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JPH0115622B2 - - Google Patents
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JPH0115622B2 - - Google Patents

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Publication number
JPH0115622B2
JPH0115622B2 JP57073420A JP7342082A JPH0115622B2 JP H0115622 B2 JPH0115622 B2 JP H0115622B2 JP 57073420 A JP57073420 A JP 57073420A JP 7342082 A JP7342082 A JP 7342082A JP H0115622 B2 JPH0115622 B2 JP H0115622B2
Authority
JP
Japan
Prior art keywords
fiber bundle
fibers
tip
temperature
fiber
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
JP57073420A
Other languages
Japanese (ja)
Other versions
JPS58191272A (en
Inventor
Masato Yoshimoto
Yukikage Matsui
Takeo Matsumoto
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.)
Teijin Ltd
Original Assignee
Teijin 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 Teijin Ltd filed Critical Teijin Ltd
Priority to JP7342082A priority Critical patent/JPS58191272A/en
Publication of JPS58191272A publication Critical patent/JPS58191272A/en
Publication of JPH0115622B2 publication Critical patent/JPH0115622B2/ja
Granted legal-status Critical Current

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  • Chemical Or Physical Treatment Of Fibers (AREA)
  • Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は、均一で鋭いテーパー状先細先端部を
有する獣毛状繊維の製造方法に関するものであ
る。 筆材、刷毛材、ブラシ等の素材として、現在
種々の天然の獣毛が広く使用されている。 しかし、天然の獣毛は資源的な面で数量に限度
があり、又価格の面においても必ずしも安価とは
いえない。そこで、獣毛代替素材として合成繊
維、特にポリエステル系繊維にて種々検討されて
いる。 従来、ポリエステル系繊維の先端部をアルカリ
水溶液に浸漬処理して、先端部を細化させ、風
合、外観が獣毛に類似したポリエステル繊維を得
る方法が知られている。例えば、特公昭48―4910
号公報には、ポリエステル繊維をパイルとして使
用した布帛において、該パイルをパイル先端から
特定の長さまでアルカリ水溶液中に浸漬した状態
で一定時間処理し、その後パイル面を上げてパイ
ル先端部のみをアルカリ水溶液中に浸漬して一定
時間処理を行ないパイル先端部を細化させる方法
が記載されている。この方法では第1段浸漬部と
第2段浸漬部との境界部に段が発生し、なだらか
なテーパー状をなした先細繊維が得られず、加え
て先端形状が台形、又は半円状となるため、外観
風合共に獣毛よりも劣つたものとなつてしまう。 一方、かかる欠点を解消せんがために、毛管現
象を生じさせうる繊維間空隙を有するポリエステ
ル繊維束の一端をアルカリ水溶液中に浸漬させ、
毛管現象によつて繊維束中を上昇するアルカリ水
溶液によつてポリエステル繊維を分解させてテー
パー状先細先端部を形成させ、アルカリ水溶液中
に浸漬させた先端部分は全部分解除去してしまう
方法が提案されている(特公昭50―40195号公
報)。この方法によると鋭い均一なテーパー状先
細先端部を有し、繊維の長さ方向に凹凸状に処理
されることがなく均一に先端部が揃えられた状態
の製品が得られるように思われるが、実際に実施
してみると、必ずしも期待したような効果を奏し
得ない。即ち、繊維束をアルカリ水溶液中に浸漬
すると繊維束が外周方向に拡がり、中心部におい
てアルカリ水溶液がより多量に浸透することにな
り、そのため繊維束中心部において繊維がより多
く分解して繊維長が短くなり、更に最外周部も繊
維が分解し易く繊維長が短くなり結局繊維束の先
端面が凹凸状となり、先端部が均一に揃えられた
状態とならない。また、浸漬部分を完全に分解除
去しようとすると処理時間が長くなり、更に加水
分解されたモノマー類が浮遊し、それが繊維のテ
ーパー状先細先端部表面に付着し、該先端部の平
滑性を損うという問題も生ずる。更にテーパー部
の長さ等の先端形状を制御するのが比較的困難で
あるという欠点も有している。 かかる欠点を解消するために、本発明者らは先
にポリエステル繊維先端部を加水分解浴中に一定
長浸漬し、次いでポリエステル繊維を連続的に
徐々に引上げるか又は加水分解浴の液面を連続的
に徐々に低下させる方法を提案した。 しかしながら、かかる方法においては、ポリエ
ステル繊維の加水分解浴からの引き上げ速度又は
加水分解浴液面の低下速度を厳密にコントロール
しないと、均一なテーパー状尖鋭先端部形状が得
られないという問題があることがわかつた。即ち
ポリエステル繊維の引き上げ速度、又は液面低下
速度が小さすぎると先端部がなだらかなテーパー
状とならず、かつ不均一な形状となり、一方速度
が大きすぎると先端形状が台形状となつて尖鋭化
しないのである。 このようにポリエステル繊維先端部を加水分解
浴に浸漬して、獣毛状繊維を得ることは原理的に
は容易であるが、繊維の直径が例えば0.10mm以下
の比較的細いポリエステル剛毛を使用した場合、
繊維束の密度が極めて高くなり、加水分解液の浸
透が極めて不良となる。従つて繊維束中心部で先
端部より離れた位置にある繊維は昇温されにく
く、細化速度が極めて遅くなる。それゆえ、製品
は均一なものが得られなく、かつテーパー長の長
さも充分なものを得ることができず、歩留りの面
でも問題があつた。 上記欠点を解決する方法として、細化条件、例
えば加水分解剤濃度、加水分解温度、加水分解時
間及び繊維束の加水分解浴への浸漬方法等色々検
討したが満足できる結果を得ることができなかつ
た。従つて、工業的レベルで大量に生産するに
は、極めて多くの未解決の問題点が残されてい
た。そこで本発明者達は、鋭意検討した結果、繊
維束内の温度分布ができるだけ狭い状態で細化処
理を行なうならば繊維束内各部分の細化速度差が
解消されることを見い出し、本発明に到つた。 本発明によると、得られる製品は極めて均一な
ものとなり、特に繊維径が0.10mm以下の比較的細
い繊維からなり、密度の非常に高い繊維束を使用
しても、毛筆、画筆等に有用なテーパー長の充分
長い獣毛状繊維を得ることができ、又歩留りの
面、作業操作性も良好であることを見出した。 すなわち、本発明の構成は以下の通りである。 1 合成繊維の先端部を加水分解浴に浸漬して先
細化せしめるに際し、該合成繊維を束状に集束
して繊維束とし、浸漬前の該繊維束内温度を以
下の()式を満足するよう予熱せしめた後、
加水分解剤を含む水溶液に浸漬することを特徴
とする獣毛状繊維の製造方法である。 TL≧50 ……() 〔ただし、TLは繊維束の中心部で先端部より
20mm離れた位置の温度(℃)である。〕 以下、本発明について詳細に説明する。 本発明においてポリエステル繊維とは、エチレ
ングリコール、トリメチレングリコール、1,4
―ブタンジオール、テトラメチレングリコール等
のグリコール成分とテレフタル酸、イソフタル
酸、マロン酸、コハク酸等のジカルボン酸成分と
の重縮合体である。グリコール成分又はジカルボ
ン酸成分の一部として他の第3成分を共重合させ
たポリエステル重合体、あるいはこれらポリエス
テル重合体と他の重合体とのブレンド体等からな
る繊維であつて、加水分解剤水溶液によつて加水
分解しうるポリエステル繊維すべてを含むが、獣
毛状触感という点でポリテトラメチレンテレフタ
レート繊維が最も好ましい。 ポリエステル繊維の単糸繊度は、20〜200deの
範囲で用いるのが獣毛状繊維を得るうえで好まし
い。単糸繊度が小さすぎると獣毛状触感が得られ
にくく、一方、単糸繊度が大きすぎると剛直にな
りすぎて用途が限定されてしまう。 ポリエステル繊維に対する加水分解剤として
は、水酸化ナトリウム、水酸化カリウム、炭酸ソ
ーダ、トリエタノールアミン等をあげることがで
きる。 これら加水分解剤は溶液の形で使用され、その
濃度は特に限定されず、処理されるポリエステル
繊維の種類、繊度、所望する細化度合、処理浴温
度に応じて適宜選定される。特に加水分解剤を含
む水溶液を加熱して、ポリエステル繊維の処理を
行なうとポリエステル繊維の溶解、分解速度が大
きくなり、処理時間を短縮することができて好ま
しい。通常採用される処理液の温度は70℃〜130
℃である。 また、加水分解剤としてアルカリ金属化合物を
使用する場合は、ラウリルジメチルベンジルアン
モニウムクロライド、セチルジメチルベンジルア
ンモニウムクロライドのような第4級アンモニウ
ム塩を添加併用すると、ポリエステル繊維の加水
分解が促進されるので望ましい。 本発明は、ポリエステル繊維の繊維束内温度
を、ある一定温度以上に予熱しておくことによつ
て、繊維束の温度をできるだけ均一ならしめなが
ら先細化処理を行うものであり、かくして繊維束
内の各部分の加水分解速度差を極めて小さくせし
めたものである。 すなわち、従来の方法では、繊維束内の中心部
から周辺部にかけての温度差(温度分布)が極め
て大きく、特に繊維束内の中心部は加水分解剤水
溶液に浸漬しても、なかなか昇温しにくいという
問題があつた。そのため、得られる製品は不均一
なものとなり、特に繊維径が0.10mm以下の比較的
細いポリエステル繊維においては、繊維束の密度
が高く、加水分解剤水溶液の繊維束内への浸透性
が低いので、テーパー長の充分長い獣毛状繊維を
得ることは、極めて困難であつた。 そこで、本発明者らは鋭意検討した結果、先細
化処理前の繊維束内温度を50℃以上、好ましくは
70℃以上に予熱した後先細化処理を行なうと、繊
維束内の内外層間にかけての先細化速度差が極め
て小さくなるため、均一で、テーパー長が充分長
い獣毛状繊維が得られることを見い出した。 ここに繊維束内温度とは、繊維束の中心部で先
端部より20mm離れた位置の温度である。 すなわち、繊維束内温度が50℃未満の場合は、
結果的に同一繊維束内でも、加水分解浴に近い先
端部と加水分解浴から離れた繊維束の中心部とで
は、繊維の細化が始まるときの繊維束内の温度差
が30℃以上の差があり、細化開始後の繊維束内昇
温挙動についても、加水分解浴に近い先端部は容
易に昇温されるが、加水分解浴から離れた繊維束
の中心部は、繊維束の先端部と比較して昇温に極
めて長時間を要する。従つて、繊維束内の細化速
度差が極めて大きくなり、細化処理条件を色々と
変更しても均一でテーパー長の長い獣毛状繊維を
得ることはできなかつた。一方、繊維束内温度を
50℃以上、好ましくは70℃以上に昇温した後、細
化処理を行なえば、上記の欠点を解消することが
できる。すなわち、加水分解浴に近い繊維束先端
部と、加水分解浴から離れた位置にある繊維束の
中心部の温度差が小さい状態で反応を開始させる
事ができる。また加水分解浴から離れた位置にあ
る繊維束内中心部のその後の昇温も比較的早い。
従つて、繊維束内の各部分の細化速度差は極めて
小さくなり、得られる獣毛状繊維は均一で、テー
パー長の充分長いものを得ることができる。 繊維束内の温度を昇温させる方法であるが、細
化処理前に、繊維束を加水分解浴の液面上に保
ち、加水分解浴の蒸気で加熱する方法が簡便で、
かつ、効果も充分大きい。昇温の程度であるが、
繊維束と加水分解液液面間の距離、あるいは液面
上で保持する時間により、所望の条件に設定可能
であり、特に加水分解浴槽に蓋等を設けて密閉を
はかれば、その効果はより一層大きなものとな
る。 尚、繊維束の温度の測定であるが、繊維束中心
部で先端部より所定の位置に温度検出端を埋めこ
みその位置の温度を経時的に測定した。 又、繊維束を予熱した後、加水分解浴に浸漬し
て細化せしめる方法であるが、従来からの公知の
方法例えば、加水分解浴中の浸漬長を減少させる
方法などで先細化させることにより、本目的を達
成することができる。 尚、繊維の太さ、テーパー長については、日本
光学製万能投影機(ニコン6C2)を用いてポリエ
ステル繊維を100倍に拡大して測定した。 以下、実施例にてさらに具体的に例示する。 実施例 固有粘度1.0のポリテトラメチレンテレフタレ
ートを溶融紡糸したのち、延伸して単糸繊度
50deの剛毛繊維を得た。この剛毛繊維を集束し
て、直径45mm、長さ50mmの繊維束を作成した。こ
の繊維束を第1図に示した装置を用いて処理し
た。 第1図は本発明の実施に使用する装置の一例を
示す縦断面図である。ここに1は処理浴槽、2は
細化処理浴、3は繊維束をしばり固定するテー
プ、4は繊維束、5は繊維束の昇降を行うワイヤ
ー、6はモーター、7はローラーである。 処理液は、水酸化ナトリウム25重量%を含む
107℃の水溶液を用いた。尚、反応を促進せしめ
るために、該繊維束を4級アンモニウム塩である
ラウリル・トリメチルアンモニウムクロライド15
%水溶液にて前処理した。処理液に浸漬する前
に、該繊維束を処理液上3mmの位置に静止し、処
理液の蒸気で予熱してから処理液に浸漬した。 静置時間は5分、10分、15分、30分、40分の5
水準行なつた。各水準における、繊維束内の温度
分布を表―に示す。
The present invention relates to a method for producing animal hair-like fibers having a uniform and sharp tapered tip. Various natural animal hairs are currently widely used as materials for brushes, brushes, etc. However, natural animal hair is limited in quantity due to resources, and is not necessarily cheap. Therefore, various synthetic fibers, particularly polyester fibers, are being investigated as substitute materials for animal hair. Conventionally, a method is known in which the tips of polyester fibers are immersed in an aqueous alkaline solution to thin the tips, thereby obtaining polyester fibers that have a texture and appearance similar to animal hair. For example, Tokuko Sho 48-4910
The publication describes that a fabric using polyester fibers as a pile is treated by immersing the pile in an alkaline aqueous solution for a certain period of time from the tip of the pile to a specific length, and then raising the pile surface and immersing only the tip of the pile in an alkali solution. A method is described in which the tip of the pile is thinned by immersing it in an aqueous solution and treating it for a certain period of time. In this method, a step occurs at the boundary between the first-stage immersed section and the second-stage immersed section, and a tapered fiber with a gently tapered shape cannot be obtained.In addition, the tip shape is trapezoidal or semicircular. As a result, both the appearance and texture are inferior to animal hair. On the other hand, in order to eliminate this drawback, one end of a polyester fiber bundle having interfiber voids that can cause capillary action is immersed in an alkaline aqueous solution.
A method has been proposed in which polyester fibers are decomposed by an alkaline aqueous solution that rises through the fiber bundle due to capillary action to form a tapered tip, and the tip portion immersed in the alkaline aqueous solution is completely decomposed and removed. (Special Publication No. 50-40195). This method seems to produce a product with a sharp and uniformly tapered tip, and the tips are uniformly aligned without being treated to create unevenness in the longitudinal direction of the fibers. However, when actually implemented, it does not necessarily produce the expected effects. That is, when a fiber bundle is immersed in an alkaline aqueous solution, the fiber bundle expands in the outer circumferential direction, and a larger amount of the alkaline aqueous solution penetrates into the center, which causes more fibers to decompose in the center of the fiber bundle and shorten the fiber length. In addition, the fibers at the outermost periphery also tend to decompose and the length of the fibers becomes short, resulting in the end surface of the fiber bundle becoming uneven and the end portions not being uniformly aligned. In addition, if you try to completely decompose and remove the immersed part, the processing time will be longer, and further hydrolyzed monomers will float and adhere to the surface of the tapered tip of the fiber, reducing the smoothness of the tip. The problem of loss also arises. Another drawback is that it is relatively difficult to control the shape of the tip, such as the length of the tapered portion. In order to eliminate this drawback, the present inventors first immersed the tips of the polyester fibers in a hydrolysis bath for a certain length, and then gradually pulled up the polyester fibers continuously or lowered the liquid level of the hydrolysis bath. A method of continuous gradual reduction was proposed. However, in this method, there is a problem that a uniform tapered tip shape cannot be obtained unless the rate at which the polyester fiber is pulled up from the hydrolysis bath or the rate at which the liquid level in the hydrolysis bath decreases is strictly controlled. I understood. That is, if the pulling speed of the polyester fiber or the rate of drop in the liquid level is too low, the tip will not be gently tapered and will have an uneven shape, while if the speed is too high, the tip will become trapezoidal and sharp. I don't. In principle, it is easy to obtain animal hair-like fibers by immersing the tips of polyester fibers in a hydrolysis bath, but it is difficult to obtain animal hair-like fibers by using relatively thin polyester bristles with a fiber diameter of, for example, 0.10 mm or less. case,
The density of the fiber bundle becomes extremely high, and penetration of the hydrolyzate becomes extremely poor. Therefore, the temperature of the fibers located in the center of the fiber bundle away from the tip portion is difficult to increase, and the rate of thinning becomes extremely slow. Therefore, it was not possible to obtain a uniform product, and it was also difficult to obtain a sufficiently long taper length, which caused problems in terms of yield. As a method to solve the above-mentioned drawbacks, we have investigated various thinning conditions such as hydrolyzing agent concentration, hydrolysis temperature, hydrolysis time, method of immersing the fiber bundle in the hydrolysis bath, etc., but we have not been able to obtain satisfactory results. Ta. Therefore, many unresolved problems remain in mass production at an industrial level. As a result of intensive studies, the inventors of the present invention found that if the thinning process is performed while the temperature distribution within the fiber bundle is as narrow as possible, the difference in thinning speed between each part within the fiber bundle can be eliminated. I reached it. According to the present invention, the product obtained is extremely uniform, and even if fiber bundles made of relatively thin fibers with a fiber diameter of 0.10 mm or less and having a very high density are used, they are useful for writing brushes, painting brushes, etc. It has been found that animal hair-like fibers with a sufficiently long taper length can be obtained, and that the yield and workability are also good. That is, the configuration of the present invention is as follows. 1. When the tips of synthetic fibers are immersed in a hydrolysis bath to make them tapered, the synthetic fibers are bundled into a fiber bundle, and the temperature inside the fiber bundle before dipping satisfies the following formula (). After preheating,
This is a method for producing animal hair-like fibers, which is characterized by immersing the fibers in an aqueous solution containing a hydrolyzing agent. T L ≧50 ……() [However, T L is the center of the fiber bundle from the tip.
This is the temperature (°C) at a distance of 20 mm. ] Hereinafter, the present invention will be explained in detail. In the present invention, polyester fibers include ethylene glycol, trimethylene glycol, 1,4
- It is a polycondensate of glycol components such as butanediol and tetramethylene glycol and dicarboxylic acid components such as terephthalic acid, isophthalic acid, malonic acid, and succinic acid. A fiber made of a polyester polymer copolymerized with another third component as a part of a glycol component or a dicarboxylic acid component, or a blend of these polyester polymers and other polymers, and an aqueous solution of a hydrolyzing agent. It includes all polyester fibers that can be hydrolyzed by water, but polytetramethylene terephthalate fibers are most preferred because of their animal hair-like feel. It is preferable to use polyester fibers with a single filament fineness in the range of 20 to 200 DE in order to obtain animal hair-like fibers. If the single yarn fineness is too small, it will be difficult to obtain an animal hair-like feel, while if the single yarn fineness is too large, the yarn will become too rigid and its uses will be limited. Examples of hydrolyzing agents for polyester fibers include sodium hydroxide, potassium hydroxide, soda carbonate, and triethanolamine. These hydrolyzing agents are used in the form of a solution, and their concentration is not particularly limited and is appropriately selected depending on the type of polyester fiber to be treated, fineness, desired degree of fineness, and treatment bath temperature. In particular, it is preferable to heat an aqueous solution containing a hydrolyzing agent to treat the polyester fibers because the dissolution and decomposition rate of the polyester fibers increases and the treatment time can be shortened. The temperature of the processing liquid usually used is 70℃ to 130℃.
It is ℃. In addition, when using an alkali metal compound as a hydrolyzing agent, it is desirable to add a quaternary ammonium salt such as lauryldimethylbenzylammonium chloride or cetyldimethylbenzylammonium chloride, as this will accelerate the hydrolysis of polyester fibers. . The present invention performs tapering treatment while making the temperature of the fiber bundle as uniform as possible by preheating the temperature inside the fiber bundle of polyester fibers to a certain temperature or higher. The difference in the rate of hydrolysis between each part is made extremely small. In other words, in the conventional method, the temperature difference (temperature distribution) from the center to the periphery of the fiber bundle is extremely large, and the temperature of the center of the fiber bundle in particular does not rise easily even when immersed in an aqueous hydrolyzing agent solution. The problem was that it was difficult. As a result, the resulting product is non-uniform, especially in the case of relatively thin polyester fibers with a fiber diameter of 0.10 mm or less, the density of the fiber bundle is high and the permeability of the hydrolyzing agent aqueous solution into the fiber bundle is low. It has been extremely difficult to obtain animal hair-like fibers with a sufficiently long taper length. Therefore, as a result of intensive study, the present inventors determined that the temperature inside the fiber bundle before the tapering treatment should be set to 50°C or higher, preferably
It was discovered that if the tapering treatment is performed after preheating to 70°C or higher, the difference in tapering speed between the inner and outer layers within the fiber bundle becomes extremely small, resulting in uniform animal hair-like fibers with a sufficiently long taper length. Ta. Here, the temperature inside the fiber bundle is the temperature at the center of the fiber bundle at a position 20 mm away from the tip. In other words, if the temperature inside the fiber bundle is less than 50℃,
As a result, even within the same fiber bundle, there is a temperature difference of 30°C or more between the tip end near the hydrolysis bath and the center of the fiber bundle away from the hydrolysis bath when the fibers begin to thin. There is also a difference in the behavior of temperature rise within the fiber bundle after the start of thinning.The tip of the fiber bundle, which is close to the hydrolysis bath, is easily heated, but the center of the fiber bundle, which is away from the hydrolysis bath, is It takes an extremely long time to heat up compared to the tip. Therefore, the difference in thinning speed within the fiber bundle becomes extremely large, and even if the thinning processing conditions are variously changed, it is not possible to obtain animal hair-like fibers that are uniform and have a long taper length. On the other hand, the temperature inside the fiber bundle is
The above-mentioned drawbacks can be overcome by performing a thinning treatment after raising the temperature to 50° C. or higher, preferably 70° C. or higher. That is, the reaction can be started in a state where the temperature difference between the tip of the fiber bundle near the hydrolysis bath and the center of the fiber bundle at a position away from the hydrolysis bath is small. Furthermore, the subsequent temperature rise in the center of the fiber bundle located away from the hydrolysis bath is also relatively quick.
Therefore, the difference in thinning speed between each part within the fiber bundle becomes extremely small, and the resulting animal hair-like fibers are uniform and have a sufficiently long taper length. This is a method of increasing the temperature inside the fiber bundle, but a simple method is to keep the fiber bundle above the liquid level of the hydrolysis bath and heat it with steam from the hydrolysis bath before the thinning treatment.
Moreover, the effect is sufficiently large. Although the degree of temperature rise is
Desired conditions can be set by changing the distance between the fiber bundle and the hydrolysis liquid surface or the time the fiber bundle is held on the liquid surface.In particular, if the hydrolysis bath is sealed with a lid etc., the effect will be improved. It becomes even bigger. To measure the temperature of the fiber bundle, a temperature detection end was embedded in a predetermined position from the tip of the fiber bundle in the center, and the temperature at that position was measured over time. Another method is to preheat the fiber bundle and then immerse it in a hydrolysis bath to make it thin. , this purpose can be achieved. The thickness and taper length of the fibers were measured by enlarging the polyester fibers 100 times using a Nippon Kogaku universal projector (Nikon 6C2). More specific examples will be given below. Example: Polytetramethylene terephthalate with an intrinsic viscosity of 1.0 is melt-spun and then stretched to obtain a single fiber fineness.
A bristle fiber of 50 de was obtained. These bristle fibers were bundled to create a fiber bundle with a diameter of 45 mm and a length of 50 mm. This fiber bundle was processed using the apparatus shown in FIG. FIG. 1 is a longitudinal sectional view showing an example of an apparatus used for carrying out the present invention. Here, 1 is a treatment bath, 2 is a thinning treatment bath, 3 is a tape that ties and fixes the fiber bundle, 4 is a fiber bundle, 5 is a wire that raises and lowers the fiber bundle, 6 is a motor, and 7 is a roller. The treatment liquid contains 25% by weight of sodium hydroxide.
An aqueous solution at 107°C was used. In order to accelerate the reaction, the fiber bundle was treated with lauryl trimethylammonium chloride 15, which is a quaternary ammonium salt.
% aqueous solution. Before being immersed in the treatment liquid, the fiber bundle was placed at a position 3 mm above the treatment liquid, preheated with steam from the treatment liquid, and then immersed in the treatment liquid. The standing time is 5 minutes, 10 minutes, 15 minutes, 30 minutes, and 40 minutes.
I did the standard. Table 1 shows the temperature distribution within the fiber bundle at each level.

【表】【table】

【表】 このように、静置時間が短いときは、繊維束中
心部の温度が低く、かつ、繊維束内の温度差△T
も大きい。 上記のサンプル(No.(1)〜(5))について、予熱後
直ちに処理浴中に35mm浸漬して35分間放置した。
処理浴に浸漬中の繊維束内の温度を表―に示
す。
[Table] As shown above, when the standing time is short, the temperature at the center of the fiber bundle is low and the temperature difference △T within the fiber bundle
It's also big. Immediately after preheating, the above samples (Nos. (1) to (5)) were immersed in a treatment bath for 35 mm and left for 35 minutes.
Table 1 shows the temperature inside the fiber bundle while it is immersed in the treatment bath.

【表】 予熱時間が短いNo.(1),(2)については、加水分解
中における繊維束内の中心部の昇温が遅く、か
つ、先端部との温度差も大きい。 一方、No.(3),(4)については、繊維束内の中心部
の昇温も極めて早く、先端部との温度差も極めて
小さい。 前述のサンプル(1)〜(5)を処理浴から取り出し水
洗し、繊維に付着した残査を除去した。ついで該
繊維束をしぼり水切りを行ない、処理浴中に再度
35mm浸漬し、毎分1、17mmの速度で30分間連続し
て引き上げた。該繊維束を処理浴から取り出し水
洗,乾燥した。得られた繊維の形態を表―に示
す。
[Table] For Nos. (1) and (2) with short preheating times, the temperature rise at the center of the fiber bundle during hydrolysis is slow, and the temperature difference between it and the tip is large. On the other hand, for Nos. (3) and (4), the temperature at the center of the fiber bundle rose extremely quickly, and the temperature difference between it and the tip was extremely small. The aforementioned samples (1) to (5) were taken out from the treatment bath and washed with water to remove residues attached to the fibers. Next, the fiber bundle is squeezed, drained, and placed in the treatment bath again.
It was immersed for 35 mm and pulled up continuously for 30 minutes at a speed of 1.17 mm per minute. The fiber bundle was taken out from the treatment bath, washed with water, and dried. Table 1 shows the morphology of the obtained fibers.

【表】 尚、得られた獣毛状繊維の形態は、以下のよう
に定義する。 Γ テーパー形態 ×:繊維束先端のテーパー長が10mmより小さ
い。 △:繊維束先端のテーパー長が10〜15mmであ
る。 ○:繊維束中心部の繊維のテーパー長が15mmよ
り大きい。 Γ 先端形態 ○:先端が完全に尖鉛化されており、やわらか
いタツチを有する。 △:先端が完全には尖鋭化されていないものも
多少混在し、粗硬なタツチを有する。 Γ 中心部と外周部の差 ○:テーパー形態、先端形態共に、繊維束中心
部と外周部とで差は極めて小さい。 △:繊維束外周部はテーパー長が15mm以上ある
が、繊維束中心部は10〜15mmである。 Γ 長さのバラツキ ○:繊維束先端の凹凸がない。 △:繊維束先端の凹凸が多少存在する。 このように、繊維束内温度50℃以上に予熱して
から細化処理を行なうと繊維束先端部は鋭いテー
パーを有し、かつ、品位の優れた獣毛状繊維を得
る事ができた。 比較例 繊維束を予熱しないで、処理浴に35mm浸漬して
細化処理を35分間行なつた。浸漬中の繊維束内温
度を表―に示す。
[Table] The morphology of the obtained animal hair-like fibers is defined as follows. Γ Taper form ×: Taper length at the tip of the fiber bundle is smaller than 10 mm. Δ: Taper length at the tip of the fiber bundle is 10 to 15 mm. ○: The taper length of the fibers at the center of the fiber bundle is greater than 15 mm. Γ Tip form ○: The tip is completely pointed and has a soft touch. Δ: The tips were not completely sharpened to some extent, and had a rough and hard touch. Γ Difference between the center and the outer periphery ○: The difference between the center and the outer periphery of the fiber bundle is extremely small in both the taper form and the tip form. Δ: The outer peripheral part of the fiber bundle has a taper length of 15 mm or more, but the tapered length in the center part of the fiber bundle is 10 to 15 mm. Γ Length variation ○: No unevenness at the tip of the fiber bundle. Δ: Some unevenness is present at the tip of the fiber bundle. As described above, by preheating the inside of the fiber bundle to a temperature of 50° C. or higher and then performing the thinning treatment, it was possible to obtain animal hair-like fibers with a sharp taper at the tip of the fiber bundle and excellent quality. Comparative Example A fiber bundle was immersed in a treatment bath for 35 mm without preheating, and a thinning treatment was performed for 35 minutes. Table 1 shows the temperature inside the fiber bundle during dipping.

【表】 上記試料を、引き続き実施例と同様に処理し獣
毛状繊維を得た。得られた獣毛状繊維の形態を表
―に示す。
[Table] The above samples were subsequently treated in the same manner as in the examples to obtain animal hair-like fibers. Table 1 shows the morphology of the animal hair-like fibers obtained.

【表】 繊維束を予熱しないと、鋭いテーパーを有する
繊維束を製造することはできない。かつ獣毛状繊
維としての品位も低い。
[Table] Unless the fiber bundle is preheated, it is not possible to produce a fiber bundle with a sharp taper. Moreover, the quality of the animal hair-like fiber is also low.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は、本発明の実施に使用する装置の一例
を示す縦断面図である。
FIG. 1 is a longitudinal cross-sectional view showing an example of an apparatus used to carry out the present invention.

Claims (1)

【特許請求の範囲】 1 合成繊維の先端部を加水分解剤水溶液に浸漬
して先細化せしめるに際し、該合成繊維を束状に
集束して繊維束とし、浸漬前の繊維束内温度を以
下の()式を満足するように予熱せしめた後、
加水分解剤水溶液に浸漬することを特徴とする獣
毛状繊維の製造方法。 TL≧50 ……() 〔ただし、TLは繊維束の中心部で、繊維束の
先端部から20mm離れた位置の温度(℃)である。〕
[Scope of Claims] 1. When the tips of synthetic fibers are immersed in an aqueous solution of a hydrolyzing agent to make them tapered, the synthetic fibers are bundled into a fiber bundle, and the temperature inside the fiber bundle before dipping is set as follows. After preheating to satisfy formula (),
A method for producing animal hair-like fibers, which comprises immersing them in an aqueous solution of a hydrolyzing agent. T L ≧50 ...() [However, T L is the temperature (°C) at the center of the fiber bundle, 20 mm away from the tip of the fiber bundle. ]
JP7342082A 1982-05-04 1982-05-04 Production of animal wool like fiber Granted JPS58191272A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7342082A JPS58191272A (en) 1982-05-04 1982-05-04 Production of animal wool like fiber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7342082A JPS58191272A (en) 1982-05-04 1982-05-04 Production of animal wool like fiber

Publications (2)

Publication Number Publication Date
JPS58191272A JPS58191272A (en) 1983-11-08
JPH0115622B2 true JPH0115622B2 (en) 1989-03-17

Family

ID=13517701

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7342082A Granted JPS58191272A (en) 1982-05-04 1982-05-04 Production of animal wool like fiber

Country Status (1)

Country Link
JP (1) JPS58191272A (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6011152B2 (en) * 1975-04-02 1985-03-23 東レ株式会社 Method for producing sharp fibers

Also Published As

Publication number Publication date
JPS58191272A (en) 1983-11-08

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