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JPS6029534B2 - Bag filter cleaning device - Google Patents
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JPS6029534B2 - Bag filter cleaning device - Google Patents

Bag filter cleaning device

Info

Publication number
JPS6029534B2
JPS6029534B2 JP1158778A JP1158778A JPS6029534B2 JP S6029534 B2 JPS6029534 B2 JP S6029534B2 JP 1158778 A JP1158778 A JP 1158778A JP 1158778 A JP1158778 A JP 1158778A JP S6029534 B2 JPS6029534 B2 JP S6029534B2
Authority
JP
Japan
Prior art keywords
bag filter
compressed air
filter
cylindrical member
exhaust chamber
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
JP1158778A
Other languages
Japanese (ja)
Other versions
JPS54105374A (en
Inventor
勝彦 杉山
圜 西山
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.)
Toyota Central R&D Labs Inc
Original Assignee
Toyota Central R&D Labs Inc
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 Toyota Central R&D Labs Inc filed Critical Toyota Central R&D Labs Inc
Priority to JP1158778A priority Critical patent/JPS6029534B2/en
Publication of JPS54105374A publication Critical patent/JPS54105374A/en
Publication of JPS6029534B2 publication Critical patent/JPS6029534B2/en
Expired legal-status Critical Current

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  • Filtering Of Dispersed Particles In Gases (AREA)

Description

【発明の詳細な説明】 本発明は、気体の流れの中に浮遊して運ばれてくる固体
の廃棄物質もしくは回収物質を気体から分離するために
使用するバッグフィル夕の清浄装置に関するものである
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a bag filter cleaning device used to separate solid waste or recovered materials suspended in a gas stream from the gas. .

バッグフィル夕装置は一般に多孔物質から成る有底筒状
のバッグフィルタ内に廃棄物質もしくは回収物質(以下
、回収物質と総称する)を導入し、櫨週された気体をバ
ッグフィル夕の関口より排出せしめるもので、気体がバ
ッグフィル夕を通過するときに回収物質が該フィル夕に
付着し気体と分離される。
A bag filter device generally introduces waste material or recovered material (hereinafter referred to as recovered material) into a cylindrical bag filter with a bottom made of porous material, and discharges the collected gas from the exit of the bag filter. When the gas passes through the bag filter, the recovered material adheres to the bag filter and is separated from the gas.

ところでこの装置においては、フィル夕に付着した回収
物質が堆積してフィル夕の気体透過性を阻害するため、
付着した回収物質をフィル夕より離脱せしめてフィル夕
を清浄化する手段が必要となる。この清浄化手段として
、バッグフィル夕を機械的に揺振させる方式と、バッグ
フィル夕内に圧縮空気を送給することにより通常の気体
の流れ方向を微小時間反転させる、いわゆる逆流方式と
が提案されているが、清浄化能の一様性、装置の簡潔性
、バッグフィルタの耐久性等から後者の逆流方式がすぐ
れている。
However, in this device, the recovered substances attached to the filter accumulate and impede the gas permeability of the filter.
A means is required to clean the filter by removing the adhering collected substances from the filter. As cleaning means, two methods have been proposed: one in which the bag filter is shaken mechanically, and the other is a so-called backflow method in which the normal gas flow direction is briefly reversed by feeding compressed air into the bag filter. However, the latter backflow method is superior in terms of uniformity of cleaning performance, simplicity of the device, and durability of the bag filter.

この逆流方式の清浄装置を具備したバッグフィルタ装置
は一般に、布局等より成る有底筒状のバッグフィル夕の
関口端に筒状部材を取り付け、該都村の鯛心部または該
部材の内壁面に沿って圧縮空気源と蓮適する圧縮空気噴
出ノズルを設け、該噴出ノズルよりバッグフィルタ内に
圧縮空気を送給して通常の気体の流れとに逆方向の気流
をバッグフィルタの内部よりフィル夕に作用せしめて、
フィル外こ付着した回収物質を除去する構成とされてい
る。
In general, a bag filter device equipped with this backflow type cleaning device has a cylindrical member attached to the entrance end of a bottomed cylindrical bag filter made of fabric etc. A compressed air source and a suitable compressed air jetting nozzle are installed along the line, and compressed air is fed into the bag filter from the jetting nozzle to generate an airflow from inside the bag filter in the opposite direction to the normal gas flow. Let it act on
It is configured to remove collected substances adhering to the outside of the filter.

本発明は、この逆流方式のバッグフィルタ清浄装置に関
し、圧縮空気のバッグフィルタ清浄化効率を向上せしめ
ることを目的とするもので、超音速で圧縮空気をバッグ
フィルタ内に送給することにより所定の圧縮空気送給量
にて最大限の反転気流を発生せしめ、上記の目的を達成
するものである。第1図は本発明の清浄装置を具備した
バッグフィルタ装置の一例を示す。
The present invention relates to this backflow type bag filter cleaning device, and its purpose is to improve the bag filter cleaning efficiency of compressed air. The above objective is achieved by generating the maximum amount of reversed air flow with the compressed air supply amount. FIG. 1 shows an example of a bag filter device equipped with the cleaning device of the present invention.

ハウジング1の内部は隔壁11により、回収物質を含む
気体の流入口121を有する櫨過室12と、嫌過された
気体を排出する排出口131を有する排気室13とに区
画されている。バッグフィル夕2の上部関口端には筒状
部材3が連結され、該筒状部村3は気密的に上記隔壁1
1に貴挿固定されてバッグフィルタ2は猿過室12内に
、また筒状部材3の漏斗状の閉口部31は排気室13内
に位置している。バッグフィルタ2は布帯より成り、所
定間隔にて該フィル夕2の外周に配設された鋼線リング
21,21,・・・・・・に固着されて筒状に維持され
その下方密封端はスプリング22を介して猿過室12の
下方に係止されている。排気室13内に位置した上記筒
状部材3内には圧縮空気を噴射する噴出ノズル42が形
成してある。
The interior of the housing 1 is divided by a partition wall 11 into a filter chamber 12 having an inlet 121 for gas containing recovered substances, and an exhaust chamber 13 having an outlet 131 for discharging filtered gas. A cylindrical member 3 is connected to the upper entrance end of the bag filter 2, and the cylindrical member 3 is airtightly connected to the partition wall 1.
1 , the bag filter 2 is located within the sieving chamber 12 , and the funnel-shaped closing portion 31 of the cylindrical member 3 is located within the exhaust chamber 13 . The bag filter 2 is made of a cloth band, and is maintained in a cylindrical shape by being fixed to steel wire rings 21, 21, . is secured to the lower part of the sieve chamber 12 via a spring 22. A jet nozzle 42 for jetting compressed air is formed in the cylindrical member 3 located in the exhaust chamber 13.

即ち、筒状部材3の上端にはノズル部材4が被冠結合さ
れ、該ノズル部材4と上記筒状部材関口部31の内周面
との間に環状の空気溜室41およびこれと蓬通しバッグ
フィル夕2の内部方向に閉口する環状の圧縮空気噴出ノ
ズル42を形成している。上記/ズル部材4の中央には
筒状部材3内と排気室とを運適する閉口35が形成して
ある。噴出ノズル42は中間部に絞り部421を形成し
頃口422へ舷関した形状にしてある。このように噴出
ノズル42を絞り拡がり形状とすることにより、圧縮空
気は絞り部421から曙口422に至って膨脹し圧力は
減少するが速度は増加し、圧縮空気を超音速で噴射する
ことを可能とする。上言己空気溜室41は配管51によ
り電磁弁52を介して圧縮空気供給源53と蓮通して、
上記開口35とは独立の経路で圧縮空気を供給するよう
になし、バッグフィルタの清浄装置を構成している。第
2図は本発明のバッグフィル夕清浄装置の他の実施例で
ある。
That is, a nozzle member 4 is crowned and connected to the upper end of the cylindrical member 3, and an annular air reservoir 41 is formed between the nozzle member 4 and the inner circumferential surface of the cylindrical member entrance portion 31, and an annular air reservoir 41 is connected thereto. An annular compressed air jet nozzle 42 that closes toward the inside of the bag filter 2 is formed. A closing opening 35 is formed in the center of the cylindrical member 4 to open the inside of the cylindrical member 3 and the exhaust chamber. The ejection nozzle 42 has a constricted part 421 formed in the middle part, and has a shape that extends to the neck opening 422. By making the ejection nozzle 42 into a constricted and expanding shape in this way, the compressed air expands from the constricted part 421 to the dawn opening 422, and the pressure decreases but the speed increases, making it possible to inject compressed air at supersonic speed. shall be. The air reservoir chamber 41 is connected to a compressed air supply source 53 via a solenoid valve 52 via a piping 51.
Compressed air is supplied through a path independent of the opening 35, forming a bag filter cleaning device. FIG. 2 shows another embodiment of the bag filler cleaning device of the present invention.

上記バッグフィル夕2の関口端に連結し、排気室13内
に位置する筒状部材30の上部は漏斗状に舷開し、その
端面に蓋体43が被冠され、該蓋体43を貫通して圧縮
空気噴出ノズル44が節状部材30の軸心部に配設され
ている。該噴出ノズル44は絞り部441が形成される
とともに暖○442が拡関した絞り拡がり形状とされて
いる。そして該噴出ノズル44は上記実施例と同様、配
管により電磁弁を介して圧縮空気源と運通している(図
示略)。なお、11はハウジング内の隔壁、35は排気
室に蓮適する関口である。第1図に示す装置により気体
中の回収物質を分離する場合には、回収物質を含む気体
を猿過室12内に導入しバッグフィル夕2を通過せしめ
て櫨過し、櫨過されたバッグフィル夕2の内部の気体を
ノズル部材4の中心閉口より導出し、図示実線矢印の経
路により排出ファン(図示略)にて排出口131より吸
引排出せしめる。
The upper part of the cylindrical member 30 connected to the entrance end of the bag filter 2 and located in the exhaust chamber 13 is opened in a funnel shape, and a lid 43 is crowned on the end surface of the cylindrical member 30, and a lid 43 is inserted through the lid 43. A compressed air jet nozzle 44 is arranged at the axial center of the joint member 30. The jet nozzle 44 is formed with a constricted portion 441 and has a widened constricted shape with a wide circle 442. The jet nozzle 44 is connected to a compressed air source via a solenoid valve via piping (not shown), as in the above embodiment. Note that 11 is a partition wall in the housing, and 35 is a gate that fits into the exhaust chamber. When a recovered substance in a gas is separated using the apparatus shown in FIG. The gas inside the filter 2 is led out from the central opening of the nozzle member 4, and is suctioned and discharged from the exhaust port 131 by an exhaust fan (not shown) along the path indicated by the solid arrow in the figure.

回収物質は気体がバッグフィル夕2を通過するとき気体
から分離される。分離された回収物質は一部は猿過室1
2の底部へ落下するが大部分はフィル夕2に付着し、作
業の継続に伴なし、フィルタ面に堆積する。そこで、電
磁弁52にて圧縮空気を制御して所定の時間的間隔をお
き、微小時間圧縮空気を送給し、噴出ノズル42よりバ
ッグフィルタ2内に噴射する。これによりバッグフィル
夕2内には噴射された圧縮空気の外に、その噴流により
吸引される空気が導入され、通常の気体の流れを図示破
線矢印方向に反転せしめ、この反転気流の作用によりバ
ッグフィル夕2に堆積した回収物質を離脱せしめるので
ある。そしてこの場合、本発明は噴出ノズルを絞り拡が
り形状として圧縮空気を超音速で噴出せしめるようにし
たことにより、後記する如く比較的少量の圧縮空気の送
給により、大きなバッグフィル夕清浄効果を発揮せしめ
得るのである。発明者らは、圧縮空気によるバッグフィ
ルタの清浄化効率を改善することを目的とし、圧縮空気
噴流作動時においてバッグフィルタ内にかかる圧力やバ
ッグフィル夕が変形する加速度を測定し、更に高速度カ
メラで回収物質がバッグフィル夕面から離脱する状況を
観察した結果、圧縮空気がバッグフィルタ内に噴射され
るとバッグフィルタはその外周に配した各リング間で鼓
状に膨脹し、表面に付着した回収物質はバッグフィルタ
の加速度によりバッグフィル夕とともに移動し、バッグ
フィルタの最大膨脹点で慣性によりバッグフィル夕より
離脱することを認めた。
The recovered material is separated from the gas as it passes through the bag filter 2. A portion of the separated recovered material is transferred to the monkey chamber 1.
Most of the particles fall to the bottom of the filter 2, but most of them adhere to the filter 2 and accumulate on the filter surface as the work continues. Therefore, the compressed air is controlled by the electromagnetic valve 52 to feed the compressed air for a minute time at predetermined time intervals, and is injected into the bag filter 2 from the jet nozzle 42. As a result, air sucked by the jet is introduced into the bag filter 2 in addition to the injected compressed air, and the normal gas flow is reversed in the direction of the broken line arrow shown in the figure, and the action of this reversed air flow causes the bag to be removed. The collected substances deposited on the filter 2 are removed. In this case, the present invention has the jet nozzle constricted and expanded so that compressed air can be jetted out at supersonic speed, thereby achieving a large bag filter cleaning effect by supplying a relatively small amount of compressed air as described later. It can be forced. With the aim of improving the cleaning efficiency of bag filters using compressed air, the inventors measured the pressure applied inside the bag filter and the acceleration of deformation of the bag filter when compressed air jets were activated, and also used a high-speed camera. As a result of observing the situation in which recovered substances were released from the surface of the bag filter, it was found that when compressed air was injected into the bag filter, the bag filter expanded in a drum shape between the rings arranged around its outer periphery and adhered to the surface. It was observed that the recovered material moved with the bag filter due to the acceleration of the bag filter, and separated from the bag filter due to inertia at the point of maximum expansion of the bag filter.

従って圧縮空気噴射時のバッグフィル夕内の圧力、そし
て加速度が大きい程清浄効果はすぐれており、更にバッ
グフィルタ内の圧力は圧縮空気流量とこれにより吸引さ
れる吸引流量が大きい程大きいことがわかった。第3図
は測定結果を示すもので、バッグフィルタ内の反転気流
全流量GT(GT=G^+GB、G^:圧縮空気流量、
GB:吸引流量)の増加とともにバッグフィルタ内の圧
力が増加する。また加速度ばも増加する。この場合、全
流量GT中において、吸引流量GBの圧縮空気流量G^
に対する割合GB/G^は極めて大きく、かつ全流量G
Tの増加、換言すればバッグフィルタ内の圧力の増加に
伴なし、G8/G^は増加する。従ってバッグフィルタ
の清浄効果を高めるためには、吸引流量GBを増加する
ようになすことが重要であることがわかる。なお、上記
測定は圧縮空気圧を6k9/地とし、圧力Pおよび加速
度Q‘まバッグフィルタの最下部で測定した。第4図は
、上記逆流方式バッグフィルタ清浄装置の従来例を示す
。バッグフィル夕の関口端に連結し、排気室内に位置す
る筒状部材35の上端にはノズル部材45が被冠結合さ
れ、該部材45と筒状部材35の上部内周面との間に圧
縮空気供給源と蓮適する環状の噴出ノズル46が形成さ
れている。該ノズル46は開口方向に断面積が狭小化す
る通常の噴出ノズルである。かかる噴出ノズルにおいて
は、贋口からの噴出速度は圧縮空気圧および圧縮空気流
量を増しても最高で音速であり、またこの頃流によって
吸引される吸引速度も最高で音速である。第5図は、音
速で圧縮空気を噴射した場合と、本発明により超音速で
圧縮空気を噴射した場合とにおける吸引流量の比較を示
すものである。
Therefore, it was found that the greater the pressure and acceleration inside the bag filter when compressed air is injected, the better the cleaning effect is, and furthermore, the greater the pressure inside the bag filter is as the compressed air flow rate and the suction flow rate sucked by it are greater. Ta. Figure 3 shows the measurement results, showing the total flow rate of reversed airflow in the bag filter GT (GT=G^+GB, G^: compressed air flow rate,
The pressure inside the bag filter increases as the GB (suction flow rate) increases. The acceleration also increases. In this case, during the total flow rate GT, the compressed air flow rate G^ of the suction flow rate GB
The ratio GB/G^ is extremely large, and the total flow rate G
As T increases, in other words as the pressure inside the bag filter increases, G8/G^ increases. Therefore, it can be seen that in order to enhance the cleaning effect of the bag filter, it is important to increase the suction flow rate GB. In addition, the above measurement was performed using a compressed air pressure of 6k9/ground, and the pressure P and acceleration Q' were measured at the lowest part of the bag filter. FIG. 4 shows a conventional example of the above-mentioned backflow type bag filter cleaning device. A nozzle member 45 is connected to the upper end of a cylindrical member 35 that is connected to the exit end of the bag filter and located in the exhaust chamber, and a nozzle member 45 is connected to the upper end of the cylindrical member 35 . An annular jet nozzle 46 is formed which is compatible with an air supply source. The nozzle 46 is a normal jet nozzle whose cross-sectional area becomes narrower in the opening direction. In such an ejection nozzle, the ejection speed from the counterfeit port is at most the sonic speed even if the compressed air pressure and compressed air flow rate are increased, and the suction speed sucked by the current at this time is also at the sonic speed at the maximum. FIG. 5 shows a comparison of the suction flow rate when compressed air is injected at sonic speed and when compressed air is injected at supersonic speed according to the present invention.

なお用いた本発明装置は第1図に示す形式で、噴出ノズ
ル絞り部421の流路面積(Ao)および贋口422の
面積凶をA/Ao=1.34に形成したものを用い、送
給圧縮空気圧力Poと噴口422の空気圧力P.とをP
,/Po=0.2に調整し、噴出速度1.7マッハとし
た。そして第5図の如く、噴射速度が音速の場合と超音
速(1.7マッハ)の場合において、反転気流全流量G
Tおよびこれによるバッグフィルタ内の圧力Pを同じに
したとき、G,中における圧縮空気流量G^は1.7マ
ッハの場合の方が約10%少ない。換言すればGB/G
^は1.7マッハの場合の方が約10%多い。即ち、同
一の清浄効果を菱せしめるためには、超音速で噴射した
方が音速で噴射した場合よりも送給圧縮空気量が少なく
てすみ、それだけ動力の節減になるのである。また、同
一流量の圧縮空気を送給したとき、超音速で噴射した場
合の方が音速で噴射した場合よりも加速度が大きくなり
すぐれたバッグフィルタ清浄効果を発揮する。上記の如
く本発明は逆流方式のバッグフィル夕清浄装置において
、圧縮空気の噴出ノズルを絞り拡がり形状とすることに
より超音速で圧縮空気をバッグフィル夕内に噴射せしめ
るようになし、これによって吸引効率(GB/G^)を
増加せしめ、バッグフィル夕の清浄化効率を向上せしめ
るとともに、動力の節減に貢献するものである。
The device of the present invention used was of the type shown in FIG. 1, and the flow path area (Ao) of the ejection nozzle constriction portion 421 and the area ratio of the counterfeit opening 422 were set to A/Ao = 1.34. Supply compressed air pressure Po and air pressure P of the nozzle 422. and P
, /Po=0.2, and the ejection speed was set at 1.7 Mach. As shown in Figure 5, when the injection speed is sonic speed and when it is supersonic speed (1.7 Mach), the total flow rate G of the reverse airflow is
When T and the resulting pressure P in the bag filter are the same, the compressed air flow rate G in G is about 10% smaller in the case of 1.7 Mach. In other words, GB/G
^ is about 10% higher in the case of 1.7 Mach. That is, in order to achieve the same cleaning effect, injection at supersonic speed requires less compressed air to be fed than injection at sonic speed, resulting in a corresponding reduction in power. Furthermore, when compressed air is fed at the same flow rate, the acceleration is greater when the air is injected at supersonic speed than when it is injected at the sonic speed, resulting in a superior bag filter cleaning effect. As described above, the present invention is a backflow type bag filter cleaning device in which the compressed air jet nozzle is shaped into a constricted and expanding shape to inject compressed air into the bag filter at supersonic speed, thereby improving suction efficiency. (GB/G^), improves the cleaning efficiency of the bag filter, and contributes to saving power.

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

第1図は本発明の清浄装置を具備したバッグフィルタ装
置の断面図、第2図は本発明の清浄装置の他の実施例断
面図、第3図はバッグフィルタ清浄化作用時におけるバ
ッグフィルタ内の圧力と反転空気流量の関係を示す図、
第4図は従来の清浄装置の一例を示す断面図、第5図は
バッグフィル夕清浄化作用時における圧縮空気噴射速度
と反転空気流量との関係を示す図である。 1・・・・・・ハウジング、12・・・・・・猿過室、
13・・・・・・排気室、2・・・・・・バッグフィル
夕、3,30,35・・・・・・バッグフィルタに取付
けた筒状部材、42,44,46・…・・圧縮空気噴出
ノズル、421,441・・・・・・噴出ノズルの絞り
部、422,442・・・…噴出ノズルの頃口。 第1図 第2図 第3図 第5図 第4図
FIG. 1 is a sectional view of a bag filter device equipped with the cleaning device of the present invention, FIG. 2 is a sectional view of another embodiment of the cleaning device of the present invention, and FIG. 3 is a sectional view of the interior of the bag filter during the bag filter cleaning action. Diagram showing the relationship between pressure and reverse air flow rate,
FIG. 4 is a sectional view showing an example of a conventional cleaning device, and FIG. 5 is a diagram showing the relationship between compressed air injection speed and reverse air flow rate during bag filling and cleaning operations. 1...Housing, 12...Sarugoshitsu,
13... Exhaust chamber, 2... Bag filter, 3, 30, 35... Cylindrical member attached to the bag filter, 42, 44, 46... Compressed air ejection nozzle, 421, 441...Constriction part of the ejection nozzle, 422,442...Earth opening of the ejection nozzle. Figure 1 Figure 2 Figure 3 Figure 5 Figure 4

Claims (1)

【特許請求の範囲】[Claims] 1 回収固体物質を含む気体を導入する濾過室と、濾過
された気体を排出する排気室とに区画されたハウジング
の上記濾過室に有底筒状のバツグフイルタを位置せしめ
るとともに、該バツグフイルタの開口端に連結した筒状
部材を上記排気室に開口せしめて成るバツグフイルタ装
置において、上記濾過室と排気室とを区画する隔壁を貫
通せしめた上記筒状部材の濾過室側の端部を上記バツグ
フイルタの開口端に連結するとともに、排気室側の端部
に筒状部材内と排気室とを連通する開口を形成し、筒状
部材内には噴出口をバツグフイルタに向けた噴出ノズル
を設けて筒状部材の上記開口とは独立の経路で圧縮空気
源と連通せしめ、かつ上記噴出ノズルには絞り部を設け
るとともに噴出口を拡開せしめて超音波で圧縮空気を上
記バツグフイルタ内へ噴出するようになしたことを特徴
とするバツグフイルタの清浄装置。
1. A bottomed cylindrical baggage filter is placed in the filtration chamber of the housing, which is divided into a filtration chamber for introducing gas containing recovered solid substances and an exhaust chamber for discharging the filtered gas, and an open end of the baggage filter is installed. In a bag filter device comprising a cylindrical member connected to the exhaust chamber, the end of the cylindrical member on the filtration chamber side, which passes through a partition wall that partitions the filtration chamber and the exhaust chamber, is connected to the opening of the bag filter. At the same time, an opening is formed at the end on the exhaust chamber side to communicate the inside of the cylindrical member and the exhaust chamber, and an ejection nozzle is provided in the cylindrical member with its ejection port facing the bug filter. communicates with a compressed air source through a path independent of the opening, and the jetting nozzle is provided with a constriction part and the jetting port is expanded to jet compressed air into the baggage filter using ultrasonic waves. A bag filter cleaning device characterized by the following.
JP1158778A 1978-02-03 1978-02-03 Bag filter cleaning device Expired JPS6029534B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1158778A JPS6029534B2 (en) 1978-02-03 1978-02-03 Bag filter cleaning device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1158778A JPS6029534B2 (en) 1978-02-03 1978-02-03 Bag filter cleaning device

Publications (2)

Publication Number Publication Date
JPS54105374A JPS54105374A (en) 1979-08-18
JPS6029534B2 true JPS6029534B2 (en) 1985-07-11

Family

ID=11782027

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1158778A Expired JPS6029534B2 (en) 1978-02-03 1978-02-03 Bag filter cleaning device

Country Status (1)

Country Link
JP (1) JPS6029534B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018122296A (en) * 2018-02-19 2018-08-09 ユーエスウラサキ株式会社 Dust collector

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0346830Y2 (en) * 1985-11-21 1991-10-03
KR20010018238A (en) * 1999-08-18 2001-03-05 이구택 A Reverse Air Cleaning Bag House System Using Outside Filtration
KR100460666B1 (en) * 1999-12-27 2004-12-09 주식회사 포스코 Method and apparatus for remove dust in filtering machine
FR2818159B1 (en) 2000-12-15 2003-10-03 Franco Belge Combustibles PROCESS AND DEVICE FOR DECOLMATING A FILTER OF A PLANT FOR THE PRODUCTION OF URANIUM OXIDE FROM URANIUM HEXAFLUORIDE
CN109838868A (en) * 2017-11-28 2019-06-04 山西彩云归科技有限公司 A kind of split type new blower fan apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018122296A (en) * 2018-02-19 2018-08-09 ユーエスウラサキ株式会社 Dust collector

Also Published As

Publication number Publication date
JPS54105374A (en) 1979-08-18

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