JP3036083U - Electrostatic precipitator shunt integration mechanism - Google Patents

Electrostatic precipitator shunt integration mechanism

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Publication number
JP3036083U
JP3036083U JP1996010942U JP1094296U JP3036083U JP 3036083 U JP3036083 U JP 3036083U JP 1996010942 U JP1996010942 U JP 1996010942U JP 1094296 U JP1094296 U JP 1094296U JP 3036083 U JP3036083 U JP 3036083U
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Japan
Prior art keywords
dust
dust collecting
electrode
electrostatic precipitator
collecting electrode
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 - Lifetime
Application number
JP1996010942U
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Japanese (ja)
Inventor
智弘 山口
Original Assignee
日南エレクトロニクス株式会社
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Priority to JP1996010942U priority Critical patent/JP3036083U/en
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Abstract

(57)【要約】 【課題】 電気集塵装置は大型で、建設費、並びに据付
面積の増大につながる。また、集塵極面積を単に小さく
すれば、集塵効率を著しく低下させる。本考案は、分流
機構、円筒状の集塵極を採用したことにより集塵効率を
落とさずに小型化できる電気集塵装置の分流集約化機構
である。 【解決手段】 本考案は、ガス通路に分流器(4)を設
け、ガス流を強制的に減速、拡散させ、ガス流を集塵機
本体(1)内に送り、かつ、集塵極(2)に同心円状の
10層とした円筒構造を採ることにより、集塵極(2)
の集約化が可能となり、効率を下げずに小型化できる。
(57) [Summary] [PROBLEMS] An electric precipitator is large in size, leading to an increase in construction cost and an installation area. Further, if the area of the dust collecting electrode is simply reduced, the dust collecting efficiency is significantly reduced. The present invention is a shunt collecting mechanism for an electric dust collector that can be downsized without reducing the dust collecting efficiency by adopting a shunting mechanism and a cylindrical dust collecting electrode. The present invention provides a flow divider (4) in a gas passage, forcibly decelerates and diffuses a gas flow, sends a gas flow into a dust collector body (1), and a dust collector electrode (2). The dust collecting electrode (2) by adopting a concentric cylindrical structure with 10 layers
Can be integrated, and the size can be reduced without lowering the efficiency.

Description

【考案の詳細な説明】[Detailed description of the invention]

【0001】[0001]

【考案の属する技術分野】[Technical field to which the invention belongs]

本考案は集塵装置にガス流の分流機構を設け、集塵極を円筒構造とする事で集 約化し、小型化した電気集塵装置に関するものである。 The present invention relates to an electric dust collector which is compact and compact by providing a dust collector with a gas flow dividing mechanism and having a cylindrical dust collecting electrode.

【0002】[0002]

【従来の技術】[Prior art]

従来の電気集塵装置では第3図に示すように、集塵機本体(12)の集塵空間 内のガス流速を自然拡散しているため、排出口(15)の断面積に対する、集塵 機本体(12)の断面積を断面積が二倍になると流速は半分になることより、大 きく採らざるを得なくなっていた。なぜなら、排出口(15)より集塵機本体( 12)に入ったダストは、放電極(14)によりマイナスイオンに帯電され、プ ラス電荷の集塵極(13)にクーロン力によって付着するが、集塵空間内のガス 流速が1〜2m/s以上になると、集塵極(13)に付着したダストの飛散及び 、ダストがクーロン力によって集塵極(13)に移動することを大きく阻害する 。排出口(15)のガス流速を20m/sとした場合、集塵空間内の流速を1m /にするには、排出口(15)断面積を1mとした場合、集塵機本体(12 )の断面積を20mとしなければならない。このため、大きなガス流速で排出 される焼却炉では断面積を大きくして流速を落とさなければならなかった。 又、集塵効率は集塵極(13)の面積が大きくなるほど高くなるので、集塵極 (13)を長方形板状にし、並べて配置していた。したがって、電気集塵装置は 大型、並びに据付面積の増大という問題点があった。In the conventional electrostatic precipitator, as shown in FIG. 3, the gas flow velocity in the dust collecting space of the dust collector body (12) is naturally diffused, so that the dust collector body with respect to the cross-sectional area of the discharge port (15) is When the cross-sectional area of (12) was doubled, the flow velocity was halved, and it had to be adopted. This is because the dust that has entered the dust collector body (12) through the discharge port (15) is charged with negative ions by the discharge electrode (14) and adheres to the dust collection electrode (13) with a positive charge due to the Coulomb force. When the gas flow velocity in the dust space is 1 to 2 m / s or more, the dust adhering to the dust collecting electrode (13) and the movement of the dust to the dust collecting electrode (13) by the Coulomb force are greatly hindered. When the gas flow velocity of the discharge port (15) is 20 m / s, the flow velocity in the dust collecting space is 1 m 2 / S. When the cross-sectional area of the discharge port (15) is 1 m 2 , the dust collector body (12) The cross-sectional area of the must be 20 m 2 . For this reason, it was necessary to increase the cross-sectional area and reduce the flow rate in an incinerator that discharges at a high gas flow rate. Further, since the dust collection efficiency increases as the area of the dust collection electrode (13) increases, the dust collection electrodes (13) are formed in a rectangular plate shape and arranged side by side. Therefore, there are problems that the electrostatic precipitator is large and the installation area is increased.

【0003】[0003]

【考案が解決しようとする課題】[Problems to be solved by the device]

電気集塵装置を小型化できれば建設費、並びに据付面積を小さくすることがで きる。しかし、ガス流の自然拡散では集塵機本体を大きくしなければならない。 また、集塵極面積を集約しようと単に小さくし、小型化しても、集塵効率を著し く低下させるだけである。従って、分流機構によりガス流の流速を強制的に抑制 し、かつ、集塵極を円筒構造とし、集塵極面積の集約化をはかることにより、集 塵効率を落とさずに電気集塵装置を小型化し、前述の問題点を解消しようとする ものである。 If the electrostatic precipitator can be miniaturized, the construction cost and the installation area can be reduced. However, for the natural diffusion of the gas flow, the dust collector body must be made larger. Moreover, even if the dust collecting electrode area is simply reduced to reduce the size of the dust collecting electrode area, the dust collecting efficiency is significantly reduced. Therefore, by forcibly suppressing the flow velocity of the gas flow by the flow dividing mechanism, and by making the dust collecting electrode a cylindrical structure and consolidating the dust collecting electrode area, the electrostatic precipitator can be installed without reducing the dust collecting efficiency. The aim is to reduce the size and eliminate the above-mentioned problems.

【0004】[0004]

【課題を解決するための手段】[Means for Solving the Problems]

本考案は、上述の問題点を解決するため、煙突出口に分流器を設け、ガス流を強 制的に拡散、減速させ、集塵装置本体内のダストの均一分布をはかる構造とし、 かつ、集塵極に同心円状の薄板を複数層とした円筒構造を採ることにより集約化 し、単位体積あたりの集塵極面積を大きくすることが可能となり、効率を下げず に小型化でき、問題点を解決している。 In order to solve the above-mentioned problems, the present invention has a structure in which a flow diverter is provided at the smoke outlet to forcibly diffuse and decelerate the gas flow, and to evenly distribute the dust in the dust collector main body. The dust collecting electrode is integrated by adopting a cylindrical structure with multiple concentric thin plates to increase the area of the dust collecting electrode per unit volume, which can be downsized without lowering efficiency. Has been resolved.

【0005】[0005]

【考案の実施の形態】[Embodiment of the invention]

煙突の上部に円筒形の集塵機本体を取り付ける。集塵機本体には、最下部に上 部が円錐形の分流器による分流機構を設ける。分流器の上部には放射状の放電極 を8カ所の碍子にて固定させる。放電極上部に集塵極を上下端の集塵極支持棒に よって集塵機本体に固定させる構造である。集塵極は最外郭を集塵機本体が兼ね 、その内側にステンレス製の円筒形の薄板を同心円状に10cm間隔で10層と した構造を採っている。 放電極を負極とし集塵極を正極とした二極間に高圧直流電圧をかけ、コロナ放 電によって負イオンを発生させ、この中をダストを含んだガス流が通過する時、 ダストは負イオンに帯電させられ、正極である集塵極にクーロン力による作用で 付着し、集塵させる構造である。 Attach the cylindrical dust collector body to the top of the chimney. At the bottom of the dust collector body, a flow dividing mechanism with a conical flow divider with a conical upper part is installed. Radial discharge electrodes are fixed to the upper part of the flow distributor with eight insulators. The structure is such that the dust collecting electrode is fixed to the dust collector main body by the dust collecting electrode support rods at the upper and lower ends above the discharge electrode. The main body of the dust collector also serves as the outermost part of the dust collector, and a cylindrical thin stainless steel plate is concentrically arranged in 10 layers at 10 cm intervals. A high-voltage DC voltage is applied between the two electrodes, with the discharge electrode as the negative electrode and the dust collection electrode as the positive electrode, to generate negative ions by corona discharge, and when the gas stream containing dust passes through them, the dust is negative ions. The structure is such that it is charged to the positive electrode and adheres to the dust collecting electrode, which is the positive electrode, by the action of Coulomb force to collect the dust.

【0006】[0006]

【実施例1】 以下、添付第1図に従って実施例1を説明する。煙突(5)より排出されたダ ストを含むガス流は分流器(4)により拡散し、集塵機本体(1)に流れる。ス テンレス製で放射状の放電極(3)は8ヶ所の碍子(6)にて集塵機本体(1) に固定させる。その上部に円筒形の集塵極(2)を10層の同心円状に取り付け る。集塵極(2)は上部と下部に溶接した集塵極支持棒(8)により集塵機本体 (1)に固定されている。放電極(3)を負極、集塵極(2)を正極とし、放電 の発生する30〜80KVの高圧直流電圧をかけ、コロナ放電によって負イオン を発生させる。ダストを含むガス流は集塵機本体(1)内に入った後、放電極( 3)を通過するとき、ダストは負イオンに帯電され、クーロン力による作用で放 電極(3)上方の正極である集塵極(2)に付着、集塵される。集塵極(2)は 最外郭を集塵機本体(1)が兼ね、各々の円筒形の内外面も集塵面となるので集 塵面積を大きくしている。付着したダストを下部に落とすため、槌支持機(10 )を通った槌打ちワイヤー(11)を引いて鉄製の槌(9)を持ち上け槌打ちワ イヤー(11)を緩めることにより槌(9)を落下させ、集塵極支持棒(8)を 叩き、ダストを落とし煤塵排出口(7)より排出する。ダストが集塵されたガス 流は、集塵機本体(1)より外気に排出される。また、集塵機本体(1)を小型 化したことにより、煙突(5)の上部に取り付けることができる。Embodiment 1 Hereinafter, Embodiment 1 will be described with reference to the attached FIG. The gas flow containing dust discharged from the chimney (5) is diffused by the flow distributor (4) and flows into the dust collector body (1). The stainless radial discharge electrode (3) is fixed to the dust collector body (1) by the insulators (6) at eight locations. A cylindrical dust collecting electrode (2) is attached to the upper part of the concentric circle of 10 layers. The dust collecting electrode (2) is fixed to the dust collector main body (1) by a dust collecting electrode supporting rod (8) welded to the upper and lower portions. Using the discharge electrode (3) as a negative electrode and the dust collection electrode (2) as a positive electrode, a high voltage direct current voltage of 30 to 80 KV at which discharge is generated is applied to generate negative ions by corona discharge. When the gas flow containing dust enters the dust collector body (1) and then passes through the discharge electrode (3), the dust is charged with negative ions and is a positive electrode above the discharge electrode (3) due to the action of Coulomb force. The dust is attached to the dust collecting electrode (2) and collected. Since the dust collector body (1) also serves as the outermost portion of the dust collecting electrode (2), and the inner and outer surfaces of each cylinder also serve as the dust collecting surface, the dust collecting area is increased. In order to drop the attached dust to the lower part, pull the hammer hammer wire (11) that has passed through the hammer support machine (10) and lift the iron hammer (9) to loosen the hammer hammer (11) ( 9) is dropped, and the dust collecting electrode support rod (8) is hit to drop dust, and the dust is discharged from the soot / dust discharge port (7). The gas flow in which the dust is collected is discharged from the dust collector body (1) to the outside air. Further, since the dust collector body (1) is downsized, it can be attached to the upper part of the chimney (5).

【0007】[0007]

【実施例2】 添付第2図により実施例2を説明する。集塵極(2)に付着したダストは肥大 化し、集塵極(2)上部の鉄製の槌(図示せず)で叩くことにより下部へ落下し 、煤塵排出口(7)より排出される。このとき分流器(4)の上部が円錐形をし ていることにより、図中のA,Bの方向に煤塵が落ち、煙突内に煤塵が落ちるこ とを防止でき、煤塵排出口(7)への排出を促進することができる。Second Embodiment A second embodiment will be described with reference to the attached FIG. The dust adhering to the dust collecting electrode (2) is enlarged and hit by an iron mallet (not shown) on the upper part of the dust collecting electrode (2) to fall to the lower part and is discharged from the soot dust discharging port (7). At this time, since the upper part of the flow divider (4) has a conical shape, it is possible to prevent soot dust from falling in the directions of A and B in the figure and prevent it from falling into the chimney, and the soot discharge port (7) Can be promoted to.

【0008】[0008]

【考案の効果】[Effect of the invention]

上述のように、本考案は、分流機構を設け強制的にガス流を減速、拡散させる 構造であることより従来の自然拡散方式に比べ、小型化ができ、集塵極を10層 の円筒構造としたことにより板状構造と比較した場合、円筒形同体積あたり集塵 面積を約85%増加させることができ、同じ集塵面積では、約54%の小型化が できる。また、分流機構の上部を円錐形としたことにより付着したダストが落下 する際、煙突内に入ることを防止する効果がある。 As described above, the present invention has a structure for forcibly decelerating and diffusing the gas flow by providing the flow dividing mechanism, so that it can be made smaller than the conventional natural diffusion method, and the dust collecting electrode has a cylindrical structure of 10 layers. Therefore, when compared with the plate-like structure, the dust collection area per cylinder of the same volume can be increased by about 85%, and the same dust collection area can be downsized by about 54%. In addition, since the upper part of the flow dividing mechanism has a conical shape, it has the effect of preventing the adhering dust from entering the stack when it falls.

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

【図1】本考案の電気集塵装置の分流集約機構の実施例
1を示す一部欠断斜視図である。
FIG. 1 is a partially cutaway perspective view showing a first embodiment of a split flow collecting mechanism of an electrostatic precipitator according to the present invention.

【図2】本考案の電気集塵装置の分流集約機構の実施例
2を示す断面図である。
FIG. 2 is a cross-sectional view showing Embodiment 2 of the split flow collecting mechanism of the electrostatic precipitator of the present invention.

【図3】従来の技術を示す一部欠断正面斜視図である。FIG. 3 is a partially cutaway front perspective view showing a conventional technique.

【符号の説明】[Explanation of symbols]

1.集塵機本体 2.集塵極 3.放電極 4.分流器 5.煙突 6.碍子 7.煤塵排出口 8.集塵極支持棒 9.槌 10.槌支持機 11.槌打ちワイヤー 12.集塵機本体 13.集塵極 14.放電極 15.排出口 16.碍子 1. Dust collector body 2. 2. Dust collection electrode Discharge electrode 4. Current divider 5. Chimney 6. Insulator 7. Dust outlet 8. Dust collecting pole support rod 9. Mallet 10. Mallet support machine 11. Hammering wire 12. Dust collector body 13. Dust collecting electrode 14. Discharge electrode 15. Outlet 16. insulator

Claims (3)

【実用新案登録請求の範囲】[Utility model registration claims] 【請求項1】電気集塵装置において、ガス流を強制的に
拡散、減速させ小型化させるため、ガス通路に分流器を
設けたことを特徴とする電気集塵装置の分流集約化機構
1. An electrostatic precipitator in which a flow diverter is provided in a gas passage for forcibly diffusing and decelerating a gas flow to reduce the size of the electrostatic precipitator.
【請求項2】電気集塵装置において、集塵極面積を集約
化させ集塵効率を落とさずに小型化させるため、集塵極
を同心円状に複数層の円筒構造としたことを特徴とする
電気集塵装置の分流集約化機構
2. The electrostatic precipitator is characterized in that the dust collecting electrode is concentrically formed into a cylindrical structure of a plurality of layers in order to consolidate the dust collecting electrode area and reduce the size without lowering the dust collecting efficiency. Electrostatic precipitator shunt integration mechanism
【請求項3】電気集塵装置において、集塵極に集塵され
た微細粒子状粉塵(以下ダストという)が下部に落下す
る際、ダストが煙突内に入ることを防止するため、分流
器上部を円錐形としたことを特徴とする電気集塵装置の
分流集約化機構
3. An electric precipitator, in order to prevent dust from entering the chimney when fine particulate dust (hereinafter referred to as dust) collected by the dust collecting electrode falls to the lower part, the upper part of the shunt. Flow concentrating mechanism of the electrostatic precipitator, characterized by the cone shape
JP1996010942U 1996-09-20 1996-09-20 Electrostatic precipitator shunt integration mechanism Expired - Lifetime JP3036083U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1996010942U JP3036083U (en) 1996-09-20 1996-09-20 Electrostatic precipitator shunt integration mechanism

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1996010942U JP3036083U (en) 1996-09-20 1996-09-20 Electrostatic precipitator shunt integration mechanism

Publications (1)

Publication Number Publication Date
JP3036083U true JP3036083U (en) 1997-04-08

Family

ID=43170862

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1996010942U Expired - Lifetime JP3036083U (en) 1996-09-20 1996-09-20 Electrostatic precipitator shunt integration mechanism

Country Status (1)

Country Link
JP (1) JP3036083U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3470144A1 (en) * 2017-10-12 2019-04-17 Aavi Technologies Ltd A collector channel having a flow adjustment device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3470144A1 (en) * 2017-10-12 2019-04-17 Aavi Technologies Ltd A collector channel having a flow adjustment device

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