JPS6018204B2 - Filter media, dust collection method and equipment that involve transportation and separation of dust - Google Patents

Filter media, dust collection method and equipment that involve transportation and separation of dust

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Publication number
JPS6018204B2
JPS6018204B2 JP547277A JP547277A JPS6018204B2 JP S6018204 B2 JPS6018204 B2 JP S6018204B2 JP 547277 A JP547277 A JP 547277A JP 547277 A JP547277 A JP 547277A JP S6018204 B2 JPS6018204 B2 JP S6018204B2
Authority
JP
Japan
Prior art keywords
dust
nitrogen gas
filter
filter media
dust collection
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
JP547277A
Other languages
Japanese (ja)
Other versions
JPS5391471A (en
Inventor
勝巳 末広
勲平 尾崎
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 Heavy Industries Ltd
Original Assignee
Kawasaki Heavy Industries 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 Kawasaki Heavy Industries Ltd filed Critical Kawasaki Heavy Industries Ltd
Priority to JP547277A priority Critical patent/JPS6018204B2/en
Publication of JPS5391471A publication Critical patent/JPS5391471A/en
Publication of JPS6018204B2 publication Critical patent/JPS6018204B2/en
Expired legal-status Critical Current

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Description

【発明の詳細な説明】 本発明は砂、砂利、セラミックス、耐火物などの粒塊状
ろ過材を用いる集じん方法および集じん装置において、
ろ過材、ダストの輸送・分離を伴う集じん方法およびそ
の装置に関するもので、とくに一酸化炭素分含有量の多
い転炉廃ガスなどの還元性ガス、爆発性ガスの除じんに
適するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides a dust collection method and a dust collection apparatus using a granular filter material such as sand, gravel, ceramics, and refractories.
This relates to filter media, dust collection methods and equipment that involve transportation and separation of dust, and is particularly suitable for removing reducing gases such as converter waste gas with a high carbon monoxide content and explosive gases. .

排ガス、とくに高温の排ガス中のダストを除去するため
に、集じん機本体に砂、砂利、セラミックスなどの粒塊
状耐熱性ろ過材をパネル状または層状に移動自在に設け
てなるろ過式集じん装置を、本発明者らは既に開発して
いるが、これらの装置においては、集じん機本体からダ
ストの付着したろ過材が連続的または断続的に抜き出さ
れるので、このダストの付着したろ過材を処理してろ過
材とダストとを効率よく分離し、分離後のる過材を有効
に循環再使用して装置全体の運転費を安価にすることが
要望されていた。
In order to remove dust from exhaust gas, especially high-temperature exhaust gas, this is a filtration type dust collector in which heat-resistant filtration material in the form of granules such as sand, gravel, or ceramics is movably installed in the dust collector body in the form of panels or layers. The present inventors have already developed this, but in these devices, the filter media with dust attached is extracted continuously or intermittently from the dust collector body, so the filter media with dust attached is removed. There has been a demand for efficient separation of filter material and dust by processing the filter material, and for effectively recycling and reusing the filter material after separation, thereby reducing the operating cost of the entire device.

またとくに、一酸化炭素分合有量の多い転炉廃ガスなど
の還元性ガス、爆発性ガスを除じん処理する場合は、漏
洩ガス(以下、リークガスという)が酸化、爆発するお
それがある上に、たとえば処理ガス温度が800〜10
00ooの場合、集じん機本体から排出されるダストの
付着したろ過材の温度は600〜800qo前後にもな
るので、その取扱いが困難で危険性が大きいという問題
点があった。本発明は上記の諸点を解決するためになさ
れたもので、ダストの付着したろ過材を集じん機本体か
ら連続的または断続的に抜き出した後、このろ過材とダ
ストとの混合物にシールガス兼移送用ガス、または単に
シールガスとして窒素ガスを吹き込んで冷却しながら高
所移送してろ過材とダストとを分離するとともに、ダス
トを含む窒素ガスを除じん、冷却または、除じん(以下
、単に除じん・冷却という)した後、循環再使用するこ
とにより、処理ガスの酸化、爆発を防止することができ
、かつ高温のろ過材を輸送する際に窒素ガスで300〜
400qo以下に冷却することにより取扱いを容易に行
なうことができるろ過材、ダストの輸送・分離を伴う集
じん方法およびその装置の提供を目的とするものである
In particular, when removing reducing gas or explosive gas such as converter waste gas with a high carbon monoxide content, there is a risk that the leaking gas (hereinafter referred to as "leak gas") may oxidize and explode. For example, when the processing gas temperature is 800 to 10
In the case of 00oo, the temperature of the filter medium with dust adhering to it discharged from the dust collector body is around 600 to 800 qo, which poses a problem in that it is difficult to handle and highly dangerous. The present invention was made to solve the above-mentioned problems, and after extracting the filter medium with dust attached continuously or intermittently from the main body of the dust collector, the mixture of the filter medium and dust is used as a seal gas. Nitrogen gas is blown in as a transfer gas or simply as a sealing gas and transferred to a high place while cooling to separate the filter material from the dust, and the nitrogen gas containing dust is removed, cooled, or dust removed (hereinafter simply referred to as By recycling and reusing the treated gas after removing dust and cooling, it is possible to prevent oxidation and explosion of the treated gas.
The object of the present invention is to provide a filter material that can be easily handled by cooling to 400 qo or less, a dust collection method that involves transportation and separation of dust, and an apparatus therefor.

本発明のろ過材、ダストの輸送・分離を伴う集じん方法
は、ダストを含む還元性ガス、爆発性ガスを粒塊状ろ過
材からなる集じん層を通過させて前記ガス中のダストを
分離・除去した後、ダストの付着した粒塊状ろ過材を抜
き出し、ついでこの3粒塊状ろ過材とダストとの混合物
に窒素ガスを吹き込んで冷却しながら高所移送して粒塊
状ろ過材とダストとを分離して粒塊状ろ過材を循環再使
用できるようにするとともに、ダストを含む窒素ガスを
除じん・冷却した後、循環再使用することを3特徴とす
るものである。
The dust collection method of the present invention involves transporting and separating dust and dust by passing reducing gas and explosive gas containing dust through a dust collection layer made of a granular filter material to separate and separate dust in the gas. After removal, the agglomerated filter media with dust attached is extracted, and then nitrogen gas is blown into the mixture of the three agglomerated filter media and the dust, and the mixture is cooled and transported to a high place to separate the agglomerated filter media and the dust. This system has three features: the granular filter material can be recycled and reused, and the nitrogen gas containing dust can be removed and cooled before being recycled.

以下、本発明の集じん方法を実施するための集じん装置
を図面に基づいて説明する。
Hereinafter, a dust collection device for carrying out the dust collection method of the present invention will be explained based on the drawings.

第1図は本発明の集じん装置の一実施態様を示すもので
、粒塊状ろ過材・ダスト移送手段として移送管を、ダチ
スト補集器としてサイクロンを用いる場合の系係的説明
図である。1は一端に含じんガス入口2を、他端に清浄
ガス出口3を有する集じん機本体で、この集じん機本体
1内の含じんガス入口2の下流側に金属製ルーバ、金網
、金属製多孔板などの支持体4を一定間隔に含じんガス
流に対して直角またはほぼ直角に設け、支持体4間に砂
、砂利、セラミックス、耐火物などの粒塊状ろ過材5を
パネル状または層状に移動自在に充填・保持させてなる
集じん層6を設け、この集じん層6の上部に粒塊状ろ過
材供給ホッパ7を接続するとともに、集じん層6の下部
にダストの付着した粒塊状ろ過材を抜き出すための排出
機8を接続して集じん機10を形成する。
FIG. 1 shows one embodiment of the dust collection device of the present invention, and is a system-related explanatory diagram in the case where a transfer pipe is used as the granular filter material/dust transfer means and a cyclone is used as the dust collector. 1 is a dust collector body having a dust-containing gas inlet 2 at one end and a clean gas outlet 3 at the other end, and a metal louver, wire mesh, metal Supports 4, such as perforated plates, are provided at regular intervals at right angles or nearly right angles to the flow of the dust-containing gas, and between the supports 4, a granular filter material 5 such as sand, gravel, ceramics, refractory material, etc. is placed in the form of a panel or A dust collection layer 6 is provided which is movably filled and retained in a layered manner, and a granular filter material supply hopper 7 is connected to the upper part of this dust collection layer 6, and the particles with dust attached are connected to the lower part of the dust collection layer 6. A dust collector 10 is formed by connecting a discharger 8 for extracting the bulk filter material.

またこの排出機8の下部に窒素ガス循環用送風機11の
吐出管12を接続するとともに、この吐出管12と排出
機8の下部に移送管13からなる粒塊状ろ過材・ダスト
移送手段を接続し、この移送管13に前記粒塊状ろ過材
供給ホッパ7の上部に設けられたサイクロン14からな
る粒塊状ろ過材・ダスト分離器を接続して、ろ過材、ダ
ストを高所移送するとともにろ過材とダストとを分離し
てろ過材を循環再使用するための輸送・分離装置15を
形成する。さらに前記サイクロン14の窒素ガス出口1
6をサイクロン17からなるダスト補集器および窒素ガ
ス冷却器18を介して前記窒素ガス循環用送風機11の
吸引側に冷却された窒素ガスを循環自在に接続する。2
0は漏洩による消耗分のみを補給するための窒素ガス供
給管、21はダスト抜出管である。
Further, a discharge pipe 12 of a nitrogen gas circulation blower 11 is connected to the lower part of the discharger 8, and a granular filter material/dust transfer means consisting of a transfer pipe 13 is connected to the discharge pipe 12 and the lower part of the discharger 8. A granular filtration material/dust separator consisting of a cyclone 14 provided above the granular filtration material supply hopper 7 is connected to this transfer pipe 13 to transport the filtration material and dust to a high place and to separate the filtration material from the filtration material. A transportation/separation device 15 is formed to separate the filter material from dust and reuse the filter material by circulation. Further, the nitrogen gas outlet 1 of the cyclone 14
6 is connected to the suction side of the nitrogen gas circulation blower 11 via a dust collector consisting of a cyclone 17 and a nitrogen gas cooler 18 so that cooled nitrogen gas can be freely circulated. 2
0 is a nitrogen gas supply pipe for replenishing only the amount consumed due to leakage, and 21 is a dust extraction pipe.

上記のように構成された集じん装置において、含じんガ
ス入口2から導入されてくるダストを含んだ高温の還元
性ガス、爆発性ガスは集じん層6によりダストが除去さ
れて、清浄ガスとして清浄ガス出口3から排出される。
すなわちガス中のダストは粒塊状ろ過材表面に付着する
とともに、ろ過材間の空間に保持されて高性能集じんさ
れる。一方、ダストの付着した粒塊状ろ過材は排出機8
により連続的または断続的に集じん機本体1から抜き出
され、窒素ガス循環用送風機11から送られてくる加圧
された冷却窒素ガスにより移送管13内に導入され、こ
の移送管13を経て第1サイクロン14内に高所移送さ
れるとともに、ダストを含む窒素ガスと粒塊状ろ過材と
が分離される。この場合、粒塊状ろ過材の直径は数肋〜
数十柳で、ダストの直径は数仏〜数十仏であり、両者の
粒径が大幅に異なるので、サイクロンのような簡単な構
造の分離器で両者の分離を容易に行なうことができる。
分離された粒塊状ろ過材は供給ホッパ7に循環されて再
使用に供され、ダストを含む窒素ガスは第2サイクロン
17へ導入されて、ダストと窒素ガスとが分離され、ダ
ストはダスト抜出管21から抜き出され、窒素ガスは窒
素ガス冷却器18で冷却された後、循環用送風機11に
より循環再使用される。なお集じん機本体をボィラタィ
プにすれば、窒素ガス冷却器の温水をこのボィラの給水
に利用することができ、熱回収をはかることができる。
またダストはダスト補集器からの一箇所のみで回収する
ことができるという利点がある。第2図は本発明の集じ
ん装置の他の実施態様を示すもので、ダスト補集器とし
てはバグフィルタを用いる場合の系係的説明図である。
In the dust collector configured as described above, the dust-containing high-temperature reducing gas and explosive gas introduced from the dust-containing gas inlet 2 are removed by the dust collection layer 6 and converted into clean gas. The clean gas is discharged from the outlet 3.
That is, the dust in the gas adheres to the surface of the granular filter material, and is retained in the spaces between the filter materials, resulting in high-performance dust collection. On the other hand, the granular filter material with dust attached is removed by the discharger 8.
The nitrogen gas is continuously or intermittently extracted from the dust collector main body 1 and introduced into the transfer pipe 13 by pressurized cooled nitrogen gas sent from the nitrogen gas circulation blower 11. While being transported to a high place into the first cyclone 14, the nitrogen gas containing dust and the granular filter material are separated. In this case, the diameter of the granular filter media is several ribs ~
The diameter of the dust is from several to several tens of diameters, and since the particle sizes of the two are significantly different, the two can be easily separated using a separator with a simple structure such as a cyclone.
The separated granular filter material is circulated to the supply hopper 7 for reuse, and the nitrogen gas containing dust is introduced to the second cyclone 17, where the dust and nitrogen gas are separated, and the dust is extracted. After being extracted from the pipe 21 and cooled by the nitrogen gas cooler 18, the nitrogen gas is circulated and reused by the circulation blower 11. If the main body of the dust collector is a boiler type, the hot water from the nitrogen gas cooler can be used to supply water to the boiler, allowing heat recovery.
Another advantage is that the dust can be collected at only one location, from the dust collector. FIG. 2 shows another embodiment of the dust collecting device of the present invention, and is a system diagram for explaining the case where a bag filter is used as the dust collector.

すなわちサイクロン14の窒素ガス出口16に窒素ガス
冷却器18を直接接続し、この冷却器18にダスト補集
器としてバグフィルタ22を接続して、ダストを含む窒
素ガスを冷却した後、除じんするように構成したもので
ある。このように冷却した含じん窒素ガスを除じんする
ものであるから、耐熱性の点で低温でしか使用できない
が微細ダストの除去に適するバグフィルタを用いること
ができるという利点を有している。23はダスト抜出管
である。
That is, a nitrogen gas cooler 18 is directly connected to the nitrogen gas outlet 16 of the cyclone 14, and a bag filter 22 is connected to this cooler 18 as a dust collector to cool the nitrogen gas containing dust and then remove the dust. It is configured as follows. Since the dust-containing nitrogen gas cooled in this way is removed, it has the advantage that a bag filter suitable for removing fine dust can be used, although it can only be used at low temperatures in terms of heat resistance. 23 is a dust extraction pipe.

他の構成および作用は第1図に示す集じん装置の場合と
同様である。つぎに本発明の集じん装置のさらに他の実
施態様を第3図に基づいて説明する。
Other configurations and operations are similar to those of the dust collector shown in FIG. Next, still another embodiment of the dust collecting device of the present invention will be described based on FIG. 3.

第3図は粒塊状ろ過材・ダスト移送手段としてバケット
ヱレベー夕24を、粒塊状ろ過材・ダスト分離器として
振動節25を用いて輸送・分離装置26を形成するもの
で、集じん機本体1から抜き出されるダストの付着した
粒塊状ろ過材を窒素ガスでシールしながらバケットェレ
ベータ24により供給ホッパ7の上部に設けられた振動
筋25に高所移送するとともに、粒塊状ろ過材とダスト
とを分離し、一方、輸送・分離装置26、詳しくはバケ
ットェレベータ24の窒素ガス出口27から排出される
含じん窒素ガスを除じん、冷却して循環再使用できるよ
うに構成したものである。この場合、第2図に示すよう
に含じん窒素ガスをまず冷却した後、バグフィルタによ
り除じんするように構成しても差し支えない。28は振
動用モータ、30はダスト抜出管である。
In FIG. 3, a transport/separation device 26 is formed using a bucket elevator 24 as a particulate filter material/dust transfer means and a vibration node 25 as a particulate filter material/dust separator. The dust-adhered granular filter material to be extracted is transported to a high place by the bucket elevator 24 to a vibrating bar 25 provided at the top of the supply hopper 7 while being sealed with nitrogen gas, and the granular filter material and the dust are removed. On the other hand, the transport/separation device 26, specifically, the dust-containing nitrogen gas discharged from the nitrogen gas outlet 27 of the bucket elevator 24 is removed, cooled, and recycled for reuse. In this case, as shown in FIG. 2, the dust-containing nitrogen gas may be first cooled and then removed by a bag filter. 28 is a vibration motor, and 30 is a dust extraction pipe.

他の構成および作用は第m図および第2図に示す集じん
装置の場合と同様である。以上説明したように、本発明
はろ過材、ダストの輸送・分離系統および窒素ガス循環
系統が閉ループ系で窒素ガスでシールされるため、リー
クガスの酸化、爆発などを防止することができ、また窒
素ガスを冷却器を介して循環するので、高温のダストの
付着したろ過材を高所移送する際にろ過材およびダスト
が冷却されて、ろ過材とダストとの分離を適当なハンド
IJングし易い低温下で行なうことができ、さらに窒素
ガスは循環使用されるため、リークによる消耗分のみを
補給すればよくきわめて経済的であるという効果を有し
ている。
The other configurations and operations are similar to those of the dust collector shown in FIGS. m and 2. As explained above, in the present invention, the filter media, the dust transport/separation system, and the nitrogen gas circulation system are sealed with nitrogen gas in a closed loop system, making it possible to prevent leak gas oxidation, explosion, etc. Since the gas is circulated through the cooler, the filter medium and dust are cooled when the filter medium with hot dust attached is transferred to a high place, making it easy to separate the filter medium and dust by appropriate hand IJ. It can be carried out at low temperatures, and since the nitrogen gas is recycled, it is extremely economical as it is only necessary to replenish the amount consumed due to leakage.

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

第1図は本発明の集じん装置の一実施態様を示すもので
、ダスト補集器としてサイクロンを用いる場合の系統的
説明図、第2図は本発明の集じん装置の他の実施態様を
示すもので、ダスト補集器としてはバグフィルタを用い
る場合の系統的説明図、第3図は本発明の集じん装置の
さらに他の実施態様を示すもので、粒塊状ろ過材・ダス
ト移送手段としてバケットェレベータを用いる場合の系
統的説明図である。 1・・・・・・集じん機本体、2・・・・・・含じんガ
ス入口、3・・・・・・清浄ガス出口、4・・・・・・
支持体、5・・・・・・粒塊状ろ過材、6・・・・・・
集じん層、7・・・・・・粒塊状ろ過材供給ホッパ、8
……排出機、10……集じん機、11…・・・窒素ガス
循環用送風機、12……吐出管、13・・・・・・移送
管、14・・・・・・サイクロン、15・・…・輸送・
分離装置、16・・・・・・窒素ガス出口、17・・・
・・・サイクロン、18・・・・・・窒素ガス冷却器、
20・・・・・・窒素ガス供給管、22・・・・・・バ
グフィルタ、24・・・・・・バケットェレベータ、2
5・・・・・・振動節、26…・・・輸送・分離装置、
27・・…・窒素ガス出口。 ※’図 第Z図 繁う図
Fig. 1 shows one embodiment of the dust collector of the present invention, and is a systematic explanatory diagram when a cyclone is used as a dust collector, and Fig. 2 shows another embodiment of the dust collector of the present invention. 3 is a systematic explanatory diagram when a bag filter is used as a dust collector. FIG. FIG. 2 is a systematic explanatory diagram when using a bucket elevator. 1... Dust collector body, 2... Dust-containing gas inlet, 3... Clean gas outlet, 4...
Support, 5... Granular filter medium, 6...
Dust collection layer, 7... Granular filter material supply hopper, 8
... Discharge machine, 10 ... Dust collector, 11 ... Nitrogen gas circulation blower, 12 ... Discharge pipe, 13 ... Transfer pipe, 14 ... Cyclone, 15. ·…·transportation·
Separation device, 16... Nitrogen gas outlet, 17...
...Cyclone, 18...Nitrogen gas cooler,
20... Nitrogen gas supply pipe, 22... Bag filter, 24... Bucket elevator, 2
5... Vibration node, 26... Transportation/separation device,
27...Nitrogen gas outlet. *Figure Z

Claims (1)

【特許請求の範囲】 1 ダストを含む還元性ガス、爆発性ガスを粒塊状ろ過
材からなる集じん層を通過させて前記ガス中のダストを
分離・除去した後、ダストの付着した粒塊状ろ過材を抜
き出し、ついでこの粒塊状ろ過材とダストとの混合物に
窒素ガスを吹き込んで冷却しながら高所移送して粒塊状
ろ過材とダストとを分離して粒塊状ろ過材を循環再使用
できるようにするとともに、ダストを含む窒素ガスを除
じん・冷却した後、循環再使用することを特徴とするろ
過材、ダストの輸送・分離を伴う集じん方法。 2 集じん機本体内に粒塊状ろ過材を支持体間にパネル
状または層状に移動自在に充填・保持させてなる集じん
層を設け、この集じん層の上部に粒塊状ろ過材供給ホツ
パを接続するとともに、集じん層の下部に排出機を接続
して集じん機を形成し、この排出機の下部に窒素ガス循
環用送風機の吐出管を接続するとともに、排出機の下部
に粒塊状ろ過材・ダスト移送手段を接続し、この移送手
段に前記粒塊状ろ過材供給ホツパの上部に設けられた粒
塊状ろ過材・ダスト分離器を接続して、ろ過材、ダスト
を高所移送するとともに分離してろ過材を循環再使用す
るための輸送・分離装置を形成し、さらにこの輸送・分
離装置の窒素ガス出口をダスト捕集器および窒素ガス冷
却器を介して前記窒素ガス循環用送風機の吸引側に冷却
された窒素ガスを循環自在に接続してなるろ過材、ダス
トの輸送・分離を伴う集じん装置。
[Scope of Claims] 1. After passing a reducing gas or an explosive gas containing dust through a dust collection layer made of a granular filter material to separate and remove dust from the gas, granular filtration with attached dust is performed. The material is extracted, and then nitrogen gas is blown into the mixture of the agglomerated filter media and dust, and the mixture is cooled and transported to a high place to separate the agglomerated filter media and dust so that the agglomerated filter media can be recycled and reused. A dust collection method that involves transporting and separating dust, a filter material that is characterized by the fact that the nitrogen gas containing dust is removed and cooled, and then recycled and reused. 2. A dust collection layer is provided in the dust collector body in which granular filter media is movably filled and held between supports in the form of panels or layers, and a granular filter material supply hopper is installed above this dust collection layer. At the same time, a discharger is connected to the bottom of the dust collection layer to form a dust collector, and a discharge pipe of a blower for nitrogen gas circulation is connected to the bottom of this discharger, and a granular filter is connected to the bottom of the discharger. A particle/dust transfer means is connected, and a particle/dust separator provided at the top of the agglomerate filter medium supply hopper is connected to this transfer means to transport the filter medium and dust to a high place and separate them. to form a transportation/separation device for circulating and reusing the filter media, and furthermore, the nitrogen gas outlet of this transportation/separation device is connected to the suction of the nitrogen gas circulation blower via a dust collector and a nitrogen gas cooler. A dust collection device that transports and separates dust and a filter material that connects cooled nitrogen gas to the side so that it can be freely circulated.
JP547277A 1977-01-20 1977-01-20 Filter media, dust collection method and equipment that involve transportation and separation of dust Expired JPS6018204B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP547277A JPS6018204B2 (en) 1977-01-20 1977-01-20 Filter media, dust collection method and equipment that involve transportation and separation of dust

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP547277A JPS6018204B2 (en) 1977-01-20 1977-01-20 Filter media, dust collection method and equipment that involve transportation and separation of dust

Publications (2)

Publication Number Publication Date
JPS5391471A JPS5391471A (en) 1978-08-11
JPS6018204B2 true JPS6018204B2 (en) 1985-05-09

Family

ID=11612175

Family Applications (1)

Application Number Title Priority Date Filing Date
JP547277A Expired JPS6018204B2 (en) 1977-01-20 1977-01-20 Filter media, dust collection method and equipment that involve transportation and separation of dust

Country Status (1)

Country Link
JP (1) JPS6018204B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2450628A1 (en) * 1979-03-05 1980-10-03 Air Ind IMPROVEMENTS RELATING TO DECOLMATION PROCESSES FOR A FILTRATION INSTALLATION, AND TO FILTRATION INSTALLATIONS IMPLEMENTING SUCH METHODS

Also Published As

Publication number Publication date
JPS5391471A (en) 1978-08-11

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