JPH07232099A - Electric precipitator - Google Patents

Electric precipitator

Info

Publication number
JPH07232099A
JPH07232099A JP6051312A JP5131294A JPH07232099A JP H07232099 A JPH07232099 A JP H07232099A JP 6051312 A JP6051312 A JP 6051312A JP 5131294 A JP5131294 A JP 5131294A JP H07232099 A JPH07232099 A JP H07232099A
Authority
JP
Japan
Prior art keywords
electrode plate
dust
dust collecting
collecting electrode
parallel
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.)
Granted
Application number
JP6051312A
Other languages
Japanese (ja)
Other versions
JP3427165B2 (en
Inventor
Keiichi Hara
恵一 原
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.)
NIPPON FILTRATION KK
Filtration Japan Co Ltd
Original Assignee
NIPPON FILTRATION KK
Filtration Japan Co Ltd
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 NIPPON FILTRATION KK, Filtration Japan Co Ltd filed Critical NIPPON FILTRATION KK
Priority to JP05131294A priority Critical patent/JP3427165B2/en
Publication of JPH07232099A publication Critical patent/JPH07232099A/en
Application granted granted Critical
Publication of JP3427165B2 publication Critical patent/JP3427165B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE:To improve a dust collection efficiency to obtain a miniaturized device in an electric precipitator which adsorbs dust due to an electric discharge which takes place between poles. CONSTITUTION:Openings (p) are provided in rectangular dust collection polar plates 2 which constitute a dust collection polar plate group. The opening is circular or elliptic, and covers 10 to 50% of the total area. When an electric precipitator is activated, an intensified electric current runs on the surface of the dust collection polar plate 2 and becomes susceptible of dust settlement. However, as the air flow generates toward the opening, dust seldom accumulates and grows not as is the case with a conventional dust collector. In addition, the whole device can be scaled down because a charging distance can be short.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、発電所、セメント工
場、産業焼却炉および道路、トンネルにおける浮遊微粒
子除去用、または放射性粉塵除去用あるいは室内空気清
浄用などに使用する電気集塵装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an electrostatic precipitator for use in power plants, cement factories, industrial incinerators, roads, tunnels, for removing fine particles, for removing radioactive dust, or for cleaning indoor air. Is.

【0002】[0002]

【従来の技術】電気集塵装置は、高電圧を使用した機械
において放電部分に塵埃、粉塵等(以下、塵埃で代表す
る。)が付着することを原理としたもので、筐体に、不
平等電界を発生させるための放電極(負極)と塵埃を付
着させるための集塵極とを間隔を開けて対向させて設
け、両電極に高電圧を印加し、放電極と集塵極との間の
空気中に放電させるようにしたものである。なお、オゾ
ンの発生量の少ないプラス放電に対し、マイナス放電も
利用されている。
2. Description of the Related Art An electrostatic precipitator is based on the principle that dust, dust, etc. (hereinafter referred to as "dust") adhere to the discharge part of a machine using a high voltage, and the case does not A discharge electrode (negative electrode) for generating a uniform electric field and a dust collection electrode for adhering dust are provided to face each other with a gap, and a high voltage is applied to both electrodes to separate the discharge electrode and the dust collection electrode. It is designed to be discharged into the air between. Negative discharge is also used as opposed to positive discharge, which generates less ozone.

【0003】本出願の発明者は、すでに従来の電気集塵
装置を提案してきた。それらは、例えば、図8に示すよ
うに多数の孔5aをその面に形成した集塵極板5を、集塵
を目的とする空気の流れ方向(矢印方向)に直交させて
設け、複数の集塵極板5の間に、金属製の矩形板の縁側
に山形の刺部6aを連続的に形成した放電極板6を、この
面を流れ方向と平行にして複数並列に設けた電気集塵装
置1が提案されている。
The inventor of the present application has already proposed a conventional electrostatic precipitator. For example, as shown in FIG. 8, a plurality of holes 5a are formed on the surface of the dust collecting electrode plate 5 so as to be orthogonal to the air flow direction (arrow direction) for the purpose of collecting dust. Between the dust collecting electrode plates 5, a plurality of discharge electrode plates 6 each having a mountain-shaped pierced portion 6a continuously formed on the edge side of a metal rectangular plate are provided in parallel with the surface parallel to the flow direction. A dust device 1 has been proposed.

【0004】また、他の従来例として図9、図10に
は、本出願の発明者が平成6年1月31日付けで出願し
た電気集塵装置が示されており、この装置では、複数枚
の矩形状の集塵極板2がスペーサー7(7a,7b,7c)
(間隔調整手段)を挟んで連結し、集塵極板群8を形成
し、また、複数枚の両縁側に山形の刺部6aを連続的に形
成した放電極板6がスペーサー9(9a,9b)(間隔調整
手段)を挟んで連結し、放電極板群10を形成している。
As another conventional example, FIGS. 9 and 10 show an electrostatic precipitator filed by the inventor of the present application on January 31, 1994. The rectangular dust collecting electrode plate 2 is a spacer 7 (7a, 7b, 7c)
The space between the spacers 9 (9a, 9a, 9a, 9a, 9b) (space adjustment means) are sandwiched and connected to form a discharge electrode plate group 10.

【0005】図10に示す電気集塵装置1は、複数の集
塵極板群8のそれぞれの間に放電極板群10を配置して固
定したユニット11を、並列して数段に筐体に吊設して装
着しており、集塵極板群8および放電極板群10は、スペ
ーサー7,9の端部から突出したねじ13でユニット11の
枠体に固定されている。そして、高電圧の負極を放電極
板群10に接続し、正極を集塵極板群8に接続させ、送風
機によって処理する空気を電極間に通すようになってい
る。
In the electrostatic precipitator 1 shown in FIG. 10, units 11 in which a discharge electrode plate group 10 is arranged and fixed between each of a plurality of dust collecting electrode plate groups 8 are arranged in parallel in several casings. The dust collecting electrode plate group 8 and the discharge electrode plate group 10 are fixed to the frame body of the unit 11 by screws 13 protruding from the ends of the spacers 7 and 9. Then, the high-voltage negative electrode is connected to the discharge electrode plate group 10, the positive electrode is connected to the dust collecting electrode plate group 8, and the air to be treated by the blower is passed between the electrodes.

【0006】この装置では図11に示すように、2つの
集塵極板群8の間に放電極板群10を配置して高電圧を印
加すると放電電流が流れ、立体的で複雑な不平等電界を
生じる。放電極板群10の放電極板6どうしでは、隣り合
った平面が同一電位であるため無電界となり、逆帯電粒
子m−の付着が著しく減少される。帯電した塵埃mは、
放電極板群10の上流側端と対向した集塵極板群8の下流
側端に吸着され、堆積される。堆積し過ぎると塵埃mの
表面が滑りやすくなって電界の束縛を抜けて飛散するよ
うになるが、放電電界によって、流体の流れに逆らって
再び、集塵極板群8の下流側端に吸着されることにな
る。塵埃どうしが固まって堆積し、吸着力で支え切れな
くなると塵埃mは下方に落下する。このようにして、処
理対象の空気中の塵埃を吸着され、落下するので、空気
が浄化される。
In this apparatus, as shown in FIG. 11, when a discharge electrode plate group 10 is arranged between two dust collecting electrode plate groups 8 and a high voltage is applied, a discharge current flows, causing a three-dimensional and complicated inequality. Generates an electric field. In the discharge electrode plates 6 of the discharge electrode plate group 10, since the adjacent planes have the same potential, there is no electric field, and the adhesion of the oppositely charged particles m- is significantly reduced. The charged dust m is
It is adsorbed and deposited on the downstream end of the dust collecting electrode plate group 8 facing the upstream end of the discharge electrode plate group 10. If it is accumulated too much, the surface of the dust m becomes slippery and escapes from the constraint of the electric field to be scattered. Will be done. When the dust particles are hardened and accumulated and cannot be supported by the suction force, the dust particles m fall down. In this way, the dust in the air to be treated is adsorbed and falls, so that the air is purified.

【0007】また、集塵極板2の平面が垂直であり、か
つ、不平等電界により、付着した塵埃mは隣接した集塵
極板2に付着、堆積し、成長して落下する。放電極板群
10においては逆帯電粒子m−の付着が少ないので放電の
抵抗がわずかであり、強い放電電流を維持することがで
き機械の寿命を長くすることができる。
Further, the plane of the dust collecting electrode plate 2 is vertical, and due to the unequal electric field, the attached dust m is attached and deposited on the adjacent dust collecting electrode plate 2, grows and drops. Discharge electrode plate group
In the case of 10, the amount of reversely charged particles m-attached is small, so that the discharge resistance is small, a strong discharge current can be maintained, and the life of the machine can be lengthened.

【0008】[0008]

【発明が解決しようとする課題】しかしながら、これら
の装置を継続して使用していくと集められた塵埃は、図
2に部分的に拡大して示すような電極への付着状態を示
すことが、本発明者の観測により判明した。すなわち、
集塵極板2には使用開始後、先ず処理空気の流れ方向先
端に塵埃が付着しはじめ、そこで塵埃が成長してほぼ砲
弾型になり、それを核として空気の流れ方向とは逆の方
が厚く、後方に向かって薄く後部へ山形にbの部分が付
着し、次に同様にしてbの上にcの部分が付着する。こ
の付着の状況は、2層に限られるものではなく、場合に
よって3層にもなる。そして堆積した塵埃は、その重量
に耐えられなくなったり、あるいは放電極板6と集塵電
極板2間の火花放電による衝撃によって落下する。そし
て、塵埃が成長していくときは集塵電極板2が塵埃によ
って覆われるので、集塵効果がその間、低下することに
なり、装置を長期間使用するときは、その集塵効率が問
題になる。
However, when these devices are continuously used, the collected dust may show a state of adhesion to the electrodes as shown in a partially enlarged view in FIG. It was found by the observation of the present inventor. That is,
After starting to use the dust collecting electrode plate 2, first, dust begins to adhere to the tip of the processing air in the flow direction, where the dust grows and becomes almost a bullet shape. Is thicker, and is thinner toward the rear, and the portion b is attached to the rear in a mountain shape, and then the portion c is attached on b in the same manner. The situation of adhesion is not limited to two layers, but may be three layers in some cases. Then, the accumulated dust cannot bear the weight or falls due to the impact due to the spark discharge between the discharge electrode plate 6 and the dust collecting electrode plate 2. When the dust grows, the dust collecting electrode plate 2 is covered with the dust, so that the dust collecting effect decreases during that period, and when the device is used for a long time, the dust collecting efficiency becomes a problem. Become.

【0009】上記図2のように塵埃の集まる原因は、本
出願の発明者の観測によれば、微視的にみて以下のとう
りと考えられる。集塵極板2上の塵埃が堆積する様子
(集塵の過程)を細かくみていくと、図3のように集塵
の初期においては、中心部に塵が多く集まり、その周辺
に徐々に塵の密度が小となっていく塵の円が見られる。
実際上のこの円の直径は、図10の放電極板6と集塵極
板2との距離cの約2倍程度とみられる。これを集塵極
板2上でみた場合、図4に示すように、放電極板6から
の電流が集塵極板2に達すると、点線で示す電流は集塵
極板2に達したときの強度が最大であり、そこを中心と
して電流強度が徐々に弱くなる電流強度の円を想定でき
る。図4ではAの文字が中心で大きく、円周上で小さく
示したことはその点を加味して描いたものである。円周
は図面上、モデル的に描かれているが、実際は電流密度
により円周が互いに重なった形になると考えられる。
According to the observation by the inventor of the present application, the cause of dust gathering as shown in FIG. A detailed view of how dust is accumulated on the dust collecting electrode plate 2 (during dust collection process). As shown in FIG. 3, in the initial stage of dust collection, a large amount of dust gathers in the central portion and gradually gathers around it. You can see dust circles with decreasing density.
The actual diameter of this circle is considered to be about twice the distance c between the discharge electrode plate 6 and the dust collecting electrode plate 2 in FIG. When this is viewed on the dust collecting electrode plate 2, when the current from the discharge electrode plate 6 reaches the dust collecting electrode plate 2 as shown in FIG. Can be assumed to be the maximum and the current intensity circle gradually decreases around that. In FIG. 4, the letter A is large at the center and small on the circumference, which is taken into consideration. The circumference is drawn as a model on the drawing, but it is considered that the circumferences actually overlap each other due to the current density.

【0010】上記集塵効率を向上させるには、極板の数
を多くしたり、その配置を工夫することが行われている
が、それらには限界がある。また、最近の環境問題に対
する認識から、既存の工場設備、例えばセメント製造工
場や産業用焼却炉での粉塵等の除去が問題になってい
る。しかし、上記工場では処理目的の空気量が膨大な量
で、従来の電気集塵装置では、その規模や効率からみて
期待に応えるものではなかった。したがって、本発明は
小型で、集塵効率が改善された電気集塵装置を提供する
ことを目的とする。
In order to improve the dust collection efficiency, the number of electrode plates has been increased and the arrangement thereof has been devised, but they have limitations. Further, due to recent recognition of environmental problems, removal of dust and the like from existing factory equipment, such as cement manufacturing plants and industrial incinerators, has become a problem. However, the above-mentioned factory has an enormous amount of air for processing purposes, and the conventional electrostatic precipitator does not meet the expectation in view of its scale and efficiency. Therefore, an object of the present invention is to provide an electrostatic precipitator having a small size and improved dust collecting efficiency.

【0011】[0011]

【課題を解決するための手段】本発明は、上記の目的を
達成するため、開口部が設けられた複数の矩形状の集塵
極板を、該集塵極板の平面を垂直にすると共に、互いに
平面を対向させて並列させ、各々の集塵極板の間に第1
の間隔調整手段を介して柵状に固定し、該柵状の集塵極
板群を、気体流路の流れ方向に対して前記平面を平行に
して、複数個間隔を開けて順次設置し、複数の矩形板の
両縁側に刺部を形成した放電極板を、該放電極板の平面
を垂直にすると共に、互いに平面を対向させて並列さ
せ、各々の放電極板の間に第2の間隔調整手段を介して
柵状に固定し、該柵状の放電極板群を、気体流路の流れ
方向に対して前記平面を平行にして、前記集塵極板群の
各間に間隔を開けて配設したことを特徴とする。また、
上記構成において、前記集塵極板に設けられた開口部の
形状は、円または長穴としたことを特徴とするものであ
り、さらに前記集塵極板に設けられた開口部の面積は、
集塵極板の面積に対して10〜50%を占めることを特
徴とするものである。
In order to achieve the above-mentioned object, the present invention provides a plurality of rectangular dust collecting electrode plates provided with openings with the planes of the dust collecting electrode plates being vertical. , The planes are opposed to each other and arranged in parallel, and the first electrode is provided between the dust collecting electrode plates.
Is fixed in a fence shape via the interval adjusting means, and the fence-shaped dust collecting electrode plate group is placed in parallel with the plane in parallel to the flow direction of the gas flow path, with a plurality of intervals provided therebetween. A plurality of rectangular plates are formed with barbed portions on both edge sides, and the planes of the discharge electrode plates are made vertical, and the planes are opposed to each other and arranged in parallel, and a second gap is adjusted between the discharge electrode plates. It is fixed in the form of a fence via a means, and the fence-shaped discharge electrode plate group is made parallel to the plane with respect to the flow direction of the gas flow path, with an interval provided between each of the dust collecting electrode plate groups. It is characterized in that it is provided. Also,
In the above configuration, the shape of the opening provided in the dust collecting electrode plate is characterized by being a circle or an elongated hole, further the area of the opening provided in the dust collecting electrode plate,
It is characterized by occupying 10 to 50% of the area of the dust collecting electrode plate.

【0012】[0012]

【作用】本発明は上記のように構成したものであるの
で、放電極板からの電流は開口部の間の部分に集中し、
付着した塵埃がより成長しようとしても付着する集塵極
板の面積が少なく、また、開口を通しての空気の流れに
よって過大な塵埃の成長は抑制されるので、集塵極板に
付着した塵埃は落下し(空気の流れの均等化)、従来の
ような塵埃の成長は見られず、長期の使用によっても装
置の集塵効率の低下が見られない。付着した塵埃の集塵
極板からの落下は、空気の流ればかりではなく、放電極
板から集塵極板への火花放電の衝撃によっても起こる。
また、塵埃は集塵極板に付着して成長するがすぐに落下
するので、単位面積あたりの送り込む空気量が増加し、
荷電距離(装置に送りこまれた空気が、装置を出るまで
に電荷をかけられる距離、実際には装置の長さ。)も短
くてすむ。このことは装置全体を小型化できるので装置
の重量を軽減することが可能となる。
Since the present invention is configured as described above, the current from the discharge electrode plate is concentrated in the portion between the openings,
Even if the attached dust tries to grow further, the area of the dust collecting electrode plate to which it adheres is small, and since the excessive dust growth is suppressed by the air flow through the opening, the dust that adheres to the collecting electrode plate falls. However, the growth of dust unlike the conventional case is not seen (equalization of air flow), and the dust collection efficiency of the device is not deteriorated even after long-term use. The fall of the attached dust from the dust collecting electrode plate is caused not only by the flow of air but also by the impact of the spark discharge from the discharge electrode plate to the dust collecting electrode plate.
Also, since dust adheres to the dust collecting electrode plate and grows, it immediately drops, increasing the amount of air sent in per unit area,
The charging distance (the distance that the air sent into the device can be charged before it leaves the device, actually the length of the device) can be short. This makes it possible to reduce the weight of the device because the entire device can be downsized.

【0013】[0013]

【実施例】以下本発明の実施例を図1、図5及び図6に
基づいて説明する。図1と図9との同一符号の箇所につ
いては説明を省略する。図5に示すように集塵極板2a
には、開口として円状開口部pが4個、3個の順にその
端部から設けられる。円状開口部は、集塵極板2aの端
から端まで設けられるが、開口部全体の面積の集塵極板
の面積に対する割合は、10〜50%である。開口の種
類としては、円ばかりではなく、図6に示す集塵極板2
bのp´のような長穴でもよい。このように開口を設け
た集塵極板2aを、図9の集塵極板2の代わりに設置し
た装置として図1でみると、矢印方向に処理する空気を
装置に送り込んだ場合、放電極板6からの電流は、図5
の矢印のように集中し、電流が分散することなく集塵極
板2上での電流の密度が大きくなるので、塵埃の付着効
率は従来に比して向上する。
Embodiments of the present invention will be described below with reference to FIGS. 1, 5 and 6. Description of the same reference numerals in FIGS. 1 and 9 will be omitted. As shown in FIG. 5, the dust collecting electrode plate 2a
In this case, four circular openings p are provided as openings in the order of 3 and from the end thereof. The circular opening is provided from end to end of the dust collecting electrode plate 2a, and the ratio of the area of the entire opening to the area of the dust collecting electrode plate is 10 to 50%. The types of openings are not limited to circles, but the dust collection electrode plate 2 shown in FIG.
An elongated hole such as p'of b may be used. As shown in FIG. 1, the dust collecting electrode plate 2a thus provided with openings is installed in place of the dust collecting electrode plate 2 in FIG. 9, and when the air to be treated is sent into the device, the discharge electrode The current from plate 6 is shown in FIG.
Since the current is concentrated as shown by the arrow and the current density on the dust collecting electrode plate 2 is increased without the current being dispersed, the dust adhesion efficiency is improved as compared with the conventional case.

【0014】したがって塵埃の付着は従来よりも多くな
るが、集塵極板2に付着してもすぐに、図7に示すよう
に集塵極板2の開口部を通じて空気の流れが生じるの
で、それによって払い落とされて剥れたり、また、付着
しても付着量が過大にならないうちに自重によって落下
(従来のものより成長が早いが、その自重に耐えかねて
落下)する。また、上記落下の原因は空気の流ればかり
ではなく、放電極板6の刺部6aから集塵極板2への火
花放電による衝撃によっても落下する。そのため、集塵
初期に集塵極板2の端部に塵埃aが付着しても、その後
の塵埃の成長は起こらず、また、aの部分もある程度堆
積後、自重に耐えかねて落下する。
Therefore, although the amount of dust adhered is greater than in the conventional case, even if the dust adheres to the dust collecting electrode plate 2, air flows immediately through the opening of the dust collecting electrode plate 2 as shown in FIG. As a result, it is scraped off and peeled off, or even if it adheres, it falls by its own weight before it becomes excessive (it grows faster than the conventional one, but it falls because it cannot bear its own weight). The cause of the drop is not only the flow of air but also the impact from the spark discharge from the pierced portion 6a of the discharge electrode plate 6 to the dust collecting electrode plate 2. Therefore, even if the dust a adheres to the end portion of the dust collecting electrode plate 2 at the initial stage of dust collection, the dust does not grow thereafter, and the portion a is also deposited to some extent and then falls due to its own weight.

【0015】[0015]

【発明の効果】本発明は、以上のように構成したもので
あるから、次のような効果が得られる。すなわち、放電
極板から集塵極板への電流密度の増加による集塵極板へ
の付着集塵量の増加があり、付着した塵埃は成長して大
きくなるものの、開口部を流れる空気により、早期に集
塵極板から剥離して落下する。また、放電極板と集塵極
板間の火花放電による衝撃によっても、付着した塵埃は
落下する。さらに、荷電距離が減少するので、装置全体
が小型化し重量も軽減され、従来と同一効率を得るのに
容積が1/5程度ですむ。また、これら効果に加えて、
間隔調整手段を用いて多段式にしたことによる、従来
(平成6年1月31日出願)の装置全体の組み付け作業
の容易性についての効果を失うこともなく、第1および
第2の間隔調整手段により下流側に行くにしたがって同
一電極間の間隔を狭くしたり、または、下流側に行くに
したがって異種電極間の間隔を短くしたりすることが容
易となり、多段式の構成を十分に活用でき、性能の良い
集塵装置を提供することができる。
Since the present invention is constructed as described above, the following effects can be obtained. That is, there is an increase in the amount of dust collected on the dust collecting electrode plate due to an increase in the current density from the discharge electrode plate to the dust collecting electrode plate, and although the dust that has adhered grows and becomes larger, due to the air flowing through the opening, Peel off the dust collecting electrode plate early and fall. In addition, the attached dust drops due to the impact caused by the spark discharge between the discharge electrode plate and the dust collecting electrode plate. Further, since the charging distance is reduced, the entire apparatus is downsized and the weight is reduced, and the volume is about 1/5 to obtain the same efficiency as the conventional one. In addition to these effects,
The first and second interval adjustments can be performed without losing the effect of the ease of assembling work of the entire device of the related art (filed on January 31, 1994) by using the interval adjusting means in a multi-stage manner. By the means, it becomes easy to narrow the gap between the same electrodes as it goes downstream, or to shorten the gap between different electrodes as it goes downstream, so that the multi-stage configuration can be fully utilized. It is possible to provide a high performance dust collector.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明による実施例の電気集塵装置の要部斜視
図である。
FIG. 1 is a perspective view of a main part of an electrostatic precipitator according to an embodiment of the present invention.

【図2】従来の集塵極板に塵埃が付着する様子を、部分
的に図示したものである。
FIG. 2 is a partial view showing how dust adheres to a conventional dust collecting electrode plate.

【図3】集塵極板に塵埃が付着する様子を微視的にみて
モデル的に描いた図である。
FIG. 3 is a model drawing of a state in which dust adheres to a dust collecting electrode plate, viewed microscopically.

【図4】集塵極板上で電流強度を表すモデルを表す図で
ある。
FIG. 4 is a diagram showing a model representing a current intensity on a dust collecting electrode plate.

【図5】本発明による集塵極板に開口部を設けた実施例
を示す図である。
FIG. 5 is a view showing an embodiment in which an opening is provided in the dust collecting electrode plate according to the present invention.

【図6】本発明による集塵極板に開口部を設けた他の実
施例を示す図である。
FIG. 6 is a view showing another embodiment in which an opening is provided in the dust collecting electrode plate according to the present invention.

【図7】集塵極板に開口部を設けた実施例においての部
分的断面図である。
FIG. 7 is a partial cross-sectional view of an embodiment in which an opening is provided in the dust collecting electrode plate.

【図8】従来の電気集塵装置の要部斜視図である。FIG. 8 is a perspective view of a main part of a conventional electrostatic precipitator.

【図9】本出願の発明者による特許出願中の電気集塵装
置の要部斜視図である。
FIG. 9 is a perspective view of a main part of an electrostatic precipitator currently applied for a patent by the inventor of the present application.

【図10】図9における電気集塵装置の電極板の配置を
平面図である。
10 is a plan view showing the arrangement of electrode plates of the electrostatic precipitator in FIG.

【図11】図9における電気集塵装置の電極板の作用を
説明するための平面図である。
FIG. 11 is a plan view for explaining the action of the electrode plate of the electrostatic precipitator in FIG. 9.

【符号の説明】[Explanation of symbols]

2 集塵極板 2a 開口部を設けた集塵極板 p 開口部 6 放電極板 6a 刺部 7 第1のスペーサー 8 集塵極板群 9 第2のスペーサー 10 放電極板群 2 Dust collecting electrode plate 2a Dust collecting electrode plate provided with opening p Opening 6 Discharge electrode plate 6a Stab part 7 First spacer 8 Dust collecting electrode plate group 9 Second spacer 10 Discharge electrode plate group

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 開口部が設けられた複数の矩形状の集塵
極板を、該集塵極板の平面を垂直にすると共に、互いに
平面を対向させて並列させ、各々の集塵極板の間に第1
の間隔調整手段を介して柵状に固定し、該柵状の集塵極
板群を、気体流路の流れ方向に対して前記平面を平行に
して、複数個間隔を開けて順次設置し、複数の矩形板の
両縁側に刺部を形成した放電極板を、該放電極板の平面
を垂直にすると共に、互いに平面を対向させて並列さ
せ、各々の放電極板の間に第2の間隔調整手段を介して
柵状に固定し、該柵状の放電極板群を、気体流路の流れ
方向に対して前記平面を平行にして、前記集塵極板群の
各間に間隔を開けて配設したことを特徴とする電気集塵
装置。
1. A plurality of rectangular dust collecting electrode plates provided with openings are arranged such that the planes of the dust collecting electrode plates are vertical and the planes are opposed to each other in parallel, and the dust collecting electrode plates are arranged in parallel with each other. First
Is fixed in a fence shape via the interval adjusting means, and the fence-shaped dust collecting electrode plate group is placed in parallel with the plane in parallel to the flow direction of the gas flow path, with a plurality of intervals provided therebetween. A plurality of rectangular plates are formed with barbed portions on both edge sides, and the planes of the discharge electrode plates are made vertical, and the planes are opposed to each other and arranged in parallel, and a second gap is adjusted between the discharge electrode plates. It is fixed in the form of a fence via a means, and the fence-shaped discharge electrode plate group is made parallel to the plane with respect to the flow direction of the gas flow path, with an interval provided between each of the dust collecting electrode plate groups. An electrostatic precipitator characterized by being provided.
【請求項2】 前記集塵極板に設けられた開口部の形状
は、円または長穴であることを特徴とする請求項1記載
の電気集塵装置。
2. The electrostatic precipitator according to claim 1, wherein the shape of the opening provided in the dust collecting electrode plate is a circle or an elongated hole.
【請求項3】 前記集塵極板に設けられた開口部の面積
は、集塵極板の面積に対して10〜50%を占めること
を特徴とする請求項1記載の電気集塵装置。
3. The electrostatic precipitator according to claim 1, wherein the area of the opening provided in the dust collecting electrode plate occupies 10 to 50% of the area of the dust collecting electrode plate.
JP05131294A 1994-02-24 1994-02-24 Electric dust collector Expired - Fee Related JP3427165B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP05131294A JP3427165B2 (en) 1994-02-24 1994-02-24 Electric dust collector

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP05131294A JP3427165B2 (en) 1994-02-24 1994-02-24 Electric dust collector

Publications (2)

Publication Number Publication Date
JPH07232099A true JPH07232099A (en) 1995-09-05
JP3427165B2 JP3427165B2 (en) 2003-07-14

Family

ID=12883409

Family Applications (1)

Application Number Title Priority Date Filing Date
JP05131294A Expired - Fee Related JP3427165B2 (en) 1994-02-24 1994-02-24 Electric dust collector

Country Status (1)

Country Link
JP (1) JP3427165B2 (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH1157531A (en) * 1997-08-21 1999-03-02 Fuji Electric Co Ltd Electric precipitator
AU2008207611B2 (en) * 2007-08-31 2013-01-17 Yoshiyasu Ehara Electric dust collector
CN103586133A (en) * 2013-12-02 2014-02-19 江苏力洁达环保设备工程有限公司 Differential wet electric precipitator
US8967080B2 (en) 2008-02-13 2015-03-03 Tokyo Electron Limited Top plate of microwave plasma processing apparatus, plasma processing apparatus and plasma processing method
KR20210062361A (en) * 2019-11-21 2021-05-31 주식회사 보성알앤디 Electric and magnetic dust collector

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5267075A (en) * 1975-12-02 1977-06-03 Keiichi Hara Electric dust collector
JPH0531399A (en) * 1991-08-02 1993-02-09 Keiichi Hara Electric dust collector
JPH0647310A (en) * 1992-07-28 1994-02-22 Keiichi Hara Electric dust collecting apparatus
JPH07213946A (en) * 1994-01-31 1995-08-15 Keiichi Hara Electrostatic precipitator

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5267075A (en) * 1975-12-02 1977-06-03 Keiichi Hara Electric dust collector
JPH0531399A (en) * 1991-08-02 1993-02-09 Keiichi Hara Electric dust collector
JPH0647310A (en) * 1992-07-28 1994-02-22 Keiichi Hara Electric dust collecting apparatus
JPH07213946A (en) * 1994-01-31 1995-08-15 Keiichi Hara Electrostatic precipitator

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH1157531A (en) * 1997-08-21 1999-03-02 Fuji Electric Co Ltd Electric precipitator
AU2008207611B2 (en) * 2007-08-31 2013-01-17 Yoshiyasu Ehara Electric dust collector
KR101375468B1 (en) * 2007-08-31 2014-03-18 후지 덴키 가부시키가이샤 Electric dust collector
US8967080B2 (en) 2008-02-13 2015-03-03 Tokyo Electron Limited Top plate of microwave plasma processing apparatus, plasma processing apparatus and plasma processing method
CN103586133A (en) * 2013-12-02 2014-02-19 江苏力洁达环保设备工程有限公司 Differential wet electric precipitator
KR20210062361A (en) * 2019-11-21 2021-05-31 주식회사 보성알앤디 Electric and magnetic dust collector

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