JP3004260B1 - Disc type high efficiency dust ionizer - Google Patents

Disc type high efficiency dust ionizer

Info

Publication number
JP3004260B1
JP3004260B1 JP26188298A JP26188298A JP3004260B1 JP 3004260 B1 JP3004260 B1 JP 3004260B1 JP 26188298 A JP26188298 A JP 26188298A JP 26188298 A JP26188298 A JP 26188298A JP 3004260 B1 JP3004260 B1 JP 3004260B1
Authority
JP
Japan
Prior art keywords
dust
discharge electrode
disk
filter cloth
efficiency
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.)
Expired - Fee Related
Application number
JP26188298A
Other languages
Japanese (ja)
Other versions
JP2000061352A (en
Inventor
ジャエ−イク ソン
ヨウン−オク パーク
チェオル−オー クー
ジェオン−フワン リム
サン−ドー キム
ホー−キュン チョイ
ホン−ヨン キム
ピル−ヒェオン クォン
Original Assignee
コリア インスティチュート オブ エナジー リサーチ
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 コリア インスティチュート オブ エナジー リサーチ filed Critical コリア インスティチュート オブ エナジー リサーチ
Application granted granted Critical
Publication of JP3004260B1 publication Critical patent/JP3004260B1/en
Publication of JP2000061352A publication Critical patent/JP2000061352A/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION 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
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/34Constructional details or accessories or operation thereof
    • B03C3/40Electrode constructions
    • B03C3/41Ionising-electrodes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/0027Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions
    • B01D46/0032Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions using electrostatic forces to remove particles, e.g. electret filters
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION 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
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/02Plant or installations having external electricity supply
    • B03C3/04Plant or installations having external electricity supply dry type
    • B03C3/09Plant or installations having external electricity supply dry type characterised by presence of stationary flat electrodes arranged with their flat surfaces at right angles to the gas stream
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION 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
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/02Plant or installations having external electricity supply
    • B03C3/04Plant or installations having external electricity supply dry type
    • B03C3/14Plant or installations having external electricity supply dry type characterised by the additional use of mechanical effects, e.g. gravity
    • B03C3/155Filtration

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrostatic Separation (AREA)

Abstract

【要約】 【課題】 微細ダスト粒子に対する集塵効率を高めて、
濾過布の圧力損失を減少させ、濾過布の寿命を延長させ
ることができ、最小の電力消費で最大のダスト電離効率
が達成できる放電極及び接地極で構成された円板形高効
率ダスト電離装置を提供する。 【解決手段】 既存の濾過布集塵装置のダスト流入口に
設置空間を追加する必要なく容易に付着できるようパイ
プの内部に円板形放電極を配置して、円板形放電極は、
接地極との間隔を一定に形成して均一な電気場を形成さ
せ低電力消費でも電流密度を高められるようにし、円板
形放電極による遊動の攪乱を最小化させながら円板形放
電極を遊動方向に多数配置させて、ダスト粒子が反復的
に電離されるようにすることによりダストの電離効率を
最大化できるようにして構成される。
Abstract: PROBLEM TO BE SOLVED: To improve dust collection efficiency for fine dust particles,
Disc type high efficiency dust ionizer composed of discharge electrode and ground electrode which can reduce the pressure loss of filter cloth, extend the life of filter cloth, and achieve maximum dust ionization efficiency with minimum power consumption I will provide a. SOLUTION: A disk-shaped discharge electrode is disposed inside a pipe so that it can be easily attached without adding an installation space to a dust inlet of an existing filter cloth dust collector.
By forming a uniform electric field by forming a constant distance from the ground electrode and increasing the current density even with low power consumption, the disk-shaped discharge electrode can be formed while minimizing the disturbance of play caused by the disk-shaped discharge electrode. A large number of dust particles are arranged in the floating direction so that dust particles are repeatedly ionized, thereby maximizing the ionization efficiency of dust.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は重油燃焼工程、廃棄
物焼却炉工程、製鉄製鋼業及び発電所の微粉炭燃焼工程
等のダスト発生工程から排出されるダスト粒子を効果的
に捕集するため濾過布集塵装置に流入されるダスト粒子
に静電気的引力を付与して濾過布で微細ダスト粒子の捕
集効率を上昇させ、濾過布表面に空隙率が大きいダスト
層形成を誘導し圧力損失を低減させるダスト電離装置に
係り、低電力消費で高速の流速条件でも微細ダストの電
離効率を高めることができるダスト電離装置の放電極と
接地極設計及びその構造に関する。
The present invention relates to a method for effectively collecting dust particles discharged from a dust generation process such as a heavy oil combustion process, a waste incinerator process, a steelmaking industry and a pulverized coal combustion process of a power plant. By applying electrostatic attraction to the dust particles flowing into the filter cloth dust collector, the collection efficiency of fine dust particles is increased by the filter cloth, and the formation of a dust layer having a large porosity on the filter cloth surface is induced to reduce pressure loss. BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a dust ionization device and a design of a discharge electrode and a ground electrode of a dust ionization device capable of increasing ionization efficiency of fine dust even under conditions of low power consumption and high flow velocity, and a structure thereof.

【0002】[0002]

【従来の技術】ダスト排出量が多量な業種では、排出ダ
ストを捕集除去するため大部分電気集塵装置と濾過布集
塵装置が広く使用される。この中で一般的に微粉炭火力
発電所のように大容量の燃焼気体を処理する工程では主
に電気集塵装置が使用され、中/小容量の燃焼気体及び
含塵気体を処理する産業体では主に濾過布集塵装置が使
用される。
2. Description of the Related Art In a business where a large amount of dust is discharged, an electric dust collector and a filter cloth dust collector are widely used to collect and remove the discharged dust. Generally, in the process of treating a large volume of combustion gas such as a pulverized coal-fired power plant, an electric precipitator is mainly used, and an industrial body for treating medium / small volume combustion gas and dust-containing gas. In this case, a filter cloth dust collector is mainly used.

【0003】しかし、電気集塵装置は、大気汚染規制値
を満足させるため燃料の使用が漸次低硫黄燃料に転換さ
れることで排出されるダストは大きい非抵抗を持つよう
になり、逆電離現象の発生により電気集塵に適合する条
件の維持を不可能にし電気集塵による集塵性能が急激に
低下される。したがって、このような電気集塵装置とは
異なるダストの電気的特性に依存しない安定的で高集塵
効率の維持が可能な集塵装置である濾過布集塵装置が開
発され、最初に1973年からアメリカのペンシルバニ
ア パワー アンド ライト社のサンベリー発電所で適
用し、ヒューストン ライティング アンド パウズパ
リッシュ発電所とコロラド コマンチェ発電所等でも電
気集塵装置を濾過布集塵装置に代替適用した。
[0003] However, in the electric dust collector, as the use of fuel is gradually switched to low-sulfur fuel to satisfy the air pollution regulation value, the discharged dust has a large non-resistance, and the reverse ionization phenomenon occurs. As a result, it becomes impossible to maintain the conditions suitable for the electric dust collection, and the dust collection performance by the electric dust is rapidly reduced. Accordingly, a filter cloth dust collector, which is a dust collector capable of maintaining a stable and high dust collection efficiency without depending on the electrical characteristics of dust different from the electric dust collector, has been developed. And applied it to the Pennsylvania Power and Light Company's Sunbury Power Plant and the Houston Lighting and Paws Parish Power Plant and the Colorado Comanche Power Plant to replace the electric dust collector with a filter cloth dust collector.

【0004】このような濾過布集塵装置は、初期には多
くの問題点が発生していたが、高集塵性能が維持され高
い信頼性が認められて、従来の電気集塵装置を充分に代
替できる可能性が認められた。しかし、濾過操作が進行
されることにより濾過布に捕集されるダスト層が厚くな
って圧力損失が多くなると正常な運転が不可能になる。
よって、周期的な脱塵操作(クリーニング)により濾過
布表面に捕集されたダストを脱塵する必要がある。
[0004] Such a filter cloth dust collector had many problems at the beginning, but it has been confirmed that high dust collecting performance is maintained and high reliability. It was recognized that there was a possibility that it could be replaced. However, if the filtration operation proceeds, the dust layer collected on the filter cloth becomes thick and the pressure loss increases, so that normal operation becomes impossible.
Therefore, it is necessary to remove dust collected on the surface of the filter cloth by a periodic dust removal operation (cleaning).

【0005】脱塵操作は主に物理的な運動または強いエ
ネルギが加わって濾過布表面に捕集されたダスト層を脱
塵する操作である。この時、入口ダスト濃度が濃いか濾
過速度が高速である場合、またはダスト層があまり脱塵
されない運転条件では大部分装置の運転を持続させるた
め脱塵操作頻度を増加させるか脱塵用高圧縮空気を多量
に噴射して脱塵操作を実行している。
[0005] The dust removal operation is mainly an operation of removing dust layers collected on the surface of the filter cloth by applying physical motion or strong energy. At this time, if the inlet dust concentration is high or the filtration speed is high, or under the operating conditions where the dust layer is not so dusty, increase the frequency of dusting operation to maintain the operation of most devices or use high compression for dust removal. A large amount of air is injected to perform the dust removal operation.

【0006】しかし、このような脱塵条件の適用から濾
過布の細孔が大きくなってダスト粒子がその細孔を通過
することにより集塵効率を低下させる要因になってい
る。また、頻繁な脱塵操作から濾過布と濾過布支持わく
(bag cage)との接触衝突により濾過布が磨耗破損されて
濾過布の寿命を短縮させる。また、濾過速度を高速で設
計すると装置の規模が小さくなる利点があるが、圧力損
失が急激に増加するため低速の濾過速度の適用が不可避
であった。
[0006] However, application of such dust removal conditions causes the pores of the filter cloth to become large and dust particles to pass through the pores, which is a factor of reducing the dust collection efficiency. In addition, the filter cloth and filter cloth support frame are removed from frequent dust removal operations.
The filter cloth is worn and damaged by contact collision with the bag cloth, thereby shortening the life of the filter cloth. Designing the filtration speed at a high speed has the advantage of reducing the size of the apparatus, but the pressure loss sharply increases, so that application of a low filtration speed is inevitable.

【0007】このような濾過布集塵装置の問題点を根本
的に解決し高効率を維持するためには、流入されるダス
ト粒子に静電気力を加え微細ダスト粒子の捕集効率を上
昇させて、濾過布表面に形成されたダスト層の空隙率を
最大限大きく維持し圧力損失を低下させる技術開発が必
要である。濾過布集塵装置に流入されるダストに静電気
力が加わると、ダスト層はダスト粒子間の電気的な力に
より濾過布の表面に多孔質の樹木状構造で形成される。
[0007] In order to fundamentally solve the problems of the filter cloth dust collector and maintain high efficiency, electrostatic force is applied to the inflowing dust particles to increase the collection efficiency of the fine dust particles. In addition, it is necessary to develop a technology for maintaining the porosity of the dust layer formed on the surface of the filter cloth as large as possible and reducing the pressure loss. When electrostatic force is applied to the dust flowing into the filter cloth dust collector, a dust layer is formed in a porous tree-like structure on the surface of the filter cloth due to electric force between the dust particles.

【0008】このように形成されたダスト層は空隙率が
高いため圧力損失を減少させて濾過布内へのダスト粒子
浸透を減少させる。また、ダスト粒子の捕集による遮断
または慣性衝突の他に電気的引力が追加されることで微
細ダスト粒子に対する捕集効率が高まる効果がある。こ
のようなダスト電離による濾過布集塵装置の性能向上効
果を利用し、現在までに開発された集塵装置とダスト電
離装置が組合わされた濾過布方式集塵器のダスト電離装
置としては、電極の形態及び位置によって、1979年
L.G.Felix等により開発されたプリシピテータチュ
ーブ(precipitator tube) 形ダスト電離装置(APITRON)
、1982年D.W.Vanosdell等により開発された
濾過布支持わく形ダスト電離装置(ESFF)、R.P.Don
ovan等により開発された流入ダクト設置形ダスト電離装
置、1984年Vanosdell等により開発された織造放電
極形ダスト電離装置、1986年A.S.Viner等が開
発した内部放電極挿入形ダスト電離装置(A-ESFF)、19
91年D.J.Helfritch等により開発されたホッパー
内部設置用スクリーンタイプダスト電離装置等があっ
た。
[0008] The dust layer thus formed has a high porosity, so that the pressure loss is reduced and the penetration of dust particles into the filter cloth is reduced. In addition, there is an effect that the collection efficiency for the fine dust particles is increased by adding an electric attractive force in addition to the interception or the inertial collision by the collection of the dust particles. Utilizing the effect of improving the performance of the filter cloth dust collector by such dust ionization, as a dust ionizer of a filter cloth type dust collector in which a dust collector and a dust ionizer that have been developed to date are combined, an electrode is used. Depending on the form and location of G. FIG. Precipitator tube type dust ionizer (APITRON) developed by Felix, etc.
1982 D.C. W. A filter cloth support frame dust ionizer (ESFF) developed by Vanosdell et al. P. Don
Ovan et al., a dust ionizer installed in an inflow duct, a woven discharge electrode type dust ionizer developed by Vanosdell et al., 1984; S. Diner ionizer with internal discharge electrode (A-ESFF) developed by Viner et al., 19
1991 D. J. There was a screen type dust ionization device for installation inside a hopper developed by Helfritch et al.

【0009】[0009]

【発明が解決しようとする課題】しかし、従来のプリシ
ピテータチューブ形ダスト電離装置(APITRON) は、濾過
布とダスト電離装置が直列に結合された形態で、商業的
に実用化段階にある装置ではあるが装置の構造が複雑で
濾過布の交替及び故障時の修理のような維持及び保守が
困難であった。また、脱塵時ダスト粒子がプリシピテー
タチューブ内に再付着するという問題も発生した。
However, the conventional precipitator tube type dust ionization device (APITRON) is a device which is in the stage of commercialization in a form in which a filter cloth and a dust ionization device are connected in series. However, the structure of the apparatus was complicated, and maintenance and maintenance such as replacement of the filter cloth and repair in case of failure were difficult. In addition, there is a problem that dust particles are re-adhered to the inside of the precipitator tube during dust removal.

【0010】濾過布支持わく形ダスト電離装置(ESFF)
は、電極が濾過布支持わくの構造物と組合わされて濾過
布の内側に位置する形式で、濾過布支持わくの構造物と
電極を連結する絶縁部位とが燃焼ガス条件と脱塵時の衝
撃に脆弱し、また、濾過布の損傷を防止するためそれ以
上の強い電界を形成させることができないという欠点が
あった。
[0010] Frame-type dust ionizer (ESFF) supporting filter cloth
The electrode is located inside the filter cloth in combination with the structure of the filter cloth support frame, and the insulating structure connecting the structure of the filter cloth support frame and the electrode has the combustion gas condition and the impact at the time of dust removal. In addition, there is a drawback that a stronger electric field cannot be formed to prevent the filter cloth from being damaged.

【0011】また、流入ダクト設置形ダスト電離装置
は、濾過布集塵装置の含塵気体流入口にワイヤ形態の放
電極を挿入した方式で、脱塵時に粒子再付着のおそれが
なく、既存の装置を活用でき、容易な構造で設置費が低
廉であり、維持及び保守が便利だという利点はあるが、
ダスト電離装置から濾過布までの距離が遠いため濾過布
近傍でダスト電離率が減少するという欠点があった。
In addition, the dust ionization device provided with an inflow duct is of a type in which a discharge electrode in the form of a wire is inserted into a dust-containing gas inlet of a filter cloth dust collection device. It has the advantages that the equipment can be used, the structure is simple, the installation cost is low, and maintenance and maintenance are convenient.
Since the distance from the dust ionizer to the filter cloth is long, there is a disadvantage that the dust ionization rate decreases near the filter cloth.

【0012】織造放電極形ダスト電離装置は、ステンレ
ス材質の電極を濾材内に包含させ繊維のように織造した
形態で、既存の濾過布に比べて3倍程度高価であり、オ
イルの燃焼によるショットまたは酸の凝集が発生すると
ダスト電離による効果が減少する等の濾過性能がダスト
の種類によって敏感である。また、繊維を損傷させるお
それがあるため加わる電界をより大きくすることができ
ないという欠点があった。
The woven discharge electrode type dust ionizer is a form in which a stainless steel electrode is contained in a filter medium and woven like a fiber, and is about three times as expensive as existing filter cloths. Alternatively, filtration performance, such as the effect of dust ionization being reduced when acid coagulation occurs, is sensitive to the type of dust. In addition, there is a disadvantage that the applied electric field cannot be increased because the fiber may be damaged.

【0013】内部放電極挿入形ダスト電離装置(A-ESFF)
は、濾過布の中心部にステンレスワイヤ形態の放電極を
設置する方法で、装置の構造が容易で追加設置面積が不
必要であるが、高電圧印加による頻繁な破損と維持及び
保守の難しさ等の欠点があった。ホッパー内部設置用ス
クリーンタイプダスト電離装置は、濾過布集塵装置のホ
ッパー内部にワイヤスクリーン接地極に向かっている一
連の尖端で構成されたスクリーン形態の放電極を挿入し
た形式で、ダスト電離装置が濾過布とホッパーとの中間
に設置されるため脱塵時、ダストがダスト電離装置を通
過するとダストが積層されて放電効率が低下されるとい
う問題点があった。
Dust ionizer with internal discharge electrode (A-ESFF)
Is a method of installing a discharge electrode in the form of a stainless wire at the center of a filter cloth. The structure of the device is easy and no additional installation area is required, but frequent breakage due to high voltage application and difficulty in maintenance and maintenance And the like. The screen type dust ionizer for installation inside the hopper is a type in which a screen type discharge electrode composed of a series of pointed ends facing the wire screen ground electrode is inserted inside the hopper of the filter cloth dust collector. Since it is installed between the filter cloth and the hopper, there is a problem in that when the dust passes through the dust ionizer during dust removal, the dust is stacked and the discharge efficiency is reduced.

【0014】従来の電気濾過布集塵装置は、微細ダスト
の集塵効率を高めて濾過布での圧力損失を減少させる等
の効果があるが、ダスト電離装置の構造が複雑で、既存
の濾過布集塵施設を新たな施設に代置する必要があるた
め多くの設置費が所要されるという欠点があった。した
がって、本発明はこのような問題点を解決するため案出
されたもので、その目的は、既存の電気集塵と濾過布集
塵技術の原理を結合させた新たな集塵装置である電気濾
過布集塵装置で、微細ダスト粒子に対する集塵効率を高
め、濾過布の圧力損失を減少させ、濾過布の寿命を延長
させることができ、最小の電力消費で最大のダスト電離
効率が達成できる放電極及び接地極で構成された高効率
ダスト電離装置を提供することにある。
[0014] The conventional electric filter cloth dust collector has the effect of increasing the dust collection efficiency of fine dust and reducing the pressure loss in the filter cloth. However, the structure of the dust ionizer is complicated and the existing filter is not used. There is a drawback that a large amount of installation cost is required because the cloth dust collection facility needs to be replaced with a new facility. Therefore, the present invention has been devised to solve such a problem, and an object of the present invention is to provide an electric precipitator, which is a new precipitator that combines the principles of existing electric precipitator and filter cloth precipitator technology. Filter cloth dust collector can increase dust collection efficiency for fine dust particles, reduce filter cloth pressure loss, prolong filter cloth life, achieve maximum dust ionization efficiency with minimum power consumption An object of the present invention is to provide a high-efficiency dust ionization device including a discharge electrode and a ground electrode.

【0015】[0015]

【課題を解決するための手段】前記の目的を達成するた
めの特徴によるに、本発明によるダスト電離装置は、低
エネルギ消費で濾過布集塵装置の集塵性能を向上させ
て、設置面積を最小化できる構造及び設計技術で構成さ
れる。また、ダスト電離装置内部に均一な電気場を形成
させるための円板形放電極の構造、配置及び組立技術、
ダスト電離装置の外壁構造の役割とともに接地極の役割
をする円筒形接地極形状、低電力消費で高密度の電気場
を形成させて高電離効率を達成するための放電極と接地
極の財源、遊動の攪乱を最小化するための放電極入口形
状、放電極の支持と接地極との絶縁のための支持台構造
等とで構成される。
According to a feature of the present invention, a dust ionizer according to the present invention improves the dust collecting performance of a filter cloth dust collector with low energy consumption and increases the installation area. It consists of a structure and design technology that can be minimized. In addition, the structure, arrangement and assembly technology of a disk-shaped discharge electrode for forming a uniform electric field inside the dust ionization device,
The cylindrical grounding pole shape that plays the role of the grounding pole together with the outer wall structure of the dust ionization device, the discharge electrode and grounding funding to achieve high ionization efficiency by forming a high-density electric field with low power consumption, It is composed of a discharge electrode inlet shape for minimizing the disturbance of movement, a support base structure for supporting the discharge electrode and insulating the ground electrode from the ground.

【0016】[0016]

【発明の実施の形態】以下、添付図面を参照して本発明
の構成及び作用について詳細に説明する。図1は本発明
による円板形高効率ダスト電離装置の構造を概略的に示
す組立図、図2は円板形高効率ダスト電離装置の絶縁部
と放電極の組立形態を示す断面図、図3は円板形高効率
ダスト電離装置の放電極及び絶縁部を構成する部品図で
ある。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The configuration and operation of the present invention will be described below in detail with reference to the accompanying drawings. FIG. 1 is an assembly view schematically showing the structure of a disk-shaped high-efficiency dust ionizer according to the present invention, and FIG. 2 is a cross-sectional view showing an assembling mode of an insulating portion and a discharge electrode of the disk-shaped high efficiency dust ionizer. FIG. 3 is a component diagram of a discharge electrode and an insulating portion of the disc-shaped high-efficiency dust ionizer.

【0017】図1に示されるように、本発明の円板形高
効率ダスト電離装置は、既存の濾過布集塵装置のダスト
流入口に設置空間を追加する必要なく容易に付着できる
ようパイプの内部に円板形コロナ放電極を配置して、円
板形コロナ放電極は、円筒形接地極との間隔を一定に形
成して均一な電気場を形成させ低電力消費でも電流密度
を高められるようにし、円板形放電極による遊動の攪乱
を最小化させながら円板形コロナ放電極を遊動方向に多
数配置させて、ダスト粒子が反復的に電離されるように
することによりダストの電離効率を最大化できるように
して構成される。
As shown in FIG. 1, the disk-type high-efficiency dust ionizer according to the present invention has a pipe-shaped high-efficiency dust ionizer which can be easily attached to the existing filter cloth dust collector without adding an installation space to the dust inlet. A disk-shaped corona discharge electrode is arranged inside, and the disk-shaped corona discharge electrode forms a uniform electric field by forming a constant interval with the cylindrical ground electrode, so that the current density can be increased even with low power consumption. In this way, a large number of disc-shaped corona discharge electrodes are arranged in the direction of movement while minimizing the disturbance of movement caused by the disc-shaped discharge electrodes, so that dust particles are repeatedly ionized, thereby improving the ionization efficiency of dust. Is configured to be maximized.

【0018】ここで、円板形コロナ放電極の挿入により
圧力損失を減少させてダストの堆積を防止し、最大のダ
スト電離効率を達成するようにしたダスト電離装置の長
さは1000mm、円板形コロナ放電極の直径は50mm、
円板形コロナ放電極間の距離は15mm、円筒形接地極と
円板形コロナ放電極との間隔は25mmである。前記円板
形高効率ダスト電離装置は、図示されるように、多数の
ステンレス材質の円板が組合わされた円板形コロナ放電
極とパイプ形態の円筒形接地極、円板形コロナ放電極の
支持及び円筒形接地極との絶縁のための絶縁支持台、遊
動の攪乱を減少させるためダスト電離装置入口に位置し
た遊動誘導円錐とで構成される。
Here, the length of the dust ionization apparatus is 1000 mm, and the length of the dust ionization apparatus is such that the pressure loss is reduced by inserting a disk-shaped corona discharge electrode to prevent the accumulation of dust and achieve the maximum dust ionization efficiency. The diameter of the corona discharge electrode is 50mm,
The distance between the disk-shaped corona discharge electrodes is 15 mm, and the distance between the cylindrical ground electrode and the disk-shaped corona discharge electrode is 25 mm. As shown, the disc-shaped high-efficiency dust ionizer has a disc-shaped corona discharge electrode in which a number of discs made of stainless steel are combined and a cylindrical ground electrode in the form of a pipe, and a disc-shaped corona discharge electrode. It consists of an insulating support for supporting and insulating from the cylindrical grounding pole, and a floating guiding cone located at the entrance of the dust ionizer to reduce the disturbance of the floating.

【0019】既存のパイプ形ダスト電離装置は、パイプ
の内部に一つのワイヤになった放電極を挿入した形態
で、電気場内の電流強度が弱い上に電力消耗も多かっ
た。また、放電極と接地極との間の距離を一定に維持す
るため一定の張力を加える必要があり、これによる放電
極の破損が頻繁であった。しかし、図2に示されるよう
に本発明の円板形高効率ダスト電離装置は、図1のA−
A’線に沿って切断した断面図のようにパイプ内にテフ
ロン材質の絶縁体(図3参照)6個で支持された中心棒
にSUS材質の円板を図1のB−B’線に沿って切断し
た断面図のようにパイプの中心に沿って多数装着した構
造である。
The existing pipe-type dust ionization apparatus has a form in which a discharge electrode formed as a single wire is inserted inside the pipe, and the current intensity in the electric field is weak and the power consumption is large. In addition, it is necessary to apply a constant tension in order to maintain a constant distance between the discharge electrode and the ground electrode, and the discharge electrode is frequently damaged due to this. However, as shown in FIG. 2, the disc-shaped high-efficiency dust ionizer of the present invention is the same as that of FIG.
As shown in the cross-sectional view taken along the line A ', a disk made of SUS is attached to a center rod supported by six insulators made of Teflon (see Fig. 3) in the pipe along the line BB' in Fig. 1. As shown in a cross-sectional view taken along the line, a large number of parts are mounted along the center of the pipe.

【0020】中心棒に装着されたSUS円板の間隔は図
3の放電極間隔調節用パイプリング(pipe ring) により
調節され固定される。円筒形接地極の中心に円板形の円
板形コロナ放電極を挿入すると、前記放電極と前記接地
極との間隔が一定に形成されることにより前記放電極と
前記接地極との間に一定な電流密度の電気場が形成でき
る。また、圧力損失があまり大きくない範囲内で該放電
極の直径を拡大させ該放電極と該接地極との間の間隔を
狭くするとコロナ開示電圧が低くなることにより、低電
力消耗でも大きい電流密度が得られ、流速が増加して電
離したダストが該接地極表面に電気的引力により付着さ
れる現状を防止できる。
The distance between the SUS disks mounted on the center rod is adjusted and fixed by the discharge electrode distance adjusting pipe ring shown in FIG. When a disk-shaped corona discharge electrode of a disk shape is inserted at the center of the cylindrical ground electrode, the interval between the discharge electrode and the ground electrode is formed to be constant, so that the space between the discharge electrode and the ground electrode is formed. An electric field with a constant current density can be formed. In addition, when the diameter of the discharge electrode is enlarged and the distance between the discharge electrode and the ground electrode is reduced within a range where the pressure loss is not so large, the corona disclosure voltage is reduced, so that even when the power consumption is low, a large current density is obtained. Is obtained, and it is possible to prevent the current state in which the ionized dust due to the increased flow velocity is attached to the surface of the ground electrode by the electric attraction.

【0021】このような形態の円板形コロナ放電極を流
体の流れ方向に多数配置することにより、装置に流入さ
れたダストは数十回にわたって電気場を通過しながら反
復的に電離されて、高速の高速条件でも微細ダスト粒子
の電離効率が高まる。
By arranging a large number of disk-shaped corona discharge electrodes in the flow direction of the fluid, dust introduced into the apparatus is repeatedly ionized while passing through an electric field several tens of times. Even under high-speed and high-speed conditions, the ionization efficiency of fine dust particles increases.

【0022】[0022]

【発明の効果】以上のように本発明による円板形高効率
ダスト電離装置は、構造が容易で、既存の濾過布集塵施
設をそのまま利用できるため追加設置費が不必要な上設
置空間が減少して、低電力消費でもダスト電離効率が高
いため経済的かつ、濾過布の寿命延長が可能である。
As described above, the disk-shaped high-efficiency dust ionization apparatus according to the present invention has a simple structure and can use the existing filter cloth dust collection facility as it is, so that an additional installation cost is unnecessary and an installation space is unnecessary. As a result, the dust ionization efficiency is high even at low power consumption, so that it is economical and the life of the filter cloth can be extended.

【0023】また、本発明による装置は、装置の構造的
なシステム構成技術と低電力で微細ダスト粒子の電離効
率を高められるため構造側面において高効率ダスト電離
装置技術開発として最初の技術である。
Further, the apparatus according to the present invention is the first technique in the technical development of a high-efficiency dust ionization apparatus in the aspect of structure since the ionization efficiency of fine dust particles can be increased with low power and the system configuration technology of the apparatus.

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

【図1】円板形高効率ダスト電離装置の構造を概略的に
示す組立図である。
FIG. 1 is an assembly view schematically showing a structure of a disk-shaped high-efficiency dust ionization apparatus.

【図2】円板形高効率ダスト電離装置の絶縁部と放電極
の組立形態を示す断面図である。
FIG. 2 is a cross-sectional view showing an assembling mode of an insulating part and a discharge electrode of the disc-shaped high-efficiency dust ionization apparatus.

【図3】円板形高効率ダスト電離装置の放電極及び絶縁
部を構成する部品図である。
FIG. 3 is a diagram showing components constituting a discharge electrode and an insulating portion of the disk-shaped high-efficiency dust ionization device.

【符号の説明】[Explanation of symbols]

1 遊動誘導円錐 2,25,31 円板形コロナ放電極 3,23 円筒形接地極 4 絶縁支持台 5,24,32 放電極間隔調節用パイプリング 6 高電圧引入線 21 絶縁支持台 22 中心棒 33 絶縁体 DESCRIPTION OF SYMBOLS 1 Idle guide cone 2, 25, 31 Disc-shaped corona discharge electrode 3, 23 Cylindrical grounding electrode 4 Insulation support base 5, 24, 32 Pipe ring for adjusting discharge electrode spacing 6 High-voltage lead-in line 21 Insulation support base 22 Center rod 33 Insulator

───────────────────────────────────────────────────── フロントページの続き (72)発明者 クー チェオル−オー 大韓民国,ダエジェオン−シ,セオ− ク,ドゥンサン−ドン,1−106,エウ ンチョロンアパート908−3 (72)発明者 リム ジェオン−フワン 大韓民国,ダエジェオン−シ,ドン− ク,ダエソン−ドン,107−107,サミッ クアパート30 (72)発明者 キム サン−ドー 大韓民国,ダエジェオン−シ,セオ− ク,サムチョン−ドン,203−1002,ボ ラアパート (72)発明者 チョイ ホー−キュン 大韓民国,ソウル,カンドン−ク,ジル −ドン,109−1 (72)発明者 キム ホン−ヨン 大韓民国,ダエジェオン−シ,セオ− ク,ドマ 1−ドン,1−505,ボケウ ンアパート (72)発明者 クォン ピル−ヒェオン 大韓民国,キュンギ−ド,クンポ−シ, サンボン−ドン,ユースンアパート1315 −2001 (56)参考文献 特開 昭63−274428(JP,A) 特開 平1−242158(JP,A) (58)調査した分野(Int.Cl.7,DB名) B03C 3/00 - 3/88 B01D 51/00 ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Ku Cheol-Oh Korea, Daejeon-shi, Theok, Dunsan-dong, 1-106, Eunchoron Apartment 908-3 (72) Inventor Lim Jeon-Hwan Republic of Korea, Daejeon-si, Dong-ku, Daesong-dong, 107-107, Samic apartment 30 (72) Inventor Kim Sang-do Republic of Korea, Daejeon-si, Theok, Samcheong-dong, 203-1002, Bo La Appart (72) Inventor Choi Ho-Kyun South Korea, Seoul, Kang-dong, Jill-dong, 109-1 (72) Inventor Kim Hong-Yong South Korea, Daejeon-shi, Theok, Doma 1-dong, 1-505, Bokehung Apartment (72) Kwon Pi, the inventor Lu-Heon Republic of Korea, Kunguido, Kumposi, Sambong-dong, Yusun apartment 1315-2001 (56) References JP-A-63-274428 (JP, A) JP-A-1-242158 (JP, A) (58) Field surveyed (Int. Cl. 7 , DB name) B03C 3/00-3/88 B01D 51/00

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】円板形高効率ダスト電離装置を構成するに
おいて、既存の濾過布集塵装置のダスト流入口に設置空
間を追加する必要なく容易に付着できるようパイプの内
部に円板形放電極を配置して、 前記円板形放電極は、接地極との間隔を一定に形成して
均一な電気場を形成させ、低電力消費でも電流密度を高
められるようにし、前記円板形放電極による遊動の攪乱
を最小化させながら前記円板形放電極を前記パイプの軸
方向に多数配置させて、ダスト粒子が反復的に電離さ
れるようにすることによりダストの電離効率を最大化で
きるようにしたことを特徴とする円板形高効率ダスト電
離装置。
In the construction of a disk-type high-efficiency dust ionizer, a disk-type discharger is installed inside a pipe so that it can be easily attached without adding an installation space to a dust inlet of an existing filter cloth dust collector. An electrode is disposed, and the disc-shaped discharge electrode is formed at a constant distance from a ground electrode to form a uniform electric field, so that current density can be increased even with low power consumption, and the disc-shaped discharge electrode is formed. While minimizing the disturbance of movement caused by the electrode, the disc-shaped discharge electrode is connected to the shaft of the pipe.
A high-efficiency disk ionization apparatus characterized in that dust particles are repeatedly ionized by arranging a large number of particles in a linear direction so that the ionization efficiency of dust can be maximized.
【請求項2】 前記円板形放電極の挿入により圧力損失
を減少させてダストの堆積を防止し、最大のダスト電離
効率を達成できるようにしたダスト電離装置の長さは1
000mm、放電極の直径は50mm、放電極間の距離は1
5mm、接地極と放電極との間隔は25mmであることを特
徴とする請求項1記載の円板形高効率ダスト電離装置。
2. The length of the dust ionization device is set to 1 to reduce the pressure loss by inserting the disk-shaped discharge electrode to prevent the accumulation of dust and to achieve the maximum dust ionization efficiency.
000mm, diameter of discharge electrode is 50mm, distance between discharge electrodes is 1
2. The high-efficiency disk ionizer according to claim 1, wherein the distance between the ground electrode and the discharge electrode is 5 mm.
JP26188298A 1998-08-17 1998-09-16 Disc type high efficiency dust ionizer Expired - Fee Related JP3004260B1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
KR33197/1998 1998-08-17
KR1019980033197A KR100292556B1 (en) 1998-08-17 1998-08-17 Disk Type High Efficiency Dust Ionizer

Publications (2)

Publication Number Publication Date
JP3004260B1 true JP3004260B1 (en) 2000-01-31
JP2000061352A JP2000061352A (en) 2000-02-29

Family

ID=19547353

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26188298A Expired - Fee Related JP3004260B1 (en) 1998-08-17 1998-09-16 Disc type high efficiency dust ionizer

Country Status (2)

Country Link
JP (1) JP3004260B1 (en)
KR (1) KR100292556B1 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106423560A (en) * 2016-11-18 2017-02-22 广西大学 High-efficiency multi-layer electrostatic dust collector
CN109404946A (en) * 2018-10-10 2019-03-01 芜湖天火新能源科技有限公司 A kind of combustion carbon boiler plant carbon slag cleaning device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106423560A (en) * 2016-11-18 2017-02-22 广西大学 High-efficiency multi-layer electrostatic dust collector
CN106423560B (en) * 2016-11-18 2018-03-27 江苏安达环保科技有限公司 A kind of multilayer electrostatic precipitator
CN109404946A (en) * 2018-10-10 2019-03-01 芜湖天火新能源科技有限公司 A kind of combustion carbon boiler plant carbon slag cleaning device

Also Published As

Publication number Publication date
KR20000014007A (en) 2000-03-06
JP2000061352A (en) 2000-02-29
KR100292556B1 (en) 2001-09-17

Similar Documents

Publication Publication Date Title
US6152988A (en) Enhancement of electrostatic precipitation with precharged particles and electrostatic field augmented fabric filtration
CA1070622A (en) Process and apparatus for electrostatic cleaning of gases
US5395430A (en) Electrostatic precipitator assembly
US4349359A (en) Electrostatic precipitator apparatus having an improved ion generating means
US5084077A (en) Apparatus for gas purification
KR20010101080A (en) Electrostatic precipitator
JP5886874B2 (en) Electrical shielding device for structures near high voltage components of electrostatic precipitator
EP1082175A1 (en) Method and apparatus for separating particles from an air flow
JP4250591B2 (en) Ionizer and its use in exhaust gas purifier for gas containing liquid particles and / or condensing moisture
CN204911799U (en) It removes smoke and dust device to revolve electric formula
US7767005B2 (en) Tunnel fan electrostatic filter
KR101721925B1 (en) Electrostatic precipitator insulator for preventing electric short and electrostatic precipitator containing the same
JP3336452B2 (en) Dust collector
CA1178217A (en) Electrostatic precipitator having high strength discharge electrode
JP3004260B1 (en) Disc type high efficiency dust ionizer
JP4094223B2 (en) Electric dust collector
KR100980341B1 (en) Electric Multi Cyclone Scrubber
US4236900A (en) Electrostatic precipitator apparatus having an improved ion generating means
CN207615021U (en) Air purification dust collecting structure, air cleaning unit and air hose
CN206763140U (en) It is double to drive board-like electronic dust-collecting purifier
KR100330964B1 (en) Helical Screw type High Efficiency Dust Ionizer
CN104888961A (en) Vehicle-mounted bionic electrostatic dusting air purifier
CN105032616A (en) Cyclone discharge type smoke dust removal method and device
JPH0331501B2 (en)
WO2000062936A1 (en) Arrangement and method for purification of flowing gas

Legal Events

Date Code Title Description
R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees