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JPS59109258A - Electrostatic precipitator - Google Patents

Electrostatic precipitator

Info

Publication number
JPS59109258A
JPS59109258A JP58224589A JP22458983A JPS59109258A JP S59109258 A JPS59109258 A JP S59109258A JP 58224589 A JP58224589 A JP 58224589A JP 22458983 A JP22458983 A JP 22458983A JP S59109258 A JPS59109258 A JP S59109258A
Authority
JP
Japan
Prior art keywords
dust
electrode
casing
collection electrode
dust collection
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
JP58224589A
Other languages
Japanese (ja)
Inventor
ウイルフリ−ト・シユナ−ベル
ベルント・コロムボ
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.)
Kloeckner Humboldt Deutz AG
Original Assignee
Kloeckner Humboldt Deutz AG
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 Kloeckner Humboldt Deutz AG filed Critical Kloeckner Humboldt Deutz AG
Publication of JPS59109258A publication Critical patent/JPS59109258A/en
Pending 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
    • B03C3/88Cleaning-out collected particles

Landscapes

  • 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】 ーシングを備え、このケーシングの中に集塵電極と放電
電極が設けられ、この集塵電極が管状に形成され、放電
電極が管状の集塵電極の中央を通っており、更に集塵電
極と放電電極で分離された塵を脱塵するための装置が設
けられている静電式集塵機に関する。
[Detailed description of the invention] A dust collection electrode and a discharge electrode are provided in the casing, the dust collection electrode is formed into a tubular shape, and the discharge electrode passes through the center of the tubular dust collection electrode. The present invention further relates to an electrostatic dust collector provided with a device for removing dust separated by a dust collection electrode and a discharge electrode.

西独国特許公開第2919989号から管型電気フィル
ターが知られている。このフィルターの場合、管状の集
塵電極がクッションに載っている複数のセット状単位に
まとめられている。単位にまとめられた管状の集塵電極
は衝撃型振い落し装置と連結されている。この振い落し
装置によって、電気フィルターの運転時に集塵電極が周
期的に垂直方向に振動する。このようにして集塵電極か
ら振い落された塵はガスの流れに逆って電気フィルター
の鞍状底に落下し、そしてスクリューコンベヤによって
中央ホッパー内へ排出される。管状集塵電極の下端部と
未処理ガス供給部の間には、ガスせき止め媒体兼ガス分
配媒体として機能する、らせん形インサートを備えた分
離格子が設けられている。この場合、集塵電極から振い
落された塵はガスの流れに逆って分離格子の開口を通っ
てフィルター底まで降下しなければならない。従って、
集塵電極から振い落された塵の一部がガス流によって再
び上方へ運ばれ、集塵機の電界で集塵効率に悪影響を及
ぼす。更に、分離格子にガスの渦が形成され、この渦に
より分離格子と集塵電極の間に、電気フィルターを停止
しなければならない程の塵が溜まる。
A tubular electrical filter is known from DE 2919989 A1. In this filter, tubular dust collecting electrodes are assembled into a plurality of set-like units that rest on a cushion. The unitized tubular dust collection electrodes are connected to an impact-type shake-off device. This shake-off device causes the dust collection electrode to periodically vibrate in the vertical direction during operation of the electric filter. The dust thus shaken off from the collecting electrode falls against the gas flow onto the saddle bottom of the electric filter and is discharged by a screw conveyor into a central hopper. Between the lower end of the tubular dust-collecting electrode and the raw gas supply, a separating grid with helical inserts is provided, which serves as gas damming and gas distribution medium. In this case, the dust shaken off from the dust collecting electrode must fall against the gas flow through the openings of the separation grid to the bottom of the filter. Therefore,
A portion of the dust shaken off from the dust collection electrode is carried upward again by the gas flow, and the electric field of the dust collector adversely affects the dust collection efficiency. Furthermore, a gas vortex is formed on the separation grid, and this vortex collects enough dust between the separation grid and the dust collecting electrode that the electric filter has to be shut down.

本発明の課題は、前記の欠点が生じないように、上記構
造の静電式集塵装置を改良することである。
An object of the present invention is to improve the electrostatic precipitator having the above structure so that the above drawbacks do not occur.

この課題は、塵排出樋が脱塵装置と連結された集塵電極
の下方に離して設けられ、かつケーシングの内部の中央
から扇形に広がってケーシング底壁に向って半径方向外
方へ円錐状に延びるように設けられていることによって
解決される。本発明に従って塵排出樋を集塵電極の下方
に配置したことによって、一方では電気フィルターの横
断面全体にわたって未処理ガス流を均一に分配すること
ができ、その際不利な渦が形成されない。他方では集塵
電極と放電電極から振い落されて塵排出樋へ落下する塵
がガス流と再接触しない。従って、分離室内での塵の堆
積や循環を確実に防ぐことができる。
This problem is solved by the fact that the dust evacuation gutter is provided at a distance below the dust collection electrode connected to the dust removal device, and spreads out in a fan shape from the center of the inside of the casing and radially outwards toward the bottom wall of the casing in a conical shape. This problem is solved by the fact that it is provided so as to extend to. By arranging the dust evacuation trough below the dust collecting electrode according to the invention, it is possible, on the one hand, to distribute the untreated gas flow uniformly over the entire cross section of the electric filter, without the formation of undesirable vortices. On the other hand, the dust that is shaken off from the collection and discharge electrodes and falls into the dust discharge trough does not come into contact with the gas stream again. Therefore, accumulation and circulation of dust within the separation chamber can be reliably prevented.

本発明の他の細かい点、特徴および効果は、図に路体し
た実施例の以下の説明から明らかになるであろう。
Other details, features and advantages of the invention will become apparent from the following description of an exemplary embodiment illustrated in the figures.

第1図に示した静電式集塵機は円筒状のケーシング上方
部分1と漏斗状の底部分2とからなっている。ケーシン
グ」二方部分1の上方区域において、管状の集塵電極4
が支持構造体3に弛く懸吊されている。ケーシング上方
部分1の下方区域では管状集塵電極4が案内板5内で小
さな遊びをもって案内されている。この案内板5には、
フィルターケーシングの外側に設けられかつ集塵電極4
を水平方向に周期的に振動ぎせる機械的な脱塵装置すな
わち掃除装置6が作用する。周期的な衝撃がこの機械的
な脱塵装置6から案内板5を経て集塵電極4に加わるこ
とによって、管状の集塵電極4は、案内板5内でのその
遊びが小さいので、きわめて有利に水平方向へ振動する
。集塵電極によって分離された塵はこの振動によって集
塵電極から確実に遊離し、そして集塵電極から下方へ排
出される。
The electrostatic precipitator shown in FIG. 1 consists of a cylindrical upper part 1 of the casing and a funnel-shaped bottom part 2. In the upper region of the two-sided part 1 of the casing, a tubular dust collecting electrode 4
is loosely suspended from the support structure 3. In the lower region of the upper part 1 of the housing, the tubular dust-collecting electrode 4 is guided in a guide plate 5 with a small play. On this information board 5,
A dust collection electrode 4 provided on the outside of the filter casing
A mechanical dust removal device, that is, a cleaning device 6, which vibrates periodically in the horizontal direction operates. By applying periodic shocks from this mechanical dedusting device 6 via the guide plate 5 to the dust collecting electrode 4, the tubular dust collecting electrode 4 is extremely advantageous since its play within the guide plate 5 is small. vibrates horizontally. The dust separated by the dust collection electrode is reliably released from the dust collection electrode by this vibration, and is discharged downward from the dust collection electrode.

相持体8に懸吊された放電電極7が管状集塵電極4の中
央を通っている。相持体8は脱塵のために図示していな
いノッキング装置すなわちハンマーリング装置と作用結
合されている。
A discharge electrode 7 suspended from a carrier 8 passes through the center of the tubular dust collecting electrode 4. The supporting body 8 is operatively connected to a knocking or hammering device (not shown) for dust removal.

集塵電極4と放電電極7の下方にお(・て塵排出樋9,
10が漏斗状底部分2の中に間隔をおいて上下に設けら
れている。この塵排出樋はケージ 5− ング内部の中央から扇形に広がってケーシング底壁2の
方へ半径方向外向きに円錐状に延びるよう設けられてい
る。この場合、上方の塵排出樋10がその下にある塵排
出樋9の間の隙間を覆うように、塵排出樋9,10は配
置されている。よって、塵が塵排出樋9,10の間を通
って下方へ落ちることはない。集塵電極4と放電電極7
を周期的に脱塵するときに樋9,10に落下する塵は漏
斗状底壁2の方へ導かれる。その際、塵がこの領域で、
管12を通って塵排出樋9,10の下方から搬入される
塵含有ガスと接触しないので非常に好都合である。従っ
て、集塵電極4と放電電極7を備えた分離領域は不都合
な塵負荷から守られ、その結果非常に高い集塵効率が得
られる。
Below the dust collection electrode 4 and discharge electrode 7 (・dust discharge gutter 9,
10 are provided one above the other at intervals in the funnel-shaped bottom portion 2. The dust evacuation trough is provided so as to fan out from the center of the interior of the cage 5-ring and extend conically outward in the radial direction towards the bottom wall 2 of the casing. In this case, the dust discharge troughs 9, 10 are arranged such that the upper dust discharge trough 10 covers the gap between the lower dust discharge troughs 9. Therefore, the dust does not pass between the dust discharge troughs 9 and 10 and fall downward. Dust collection electrode 4 and discharge electrode 7
Dust that falls into the gutters 9, 10 during periodic dedusting is guided towards the funnel-shaped bottom wall 2. At that time, dust is in this area,
This is very advantageous since it does not come into contact with the dust-containing gas which is introduced from below the dust discharge troughs 9, 10 through the pipes 12. The separation area with the dust collection electrode 4 and the discharge electrode 7 is thus protected from undesirable dust loads, resulting in a very high dust collection efficiency.

更に、塵排出樋9.10を本発明に従って集塵電極4と
放電電極7の下に配置することにより、塵を含むガスが
集塵機の横断面全体にわたって均一に分配されるので非
常に好都合である。このガスの均一な分配によって、静
電式集塵機内に設けられた集塵電極4と放電電極7をあ
らゆる 6− 方向で均一に負荷することができる。集塵機内でガスか
ら分離された塵は矢印13に沿って底部分2から下方へ
連続的にまたは周期的に排出され、そして塵が遊離した
ガスは集塵機から矢印14に沿って上方へ排出される。
Furthermore, by arranging the dust evacuation trough 9.10 according to the invention below the dust collection electrode 4 and the discharge electrode 7, it is very advantageous that the dust-laden gas is evenly distributed over the entire cross section of the dust collector. . This uniform distribution of gas makes it possible to load the collecting electrode 4 and the discharge electrode 7 provided in the electrostatic precipitator uniformly in all directions. The dust separated from the gas in the dust collector is continuously or periodically discharged downwards from the bottom part 2 along the arrow 13, and the gas from which the dust is liberated is discharged upwards from the dust collector along the arrow 14. .

第2図に示すように、本発明に係る静電式集塵機の管状
集塵電極15が空気圧作動の脱塵装置を備えていると好
都合である。このために、管状の集塵電極15の上方領
域は間隔をおいて上下に設けられた2枚の被覆板16.
17と気密に連結されている。管15は板16と17の
間の領域において管壁にリング状に設けられた多数のス
リット18を備えている。このスリットは管の中心に向
って斜め下方に延びている。突出した圧力例えば10気
圧の空気、蒸気またはその他の不活性ガスが外側から被
覆板16と17の間の室19を通って前記スリット18
に吹込まれ、それによって管状集塵電極15の内壁に付
着している塵が遊離する。
As shown in FIG. 2, it is advantageous if the tubular dust collecting electrode 15 of the electrostatic dust collector according to the invention is equipped with a pneumatically operated dust removal device. For this purpose, the upper region of the tubular dust collection electrode 15 is covered with two covering plates 16.
17 and is airtightly connected. The tube 15 is provided with a number of ring-shaped slits 18 in the tube wall in the region between the plates 16 and 17. This slit extends diagonally downward toward the center of the tube. Air, steam or other inert gas at a projecting pressure, for example 10 atmospheres, passes from the outside through the chamber 19 between the cover plates 16 and 17 into the slit 18.
The dust adhering to the inner wall of the tubular dust collecting electrode 15 is thereby liberated.

この方法でも、静電式集塵機の集塵電極と放電電極を効
果的に脱塵することができる。
This method can also effectively remove dust from the dust collection electrode and discharge electrode of the electrostatic dust collector.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は機械的な脱塵装置を備えた本発明に係る静電式
集塵機の縦断面図、第2図は本発明に係る空気圧式脱塵
装置を備えた管状集塵電極の部分拡大縦断面図である。 l・・−ケーシング 2・・・ケーシング底壁 4・・・集塵電極 6.18・・・脱塵装置 9.10・・・塵排出樋 代理人  江 崎 光 好 代理人  江 崎 光 史
FIG. 1 is a longitudinal sectional view of an electrostatic dust collector according to the present invention equipped with a mechanical dust removal device, and FIG. 2 is a partially enlarged longitudinal section of a tubular dust collecting electrode equipped with a pneumatic dust removal device according to the present invention. It is a front view. l...-Casing 2...Casing bottom wall 4...Dust collection electrode 6.18...Dust removal device 9.10...Dust discharge gutter Agent: Hikaru Esaki Good agent: Hikaru Esaki

Claims (1)

【特許請求の範囲】 ■、 ガスが下方から上方へ流過するケーシングを備え
、このケーシングの中に集塵電極と放電電極が設けられ
、この集塵電極が管状に形成され、放電電極が管状の集
塵電極の中央を通っており、更に集塵電極と放電電極で
分離された塵を脱塵するための装置が設けられている静
電式集塵機において、塵排出樋(9,10)が脱塵装置
(6,18)と連結された集塵電極(4)の下方に離し
て設けられ、かつケーシングの内部の中央から扇形に広
がってケーシング底壁(2)に向って半径方向外方へ円
錐状に延びるよう設けられていることを特徴とする静電
式集塵機。 2、脱塵装置(6)が機械式であることを特徴とする特
許請求の範囲第1項記載の静電式集塵機。 3、脱塵装置(18)が空気圧式であることを特徴とす
る特許請求の範囲第1項記載の静電式集塵機。 4、 ケーシング(1)が円筒状に形成され、かつ漏斗
状底(2)を備えていることを特徴とする特許請求の範
囲第1項から第3項までのいずれか1つに記載の静電式
集塵機。
[Claims] ■. A casing through which gas flows from below to above is provided, a dust collection electrode and a discharge electrode are provided in this casing, the dust collection electrode is formed into a tubular shape, and the discharge electrode is formed into a tubular shape. In an electrostatic dust collector, the dust discharge gutter (9, 10) passes through the center of the dust collection electrode and is further provided with a device for removing dust separated by the dust collection electrode and the discharge electrode. It is provided separately below the dust collection electrode (4) connected to the dust removal device (6, 18), and spreads out in a fan shape from the center of the inside of the casing and radially outward toward the casing bottom wall (2). An electrostatic dust collector characterized by being provided so as to extend in a conical shape. 2. The electrostatic dust collector according to claim 1, wherein the dust removal device (6) is mechanical. 3. The electrostatic dust collector according to claim 1, wherein the dust removing device (18) is of a pneumatic type. 4. The static device according to any one of claims 1 to 3, characterized in that the casing (1) is cylindrical and has a funnel-shaped bottom (2). Electric dust collector.
JP58224589A 1982-12-01 1983-11-30 Electrostatic precipitator Pending JPS59109258A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE19823244397 DE3244397A1 (en) 1982-12-01 1982-12-01 ELECTROSTATIC DUST SEPARATOR
DE32443978 1982-12-01

Publications (1)

Publication Number Publication Date
JPS59109258A true JPS59109258A (en) 1984-06-23

Family

ID=6179509

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58224589A Pending JPS59109258A (en) 1982-12-01 1983-11-30 Electrostatic precipitator

Country Status (7)

Country Link
JP (1) JPS59109258A (en)
BR (1) BR8306502A (en)
DE (1) DE3244397A1 (en)
DK (1) DK547583A (en)
ES (1) ES8406899A1 (en)
FR (1) FR2537015A1 (en)
GB (1) GB2131330A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005103357A (en) * 2003-09-29 2005-04-21 Sawafuji Electric Co Ltd Oil mist collector

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4968330A (en) * 1989-09-01 1990-11-06 Fmc Corporation Apparatus for separating particulates in an electrostatic precipitator
ES2133116B1 (en) * 1997-10-10 2000-03-16 Unisystems S A ELECTROSTATIC FILTER.
DE102015204168A1 (en) 2015-03-09 2016-09-15 Kutzner + Weber Gmbh Electrostatic particle separation device
EP3470144A1 (en) * 2017-10-12 2019-04-17 Aavi Technologies Ltd A collector channel having a flow adjustment device

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE480801C (en) * 1929-08-10 Oski Akt Ges Electric gas cleaner with dust removal channels
US2374715A (en) * 1943-01-20 1945-05-01 Research Corp Adjustable gas distribution means for multiple tube electrical precipitators
US2508133A (en) * 1944-08-29 1950-05-16 Smidth & Co As F L Electric precipitating apparatus
FR1091078A (en) * 1952-11-14 1955-04-06 Air Preheater Device for cleaning, by zones, the collecting tubes of an electrostatic precipitation device
GB796624A (en) * 1955-10-10 1958-06-18 Research Corp Improvements in or relating to electro-static precipitators
GB1411107A (en) * 1972-11-17 1975-10-22 Seversky A P De High-velocity wet electrostatic precipitators for removing gaseous and particulate contaminants
GB1529505A (en) * 1975-06-19 1978-10-25 Dart Ind Inc Electrostatic precipitator
US4244814A (en) * 1979-05-14 1981-01-13 Chisso Corporation Floss separator

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005103357A (en) * 2003-09-29 2005-04-21 Sawafuji Electric Co Ltd Oil mist collector

Also Published As

Publication number Publication date
GB2131330A (en) 1984-06-20
DE3244397A1 (en) 1984-06-07
DK547583A (en) 1984-06-02
DK547583D0 (en) 1983-11-30
ES527645A0 (en) 1984-08-16
GB8331843D0 (en) 1984-01-04
ES8406899A1 (en) 1984-08-16
BR8306502A (en) 1984-07-31
FR2537015A1 (en) 1984-06-08

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