JP2003299929A - Method for regenerating filter cloth for dust-collector - Google Patents

Method for regenerating filter cloth for dust-collector

Info

Publication number
JP2003299929A
JP2003299929A JP2002103383A JP2002103383A JP2003299929A JP 2003299929 A JP2003299929 A JP 2003299929A JP 2002103383 A JP2002103383 A JP 2002103383A JP 2002103383 A JP2002103383 A JP 2002103383A JP 2003299929 A JP2003299929 A JP 2003299929A
Authority
JP
Japan
Prior art keywords
filter cloth
dust collector
temperature
dust
gas
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP2002103383A
Other languages
Japanese (ja)
Inventor
Sumio Tsujii
澄生 辻井
Yoshio Iio
良夫 飯尾
Takamasa Kijima
敬昌 木嶋
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.)
Nihon Spindle Manufacturing Co Ltd
Original Assignee
Nihon Spindle Manufacturing Co 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 Nihon Spindle Manufacturing Co Ltd filed Critical Nihon Spindle Manufacturing Co Ltd
Priority to JP2002103383A priority Critical patent/JP2003299929A/en
Publication of JP2003299929A publication Critical patent/JP2003299929A/en
Pending legal-status Critical Current

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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for regenerating a filter cloth for a dust-collector realizing a use of the filter cloth for a long period of time by scattering an oil content deposited on the filter cloth of the dust-collector for treating gas discharged from a gasification furnace. <P>SOLUTION: In the filtration type dust-collector 1, the oil content attached and deposited on a surface of the filter cloth 4 and accumulated at the inside is decomposed and volatilized by raising a temperature of the filter cloth to a predetermined set temperature against a usual operation temperature. <P>COPYRIGHT: (C)2004,JPO

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、濾過式集塵機の濾
布表面に付着、堆積した油分や濾布の内部に蓄積し絡み
ついた油分を飛散させ、濾布を再生させる方法に関し、
特にガス化炉等のように油分が多く含まれる排出ガスを
処理する集塵機に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method of regenerating a filter cloth of a filtration type dust collector by scattering oil accumulated on the surface of the filter cloth or oil accumulated and entangled inside the filter cloth to regenerate the filter cloth,
Particularly, the present invention relates to a dust collector that treats exhaust gas containing a large amount of oil, such as a gasification furnace.

【0002】[0002]

【従来の技術】従来のガス化炉等から排出されるガスを
処理する集塵機の集塵ガス温度は、排出されるガス温度
を基準に当該温度と同一温度又は集塵機入口側に備えた
冷却装置などの温度制御機構によって対応できる耐熱温
度を有する濾布を用い、それらに応じた濾過風速の設定
とともに、濾布の耐熱温度以下となるよう、その温度を
設定し集塵機を設計している。
2. Description of the Related Art The temperature of the dust collecting gas of a dust collector that processes gas discharged from a conventional gasification furnace or the like is the same as the temperature of the discharged gas or a cooling device provided at the dust collector inlet side. Using a filter cloth having a heat-resistant temperature that can be handled by the temperature control mechanism, the dust collector is designed by setting the filtration wind speed according to the temperature and setting the temperature so that it is below the heat-resistant temperature of the filter cloth.

【0003】[0003]

【発明が解決しようとする課題】しかし、ガス化炉等か
ら排出されるガスを処理する集塵機の場合、集塵ガス温
度は400℃程度までとすることが通常でありかかる温
度範囲では濾布に油分や未燃物の付着がおこり、集塵機
の集塵効率が大幅に低下し、集塵機排出側に備えられる
誘引送風機の吸引能力以上に、濾布への油分などの付着
が進行し濾布通過時の圧力損失が上昇した時点が濾布の
寿命となる。
However, in the case of a dust collector for treating gas discharged from a gasification furnace or the like, the temperature of the dust collecting gas is usually up to about 400 ° C. Adhesion of oil and unburned materials causes the dust collection efficiency of the dust collector to drop significantly, and the oil content, etc., will adhere to the filter cloth more than the suction capacity of the induction blower installed on the discharge side of the dust collector, and when passing through the filter cloth. The life of the filter cloth is reached when the pressure loss increases.

【0004】現状、濾布に油分等の付着を防止する対策
として、炉燃焼制御により油分や未燃物を生成させない
よう努めるのみであった。
At present, as a measure for preventing the oil content from adhering to the filter cloth, it has only been attempted to prevent the oil content and unburned matter from being produced by furnace combustion control.

【0005】本発明はかかる点に鑑み、ガス化炉等から
排出されるガスを処理する集塵機の濾布に付着する油分
を飛散せしめ、長期間の濾布の使用が可能な集塵機用濾
布の再生方法を提供することを目的とする。
In view of the above problems, the present invention provides a filter cloth for a dust collector which scatters oil content adhering to the filter cloth of a dust collector for treating gas discharged from a gasification furnace or the like and allows the filter cloth to be used for a long period of time. The purpose is to provide a reproducing method.

【0006】[0006]

【課題を解決するための手段】上記目的を達成するた
め、本発明の集塵機用濾布の再生方法は、濾過式集塵機
において、通常運転温度に対し、集塵機に流入するガス
温度を所定の設定温度に上昇せしめ濾布表面に付着、堆
積及び内部に蓄積した油分を分解・揮発させることを特
徴とする。ここで、「所定の設定温度」とは、濾布表面
に付着、堆積及び内部に蓄積し絡みついた油分を分解・
揮発させることができる温度をいう。
In order to achieve the above object, a method of regenerating a filter cloth for a dust collector according to the present invention is a filter type dust collector in which a gas temperature flowing into the dust collector is set to a predetermined set temperature with respect to a normal operating temperature. It is characterized in that it decomposes and volatilizes the oil that adheres to the surface of the filter cloth, accumulates, and accumulates inside. Here, the "predetermined set temperature" means that the oil content that adheres to the surface of the filter cloth, accumulates, and is entangled and accumulated inside is decomposed.
It refers to the temperature at which it can be volatilized.

【0007】これにより圧力損失の上がった濾布の交換
時期を先送りし濾布の寿命を大幅に延ばすことができ
る。
As a result, it is possible to postpone the replacement time of the filter cloth having the increased pressure loss, and to prolong the life of the filter cloth significantly.

【0008】この場合において、濾過式集塵機に流入す
るガスの冷却度合いを低減せしめることによって流入ガ
ス温度を上昇させることができる。
In this case, the temperature of the inflowing gas can be raised by reducing the cooling degree of the gas flowing into the filtration type dust collector.

【0009】これにより、集塵機入口側に備えた冷却装
置を制御することにより簡単に集塵ガス温度を上昇する
ことができる。
Thus, the temperature of the dust collecting gas can be easily increased by controlling the cooling device provided on the inlet side of the dust collector.

【0010】また、濾過式集塵機に流入するガスを加熱
することによって流入ガス温度を上昇させることができ
る。
Further, the temperature of the inflowing gas can be raised by heating the gas flowing into the filtration type dust collector.

【0011】これにより、集塵機入口において低温とな
るガスの処理を行う集塵機においてもガス温度を上昇さ
せることができる。
As a result, the gas temperature can be raised even in the dust collector that processes the gas having a low temperature at the dust collector inlet.

【0012】[0012]

【発明の実施の形態】以下、本発明の集塵機用濾布の再
生方法の実施の形態を図面に基づいて説明する。
BEST MODE FOR CARRYING OUT THE INVENTION An embodiment of a method for recycling a filter cloth for a dust collector according to the present invention will be described below with reference to the drawings.

【0013】図1は、比較的高温のガスを処理する濾過
式集塵機1の実施例を示し、集塵機に送られるガスが常
時は冷却装置2によって冷却された後に、濾過式集塵機
1内で処理される場合の説明図である。
FIG. 1 shows an embodiment of a filter-type dust collector 1 for treating a gas having a relatively high temperature. The gas sent to the dust-collector is always cooled by a cooling device 2 and then treated in the filter-type dust collector 1. FIG.

【0014】ガス化炉等から排出されるガスや含塵空気
は、濾過式集塵機1の流入管5を介し濾過式集塵機1の
含塵空気室へ送られる。この際、送られるガスが予め設
計された集塵機内で処理すべき運転温度を上回る場合に
おいては、冷却装置2を作動せしめ規定の温度に冷却し
た後に濾過式集塵機1内部へ送られる。
Gas and dust-containing air discharged from the gasification furnace or the like are sent to the dust-containing air chamber of the filter-type dust collector 1 through the inflow pipe 5 of the filter-type dust collector 1. At this time, when the gas to be sent exceeds the operating temperature to be processed in the predesigned dust collector, the cooling device 2 is operated to cool it to a specified temperature, and then the gas is sent to the inside of the filter dust collector 1.

【0015】濾過式集塵機1の含塵空気室7に送られた
ガスや含塵空気は、濾布4にて濾過され浄化空気室8へ
送られ排出管6を介し外気に放出される。流入管5から
排出管6までのガスの流れは排出管6に設けられた吸引
ファンFにより行われる。
The gas and dust-containing air sent to the dust-containing air chamber 7 of the filter-type dust collector 1 are filtered by the filter cloth 4 and sent to the purified air chamber 8 and discharged to the outside air through the discharge pipe 6. The gas flow from the inflow pipe 5 to the exhaust pipe 6 is performed by a suction fan F provided in the exhaust pipe 6.

【0016】濾布4の濾過に際し、ガスや含塵空気に含
まれる塵等の有害物質は濾布4の表面に付着堆積し、一
定量以上の付着によって集塵効率(濾過効率)が低下し
てきた場合、定期的に圧力空気供給切替弁11を解放せ
しめ、逆洗用パイプ9を介し、圧力空気噴出ノズル10
から濾布4の内部に圧力空気を噴出し、濾布4の表面に
付着堆積した塵埃を払い落とし、濾過式集塵機1の下部
に堆積させる。
When the filter cloth 4 is filtered, harmful substances such as dust contained in gas and dust-containing air are deposited on the surface of the filter cloth 4, and the dust collection efficiency (filtration efficiency) is reduced by a certain amount or more. In this case, the pressure air supply switching valve 11 is opened periodically, and the pressure air jet nozzle 10 is inserted through the backwashing pipe 9.
The compressed air is blown into the inside of the filter cloth 4 to scavenge the dust adhering to the surface of the filter cloth 4 and deposit it on the lower part of the filter type dust collector 1.

【0017】一定量堆積された塵埃は、ロータリーバル
ブ13の開閉によってストッカー(図示省略)に蓄えら
れ空気搬送手段等を用いて処理される。
The dust accumulated in a certain amount is stored in a stocker (not shown) by opening and closing the rotary valve 13 and processed by using an air conveying means or the like.

【0018】油分以外の塵埃等は、上述した圧力空気を
噴出することによる逆洗によって払い落とされ集塵効率
は回復する。しかし、ガス中に含まれる油分(タール
等)は、濾布表面に付着、堆積したり、濾布の内部に蓄
積し絡みついた状態となる。
Dust and the like other than the oil content is removed by backwashing by ejecting the above-mentioned pressurized air, and the dust collection efficiency is restored. However, the oil component (tar etc.) contained in the gas adheres to and accumulates on the surface of the filter cloth, or accumulates inside the filter cloth and becomes entangled.

【0019】これらの油分は、上述した圧力空気を噴出
することによる逆洗によっては除去することができず、
集塵効率を大幅に低下させる。これは、油分には不燃性
粒子(アルミナ、シリカ等)を接着する作用があり、濾
布表面に濾布表面に付着、堆積する油分が増加すれば油
分以外の塵埃等も油分の接着作用により逆洗によっては
払い落とせなくなり濾布の寿命を短くすることとなる。
These oils cannot be removed by backwashing by jetting pressurized air as described above,
Dust collection efficiency is significantly reduced. This has the effect of adhering non-combustible particles (alumina, silica, etc.) to oil, and if the amount of oil that adheres to and accumulates on the surface of the filter cloth increases, the dust, etc. other than oil will also adhere to the oil. It cannot be washed off by backwashing, which shortens the life of the filter cloth.

【0020】本発明においては、通常の運転時におい
て、冷却装置2の冷却度合いを低下せしめ、集塵機内に
送り込むガス温度を上昇させ、濾布4表面に付着、堆積
した油分や濾布の内部に蓄積し絡みついた油分を分解・
揮発させることによって飛散させ、濾布4を油分が付
着、堆積していない状態に戻すことにより濾布の寿命を
大幅に向上させる。
In the present invention, during normal operation, the cooling degree of the cooling device 2 is lowered, the temperature of the gas fed into the dust collector is increased, and the oil content deposited on the surface of the filter cloth 4 or the inside of the filter cloth is accumulated. Decomposes oil that accumulates and is entangled
The filter cloth 4 is scattered by being volatilized, and the filter cloth 4 is returned to a state in which oil is not attached and accumulated, thereby significantly improving the life of the filter cloth.

【0021】本発明者等の実験によると、濾過式集塵機
1の通常運転が400℃である場合、冷却装置2の冷却
度合いを低下し、濾過式集塵機1内に送り込むガス温度
を480℃以上(好ましくは500℃以上)にすること
により濾布表面に付着、堆積したり、濾布の内部に蓄積
し絡みついた油分の殆どを分解・揮発させることによっ
て飛散させることに成功した。
According to the experiments conducted by the present inventors, when the normal operation of the filter type dust collector 1 is 400 ° C., the cooling degree of the cooling device 2 is lowered and the temperature of the gas fed into the filter type dust collector 1 is 480 ° C. or more ( By setting the temperature to preferably 500 ° C. or higher), most of the oil that adheres to and deposits on the surface of the filter cloth or that accumulates inside the filter cloth and is entangled is decomposed and volatilized to be scattered.

【0022】図2は、比較的低温のガスを処理する濾過
式集塵機1の実施例を示し、集塵機に送られるガスが常
時は、排出された温度のまま、又は加熱装置3によって
加熱された後に、濾過式集塵機1内で処理される場合の
説明図である。
FIG. 2 shows an embodiment of a filter type dust collector 1 for treating a gas having a relatively low temperature. The gas sent to the dust collector is always at the discharged temperature or after being heated by the heating device 3. FIG. 3 is an explanatory diagram of a case of processing in the filtration dust collector 1.

【0023】この場合も上述した場合と同様、濾過式集
塵機1の運転時間に比例して、油分が濾布表面に付着、
堆積したり、濾布の内部に蓄積し絡みつく。
Also in this case, as in the case described above, the oil content adheres to the surface of the filter cloth in proportion to the operating time of the filter type dust collector 1.
Accumulates or accumulates inside the filter cloth and becomes entangled.

【0024】本発明における第2実施例においては、通
常の運転時において、加熱装置3による加熱(常時加熱
している場合は加熱度合いを向上させる)によって、集
塵機内に送り込むガス温度を上昇させ、濾布4表面に付
着、堆積した油分や濾布の内部に蓄積し絡みついた油分
を分解・揮発させることによって飛散させ、濾布4を油
分が付着、堆積していない状態に戻すことにより濾布の
寿命を大幅に向上させる。
In the second embodiment of the present invention, during normal operation, the temperature of the gas fed into the dust collector is raised by heating by the heating device 3 (in the case of constant heating, the heating degree is increased). The oil that has adhered to and accumulated on the surface of the filter cloth 4 or the oil that has accumulated and entangled inside the filter cloth is decomposed and volatilized to be scattered, and the filter cloth 4 is returned to the state in which the oil has not been adhered and accumulated. Greatly improve the life of.

【0025】この際、処理するガスの種類温度によって
は、冷却装置2と加熱装置3を併用して使用することも
できる。
At this time, the cooling device 2 and the heating device 3 may be used in combination depending on the kind and temperature of the gas to be treated.

【0026】図3は、ガス化炉等から排出されるガスや
含塵空気を処理する通常運転時ではなく、濾布の再生の
みを目的とした運転の説明図である。
FIG. 3 is an explanatory view of an operation intended only for regenerating the filter cloth, not during the normal operation for treating the gas or dust-containing air discharged from the gasification furnace or the like.

【0027】14は排出管6の後方と、流入管5の前方
を連結する循環ダクトを示し、常時はバルブV3、V4
を閉栓し、バルブV1、V2が解放されておりガス化炉
等から排出されるガスや含塵空気は上述された方法で処
理される。
Reference numeral 14 denotes a circulation duct which connects the rear side of the discharge pipe 6 and the front side of the inflow pipe 5, and normally, valves V3 and V4.
Is closed and the valves V1 and V2 are opened, and the gas and dust-containing air discharged from the gasification furnace or the like are treated by the method described above.

【0028】一定時間の運転により、濾布4表面に付
着、堆積した油分や濾布の内部に蓄積し絡みついた油分
が増加してきたとき集塵機の通常運転を停止する。
When the oil content adhering to and accumulated on the surface of the filter cloth 4 or the oil content accumulated and entangled inside the filter cloth increases by the operation for a certain period of time, the normal operation of the dust collector is stopped.

【0029】しかる後、バルブV1、V2を閉栓し、バ
ルブV3、V4を解放する。これにより、濾過式集塵機
1は、排出管6の後方と、流入管5の前方が繋がれた閉
回路となり、循環ファンF’によって濾過式集塵機1の
空気が循環するのみとなる。
Thereafter, the valves V1 and V2 are closed and the valves V3 and V4 are opened. As a result, the filter dust collector 1 becomes a closed circuit in which the rear of the discharge pipe 6 and the front of the inflow pipe 5 are connected, and only the air of the filter dust collector 1 is circulated by the circulation fan F ′.

【0030】この時、加熱装置3’を作動せしめ循環す
る空気温度を上昇させることにより濾布4表面に付着、
堆積した油分や濾布の内部に蓄積し絡みついた油分を分
解・揮発させることによって飛散させ、濾布4を油分が
付着、堆積していない状態に戻すことにより濾布の寿命
を大幅に向上させる。
At this time, the heating device 3'is operated to raise the temperature of the circulating air, thereby adhering to the surface of the filter cloth 4,
The accumulated oil and the oil entangled and entangled inside the filter cloth are decomposed and volatilized to be scattered, and the filter cloth 4 is returned to a state in which the oil is not adhered and accumulated, thereby significantly improving the life of the filter cloth. .

【0031】循環させる空気温度は、上述した場合と同
様、480℃以上(好ましくは500℃以上)にするこ
とにより油分を飛散させることができる。
The temperature of the air to be circulated can be set to 480 ° C. or higher (preferably 500 ° C. or higher) to scatter the oil content, as in the case described above.

【0032】なお、上昇させる温度の限界は、使用され
る濾布の耐熱温度が限界とされる。一般的な濾布の素材
として、セラミック、アルミナ・シリケート繊維の成型
タイプ濾布やコーディエライト、焼結タイプ濾布の場合
は耐熱温度は850℃、セラミック繊維を用いた織布タ
イプやステンレス繊維織布、セラミックコーティングタ
イプのものでは耐熱温度は500℃となる。
The upper limit of the temperature to be raised is the heat resistant temperature of the filter cloth used. As a material for general filter cloth, ceramic, alumina-silicate fiber molded type filter cloth or cordierite, and sintered type filter cloth have a heat resistant temperature of 850 ° C., woven type using ceramic fiber or stainless fiber The heat resistant temperature of the woven cloth and ceramic coating type is 500 ° C.

【0033】以上、本発明の集塵機用濾布の再生方法に
ついて、その実施例に基づいて説明したが、本発明は上
記実施例に記載した構成に限定されるものではなく、そ
の趣旨を逸脱しない範囲において適宜その構成を変更す
ることができるものである。
Although the method for recycling the filter cloth for the dust collector of the present invention has been described above based on the embodiments thereof, the present invention is not limited to the configurations described in the above embodiments and does not deviate from the spirit thereof. The configuration can be appropriately changed within the range.

【0034】[0034]

【発明の効果】以上の如く本発明によるときは、濾布の
表面に付着、堆積した油分や濾布の内部に蓄積し絡みつ
いた油分により集塵効率の低下した集塵機(捕集効率の
低下した濾布)に対して、集塵機に流入するガス温度を
通常処理温度から80乃至120℃程度上昇させるとい
う簡単な方法で再生することができ、濾布の寿命を大幅
に向上させることができる。
As described above, according to the present invention, the dust collector having a reduced dust collection efficiency due to the oil components attached to and deposited on the surface of the filter fabric or the oil components accumulated and entangled inside the filter fabric (the collection efficiency is reduced). The filter cloth can be regenerated by a simple method of raising the temperature of the gas flowing into the dust collector from the normal processing temperature by about 80 to 120 ° C., and the life of the filter cloth can be greatly improved.

【0035】また、処理温度の上昇を冷却装置の冷却度
合いを低減させることによって行うときは、殆どの既設
の集塵装置において利用することができる。
When the treatment temperature is raised by reducing the cooling degree of the cooling device, it can be used in almost all existing dust collectors.

【0036】さらに、処理温度の上昇を加熱装置を使っ
て行う場合は比較的低温なガスを処理する集塵機におい
ても濾布の表面に付着、堆積した油分を飛散せしめ濾布
を再生することができる等の効果を有する。
Further, when the treatment temperature is raised by using a heating device, even in a dust collector for treating a gas having a relatively low temperature, the oil content attached to and deposited on the surface of the filter cloth can be scattered to regenerate the filter cloth. And so on.

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

【図1】本発明の集塵機用濾布の再生方法の一実施例の
説明図である。
FIG. 1 is an explanatory view of an embodiment of a method for recycling a filter cloth for a dust collector of the present invention.

【図2】本発明の集塵機用濾布の再生方法の別の実施例
の説明図である。
FIG. 2 is an explanatory view of another embodiment of the method for recycling the filter cloth for the dust collector of the present invention.

【図3】本発明の集塵機用濾布の再生方法の別の実施例
の説明図である。
FIG. 3 is an explanatory view of another embodiment of the method for recycling the filter cloth for the dust collector of the present invention.

【符号の説明】[Explanation of symbols]

1 濾過式集塵機 2 冷却装置 3 加熱装置 4 濾布 1 Filter dust collector 2 Cooling device 3 heating devices 4 filter cloth

───────────────────────────────────────────────────── フロントページの続き (72)発明者 木嶋 敬昌 兵庫県尼崎市潮江4丁目2番30号 日本ス ピンドル製造株式会社内 Fターム(参考) 4D058 JA02 JA04 MA41 SA15 SA20   ─────────────────────────────────────────────────── ─── Continued front page    (72) Inventor Takamasa Kijima             4-30 Shioe, Amagasaki-shi, Hyogo Japan Su             Inside Pindle Manufacturing Co., Ltd. F-term (reference) 4D058 JA02 JA04 MA41 SA15 SA20

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 濾過式集塵機において、通常運転温度に
対し、集塵機に流入するガス温度を所定の設定温度に上
昇せしめ濾布表面に付着、堆積及び内部に蓄積した油分
を分解・揮発させることを特徴とする集塵機用濾布の再
生方法。
1. In a filter type dust collector, the gas temperature flowing into the dust collector is raised to a predetermined set temperature with respect to the normal operating temperature, and the oil content adhering to the surface of the filter cloth, accumulated, and decomposed and volatilized is volatilized. A method for recycling a filter cloth for a dust collector, which is characterized.
【請求項2】 濾過式集塵機に流入するガスの冷却度合
いを低減せしめることによって流入ガス温度を上昇させ
ることを特徴とする請求項1記載の集塵機用濾布の再生
方法。
2. A method of regenerating a filter cloth for a dust collector according to claim 1, wherein the temperature of the inflowing gas is raised by reducing the cooling degree of the gas flowing into the filtration dust collector.
【請求項3】 濾過式集塵機に流入するガスを加熱する
ことによって流入ガス温度を上昇させることを特徴とす
る請求項1記載の集塵機用濾布の再生方法。
3. The method for recycling a filter cloth for a dust collector according to claim 1, wherein the temperature of the inflowing gas is raised by heating the gas flowing into the filter type dust collector.
JP2002103383A 2002-04-05 2002-04-05 Method for regenerating filter cloth for dust-collector Pending JP2003299929A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2002103383A JP2003299929A (en) 2002-04-05 2002-04-05 Method for regenerating filter cloth for dust-collector

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2002103383A JP2003299929A (en) 2002-04-05 2002-04-05 Method for regenerating filter cloth for dust-collector

Publications (1)

Publication Number Publication Date
JP2003299929A true JP2003299929A (en) 2003-10-21

Family

ID=29389251

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2002103383A Pending JP2003299929A (en) 2002-04-05 2002-04-05 Method for regenerating filter cloth for dust-collector

Country Status (1)

Country Link
JP (1) JP2003299929A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006090549A1 (en) * 2005-02-23 2006-08-31 Bussan Nanotech Research Institute Inc. Gas filtration apparatus
JP2016016406A (en) * 2014-07-07 2016-02-01 バルメット テクノロジーズ オサケユキチュア Configuration and method

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006090549A1 (en) * 2005-02-23 2006-08-31 Bussan Nanotech Research Institute Inc. Gas filtration apparatus
JP2006263707A (en) * 2005-02-23 2006-10-05 Bussan Nanotech Research Institute Inc Gas filtration apparatus
JP2016016406A (en) * 2014-07-07 2016-02-01 バルメット テクノロジーズ オサケユキチュア Configuration and method
JP7133284B2 (en) 2014-07-07 2022-09-08 バルメット テクノロジーズ オサケユキチュア Composition and method

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