JPS5941776B2 - Collected dust removal method and device - Google Patents

Collected dust removal method and device

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Publication number
JPS5941776B2
JPS5941776B2 JP52059336A JP5933677A JPS5941776B2 JP S5941776 B2 JPS5941776 B2 JP S5941776B2 JP 52059336 A JP52059336 A JP 52059336A JP 5933677 A JP5933677 A JP 5933677A JP S5941776 B2 JPS5941776 B2 JP S5941776B2
Authority
JP
Japan
Prior art keywords
dust
dust collection
passage
gas
collection passage
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
Application number
JP52059336A
Other languages
Japanese (ja)
Other versions
JPS53145164A (en
Inventor
隆夫 小松
次郎 加藤
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.)
TORINITEI KOGYO KK
Original Assignee
TORINITEI KOGYO KK
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 TORINITEI KOGYO KK filed Critical TORINITEI KOGYO KK
Priority to JP52059336A priority Critical patent/JPS5941776B2/en
Publication of JPS53145164A publication Critical patent/JPS53145164A/en
Publication of JPS5941776B2 publication Critical patent/JPS5941776B2/en
Expired legal-status Critical Current

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Description

【発明の詳細な説明】 本発明は、狭極間の集塵通路が少なくとも一以上並設さ
れた集塵装置における捕集ダストの除去装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a device for removing collected dust in a dust collector in which at least one dust collection passage between narrow poles is arranged in parallel.

近年、狭極間の集塵通路を多数備えて成る静電集塵装置
は、前記集塵通路内の粉塵捕集用静電界が数茸乃至数十
茸程度の低い電圧で構成できること、また該静電界の構
成されている前記集塵通路への粉塵含有ガスの供給が5
乃至10 mAecという高速で行えることなどの理由
から、装置価格および維持管理経費の低減化、更には装
置規模の小型化が期待できるので、特に処理風量が大き
く、かつ設置面積に制約のある各種の粉塵発生現場にお
いて注目されている。
In recent years, electrostatic precipitators equipped with a large number of dust collection passages between narrow electrodes have been developed in such a way that the electrostatic field for collecting dust in the dust collection passages can be configured with a voltage as low as several to several tens of degrees. The supply of dust-containing gas to the dust collection passage where an electrostatic field is formed is
Because it can perform at high speeds of 10 mAec to 10 mAec, it is expected to reduce the equipment price and maintenance costs, as well as reduce the size of the equipment. It is attracting attention at sites where dust is generated.

しかしながら、該装置は、集塵通路が10乃至50rr
R程度の狭極間であるために、経時と共に該集塵通路内
で捕集され、かつ堆積する粉塵の除去が非常に困難であ
った。
However, this device has a dust collection passage of 10 to 50rr.
Since the distance between the poles is as narrow as R, it is very difficult to remove the dust that is collected and accumulated in the dust collection passage over time.

すなわち、この種の集塵通路における捕集粉塵ノ除去は
、一般にスクレーパー、ブラシ等の摺接部材から成る粉
塵除去機構を各通路間に上下移動自在に保持し、これに
よって機械的に行うものであり、集塵通路が少しでも長
くなると摺接部材の撓みにより安定した摺接が行えず、
その結果、捕集粉赦の確実な除去が期待できなかった。
That is, the removal of collected dust in this type of dust collection passage is generally performed mechanically by holding a dust removal mechanism consisting of sliding members such as scrapers and brushes so as to be movable up and down between each passage. If the dust collection path becomes even slightly longer, the sliding contact member will flex and stable sliding contact will not be possible.
As a result, reliable removal of collected powder could not be expected.

また、前記狭極間から成る集塵通路は、一般に多数並設
されることから、前記除去機構の構造が必然的に複雑化
するために、摺接部材の消耗による交換時、その作業性
が極めて悪かった。
In addition, since a large number of dust collection passages consisting of the narrow electrode spaces are generally arranged in parallel, the structure of the removal mechanism is inevitably complicated, so that the workability is reduced when replacing the sliding contact member due to wear. It was extremely bad.

更に、正常運転時における前記除去機構の絶縁維持対策
が難かしく、場合によっては、集塵通路内に死角が生じ
、集塵効率の低下の原因ともなっていた。
Furthermore, it is difficult to maintain the insulation of the removal mechanism during normal operation, and in some cases, a blind spot is created in the dust collection passage, causing a reduction in dust collection efficiency.

しかして最近、この種の狭極間の集塵通路における捕集
粉塵の除去手段として、噴射液体流を用いるととが試み
られている。
Recently, however, attempts have been made to use a jetted liquid stream as a means for removing the collected dust in this type of narrow dust collection passage.

たしかに、前記噴射液体流を用いた除去手段は、従来の
除去手段と比較して、確実性、簡便性の面で改善されて
いるが、液体供給源(主として水源)を必要とすること
から設置場所が制約されること、また回収した粉塵の後
処理(分離回収)が困難なことなどの不可避々問題を帯
有しているために、該手段も必ずしも満足された解決策
とは云えなかった。
It is true that the removal means using the jetted liquid stream is improved in terms of reliability and simplicity compared to conventional removal means, but it requires a liquid supply source (mainly a water source), so it is difficult to install. This method could not necessarily be said to be a satisfactory solution, as it had unavoidable problems such as space restrictions and difficulty in post-processing (separation and recovery) of the collected dust. .

以上の説明の通り、この種の狭極間の集塵通路から成る
装置は、広極間のものと較べて種々特徴を有しているが
、未だ捕集粉塵の除去の点で解決すべき問題が残されて
いるために、あまり実用化されていないのが現状である
As explained above, this type of device consisting of a dust collection passage between narrow poles has various features compared to one between wide poles, but there are still problems to be solved in terms of removing the collected dust. Currently, it is not put into practical use much because of the remaining problems.

そこで、本発明者等は、処理風量が大きく、かつ設置面
積に制約のある粉塵発生現場において、その最適使用が
期待できる前記狭極間の集塵通路から成る装置の実用化
を図るために鋭意研究を重゛ねた結果、処理対象の粉塵
をダストのごとく非粘着性のものに特定することにより
、前記集塵通路面に捕集された粉塵(ダスト)の除去が
、その処理時、集塵通路内に残存するガス体を循環流動
させ、この循環気体流を前記集塵通路内のダスト捕集面
に向ってダスト含有ガスの流れ方向とほぼ平行な方向に
噴射するだけで、極めて簡単かつ確実に除去できること
を見出した。
Therefore, the present inventors have worked hard to put into practical use a device consisting of the dust collection passage between the narrow electrodes, which can be expected to be optimally used in dust generating sites where the processing air volume is large and the installation area is limited. As a result of repeated research, by specifying the dust to be treated as non-adhesive dust, we were able to remove the dust collected on the dust collection passage surface during the treatment. It is extremely simple, just by circulating the gas remaining in the dust passage and injecting this circulating gas flow toward the dust collection surface in the dust collection passage in a direction almost parallel to the flow direction of the dust-containing gas. It was also found that it can be removed reliably.

しかして、上記知見に基づく本発明によれば狭極間の集
塵通路が少なくとも一以上並設された静電集塵装置にお
ける捕集ダストの除去装置であって、 該除去装置は、前記集塵通路の両端部を閉鎖するための
開閉機構と、密閉された集塵通路内のガス体を該集塵通
路の一端から吸引しかつ他端から再導入するための循環
通路と、該循環通路の適宜な場所に配設される循環気体
流形成機構と、前記循環気体流を前記集塵通路内のダス
ト捕集面に向ってダスト含有ガスの流れ方向とほぼ平行
な方向に噴射するだめの噴射機構とで構成されることを
特徴とする捕集ダストの除去装置が提供される。
According to the present invention based on the above knowledge, there is provided a device for removing collected dust in an electrostatic precipitator in which at least one dust collection passage between narrow electrodes is arranged in parallel, the removal device comprising: an opening/closing mechanism for closing both ends of the dust passage; a circulation passage for sucking the gas in the sealed dust collection passage from one end of the dust collection passage and reintroducing it from the other end; and the circulation passage. a circulating gas flow forming mechanism disposed at an appropriate location, and a mechanism for injecting the circulating gas flow toward the dust collection surface in the dust collection passageway in a direction substantially parallel to the flow direction of the dust-containing gas. There is provided a collected dust removal device characterized by comprising an injection mechanism.

本発明における狭極間集塵通路とは、極間距離が5乃至
6〇一度の間隙のものを総称する。
In the present invention, the narrow inter-electrode dust collecting passage generally refers to those with an inter-electrode distance of 5 to 60 degrees.

通常、前記狭極間集塵通路を形成する一方の極には、一
般的に云って5乃至30KV程度の高電圧が印加され、
これによって他方の極との間にダスト捕集用静電界が構
成される。
Usually, a high voltage of approximately 5 to 30 KV is applied to one pole forming the narrow inter-electrode dust collection passage,
This creates a dust-collecting electrostatic field between the other pole and the other pole.

また、前記集塵通路を形成する一対の電極の組合せは、
平板対平板或は線対平板が一般的である。
Furthermore, the combination of the pair of electrodes forming the dust collection passage is
Plate-to-plate or wire-to-plate is common.

この組合せにおいて、前者の平板対平板を採用する場合
には、後者の線対平板のものと異なって、集塵通路内で
の荷電作用が殆んど行われ々いために、排ガス中のダス
トを前記集塵通路に供給する前に予めイオン化しておく
ことが必要である。
In this combination, when the former flat plate-to-flat type is used, unlike the latter wire-to-flat type, since almost no charging action takes place in the dust collection passage, the dust in the exhaust gas is It is necessary to ionize the dust in advance before supplying it to the dust collecting passage.

このガス中のダストをイオン化させるための荷電域は、
荷電電極と対極との間に積極的かつ安定なコロナ放電が
発生するものであるならば任意の構造のものが何等制限
なく採用し得る。
The charge range for ionizing dust in this gas is
Any structure can be adopted without any restriction as long as it generates active and stable corona discharge between the charged electrode and the counter electrode.

なお、前記荷電域を構成するだめの荷電電極は、1問以
下の導電性細線か或は対極に対向する荷電電極面を尖鋭
化した導電性部材が好ましく採用される。
It is to be noted that, as the remaining charging electrode constituting the charging region, a conductive thin wire having one or less conductive wires or a conductive member having a sharpened charging electrode surface facing the counter electrode is preferably employed.

以下に本発明の一実施例を添附図面に基づいて詳細に説
明する。
An embodiment of the present invention will be described in detail below with reference to the accompanying drawings.

第1図は、狭極間の集塵通路1が少なくとも一以上並設
された集塵装置21における捕集ダストの除去装置を説
明するだめの一部系統的断面図であって、本発明の装置
の特徴は、前記集塵通路1の両端部を閉鎖するための開
閉機構32および33と、密閉された集塵通路1内のガ
ス体を該集塵通路1の一端から吸引しかつ他端から再導
入するための循環通路5と、該循環通路5の適宜な場所
に配設されるファン或はブロアー等の循環気体流形成機
構6と、前記循環気体流を前記集塵通路1内の平板状集
塵電極23および高電位維持電極26、すなわちダスト
捕集面に向ってダスト含有ガスの流れ方向とほぼ平行表
方向に噴射するための噴射機構35とで構成されること
にある。
FIG. 1 is a partial systematic sectional view illustrating a device for removing collected dust in a dust collector 21 in which at least one dust collection passage 1 between narrow electrodes is arranged in parallel, The device is characterized by opening/closing mechanisms 32 and 33 for closing both ends of the dust collection passage 1, and for sucking the gas inside the sealed dust collection passage 1 from one end of the dust collection passage 1 and from the other end. a circulating gas flow forming mechanism 6 such as a fan or blower disposed at an appropriate location in the circulating gas flow, and a circulating gas flow forming mechanism 6 for reintroducing the circulating gas into the dust collection channel 1. It is composed of a flat dust collecting electrode 23 and a high potential sustaining electrode 26, that is, an injection mechanism 35 for injecting the dust toward the dust collecting surface in a direction substantially parallel to the flow direction of the dust-containing gas.

本実施例における集塵通路1は、大地電位に維持される
平板状集塵電極23と、該集塵電極23に10rrrI
n程度の間隙で離隔対向し、かつ8乃至10KV程度の
高電圧が高電圧発生装置24に高電圧ケーブル25を介
して電気的に接続される平板状高電位維持電極26とで
形成されているが、何もこれに限定されることはなく、
大地電位に維持される平板状集塵電極と、該平板状集塵
電極に10m程度の間隙で離隔対向し、かっ8乃至10
茸程度の高電圧が印加維持される径]−m以下、好まし
くは0.8園以下の細線状荷電電極とによって構成させ
てもよい。
The dust collection passage 1 in this embodiment includes a flat dust collection electrode 23 maintained at ground potential, and a 10rrr I
It is formed of a plate-shaped high potential sustaining electrode 26 that faces apart from each other with a gap of about n, and a high voltage of about 8 to 10 KV is electrically connected to the high voltage generator 24 via a high voltage cable 25. However, nothing is limited to this,
A flat dust-collecting electrode maintained at ground potential, and facing the flat dust-collecting electrode with a gap of about 10 m.
It may also be configured by a thin wire-shaped charged electrode having a diameter of less than -m, preferably less than 0.8 mm, at which a voltage as high as that of a mushroom can be maintained.

また、本実施例においては、前述の通り、集塵通路1を
平板対平板の組合せで形成させたことから、該集塵通路
1の前側に直径約0.8rIunの細線状荷電電極27
と、該荷電電極27から10乃至20rrvn程度離隔
対向し、かつ大地電位に維持された格子状の対極28と
で構成される荷電域29が備えられている。
In addition, in this embodiment, as described above, since the dust collection passage 1 is formed by a combination of flat plates, a thin wire-shaped charging electrode 27 with a diameter of about 0.8 rIun is provided on the front side of the dust collection passage 1.
and a grid-shaped counter electrode 28 which faces the charging electrode 27 at a distance of about 10 to 20 rrvn and is maintained at ground potential.

対極28として格子状部材を採用するとガス流の整流と
ガス流中の微細ダストの凝集粗大化等の各作用効果が期
待できるが、熱論本発明における荷電域29の構成は何
等これに限定されるもので々く、前記荷電電極27と対
極28との間に積極的かつ安定なコロナ放電が得られる
構成ならば任意に採用し得る。
If a lattice-like member is used as the counter electrode 28, various effects such as rectification of the gas flow and coagulation and coarsening of fine dust in the gas flow can be expected, but the configuration of the charged region 29 in the present invention is not limited to this in any way. Of course, any structure can be adopted as long as it is possible to obtain a positive and stable corona discharge between the charging electrode 27 and the counter electrode 28.

通常、前記荷電電極27には、5乃至20KV程度の高
電圧が高電圧ケーブル30を介して高電圧発生装置31
より供給される。
Usually, a high voltage of about 5 to 20 KV is applied to the charging electrode 27 via a high voltage cable 30 to a high voltage generator 31.
Supplied by

しかして、トンネル等のダスト発生源(図示せず)にて
形成されたダスト含有ガスは、ダストを介して多数並設
された集塵通路1を備えた集塵装置21の本体内に供給
されて静電作用により清浄化される。
Therefore, the dust-containing gas formed in a dust generation source (not shown) such as a tunnel is supplied through the dust into the main body of the dust collector 21, which is equipped with a large number of dust collection passages 1 arranged in parallel. It is cleaned by electrostatic action.

このダスト含有ガスの清浄化処理において、常時一定の
捕集効率を維持するためには、すでに知られているよう
に、前記集塵通路1を構成する平板状集塵電極23と、
該平板状集塵電極23に離隔対向する平板状高電位維持
電極26とに各々経時と共に捕集されて堆積するダスト
を適宜に除去することが必要である。
In this cleaning process of dust-containing gas, in order to maintain a constant collection efficiency at all times, as is already known, the flat dust collecting electrode 23 constituting the dust collecting passage 1,
It is necessary to appropriately remove the dust that is collected and deposited over time on the flat high-potential sustaining electrode 26 which is spaced apart from and faces the flat dust collecting electrode 23.

本発明における捕集ダストの除去の特徴は、前述の通り
、捕集ダストが非粘着性物質であることに着目し、集塵
通路1の両端部を開閉機構32および33を閉じること
によって閉鎖してダスト含有ガスの流れを遮断し、この
密閉された集塵通路1内に循環通路5および循環気体流
形成機構6によって循環気体流を形成して、この循環気
体流を前記集塵通路1内の平板状集塵電極23および高
電位維持電極26、すなわちダスト捕集面に向って噴射
機構35からダスト含有ガスの流れ方向とほぼ平行な方
向に噴射することによって、捕集ダストを吹掃除去する
ことにある。
As mentioned above, the feature of removing the collected dust in the present invention is that the collected dust is a non-adhesive substance, and both ends of the dust collecting passage 1 are closed by closing the opening/closing mechanisms 32 and 33. The flow of the dust-containing gas is cut off, a circulating gas flow is formed in the sealed dust collecting passage 1 by the circulating passage 5 and the circulating gas flow forming mechanism 6, and this circulating gas flow is passed through the dust collecting passage 1. The collected dust is blown away by spraying from the jetting mechanism 35 toward the flat dust collecting electrode 23 and the high potential maintaining electrode 26, that is, the dust collecting surface in a direction substantially parallel to the flow direction of the dust-containing gas. It's about doing.

前記循環気体流の形成は、前述の通り、集塵通路1が密
閉されかつ高電圧の供給が停止された時、前記集塵通路
1内に存在するガス体を該集塵通路1の一端から吸引し
、かつ他端から再導入するだめの循環通路5に配設され
る循環気体流形成機構6によって行なわれる。
As described above, the circulating gas flow is formed by removing the gas present in the dust collecting passage 1 from one end of the dust collecting passage 1 when the dust collecting passage 1 is sealed and the supply of high voltage is stopped. This is carried out by a circulating gas flow forming mechanism 6 disposed in the circulation passage 5 of the reservoir, which is sucked in and reintroduced from the other end.

通常、前記循環気体流は、少々くとも1mAec以上の
流速で集塵通路1に供給され、これによって集塵通路面
から捕集されたダストが除去される。
Usually, the circulating gas flow is supplied to the dust collection passage 1 at a flow rate of at least 1 mAec or more, thereby removing the collected dust from the dust collection passage surface.

なお、前記循環気体流によって集塵通路面から除去され
たダストを集塵通路1の下部から直接外部に排出する場
合には、集塵通路1内を流れる前記循環気体流の風速は
あまり速くない方が好ましい。
Note that when the dust removed from the dust collection passage surface by the circulating gas flow is directly discharged to the outside from the lower part of the dust collection passage 1, the wind speed of the circulating gas flow flowing inside the dust collection passage 1 is not very high. is preferable.

即ち、集塵通路面から除去されるダストは、凝集粗大化
しているので、風速が遅いとその自重により大部分が低
部13に沈降し、また、低部13に沈降しないで循環気
体流中に混入する場合であっても、その循環過程におい
てその殆んどが前記低部13に沈降するからである。
That is, since the dust removed from the dust collection passage surface is agglomerated and coarsened, if the wind speed is slow, most of it will settle in the lower part 13 due to its own weight, and it will not settle in the lower part 13 but will remain in the circulating gas flow. This is because even if it is mixed into the water, most of it will settle in the lower part 13 during the circulation process.

前記捕集ダストの除去処理においては、その循環気体流
の流速を一定に維持させて行うよりも経時と共に遅くな
るようにして行うことが確実かつ短時間にダストを回収
できるので好ましい。
In the removal process of the collected dust, it is preferable to perform the process by slowing down the flow rate of the circulating gas flow over time rather than by maintaining the flow rate constant, because the dust can be collected reliably and in a short time.

前記低部13に沈降したダストは、その低部13に形成
されるパンチングメタル、金網、格子部材等の所謂多孔
性部材14を介してダスト回収槽15に回収され、次い
でバイブレータ−16の振動作用を受けて一箇所に集め
られ、しかる後適宜に外部に排出される。
The dust settled in the lower part 13 is collected in a dust collection tank 15 through a so-called porous member 14 formed in the lower part 13 such as a punching metal, a wire mesh, a lattice member, etc., and is then collected by the vibration action of a vibrator 16. It is collected in one place and then discharged to the outside as appropriate.

本実施例における前記循環気体流を用いた捕集ダストの
除去は、集塵通路1内へのダスト含有ガスおよび高電圧
の供給が遮断され、かつ前記集塵通路1を備える本体内
が密閉された状態下で行われるので、捕集ダストの除去
が簡単かつ確実に行なえる。
In this embodiment, the collected dust is removed using the circulating gas flow when the supply of dust-containing gas and high voltage to the dust collection passage 1 is cut off, and the inside of the main body including the dust collection passage 1 is sealed. Since the removal is carried out under the same conditions, the collected dust can be easily and reliably removed.

前記集塵通路1へのダスト含有ガスの供給遮断および該
通路1を密閉にするには、ガス導入側のダクト内に設け
られるダンパー32とガス排出側に設けられる他のダン
パー33とを閉じることによって行う。
In order to cut off the supply of dust-containing gas to the dust collection passage 1 and to seal the passage 1, the damper 32 provided in the duct on the gas introduction side and the other damper 33 provided on the gas discharge side are closed. done by.

また高電圧供給の遮断は、前記高電圧発生装置24の入
力側または出力側を制御することによって行う。
Further, the high voltage supply is cut off by controlling the input side or the output side of the high voltage generator 24.

また、前記循環通路5の各端部側には、ダンパー19,
20が配設され、捕集ダストの除去処理時のみ集塵通路
内のガス体を循環通路5を通して循環流動をさせるよう
に々っている。
Furthermore, dampers 19,
20 is arranged so that the gas in the dust collection passage is circulated through the circulation passage 5 only during the removal process of the collected dust.

前記各ダンパー32.33,19,20、高電圧発生装
置24、ファン6の各作動は、前記集塵通路1内で捕集
されるダストの付着状態を経時と共に監視し、成る一定
状態になったとき制御信号を発生させて自動的に関連制
御させる。
Each operation of the dampers 32, 33, 19, 20, the high voltage generator 24, and the fan 6 is performed by monitoring the state of adhesion of the dust collected in the dust collection passage 1 over time to maintain a constant state. When this happens, a control signal is generated to automatically perform related controls.

前記経時変化に係わる捕集ダストの監視は、集塵電極2
3に電流計を配設して放電電流の変化を検出すること、
或は排ガスの排出側に濃度計を配設して排ガス濃度の変
化を検出すること等の公知手段によって行われる。
Monitoring of the collected dust related to the change over time is carried out using the dust collecting electrode 2.
3 to detect changes in discharge current by installing an ammeter;
Alternatively, this can be carried out by known means such as arranging a concentration meter on the exhaust gas exhaust side to detect changes in the exhaust gas concentration.

なお本発明における前記捕集ダストの除去は、前述の通
り、その処理時ダスト含有ガスの清浄化作業を中断した
状態で行うことから、通常、前記構造の装置21が少な
くとも二以上並設されて選択操作される方が望ましい。
Note that, as described above, the collected dust in the present invention is removed while the cleaning operation of the dust-containing gas is interrupted during the processing, so normally at least two or more devices 21 having the above structure are installed in parallel. It is preferable to use a selection operation.

しかして、前記捕集ダストの除去処理が終了すると、集
塵通路1内へのダスト含有ガスおよび高電圧の各供給が
自動的に復帰し、これによって、ダスト含有ガスの溝状
化処理が再開される。
When the removal process of the collected dust is completed, the supply of dust-containing gas and high voltage to the dust collecting passage 1 is automatically restored, thereby restarting the groove-forming process of the dust-containing gas. be done.

なお、この場合、ダスト含有ガスの供給に先立ち、高電
圧供給を予め先に行っておくことが、運転再開時におけ
るダストの再飛散を防止する上で好ましい。
In this case, it is preferable to supply high voltage in advance before supplying the dust-containing gas in order to prevent the dust from scattering again when restarting the operation.

また、捕集ダストの除去および排出をより効果的に行な
うには、本実施例に示されている様に、前記循環通路5
の途中に吸引ガス流を清浄化するためのガス清浄機構2
2を設け、それによって循環気体流中のダストを積極的
に分離回収する様にした方が好ましい。
In addition, in order to more effectively remove and discharge the collected dust, as shown in this embodiment, the circulation passage 5
Gas cleaning mechanism 2 for cleaning the suction gas flow during the
2 is preferably provided, thereby actively separating and collecting dust in the circulating gas flow.

即ち、集塵通路1内のダストを循環気体流によって集塵
通路1外に搬出し、循環気体流中に浮遊するダストを循
環通路5の途中に配設されたガス清浄機構22により分
離回収して除去することにより、集塵通路1内において
ダストを沈降させ排出することを考慮しなくてよいので
集塵通路1内に形成される循環気体流の風速をより高め
ることができ、これにより集塵通路面のダストの除去が
より早くかつより確実に行なえるからである。
That is, the dust in the dust collection passage 1 is carried out to the outside of the dust collection passage 1 by the circulation gas flow, and the dust floating in the circulation gas flow is separated and collected by the gas cleaning mechanism 22 disposed in the middle of the circulation passage 5. Since there is no need to consider settling and discharging the dust in the dust collection passage 1, the wind speed of the circulating gas flow formed in the dust collection passage 1 can be further increased. This is because the dust on the dust passage surface can be removed faster and more reliably.

本発明におけるガス清浄機構22とは、バックフィルタ
ー、電気集塵機、サイクロン等のそれ自体公知の各種ガ
ス清浄機構を総称する。
The gas cleaning mechanism 22 in the present invention is a general term for various gas cleaning mechanisms known per se, such as a back filter, an electrostatic precipitator, and a cyclone.

特に本発明に用いられる前記各種のガス清浄機構22は
、循環気体流中に混入されるダストが凝集粗大化されて
おり、かつその処理風量が比較的少なく、シかも該ガス
清浄機構22において完全にガスを清浄化する必要のな
いことから、著しく小型化されかつ比較的簡単な構造の
もので良い。
In particular, in the various gas cleaning mechanisms 22 used in the present invention, the dust mixed into the circulating gas flow is aggregated and coarsened, and the processing air volume is relatively small. Since there is no need to clean the gas, it can be significantly miniaturized and have a relatively simple structure.

また、該機構22は、前記狭極間の集塵通路1を多数備
えた装置21がユニット化され多設される場合であって
も、選択的切換操作を行うことにより一基で良い。
Further, even if the device 21 having a large number of dust collection passages 1 between the narrow electrodes is unitized and installed in multiple units, only one mechanism 22 can be provided by performing a selective switching operation.

本実施例においては、前記循環通路5にガス清浄機構2
2が配設さへこれによって集塵通路1に供給される循環
気体流中のダストが集塵通路1部での自重による沈降の
他に前記ガス清浄機構22部で積極的に分離回収される
ので、前記集塵通路1へ供給する循環気体流を比較的小
径な噴射口34から成る噴射機構35を介して効果的に
噴射することができ、その結果より一層有効な除去が行
える。
In this embodiment, a gas cleaning mechanism 2 is provided in the circulation passage 5.
2 is arranged so that the dust in the circulating gas flow supplied to the dust collection passage 1 is not only settled due to its own weight in the dust collection passage 1 part, but also is actively separated and collected by the gas cleaning mechanism 22 part. Therefore, the circulating gas flow supplied to the dust collection passage 1 can be effectively injected through the injection mechanism 35 consisting of the injection port 34 having a relatively small diameter, and as a result, even more effective removal can be achieved.

また、前記ガス清浄機構22を循環通路5に配設したこ
とによ欠循環気体流の流速を比較的速くでき、しかも、
その流速を経時と共に遅くするという必要が全くないた
めに処理時間を著しく短縮化することができる。
Further, by disposing the gas purifying mechanism 22 in the circulation passage 5, the flow rate of the partially circulated gas flow can be made relatively high, and furthermore,
Since there is no need to slow down the flow rate over time, the processing time can be significantly shortened.

本実施例における噴射機構35は、集塵通路1の数に対
応した噴射口34を備えるパイプ材を複数段配設するこ
とによって構成されている。
The injection mechanism 35 in this embodiment is constructed by arranging a plurality of pipe materials having injection ports 34 corresponding to the number of dust collection passages 1 in multiple stages.

熱論、本発明における噴射機構35の構造は、これに限
定されることなく種々の構造のものが採用し得る。
Thermal theory, the structure of the injection mechanism 35 in the present invention is not limited to this, and various structures can be adopted.

通常、該噴射機構35からは少なくとも]、m/sec
以上の流速で循環気体が噴射される。
Typically, the injection mechanism 35 delivers at least ], m/sec.
Circulating gas is injected at the above flow rate.

なお、該噴射気体流は、より少ない風量で確実かつ効果
的な除去を期待するために、噴射機構35が可変して、
変動流となって噴射される場合もあり、その選択は自由
で匍1限されない。
In addition, in order to expect reliable and effective removal of the injected gas flow with a smaller air volume, the injection mechanism 35 is variable.
In some cases, it is injected as a fluctuating flow, and the choice is free and not limited to one.

なお、循環通路5には、気体の吸引量と排出(噴射)量
とのバランスを調整するための制御弁36が設けられて
いる。
Note that the circulation passage 5 is provided with a control valve 36 for adjusting the balance between the suction amount and the discharge (injection) amount of gas.

以上の技術的思想に基づく本発明の装置を処理風量が著
しく多く、かつ排ガス中のダストの主成分が灰分て、し
かも装置の占有面積および水源に制約のある実際の自動
車用トンネル向の静電集塵装置で実施したところ狭極間
の集塵通路から成る装置の特徴が最大限に生かせ、かつ
従来、この種の装置において極めて困難とされていだ捕
集ダストの除去が簡便な手段で確実かつ容易に行えた。
The device of the present invention based on the above-mentioned technical idea is suitable for use in actual automobile tunnels, where the processing air volume is extremely large, the main component of dust in the exhaust gas is ash, and the area occupied by the device and the water source are limited. When implemented with a dust collector, the characteristics of the device consisting of a dust collection passage between narrow electrodes can be maximized, and the collected dust, which has traditionally been considered extremely difficult with this type of device, can be removed reliably with a simple method. And it was easy to do.

また、本発明においては、捕集ダストの除去用気体とし
て、雨等の天候によりその湿度が大きく変化する大気を
直接的に用いることなく、処理等、装置本体内に残存す
る気体を用いるので、気体乾燥装置が不要で、しかも天
候変化にかかわらず常に最適条件でその除去処理が行え
た。
In addition, in the present invention, as the gas for removing the collected dust, the gas remaining in the main body of the device is used for processing, etc., without directly using the atmosphere whose humidity changes greatly depending on the weather such as rain. There was no need for a gas drying device, and the removal process could always be performed under optimal conditions regardless of weather changes.

特に、ガス清浄機構22としてバックフィルターを採用
した場合、前記捕集ダストの除去用気体の選択による作
用効果は顕著に認められた。
In particular, when a back filter was employed as the gas cleaning mechanism 22, the effect of selecting the gas for removing the collected dust was remarkable.

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

第1図は、本発明の一実施例を示す一部系統的断面図で
あって、 側照数字1は狭極間から成る集塵通路、5は循環通路、
6は循環気体流形成機構、21は集塵装置、22はガス
清浄機構、23は平板状集塵電極、24.31は高電圧
発生装置、26は高電位維持電極、32,33は開閉機
構、35は噴射機構を夫々示す。
FIG. 1 is a partial systematic sectional view showing an embodiment of the present invention, in which the side illumination numeral 1 indicates a dust collection passage consisting of a narrow gap, 5 a circulation passage;
6 is a circulating gas flow forming mechanism, 21 is a dust collector, 22 is a gas cleaning mechanism, 23 is a flat dust collection electrode, 24.31 is a high voltage generator, 26 is a high potential maintenance electrode, 32 and 33 are opening/closing mechanisms , 35 indicate injection mechanisms, respectively.

Claims (1)

【特許請求の範囲】 1 狭極間の集塵通路が少なくとも一以上並設された静
電集塵装置における捕集ダストの除去装置であって、 該除去装置は、前記集塵通路の両端部を閉鎖するだめの
開閉機構と、密閉された集塵通路内のガス体を該集塵通
路の一端から吸引しかつ他端から再導入するだめの循環
通路と、該循環通路の適宜な場所に配設される循環気体
流形成機構と、前記循環気体流を前記集塵通路内のダス
ト捕集面に向ってダスト含有ガスの流れ方向とほぼ平行
な方向に噴射するだめの噴射機構とで構成されることを
特徴とする捕集ダストの除去装置。 2 前記循環通路の適宜な場所に、循環するガス流を清
浄化するためのガス清浄機構が配設されることを特徴と
する特許請求の範囲第1項に記載の装置。 3 前記噴射機構が、ガス体を変動流として噴射させる
だめの噴射機構であることを特徴とする特許請求の範囲
第1項に記載の装置。
[Scope of Claims] 1. A device for removing collected dust in an electrostatic precipitator in which at least one dust collection passage between narrow electrodes is arranged in parallel, the removal device comprising: an opening/closing mechanism for a reservoir that closes the dust collection passage; a circulation passage for sucking the gas in the sealed dust collection passage from one end of the dust collection passage and reintroducing it from the other end; A circulating gas flow forming mechanism is provided, and an injection mechanism that injects the circulating gas flow toward a dust collection surface in the dust collection passageway in a direction substantially parallel to the flow direction of the dust-containing gas. A device for removing collected dust. 2. The device according to claim 1, characterized in that a gas cleaning mechanism for cleaning the circulating gas flow is disposed at an appropriate location in the circulation passage. 3. The apparatus according to claim 1, wherein the injection mechanism is an injection mechanism for ejecting the gas body as a fluctuating flow.
JP52059336A 1977-05-24 1977-05-24 Collected dust removal method and device Expired JPS5941776B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP52059336A JPS5941776B2 (en) 1977-05-24 1977-05-24 Collected dust removal method and device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP52059336A JPS5941776B2 (en) 1977-05-24 1977-05-24 Collected dust removal method and device

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP59123645A Division JPS6041559A (en) 1984-06-18 1984-06-18 Process for recovering collected dust in electrostatic dust collector

Publications (2)

Publication Number Publication Date
JPS53145164A JPS53145164A (en) 1978-12-18
JPS5941776B2 true JPS5941776B2 (en) 1984-10-09

Family

ID=13110369

Family Applications (1)

Application Number Title Priority Date Filing Date
JP52059336A Expired JPS5941776B2 (en) 1977-05-24 1977-05-24 Collected dust removal method and device

Country Status (1)

Country Link
JP (1) JPS5941776B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011131132A (en) * 2009-12-22 2011-07-07 Shimizu Corp Welding fume collector

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4839565U (en) * 1971-09-14 1973-05-17

Also Published As

Publication number Publication date
JPS53145164A (en) 1978-12-18

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