JPS60212255A - Electrostatic filter apparatus - Google Patents

Electrostatic filter apparatus

Info

Publication number
JPS60212255A
JPS60212255A JP59070337A JP7033784A JPS60212255A JP S60212255 A JPS60212255 A JP S60212255A JP 59070337 A JP59070337 A JP 59070337A JP 7033784 A JP7033784 A JP 7033784A JP S60212255 A JPS60212255 A JP S60212255A
Authority
JP
Japan
Prior art keywords
filter
collection
charged
collection efficiency
dust
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
JP59070337A
Other languages
Japanese (ja)
Inventor
Hiroshi Umehara
梅原 博
Yoshikazu Tashiro
義和 田代
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
Panasonic Holdings Corp
Original Assignee
Matsushita Seiko Co Ltd
Matsushita Electric Industrial 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, Matsushita Electric Industrial Co Ltd filed Critical Matsushita Seiko Co Ltd
Priority to JP59070337A priority Critical patent/JPS60212255A/en
Publication of JPS60212255A publication Critical patent/JPS60212255A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To supplement the lowering in the collection efficiency of a fibrous charged filter, in an electrostatic filter apparatus, by forming the fibrous charged filter in a two-layered structure and arranging a charge part to the upstream side thereof. CONSTITUTION:Dirty air is introduced into a duct 10 from an arrow C and passes through a charge part 11 consisting of a discharge electrode 12 and an earthing electrode 13. Plus corona discharge is performed between the discharge electrode 12 and the earthing electrode 13 to charge dust while the charged dust is introduced into a collection part 20 and collected by the upstream side filter 15 or downstream side filter 16 of a fibrous charged filter brought to an electret state. Because two filters are used as mentioned above, the downstream side filter performs mechanical collection when the collection efficiency of the upstream side filter is lowered and the upstream side filter performs mechanical collection when the efficiency of the downstream side filter is lowered and collection efficiency is kept high as a whole.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は捕集部に沖材としてエレクトレット化した繊維
状帯電フィルタを二層にして使用するクリーンルーム等
に利用する静電フィルタ装置に係わるものである。
[Detailed Description of the Invention] Industrial Field of Application The present invention relates to an electrostatic filter device used in clean rooms, etc., in which a two-layer fibrous charged filter made of electret material is used in the collection section. .

従来例の構成とその問題点 空気など気体中の粉じんを除去するための集じん機とし
ては、過去から数多くの形式のものかある。その捕集部
に炉材としてエレクトレット化した繊維状帯電フィルタ
を使用することは、すでに公知である。その代表的な構
成を第1図および第2図に示す。第1図は、円形又は矩
形筒状ダクト1の内部に、前記繊維状帯電フィルタ2を
設置し汚染空気は矢印aから導入され、繊維状帯電フィ
ルタ2を通過することにより清浄化され、矢印すの方向
に排出される。第2図は、前記繊維状帯電フィルタ2の
上流側に、汚染空気の粉じんを電気的に荷電する荷電部
3を設け、前記荷電部3は放電極4と接地極5をダクト
1の内部に等間隔に配設し、放電極4と接地極5の両端
に直流高圧電源6を接続する構成である。
Conventional configurations and their problems There have been many types of dust collectors for removing dust from gases such as air. It is already known to use an electret fibrous charged filter as a furnace material in the collection section. Its typical configuration is shown in FIGS. 1 and 2. FIG. 1 shows that the fibrous charged filter 2 is installed inside a circular or rectangular cylindrical duct 1, and contaminated air is introduced from arrow a and is purified by passing through the fibrous charged filter 2. is ejected in the direction of In FIG. 2, a charging section 3 for electrically charging dust in contaminated air is provided upstream of the fibrous charged filter 2, and the charging section 3 connects a discharge electrode 4 and a ground electrode 5 to the inside of the duct 1. They are arranged at equal intervals, and a DC high voltage power source 6 is connected to both ends of the discharge electrode 4 and the ground electrode 5.

上記構成において、汚染空気の粉じんは荷電部3におい
て荷電され荷電された粉じんは、繊維状帯電フィルタ2
により捕集されることとなる。また、第1図および第2
図の捕集効率は、荷電部3を有する第2図の構成の方が
良くなる。ところが、その捕集効率の経時変化は、第3
図に示すように、初期から集じんが進むに従いダウンし
てゆく0この原因は、繊維状帯電フィルタ2の繊維の表
面に粉じんが付着しその静電気効果が弱まってゆくため
である。ただし、その後、ある一定のところまでダウン
すると再び上昇することになる。これは、静電気効果で
はなく、機械的捕集効果によるものである。
In the above configuration, the dust of contaminated air is charged in the charging section 3, and the charged dust is transferred to the fibrous charged filter 2.
It will be collected by. Also, Figures 1 and 2
The collection efficiency shown in the figure is better in the configuration shown in FIG. 2 having the charging section 3. However, the change in collection efficiency over time is
As shown in the figure, as the dust collection progresses, it decreases from the initial stage. The reason for this is that dust adheres to the surface of the fibers of the fibrous charged filter 2, and the electrostatic effect weakens. However, after that, if it drops to a certain point, it will rise again. This is due to mechanical trapping effects rather than electrostatic effects.

以上の説明から明らかなように、繊維状帯電フィルタは
クリーンルーム等の高清浄度を必要とするところでは捕
集効率がダウンするため、清浄度を維持することが困難
であるという欠点を有していた0 発明の目的 そこで本発明は、繊維状帯電フィルタの捕集効率のダウ
ンを補ない、高清浄度を必要とするところへ応用するこ
とを目的とする。
As is clear from the above explanation, fibrous charged filters have the disadvantage that in areas that require high cleanliness, such as clean rooms, the collection efficiency decreases, making it difficult to maintain cleanliness. OBJECT OF THE INVENTION Therefore, the present invention aims to compensate for the decrease in collection efficiency of the fibrous charged filter and to apply it to places where high cleanliness is required.

発明の構成 この目的を達成するため本発明は、繊維状帯電フィルタ
を2層にし、その上流側に荷電部を配設することにより
、上流側の繊維状帯電フィルタの捕集効率ダウンを下流
側の繊維状帯電フィルタの捕集効率で補ない下流側の繊
維状帯電フィルタの捕集効率ダウンの際には、上流側の
繊維状帯電フィルタで捕集効率を補ない全体として、捕
集効率の低下を補なうようにしたものである0実施例の
説明 以下本発明の一実施例を添付図面に従い説明する。第4
図において、1oは円形又は矩形筒状のダクトで内部に
汚染空気の中に含まれる粉じんを荷電するための荷電部
11とその下流側に捕集部2oを有する。荷電部11は
、放電極12と接地極13が前記ダクト10内に均一に
配設されている。放電極12と接地極13の間には、直
流高電圧電源14が接続されている0下流側にある捕集
部2oは、エレクトレット化した繊維状帯電フィルタを
用いた、上流側フィルタ16と下流側フィルタ16によ
り構成されている0 上記構成において、汚染空気は矢印Cの方向よりダク)
10の内部に導入される。汚染空気の中の粉じんはまず
最初に荷電部11を通過する0荷電部11では、放電極
12と接地極13との間でプラスコロナ放電を行なって
いるため、粉じんは荷電部11を通過する間にプラスに
荷電されることになる。次に荷電された粉じんは、捕集
部20に導入される。捕集部20では、エレクトレット
化した繊維状帯電フィルタの上流側フィルタ16又は下
流側フィルタ16によシ捕集される。その捕集効率は、
第6図に示す毎く得られるものである。曲線eは、上流
側フィルタ16の捕集効率であり初期よp e/まで、
集じんが進むにつれて捕集効率が低下してゆく。この原
因は前述の毎く繊維状帯電フィルタの繊維の表面に粉じ
んが付着し、そのだめ静電効果が弱まってゆくための低
下である。e′をすぎると粉じん付着による通過空隙の
減少による機械的捕集効果により捕集効率の増加が生ず
る。問題となるのは、一層の時にはe′まで低下するこ
とであシ、これを補なうため下流側フィルタ16を設け
ている。下流側フィルタ16の補集効率の変化は、曲線
fで示される。上流側フィルタ16の効果により、粉じ
ん通過量が少ないため捕集効率の低下は、曲線eに比べ
て遅くなめらかになり、最低下点f′は時間遅れが生じ
る。下流側フィルタ16の効率低下時は上流側フィルタ
16の機械的捕集により効率低下を防ぐ。このため上流
側フィルタ15と下流側フィルタ16の合成した効果に
よシ捕集部20での捕集効率は、曲線qの毎くなり上流
側フィルタ15の捕集効率低下時には下流側フィルタ1
6で補ない、下流側フィルタ16の捕集効率の低下時に
は上流側フィルタ15によシ補ない、全体としては捕集
効率の高効率化を維持することができるものとなる。
Structure of the Invention In order to achieve this object, the present invention has two layers of fibrous charged filters, and a charging section is provided on the upstream side of the fibrous charged filter, thereby reducing the collection efficiency of the fibrous charged filter on the upstream side. When the collection efficiency of the fibrous charged filter on the downstream side decreases, the collection efficiency of the fibrous charged filter on the upstream side is not compensated for. DESCRIPTION OF EMBODIMENT 0 DESCRIPTION OF THE EMBODIMENTS DESCRIPTION OF EMBODIMENTS DESCRIPTION OF EMBODIMENTS OF THE INVENTION An embodiment of the present invention will be described below with reference to the accompanying drawings. Fourth
In the figure, 1o is a circular or rectangular cylindrical duct which has inside thereof a charging section 11 for charging dust contained in contaminated air and a collection section 2o on the downstream side thereof. In the charging section 11, a discharge electrode 12 and a ground electrode 13 are uniformly arranged within the duct 10. A DC high-voltage power supply 14 is connected between the discharge electrode 12 and the ground electrode 13. The collecting section 2o on the downstream side is connected to an upstream filter 16 using an electret fibrous charged filter. In the above configuration, the contaminated air is ducted from the direction of arrow C).
10 is introduced inside. Dust in contaminated air first passes through the charging section 11. In the zero charging section 11, positive corona discharge is occurring between the discharge electrode 12 and the grounding electrode 13, so the dust passes through the charging section 11. During this period, it becomes positively charged. Next, the charged dust is introduced into the collection section 20. In the collection section 20, the particles are collected by the upstream filter 16 or the downstream filter 16, which is an electret fibrous charged filter. Its collection efficiency is
This is what is obtained as shown in FIG. Curve e is the collection efficiency of the upstream filter 16, from the initial stage to p e/.
As the dust collection progresses, the collection efficiency decreases. The reason for this is, as mentioned above, that dust adheres to the surface of the fibers of the fibrous charged filter, which weakens the electrostatic effect. Beyond e', the collection efficiency increases due to the mechanical collection effect due to the reduction of the passing gap due to dust adhesion. The problem is that in the worst case, the value drops to e', and to compensate for this, the downstream filter 16 is provided. The change in collection efficiency of the downstream filter 16 is shown by a curve f. Due to the effect of the upstream filter 16, the amount of dust passing through is small, so the reduction in collection efficiency is slower and smoother than in the curve e, and the lowest point f' is reached with a time delay. When the efficiency of the downstream filter 16 decreases, the efficiency decrease is prevented by mechanical collection of the upstream filter 16. Therefore, due to the combined effect of the upstream filter 15 and the downstream filter 16, the collection efficiency in the collection section 20 is as shown by the curve q, and when the collection efficiency of the upstream filter 15 decreases, the downstream filter 1
When the collection efficiency of the downstream filter 16 decreases, the upstream filter 15 does not compensate, and the collection efficiency as a whole can be maintained at a high level.

発明の効果 以上の説明からも明らかなように、本発明は捕集部にエ
レクトレット化した繊維状帯電フィルタを上流、下流の
二層にして互いの捕集効率の低下を補なうようにしたの
ものであるから捕集効率の高効率化を維持することがで
きるという効果が得られるものである。
Effects of the Invention As is clear from the above explanation, the present invention uses two layers of electret fibrous charged filters in the collection section, one upstream and one downstream, to compensate for each other's decrease in collection efficiency. Since it is a material, it is possible to maintain a high level of collection efficiency.

【図面の簡単な説明】 第1図および第2図は、従来の静電フィルタの断面図、
第3図は従来の静電フィルタの捕集効率を示すグラフ、
第4図は本発明の静電フィルタの一実施例を示す断面図
、第6図は本発明の静電フィルタによる捕集効率を示す
グラフである011・・・・・・荷電部、12・・・・
・・放電極、13・・・・・・接地極、14・・・・・
・直流高圧電源、15・・・・・・繊維状帯電フィルタ
(上流側フィルタ)、16・・・・・・繊維状帯電フィ
ルタ(下流側フィルタ)、2o・・・・・・捕集部0
[Brief Description of the Drawings] Figures 1 and 2 are cross-sectional views of conventional electrostatic filters;
Figure 3 is a graph showing the collection efficiency of conventional electrostatic filters.
FIG. 4 is a sectional view showing an embodiment of the electrostatic filter of the present invention, and FIG. 6 is a graph showing the collection efficiency of the electrostatic filter of the present invention. ...
...Discharge electrode, 13...Ground electrode, 14...
・DC high voltage power supply, 15... Fibrous charged filter (upstream filter), 16... Fibrous charged filter (downstream filter), 2o... Collection section 0

Claims (2)

【特許請求の範囲】[Claims] (1)筒状ダクト内部に、エレクトレット化した繊維状
帯電フィルタを上流と下流の二層に配設した静電フィル
タ装置。
(1) An electrostatic filter device in which electret fibrous charged filters are arranged in two layers, upstream and downstream, inside a cylindrical duct.
(2) エレクトレット化した二層の繊維状帯電フィル
タの上流側に粉じんを荷電する荷電部を有し前
(2) A charging section that charges dust is provided on the upstream side of the two-layer electret fibrous charged filter.
JP59070337A 1984-04-09 1984-04-09 Electrostatic filter apparatus Pending JPS60212255A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59070337A JPS60212255A (en) 1984-04-09 1984-04-09 Electrostatic filter apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59070337A JPS60212255A (en) 1984-04-09 1984-04-09 Electrostatic filter apparatus

Publications (1)

Publication Number Publication Date
JPS60212255A true JPS60212255A (en) 1985-10-24

Family

ID=13428500

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59070337A Pending JPS60212255A (en) 1984-04-09 1984-04-09 Electrostatic filter apparatus

Country Status (1)

Country Link
JP (1) JPS60212255A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100503759B1 (en) * 2002-09-17 2005-07-26 삼성전자주식회사 Electric precipitator

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100503759B1 (en) * 2002-09-17 2005-07-26 삼성전자주식회사 Electric precipitator

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