JPH01221558A - Stretchable nonwoven cloth and production thereof - Google Patents
Stretchable nonwoven cloth and production thereofInfo
- Publication number
- JPH01221558A JPH01221558A JP63045348A JP4534888A JPH01221558A JP H01221558 A JPH01221558 A JP H01221558A JP 63045348 A JP63045348 A JP 63045348A JP 4534888 A JP4534888 A JP 4534888A JP H01221558 A JPH01221558 A JP H01221558A
- Authority
- JP
- Japan
- Prior art keywords
- web
- fibers
- entangled
- water
- weight
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000004519 manufacturing process Methods 0.000 title claims description 7
- 239000004744 fabric Substances 0.000 title abstract description 6
- 239000000835 fiber Substances 0.000 claims abstract description 54
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 15
- 238000011084 recovery Methods 0.000 claims abstract description 7
- 239000004745 nonwoven fabric Substances 0.000 claims description 24
- 239000002131 composite material Substances 0.000 claims description 15
- 239000000853 adhesive Substances 0.000 claims description 12
- -1 polypropylene Polymers 0.000 claims description 9
- 239000004743 Polypropylene Substances 0.000 claims description 7
- 229920001155 polypropylene Polymers 0.000 claims description 7
- 238000007664 blowing Methods 0.000 claims description 3
- 238000010438 heat treatment Methods 0.000 abstract description 11
- 230000000694 effects Effects 0.000 abstract description 2
- 239000002994 raw material Substances 0.000 abstract description 2
- 238000005422 blasting Methods 0.000 abstract 1
- 230000001747 exhibiting effect Effects 0.000 abstract 1
- 238000005188 flotation Methods 0.000 abstract 1
- 239000000203 mixture Substances 0.000 abstract 1
- 238000002844 melting Methods 0.000 description 10
- 230000008018 melting Effects 0.000 description 10
- 230000000052 comparative effect Effects 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 238000009987 spinning Methods 0.000 description 4
- 230000037303 wrinkles Effects 0.000 description 4
- 229920000728 polyester Polymers 0.000 description 3
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 2
- 229920001577 copolymer Polymers 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000000123 paper Substances 0.000 description 2
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- SGTNSNPWRIOYBX-UHFFFAOYSA-N 2-(3,4-dimethoxyphenyl)-5-{[2-(3,4-dimethoxyphenyl)ethyl](methyl)amino}-2-(propan-2-yl)pentanenitrile Chemical compound C1=C(OC)C(OC)=CC=C1CCN(C)CCCC(C#N)(C(C)C)C1=CC=C(OC)C(OC)=C1 SGTNSNPWRIOYBX-UHFFFAOYSA-N 0.000 description 1
- 229920000742 Cotton Polymers 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- 239000004952 Polyamide Substances 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 229920000297 Rayon Polymers 0.000 description 1
- 239000004433 Thermoplastic polyurethane Substances 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- QZPSXPBJTPJTSZ-UHFFFAOYSA-N aqua regia Chemical compound Cl.O[N+]([O-])=O QZPSXPBJTPJTSZ-UHFFFAOYSA-N 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 238000009960 carding Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000007334 copolymerization reaction Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000002594 fluoroscopy Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000012943 hotmelt Substances 0.000 description 1
- 239000002655 kraft paper Substances 0.000 description 1
- 238000000691 measurement method Methods 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920005629 polypropylene homopolymer Polymers 0.000 description 1
- 229920006306 polyurethane fiber Polymers 0.000 description 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- 229920001384 propylene homopolymer Polymers 0.000 description 1
- 239000002964 rayon Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 229920006027 ternary co-polymer Polymers 0.000 description 1
- 229920002803 thermoplastic polyurethane Polymers 0.000 description 1
- 239000002759 woven fabric Substances 0.000 description 1
- 239000004711 α-olefin Substances 0.000 description 1
Landscapes
- Nonwoven Fabrics (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明はサポータ−1包帯、パップ剤基布等の用途に好
適な柔軟で伸縮性に優れた不織布及びその製造方法に関
する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a flexible and highly stretchable nonwoven fabric suitable for uses such as Supporter-1 bandages and poultice base fabrics, and a method for producing the same.
従来から伸縮性不織布には各種の製造方法があり、熱可
塑性ポリウレタン繊維を用いるもの(特開昭59−15
7362号)、高捲縮性のポリエステル懺維をホットメ
ルト型バインダー繊維で熱接着したもの(特開昭62−
177269号)等が例示できる。There have been various manufacturing methods for stretchable nonwoven fabrics, including those using thermoplastic polyurethane fibers (Japanese Patent Laid-Open No. 59-15
No. 7362), highly crimpable polyester fibers thermally bonded with hot-melt binder fibers (JP-A No. 62-
177269) and the like.
しかしながら、ポリウレタン繊維を用いた不織布は比重
が大きいことや風合がゴム様のペタツキ感を示すという
難点があシ、ポリエステル繊維を用いた場合には風合が
硬すぎるという欠点がある。However, nonwoven fabrics using polyurethane fibers have drawbacks such as high specific gravity and a flat, rubber-like feel, while polyester fibers have the drawback of being too hard.
本発明は柔軟でペタツキ感が無く、かつ伸縮性に優れた
不織布の製造方法を提供するにある。The present invention provides a method for producing a nonwoven fabric that is flexible, does not have a sticky feeling, and has excellent stretchability.
すなわち本願第1の発明は低温ウェブ収縮率が15%以
下で、高温ウェブ収縮率が50%以上であるようなポリ
プロピレン系の熱接着性複合繊維70重量係以上と、他
の有機繊維30重重量風下を用いて均質のウェブを作シ
、該ウェブに水流を噴射して繊維を互に絡合させた絡合
ウェブとし、次いで含水状態の絡合ウェブを無緊張状態
で搬送しながらその表裏両面に150℃以上の熱風を交
互・多段に吹付けることにより、絡合ウェブを遊動させ
ながら収縮の発生と繊維相互の接着を行なわせることに
より得られる30%伸長時の弾性回復率が縦方向・横方
向共に80%以上である伸縮性不織布及びその製造方法
である。That is, the first invention of the present application is a polypropylene-based thermoadhesive composite fiber having a low-temperature web shrinkage rate of 15% or less and a high-temperature web shrinkage rate of 50% or more, and 70% by weight or more, and other organic fibers of 30% by weight. A homogeneous web is produced using a leeward direction, a water jet is jetted onto the web to form an entangled web in which the fibers are intertwined with each other, and then the front and back sides of the entangled web in a water-containing state are conveyed in a non-tensioned state. By blowing hot air of 150°C or higher alternately and in multiple stages, the entangled web is allowed to move while causing shrinkage and mutual adhesion of the fibers.The elastic recovery rate at 30% elongation is A stretchable nonwoven fabric having a stretchability of 80% or more in both the transverse directions and a method for producing the same.
本発明において不織布の主成分として用いるポリプロピ
レン系の熱接着性複合繊維は、融点の異る2種のポリプ
ロピレン系樹脂を並列型に、あるいはその低融点の樹脂
を鞘成分とするように偏心鞘芯型に配して複合紡糸した
繊維であって、該複合繊維を70重重量%以上含有する
ウェブの熱収縮率が、100’C5分間の加熱では15
%以下であシ、150℃5分間の加熱では50%以上で
あるような複合繊維である。このような熱接着性複合繊
維の高融点成分としてMFRが2〜7oの結晶性ポリプ
ロピレン(ホモポリマー)、好ましくは分子量分布の指
標のQ値が5以下のプロピレンホモポリマーが用いられ
、低融点成分として、プロピレンを主成分としエチレン
、ブテン−1等の他のα−オレフィンを共重合成分とす
る二元系あるいは三元系の共重合体、好ましくは前記高
融点成分より融点が15℃以上低い共重合体が用いられ
る。この両成分の選択・組み合せおよび紡糸・延伸条件
の選択によシ、熱接着性複合繊維のウェブの熱収縮率を
所望の値とすることができる。また熱接着性複合繊維は
後述のウェブの製造を容易にするために機械捲縮を付与
することが望ましい。In the present invention, the polypropylene thermoadhesive composite fiber used as the main component of the nonwoven fabric is made of two types of polypropylene resins with different melting points in parallel, or with an eccentric sheath-core so that the resin with a low melting point is used as the sheath component. The heat shrinkage rate of a web containing 70% by weight or more of composite fibers, which is composite fibers arranged in a mold and spun, is 15 when heated at 100'C for 5 minutes.
% or less, and 50% or more when heated at 150° C. for 5 minutes. A crystalline polypropylene (homopolymer) having an MFR of 2 to 7o, preferably a propylene homopolymer having a Q value of 5 or less, which is an index of molecular weight distribution, is used as a high melting point component of such a heat-adhesive composite fiber, and a low melting point component is used. A binary or ternary copolymer containing propylene as the main component and other α-olefins such as ethylene and butene-1 as a copolymerization component, preferably having a melting point 15°C or more lower than the high melting point component. Copolymers are used. By selecting/combining these two components and selecting the spinning/drawing conditions, the heat shrinkage rate of the web of heat-adhesive conjugate fibers can be set to a desired value. Further, it is desirable that the heat-adhesive conjugate fibers be mechanically crimped in order to facilitate the production of the web described below.
このようにして得られた熱接着性複合繊維はそれ自身単
独で、あるいは他の有機繊維と混合してウェブとする。The thermoadhesive conjugate fiber thus obtained is made into a web either alone or mixed with other organic fibers.
ここで他の有機繊維とは、木綿、麻、レーヨン、ポリア
ミド、ポリエステル等の有機繊維であって、後述の熱処
理によって変質しないものを指し、製品の風合、吸水性
等の改善の目的で使用される。このような他の有機繊維
のウェブ中の含量が30重量係を超すと、熱接着性複合
繊維による接着点が過少となシネ織布強力が低下したり
、ウェブの収縮率が低下して不織布の伸縮性が不充分と
なる等の結果を生ずるので好ましくない。ウェブの製造
にはカード機や気流式ランダムウニバー等公知の方法が
利用でき、更にクロスラッパーを用いてクロスラッパー
ウェブとしても良い。Here, other organic fibers refer to organic fibers such as cotton, linen, rayon, polyamide, and polyester that do not change in quality through heat treatment described below, and are used for the purpose of improving the texture, water absorption, etc. of products. be done. If the content of such other organic fibers in the web exceeds 30% by weight, the bonding points of the heat-adhesive composite fibers will be too few and the strength of the cine woven fabric will decrease, and the shrinkage rate of the web will decrease, resulting in a non-woven fabric. This is not preferable because it results in insufficient elasticity. A known method such as a card machine or an air flow random univer can be used to produce the web, and a crosslapper web may also be produced using a crosslapper.
次に、上記ウェブに多数のノズルよシ噴出す、る高王水
を吹き付けて繊維相互に絡合を発生させる。Next, high aqua regia is sprayed onto the web from a number of nozzles to cause the fibers to become entangled with each other.
このような水流絡合の方法としては、特開昭62−22
3355号公報あるいは特開昭59−26561号公報
に開示されたものが利用できる。A method of such hydroentanglement is disclosed in Japanese Patent Application Laid-Open No. 62-22
3355 or Japanese Patent Laid-Open No. 59-26561 can be used.
上記水流絡合処理を受けたウェブ(以下絡合ウェブ)は
含水状態のまま後続の熱処理工程に搬送される。熱処理
工程において、絡合ウェブは無緊張状態で搬送されなが
ら表裏両面よシ熱風により加熱される。この熱処理を行
う装置の1例の模式図である第1図によって具体的に説
明する。一定間隔を保って走行する一対のガイドネット
(2)、(2γの間に送シ込まれた含水状態の絡合ウェ
ブ(1)は、ウェブの幅方向に長くスリット状に開口し
た熱風吹出口(3)、(3)′よシ絡合ウェブの表裏両
面に交互に吹きつけられる熱風によりガイドネット(2
)、<2Yと接触しその摩擦力によシ蛇行しながら搬送
される。The web that has undergone the hydroentanglement treatment (hereinafter referred to as an entangled web) is transported to the subsequent heat treatment step while still containing water. In the heat treatment process, the entangled web is heated by hot air on both the front and back surfaces while being conveyed without tension. A detailed explanation will be given with reference to FIG. 1, which is a schematic diagram of an example of an apparatus for performing this heat treatment. A pair of guide nets (2) running at a constant interval, the tangled web (1) in a water-containing state fed between (2γ) has a hot air outlet opening in the shape of a long slit in the width direction of the web. (3), (3)' The guide net (2
), <2Y and is conveyed in a meandering manner due to the frictional force.
この搬送の間に絡合ウェブは乾燥され、熱接着性複合繊
維の収縮発生と熱接着が行なわれ伸縮性不織布(4)と
して取出される。ガイドネット(2J 、(Zl’の間
隔は絡合ウェブの厚みの2〜200倍、好ましくは5〜
20倍のものが用いられる。During this conveyance, the entangled web is dried, the heat-adhesive conjugate fibers undergo shrinkage and heat bonding, and are taken out as a stretchable nonwoven fabric (4). Guide net (2J, (Zl' spacing is 2 to 200 times the thickness of the entangled web, preferably 5 to
20 times as large is used.
本発明において不織布の主構成繊維として100℃5分
間の加熱によるウェブの熱収縮率が15%以下であるよ
うな熱接着性複合繊維を用い、かつ含水状態の絡合ウェ
ブとして熱処理を行うため、熱処理時に発生しゃすいウ
ェブの急激な収縮およびこれに基づく不織布の密度斑や
シワの発生が防止されている。また、熱接着性複合繊維
は150℃5分間の加熱によるウェブの収縮率が50%
以上であり、かつ無緊張状態で搬送されながら熱処理を
受けることから、得られる不織布は充分に捲縮の発生し
た複合繊維が互に接点で融着した構造となり、縦横いず
れの方向にも30%伸長後の弾性回復率が80%以上で
あるような伸縮性の大きな不織布となる。このような不
織布は、15〜30097 m”の低目付のものでは包
帯、紙おしめの表面材、衣料用芯地等の用途に、また3
00〜1000 j! / rrlの高目付のものでは
椅子やベツドの詰物あるいは包装用バッキング材の用途
に有用である。In the present invention, heat-adhesive conjugate fibers are used as the main constituent fibers of the nonwoven fabric, and the heat shrinkage rate of the web is 15% or less when heated at 100°C for 5 minutes, and heat treatment is performed as an entangled web in a water-containing state. Rapid shrinkage of the web that occurs during heat treatment and the resulting density unevenness and wrinkles in the nonwoven fabric are prevented. In addition, the thermal adhesive composite fiber has a web shrinkage rate of 50% when heated at 150°C for 5 minutes.
As above, and since the nonwoven fabric is heat-treated while being conveyed without tension, the resulting nonwoven fabric has a structure in which sufficiently crimped composite fibers are fused to each other at the contact points, and 30% in both the vertical and horizontal directions. The result is a highly stretchable nonwoven fabric with an elastic recovery rate of 80% or more after stretching. Such non-woven fabrics have a low basis weight of 15 to 30,097 m" and are used for applications such as bandages, surface materials for paper diapers, interlining for clothing, etc.
00~1000 j! /rrl high basis weight is useful for filling chairs and beds or as a backing material for packaging.
実施例および比較例によシ本発明をさらに具体的に説明
する。なお、各側で用いた物性測定方法を一括して以下
に示す。The present invention will be explained in more detail with reference to Examples and Comparative Examples. The physical property measurement methods used on each side are summarized below.
ウェブの熱収縮率:ガード機を用いて作った目付100
g/イのランダムウェブよシ縦25cmX横25cIn
の正方形の試料片を切シ取シ、クラフト紙(25cII
LX 25m )に挟んで所定温度(100℃、150
℃)の乾燥話中に5分間放置後、室温で30分間冷却し
、その面積(Scrl”)を測定し、下式よシ算出する
。5個の試料の平均値で表わす。Heat shrinkage rate of web: Fabric weight 100 made using a guard machine
G/I's random web 25cm long x 25cm wide
Cut out a square sample piece from kraft paper (25cII).
LX 25m) at a specified temperature (100℃
℃) for 5 minutes, then cooled at room temperature for 30 minutes, and the area (Scrl'') was measured and calculated using the following formula. It is expressed as the average value of 5 samples.
ウェブの熱収縮率(ト)=I00X(625−8)/6
25不織布の弾性回復率:不織布の縦方向あるいは横方
向に長さ15cl1幅2.5 cmの試料片を切シ取シ
、定速伸長型の自記式引張試験器を用い、つかみ間隔1
0cIIL、引張速度10cIrL/mで3cILだけ
伸長しそのまま1分間放置後、10α/Mの速度で弛緩
させる。この弛緩の過程で応力が零になった時点の残存
伸び(Am)を記録紙より読み取シ、下式より算出する
。縦、横共に5個の試料の平均値で表わす。Heat shrinkage rate of web (g)=I00X(625-8)/6
25 Elastic recovery rate of non-woven fabric: Cut a sample piece of 15 cm long and 2.5 cm wide in the vertical or horizontal direction of the non-woven fabric.
It was stretched by 3 cIL at 0 cIIL and a tensile rate of 10 cIrL/m, left as it was for 1 minute, and then relaxed at a rate of 10α/M. The residual elongation (Am) at the time when the stress becomes zero during this relaxation process is read from the recording paper and calculated using the following formula. Both vertical and horizontal values are expressed as the average value of 5 samples.
不織布の均一性:25cmX25cmの正方形の試料片
4枚の表裏両面の平滑性の観察および蛍光灯下での透視
による密度斑の観察を行い、下記の基準により区分する
。Uniformity of nonwoven fabric: Observe the smoothness of both the front and back surfaces of four 25 cm x 25 cm square sample pieces, and observe the density irregularities by fluoroscopy under a fluorescent lamp, and classify them according to the following criteria.
良:4枚共に表面に皺が無くかつ密度斑が無いもの
可:4枚のうち1枚に、表面の皺または密度斑が認めら
れるもの
不可:表面の皺または密度斑の認められるものが4枚の
うち2枚以上あるもの
実施例1〜6、比較例1〜3
第1表に示した各種の高融点のポリプロピレンと低融点
のプロピレン系共重合体またはポリエチレンとの組み合
せで複合紡糸し、種々の複合繊維を得た。紡糸条件はい
ずれの場合も下記の同一条件とした。Good: All 4 sheets have no wrinkles or density spots on the surface. Acceptable: 1 of the 4 sheets has wrinkles or density spots on the surface. Not acceptable: 4 sheets have wrinkles or density spots on the surface. Examples 1 to 6, Comparative Examples 1 to 3 Composite spinning of a combination of various high melting point polypropylenes and low melting point propylene copolymers or polyethylene shown in Table 1, Various composite fibers were obtained. The spinning conditions were the same as described below in both cases.
紡糸口金は、ノズル孔径0.6m、ノズル数120個、
複合比1対1、紡糸温度高融点側280’C1低融点側
240℃であシ、得られた未延伸系を70℃の第1段セ
ブンロールと35℃の第2段セブンロールの間で4.4
倍に延伸し単糸繊度3 d/fの延伸糸とし、総デニー
ル12,000のトウに収束した後、スタフィンボック
ス式クリンパ−で12山725Bの捲縮を付与した後、
繊維長65龍に切断してステープル繊維とした。The spinneret has a nozzle hole diameter of 0.6 m and 120 nozzles.
The composite ratio was 1:1, the spinning temperature was 280'C on the high melting point side and 240'C on the low melting point side. 4.4
After drawing the yarn to double its original size and converging it into a tow with a total denier of 12,000, it was crimped with 12 threads of 725B using a stuffing box crimper.
The fibers were cut into fiber lengths of 65 mm to obtain staple fibers.
上記ステープル繊維をカード機を通して、実施例1〜4
および比較例1〜3では目付40 fi / trlの
ランダムウェブとし、実施例5.6では目付4oy/r
r?のクロスラッパーウェブとした。Examples 1 to 4 The above staple fibers were passed through a carding machine.
In Comparative Examples 1 to 3, a random web with a basis weight of 40 fi/trl was used, and in Example 5.6, a basis weight of 4oy/r was used.
r? It was made into a cross wrapper web.
次に、これらのウェブを水流噴射絡合装置に移送し、孔
径0.15mm、ピッチ1.0龍の多数のノズルから3
0に9/citの高圧水を噴きつけ、移送速度30m/
mで水流絡合を付与し、含水率(水分重量/繊維重量比
)約110%の絡合ウェブとし、引き続き第1図に示し
たような熱処理装置(ベルト間隔18冨り長さ4.5m
、熱風吹出口35個)を用い熱風温度150℃1滞留時
間1分50秒で熱処理し不織布とした。These webs are then transferred to a water-jet entangling device, where 3
Spray high-pressure water at 9/cit on 0, transfer speed 30m/
Hydroentanglement was applied at 100 m to form an entangled web with a moisture content (moisture weight/fiber weight ratio) of approximately 110%, followed by a heat treatment apparatus as shown in Fig. 1 (belt spacing: 18, depth: 4.5 m).
A nonwoven fabric was obtained by heat treatment using a hot air outlet (35 hot air outlets) at a temperature of 150° C. and a residence time of 1 minute and 50 seconds.
上記各側で用いた熱接着性複合繊維の性状ならびに得ら
れた不織布の性状を第2表に示した。また、上記の各熱
接着性複合繊維の熱収縮挙動(ウェブ面積収縮率)を第
2図に示した。Table 2 shows the properties of the heat-adhesive conjugate fibers used on each side and the properties of the obtained nonwoven fabric. Further, the heat shrinkage behavior (web area shrinkage rate) of each of the above heat-adhesive conjugate fibers is shown in FIG.
第 1 表 第2表に示された結果から以下のことが明らかとなる。Chapter 1 Table The following becomes clear from the results shown in Table 2.
低温ウェブ収縮率が小さく、かつ、高温ウェブ収縮率が
大きなポリプロピレン系熱接着性複合繊維を用いた実施
例1〜6において、得られた不織布の30%伸長後の弾
性回復率は縦方向、横方向共に90%以上であシ、原料
ウェブがランダムウェブであっても(実施例1〜4)、
クロスラッパーウェブであっても同様の結果が得られた
。In Examples 1 to 6, in which polypropylene thermoadhesive composite fibers having a small low-temperature web shrinkage rate and a large high-temperature web shrinkage rate were used, the elastic recovery rates after 30% elongation of the obtained nonwoven fabrics were as follows: 90% or more in both directions, even if the raw material web is a random web (Examples 1 to 4),
Similar results were obtained for cross-wrapper webs.
低温ウェブ収縮率が大きな熱接着性複合繊維を用いた比
較例1.2では、得られる不織布は均一性が劣り、高温
ウェブ収縮率の低い熱接着性複合繊維を用いた比較例2
.3では得られる不織布は弾性回復率が劣ったものであ
る。In Comparative Example 1.2 using heat-adhesive conjugate fibers with a high low-temperature web shrinkage rate, the resulting nonwoven fabric was poor in uniformity, and in Comparative Example 2 using heat-adhesive conjugate fibers with a low high-temperature web shrinkage rate.
.. The nonwoven fabric obtained in Sample No. 3 had an inferior elastic recovery rate.
【図面の簡単な説明】
第1図は実施例で用いた熱処理装置の概念図、第2図は
実施例で用いた複合繊維の熱収縮挙動を示すグラフであ
る。
以上
第2回
手 続 補 正 書BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a conceptual diagram of the heat treatment apparatus used in the examples, and FIG. 2 is a graph showing the thermal shrinkage behavior of the composite fibers used in the examples. Amendment to the above second proceedings
Claims (2)
率が50%以上であるようなポリプロピレン系の熱接着
性複合繊維70重量%以上と、他の有機繊維30重量%
以下を用いて均質のウエブを作り、該ウエブに水流を噴
射して繊維を互に絡合させた絡合ウエブとし、次いで含
水状態の絡合ウエブとし、次いで含水状態の絡合ウエブ
を無緊張状態で搬送しながらその表裏両面に150℃以
上の熱風を交互・多段に吹付けることにより、絡合ウエ
ブを遊動させながら収縮の発生と繊維相互の接着を行う
ことによつて得られる30%伸長の弾性回復率が縦方向
、横方向共に80%以上であることを特徴とする伸縮性
不織布。(1) 70% by weight or more of polypropylene-based thermoadhesive composite fibers with a low-temperature web shrinkage rate of 15% or less and a high-temperature web shrinkage rate of 50% or more, and 30% by weight of other organic fibers.
A homogeneous web is made using the following, a water jet is jetted onto the web to form an entangled web in which the fibers are entangled with each other, then an entangled web in a water-containing state is made, and then the entangled web in a water-containing state is made into an unstrained web. 30% elongation achieved by blowing hot air of 150°C or higher alternately and in multiple stages on both the front and back sides of the web while transporting it, causing shrinkage and mutual adhesion of fibers while allowing the entangled web to move freely. A stretchable nonwoven fabric having an elastic recovery rate of 80% or more in both the longitudinal and transverse directions.
縮率が50%以上であるようなポリプロピレン系の熱接
着性複合繊維70重量%以上と、他の有機繊維30重量
%以下を用いて均質のウエブを作り、該ウエブに水流を
噴射して繊維を互に絡合させた絡合ウエブとし、次いで
含水状態の絡合ウエブを無緊張状態で搬送しながらその
表裏両面に150℃以上の熱風を交互・多段に吹付ける
ことにより、絡合ウエブを遊動させながら収縮の発生と
繊維相互の接着を行なわせることを特徴とする伸縮性不
織布の製造方法。(2) Using 70% by weight or more of polypropylene-based heat-adhesive composite fibers with a low-temperature web shrinkage rate of 15% or less and a high-temperature web shrinkage rate of 50% or more, and 30% by weight or less of other organic fibers. A homogeneous web is made, a water jet is jetted onto the web to form an entangled web in which the fibers are entangled with each other, and then the front and back surfaces of the entangled web are heated at 150°C or higher while conveying the water-containing entangled web in a non-tensioned state. A method for producing a stretchable nonwoven fabric, characterized by blowing hot air alternately and in multiple stages to cause shrinkage and mutual adhesion of fibers while allowing entangled webs to move freely.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63045348A JPH0811861B2 (en) | 1988-02-27 | 1988-02-27 | Stretchable nonwoven fabric and method for producing the same |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63045348A JPH0811861B2 (en) | 1988-02-27 | 1988-02-27 | Stretchable nonwoven fabric and method for producing the same |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH01221558A true JPH01221558A (en) | 1989-09-05 |
JPH0811861B2 JPH0811861B2 (en) | 1996-02-07 |
Family
ID=12716775
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63045348A Expired - Fee Related JPH0811861B2 (en) | 1988-02-27 | 1988-02-27 | Stretchable nonwoven fabric and method for producing the same |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0811861B2 (en) |
-
1988
- 1988-02-27 JP JP63045348A patent/JPH0811861B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH0811861B2 (en) | 1996-02-07 |
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