JP2008104937A - Electric dust collector - Google Patents
Electric dust collector Download PDFInfo
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- JP2008104937A JP2008104937A JP2006289497A JP2006289497A JP2008104937A JP 2008104937 A JP2008104937 A JP 2008104937A JP 2006289497 A JP2006289497 A JP 2006289497A JP 2006289497 A JP2006289497 A JP 2006289497A JP 2008104937 A JP2008104937 A JP 2008104937A
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- discharge
- electrode plate
- side edge
- plate
- electrostatic precipitator
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/34—Constructional details or accessories or operation thereof
- B03C3/40—Electrode constructions
- B03C3/45—Collecting-electrodes
- B03C3/47—Collecting-electrodes flat, e.g. plates, discs, gratings
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/34—Constructional details or accessories or operation thereof
- B03C3/40—Electrode constructions
- B03C3/41—Ionising-electrodes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C2201/00—Details of magnetic or electrostatic separation
- B03C2201/10—Ionising electrode has multiple serrated ends or parts
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- Electrostatic Separation (AREA)
Abstract
Description
本発明は電気集塵機に関し、特に、捕集部に向かう粉塵粒子を帯電させるための帯電部における極板形状を改良することによって寿命の延長と運転コストの低減を図った電気集塵機に関する。 The present invention relates to an electrostatic precipitator, and more particularly, to an electrostatic precipitator that is intended to extend the life and reduce the operating cost by improving the electrode plate shape in a charging unit for charging dust particles toward a collecting unit.
電気集塵機は一般に帯電部と集塵部を備え、帯電部に形成された放電雰囲気中に汚染空気を流入させ当該汚染空気中に含まれる粉塵粒子等を帯電させて、これを後段の集塵部で吸引捕集して、清浄空気として流出させている。 An electrostatic precipitator generally includes a charging unit and a dust collecting unit, and flows contaminated air into a discharge atmosphere formed in the charging unit to charge dust particles and the like contained in the contaminated air. It is sucked and collected with the air and is discharged as clean air.
上記帯電部には従来、接地された極板に対向させて、直流負電圧を印加した放電線を設けて、放電線と接地極板との間にコロナ放電を生じさせ、当該コロナ放電雰囲気中に汚染空気を通過させて粉塵粒子等を帯電させていた。ところで、放電線は、比較的低い投入電力で高い除塵効率を得ることができるという利点があるが、断線等により寿命が短いという問題があった。 Conventionally, the charging unit is provided with a discharge wire to which a negative DC voltage is applied so as to face a grounded electrode plate, and a corona discharge is generated between the discharge wire and the ground electrode plate. The polluted air was passed through to charge the dust particles. By the way, although the discharge wire has an advantage that high dust removal efficiency can be obtained with relatively low input power, there is a problem that the life is short due to disconnection or the like.
そこで、例えば特許文献1では、放電線に代えて接地極板に平行に放電極板を設けて、当該放電極板の側縁に突起長の異なる三角突起を交互に複数形成することにより、除塵効率を低下させることなく、寿命の延長を図った電気集塵機が提案されている。
しかし、上記公報記載の従来の電気集塵機では、除塵効率を高く維持しようとすると投入電力が大きくなって、運転コストがかかるという問題があった。 However, the conventional electrostatic precipitator described in the above publication has a problem that the input power becomes large and the operation cost increases when it is attempted to maintain high dust removal efficiency.
そこで、本発明はこのような課題を解決するもので、投入電力を低くしても除塵効率を高く維持できるとともに、寿命のさらなる延長も実現した電気集塵機を提供することを目的とする。 Therefore, the present invention solves such a problem, and an object of the present invention is to provide an electrostatic precipitator that can maintain high dust removal efficiency even when input power is lowered and that further extends the life.
上記目的を達成するために、本第1発明では、対向させて互いに平行に設けた一対の極板(1,2)間に放電雰囲気を生じさせて、ここを通過する粒子を帯電させる帯電部(EP)を備えた電気集塵機において、上記極板の一方(1)を、少なくとも一方の側縁(12,13)に長手方向へ間隔をおいて複数の矩形の放電突起(11)を形成した長尺板体で構成する。 In order to achieve the above object, according to the first aspect of the present invention, a charging unit that generates a discharge atmosphere between a pair of opposed electrode plates (1, 2) provided in parallel to each other and charges particles passing therethrough In the electrostatic precipitator provided with (EP), a plurality of rectangular discharge protrusions (11) are formed on one (1) of the electrode plates at intervals in the longitudinal direction on at least one side edge (12, 13). It consists of a long plate.
本第1発明においては、他方の極板との間の放電が、一方の極板における矩形の放電突起の、一対の直角コーナ部でそれぞれ生じるから、均一かつ密な放電雰囲気が生成され、汚染空気の粉塵粒子等が確実に帯電させられて後段の集塵部で吸引捕集される。これにより除塵効率が高く維持されるとともに、放電電流を小さくできるから電気集塵機への投入電力を少なくできる。また、矩形の放電突起は二箇所の放電部があるため従来の三角突起に比して放電部一箇所当たりの放電量が少なくなり消耗が少ないから、寿命も長くできる。 In the first invention, the discharge between the other electrode plate occurs at the pair of right-angled corner portions of the rectangular discharge protrusions on the one electrode plate, so that a uniform and dense discharge atmosphere is generated and contamination occurs. Air dust particles and the like are reliably charged and sucked and collected by the dust collecting section at the subsequent stage. As a result, the dust removal efficiency is maintained high, and the discharge current can be reduced, so that the input power to the electric dust collector can be reduced. In addition, since the rectangular discharge protrusion has two discharge portions, the discharge amount per discharge portion is reduced and consumption is reduced as compared with the conventional triangular protrusion, so that the life can be extended.
本第2発明では、上記放電突起(11)を長尺板体の両側縁(12,13)に形成するとともに、その形成位置を一方の側縁と他方の側縁で互いに長手方向へずらす。 In the second aspect of the invention, the discharge protrusions (11) are formed on both side edges (12, 13) of the long plate body, and the positions of the discharge protrusions (11, 13) are shifted from each other in the longitudinal direction between one side edge and the other side edge.
本第2発明においては、均一かつ密なコロナ放電雰囲気をより効果的に生じさせることができるから、さらなる除塵効率の向上と投入電力の減少が実現される。 In the second aspect of the invention, a uniform and dense corona discharge atmosphere can be generated more effectively, so that further improvement of dust removal efficiency and reduction of input power are realized.
なお、上記カッコ内の符号は、後述する実施形態に記載の具体的手段との対応関係を示すものである。 In addition, the code | symbol in the said parenthesis shows the correspondence with the specific means as described in embodiment mentioned later.
以上のように、本発明の電気集塵機によれば、投入電力を低くしても除塵効率を高く維持することができ、しかも寿命を延長することができる。 As described above, according to the electric dust collector of the present invention, the dust removal efficiency can be maintained high even if the input power is lowered, and the life can be extended.
図1には帯電部EPの概念的な構造を示す。図1において、帯電部EPには、平板状の接地極板2に対し平行に対向させて放電極板1が設けてある。放電極板1は長板体で、その両側縁には長手方向へ一定間隔で多数の放電突起11が形成されている。放電突起11は図2に示すように、先端に左右一対の直角のコーナ部111を有する矩形状に成形されている。このような放電極板1に直流負電圧を印加すると、上記各コーナ部111と接地極板2との間でそれぞれコロナ放電が生じて、接地極板2との間に均一かつ密なコロナ放電雰囲気が生成される。
FIG. 1 shows a conceptual structure of the charging unit EP. In FIG. 1, the
これにより、汚染空気の粉塵粒子等が確実に帯電させられて後段の集塵部で吸引捕集される。なお、本実施形態では図3に示すように、長板体の放電極板1の、一方の側縁12(図1)の放電突起11を他方の側縁13の放電突起11と互いに位置をずらして形成してあるから、均一かつ密なコロナ放電雰囲気をより効果的に生じさせることができる。また、先が尖った従来の三角状放電突起に比して、矩形状の放電突起11は矩形の放電突起は二箇所の放電部(コーナ部111)があるため従来の三角突起に比して放電部一箇所当たりの放電量が少なくなり消耗が少ないから寿命が長くなる。
As a result, the dust particles of the contaminated air are reliably charged and sucked and collected by the subsequent dust collecting section. In the present embodiment, as shown in FIG. 3, the
図2における矩形状放電突起11の幅Wを3mm、高さHを10mmとし、これら放電突起11の間隔Dを15mmとしたタイプI放電極板と、幅W、高さHをタイプIと同一にし、放電突起の間隔Dを20mmとしたタイプIIの放電極板について、間隔を10mm、三角突起の高さを交互に10mm、5mmとした従来の放電極板と比較して、帯電部への印加電圧と電流の関係、および帯電部への印加電圧と除塵効率の関係を調べたものをそれぞれ、図4、図5に示す。なお、図中、線xはタイプI極板、線yはタイプII極板、線zは従来極板のものである。
The type I discharge electrode plate in which the width W of the
図4より明らかなように、各印加電圧について帯電部に流れる電流は、従来の極板に対しタイプI極板やタイプII極板ではいずれも小さく、したがって電気集塵機への投入電力を低くすることができる。この状態で、各帯電部印加電圧に対する除塵効率は、処理風速13m/sでは、タイプI極板(線x)、タイプII極板(線y)いずれも従来極板(線z)と殆ど変わらない(図5(1))。処理風速が11m/sではタイプII極板(線y)の除塵効率がやや低下し(図5(2))、9m/sになるとタイプI極板(線x)の除塵効率もやや低下するが(図5(3))、実用上必要とされる80%以上の除塵効率はいずれも達成されている。 As is clear from FIG. 4, the current flowing through the charging unit for each applied voltage is smaller in the type I plate and the type II plate than in the conventional plate, and therefore the input power to the electrostatic precipitator should be lowered. Can do. In this state, the dust removal efficiency with respect to each charging portion applied voltage is almost the same as that of the conventional electrode plate (line z) for both the type I electrode plate (line x) and the type II electrode plate (line y) at a processing wind speed of 13 m / s. No (FIG. 5 (1)). When the processing wind speed is 11 m / s, the dust removal efficiency of the type II electrode plate (line y) is slightly reduced (FIG. 5 (2)), and when it is 9 m / s, the dust removal efficiency of the type I electrode plate (line x) is slightly reduced. However (FIG. 5 (3)), the dust removal efficiency of 80% or more required for practical use has been achieved.
1…放電極板(極板)、11…放電突起、12,13…側縁、2…接地極板(極板)、EP…帯電部。
DESCRIPTION OF
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Application Number | Priority Date | Filing Date | Title |
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JP2006289497A JP2008104937A (en) | 2006-10-25 | 2006-10-25 | Electric dust collector |
KR1020070107174A KR101065967B1 (en) | 2006-10-25 | 2007-10-24 | Electrostatic Precipitator |
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JP2006289497A JP2008104937A (en) | 2006-10-25 | 2006-10-25 | Electric dust collector |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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JP2009285561A (en) * | 2008-05-29 | 2009-12-10 | Panasonic Corp | Electrostatic dust collecting apparatus |
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KR101383313B1 (en) | 2012-12-06 | 2014-04-09 | 한라산업개발 주식회사 | The discharge electrode for electrostatic precipitator |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5460382A (en) * | 1978-06-12 | 1979-05-15 | Nippon Tokuzai Kk | Method of making feeding roller |
JPS61222555A (en) * | 1985-01-28 | 1986-10-03 | フレ−クト、アクチエボラ−グ | Discharge electrode |
JP2000197833A (en) * | 1999-01-08 | 2000-07-18 | Sumitomo Heavy Ind Ltd | Electric dust collector for tunnel |
Family Cites Families (2)
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JPH0239945B2 (en) * | 1985-02-28 | 1990-09-07 | Nippon Light Metal Co | HODENKYOKUBANNOSEIZOHOHO |
JP2938423B1 (en) * | 1998-02-24 | 1999-08-23 | 川崎重工業株式会社 | Electric dust collector |
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Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
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JPS5460382A (en) * | 1978-06-12 | 1979-05-15 | Nippon Tokuzai Kk | Method of making feeding roller |
JPS61222555A (en) * | 1985-01-28 | 1986-10-03 | フレ−クト、アクチエボラ−グ | Discharge electrode |
JP2000197833A (en) * | 1999-01-08 | 2000-07-18 | Sumitomo Heavy Ind Ltd | Electric dust collector for tunnel |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2009285561A (en) * | 2008-05-29 | 2009-12-10 | Panasonic Corp | Electrostatic dust collecting apparatus |
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KR101065967B1 (en) | 2011-09-19 |
KR20080037553A (en) | 2008-04-30 |
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