JPH0441706A - Polyvinyl alcohol-based fiber having high toughness and its production - Google Patents
Polyvinyl alcohol-based fiber having high toughness and its productionInfo
- Publication number
- JPH0441706A JPH0441706A JP14493590A JP14493590A JPH0441706A JP H0441706 A JPH0441706 A JP H0441706A JP 14493590 A JP14493590 A JP 14493590A JP 14493590 A JP14493590 A JP 14493590A JP H0441706 A JPH0441706 A JP H0441706A
- Authority
- JP
- Japan
- Prior art keywords
- toughness
- fiber
- pva
- fibers
- polyvinyl alcohol
- 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.)
- Pending
Links
- 239000000835 fiber Substances 0.000 title claims abstract description 67
- 239000004372 Polyvinyl alcohol Substances 0.000 title claims description 53
- 229920002451 polyvinyl alcohol Polymers 0.000 title claims description 53
- 238000004519 manufacturing process Methods 0.000 title claims description 7
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 18
- 238000006116 polymerization reaction Methods 0.000 claims abstract description 15
- 238000010438 heat treatment Methods 0.000 claims description 19
- 239000000203 mixture Substances 0.000 claims description 11
- 229920003023 plastic Polymers 0.000 abstract description 2
- 239000004033 plastic Substances 0.000 abstract description 2
- 239000012779 reinforcing material Substances 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 13
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 description 12
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 12
- 230000007423 decrease Effects 0.000 description 11
- 238000009987 spinning Methods 0.000 description 10
- 239000012770 industrial material Substances 0.000 description 6
- 239000007788 liquid Substances 0.000 description 6
- 230000002040 relaxant effect Effects 0.000 description 6
- 230000000052 comparative effect Effects 0.000 description 5
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 4
- 238000005520 cutting process Methods 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- 239000011550 stock solution Substances 0.000 description 4
- 238000002166 wet spinning Methods 0.000 description 4
- 239000004952 Polyamide Substances 0.000 description 3
- 238000009954 braiding Methods 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 239000012467 final product Substances 0.000 description 3
- 238000009940 knitting Methods 0.000 description 3
- 229920002647 polyamide Polymers 0.000 description 3
- 238000012805 post-processing Methods 0.000 description 3
- 230000002787 reinforcement Effects 0.000 description 3
- 238000007127 saponification reaction Methods 0.000 description 3
- 238000009941 weaving Methods 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- KGBXLFKZBHKPEV-UHFFFAOYSA-N boric acid Chemical compound OB(O)O KGBXLFKZBHKPEV-UHFFFAOYSA-N 0.000 description 2
- 230000015271 coagulation Effects 0.000 description 2
- 238000005345 coagulation Methods 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 238000000578 dry spinning Methods 0.000 description 2
- 235000011187 glycerol Nutrition 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 229920000728 polyester Polymers 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 1
- PPWHTZKZQNXVAE-UHFFFAOYSA-N Tetracaine hydrochloride Chemical compound Cl.CCCCNC1=CC=C(C(=O)OCCN(C)C)C=C1 PPWHTZKZQNXVAE-UHFFFAOYSA-N 0.000 description 1
- 229910001854 alkali hydroxide Inorganic materials 0.000 description 1
- 150000008044 alkali metal hydroxides Chemical class 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000004327 boric acid Substances 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000009958 sewing Methods 0.000 description 1
- 229910052938 sodium sulfate Inorganic materials 0.000 description 1
- 235000011152 sodium sulphate Nutrition 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- JOXIMZWYDAKGHI-UHFFFAOYSA-N toluene-4-sulfonic acid Chemical compound CC1=CC=C(S(O)(=O)=O)C=C1 JOXIMZWYDAKGHI-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Artificial Filaments (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、高強度、高初期弾性率を有し、しかも高タフ
ネスであるポリビニルアルコール(以下。Detailed Description of the Invention (Industrial Application Field) The present invention provides polyvinyl alcohol (hereinafter referred to as "polyvinyl alcohol") which has high strength, high initial modulus, and high toughness.
PVAと略記する。)系重合体からなる繊維及びその製
造法に関するものである。It is abbreviated as PVA. ) type polymer and its manufacturing method.
(従来の技術) PVA繊維は、汎用繊維の中では最も高強度。(Conventional technology) PVA fiber has the highest strength among general purpose fibers.
高初期弾性率を有し、ゴムホース、コンベアベルト、セ
メント強化用繊維、資材用縫糸1畳糸、漁網、陸上網1
重布、ロープ等の産業資材用繊維上して広く用いられて
いる。Has a high initial modulus of elasticity, rubber hoses, conveyor belts, fibers for cement reinforcement, sewing thread for materials 1 tatami thread, fishing nets, land nets 1
It is widely used as a fiber for industrial materials such as heavy fabrics and ropes.
近年、高度化する市場の要望に応じてPVA繊維の強度
や初期弾性率をさらに高めようとする試みが種々なされ
ており1例えば特開昭59−130314号公報には2
重量平均分子量50万以上のPVAのグリセリン溶液を
冷却浴中にゲル紡糸し、固化糸条のグリセリンを除去し
た後、熱延伸する方法が開示されている。また、特開昭
60−126312号公報には1重合度1800以上の
PVAのDMSO溶液をメタノール浴中に乾・湿式紡糸
し、得られた未延伸糸を熱延伸する方法が開示されてい
る。In recent years, various attempts have been made to further increase the strength and initial elastic modulus of PVA fibers in response to increasingly sophisticated market demands.
A method is disclosed in which a glycerin solution of PVA having a weight average molecular weight of 500,000 or more is gel-spun in a cooling bath, the glycerin of the solidified yarn is removed, and then hot-stretched. Further, JP-A-60-126312 discloses a method in which a DMSO solution of PVA having a degree of polymerization of 1,800 or more is dry-wet-spun in a methanol bath, and the resulting undrawn yarn is hot-stretched.
しかしながら、これらの方法では、延伸倍率を高くする
ほど切断伸度が低下するので1強度と初期弾性率をある
程度改良することはできても、タフネスを改良すること
はできなかった。However, with these methods, the higher the stretching ratio, the lower the elongation at break, so although it was possible to improve the strength and initial elastic modulus to some extent, it was not possible to improve the toughness.
一方、延伸後の繊維にリラックス処理を施す方法は一般
によく知られており、ポリアミド、ポリエステル繊維だ
けでなく、PVA繊維に対しても適用されている。On the other hand, the method of subjecting fibers after stretching to a relaxing treatment is generally well known and is applied not only to polyamide and polyester fibers but also to PVA fibers.
しかしながら、これらの方法は、単に延伸後の繊維にさ
らに熱を加え、結晶化度を高めて繊維構造を安定化させ
ることを目的としたものであり。However, these methods merely apply further heat to the stretched fibers to increase the degree of crystallinity and stabilize the fiber structure.
タフネスの向上を目的とするものではなかった。It was not intended to improve toughness.
産業資材用途においては、繊維がそのままの形で最終用
途に供されることはほとんどなく、最終製品となるまで
には製織、製編、撚糸1組紐加工等の二次加工、三次加
工が施されるのが一般的である。ところが、切断伸度が
低く、タフネスの低い繊維は、これらの後加工時に単糸
の切断が頻発したり9強力の低下が著しく、原糸の強度
が高くても加工品の強度が大きく低下してしまうという
問題があった。このため1強度が高いと同時にタフネス
の高いPVA繊維の開発が強く望まれていた。In industrial material applications, fibers are rarely used in their final form as they are; they undergo secondary and tertiary processing such as weaving, knitting, and single-strand braiding before becoming final products. It is common to However, fibers with low cutting elongation and low toughness often break single filaments during post-processing or have a significant decrease in tenacity, resulting in a significant decrease in the strength of the processed product even if the strength of the raw yarn is high. There was a problem with this. For this reason, there has been a strong desire to develop PVA fibers that have both high strength and high toughness.
(発明が解決しようとする課題)
上述したように、高強度、高初期弾性率を有するPVA
繊維は種々提案されているが、同時にタフネスの向上が
図られた繊維ではなく、産業資材用途、特にゴム補強用
として好適な高強度、高初期弾性率と高タフネスを有す
るPVA繊維は知られていなかった。(Problems to be Solved by the Invention) As mentioned above, PVA having high strength and high initial elastic modulus
Various types of fibers have been proposed, but PVA fibers, which have high strength, high initial elastic modulus, and high toughness and are suitable for industrial material applications, especially for rubber reinforcement, are not known to have improved toughness. There wasn't.
したがって1本発明の第1の課題は、高強度。Therefore, the first object of the present invention is high strength.
高初期弾性率を有し、しかもゴム補強用として中ましい
高タフネスを有するPVA系繊維を提供することにある
。The object of the present invention is to provide a PVA fiber having a high initial modulus of elasticity and moderately high toughness for use in rubber reinforcement.
また1本発明の第2の課題は、かかる高タフネスPVA
系繊維を生産性よく製造する方法を提供することにある
。A second object of the present invention is to use such high toughness PVA.
An object of the present invention is to provide a method for manufacturing fibers with high productivity.
(課題を解決するための手段)
本発明者らは、上記の課題を解決するために鋭意検討し
た結果、熱延伸後のPVA繊維に水もしくはアルコール
、又はこれらの混合液を付与した後、リラックス下で熱
処理することにより、大幅な強度低下を引き起こすこと
をなく切断伸度を増大させてタフネスを向上させ得るこ
とを見出して本発明に到達した。(Means for Solving the Problems) As a result of intensive studies to solve the above problems, the present inventors have found that after applying water, alcohol, or a mixture thereof to hot-stretched PVA fibers, relaxing The present invention was achieved by discovering that by heat-treating the material, the elongation at break can be increased and the toughness can be improved without causing a significant decrease in strength.
′すなわち1本発明は次の構成を有するものである。That is, the present invention has the following configuration.
(1)重合度1500以上、 7000以下のポリビニ
ルアルコールからなり、引張り強度が14g/d以上、
初期弾性率が250g/d以上であり、かつ、タフネス
が40g/d%以上であることを特徴とする高タフネス
ポリビニルアルコール系繊維。(1) Made of polyvinyl alcohol with a degree of polymerization of 1500 or more and 7000 or less, with a tensile strength of 14 g/d or more,
A high toughness polyvinyl alcohol fiber having an initial elastic modulus of 250 g/d or more and a toughness of 40 g/d% or more.
(2)重合度1500以上、 7000以下のポリビニ
ルアルコールからなる熱延伸後の繊維に、水もしくはア
ルコール、又はこれらの混合液を付与した後、0.5〜
10%のリラックス率下で150℃以上の温度で熱処理
することを特徴とする高タフネスポリビニルアルコール
系繊維の製造法。(2) After applying water, alcohol, or a mixture thereof to a hot-stretched fiber made of polyvinyl alcohol with a degree of polymerization of 1,500 or more and 7,000 or less,
A method for producing high-toughness polyvinyl alcohol fibers, which is characterized by heat treatment at a temperature of 150° C. or higher under a relaxation rate of 10%.
なお9本発明における引張り強度と初期弾性率はJIS
−L−1013に準じて、つかみ間隔25cm、引張り
速度30CO+/分で測定するものである。9 The tensile strength and initial elastic modulus in the present invention are based on JIS
-L-1013, the measurement is performed at a gripping interval of 25 cm and a pulling speed of 30 CO+/min.
また、タフネスは、上記の測定で得られる荷重伸度曲線
と伸度軸の間の面積を積分して求めるものである。Moreover, toughness is determined by integrating the area between the load-elongation curve and the elongation axis obtained in the above measurement.
以下1本発明をさらに詳しく説明する。The present invention will be explained in more detail below.
本発明のPVA系繊維は、 14g/d以上の引張り強
度と250g/d以上の初期弾性率という汎用のポリア
ミドやポリエステル繊維に比べ格段に高い性能を有して
いる。しかも、従来のPVA系繊維が30g/d%程度
のタフネスしか有していなかったのに対して1本発明の
PVA系繊維は、 40g/d%以上という、高タフネ
ス繊維の代表であるポリアミド繊維に近いタフネスを有
し、また、伸度も通常の高強度PVA繊維が4〜5%程
度であるのに対して。The PVA fiber of the present invention has a tensile strength of 14 g/d or more and an initial elastic modulus of 250 g/d or more, which is much higher performance than general-purpose polyamide or polyester fibers. Moreover, while conventional PVA fibers had a toughness of only about 30 g/d%, the PVA fiber of the present invention has a toughness of 40 g/d% or more, which is a typical high toughness fiber. It has a toughness close to that of PVA fiber, and its elongation is about 4 to 5% for ordinary high-strength PVA fibers.
通常5.5%以上の伸度を有しているので、産業上の有
用性が極めて高い。Since it usually has an elongation of 5.5% or more, it is extremely useful industrially.
すなわち、前述したように、産業資材用途においては、
最終製品となるまでに製織、製編、撚糸組紐加工等の後
加工が施されるのが一般的であるが1本発明のPVA系
繊維は、 40g/d%以上という高タフネスを有して
いるので、後加工時に単糸の切断や強力の低下が少なく
、加工品の強度低下を防止することができるものである
。In other words, as mentioned above, in industrial material applications,
Although post-processing such as weaving, knitting, and twist braiding is generally performed before the final product is obtained, the PVA fiber of the present invention has a high toughness of 40 g/d% or more. Therefore, during post-processing, single yarns are less likely to be cut or the strength decreases, and it is possible to prevent a decrease in the strength of the processed product.
本発明のPVA系繊維の繊度やフィラメント数は特に限
定されるものではなく 、 1200d1500f、
1500d/300fといったマルチフィラメントであ
っても。The fineness and number of filaments of the PVA fiber of the present invention are not particularly limited, and may be 1200d1500f,
Even if it is a multifilament such as 1500d/300f.
繊度が100デニール以上のモノフィラメントであって
もよい。The monofilament may have a fineness of 100 deniers or more.
本発明で用いるPVAは1重合度が1500以上。The PVA used in the present invention has a degree of polymerization of 1500 or more.
7000以下である必要があり、好ましくは3000以
上。It must be 7000 or less, preferably 3000 or more.
5000以下である。重合度が1500未満では、最終
製品の引張り強度や初期弾性率等が目的とする値よりも
小さくなるので不適当である。また1重合度が7000
を超えるPVAはポリマーコストが高くなり、最終製品
のコストアップにつながるため産業資材用途への広凡な
適用が困難となる。5000 or less. A degree of polymerization of less than 1500 is unsuitable because the tensile strength, initial elastic modulus, etc. of the final product will be lower than the desired values. Also, the degree of polymerization is 7000
PVA that exceeds 100% has a high polymer cost, leading to an increase in the cost of the final product, making it difficult to widely apply it to industrial material applications.
本発明の製造法において、供給系となるPVA繊維の紡
糸方式は特に限定されるものではないが。In the production method of the present invention, the spinning method of the PVA fiber serving as the supply system is not particularly limited.
例えば本発明者らが先に提案した特願平1−12203
0号に記載の乾・湿式(ゲル)紡糸方法を採用すること
ができる。For example, patent application No. 1-12203 proposed by the present inventors
The dry/wet (gel) spinning method described in No. 0 can be adopted.
すなわち1重合度1500以上のPVAをDMSOを主
成分とする溶媒に溶解して調製した紡糸原液を乾・湿式
紡糸し、得られた未延伸糸を熱延伸してPVAm、!を
製造するに際し、紡糸原液出口側に突出する形状の吐出
孔を有する紡糸口金を用いて乾・湿式紡糸し、しかる後
に熱延伸することにより製造することができる。That is, a spinning stock solution prepared by dissolving PVA with a degree of polymerization of 1,500 or more in a solvent mainly composed of DMSO is dry/wet-spun, and the resulting undrawn yarn is hot-stretched to form PVAm,! can be produced by performing dry/wet spinning using a spinneret having a discharge hole protruding from the spinning dope exit side, followed by hot stretching.
また、従来公知の紡糸方法1例えばホウ酸又はホウ酸塩
を含有したPVA水溶液を紡糸原液とし。In addition, conventionally known spinning method 1, for example, a PVA aqueous solution containing boric acid or a boric acid salt is used as the spinning stock solution.
水酸化アルカリと硫酸ナトリウム等を凝固浴とする湿式
紡糸方法によっても製造することが可能である。It can also be produced by a wet spinning method using a coagulation bath of alkali hydroxide, sodium sulfate, or the like.
本発明においては、熱延伸後のこれらのPVA繊維に水
もしくはアルコール、又はこれらの混合物を付与した後
、0.5〜10%のリラックス率下で熱処理を行う。In the present invention, after applying water, alcohol, or a mixture thereof to these hot-stretched PVA fibers, heat treatment is performed at a relaxation rate of 0.5 to 10%.
すなわち1通常熱延伸は、工業的には周速度の異なる一
対のローラ(このうち周速度の低いものを供給ローラ、
高いものを延伸ローラとする。)間に糸条を走行させ、
このローラ間の糸条を様々な手段で加熱することによっ
て行われ、さらに。In other words, 1. In normal hot stretching, industrially, a pair of rollers with different circumferential speeds (the one with the lower circumferential speed is the supply roller,
Use the taller one as the stretching roller. ), run the yarn between
This is done by heating the yarn between the rollers by various means, and further.
これを多段で行う場合もあるが1本発明においては2最
終延伸段の延伸ローラ以降にさらにリラックスローラを
設け、延伸ローラとリラックスローラとの間で熱延伸後
の糸条に水もしくはアルコール、又はこれらの混合物を
付与した後、下式で定義される0、5〜10%のリラッ
クス率下で150℃以上の温度で熱処理を行う。Although this may be carried out in multiple stages, in the present invention, a relaxation roller is further provided after the stretching roller of the second final stretching stage, and between the stretching roller and the relaxing roller, water, alcohol, or After applying these mixtures, heat treatment is performed at a temperature of 150° C. or higher under a relaxation rate of 0.5 to 10% defined by the following formula.
未延伸糸に水等を付与して熱処理してもタフネスの増加
は達成されないので9本発明では延伸糸を供給系として
実施する必要があり、好ましくは最高延伸倍率の85%
以上の延伸、より好ましくは90%以上の延伸を行い、
切断伸度が5%以下とした熱延伸糸を用いるのがよい。Even if undrawn yarn is heat-treated by adding water or the like, no increase in toughness will be achieved.9 Therefore, in the present invention, it is necessary to implement the drawn yarn as a supply system, and preferably 85% of the maximum drawing ratio.
or more stretching, more preferably 90% or more stretching,
It is preferable to use hot-drawn yarn with a breaking elongation of 5% or less.
本発明者らは、リラックス率とタフネスとの関係につい
て詳細な検討を加えた結果、熱延伸後のPVA繊維をそ
のまま熱処理を行った場合、リラックス率を高くすると
、切断伸度は増大するものの強度低下が大きく、タフネ
スは増加しないのに対して、水もしくはアルコール、又
はこれらの混合物を付与して熱処理すると1強度低下が
抑制されつつ伸度が増大し、タフネスが増大するという
事実を見出した。さらに、リラックス率が高いほど強度
低下は小さく、シかも切断伸度が大きくなるため、より
効果的にタフネスを増大させ得ることも見出した。As a result of detailed study on the relationship between relaxation rate and toughness, the present inventors found that when PVA fibers are directly heat-treated after hot drawing, when the relaxation rate is increased, the elongation at break increases, but the strength increases. It has been found that, while the decrease is large and the toughness does not increase, when water, alcohol, or a mixture thereof is applied and heat treated, the elongation increases while suppressing the decrease in strength by 1, and the toughness increases. Furthermore, the inventors have also found that the higher the relaxation rate, the smaller the decrease in strength and the greater the cutting elongation, which makes it possible to increase toughness more effectively.
また、水を付与した際には1強度低下は小さいものの、
可能なリラックス率の上限は5%程度であるのに対して
、アルコールを付与した際には。In addition, when adding water, although the decrease in strength by 1 is small,
The upper limit of the possible relaxation rate is about 5%, whereas when alcohol is added.
可能なリラックス率の上限は10%になるが1強度低下
は水の場合に比べて大きいことも知見した。It was also found that although the upper limit of the possible relaxation rate is 10%, a decrease in strength of 1 is larger than in the case of water.
以上の事実により1本発明において、熱処理時のリラッ
クス率を0.5〜lO%、好ましくは2〜10%にする
必要があり、この範囲で可能な限り高い方が好ましい。Based on the above facts, in the present invention, it is necessary to set the relaxation rate during heat treatment to 0.5 to 10%, preferably 2 to 10%, and it is preferable that it be as high as possible within this range.
リラックス率が0.5%よりも小さいと切断伸度の増加
が小さくてタフネスが40g/d以上とはならず、また
、10%よりも大きいと、熱処理時に糸条に掛かる張力
が低くなりすぎ、糸条の溶断が起こるので好ましくない
。If the relaxation rate is less than 0.5%, the increase in cutting elongation will be small and the toughness will not exceed 40 g/d, and if it is greater than 10%, the tension applied to the yarn during heat treatment will be too low. , which is not preferable because the threads may be fused and cut.
本発明において、熱延伸後のPVA繊維に付与するアル
コールとしては、メタノール、エタノール、プロパツー
ル等を挙げることができるが、エタノールが好適に用い
られ、さらには水とエタノールの混合物がより好ましい
。水とエタノールの混合物が特に好ましいのは、リラッ
クス率が高いほど高タフネス化が可能であるものの、水
単独を付与する場合には高いリラックス率がとれず、逆
にアルコール単独を付与する場合にはリラックス率は高
くとれるものの1強度低下が大きくなるので、この両方
の長所をとり入れることができるからである。水とアル
コールの容積混合比は90 : 10〜50 : 50
の範囲が好ましい。In the present invention, examples of the alcohol to be applied to the PVA fiber after hot drawing include methanol, ethanol, propatool, etc., but ethanol is preferably used, and a mixture of water and ethanol is more preferable. A mixture of water and ethanol is particularly preferable because the higher the relaxation rate, the higher the toughness. This is because although the relaxation rate can be high, the reduction in strength by one level is large, so the advantages of both can be taken advantage of. The volume mixing ratio of water and alcohol is 90:10~50:50
A range of is preferred.
本発明においては、これらの液に塩酸、リン酸。In the present invention, these liquids include hydrochloric acid and phosphoric acid.
パラトルエンスルホン酸等の脱水反応促進用の触媒や、
油剤、顔料等を混入してもよい。Catalysts for promoting dehydration reactions such as para-toluenesulfonic acid,
Oil agents, pigments, etc. may be mixed.
水等の液を付与する方法は特に限定されるものではなく
、いわゆるオイリングローラで付与する方法、これらの
液中に浸漬させる方法、液を噴霧する方法等を用いるこ
とができる。The method of applying liquid such as water is not particularly limited, and methods such as applying with a so-called oiling roller, immersing in these liquids, and spraying the liquid can be used.
付与量は特に限定されるものではないが、繊維に対し0
.1〜3.0重量%の液を付与するのが好ましい。The amount applied is not particularly limited, but 0 to the fiber
.. It is preferable to apply 1 to 3.0% by weight of the liquid.
また、これらの液を付与し、連続的に乾燥処理を施した
後、熱処理を行ってもよいが、その場合には、乾燥時の
収縮応力を熱処理工程に波及させ、熱処理時の張力が低
下しないようにするのがよい。In addition, heat treatment may be performed after applying these liquids and performing continuous drying treatment, but in that case, the shrinkage stress during drying will spread to the heat treatment process and the tension during heat treatment will decrease. It is best to avoid doing so.
熱処理時の張力は0.1〜1.0g/dとするのが好ま
しい。The tension during heat treatment is preferably 0.1 to 1.0 g/d.
熱処理は150℃以上で行う必要があるが、その上限は
繊維の融点であり、好ましくは180〜260℃で、1
〜60秒間、特に3〜20秒間行うのがよい。The heat treatment must be performed at a temperature of 150°C or higher, but the upper limit is the melting point of the fiber, preferably 180 to 260°C, and 1
It is preferable to carry out for ~60 seconds, especially for 3 to 20 seconds.
熱処理温度が150℃未満では、繊維の十分な応力除去
ができず、目的とする高タフネスが得られない。If the heat treatment temperature is less than 150° C., sufficient stress relief from the fibers cannot be achieved, and the desired high toughness cannot be obtained.
(作 用)
本発明において、 40g/d%以上という高タフネス
PVA系繊維が得られるのは、付与された水やアルコー
ル分子が繊維を構成するPVA分子鎮間に侵入し、その
PVA分子鎖を収縮させるので、0.5〜10%という
リラックス率下でも糸条の張力が維持された状態で熱処
理されることになり、このためPVA分子鎖のひずみが
除去されるためと認められる。(Function) In the present invention, high toughness PVA fibers of 40 g/d% or more can be obtained because the applied water and alcohol molecules enter the PVA molecular chains constituting the fibers and break down the PVA molecular chains. This is believed to be due to the fact that, since the fibers are shrunk, the tension of the threads is maintained during the heat treatment even under a relaxation rate of 0.5 to 10%, which removes the strain in the PVA molecular chains.
(実施例) 次に1本発明を実施例により具体的に説明する。(Example) Next, one embodiment of the present invention will be specifically explained using examples.
実施例1
重合度3900(7)PVA (ケン化度99.9%
Jl/%)の15重量%DMSO溶液を調製し、この紡
糸原液を内径0.54mmのステンレス製円筒状細管3
00本を紡糸原液出口側に3a+m突出するように埋め
込んだ紡糸口金を用いて吐出線速度4m1分、紡糸ドラ
フト4.0でメタノール凝固浴中に10mmのエアギャ
ップを通して乾・湿式紡糸し、メタノールでDMSOを
抽出した後、乾燥して未延伸糸を得た。Example 1 Polymerization degree 3900 (7) PVA (saponification degree 99.9%
Jl/%) was prepared, and this spinning stock solution was passed through a stainless steel cylindrical capillary tube 3 with an inner diameter of 0.54 mm.
Dry/wet spinning was carried out using a spinneret embedded so that 00 fibers protruded 3a+m toward the outlet side of the spinning dope through a 10mm air gap in a methanol coagulation bath at a linear discharge speed of 4m1 min and a spinning draft of 4.0. After extracting DMSO, it was dried to obtain an undrawn yarn.
次いでこの未延伸糸を、供給ローラと延伸ローラ間に設
けられ、入口温度205℃、出口温度265℃に設定さ
れた熱風温で延伸し、延伸ローラを出た延伸糸に水/エ
タノール混合液(70/30容積比)をオイリングロー
ラで0.7重量%付与した後、内部温度が135℃に設
定された乾燥機中で60!>間乾燥した。さらにこの糸
条を、内部温度が220tに設定された熱処理機中を3
秒間走行させ、リラックスローラで把持した後捲取り、
1500d/300fの繊維を得た。このとき、延伸
ローラとリラックスローラの速度比は1:0.95で5
%のリラックス率であり。Next, this undrawn yarn is drawn with hot air provided between a supply roller and a drawing roller, with an inlet temperature of 205°C and an outlet temperature of 265°C, and a water/ethanol mixture ( After applying 0.7% by weight of 70/30 volume ratio) with an oiling roller, 60! > Dry for a while. Furthermore, this yarn was passed through a heat treatment machine with an internal temperature of 220 tons for 3
Run it for seconds, grip it with a relaxing roller, and then wind it up.
A fiber of 1500d/300f was obtained. At this time, the speed ratio of the stretching roller and relaxing roller is 1:0.95, which is 5
% relaxation rate.
熱処理時の張力は0.7g/dであった。The tension during heat treatment was 0.7 g/d.
上記で得られた繊維は、引張り強度15.5g/d、初
期弾性率298g/d、伸度5.6%、タフネス49.
5g/d%と極めて優れた性能を有していた。The fiber obtained above had a tensile strength of 15.5 g/d, an initial elastic modulus of 298 g/d, an elongation of 5.6%, and a toughness of 49.
It had an extremely excellent performance of 5 g/d%.
比較例1
水/エタノール混合液を付与しない以外は実施例1と同
様にしてPVA系繊維を製造したところ。Comparative Example 1 PVA-based fibers were produced in the same manner as in Example 1 except that the water/ethanol mixture was not applied.
得られた繊維は引張り強度12.5g/d、初期弾性率
220g/d、伸度5,5%、タフネス39.2g/d
%でしかなかった。The obtained fiber had a tensile strength of 12.5 g/d, an initial modulus of elasticity of 220 g/d, an elongation of 5.5%, and a toughness of 39.2 g/d.
It was only a percentage.
比較例2
熱処理機の内部温度を145℃に設定した以外は実施例
1と同様にしてPVA系繊維を製造したところ、得られ
た繊維は引張り強度14.8g/d、初期弾性率317
g/d、伸度4.5%であったが、タフネスは38、0
g/d%でしかなかった。Comparative Example 2 PVA-based fibers were produced in the same manner as in Example 1 except that the internal temperature of the heat treatment machine was set at 145°C. The obtained fibers had a tensile strength of 14.8 g/d and an initial elastic modulus of 317.
g/d, elongation was 4.5%, but toughness was 38.0
It was only g/d%.
比較例3.4
延伸ローラとリラックスローラの速度比をに0.997
(リラックス比0.3%)及び1:0.85(リラック
ス比15%)とした以外は実施例1と同様にしてPVA
系繊維を製造した。Comparative Example 3.4 The speed ratio of the stretching roller and relaxing roller is 0.997
(relaxation ratio 0.3%) and 1:0.85 (relaxation ratio 15%) in the same manner as in Example 1.
produced fibers.
リラックス比0.3%の場合に得られた繊維は。The fiber obtained when the relaxation ratio was 0.3%.
引張り強度15.3g/d、初期弾性率312g/dで
あったが。The tensile strength was 15.3 g/d and the initial elastic modulus was 312 g/d.
伸度は4.5%、タフネスは32.3g/d%と低下し
ていた。また、リラックス比15%の場合には、熱処理
機中で繊維の溶断が多発し、試料の採取ができなかった
。The elongation was decreased to 4.5% and the toughness was decreased to 32.3 g/d%. Furthermore, when the relaxation ratio was 15%, the fibers were frequently fused and cut in the heat treatment machine, making it impossible to collect samples.
実施例2.比較例5
重合度1300のPVA (ケン化度99.9モル%)
の29重量%DMSO溶液、及び重合度1700のPV
A(ケン化度99.7モル%)の24重量%DMS○溶
液を調製し、これらの紡糸原液を実施例1と同様に乾・
湿式紡糸して未延伸を得た。Example 2. Comparative Example 5 PVA with a polymerization degree of 1300 (saponification degree 99.9 mol%)
29 wt% DMSO solution of and PV with a degree of polymerization of 1700
A 24% by weight DMS○ solution of A (saponification degree 99.7 mol%) was prepared, and these spinning stock solutions were dried in the same manner as in Example 1.
An unstretched product was obtained by wet spinning.
次いで、この未延伸糸に対し、実施例1と同様の熱延伸
、水/メタノール混合液付与、乾燥及び熱処理を行った
。Next, this undrawn yarn was subjected to the same hot stretching, application of a water/methanol mixture, drying, and heat treatment as in Example 1.
重合度1300のPVAから得られた繊維(比較例5)
は、切断伸度が5.7%であったものの、引張り強度1
2.5g/d、初期弾性率230g/d、タフネス30
.7g/d%にすぎなかった。Fiber obtained from PVA with a degree of polymerization of 1300 (Comparative Example 5)
Although the elongation at break was 5.7%, the tensile strength was 1
2.5g/d, initial elastic modulus 230g/d, toughness 30
.. It was only 7 g/d%.
一方1重合度1700のPVAから得られた繊1/#(
実施例2)は、引張り強度14.2g/d、初期弾性率
260g/d%。On the other hand, fibers obtained from PVA with a degree of polymerization of 1700 1/# (
Example 2) has a tensile strength of 14.2 g/d and an initial elastic modulus of 260 g/d%.
切断伸度5.6%、タフネス41.3g/d%と満足な
性能を有していた。It had satisfactory performance with cutting elongation of 5.6% and toughness of 41.3 g/d%.
(発明の効果)
本発明のPVA系繊維は、ポリアミド繊維に近い高いタ
フネスを有する。PVA系としては従来にない繊維であ
り、このためPVA繊維の代表的な用途である漁網やロ
ープとしての用途拡大が図れるばかりでなく、製織、製
編、撚糸1組紐加工等の二次加工による強度低下が小さ
いので、ゴム。(Effects of the Invention) The PVA-based fiber of the present invention has high toughness close to that of polyamide fiber. This is an unprecedented PVA-based fiber, which not only makes it possible to expand its use in fishing nets and ropes, which are the typical uses of PVA fibers, but also allows for secondary processing such as weaving, knitting, and single-twist braiding. Rubber because the strength loss is small.
プラスチック等の補強材料としての使用も可能であり、
各種の産業資材用途に好適な繊維である。It can also be used as a reinforcing material for plastics, etc.
It is a fiber suitable for various industrial material applications.
また1本発明の高タフネスPVA系繊維の製造法によれ
ば、上記の利点を有するPVA系繊維を生産性よく、低
コストで製造することが可能となる。Furthermore, according to the method for producing high-toughness PVA-based fibers of the present invention, it is possible to produce PVA-based fibers having the above-mentioned advantages with good productivity and at low cost.
Claims (2)
アルコールからなり、引張り強度が14g/d以上、初
期弾性率が250g/d以上であり、かつ、タフネスが
40g/d%以上であることを特徴とする高タフネスポ
リビニルアルコール系繊維。(1) It is made of polyvinyl alcohol with a degree of polymerization of 1500 or more and 7000 or less, has a tensile strength of 14 g/d or more, an initial elastic modulus of 250 g/d or more, and a toughness of 40 g/d% or more. High toughness polyvinyl alcohol fiber.
アルコールからなる熱延伸後の繊維に、水もしくはアル
コール、又はこれらの混合液を付与した後、0.5〜1
0%のリラックス率下で150℃以上の温度で熱処理す
ることを特徴とする高タフネスポリビニルアルコール系
繊維の製造法。(2) After applying water, alcohol, or a mixture thereof to a hot-stretched fiber made of polyvinyl alcohol with a degree of polymerization of 1,500 or more and 7,000 or less,
A method for producing high-toughness polyvinyl alcohol fiber, characterized by heat treatment at a temperature of 150° C. or higher under a relaxation rate of 0%.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14493590A JPH0441706A (en) | 1990-06-01 | 1990-06-01 | Polyvinyl alcohol-based fiber having high toughness and its production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14493590A JPH0441706A (en) | 1990-06-01 | 1990-06-01 | Polyvinyl alcohol-based fiber having high toughness and its production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0441706A true JPH0441706A (en) | 1992-02-12 |
Family
ID=15373617
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP14493590A Pending JPH0441706A (en) | 1990-06-01 | 1990-06-01 | Polyvinyl alcohol-based fiber having high toughness and its production |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0441706A (en) |
-
1990
- 1990-06-01 JP JP14493590A patent/JPH0441706A/en active Pending
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