JPS6015747B2 - Method for manufacturing fiber structures - Google Patents

Method for manufacturing fiber structures

Info

Publication number
JPS6015747B2
JPS6015747B2 JP51049187A JP4918776A JPS6015747B2 JP S6015747 B2 JPS6015747 B2 JP S6015747B2 JP 51049187 A JP51049187 A JP 51049187A JP 4918776 A JP4918776 A JP 4918776A JP S6015747 B2 JPS6015747 B2 JP S6015747B2
Authority
JP
Japan
Prior art keywords
component
weight
surfactant
polyolefin
aqueous solution
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.)
Expired
Application number
JP51049187A
Other languages
Japanese (ja)
Other versions
JPS52132192A (en
Inventor
洋文 佐野
潤洋 中川
孝夫 赤木
晧二 平松
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kuraray Co Ltd
Original Assignee
Kuraray Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kuraray Co Ltd filed Critical Kuraray Co Ltd
Priority to JP51049187A priority Critical patent/JPS6015747B2/en
Publication of JPS52132192A publication Critical patent/JPS52132192A/en
Publication of JPS6015747B2 publication Critical patent/JPS6015747B2/en
Expired legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明は繊維構造物の製造方法であり、より詳しくはポ
リオレフィンとポリエステルから成る複合繊維を2の重
量%以上含有する構造物を非溶剤系で処理することによ
ってポリオレフィンを容易に除去して成る繊維構造物の
製造方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention is a method for producing a fibrous structure, and more specifically, a structure containing 2% or more by weight of composite fibers consisting of polyolefin and polyester is treated with a non-solvent system to produce polyolefin. The present invention relates to a method for manufacturing a fiber structure that can be easily removed.

従来、2成分以上からなる複合繊維から構造物を作り、
その後に1成分を除去することは次の目的でいまいま行
われている。
Traditionally, structures were made from composite fibers consisting of two or more components.
The subsequent removal of one component is currently being carried out for the following purposes.

■ 極細繊維を得る場合、紡糸延伸を直接行うと毛羽や
断糸等のトラブルが多発するので、海島構造繊維として
級糸延伸した後に海成分を抽出除去して極細繊維を得る
■ When obtaining ultrafine fibers, direct spinning and drawing often causes problems such as fuzz and yarn breakage, so after drawing grade yarns as sea-island structure fibers, the sea component is extracted and removed to obtain ultrafine fibers.

■ 海島構造繊維の海成分又はコンジュゲート繊維の1
成分の存在を有効利用し工程の簡略化を計る。
■ Sea component of sea-island structure fiber or conjugate fiber 1
Effectively utilize the presence of ingredients to simplify the process.

例えば海成分を糊剤又は接着剤の代りに用い特殊性能を
有する糸として使用する。■ 極細繊維又は特殊断面繊
維のシート、不織布の製造、紡績及び製編織は困難な点
が多いので、海島構造繊維又はコンジュゲート繊維で構
造物を製造した後にポリオレフィンである一成分を分離
除去し、極細繊維又は特殊断面繊維からなるシート、不
織布、織物又は編物を得る。
For example, sea ingredients can be used in place of sizing agents or adhesives and used as threads with special properties. ■ Manufacturing, spinning, weaving, and weaving of ultrafine fibers or special cross-section fiber sheets and nonwoven fabrics are difficult, so after manufacturing structures using sea-island structural fibers or conjugate fibers, one component, which is polyolefin, is separated and removed. A sheet, nonwoven fabric, woven fabric, or knitted fabric made of ultrafine fibers or fibers with a special cross section is obtained.

従来、これらポリオレフィンの除去方法はポリエステル
と溶剤抽出性の異なる点を利用してテトラクロルエチレ
ン,トリクロルエチレン,トルヱン,キシレン、nーヘ
プタンなどの有機溶剤による抽出法がとられていたが、
有機溶剤による毒性、危険性の問題さらには回収と環境
汚染の問題があり、これらを工業的規模で行うには上記
問題を解決した設備と充分な運転管理が必要であった。
また特閥昭50‐13620に見られる如く、二成分か
らなる複合織総又はその構造物に界面活性剤を付着せし
めた後、フェーノール、ベンジンアルコールなどの水溶
液で処理し二成分を分離、フィブリル化する方法もある
が、本発明の如く界面活性剤水溶液のみで一成分のポリ
オレフインを水溶液中に分散せしめ完全に分離除去する
方法は皆無である。本発明者らは長年にわたり鋭意研究
を重ねた結果、毒性や危険性が全くなく特別な設備も必
要としない水系で一成分を除去するという画期的な方法
を見出した。
Conventionally, methods for removing these polyolefins have been extraction methods using organic solvents such as tetrachloroethylene, trichlorethylene, toluene, xylene, n-heptane, etc., taking advantage of the difference in solvent extractability from polyesters.
There are problems of toxicity and danger due to organic solvents, as well as problems of recovery and environmental pollution, and in order to conduct these on an industrial scale, equipment that solves the above problems and sufficient operational management are required.
In addition, as seen in Tokubatsu 13620-1980, a composite fabric consisting of two components or its structure is coated with a surfactant, and then treated with an aqueous solution of phenol, benzine alcohol, etc. to separate the two components and form fibrils. However, there is no method to completely separate and remove one component of polyolefin by dispersing it in an aqueous solution using only an aqueous surfactant solution as in the present invention. As a result of extensive research over many years, the present inventors have discovered an innovative method for removing one component using an aqueous system that is completely non-toxic and dangerous and does not require any special equipment.

すなわち、一成分Aがポリオレフィン、他成分Bがポリ
エステルからなる複合繊維を2の重量%以上含有する構
造物を、0.01重量%以上の界面活性剤を含む水溶液
に浸潰し、麓梓下で、A成分の融点以上、B成分の融点
未満の温度の水溶液で処理することによって、誠に驚く
べきことにポリオレフィンを構造物中から除去すること
が可能であることを発見したのである。
That is, a structure containing 2% by weight or more of composite fibers in which one component A is polyolefin and the other component B is polyester is immersed in an aqueous solution containing 0.01% by weight or more of a surfactant, and then placed under the foot of Azusa. It has been surprisingly discovered that polyolefins can be removed from structures by treatment with an aqueous solution at a temperature higher than the melting point of component A and lower than the melting point of component B.

本方法によれば有機溶剤を用いた場合の毒性、危険性、
環境汚染さらには容器の腐蝕といった問題は全くなく、
通常の高圧容器例えばポリエステル織編物用の高温染色
機、高温リラクサー等をそのまま使用してポリオレフィ
ンを除去してなる繊維構造物の製造が可能であり、しか
も除去されたポリオレフィンは粒状で水溶液中に浮上す
るので簡単な分離操作のみで回収装置等は全く不要であ
り、かつ溶剤抽出の場合とは異なり1バッチ方式で一成
分を完全に除去することが可能であるという全く新規で
画期的なものである。本発明に言うポリエステル系ポリ
マーとは、テレフタール酸,ィソフタール酸,ナフタリ
ン2,6ジカルボン酸などの芳香族ジカルポン酸及びア
ジピン酸,セバシン酸などの脂肪族ジカルボン酸又はこ
れらのェステル類とエチレングリコール,ジエチレング
リコール,1.4ープタンジオール,ネオベンチルグリ
コール,ジクロヘキサン1,4ージメタノールなどのジ
オ−ル化合物とから合成されるポリエステルであり、反
復単位の75%以上がポリエチレンテレフタレートであ
るポリエステルを意味する。
According to this method, toxicity and danger when using organic solvents,
There are no problems such as environmental pollution or corrosion of containers.
It is possible to manufacture fiber structures by removing polyolefins using ordinary high-pressure containers, such as high-temperature dyeing machines for polyester woven and knitted fabrics, high-temperature relaxers, etc., and the removed polyolefins float in the aqueous solution in the form of particles. Therefore, it is a completely new and revolutionary method that requires only a simple separation operation and does not require any recovery equipment, and unlike solvent extraction, it is possible to completely remove one component in a single batch method. It is. The polyester polymer referred to in the present invention refers to aromatic dicarboxylic acids such as terephthalic acid, isophthalic acid, and naphthalene-2,6-dicarboxylic acid, aliphatic dicarboxylic acids such as adipic acid and sebacic acid, or esters thereof, and ethylene glycol and diethylene glycol. , 1,4-butanediol, neobentyl glycol, dichlorohexane, 1,4-dimethanol, and other diol compounds, and refers to a polyester in which 75% or more of the repeating units are polyethylene terephthalate.

特に、界面活性剤水溶液中でボリオレフィンとポリエス
テルを分離し易くする為にスルホン酸,炭酸,リン酸又
はカルボン酸の金属塩を含有する脂肪族又は芳香族化合
物,第1〜第4級アミン化合物,酸アミド化合物,ポリ
アルキレンオキサイド化合物などをポリエチレンテレフ
タレートに対して1〜20モル%共重合又は/及びブレ
ンド(練り込み)したものが好ましく、より好ましい化
合物としてジカルボン酸,アルキル基,アルキルェーテ
ル及びアルキルェステルのスルホン酸,炭酸,リン酸又
はカルボン酸の金属塩,並びに基又は 基又はアルキルアミン基を 有する分子量が500〜50000のポリアルキレンオ
キサイドがある。
In particular, aliphatic or aromatic compounds, primary to quaternary amine compounds containing metal salts of sulfonic acid, carbonic acid, phosphoric acid, or carboxylic acid to facilitate separation of polyolefin and polyester in an aqueous surfactant solution. , acid amide compounds, polyalkylene oxide compounds, etc. are preferably copolymerized or/and blended (kneaded) with polyethylene terephthalate in an amount of 1 to 20 mol %, and more preferable compounds include dicarboxylic acids, alkyl groups, alkyl ethers, and alkyl ethers. There are metal salts of sulfonic acid, carbonic acid, phosphoric acid or carboxylic acid of ster, as well as polyalkylene oxides having a molecular weight of 500 to 50,000 and having groups or groups or alkylamine groups.

一方、本発明に言うポリオレフィンとはポリエチレン,
ポリプロピレンなどを意味し、より好ましくは融点の低
い低密度ポリエチレンである。
On the other hand, the polyolefin referred to in the present invention is polyethylene,
It means polypropylene, etc., and more preferably low density polyethylene with a low melting point.

本発明に言う複合繊維とは、例えば公知のサイド/ゞィ
サィド型、芯鞘型複合繊維あるいはチップブレンド法,
多層化−接合−分割型の溶融混合法又は多芯々鞘複合織
糸法などによって得られる梅島構造繊維が含まれ、その
繊維横断面例を示せば第1〜8図の如きものが含まれる
。図中、斜線部分は非除去成分Bであるポリエステルを
示す。本発明において、上記複合織絵を2の重量%以上
含む構造物は、0.01重量%以上の界面活性剤水溶液
に浸糟し、蝿梓下で、除去成分Aの融点以上、非除去成
分Bの融点未満の温度で処理されるか、又は予め界面活
性剤水溶液で処理したのち、最終的に、界面活性剤が0
.01重量%以上存在する水溶液となる水中で、A成分
の融点以上、B成分の融点未満の温度下で鷹梓下に処理
され、いずれの方法においても、その結果、A成分のポ
リオレフィンはB成分のポリエステルから分離されて水
溶液中に浮上する。この場合、ポリオレフィンの融点未
満の温度で処理するとポリオレフィンがポリエステルに
固着したまま分離せず本発明の効果を失う。またポリエ
ステル繊維の損傷の点からボリオレフインの融点以上で
かつポリオレフィンの除去が可能な限り低い温度が望ま
しい。界面活性剤の水溶液濃度は0.01重量%以上が
好ましく、さらに好ましくは0.1〜10重量%である
。0.01重量%未満ではポリオレフインの除去が難し
く高温長時間処理が必要となり水だけでは除去不能とな
る。
The composite fibers referred to in the present invention are, for example, known side/side type, core-sheath type composite fibers, chip blend method,
Umejima structural fibers obtained by a multi-layered-jointed-divided melt-mixing method or a multi-core-to-sheath composite weaving method are included, and examples of the fiber cross sections are shown in FIGS. 1 to 8. In the figure, the shaded area indicates polyester, which is the non-removed component B. In the present invention, a structure containing 2% by weight or more of the above-mentioned composite weave is soaked in an aqueous surfactant solution of 0.01% by weight or more, and heated to a temperature equal to or higher than the melting point of the removed component A and the non-removed component B. or after treatment with an aqueous surfactant solution, the surfactant is finally reduced to 0.
.. In water to form an aqueous solution containing 0.1% by weight or more, the polyolefin of component A is treated under temperature at a temperature higher than the melting point of component A and lower than the melting point of component B. In either method, as a result, the polyolefin of component A becomes a component of B. is separated from the polyester and floats in the aqueous solution. In this case, if the treatment is carried out at a temperature below the melting point of the polyolefin, the polyolefin will remain fixed to the polyester and will not separate, thereby losing the effect of the present invention. In addition, from the viewpoint of damage to the polyester fibers, it is desirable that the temperature be higher than the melting point of polyolefin and as low as possible to remove the polyolefin. The concentration of the surfactant in the aqueous solution is preferably 0.01% by weight or more, more preferably 0.1 to 10% by weight. If it is less than 0.01% by weight, it will be difficult to remove the polyolefin, requiring long-term treatment at high temperatures, and it will not be possible to remove it with water alone.

また不必要に界面活性剤が多い場合は、ポリオレフィン
除去後の構造物の洗浄に時間を資し、界面活性剤のロス
も大きくなるので好ましくない。なお、複合繊維が2の
重量%未満の場合は一成分を除去される繊維構造物の特
徴が発揮され難い。界面活性剤としてはアニオン,カチ
オン,ノニオン及び両性系のいずれでも使用可能である
が、ポリエステルの敦質剤がアニオン系の場合はカチオ
ン界面活性剤以外のアニオン,ノニオン及両性界面活性
剤がポリオレフィンの除去効果に対して大きく寄与し、
改質剤がカチオン系の場合はカチオン,ノニオン及び両
性界面活性剤が好ましい。またポリオレフィン除去後に
繊維構造物に付着している界面活性剤は水洗又は濠洗に
より容易に脱落するものが好ましい。アニオン界面活性
剤としては、例えば脂肪酸塩,硫酸ェステル塩,スルホ
ン酸塩又はリン酸ェステル塩を含有する有機化合物が、
カチオン界面活性剤としては例えば第4級アンモニウム
塩又は高級アミン塩を含む有機化合物が挙げられ、/ニ
オン系界面活性剤としては例えばポリエチレングリコー
ル型又は多価アルコール型の有機化合物が、両性界面活
性剤としては例えばカルボン酸塩型,硫酸ェステル塩型
,スルホン酸塩型又はリン酸ェステル塩型の第4級アミ
ン化合物を意味する。また、界面活性剤は水に溶解又は
乳化して用いられるが、この状態を維持するために混合
系で使用することも可能である。さらにボリオレフィン
の除去に関しては機械的振動,超音波振動,溶液噴射な
ど、要するに鷹梓が必要である。この蝿拝は、水溶液と
複合繊維とのいずれか一方に対して動く状態であればよ
く、より好ましくは両者が共に動く状態を意味する。こ
のような蝿梓をともなった水溶液中での処理手段として
は、例えば染色機、リラックサー、精練機等が好適であ
る。浴比は1:15以上、好ましくは1:30〜10栃
畠度が用いられる。本発明に言う繊維構造物とは繊維状
物から製造される織物,編物.不織布,紙などであり、
この場合繊維以外の物例えば樹脂,糊剤を30%以下含
有するもものも含まれ、該構造物からポリオレフインを
実質的に除去したものを言う。
Further, if the amount of surfactant is unnecessarily large, it is not preferable because it takes time to clean the structure after removing the polyolefin and the loss of surfactant becomes large. In addition, when the amount of composite fibers is less than 2% by weight, it is difficult to exhibit the characteristics of a fiber structure in which one component is removed. Anionic, cationic, nonionic, and amphoteric surfactants can be used as surfactants, but if the polyester modifier is anionic, anionic, nonionic, and amphoteric surfactants other than cationic surfactants can be used for polyolefin. It greatly contributes to the removal effect,
When the modifier is cationic, cationic, nonionic and amphoteric surfactants are preferred. Further, it is preferable that the surfactant adhering to the fibrous structure after polyolefin removal be easily removed by washing with water or washing with a moat. Examples of anionic surfactants include organic compounds containing fatty acid salts, sulfate ester salts, sulfonate salts, or phosphate ester salts.
Examples of cationic surfactants include organic compounds containing quaternary ammonium salts or higher amine salts, examples of ionic surfactants include organic compounds of polyethylene glycol type or polyhydric alcohol type, and amphoteric surfactants. For example, it means a carboxylate type, sulfate ester salt type, sulfonate type, or phosphate ester salt type of quaternary amine compound. Further, the surfactant is used after being dissolved or emulsified in water, but it is also possible to use it in a mixed system to maintain this state. Furthermore, in order to remove polyolefin, mechanical vibration, ultrasonic vibration, solution jetting, etc., in short, are necessary. This movement may be any state in which it moves relative to either the aqueous solution or the composite fiber, and more preferably means a state in which both move together. For example, a dyeing machine, a relaxer, a scouring machine, etc. are suitable as a means for treating the material in an aqueous solution with such fly lye. The bath ratio used is 1:15 or more, preferably 1:30 to 10 Tochihata. The fibrous structure referred to in the present invention refers to woven or knitted fabrics manufactured from fibrous materials. Nonwoven fabrics, paper, etc.
In this case, it also includes peaches containing 30% or less of materials other than fibers, such as resins and sizing agents, and refers to structures from which polyolefin has been substantially removed.

本発明に言う実質的除去とはポリオレフィンの残留量が
構造物の3%以下にすることを意味する。上記繊維構造
物は例えば通常の梁色仕上加工を行った製品又は起毛及
び仕上加工を施した立毛製品又は樹脂などをコートした
人工皮革として用いられる。
In the present invention, "substantially removed" means that the amount of residual polyolefin is reduced to 3% or less of the structure. The above-mentioned fibrous structure is used, for example, as a product with a normal beam color finish, a raised product with a raised and finished finish, or an artificial leather coated with a resin or the like.

以下、実施例により本発明方法を具体的に説明する。Hereinafter, the method of the present invention will be specifically explained with reference to Examples.

実施例 1 島成分として〔り〕=0.60そ/夕(フェノールとテ
トラクロルェタン等量混合溶媒を用い30qoの恒温槽
中でウッベローデ型粘度計を用いて測定した極限粘度)
のポリエチレンテレフタレートを、海成分として高圧法
で製造された融点115qoのポリエチレンから成る海
島成分比2対3で、島平均デニール0.1の海島構造繊
維を特殊混合級糸法により製造し500デニールとして
ョコ糸に用い、150デニールのポリエステル加工糸を
タテ糸に用いてョコ糸密度6タ本/吋,タテ糸密度91
本/吋の3飛5枚ョコ朱子の織物を構成した。
Example 1 As an island component, [ri] = 0.60 so/min (intrinsic viscosity measured using an Ubbelohde viscometer in a constant temperature bath at 30 qo using a mixed solvent of equal amounts of phenol and tetrachloroethane)
Polyethylene terephthalate is used as the sea component, and polyethylene with a melting point of 115 qo produced by a high-pressure method is used as a sea-island component ratio of 2:3, and a sea-island structure fiber with an island average denier of 0.1 is manufactured by a special mixed grade yarn method to produce 500 denier. 150 denier polyester processed thread is used for the warp thread, the density of the thread is 6 t/inch, and the density of the warp thread is 91.
This is made up of 3 pieces of 5 pieces of chocolate satin fabric.

この場合、海島構造繊維は全布重量の65%でありこの
織物をPOE{71ラウリルエーテル(ラウリルアルコ
ールのエチレンオキサイド7モル付加物)の5%水溶液
で125℃×2時間溶液噴射型装置で処理するとポリエ
チレンがポリエステルより分離し水溶液中に粒状となっ
て浮上した。次いで織物を水洗して該ノニオン界面活性
剤を洗い落し、乾燥後、針布起毛機にて起毛し、梁色仕
上加工を施して天然ラィクなスエード織物を得た。なお
、界面活性剤処理−水洗−乾燥後の織物を更に7ぴ0の
パークレンにてポリエチレンを完全抽出し、抽出前後の
織物の重量変化によりポリエチレンの残留率を算出した
が、実施例1では0.2重量%であった。実施例 2〔
り〕=0.6紅〆/夕のポリエチレンテレフタレートに
ジメチルイソフタール酸のスルホン酸ナトリウム塩を2
.5 モル%共重合したものを島成分とし、海成分として融点
130午0の高密度ポリエチレンを用いた海島成分比1
対2で島平均デニール0.7の海島構造繊維を特殊混合
級糸法に.より製造し250デニールにしてトリコツト
編のフロントヤーンとして使用し、バックヤーンに10
0デニールのポリエステル加工糸を用いて、浮糸の長い
縞地を構成した。
In this case, the sea-island structure fibers account for 65% of the total weight of the fabric, and this fabric was treated with a 5% aqueous solution of POE {71 lauryl ether (7 moles of ethylene oxide adduct of lauryl alcohol) at 125°C for 2 hours using a solution injection type device. Then, the polyethylene separated from the polyester and floated in the form of particles in the aqueous solution. Next, the woven fabric was washed with water to remove the nonionic surfactant, dried, and then raised using a needle cloth raising machine and given a beam color finish to obtain a natural-like suede fabric. In addition, the polyethylene was completely extracted from the fabric after surfactant treatment, water washing, and drying using 7.0% perchloren, and the residual percentage of polyethylene was calculated from the change in weight of the fabric before and after extraction. .2% by weight. Example 2 [
= 0.6 Sodium sulfonate of dimethyl isophthalic acid is added to polyethylene terephthalate.
.. 5 mol% copolymerized material was used as the island component, and the sea component was high-density polyethylene with a melting point of 130°C.The sea-island component ratio was 1.
Sea-island structure fiber with island average denier of 0.7 in pair 2 is processed using special mixed grade yarn method. It is made from 250 denier and used as the front yarn of the tricot knit, and the back yarn is 10 denier.
A striped fabric with long floats was constructed using 0 denier processed polyester yarn.

海島構造繊維は全編地重量の50%であり、この編物*
を以下の界面活性剤水溶液で150℃×1時間もみ効果
を有する高圧容器中で処理した後に濠洗し乾燥した。ポ
リエチレン除去結果を第1表に示した。第1表 ※ポリエチレン残留率は界面活性剤処理‐湯洗−乾燥後
の全編地重量K対する百分率を示す。
Sea-island structure fibers account for 50% of the total weight of the knitted fabric*
was treated with the following surfactant aqueous solution at 150° C. for 1 hour in a high-pressure container with a kneading effect, then washed in a moat and dried. The polyethylene removal results are shown in Table 1. Table 1 *Polyethylene residual rate indicates the percentage of the total knitted fabric weight K after surfactant treatment, hot water washing, and drying.

実施例 3 〔り〕=0.62夕/そのポリエチレン
テレフタレ ートに(分子量20000)を1の重量%
練り込んだものと融点120℃のポリエチレンを3対2
のサイドバイサイド型にして複合繊維を作り50デニー
ルで平織りにて織物を構成した。
Example 3 〔〔〔〕=0.62゜/The polyethylene terephthalate (molecular weight 20,000) was added at 1% by weight.
3:2 ratio of kneaded material and polyethylene with melting point of 120℃
Composite fibers were made in a side-by-side type, and a 50-denier plain-woven fabric was constructed.

得られた織物を次の界面活性剤水溶液で各条件にて溶液
還流型の高圧容器中で処理した後、濠洗し乾燥して異型
断面ポリエステルの裏地を得た。この結果を第2表に示
した。第2表実施例 4 〔り〕=0.7のクノタのポリエチレンテレフタレート
にラウリルアミンのポリプロピレングリコールポリ′エ
チレンオキサィド付加物(q2日2ふくミ三さミミ轟き
申かつm+n=側を15重量%共重合したものを島成分
にし、融点110℃のポリエチレンを海成分としてチッ
プブレンド方式により海島構造繊維を製造した。
The obtained fabric was treated with the following surfactant aqueous solution under various conditions in a solution reflux type high-pressure container, washed in a moat, and dried to obtain a polyester lining with an irregular cross section. The results are shown in Table 2. Table 2 Example 4 Adduct of polypropylene glycol poly'ethylene oxide of laurylamine to Kunota's polyethylene terephthalate with [ri] = 0.7 (q2 days, 2 days, 2 days) % copolymerized as an island component, and polyethylene with a melting point of 110° C. as a sea component, a sea-island structure fiber was produced by a chip blending method.

次いで、該繊維にてランダムウェツプを作成しポリウレ
タンを合浸した後にラゥリルトリメチルアンモニウムク
ロラィドの1%水溶液で120qo×2時間超音波振動
を与えながら圧力容器中で処理したところ、ポリエチレ
ンがポリエステルより完全に分離し水溶液中に粒状とな
って浮上した。次いで、該不織布を水洗し乾燥後、サン
ドペーパーにて表面を毛羽立て、染色仕上加工を施して
スエード調布精を得た。実施例 5 〔り〕=0.6幻そ/夕のポリエチレンテレフタレート
にペンタエリスリトール0.25モル%及びメト キシポリエチレンゲリコール(CH30一(CQC日2
0)n一日かつn=30〜45)を0.5モル%共重合
したものを島成分とし、融点160℃のポリプロピレン
を海成分として特殊濠合紡糸法により島平均デニール0
.3の海島構造繊維を製造した。
Next, a random web was prepared from the fibers and polyurethane was impregnated therein, and then treated with a 1% aqueous solution of lauryltrimethylammonium chloride in a pressure vessel while applying ultrasonic vibration for 2 hours at 120 qo. was completely separated from the polyester and floated in the form of particles in the aqueous solution. Next, the nonwoven fabric was washed with water, dried, and then the surface was fluffed with sandpaper and dyed to obtain a suede finish. Example 5 Pentaerythritol 0.25 mol% and methoxypolyethylene gelicol (CH30-(CQC day 2
0) n day and n = 30 to 45) was copolymerized with 0.5 mol% as the island component, and polypropylene with a melting point of 160°C was used as the sea component to produce an island average denier of 0 using a special moat joint spinning method.
.. A sea-island structure fiber of No. 3 was manufactured.

次いで、該繊維を1000デニールにして目付350タ
ノあのポリエステル基布にゲージ1′8インチ,ステッ
チlq団/インチ,パイル長5肌の条件でタフティング
しパイル布帯を構成した。該布用を予めPOE15ステ
アリン酸ェステルの20%水溶液で処理し、100午0
×1び分乾燥して該界面活性剤を1の重量%付着せしめ
た後、170℃水溶液で2時間溶液噴射型高圧容器で処
理したところ、ポリプロピレンがポリエステルから分離
し、水溶液中に粒状となって浮上した。次いで、布幕を
湯洗して該アニオン界面活性剤を洗い落し乾燥してパイ
ル布常を得た。ポリプロピレン残留率は1.2重量%で
あった。図面の簡単な説明図面として示した第1〜8図
はいづれも本発明で用いることのできる種々の複合繊維
についてその断面を示す榛式図であり第1〜8図におい
て斜線部分がポリエステル成分、その他の部分がポリオ
レフィン成分である。
Next, the fibers were made into 1,000 denier and tufted onto a polyester base fabric having a basis weight of 350 denier under the conditions of a gauge of 1'8 inches, a stitch rate of 1q folds/inch, and a pile length of 5 skins to form a pile fabric band. The fabric was previously treated with a 20% aqueous solution of POE15 stearate, and
After drying for 1 minute to deposit 1% by weight of the surfactant, it was treated with a 170°C aqueous solution for 2 hours in a solution injection type high-pressure vessel, and the polypropylene separated from the polyester and became granular in the aqueous solution. It surfaced. Next, the cloth was washed with hot water to remove the anionic surfactant and dried to obtain a pile cloth. The polypropylene residual rate was 1.2% by weight. Brief explanation of the drawings Figures 1 to 8, which are shown as drawings, are all cross-sectional views of various composite fibers that can be used in the present invention. The other part is a polyolefin component.

第1図 繁2図 第3図 第4図 第5図 第6図 第7図 第8図Figure 1 Traditional 2 illustrations Figure 3 Figure 4 Figure 5 Figure 6 Figure 7 Figure 8

Claims (1)

【特許請求の範囲】 1 一成分Aがポリオレフイン、他成分Bがポリエステ
ルからなる複合繊維を20重量%以上含有する繊維構造
物を、最終的に界面活性剤が、0.01重量%以上存在
する状態の水中で浸漬し、撹拌下、A成分の融点以上、
B成分の融点未満の温度で処理することによつてA成分
を除去することを特徴とする繊維構造物の製造方法。 2 繊維構造物を、0.01重量%以上の活面活性剤を
含む水溶液中浸漬し撹拌下で処理することを特徴とする
特許請求の範囲第1項記載の繊維構造物の製造方法。 3 繊維構造物を予め界面活性剤水溶液で処理したのち
、最終的に界面活性剤が0.01重量%以上存在する水
溶液となる水中で撹拌下に処理することを特徴とする特
許請求の範囲第1項記載の繊維構造物の製造方法。
[Scope of Claims] 1 A fiber structure containing 20% by weight or more of a conjugate fiber in which one component A is polyolefin and the other component B is polyester, and the final surfactant is 0.01% by weight or more. immersed in water at a temperature higher than the melting point of component A under stirring,
A method for producing a fibrous structure, characterized in that component A is removed by treatment at a temperature below the melting point of component B. 2. The method for producing a fibrous structure according to claim 1, characterized in that the fibrous structure is immersed in an aqueous solution containing 0.01% by weight or more of an active surfactant and treated under stirring. 3. The fibrous structure is treated in advance with an aqueous surfactant solution, and then treated under stirring in water to finally form an aqueous solution containing 0.01% by weight or more of the surfactant. A method for producing a fibrous structure according to item 1.
JP51049187A 1976-04-27 1976-04-27 Method for manufacturing fiber structures Expired JPS6015747B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP51049187A JPS6015747B2 (en) 1976-04-27 1976-04-27 Method for manufacturing fiber structures

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP51049187A JPS6015747B2 (en) 1976-04-27 1976-04-27 Method for manufacturing fiber structures

Publications (2)

Publication Number Publication Date
JPS52132192A JPS52132192A (en) 1977-11-05
JPS6015747B2 true JPS6015747B2 (en) 1985-04-22

Family

ID=12824018

Family Applications (1)

Application Number Title Priority Date Filing Date
JP51049187A Expired JPS6015747B2 (en) 1976-04-27 1976-04-27 Method for manufacturing fiber structures

Country Status (1)

Country Link
JP (1) JPS6015747B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61166450U (en) * 1985-04-03 1986-10-15
JPS61166448U (en) * 1985-04-03 1986-10-15

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6039412A (en) * 1983-08-11 1985-03-01 Kuraray Co Ltd Mixed yarn for forming nonwoven fabric
JP2783602B2 (en) * 1989-07-19 1998-08-06 チッソ株式会社 Ultrafine composite fiber for thermal bonding and its woven or nonwoven fabric
JP2599847B2 (en) * 1991-08-13 1997-04-16 株式会社クラレ Polyethylene terephthalate type melt blown nonwoven fabric and its manufacturing method
JP4950856B2 (en) * 2007-11-26 2012-06-13 帝人ファイバー株式会社 Sea-island composite fiber melt spinneret

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61166450U (en) * 1985-04-03 1986-10-15
JPS61166448U (en) * 1985-04-03 1986-10-15

Also Published As

Publication number Publication date
JPS52132192A (en) 1977-11-05

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