增粗了,可见凝聚增粗效果明显。从图3交变电场强度对粒径0.1μm一次颗粒物质量占有率的影响曲线可见,在高频高压交变电场频率为11kHz条件下,当高频高压交变电场强度为5kV/cm时,粒径0.1μm一次颗粒物质量占有率约为28%,可见在此参数下有72%粒径0.1μm一次颗粒物荷电增粗。The implementation results of the present invention are shown in Figures 2 and 3. From the influence curve of alternating electric field frequency on the mass occupancy rate of primary particles with a particle size of 0.1 μm in Figure 2, it can be seen that under the condition of high frequency and high voltage electric field strength of 5 kV/cm, when the alternating electric field frequency is 10 kHz, the particle size is 0.1 μm The mass occupancy rate of primary particulate matter is about 28%, that is, 72% of the primary particulate matter with a particle size of 0.1 μm is charged and thickened, which shows that the effect of agglomeration and thickening is obvious. It can be seen from the influence curve of alternating electric field intensity on the mass occupancy rate of primary particles with a particle size of 0.1 μm in Fig. The mass occupancy rate of primary particles with a diameter of 0.1 μm is about 28%. It can be seen that 72% of the primary particles with a diameter of 0.1 μm are charged and thickened under this parameter.

Claims (2)

1. a particle diffusional charging increases thick method, it is characterized in that concentration up to 10 10/ cm 3~10 14/ cm 3The unipolarity ion injects long 0.1m~4m together with the gas that contains the PM0.1 primary particulate, electric-field intensity is the high-frequency and high-voltage alternating electric field of 0.8kV~40kV; After the PM0.1 primary particulate increased slightly by high-frequency and high-voltage alternating electric field diffusional charging, its particle diameter increased 10~10 3Doubly, the charged particle diameter>2 μ m primary particulates that are condensed into.
2. method according to claim 1 is characterized in that, described high-frequency and high-voltage alternating electric field comprises Al 2O 3Thin slice (9), earthing pole (10), high-field electrode (11), its clearance distance is 10cm~60cm; The rectangle pole plate that earthing pole (10), high-field electrode (11) all adopt 304 stainless sheet metals to process; High-frequency and high-voltage alternating source (8) frequency range is 80Hz~12kHz, and the output voltage amplitude scope is 10kV~600kV.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106466535A (en) * 2015-08-21 2017-03-01 蔡小兵 A kind of particulate filter arrangement

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20110195002A1 (en) * 2010-02-11 2011-08-11 Energy & Environmental Research Center Foundation Advanced particulate matter control apparatus and methods
CN102631990A (en) * 2012-04-17 2012-08-15 中国科学院过程工程研究所 Method and device for efficiently catching nanometer micro-particles
CN102836779A (en) * 2011-06-24 2012-12-26 宝山钢铁股份有限公司 Fine particle removal method and device

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20110195002A1 (en) * 2010-02-11 2011-08-11 Energy & Environmental Research Center Foundation Advanced particulate matter control apparatus and methods
CN102836779A (en) * 2011-06-24 2012-12-26 宝山钢铁股份有限公司 Fine particle removal method and device
CN102631990A (en) * 2012-04-17 2012-08-15 中国科学院过程工程研究所 Method and device for efficiently catching nanometer micro-particles

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
刘栋: "微细粉尘在电除尘器烟道中的荷电凝聚特性研究", 《中国优秀硕士学位论文全文数据库》, 30 May 2009 (2009-05-30) *
陈志刚等: "高流场中微细粉尘荷电凝并粗化对电捕集效率的影响", 《科技导报》, no. 06, 31 December 2010 (2010-12-31) *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106466535A (en) * 2015-08-21 2017-03-01 蔡小兵 A kind of particulate filter arrangement

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Application publication date: 20130904