JPS5982955A - Circulation electrode type electrostatic dust collector - Google Patents

Circulation electrode type electrostatic dust collector

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Publication number
JPS5982955A
JPS5982955A JP57186851A JP18685182A JPS5982955A JP S5982955 A JPS5982955 A JP S5982955A JP 57186851 A JP57186851 A JP 57186851A JP 18685182 A JP18685182 A JP 18685182A JP S5982955 A JPS5982955 A JP S5982955A
Authority
JP
Japan
Prior art keywords
dust collection
electrode
dust
chamber
section
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
JP57186851A
Other languages
Japanese (ja)
Inventor
張 均仁
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP57186851A priority Critical patent/JPS5982955A/en
Publication of JPS5982955A publication Critical patent/JPS5982955A/en
Pending legal-status Critical Current

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  • Electrostatic Separation (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 静電気集塵は気流(空気流)中に浮遊する液体、固体な
どの微粒子に電気力(高圧直流電圧)を作用させこれを
分誦抽集する技術であって、通當はコロナ放電を利用し
て微粒子に電荷を与え、次に電界を作用させてクーロン
力により集塵電極に向って駆動し効率の高い集塵を行う
ことはよく知られている。
[Detailed description of the invention] Electrostatic precipitator is a technology that applies electric force (high voltage DC voltage) to fine particles such as liquids and solids suspended in airflow (airflow) and extracts them separately. It is well known that highly efficient dust collection is achieved by applying a charge to fine particles using corona discharge, and then applying an electric field to drive them toward a dust collecting electrode using Coulomb force.

捷だ静電気集塵装置はその構造形式によって微粒子の荷
′眠と集塵とを同一空間で行う1段式と、別々の空間′
すなわち別々の電界で行う2段寿(2段荷′亀形)とに
大別されろ。本発明は2段式に属するが、従来の集塵装
置の欠点を除去した全く新しい構成と効果を持つ集塵装
置に関するものである。なお本発明は2段以上の連続形
にすることもできる。
Depending on the structure of the static electricity precipitator, there are two types: a single-stage type that stores fine particles and collects dust in the same space, and a separate type that stores particles and collects dust in separate spaces.
In other words, it can be roughly divided into two stages (two stages 'tortoise shape'), which are performed using separate electric fields. Although the present invention belongs to the two-stage type dust collector, it relates to a dust collector having a completely new configuration and effect that eliminates the drawbacks of conventional dust collectors. Note that the present invention can also be of a continuous type with two or more stages.

第11スは従来の2段式静電気集塵器の構成概要図で、
煙々どの気流6は粒度がたとえば5 lt以下の微粒子
のみ含まれるものと1゛る。5μ以上の微粒子は他の公
知の装置にて容易に除去され、5μ」ソトの(:にべ1
−1−を抽1[除去するのは静心気集塵器の最も効果的
々使)開法であるからである。第1図に4パいて1(・
よ荷′it部で煙塵に眠1iirTを与える。6と4(
、)、lJ’l 電jki lj返−Cたとえ(71、
T OKV前?& )N If カJfJ イfりねる
が、−役乙て放電に伴うオゾンや酸化窒素の発生を′少
なくずろために正のコロナ放電か用いられる。この例で
は6は負極の細い金属線、4ば5に対向ずろ比較的表面
積の大きな接地正極である。
No. 11 is a schematic diagram of the configuration of a conventional two-stage electrostatic precipitator.
It is assumed that the smoke air stream 6 contains only fine particles having a particle size of, for example, 5 lt or less. Fine particles larger than 5μ can be easily removed using other known equipment,
This is because removing -1- is the most effective method of using a static air precipitator. Figure 1 shows 4 pads and 1 (・
Give the smoke 1iirT to the smoke and dust in the load section. 6 and 4 (
, ), lJ'l den jki lj return - C analogy (71,
T Before OKV? & )N If KaJfJ If the discharge occurs, a positive corona discharge is used to reduce the generation of ozone and nitrogen oxides accompanying the discharge. In this example, 6 is a thin metal wire of the negative electrode, and opposite to 4 and 5 is a grounded positive electrode with a relatively large surface area.

この荷電部1では中心電極6近くの気体は電離し1]−
負のイオンを生ずるが、夕1周部は電界が弱く種工突電
前は行われず、気体中に含まれろ微粒子はこのイオンを
付着して帯電し、電気力によって集塵部2の集塵′上極
側に、駆動される。このとき放電極に近接した一部の微
粒子は放電電極4に集塵されるが、これは電極の構造上
僅かである。2は集塵部でたとえ(d厚み1酎以下の極
板5を40〜80m11程度の間隔に平行に配置し7、
交互に負の高1EIE電Δbt(50KV 前後)と正
の接地極に接続される。
In this charging section 1, the gas near the center electrode 6 is ionized 1]-
Negative ions are generated, but the electric field is weak in the first part of the evening and is not carried out before the seeding charge.The fine particles contained in the gas adhere to these ions and become charged, and the electric force collects the dust in the dust collecting section 2. ' Driven to the upper pole side. At this time, some particulates near the discharge electrode are collected on the discharge electrode 4, but this is small due to the structure of the electrode. 2 is a dust collection part (d) where electrode plates 5 with a thickness of 1 mm or less are arranged in parallel at intervals of about 40 to 80 m11,
It is alternately connected to the negative high 1EIE voltage Δbt (around 50KV) and the positive ground electrode.

イY;ス屯部1より集塵部2に駆動された帯電微粒子は
極板5Q)−方(この例では正の極板)に刺着集塵され
る。浄た第1図の形式の装置をもう1つ直列1で並べ、
2・1図の装置で集塵し難い微粒子を第2段の装置′f
f1(第1図と同一であるがポ板5の間隔を狭くする)
で捕捉する2段連続形、さらに多段のものも実用されて
いる。
AY; Charged fine particles driven from the bottom part 1 to the dust collecting part 2 stick to the electrode plate 5Q) (the positive electrode plate in this example) and are collected. Arrange another clean device of the type shown in Figure 1 in series,
The fine particles that are difficult to collect with the device shown in Figure 2.1 are collected by the second stage device'f.
f1 (same as Fig. 1, but narrow the gap between the board 5)
A two-stage continuous type that captures images with a 2-stage system, and a multi-stage system are also in use.

これら従来の静電気集塵装置において問題となっている
のは、正、負いずれの電極であっても集塵電極に旧着し
た微粒子・(タスト)を除去する方法であって、集塵量
が豊かで堆積する塵埃が多い実際の場合ンこは少くとも
集塵部2を2紹設けて定期的に入替え、比較的1項繁に
清掃するが一時停止シテハンマリンク(機械的衝撃)、
ブラノンンク、浣1浄等(・こて清掃ずろ等の手段が用
いられている。
The problem with these conventional electrostatic precipitators is the method of removing old particulates and dust that have adhered to the dust collection electrode, whether it is a positive or negative electrode, and the amount of dust collected is In actual cases where there is a lot of accumulated dust, at least two dust collection sections 2 should be installed, replaced regularly, and cleaned relatively frequently, but there should be a temporary stoppage due to mechanical impact.
Techniques such as buranonku, kasuri 1 jo, etc. are used.

このため取扱が厄介で、停止時間が長く、占有面積が大
きく、高価になる々どの欠点があった。斗だ集塵された
塵埃の堆積による再飛散の防止や、使用時間につれて集
塵効率が下ることの対策も重要である。本発明はこれら
の欠点を除くために行ったもので、以下詳細に説明する
This has disadvantages such as being difficult to handle, requiring a long downtime, occupying a large area, and being expensive. It is also important to prevent collected dust from accumulating and scattering again, and to prevent the dust collection efficiency from decreasing over time. The present invention was made to eliminate these drawbacks, and will be described in detail below.

第2図は本発明による静電気集塵装置の構造例1))又
、()′\):γ、ii:、 1R11+升而図、(B
):よlli而断面断面図0)は(B)中の−771(
:+14111図である。(B)[≧811でおいて気
流(50/I以1:の微粒子を介む)6は人ロアを径て
荷電部(光′i1管X1票も四つ)1に入りこ\で帯電
した微粒子−は集J4:lX1t 10に、jiJス動
されろことは第1図と同様である。
Figure 2 shows a structural example of an electrostatic precipitator according to the present invention.
): Yolli cross-sectional view 0) is -771 ( in (B)
:+14111 figure. (B) [At ≧811, the airflow (via fine particles of 50/I or more) 6 enters the charging part (light 1 tube The microparticles are moved to a collection J4:lX1t 10 in the same manner as in FIG.

第2図()\)は集17;13 @1510の断1fj
i図で、本発明のii1点きなる部分を示している。気
流の方向はたとえば紙背かも紙面の方向とし、14は集
塵量1夕の一力の複数並列の固定極で、正、負いずれで
もよいがこ\では負の高圧が与えられるものとする。
Figure 2 ()\) is collection 17; 13 @1510 cut 1fj
Figure i shows the part where point ii is the difference in the present invention. The direction of the air flow is, for example, the direction of the back of the paper or the surface of the paper, and 14 is a plurality of parallel fixed poles that have a force corresponding to the amount of dust collected per night.They can be either positive or negative, but in this case, a negative high pressure is applied.

15は14に対向して正電極(接地)(!:なる循[獄
移動(エンドレス)屯極で、複数のローラ16と図示省
略のモータを用い、′眠1J15はj−ンiレーアに定
められた速度で比較的ゆるやかに電極141・ζ対向し
ながら蛇行し、下記のように10.i lの2字間なり
11県する。15は非常に司鋺性に富む導体よりなる弗
状電極であることが望外しく、た吉え(・;↓扁平−な
廉状に編んだ細いステンレス鋼の扁平Illゼ、′1F
LI+@が用いられろ。第2図(C)は(A)の一部詳
細図で、固定極14は絶縁体23ンこて両端を遮蔽22
に取付けられろ。
15 is a positive electrode (ground) (!: endless movement) opposite to 14, using a plurality of rollers 16 and a motor (not shown); The electrodes 141 and ζ meander at a relatively gentle speed, facing each other, and make 11 prefectures between the two characters 10.i l as shown below. 15 is a flat electrode made of a conductor with very good conductivity. It was undesirable, Tayoshie (・; ↓ Flat Illze of thin stainless steel knitted in a flat shape, '1F
LI+@ should be used. FIG. 2(C) is a partially detailed view of FIG. 2(A).
Be installed on.

本発明の重要事項の1つは集塵部10と集塵電極清掃部
11となぞれそれ独立した部屋に分けて収容したことで
、集塵部1o o)%極の周囲は肋に十分の気密遮蔽2
2が施され清掃部11はさらに仕切り17によってゴミ
搬送部18とも分離されている。集塵部10すなわち気
流清浄室の集塵量(玉+5に41着しまた塵は直ちに電
極清掃部11に運tI′liれろが、電極に刺着した塵
埃は落ちにくく、さらに電荷を保持しているため急速に
は落ちないのか]山側である。そこで電極清掃部11の
入[]緘二は浄′1毘除去装置1?を設けて、集塵循■
股ベルト′眠極15に付着している塵埃の保イイ屯荷を
逆極・l・の′市川をんえて中和消失させ一塵埃すなわ
ちコミのホッパー状清掃部71への落ドヲ容易[する。
One of the important features of the present invention is that the dust collection section 10 and the dust collection electrode cleaning section 11 are housed in separate rooms, so that the area around the dust collection section 1o o)% pole is sufficient for the ribs. Airtight shielding 2
2, and the cleaning section 11 is further separated from the dust conveying section 18 by a partition 17. The amount of dust collected in the dust collection unit 10, that is, the airflow cleaning chamber (41 particles landed on the ball +5), and the dust should be immediately transported to the electrode cleaning unit 11, but the dust stuck to the electrodes is difficult to fall off and further retains the charge. Therefore, the entrance of the electrode cleaning section 11 is equipped with a cleaning device 1 and a dust collection circulation system.
A large amount of dust adhering to the crotch belt's sleeping pole 15 is neutralized and disappears by placing it in the reverse pole L's Ichikawa, so that the dust, i.e., the dust, can easily fall into the hopper-like cleaning section 71. do.

20はベルト酸(夕15に打撃(ハフ−2−リング)を
−りえてゴミを除去する回転ハンマー、21はベルミル
状電極15にプランシンクを行い′市価上のゴミを除く
金属線などで製作したプランである。
20 is a rotary hammer that removes dust by applying a blow (huff ring) to the bell mill electrode 15, and 21 is a metal wire that removes dust on the bell mill-shaped electrode 15. This is the plan.

なお咀塵部10と集i7μ′市(會清掃部11とは室内
気比を回・−にする心安があり、画室は同一気圧になる
j二うに′完全に夕(部、と遮蔽する。遮蔽22から旨
fi′に都11にベルト状′上極]5が出入するノ繕・
ま′諷(+jly + 5が薄い帯状で接地]りである
のでごく小さくて、■い。芥た清掃部11の底部b・こ
は周知のスルースバルブ(5luice va’lve
 、仕切り弁)12を設置し、このバルブを回転ずれは
コミは室の気圧に影響を力えることなく直ちにヘルドコ
ンベア〕6−4二に押出され、集塵装置の夕を部にシュ
ータなとによって自動的に運び出されろ。従って清掃落
下したコミが飛散して1[J汚染するなどのおそれもな
い。
In addition, the dust collecting section 10 and the gathering room cleaning section 11 can be safely shielded from each other by keeping the indoor air ratio between 1 and 2, and the room has the same atmospheric pressure. The belt-shaped upper pole 5 enters and exits from the shield 22 to the top 11.
The bottom b of the cleaned part 11 is a well-known sluice valve.
, a gate valve) 12 is installed, and if the rotation of this valve deviates, the dust is immediately pushed out to the held conveyor] 6-42 without affecting the air pressure in the chamber, and a chute is installed in the dust collector's space. be automatically carried away by. Therefore, there is no risk of dust particles falling during cleaning scattering and causing contamination.

こ0)ように2つの区切り間を循環移動する電極15を
用いた場合には、集塵部10で集塵したコミが集塵電極
15の面νこf=J着しているものを清掃部11に運び
、そこで電極面の清掃をイ]い清浄化された電極15は
再び集塵部]0に戻り、いつも最も請浄な電極面で集塵
を白うことを無限に繰返l〜で行うことができる。こび
〕ため本発明装置は集塵効率が高い(d:かりでなく、
電極の清掃のために装置を停Ca停止する心安がなく、
稼動率が商いとυθう効果が得ら”(tろ。
When using the electrode 15 that circulates between two partitions as shown in Fig. 0), it is necessary to clean the dust collected in the dust collection section 10 that has adhered to the surface of the dust collection electrode 15. The cleaned electrode 15 is carried to the dust collection section 11, where the electrode surface is cleaned.The cleaned electrode 15 is returned to the dust collection section 0, and the process of collecting dust on the cleanest electrode surface is repeated indefinitely. It can be done with ~. Because of this, the device of the present invention has high dust collection efficiency.
I don't have the peace of mind to stop the device to clean the electrodes,
The effect of increasing the operating rate is υθ.

集塵効率についても従来の集塵装置では一般に気流清浄
と′電極(′^掃とを時(↑;]足置いて同一場所、同
一空間で行っているのに対して、本発明の集塵装置では
2つの別/2な場所で集塵と清掃とをそれぞれ独立に行
い、集塵′電極を2つの場所(区分)の間を絶えず循環
させろθ)で、集塵効率は本発明装置の方か著しく優れ
ていイ;)。
In terms of dust collection efficiency, conventional dust collection equipment generally performs airflow cleaning and 'electrode ('^^ cleaning) in the same place and space at different times (↑;), whereas the dust collection of the present invention In the device, dust collection and cleaning are performed independently at two separate/two locations, and the dust collection electrode is constantly circulated between the two locations (sections).The dust collection efficiency of the device of the present invention is That's significantly better ;).

4 図面り)筒中、な説明 第1L’:i (i従来の静電気集塵器の構成概敬図、
3・2図は本発明itCよる静電気集塵器置の構造例図
で、fAlは上前1イノi INtll:イ]、jB)
は側面断面図、(C)ば[B)の一部左ηイill +
図−(二あ イ)。
4 Drawing) Inside the cylinder, explanation 1st L': i (i Schematic diagram of the configuration of a conventional electrostatic precipitator,
Figures 3 and 2 are structural examples of an electrostatic precipitator device according to the present invention.
is a side sectional view, (C) is a part of the left side of [B]
Figure-(2a-a).

1・・・荷電部、  2.コ0・・・集塵部(集塵室)
、5・・中心電極、  4・・3に対する放電電極、5
・・集塵部電極、  6・・・汚れた入力気流、  7
・・・気流感の入口、  8・・・清浄された気流出口
、9−・・清浄気流、  11・・・ホッパ状電極晴掃
j<B、コ2 スルースハル7’、  +3・・・ヘル
ドコンベア、14 、1!5  ・集l″:堅部の対向
ずろIY、ftの電極で14ば(j;l定、15は連続
して動く循虚電(函、  16・・・τコーラ、  1
7・・什1ノノリ、  18・・・コミ搬jA部、19
・・・静電除ハ装置、  20・・ハンマー、2トブン
7・、  22・・遮14シ、  26・・絶隊体。
1...Charging part, 2. Co0...Dust collection section (dust collection chamber)
, 5...center electrode, 4...discharge electrode for 3, 5
...Dust collecting part electrode, 6...Dirty input airflow, 7
...Airflow inlet, 8.Cleaned air outlet, 9-.Cleaned airflow, 11.Hopper-shaped electrode cleaning j<B, ko2 through hull 7', +3.Heald conveyor. , 14 , 1!5 ・Collection l'': Opposing gap IY, ft electrode on stiff part, 14 ba (j; l constant, 15 is a continuously moving circulating imaginary current (box, 16...τ cola, 1
7... 1 tithe, 18... Komi Transport JA Department, 19
...Static electricity removal device, 20..Hammer, 2 parts, 7., 22..Shielding 14., 26..Zone unit.

持1拍出願人   張  均  仁 代理人 大塚 学 タリ名 第 I M 第 2 (A) 晒 2 閃 (C+   +gApplicant: Ren Zhang Agent Manabu Otsuka Tali name No. IM 2nd (A) Bleaching 2 Flash (C+ +g

Claims (1)

【特許請求の範囲】[Claims] 荷電部吉集塵部とよりなる静電気集塵装置の集塵部を集
塵室と集塵成極清掃室とに区分し集塵室には正寸たは負
の直流高電圧を与えた複数並列設置の固定同極性の電極
群さ、これらの固定覗極群と反対の極性で接地電位にあ
り固定電極群の冬眠(ヴに対向しつつ連続して蛇行し上
記区分の2室に亘って循環移動する帯状の循環移動電極
点を備え、捷だ集塵電極清浄室には残留電荷を中第1−
ずろ静電除去装置其他の塵埃除去装置を備えて、集塵室
にて循環覗袷面にてイ」着せる塵埃を集塵電極清掃室中
を循環移動電極が移動する時間内に除去し集塵室内の循
環電極面を常に清浄に保つこと乞特歯吉する循環上極式
静電気集塵装置。
The dust collection section of the electrostatic precipitator, which consists of a charging section and a dust collection section, is divided into a dust collection chamber and a dust collection polarization cleaning chamber. Groups of fixed electrodes of the same polarity installed in parallel, which are at ground potential with opposite polarity to the group of fixed viewing electrodes, meander continuously while facing the hibernation of the group of fixed electrodes, spanning the two chambers of the above division. Equipped with a band-shaped circulating electrode point that circulates, the dust collection electrode clean chamber is equipped with a
Equipped with a static electricity removal device and other dust removal devices, the dust that accumulates on the circulation liner surface in the dust collection chamber is removed and collected within the time that the circulating electrode moves in the dust collection electrode cleaning chamber. A circulating upper electrode type electrostatic precipitator that is particularly useful for keeping indoor circulating electrode surfaces always clean.
JP57186851A 1982-10-26 1982-10-26 Circulation electrode type electrostatic dust collector Pending JPS5982955A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57186851A JPS5982955A (en) 1982-10-26 1982-10-26 Circulation electrode type electrostatic dust collector

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57186851A JPS5982955A (en) 1982-10-26 1982-10-26 Circulation electrode type electrostatic dust collector

Publications (1)

Publication Number Publication Date
JPS5982955A true JPS5982955A (en) 1984-05-14

Family

ID=16195753

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57186851A Pending JPS5982955A (en) 1982-10-26 1982-10-26 Circulation electrode type electrostatic dust collector

Country Status (1)

Country Link
JP (1) JPS5982955A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012521866A (en) * 2009-03-27 2012-09-20 エーペーエール2 Method for electrostatic separation of fine-grained mixtures made of various materials and apparatus for carrying out this method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012521866A (en) * 2009-03-27 2012-09-20 エーペーエール2 Method for electrostatic separation of fine-grained mixtures made of various materials and apparatus for carrying out this method

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