JPS6223459A - Electric precipitator - Google Patents

Electric precipitator

Info

Publication number
JPS6223459A
JPS6223459A JP60160627A JP16062785A JPS6223459A JP S6223459 A JPS6223459 A JP S6223459A JP 60160627 A JP60160627 A JP 60160627A JP 16062785 A JP16062785 A JP 16062785A JP S6223459 A JPS6223459 A JP S6223459A
Authority
JP
Japan
Prior art keywords
dust particles
electric field
downstream side
wire mesh
downstream
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.)
Pending
Application number
JP60160627A
Other languages
Japanese (ja)
Inventor
Hiromi Toida
樋田 洋実
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.)
Panasonic Ecology Systems Co Ltd
Original Assignee
Matsushita Seiko 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 Matsushita Seiko Co Ltd filed Critical Matsushita Seiko Co Ltd
Priority to JP60160627A priority Critical patent/JPS6223459A/en
Publication of JPS6223459A publication Critical patent/JPS6223459A/en
Pending legal-status Critical Current

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  • Electrostatic Separation (AREA)

Abstract

PURPOSE:To enhance the collection efficiency of charged dust particles and to make it possible to keep said effiency for a long period of time, by successively and alternately arranging electret filters and metal net like electrodes in this order in the downstream side of a charge part and constituting an electric field between two metal net like electrodes. CONSTITUTION:The dust particles flowing in a charge part where corona discharge is generated between the discharge wires 3 and opposed electrodes 4 are positively charged to be collected by electret filters 6, 8. At this time, an electric field directing from the downstream side to the upstream side has been generated between an upstream side metal net like electrode 7 and a downstream side metal like electrode 9 and the charged dust particles receive force in the reverse direction to pass through the filter 8 at a slow speed and, therefore, collection efficiency is enhanced. Because the polarization of the electret filter 8 is promoted by the electric field, the reduction of charge due to the adhesion of dust particles and the mutual negation of charge is reduced and high efficiency can be kept.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、粉塵粒子を荷電して捕集する電気集塵装置に
関するものである。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to an electrostatic precipitator that charges and collects dust particles.

従来の技術 従来の電気集塵装置は第3図に示すような構成であった
。第3図において電気集塵装置外枠11の内部に空気流
12に対して上流側に荷電部16と下流側にエレクトレ
ットフィルタ16が設けられている。荷電部15ば、放
電線13と対向極14とから成り、放電a13と対向電
極14との間は直流高圧電源17を備え、放電線13に
(+)、対向極14に(−)が接続されている(特開昭
57−16856号公報)。
Prior Art A conventional electrostatic precipitator has a configuration as shown in FIG. In FIG. 3, inside the electrostatic precipitator outer frame 11, a charging section 16 is provided on the upstream side with respect to the air flow 12, and an electret filter 16 is provided on the downstream side. The charging section 15 consists of a discharge wire 13 and a counter electrode 14, and a DC high voltage power supply 17 is provided between the discharge wire 13 and the counter electrode 14, and (+) is connected to the discharge wire 13 and (-) is connected to the counter electrode 14. (Japanese Unexamined Patent Publication No. 16856/1983).

上記構成において、粉塵粒子を含む空気流12が送風機
等により、荷電部15に流入すると荷電部16にオイテ
放電線13K(+)、対向極14に(−)の直流高圧電
圧が印加されているため、(+)のコロナ放電を生じ、
このコロナ放電によって粉塵粒子は(+)に荷電される
In the above configuration, when the air flow 12 containing dust particles flows into the charging section 15 by a blower or the like, a high DC voltage of Oite discharge wire 13K (+) is applied to the charging section 16 and (-) is applied to the counter electrode 14. Therefore, (+) corona discharge occurs,
The dust particles are charged (+) by this corona discharge.

この荷電された粉塵粒子は、下流側に配置したエレクト
レットフィルタ16のp材の静電気力により引きつけら
れ、粉塵粒子が捕集される。
These charged dust particles are attracted by the electrostatic force of the P material of the electret filter 16 disposed on the downstream side, and the dust particles are collected.

発明が解決しようとする問題点 しかしながら従来の構成では、エレクトレットフィルタ
16の戸材に荷電された粉塵粒子が付着すると粉塵粒子
の電荷と、エレクトレットフィルタ16の電荷とが打ち
消し合って静電気力が弱まり捕集効率の低下を生じる。
Problems to be Solved by the Invention However, in the conventional configuration, when charged dust particles adhere to the door material of the electret filter 16, the electric charge of the dust particles and the electric charge of the electret filter 16 cancel each other out, weakening the electrostatic force and making it impossible to capture the dust particles. This results in a decrease in collection efficiency.

すなわち初期は効率が非常にすぐれているが、捕集が進
むにつれて効率が低下するという問題点があった・ i ftエレクI・レットフィルタ16は、その密度を
あまり高くできないという性質があり、細かい粒子に対
しては機械的なフィルタとしての捕集効率が低いという
問題点もあった・ 本発明はこのような問題点を解決するもので、高効率を
維持し、粉塵の集塵効率の低下をおさえ、寿命を伸ばす
ことを目的とするものである。
In other words, the efficiency is very high at the beginning, but as the collection progresses, the efficiency decreases. There was also the problem that the collection efficiency of mechanical filters was low for particles.The present invention solves this problem by maintaining high efficiency and reducing the dust collection efficiency. The purpose is to suppress this and extend lifespan.

問題点を解決するだめの手段 この問題点を解決するため、本発明の電気集塵装置は、
空気の流れに対して上流側に放電線と対向極板と直流高
圧電源からなる荷電部を設け、下流側には2組のエレク
トレットフィルタと金網状電極を上流側から見て、エレ
クトレットフィルタ。
Means for Solving the Problem In order to solve this problem, the electrostatic precipitator of the present invention has the following features:
A charging section consisting of a discharge wire, a counter electrode plate, and a DC high-voltage power supply is provided on the upstream side of the air flow, and two sets of electret filters and wire mesh electrodes are provided on the downstream side, as seen from the upstream side.

金網状電極の順に交互に配置し、前記放電線と下流側金
網状電極、対向極板と上流側金網状電極とをそれぞれ同
電位とした構成である。
The wire mesh electrodes are arranged alternately in this order, and the discharge wire and the downstream wire mesh electrode, and the counter electrode plate and the upstream wire mesh electrode are set to the same potential.

作  用 この構成により、荷電部で荷電された粉塵粒子は上流側
エレクトレットフィルタで捕集され、一部捕集されなか
った粒子も、2つの金網状電極により構成される電界中
にある下流側エレクトレットフィルタに捕集され、高い
効率が維持され、寿命も長くなる。
With this configuration, dust particles charged in the charging section are collected by the upstream electret filter, and some of the particles that are not collected are also collected by the downstream electret filter in the electric field formed by the two wire mesh electrodes. It is collected by the filter, maintaining high efficiency and extending its life.

実施例 以下、本発明の一実施例を第1図および第2図にもとづ
いて説明する。
EXAMPLE Hereinafter, an example of the present invention will be described based on FIGS. 1 and 2.

第1図において、外枠1の内部に、空気流2に対して上
流側に放電線3と対向極板4とがら成る荷電部5を設け
ている。下流側には上流側から順にエレクトレットフィ
ルタ6、上流側金網状電極7、下流側エレクトレットフ
ィルタ8.下流側金網状電極9が配置されている。外枠
1の外部には直流高圧電源10を設け、その直流高圧電
源10の(+)側は放電M3と下流側金網状電極9に接
続され、(−)側は対向極板4と前記上流側金網状電極
7に接続されている。
In FIG. 1, a charging section 5 consisting of a discharge wire 3 and a counter electrode plate 4 is provided inside the outer frame 1 on the upstream side with respect to the air flow 2. On the downstream side, in order from the upstream side, there is an electret filter 6, an upstream wire mesh electrode 7, and a downstream electret filter 8. A downstream wire mesh electrode 9 is arranged. A DC high-voltage power supply 10 is provided outside the outer frame 1, and the (+) side of the DC high-voltage power supply 10 is connected to the discharge M3 and the downstream wire mesh electrode 9, and the (-) side is connected to the opposing electrode plate 4 and the upstream wire mesh electrode 9. It is connected to the side wire mesh electrode 7.

上記構成において、粉塵粒子を含む空気流2が送風機等
により前記荷電部5に流入すると、前記荷電部5では、
前記放電線3と前記対向極板4との間にコロナ放電が発
生しておυ、このコロナ放電により粉塵粒子がプラスに
荷電される。荷電された粒子は、分極されている上流側
エレクトレットフィルタ6に静電気的な引力により吸着
され捕集される。前記上流側エレクトレットフィルタ6
により粉塵粒子の大半は捕集されるが一部捕集されずに
、通過する粉塵粒子は同様にして前記下流側エレクトレ
ットフィルタ8で捕集される。このとき前記上流側金網
状電極7と前記下流側金網状電極9との間に、前記直流
高圧電源10により高電圧がかかり電界が生じている。
In the above configuration, when the airflow 2 containing dust particles flows into the charging section 5 by a blower or the like, the charging section 5:
A corona discharge occurs between the discharge wire 3 and the counter electrode plate 4, and the dust particles are positively charged by this corona discharge. The charged particles are attracted and collected by the polarized upstream electret filter 6 by electrostatic attraction. The upstream electret filter 6
Most of the dust particles are collected by this, but some of the dust particles that pass through are collected by the downstream electret filter 8 in the same way. At this time, a high voltage is applied between the upstream wire mesh electrode 7 and the downstream wire mesh electrode 9 by the DC high voltage power supply 10, creating an electric field.

この電界には、下流側から上流側に向いており、プラス
に電荷された粉塵粒子は、空気流2の方向と逆方向のカ
を受は空気流2の速度より遅い速度で前記下流側エレク
トレットフィルタ8を通過するので捕集効率は電界の生
じていない場合に較べ向上する。
This electric field is oriented from the downstream side to the upstream side, and the positively charged dust particles receive a force in the opposite direction to the direction of the air flow 2, and the downstream electrets move at a speed slower than the speed of the air flow 2. Since it passes through the filter 8, the collection efficiency is improved compared to when no electric field is generated.

また、前記電界中に前記下流側エレクトレットフィルタ
8が配置されているため、エレクトレットフィルタの分
極が促進されるため、粉塵粒子が付着してエレクトレッ
トフィルタの電荷がうち消し合って減少することが少な
く、高い効率を維持することが可能である。
Furthermore, since the downstream electret filter 8 is disposed in the electric field, the polarization of the electret filter is promoted, so that the charges on the electret filter are less likely to be reduced by canceling each other out due to the attachment of dust particles. It is possible to maintain high efficiency.

第2図は、本発明による電気集塵装置と従来の電気集塵
装置との集塵効率と比較したグラフである。このグラフ
に示されるように、本発明品は従来品に較べ初期集塵効
率が非常に高い(本発明品99.97%、従来品96係
)。また、タバコ2Q○本分の煙を集塵した後の効率も
本発明品ではほとんど低下していない(99,5% )
のに比較して従来品では73係前後にまで低下している
FIG. 2 is a graph comparing the dust collection efficiency of the electrostatic precipitator according to the present invention and a conventional electrostatic precipitator. As shown in this graph, the product of the present invention has a much higher initial dust collection efficiency than the conventional product (99.97% for the product of the present invention, 96% for the conventional product). In addition, the efficiency of the product after collecting dust for 2Q cigarettes is almost unchanged (99.5%).
Compared to that of the conventional product, it has decreased to around 73 coefficients.

以上のように本発明品が高効率であり、しかもその高効
率を長期間維持していることがわかる。
As described above, it can be seen that the product of the present invention has high efficiency and maintains this high efficiency for a long period of time.

発明の効果 以上のように本発明によれば、エレクトレットフィルタ
と金網状電極と交互に配置することにより、エレクトレ
ットフィルタに電界を与え分極を促進し捕集効率を上げ
、しかもその効率を長期間維持することができる。また
電界により荷電粉塵粒子の速度を減少させエレクトレッ
トフィルタへの吸着性を向上させることができるという
効果が得られる。
Effects of the Invention As described above, according to the present invention, by alternately arranging the electret filter and the wire mesh electrode, an electric field is applied to the electret filter to promote polarization and increase the collection efficiency, and the efficiency can be maintained for a long period of time. can do. Further, the electric field can reduce the speed of charged dust particles and improve adsorption to the electret filter.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の一実施例による電気集塵装置の構成を
示す断面図、第2図は本発明と従来の電気集塵装置との
捕集効率の経時変化を示すグラフ、第3図は従来の電気
集塵装置の構成を示す断面図である。 3・・・・・・放電線、4・・・・・・対向極板、5・
・・・・・荷電部、6・・・・・・上流側エレクトレッ
トフィルタ、7・・・・・・上流側金網状電極、8・・
・・・下流側エレクトレットフィルタ、9・・・・・−
下流側金網状電極、10・・・・・・直流高圧電源。 代理人の氏名 弁理士 中 尾 敏 男 ほか1名5−
−−riT才部
FIG. 1 is a cross-sectional view showing the configuration of an electrostatic precipitator according to an embodiment of the present invention, FIG. 2 is a graph showing changes over time in collection efficiency between the present invention and a conventional electrostatic precipitator, and FIG. 3 1 is a sectional view showing the configuration of a conventional electrostatic precipitator. 3...Discharge wire, 4...Counter electrode plate, 5...
...Charging section, 6... Upstream electret filter, 7... Upstream wire mesh electrode, 8...
...Downstream electret filter, 9...-
Downstream side wire mesh electrode, 10... DC high voltage power supply. Name of agent: Patent attorney Toshio Nakao and 1 other person5-
--riT Saibu

Claims (1)

【特許請求の範囲】[Claims] 空気の流れに対して上流側に放電線、対向極板および直
流高圧電源からなる荷電部を設け、下流側には上流側か
ら見てエレクトレットフィルタ、金網状電極の順に交互
に配置し、前記放電線と下流側金網状電極、および前記
対向極板と上流側金網状電極とをそれぞれ同電位とした
電気集塵装置。
A charging section consisting of a discharge wire, a counter electrode plate, and a DC high-voltage power source is provided on the upstream side of the air flow, and an electret filter and a wire mesh electrode are arranged alternately on the downstream side in this order as viewed from the upstream side. An electrostatic precipitator in which the electric wire and the downstream wire mesh electrode, and the opposing electrode plate and the upstream wire mesh electrode are set at the same potential.
JP60160627A 1985-07-19 1985-07-19 Electric precipitator Pending JPS6223459A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60160627A JPS6223459A (en) 1985-07-19 1985-07-19 Electric precipitator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60160627A JPS6223459A (en) 1985-07-19 1985-07-19 Electric precipitator

Publications (1)

Publication Number Publication Date
JPS6223459A true JPS6223459A (en) 1987-01-31

Family

ID=15719018

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60160627A Pending JPS6223459A (en) 1985-07-19 1985-07-19 Electric precipitator

Country Status (1)

Country Link
JP (1) JPS6223459A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100890199B1 (en) 2007-06-27 2009-03-25 주식회사 애니텍 Electrostatic Oil Mist Space Filter Trap Using Pre-Charge and Metal Fiber Layer
WO2012046309A1 (en) * 2010-10-06 2012-04-12 Necディスプレイソリューションズ株式会社 Dust-removing device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100890199B1 (en) 2007-06-27 2009-03-25 주식회사 애니텍 Electrostatic Oil Mist Space Filter Trap Using Pre-Charge and Metal Fiber Layer
WO2012046309A1 (en) * 2010-10-06 2012-04-12 Necディスプレイソリューションズ株式会社 Dust-removing device
US8932380B2 (en) 2010-10-06 2015-01-13 Nec Display Solutions, Ltd. Dust removal device

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