JPS58156323A - Filtering type dust collector - Google Patents

Filtering type dust collector

Info

Publication number
JPS58156323A
JPS58156323A JP3950382A JP3950382A JPS58156323A JP S58156323 A JPS58156323 A JP S58156323A JP 3950382 A JP3950382 A JP 3950382A JP 3950382 A JP3950382 A JP 3950382A JP S58156323 A JPS58156323 A JP S58156323A
Authority
JP
Japan
Prior art keywords
filter
fume
dust
mist
charged
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
JP3950382A
Other languages
Japanese (ja)
Inventor
Tsugita Yukitake
雪竹 次太
Kazuichi Saito
斎藤 一一
Keizo Otsuka
大塚 馨象
Isamu Akiba
勇 秋葉
Atsuo Ishida
石田 敦夫
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.)
Hitachi Ltd
Original Assignee
Hitachi Ltd
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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP3950382A priority Critical patent/JPS58156323A/en
Publication of JPS58156323A publication Critical patent/JPS58156323A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To provide a dust collector capable of easily carrying out regeneration of a filter, constituted so as to separately collect mist and fume by using two kinds of different filters. CONSTITUTION:When dust having mist and fume mixed therein introduced from a gas inflow port 1 is introduced into a primary filter 3, oil mist with a coarse particle size is selectively collected. In order to shake off the collected oil mist, a washing liquid supplied from a washing liquid storage tank 5 through a dust separator 6 by a pump 7 is sprayed from a spray nozzle 4 to wash the filter 3. Welding fume passing the primary filter 3 is introduced into a charging apparatus 8 constituted from a discharge electrode 81 and an earth electrode 82 and, while charged by corona discharge generated by applying high voltage between both electrodes, introduced into a secondary filter 9. By electrostatic attraction force acted between charged fume and the filter, high dust collecting efficiency can be obtained with low gas passing loss.

Description

【発明の詳細な説明】 本発明は、気体中に混在して浮遊する液体のミストと固
体の粉じんを分離捕集するろ適業じん様に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a dust filter that separates and collects liquid mist and solid dust mixed and suspended in gas.

防錆油や加工油が塗布された鋼材の溶接作業では、固体
粒子であるヒユームとともに、高熱によって油が気化し
て生ずる液状のミストが生成する。
When welding steel materials coated with anti-corrosion oil or processing oil, a liquid mist is produced when the oil vaporizes due to high heat, as well as solid particles of fume.

この穐の粉じんを従来の乾式のろ適業じん機で捕集する
と、ヒユームとともにミストも捕集されるためにフィル
タの目詰りが早くなるはかりでなく、フィルタが湿りを
帯びヒユームの払い落しが困難となる。したがつ゛て、
従来のろ適業じん方式ではフィルタの交換頻度が高くな
り、保守性が悪いはかりでなく、ランニングコストがか
さむという問題が生じている。このように粘着性を有す
る粉体を捕集するには、一般にはフィルタに捕集された
粉じん等倉払い落すための湿式洗浄方式が用いられてい
る。しかし、溶接ヒユームの如きヒユームの平均粒子径
が0.2μm と極めて微細な粒子を捕集するには、目
開きが非常に小さな高性能フィルタを必要とし、洗浄方
式を採用すると洗浄液によってフィルタの開口部を閉塞
する仁ととな9、フィルタの通風損失が急激に上昇し、
使用に耐え難いという問題が生じた。
If this dust is collected using a conventional dry type filtration machine, the mist will be collected along with the fume, which will cause the filter to become clogged more quickly. It becomes difficult. However,
With the conventional filtration system, the filters have to be replaced more frequently, resulting in problems such as poor maintenance and high running costs. To collect such sticky powder, a wet cleaning method is generally used to remove the dust collected by the filter. However, in order to collect extremely fine particles such as welding fume with an average particle diameter of 0.2 μm, a high-performance filter with extremely small openings is required. 9, the ventilation loss of the filter increases rapidly,
The problem arose that it was difficult to use.

以上の如く、従来の乾式または湿式のろ適業じん方式で
もオイルミスl含む溶接ヒユームの集じん方式には欠点
があり、効果的な集じん方式が望まれている。
As mentioned above, even in the conventional dry or wet filtration method, there are drawbacks to the method for collecting dust from welding fumes containing oil mistakes, and an effective dust collection method is desired.

本発明の目的は、二棟の異ったフィルタを用いて、ミス
トとヒユームをそれそtし分離捕集し、フイルタの再生
が容易に実施できる集じん機を提供するものである。
An object of the present invention is to provide a dust collector in which mist and fume are separately collected using two different filters, and the filters can be easily regenerated.

本発明は、ミストとヒユームの粒子径の差に着目し、粗
粒子のミストのみを一部フィルタで捕集し、−次フィル
タを通過した細いヒユームに電荷を与えることにより二
次フィルタの捕集効果を促進し、前記−次フィルタは洗
浄液により洗浄し二次フィルタは振動によシ摘果された
ヒユームを払い落丁ことを%黴とするろ適業じん機を提
供するものである。
The present invention focuses on the difference in particle size between mist and fume, and collects only part of the coarse mist with a filter, and collects it with a secondary filter by applying an electric charge to the thin fume that has passed through the -order filter. The purpose of the present invention is to provide a filtration and dusting machine in which the secondary filter is cleaned with a cleaning liquid and the secondary filter is shaken off by vibration to eliminate mold.

以下本発明の一実施例を図面に基ついて説明する。An embodiment of the present invention will be described below with reference to the drawings.

第1図は、本発明に係るろ適業じん慎の一実施例の構成
図を示す。1はガス流入孔、2にガス流出孔、3は調法
フィルタ、9は二次フィルタを示し、該−次フィルタ3
と二次フィルタ9とのカス流路中にヒユームにIll 
OIを与える荷vIL装置8とがら構成さ扛る、ファン
11の起動により、ガス流入孔1よシ導入さjLるミス
トとヒュームカ混在した粉じんは、まず−次フィルタ3
に導入さ扛る。
FIG. 1 shows a configuration diagram of an embodiment of the law enforcement agency according to the present invention. 1 is a gas inflow hole, 2 is a gas outflow hole, 3 is a preparation filter, 9 is a secondary filter, and the -order filter 3
In the waste flow path between the secondary filter 9 and the
When the fan 11 is started, the dust mixed with mist and fumes is introduced into the gas inflow hole 1 and is first passed through the next filter 3.
Introduced in the.

−次フィルタ3の構成は、不織の起毛縁lI&をガス流
力向に平行に配列し、十分な通気性を有する構造を待つ
ものでるる。油が産布芒rL7’(母材の浴接に伴って
発生する溶接ヒユーム(固体)とオイルミスト(液体)
の粒子住は、ダストモニタで当発明省等が6111定し
た結果、オイルミストの平均粒子径は1.2μn1に対
し溶接ヒユームは0.2μmと6活の粒径六が認めらf
た。このような粉じん等が−Fフィルタ3に導入’dB
ると、粒子径が粗いオイルミストが選択的に捕集さrし
る。−次フィルタ3を通過するガス流速は3〜5111
/Sと通常のフィルタ果じんの数clT’+/Sの流速
に比べると尚速を南するので、−次フィルタ3における
捕集機楕は、起毛繊維上における慣性衝欠が支配的であ
る。溶接ヒユームの如き0.2μri・の微細な粒子は
慣性力の作用は、#ヨとんど受けないため、−次フィル
タ3では補集さjLない。しかし、長期間の運転ケ行な
うと、−次フィルタ3にも固体のヒユームが堆積するた
めに通風損失が上昇してくる。したがって、−次フィル
タ3に捕促さ′nたヒユーム會払い落すために、洗浄機
1flを設けている。洗浄方法は、洗浄液貯溜タンク5
より、タストセパレータ6を介して、ポンプ7により洗
浄液をスゲレイノズル4より調成フィルタ3に噴霧して
洗浄する 洗浄液は水性または油性でもよい。従来の湿
式洗浄方式と本発明の洗浄方式との大きな違いは、フィ
ルタでの粉じんの捕集方式である。すなわち、従来の方
式では、フィルタは粉じん等(t1iU体9g、体を含
む)を捕集することを目的としているが、本発明では固
体粒子は極力捕集しないために、洗浄液のよどれが極端
に少く、洗浄液の交換または再生などにほとんど手間を
必要としないことにある。
The second filter 3 has a structure in which non-woven raised edges are arranged parallel to the direction of gas flow force and has sufficient air permeability. Oil is produced (welding fume (solid) and oil mist (liquid) generated as the base metal comes into contact with the bath).
The particle size was determined by the Ministry of Invention and others using a dust monitor, and found that the average particle size of oil mist was 1.2 μm, while that of welding fume was 0.2 μm, which was 6111 times.
Ta. Such dust etc. is introduced into the -F filter 3'dB.
As a result, oil mist with coarse particle diameters is selectively collected. -The gas flow rate passing through the filter 3 is 3 to 5111
/S and the normal filter dust number clT'+/S, the flow velocity is southerly, so the collector ellipse in the -order filter 3 is dominated by the inertial gap on the nap fibers. . Fine particles of 0.2 .mu.ri., such as welding fumes, are hardly affected by the inertial force, so they are not collected by the -order filter 3. However, if the filter is operated for a long period of time, solid fumes will also accumulate on the -order filter 3, resulting in an increase in ventilation loss. Therefore, a washing machine 1fl is provided in order to remove the fumes trapped in the -order filter 3. The cleaning method uses the cleaning liquid storage tank 5.
Then, the filter 3 is sprayed with a cleaning liquid from the sedge spray nozzle 4 by the pump 7 through the tasto separator 6 for cleaning.The cleaning liquid may be aqueous or oil-based. The major difference between the conventional wet cleaning method and the cleaning method of the present invention is the method of collecting dust with a filter. In other words, in the conventional method, the purpose of the filter is to collect dust, etc. (including 9 g of t1iU bodies), but in the present invention, since solid particles are not collected as much as possible, the stagnation of the cleaning solution is extremely high. The reason is that it requires little effort to replace or regenerate the cleaning solution.

−次フィルタ3で捕集されたオイルミスト及び惨く一部
の溶接ヒユームは、洗浄液貯油タンク5に貯溜さfシ、
一定の濃度に達したら糸外に排出し、新しい洗浄液と交
換さする。−次フィルタ3を通過した溶接ヒユームは、
放電極81と接地極82で構成された荷を装置8へ導入
される。83は直流商電圧発生!aを示し、放電極81
と接地極82の両&間に高電圧が印力Vさnるとコロナ
放電が発生する。このコロナ放電場を溶接ヒユームが通
過すると、高濃度のイオンによってヒユームはitされ
る。荷電1jet18を通過する時間は数IQmsと非
常に短い時間であるために、荷電装置8ではヒユームは
ほとんど捕集されない。荷電装置8を通過し次帯電−g
nycヒユームは二次フィルタ9に導入される。二次フ
ィルタ9iiナイロンまたはテトロン等のバグフィルタ
であり、ろ過速度は数cm/sである。バグフィルタに
おける帯電ヒユームの儒桑機構は、機憶的な拡散または
衝突等の捕集作用のはかに、帯電ヒユームとフィルタ間
に働く静電誘引力により捕集力は促進されるために、低
い通風損失で商い果しん率を得ることができる。
- The oil mist and some of the welding fumes collected by the next filter 3 are stored in the cleaning liquid oil storage tank 5.
When it reaches a certain concentration, drain it out of the thread and replace it with new cleaning solution. The welding fume that has passed through the -order filter 3 is
A load consisting of a discharge electrode 81 and a ground electrode 82 is introduced into the device 8 . 83 generates DC commercial voltage! a, discharge electrode 81
When a high voltage is applied between V and the ground electrode 82, corona discharge occurs. When the welding fume passes through this corona discharge field, the welding fume is exposed to a high concentration of ions. Since the time for passing through the charging jet 18 is very short, several IQms, the charging device 8 hardly collects the fume. Passes through charging device 8 and is then charged -g
The nyc hum is introduced into a secondary filter 9. Secondary filter 9ii is a bag filter made of nylon or Tetron, and the filtration speed is several cm/s. The mechanism of the charged fume in a bag filter is that the collecting force is promoted by the electrostatic attraction force that acts between the charged fume and the filter, in addition to the collecting action such as mechanical diffusion or collision. It is possible to obtain high commercial efficiency with low ventilation loss.

二次フィルタ9に捕集さ扛た浴接ヒユームは、振動ある
いはかきとりなど1!!A轟な方法によシ谷易に払い落
すことができる。払い洛されたヒユームはタストボック
ス10に貯えられた後、系外へ排出される。
The bath fluid collected by the secondary filter 9 may be vibrated or scraped off. ! A: It can be easily brushed off by a powerful method. The dispelled hume is stored in the tast box 10 and then discharged out of the system.

以上述べた如く、防錆油や切削油等が塗布された母材を
溶接したときに生成するオイルミストを含む溶接ヒユー
ムを、−次フィルタ、荷電装置及び二次フィルタから4
111成されたろ適業じん機において、捕集さ1むたミ
ストまたはヒユームを9jJ率よく捕集し、しかも、捕
集されたミヌr及びヒユームを容易に払い落すことが可
能となシ、捕集性及び保守性に優れたろ適業じん機を提
供するものである。
As mentioned above, welding fume containing oil mist generated when welding base metals coated with anti-corrosion oil, cutting oil, etc. is removed from the -order filter, charging device, and secondary filter.
111, it is possible to collect one filtration of mist or fume with a high rate of 9JJ, and also to easily shake off the collected mist and fume. The purpose of this invention is to provide a filtration dust machine with excellent collection and maintainability.

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

図thl+は、本発明に係るろ適業じん磯の一実施例の
m成因を示す。
FIG.

Claims (1)

【特許請求の範囲】[Claims] 1、気体の流入孔と流出孔を有し、流入孔より導入され
た粉じんのうち粗い粒子を補集する調法フィルタと、該
−次フィルタを洗浄する洗浄機構を有し、次いで調法フ
ィルタを通過した粉じんに電何を与える荷電装置と、該
荷電装置によって帯電された粉じんを捕集する二次フィ
ルタから構成さしたことを特徴とするろ適業じん機。
1. A preparation filter that has a gas inflow hole and an outflow hole and that collects coarse particles from the dust introduced through the inflow hole, and a cleaning mechanism that washes the secondary filter; 1. A filtration dust machine comprising: a charging device that applies electricity to the dust that has passed through the charging device; and a secondary filter that collects the dust charged by the charging device.
JP3950382A 1982-03-15 1982-03-15 Filtering type dust collector Pending JPS58156323A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3950382A JPS58156323A (en) 1982-03-15 1982-03-15 Filtering type dust collector

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3950382A JPS58156323A (en) 1982-03-15 1982-03-15 Filtering type dust collector

Publications (1)

Publication Number Publication Date
JPS58156323A true JPS58156323A (en) 1983-09-17

Family

ID=12554844

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3950382A Pending JPS58156323A (en) 1982-03-15 1982-03-15 Filtering type dust collector

Country Status (1)

Country Link
JP (1) JPS58156323A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100502830B1 (en) * 2000-12-28 2005-07-20 주식회사 포스코 Oil removal apparatus using static electricity
CN113350942A (en) * 2021-06-03 2021-09-07 安徽信息工程学院 Welding smoke purification system and method based on plasma

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5393480A (en) * 1977-01-28 1978-08-16 Hitachi Ltd Apparatus for collecting suspended dust
JPS556689U (en) * 1978-06-27 1980-01-17
JPS56139147A (en) * 1980-04-01 1981-10-30 Hitachi Ltd Filtering type dust collector

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5393480A (en) * 1977-01-28 1978-08-16 Hitachi Ltd Apparatus for collecting suspended dust
JPS556689U (en) * 1978-06-27 1980-01-17
JPS56139147A (en) * 1980-04-01 1981-10-30 Hitachi Ltd Filtering type dust collector

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100502830B1 (en) * 2000-12-28 2005-07-20 주식회사 포스코 Oil removal apparatus using static electricity
CN113350942A (en) * 2021-06-03 2021-09-07 安徽信息工程学院 Welding smoke purification system and method based on plasma

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