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JP4318620B2 - Filter and filter surface processing method - Google Patents
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JP4318620B2 - Filter and filter surface processing method - Google Patents

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JP4318620B2
JP4318620B2 JP2004300079A JP2004300079A JP4318620B2 JP 4318620 B2 JP4318620 B2 JP 4318620B2 JP 2004300079 A JP2004300079 A JP 2004300079A JP 2004300079 A JP2004300079 A JP 2004300079A JP 4318620 B2 JP4318620 B2 JP 4318620B2
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嘉一 斉藤
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Description

本発明は集塵機のバグフルタのような耐熱性を必要とされるフィルタ及びこの種フィルタにおいて所望の耐熱性、耐薬品性、耐久性を得るためのフィルタ表面加工方法に関するものである。   The present invention relates to a filter that requires heat resistance, such as a bag filter of a dust collector, and a filter surface processing method for obtaining desired heat resistance, chemical resistance, and durability in this type of filter.

ダイオキシン類など有害物質による環境汚染は深刻な地球環境問題となり世界的に規制が強化され、ボイラ、焼却炉など産業燃焼炉においては確実な集塵除去が義務付けられている。   Environmental pollution caused by harmful substances such as dioxins has become a serious global environmental problem, and regulations have been strengthened globally. In industrial combustion furnaces such as boilers and incinerators, it is mandatory to remove dust.

ダイオキシン類は、燃焼温度が比較的低い不完全燃焼時に炭化水素と塩素が金属化合物の触媒作用で生成するといわれており、焼却室で厳格な管理の下に完全燃焼を行っても、排ガスの冷却過程で飛灰中の金属類を触媒として極微量の前駆物質から合成される。従って高温の燃焼室排ガスは、急冷してダイオキシン類生成温度域にある時間を短くして、バグフィルタで集塵するときには250℃以下になるようにしている。バグフィルタでの排ガス温度が下がったことで、濾材として有機繊維の使用が可能となったが、一方で、排ガス温度を低くしたことから排ガス中の硫酸ミスト、塩酸ミストなど酸性物質が水分に溶解して凝縮し、酸により濾材を傷めるという問題がでてきた。従って、濾材に使用される有機繊維の耐薬品性(耐酸性、耐アルカリ性)が強く要求されるようになってきた。   Dioxins are said to generate hydrocarbons and chlorine by the catalytic action of metal compounds during incomplete combustion at a relatively low combustion temperature. Even if complete combustion is performed under strict control in an incineration chamber, In the process, it is synthesized from a very small amount of precursor using metals in fly ash as a catalyst. Therefore, the high-temperature combustion chamber exhaust gas is rapidly cooled to shorten the time in the dioxin generation temperature range so that the temperature is 250 ° C. or lower when dust is collected by the bag filter. The use of organic fibers as a filter medium has become possible because the exhaust gas temperature in the bag filter has decreased, but on the other hand, since the exhaust gas temperature has been lowered, acidic substances such as sulfuric acid mist and hydrochloric acid mist in the exhaust gas dissolve in moisture. As a result, it has condensed, and the problem of damaging the filter medium by acid has arisen. Therefore, the chemical resistance (acid resistance and alkali resistance) of the organic fiber used for the filter medium has been strongly demanded.

バグフィルタの耐薬品性向上には、濾材表面をメラミン系樹脂や尿素系樹脂で被覆する方法(例えば、特許文献1参照)、全芳香族ポリアミド繊維及び布帛をフッ素系樹脂エマルションで処理する方法(例えば、特許文献2参照)、フッ素樹脂、ブロックドポリイソシアネート化合物およびフェノールノボラック化合物を配した加工剤で処理する方法(例えば、特許文献3参照)などがあり、濾材表面に耐酸性の化合物で覆う方法が中心である。   In order to improve the chemical resistance of the bag filter, the surface of the filter medium is coated with a melamine resin or urea resin (for example, see Patent Document 1), and the wholly aromatic polyamide fiber and fabric are treated with a fluorine resin emulsion ( For example, see Patent Document 2), a method of treating with a processing agent in which a fluororesin, a blocked polyisocyanate compound and a phenol novolak compound are arranged (see Patent Document 3, for example), and the surface of the filter medium is covered with an acid-resistant compound. The method is central.

また、濾材として繊維の代わりにポリテトラフルオロエチレン(PTFE)のような耐熱性樹脂多孔質膜材(メンブレン)を使用したものもある(例えば、特許文献4参照)。   Also, there is a filter medium that uses a heat-resistant resin porous membrane material (membrane) such as polytetrafluoroethylene (PTFE) instead of fibers (see, for example, Patent Document 4).

特開昭48−36770号公報JP 48-36770 A 特開昭56−107073号公報JP 56-107073 A 特開平9−122415号公報JP-A-9-122415 特表平11−506987号公報Japanese National Patent Publication No. 11-506987

濾材としての織布や不織布を構成する有機繊維の耐薬品性向上のため濾材表面を加工剤で被覆処理する従来技術は処理剤成分がフィルタ素材表面に付着しただけでは容易に脱落してしまい、またフィルタ素材表面に被膜を形成させるとフィルタの目詰まりとなり、耐久性と濾過性能は相容れないものがあった。   In order to improve the chemical resistance of organic fibers constituting the woven fabric and non-woven fabric as the filter medium, the conventional technique of coating the filter medium surface with a processing agent easily drops off when the processing agent component only adheres to the filter material surface. Moreover, when a film was formed on the surface of the filter material, the filter was clogged, and there was a conflict between durability and filtration performance.

PTFEメンブレンの場合は耐熱性に優れるが、高コストという問題に加えメンブレン膜の剥がれ、破れによる性能の劣化が生じ易い問題があった。   In the case of PTFE membrane, it has excellent heat resistance, but in addition to the problem of high cost, there has been a problem that the performance of the membrane film is likely to deteriorate due to peeling or tearing of the membrane film.

この発明は以上の問題点に鑑みてなされたものであり、濾過性能を損なわずに耐熱性、耐薬品性、撥水性、低摩擦抵抗、ダスト剥離性を向上することができるようにすることを目的とする。   The present invention has been made in view of the above problems, and is intended to improve heat resistance, chemical resistance, water repellency, low friction resistance, and dust peelability without impairing filtration performance. Objective.

本発明によれば、濾材表面に耐熱性短繊維を耐熱性樹脂にて溶着してなるフィルタが提供される。   ADVANTAGE OF THE INVENTION According to this invention, the filter formed by welding a heat resistant short fiber to a filter medium surface with a heat resistant resin is provided.

好ましくは、フィルタは濾材と、濾材の表面に溶着された低融点の第1の樹脂よりなる第1層と、第1の樹脂層の上に固着形成され、第1の樹脂より高融点の第2の樹脂と耐熱性短繊維との混在よりなる第2層とからなる。   Preferably, the filter is fixedly formed on the filter medium, the first layer made of the first resin having a low melting point welded to the surface of the filter medium, and the first resin layer having a higher melting point than the first resin. 2 and a second layer made of a mixture of heat-resistant short fibers.

また、フィルタは濾材表面に耐熱性短繊維と、乾燥時の温度より実質的に低融点の第1の樹脂と第1の樹脂より高融点の第2の樹脂との分散液を含浸後乾燥固化して形成してなる被覆層から構成することもできる。   The filter is impregnated with heat-resistant short fibers, a dispersion of a first resin having a melting point substantially lower than the drying temperature and a second resin having a melting point higher than that of the first resin, and then dried and solidified. It can also comprise from the coating layer formed.

第1の樹脂としては粒状フッ素系樹脂及び第2の樹脂としては粒状ポリイミド樹脂とすることができる。   The first resin can be a granular fluororesin and the second resin can be a granular polyimide resin.

より好ましくはフィルタは単糸繊度が0.3〜20DTEXで目付が80〜900g/mの繊維集合体より構成された濾材と、濾材の表面に溶融形成されたポリイミド樹脂層と、ポリイミド樹脂層の表面に形成されたフッ素系樹脂及び耐熱短繊維を含む混合層とから構成され、前記耐熱性短繊維は単糸繊度が0.2〜10DTEXである長繊維を0.4mm〜5mmの範囲の長さにカットしたものである。 More preferably, the filter is a filter medium composed of a fiber aggregate having a single yarn fineness of 0.3 to 20 DTEX and a basis weight of 80 to 900 g / m 2 , a polyimide resin layer melt-formed on the surface of the filter medium, and a polyimide resin layer The heat-resistant short fibers are made of long fibers having a single yarn fineness of 0.2 to 10 DTEX in the range of 0.4 mm to 5 mm. Cut to length.

本発明によれば、耐熱性繊維を所定長にカットし、カットされた前記耐熱性繊維をフッ素系樹脂微粒子及びポリイミド樹脂微粒子を含む分散液に混合し、この混合液に濾材を含浸し、混合液含浸後の濾材を樹脂を固定するべく加熱処理するフィルタ表面加工方法が提供される。   According to the present invention, the heat-resistant fiber is cut into a predetermined length, the cut heat-resistant fiber is mixed with a dispersion liquid containing fluorine-based resin fine particles and polyimide resin fine particles, the mixed liquid is impregnated with a filter medium, and mixed. A filter surface processing method is provided in which the filter medium after liquid impregnation is heat-treated to fix the resin.

本発明においては、耐熱性繊維のカット長は0.4mm〜5mmの範囲であり、フッ素系樹脂微粒子とポリイミド樹脂微粒子を含む分散液に混合・含浸後の濾材加熱温度(乾燥温度)は150℃〜330℃の範囲である。   In the present invention, the heat-resistant fiber has a cut length in the range of 0.4 mm to 5 mm. It is in the range of ~ 330 ° C.

本発明のフィルタは濾材表面に耐熱性短繊維を耐熱性樹脂にて溶着して構成される。濾材としては織布や不織布などの繊維集合体が好ましく、濾材を被覆する樹脂層は好ましくは内外2層であり、外層中に耐熱性短繊維が位置している。   The filter of the present invention is constructed by welding heat-resistant short fibers to a filter medium surface with a heat-resistant resin. The filter medium is preferably a fiber assembly such as a woven fabric or a non-woven fabric. The resin layer covering the filter medium is preferably an inner and outer two layers, and heat-resistant short fibers are located in the outer layer.

濾材を構成する繊維としては、ポリテトラフルオロエチレン(PTFE)、ポリイミド繊維、P84(Inspec Fiber社)、ポリイミドアミド、アラミド、m−アラミド(帝人・デュポン社)、ポリフェニレンサルフィド、ポリエステル、ポリアクリロニトリル等の有機繊維、並びに金属繊維、ガラス繊維、シリカ繊維(ニチヤス、3M、belChem社製のbelCoTex)、炭素繊維、バサルト繊維等の無機繊維などであるが、これらに限定するものではない。   As fibers constituting the filter medium, polytetrafluoroethylene (PTFE), polyimide fiber, P84 (Inspec Fiber), polyimide amide, aramid, m-aramid (Teijin / DuPont), polyphenylene sulfide, polyester, polyacrylonitrile, etc. Organic fibers, and inorganic fibers such as metal fibers, glass fibers, silica fibers (Nichias, 3M, belCoTex manufactured by belChem), carbon fibers, and basalt fibers, but are not limited thereto.

濾材を織布により構成した場合、単繊維(モノフィラメント)の繊度としては0.3〜2.0DTEXで目付けとしては80〜900g/m、好ましくは300〜900g/mであり、織組織としては二重平(筒織)等が好適である。また、織布の代わりにニードルパンチなどの不織布により濾布を構成することもでき、この場合、不織布を構成する単繊維(モノフィラメント)の繊度としては1.0〜6.0DTEXで目付けとしては80〜900g/m、好ましくは300〜850g/mである。 When the filter medium is composed of a woven fabric, the fineness of a single fiber (monofilament) is 0.3 to 2.0 DTEX, and the basis weight is 80 to 900 g / m 2 , preferably 300 to 900 g / m 2. A double flat (tubular weave) or the like is suitable. Moreover, a filter cloth can also be comprised with nonwoven fabrics, such as a needle punch, instead of a woven fabric. In this case, the fineness of the single fiber (monofilament) which comprises a nonwoven fabric is 1.0-6.0DTEX, and is 80 as a fabric weight. ˜900 g / m 2 , preferably 300 to 850 g / m 2 .

本発明において、濾材表面に溶着すべき耐熱性繊維としてはフッ素系繊維、ガラス系繊維、シリカ系繊維、耐熱イミド系繊維、アミド系繊維から選ばれる一種又はそれ以上であり、耐熱性繊維としてのフッ素系繊維、ガラス系繊維、シリカ系繊維、耐熱イミド系繊維、アミド系繊維は通常は繊維長が無限大(フィラメント状)のロービング(ストランド)として供給されるが、ロービングは切断工程を通すことにより0.4mm〜5mmの範囲の長さの短繊維にカットされる。耐熱繊維の繊度(単繊維の繊度)としては0.2〜10DTEX 、好ましくは0.2〜4.5DTEXであり、濾材を構成する単繊維の繊度より相当に細い。濾材を構成する短繊維を太くできるため濾材コストは低減されるが、繊維間の空隙を細い短繊維で閉塞することができ、これより高いフィルタ性能を少しも損なうことなく確保することができる。   In the present invention, the heat-resistant fiber to be welded to the filter medium surface is one or more selected from fluorine-based fiber, glass-based fiber, silica-based fiber, heat-resistant imide-based fiber, and amide-based fiber. Fluorine fiber, glass fiber, silica fiber, heat-resistant imide fiber, and amide fiber are usually supplied as rovings (strands) with an infinite fiber length. Is cut into short fibers having a length in the range of 0.4 mm to 5 mm. The fineness of the heat-resistant fiber (fineness of the single fiber) is 0.2 to 10 DTEX, preferably 0.2 to 4.5 DTEX, which is considerably thinner than the fineness of the single fiber constituting the filter medium. Since the short fibers constituting the filter medium can be thickened, the cost of the filter medium is reduced, but the gaps between the fibers can be blocked with thin short fibers, and higher filter performance can be ensured without any loss.

本発明によれば、耐熱性短繊維は耐熱性樹脂により濾材表面に溶着される構造となっている。耐熱性樹脂はバインダ用の樹脂のみ(1種類の樹脂)で構成することも可能であるが、ポリイミド樹脂(本発明の第1の樹脂)などのバインダ層とフッ素系樹脂(本発明の第2の樹脂)などの表面処理層ととの2種類とからなるのが好ましい。ここに第1の樹脂は融点が含浸後の乾燥固化温度より相当低く、乾燥工程で完全に溶融し濾材表面に溶着され、第2の樹脂は融点が第1の樹脂のそれより相当高く、乾燥工程の高温においても即座に完全溶融せず、樹脂の粒状状態を維持することができる。即ち、図1は濾材(基布)を織布とした場合におけるこの発明の好ましいフィルタの構造を相当に模式化して示しており、繊維(フィラメント)の交絡により構成される濾材1はポリイミド樹脂などの完全に溶解したバインダ層2(本発明の第1層)により被覆され、このバインダ層2に相当の粒状状態を残しうるようにフッ素系樹脂層3(本発明の第2層)が形成され、フッ素系樹脂層3に耐熱性短繊維4が埋め込まれて、結果的に短繊維4を樹脂層2,3の介在により濾材(基布)1に溶着した構造を呈している。高い濾過性能を得るためには濾材1における繊維間空隙はその大きさが小さいことが望ましいが、濾材1を構成する単繊維の繊度をあまり小さくできないことから濾材1そのものの繊維間空隙の大きさには限界があるが、この発明では濾材1を構成する単繊維より小さな繊度の(細い)短繊維4で濾材1を被覆する構造となっており、濾材1の繊維間空隙の大きさが短繊維4の存在によって補償され、より小さな空隙構造のフィルタを得ることができる。   According to the present invention, the heat-resistant short fiber has a structure that is welded to the surface of the filter medium by the heat-resistant resin. The heat-resistant resin can be composed of only a binder resin (one type of resin), but a binder layer such as a polyimide resin (first resin of the present invention) and a fluorine-based resin (second resin of the present invention). And a surface treatment layer such as a resin. Here, the first resin has a melting point considerably lower than the drying and solidification temperature after impregnation, and is completely melted and welded to the surface of the filter medium in the drying step, and the second resin has a melting point substantially higher than that of the first resin and is dried. Even at a high temperature in the process, the resin is not completely melted immediately and the granular state of the resin can be maintained. That is, FIG. 1 schematically shows a preferable filter structure of the present invention when the filter medium (base cloth) is a woven cloth. The filter medium 1 formed by entanglement of fibers (filaments) is a polyimide resin or the like. The fluorine resin layer 3 (second layer of the present invention) is formed so as to be covered with the completely dissolved binder layer 2 (first layer of the present invention) and leave a considerable granular state on the binder layer 2. The heat-resistant short fibers 4 are embedded in the fluorine-based resin layer 3, and as a result, the short fibers 4 are welded to the filter medium (base fabric) 1 through the resin layers 2 and 3. In order to obtain high filtration performance, it is desirable that the inter-fiber gap in the filter medium 1 is small. However, since the fineness of the single fibers constituting the filter medium 1 cannot be reduced so much, the size of the inter-fiber gap in the filter medium 1 itself. However, in the present invention, the filter medium 1 is covered with short fibers 4 having a fineness (thin) smaller than the single fibers constituting the filter medium 1, and the size of the inter-fiber gap of the filter medium 1 is short. Compensated by the presence of the fibers 4, a filter with a smaller void structure can be obtained.

後述の通り、樹脂層2、3を形成するためフッ素系樹脂及びはポリイミド樹脂は微粒子を液分散させた状態で濾材1に塗布され、加熱固化することにより樹脂層2、3とするが、ポリイミド樹脂は完全溶融しフッ素樹脂+短繊維を濾材1に溶着するバインダとして機能し、他方フッ素系樹脂はフィルタに所定の耐表面摩耗を付与させると共に、高温でフィルタ表面の堆積物によりフィルタ材料が伸びて形体が損なわれるのを抑えるように機能させることができる。尚、ポリイミド樹脂は前記フッ素系樹脂微粒子をフィルタ表面に固着させる前記作用に加え、耐表面摩耗を向上させ、高温でフィルタ表面の堆積物によりフィルタ材料が伸びて形体が損なわれるのを抑える機能も発揮する。   As will be described later, in order to form the resin layers 2 and 3, the fluororesin and the polyimide resin are applied to the filter medium 1 in a state in which fine particles are dispersed in liquid, and are heated and solidified to form the resin layers 2 and 3. The resin completely melts and functions as a binder to weld the fluororesin + short fibers to the filter medium 1, while the fluororesin imparts a predetermined surface wear resistance to the filter and the filter material is stretched by deposits on the filter surface at high temperatures. It can be made to function so as to prevent the form from being damaged. In addition to the above-mentioned action of fixing the fluororesin fine particles to the filter surface, the polyimide resin also has a function of improving surface wear resistance and suppressing the shape of the filter material from being stretched by deposits on the filter surface at high temperatures. Demonstrate.

本発明において、ポリイミド樹脂としては、ポリ(N,N’− p−フェニレン−ピロメリット酸イミド)、ポリ(N,N’− p−フェニレン−ベンゾフェノンテトラカルボン酸イミド)、ポリ(N,N’− p−フェニレン−トリメリット酸アミドイミド)から選ばれる一種以上であり、これらの化学構造は   In the present invention, as the polyimide resin, poly (N, N′-p-phenylene-pyromellitic imide), poly (N, N′-p-phenylene-benzophenone tetracarboxylic imide), poly (N, N ′ -P-phenylene-trimellitic acid amide imide), and their chemical structure is

Figure 0004318620
の通りであり、これらのものは東レ・デュポン株式会社、東洋紡績株式会社などにより市販されている。上記のものの他、ポリイミド樹脂として、ポリ(N,N’− p−フェニレン−ビフェニルテトラカルボン酸イミド)、ポリ(N,N’− m−フェニレン−ピロメリット酸イミド)なども使用できるが、前記のものより耐熱性としては劣っている。
Figure 0004318620
These are commercially available from Toray DuPont Co., Ltd. and Toyobo Co., Ltd. In addition to the above, poly (N, N′-p-phenylene-biphenyltetracarboxylic imide), poly (N, N′-m-phenylene-pyromellitic imide) and the like can be used as the polyimide resin. It is inferior in heat resistance than the ones.

フッ素系樹脂としては、好ましくは、ポリテトラフルオロエチレン、ポリクロロトリフルオロエチレンから選ばれる一種以上である。ポリテトラフルオロエチレン、ポリクロロトリフルオロエチレン以外に、テトラフルオロエチレンやクロロトリフルオロエチレンとエチレンなど他のビニル系モノマーとのコポリマーでも可能であるが、含水素モノマーの混合比が高くなると、フッ素系樹脂の特性が損なわれるので好ましくない。フッ素系樹脂微粒子は、旭硝子株式会社、シャムロックテクノロジー社(米国)から市販されており、これらを使用することができる。   The fluororesin is preferably at least one selected from polytetrafluoroethylene and polychlorotrifluoroethylene. In addition to polytetrafluoroethylene and polychlorotrifluoroethylene, copolymers of tetrafluoroethylene and other vinyl monomers such as chlorotrifluoroethylene and ethylene are also possible. However, when the mixing ratio of hydrogen-containing monomers increases, Since the characteristic of resin is impaired, it is not preferable. Fluorine-based resin fine particles are commercially available from Asahi Glass Co., Ltd. and Shamrock Technology (USA), and these can be used.

本発明のフィルタ表面加工方法によれば、耐熱性繊維は0.4mm〜5mmの範囲といった長さの短繊維にカットされ、カットされた短繊維をフッ素系樹脂微粒子とポリイミド樹脂微粒子を含む分散液に混合し、この混合液に濾材を含浸して、混合液を含浸後の濾材を150℃〜330℃といったの範囲の高温度に加熱されることにより、樹脂は固定乾燥される。ポリイミド樹脂は融点が180℃程度と低く、他方フッ素の融点は320℃程度でポリイミド樹脂の融点より相当高い。短繊維を含んだフッ素系樹脂微粒子及びポリイミド樹脂微粒子を含む分散液を濾材に含浸させ、150℃〜330℃の温度で加熱することにより、ポリイミド樹脂は実質的に完全に融解されるもフッ素系樹脂は軟化するに留まる。そのため、加熱処理後においては、ポリイミド樹脂より成る第1層2は濾材1を構成する繊維表面に均一にコーティングされ、粒状のフッ素系樹脂及び短繊維は第2層3として第1層2に固定された図1の構造が得られる。   According to the filter surface processing method of the present invention, the heat-resistant fiber is cut into short fibers having a length in the range of 0.4 mm to 5 mm, and the cut short fiber is a dispersion containing fluorine resin fine particles and polyimide resin fine particles. The resin is fixed and dried by impregnating the mixture with the filter medium and heating the filter medium after impregnating the mixture to a high temperature such as 150 ° C. to 330 ° C. The melting point of the polyimide resin is as low as about 180 ° C., while the melting point of fluorine is about 320 ° C., which is considerably higher than the melting point of the polyimide resin. The polyimide resin is substantially completely melted by impregnating the dispersion containing the fluorine resin fine particles containing short fibers and the polyimide resin fine particles into the filter medium and heating at a temperature of 150 ° C. to 330 ° C. The resin will only soften. Therefore, after the heat treatment, the first layer 2 made of polyimide resin is uniformly coated on the surface of the fibers constituting the filter medium 1, and the granular fluororesin and short fibers are fixed to the first layer 2 as the second layer 3. The resulting structure of FIG. 1 is obtained.

耐熱性短繊維としてのPTFE繊維は、プロフィレン(レンチング社)、ユミフロン(YMT社)トヨフロン(東レ社)等があるが特に前2社のPTFE繊維は異型断面でありよりフィルタの性能を向上させることができる。使用繊維は使用目的によるが、1.5DTEX(平均値)から4.0DTEX(平均値)が好ましい。混合樹脂との混合比(短繊維−混合樹脂重量比)は、5−50%が好ましく、加工上からすると、10%〜30%の範囲が特に望ましい。   PTFE fibers as heat-resistant short fibers include Profilene (Lentining), Yumiflon (YMT) and Toyoflon (Toray), but the PTFE fibers of the previous two companies have a modified cross section and improve the filter performance more. be able to. The fiber used depends on the purpose of use, but 1.5 DTEX (average value) to 4.0 DTEX (average value) is preferable. The mixing ratio with the mixed resin (short fiber-mixed resin weight ratio) is preferably 5 to 50%, and from the viewpoint of processing, a range of 10% to 30% is particularly desirable.

フッ素系樹脂微粒子、ポリイミド樹脂微粒子の粒子の大きさは、両方とも細かいほど好ましいが、実用上は0.5〜10μmである。   The size of the fluorine resin fine particles and the polyimide resin fine particles is preferably as small as possible, but is practically 0.5 to 10 μm.

耐熱性繊維を含浸させる際のフッ素系樹脂微粒子とポリイミド樹脂微粒子の混合比(重量比)は、好ましくは100:5〜70、さらに好ましくは100:20〜40である。フッ素系樹脂微粒子100(重量部)に対しポリイミド樹脂微粒子が70(重量部)より多くなるとフッ素系樹脂微粒子がポリイミド樹脂にコーティングされて、特に撥水性においてポリイミド樹脂微粒子のもつ効果が充分に発揮されず、5(重量部)より少ないと、ポリイミド樹脂微粒子が脱落し易くなり耐久性に劣ることになる。   The mixing ratio (weight ratio) of the fluororesin fine particles and the polyimide resin fine particles when impregnating the heat resistant fiber is preferably 100: 5-70, more preferably 100: 20-40. When the amount of polyimide resin fine particles exceeds 70 (parts by weight) with respect to 100 (parts by weight) of the fluorine resin fine particles, the fluorine resin fine particles are coated on the polyimide resin, and the effect of the polyimide resin fine particles is sufficiently exerted particularly in water repellency. If the amount is less than 5 (parts by weight), the polyimide resin fine particles easily fall off and the durability is inferior.

混合する短繊維(カットファイバ)を均一に分散させるため、フッ素系樹脂微粒子とポリイミド樹脂微粒子は、それらを含む分散液、好ましくは水を分散媒体にした水分散液にして、これを濾材に含浸させる。分散液中の固体分濃度は高いほど一度に多く付着させることができるが、固体分10〜60重量%程度が取扱い上から好ましい。さらに好ましいのは、15−30重量%程度である。分散液を製造する際に、界面活性剤などの分散安定剤を加えることがあるが本発明はこれらの添加についてなんら制限するものではない。   In order to uniformly disperse the short fibers (cut fibers) to be mixed, the fluororesin fine particles and the polyimide resin fine particles are made into a dispersion containing them, preferably an aqueous dispersion using water as a dispersion medium, and this is impregnated into the filter medium. Let The higher the solid content concentration in the dispersion, the more can be deposited at a time, but the solid content is preferably about 10 to 60% by weight from the viewpoint of handling. More preferred is about 15-30% by weight. In the production of the dispersion, a dispersion stabilizer such as a surfactant may be added, but the present invention does not limit these additions.

濾材に上記分散液を含浸させるには、ローラーコート法、ディッピング法、(簡易法としてはスプレーコート法も考えられる。)などによってできる。これらの方法により短繊維を含有の、フッ素系樹脂微粒子とポリイミド樹脂微粒子を濾材表面に付着させるが、分散液の濃度や含浸方法によって一度の含浸では必要な付着量が得られないことがあり、この場合には固体分をできるだけ少なくして、含浸と乾燥を繰り返して所定の付着量を満たすようにする。   The filter medium can be impregnated with the dispersion by a roller coating method, a dipping method, or a spray coating method as a simple method. Fluorine-based resin particles and polyimide resin particles containing short fibers are attached to the filter medium surface by these methods, but the required amount of adhesion may not be obtained by one impregnation depending on the concentration of the dispersion and the impregnation method, In this case, the solid content is reduced as much as possible, and the impregnation and drying are repeated to satisfy a predetermined adhesion amount.

濾材上に付着する短繊維はフッ素系樹脂微粒子とポリイミド樹脂微粒子により固定されるが、好ましくは合計で10〜100g/m、さらに好ましくは25〜60g/mである。この付着量の範囲は、本発明の目的とするフィルタの耐熱性、耐薬品性、耐久性の点から最適値として求められたものであり、使用する短繊維の線径と樹脂の固化により確定する。100g/mより多いと、効果は充分であるが、付着量の増加に伴う効果のさらなる向上が少なく、経済的に見て不利になることがあり、さらに通気性や硬さなどフィルタの特性が損なわれることがある。逆に、10g/mより少ないと本発明の目的が充分達せられないことがある。 The short fibers adhering to the filter medium are fixed by the fluorine resin fine particles and the polyimide resin fine particles, but the total amount is preferably 10 to 100 g / m 2 , more preferably 25 to 60 g / m 2 . The range of the amount of adhesion is determined as an optimum value from the viewpoint of heat resistance, chemical resistance and durability of the filter targeted by the present invention, and is determined by the diameter of the short fiber used and solidification of the resin. To do. When the amount is more than 100 g / m 2 , the effect is sufficient, but there is little further improvement in the effect due to the increase in the amount of adhesion, which may be disadvantageous from an economical point of view, and further filter characteristics such as air permeability and hardness. May be damaged. Conversely, if it is less than 10 g / m 2 , the object of the present invention may not be sufficiently achieved.

短繊維を濾材に固着させるには、フッ素系樹脂微粒子とポリイミド樹脂微粒子を含む分散液に均一に短繊維を分散させ含浸させた後、予備乾燥で水分のほとんどを蒸発させた後、150〜330℃、好ましくは180〜200℃にて、5〜60分間、好ましくは10〜30分間加熱し樹脂をキュアリングさせる。この加処理により、濾材表面のポリイミド樹脂微粒子が軟化し、部分的に短繊維が、濾材表面に固定することになる。従って、この加熱温度は、用いるポリイミド樹脂の種類を考慮して選ぶべきである。   In order to fix the short fibers to the filter medium, the short fibers are uniformly dispersed and impregnated in a dispersion containing fluorine resin fine particles and polyimide resin fine particles, and then most of the water is evaporated by preliminary drying, and then 150 to 330. The resin is cured by heating at ℃, preferably 180-200 ℃, for 5-60 minutes, preferably 10-30 minutes. By this treatment, the polyimide resin fine particles on the surface of the filter medium are softened, and the short fibers are partially fixed on the surface of the filter medium. Therefore, this heating temperature should be selected in consideration of the type of polyimide resin used.

フッ素系短繊維(カットファイバ)を使用する場合、融点の327℃近辺で加工することにより、より繊維を被服布に均一に固定する。(高温カレンダー処理等)フィルタ効果の性能を向上させることができる。   In the case of using fluorine-based short fibers (cut fibers), the fibers are more uniformly fixed to the clothing cloth by processing at around 327 ° C. of the melting point. (High temperature calendar process etc.) The performance of the filter effect can be improved.

上記加熱処理では短繊維は変形しながら、濾材を構成する繊維表面にポリイミド樹脂が薄くコートされ、そのポリイミド樹脂により短繊維が固定された状態になっている。ポリイミド樹脂のコートによりフィルタの耐薬品性、耐酸性が実現する。この状態でフィルタを使用してPTFE樹脂が短繊維等の表面構成に付加され、メンブレン膜に匹敵する性能向上となる。   In the heat treatment, the short fibers are deformed, and the surface of the fibers constituting the filter medium is thinly coated with polyimide resin, and the short fibers are fixed by the polyimide resin. Chemical resistance and acid resistance of the filter are realized by the polyimide resin coating. In this state, a filter is used to add PTFE resin to the surface structure of short fibers and the like, and the performance is improved comparable to a membrane film.

本発明のフィルタの表面加工方法により得られたフィルタは、濾過特性を損なわずに、耐熱性、耐薬品性、撥水性、低摩擦抵抗、ダスト剥離性を向上することができる。さらに、ダストの付着による、丈伸びを少なく、より安定した寸法変化により劣化(濾布破れ)を防止できる利点もある。また、ガラス繊維を用いたフィルタでは、屈曲摩耗の問題が発生することがあるが、本発明の表面加工処理によりこの問題も軽減される。   The filter obtained by the surface processing method for a filter of the present invention can improve heat resistance, chemical resistance, water repellency, low friction resistance, and dust releasability without impairing filtration characteristics. Furthermore, there is an advantage that the length elongation due to the adhesion of dust is small, and deterioration (filter cloth breakage) can be prevented by a more stable dimensional change. Moreover, in the filter using glass fiber, the problem of bending wear may occur, but this problem is also reduced by the surface processing treatment of the present invention.

ガラス2重織からなる目付580g/mの濾材を、1.7DTEX(平均)のPTFE短繊維15%重量比(樹脂総重量に対する比)で含み、ポリテトラフルオロエチレンからなるフッ素系樹脂微粒子(粒径:約1μm)とポリ(N,N’− p−フェニレン−ピロメリット酸イミド)からなるポリイミド樹脂微粒子(粒径:約1μm)を重量比100:20で含む水分散液に含浸し、濾材表面に固形分20g/mを付着させた。水分のほとんどを蒸発させた後、200℃にて、30分間加熱し樹脂をキュアリングした。さらに330℃で表面カレンダー処理を行った。 Fluorine-based resin fine particles comprising polytetrafluoroethylene containing a filter medium having a basis weight of 580 g / m 2 made of glass double weave at a weight ratio of 1.7 DTEX (average) of PTFE short fibers of 15% (ratio to the total resin weight) ( Impregnating an aqueous dispersion containing polyimide resin fine particles (particle size: about 1 μm) composed of poly (N, N′-p-phenylene-pyromellitic imide) at a weight ratio of 100: 20 with a particle size of about 1 μm), A solid content of 20 g / m 2 was adhered to the surface of the filter medium. After most of the water was evaporated, the resin was cured by heating at 200 ° C. for 30 minutes. Furthermore, the surface calendar process was performed at 330 degreeC.

これをバグフィルタとして焼却炉で使用した。無処理のフィルタが従来約半年で目詰まりによって使用不可能となっていたのに対し、約1年以上使用可能となった。半年使用時の抜き取り検査で無処理品の通気度が0.31cm/cm/secまで落ち込んでいたのに対して、本発明の加工品は約5.0cm/cm/secと良好な通気性を保っている(新品時の通気度8cm/cm/sec)。また、バグフィルタへのダスト付着量は無処理品が1000g/mを越えていたのに対して、加工品では180g/m程度であり、ダストの払落しが良好であることが確認できた。 This was used in an incinerator as a bug filter. The untreated filter has been unusable due to clogging in about half a year, whereas it has been usable for more than one year. The air permeability of the untreated product fell to 0.31 cm 3 / cm 2 / sec in the sampling inspection during half-year use, whereas the processed product of the present invention was good at about 5.0 cm 3 / cm 2 / sec. Air permeability is maintained (air permeability when new is 8 cm 3 / cm 2 / sec). In addition, the amount of dust adhering to the bag filter was over 1000 g / m 2 for the untreated product, whereas it was about 180 g / m 2 for the processed product, confirming that the dust was removed well. It was.

ポリイミドからなる目付480g/mの濾材を、実施例1と同様に、1.7DTEX(平均)のPTFEの短繊維を15%重量比(樹脂総重量に対する比)で含み、フッ素系樹脂微粒子とポリイミド樹脂微粒子を重量比100:20で含む水分散液に含浸し、濾材表面に固形分25g/mを付着させた。水分のほとんどを蒸発させた後、200℃にて、30分間加熱し樹脂をキュアリングしてバグフィルタとし、酸性雰囲気の強い石炭コークス炉で使用した。従来の無処理品が約2年の使用でバグフィルタ円筒方向の切断時強度が新品時の約30%まで落ち込んでいたのに対して、フッ素系樹脂微粒子とポリイミド樹脂微粒子加工品は3年の使用で新品時対して60%近い切断時強度を保持していた。 A filter medium having a weight per unit area of 480 g / m 2 made of polyimide contains 1.7 DTEX (average) PTFE short fibers in a 15% weight ratio (ratio to the total resin weight) in the same manner as in Example 1. An aqueous dispersion containing polyimide resin fine particles at a weight ratio of 100: 20 was impregnated, and a solid content of 25 g / m 2 was adhered to the surface of the filter medium. After most of the water was evaporated, it was heated at 200 ° C. for 30 minutes to cure the resin to form a bag filter, which was used in a coal coke oven with a strong acidic atmosphere. The conventional untreated product has been used for about 2 years, and the strength when cutting in the cylindrical direction of the bag filter has dropped to about 30% of the new product, whereas the fluororesin fine particle and polyimide resin fine particle processed product are 3 years old. In use, the strength at cutting was close to 60% of the new product.

3.5DTEX(平均)のPTFE短繊維、2.2DTEXのポリイミド繊維短繊維重量比60:40の混合比で、実質塗布量30g/mとなる量をポリイミド樹脂・PTFE
樹脂混合液に混合させ、実施例1と同様目付が650g/mガラスの2重織の織布にコート塗布し乾燥後、280度にて2分間加熱乾燥させた。分散、フッ素系樹は高温でやわらかくなる特性があり、実施例1よりパルステスト機での目詰まりテストで性能の向上がみられた。
3.5DTEX (average) PTFE short fiber, 2.2DTEX polyimide fiber short fiber weight ratio of 60:40 mixing ratio of 30g / m 2 in polyimide resin / PTFE
The mixture was mixed with the resin mixed solution, coated onto a double woven fabric having a basis weight of 650 g / m 2 glass as in Example 1, dried, and then heated and dried at 280 ° C. for 2 minutes. Dispersion and fluorine-based trees have the property of softening at high temperatures. From Example 1, performance was improved in a clogging test using a pulse test machine.

100%PTFEからなる目付700g/mの濾材表面に、3.5DTEX(平均)のPTFE短繊維/9ミクロンのバサルトファイバー(混合比5:5)を、樹脂に対する混合比20%で、ポリテトラフルオロエチレンからなるフッ素系樹脂微粒子(粒径:約1μm)とポリ(N,N’− p−フェニレン−ピロメリット酸イミド)からなるポリイミド樹脂微粒子(粒径:約1μm)を重量比100:20で含む水分散液に含浸し、濾材表面に固形分20g/mを付着させた。水分のほとんどを蒸発させた後、200℃にて、30分間加熱し樹脂をキュアリングして、さらにPTFE溶融温度以上の330度ヒートセットをおこなった。 On the surface of a filter medium having a basis weight of 700 g / m 2 made of 100% PTFE, 3.5 DTEX (average) PTFE short fibers / 9 micron basalt fiber (mixing ratio 5: 5) is mixed with polytetra Fluorine-based resin fine particles (particle size: about 1 μm) made of fluoroethylene and polyimide resin fine particles (particle size: about 1 μm) made of poly (N, N′-p-phenylene-pyromellitic imide) in a weight ratio of 100: 20 The solid dispersion was impregnated in an aqueous dispersion containing 1 to allow a solid content of 20 g / m 2 to adhere to the surface of the filter medium. After most of the water was evaporated, the resin was cured by heating at 200 ° C. for 30 minutes, and then heat setting was performed at 330 ° C. above the PTFE melting temperature.

実施例4について常温および高温(180℃)時の滑り性、および耐摩耗性を評価した。比較例1として、ポリテトラフルオロエチレンに代えてブチルゴム等の混合品のフッ素系樹脂微粒子(粒径:約1μm)を用い、固形分100g/mを濾材表面に付着させ、水分がなくなるまで乾燥、180℃で10分間キュアリングした。 PTFEフィルタの高温時の寸法不安定が一部改善された。即ち、丈600cmの同一品 の半年使用(使用温度平均 180度C)比較で処理品の伸び3cmに過ぎず、無処理品の伸び25cmに対して大幅な改善があった。 Example 4 was evaluated for slip properties and wear resistance at normal temperature and high temperature (180 ° C.). As Comparative Example 1, fluorinated resin fine particles (particle size: about 1 μm) of a mixed product such as butyl rubber are used instead of polytetrafluoroethylene, and a solid content of 100 g / m 2 is adhered to the surface of the filter medium and dried until no moisture is present. And curing at 180 ° C. for 10 minutes. The dimensional instability of the PTFE filter at high temperature was partially improved. That is, compared with half-year use of the same product with a length of 600 cm (operating temperature average 180 ° C.), the treated product had an elongation of only 3 cm, and there was a significant improvement over the untreated product with an elongation of 25 cm.

本発明フィルタ(この場合は実施例2で得られたフィルタ)について滑り性(常温(25℃)及び高温(180℃))並びに耐磨耗性の評価を行った。滑り性は傾斜法により静摩擦係数を測定を測定して行った。また、耐磨耗性はJIS1096.8.17.3C法(テーパ形法)で基布が露出するまでの摩耗テストのこすり回数を測定して行った。比較例2として分散液中にPTFEの短繊維を含まないこと以外は実施例2と同様の処理を行い、表面にフッ素系樹脂及びポリイミド樹脂を処理したフィルタを得た。また、比較例3として三フッ化樹脂成分を1〜10%含んだ溶液を100〜300g/mにて濾材表面に塗布し、水分がなくなるまで乾燥し後、130〜180℃で3〜10分間樹脂をキュアリングすることにより得られたフィルタを調整した。測定結果を表1に示す。 The filter of the present invention (in this case, the filter obtained in Example 2) was evaluated for slipperiness (normal temperature (25 ° C.) and high temperature (180 ° C.)) and wear resistance. The slip property was measured by measuring the coefficient of static friction by the gradient method. Further, the abrasion resistance was measured by measuring the number of rubbing of the abrasion test until the base fabric was exposed by the JIS1096.88.17.3C method (taper type method). As Comparative Example 2, the same treatment as in Example 2 was carried out except that the dispersion did not contain PTFE short fibers to obtain a filter having a surface treated with a fluororesin and a polyimide resin. Further, as Comparative Example 3, a solution containing 1 to 10% of a trifluoride resin component was applied to the surface of the filter medium at 100 to 300 g / m 2 , dried until no water was left, and then 3 to 10 at 130 to 180 ° C. The filter obtained by curing the resin for minutes was prepared. The measurement results are shown in Table 1.

表1
本発明 比較例2 比較例3
滑り性(常温) ◎0.13 ◎0.16 ◎0.18
滑り性(高温時) ◎0.15 ◎0.17 ○0.29*1
耐摩耗性 ◎27000回 ○21000回 ×17000回
*1:幾分の樹脂軟化が認められた。
Table 1
Comparative Example 2 Comparative Example 3 of the present invention
Sliding property (room temperature) ◎ 0.13 ◎ 0.16 ◎ 0.18
Sliding property (at high temperature) ◎ 0.15 ◎ 0.17 ○ 0.29 * 1
Abrasion resistance ◎ 27000 times ○ 21000 times × 17000 times
* 1: Some softening of the resin was observed.

表1に示すように、本発明により滑り性及び耐磨耗性について優れた特性を得ることができることが分かった。   As shown in Table 1, it was found that excellent characteristics with respect to slipping and abrasion resistance can be obtained by the present invention.

本発明のフィルタ(実施例2のフィルタ)に濾過性能の確認試験を実施した。試験機はミニチュアのバグフィルタテスト機であった。テスト用ダストはフライアッシュ10種、濾過速度3.0m/min、ダスト濃度は10g/m 、テスト時間は7時間であった。比較としてゴア社製4427型PTFEメンブレンB(比較例4)、前記比較例2、無処理の生の濾材(比較例5)を同一条件にて試験した。結果を表2に示す。 A filter performance confirmation test was performed on the filter of the present invention (filter of Example 2). The testing machine was a miniature bug filter testing machine. The test dust was 10 types of fly ash, the filtration rate was 3.0 m / min, the dust concentration was 10 g / m 3 , and the test time was 7 hours. For comparison, Gore 4427 type PTFE membrane B (Comparative Example 4), Comparative Example 2, and untreated raw filter medium (Comparative Example 5) were tested under the same conditions. The results are shown in Table 2.





表2
ダスト通過量 濾過性能
本発明 極少量 ◎
比較例4 極少量 ◎
比較例2 少量 ○
比較例5 最初にダスト通過有 △




Table 2
Dust passage amount Filtration performance The present invention Very small amount ◎
Comparative Example 4 Very small amount ◎
Comparative Example 2 Small amount ○
Comparative Example 5 First with dust passing △

表2の目詰まりテストより本発明のフィルタはPTFEメンブレン(比較例4)と同等の濾過性能を有していることが分かった。   From the clogging test in Table 2, it was found that the filter of the present invention had a filtration performance equivalent to that of the PTFE membrane (Comparative Example 4).

この発明によれば、単に濾材表面樹脂コートしただけの場合と比較して、樹脂コートに加えて樹脂層に耐熱性短繊維を混入することにより、剥離性を向上させつつ、必要な濾過性能を確保する効果が奏される。   According to this invention, compared with the case where the filter medium surface is simply coated with a resin, by adding heat-resistant short fibers to the resin layer in addition to the resin coat, the required filtration performance is improved while improving the peelability. The effect to ensure is produced.

図1はこの発明のフィルタの表面構造を模式的に示す図である。FIG. 1 is a diagram schematically showing the surface structure of the filter of the present invention.

符号の説明Explanation of symbols

1…濾材
2…バインダ
3…フッ素系樹脂層
4…耐熱性短繊維






DESCRIPTION OF SYMBOLS 1 ... Filter medium 2 ... Binder 3 ... Fluorine-type resin layer 4 ... Heat-resistant short fiber






Claims (1)

濾材表面に耐熱性短繊維を耐熱性樹脂にて溶着してなり、前記耐熱性短繊維はシリカ系繊維としてのバサルトファイバー、耐熱イミド系繊維としてのポリイミド繊維から選ばれる一種以上であり、かつこれにポリテトラフルオロエチレン繊維が加えられて構成され、また、濾材表面の耐熱性樹脂はポリイミド樹脂よりなる第1層と、第1の樹脂層の上に固着形成されるフッ素系樹脂よりなる第2層とからなり、この第2層に前記耐熱性短繊維が埋め込まれているフィルタ。 A heat-resistant short fiber is welded to a filter medium surface with a heat-resistant resin, and the heat-resistant short fiber is at least one selected from basalt fiber as a silica-based fiber and polyimide fiber as a heat-resistant imide-based fiber. polytetrafluoroethylene fibers are constituted by added, also heat-resistant resin of the filter medium surface a first layer made of a polyimide resin, by a fluorine-based resin is fixed formed on the first resin layer Li Cheng first Ri Do from a two-layer, the heat-resistant staple fibers that are embedded filter to the second layer.
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