JPS6344093Y2 - - Google Patents

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Publication number
JPS6344093Y2
JPS6344093Y2 JP1980100450U JP10045080U JPS6344093Y2 JP S6344093 Y2 JPS6344093 Y2 JP S6344093Y2 JP 1980100450 U JP1980100450 U JP 1980100450U JP 10045080 U JP10045080 U JP 10045080U JP S6344093 Y2 JPS6344093 Y2 JP S6344093Y2
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JP
Japan
Prior art keywords
dust
main body
gas
passage
divided
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
JP1980100450U
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Japanese (ja)
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JPS5725718U (en
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Priority to JP1980100450U priority Critical patent/JPS6344093Y2/ja
Publication of JPS5725718U publication Critical patent/JPS5725718U/ja
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Expired legal-status Critical Current

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  • Filtering Of Dispersed Particles In Gases (AREA)

Description

【考案の詳細な説明】 (産業上の利用分野) 本考案は、集塵システムにおける粉塵分離装置
に関する。
[Detailed Description of the Invention] (Industrial Application Field) The present invention relates to a dust separation device in a dust collection system.

(従来の技術) 一般に集塵システムにおける粉塵の濾過並びに
粉塵の分離捕集は、粉塵を含む気体を所定方向に
流動させるための流動路と、流動路に介装された
濾過要素と、濾過要素通過後の清浄気体排出路
と、濾過要素内に圧縮空気を逆流させて濾過要素
に付着した粉塵を払い落す粉塵分離手段とで主構
成されている。
(Prior art) In general, dust filtration and dust separation and collection in a dust collection system are performed using a flow path for causing a gas containing dust to flow in a predetermined direction, a filtration element interposed in the flow path, and a filtration element. It mainly consists of a clean gas discharge path after passing through, and a dust separation means that blows off dust adhering to the filter element by causing compressed air to flow back into the filter element.

前記圧縮空気の逆流方式として、低圧空気を低
速で送り込み、濾過要素に付着した粉塵を払い落
す低圧逆洗方式と、高圧ジエツトを瞬間的に送り
込み、濾過要素を激しく振動させて払い落すパル
スジエツト方式とがある。
The compressed air backflow method includes a low-pressure backwash method in which low-pressure air is sent at a low speed to brush off dust attached to the filter element, and a pulse jet method in which high-pressure jet is sent instantaneously to violently vibrate the filter element to remove it. There is.

前記低圧逆洗方式のものとして、例えば、実公
昭51−3095号公報、実開昭48−37469号公報に記
載のものが公知である。
As examples of the low-pressure backwashing method, those described in Japanese Utility Model Publication No. 3095/1983 and Japanese Utility Model Application Publication No. 37469/1988 are known.

前記実公昭51−3095号公報に記載のものは、粉
塵含有気体の流動路を分割路とし、かつ、清浄気
体排出路も分割路とし、各排出分割路と排出管と
の接続部に開閉装置を設け、更に各排出分割路に
逆洗用空気供給口を設け、この供給口にも開閉弁
が設けられている。そして、流動路においては粉
塵含有気体は上方から下方に流れるよう構成され
ている。また排出分割路の開閉装置および供給口
の開閉弁は一本のシヤフトによつて連動されるク
ランクにより、順次開閉操作されるように構成さ
れている。
In the device described in the above-mentioned Japanese Utility Model Publication No. 51-3095, the dust-containing gas flow path is a divided path, the clean gas discharge path is also a divided path, and a switch is installed at the connection between each discharge divided path and the discharge pipe. Furthermore, a backwashing air supply port is provided in each discharge divided passage, and this supply port is also provided with an on-off valve. The flow path is configured such that the dust-containing gas flows from above to below. Further, the opening/closing device for the discharge branch passage and the opening/closing valve for the supply port are configured to be sequentially opened and closed by a crank that is interlocked by a single shaft.

前記構成の粉塵分離装置によれば、一の排出分
割路の開閉装置が閉じられ、その分割路の逆洗用
空気供給口の開閉弁が開き、逆洗用空気が排出分
割路に供給され、濾過要素を逆流して濾過要素に
付着した粉塵を払い落す。払い落された粉塵の大
きなものは落下するが微細なものは逆洗気体と共
に上方に流れ、他の流動分割路に入つて下方に流
れる。
According to the dust separator having the above configuration, the opening/closing device of one discharge division passage is closed, the opening/closing valve of the backwash air supply port of the division passage is opened, and backwash air is supplied to the discharge division passage, Brush off the dust adhering to the filter element by backflowing the filter element. The large pieces of dust that are brushed off fall, but the fine particles flow upward together with the backwashing gas, enter another flow dividing path, and flow downward.

また、前記実開昭48−37469号公報に記載のも
のは、流動路は単一とされ、排出路が分割路とさ
れ、各分割路には前記と同様開閉装置および開閉
弁が設けられ、粉塵含有気体は流動路を下方から
上方に流れる構造とされている。
In addition, in the device described in the above-mentioned Japanese Utility Model Application Publication No. 48-37469, the flow path is single, the discharge path is a divided path, and each divided path is provided with an opening/closing device and an opening/closing valve as described above. The structure is such that the dust-containing gas flows from the bottom to the top in the flow path.

この装置においても、一の排出分割路の開閉装
置が閉じられ、逆洗用空気供給口の開閉弁が開
き、逆洗用空気は濾過要素を通過して付着した粉
塵を払い落す。払い落された粉塵の重いものは落
下するが、軽いものは流動路の流れ(下方から上
方)によつてその付近に滞留する。
In this device as well, the opening/closing device of one discharge split passage is closed, the opening/closing valve of the backwashing air supply port is opened, and the backwashing air passes through the filter element to blow off the attached dust. The heavier part of the dust that is brushed off falls, but the lighter part stays in the vicinity due to the flow of the flow path (from the bottom to the top).

一方、前記パルスジエツト方式のものとして、
実公昭38−10289号公報、実開昭54−74381号公報
に記載のものが公知である。
On the other hand, as for the pulse jet method,
Those described in Japanese Utility Model Publication No. 38-10289 and Japanese Utility Model Application Publication No. 54-74381 are known.

前記実公昭38−10289号公報に記載のものは、
流動路及び排出路ともに単一なものとして構成さ
れ、粉塵含有気体は下方から上方に流れるよう構
成されている。そして、排出路内に、各濾過要素
に対応して噴射管が設けられており、各噴射管は
順次ジエツトを濾過要素内に吹き込む。そして、
このジエツトの瞬間的な噴射により濾過要素が振
動し、粉塵を払い落す。このジエツトの噴射は濾
過要素の濾過作用中に行なわれ、かつ払い落され
た粉塵の内軽いものは流動路の流れによつて落下
がさまたげられる。
What is described in the above-mentioned Utility Model Publication No. 38-10289 is
Both the flow path and the discharge path are configured as a single unit, and the dust-containing gas is configured to flow from the bottom to the top. An injection pipe is provided in the discharge passage corresponding to each filter element, and each injection pipe sequentially blows jet into the filter element. and,
This instantaneous jet of jet causes the filtration element to vibrate and dislodge dust. This injection of the jet is carried out during the filtering action of the filter element, and the lighter dust particles are prevented from falling by the flow in the flow path.

また、実開昭57−74381号公報に記載のものは、
流動路は単一とされ、排出路が分割路とされ、各
分割路に開閉装置が設けられ、かつ各分割路に噴
射管が配置されている。この装置においても流動
路における粉塵含有気体は下方から上方に流れる
よう構成されている。従つて、噴射流の振動によ
り払い落された粉塵の内、軽いものは落下しにく
かつた。
In addition, the one described in Utility Model Application Publication No. 57-74381 is
The flow path is single, the discharge path is a divided path, each divided path is provided with an opening/closing device, and each divided path is provided with an injection pipe. Also in this device, the dust-containing gas in the flow path is configured to flow from the bottom to the top. Therefore, among the dust particles that were blown away by the vibrations of the jet stream, light particles were less likely to fall.

(考案が解決しようとする課題) 前記低圧逆洗方式のものは、低圧空気を逆送す
るものであるから、粉塵払い落すのに長時間を要
すると云う問題があつた。また逆洗空気として脈
動流を供給し、濾過要素を振動させるようにして
も、その振動の周期は長いものになり、時間を大
巾に短縮するには至らない。
(Problems to be Solved by the Invention) Since the low-pressure backwash method described above sends low-pressure air back, there is a problem in that it takes a long time to remove dust. Furthermore, even if a pulsating flow is supplied as backwash air to vibrate the filter element, the period of the vibration will be long, and the time will not be significantly shortened.

その点、パルスジエツト方式は、瞬時に激しい
振動を生じさせるので短時間に粉塵を払い落すこ
とができると云う利点がある。
On this point, the pulse jet method has the advantage that dust can be removed in a short time because it instantly generates intense vibrations.

しかし、前記すべての従来のものは、払い落さ
れた粉塵が逆洗空気により、又は、流動路内の粉
塵含有気体の流動により、落下が妨げられ、付近
に漂い、隣りの濾過要素に付着しやすく、完全な
分離ができないと云う問題があつた。
However, in all of the above-mentioned conventional methods, the dust that is brushed off is prevented from falling by backwash air or by the flow of dust-containing gas in the flow path, floats nearby, and adheres to the adjacent filter element. There was a problem that it was easy to separate the particles and that complete separation was not possible.

また、開閉装置の部分的修理をしたい場合、前
記従来のものでは、開閉装置や開閉弁が、機械的
なクランクやカムで行なわれていたので、各開閉
装置は連動しており、一つだけを停止させること
ができないので、装置全体を停止させて交換しな
ければならないと云う問題があつた。
In addition, if you want to partially repair a switchgear, in the conventional systems mentioned above, the switchgear and on-off valves were operated using mechanical cranks and cams, so each switchgear is interlocked and only one can be repaired. There was a problem in that the entire device had to be stopped and replaced because it could not be stopped.

そこで、本考案は、パルスジエツト方式の利点
を生かした装置とすると共に、流動路における粉
塵含有気体の流動方向と、払い落した粉塵の落下
方向とを同一にして、速やかに粉塵を落下させる
ようにし、かつ隣の濾過要素に吸着されないよう
にし、更に、装置の稼動中においても、一部の開
閉装置を交換可能とした粉塵分離装置を提供する
ことを目的とする。
Therefore, the present invention is a device that takes advantage of the advantages of the pulse jet method, and also makes the flow direction of the dust-containing gas in the flow path the same as the falling direction of the dust that has been brushed off, so that the dust can fall quickly. It is an object of the present invention to provide a dust separator which prevents dust from being adsorbed by adjacent filter elements, and which also allows part of the opening/closing device to be replaced even while the device is in operation.

(課題を解決するための手段) 前記目的を達成するための本考案の特徴とする
処は、集塵装置本体1が長方体形状の単一室とし
て形成され、該本体1の上部に粉塵を含む気体を
吸引する吸引部2が開口形成され、前記本体1の
下部に粉塵落下路4が形成され、前記本体1の一
側壁8に上下方向に細長い濾過要素挿脱口9が横
方向に多数開口形成され、該挿脱口9は横方向に
相隣接する複数個が1グループとされ、相隣接す
るグループ間における挿脱口9間の間隔は1グル
ープ内の挿脱口9間の間隔より広く形成され、前
記挿脱口9に偏平箱形状の濾過要素10が挿脱自
在に挿入されており、該濾過要素10の挿脱口9
に位置する一側面が清浄気体送出口15とされ、
該気体送出口15を覆つて本体側壁8に取付けら
れた壁面24と本体側壁8とにより気体排出路2
6が形成され、該気体排出路26は前記挿脱口9
の各グループに対応して横方向に分割区成された
複数の分割路26′を備え、前記壁面24には濾
過要素取出用ドア34が開閉自在に設けられ、前
記各分割路26′の下部は清浄気体排出管29に
接続されており、前記各分割路26′と排出管2
9との連通部を開閉自在とする開閉装置27が各
分割路26′ごとに独立操作可能に設けられ、前
記各分割路26′には前記開閉装置27により閉
塞された分割路26′における気体送出口15に
圧縮空気を噴射する噴射管22が設けられている
点にある。
(Means for Solving the Problems) A feature of the present invention for achieving the above object is that the dust collector main body 1 is formed as a single rectangular chamber, and the dust collector body 1 is formed as a single rectangular chamber, and the dust collector A suction part 2 for sucking gas containing gas is formed as an opening, a dust fall path 4 is formed in the lower part of the main body 1, and one side wall 8 of the main body 1 has many vertically elongated filter element insertion/removal ports 9 in the horizontal direction. A plurality of insertion/ejection ports 9 adjacent to each other in the horizontal direction are formed into one group, and the spacing between the insertion/ejection ports 9 in adjacent groups is wider than the spacing between the insertion/ejection ports 9 in one group. , a flat box-shaped filtration element 10 is removably inserted into the insertion/removal port 9;
One side located at is a clean gas outlet 15,
The gas discharge path 2 is formed by the wall surface 24 attached to the main body side wall 8 covering the gas outlet 15 and the main body side wall 8.
6 is formed, and the gas discharge path 26 is connected to the insertion/removal port 9.
The wall surface 24 is provided with a door 34 for taking out the filtration element, which can be freely opened and closed. are connected to the clean gas discharge pipe 29, and the respective divided passages 26' and the discharge pipe 29 are connected to the clean gas discharge pipe 29.
An opening/closing device 27 that can freely open and close the communicating portion with the opening/closing device 9 is provided for each division passage 26' so as to be able to operate independently. The point is that an injection pipe 22 for injecting compressed air is provided at the outlet 15.

(作用) 本考案によれば、粉塵含有気体は、集塵装置本
体の上部の吸引部から本体的に入る。重量の重い
粉塵は、そのまま落下して下方の粉塵落下路に落
ちる。軽い粉塵は気体と共に下方に流動し、気体
は濾過要素を通過し、粉塵は濾過要素に付着す
る。濾過要素を通過した清浄気体は排出路を通り
排出管を経て流れる。
(Function) According to the present invention, the dust-containing gas enters the main body of the dust collector from the suction section at the upper part of the main body. The heavy dust falls directly onto the dust fall path below. The light dust flows downward with the gas, the gas passes through the filtration element, and the dust adheres to the filtration element. The clean gas that has passed through the filter element flows through the exhaust channel and through the exhaust pipe.

前記排出路は分割路とされており、各分割路は
開閉装置によつて順次開閉されている。開閉装置
によつて閉じられた分割路には清浄気体は流れな
い。この閉じられた分割路において噴出管からジ
エツト流が濾過要素内に噴射される。これによ
り、濾過要素が膨張収縮の振動を行ない、付着し
た粉塵が払い落される。本体内は単一の室とされ
ているので、払い落された粉塵は粉塵含有気体の
流れと共に下方に速やかに落下する。このとき、
濾過要素はグループ分けされており、隣りのグル
ープの濾過要素との間に広い間隔を有しているの
で、払い落された粉塵は隣りの濾過要素に付着し
にくくなり、速やかに落下する。
The discharge passage is a divided passage, and each divided passage is sequentially opened and closed by an opening/closing device. No clean gas flows through the divided passages closed by the switchgear. In this closed division, the jet stream is injected into the filter element from the jet tube. This causes the filtration element to vibrate as it expands and contracts, and the attached dust is brushed off. Since the interior of the main body is a single chamber, the dust that is brushed off quickly falls downward along with the flow of dust-containing gas. At this time,
The filtration elements are divided into groups and there is a wide interval between the filtration elements of adjacent groups, so that the dust that is brushed off is less likely to adhere to the adjacent filtration elements and falls quickly.

尚、開閉装置は独立操作可能なものとされてい
るので、開閉装置の一部が損傷した場合は、集塵
装置全体を停止することなく、その装置のみを修
理することができる。
Note that since the opening/closing device is designed to be able to be operated independently, if a part of the opening/closing device is damaged, only that device can be repaired without stopping the entire dust collector.

また、排出路を形成する壁面に濾過要素取出用
ドアが設けられているので、清浄空気側から濾過
要素の取替ができる。
Furthermore, since the filter element removal door is provided on the wall surface forming the discharge passage, the filter element can be replaced from the clean air side.

(実施例) 以下、本考案の実施例を図面に基づいて詳細に
説明する。
(Example) Hereinafter, an example of the present invention will be described in detail based on the drawings.

第1図及び第2図は集塵システムの一例を全体
図で示し、上方から粉塵を含む気体を吸引して側
方から気体のみを取出す一方、下方へと気体流と
同一方向をなして粉塵を分離かつ捕集する所謂タ
ワー型の集塵システムである。
Figures 1 and 2 show an overall view of an example of a dust collection system, in which the gas containing dust is sucked in from above and only the gas is extracted from the sides, while the dust is collected downward in the same direction as the gas flow. This is a so-called tower-type dust collection system that separates and collects dust.

1は集塵装置本体で、角形筒状単一室に形成さ
れており、その本体1は上端に粉塵を含む気体が
吸引される開口状の吸引部2及び該吸引部2に対
面する如く配備されたポペツト3を、又下端に粉
塵落下路4並びに集塵口5とを具備して構成され
ると共に、本体1は集塵口5に粉塵排出用ロータ
リバルブ6を連通状に装備した状態で、支持フレ
ーム7上に設置されている。
Reference numeral 1 denotes the main body of the dust collector, which is formed into a single rectangular cylindrical chamber, and the main body 1 has an opening-shaped suction part 2 at the upper end through which gas containing dust is sucked, and is arranged so as to face the suction part 2. The main body 1 is equipped with a dust fall path 4 and a dust collection port 5 at the lower end thereof, and a rotary valve 6 for discharging dust is connected to the dust collection port 5. , installed on the support frame 7.

前記、本体1の一側壁8には、縦長長方形状に
開口された濾過要素挿脱口9が、横方向に列設状
態でかつ上下多段に渡つて設けられ、前記挿脱口
9を介して複数の濾過要素10がそれぞれ前記本
体1内に片持状に挿着され、第3図及び第4図に
示す如く、各濾過要素10は支持パツト11を介
して固定手段12により適宜着脱自在とされてい
る。
In the side wall 8 of the main body 1, filter element insertion/removal ports 9 each having a vertically elongated rectangular shape are provided in rows in the horizontal direction and in multiple stages vertically. The filter elements 10 are each inserted into the main body 1 in a cantilevered manner, and as shown in FIGS. 3 and 4, each filter element 10 can be attached or detached as needed by a fixing means 12 via a support part 11. There is.

各挿脱口9は横方向に3個が1グループとさ
れ、相隣接するグループ間の挿脱口9の間隔は、
1グループ内の挿脱口9の間隔よりも広くされて
いる。
Each insertion/extraction port 9 is made into a group of three in the horizontal direction, and the spacing between the insertion/extraction ports 9 between adjacent groups is as follows:
The interval is wider than the interval between the insertion/removal ports 9 within one group.

前記濾過要素10は第3図及び第4図に示す如
く、前記挿脱口9に対応して嵌入自在な箱形状に
枠組構成された濾過枠13と、前記本体1内に嵌
入される濾過枠13の外周を被覆して設けられた
濾過材(濾布)14とからなる所謂偏平箱型形状
に構成され、また濾過要素10は前記本体1の一
側壁8側に気体送出口15が形成されている。さ
らに濾過材14の外周には、濾過材14の過膨脹
を防止する抑圧部材16が巻かれており、該抑圧
部材16は濾過要素10の横方向に複数配設さ
れ、第4図に示す如く、濾過材14を分割状態で
衝撃的に微振動可能に構成されている。前記気体
送出口15には上下方向に適宜間隔を有してベン
チユリ17が、濾過枠13の横方向と同一方向を
なして装備されている。このベンチユリ17は圧
縮流噴出手段であり、圧縮流受入口18と圧縮流
放出口19とを各々具備し、上記圧縮流放出口1
9は濾過要素10内に侵入する状態で装着されて
いる。
As shown in FIGS. 3 and 4, the filter element 10 includes a box-shaped filter frame 13 that can be fitted into the insertion/removal port 9, and a filter frame 13 that is fitted into the main body 1. The filtration element 10 has a so-called flat box shape, and has a gas outlet 15 formed on one side wall 8 of the main body 1. There is. Further, a suppressing member 16 is wound around the outer circumference of the filtering medium 14 to prevent excessive expansion of the filtering medium 14, and a plurality of suppressing members 16 are arranged in the lateral direction of the filtering element 10, as shown in FIG. , the filter medium 14 is configured to be able to vibrate slightly in a divided state. Bench lilies 17 are installed in the gas outlet 15 at appropriate intervals in the vertical direction and extend in the same direction as the lateral direction of the filter frame 13. This bench lily 17 is a compressed flow jetting means, and is provided with a compressed flow receiving port 18 and a compressed flow discharge port 19.
9 is installed so as to penetrate into the filter element 10.

20は圧縮空気噴射装置で、前記各濾過要素1
0のベンチユリ17に各々臨む圧縮流噴射口21
を縦方向に連設した圧縮流噴射管22を濾過要素
10と対応して横方向に複数本並列配備すると共
に、上方で集束管35に連通され、該集束管35
は図示省略したコンプレツサーに連設されてい
る。また集束管35と各圧縮流噴射管22の間に
は電磁弁23を具備する噴射コントロール部が装
備され、該コントロール部により所定時間的間隔
をもつて適宜圧縮空気を噴射自在として構成され
ている。
20 is a compressed air injection device, and each of the filter elements 1
Compressed flow injection ports 21 each facing the bench lily 17 of 0
A plurality of compressed flow injection pipes 22 are arranged in parallel in the horizontal direction in correspondence with the filtration elements 10, and are communicated with a focusing pipe 35 at the upper part.
is connected to a compressor (not shown). Further, an injection control unit including an electromagnetic valve 23 is provided between the focusing pipe 35 and each compressed flow injection pipe 22, and the control unit is configured to freely inject compressed air as appropriate at predetermined time intervals. .

前記本体1の前記一側壁8外面に前記複数の濾
過要素10の気体送出口15及び噴射管22を包
囲状として気体排出路用壁面24が設けられ、該
壁面24と一側壁8により気体排出路26が形成
されている。そして前記気体排出路26は並設さ
れた濾過要素10の単位(実施例では3列毎)に
応じて縦方向に設けられた複数の仕切り板25に
よつて横方向に分割区成され、複数(実施例では
6)の分割路26′が構成されている。また各々
の分割路26′の下端部には外側方に突出する連
通管28を各々設けられており、該各連通管36
と気体の排出路28を構成する排出管29とがエ
ルボ管37により各々連通されている。そして連
通管36とエルボ管37との各接続部内に突出形
成されたフランジ部33を外側、即ちエルボ管3
7側より直線往復運動により開閉する開閉装置2
7が分割路26′毎に設けられている。また、前
記各分割路26′内の気体を吸引排出すべく、ブ
ロアよりなる流動装置が前記排出管29に連設さ
れ、その流動装置により前記吸引部2から排出部
28へ気体を流動させている。前記開閉装置27
はエアシリンダ30とシリンダロツド31端部に
設けられたポペツトダンパ32とによつて構成さ
れ、前記ロツド31の進退作動により、前記フラ
ンジ部33をポペツトダンパ32で閉塞自在とす
る弁開閉式として構成されている。各分割路2
6′の開閉装置27は、夫々独立して操作できる
よう構成されている。そして、前記分割路26′
が開閉装置27の作動により閉塞され、所定時間
(実施例では5秒)経過後、その分割路26′内に
備えられた各圧縮流噴射管22の電磁弁23が作
動して、所定時間(実施例では0.1秒)各濾過要
素10内に圧縮空気が噴射され、さらに所定時間
(実施例では5秒)経過後、再度開閉装置27の
作動により前記分割路26′が開通され、順次他
の分割路26′において前記同様に作動すべく循
環形式に構成されている。
A wall surface 24 for a gas discharge path is provided on the outer surface of the one side wall 8 of the main body 1 and surrounds the gas outlet ports 15 and injection pipes 22 of the plurality of filtration elements 10, and the wall surface 24 and the one side wall 8 form a gas discharge path. 26 is formed. The gas discharge path 26 is divided into sections in the horizontal direction by a plurality of partition plates 25 provided in the vertical direction according to the units of the filter elements 10 arranged in parallel (every three rows in the embodiment). (6 in the embodiment) dividing paths 26' are constructed. Further, a communication pipe 28 projecting outward is provided at the lower end of each divided passage 26', and each communication pipe 36 is provided with a communication pipe 28 projecting outward.
and a discharge pipe 29 constituting the gas discharge path 28 are communicated with each other through an elbow pipe 37. Then, the flange portion 33 protrudingly formed within each connection portion between the communication pipe 36 and the elbow pipe 37 is connected to the outside, that is, the elbow pipe 3
Opening/closing device 2 that opens and closes from the 7 side by linear reciprocating motion
7 is provided for each dividing path 26'. Further, in order to suck and discharge the gas in each of the divided passages 26', a flow device consisting of a blower is connected to the discharge pipe 29, and the flow device causes the gas to flow from the suction section 2 to the discharge section 28. There is. The opening/closing device 27
is constituted by an air cylinder 30 and a poppet damper 32 provided at the end of a cylinder rod 31, and is configured as a valve opening/closing type in which the flange portion 33 can be freely closed by the poppet damper 32 as the rod 31 advances and retreats. . Each dividing road 2
The opening/closing devices 27 of 6' are constructed so that they can be operated independently. Then, the dividing path 26'
is closed by the operation of the opening/closing device 27, and after a predetermined time (5 seconds in the embodiment) has elapsed, the solenoid valve 23 of each compressed flow injection pipe 22 provided in the divided passage 26' is operated, and the valve is closed for a predetermined time (5 seconds in the embodiment). Compressed air is injected into each filter element 10 (0.1 seconds in the embodiment), and after a predetermined period of time (5 seconds in the embodiment), the opening/closing device 27 is operated again to open the dividing passage 26', and the other The dividing passage 26' is configured in a circulating manner to operate in the same manner as described above.

尚、前記気体排出路用壁面24に開閉自在な濾
過要素取出用ドア34が設けられている。
In addition, a door 34 for taking out a filter element that can be opened and closed is provided on the wall surface 24 for the gas discharge path.

本考案の実施例は以上のように構成されてお
り、ブロアよりなる流動装置を作動させると吸引
部2から排出部28に至る吸引状態が得られ、こ
こに粉塵を含む気体を吸引部2からポペツト3を
介して送ると、まず各濾過要素10の濾過材14
で粉塵が吸着されて、残る気体のみが各気体送出
口15を経て、各分割路26′及び排出管29を
介して、所謂濾過気体が流動装置から排出され
る。そしてこの一連過程中に各々の分割路26′
毎において、分割路26′の閉塞、圧縮空気の噴
出、分割路26′の開通の行程が所定時間ごとに
順次循環して行なわれる。従つてコンプレツサー
からの圧縮空気をベンチユリ17が受けて、瞬間
的に膨脹気体とし、これによつて濾過要素10の
濾過材14に瞬間的膨脹並びに微振動が発生し、
その膨脹並びに微振動によつて濾過材14に吸着
した粉塵が濾過材14より払い落とされる。また
この際、分割路26′が閉塞状態とされて所定時
間後に圧縮空気を噴射させる構成であり、つま
り、前記吸引状態によつて流動する気体がこの分
割路26′内に流れ込まない状態において圧縮空
気を噴射させるので、対向方向より流動気体が流
れ込む場合と違つて、その圧縮空気の噴射力の低
下が防止でき、効率よく濾過材14に対して前記
膨脹並びに微振動を発生させることができる。さ
らに、圧縮空気噴射後、所定時間経過させた後、
分割路26′を開通させる構成であるので、前記
払い落とされた粉塵は流動気体と共に再度、その
分割路26′方向に吸引されることなく、十分下
方に落下する。
The embodiment of the present invention is constructed as described above, and when the flow device consisting of a blower is operated, a suction state from the suction section 2 to the discharge section 28 is obtained, and the gas containing dust is removed from the suction section 2. When feeding through the poppet 3, first the filter medium 14 of each filter element 10 is
After the dust is adsorbed, only the remaining gas passes through each gas outlet 15, and then through each dividing path 26' and discharge pipe 29, so-called filtration gas is discharged from the flow device. During this series of processes, each dividing path 26'
At each time, the steps of closing the dividing passage 26', blowing out compressed air, and opening the dividing passage 26' are performed in sequence at predetermined time intervals. Therefore, the compressed air from the compressor is received by the bench lily 17 and instantaneously becomes expanded gas, which causes instantaneous expansion and slight vibrations in the filter medium 14 of the filter element 10.
Due to the expansion and slight vibration, dust adsorbed on the filter medium 14 is brushed off from the filter medium 14. At this time, the divided passage 26' is closed and the compressed air is injected after a predetermined period of time. In other words, the compressed air is compressed when the gas flowing due to the suction state does not flow into the divided passage 26'. Since the air is injected, unlike the case where fluid gas flows in from the opposite direction, a reduction in the jetting force of the compressed air can be prevented, and the expansion and micro vibration can be efficiently generated in the filter medium 14. Furthermore, after a predetermined period of time has elapsed after compressed air injection,
Since the dividing path 26' is configured to be opened, the dust particles that have been brushed off are sufficiently dropped downward together with the flowing gas without being sucked in the direction of the dividing path 26'.

従つて、粉塵の払い落しが完全であり、十分な
粉塵の分離機能が発揮でき、従つて常に良好な濾
過作用を維持できる。以上のように、流動気体に
逆らつて高圧の圧縮空気を噴射させる場合と違い
圧縮空気の噴射力が有効に利用できるため、低圧
の圧縮空気でも十分目的を果たせ、従つてコンプ
レツサーの容量も小でよく、エネルギーの省力化
が図れる。尚、濾過要素10を偏平箱型形状とし
ていることにより、通常の円筒タイプに比べて、
圧縮空気の噴射による振巾が大となり、これによ
つて濾過材14からの粉塵の分離効果も大であ
る。また前記閉塞状態の分割路26′以外の分割
路26′によつて所望の気体流量を設定しておけ
ば、流動気体中に圧縮空気を噴射する場合と違つ
て、常に安定した濾過気体の一定流量が得られ
る。
Therefore, the dust can be completely removed, a sufficient dust separation function can be achieved, and a good filtration effect can always be maintained. As mentioned above, unlike when high-pressure compressed air is injected against the flowing gas, the jet force of compressed air can be used effectively, so even low-pressure compressed air can serve the purpose, and the capacity of the compressor is also small. This can save energy. In addition, by making the filter element 10 into a flat box shape, compared to a normal cylindrical type,
The amplitude of the jet of compressed air is increased, and thereby the effect of separating dust from the filter medium 14 is also increased. Furthermore, if a desired gas flow rate is set using the divided passages 26' other than the blocked divided passage 26', the filtration gas can be kept at a constant constant level, unlike when compressed air is injected into the flowing gas. Flow rate can be obtained.

さらに第5図及び第6図に示される如く、上端
の吸引部2より吸引された気体は単一室の装置本
体1内に案内され、装置本体1内を上方より下方
に案内される間に各濾過要素10を通過して装置
本体1の側部の各分割路26′に案内され、その
後、下方の排出管29より濾過気体が排出され、
一方その間に各濾過要素10単位毎に粉塵分離処
理が行われ、下方の粉塵落下路4より集塵口5を
介して排出される構成であり、即ち、気体の流れ
は、装置本体1の上端より装置本体1内に案内さ
れ、その側壁8より各分割路26′を介して下方
の排出管29より排出される常に一定した方向の
流れであり、瞬間的な圧縮空気の噴出によつても
何等、気体の流れが乱されず、従つて安定した流
量の濾過気体が得られる。また、粉塵分離処理が
行われている間においても、装置本体1が単一室
とされていることから、装置本体1内においては
矢印で示される如く、常に下方向の一定した流れ
が生じており、各濾過材14から分離された粉塵
は舞い上がることなく、重力による自然落下と気
体の下方向への流れとの協働作用により、浮遊す
る軽量の粉塵であつても効率よく、迅速に十分下
方に落下され、かつ、隣のグループの濾過要素と
の間隔は広いものとされているので、再度、濾過
材14に吸引されるおそれがなく、粉塵の払い落
としが完全となり、十分な粉塵の分離機能が発揮
できる。
Further, as shown in FIGS. 5 and 6, the gas sucked from the suction part 2 at the upper end is guided into the single-chamber device main body 1, and while being guided inside the device main body 1 from the top to the bottom. The filtered gas passes through each filter element 10 and is guided to each dividing passage 26' on the side of the device main body 1, and then is discharged from a lower discharge pipe 29,
On the other hand, during this time, dust separation processing is performed for each 10 unit of each filter element, and the dust is discharged from the lower dust fall passage 4 through the dust collection port 5. It is a flow in a constant direction that is guided into the device main body 1 from the side wall 8 and discharged from the lower discharge pipe 29 through each dividing passage 26', and even by an instantaneous jet of compressed air. After all, the gas flow is not disturbed, and therefore a stable flow rate of filtered gas is obtained. In addition, even while the dust separation process is being performed, since the main body 1 of the apparatus is a single chamber, a constant downward flow is always generated within the main body 1, as shown by the arrow. Therefore, the dust separated from each filter medium 14 does not fly up, and due to the cooperation between the natural fall due to gravity and the downward flow of gas, even light floating dust can be efficiently and quickly removed. Since it is dropped downward and the distance between the filter elements in the adjacent group is wide, there is no risk of the dust being sucked into the filter material 14 again, and the dust is completely brushed off. Separation function can be demonstrated.

さらに、各分割路26′と排出部28との連通
部が、分割路26′下端部に外側方に突出して設
けられた連通管36とエルボ管37とで構成され
ており、フランジ部33をポペツトダンパ32で
エルボ管37側、即ち外側より開閉する構成とし
ているため、シリンダロツド31等が分割路2
6′内に位置されず、従つて分割路26′内を通過
する気体の流れの乱れが防止でき、安定した気体
の流れが得られる。また直線往復運動により開閉
する開閉装置27を分割路26′毎に設けている
ため、フランジ部33の開閉状態の切換が瞬間的
に行なえ、効率がよい。さらに、分割路26′下
端部の外側にエルボ管37、開閉装置27を配置
した構成であるため、集塵装置本体1が大型であ
つても、それら位置が比較的低位置であり、開閉
装置27の保守点検作業が容易となり、メンテナ
ンス性向上を図れる。更に開閉装置27は単独操
作可能なシリンダ30で駆動されるため、その一
つが故障しても、他を止めることなく修理でき
る。
Further, the communication portion between each division passage 26' and the discharge portion 28 is composed of a communication pipe 36 and an elbow pipe 37 provided at the lower end of the division passage 26' so as to protrude outward. Since the poppet damper 32 is configured to open and close from the elbow pipe 37 side, that is, from the outside, the cylinder rod 31 etc.
6', therefore, disturbances in the flow of gas passing through the dividing passage 26' can be prevented, and a stable gas flow can be obtained. Further, since the opening/closing device 27 which opens and closes by linear reciprocating motion is provided for each divided path 26', the opening/closing state of the flange portion 33 can be switched instantaneously, which is efficient. Furthermore, since the elbow pipe 37 and the opening/closing device 27 are arranged outside the lower end of the dividing path 26', even if the dust collector main body 1 is large, they are located at a relatively low position, and the opening/closing device 27 maintenance and inspection work becomes easier, and maintainability can be improved. Further, since the opening/closing device 27 is driven by a cylinder 30 that can be operated independently, even if one of them breaks down, it can be repaired without stopping the others.

尚、以上実施例において、単一の分割路26′
ごとに、粉塵の分離処理を行なう方式として説明
しているが、複数(例えば2つ)の分割路26′
ごとに前記処理を行ない、順次循環させる形式で
あつてもよく、実施例に限定されない。
Incidentally, in the above embodiment, the single dividing path 26'
Although this is explained as a method for separating dust in each case, a plurality of (for example, two) dividing paths 26'
It may be possible to perform the above-mentioned processing for each cycle and sequentially circulate, and is not limited to the embodiment.

(考案の効果) 本考案によれば、粉塵含有気体の流れと払い落
とされた粉塵の落下方向が一致しているので、浮
遊する軽量の粉塵であつても効率よく落下する。
また濾過要素がグループ分けされ、そのグループ
間に広い間隔が設けられているので落下する粉塵
が再度、隣の濾過要素に付着することがない。
(Effects of the invention) According to the invention, since the flow of the dust-containing gas and the falling direction of the dust that has been brushed off are the same, even light floating dust can fall efficiently.
Furthermore, since the filter elements are divided into groups and wide intervals are provided between the groups, falling dust will not adhere to adjacent filter elements again.

更に、開閉装置は独立操作可能なものとされて
いるので、その一つが故障しても他を止めること
なく修理でき、メンテナンス容易になる。
Furthermore, since the switching devices are designed to be able to be operated independently, even if one of them breaks down, it can be repaired without stopping the others, making maintenance easier.

更に、排出路を形成する壁面に濾過要素取出用
ドアを設けているので濾過要素を正常空気側から
取替えることができ、メンテナンス容易になる。
Furthermore, since the filter element removal door is provided on the wall surface forming the discharge passage, the filter element can be replaced from the normal air side, making maintenance easier.

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

第1図は本考案の実施例の装置全体を示す中央
半断面正面図、第2図は第1図の側断面図、第3
図は第2図における部分拡大図、第4図は第3図
に基づく平面図、第5図及び第6図は気体の流れ
を示す説明図である。 1……集塵装置本体、2……吸引部、4……粉
塵落下路、8……側壁、9……挿脱口、10……
濾過要素、15……気体送出口、22……噴射
管、24……壁面、26……気体排出路、26′
……分割路、27……開閉装置、29……排出
管、30……シリンダ、34……濾過要素取出用
ドア、36……連通管。
Fig. 1 is a central half-sectional front view showing the entire device according to an embodiment of the present invention, Fig. 2 is a side sectional view of Fig. 1, and Fig. 3 is a side sectional view of Fig. 1.
The figure is a partially enlarged view of FIG. 2, FIG. 4 is a plan view based on FIG. 3, and FIGS. 5 and 6 are explanatory diagrams showing the flow of gas. 1... Dust collector main body, 2... Suction section, 4... Dust falling path, 8... Side wall, 9... Insertion/removal port, 10...
Filtration element, 15... Gas outlet, 22... Injection pipe, 24... Wall surface, 26... Gas discharge path, 26'
... Divided path, 27 ... Opening/closing device, 29 ... Discharge pipe, 30 ... Cylinder, 34 ... Filter element extraction door, 36 ... Communication pipe.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 集塵装置本体1が長方体形状の単一室として形
成され、該本体1の上部に粉塵を含む気体を吸引
する吸引部2が開口形成され、前記本体1の下部
に粉塵落下路4が形成され、前記本体1の一側壁
8に上下方向に細長い濾過要素挿脱口9が横方向
に多数開口形成され、該挿脱口9は横方向に相隣
接する複数個が1グループとされ、相隣接するグ
ループ間における挿脱口9間の間隔は1グループ
内の挿脱口9間の間隔より広く形成され、前記挿
脱口9に偏平箱形状の濾過要素10が挿脱自在に
挿入されており、該濾過要素10の挿脱口9に位
置する一側面が清浄気体送出口15とされ、該気
体送出口15を覆つて本体側壁8に取付けられた
壁面24と本体側壁8とにより気体排出路26が
形成され、該気体排出路26は前記挿脱口9の各
グループに対応して横方向に分割区成された複数
の分割路26′を備え、前記壁面24には濾過要
素取出用ドア34が開閉自在に設けられ、前記各
分割路26′の下部は清浄気体排出管29に接続
されており、前記各分割路26′と排出管29と
の連通部を開閉自在とする開閉装置27が各分割
路26′ごとに独立操作可能に設けられ、前記各
分割路26′には前記開閉装置27により閉塞さ
れた分割路26′における気体送出口15に圧縮
空気を噴射する噴射管22が設けられていること
を特徴とする集塵システムにおける粉塵分離装
置。
A dust collector main body 1 is formed as a single rectangular chamber, a suction part 2 for sucking dust-containing gas is formed in the upper part of the main body 1, and a dust fall path 4 is formed in the lower part of the main body 1. A large number of vertically elongated filtration element insertion/removal ports 9 are formed in one side wall 8 of the main body 1 in the horizontal direction, and a plurality of the insertion/removal ports 9 that are adjacent to each other in the horizontal direction are grouped into one group. The spacing between the insertion/ejection ports 9 between groups is wider than the spacing between the insertion/ejection ports 9 in one group, and a flat box-shaped filtration element 10 is removably inserted into the insertion/ejection port 9. One side of the element 10 located at the insertion/removal port 9 is a clean gas outlet 15, and a gas exhaust path 26 is formed by the main body side wall 8 and a wall surface 24 attached to the main body side wall 8 covering the gas outlet 15. , the gas discharge passage 26 is provided with a plurality of division passages 26' divided in the horizontal direction corresponding to each group of the insertion/removal ports 9, and a filter element extraction door 34 is provided on the wall surface 24 so as to be openable and closable. The lower part of each divided passage 26' is connected to a clean gas discharge pipe 29, and an opening/closing device 27 that freely opens and closes the communication portion between each divided passage 26' and the discharge pipe 29 is connected to each divided passage 26. Each division passage 26' is provided with an injection pipe 22 for injecting compressed air to the gas outlet 15 in the division passage 26' which is closed by the opening/closing device 27. A dust separation device in a dust collection system characterized by:
JP1980100450U 1980-07-15 1980-07-15 Expired JPS6344093Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1980100450U JPS6344093Y2 (en) 1980-07-15 1980-07-15

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1980100450U JPS6344093Y2 (en) 1980-07-15 1980-07-15

Publications (2)

Publication Number Publication Date
JPS5725718U JPS5725718U (en) 1982-02-10
JPS6344093Y2 true JPS6344093Y2 (en) 1988-11-16

Family

ID=29462019

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1980100450U Expired JPS6344093Y2 (en) 1980-07-15 1980-07-15

Country Status (1)

Country Link
JP (1) JPS6344093Y2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0340333Y2 (en) * 1985-08-09 1991-08-26

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS513095U (en) * 1974-06-24 1976-01-10

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS513095U (en) * 1974-06-24 1976-01-10

Also Published As

Publication number Publication date
JPS5725718U (en) 1982-02-10

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