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JP4800643B2 - Cylindrical filter and manufacturing method thereof - Google Patents
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JP4800643B2 - Cylindrical filter and manufacturing method thereof - Google Patents

Cylindrical filter and manufacturing method thereof Download PDF

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JP4800643B2
JP4800643B2 JP2005076043A JP2005076043A JP4800643B2 JP 4800643 B2 JP4800643 B2 JP 4800643B2 JP 2005076043 A JP2005076043 A JP 2005076043A JP 2005076043 A JP2005076043 A JP 2005076043A JP 4800643 B2 JP4800643 B2 JP 4800643B2
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fiber
heat
nonwoven fabric
melting point
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庸輔 高井
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DaiwaboPolytecCo.,Ltd.
Daiwabo Holdings Co Ltd
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Description

本発明は流体を濾過するために用いられる筒状フィルターであり、主として、水、油、塗料、界面活性剤、食品などの液体の濾過や、圧縮空気中の金属粉などの塵埃、油滴や水分・ミストの除去、自動車の空気エレメントなどの気体の濾過に用いられる円筒状の筒状フィルターおよびその製造方法に関する。さらに詳しくは、濾過ライフが長く、耐圧強度が大きく、濾過精度が高い筒状フィルターおよびその製造方法に関する。   The present invention is a cylindrical filter used to filter a fluid, mainly filtering water, oil, paint, surfactant, food and other liquids, dust such as metal powder in compressed air, oil droplets, The present invention relates to a cylindrical tube filter used for removing moisture and mist, and filtering a gas such as an automobile air element, and a method for manufacturing the same. More specifically, the present invention relates to a cylindrical filter having a long filtration life, a high pressure resistance, and a high filtration accuracy, and a method for manufacturing the same.

濾過層の構成成分として繊維を用いた筒状タイプのフィルターは、通常、繊維で構成された濾過層が中空円筒状に形成され、目的とする濾過対象物が中空円筒の最外周部から中心部に集められて濾過するのに用いられるもので、特に液体の濾過に有用である。   A cylindrical type filter using fibers as a constituent component of the filtration layer is usually formed by forming a filtration layer made of fibers into a hollow cylindrical shape, and the target filtration object is from the outermost peripheral part of the hollow cylinder to the central part. And is used for filtering and is particularly useful for liquid filtration.

筒状フィルターは、液体が濾過層を通過する間にこの濾過層が液体中の微粒子を捕捉する構造になっている。そしてこの筒状フィルターは、製薬工業、電子工業等における精製水の濾過、或いは食品工業における飲料水製造工程内での液体濾過、自動車工業における塗装剤の濾過など、各種産業界において広く利用されている。   The cylindrical filter has a structure in which the filtration layer captures fine particles in the liquid while the liquid passes through the filtration layer. This cylindrical filter is widely used in various industries such as filtration of purified water in the pharmaceutical industry, electronics industry, etc., liquid filtration in the drinking water production process in the food industry, and filtration of coating agents in the automobile industry. Yes.

従来、上記のような分野に使用されてきた筒状フィルターとしては、例えば特許文献1や特許文献2にあるように、前者はステープル繊維をカードで、後者はスパンボンド不織布製造手法で、それぞれ開繊して熱接着性複合繊維のウェブとし、前記ウェブを加熱下で巻回し、複合繊維の低融点成分で熱接着して接着一体化して成型された筒状フィルターが開示されている。これらの筒状フィルターは、熱接着性複合繊維が使用されているために濾過圧の上昇によっても熱接着された繊維間の剥離が起こりにくいので、安定した濾過精度が得られるといった利点がある。   Conventionally, as a cylindrical filter used in the above fields, for example, as described in Patent Document 1 and Patent Document 2, the former is a staple fiber card, and the latter is a spunbond nonwoven fabric manufacturing method. A tubular filter is disclosed in which a web of a heat-adhesive conjugate fiber is formed by fibering, the web is wound under heating, and heat-bonded with a low melting point component of the conjugate fiber to be bonded and integrated. Since these cylindrical filters use heat-adhesive conjugate fibers, peeling between the heat-bonded fibers hardly occurs even when the filtration pressure is increased, so that there is an advantage that stable filtration accuracy can be obtained.

また、特許文献3には、メルトブロー紡糸をしながら繊維径を変化させて堆積して得られた極細複合繊維ウェブを熱処理して巻芯に巻き取り、その後巻芯を抜き取ることにより成型された筒型フィルターが開示されている。さらに、特許文献4には、繊維径や見かけ密度の異なる数種のメルトブローン不織布を、多孔芯筒の外側になるほど、平均繊維径、平均孔径の大きくなるように複数層巻き返してなる筒状フィルターが開示されている。一般的に、メルトブローン不織布を濾過層に使用した筒状フィルターは濾過精度がよく、製造工程も簡素化されるといった利点がある。   Further, Patent Document 3 discloses a cylinder formed by heat-treating an ultrafine composite fiber web obtained by changing the fiber diameter while performing melt blow spinning and winding it around a core, and then pulling out the core. A mold filter is disclosed. Furthermore, Patent Document 4 discloses a cylindrical filter in which several types of melt-blown nonwoven fabrics having different fiber diameters and apparent densities are rolled back so that the average fiber diameter and the average pore diameter become larger toward the outer side of the porous core cylinder. It is disclosed. In general, a cylindrical filter using a melt blown nonwoven fabric as a filtration layer has advantages that the filtration accuracy is good and the manufacturing process is simplified.

さらには、特許文献5には、熱融着性複合繊維を含む繊維集合層を熱融着する温度に加熱し、巻芯に巻き付け、引き続き所望の穴径を有するシート(例えば、濾紙、メンブレンフィルター等)を繊維集合層とともに巻き込んで精密濾過層を形成せしめ、引き続いて繊維集合層のみを巻き取って前濾過層を形成せしめ、冷却後巻芯を抜き取って、精密濾過用筒状フィルターを製造する方法が開示されている。
特開平52−152575号公報 特開平8−226064号公報 特開平5−96110号公報 特開平1−297113号公報 特公昭56−49605号公報
Furthermore, Patent Document 5 discloses a sheet (for example, filter paper, membrane filter) having a desired hole diameter after heating a fiber assembly layer containing a heat-fusible conjugate fiber to a temperature for heat-sealing, winding it around a core. Etc.) are wound together with the fiber assembly layer to form a microfiltration layer, and then only the fiber assembly layer is wound up to form a prefiltration layer, and after cooling, the winding core is pulled out to produce a cylindrical filter for microfiltration. A method is disclosed.
Japanese Patent Laid-Open No. 52-152575 JP-A-8-222604 JP-A-5-96110 JP-A-1-297113 Japanese Patent Publication No.56-49605

しかしながら、上記の従来の技術には、以下のような問題点があった。なお、説明を簡略化するため、以下の説明では液体濾過を主体に説明する。特許文献1では、構成繊維(ステープル繊維)同士が強固に熱接着されているために、高い濾過圧に対しての変形抵抗力はあるものの、繊維間に形成される空隙径分布範囲が狭いため、目詰まりが早く濾過ライフが比較的短いという問題があった。特許文献2のようにスパンボンド不織布製造手法で作られた繊維は、熱延伸されておらず腰のないウェブや不織布であり、熱接着させると前記したステープル繊維の不織布よりも薄くて繊維密度の高い不織布となって、これを巻回した筒状フィルターは、細かい粒子もきっちり取れて捕集精度の良いものであるが、筒状フィルターの表面で濾過する表面濾過の傾向がさらに強くなり、濾過面積も小さいためにさらに目詰まりが早く濾過ライフが比較的短いというフィルターとして重大な問題があった。   However, the above conventional techniques have the following problems. In addition, in order to simplify description, in the following description, it demonstrates focusing on liquid filtration. In Patent Document 1, since the constituent fibers (staple fibers) are firmly heat-bonded to each other, there is a deformation resistance against a high filtration pressure, but the void diameter distribution range formed between the fibers is narrow. There was a problem that clogging was quick and the filtration life was relatively short. The fiber made by the spunbond nonwoven fabric manufacturing method as in Patent Document 2 is a web or nonwoven fabric that is not heat stretched and has no waist, and is thinner than the staple fiber nonwoven fabric described above when thermally bonded. The cylindrical filter that is made of a high non-woven fabric and wound around it has fine collection of fine particles and has good collection accuracy, but the tendency of surface filtration to filter on the surface of the cylindrical filter is further increased, Since the area is small, there is a serious problem as a filter that clogging is quicker and the filter life is relatively short.

また、特許文献3及び特許文献4では、使用するメルトブローン不織布は1dtex以下の極細繊維で構成することができるために、繊維間空隙が小さくなり、濾過材として汎用されているが、その反面、濾過流量が小さくなり目詰まりが生じやすく濾過ライフが短くなるといった問題があった。   Moreover, in patent document 3 and patent document 4, since the melt blown nonwoven fabric to be used can be comprised by the ultrafine fiber of 1 dtex or less, the space | gap between fibers becomes small and is used widely as a filter material, On the other hand, filtration There was a problem that the flow rate was small and clogging was likely to occur, and the filtration life was shortened.

さらに、特許文献5では、熱融着繊維集合層の中に同一幅の精密濾過層を介在せしめてあり、その使用に当たっては、前濾過層である熱融着繊維集合層から精密濾過層に向かって濾過を行うのであるが、前濾過層は熱融着繊維で形成される空隙径の分布範囲が狭く、また精密濾過層が熱融着繊維層の中に強圧された状態で存在するめ、濾過材の表面濾過の傾向が強く、プリーツ折りフィルターのように濾過面積が大きくないため、濾過による目詰まりが比較的早くて濾過ライフが短いという問題点があった。   Further, in Patent Document 5, a microfiltration layer having the same width is interposed in the heat-bonding fiber assembly layer, and in use, the heat-bonding fiber assembly layer, which is the pre-filtration layer, is directed to the microfiltration layer. In the pre-filtration layer, the distribution range of the void diameter formed by the heat-sealing fiber is narrow, and the microfiltration layer exists in a state of being strongly pressed in the heat-sealing fiber layer. Since the surface filtration of the material is strong and the filtration area is not large like a pleated fold filter, there is a problem that clogging by filtration is relatively fast and the filtration life is short.

不織布を単純に紙管に巻き上げる時に生じる、巻き直径が小さい時は大きい時より張力が強くかかり、紙管中心部に巻かれた不織布は、外周に巻かれた不織布より厚みが薄くなる(へたる)現象を使い、一般に供されている熱接着して一体化した、熱接着性複合繊維からなるウェブまたは不織布を巻回して熱接着した筒状フィルターは、自然に中心部に近づくと徐々に繊維密度が高くなる繊維密度勾配が付き、中心の内筒部は外周部より繊維密度が高い状態に巻かれているため、一般に筒状フィルターは濾過ライフの長い深層濾過材と思われている。しかし、単に熱接着性複合繊維からなるウェブまたは不織布を巻回して熱接着して筒状フィルターを作っても、前記繊維密度勾配は十分とはいえず、筒状フィルターの表面で濾過する表面濾過現象が支配的で、捕集粒子による目詰まりが早く濾過ライフが短い問題が常につきまとっていた。   When a non-woven fabric is simply rolled up on a paper tube, when the winding diameter is small, the tension is stronger than when it is large, and the non-woven fabric wound around the center of the paper tube is thinner than the non-woven fabric wound around the outer circumference ) The cylindrical filter, which is a heat-bonded composite fiber or web made of heat-adhesive composite fibers, which is generally bonded by heat bonding using a phenomenon, is a fiber that gradually becomes closer to the center. Since the fiber density gradient which increases the density is attached and the central inner cylindrical part is wound in a state where the fiber density is higher than that of the outer peripheral part, the cylindrical filter is generally considered to be a deep-layer filtration material having a long filtration life. However, even if a cylindrical filter is made by simply winding a web or non-woven fabric made of heat-adhesive conjugate fibers and thermally bonding them, the fiber density gradient is not sufficient, and surface filtration that filters on the surface of the cylindrical filter The phenomenon was dominant, and the problem of fast clogging by collected particles and short filtration life was always present.

また、不織布などの扁平な繊維集合物をプリーツ折りして濾過表面積を極端に拡大したプリーツフィルターは濾過精度がよく、また濾過ライフの長い濾過材であるのに対し、繊維ウェブや不織布などの繊維集合物を筒状に巻上げながら繊維間を熱接着させたモールド型筒状フィルターに代表される深層濾過フィルターは、幾ら繊維密度勾配を付けても、プリーツフィルターに比べて濾過精度が劣り、濾過精度を向上させようとすると、濾過ライフが極端に低下するという問題があって、モールド型フィルターでは濾過精度と濾過ライフの両立は極めて困難であった。したがって、濾過ライフが長く、耐圧強度が大きく、濾過精度が高い筒状フィルターが得られていないのが実情であった。   In addition, a pleated filter with a pleat-folded flat fiber aggregate such as a nonwoven fabric that has an extremely expanded filtration surface area has good filtration accuracy and has a long filtration life. The depth filtration filter represented by a mold-type cylindrical filter in which the fibers are thermally bonded while winding the aggregate into a cylindrical shape is inferior in filtration accuracy compared to the pleated filter regardless of the fiber density gradient. When trying to improve the filtration life, there is a problem that the filtration life is extremely reduced, and it is extremely difficult to achieve both filtration accuracy and filtration life in the mold type filter. Accordingly, the fact is that a cylindrical filter having a long filtration life, a high pressure strength, and a high filtration accuracy has not been obtained.

本発明者らは、濾過不織布層の片側に、熱収縮繊維からなる熱収縮層が繊維交絡されて一体化した交絡不織布を熱処理して熱収縮繊維を収縮させて濾過不織布層を一種のプリーツ状とした多数の皺状物を有する多皺不織布状にし、これを巻回した筒状フィルターとすることにより、モールド型のフィルターでありながらプリーツ折りフィルターの特徴を持つ多層型深層濾過フィルターとすることで上記課題を解決した。すなわち、本発明の第1の筒状フィルターは、複数の繊維層からなる複層不織布が巻回された筒状体を含み、隣り合う複層不織布同士が熱接着されて成る筒状フィルターであって、前記複層不織布が、140℃における熱収縮率が9%以上の熱収縮繊維を含む熱収縮繊維層及び140℃における熱収縮率が4%以下の主体繊維を含む主体繊維層を含み、かつ複層不織布の少なくとも一方の表面を構成する繊維層が熱接着樹脂成分を含む熱接着性繊維を含み、前記熱収縮繊維と主体繊維の熱接着温度におけるそれぞれの熱収縮率の差が5%以上であることを特徴とする。   The present inventors, on one side of the filtration nonwoven fabric layer, heat-treating the entangled nonwoven fabric in which the heat-shrinkable layer made of heat-shrinkable fibers is integrated to heat-shrink the heat-shrinkable fibers to form a kind of pleated filter nonwoven fabric layer. A multi-layered depth filtration filter with the characteristics of a pleated fold filter while being a mold-type filter by forming a multi-layered nonwoven fabric having a large number of ridges and winding it into a cylindrical filter The above problem was solved. That is, the first cylindrical filter of the present invention is a cylindrical filter including a cylindrical body in which a multilayer nonwoven fabric composed of a plurality of fiber layers is wound, and adjacent multilayer nonwoven fabrics are thermally bonded. The multilayer nonwoven fabric includes a heat-shrinkable fiber layer containing a heat-shrinkable fiber having a heat shrinkage rate of 9% or more at 140 ° C and a main fiber layer containing a main fiber having a heat-shrinkage rate of 140% or less at 4%, And the fiber layer which comprises at least one surface of a multilayer nonwoven fabric contains the heat bondable fiber containing a heat bonding resin component, and the difference of each heat shrink rate in the heat bonding temperature of the said heat shrink fiber and a main fiber is 5% It is the above.

本発明の第2の筒状フィルターは、複数の繊維層からなる複層不織布が巻回された筒状体を含み、隣り合う複層不織布同士が熱接着されて成る筒状フィルターであって、前記複層不織布が、140℃における熱収縮率が9%以上の熱収縮繊維を含む熱収縮繊維層及び140℃における熱収縮率が4%以下の主体繊維を含む主体繊維層を含み、かつ複層不織布の少なくとも一方の表面を構成する繊維層が熱接着樹脂成分を含む熱接着性繊維を含み、前記複層不織布が、熱収縮により多数の皺状物を形成する多皺不織布であることを特徴とする。   The second tubular filter of the present invention is a tubular filter comprising a tubular body in which a multilayer nonwoven fabric composed of a plurality of fiber layers is wound, and adjacent multilayer nonwoven fabrics are thermally bonded to each other, The multilayer nonwoven fabric includes a heat-shrinkable fiber layer including a heat-shrinkable fiber having a heat shrinkage rate of 9% or more at 140 ° C. and a main fiber layer including a main fiber having a heat-shrinkage rate of 140% or less at 4%. The fiber layer constituting at least one surface of the layered nonwoven fabric includes heat-adhesive fibers containing a heat-adhesive resin component, and the multilayer nonwoven fabric is a multi-layered nonwoven fabric that forms a number of ridges by heat shrinkage. Features.

本発明の筒状フィルターの製造方法は、複数の繊維層からなる複層不織布が巻回された筒状体を含み、隣り合う複層不織布同士が熱接着されて成る筒状フィルターの製造方法であって、前記複層不織布が、140℃における熱収縮率が9%以上の熱収縮繊維を含む熱収縮繊維層及び140℃における熱収縮率が4%以下の主体繊維を含む主体繊維層を含み、かつ複層不織布の少なくとも一方の表面を構成する繊維層が熱接着樹脂成分を含む熱接着性繊維を含み、かつ熱収縮繊維と主体繊維の熱接着温度におけるそれぞれの熱収縮率の差が5%以上であり、前記複層不織布を、前記熱接着性繊維の熱接着樹脂成分の融点を5℃下回る温度以上に加熱して熱収縮繊維層を収縮させて多数の皺状物を形成させて多皺不織布を形成し、前記多皺不織布を前記熱接着性繊維の熱接着温度で加熱して熱接着しながら巻芯に巻き取り、巻き取られた前記複層不織布から前記巻芯を抜き取って、前記複層不織布が巻回された筒状体を形成することを特徴とする。   The manufacturing method of the cylindrical filter of the present invention is a manufacturing method of a cylindrical filter including a cylindrical body in which a multilayer nonwoven fabric composed of a plurality of fiber layers is wound, and adjacent multilayer nonwoven fabrics are thermally bonded. The multilayer nonwoven fabric includes a heat-shrinkable fiber layer containing a heat-shrinkable fiber having a heat shrinkage rate of 9% or more at 140 ° C. and a main fiber layer containing a main fiber having a heat shrinkage rate of 140% or less at 140 ° C. And the fiber layer which comprises at least one surface of a multilayer nonwoven fabric contains the heat-adhesive fiber containing a heat-bonding resin component, and the difference of each heat contraction rate in the heat-bonding temperature of a heat-shrink fiber and a main fiber is 5 %, And the multilayer nonwoven fabric is heated to a temperature lower than the melting point of the heat-adhesive resin component of the heat-adhesive fiber by 5 ° C. or more to shrink the heat-shrinkable fiber layer to form a large number of wrinkles. Forming a multi-layered nonwoven fabric, said multi-layered nonwoven fabric A cylindrical shape in which the multilayer nonwoven fabric is wound by winding the core from the multilayer nonwoven fabric wound around the core while being heated and bonded at the thermal bonding temperature of the thermal adhesive fiber. It is characterized by forming a body.

本発明の筒状フィルターは、多皺不織布がプリーツ状に濾過することを主体とする主体濾過層がなっており、しかも濾過ライフの長いプリーツ折りフィルターが多段に積層されたフィルターと同じ形態となっているため、従来のモールド型筒状フィルターよりも濾過精度が高くかつ濾過ライフが長い。特に、従来のモールド型筒状フィルターで、濾過精度を上げるため巻回の途中で濾過精度の高い不織布層を巻回して濾過精度を上げたフィルターに比べ、本発明の筒状フィルターは濾過面積が圧倒的に大きく、濾過ライフが長い。   The cylindrical filter of the present invention has a main filtration layer mainly composed of filtration of a multi-layered nonwoven fabric into a pleat shape, and has the same form as a filter in which pleated folded filters having a long filtration life are laminated in multiple stages. Therefore, the filtration accuracy is higher and the filtration life is longer than the conventional mold-type cylindrical filter. In particular, the tubular filter of the present invention has a filtration area larger than that of a conventional mold-type tubular filter, in which a non-woven fabric layer with high filtration accuracy is wound in the middle of winding to increase filtration accuracy, and the filtration accuracy is increased. Overwhelmingly large and long filtration life.

また、本発明の筒状フィルターは、繊維交絡を水流交絡加工によれば、繊維処理剤を水流交絡加工で水洗除去することができるので、繊維処理剤の残留が極めて少なく、残留量を0.05質量%以下とする、(溶出)不純物の極めて少ない筒状フィルターを得ることができる。このため、使用時に泡立ちが少ないので、本発明の筒状フィルターは、(溶出)不純物を嫌う食品、医薬品、半導体など電子機器部材の洗浄液の濾過用に好適である。   In addition, according to the cylindrical filter of the present invention, according to the hydroentanglement process, the fiber treatment agent can be washed and removed by the hydroentanglement process, so that the fiber treatment agent remains very little, and the residual amount is set to 0. A cylindrical filter having a very low (elution) impurity content of 05% by mass or less can be obtained. For this reason, since there is little foaming at the time of use, the cylindrical filter of this invention is suitable for filtration of the washing | cleaning liquid of electronic device members, such as a foodstuff, a pharmaceutical, and a semiconductor which dislike (elution) impurities.

本発明の筒状フィルターの製造方法によれば、熱接着温度で熱収縮差が5%以上有する熱収縮性繊維層と濾過することを主体とする主体繊維層の少なくとも2種類の繊維層が積層された複層不織布を、巻回する前の別工程で、または巻回するときの予熱工程で熱収縮繊維層を熱収縮させて、不織布の幅方向に延びているプリーツ状の多数の皺状物を有する多皺不織布を得ることができる。前記多皺不織布は、見かけ上繊維密度が低い嵩高不織布となっており、これを巻芯に巻き取ると、巻芯近傍は繊維密度が高く、外周は繊維密度が低い筒状フィルターを容易に得ることができる。   According to the method for producing a cylindrical filter of the present invention, at least two kinds of fiber layers, ie, a heat shrinkable fiber layer having a heat shrinkage difference of 5% or more at a heat bonding temperature and a main fiber layer mainly composed of filtration, are laminated. A plurality of pleated ridges extending in the width direction of the nonwoven fabric by heat-shrinking the heat-shrinkable fiber layer in a separate process before winding the wound multilayer nonwoven fabric or in a preheating process when winding A multi-layered nonwoven fabric having an object can be obtained. The multi-layered nonwoven fabric is a bulky nonwoven fabric with apparently low fiber density, and when this is wound around a core, a cylindrical filter having a high fiber density in the vicinity of the core and a low fiber density at the outer periphery can be easily obtained. be able to.

本発明者らは、鋭意検討した結果、主として濾過機能を有する主体繊維層と、熱収縮繊維を含む熱収縮繊維層を含む複数の繊維層から成る複層不織布を、熱処理して熱収縮繊維を収縮させることにより、濾過層を一種のプリーツ状の形態をなした多数の皺状物を有する多皺不織布とし、さらにこれを巻回することにより、一種のプリーツ折りフィルターが多層化したカートリッジフィルターとなして、モールド型のフィルターでありながらプリーツ折りフィルターの特徴を合わせ持つ多層型深層濾過フィルターとすることで課題を解決したのである。   As a result of intensive studies, the inventors of the present invention heat-treated a heat-shrinkable fiber by heat-treating a multilayer nonwoven fabric composed of a plurality of fiber layers including a main fiber layer mainly having a filtration function and a heat-shrinkable fiber layer containing heat-shrinkable fibers. By making the filter layer into a multi-layered nonwoven fabric having a large number of ridges in the form of a pleated shape, and further winding this, a cartridge filter in which a type of pleated folding filter is multilayered However, the problem was solved by using a multilayer type depth filtration filter having the characteristics of a pleated folding filter while being a mold type filter.

特に、主として濾過機能を有する主体繊維層は、濾過面積を大きくすると濾過ライフが長くなること、及び筒状フィルターの内径部が外周部より不織布が圧縮されて巻回されることにより繊維間距離が小さくなる、即ち繊維間隙が小さくなることから、遮断したい粒子径を遮断するプリーツ折りフィルターに用いられる不織布よりも少し繊維径が大きいもしくは繊維密度の小さい不織布(主体濾過層)と、その両表面に通液機能を要求する前記主体濾過層よりもさらに繊維径の大きい繊維で構成した不織布(通液層)を積層した繊維層であって、主体繊維層の片面に熱収縮繊維層を積層した複層不織布を加熱して収縮させて多皺不織布化すると共に、巻芯に巻き取った筒状フィルターとすると、巻芯近傍の複層不織布は強い張力を受けて押しつぶされ、繊維間隙が不織布の時よりもかなり小さくなった状態となる。その結果、複層不織布がプリーツ折りフィルターでの不織布より少し繊維径が大きいもしくは繊維密度の小さい不織布であっても、これらに相当する繊維間隙の不織布となってより微細な粒子を捕集できるようになる。   In particular, the main fiber layer mainly having a filtration function increases the filtration life when the filtration area is increased, and the inner fiber portion of the cylindrical filter is wound by compressing and winding the nonwoven fabric from the outer peripheral portion. Since the fiber gap is small, that is, the fiber gap is small, a nonwoven fabric (main filtration layer) having a slightly larger fiber diameter or lower fiber density than the nonwoven fabric used for the pleated fold filter that blocks the particle diameter to be blocked, A fiber layer obtained by laminating a nonwoven fabric (fluid layer) made of fibers having a fiber diameter larger than that of the main filtration layer that requires a liquid permeation function, wherein a heat shrink fiber layer is laminated on one side of the main fiber layer. When the layered nonwoven fabric is heated to shrink to form a multi-layered nonwoven fabric, and the cylindrical filter wound around the core, the multilayered nonwoven fabric in the vicinity of the core is pushed under strong tension. Busa is, fiber gap in a state of considerably smaller than when the non-woven fabric. As a result, even if the multilayer nonwoven fabric is a nonwoven fabric having a slightly larger fiber diameter or smaller fiber density than the nonwoven fabric in the pleated fold filter, it becomes a nonwoven fabric with a fiber gap corresponding to these so that finer particles can be collected. become.

また、見かけが嵩高である多皺不織布を巻回するので、繊維密度勾配を十分にとることができるため、筒状フィルターとしては深層濾過となる。そして、多皺化した通液層に挟まれた主体濾過層からなる主体繊維層は、一種のプリーツ折りフィルターであるため、徐々に繊維密度が大きくなるプリーツ折りフィルター多段濾過の状態を呈するので、従来のモールド型フィルターに比べ、目の細かい主体濾過層を持つので濾過精度が格段に高く、かつ濾過ライフも長い筒状フィルターとなるのである。   Moreover, since a multi-layered nonwoven fabric having a bulky appearance is wound, a sufficient fiber density gradient can be obtained, so that the cylindrical filter is a depth filtration. And since the main fiber layer consisting of the main filtration layer sandwiched between the multi-layered fluid-permeable layers is a kind of pleated fold filter, it exhibits a state of pleated fold filter multistage filtration in which the fiber density gradually increases, Compared with the conventional mold type filter, it has a finer main filtration layer, so that the filtration accuracy is remarkably high and the filtration life is long.

本発明の筒状フィルターは、具体的には、140℃における熱収縮率が9%以上の熱収縮繊維を含む熱収縮繊維層と、好ましくは少なくともその片面に140℃における熱収縮率が4%以下の主体繊維を含む主体繊維層とが積層された積層ウェブ(好ましくは、繊維交絡されて一体化した積層ウェブ)であり、熱収縮繊維と主体繊維の熱収縮差が熱接着温度で5%以上有する複層不織布であって、少なくとも一方の繊維層を構成する繊維が、熱接着樹脂成分を含む熱接着性繊維(好ましくは、熱接着樹脂成分である低融点熱可塑性樹脂と、繊維主体成分である高融点熱可塑性樹脂の融点差が10℃以上ある熱接着性複合繊維)であり、この熱接着性繊維を含む繊維層で少なくとも1表面を形成している複層不織布(好ましくは、水流交絡加工などの繊維交絡によって一体化させた複層不織布)を、前記熱接着性繊維の熱接着樹脂成分の融点を5℃下回る温度以上に加熱して、熱収縮繊維層を熱収縮させて、不織布の幅方向に延びているプリーツ状の多数の皺状物を形成する嵩高な多皺不織布とする。続いて、多皺不織布を構成する熱接着性繊維の熱接着樹脂成分の融点以上(熱接着性複合繊維の場合は、熱接着樹脂成分(低融点熱可塑性樹脂)の融点以上、高融点熱可塑性樹脂の融点−10℃未満)に加熱しながら巻回して、少なくとも熱接着樹脂成分で不織布間を熱接着して一体化することにより、フィルター外周がフィルター内部に比べ繊維密度が低く深層濾過ができ、かつ、多皺によるプリーツ形状の濾過層によって多段の精密濾過類似の濾過ができるようになした筒状フィルターを得ることができる。   Specifically, the cylindrical filter of the present invention has a heat-shrinkable fiber layer containing a heat-shrinkable fiber having a heat-shrinkage rate of 9% or more at 140 ° C, and preferably has a heat-shrinkage rate of 4% at 140 ° C on at least one surface thereof. A laminated web in which a main fiber layer containing the following main fibers is laminated (preferably a laminated web in which fibers are entangled and integrated), and the heat shrinkage difference between the heat shrinkable fibers and the main fibers is 5% at the heat bonding temperature. A multi-layer nonwoven fabric having at least one fiber layer in which at least one of the fiber layers is a heat-adhesive fiber containing a heat-adhesive resin component (preferably, a low-melting point thermoplastic resin that is a heat-adhesive resin component and a fiber-based component) A high-melting thermoplastic resin having a melting point difference of 10 ° C. or more, and a multilayer nonwoven fabric (preferably a water stream) having at least one surface formed of a fiber layer containing the thermo-adhesive fiber Confounding processing The multilayer nonwoven fabric integrated by which fiber entanglement) is heated to a temperature lower than the melting point of the heat-adhesive resin component of the heat-adhesive fiber by 5 ° C. or more to heat-shrink the heat-shrinkable fiber layer, and the width of the nonwoven fabric A bulky non-woven fabric that forms a large number of pleated ridges extending in the direction. Subsequently, the melting point of the heat-bonding resin component of the heat-bonding fiber constituting the multi-layered nonwoven fabric is equal to or higher than the melting point of the heat-bonding resin component (low-melting point thermoplastic resin in the case of a heat-bonding conjugate fiber), and the high-melting point thermoplasticity. The resin is melted at a melting point of less than −10 ° C.), and at least the non-woven fabric is thermally bonded and integrated with at least the thermo-adhesive resin component, so that the filter outer periphery has a lower fiber density than the inside of the filter and depth filtration is possible. In addition, it is possible to obtain a cylindrical filter that can perform filtration similar to multi-stage microfiltration with a pleated filter layer of multiple ridges.

本発明に用いられる複層不織布は、濾過機能を目的とした主体繊維層と、主体繊維層を多皺化するための熱収縮繊維層で構成されている。繊維層間は、水流交絡加工またはニードルパンチ加工などの繊維交絡手法で一体化しているものが好ましい。無論、主体繊維層が多層化している場合にあってはこれらが熱接着などの他の手段で一体化しているものであっても何ら不都合ではない。なお、フィルターでの使用を主目的としているので、前記繊維交絡手法には水流によって交絡させる水流交絡加工は、繊維表面に付着している繊維処理剤や構成する熱可塑性樹脂から発生するオリゴマーなどの不純物をも同時に除去できるので最も好ましい。   The multilayer nonwoven fabric used in the present invention is composed of a main fiber layer for the purpose of filtration and a heat-shrinkable fiber layer for increasing the number of main fiber layers. The fiber layers are preferably integrated by a fiber entanglement technique such as hydroentanglement or needle punching. Of course, when the main fiber layer is multi-layered, it is not inconvenient even if these are integrated by other means such as heat bonding. Since the main purpose is to use in a filter, the hydroentanglement process in which the fiber entanglement method is entangled by a water stream is a fiber treatment agent adhering to the fiber surface or an oligomer generated from a constituent thermoplastic resin. It is most preferable because impurities can be removed at the same time.

前記熱収縮繊維と主体繊維の熱接着温度におけるそれぞれの熱収縮率の差は、5%以上であり、好ましくは20%以上、より好ましくは30%以上である。ここで、「熱接着温度」とは、熱接着樹脂成分の融点−5℃から主体繊維の最も融点の高い樹脂の融点−10℃までの範囲において、熱収縮率の差が5%以上となる温度を任意に選択したものである。熱収縮率の差が5%未満では、複層不織布を収縮させても多皺化しにくい場合がある。一般に収縮加工は、140℃近辺で実施するため、収縮加工を想定して用いる繊維の熱収縮率を140℃で測定した値で規定した。この場合、上記した熱収縮率の差5%は、繊維の熱収縮率に置き換えると、主体繊維が4%以下とすると、熱収縮繊維は9%以上に熱収縮する必要がある。熱収縮繊維の具体例として、融点が138℃のブロック共重合的なプロピレン主体のランダム共重合体であるエチレン−プロピレン共重合体を3〜4倍延伸したエチレン−プロピレン共重合体繊維は、140℃でほぼ瞬間的に85%熱収縮(100mmが15mmとなる)する。また、前記エチレン−プロピレン共重合体を鞘成分とし、芯成分をポリプロピレン樹脂とした偏心鞘芯型複合繊維は、潜在捲縮性を有しており、130℃で激しい捲縮発生現象を起こして見かけの繊維長が約半分になる。これも本発明では熱収縮と見なしており、熱収縮率は約50%としている。   The difference in thermal shrinkage ratio between the heat shrinkable fiber and the main fiber at the heat bonding temperature is 5% or more, preferably 20% or more, more preferably 30% or more. Here, the “thermal bonding temperature” means that the difference in thermal shrinkage is 5% or more in the range from the melting point of the thermal bonding resin component to −5 ° C. to the melting point of the resin with the highest melting point of the main fiber to −10 ° C. The temperature is arbitrarily selected. If the difference in thermal shrinkage is less than 5%, it may be difficult to increase the number of layers even when the multilayer nonwoven fabric is contracted. In general, since shrinkage processing is performed at around 140 ° C., the thermal shrinkage rate of the fiber used assuming shrinkage processing is defined by a value measured at 140 ° C. In this case, if the difference 5% in the heat shrinkage rate described above is replaced with the heat shrinkage rate of the fiber, if the main fiber is 4% or less, the heat shrinkable fiber needs to be heat shrunk to 9% or more. As a specific example of the heat-shrinkable fiber, an ethylene-propylene copolymer fiber obtained by stretching an ethylene-propylene copolymer, which is a block copolymer-like propylene-based random copolymer having a melting point of 138 ° C., 3-4 times, 85% thermal shrinkage (100 mm becomes 15 mm) almost instantaneously at ° C. Moreover, the eccentric sheath-core type composite fiber having the ethylene-propylene copolymer as a sheath component and the core component as a polypropylene resin has latent crimping properties, and causes severe crimping phenomenon at 130 ° C. The apparent fiber length is halved. This is also regarded as heat shrinkage in the present invention, and the heat shrinkage rate is about 50%.

なお、一般の熱接着不織布に用いる繊維は、140℃における熱収縮率が4%未満であり、4%を超えると繊維の熱収縮による不織布の地合い低下と、熱接着強力が低下するため、ステープル繊維の製造の段階で熱収縮を抑制するための熱処理が行われているので、主体繊維はこれら汎用の熱接着性複合繊維から容易に選定することができ、無論、これに合わせた繊維を特別に作っても良いのは当然である。   In addition, the fiber used for a general heat-bonding nonwoven fabric has a heat shrinkage rate of less than 4% at 140 ° C., and if it exceeds 4%, the texture of the nonwoven fabric is lowered due to the heat shrinkage of the fiber, and the heat bond strength is reduced. Since heat treatment is performed to suppress thermal shrinkage at the fiber production stage, the main fiber can be easily selected from these general-purpose heat-adhesive conjugate fibers. It is natural that you can make it.

本発明に用いる主体繊維層は、単層であっても良いが、濾過を目的とする主体濾過層の少なくとも片面に、これより太い繊維からなる通液を目的とする通液層が配されている繊維層であるのが好ましく、主体濾過層の両面に通液層が配されている繊維層であることがより好ましい。これは、主体繊維層がプリーツ状に多皺化し、巻回して圧縮状態で熱接着して成形した時に、主体繊維層同士が隣り合って圧縮固定されると、濾過液などが通過しにくくなるためで、主体濾過層の前後に通液層があれば被濾過流体の通過がスムーズとなることと、濾過したものをトラップする場所を確保するためにも好ましいのである。また、主体繊維層の目付は、15〜100g/m2が都合良く、巻回後の不織布を熱線で切断する場合は、60g/m2以下が好ましい。また、主体繊維層が複数層で成る場合、主体濾過層は目付斑を生じ難い20g/m2以上が好ましい。 The main fiber layer used in the present invention may be a single layer, but at least one side of the main filter layer for filtration is provided with a liquid-pass layer for the purpose of passing a thicker fiber. The fiber layer is preferably a fiber layer, and more preferably a fiber layer in which a liquid-permeable layer is disposed on both sides of the main filtration layer. This is because when the main fiber layers are pleated into a pleated shape and wound and compressed and thermally bonded in a compressed state, if the main fiber layers are adjacent to each other and compressed and fixed, the filtrate or the like will not easily pass. Therefore, if there is a liquid-permeable layer before and after the main filtration layer, it is preferable for smooth passage of the fluid to be filtered and for securing a place for trapping the filtered material. Also, the basis weight of the main fiber layer is 15 to 100 / m 2 is conveniently if the nonwoven fabric after the winding is cut at heat rays is preferably 60 g / m 2 or less. Further, when the main fiber layer is composed of a plurality of layers, the main filtration layer is preferably 20 g / m 2 or more which is less likely to cause spotted spots.

また、熱収縮繊維層は、用いる熱収縮繊維の熱応力にもよるが、目付が15〜50g/m2であることが好ましく、所望の多皺化となる最少の目付に通常設定するとよい。なお、熱収縮させながら筒状フィルターを成形する時またはその後に熱収縮繊維を溶融させて不織布間の熱接着に用いることも合理的であり、好ましい。 Further, the heat shrinkable fiber layer preferably has a basis weight of 15 to 50 g / m 2 depending on the thermal stress of the heat shrinkable fiber to be used, and is usually set to a minimum basis weight that achieves a desired increase in number. In addition, it is reasonable and preferable to melt the heat-shrinkable fiber and use it for heat-bonding between the nonwoven fabrics when forming the cylindrical filter while heat-shrinking.

本発明に用いる熱収縮繊維は、用いる主体繊維層の繊維にもよるが、1.7〜13dtexが都合良く、一般的にはカードを用いて開繊するので2〜6dtexが特に好ましい。また、本発明の熱収縮繊維として、使用する樹脂の溶融流動性の指標であるMFR(測定温度を230℃とする)が100g/10分を超えるポリプロピレン樹脂からなるスパンボンド不織布は熱収縮が大きい傾向があり、本発明の熱収縮繊維として用いることができる。なお、スパンボンド不織布においては、一般的に3dtex以下の細い繊維のスパンボンド不織布に高いMFRの樹脂が用いられ、熱収縮が大きい繊維となる。従って前記スパンボンド不織布を熱収縮繊維層として用いる場合は、主体繊維層の主体濾過層を構成する繊維は3dtex以下とするのが妥当である。なお、スパンボンド不織布メーカーによって使用される樹脂に差があって、スパンボンド不織布の熱収縮にメーカー間格差があるので、熱収縮について調査すれば容易に選定できる。また、スパンボンド不織布を熱収縮繊維層として用いる場合、エチレン−プロピレン共重合体のスパンボンド不織布を用いることも好ましく、エチレン−プロピレン共重合体を鞘成分とする複合繊維からなるスパンボンド不織布を用いると、不織布を複合化するため、熱接着加工する時、捲縮発現して嵩高化すると共に熱収縮も大きいので、利用価値が高い。   Although the heat-shrinkable fiber used in the present invention depends on the fiber of the main fiber layer to be used, 1.7 to 13 dtex is convenient, and generally 2 to 6 dtex is particularly preferable since it is opened using a card. Moreover, as a heat shrinkable fiber of the present invention, a spunbond nonwoven fabric made of a polypropylene resin having an MFR (measurement temperature of 230 ° C.), which is an index of the melt fluidity of the resin used, exceeds 100 g / 10 minutes has a large heat shrinkage. There is a tendency, and can be used as the heat-shrinkable fiber of the present invention. In spunbonded nonwoven fabrics, high MFR resin is generally used for spunbonded nonwoven fabrics of fine fibers of 3 dtex or less, resulting in fibers with large heat shrinkage. Therefore, when the spunbonded nonwoven fabric is used as a heat-shrinkable fiber layer, it is appropriate that the fibers constituting the main filtration layer of the main fiber layer be 3 dtex or less. In addition, since there is a difference in the resin used by the spunbond nonwoven fabric manufacturer and there is a difference between manufacturers in the heat shrinkage of the spunbond nonwoven fabric, it can be easily selected by investigating the heat shrinkage. Moreover, when using a spunbond nonwoven fabric as a heat-shrinkable fiber layer, it is also preferable to use a spunbond nonwoven fabric of an ethylene-propylene copolymer, and a spunbond nonwoven fabric composed of a composite fiber having an ethylene-propylene copolymer as a sheath component is used. Since the nonwoven fabric is composited, when it is heat-bonded, it is crimped to be bulky and has a large thermal shrinkage, so it has a high utility value.

前記主体繊維層は、主体濾過層と通液層の複数層、もしくは主体濾過層単独であることが好ましい。用いる主体繊維は、主体濾過層を主として構成する繊維、すなわち主体濾過層中で最も含有量の多い繊維のことであり、ステープル繊維、メルトブローン不織布、スパンボンド不織布、エアレイド不織布や合成繊維紙が好ましく用いられ、ステープル繊維にあっては、開繊工程を経る必要があるために、繊度は1〜100dtexに限定され、スパンボンド不織布とエアレイド不織布にあっては、0.5〜500dtex、メルトブローン不織布と合成繊維紙にあっては、その繊維直径を1〜100μmとする繊維が都合良く用いられる。なお、主体濾過層は地合いの良いものが特に好ましい。また、求める遮断粒子の大きさ(直径)をプリーツ折りフィルターを参考にして決定する場合、本発明の筒状フィルターは一種の多段濾過型プリーツ折りフィルターなので、相当するプリーツ折りフィルターで使用されている繊維より繊度が大きくかつ低目付の主体濾過層とすると圧力損失の上昇を抑制できて、都合が良い。また、前記熱収縮繊維層及び主体繊維層は、各繊維層をそれぞれ構成する繊維の繊度が相違し、いずれか一方が太繊度繊維で構成される太繊度繊維層を形成し、他方が細繊度繊維で構成される細繊度繊維層を形成しており、前記太繊度繊維層の平均繊度が細繊度繊維層の平均繊度の2倍以上であると、深層濾過効果が向上し、好ましい。   The main fiber layer is preferably a plurality of main filter layers and liquid-permeable layers, or a main filter layer alone. The main fibers to be used are fibers mainly constituting the main filtration layer, that is, fibers having the largest content in the main filtration layer, and staple fibers, meltblown nonwoven fabrics, spunbond nonwoven fabrics, airlaid nonwoven fabrics and synthetic fiber papers are preferably used. In the case of staple fibers, the fineness is limited to 1 to 100 dtex because it is necessary to go through an opening process, and in the case of spunbond nonwoven fabrics and airlaid nonwoven fabrics, 0.5 to 500 dtex, it is synthesized with meltblown nonwoven fabrics. For fiber paper, fibers having a fiber diameter of 1 to 100 μm are conveniently used. In addition, the main filtration layer is particularly preferably a good texture. In addition, when determining the size (diameter) of the required blocking particles with reference to a pleated fold filter, the cylindrical filter of the present invention is a kind of multi-stage filtration type pleated fold filter, so it is used in the corresponding pleated fold filter. A main filtration layer having a fineness greater than that of the fiber and having a low basis weight is advantageous because it can suppress an increase in pressure loss. The heat-shrinkable fiber layer and the main fiber layer have different finenesses of the fibers constituting each fiber layer, and either one forms a thick fineness fiber layer composed of thick fineness fibers, and the other has a fineness. A fine fiber layer composed of fibers is formed, and the average fineness of the thick fine fiber layer is more than twice the average fineness of the fine fine fiber layer, which is preferable because the depth filtration effect is improved.

前記主体繊維層が主体濾過層と通液層の複数層の場合、前記通液層を構成する繊維は、通液の目的からして、主体濾過層を構成する繊維よりも太くなして繊維の腰を高くし、繊維間隙を大きくする要求と巻回時のへたりを少なくする機能を持つ必要があり、同じ素材で作った場合では繊維の腰の有意差から、繊度で1.5倍以上太い繊維であることが好ましく、2倍以上の繊維がより好ましい。すなわち主体繊維層は、細繊度繊維を含む細繊度繊維層の両面に太繊度繊維を含む太繊度繊維層を配して成る三層構造であることが好ましい。この場合、細繊度繊維層が主体濾過層を形成し、太繊度繊維層が通液層を形成している。また、上記の様に繊維の腰は主体濾過層の繊維より大きいことが当然のことながら好ましいが、太過ぎるなどで主体濾過層を乱すものであっては良くない。一般に主体濾過層の繊維が3dtex以下の時は、通液繊維層の繊維を6dtex前後、5〜13dtexの時は10〜30dtexとする。15dtex以上ではその1.3以上の繊維を用いるのが普通である。しかし、通液層の繊維をより太い繊維としても主体濾過層を乱すものでなければ不都合ではない。また、熱収縮繊維が主体濾過層の繊維より細い場合においては、熱収縮繊維層の目付を少なくするなどの対応を行って、熱収縮繊維層がメインの濾過層となるのを防ぐのがより好ましいが、一般に熱収縮させた熱収縮繊維層は地合いが乱れるので、熱収縮繊維が主体濾過層の繊維より、繊度で半分以上であれば余り問題とならない。   When the main fiber layer is a plurality of layers including a main filtration layer and a liquid passage layer, the fibers constituting the liquid passage layer are made thicker than the fibers constituting the main filtration layer for the purpose of liquid passage. It is necessary to have a function to increase the waist, increase the fiber gap, and reduce the sag at the time of winding. When made of the same material, the fineness is 1.5 times or more due to a significant difference in the waist of the fiber A thick fiber is preferable, and a fiber twice or more is more preferable. That is, it is preferable that the main fiber layer has a three-layer structure in which a thick fine fiber layer containing thick fine fibers is arranged on both surfaces of a fine fine fiber layer containing fine fine fibers. In this case, the fine fineness fiber layer forms a main filtration layer, and the thick fineness fiber layer forms a liquid passing layer. Further, as described above, it is preferable that the waist of the fiber is larger than the fiber of the main filtration layer, but it is not good that the main filtration layer is disturbed by being too thick. Generally, when the fiber of the main filtration layer is 3 dtex or less, the fiber of the liquid-permeable fiber layer is around 6 dtex, and when it is 5 to 13 dtex, the fiber is 10 to 30 dtex. In the case of 15 dtex or more, it is usual to use a fiber of 1.3 or more. However, even if the fibers of the liquid passing layer are made thicker, it is not inconvenient unless the main filtration layer is disturbed. In addition, when the heat-shrinkable fibers are thinner than the fibers of the main filtration layer, it is better to take measures such as reducing the basis weight of the heat-shrinkable fiber layer to prevent the heat-shrinkable fiber layer from becoming the main filtration layer. In general, the heat-shrinkable fiber layer that has been heat-shrinked is disturbed in texture. Therefore, if the heat-shrinkable fiber has a fineness that is more than half that of the fiber of the main filtration layer, there is little problem.

なお、本発明に用いられる繊維は、繊維垂直断面が円形だけでなく、楕円や星型などの異型繊維や中空繊維であっても何ら不都合はなく、主体繊維にあっては分割型繊維も都合良く用いることができる。また、繊維を構成する素材は、ポリプロピレンやポリエチレン樹脂などのポリオレフィン樹脂、ポリエチレンテレフタレート樹脂やポリブチレンテレフタレート樹脂などのポリエステル樹脂、ナイロン6などのポリアミド樹脂などのホモポリマーや共重合体が好ましく用いられ、熱接着性複合繊維は具体的には、鞘成分を高密度ポリエチレン、中密度ポリエチレンや低密度ポリエチレンなどのポリエチレン、エチレン−プロピレン共重合体またはポリブテン−1とし、ポリプロピレンを芯成分とする、両成分の融点差が10℃以上ある芯鞘型複合繊維が都合良く、単一成分繊維の場合はポリプロピレン繊維が都合良く用いられる。   The fibers used in the present invention are not limited to circular fibers in the vertical cross section, and there are no inconveniences if the fibers are elliptical or star-shaped or hollow fibers, and split fibers are convenient for the main fibers. Can be used well. The material constituting the fiber is preferably a polyolefin resin such as polypropylene or polyethylene resin, a polyester resin such as polyethylene terephthalate resin or polybutylene terephthalate resin, or a homopolymer or copolymer such as polyamide resin such as nylon 6. Specifically, the heat-adhesive conjugate fiber has a sheath component of high-density polyethylene, polyethylene such as medium-density polyethylene and low-density polyethylene, ethylene-propylene copolymer or polybutene-1, and polypropylene as a core component. A core-sheath type composite fiber having a melting point difference of 10 ° C. or more is convenient, and in the case of a single component fiber, a polypropylene fiber is conveniently used.

主体繊維層及び/又は熱収縮繊維層で使用する熱接着性繊維は、熱接着樹脂成分を含む熱接着性繊維である。熱接着樹脂成分である低融点熱可塑性樹脂と繊維主体成分である高融点熱可塑性樹脂の融点差が10℃以上ある熱接着性複合繊維であることが好ましい。熱接着性複合繊維としては、低融点熱可塑性樹脂で繊維表面の過半が占められている偏心または同心の鞘芯型複合繊維が好ましく、芯成分の繊維断面形状は、円形、猫目型や、クローバー型などの円形でない異型であっても良い。更に、複合繊維では鞘成分は芯成分よりもその融点が少なくとも20℃低い樹脂を選ぶと熱接着加工上、より都合がよい。耐酸性、耐アルカリ性などの耐薬品性と耐腐食性を重視する分野のフィルターに最適な熱接着ポリオレフィン複合繊維では、鞘成分を高密度ポリエチレン、中密度ポリエチレンや低密度ポリエチレンなどのポリエチレン、エチレン−プロピレン共重合体またはポリブテン−1とし、ポリプロピレンを芯成分とする、両成分の融点差が10℃以上ある芯鞘型複合繊維が特に好ましく、単一成分スパンボンド不織布を併用する場合は、ポリプロピレン繊維が経済的に特に好ましい。   The heat-adhesive fiber used in the main fiber layer and / or the heat-shrinkable fiber layer is a heat-adhesive fiber containing a heat-adhesive resin component. It is preferably a heat-adhesive conjugate fiber having a melting point difference of 10 ° C. or more between a low-melting point thermoplastic resin that is a heat-bonding resin component and a high-melting point thermoplastic resin that is a fiber-based component. As the heat-adhesive conjugate fiber, an eccentric or concentric sheath-core type conjugate fiber in which a majority of the fiber surface is occupied by a low-melting point thermoplastic resin is preferable, and the fiber cross-sectional shape of the core component is circular, cat-eye type, A non-circular variant such as a clover shape may be used. Furthermore, in the case of a composite fiber, it is more convenient in terms of heat bonding processing to select a resin whose melting point is at least 20 ° C. lower than that of the core component. The heat-bonding polyolefin composite fiber is ideal for filters in fields where chemical resistance such as acid resistance and alkali resistance and corrosion resistance are important. Polyethylene such as high-density polyethylene, medium-density polyethylene and low-density polyethylene, and ethylene- A core-sheath type composite fiber having propylene copolymer or polybutene-1 and having polypropylene as a core component and having a melting point difference of 10 ° C. or more is particularly preferable. When a single-component spunbond nonwoven fabric is used in combination, polypropylene fiber is used. Is particularly preferred economically.

本発明の筒状フィルターは、流体の濾過に供するものであり、酸やアルカリに犯されない素材で構成すると汎用性が高い。その具体的な例は、熱収縮繊維が、融点を125〜140℃とするプロピレン主体のエチレン−プロピレン共重合体からなり、もう一方の繊維が熱接着性繊維、好ましくは熱接着性繊維がポリオレフィン樹脂からなる鞘芯型複合繊維であり、熱接着樹脂成分の融点がエチレン−プロピレン共重合体の融点以下である筒状フィルターであることが好ましい。   The cylindrical filter of the present invention is used for fluid filtration, and is highly versatile if it is made of a material that is not violated by acid or alkali. Specific examples thereof include a heat-shrinkable fiber made of a propylene-based ethylene-propylene copolymer having a melting point of 125 to 140 ° C., and the other fiber being a heat-adhesive fiber, preferably a heat-adhesive fiber being a polyolefin. It is a sheath-core type composite fiber made of a resin, and is preferably a cylindrical filter in which the thermal adhesive resin component has a melting point equal to or lower than the melting point of the ethylene-propylene copolymer.

また別の一例は、熱収縮繊維が、融点を125〜140℃とするプロピレン主体のエチレン−プロピレン共重合体とポリプロピレンの偏心鞘芯型またはサイドバイサイド型複合繊維からなり、もう一方の繊維が熱接着性繊維、好ましくはポリオレフィン樹脂からなる鞘芯型複合繊維であり、熱接着樹脂成分の融点がエチレン−プロピレン共重合体の融点以下である筒状フィルターであることが好ましい。   In another example, the heat-shrinkable fiber is composed of an ethylene-propylene copolymer mainly composed of propylene having a melting point of 125 to 140 ° C. and an eccentric sheath core type or side-by-side type composite fiber of polypropylene, and the other fiber is thermally bonded. It is preferably a cylindrical filter in which the melting point of the thermoadhesive resin component is equal to or lower than the melting point of the ethylene-propylene copolymer.

本発明の筒状フィルターは、塗料などの有機溶剤を含むものの濾過にも使用され、耐溶剤性が要求される用途には、熱収縮繊維が、融点を110〜160℃とする共重合ポリエステル樹脂を低融点成分とし、ポリエチレンテレフタレート樹脂またはポリブチレンテレフタレート樹脂を高融点成分とする偏心鞘芯型またはサイドバイサイド型ポリエステル系熱接着性複合繊維であり、主体繊維層を構成する主体繊維が融点を220℃以上とするポリエステル系繊維及び湿式紡糸または乾式紡糸のセルロースからなる繊維から選ばれる少なくとも一つの繊維である筒状フィルターが好ましく用いられる。   The cylindrical filter of the present invention is also used for filtration of organic solvents such as paints. For applications where solvent resistance is required, the heat-shrinkable fiber is a copolyester resin having a melting point of 110 to 160 ° C. Is an eccentric sheath core type or side-by-side type polyester-based heat-adhesive composite fiber having a low melting point component and polyethylene terephthalate resin or polybutylene terephthalate resin as a high melting point component. The main fiber constituting the main fiber layer has a melting point of 220 ° C. A cylindrical filter which is at least one fiber selected from the above-described polyester fibers and fibers made of wet-spun or dry-spun cellulose is preferably used.

また別の好ましい一例は、前記熱収縮繊維層を構成する熱収縮繊維が、融点を80〜160℃とする生分解性共重合ポリエステル樹脂を低融点成分とし、低融点成分の融点より10℃を超える生分解性ポリエステル樹脂を高融点成分とする偏心鞘芯型またはサイドバイサイド型の生分解性ポリエステル系熱接着性複合繊維であり、前記主体繊維層を構成する繊維が、湿式紡糸または乾式紡糸のセルロースからなる繊維である筒状フィルターである。   Another preferred example is that the heat-shrinkable fibers constituting the heat-shrinkable fiber layer have a biodegradable copolymer polyester resin having a melting point of 80 to 160 ° C. as a low melting point component, and 10 ° C. higher than the melting point of the low melting point component. An eccentric sheath-core type or side-by-side type biodegradable polyester-based heat-adhesive composite fiber having a high melting point component that exceeds the biodegradable polyester resin, and the fiber constituting the main fiber layer is cellulose of wet spinning or dry spinning It is a cylindrical filter which is the fiber which consists of.

また、熱収縮繊維が、融点を110〜160℃とする共重合ポリエステル樹脂を低融点成分とし、ポリエチレンテレフタレート樹脂またはポリブチレンテレフタレート樹脂とする偏心鞘芯型またはサイドバイサイド型ポリエステル系熱接着性複合繊維であり、主体繊維層を構成する主体繊維が、融点が180〜210℃である芳香族脂肪族ポリエステル樹脂を第1成分とし、融点が250℃以上の芳香族ポリエステル樹脂を第2成分とし、第1成分の少なくとも一部が繊維表面に露出した複合繊維を用いた筒状フィルターも好ましい一例である。   Further, the heat-shrinkable fiber is an eccentric sheath core type or side-by-side type polyester-based heat-adhesive composite fiber in which a copolymer polyester resin having a melting point of 110 to 160 ° C. is used as a low melting point component and polyethylene terephthalate resin or polybutylene terephthalate resin The main fiber constituting the main fiber layer has an aromatic aliphatic polyester resin having a melting point of 180 to 210 ° C. as a first component, an aromatic polyester resin having a melting point of 250 ° C. or higher as a second component, and a first component. A cylindrical filter using a composite fiber in which at least a part of the component is exposed on the fiber surface is also a preferred example.

前記筒状体の外周に巻回された外装不織布を更に含み、外装不織布は熱接着性繊維からなり、かつ前記筒状体の外周に熱接着されていることが好ましい。外装不織布は、筒状体の外周に粗濾過用の濾過材として用いられる。外装不織布を巻きつけ、接着一体化させるには、前記筒状体を巻き上げ用の回転装置に載置し、外装不織布を外周に巻いた後、回転させながら、外方より熱接着温度以上の温度を有する加熱体を押し当てて部分熱圧着するとよい。   It is preferable that the exterior nonwoven fabric wound further on the outer periphery of the said cylindrical body is further included, and an exterior nonwoven fabric consists of a heat bondable fiber, and is thermally bonded to the outer periphery of the said cylindrical body. The exterior nonwoven fabric is used as a filter material for rough filtration on the outer periphery of the cylindrical body. In order to wind and wrap the exterior nonwoven fabric, the tubular body is placed on a rotating device for winding, and the exterior nonwoven fabric is wound around the outer periphery and then rotated and rotated at a temperature equal to or higher than the thermal bonding temperature from the outside. It is good to perform partial thermocompression bonding by pressing a heating body having

本発明の筒状フィルターの製造方法は、まず、140℃における熱収縮率が9%以上の熱収縮繊維を含む熱収縮繊維層と、熱収縮率が4%以下の主体繊維を含む主体繊維層を準備する。そして熱収縮繊維層と主体繊維層を積層して複層不織布を形成させる。このとき、少なくとも一方の表面を構成する繊維層が熱接着樹脂成分を含む熱接着性繊維を含有させる。また、熱収縮繊維と主体繊維の熱接着温度におけるそれぞれの熱収縮率の差が5%以上となるように調整する。また複層不織布は、水流交絡加工またはニードルパンチ加工などの繊維交絡手法で一体化させるとよい。収縮加工したときに多数の皺状物を形成しやすいからである。   The method for producing a cylindrical filter of the present invention includes a heat-shrinkable fiber layer containing a heat-shrinkable fiber having a heat shrinkage rate of 9% or more at 140 ° C. and a main fiber layer containing a main fiber having a heat shrinkage rate of 4% or less. Prepare. The heat-shrinkable fiber layer and the main fiber layer are laminated to form a multilayer nonwoven fabric. At this time, the fiber layer which comprises at least one surface contains the heat bondable fiber containing a heat bond resin component. Moreover, it adjusts so that the difference of each heat contraction rate in the heat bonding temperature of a heat shrink fiber and a main fiber may be 5% or more. The multilayer nonwoven fabric may be integrated by a fiber entanglement technique such as hydroentanglement or needle punching. This is because it is easy to form a large number of ridges when contracted.

次いで、前記複層不織布は、加熱して熱収縮繊維層を収縮させて多数の皺状物を形成させて多皺不織布を形成する。このとき、前記熱接着性繊維の熱接着樹脂成分の融点を5℃下回る温度以上に加熱するとよい。さらに続いて、多皺不織布を構成する熱接着性繊維の熱接着温度に加熱しながら巻回して、少なくとも熱接着樹脂成分で不織布間を熱接着して一体化しながら巻き取り、モールド型の筒状体を成形することができる。好ましい熱接着温度は、熱接着樹脂成分の融点以上(熱接着性複合繊維の場合は、熱接着樹脂成分(低融点熱可塑性樹脂)の融点以上、高融点熱可塑性樹脂の融点−10℃未満)に加熱しながら巻回して、少なくとも熱接着樹脂成分で不織布間を熱接着して一体化しながら巻き取り、モールド型の筒状体を成形することができる。そして、巻き取られた複層不織布を必要に応じて冷却し、巻芯を抜き取って、複層不織布が巻回された筒状体を形成する。   Next, the multi-layer nonwoven fabric is heated to shrink the heat-shrinkable fiber layer to form a plurality of ridges to form a multi-layer nonwoven fabric. At this time, it is good to heat to the temperature below 5 degreeC below melting | fusing point of the thermobonding resin component of the said thermobonding fiber. Furthermore, it is wound while being heated to the heat bonding temperature of the heat-adhesive fibers constituting the multi-layered nonwoven fabric, and is wound while being integrally bonded by thermal bonding between the nonwoven fabrics with at least a heat-bonding resin component, and is molded into a cylindrical shape The body can be shaped. Preferred thermal bonding temperature is not less than the melting point of the thermoadhesive resin component (in the case of a thermoadhesive conjugate fiber, not less than the melting point of the thermoadhesive resin component (low melting thermoplastic resin) and the melting point of the high melting thermoplastic resin is less than −10 ° C.) It is wound while being heated, and the nonwoven fabric is heat-bonded at least with the heat-adhesive resin component and wound while being integrated to form a mold-shaped cylindrical body. Then, the wound multilayer nonwoven fabric is cooled as necessary, the core is removed, and a cylindrical body around which the multilayer nonwoven fabric is wound is formed.

本発明の筒状フィルターを図面でもって説明する。図1は、本発明に使用する多皺不織布の断面拡大図の一例である。140℃における熱収縮率が9%以上の熱収縮繊維を含む熱収縮繊維層1と、主体濾過層4の両面に通液層3,5を積層した主体繊維層2を積層し、加熱して熱収縮繊維層を収縮させて多数の皺状物6を形成させて複層不織布(多皺不織布)7を形成している。図2は、本発明における筒状体外周付近の筒状体断面拡大図の一例である。隣り合う複層不織布(多皺不織布)7は、折り重なるようにして熱接着されて筒状体8を形成している。   The cylindrical filter of the present invention will be described with reference to the drawings. FIG. 1 is an example of an enlarged cross-sectional view of a multi-layered nonwoven fabric used in the present invention. A heat-shrinkable fiber layer 1 containing heat-shrinkable fibers having a heat shrinkage rate of 9% or more at 140 ° C. and a main fiber layer 2 in which liquid-permeable layers 3 and 5 are laminated on both surfaces of the main filtration layer 4 are laminated and heated. The heat-shrinkable fiber layer is contracted to form a large number of ridges 6 to form a multilayer nonwoven fabric (multi-layer nonwoven fabric) 7. FIG. 2 is an example of an enlarged cross-sectional view of the cylindrical body near the outer periphery of the cylindrical body in the present invention. Adjacent multilayer nonwoven fabrics (multi-layered nonwoven fabrics) 7 are thermally bonded so as to be folded to form a cylindrical body 8.

以下、本発明の実施例について説明する。なお、本発明は、以下の実施例に限定されるものではない。なおここで各評価方法は次の方法による。   Examples of the present invention will be described below. The present invention is not limited to the following examples. Here, each evaluation method is as follows.

[熱収縮率]
(繊維の熱収縮率)
単繊維の熱収縮率は、10本束ねて2点間の長さが100mmに印を付けた捲縮を掛けてない繊維を金網のコップの底に吊るし、任意の温度に加熱した乾燥機に5秒間入れて、取り出して熱収縮後の長さを測定し、下記式で算出した。
熱収縮率(%)=[(100−熱収縮後の長さ)×100]/100
なお、乾熱収縮率はJISに準拠して1mg/dの加重を掛けて測定した。
[Heat shrinkage]
(Fiber thermal shrinkage)
The heat shrinkage rate of a single fiber is 10% bundled and the length between two points is marked as 100mm. The uncrimped fiber is hung on the bottom of a wire mesh cup and heated to an arbitrary temperature. It was put in for 5 seconds, taken out, measured for the length after heat shrinkage, and calculated by the following formula.
Heat shrinkage rate (%) = [(100−length after heat shrinkage) × 100] / 100
The dry heat shrinkage was measured by applying a weight of 1 mg / d according to JIS.

(不織布の熱収縮率)
140℃に加熱した熱風貫通型熱接着不織布加工機中で、コンベアに沿わせて試験不織布を繰出し、20秒間熱処理したとき、下記式で不織布の熱収縮率を算出した。
元の不織布幅をA(cm)とし、熱処理後の不織布の幅B(cm)とすると、
熱収縮率(%)=[100×(A−B)]/A
(Heat shrinkage of nonwoven fabric)
When the test nonwoven fabric was fed along the conveyor and heat-treated for 20 seconds in a hot-air penetrating thermal adhesive nonwoven fabric processing machine heated to 140 ° C., the thermal shrinkage rate of the nonwoven fabric was calculated by the following formula.
If the original nonwoven fabric width is A (cm) and the nonwoven fabric width B (cm) after heat treatment,
Thermal contraction rate (%) = [100 × (A−B)] / A

[繊維処理剤付着率]
JIS L 1015−7.22(6)のメタノール抽出分による。
[Fiber treatment agent adhesion rate]
According to the methanol extract of JIS L 1015-7.22 (6).

[濾過ライフ]
濃度200ppmに調製された試験用ダスト(JIS8種[中位径6.6〜8.6μmと11種[中位径1.6〜2.3μm]を1:1の質量割合で混合したもの、関東ローム製)の試験用懸濁液を均一に攪拌しながら筒状フィルターの外側から中空部に向かって15リットル/分の流量で流し、この流量を維持するための通水圧力が0.2MPaになったときの総通水量(リットル)で表す。
[Filtration life]
Test dust prepared to a concentration of 200 ppm (mixed JIS 8 types [median diameter 6.6 to 8.6 μm and 11 types [median diameter 1.6 to 2.3 μm] in a mass ratio of 1: 1, The suspension for test of Kanto Loam) was allowed to flow at a flow rate of 15 liters / minute from the outside of the cylindrical filter toward the hollow portion while stirring uniformly, and the water flow pressure for maintaining this flow rate was 0.2 MPa. Expressed as total water flow (liters) when

[濾過精度]
試験用懸濁液の所定量に含まれるダストの粒子径別の個数(M)と、これを濾過した後の液に残るダストの粒子径別の個数(N)を粒度分布測定機(商品名:コールターカウンターZM型:コールターエレクトロニクス社製)を用いて測定した。各粒子径別に下記式から遮断率を算出した。遮断率はある粒子径以上は100%になる。その直前の遮断率が99%になる粒子径(r)を濾過精度とした。
遮断率(%)=[(M−N)×100]/M
濾過精度はrが小さいほど微小な粒子をフィルターが補足できることを示す。
試験用懸濁液は、50ppmのJIS7種[中位径27〜31μm]とJIS8種[中位径6.6〜8.6μm]を1:1の質量割合で混合したダスト水分散液を、流速40リットル/分で濾過し、濾過開始後5分の濾過液について測定した。
[Filtration accuracy]
A particle size distribution measuring device (trade name) is used to determine the number (M) of each dust particle size contained in a predetermined amount of the test suspension and the number (N) of each dust particle size remaining in the liquid after filtration. : Coulter counter ZM type: manufactured by Coulter Electronics Co., Ltd.). The blocking rate was calculated from the following formula for each particle size. The blocking rate is 100% above a certain particle size. The particle diameter (r) at which the blocking rate immediately before that was 99% was defined as the filtration accuracy.
Blocking rate (%) = [(MN) × 100] / M
The filtration accuracy indicates that the smaller the r, the more fine particles can be captured by the filter.
The suspension for testing was a dust water dispersion in which 50 ppm of JIS 7 [median diameter 27 to 31 μm] and JIS 8 [median diameter 6.6 to 8.6 μm] were mixed at a mass ratio of 1: 1. Filtration was performed at a flow rate of 40 liters / minute, and the filtrate was measured for 5 minutes after the start of filtration.

[通水圧損]
水を流速40リットル/分で通水した時の、フィルターの入口、出口の圧力差を測定し、(KPa)で表示した。
[Water pressure loss]
The pressure difference between the inlet and outlet of the filter when water was passed at a flow rate of 40 liters / minute was measured and displayed in (KPa).

以下に、実施例および比較例で使用する繊維を示す。
(熱収縮繊維)
プロピレンが96質量%で、融点が136℃、230℃のMFRが15g/10分のエチレン−プロピレン共重合体(EP)を265℃で溶融紡糸し、90℃の熱水中で3.2倍に熱延伸し、続いて静電防止剤などを含む繊維処理剤を付与して、スタフィングボックスで機械捲縮をかけ、60℃のコンベア型熱風貫通型乾燥機で乾燥して51mmに切断した、4dtex(EP1繊維)、8dtex(EP2繊維)、及び15dtex(EP3繊維)のステープル繊維を用いた。上記EP1〜EP3繊維の熱収縮率は、130℃で45%(100mmが55mmとなった)、140℃で85%、そして150℃で92%の単繊維熱収縮率を示した。一方、JISに準拠した1mg/dの加重を掛ける乾熱収縮率は、4dtexのEP1繊維では、130℃で50%、140℃で70%、そして150℃で76%であった。また4dtexのEP1繊維の熱応力は、100℃で15gf/dtex、120℃で25gf/dtex、そして140℃で20gf/dtexであった。なお、これらEP繊維は、熱収縮させた後に150℃に暴露すると溶融した粒状となり、少しの押し圧をかけると熱接着に利用できる。
Below, the fiber used by an Example and a comparative example is shown.
(Heat shrink fiber)
An ethylene-propylene copolymer (EP) having a propylene content of 96% by mass, a melting point of 136 ° C. and an MFR of 230 ° C. of 15 g / 10 min was melt-spun at 265 ° C., and 3.2 times in hot water at 90 ° C. Next, a fiber treatment agent containing an antistatic agent or the like was applied, and mechanical crimping was applied with a stuffing box, followed by drying with a conveyor type hot air through dryer at 60 ° C. and cutting into 51 mm. Staple fibers of 4 dtex (EP1 fiber), 8 dtex (EP2 fiber), and 15 dtex (EP3 fiber) were used. The EP1 to EP3 fibers exhibited a single fiber heat shrinkage of 45% at 130 ° C. (100 mm became 55 mm), 85% at 140 ° C., and 92% at 150 ° C. On the other hand, the dry heat shrinkage applied with a load of 1 mg / d according to JIS was 50% at 130 ° C., 70% at 140 ° C., and 76% at 150 ° C. for 4 dtex EP1 fiber. The thermal stress of 4 dtex EP1 fiber was 15 gf / dtex at 100 ° C., 25 gf / dtex at 120 ° C., and 20 gf / dtex at 140 ° C. In addition, these EP fibers are melted granular when exposed to 150 ° C. after being thermally contracted, and can be used for thermal bonding when a little pressing pressure is applied.

(熱接着・熱収縮複合繊維)
熱接着・熱収縮複合繊維は、前記EP樹脂を芯成分とし、鞘成分に融点が122℃で190℃のMFRが20g/10分の直鎖状低密度ポリエチレンを用いて、複合断面積比が1:1の偏芯した鞘芯型複合繊維を前記EP繊維と同様にして6dtexのステープル繊維(EL繊維)とした。120℃と140℃の乾熱収縮率は、夫々10%と25%であった。なお、無加重下での単繊維熱収縮率は、140℃において35%であった。
(Heat bonding / heat shrinkable composite fiber)
The heat-bonding / heat-shrinkable composite fiber uses the above-mentioned EP resin as a core component, and the sheath component uses a linear low density polyethylene having a melting point of 122 ° C. and a 190 ° C. MFR of 20 g / 10 min. 1: 1 eccentric sheath-core type composite fibers were made into 6 dtex staple fibers (EL fibers) in the same manner as the EP fibers. The dry heat shrinkage rates at 120 ° C. and 140 ° C. were 10% and 25%, respectively. The single fiber heat shrinkage under no load was 35% at 140 ° C.

また、前記EP樹脂を50質量%と融点が138℃で230℃のMFRが12g/10分であるエチレン−プロピレン−ブテン−1の三元共重合体樹脂50質量%を混合した樹脂を用いて、前記EP繊維と全く同様にして4dtexのステープル繊維(EPB繊維)を作製した。140℃におけるその単繊維熱収縮率は30%であった。   Also, a resin obtained by mixing 50% by mass of the EP resin with 50% by mass of an ethylene-propylene-butene-1 terpolymer resin having a melting point of 138 ° C. and an MFR of 230 ° C. of 12 g / 10 min is used. A 4 dtex staple fiber (EPB fiber) was produced in exactly the same manner as the EP fiber. Its single fiber heat shrinkage at 140 ° C. was 30%.

比較例用に市販されているホモポリマーのポリプロピレン樹脂を60質量%と前記EP樹脂を40質量%混合したステープル繊維(PP繊維)をEP繊維と同様にして作製した。140℃におけるその単繊維熱収縮率は8%であった。   A staple fiber (PP fiber) in which 60% by mass of a homopolymer polypropylene resin commercially available for a comparative example and 40% by mass of the EP resin were mixed was prepared in the same manner as the EP fiber. Its single fiber heat shrinkage at 140 ° C. was 8%.

(潜在捲縮性繊維)
鞘成分として前記EP樹脂を50質量%と、芯成分として融点が163℃で230℃のMFRが30g/10分であるポリプロピレン樹脂を50質量%で大きく偏芯した鞘芯型の4dtexの複合繊維を、EP繊維と同様にしてステープル繊維(CPP繊維)とした。なお、延伸温度を60℃、延伸倍率を3.5倍とした。140℃におけるその単繊維熱収縮率は20%であり、激しく立体状の微細な捲縮が発生して、微細なコイルがさらに大きなコイル状に渦巻く、バイラテラル捲縮となった。
(Latent crimped fiber)
50% by mass of the EP resin as a sheath component, and a 4dtex composite fiber of a sheath core type in which a polypropylene resin having a melting point of 163 ° C. and an MFR of 230 ° C. of 30 g / 10 min as a core component is greatly eccentric at 50% by mass. Was made into staple fibers (CPP fibers) in the same manner as EP fibers. The stretching temperature was 60 ° C. and the stretching ratio was 3.5 times. The single fiber heat shrinkage rate at 140 ° C. was 20%, and severe three-dimensional fine crimps were generated, resulting in bilateral crimps in which the fine coils were swirled into a larger coil shape.

(熱接着性複合繊維)
ポリエチレン樹脂を鞘成分とし、芯成分をポリプロピレン樹脂とする熱接着性複合繊維(大和紡績(株)製、商品名NBF)を使用した。140℃におけるその単繊維熱収縮率は1%であった。
(Thermoadhesive conjugate fiber)
A heat-adhesive conjugate fiber (trade name NBF, manufactured by Daiwabo Co., Ltd.) having a polyethylene resin as a sheath component and a core component as a polypropylene resin was used. Its single fiber heat shrinkage at 140 ° C. was 1%.

(熱接着・分割性複合繊維)
ポリエチレン樹脂を1成分とし、もう1つの成分をポリプロピレン樹脂とする繊維断面が蜜柑の様に放射状となっているポリオレフィン樹脂のみでなる分割型繊維(大和紡績(株)製、DF7)を使用した。140℃におけるその単繊維熱収縮率は2%以下であった。
(Thermal bonding and splitting composite fiber)
A split type fiber (DF7, manufactured by Daiwabo Co., Ltd.) was used, which was composed of only a polyolefin resin in which the cross section of the fiber having a polyethylene resin as one component and the other component as a polypropylene resin was radial like mikan. The single fiber heat shrinkage at 140 ° C. was 2% or less.

また、ポリエチレンテレフタレート樹脂を1成分とし、もう1つの成分を前記したEP樹脂とする繊維断面が蜜柑の様に放射状となっている、熱によって分割できる熱分割性繊維(TF15)を使用した。140℃におけるその単繊維熱収縮率は2%以下であった。   Further, a heat-splitting fiber (TF15) that can be divided by heat and that has a fiber cross-section in a radial shape like tangerine, in which polyethylene terephthalate resin is one component and the other component is the above-described EP resin was used. The single fiber heat shrinkage at 140 ° C. was 2% or less.

(非熱接着性単一繊維)
ポリプロピレン樹脂からなるポリプロピレン繊維(PP繊維)を使用した。140℃におけるその単繊維熱収縮率は2%以下であった。
(Non-thermal adhesive single fiber)
Polypropylene fiber (PP fiber) made of polypropylene resin was used. The single fiber heat shrinkage at 140 ° C. was 2% or less.

(熱収縮を有するスパンボンド不織布)
三井化学(株)製の6dtex弱のポリプロピレンスパンボンド不織布(SB1)PK103を使用した。140℃における幅方向の熱収縮率は15%であった。
(Spunbond nonwoven fabric with thermal shrinkage)
Polypropylene spunbond nonwoven fabric (SB1) PK103 made by Mitsui Chemicals Co., Ltd. was used. The thermal contraction rate in the width direction at 140 ° C. was 15%.

(熱収縮を期待しないスパンボンド不織布)
チッソ(株)製のポリエチレン樹脂を鞘成分とし、芯成分をポリプロピレン樹脂とする熱接着性複合繊維の2dtexスパンボンド不織布(SB2)を使用した。140℃における長さ方向の熱収縮率は2%であった。
(Spunbond nonwoven fabric that does not expect thermal shrinkage)
A 2 dtex spunbonded non-woven fabric (SB2) of a heat-adhesive conjugate fiber using a polyethylene resin manufactured by Chisso Corporation as a sheath component and a core component as a polypropylene resin was used. The thermal contraction rate in the length direction at 140 ° C. was 2%.

[実施例1]
使用する繊維は、それぞれ別個にローラカードを用いて開繊してウェブとなした。まず、主体繊維層として、目付15g/m2の繊度2dtexのNBF(細繊度繊維)からなるカードウェブの両側に、それぞれ目付13g/m2の繊度6dtexのNBF(太繊度繊維)からなるカードウェブを積層して、細繊度繊維層が主体濾過層となるようにし、太繊度繊維層が通液層となるように、三層の積層ウェブとした。熱収縮繊維層として、目付15g/m2の繊度4dtexEP1繊維からなるカードウェブを使用し、熱収縮繊維層の上に主体繊維層(積層ウェブ)をネットコンベア上で積層して、4MPaの圧力水で、上下の両面から水流交絡加工し、厚みが約1mmの繊維交絡不織布(複層不織布)を作製した。この複層不織布を、スリット型吸引ボックスを用いて十分水切りした後に、135℃のネットコンベア式熱風貫通型乾燥機で、非拘束状態下、オーバーフィードさせて、乾燥と熱収縮加工を行い、EP1繊維が熱収縮して三層の積層ウェブに多数の皺状物を形成させた、目付が130g/m2で見かけの厚みが4mmの多皺不織布を作製した。
[Example 1]
The fibers used were individually opened using roller cards to form webs. First, a card web made of NBF (thick fine fiber) having a basis weight of 13 g / m 2 and a fineness of 6 dtex on both sides of a card web made of NBF (fine fine fiber) having a basis weight of 15 g / m 2 and a fineness of 2 dtex. Are laminated to form a three-layer laminated web so that the fine fiber layer becomes a main filtration layer and the thick fiber layer becomes a liquid-permeable layer. A card web made of 4 dtex EP1 fibers with a basis weight of 15 g / m 2 is used as the heat-shrinkable fiber layer. A main fiber layer (laminated web) is laminated on the heat-shrinkable fiber layer on a net conveyor, and pressure water of 4 MPa. Then, hydroentangled from both the upper and lower sides to produce a fiber entangled nonwoven fabric (multilayer nonwoven fabric) having a thickness of about 1 mm. After this multi-layered nonwoven fabric is sufficiently drained using a slit type suction box, it is over-feeded in a net conveyor type hot air penetration dryer at 135 ° C. in an unrestrained state, and dried and heat-shrinked. EP1 A multi-layered nonwoven fabric having a basis weight of 130 g / m 2 and an apparent thickness of 4 mm, in which the fibers were heat-shrinked to form a large number of ridges on a three-layer laminated web, was produced.

次いで、多皺不織布をカートリッジフィルターに巻き上げる機構を持った145℃に加熱した熱風貫通型乾燥機に通して外径が28mmの鉄製の巻芯に巻きつけて外径が60mmの巻回したモールド型筒状体を作製した。これを巻き上げた直後のまだ熱いうちに10mm毎に約1mmの高さに突出したリング状の周回した突起を持つ金属ローラーで圧迫して、周回した溝を持つカートリッジフィルターとして、多皺不織布の幅方向に伸びる切断面を圧着して仕上げを施し、長さ250mmに切断して、本発明の筒状フィルターを得た。得られた熱収縮繊維層を内巻きとするカートリッジフィルターの濾過精度は5μm、濾過ライフは700リットル、通水圧損は5KPaであり、従来の相当するモールド型カートリッジフィルターより濾過ライフと通水圧損の性能が向上したものになっていた。なお、熱収縮繊維層を外巻きとするカートリッジフィルターも作製して性能を評価したが、ほぼ同一の結果であった。   Next, the mold mold was wound around an iron core having an outer diameter of 28 mm by passing it through a hot air penetration type dryer heated to 145 ° C. having a mechanism for winding the multi-layered nonwoven fabric around the cartridge filter. A cylindrical body was produced. The width of the multi-layered non-woven fabric as a cartridge filter with a grooved groove by pressing it with a metal roller with a ring-shaped circumferential protrusion protruding to a height of about 1 mm every 10 mm while it is still hot The cut surface extending in the direction was pressed and finished, and cut to a length of 250 mm to obtain a cylindrical filter of the present invention. The obtained filter with the heat-shrinkable fiber layer as the inner winding has a filtration accuracy of 5 μm, a filtration life of 700 liters, and a water pressure loss of 5 KPa. The performance was improved. A cartridge filter having a heat-shrinkable fiber layer as an outer winding was also produced and performance was evaluated, but the results were almost the same.

[実施例2]
実施例1で、乾燥用のネットコンベア式熱風貫通型乾燥機とカートリッジフィルターに巻き上げる機構を持った145℃に加熱した熱風貫通型乾燥機を連結した装置を用いて、他の条件は実施例1と同様にして、収縮加工と熱接着加工を連続して行い、本発明の筒状フィルターを得た。実施例1と同様にして、熱収縮繊維層を外巻きとするものと内巻きとするものの評価をしたところ、実施例1とほぼ同一の性能であった。
[Example 2]
In Example 1, using a device in which a net conveyor type hot air penetrating dryer for drying and a hot air penetrating dryer heated to 145 ° C. having a mechanism for winding up on a cartridge filter were connected, other conditions were as in Example 1. In the same manner as described above, shrinkage processing and heat bonding processing were continuously performed to obtain a cylindrical filter of the present invention. In the same manner as in Example 1, when the outer shrinkage and the inner shrinkage of the heat-shrinkable fiber layer were evaluated, the performance was almost the same as in Example 1.

[実施例3]
実施例1の細繊度繊維に代え、繊度1dtexのNBF繊維を使用した以外は、実施例1と同様の方法で、熱収縮繊維層を内巻きとする本発明の筒状フィルターを得た。この熱収縮繊維層を内巻きとするカートリッジフィルターの濾過精度は4μm、濾過ライフは600リットル、通水圧損は6KPaであり、実施例1の筒状フィルターよりも濾過精度がさらに向上したものであった。
[Example 3]
A cylindrical filter of the present invention having a heat-shrinkable fiber layer as an inner winding was obtained in the same manner as in Example 1 except that NBF fibers having a fineness of 1 dtex were used instead of the fineness fibers of Example 1. The filtration accuracy of the cartridge filter having the heat-shrinkable fiber layer as the inner winding is 4 μm, the filtration life is 600 liters, and the water pressure loss is 6 KPa. The filtration accuracy is further improved as compared with the tubular filter of Example 1. It was.

[実施例4]
実施例1の各繊維に代えて、主体繊維層として、目付25g/m2の繊度10dtexのNBF(細繊度繊維)からなるカードウェブの両側に、それぞれ目付13g/m2の繊度15dtexのNBF(太繊度繊維)からなるカードウェブを積層して三層積層ウェブを使用し、熱収縮繊維層として、目付15g/m2の繊度15dtexEP3繊維からなるカードウェブを使用した以外は、実施例1と同様の方法で、熱収縮繊維層を内巻きとする本発明の筒状フィルターを得た。このカートリッジフィルターの濾過精度は15μm、濾過ライフは1600リットル、通水圧損は2KPaであった。
[Example 4]
Instead of each fiber of Example 1, as the main fiber layer, NBF with a fineness of 15 dtex with a basis weight of 13 g / m 2 and a fineness of 15 dtex on each side of the card web made of NBF (fine fineness fiber) with a fineness of 10 dtex with a basis weight of 25 g / m 2 Example 3 except that a three-layer laminated web is used by laminating card webs made of thick fine fibers) and a card web made of 15 dtex EP3 fibers having a basis weight of 15 g / m 2 is used as the heat-shrinkable fiber layer. By this method, the cylindrical filter of the present invention having the heat-shrinkable fiber layer as an inner winding was obtained. This cartridge filter had a filtration accuracy of 15 μm, a filtration life of 1600 liters, and a water pressure loss of 2 KPa.

[実施例5]
実施例1で使用した細繊度繊維に代えて、繊度2.5dtex、8分割型のDF7を使用して、水流交絡加工の水圧を7MPaに上げた以外は、実施例1と同様の方法で、熱収縮繊維層を内巻きとする本発明の筒状フィルターを得た。このカートリッジフィルターの濾過精度は2μm、濾過ライフは500リットル、通水圧損は7KPaであり、実施例3のカートリッジフィルターより濾過精度がさらに向上したものであった。
[Example 5]
Instead of the fine fiber used in Example 1, using a fineness of 2.5 dtex, DF7 of 8 split type, except that the hydroentangled water pressure was raised to 7 MPa, the same method as in Example 1, A cylindrical filter of the present invention having a heat-shrinkable fiber layer as an inner winding was obtained. The filtration accuracy of this cartridge filter was 2 μm, the filtration life was 500 liters, and the water pressure loss was 7 KPa. The filtration accuracy was further improved over the cartridge filter of Example 3.

[実施例6]
実施例1で使用した細繊度繊維に代えて、繊度2dtex、8分割型のTF15を使用した以外は、実施例1と同様の方法で、熱収縮繊維層を内巻きとする本発明の筒状フィルターを得た。このカートリッジフィルターは、水圧を実施例1と同様の4MPaとしたものの濾過精度は4μmであり、実施例5と類似の6MPaとしたものの濾過精度は3μmあり、圧損は5KPaと向上した。これは、極細繊維の半分が熱収縮したことに起因すると推定される。
[Example 6]
A cylindrical shape of the present invention having a heat-shrinkable fiber layer as an inner winding in the same manner as in Example 1 except that TF15 having a fineness of 2 dtex and an 8-split type is used in place of the fineness fiber used in Example 1. A filter was obtained. Although this cartridge filter had a water pressure of 4 MPa similar to that of Example 1, the filtration accuracy was 4 μm, while that of 6 MPa similar to Example 5 was 3 μm, the filtration accuracy was improved to 5 KPa. This is presumed to be caused by heat shrinkage of half of the ultrafine fibers.

[実施例7]
実施例1で使用した細繊度繊維層に代えて、目付20g/m2の繊度2dtexの複合繊維スパンボンド不織布SB2を使用した以外は、実施例1と同様の方法で、熱収縮繊維層を内巻きとする本発明の筒状フィルターを得た。性能は、実施例1とほぼ同様であった。
[Example 7]
In place of the fine fiber layer used in Example 1, a composite fiber spunbond nonwoven fabric SB2 having a basis weight of 20 g / m 2 and a fineness of 2 dtex was used. A cylindrical filter of the present invention to be wound was obtained. The performance was almost the same as in Example 1.

[実施例8]
実施例1で使用した細繊度繊維に代えて、目付20g/m2の繊度2dtexのポリプロピレン繊維(PP繊維)を使用した以外は、実施例1と同様の方法で、熱収縮繊維層を内巻きとする本発明の筒状フィルターを得た。性能は、実施例1とほぼ同様であった。
[Example 8]
The heat-shrinkable fiber layer was internally wound in the same manner as in Example 1 except that polypropylene fibers (PP fibers) having a basis weight of 20 g / m 2 and a fineness of 2 dtex were used instead of the fineness fibers used in Example 1. A cylindrical filter of the present invention was obtained. The performance was almost the same as in Example 1.

[実施例9]
実施例8の熱収縮繊維層に代えて、目付16g/m2の繊度6dtex弱のポリプロピレンスパンボンド不織布(SB1)PK103を使用した。このとき作製した多皺不織布は、不織布の長手方向に皺が伸びる形態で、難点は不織布幅を広くすると不織布幅方向において中央部にやや皺が入り難い点であるが、30cm幅ではほぼ均一な多皺を形成することができた。この30cm幅の多皺不織布を用いて、実施例8と同様の方法で、熱収縮繊維層を外巻きとする本発明の筒状フィルターを得た。得られたカートリッジフィルターの濾過精度は8μm、濾過ライフは800リットル、通水圧損は7KPaであり、従来の相当するモールド型カートリッジフィルターより濾過ライフと通水圧損の性能が向上したものであった。
[Example 9]
Instead of the heat-shrinkable fiber layer of Example 8, a polypropylene spunbond nonwoven fabric (SB1) PK103 having a basis weight of 16 g / m 2 and a fineness of slightly less than 6 dtex was used. The multi-woven fabric produced at this time is a form in which wrinkles extend in the longitudinal direction of the non-woven fabric, and the difficulty is that if the width of the nonwoven fabric is widened, wrinkles are not likely to enter the central part in the width direction of the nonwoven fabric, but it is almost uniform at 30 cm width. It was possible to form a cocoon. Using this 30 cm wide multi-layered nonwoven fabric, a cylindrical filter of the present invention having a heat-shrinkable fiber layer as an outer winding was obtained in the same manner as in Example 8. The obtained cartridge filter had a filtration accuracy of 8 μm, a filtration life of 800 liters, and a water passage pressure loss of 7 KPa. The performance of the filtration life and water passage pressure loss was improved as compared with the conventional mold-type cartridge filter.

[実施例10]
実施例1の熱収縮繊維層に代えて、繊度4dtexの潜在捲縮性繊維(CPP繊維)を使用した以外は、実施例1と同様の方法で、多皺不織布を作製した。この多皺不織布は、多皺化だけでなく熱収縮繊維層も少し伸び加減の微細なクリンプが集まったものになっており、張力をかけないように繊維を加熱したコンベア上で熱収縮繊維層を外側としてそのまま巻き上げて、本発明の筒状フィルターを得た。これを評価したところ、実施例1よりも深層濾過効果が大きく、濾過ライフは900リットルであった。
[Example 10]
In place of the heat-shrinkable fiber layer of Example 1, a multi-woven fabric was produced in the same manner as in Example 1 except that latent crimpable fibers (CPP fibers) having a fineness of 4 dtex were used. This multi-layered nonwoven fabric is not only multi-layered but also a heat-shrinkable fiber layer that is a collection of fine crimps that stretch slightly, and heat-shrinkable fiber layer on a conveyor heated to prevent tension As a result, the cylindrical filter of the present invention was obtained. When this was evaluated, the depth filtration effect was larger than in Example 1, and the filtration life was 900 liters.

[実施例11]
実施例1において、熱収縮繊維層の上に目付20g/m2の繊度2dtexのNBF繊維ウェブ層を乗せ、さらに繊度4dtexのNBF繊維ウェブ層を積層した三層重ねのウェブとし、実施例1と同様の方法で、本発明の筒状フィルターを得た。得られたカートリッジフィルターの濾過精度は6μm、濾過ライフは700リットル、通水圧損は7KPaであった。
[Example 11]
In Example 1, an NBF fiber web layer having a basis weight of 20 g / m 2 and a fineness of 2 dtex was placed on the heat-shrinkable fiber layer, and an NBF fiber web layer having a fineness of 4 dtex was laminated to form a three-layered web. A cylindrical filter of the present invention was obtained by the same method. The resulting cartridge filter had a filtration accuracy of 6 μm, a filtration life of 700 liters, and a water pressure loss of 7 KPa.

[実施例12]
実施例11において、熱収縮繊維を8dtexのEP2繊維に代えて、4dtexのNBF繊維に代えて8dtexのNBF繊維を使用した以外は、実施例11と同様の方法で、本発明の筒状フィルターを得た。得られたカートリッジフィルターの濾過精度は6μm、濾過ライフは800リットル、通水圧損は6KPaであった。
[Example 12]
In Example 11, the tubular filter of the present invention was prepared in the same manner as in Example 11 except that the heat-shrinkable fiber was replaced with 8 dtex EP2 fiber and 8 dtex NBF fiber was used instead of 4 dtex NBF fiber. Obtained. The resulting cartridge filter had a filtration accuracy of 6 μm, a filtration life of 800 liters, and a water pressure loss of 6 KPa.

[実施例13]
目付15g/m2の繊度4dtexの熱収縮繊維EP1の繊維ウェブの上に、目付30g/m2の繊度2dtexのNBF繊維ウェブを積層し、3MPaの圧力水で実施例1と同様の方法で乾燥した図1に示す厚み2mmの水流交絡不織布とした。これを、熱収縮繊維層を外側として巻回して、本発明の筒状フィルターを得た。得られたカートリッジフィルターの濾過精度は13μm、濾過ライフは600リットル、通水圧損は10KPaであった。
[Example 13]
An NBF fiber web with a basis weight of 30 g / m 2 and a fineness of 2 dtex is laminated on the fiber web of heat-shrinkable fiber EP1 with a basis weight of 15 g / m 2 and a fineness of 4 dtex, and dried in the same manner as in Example 1 with 3 MPa pressure water. The hydroentangled nonwoven fabric having a thickness of 2 mm shown in FIG. This was wound with the heat-shrinkable fiber layer as the outside to obtain a cylindrical filter of the present invention. The resulting cartridge filter had a filtration accuracy of 13 μm, a filtration life of 600 liters, and a water pressure loss of 10 KPa.

[比較例1]
目付40g/m2の繊度2dtexのNBF繊維ウェブを、3MPaの圧力水で実施例1と同様の方法で乾燥した水流交絡不織布とし、これを巻回してカートリッジフィルターとした。得られたカートリッジフィルターの濾過精度は15μm、濾過ライフは400リットル、通水圧損は13KPaであった。
[Comparative Example 1]
An NBF fiber web having a basis weight of 40 g / m 2 and a fineness of 2 dtex was made into a hydroentangled nonwoven fabric dried by 3 MPa pressure water in the same manner as in Example 1, and this was wound to obtain a cartridge filter. The resulting cartridge filter had a filtration accuracy of 15 μm, a filtration life of 400 liters, and a water pressure loss of 13 KPa.

[比較例2]
目付20g/m2の繊度2dtexの複合繊維スパンボンド不織布SB2を、実施例1に準じて直接巻回してカートリッジフィルターとした。得られたカートリッジフィルターは堅く巻かれて、比較例の1.3倍を超える重さとなり、これを評価したところ、カートリッジフィルターの表面に濾過物が薄く付着している表層濾過であり、その濾過精度は5μmと高いが、濾過ライフは100リットル、通水圧損は18KPaであった。
[Comparative Example 2]
A composite fiber spunbonded nonwoven fabric SB2 having a basis weight of 20 g / m 2 and a fineness of 2 dtex was directly wound in accordance with Example 1 to obtain a cartridge filter. The obtained cartridge filter was tightly wound and weighed 1.3 times that of the comparative example. When this was evaluated, it was a surface layer filtration in which the filtrate was thinly attached to the surface of the cartridge filter. The accuracy was as high as 5 μm, but the filtration life was 100 liters, and the water pressure loss was 18 KPa.

これらの筒状フィルターを、その一部を削り取って、繊維処理剤(界面活性剤)の付着の有無を、界面活性剤付着率を測定するメタノール抽出した結果、概ね全てで、0.05質量%未満の質量減少を生じたが、これらの大半は、繊維表面に析出したオリゴマーによるものと推定される。なお、実際に通水しても通過液の発泡は全くなかった。   Part of these cylindrical filters are scraped off, and the presence or absence of the fiber treatment agent (surfactant) is extracted with methanol to measure the surfactant adhesion rate. It was estimated that most of these were due to oligomers deposited on the fiber surface, although less than mass loss occurred. In addition, even if it actually flowed through, there was no foaming of the passage liquid at all.

実施例の筒状フィルターを実際に茶色の粉体を使用して、通水圧力が0.2MPaになるまで濾過したところ、中心の空洞近くまで、茶色に着色していた。一方、比較例1のものは、外周から5mmほどまでしか着色しておらず、実施例の筒状フィルターは、比較例1に比べてより深層濾過されていることを確認できた。   When the cylindrical filter of the example was actually filtered using a brown powder until the water flow pressure became 0.2 MPa, it was colored brown to the vicinity of the central cavity. On the other hand, the thing of the comparative example 1 was colored only about 5 mm from the outer periphery, and it has confirmed that the cylindrical filter of an Example was deeply filtered compared with the comparative example 1. FIG.

本発明の筒状フィルターは、特に、製薬工業、電子工業で使用される精製水の濾過や、食品工業におけるアルコール飲料の製造工程における濾過、更には自動車工業における塗装剤の濾過など様々な用途に経済的に使用することが可能である。   The cylindrical filter of the present invention is used in various applications such as filtration of purified water used in the pharmaceutical industry and electronics industry, filtration in the production process of alcoholic beverages in the food industry, and filtration of coating agents in the automobile industry. It can be used economically.

本発明に使用する多皺不織布の断面拡大図の一例である。It is an example of the cross-sectional enlarged view of the multi-layered nonwoven fabric used for this invention. 本発明における筒状体外周付近の筒状体断面拡大図の一例である。It is an example of the cylindrical body cross-sectional enlarged view of the cylindrical body outer periphery vicinity in this invention.

符号の説明Explanation of symbols

1 熱収縮繊維層
2 主体繊維層
3、5 通液層
4 主体濾過層
6 皺状物
7 複層不織布(多皺不織布)
8 筒状体
DESCRIPTION OF SYMBOLS 1 Heat-shrinkable fiber layer 2 Main fiber layer 3, 5 Liquid passing layer 4 Main filtration layer 6 Saddle 7 Multi-layer non-woven fabric
8 Cylindrical body

Claims (11)

複数の繊維層からなる複層不織布が巻回された筒状体を含み、隣り合う複層不織布同士が熱接着されて成る筒状フィルターであって、
前記複層不織布が、140℃における熱収縮率が9%以上の熱収縮繊維を含む熱収縮繊維層及び140℃における熱収縮率が4%以下の主体繊維を含む主体繊維層を含み、かつ複層不織布の少なくとも一方の表面を構成する繊維層が熱接着樹脂成分を含む熱接着性繊維を含み、
前記複層不織布が、熱収縮により多数の皺状物を形成する多皺不織布であり、
少なくとも前記熱接着樹脂成分で前記複層不織布間を熱接着により一体化してなる筒状フィルター。
A cylindrical filter comprising a cylindrical body wound with a multilayer nonwoven fabric composed of a plurality of fiber layers, wherein adjacent multilayer nonwoven fabrics are thermally bonded to each other,
The multilayer nonwoven fabric includes a heat-shrinkable fiber layer including a heat-shrinkable fiber having a heat shrinkage rate of 9% or more at 140 ° C. and a main fiber layer including a main fiber having a heat-shrinkage rate of 140% or less at 4%. The fiber layer constituting at least one surface of the layer nonwoven fabric includes a thermoadhesive fiber containing a thermoadhesive resin component,
The multilayer nonwoven fabric, Ri Tashiwa nonwoven der to form multiple wrinkle-like material by thermal contraction,
Cylindrical filter ing and integrated by thermal bonding between the multilayer nonwoven fabric in at least the heat-adhesive resin component.
前記熱接着性繊維が、熱接着成分である低融点熱可塑性樹脂と、繊維主体成分である高融点熱可塑性樹脂を含み、その融点差が10℃以上有する熱接着性複合繊維である、請求項1に記載の筒状フィルター。 The thermoadhesive fiber is a thermoadhesive conjugate fiber that includes a low-melting-point thermoplastic resin that is a thermal-adhesive component and a high-melting-point thermoplastic resin that is a fiber-based component, and has a melting point difference of 10 ° C or more. cylindrical filter according to 1. 前記熱収縮繊維層を構成する熱収縮繊維が、融点を110〜160℃とする共重合ポリエステル樹脂を低融点成分とし、ポリエチレンテレフタレート樹脂またはポリブチレンテレフタレート樹脂を高融点成分とする偏心鞘芯型またはサイドバイサイド型ポリエステル系熱接着性複合繊維であり、
前記主体繊維層を構成する繊維が、融点を220℃以上とするポリエステル系繊維、及び湿式紡糸または乾式紡糸のセルロースからなる繊維から選ばれる少なくとも一つの繊維である、請求項1又は2に記載の筒状フィルター。
The heat-shrinkable fiber constituting the heat-shrinkable fiber layer is an eccentric sheath core type in which a copolyester resin having a melting point of 110 to 160 ° C. is a low melting point component, and a polyethylene terephthalate resin or polybutylene terephthalate resin is a high melting point component It is a side-by-side polyester thermal adhesive composite fiber,
Fibers constituting the main fiber layer is at least one fiber selected from polyester fibers, and fibers of cellulose wet spinning or dry spinning of a melting point and 220 ° C. or higher, according to claim 1 or 2 Tubular filter.
前記熱収縮繊維層を構成する熱収縮繊維が、融点を80〜160℃とする生分解性共重合ポリエステル樹脂を低融点成分とし、低融点成分の融点より10℃を超える生分解性ポリエステル樹脂を高融点成分とする偏心鞘芯型またはサイドバイサイド型の生分解性ポリエステル系熱接着性複合繊維であり、
前記主体繊維層を構成する繊維が、湿式紡糸または乾式紡糸のセルロースからなる繊維である、請求項1又は2に記載の筒状フィルター。
The heat-shrinkable fiber constituting the heat-shrinkable fiber layer comprises a biodegradable copolymer polyester resin having a melting point of 80 to 160 ° C. as a low melting point component, and a biodegradable polyester resin having a melting point of 10 ° C. higher than the melting point of the low melting point component. It is an eccentric sheath core type or side-by-side type biodegradable polyester-based heat-adhesive conjugate fiber with a high melting point component,
The cylindrical filter according to claim 1 or 2 , wherein the fiber constituting the main fiber layer is a fiber made of wet-spun or dry-spun cellulose.
前記熱収縮繊維層を構成する熱収縮繊維が、融点を110〜160℃とする共重合ポリエステル樹脂を低融点成分とし、ポリエチレンテレフタレート樹脂またはポリブチレンテレフタレート樹脂を高融点成分とする偏心鞘芯型またはサイドバイサイド型ポリエステル系熱接着性複合繊維であり、
前記主体繊維層を構成する繊維が、融点が180〜210℃である芳香族脂肪族ポリエステル樹脂を第1成分とし、融点が250℃以上の芳香族ポリエステル樹脂を第2成分とし、第1成分の少なくとも一部が繊維表面に露出した複合繊維である、請求項1又は2に記載の筒状フィルター。
The heat-shrinkable fiber constituting the heat-shrinkable fiber layer is an eccentric sheath core type in which a copolyester resin having a melting point of 110 to 160 ° C. is a low melting point component, and a polyethylene terephthalate resin or polybutylene terephthalate resin is a high melting point component It is a side-by-side polyester thermal adhesive composite fiber,
The fiber constituting the main fiber layer has an aromatic aliphatic polyester resin having a melting point of 180 to 210 ° C. as a first component, an aromatic polyester resin having a melting point of 250 ° C. or more as a second component, The cylindrical filter according to claim 1 or 2 , wherein at least a part is a composite fiber exposed on the fiber surface.
前記複層不織布が、水流交絡により一体化されており、複層不織布における繊維処理剤の付着量が0.05質量%以下である、請求項1〜のいずれかに記載の筒状フィルター。 The cylindrical filter according to any one of claims 1 to 5 , wherein the multilayer nonwoven fabric is integrated by hydroentanglement, and the amount of the fiber treatment agent attached to the multilayer nonwoven fabric is 0.05% by mass or less. 前記熱収縮繊維層及び主体繊維層が、各繊維層をそれぞれ構成する繊維の繊度が異なり、いずれか一方が太繊度繊維で構成される太繊度繊維層を形成し、他方が細繊度繊維で構成される細繊度繊維層を形成しており、前記太繊度繊維層の平均繊度が細繊度繊維層の平均繊度の2倍以上である、請求項1〜のいずれかに記載の筒状フィルター。 The heat-shrinkable fiber layer and the main fiber layer are different in the fineness of the fibers constituting each fiber layer, either one forms a thick fineness fiber layer composed of thick fineness fibers, and the other consists of fineness fineness fibers. The cylindrical filter according to any one of claims 1 to 6 , wherein a fine fineness fiber layer is formed, and an average fineness of the thick fineness fiber layer is twice or more an average fineness of the fine fineness fiber layer. 前記複層不織布は、前記主体繊維層が細繊度繊維を含む細繊度繊維層の両面に太繊度繊維を含む太繊度繊維層を配して成る三層構造である、請求項1〜のいずれかに記載の筒状フィルター。 The multilayer nonwoven fabric, the main fiber layer is a three layer structure formed by arranging a large fineness fiber layer comprising a large fineness fibers on both surfaces of the fine denier fiber layer comprising fine denier fibers, any of claim 1-7 The cylindrical filter of crab. 前記複層不織布を構成するいずれか一方の繊維層が、スパンボンド不織布である、請求項1〜のいずれかに記載の筒状フィルター。 The cylindrical filter according to any one of claims 1 to 8 , wherein any one of the fiber layers constituting the multilayer nonwoven fabric is a spunbond nonwoven fabric. 前記筒状体の外周に巻回された外装不織布を更に含み、
前記外装不織布は、前記熱接着性繊維からなり、かつ前記筒状体の外周に熱接着されている請求項1に記載の筒状フィルター。
It further includes an exterior nonwoven fabric wound around the outer periphery of the cylindrical body,
The cylindrical filter according to claim 1, wherein the exterior nonwoven fabric is made of the thermoadhesive fiber and is thermally bonded to an outer periphery of the cylindrical body.
複数の繊維層からなる複層不織布が巻回された筒状体を含み、隣り合う複層不織布同士が熱接着されて成る筒状フィルターの製造方法であって、
前記複層不織布が、140℃における熱収縮率が9%以上の熱収縮繊維を含む熱収縮繊維層及び140℃における熱収縮率が4%以下の主体繊維を含む主体繊維層を含み、かつ複層不織布の少なくとも一方の表面を構成する繊維層が熱接着樹脂成分を含む熱接着性繊維を含み、かつ前記熱接着樹脂成分の融点−5℃から前記主体繊維の最も融点の高い樹脂の融点−10℃までの範囲の温度における熱収縮繊維と主体繊維との熱収縮率の差が5%以上であり、
前記複層不織布を、前記熱接着性繊維の熱接着樹脂成分の融点を5℃下回る温度以上に加熱して熱収縮繊維層を収縮させて多数の皺状物を形成させて多皺不織布を形成し、
前記多皺不織布を前記熱接着性繊維の熱接着温度で加熱して少なくとも前記熱接着樹脂成分で前記複層不織布間を熱接着により一体化しながら巻芯に巻き取り、
巻き取られた前記複層不織布から前記巻芯を抜き取って、前記複層不織布が巻回された筒状体を形成する筒状フィルターの製造方法。
A method for producing a cylindrical filter comprising a cylindrical body wound with a multilayer nonwoven fabric composed of a plurality of fiber layers, wherein adjacent multilayer nonwoven fabrics are thermally bonded to each other,
The multilayer nonwoven fabric includes a heat-shrinkable fiber layer including a heat-shrinkable fiber having a heat shrinkage rate of 9% or more at 140 ° C. and a main fiber layer including a main fiber having a heat-shrinkage rate of 140% or less at 4%. The fiber layer constituting at least one surface of the layered nonwoven fabric includes a thermoadhesive fiber containing a thermoadhesive resin component, and the melting point of the thermoadhesive resin component is from −5 ° C. to the melting point of the resin having the highest melting point of the main fiber. difference in thermal shrinkage between the heat-shrinkable fibers and main fibers at a temperature in the range of up to 10 ° C. is not less than 5%,
The multi-layer non-woven fabric is formed by heating the multi-layer non-woven fabric to a temperature lower than the melting point of the heat-adhesive resin component of the heat-adhesive fiber by 5 ° C. or more to shrink the heat-shrinkable fiber layer to form a plurality of cocoons. And
The multi-layered nonwoven fabric is heated at the heat bonding temperature of the heat-adhesive fiber and wound around a core while at least the heat-bonding resin component is integrated by thermal bonding between the multilayered nonwoven fabrics ,
The manufacturing method of the cylindrical filter which extracts the said core from the wound said multilayer nonwoven fabric, and forms the cylindrical body by which the said multilayer nonwoven fabric was wound.
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CN107398134B (en) * 2016-05-18 2021-06-29 现代自动车株式会社 Air filter and air purifier using high-density filter paper and vehicle using the same
CN108096927A (en) * 2017-12-29 2018-06-01 北昌君控(北京)科技有限公司 A kind of air filting material and preparation method thereof, application

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