JPH0757295B2 - Method and apparatus for detecting abnormality of filter element assembly type dust collecting equipment - Google Patents

Method and apparatus for detecting abnormality of filter element assembly type dust collecting equipment

Info

Publication number
JPH0757295B2
JPH0757295B2 JP6269590A JP6269590A JPH0757295B2 JP H0757295 B2 JPH0757295 B2 JP H0757295B2 JP 6269590 A JP6269590 A JP 6269590A JP 6269590 A JP6269590 A JP 6269590A JP H0757295 B2 JPH0757295 B2 JP H0757295B2
Authority
JP
Japan
Prior art keywords
filter element
group
dust
valve
row
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 - Lifetime
Application number
JP6269590A
Other languages
Japanese (ja)
Other versions
JPH03267105A (en
Inventor
健治 亀井
健三郎 児玉
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.)
Kawasaki Motors Ltd
Original Assignee
Kawasaki Jukogyo 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 Kawasaki Jukogyo KK filed Critical Kawasaki Jukogyo KK
Priority to JP6269590A priority Critical patent/JPH0757295B2/en
Publication of JPH03267105A publication Critical patent/JPH03267105A/en
Publication of JPH0757295B2 publication Critical patent/JPH0757295B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Filtering Of Dispersed Particles In Gases (AREA)

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、多くのバグあるいはセラミックチューブ等に
よって構成され、長時間の連続運転を行なう集塵設備に
おいて、集塵設備の運転を休止することなく異常を生じ
たフィルタエレメントを的確に検出する方法およびその
装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention is a dust collecting apparatus which is constituted by many bugs or ceramic tubes and which is continuously operated for a long time, and to stop the operation of the dust collecting apparatus. TECHNICAL FIELD The present invention relates to a method and an apparatus for accurately detecting a filter element in which an abnormality has occurred.

[従来の技術] 第3図は従来技術の例で、特開昭55−61911号公報に記
載された逆洗装置付高温用除塵機の側断面図である。第
3図において51はセラミックフィルタエレメント、52は
密封容器、53は排ガス入口、54は排ガス排出口、55は排
ガス導入室、56はダスト取出口、57は支持盤、58は逆洗
空気噴射ノズル、59は空気供給導管、60は圧縮空気供給
装置、61は排ガス排出室である。
[Prior Art] FIG. 3 is an example of the prior art and is a side sectional view of a high temperature dust remover with a backwash device described in Japanese Patent Laid-Open No. 55-61911. In FIG. 3, 51 is a ceramic filter element, 52 is a sealed container, 53 is an exhaust gas inlet, 54 is an exhaust gas outlet, 55 is an exhaust gas introducing chamber, 56 is a dust outlet, 57 is a support plate, and 58 is a backwash air injection nozzle. , 59 is an air supply conduit, 60 is a compressed air supply device, and 61 is an exhaust gas discharge chamber.

該従来技術における除塵機の構造は、有底筒状を呈する
多孔質のセラミックフィルタエレメントが支持盤57によ
って懸架され、密封容器52内に形設された排ガス導入室
55の上部に複数列配設されている。排ガス入口53から密
封容器52内に流入したダストを含有した排ガスは排ガス
導入室55内を上昇してセラミックフィルタエレメント51
によって濾過され、ダストを前記セラミックフィルタエ
レメント51の外面に付着させ、清浄な状態になった排ガ
スのみが支持盤57上部の排ガス排出室61を経て排ガス排
出口54から排出される。
The structure of the dust remover in the prior art is an exhaust gas introducing chamber in which a porous ceramic filter element having a bottomed cylindrical shape is suspended by a support board 57 and formed in a sealed container 52.
A plurality of rows are arranged above the 55. The exhaust gas containing dust that has flowed into the sealed container 52 from the exhaust gas inlet 53 rises in the exhaust gas introduction chamber 55 and rises to the ceramic filter element 51.
Only the exhaust gas which has been filtered and dust adheres to the outer surface of the ceramic filter element 51 and is in a clean state is exhausted from the exhaust gas exhaust port 54 through the exhaust gas exhaust chamber 61 above the support board 57.

排ガスの除去作業を継続することにより、セラミックフ
ィルタエレメント51の外表面に付着するダスト量が増加
し、それに基づく通風抵抗の増加によって排ガスの処理
能力が低下して来る。該従来技術においてはそれに対処
するために第3図に示すように各フィルタエレメント51
の個々の上部開口端部に逆洗空気噴射ノズル58を配設
し、圧縮空気供給装置60から空気供給導管59を通じて送
られて来る圧縮空気を各セラミックフィルタエレメント
51内に噴出させる。噴出された圧縮空気はセラミックフ
ィルタエレメント51内の圧力を高め、その一部はセラミ
ックフィルタエレメント51内に穿設された微細孔を通じ
て排ガス導入室55内に排ガスと逆の方向に流れる。これ
によってセラミックフィルタエレメント51の外面に付着
していたダストの大部分は剥離し、排ガス導入室55の下
部に落下し、落下したダストはさらに底部に形設されて
いるダスト取出口56から外部に排出、除去される。
By continuing the exhaust gas removal work, the amount of dust adhering to the outer surface of the ceramic filter element 51 increases, and the ventilation resistance based on this increases the exhaust gas treatment capacity. In the prior art, each filter element 51 is provided as shown in FIG.
A backwash air injection nozzle 58 is arranged at each upper open end of the compressed air supplied from the compressed air supply device 60 through the air supply conduit 59 to each ceramic filter element.
Eject into 51. The jetted compressed air increases the pressure in the ceramic filter element 51, and a part of the compressed air flows in the exhaust gas introduction chamber 55 in the direction opposite to the exhaust gas through the fine holes formed in the ceramic filter element 51. As a result, most of the dust adhering to the outer surface of the ceramic filter element 51 is peeled off and falls to the lower part of the exhaust gas introducing chamber 55, and the fallen dust is further discharged from the dust outlet 56 formed at the bottom. Ejected and removed.

[発明が解決しようとする課題] このように上記従来技術においても、セラミックフィル
タエレメント等からなる除塵機によって排ガス中のダス
トを濾過し、排ガスを清浄な状態で排出させると共に、
前記フィルタエレメントの外面に付着したダストを圧縮
空気の噴出によって剥離除去することによって長時間の
連続的操業を行なわしめることが可能であった。
[Problems to be Solved by the Invention] As described above, also in the above-mentioned conventional technique, the dust in the exhaust gas is filtered by the dust remover including the ceramic filter element and the exhaust gas is discharged in a clean state.
It was possible to carry out continuous operation for a long time by separating and removing the dust adhering to the outer surface of the filter element by jetting compressed air.

しかしながら上記従来の技術においては、操業中に前記
フィルタエレメントの一部に破損等の不具合が発生した
場合に、除塵機から排出される排ガス中のダスト濃度を
測定することによって異常そのものは検知することが可
能であったが、それがどのフィルタエレメントにおいて
発生したものであるか特定することが不可能であったこ
とから、それが特定のフィルタエレメントのみに発生し
た偶発的不具合であるか、あるいはまた全てのフィルタ
エレメントに発生しつつある経年劣化等によるものであ
るか等を確認するためには除塵機の操業を停止した上、
フィルタエレメント1本宛チェックする必要があり、長
時間の操業の休止を必要とすると言う不都合を有してい
た。
However, in the above-mentioned conventional technique, when a defect such as damage occurs in a part of the filter element during operation, the abnormality itself can be detected by measuring the dust concentration in the exhaust gas discharged from the dust remover. Was possible, but it was not possible to specify in which filter element it occurred, so whether it was an accidental failure that occurred only in a specific filter element, or In order to confirm whether it is due to aging deterioration that is occurring in all filter elements, etc., stop the operation of the dust remover,
It is necessary to check only one filter element, and there is the inconvenience that the operation must be stopped for a long time.

本発明はこのような現状に鑑みてなされたもので、簡潔
な構成によって操業中においても非常に多数のフィルタ
エレメントの中から特定の不具合フィルタエレメントを
容易にかつ的確に確認し得る検知方法およびその装置を
提供することを目的としている。
The present invention has been made in view of the above circumstances, and a detection method and a detection method capable of easily and accurately confirming a specific defective filter element from among a large number of filter elements even during operation with a simple configuration. The purpose is to provide a device.

[課題を解決するための手段] 上記の目的は、前記特許請求の範囲に記載された異常検
知方法およびその装置によって達成される。すなわち、 (1) 多数のシリンダ状等のフィルタエレメントの集
合で構成される集塵設備において、各フィルタエレメン
ト毎にガスを吸引する異常検知パイプを2本配設し、前
記2本の異常検知パイプはそれぞれの縦列毎およびそれ
ぞれの横列毎に各1本を割り当てて各列毎に一つの組を
構成させ、前記各組毎にガスの吸引を行なってダストの
濃度を測定するフィルタエレメント集合型集塵設備の異
常検知方法。
[Means for Solving the Problems] The above object can be achieved by the abnormality detection method and the apparatus thereof described in the claims. That is, (1) In a dust collecting facility composed of a large number of cylindrical filter elements, two abnormality detection pipes for sucking gas are provided for each filter element, and the two abnormality detection pipes are provided. Is a filter element assembly type collection unit for allocating one to each column and each row to configure one group for each column, and suctioning gas for each group to measure the dust concentration. Dust equipment abnormality detection method.

(2) 多数のシリンダ状等のフィルタエレメントの集
合で構成される集塵設備において、各フィルタエレメン
ト毎にガスを吸引する異常検知パイプを2本配設し、前
記2本の異常検知パイプはそれぞれの縦列毎およびそれ
ぞれの横列毎に各1本を割り当てて各列毎に一つの組を
構成させ、前記各組毎にガスの吸引を行なえるようにバ
ルブを設けて、それらをダスト濃度測定装置につなぐフ
ィルタエレメント集合型集塵設備の異常検知装置。
(2) In a dust collection facility composed of a large number of cylindrical filter elements, two abnormality detection pipes for sucking gas are provided for each filter element, and the two abnormality detection pipes are respectively provided. One column is assigned to each column and each row to configure one group for each column, and a valve is provided for each group so that gas can be sucked, and each of the groups is provided with a dust concentration measuring device. An anomaly detection device for a filter element assembly type dust collection facility.

である。Is.

以下、本発明の作用等について実施例に基づいて説明す
る。
Hereinafter, the operation and the like of the present invention will be described based on Examples.

[実施例] 第1〜2図は本発明に基づく実施例を示す図で、第1図
はその系統図、第2図はフィルタエレメント上端部と検
知管の部分断面図である。第1〜2図において、1はフ
ィルタエレメント、2は集塵機胴、3はダスト濃度測定
器、4は吸引ファン、5はA群検知主管、6はB群検知
主管、7はA群主弁、8はB群主弁、9〜14はそれぞれ
A群支管の弁A1〜弁A6、15〜20はそれぞれB群支管の弁
B1〜弁B6、21は管板、22はA群支管、23はA群検知管、
24はB群支管、25はB群検知管である。
[Embodiment] FIGS. 1 and 2 are views showing an embodiment based on the present invention, FIG. 1 is a system diagram thereof, and FIG. 2 is a partial sectional view of a filter element upper end portion and a detection tube. 1 and 2, 1 is a filter element, 2 is a dust collector body, 3 is a dust concentration measuring instrument, 4 is a suction fan, 5 is an A group detection main pipe, 6 is a B group detection main pipe, 7 is an A group main valve, 8 is a B group main valve, 9 to 14 are A group branch pipe valves A 1 to A 6 , 15 to 20 are B group branch pipe valves.
B 1 ~ valve B 6, 21 is a tube plate, 22 is the group A branch pipe, 23 Group A detector tube,
Reference numeral 24 is a group B branch tube, and 25 is a group B detection tube.

第1〜2図はフィルタエレメントが集塵機胴内に碁盤目
状に配列されている場合の例である。第1図において図
面の縦方向の列をA列とし横方向の列をB列とする。同
図においてはA列およびB列共にそれぞれ6列からなっ
ている。以下、各列について弁A19,弁A210,……弁A614
を有する列をそれぞれA1列,A2列,……A6列と呼び、同
様に弁B115,弁B216,……弁B620を有する列をそれぞれB1
列,B2列,……B6列と呼ぶ。フィルタエレメント1は第
2図に示すように、その上端部を集塵機胴2の上部空間
に開口し、管板21にボルト等によって取着されている。
すべてのフィルタエレメント1の上端開口部には第2図
に示すようにそれぞれA群検知管23およびB群検知管25
が挿設されている。A群検知管は各列毎にそれぞれのA
群支管22に連通されており、さらに前記A群支管22はそ
れぞれの電磁弁等の弁A19,弁A210,……弁A614を通じて
A群検知主管5に連通している。B群検知管25もA群検
知管23と同様に各列毎にまとめられてB群支管24に連通
し、各B群支管24はさらにそれぞれの弁B115,弁B216,…
…弁B620を通じてB群検知主管6に連通している。A群
検知主管5とB群検知主管6はそれぞれA群主弁7およ
びB群主弁8を通じて1本にまとめられ、ダスト濃度測
定器3および吸引ファン4を通じて所定の位置まで連通
されている。(集塵機胴2内のガスの圧力が大気圧より
も十分高い場合には吸引ファン4は省略し得る。) 次に上記装置によるフィルタエレメント1の異常検知の
方法について説明する。まず第1図においてA群から検
知を行なう場合、フィルタエレメント1の非逆洗工程時
(以下同じ)にA群主弁7を開としB群主弁8を閉とす
る。次に弁A19を開とし弁A210〜弁A614をすべて閉とす
る。これによって第1図におけるフィルタエレメント1
はA1列の2本のみが内部のガスを吸引ファン4によって
吸引され、そのガス中のダスト濃度をダスト濃度測定器
3によって測定される。次に弁A19を閉じ、弁A210のみ
を開く。この時、他の弁A311〜A614およびB群主弁8は
すべて全閉の状態を保持している。それによってA2列の
4本のフィルタエレメント1内のガスが吸引され、該ガ
ス中のダスト濃度が測定される。
1 and 2 show an example in which the filter elements are arranged in a grid pattern in the dust collector body. In FIG. 1, a vertical row in the drawing is an A row and a horizontal row is a B row. In the figure, each of the rows A and B has six rows. Below, for each row, valve A 1 9, valve A 2 10, ... valve A 6 14
Each A 1 rows of columns having, A 2 columns, ...... A is called the six columns, similarly the valve B 1 15, valve B 2 16, ...... valve train respectively B 1 with B 6 20
Row, B row 2 , ... B 6 row. As shown in FIG. 2, the filter element 1 has its upper end opened to the upper space of the dust collector body 2 and is attached to the tube plate 21 by bolts or the like.
At the upper end openings of all the filter elements 1, as shown in FIG.
Has been inserted. The A group detector tubes have their own A for each row.
Is communicated with a group branch pipe 22, and further communicates the valve A 1 9, such as group A branch pipe 22 and each of the solenoid valves, the valve A 2 10, the group A sensing main pipe 5 through ...... valve A 6 14. Similarly to the A group detection pipe 23, the B group detection pipe 25 is also grouped into each row and communicates with the B group branch pipe 24, and each B group branch pipe 24 further has its respective valve B 1 15, valve B 2 16, ...
... communicates with the group B detects main 6 through valve B 6 20. The A-group detection main pipe 5 and the B-group detection main pipe 6 are combined into one via the A-group main valve 7 and the B-group main valve 8, respectively, and communicated to a predetermined position through the dust concentration measuring device 3 and the suction fan 4. (When the pressure of the gas in the dust collector body 2 is sufficiently higher than the atmospheric pressure, the suction fan 4 may be omitted.) Next, a method of detecting abnormality of the filter element 1 by the above device will be described. First, in the case of performing detection from the group A in FIG. 1, the group A main valve 7 is opened and the group B main valve 8 is closed during the non-backwashing process of the filter element 1 (the same applies hereinafter). Next, valve A 1 9 is opened and valves A 2 10 to A 6 14 are all closed. As a result, the filter element 1 in FIG.
Only the two A 1 rows have their internal gas sucked by the suction fan 4, and the dust concentration in the gas is measured by the dust concentration measuring device 3. Then close valve A 1 9 and open valve A 2 10 only. At this time, all other valves A 3 11~A 6 14 and B group main valve 8 holds the state of all closed. As a result, the gas in the four filter elements 1 in the A 2 row is sucked, and the dust concentration in the gas is measured.

このようにして各A列毎のダスト濃度を順次測定し、す
べてのA列の測定が完了した後A群主弁7を閉じてB群
主弁8を開き、以下A群と同様にB1列,B2列,……B6
と、各列毎にフィルタエレメント1中のガスのダスト濃
度を測定する。このようにしてすべての列のフィルタエ
レメント1中のガスのダスト濃度の測定を行ない、それ
が完了した後は必要に応じて各検知用配管中に不活性ガ
スあるいは圧縮空気等を送入して検知装置内配管系の逆
洗洗浄等を行ない、検知装置中のすべての弁を閉止し、
吸引ファン4を停止する。
Thus successively measured dust concentration in each A column, all close the group A main valve 7 after the measurement of the A column is complete open the B group main valve 8, as in the following Group A B 1 column, B 2 columns, and ...... B 6 columns, measuring the dust concentration of the gas in the filter element 1 in each column. In this way, the dust concentration of the gas in the filter elements 1 in all the rows is measured, and after the measurement, the inert gas or compressed air is fed into each detection pipe as needed. Backwash and clean the piping system inside the detector, close all the valves in the detector,
The suction fan 4 is stopped.

上記手順によるダスト濃度の測定結果を検討し、例えば
A群中においてA3列のダスト濃度に異常値が存在し、ま
たB群中においてB2列のダスト濃度に異常値が存在した
場合には、A3列とB2列とが交差する位置のフィルタエレ
メント1(第1図において※印を付したフィルタエレメ
ント1)が異常対象フィルタエレメントであると知り得
る。
Examining the measurement results of the dust concentration by the above procedure, for example, if there is an abnormal value in the dust concentration in the A 3 row in the group A and an abnormal value in the dust concentration in the B 2 row in the group B, , A 3 row and B 2 row cross each other, it can be known that the filter element 1 (filter element 1 marked with * in FIG. 1) is the abnormality target filter element.

[発明の効果] このように本発明は上記実施例から明らかなように、以
下に示す効果を有している。すなわち、多数のフィルタ
エレメントの集合で構成される集塵設備から送出される
ガス中に異常濃度のダストが存在した場合において、 従来不可能であった運転中における異常フィルタエ
レメントの特定を的確になし得る。
[Effects of the Invention] As described above, the present invention has the following effects, as is apparent from the above-described embodiments. In other words, if there is an abnormal concentration of dust in the gas sent from the dust collection equipment that is composed of a large number of filter elements, it is possible to accurately identify the abnormal filter element during operation, which was impossible in the past. obtain.

異常フィルタエレメントが複数である場合にも、そ
れぞれ個々のフィルタエレメントの不具合程度やその経
時変化等を把握し得る。
Even when there are a plurality of abnormal filter elements, it is possible to grasp the degree of failure of each individual filter element and its change over time.

集塵設備稼働中においても、非逆洗時であれば随時
測定が可能であり、従来におけるが如くフィルタエレメ
ントの点検の都度当該集塵設備を停止する必要がないた
め生産ラインへ与える影響を著しく低減し得る。
Even when the dust collector is in operation, it can be measured at any time during non-backwashing.Since it is not necessary to stop the dust collector every time the filter element is inspected as in the conventional case, the effect on the production line is significant. Can be reduced.

大型で極めてフィルタエレメントの数の多い集塵機
において、従来発見が困難であったフィルタエレメント
群の中央部あるいは高所部に不具合個所を有するフィル
タエレメントを容易にかつ的確に特定し得る。
In a dust collector having a large size and a large number of filter elements, it is possible to easily and accurately identify a filter element having a defective portion at the central portion or high portion of the filter element group, which has been difficult to find conventionally.

フィルタエレメントの配列が碁盤目配列以外の千鳥
配列等であっても検知し得る。
It can be detected even if the arrangement of the filter elements is a staggered arrangement other than the grid arrangement.

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

第1〜2図は本発明に基づく実施例を示す図で、第1図
はその系統図、第2図はフィルタエレメント上端部の部
分断面図である。 第3図は従来技術の例である。 1……フィルタエレメント、2……集塵機胴、3……ダ
スト濃度測定器、4……吸引ファン、5……A群検知主
管、6……B群検知主管、7……A群主弁、8……B群
主弁、9〜14……弁A1〜弁A6、15〜20……弁B1〜B6、21
……管板、22……A群支管、23……A群検知管、24……
B群支管、25……B群検知管、51……セラミックフィル
タエレメント、52……密封容器、53……排ガス入口、54
……排ガス排出口、55……排ガス導入室、56……ダスト
取出口、57……支持盤、58……逆洗空気噴射ノズル、59
……空気供給導管、60……圧縮空気供給装置、61……排
ガス排出室。
1 and 2 are views showing an embodiment based on the present invention, FIG. 1 is a system diagram thereof, and FIG. 2 is a partial sectional view of an upper end portion of a filter element. FIG. 3 is an example of the prior art. 1 ... Filter element, 2 ... Dust collector body, 3 ... Dust concentration measuring device, 4 ... Suction fan, 5 ... A group detection main pipe, 6 ... B group detection main pipe, 7 ... A group main valve, 8 ... B group main valve, 9-14 ... Valve A 1 -Valve A 6 , 15-20 ... Valve B 1- B 6 , 21
...... Tube plate, 22 …… A group branch pipe, 23 …… A group detector tube, 24 ……
Group B branch pipe, 25 ... B group detection pipe, 51 ... Ceramic filter element, 52 ... Sealed container, 53 ... Exhaust gas inlet, 54
...... Exhaust gas exhaust port, 55 …… Exhaust gas introduction chamber, 56 …… Dust extraction port, 57 …… Support plate, 58 …… Backwash air injection nozzle, 59
...... Air supply conduit, 60 ...... Compressed air supply device, 61 ...... Exhaust gas discharge chamber.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】多数のシリンダ状等のフィルタエレメント
の集合で構成される集塵設備において、各フィルタエレ
メント毎にガスを吸引する異常検知パイプを2本配設
し、前記2本の異常検知パイプはそれぞれの縦列毎およ
びそれぞれの横列毎に各1本を割り当てて各列毎に一つ
の組を構成させ、前記各組毎にガスの吸引を行なってダ
ストの濃度を測定することを特徴とするフィルタエレメ
ント集合型集塵設備の異常検知方法。
1. A dust collecting facility comprising a large number of cylindrical filter elements, wherein two abnormality detection pipes for sucking gas are provided for each filter element, and the two abnormality detection pipes are provided. Is characterized in that one column is assigned to each column and each row is configured to form one group, and gas is sucked for each group to measure the dust concentration. Abnormality detection method for filter element assembly type dust collection equipment.
【請求項2】多数のシリンダ状等のフィルタエレメント
の集合で構成される集塵設備において、各フィルタエレ
メント毎にガスを吸引する異常検知パイプを2本配設
し、前記2本の異常検知パイプはそれぞれの縦列毎およ
びそれぞれの横列毎に各1本を割り当てて各列毎に一つ
の組を構成させ、前記各組毎にガスの吸引を行なえるよ
うにバルブを設けて、それらをダスト濃度測定装置につ
なぐことを特徴とするフィルタエレメント集合型集塵設
備の異常検知装置。
2. A dust collecting facility comprising a large number of cylindrical filter elements, wherein two abnormality detection pipes for sucking gas are provided for each filter element, and the two abnormality detection pipes are provided. Assigns one line to each column and each row to configure one group for each column, and a valve is provided for each group so that gas can be sucked and dust concentration is set for each group. An abnormality detection device for a filter element assembly type dust collection facility characterized by being connected to a measuring device.
JP6269590A 1990-03-15 1990-03-15 Method and apparatus for detecting abnormality of filter element assembly type dust collecting equipment Expired - Lifetime JPH0757295B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6269590A JPH0757295B2 (en) 1990-03-15 1990-03-15 Method and apparatus for detecting abnormality of filter element assembly type dust collecting equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6269590A JPH0757295B2 (en) 1990-03-15 1990-03-15 Method and apparatus for detecting abnormality of filter element assembly type dust collecting equipment

Publications (2)

Publication Number Publication Date
JPH03267105A JPH03267105A (en) 1991-11-28
JPH0757295B2 true JPH0757295B2 (en) 1995-06-21

Family

ID=13207691

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6269590A Expired - Lifetime JPH0757295B2 (en) 1990-03-15 1990-03-15 Method and apparatus for detecting abnormality of filter element assembly type dust collecting equipment

Country Status (1)

Country Link
JP (1) JPH0757295B2 (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3538238B2 (en) * 1994-10-03 2004-06-14 進和テック株式会社 Moving pulse jet type bag filter
WO2007106003A1 (en) * 2006-03-14 2007-09-20 Camfil Ab Air filter housing with means for measuring particle concentration
US8007568B2 (en) * 2006-04-12 2011-08-30 Millipore Corporation Filter with memory, communication and pressure sensor
JP6374133B1 (en) * 2018-05-17 2018-08-15 曜一 堀 Filter leak monitoring device and particle separator equipped with the same
JP6782038B1 (en) * 2019-12-26 2020-11-11 エンジニアリング・クルー株式会社 Filter leak monitoring device for particle separator and particle separator equipped with it
JP7197937B1 (en) * 2021-12-08 2022-12-28 株式会社フクハラ Separator

Also Published As

Publication number Publication date
JPH03267105A (en) 1991-11-28

Similar Documents

Publication Publication Date Title
KR100276836B1 (en) Method and apparatus for rapidly testing the integrity of filter elements
JPS623367B2 (en)
US4655799A (en) Pulse cleaning system for dust filters
US4158554A (en) Apparatus for filtering particulate-laden gases
JPH0757295B2 (en) Method and apparatus for detecting abnormality of filter element assembly type dust collecting equipment
CN207641157U (en) A kind of self-test leakage sack cleaner
US4113449A (en) Baghouse cleaning method
SE543277C2 (en) Aerosol distribution in filter testing systems
CN115591325A (en) Device and method for testing and evaluating bag type dust removal pulse blowing performance
AU737828B2 (en) Process for monitoring the integrity of hollow fibre filtration modules
JP2007130566A (en) Breakage sensing method of filter cloth of dust collector
US3490205A (en) High pressure gas filter system
JP3215757B2 (en) Inspection method and inspection device for dust collector
JPH07328363A (en) Damaged filter cloth sensing method for bag filter
CN114152714A (en) Dioxin monitoring system suitable for high dust environment
Letourneau et al. Effects of the particle penetration inside the filter medium on the HEPA filter pressure drop
JPH08503654A (en) Method for cleaning a filter bag of a bag filter device
JPH01307424A (en) Device for detecting damaged filter cloth in bag filter
JP3460991B2 (en) Pulse cleaning method for multi-chamber bag filter
CN216386967U (en) Dioxin monitoring system suitable for high dust environment
EP3528923A1 (en) Determination of dust load in a bag filter
EP0704234A1 (en) Dust removing apparatus
JP6782038B1 (en) Filter leak monitoring device for particle separator and particle separator equipped with it
CN216677449U (en) Dust removal device for smoke detection equipment and smoke detection equipment
WO2019141498A1 (en) Membrane modules with limited defects and related methods