JP2000140531A - Filter cloth for bag filter excellent in dimensional stability and its production - Google Patents

Filter cloth for bag filter excellent in dimensional stability and its production

Info

Publication number
JP2000140531A
JP2000140531A JP31500898A JP31500898A JP2000140531A JP 2000140531 A JP2000140531 A JP 2000140531A JP 31500898 A JP31500898 A JP 31500898A JP 31500898 A JP31500898 A JP 31500898A JP 2000140531 A JP2000140531 A JP 2000140531A
Authority
JP
Japan
Prior art keywords
filter
filter cloth
dimensional stability
bag filter
fiber
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
JP31500898A
Other languages
Japanese (ja)
Inventor
Hirobumi Sugiyama
博文 杉山
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.)
Toyobo Co Ltd
Original Assignee
Toyobo 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 Toyobo Co Ltd filed Critical Toyobo Co Ltd
Priority to JP31500898A priority Critical patent/JP2000140531A/en
Publication of JP2000140531A publication Critical patent/JP2000140531A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To prepare filter cloth for a bag filter having a fluoroplastic fiber support and excellent in long-term dimensional stability under high temp. and load. SOLUTION: In filter cloth for a bag filter excellent in dimensional stability constituted by laminating a filter layer on at least the single surface of a support, the support is formed from a knitted fabric comprising a fluoroplastic fiber and the filter layer contains staple fibers with Tg of 200 deg.C or higher. The filter cloth for the bag filter has excellent dimensional stability such that a longitudinal stretching ratio is 2% or less under load of 230 deg.C×720 hr/1 (kgf/5 cm) and is produced by laminating and integrating the support comprising the fluoroplastic fiber and the filter layer containing staple fibers with Tg of 200 deg.C or higher and subjecting them to hot air treatment of 200-350 deg.C or heating steam treatment.

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、スクリムがポリテ
トラフルオロエチレン繊維からなるバグフィルター用ろ
布に関するものである。詳しくは、実使用の高温度下で
かかると推測される荷重下において、長期間にわたり寸
法安定性に優れるバグフィルター用ろ布及びその製造方
法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a filter cloth for a bag filter in which a scrim is made of polytetrafluoroethylene fiber. More specifically, the present invention relates to a filter cloth for a bag filter having excellent dimensional stability over a long period of time under a load which is assumed to be applied at a high temperature in actual use, and a method for producing the same.

【0002】[0002]

【従来の技術】石炭炊きボイラー、都市ゴミ焼却炉、産
業廃棄物焼却炉等から排出される排ガス中には煤塵のみ
ならずダイオキシン等の有害物質等も含まれており、大
気汚染防止として各種排ガス集塵は非常に重要である。
かかる排ガスからのダストの分離捕集には集塵装置が用
いられ、集塵機内でのダイオキシンの再合成の抑制や、
捕集効率の面からもバグフィルターの使用が有望視され
ている。バグフィルターに用いられるろ布としては、一
般に織物やフェルトが用いられており、高捕集効率やろ
過速度の面からもフェルトろ布の使用が望ましい。
2. Description of the Related Art Exhaust gas emitted from coal-fired boilers, municipal waste incinerators, industrial waste incinerators, etc. contains not only dust but also harmful substances such as dioxin. Dust collection is very important.
A dust collector is used for separating and collecting dust from the exhaust gas, and suppression of resynthesis of dioxin in the dust collector,
The use of bag filters is also promising in terms of collection efficiency. As the filter cloth used for the bag filter, a woven cloth or a felt is generally used, and the use of a felt filter cloth is desirable from the viewpoint of high collection efficiency and filtration speed.

【0003】各種焼却設備の排ガス集塵において、バグ
フィルターの使用条件は多岐に渡る。例えば、一般都市
ゴミ焼却炉においては、24時間運転を行う全連、間欠
運転を行う准連、機械バッチ式等あり、使用温度も各設
備・条件によって異なる。また、排ガス中の有害ガスの
種類や濃度、およびこれら有害ガスを除去するための消
石灰や触媒を用いた還元剤の使用もあり、耐熱性のみな
らづず、高い耐薬品性も要求される。准連や機械バッチ
式では、繰り返し運転停止することによる結露の影響に
も耐えうる耐久性が要求される。また、ダスト分離・捕
集においても、パルスジェット式や逆洗式の違いがあ
り、ろ過速度やダストの濃度・粒径によっても条件は種
々異なる。
[0003] In exhaust gas collection of various incineration facilities, use conditions of a bag filter are various. For example, in general city waste incinerators, there are a full-scale station that operates for 24 hours, a semi-series station that performs intermittent operation, a mechanical batch type, and the like. In addition, the type and concentration of harmful gases in exhaust gas and the use of slaked lime or a reducing agent using a catalyst for removing these harmful gases require not only heat resistance but also high chemical resistance. In the cascade or mechanical batch method, durability that can withstand the effects of dew condensation due to repeated shutdowns is required. In addition, there are differences between the pulse jet method and the backwash method in dust separation and collection, and the conditions are variously different depending on the filtration speed and the concentration and particle size of the dust.

【0004】このように、バグフィルターの使用条件が
多岐に渡るため、バグフィルター用ろ布も各種条件に適
合したものが選択され使用される。中でも織物に比べて
ダスト捕集効率の高いフェルトろ布が適切であり、その
素材としては、ポリイミド、ポリフェニレンサルファイ
ド、ポリアミド、ポリアミドイミド、ポリテトラフルオ
ロエチレン等が使用される。これらろ布は、フィラメン
ト糸や紡績糸からなる織物をスクリムとし、この上下に
各種短繊維からなるウエブを積層・絡み合わせることに
よりフェルトとし、ろ過特性のみならず物理的強度にも
優れるバグフィルター用ろ布を得ている。
[0004] As described above, since the conditions for using the bag filter vary widely, filter cloths suitable for various conditions are selected and used for the bag filter. Among them, a felt filter cloth having a higher dust collection efficiency than a woven fabric is suitable, and as its material, polyimide, polyphenylene sulfide, polyamide, polyamide imide, polytetrafluoroethylene, or the like is used. These filter cloths are made of a woven fabric consisting of filament yarn or spun yarn as a scrim, and a web made of various short fibers is laminated and entangled on the top and bottom to form a felt, which is used for bag filters that are excellent not only in filtration characteristics but also in physical strength. I have a filter cloth.

【0005】これらろ布は使用条件やろ布がもつ各種耐
久性によって適時選択されるが、200℃以上での連続
使用及び運転ピーク値が200℃以上の運転が可能なも
のとしては、ポリイミド繊維、ポリテトラフルオロエチ
レン繊維(PTFE)、ガラス繊維が挙げられ、汎用素
材として使用されている。中でもポリテトラフルオロエ
チレン繊維は耐薬品性が優れることから、有害ガスの発
生等、最も条件の厳しいところに使用され、ポリテトラ
フルオロエチレン繊維100%のバグフィルター用ろ布
や、スクリムにポリテトラフルオロエチレン繊維を使用
し、ろ過層の短繊維はポリテトラフルオロエチレン繊維
とガラス繊維を混綿したものを使用したバグフィルター
用ろ布が知られている。
[0005] These filter cloths are appropriately selected depending on the use conditions and the various durability of the filter cloth. Polyimide fibers, which can be used continuously at 200 ° C or higher and have an operation peak value of 200 ° C or higher, include polyimide fibers, Examples thereof include polytetrafluoroethylene fiber (PTFE) and glass fiber, which are used as general-purpose materials. Among them, polytetrafluoroethylene fiber has excellent chemical resistance, so it is used in the most severe conditions such as generation of harmful gas. Polytetrafluoroethylene fiber is 100% polytetrafluoroethylene fiber filter cloth and scrim polytetrafluoroethylene. There is known a filter cloth for a bag filter using ethylene fibers and using short fibers of a filtration layer made of a mixture of polytetrafluoroethylene fibers and glass fibers.

【0006】[0006]

【発明が解決しようとする課題】しかしながら、上記の
ようにスクリムにポリテトラフルオロエチレン繊維を使
用したバグフィルター用ろ布は、バグフィルター自体が
伸び易く、ひいてはろ布が目詰まりを起こし長期にわた
るダスト分離・捕集ができないという問題が実用面で生
じている。これは、バグフィルター用ろ布でより大きな
負荷のかかる逆洗式のダスト払い落とし方法ではもちろ
ん、パルスジェット払い落としにおいても発生している
現象であり改善が望まれている。この現象は、ろ過層が
ポリテトラフルオロエチレン繊維とガラス繊維が混綿さ
れたろ布においても同様であり、ポリテトラフルオロエ
チレン繊維自体が持つ繊維特性によるものと推測され
る。同じ200℃以上の連続使用が可能なポリイミド繊
維においては、融点がなく、ガラス転移温度が315℃
であるのに対し、ポリテトラフルオロエチレン繊維は、
融点327℃、ガラス転移温度が126℃(文献値、高
分子化学序論、化学同人)と熱的性質が比較的低いレベ
ルにある。短繊維の絡みつきの効果においても、ガラス
繊維は全く収縮しないため、単なる物理的な絡みによる
効果しかない。ポリテトラフルオロエチレンの短繊維の
絡みによる効果は、ガラス転移温度が実使用よりも小さ
いため、高温・実荷重下ではその絡みは小さくなってし
まう。ゆえに、支持体がポリテトラフルオロエチレン繊
維からなり、ろ過層がポリテトラフルオロエチレン繊維
やガラス繊維からなるバグフィルター用ろ布は、ガラス
転移温度よりも高い温度の使用においては、ろ布の自重
やリテーナーの重量、さらにダスト重量等の荷重によっ
てでさえもろ布が伸びが生じ、その結果、ろ布の目開き
が起こりダストが侵入して目詰まりを起こすものと推測
される。
However, as described above, the filter cloth for bag filter using the polytetrafluoroethylene fiber for the scrim has a problem that the bag filter itself is easily stretched, and thus the filter cloth is clogged and dust for a long time is generated. The problem that separation and collection cannot be performed has occurred in practical use. This is a phenomenon that occurs not only in the back-washing type dust removing method that places a greater load on the bag filter cloth, but also in the pulse jet removing method, and improvement is desired. This phenomenon is the same in a filter cloth in which a polytetrafluoroethylene fiber and a glass fiber are mixed in a filter layer, and it is presumed that the filtration property is caused by the fiber characteristics of the polytetrafluoroethylene fiber itself. The same polyimide fiber that can be used continuously at 200 ° C. or higher has no melting point and a glass transition temperature of 315 ° C.
Whereas, the polytetrafluoroethylene fiber is
With a melting point of 327 ° C and a glass transition temperature of 126 ° C (literature value, introduction to polymer chemistry, chemical coterie), the thermal properties are at relatively low levels. Even with the effect of entanglement of short fibers, glass fibers do not shrink at all, and therefore have the effect of mere physical entanglement. The effect of the entanglement of the short fibers of polytetrafluoroethylene is smaller at high temperatures and under an actual load because the glass transition temperature is lower than in actual use. Therefore, the filter cloth for a bag filter in which the support is made of polytetrafluoroethylene fiber and the filtration layer is made of polytetrafluoroethylene fiber or glass fiber, when using a temperature higher than the glass transition temperature, the weight of the filter cloth and It is presumed that the filter cloth is stretched even by a load such as the weight of the retainer and the weight of the dust, and as a result, the filter cloth is opened and dust enters and causes clogging.

【0007】本発明は、上記従来技術のバグフィルター
用ろ布の持つ問題点に対し、特に、ポリテトラフルオロ
エチレン繊維を支持体に使用したろ布においても、20
0℃前後の実使用において、ろ布の伸びやダストの目詰
まりがなく、長期にわたり寸法安定性に優れるバグフィ
ルター用ろ布を提案する事を目的とする。
[0007] The present invention solves the above-mentioned problems of the filter cloth for a bag filter of the prior art, and in particular, a filter cloth using polytetrafluoroethylene fibers as a support.
An object of the present invention is to propose a filter cloth for a bag filter which is free from elongation of the filter cloth and clogging of dust and has excellent dimensional stability over a long period of time in actual use at about 0 ° C.

【0008】[0008]

【課題を解決するための手段】即ち、本発明は、支持体
の少なくとも片面にろ過層が積層されたバグフィルター
用ろ布において、前記支持体はフッ素系繊維からなる織
編物であり、前記ろ過層はTgが200℃以上の短繊維
を含有する230℃×720時間、1(kgf/5cm) の荷重
下における、タテ方向の伸び率が2%以下であることを
特徴とする寸法安定性に優れたバグフィルター用ろ布で
ある。具体的にはろ過層に15〜100重量%の割合で
Tgが200℃以上の繊維の短繊維が含有されているこ
とを特徴とする上記記載の寸法安定性に優れたバグフィ
ルター用ろ布、230℃×3時間、1(kg/5cm)の荷重下
におけるタテ方向の伸び率が1%以下であることを特徴
とする上記記載の寸法安定性に優れたバグフィルター用
ろ布、及びフッ素系繊維がポリテトラフルオロエチレン
であることを特徴とする上記記載の寸法安定性に優れた
バ グフィルター用ろ布である。
That is, the present invention relates to a filter cloth for a bag filter in which a filter layer is laminated on at least one surface of a support, wherein the support is a woven or knitted fabric made of a fluorine-based fiber, The layer has a dimensional stability characterized by a vertical elongation of 2% or less under a load of 1 (kgf / 5cm) at 230 ° C for 720 hours containing short fibers having a Tg of 200 ° C or higher. It is an excellent filter cloth for bag filters. Specifically, the filter cloth for a bag filter having excellent dimensional stability as described above, wherein the filter layer contains short fibers of fibers having a Tg of 200 ° C. or more at a ratio of 15 to 100% by weight, A filter cloth for a bag filter having excellent dimensional stability as described above, wherein the elongation in the vertical direction under a load of 1 (kg / 5 cm) at 230 ° C. for 3 hours is 1% or less; The filter cloth for a bag filter having excellent dimensional stability as described above, wherein the fiber is polytetrafluoroethylene.

【0009】更に、本発明はフッ素系繊維からなる支持
体とTgが200℃以上の短繊維を含有するろ過層を積
層一体化後、200〜350℃の熱風処理あるいは,加
熱スチーム処理することを特徴とする寸法安定性に優れ
たバグフィルター用ろ布の製造方法である。具体的には
積層一体化処理が、ニードルパンチ、あるいは、ウオー
ターパンチによることを特徴とする上記記載の寸法安定
性に優れたバグフィルター用ろ布の製造方法、積層一体
化処理後に、加熱ロールによるろ過面の溶融プレスを施
すことを特徴とする上記記載の寸法安定性に優れたバグ
フィルター用ろ布の製造方法、及び積層一体化処理後
に、ろ過面の毛焼き処理を施すことを特徴とする上記記
載の寸法安定性に優れたバグフィルター用ろ布の製造方
法である。
Further, the present invention provides a method comprising laminating and integrating a support made of a fluorine-based fiber and a filtration layer containing short fibers having a Tg of 200 ° C. or more, followed by a hot air treatment at 200 to 350 ° C. or a steam treatment. This is a method for producing a filter cloth for a bag filter having excellent dimensional stability. Specifically, the lamination and integration process is a needle punch, or a method for producing a filter fabric for a bag filter having excellent dimensional stability as described above, which is characterized by using a water punch. The method for producing a filter fabric for a bag filter having excellent dimensional stability as described above, characterized by applying a melt press to the filtration surface, and performing a baking treatment on the filtration surface after the lamination and integration process. A method for producing a filter cloth for a bag filter having excellent dimensional stability as described above.

【0010】ポリテトラフルオロエチレン繊維はガラス
転移温度が126℃と低いため、200℃付近の実使用
の荷重下では伸びてしまう。一方、Tgが200℃の例
としてポリイミド繊維があげられる。ポリイミド繊維は
融点が無く、ガラス転移温度が315℃と耐熱性が高
く、200℃以下では無荷重でもほとんど収縮しない。
しかし、ガラス転移温度付近の熱処理で大きく収縮し最
大の収縮応力を生ずる。この性質を利用し、ポリテトラ
フルオロエチレン繊維支持体からなり、ろ過層にTgが
200℃以上の短繊維を含有し、支持体と一体化させ、
熱処理することにより、200℃前後の実使用におい
て、自重やリテーナー、ダスト負荷によっても、ろ布の
伸びがなく、ダスト目詰まりもない、長期にわたり優れ
た寸法安定性を示すことができる。
[0010] Since the polytetrafluoroethylene fiber has a low glass transition temperature of 126 ° C, it expands under a practical load of around 200 ° C. On the other hand, as an example of Tg of 200 ° C., there is polyimide fiber. The polyimide fiber has no melting point, has a high glass transition temperature of 315 ° C., and has high heat resistance, and hardly shrinks at 200 ° C. or less even under no load.
However, heat treatment near the glass transition temperature causes a large shrinkage and a maximum shrinkage stress. Utilizing this property, it is composed of a polytetrafluoroethylene fiber support, and the filter layer contains short fibers having a Tg of 200 ° C. or more, and is integrated with the support,
By performing the heat treatment, in actual use at about 200 ° C., the filter cloth does not elongate and has no dust clogging due to its own weight, retainer, and dust load, and can exhibit excellent dimensional stability over a long period of time.

【0011】以下本発明を詳述する。支持体がフッ素系
繊維からなるバグフィルター用ろ布で、高温下で長期に
わたり寸法安定性が優れるバグフィルター用ろ布を得る
には、ろ過層が少なくともTgが200℃以上の短繊維
を含有し、支持体とろ過層の積層一体化後に熱処理する
必要がある。本発明では、バグフィルターの実使用温度
よりもTgが高く、さらに高温処理により収縮するポリ
イミド繊維をろ過層に使用し、ポリテトラフルオロエチ
レン繊維からなる支持体と積層一体化し熱処理すること
により、ろ過層の短繊維の絡みが大きくなりスクリムに
よる伸びを抑制することができる。その結果、高温下で
寸法安定性に優れるバグフィルター用ろ布を得ることが
できる。
Hereinafter, the present invention will be described in detail. In order to obtain a filter cloth for a bag filter in which the support is made of a fluorine-based fiber and has excellent dimensional stability over a long period of time at a high temperature, the filter layer contains at least a short fiber having a Tg of 200 ° C. or more. It is necessary to perform a heat treatment after laminating and unifying the support and the filtration layer. In the present invention, the filtration temperature is higher than the actual use temperature of the bag filter, and a polyimide fiber that contracts due to a high-temperature treatment is used for the filtration layer, and is laminated and integrated with a support made of polytetrafluoroethylene fiber and heat-treated. The entanglement of the short fibers in the layer increases, and the elongation due to the scrim can be suppressed. As a result, a filter cloth for a bag filter having excellent dimensional stability at high temperatures can be obtained.

【0012】本発明の支持体を構成するフッ素系繊維と
しては、好ましくは90%以上がフッ素原子を主鎖また
は側鎖に1個以上有する繊維であればよいが、フッ素原
子数の比率の高いものほど好ましい。なかでもポリテト
ラフルオロエチレンが好ましい。
The fluorine-containing fiber constituting the support of the present invention is preferably a fiber having at least 90% or more of fluorine atoms in a main chain or a side chain. The more preferred. Among them, polytetrafluoroethylene is preferred.

【0013】支持体に用いるフッ素系繊維は、マルチフ
ィラメント糸、紡績糸、あるいはモノフィラメント糸な
どで構成された織物が使用され、織り組織としては、平
織り、綾織り、朱子織り等があげられ適時使用すること
ができる。
As the fluorine-based fiber used for the support, a woven fabric composed of a multifilament yarn, a spun yarn, a monofilament yarn or the like is used. can do.

【0014】本発明に用いる、ろ過層形成用短繊維は、
Tgが200℃以上ののポリイミド繊維が最も好まし
い。該短繊維のろ過層繊維に占める割合が15〜100
重量%であることが好ましい。さらに好ましくは、30
〜100重量%である。Tgが200℃以上の繊維と混
綿しろ過層を形成する短繊維としては、ポリテトラフル
オロエチレン、ポリフェニレンサルファイド、ポリアミ
ド、ポリアミドイミド、ポリベンゾイミダゾール、ガラ
ス等があげられる。
[0014] The short fibers for forming a filtration layer used in the present invention are:
A polyimide fiber having a Tg of 200 ° C. or higher is most preferable. The ratio of the short fibers to the filtration layer fibers is 15 to 100.
% By weight. More preferably, 30
100100% by weight. Examples of short fibers that form a filtration layer by mixing with fibers having a Tg of 200 ° C. or higher include polytetrafluoroethylene, polyphenylene sulfide, polyamide, polyamideimide, polybenzimidazole, and glass.

【0015】また、ろ過層を形成するポリイミドおよび
その他短繊維の繊維径はろ過の面から、0.1〜100
μmが好ましく、さらに好ましくは1〜50μmが好ま
しい。さらに繊維断面形状については、丸形、三角、ト
ライローバル、ランダム等種々あるが、特に限定された
ものではない。微粒子の捕捉という面から考えると比表
面積が大きいものが好ましく、ランダムな異形断面をし
たポリイミド繊維は伸びの抑制のみならず、排気濃度が
小さいというろ過においても最適である。
The fiber diameter of the polyimide and other short fibers forming the filtration layer is 0.1 to 100 from the viewpoint of filtration.
μm is preferred, and more preferably 1 to 50 μm. Furthermore, there are various fiber cross-sectional shapes such as a round shape, a triangular shape, a trilobal shape, and a random shape, but the shape is not particularly limited. From the viewpoint of capturing fine particles, those having a large specific surface area are preferable, and a polyimide fiber having a random irregular cross section is most suitable not only for suppression of elongation but also for filtration with a low exhaust gas concentration.

【0016】本発明に用いる熱処理としては、熱風処理
温度が200〜350℃、好ましくは、280〜340
℃である。ポリイミド繊維のガラス転移温度付近での熱
処理をすることにより、短時間に十分なポリイミド繊維
の収縮を与えることができる。それ以外に加熱スチーム
や熱カレンダーによる熱処理も行うことができる。熱処
理後は、ろ過特性の向上を目的とした加熱ロールによる
プレスやろ過面の毛焼き等を行うことができる。
As the heat treatment used in the present invention, the hot air treatment temperature is 200 to 350 ° C., preferably 280 to 340.
° C. By performing the heat treatment near the glass transition temperature of the polyimide fiber, sufficient shrinkage of the polyimide fiber can be given in a short time. In addition, heat treatment using a heating steam or a heat calender can also be performed. After the heat treatment, a press with a heating roll for the purpose of improving the filtration characteristics, a baking of the filtration surface, or the like can be performed.

【0017】本発明では、230℃、3時間、1(kg/5c
m)荷重下でのろ布タテ方向の伸び率が1%以下であるこ
とが好ましい。従来この種の伸び率測定としてホットス
トレッチ率というものがあり、230℃、3時間、1ポ
ンド(453g)荷重下での評価である。しかし、一般
的にバグは約5mあり、それに相応するリテーナーの自
重、およびダスト自体の荷重がかかるため、5(cm)あた
り少なくとも1(kg/5cm)の荷重がかかると推定され、1
ポンドの荷重下でしかも3時間では適切な評価ができて
いない。少なくともバグタテ方向の5(cm)巾あたりでは
1(kgf/5cm) かかると推定され、短時間でのより適切な
評価として、1(kgf/5cm) でのホットストレッチ評価を
行った。
In the present invention, at 230 ° C. for 3 hours, 1 (kg / 5c
m) It is preferable that the elongation percentage in the filter cloth length direction under load is 1% or less. Conventionally, there is a hot stretch rate as this type of elongation rate measurement, which is evaluated under a load of 1 pound (453 g) at 230 ° C. for 3 hours. However, since a bug is generally about 5 m and the corresponding weight of the retainer and the load of the dust itself are applied, it is estimated that a load of at least 1 (kg / 5 cm) is applied per 5 (cm).
Under a load of pounds and for 3 hours, proper evaluation was not possible. It is estimated that it takes 1 (kgf / 5cm) at least for a width of 5 (cm) in the bagate direction, and a hot stretch evaluation of 1 (kgf / 5cm) was performed as a more appropriate evaluation in a short time.

【0018】また、実使用では200℃前後で通常3〜
5年はバグフィルター用ろ布を使用するため、高温・荷
重下での長期にわたる評価が必要である。そこで、本発
明では、約1ヶ月に相当する720時間での高温・荷重
下でのホットストレッチ評価を行った。本発明では、2
30℃、720時間、1(kgf/5cm) 荷重下でのろ布タテ
方向の伸び率は2%以下、好ましくは1%以下であるこ
とが肝要である。
In actual use, the temperature is usually about 3 to about 200 ° C.
For 5 years, a long-term evaluation under high temperature and load is necessary because a filter cloth for bag filters is used. Therefore, in the present invention, a hot stretch evaluation under a high temperature and a load of 720 hours corresponding to about one month was performed. In the present invention, 2
It is important that the elongation in the vertical direction of the filter cloth under a load of 1 (kgf / 5 cm) at 30 ° C. for 720 hours is 2% or less, preferably 1% or less.

【0019】本発明に用いるバグフィルター用ろ布は、
ポリテトラフルオロエチレン繊維からなる支持体と、T
gが200℃以上のポリイミド短繊維を含むろ過層から
構成され、該ろ布の形成方法としては、ニードルパンチ
ング法やウオーターパンチング法があげられる。
The filter cloth for a bag filter used in the present invention comprises:
A support made of polytetrafluoroethylene fiber;
The filter cloth is composed of a filtration layer containing polyimide short fibers having a temperature of 200 ° C. or higher. Examples of a method for forming the filter cloth include a needle punching method and a water punching method.

【実施例】【Example】

【0020】以下本発明を実施例によりさらに具体的に
説明する。なお、本発明はこれら実施例のみに限定され
るものではない。実施例、比較例に記載した各物性値は
次のような測定法に従って測定した。
Hereinafter, the present invention will be described more specifically with reference to examples. Note that the present invention is not limited to only these examples. Each physical property value described in Examples and Comparative Examples was measured according to the following measurement methods.

【0021】(1) 230℃、3時間におけるろ布タテ方
向の伸び率(%)測定。 タテ方向に長さ25(cm)、巾5(cm)のバグフィルター用
ろ布サンプルの中央部に、タテ方向に20(cm)のマーク
を入れ、1ポンド、1(kgf/5cm) の荷重をかけ230℃
で3時間処理した後の長さを測定し、伸び率を測定し
た。なお、熱処理オーブンとしては、送風定温恒温器
(ヤマト科学株式会社製)を用いた。
(1) Measurement of elongation (%) in the direction of filter cloth length at 230 ° C. for 3 hours. Insert a mark of 20 (cm) in the vertical direction at the center of a filter cloth sample for a bag filter with a length of 25 (cm) and a width of 5 (cm) in the vertical direction, and load 1 pound and 1 (kgf / 5cm). 230 ° C
For 3 hours, and the elongation was measured. In addition, as the heat treatment oven, a blast constant temperature oven (manufactured by Yamato Scientific Co., Ltd.) was used.

【0022】(2) 230℃、720時間におけるろ布タ
テ方向の伸び率測定。 (1) の3時間評価と同様に、サンプルにマークを入れ、
1ポンド、1(kgf/5cm)の荷重をかけ230℃で720
時間処理した後の長さをで測定し、伸び率を測定した。
(1) と同様に送風定温恒温器(ヤマト科学株式会社製)
を用いて評価した。
(2) Measurement of elongation in the vertical direction of the filter cloth at 230 ° C. for 720 hours. As in the three-hour evaluation in (1), mark the sample,
1 pound, 1 (kgf / 5cm) load, 720 ℃ at 230 ℃
The length after the time treatment was measured, and the elongation was measured.
As in (1), constant temperature air ventilator (Yamato Scientific Co., Ltd.)
Was evaluated using

【0023】(3) 引張強力 JIS L 1096に従い、カットストリップ法にて
ろ布の、タテ方向の引張強力を測定した。
(3) Tensile Strength According to JIS L 1096, the tensile strength of the filter cloth in the vertical direction was measured by a cut strip method.

【0024】(4) 通気度 JIS L 1096に従い、フラジール法にてろ布の
通気度を測定した。
(4) Air permeability The air permeability of the filter cloth was measured by the Frazier method according to JIS L 1096.

【0025】(実施例1)バグフィルター用ろ布は、下
記のようなスクリムを製織し、短繊維からなるろ過層
と、一般的なニードルパンチ法によって一体化させた。
支持体は、平均繊度400デニールのポリテトラフルオ
ロエチレン繊維(レンチング社製PTFE繊維、PROFIL
EN)を平織りにし、タテ/ヨコ、25本/25本/inch
にて製職した。目付は90(g/m2)であり、バグフィルタ
ー用ろ布のスクリムとした。
Example 1 A filter fabric for a bag filter was prepared by weaving a scrim as described below and integrating it with a filter layer made of short fibers by a general needle punching method.
The support is made of polytetrafluoroethylene fiber having an average fineness of 400 denier (a PTFE fiber manufactured by Lenting, PROFIL
EN) with plain weave, vertical / horizontal, 25/25 / inch
Made a job at. The basis weight was 90 (g / m 2 ), and the scrim of the filter cloth for bag filter was used.

【0026】実施例1で用いたろ過層用短繊維は、ポリ
イミド繊維(東洋紡績社製、P84)100%であり、
2デニール、60mmであった。ろ過層用ポリイミド短繊
維は、まず予備開繊を行った後、ローラーカードに供し
細かな開繊・繊維配列を行った。そして、クロスレイヤ
ーによりウエブを積層し、プレニーパン、仕上げニーパ
ンを経てろ過層を得た。その後、ポリテトラフルオロエ
チレンからなるスクリムの上下に該ろ過層を積層し、同
じくプレニーパン、仕上げニーパンを行った熱カレンダ
ーロール処理を行った。その後、320℃×30秒の熱
風処理を行い、さらにバーナーによりろ過面を毛焼きし
た。目付は521(g/m2)、厚み2.1(mm)、通気度16
(cc/cm2 ・ s)であり、PTFE支持体からなりろ過層が
ポリイミド繊維からなるバグフィルター用ろ布を得た。
The short fibers for the filtration layer used in Example 1 were 100% polyimide fibers (P84, manufactured by Toyobo Co., Ltd.)
It was 2 denier and 60 mm. The polyimide short fiber for the filtration layer was first preliminarily opened, and then supplied to a roller card for fine opening and fiber arrangement. And the web was laminated | stacked by the cross layer, and the filtration layer was obtained through the pre knee pan and the finishing knee pan. Thereafter, the filtration layers were laminated on and under a scrim made of polytetrafluoroethylene, and subjected to a heat calender roll treatment in which a pre-kneader and a finishing kneader were similarly performed. Thereafter, a hot air treatment was performed at 320 ° C. for 30 seconds, and the filter surface was burnt with a burner. The basis weight is 521 (g / m 2 ), thickness 2.1 (mm), air permeability 16
(cc / cm 2 · s), and a filter cloth for a bag filter comprising a PTFE support and a filtration layer comprising polyimide fibers was obtained.

【0027】(実施例2)実施例1と同様なポリテトラ
フルオロエチレン繊維を用いた支持体を用い、ろ過層を
形成する短繊維は、実施例1と同様なポリイミド繊維と
ポリテトラフルオロエチレン短繊維(レンチング社製P
TFE繊維、PROFILEN)をP84/PROFILEN=70/3
0の重量比で用いた。PROFILEN短繊維は2.5デニー
ル、53(mm)のものを用いた。ろ過層を形成するP84
短繊維とPTFE短繊維は、実施例1と同様に予備開繊
を経てローラーカードに供し、細かな開繊、繊維配列を
行った後、クロスレイヤーによりウエブを積層しプレニ
ーパン、仕上げニーパンを経てろ過層を得た。実施例1
と同様に支持体上下に該ろ過層を積層し、プレニーパ
ン、仕上げニーパンを行った。そして、実施例1と同様
に熱カレンダー加工、毛焼き処理を行った。その後、実
施例1と同様に320℃×30秒の熱風処理を行い、P
TFE支持体からなりろ過層がポリイミド繊維とPTF
E繊維からなるバグフィルター用ろ布を得た。目付は、
542(g/m2)、厚み2.2(mm)、通気度17(cc/cm2・s)
であった。
Example 2 Using a support made of the same polytetrafluoroethylene fiber as in Example 1, the short fibers forming the filtration layer were made of the same polyimide fiber and polytetrafluoroethylene short fiber as in Example 1. Fiber (Lenting P
P84 / PROFILEN = 70/3 for TFE fiber, PROFILEN)
It was used at a weight ratio of 0. PROFILEN short fibers of 2.5 denier and 53 (mm) were used. P84 forming a filtration layer
Short fibers and PTFE short fibers are subjected to pre-spreading as in Example 1, subjected to a roller card, finely spread, fiber arrangement is performed, and then a web is laminated by a cross layer, and then filtered through a pre-knee pan and a finished knee pan. Layer obtained. Example 1
The filtration layers were laminated on the upper and lower sides of the support in the same manner as described above, and pre-kneading and finishing kneading were performed. Then, in the same manner as in Example 1, hot calendering and scalding were performed. Thereafter, hot air treatment at 320 ° C. for 30 seconds is performed in the same manner as in Example 1, and P
Filtration layer consisting of TFE support, polyimide fiber and PTF
A filter cloth for bag filter made of E fiber was obtained. The basis weight is
542 (g / m 2 ), thickness 2.2 (mm), air permeability 17 (cc / cm 2 · s)
Met.

【0028】(実施例3)実施例1と同様なPTFE繊
維よりなる支持体を用い、ろ過層には実施例1,2と同
様なポリイミド繊維とPTFE繊維を用い、さらに、ポ
リフェニレンサルファイド(PPS)短繊維(東洋紡績
社製、PROCON)2デニール、60(mm)の3種類を用い
た。ろ過層を形成する短繊維の混率はポリイミド/PT
FE/PPS=40/30/30で用いた。実施例1,
2と同様な方法によりニードルパンチ加工を行い、熱カ
レンダー加工、毛焼き処理を行い、熱処理も行った。目
付551(g/m2)、厚み2.2(mm)、通気度14(cc/cm2
s)の支持体がPTFE繊維からなりろ過層がP84、P
TFE、PPSからなるバグフィルター用ろ布を得た。
(Example 3) A support made of PTFE fiber similar to that of Example 1 was used, and a polyimide layer and PTFE fiber similar to those of Examples 1 and 2 were used for a filtration layer. Further, polyphenylene sulfide (PPS) was used. Three types of short fibers (PROCON, manufactured by Toyobo Co., Ltd.) of 2 denier and 60 (mm) were used. The mixing ratio of the short fibers forming the filtration layer is polyimide / PT.
FE / PPS = 40/30/30. Example 1,
Needle punching was performed in the same manner as in Example 2, heat calendering, hair sintering, and heat treatment were also performed. Weight 551 (g / m 2 ), thickness 2.2 (mm), air permeability 14 (cc / cm 2 ·
s) The support is made of PTFE fiber and the filtration layer is P84, P
A filter cloth for bag filter consisting of TFE and PPS was obtained.

【0029】(比較例1)実施例1と同様なPTFE繊
維からなる支持体を用い、ろ過層はPTFE繊維100
%にて形成した。実施例1と同様にニードルパンチ加
工、熱カレンダー加工、熱処理を行い、PTFE繊維1
00%からなるバグフィルター用ろ布を得た。目付は6
71(g/m2)、厚み1.6(mm) 、通気度13(cc/cm2 ・ s)
のバグフィルター用ろ布を得た。
(Comparative Example 1) A support made of the same PTFE fiber as in Example 1 was used, and the filtration layer was made of PTFE fiber 100
%. Needle punching, heat calendering, and heat treatment were performed in the same manner as in Example 1, and PTFE fiber 1
A filter cloth for bag filters consisting of 00% was obtained. The basis weight is 6
71 (g / m 2 ), thickness 1.6 (mm), air permeability 13 (cc / cm 2 · s)
A filter cloth for a bag filter was obtained.

【0030】(比較例2)実施例1と同様なPTFE繊
維からなる支持体を用い、ろ過層はPTFE繊維85%
とガラス繊維15%にて、実施例2と同様にニードルパ
ンチ、熱カレンダー加工、熱処理を行いバグフィルター
用ろ布を得た。目付は660(g/m2)、厚みは1.5(m
m)、通気度は12(cc/cm2 ・ s)であった。
(Comparative Example 2) The same support made of PTFE fiber as in Example 1 was used, and the filtration layer was made of 85% PTFE fiber.
Needle punching, heat calendering, and heat treatment were performed in the same manner as in Example 2 with the glass fiber and 15% of glass fiber to obtain a filter cloth for a bag filter. The basis weight is 660 (g / m 2 ) and the thickness is 1.5 (m
m) and the air permeability was 12 (cc / cm 2 · s).

【0031】上記実施例1〜3、および、比較例1,2
について、230℃×3時間や230℃×720時間で
の伸び率、およびその他物性値を表1に示す。
Examples 1 to 3 and Comparative Examples 1 and 2
Table 1 shows the elongation percentage at 230 ° C. for 3 hours and 230 ° C. for 720 hours, and other physical properties of the sample.

【0032】以上のように、測定結果を見ると、荷重を
かけることにより実機で問題が起こったように、ろ布が
伸びる傾向があるものがある。ホットストレッチと称す
る230℃×3時間、1ポンド荷重下では、いずれのろ
布もその伸び率が1%以内にあり良好であるが、短時間
でも実使用でかかると想定される1(kgf/5cm) の荷重を
かけると、ポリイミド繊維を含まない比較例1、2の伸
び率は1%を越えてしまい、実使用で伸びの問題が起こ
る可能性があるばかりでなく、評価としても適切出ない
ことが分かる。さらに、720時間の長期評価になると
比較例1,2の伸び率はさらに大きくなり、1(kgf/5c
m) の荷重下では2%以上の伸び率を示し、ダスト目詰
まりの原因になっていると推測される。
As described above, from the results of the measurement, it can be seen that the filter cloth tends to stretch as if a problem occurred in an actual machine when a load was applied. Under a load of 1 pound under 230 ° C. × 3 hours called hot stretch, all of the filter cloths have good elongation within 1%, but are expected to be used even in a short time in actual use (1 kgf / kg). When a load of 5 cm) is applied, the elongation percentages of Comparative Examples 1 and 2, which do not contain polyimide fiber, exceed 1%, which may not only cause a problem of elongation in actual use, but also give an appropriate evaluation. I understand that there is no. Furthermore, in the long-term evaluation of 720 hours, the elongation rate of Comparative Examples 1 and 2 was further increased, and 1 (kgf / 5c
Under the load of m), it shows an elongation of 2% or more, which is presumed to be the cause of dust clogging.

【0033】一方、ろ過層にポリイミド繊維を含有した
実施例1〜3は、230℃×3時間の1ポンドはもちろ
ん1(kgf/5cm) でも非常に小さい伸び率を示している。
720時間の長期評価でも1ポンド、1(kgf/5cm) とも
にその伸び率は1%以下にあり、比較例と比べても非常
に小さいレベルにあることが分かり、高温・荷重下で高
い寸法安定性を示している。
On the other hand, Examples 1 to 3 in which the filtration layer contains polyimide fiber showed a very small elongation even at 1 (kgf / 5 cm) as well as 1 pound at 230 ° C. for 3 hours.
In the long-term evaluation of 720 hours, the elongation rate was 1% or less for both 1pound and 1 (kgf / 5cm). It was found that the elongation was very small compared to the comparative example, and high dimensional stability under high temperature and load. Shows sex.

【0034】[0034]

【発明の効果】本発明によれば、ポリテトラフルオロエ
チレン繊維支持体からなるバグフィルター用ろ布におい
て、ろ過層に実使用よりもガラス転移温度の高いポリイ
ミド繊維を含有させ、熱処理することにより、高温・荷
重下で長期にわたり優れた寸法安定性を示すバグフィル
ター用ろ布を提供することを可能とした。
According to the present invention, in a filter fabric for a bag filter comprising a polytetrafluoroethylene fiber support, a polyimide fiber having a higher glass transition temperature than that actually used is contained in a filtration layer, and heat treatment is performed. It has made it possible to provide a filter fabric for a bag filter that exhibits excellent dimensional stability over a long period of time under high temperature and load.

Claims (8)

【特許請求の範囲】[Claims] 【請求項1】支持体の少なくとも片面にろ過層が積層さ
れたバグフィルター用ろ布において、前記支持体はフッ
素系繊維からなる織編物であり、前記ろ過層はTgが2
00℃以上の短繊維を含有する230℃×720時間、
1(kgf/5cm)の荷重下における、タテ方向の伸び率が2
%以下であることを特徴とする寸法安定性に優れたバグ
フィルター用ろ布。
1. A bag filter fabric in which a filter layer is laminated on at least one side of a support, wherein the support is a woven or knitted fabric made of fluorine-based fibers, and the filter layer has a Tg of 2 or more.
230 ° C x 720 hours containing short fibers of 00 ° C or more,
The elongation percentage in the vertical direction under a load of 1 (kgf / 5cm) is 2
% Or less, the filter cloth for a bag filter having excellent dimensional stability.
【請求項2】ろ過層に15〜100重量%の割合でTg
が200℃以上の繊維の短繊維が含有されていることを
特徴とする請求項1記載の寸法安定性に優れたバグフィ
ルター用ろ布。
2. The filtration layer contains 15 to 100% by weight of Tg.
2. The filter cloth for a bag filter having excellent dimensional stability according to claim 1, wherein the filter cloth contains short fibers of fibers having a temperature of 200 ° C. or higher.
【請求項3】230℃×3時間、1(kg/5cm)の荷重下に
おけるタテ方向の伸び率が1%以下であることを特徴と
する請求項1記載の寸法安定性に優れたバグフィルター
用ろ布。
3. The bag filter having excellent dimensional stability according to claim 1, wherein the elongation in the vertical direction under a load of 1 (kg / 5 cm) at 230 ° C. for 3 hours is 1% or less. Filter cloth.
【請求項4】フッ素系繊維がポリテトラフルオロエチレ
ンであることを特徴とする請求項1記載の寸法安定性に
優れたバグフィルター用ろ布。
4. The filter cloth for a bag filter having excellent dimensional stability according to claim 1, wherein the fluorine-based fiber is polytetrafluoroethylene.
【請求項5】フッ素系繊維からなる支持体とTgが20
0℃以上の短繊維を含有するろ過層を積層一体化後、2
00〜350℃の熱風処理あるいは,加熱スチーム処理
することを特徴とする寸法安定性に優れたバグフィルタ
ー用ろ布の製造方法。
5. A support comprising a fluorine-based fiber and having a Tg of 20
After laminating and integrating a filtration layer containing short fibers of 0 ° C. or higher, 2
A method for producing a filter fabric for a bag filter having excellent dimensional stability, characterized by performing a hot air treatment at 00 to 350 ° C. or a steam treatment.
【請求項6】積層一体化処理が、ニードルパンチ、ある
いは、ウオーターパンチによることを特徴とする請求項
5記載の寸法安定性に優れたバグフィルター用ろ布の製
造方法。
6. The method for producing a filter cloth for a bag filter having excellent dimensional stability according to claim 5, wherein the lamination and integration treatment is performed by a needle punch or a water punch.
【請求項7】積層一体化処理後に、加熱ロールによるろ
過面の溶融プレスを施すことを特徴とする請求項5記載
の寸法安定性に優れたバグフィルター用ろ布の製造方
法。
7. The method for producing a filter cloth for a bag filter having excellent dimensional stability according to claim 5, wherein after the lamination and integration treatment, the filtration surface is subjected to a melt press by a heating roll.
【請求項8】積層一体化処理後に、ろ過面の毛焼き処理
を施すことを特徴とする請求項5記載の寸法安定性に優
れたバグフィルター用ろ布の製造方法。
8. The method for producing a filter cloth for a bag filter having excellent dimensional stability according to claim 5, further comprising subjecting the filtration surface to a hair burning treatment after the lamination and integration processing.
JP31500898A 1998-11-05 1998-11-05 Filter cloth for bag filter excellent in dimensional stability and its production Pending JP2000140531A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100461227B1 (en) * 2001-01-31 2004-12-13 가부시끼가이샤 도시바 Filter, reverse-washing method of filter, filtering unit and power plant
JP2015000378A (en) * 2013-06-17 2015-01-05 倉敷繊維加工株式会社 Air filter medium, its manufacturing method, and air filter
KR101718728B1 (en) * 2016-11-25 2017-03-22 한장훈 Method for forming pattern of knit and knit using it
US11344836B2 (en) 2017-11-24 2022-05-31 Lg Chem, Ltd. Porous fluorine resin film and preparation method thereof

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100461227B1 (en) * 2001-01-31 2004-12-13 가부시끼가이샤 도시바 Filter, reverse-washing method of filter, filtering unit and power plant
US7309424B2 (en) 2001-01-31 2007-12-18 Kabushiki Kaisha Toshiba Filtering apparatus, back wash method therefor, filtering device and power plant
US7754074B2 (en) 2001-01-31 2010-07-13 Kabushiki Kaisha Toshiba Filtering apparatus, back wash method therefor, filtering device and power plant
JP2015000378A (en) * 2013-06-17 2015-01-05 倉敷繊維加工株式会社 Air filter medium, its manufacturing method, and air filter
KR101718728B1 (en) * 2016-11-25 2017-03-22 한장훈 Method for forming pattern of knit and knit using it
US11344836B2 (en) 2017-11-24 2022-05-31 Lg Chem, Ltd. Porous fluorine resin film and preparation method thereof

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