JP2004270041A - Heat adhesive conjugated fiber for air-laid nonwoven fabric - Google Patents

Heat adhesive conjugated fiber for air-laid nonwoven fabric Download PDF

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JP2004270041A
JP2004270041A JP2003058270A JP2003058270A JP2004270041A JP 2004270041 A JP2004270041 A JP 2004270041A JP 2003058270 A JP2003058270 A JP 2003058270A JP 2003058270 A JP2003058270 A JP 2003058270A JP 2004270041 A JP2004270041 A JP 2004270041A
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fiber
heat
nonwoven fabric
unsaturated carboxylic
carboxylic acid
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JP2003058270A
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JP4031382B2 (en
Inventor
Hironori Aida
裕憲 合田
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Teijin Frontier Co Ltd
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Teijin Fibers Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a heat adhesive fiber for an air-laid nonwoven fabric having good adhesion to cellulosic fibers and efficiently stably producing the nonwoven fabric having a uniform weave. <P>SOLUTION: In the heat adhesive conjugated fiber for the air-laid nonwoven fabric, a modified polyolefin prepared by carrying out graft copolymerization of a vinyl monomer having an unsaturated carboxylic acid or an unsaturated carboxylic acid anhydride or a mixed polymer of the modified polyolefin with other polymers is used as a heat adhesive component. A polymer having a higher melting point than that of the modified polyolefin is used as a fiber-forming component. Both components are composited so as to expose at least the heat adhesive component to the surface and a finish oil is applied to the fiber surface. The heat adhesive conjugated fiber is prepared by regulating the content of the vinyl monomer having the unsaturated carboxylic acid or the unsaturated carboxylic acid anhydride to 0.005-0.04 mol/kg based on the weight of the modified polyolefin, the melt index of the modified polyolefin to 15-200 g/10 min, the ratio of the heat adhesive component accounting for the conjugated fiber to 55-95 wt.%, the fiber length to 2-30 mm, the number of crimps to ≤13 peaks/25 mm, the percent crimp to ≤11%, the finish oil pickup to 0.01-0.30 wt.% and the moisture content to ≤0.5 wt.%. <P>COPYRIGHT: (C)2004,JPO&NCIPI

Description

【0001】
【発明の属する技術分野】
本発明はエアレイド不織布用熱接着性複合繊維に関し、さらにはパルプ等のセルロース系繊維との接着性が良好であり、効率よく安定して、地合いの均一な不織布を製造できるエアレイド不織布用熱接着性複合繊維に関するものである。
【0002】
【従来の技術】
従来、木材パルプをドライレイドし、これに接着剤を含浸させ、繊維同士を接着させたエアレイド不織布が主に使用されてきた。しかし、近年では、低融点樹脂を鞘成分(熱接着性成分)に配した芯鞘型熱接着性複合繊維を用い、この繊維とパルプとを混綿してエアレイドした後、熱処理して、繊維同士を接着させたエアレイド不織布が提案されている(例えば、特許文献1など)。
【0003】
さらに、セルロース系繊維との接着性が良好な熱接着性複合繊維として、特許文献2および3に、不飽和カルボン酸もしくは不飽和カルボン酸無水物から選ばれた少なくとも1種を含むビニルモノマーが0.05〜2モル/kgグラフト重合された変成ポリオレフィンを熱接着成分とする、単糸繊度が0.55〜55dtex(0.5〜50デニール)、繊維長が3〜25mm、捲縮数が5〜30である熱接着性複合繊維が提案されている。また、特許文献4には、不飽和ジカルボン酸あるいはその無水物がグラフト共重合されたポリオレフィンを熱接着性成分とする熱接着性複合繊維が開示されている。
【0004】
しかしながら、従来提案されている上記熱接着性複合繊維は、セルロース系繊維との接着性には優れているものの、開繊性が非常に悪く、エアレイドウェブ上に未開繊が発生したり、ウェブの地合いが不均一となるといった問題がある。また、スクリーン法でエアレイド成形した場合にはウェブフォーマーの金属製スクリーン上に、ピッカーローター法でエアレイド成形した場合にはピッカーローター上に、熱接着性複合繊維が留まって、紡出量が著しく低下し、生産性が極めて悪くなるといった問題がある。
【0005】
また、上記熱接着性複合繊維からなるウェブを、熱カレンダー方式で熱接着する場合は、エンボスローラーやフラットローラーなどの金属製熱ローラーに、熱風エアスルー方式で熱接着する場合には、金網またはプラスチック製ネットにウェブが粘着するといった、生産上のトラブルがある。
【0006】
【特許文献1】
国際公開第97/30223号パンフレット
【0007】
【特許文献2】
特開2000−212866号公報
【0008】
【特許文献3】
特開2001−329432号公報
【0009】
【特許文献4】
国際公開第98/45519号パンフレット
【0010】
【発明が解決しようとする課題】
本発明は、上記従来技術を背景になされたもので、その目的は、セルロース系繊維との接着性が良好で、効率良く安定して、地合いの均一な不織布を製造できるエアレイド不織布用熱接着性繊維を提供することにある。
【0011】
【課題を解決するための手段】
本発明者は、熱接着性成分を構成するポリオレフィンの種類、熱接着性複合繊維の複合状態および形状などが、パルプとの接着性に大きく影響することに着目し、変成量の少ないポリオレフィンを熱接着成分に用いた複合繊維でも、パルプとの接着性が悪くならず、同時に、効率良く品位の優れたエアレイド不織布が得られることを見出し、本発明に到達した。
【0012】
かくして、本発明によれば、不飽和カルボン酸または不飽和カルボン酸無水物を有するビニルモノマーがグラフト共重合された変成ポリオレフィン、または、該変成ポリオレフィンと他のポリマーとの混合ポリマーを熱接着性成分とし、該変成ポリオレフィンより融点の高いポリマーを繊維形成性成分とし、少なくとも該熱接着成分が表面に露出するように両成分が複合化された熱接着性複合繊維であって、該繊維表面に油剤が付着し、下記(1)〜(7)を満足していることを特徴とするエアレイド不織布用熱接着性複合繊維が提供される。
(1)不飽和カルボン酸または不飽和カルボン酸無水物を有するビニルモノマーの含有率が熱接着性成分の重量に対して0.005〜0.04モル/kg
(2)熱接着性成分のメルトインデックスが15〜200g/10分
(3)熱接着性成分の複合繊維に占める割合が55〜95重量%
(4)繊維長が2〜30mm
(5)捲縮数が13山/25mm以下、捲縮率が11%以下
(6)油剤付着率が0.01〜0.30重量%
(7)水分率が0.5重量%以下
【0013】
【発明の実施の形態】
先ず、本発明の熱接着性複合繊維(以下単に複合繊維と称す)の機能を明らかにするために、エアレイド法不織布製造工程の一例について、その概略を説明する。
【0014】
不織布の基質であるパルプなどのセルロース系繊維を粉砕機により繊維状に粉砕したものが使用される。粉砕されたセルロース系繊維は送綿循環ダクトへ送られる。一方、複合繊維は、開繊機に投入され、均一な状態に開繊させた後、送綿循環ダクトへ送られる。複合繊維とセルロース系繊維とは送綿循環ダクト内で混綿され、エアレイド機に供給される。混綿された繊維は、エアレイド機に備えられた平面状スクリーンまたは回転している円筒状スクリーン(フォーミングドラム)表面の小孔スクリーン部位より吐出され、サクション装置で吸引され、積層された繊維集合体となる。続いて、得られた積層繊維集合体を熱風ドライヤー、フラットカレンダーヒートローラー、エンボスカレンダーヒートローラー等の方法で加熱処理し熱接着させる。熱接着性成分の融点以上の温度で加熱処理を施すことによって、複合繊維の熱接着性成分が溶融し複合繊維同士、もしくはそれとセルロース系繊維との交点とが熱接着され、不織布となる。
【0015】
本発明の複合繊維は、不飽和カルボン酸または不飽和カルボン酸無水物を有するビニルモノマーが共重合された変成ポリオレフィン、または、該変成ポリオレフィンと他のポリマーとの混合ポリマーを熱接着性成分とし、該変成ポリオレフィンより融点の高いポリマーを繊維形成性成分とする熱接着性複合繊維である。
【0016】
上記不飽和カルボン酸または不飽和カルボン酸無水物を有するビニルモノマーの具体例としては、無水マレイン酸、マレイン酸、アクリル酸、メタクリル酸などを挙げることができる。これらのビニルモノマーをポリオレフィンに共重合させることにより、セルロース系繊維表面の水酸基との親和性を向上させることができる。殊に無水マレイン酸は、無水カルボン酸基が開裂してセルロース繊維表面の水酸基と共有結合するために、セルロース繊維との接着性がきわめて良好であり、ポリオレフィンへの共重合量が少なくても上記のような効果が得られる。また、このように共重合量を少なくすることができるため、複合繊維同士や、複合繊維と金属との摩擦を小さくできる点でも有利である。
【0017】
上記ビニルモノマーを共重合する、変成ポリオレフィンの幹ポリマーとしては、ポリエチレン、ポリプロピレン、ポリブテンー1などが挙げられる。ポリエチレンは高密度、直鎖状低密度、低密度ポリエチレンを用いることができる。また、これらのポリマーは、ホモポリマーあるいは他のオレフィンとの共重合であってもよい。これらのポリマーの中では、融点の範囲、グラフト反応の容易性を考慮するとポリエチレンが好ましい。
【0018】
前述のビニルモノマーを、上記幹ポリマーにグラフト共重合するのは通常の方法で行なうことができ、ラジカル開始剤を用いて、ポリオレフィンに不飽和カルボン酸または不飽和カルボン酸無水物とビニルモノマーを混合してランダム共重合体からなる側鎖を導入するか、あるいは異種モノマーを順次重合することによるブロック共重合体からなる側鎖を導入することができる。
【0019】
また、幹ポリマーには、前述のビニルモノマー以外に、スチレン、α−メチルスチレン等のスチレン類、メタクリル酸メチル、メタクリル酸エチル、メタクリル酸2−ヒドロキシエチル、メタクリル酸ジメチルアミノエチルなどのメタクリル酸エステル類、あるいは同様なアクリル酸エステルなどのビニルモノマーが共重合されていてもよい。
【0020】
熱接着性成分を構成するポリマーとしては、上記変成ポリオレフィン単独であっても、該変成ポリオレフィンと他のポリマーとの混合ポリマーであってもよい。ここで、他のポリマーとしてはポリオレフィンが好ましく、変成ポリオレフィンの幹ポリマーと同種のポリオレフィンがより好ましい。つまり、幹ポリマーがポリエチレンである場合は、他のポリマーもポリエチレンであることが好ましい。
【0021】
本発明の繊維形成性成分を構成する、熱接着性成分より融点の高いポリマーとしては、前記変成ポリオレフィンの幹ポリマー、あるいはポリエステル、ポリアミドなどの結晶性ポリマーを挙げることができる。特にポリエステル、中でもポリエチレンテレフタレートが、不織布の地合いを均一にでき、紡出量を高くできる傾向にあり、好ましい。
【0022】
上記の熱接着性成分および繊維形成性成分に使用されるポリマーには、本発明の効果を妨げない範囲でさらに、酸化防止剤、光安定剤、紫外線吸収剤、中和剤、造核剤、エポキシ安定剤、滑剤、抗菌剤、難燃剤、帯電防止剤、顔料、可塑剤などの添加剤が必要に応じて含有されていてもよい。
【0023】
本発明の複合繊維は、少なくとも熱接着性成分が該繊維の表面に露出している複合繊維であり、熱接着性成分と繊維形成性成分とが並列型に複合化されたもの、熱接着性成分を鞘成分とし繊維形成性成分を芯成分とし、両成分が鞘芯型または偏芯鞘芯型に複合化された複合繊維である。本発明の複合繊維においては、熱接着性成分の該繊維表面に占める割合が小さくても高い接着力を示すが、パルプを均一に濡らすことができる点で芯鞘型に複合化させるのが特に好ましい。
【0024】
本発明においては、前述の複合繊維が前述した(1)〜(7)の要件を同時に満足していることが肝要である。これにより、上記各要件の奏する効果があいまって、セルロース系繊維との接着性を良好とすることと、効率良く地合いの均一なエアレイド不織布を製造することの両方の課題を同時に達成することができる。
【0025】
つまり、従来の技術では、不飽和カルボン酸または不飽和カルボン酸の酸無水物を有するビニルモノマーの変成ポリオレフィン中の含有量が多く、エアレイド不織布を効率良く安定して生産することができず、また地合いの均一な不織布を得ることが難しかった。しかしながら、本発明においては、(2)〜(7)の要件を同時に満足させることによって、(1)に規定するように不飽和カルボン酸または不飽和カルボン酸の酸無水物を有するビニルモノマーの含有率を低減しても、セルロース系繊維との高い接着性を維持でき、同時にもう一方の課題も達成することができる。以下、上記(1)〜(7)の各要件について説明する。
【0026】
まず、本発明においては、(1)不飽和カルボン酸または不飽和カルボン酸の酸無水物を有するビニルモノマーの含有率を、熱接着性成分の重量に対して0.005〜0.04モル/kgとする必要がある。上記含有率が0.04モル/kgを超えると、繊維−繊維間および繊維−金属間の摩擦係数が高くなりエアレイドウェブの開繊不良が発生したり、紡出量が上がらないといった問題がおきる。また、エアレイドウェブを、熱カレンダー方式で熱接着する場合は、エンボスローラーやフラットローラーなどの金属製熱ローラーに、熱風エアスルー方式で熱接着する場合には、金網またはプラスチック製ネットにウェブが粘着するといった生産トラブルが多発する。一方、上記含有率が0.005モル/kg未満では、セルロース系繊維との接着性が十分でなく、接着後の不織布からパルプの脱落が多くなる。より好ましい含有率は0.01〜0.035モル/kgの範囲である。
【0027】
次に、(2)熱接着成分のメルトインデックス(MI)を15〜200g/10分とする必要がある。上記MIが15g/10分未満であると、溶融してセルロース系繊維の表面を十分濡らすだけの熱流動性に欠け、該繊維との接着性が不十分となり、接着後の不織布からのパルプ脱落量が多くなる。一方、上記MIが200g/10分を超えると、溶融粘度が低く過ぎ、後述するような熱接着性成分の比率を55〜95重量%の範囲として複合紡糸するのが難しくなり、断糸が多くなる。MIとしては20〜150g/10分の範囲であり、より好しくは40〜100g/10分の範囲である。
【0028】
また、(3)熱接着性成分の複合繊維に占める割合を55〜95重量%とする必要がある。55重量%未満では、セルロース系繊維表面を十分濡らすだけのポリマー量がないため、該セルロース系繊維パルプとの熱接着性が十分でなく、熱接着後も不織布からのパルプ脱落量が多くなる。95重量%を超えると、複合繊維の安定した溶融紡糸が困難となる。上記割合としては60〜90重量%の範囲が好ましく、より好ましくは65〜80重量%の範囲である。
【0029】
さらに(4)繊維長は、2〜30mmとする必要がある。繊維長が2mmを下回ると、セルロース系繊維を強固に接着させるためのネットワークが形成しにくくなり、一方、繊維長が30mmを超えると、スクリーンやピッカーローターからの紡出性が悪くなり、生産性に障害をきたす。紡出量を高くするためには、できるだけ繊維長を短くするのが効果的であり、3〜8mmがより好適である。
【0030】
本発明の複合繊維には捲縮が付与されていても付与されていなくてもよい。つまり、不織布に嵩高性を与えたい場合は捲縮を付与すればよいし、その必要がなく空気開繊性および吐出能力をより向上させたい場合は、捲縮を付与しなくてもよい。但し、本発明においては、(5)捲縮数を13山/25mm以下、捲縮率を11%以下とする必要がある。これにより、空気開繊性が良好になり、均一な地合いの不織布が得られる。捲縮数が13山/25mmまたは捲縮率が11%を超えると、未開繊の発生や紡出量の低下を生じる。捲縮の形態としては、平面内に包含される平面ジグザグ型あるいはオメガ型の捲縮が、スパイラル状の3次元捲縮よりも開繊性の点でより好ましい。
【0031】
また、本発明の複合繊維には油剤が付着しており、(6)油剤付着率を0.01〜0.30重量%の範囲とする必要がある。油剤付着量が0.01重量%を下回ると、繊維−繊維間の摩擦が大きくなり、未開繊性や紡出量が低下するだけでなく、静電気が発生し易くなる。また、油剤付着量が0.30重量%を超えると、油剤自体の摩擦の影響で主として繊維−繊維間の摩擦が高くなり、開繊性が低下し、セルロース系繊維との接着性も悪くなる。油剤付着率の好ましい範囲は0.1〜0.25重量%である。
【0032】
また、(7)水分率を0.5重量%以下に抑える必要がある。該水分率が0.5重量%を超える場合は、変成ポリオレフィンと、スクリーンやピッカーローターを構成する金属との摩擦が著しく増大し、紡出量が低下し、生産性が悪くなる。好ましい水分率は0.3重量%以下であり、より好ましくは0.15重量%以下である。
【0033】
本発明の複合繊維の繊度は特に限定されないが、0.1〜3デシテックスの範囲がセルロース系繊維との熱接着性をより強固にでき好ましい。特に繊度を細くすればするほど構成本数を多くでき、よりセルロース系繊維の脱落量を抑えることができる点で有利である。
【0034】
本発明の複合繊維をセルロース系繊維と混綿して用いる場合、該複合繊維がエアレイド不織布中に3〜30重量%程度含まれるようにすれば、十分な接着性能を発揮できる。
【0035】
【実施例】
以下、実施例により、本発明をさらに具体的に説明するが、本発明はこれらの実施例に限定されるものではない。なお、実施例における各項目は次の方法で測定した。
【0036】
(1)繊度
JIS L 1015 7.5.1 A法に記載の方法により測定した。
【0037】
(2)繊維長
JIS L 1015 7.4.1 C法に記載の方法により測定した。
【0038】
(3)捲縮数、捲縮率
JIS L 1015 7.12に記載の方法により測定した。
【0039】
(4)固有粘度([η])
オルトクロロフェノールを溶媒として、温度35℃で測定した。
【0040】
(5)メルトインデックス(MI)
JIS K 7210 条件4に記載の方法により測定した。
【0041】
(6)ガラス転移点(Tg)、融点(Tm)
パーキンエルマー社製の示差走査熱量計DSC−7型を使用し、昇温速度20℃/分で測定した。
【0042】
(7)水分率
JIS L 1015 7.1.2に記載の方法により測定した。
【0043】
(8)最大紡出量
パルプ/バインダー繊維=80/20(重量比)の混綿体を、図1に示したDan Webforming International A/S(デンマーク)社製のエアレイド製造装置(1.2m幅)に供給して処理した。すなわち混綿体を送綿循環ダクト2および3に送入し、回転する筒状スクリーン4aおよび5aから繊維を排出させた。排出された繊維を100m/分で運転するサクション装置8を有するネットコンベア7で捕集しながらエアレイドウェブ6を得るが、この際、フォーミングヘッド1から繊維の詰り無しに吐出される最大紡出量(kg/時間)を測定した。このとき、筒状スクリーン4aおよび5aのスクリーンの孔の形状は、縦の長さが1.5mm、横の長さが20mmの長方形とし、スクリーン開孔率は23%であった。
【0044】
(9)未開繊率
前述のエアレイド法により目付35g/mで成型したウェブ10g中から未開繊塊を取り出して、その重量xを測定し、下式により未開繊率uを算出した。u(%)=x/10×100
(10)不織布地合い
図1に示した前記エアレイド製造装置により、前述の目付35g/mで成型したウェブをウェブ圧縮ロール9で圧縮した後、サクションドライヤー10を使用して150℃で3秒間加熱処理することにより、熱接着性成分を溶融接着させ、不織布11を作製し、巻き取りロール12に巻き取って、評価用の熱接着不織布を作成した。
【0045】
ウェブの外観を観察し、以下の基準で評価する。
レベル1:未開繊塊や目付斑(濃淡)が見られず、均一な地合いである。
レベル2:未開繊塊は目立たないが、目付斑(濃淡)が目視で確認できる。
レベル3:未開繊塊と目付斑(濃淡)が目立ち、不均一な地合いである。
【0046】
(11)パルプ脱落率
前述の熱接着不織布を面積10cm×10cmの正方形状に切り出して、不織布の重量(W1)を測定し、次にエアレイド機のフォーミングドラム内に不織布を投入してフォーミングドラム、ニードルロール、サクションを1分間運転し、その後フォーミングドラムから取り出して重量(W2)を測定し、次式より算出した。
パルプ脱落率(%)={(W1)−(W2)}÷(W1)×100
これはニードルロールにより不織布内の未接着パルプを叩き出し、離脱したパルプをサクションで除去する考え方に基づく。小さい方がパルプとの接着性が良好であることを示す。
【0047】
[実施例1]
MIが40g/10分、Tmが131℃の高密度ポリエチレン(HDPE)のチップと、MIが80g/10分、Tmが98℃の直鎖状低密度ポリエチレン(LLDPE)を幹ポリマーとし、無水マレイン酸が0.20モル/kg、アクリル酸メチルが0.8モル/kg共重合された変成ポリエチレン(MPE−1)のチップを87:13の割合で混合し、これを二軸エクストルーダーで溶融し、250℃の溶融混合ポリマーとした。この溶融混合ポリマー(熱接着性成分)の無水マレイン酸含有率は0.026モル/kg、MIは43g/10分であった。一方、120℃で16時間真空乾燥した固有粘度[η]が0.61のPETのペレットをエクストルーダーで溶融し、280℃の溶融ポリマー(繊維形成性成分)とした。両溶融ポリマーを、前者を鞘成分A、後者を芯成分Bとし、かつ重量比がA:B=65:35となるように、直径0.3mmの丸穴キャピラリーを900孔有する公知の芯鞘型複合紡糸口金から、複合化して溶融吐出させた。この際、口金温度は285℃、吐出量は615g/分であった。さらに、吐出ポリマーを30℃の冷却風で空冷し1150m/分で巻き取り、未延伸糸を得た。この未延伸糸を72℃の温水中で3倍に延伸した後、ラウリルホスフェートカリウム塩/ポリオキシエチレン変成シリコーン=80/20からなる油剤を0.2重量%付与した後、押込み型クリンパーで捲縮数9.9山/25mm、捲縮率4.9%の平面ジグザグ型捲縮を付与し、110℃で乾燥した後、5mmの繊維長にカットした。得られた短繊維の繊度は2.3デシテックス、水分率は0.2重量%であった。
【0048】
エアレイド法で作成した不織布サンプルの地合いは良好でレベル1に格付けされ、未開繊率は0.8%、パルプ脱落率は2.4%と良好であった。また、最大紡出量は170kg/時間であった。また、サクションドライヤーのネットコンベア7b金網へのウェブの粘着はなかった。
【0049】
[実施例2]
MIが21g/10分、Tmが131℃の高密度ポリエチレン(HDPE)のチップとMIが52g/10分、Tmが121℃の直鎖状低密度ポリエチレン(LLDPE)のチップと、MIが8g/10分、Tmが98℃の直鎖状低密度ポリエチレン(LLDPE)を幹ポリマーとし、無水マレイン酸が0.20モル/kg、アクリル酸メチルが0.8モル/kg共重合された変成ポリエチレン(MPE−1)のチップを各々50:40:10の割合で混合し、これを二軸エクストルーダーで溶融し、250℃の溶融混合ポリマーとした。この溶融混合ポリマー(熱接着性成分)の無水マレイン酸含有率は0.02モル/kg、MIは27g/10分であった。一方、120℃で16時間真空乾燥した固有粘度[η]が0.61のPETのペレットをエクストルーダーで溶融し、280℃の溶融ポリマー(繊維形成性成分)とした。両溶融ポリマーを、前者を鞘成分A、後者を芯成分Bとし、かつ重量比がA:B=60:40となるように、直径0.3mmの丸穴キャピラリーを900孔有する公知の芯鞘型複合紡糸口金から、複合化して溶融吐出させた。この際、口金温度は285℃、吐出量は450g/分であった。さらに、吐出ポリマーを30℃の冷却風で空冷し1150m/分で巻き取り、未延伸糸を得た。この未延伸糸を72℃の温水中で3倍に延伸した後、ラウリルホスフェートカリウム塩/ポリオキシエチレン変成シリコーン=80/20からなる油剤を0.2重量%付与した後、押込み型クリンパーで捲縮数10.1山/25mm、捲縮率6.3%の平面ジグザグ型捲縮を付与し、110℃で乾燥した後、5mmの繊維長にカットした。得られた短繊維の繊度は1.8デシテックス、水分率は0.17重量%であった。
【0050】
エアレイド法で作成した不織布サンプルの地合いはレベル1に格付けされ、未開繊率は0.8%、パルプ脱落率は1.8%と良好であった。また、最大紡出量は160kg/時間であり、サクションドライヤーのネットコンベア7bの金網へのウェブの粘着はなかった。
【0051】
[比較例1]
MIが20g/10分、Tmが131℃の高密度ポリエチレン(HDPE)のチップと、MIが8g/10分、Tmが98℃の直鎖状低密度ポリエチレン(LLDPE)を幹ポリマーとし、無水マレイン酸が0.20モル/kg、アクリル酸メチルが0.8モル/kg共重合された変成ポリエチレン(MPE−1)のチップを50:50の割合で混合し、これを二軸エクストルーダーで溶融し、250℃の溶融混合ポリマーとした。この溶融混合ポリマー(熱接着性成分)の無水マレイン酸含有率は0.10モル/kg、MIは13g/10分であった。一方、120℃で16時間真空乾燥した固有粘度[η]が0.61のPETのペレットをエクストルーダーで溶融し、280℃の溶融ポリマー(繊維形成性成分)とした。両溶融ポリマーを、前者を鞘成分A、後者を芯成分Bとし、かつ重量比がA:B=65:35となるように、直径0.3mmの丸穴キャピラリーを900孔有する公知の芯鞘型複合紡糸口金から、複合化して溶融吐出させた。この際、口金温度は285℃、吐出量は450g/分であった。さらに、吐出ポリマーを30℃の冷却風で空冷し1150m/分で巻き取り、未延伸糸を得た。この未延伸糸を72℃の温水中で2.8倍に延伸した後、ラウリルホスフェートカリウム塩/ポリオキシエチレン変成シリコーン=80/20からなる油剤を0.2重量%付与した後、押込み型クリンパーで捲縮数11.1山/25mm、捲縮率7.2%の平面ジグザグ型捲縮を付与し、110℃で乾燥した後、5mmの繊維長にカットした。得られた短繊維の繊度は1.8デシテックス、水分率は0.21重量%であった。
【0052】
エアレイド法で作成した不織布サンプルのパルプ脱落率は2.3%と良好であった。しかし、不織布地合いはレベル3に格付けされ、未開繊率は5.3%、最大紡出量は75kg/時間であった。サクションドライヤーのネットコンベア7bの金網にウェブが粘着し、安定した生産ができなかった。
【0053】
[比較例2]
A:Bのポリマー重量比を45:55とした他は、実施例1と同様にした。エアレイド法で作成した不織布サンプルの地合いは良好でレベル1に格付けされ、未開繊率は0.2%、最大紡出量は185kg/時間と良好であったが、パルプ脱落率は10.1%であった。また、サクションドライヤーのネットコンベア7bの金網へのウェブの粘着はなかった。
【0054】
[比較例3]
捲縮数を18山/25mm、捲縮率を12.5%とした他は、実施例1と同様にした。エアレイド法で作成した不織布サンプルのパルプ脱落率は2.6%、最大紡出量は155kg/時間と良好であった。しかし、不織布地合いはレベル3に格付けされ、未開繊率は3.4%であった。サクションドライヤーのネットコンベア7bの金網へのウェブの粘着はなかった。
【0055】
[比較例4]
油剤付着率を0.5重量%とした他は、実施例1と同様にした。エアレイド法で作成した不織布サンプルのパルプ脱落率は5.6%、最大紡出量は130kg/時間と若干悪くなり、不織布地合いはレベル2に格付けされ、未開繊率は2.9%であった。サクションドライヤーのネットコンベア7bの金網へのウェブの粘着はなかった。
【0056】
[比較例5]
水分率を0.5重量%とした他は、実施例1と同様にした。エアレイド法で作成した不織布サンプルのパルプ脱落率は2.2%で問題なかった。しかし、不織布地合いはレベル2に格付けされ、未開繊率は4.9%、最大紡出量は100kg/時間であった。サクションドライヤーのネットコンベア7bの金網へのウェブの粘着はなかった。
【0057】
【発明の効果】
本発明の熱接着性複合繊維はセルロース系繊維との接着性が良好であるだけでなく、かかる複合繊維によれば、エアレイド不織布の地合いを均一なものとすることができる。このため、本発明の複合繊維からは、極めて高品質の不織布を製造することができる。また、上記複合繊維によれば、エアレイド成形時の紡出量を高くでき、また、熱風エアスルー法による熱接着でも金網への粘着がないため、効率良く安定してエアレイド不織布を製造することができ、その工業的価値が極めて高いものである。加えて、本発明の複合繊維は、熱接着性成分の変成ポリオレフィンの変成量が少なくて済むため、従来よりも安価な熱接着性繊維を提供できるといった効果をも奏するものである。
【図面の簡単な説明】
【図1】図1は、本発明の不織布を製造する装置の側面図である。
【符号の説明】
1 ウェブフォーミングヘッド
2 送綿循環ダクト
3 送綿循環ダクト
4a フォーミングドラム(円筒状スクリーン)
5a フォーミングドラム(円筒状スクリーン)
4b ニードルロール
5b ニードルロール
6 ウェブ
7a ネットコンベア
7b ネットコンベア
8 サクション装置
9 ウェブ圧縮ロール
10 サクションドライヤー
11 不織布
12 巻き取りロール
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a thermoadhesive conjugate fiber for an airlaid nonwoven fabric, and further has a good adhesiveness with a cellulosic fiber such as pulp, and is capable of efficiently and stably producing a nonwoven fabric having a uniform formation. It relates to a conjugate fiber.
[0002]
[Prior art]
Conventionally, an air-laid nonwoven fabric in which wood pulp is dry-laid, impregnated with an adhesive, and fibers are adhered to each other has been mainly used. However, in recent years, a core-sheath type heat-adhesive conjugate fiber in which a low-melting-point resin is disposed in a sheath component (heat-adhesive component) is used. There has been proposed an air-laid nonwoven fabric to which is adhered (for example, Patent Document 1).
[0003]
Further, Patent Documents 2 and 3 disclose a vinyl monomer containing at least one kind selected from unsaturated carboxylic acids or unsaturated carboxylic anhydrides as a heat-adhesive conjugate fiber having good adhesion to cellulosic fibers. The modified polyolefin graft-polymerized as a heat-adhesive component has a single fiber fineness of 0.55 to 55 dtex (0.5 to 50 denier), a fiber length of 3 to 25 mm, and a number of crimps of 5.05 to 2 mol / kg. A heat-adhesive conjugate fiber of ~ 30 has been proposed. Patent Document 4 discloses a heat-adhesive conjugate fiber containing a polyolefin obtained by graft-copolymerizing an unsaturated dicarboxylic acid or an anhydride thereof as a heat-adhesive component.
[0004]
However, the above-mentioned conventionally proposed heat-adhesive conjugate fibers, although excellent in adhesion to cellulosic fibers, have very poor spreadability and unspread on an airlaid web, There is a problem that formation is uneven. In addition, when the air-laid molding is performed by the screen method, the heat-adhesive conjugate fibers remain on the metal screen of the web former, and when the air-laid molding is performed by the picker rotor method, the heat-adhesive conjugate fibers remain. There is a problem that the productivity is extremely lowered.
[0005]
When the web made of the above-mentioned heat-adhesive conjugate fiber is heat-bonded by a heat calender method, a metal mesh or a plastic is used when heat-bonding to a metal heat roller such as an emboss roller or a flat roller by a hot air air through method. There are production problems, such as the web sticking to the net.
[0006]
[Patent Document 1]
WO 97/30223 pamphlet
[0007]
[Patent Document 2]
JP 2000-212866 A
[0008]
[Patent Document 3]
JP 2001-329432 A
[0009]
[Patent Document 4]
International Publication No. 98/45519 pamphlet
[0010]
[Problems to be solved by the invention]
The present invention has been made on the background of the above-mentioned prior art, and its object is to provide a heat-adhesive property for an air-laid nonwoven fabric capable of producing a nonwoven fabric having a good adhesion to cellulosic fibers, efficiently and stably, and a uniform formation. To provide fibers.
[0011]
[Means for Solving the Problems]
The present inventor has focused on the fact that the type of polyolefin constituting the heat-adhesive component, the composite state and shape of the heat-adhesive conjugate fiber greatly affect the adhesion to pulp, The present inventors have found that even with the conjugate fiber used as the adhesive component, the adhesiveness to pulp does not deteriorate, and at the same time, an air-laid nonwoven fabric of excellent quality can be obtained efficiently, and the present invention has been achieved.
[0012]
Thus, according to the present invention, a modified polyolefin in which a vinyl monomer having an unsaturated carboxylic acid or an unsaturated carboxylic anhydride is graft-copolymerized, or a mixed polymer of the modified polyolefin and another polymer is used as a heat-adhesive component. A heat-adhesive conjugate fiber in which a polymer having a melting point higher than that of the modified polyolefin is used as a fiber-forming component, and both components are compounded so that at least the heat-adhesive component is exposed on the surface; Are provided, and the following (1) to (7) are satisfied, and a thermoadhesive conjugate fiber for an airlaid nonwoven fabric is provided.
(1) The content of the vinyl monomer having an unsaturated carboxylic acid or an unsaturated carboxylic acid anhydride is 0.005 to 0.04 mol / kg based on the weight of the heat-adhesive component.
(2) The melt index of the heat-adhesive component is 15 to 200 g / 10 min.
(3) The ratio of the heat-adhesive component to the composite fiber is 55 to 95% by weight.
(4) The fiber length is 2 to 30 mm
(5) The number of crimps is 13 peaks / 25 mm or less, and the crimp rate is 11% or less.
(6) Oil adhesion rate of 0.01 to 0.30% by weight
(7) Moisture percentage is 0.5% by weight or less
[0013]
BEST MODE FOR CARRYING OUT THE INVENTION
First, in order to clarify the function of the heat-adhesive conjugate fiber (hereinafter, simply referred to as conjugate fiber) of the present invention, an outline of an example of an air-laid nonwoven fabric manufacturing process will be described.
[0014]
Cellulose fibers such as pulp, which is the substrate of the nonwoven fabric, are pulverized into fibers by a pulverizer. The pulverized cellulosic fibers are sent to a cotton circulation duct. On the other hand, the conjugate fiber is fed into a fiber opening machine, spread to a uniform state, and then sent to a cotton feeding circulation duct. The conjugate fiber and the cellulosic fiber are mixed in a cotton circulation duct and supplied to an air laid machine. The mixed fiber is discharged from a flat screen provided in the air laid machine or a small hole screen portion on a rotating cylindrical screen (forming drum) surface, sucked by a suction device, and a laminated fiber assembly. Become. Subsequently, the obtained laminated fiber aggregate is subjected to a heat treatment by a method such as a hot air drier, a flat calender heat roller, an emboss calender heat roller or the like to be thermally bonded. By performing the heat treatment at a temperature equal to or higher than the melting point of the heat-adhesive component, the heat-adhesive component of the conjugate fiber is melted and the conjugate fibers are heat-bonded to each other or to the intersection between the conjugate fiber and the cellulosic fiber, thereby forming a nonwoven fabric.
[0015]
The composite fiber of the present invention is a modified polyolefin in which a vinyl monomer having an unsaturated carboxylic acid or an unsaturated carboxylic acid anhydride is copolymerized, or a mixed polymer of the modified polyolefin and another polymer as a heat-adhesive component, A heat-adhesive conjugate fiber containing a polymer having a higher melting point than the modified polyolefin as a fiber-forming component.
[0016]
Specific examples of the vinyl monomer having an unsaturated carboxylic acid or an unsaturated carboxylic acid anhydride include maleic anhydride, maleic acid, acrylic acid, methacrylic acid, and the like. By copolymerizing these vinyl monomers with polyolefin, the affinity with the hydroxyl groups on the surface of the cellulosic fiber can be improved. In particular, maleic anhydride has very good adhesion to cellulose fibers because the carboxylic anhydride groups are cleaved and covalently bond with the hydroxyl groups on the surface of the cellulose fibers. The following effects can be obtained. Further, since the copolymerization amount can be reduced in this way, it is advantageous in that the friction between the composite fibers or between the composite fiber and the metal can be reduced.
[0017]
Examples of the modified polyolefin backbone copolymer obtained by copolymerizing the vinyl monomer include polyethylene, polypropylene, and polybutene-1. As the polyethylene, high-density, linear low-density, low-density polyethylene can be used. These polymers may be homopolymers or copolymers with other olefins. Among these polymers, polyethylene is preferable in consideration of the range of the melting point and the ease of the graft reaction.
[0018]
Graft copolymerization of the above-mentioned vinyl monomer with the above-mentioned backbone polymer can be carried out by a usual method. Using a radical initiator, an unsaturated carboxylic acid or an unsaturated carboxylic anhydride and a vinyl monomer are mixed with a polyolefin. Then, a side chain composed of a random copolymer can be introduced, or a side chain composed of a block copolymer can be introduced by sequentially polymerizing different kinds of monomers.
[0019]
Further, in addition to the above-mentioned vinyl monomers, styrenes such as styrene and α-methylstyrene, methacrylates such as methyl methacrylate, ethyl methacrylate, 2-hydroxyethyl methacrylate, and dimethylaminoethyl methacrylate are also used as the trunk polymer. Or a similar vinyl monomer such as an acrylate ester.
[0020]
The polymer constituting the heat-adhesive component may be the modified polyolefin alone or a mixed polymer of the modified polyolefin and another polymer. Here, the other polymer is preferably a polyolefin, and more preferably a polyolefin of the same type as the modified polyolefin backbone polymer. That is, when the trunk polymer is polyethylene, it is preferable that the other polymers are also polyethylene.
[0021]
Examples of the polymer constituting the fiber-forming component of the present invention, which has a higher melting point than the heat-adhesive component, include the above-mentioned modified polyolefin backbone polymer and crystalline polymers such as polyester and polyamide. In particular, polyester, especially polyethylene terephthalate, is preferable since it tends to make the texture of the nonwoven fabric uniform and can increase the spinning amount.
[0022]
The polymer used for the heat-adhesive component and the fiber-forming component described above further includes an antioxidant, a light stabilizer, an ultraviolet absorber, a neutralizer, a nucleating agent, as long as the effects of the present invention are not impaired. If necessary, additives such as an epoxy stabilizer, a lubricant, an antibacterial agent, a flame retardant, an antistatic agent, a pigment, and a plasticizer may be contained.
[0023]
The conjugate fiber of the present invention is a conjugate fiber in which at least the heat-adhesive component is exposed on the surface of the fiber, in which the heat-adhesive component and the fiber-forming component are conjugated in a parallel type, It is a composite fiber in which the component is a sheath component, the fiber-forming component is a core component, and both components are complexed into a sheath-core type or an eccentric sheath-core type. In the conjugate fiber of the present invention, a high adhesive strength is exhibited even if the ratio of the heat-adhesive component to the fiber surface is small, but it is particularly preferable to form a core-sheath composite in that pulp can be uniformly wetted. preferable.
[0024]
In the present invention, it is important that the above-mentioned conjugate fiber simultaneously satisfies the above-mentioned requirements (1) to (7). Thereby, combined with the effects of the above requirements, both the problems of improving the adhesiveness with the cellulosic fiber and efficiently producing an air-laid nonwoven fabric having a uniform formation can be achieved at the same time. .
[0025]
In other words, in the conventional technology, the content of the vinyl monomer having the unsaturated carboxylic acid or the anhydride of the unsaturated carboxylic acid in the modified polyolefin is large, and the air-laid nonwoven fabric cannot be efficiently and stably produced. It was difficult to obtain a nonwoven fabric having a uniform formation. However, in the present invention, by simultaneously satisfying the requirements of (2) to (7), the content of a vinyl monomer having an unsaturated carboxylic acid or an acid anhydride of an unsaturated carboxylic acid as defined in (1) is included. Even if the ratio is reduced, high adhesiveness to the cellulosic fiber can be maintained, and at the same time, the other problem can be achieved. Hereinafter, the requirements (1) to (7) will be described.
[0026]
First, in the present invention, the content of (1) a vinyl monomer having an unsaturated carboxylic acid or an acid anhydride of an unsaturated carboxylic acid is set to 0.005 to 0.04 mol /% based on the weight of the heat adhesive component. kg. If the content exceeds 0.04 mol / kg, the friction coefficient between the fiber and the fiber and between the fiber and the metal becomes high, which causes problems such as poor opening of the airlaid web and an increase in the spinning amount. . In addition, when air-laid webs are heat-bonded by a heat calender method, to a metal heat roller such as an emboss roller or a flat roller, and when heat-bonded by a hot air air-through method, the web adheres to a wire mesh or a plastic net. Production troubles occur frequently. On the other hand, if the content is less than 0.005 mol / kg, the adhesiveness to the cellulosic fiber is not sufficient, and the pulp tends to fall off from the nonwoven fabric after the adhesion. A more preferred content is in the range of 0.01 to 0.035 mol / kg.
[0027]
Next, (2) the melt index (MI) of the heat bonding component needs to be 15 to 200 g / 10 minutes. When the MI is less than 15 g / 10 minutes, the fluidity lacks enough to melt and wet the surface of the cellulosic fiber sufficiently, the adhesiveness with the fiber becomes insufficient, and the pulp falls off the nonwoven fabric after bonding. The amount increases. On the other hand, when the MI exceeds 200 g / 10 minutes, the melt viscosity is too low, and it becomes difficult to perform composite spinning with the ratio of the heat-adhesive component as described later in the range of 55 to 95% by weight, and many yarn breaks occur. Become. MI is in the range of 20 to 150 g / 10 min, and more preferably in the range of 40 to 100 g / 10 min.
[0028]
Further, (3) the proportion of the heat-adhesive component in the composite fiber must be 55 to 95% by weight. If the amount is less than 55% by weight, there is not enough polymer to sufficiently wet the surface of the cellulosic fiber, so that the thermal adhesion to the cellulosic fiber pulp is not sufficient, and the amount of pulp falling off the nonwoven fabric after thermal bonding is large. When it exceeds 95% by weight, stable melt spinning of the conjugate fiber becomes difficult. The proportion is preferably in the range of 60 to 90% by weight, more preferably in the range of 65 to 80% by weight.
[0029]
Further, (4) the fiber length needs to be 2 to 30 mm. When the fiber length is less than 2 mm, it is difficult to form a network for firmly adhering the cellulosic fibers. On the other hand, when the fiber length is more than 30 mm, the spinning property from a screen or a picker rotor is deteriorated, and the productivity is reduced. Cause obstacles. In order to increase the spinning amount, it is effective to shorten the fiber length as much as possible, and 3 to 8 mm is more preferable.
[0030]
The composite fiber of the present invention may or may not be crimped. In other words, when it is desired to give the nonwoven fabric bulkiness, crimping may be provided. When it is not necessary to further improve the air opening property and the discharging ability, crimping may not be provided. However, in the present invention, (5) the number of crimps must be 13 peaks / 25 mm or less, and the crimp rate must be 11% or less. Thereby, air opening property becomes favorable and a nonwoven fabric having a uniform texture can be obtained. When the number of crimps is 13 peaks / 25 mm or the crimp rate exceeds 11%, unspread fibers are generated and the spinning amount is reduced. As a form of the crimp, a plane zigzag type or an omega type crimp included in a plane is more preferable than the spiral three-dimensional crimp in terms of the opening property.
[0031]
Further, an oil agent is attached to the conjugate fiber of the present invention, and (6) the oil agent adhesion rate needs to be in the range of 0.01 to 0.30% by weight. If the amount of the oil agent is less than 0.01% by weight, the friction between the fibers becomes large, and not only the unspreading property and the spinning amount are reduced, but also static electricity is easily generated. If the amount of the oil agent exceeds 0.30% by weight, the friction between the fibers mainly increases due to the effect of the friction of the oil agent itself, the spreadability decreases, and the adhesion to the cellulosic fiber deteriorates. . The preferable range of the oil agent adhesion rate is 0.1 to 0.25% by weight.
[0032]
(7) It is necessary to suppress the water content to 0.5% by weight or less. If the water content exceeds 0.5% by weight, the friction between the modified polyolefin and the metal constituting the screen or picker rotor is significantly increased, the spinning amount is reduced, and the productivity is reduced. The preferred moisture content is 0.3% by weight or less, more preferably 0.15% by weight or less.
[0033]
The fineness of the conjugate fiber of the present invention is not particularly limited, but is preferably in the range of 0.1 to 3 dtex because the thermal adhesion to the cellulosic fiber can be further enhanced. In particular, the finer the fineness, the more the number of components can be increased, which is advantageous in that the amount of cellulosic fibers falling off can be further suppressed.
[0034]
When the conjugate fiber of the present invention is used by mixing with a cellulosic fiber, sufficient adhesion performance can be exhibited if the conjugate fiber is contained in the airlaid nonwoven fabric in an amount of about 3 to 30% by weight.
[0035]
【Example】
Hereinafter, the present invention will be described more specifically with reference to Examples, but the present invention is not limited to these Examples. Each item in the examples was measured by the following method.
[0036]
(1) Fineness
It was measured by the method described in JIS L 1015 7.5.1 Method A.
[0037]
(2) Fiber length
It was measured by the method described in JIS L 1015 7.4.1 C method.
[0038]
(3) Number of crimps, crimp rate
It was measured by the method described in JIS L 1015 7.12.
[0039]
(4) Intrinsic viscosity ([η])
The measurement was performed at a temperature of 35 ° C. using orthochlorophenol as a solvent.
[0040]
(5) Melt index (MI)
It was measured by the method described in JIS K7210 condition 4.
[0041]
(6) Glass transition point (Tg), melting point (Tm)
The measurement was performed at a heating rate of 20 ° C./min using a differential scanning calorimeter DSC-7 manufactured by Perkin Elmer.
[0042]
(7) Moisture percentage
It was measured by the method described in JIS L 1015 7.1.2.
[0043]
(8) Maximum spinning amount
The pulp / binder fiber = 80/20 (weight ratio) mixed cotton body was supplied to an air laid manufacturing apparatus (1.2 m width) manufactured by Dan Webforming International A / S (Denmark) shown in FIG. 1 to be treated. That is, the mixed cotton body was fed into the cotton feeding circulation ducts 2 and 3, and the fibers were discharged from the rotating cylindrical screens 4a and 5a. The air-laid web 6 is obtained while collecting the discharged fibers by a net conveyor 7 having a suction device 8 operating at 100 m / min. In this case, the maximum spinning amount discharged without clogging of the fibers from the forming head 1 (Kg / hour) was measured. At this time, the shape of the holes of the cylindrical screens 4a and 5a was a rectangle having a vertical length of 1.5 mm and a horizontal length of 20 mm, and the screen aperture ratio was 23%.
[0044]
(9) Unopened rate
According to the airlaid method described above, the basis weight is 35 g / m. 2 An unopened lump was taken out from 10 g of the web molded by the method described above, the weight x was measured, and the unopened ratio u was calculated by the following equation. u (%) = x / 10 × 100
(10) Non-woven fabric formation
With the airlaid manufacturing apparatus shown in FIG. 2 After the web formed by the above is compressed by a web compression roll 9, it is subjected to a heat treatment at 150 ° C. for 3 seconds using a suction drier 10 so that the heat-adhesive component is melt-bonded, and a nonwoven fabric 11 is produced. 12 to prepare a heat-bonded nonwoven fabric for evaluation.
[0045]
The appearance of the web is observed and evaluated according to the following criteria.
Level 1: An unspread fibrous mass and spots (shading) are not seen, and the texture is uniform.
Level 2: Unspread fibrous mass is inconspicuous, but spots (shading) can be visually confirmed.
Level 3: Unopened lumps and spots (shading) are conspicuous and have uneven texture.
[0046]
(11) Pulp shedding rate
The above-mentioned heat-bonded non-woven fabric was cut into a square having an area of 10 cm × 10 cm, the weight (W1) of the non-woven fabric was measured, and then the non-woven fabric was put into a forming drum of an air laid machine, and the forming drum, needle roll, and suction were removed. After the operation, the weight (W2) was measured after taking out from the forming drum and calculated by the following equation.
Pulp shedding rate (%) = {(W1)-(W2)} (W1) × 100
This is based on the idea that the unbonded pulp in the nonwoven fabric is beaten out by a needle roll, and the pulp released is removed by suction. A smaller one indicates better adhesion to pulp.
[0047]
[Example 1]
A high-density polyethylene (HDPE) chip having an MI of 40 g / 10 min and a Tm of 131 ° C. and a linear low-density polyethylene (LLDPE) having an MI of 80 g / 10 min and a Tm of 98 ° C. are used as a trunk polymer, and anhydrous maleic is used. Chips of modified polyethylene (MPE-1) copolymerized with 0.20 mol / kg of acid and 0.8 mol / kg of methyl acrylate were mixed at a ratio of 87:13 and melted with a twin-screw extruder. Thus, a melt-mixed polymer at 250 ° C. was obtained. The maleic anhydride content of the melt-blended polymer (the heat-adhesive component) was 0.026 mol / kg, and the MI was 43 g / 10 minutes. On the other hand, PET pellets having an intrinsic viscosity [η] of 0.61 vacuum-dried at 120 ° C. for 16 hours were melted with an extruder to obtain a molten polymer (fiber-forming component) at 280 ° C. A known core-sheath having 900 melt-hole capillaries having a diameter of 0.3 mm so that both melted polymers have a sheath component A of the former and a core component B of the latter and have a weight ratio of A: B = 65: 35. The mixture was melted and discharged from the composite spinneret. At this time, the die temperature was 285 ° C., and the discharge rate was 615 g / min. Further, the discharged polymer was air-cooled with a cooling air at 30 ° C. and wound at 1150 m / min to obtain an undrawn yarn. The undrawn yarn is drawn three times in warm water at 72 ° C., and then 0.2% by weight of an oil agent composed of lauryl phosphate potassium salt / polyoxyethylene modified silicone = 80/20 is applied. A flat zigzag type crimp having a shrinkage of 9.9 peaks / 25 mm and a crimp rate of 4.9% was provided, dried at 110 ° C., and then cut into a fiber length of 5 mm. The fineness of the obtained short fibers was 2.3 dtex, and the water content was 0.2% by weight.
[0048]
The texture of the nonwoven fabric sample prepared by the airlaid method was good and rated at level 1, and the unopened rate was 0.8% and the pulp shedding rate was good at 2.4%. The maximum spinning amount was 170 kg / hour. Also, there was no sticking of the web to the wire mesh of the net conveyor 7b of the suction dryer.
[0049]
[Example 2]
A high-density polyethylene (HDPE) chip with an MI of 21 g / 10 min and a Tm of 131 ° C. and a linear low-density polyethylene (LLDPE) chip with an MI of 52 g / 10 min and a Tm of 121 ° C. have an MI of 8 g / Modified polyethylene obtained by copolymerizing linear low-density polyethylene (LLDPE) having a Tm of 98 ° C. for 10 minutes with maleic anhydride at 0.20 mol / kg and methyl acrylate at 0.8 mol / kg. The MPE-1) chips were mixed at a ratio of 50:40:10, respectively, and melted with a twin-screw extruder to obtain a melt-mixed polymer at 250 ° C. The maleic anhydride content of the melt-blended polymer (the heat-adhesive component) was 0.02 mol / kg, and the MI was 27 g / 10 minutes. On the other hand, PET pellets having an intrinsic viscosity [η] of 0.61 vacuum-dried at 120 ° C. for 16 hours were melted with an extruder to obtain a molten polymer (fiber-forming component) at 280 ° C. A well-known core-sheath having 900 both round capillaries having a diameter of 0.3 mm so that the weight ratio of A: B = 60: 40 and the weight ratio of A: B = 60: 40. The mixture was melted and discharged from the composite spinneret. At this time, the die temperature was 285 ° C., and the discharge rate was 450 g / min. Further, the discharged polymer was air-cooled with a cooling air at 30 ° C. and wound at 1150 m / min to obtain an undrawn yarn. The undrawn yarn is drawn three times in warm water at 72 ° C., and then 0.2% by weight of an oil agent composed of lauryl phosphate potassium salt / polyoxyethylene modified silicone = 80/20 is applied. A flat zigzag type crimp having a shrinkage of 10.1 peaks / 25 mm and a crimp rate of 6.3% was provided, dried at 110 ° C., and then cut into a fiber length of 5 mm. The fineness of the obtained short fibers was 1.8 decitex, and the water content was 0.17% by weight.
[0050]
The formation of the nonwoven fabric sample prepared by the airlaid method was graded at level 1, and the unopened rate was 0.8% and the pulp shedding rate was good at 1.8%. The maximum spinning amount was 160 kg / hour, and there was no sticking of the web to the wire mesh of the net conveyor 7b of the suction dryer.
[0051]
[Comparative Example 1]
A high-density polyethylene (HDPE) chip having an MI of 20 g / 10 min and a Tm of 131 ° C. and a linear low-density polyethylene (LLDPE) having an MI of 8 g / 10 min and a Tm of 98 ° C. as a backbone polymer, and anhydrous maleic Modified polyethylene (MPE-1) chips in which acid was copolymerized at 0.20 mol / kg and methyl acrylate at 0.8 mol / kg were mixed at a ratio of 50:50, and melted with a twin-screw extruder. Thus, a melt-mixed polymer at 250 ° C. was obtained. The maleic anhydride content of the melt-blended polymer (the heat-adhesive component) was 0.10 mol / kg, and the MI was 13 g / 10 min. On the other hand, PET pellets having an intrinsic viscosity [η] of 0.61 vacuum-dried at 120 ° C. for 16 hours were melted with an extruder to obtain a molten polymer (fiber-forming component) at 280 ° C. A known core-sheath having 900 melt-hole capillaries having a diameter of 0.3 mm so that both melted polymers have a sheath component A of the former and a core component B of the latter and have a weight ratio of A: B = 65: 35. The mixture was melted and discharged from the composite spinneret. At this time, the die temperature was 285 ° C., and the discharge rate was 450 g / min. Further, the discharged polymer was air-cooled with a cooling air at 30 ° C. and wound at 1150 m / min to obtain an undrawn yarn. The undrawn yarn is drawn 2.8 times in warm water at 72 ° C., and then 0.2% by weight of an oil agent composed of lauryl phosphate potassium salt / polyoxyethylene modified silicone = 80/20 is applied. Then, a flat zigzag type crimp having a number of crimps of 11.1 peaks / 25 mm and a crimp rate of 7.2% was applied, dried at 110 ° C., and cut into a fiber length of 5 mm. The fineness of the obtained short fibers was 1.8 decitex, and the moisture content was 0.21% by weight.
[0052]
The pulp shedding rate of the nonwoven fabric sample prepared by the airlaid method was as good as 2.3%. However, the nonwoven fabric formation was rated at level 3, the unopened rate was 5.3%, and the maximum spinning amount was 75 kg / hour. The web adhered to the wire mesh of the net conveyor 7b of the suction dryer, and stable production was not possible.
[0053]
[Comparative Example 2]
Except that the polymer weight ratio of A: B was 45:55, the procedure was the same as in Example 1. The texture of the nonwoven fabric sample prepared by the airlaid method was good and rated at level 1, the unspread rate was 0.2%, and the maximum spinning amount was 185 kg / hour, but the pulp shedding rate was 10.1%. Met. Also, there was no sticking of the web to the wire mesh of the net conveyor 7b of the suction dryer.
[0054]
[Comparative Example 3]
Example 1 was repeated except that the number of crimps was 18 peaks / 25 mm and the crimp rate was 12.5%. The pulp shedding rate of the nonwoven fabric sample prepared by the airlaid method was 2.6%, and the maximum spinning amount was 155 kg / hour, which was good. However, the nonwoven fabric was rated at level 3, with an unopened rate of 3.4%. There was no sticking of the web to the wire mesh of the net conveyor 7b of the suction dryer.
[0055]
[Comparative Example 4]
The procedure was the same as in Example 1, except that the oil agent adhesion rate was 0.5% by weight. The pulp shedding rate of the nonwoven fabric sample prepared by the airlaid method was 5.6%, the maximum spinning amount was slightly worse at 130 kg / hour, the nonwoven fabric formation was rated at level 2, and the unspread rate was 2.9%. . There was no sticking of the web to the wire mesh of the net conveyor 7b of the suction dryer.
[0056]
[Comparative Example 5]
Example 1 was repeated except that the water content was changed to 0.5% by weight. The pulp shedding rate of the nonwoven fabric sample prepared by the airlaid method was 2.2%, which was no problem. However, the nonwoven fabric was rated at level 2, the unspread rate was 4.9%, and the maximum spinning rate was 100 kg / hour. There was no sticking of the web to the wire mesh of the net conveyor 7b of the suction dryer.
[0057]
【The invention's effect】
The heat-adhesive conjugate fiber of the present invention not only has good adhesiveness to the cellulosic fiber, but also allows the airlaid nonwoven fabric to have a uniform texture according to the conjugate fiber. For this reason, a very high-quality nonwoven fabric can be produced from the conjugate fiber of the present invention. Further, according to the composite fiber, the spinning amount at the time of air-laid molding can be increased, and since there is no sticking to the wire mesh even by thermal bonding by a hot air air through method, it is possible to efficiently and stably produce an air-laid nonwoven fabric. , Its industrial value is extremely high. In addition, the conjugate fiber of the present invention also has an effect of providing a thermoadhesive fiber which is less expensive than the conventional one, since the denatured amount of the modified polyolefin as the heat adhesive component is small.
[Brief description of the drawings]
FIG. 1 is a side view of an apparatus for producing a nonwoven fabric of the present invention.
[Explanation of symbols]
1 Web forming head
2 Cotton circulation duct
3 Cotton circulation duct
4a Forming drum (cylindrical screen)
5a Forming drum (cylindrical screen)
4b Needle roll
5b Needle roll
6 Web
7a Net conveyor
7b Net conveyor
8 Suction device
9 Web compression roll
10 Suction dryer
11 Non-woven fabric
12 Take-up roll

Claims (4)

不飽和カルボン酸または不飽和カルボン酸無水物を有するビニルモノマーがグラフト共重合された変成ポリオレフィン、または、該変成ポリオレフィンと他のポリマーとの混合ポリマーを熱接着性成分とし、該変成ポリオレフィンより融点の高いポリマーを繊維形成性成分とし、少なくとも該熱接着成分が表面に露出するように両成分が複合化された熱接着性複合繊維であって、該繊維表面に油剤が付着し、下記(1)〜(7)を満足していることを特徴とするエアレイド不織布用熱接着性複合繊維。
(1)不飽和カルボン酸または不飽和カルボン酸無水物を有するビニルモノマーの含有率が熱接着性成分の重量に対して0.005〜0.04モル/kg
(2)熱接着性成分のメルトインデックスが15〜200g/10分
(3)熱接着性成分の複合繊維に占める割合が55〜95重量%
(4)繊維長が2〜30mm
(5)捲縮数が13山/25mm以下、捲縮率が11%以下
(6)油剤付着率が0.01〜0.30重量%
(7)水分率が0.5重量%以下
A modified polyolefin in which a vinyl monomer having an unsaturated carboxylic acid or an unsaturated carboxylic anhydride is graft-copolymerized, or a mixed polymer of the modified polyolefin and another polymer is used as a heat-adhesive component, and has a melting point higher than that of the modified polyolefin. A heat-adhesive conjugate fiber in which a high polymer is used as a fiber-forming component and both components are compounded so that at least the heat-adhesive component is exposed on the surface, and an oil agent adheres to the fiber surface, and the following (1) A heat-adhesive conjugate fiber for an airlaid nonwoven fabric, which satisfies (7).
(1) The content of the vinyl monomer having an unsaturated carboxylic acid or an unsaturated carboxylic acid anhydride is 0.005 to 0.04 mol / kg based on the weight of the heat-adhesive component.
(2) The melt index of the heat-adhesive component is 15 to 200 g / 10 min. (3) The ratio of the heat-adhesive component to the composite fiber is 55 to 95% by weight.
(4) The fiber length is 2 to 30 mm
(5) The number of crimps is 13 peaks / 25 mm or less, the crimp rate is 11% or less. (6) The oil agent adhesion rate is 0.01 to 0.30% by weight.
(7) Moisture percentage is 0.5% by weight or less
不飽和カルボン酸または不飽和カルボン酸無水物を有するビニルモノマーが、無水マレイン酸である請求項1記載のエアレイド不織布用熱接着性複合繊維。The heat-adhesive conjugate fiber for an airlaid nonwoven fabric according to claim 1, wherein the vinyl monomer having an unsaturated carboxylic acid or an unsaturated carboxylic acid anhydride is maleic anhydride. 熱接着性複合繊維が、熱接着性成分を鞘、繊維形成性成分を芯とする芯鞘型複合繊維である請求項1または2記載のエアレイド不織布用熱接着性複合繊維。The heat-adhesive conjugate fiber for airlaid nonwoven fabric according to claim 1 or 2, wherein the heat-adhesive conjugate fiber is a core-sheath conjugate fiber having a heat-adhesive component as a sheath and a fiber-forming component as a core. 繊維形成性成分がポリエチレンテレフタレートである請求項1〜3のいずれかに記載のエアレイド不織布用熱接着性複合繊維。The heat-adhesive conjugate fiber for an air-laid nonwoven fabric according to any one of claims 1 to 3, wherein the fiber-forming component is polyethylene terephthalate.
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