JPH03213510A - Polyvinyl alcohol-based fiber and its production - Google Patents
Polyvinyl alcohol-based fiber and its productionInfo
- Publication number
- JPH03213510A JPH03213510A JP319590A JP319590A JPH03213510A JP H03213510 A JPH03213510 A JP H03213510A JP 319590 A JP319590 A JP 319590A JP 319590 A JP319590 A JP 319590A JP H03213510 A JPH03213510 A JP H03213510A
- Authority
- JP
- Japan
- Prior art keywords
- fiber
- fibers
- pva
- hot water
- water resistance
- 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 127
- 229920002451 polyvinyl alcohol Polymers 0.000 title claims description 87
- 239000004372 Polyvinyl alcohol Substances 0.000 title claims description 83
- 238000004519 manufacturing process Methods 0.000 title claims description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 64
- 239000003054 catalyst Substances 0.000 claims abstract description 27
- 238000006116 polymerization reaction Methods 0.000 claims abstract description 20
- 238000006297 dehydration reaction Methods 0.000 claims description 19
- 230000001737 promoting effect Effects 0.000 claims description 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 abstract description 24
- 239000004566 building material Substances 0.000 abstract description 7
- 238000006243 chemical reaction Methods 0.000 abstract description 6
- JOXIMZWYDAKGHI-UHFFFAOYSA-N toluene-4-sulfonic acid Chemical compound CC1=CC=C(S(O)(=O)=O)C=C1 JOXIMZWYDAKGHI-UHFFFAOYSA-N 0.000 abstract description 6
- 230000003014 reinforcing effect Effects 0.000 abstract description 4
- 239000012783 reinforcing fiber Substances 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 33
- 238000010438 heat treatment Methods 0.000 description 26
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 18
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 description 14
- 239000000243 solution Substances 0.000 description 13
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 12
- 238000009987 spinning Methods 0.000 description 12
- 239000002253 acid Substances 0.000 description 9
- 239000004568 cement Substances 0.000 description 8
- 229920000642 polymer Polymers 0.000 description 8
- 230000000052 comparative effect Effects 0.000 description 7
- 238000002166 wet spinning Methods 0.000 description 7
- 230000000704 physical effect Effects 0.000 description 6
- 238000000578 dry spinning Methods 0.000 description 5
- 239000012770 industrial material Substances 0.000 description 5
- 239000011550 stock solution Substances 0.000 description 5
- 238000006359 acetalization reaction Methods 0.000 description 4
- 239000010425 asbestos Substances 0.000 description 4
- KGBXLFKZBHKPEV-UHFFFAOYSA-N boric acid Chemical compound OB(O)O KGBXLFKZBHKPEV-UHFFFAOYSA-N 0.000 description 4
- 239000004327 boric acid Substances 0.000 description 4
- 238000004132 cross linking Methods 0.000 description 4
- 230000007423 decrease Effects 0.000 description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- -1 polyvinylene structure Polymers 0.000 description 4
- 230000002787 reinforcement Effects 0.000 description 4
- 229910052895 riebeckite Inorganic materials 0.000 description 4
- 229920000049 Carbon (fiber) Polymers 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000007864 aqueous solution Substances 0.000 description 3
- 239000004917 carbon fiber Substances 0.000 description 3
- 230000005611 electricity Effects 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- 230000003068 static effect Effects 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 2
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 2
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 description 2
- 239000000378 calcium silicate Substances 0.000 description 2
- 229910052918 calcium silicate Inorganic materials 0.000 description 2
- OYACROKNLOSFPA-UHFFFAOYSA-N calcium;dioxido(oxo)silane Chemical compound [Ca+2].[O-][Si]([O-])=O OYACROKNLOSFPA-UHFFFAOYSA-N 0.000 description 2
- 230000015271 coagulation Effects 0.000 description 2
- 238000005345 coagulation Methods 0.000 description 2
- 239000003431 cross linking reagent Substances 0.000 description 2
- 229920001971 elastomer Polymers 0.000 description 2
- ZBGRMWIREQJHPK-UHFFFAOYSA-N ethenyl 2,2,2-trifluoroacetate Chemical compound FC(F)(F)C(=O)OC=C ZBGRMWIREQJHPK-UHFFFAOYSA-N 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 150000001451 organic peroxides Chemical class 0.000 description 2
- 239000002243 precursor Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000012779 reinforcing material Substances 0.000 description 2
- 239000005060 rubber Substances 0.000 description 2
- 239000010454 slate Substances 0.000 description 2
- 229910052938 sodium sulfate Inorganic materials 0.000 description 2
- 235000011152 sodium sulphate Nutrition 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- 229920001169 thermoplastic Polymers 0.000 description 2
- RXNOYRCWKRFNIM-UHFFFAOYSA-N 2-carbonochloridoylbenzoic acid Chemical compound OC(=O)C1=CC=CC=C1C(Cl)=O RXNOYRCWKRFNIM-UHFFFAOYSA-N 0.000 description 1
- BTBUEUYNUDRHOZ-UHFFFAOYSA-N Borate Chemical compound [O-]B([O-])[O-] BTBUEUYNUDRHOZ-UHFFFAOYSA-N 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 239000004952 Polyamide Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- PWAXUOGZOSVGBO-UHFFFAOYSA-N adipoyl chloride Chemical compound ClC(=O)CCCCC(Cl)=O PWAXUOGZOSVGBO-UHFFFAOYSA-N 0.000 description 1
- 150000001299 aldehydes Chemical class 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
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 229910021538 borax Inorganic materials 0.000 description 1
- 230000000711 cancerogenic effect Effects 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 231100000315 carcinogenic Toxicity 0.000 description 1
- 239000007809 chemical reaction catalyst Substances 0.000 description 1
- 230000001112 coagulating effect Effects 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 239000004567 concrete Substances 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- NBVXSUQYWXRMNV-UHFFFAOYSA-N fluoromethane Chemical compound FC NBVXSUQYWXRMNV-UHFFFAOYSA-N 0.000 description 1
- 239000010881 fly ash Substances 0.000 description 1
- 238000001891 gel spinning Methods 0.000 description 1
- 235000011187 glycerol Nutrition 0.000 description 1
- 239000010440 gypsum Substances 0.000 description 1
- 229910052602 gypsum Inorganic materials 0.000 description 1
- 238000001027 hydrothermal synthesis Methods 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 239000011044 quartzite Substances 0.000 description 1
- 238000005464 sample preparation method Methods 0.000 description 1
- 238000007127 saponification reaction Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000009958 sewing Methods 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- 239000004328 sodium tetraborate Substances 0.000 description 1
- 235000010339 sodium tetraborate Nutrition 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
Landscapes
- Chemical Treatment Of Fibers During Manufacturing Processes (AREA)
- 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、しかも耐熱水性
に優れたポリビニルアルコール(以下。Detailed Description of the Invention (Industrial Field of Application) The present invention is a polyvinyl alcohol (hereinafter referred to as "polyvinyl alcohol") which has high strength, high initial modulus, and excellent hot water resistance.
PVAと略記する。)系重合体からなる繊維、並びに、
引張り強度に優れた導電性ポリビニルアルコール系繊維
、及びそれらの製造法に関するものである。It is abbreviated as PVA. ) type polymer, and
This invention relates to conductive polyvinyl alcohol fibers with excellent tensile strength and methods for producing them.
(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9畳糸、漁網、陸上網1
重布、ロープ等の産業資材用繊維として広く用いられて
いる。Has a high initial modulus of elasticity, rubber hoses, conveyor belts, cement reinforcement fibers, sewing threads for materials 9 tatami threads, fishing nets, land nets 1
It is widely used as a fiber for industrial materials such as heavy fabrics and ropes.
しかしながら、PVA繊維は熱水に対する抵抗性が低い
ため、熱水に対する耐久性が要求される産業資材用途へ
の適用が阻まれる原因となっている。However, PVA fibers have low resistance to hot water, which prevents them from being applied to industrial materials that require durability against hot water.
特に、アスベストに発ガン性があることが明らかになっ
てからは、アスベストを補強繊維としていた。いわゆる
アスベストスレート板やケイ酸カルシウム板等の建築材
料にアスベスト代替としてPVA繊維を使用することが
検討されているが。In particular, after it became clear that asbestos was carcinogenic, asbestos was used as a reinforcing fiber. The use of PVA fibers as a substitute for asbestos in building materials such as so-called asbestos slate boards and calcium silicate boards is being considered.
PVA繊維は熱水に対する抵抗性が低いため9次のよう
な問題があった。PVA fibers have the following problems because they have low resistance to hot water.
すなわち、PVA繊維はセメントとのなじみがよく、か
つ、高強度を有するものの、これらの建築材料はオート
クレーブ養生によって大量生産されるため、従来のPV
A繊維では下記の理由によりオートクレーブ養生によっ
て繊維が著しく劣化し、得られる建築材料の強度が低く
なり実用に供しえないものとなる。In other words, although PVA fibers are compatible with cement and have high strength, these building materials are mass-produced by autoclave curing, so conventional PV
Due to the following reasons, the fiber A deteriorates significantly during autoclave curing, and the strength of the resulting building material decreases, making it unsuitable for practical use.
オートクレーブ養生は、セメント、ケイ石、フライアッ
シュ、石膏等の水硬性無機物質の成形体をオートクレー
ブ内にて高温・高圧の飽和水蒸気で加熱し、水硬性無機
物質を水熱反応によって硬化させる処理であり1通常、
養生温度は130〜160℃、養生時間は4〜24時間
の範囲である。したがって、従来のPVA繊維は耐熱水
性が劣るため。Autoclave curing is a process in which molded bodies of hydraulic inorganic substances such as cement, quartzite, fly ash, and gypsum are heated in an autoclave with high-temperature, high-pressure saturated steam to harden the hydraulic inorganic substances through a hydrothermal reaction. Yes 1 Usually,
The curing temperature is in the range of 130 to 160°C, and the curing time is in the range of 4 to 24 hours. Therefore, conventional PVA fibers have poor hot water resistance.
上記のような条件でのオートクレーブ養生に耐えること
ができず、得られる建築材料の強度が低くなるものであ
る。It cannot withstand autoclave curing under the above conditions, and the strength of the resulting building material decreases.
PVA繊維は、原料のPVAの重合度が高い程。For PVA fibers, the higher the degree of polymerization of the raw material PVA.
得られる繊維の耐熱水性が高くなることが知られている
。したがって1重合度の高いPVAを用いれば、耐熱水
性の優れたPVA繊維が得られることは自明であるが、
産業資材用途への広い適用が可能となるような、140
℃以上という高い耐熱水性を得るためには重合度100
00以上の超高重合度PVAを用いなければならなかっ
た。ところが、このような超高重合度PVAは商業的な
入手が困難なばかりか、溶媒への溶解性が悪いために紡
糸が困難であり、高強度の繊維が得られないという問題
があった。It is known that the resulting fibers have high hot water resistance. Therefore, it is obvious that PVA fibers with excellent hot water resistance can be obtained by using PVA with a high degree of monopolymerization.
140, which can be widely applied to industrial material applications.
In order to obtain high hot water resistance of ℃ or higher, the degree of polymerization is 100.
PVA with an ultra-high polymerization degree of 0.00 or higher had to be used. However, such ultra-high polymerization degree PVA is not only difficult to obtain commercially, but also has poor solubility in solvents, making it difficult to spin, making it difficult to obtain high-strength fibers.
このため、特開昭61−108713号公報には、トリ
フルオロ酢酸ビニルを原料として作製したシンジオタク
チック構造に富んだPVAのジメチルスルホキシド(以
下、DMS○と略記する。)溶液。For this reason, JP-A-61-108713 discloses a dimethyl sulfoxide (hereinafter abbreviated as DMS○) solution of PVA rich in syndiotactic structure prepared using vinyl trifluoroacetate as a raw material.
あるいはグリセリン溶液を乾・湿式紡糸、あるいはゲル
紡糸することにより耐熱水性に優れたPVA繊維を得る
方法が開示されている。Alternatively, a method for obtaining PVA fibers with excellent hot water resistance by dry/wet spinning or gel spinning a glycerin solution is disclosed.
しかしながら、この方法では確かにある程度耐熱水性と
強度、初期弾性率に優れたPVA繊維が得られるものの
、耐熱水性は高々120℃でしかなく、シかもトリフル
オロ酢酸ビニルを原料とするPVAは極めて高価である
ばかりか、商業的に入手することが困難であり、工業的
な規模では実施し難いという欠点がある。However, although this method does yield PVA fibers with excellent hot water resistance, strength, and initial elastic modulus, the hot water resistance is only 120°C at most, and PVA made from vinyl trifluoroacetate is extremely expensive. Moreover, it has the disadvantage that it is difficult to obtain commercially and difficult to implement on an industrial scale.
一方、商業的に入手可能なPVAを用いて耐熱水性を改
良しようとする試みとして、特開昭63120107号
公報には、延伸糸条を一10〜7%のストレッチ率下で
アセタール化度が5モル%以上、15モル%以下になる
ようにアセタール化処理する方法が開示されている。On the other hand, as an attempt to improve the hot water resistance using commercially available PVA, Japanese Patent Application Laid-Open No. 63120107 discloses that the degree of acetalization of drawn yarn is 5% under a stretch rate of -10% to 7%. A method is disclosed in which the acetalization treatment is performed so that the amount is mol % or more and 15 mol % or less.
しかしながら1本発明者らが詳細に追試した結果、この
方法とても、得られる繊維の耐熱水性は120℃程度に
すぎず、しかもアセタール化処理時に延伸糸条にホルマ
リンのようなアルデヒド類を導入して反応させるもので
あるため、目的のアセタール化度を得るためには長時間
の処理が必要であることが明らかとなり、前記の方法と
同様に工業的な規模では実施しがたいという欠点がある
。However, as a result of detailed trials by the present inventors, we found that the hot water resistance of the fiber obtained using this method was only about 120°C, and that aldehydes such as formalin were introduced into the drawn yarn during the acetalization process. Since this method involves a reaction, it is clear that a long treatment time is required to obtain the desired degree of acetalization, and like the above-mentioned method, it is difficult to implement on an industrial scale.
また、特開平1−104815号公報には、ゲル状未延
一
伸繊維を7倍以上に熱延伸した後、ホウ酸水溶液で処理
し、引き続いて熱延伸することにより、耐熱水性の高い
PVA繊維を製造する方法が記載されている。しかしな
がら、この方法でも得られる繊維の耐熱水性は高々12
5℃でしかなく、セメント補強用としてオートクレーブ
養生に耐えるものではなかった。Furthermore, in JP-A-1-104815, PVA fibers with high hot water resistance are produced by hot-stretching gel-like undrawn single-stretched fibers to 7 times or more, treating them with a boric acid aqueous solution, and then hot-stretching them. A method of manufacturing is described. However, the hot water resistance of the fiber obtained even with this method is at most 12
The temperature was only 5°C, and it could not withstand autoclave curing for cement reinforcement.
さらに、特開平1−156517号公報には、3倍以上
に延伸した糸条に架橋性薬剤を付着させた後、3倍以上
に乾熱延伸して耐熱水性の高いPVA繊維を製造する方
法が記載されている。しかしながら。Furthermore, JP-A-1-156517 discloses a method of producing PVA fibers with high hot water resistance by attaching a crosslinking agent to yarns that have been stretched three times or more, and then dry-heat stretching them three times or more. Are listed. however.
この方法でも得られる繊維もセメント補強用としてオー
トクレーブ養生に耐える程の耐熱水性を有するものでは
なかった。しかも、この方法で用いられる架橋性薬剤と
しての有機系過酸化物は非常に高価なため、コストアッ
プになるだけでなく。The fibers obtained by this method also did not have enough hot water resistance to withstand autoclave curing for cement reinforcement. Moreover, the organic peroxide used as the crosslinking agent used in this method is very expensive, which not only increases the cost.
空気中の酸素は前記薬剤による架橋反応の停止剤として
作用するため、架橋効率が悪いという欠点があった。Since oxygen in the air acts as a terminator for the crosslinking reaction caused by the above-mentioned chemicals, there is a drawback that the crosslinking efficiency is poor.
一方、従来より、繊維製品の静電気障害を解消6
するには、導電性を有する繊維を少量混入する方法が有
効であることが知られている。一般に、このような導電
性を有する繊維としては、導電性のカーボンブラック粒
子を含有する重合体からなる導電性繊維が用いられてい
る。しかしながら、従来の導電性繊維は、熱可塑性の重
合体(例えばポリアミド、ポリエステル、フルオロカー
ボン等)と、これらの重合体に導電性カーボンブラック
粒子を混入した熱可塑性重合体から形成された複合繊維
であるため、その引張り強度は高々4g/dに過ぎなか
った。On the other hand, it has been conventionally known that a method of mixing a small amount of conductive fibers is effective in eliminating static electricity problems in textile products. Generally, as such fibers having conductivity, conductive fibers made of a polymer containing conductive carbon black particles are used. However, conventional conductive fibers are composite fibers formed from thermoplastic polymers (e.g., polyamide, polyester, fluorocarbon, etc.) and thermoplastic polymers in which these polymers are mixed with conductive carbon black particles. Therefore, its tensile strength was only 4 g/d at most.
また、高い引張り強度を有する導電性繊維としては炭素
繊維が知られており、その引張り強度は20g/d以上
にも達している。しかしながら、炭素繊維は製造工程が
複雑で、特殊な酸化、炭化工程等を要するために極めて
高価格であり、汎用導電性繊維としては用いられていな
いのが実情である。Further, carbon fiber is known as a conductive fiber having high tensile strength, and its tensile strength reaches 20 g/d or more. However, carbon fiber has a complicated manufacturing process and requires special oxidation, carbonization, etc. processes, making it extremely expensive, and the fact is that it is not used as a general-purpose conductive fiber.
PVA繊維は、前述したとおり汎用繊維の中では最も高
強度・高初期弾性率を有しているので。As mentioned above, PVA fiber has the highest strength and highest initial elastic modulus among general-purpose fibers.
PVA繊維に導電性を賦与することができれば産業資材
用繊維として極めて有用であることは明かである。It is clear that if conductivity could be imparted to PVA fibers, they would be extremely useful as fibers for industrial materials.
しかしながら、導電性粒子を含有しないPVAからなる
導電性繊維は従来全く知られておらず。However, conductive fibers made of PVA that do not contain conductive particles have not been known at all.
その可能性を示唆する文献等も見られない。There are no documents that suggest this possibility.
(発明が解決しようとする課題)
上述したように、PVA繊維の本質的な欠点である耐熱
水性を改良し、しかも高強度・高初期弾性率を付与しよ
うとする試みが種々なされているが、いずれも耐熱水性
の向上が充分ではないという欠点があり、セメント補強
用としてオートクレーブ養生に耐える程度の極めて高い
耐熱水性を有するPVA繊維は知られていなかった。(Problems to be Solved by the Invention) As mentioned above, various attempts have been made to improve the hot water resistance, which is an essential drawback of PVA fibers, and to provide them with high strength and high initial elastic modulus. All of them have the disadvantage that their hot water resistance is not sufficiently improved, and PVA fibers that have extremely high hot water resistance that can withstand autoclave curing for cement reinforcement have not been known.
また、従来の汎用導電性繊維は、引張り強度が低いとい
う問題があり、引張り強度の高い炭素繊維は極めて高価
であり、産業資材用繊維として広く用いることは困難で
あるという問題があった。Further, conventional general-purpose conductive fibers have a problem of low tensile strength, and carbon fibers with high tensile strength are extremely expensive, making it difficult to widely use them as fibers for industrial materials.
したがって1本発明の第1の課題は、高強度・高初期弾
性率を有し、しかもセメント補強用としてオートクレー
ブ養生に耐える程度の耐熱水性を有するPVA系繊維を
提供することにある。Therefore, the first object of the present invention is to provide a PVA-based fiber that has high strength and high initial modulus of elasticity, and also has hot water resistance to the extent that it can withstand autoclave curing for use in reinforcing cement.
また9本発明の第2の課題は、高強度であり。A second object of the present invention is high strength.
かつ、導電性を有するPVA系繊維を提供することにあ
る。Another object of the present invention is to provide a PVA-based fiber having conductivity.
さらに1本発明の第3の課題は、商業的に入手可能な重
合度のPVA繊維から、上記の耐熱水性PVA系繊維及
び導電性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。Furthermore, a third object of the present invention is to provide a method for producing the above hot water-resistant PVA fibers and conductive PVA fibers with high productivity from commercially available PVA fibers with a degree of polymerization. .
(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、PVA繊維を脱水反応促進用の触媒の存在下に
熱処理することにより、繊維の非晶部に存在する水酸基
に脱水反応を生じさせ、非晶部の水酸基を実質的に減少
させることが耐熱水性の改良、並びに導電性の賦与に有
効であることを知見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 by heat-treating PVA fibers in the presence of a catalyst for promoting the dehydration reaction, the fibers can be amorphous. The present invention was achieved based on the finding that causing a dehydration reaction on the hydroxyl groups present in the amorphous part to substantially reduce the hydroxyl groups in the amorphous part is effective in improving hot water resistance and imparting conductivity.
すなわち1本発明は次の構成を要旨とするものである。That is, one aspect of the present invention has the following configuration.
(1)ポリビニルアルコール系重合体からなり、引張り
強度が10g/d以上、初期弾性率が200g/d以上
で−
あり、かつ、耐熱水性が140℃以上であることを特徴
とする耐熱水性ポリビニルアルコール系繊維。(1) A hot water-resistant polyvinyl alcohol made of a polyvinyl alcohol polymer, having a tensile strength of 10 g/d or more, an initial elastic modulus of 200 g/d or more, and a hot water resistance of 140°C or more. type fiber.
(2)ポリビニルアルコール系重合体からなり、引張り
強度が7g/d以上、電気抵抗値が1.0X108Ω/
cm以下であることを特徴とする導電性ポリビニルアル
コール系繊維。(2) Made of polyvinyl alcohol polymer, has a tensile strength of 7 g/d or more and an electrical resistance of 1.0 x 108 Ω/
1. A conductive polyvinyl alcohol fiber characterized by having a thickness of less than cm.
(3)重合度1500以上、 7000以下のポリビニ
ルアルコールからなる繊維に脱水反応促進用の触媒を付
与した後、150℃以上の温度で熱処理することを特徴
とするポリビニルアルコール系繊維の製造法。(3) A method for producing polyvinyl alcohol fibers, which comprises applying a catalyst for promoting a dehydration reaction to fibers made of polyvinyl alcohol having a degree of polymerization of 1,500 or more and 7,000 or less, and then heat-treating the fibers at a temperature of 150° C. or more.
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.
高強度・高初期弾性率を有し、特に耐熱水性に優れた本
発明の耐熱水性PVA系繊維、並びに。The hot water resistant PVA fiber of the present invention which has high strength and high initial elastic modulus and is particularly excellent in hot water resistance.
引張り強度に優れた導電性PVA系繊維のプリカーサ−
となるPVA繊維は、特に限定されるものではないが1
例えば本発明者らが先に提案した特願平1−12203
0に記載の乾・湿式(ゲル)紡糸方法に準じてその最適
条件下に製造することができる。Precursor for conductive PVA fiber with excellent tensile strength
The PVA fiber used is not particularly limited, but 1
For example, patent application No. 1-12203 proposed by the present inventors
It can be produced under optimal conditions according to the dry/wet (gel) spinning method described in 0.
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0
を乾・湿式紡糸し、得られた未延伸糸を延伸してPVA
繊維を製造するに際し、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 containing DMSO as a main component is subjected to dry/wet spinning, and the resulting undrawn yarn is stretched to form PVA.
When producing fibers, the fibers can be produced by dry/wet spinning using a spinneret having a discharge hole protruding from the spinning dope exit side.
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、水酸化アル
カリと硫酸ナトリウム等を凝固浴とする従来の紡糸方法
(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 conventional spinning method (wet spinning method), for example, using a PVA aqueous solution containing boric acid or a borate as a spinning stock solution and a coagulating bath of alkali hydroxide, sodium sulfate, etc. It is possible to do so.
このように1本発明の耐熱水性PVA系繊維並びに導電
性PVA系繊維のプリカーサ−となるPVA繊維は種々
の方法によって製造することが可能であるが、用いるP
VAの重合度は1500以上である必要がある。重合度
が1500よりも小さいと。As described above, the PVA fibers that serve as precursors for the hot water-resistant PVA fibers and conductive PVA fibers of the present invention can be produced by various methods, but the PVA fibers used can be
The degree of polymerization of VA needs to be 1500 or more. When the degree of polymerization is less than 1500.
最終製品の引張り強度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重合度の上限は。This is unsuitable because the tensile strength of the final product will be lower than the desired value. Also, what is the upper limit of the degree of polymerization?
ポリマーコストの点から7000以下である。7,000 or less in terms of polymer cost.
本発明においては、上記のPVA繊維に脱水反応促進用
の触媒を付与した後、熱延伸あるいは熱処理することに
より、非晶部の水酸基を減少させることが極めて重要で
ある。In the present invention, it is extremely important to reduce the hydroxyl groups in the amorphous portion by applying a catalyst for promoting the dehydration reaction to the PVA fiber and then subjecting it to hot stretching or heat treatment.
すなわち、PVA繊維の湿熱による溶解は、繊維中の非
晶部の水酸基と水分子が結合することによって進行する
。したがって、耐熱水性を向上させるには、非晶部の分
率を減少させるか、非晶部の水酸基を減少させることが
必要である。しかしながら、いかに高重合度のポリマー
を用いて高配向させたとしても、非晶部の存在しない完
全結晶体は得られるものではなく、耐熱水性の改良にも
おのずと限界がある。That is, the dissolution of PVA fibers by moist heat progresses as water molecules bond with hydroxyl groups in the amorphous portions of the fibers. Therefore, in order to improve the hot water resistance, it is necessary to reduce the fraction of the amorphous part or to reduce the hydroxyl groups in the amorphous part. However, no matter how highly oriented the polymer is using a polymer with a high degree of polymerization, it is not possible to obtain a perfectly crystalline body free of amorphous parts, and there is a limit to the improvement of hot water resistance.
これに対して、非晶部の水酸基を減少させる方法は、高
重合度のポリマーを用いる必要もなく有利であり、さら
に、耐熱水性に劣る非晶部を選択的に改質するものなの
で効果的である。On the other hand, the method of reducing the hydroxyl groups in the amorphous part is advantageous because it does not require the use of polymers with a high degree of polymerization, and is also effective because it selectively modifies the amorphous part, which has poor hot water resistance. It is.
触媒の存在下でPVA繊維を熱処理すると、下式に示す
ようなPVAの水酸基による分子内脱水反応1分子間脱
水反応、あるいはその両方の脱水反応が生じる。分子内
の水酸基が脱水反応して生成したPVA変性物は共役二
重結合からなるポリビニレン構造を有するものであり1
分子間の水酸基が脱水反応して生成したものは分子間架
橋構造を有するものとなる。When PVA fibers are heat-treated in the presence of a catalyst, an intramolecular dehydration reaction, an intermolecular dehydration reaction, or both dehydration reactions occur due to the hydroxyl groups of PVA as shown in the following formula. The PVA modified product produced by the dehydration reaction of the hydroxyl group in the molecule has a polyvinylene structure consisting of conjugated double bonds.
The product produced by the dehydration reaction of intermolecular hydroxyl groups has an intermolecular crosslinked structure.
1
H
また、一般に、共役二重結合を有する分子構造を持つ高
分子は、そのパイ電子が分子鎮中を自由に動きまわれる
ために導電性を示すことが知られている。上記のように
して熱処理して得られるPVA系繊維は1分子内の水酸
基が脱水して生成した共役二重結合を有するため、良好
な導電性を示すようになる
本発明で使用する脱水反応促進用の触媒としては9例え
ば、リン酸や塩酸等の無機酸、フタル酸クロライドやア
ジピン酸クロライド等の有機酸ハロゲン化物、p−トル
エンスルホン酸やテレフタル酸等の有機酸など種々の触
媒を用いることができ3
るが、特に塩酸やp−)ルエンスルホン酸が好適に用い
られる。1 H Furthermore, it is generally known that polymers having a molecular structure having a conjugated double bond exhibit conductivity because their pi electrons can move freely within the molecule. The PVA fiber obtained by heat treatment as described above has a conjugated double bond generated by dehydration of the hydroxyl group in one molecule, so it exhibits good electrical conductivity and is used to promote the dehydration reaction used in the present invention. Various catalysts can be used, such as inorganic acids such as phosphoric acid and hydrochloric acid, organic acid halides such as phthalic acid chloride and adipic acid chloride, and organic acids such as p-toluenesulfonic acid and terephthalic acid. However, hydrochloric acid and p-)luenesulfonic acid are particularly preferably used.
これらの酸の溶剤としては、水、アルコール。Solvents for these acids include water and alcohol.
ケトン類を用いることができるが、塩酸の場合にlt水
、p−トルエンスルホン酸の場合にはメタノールが好適
に用いられる。Although ketones can be used, lt water is preferably used in the case of hydrochloric acid, and methanol is preferably used in the case of p-toluenesulfonic acid.
本発明は、上記のような水酸基による脱水反応を応用し
たものであるから、脱水反応を促進しないホウ酸、ホウ
砂、あるいは有機過酸化物等は触媒として使用できない
。Since the present invention applies the dehydration reaction using hydroxyl groups as described above, boric acid, borax, organic peroxides, etc. that do not promote the dehydration reaction cannot be used as catalysts.
本発明で使用する触媒の酸濃度は、後工程における熱処
理条件と連動して設定されるが、耐熱水性PVA系繊維
を目的とする場合には0.01〜5規定が好ましく、よ
り好ましくは0.1〜3規定である。酸濃度が0.01
規定よりも薄いと、脱水反応又は架橋反応を十分に進行
させるために長時間の熱処理が必要となり好ましくない
。一方、5規定より高い場合には、引張り強度が低下す
る傾向にあり好ましくない。The acid concentration of the catalyst used in the present invention is set in conjunction with the heat treatment conditions in the subsequent process, but when the purpose is to produce hot water-resistant PVA fibers, it is preferably 0.01 to 5N, more preferably 0. .1 to 3 regulations. Acid concentration is 0.01
If it is thinner than the specified value, a long heat treatment will be required to sufficiently advance the dehydration reaction or crosslinking reaction, which is not preferable. On the other hand, if it is higher than 5 normal, the tensile strength tends to decrease, which is not preferable.
また、PVA系導電性繊維を目的とする場合に14
は3〜10規定が好ましく、より好ましくは5〜7規定
である。酸濃度が3規定よりも薄いと、脱水反応が十分
に進行せず、目的とする導電性が得難<、10規定より
高い場合には引張り強度の低下が著しく 7g/d以上
の引張り強度が得難い。Moreover, when the purpose is a PVA-based conductive fiber, 14 is preferably 3 to 10 normal, more preferably 5 to 7 normal. If the acid concentration is lower than 3N, the dehydration reaction will not proceed sufficiently, making it difficult to achieve the desired conductivity. If the acid concentration is higher than 10N, the tensile strength will drop significantly. Hard to get.
本発明においては、熱処理に先立ちPVA繊維に上記の
触媒を付与するのであるが、触媒を繊維に付与する方法
は特に限定されないものの、触媒の溶液中に浸漬させる
方法、いわゆるオイリングローラで付与する方法、触媒
溶液を噴霧する方法等を用いることができる。中でも繊
維を上記触媒の溶液中を走行させる方法は、触媒濃度、
繊維の形状及び走行速度等に応じて触媒溶液中での走行
時間を加減することにより触媒の付与量を調整できるの
で都合がよい。In the present invention, the above-mentioned catalyst is applied to the PVA fibers prior to heat treatment, but the method of applying the catalyst to the fibers is not particularly limited, but there is a method of immersing the fibers in a catalyst solution, a method of applying the catalyst with a so-called oiling roller. , a method of spraying a catalyst solution, etc. can be used. Among these methods, the method of running fibers through a solution of the catalyst mentioned above is based on the concentration of the catalyst,
It is convenient because the amount of catalyst applied can be adjusted by adjusting the running time in the catalyst solution depending on the shape of the fibers, running speed, etc.
また、触媒を付与する時期としては、繊維がある程度の
耐熱水性を有するようになった後が好ましく、具体的に
は熱延伸後に付与するのがよい。Further, the timing of applying the catalyst is preferably after the fibers have a certain degree of hot water resistance, and specifically, it is preferable to apply the catalyst after hot stretching.
本発明の第1の発明である高強度・高初期弾性率を有し
、しかも耐熱水性の優れたPVA系繊維。The first invention of the present invention is a PVA-based fiber that has high strength and high initial elastic modulus and has excellent hot water resistance.
並びに、第2の発明である導電性PVA系繊維を得るた
めには、上記で触媒が付与されたPVA繊維を熱処理す
ることが必要である。Furthermore, in order to obtain the conductive PVA fiber according to the second invention, it is necessary to heat-treat the PVA fiber to which the catalyst has been applied as described above.
熱処理の方法としては、触媒が付与された糸条(好まし
くは延伸糸条)を連続して熱風加熱炉等の熱処理機中を
走行させる方法や、−旦捲き取った後、熱処理機中でバ
ッチで処理する方法等が挙げられる。Heat treatment methods include a method in which a yarn (preferably a drawn yarn) to which a catalyst has been applied is continuously run through a heat treatment machine such as a hot air heating furnace, or a method in which the yarn is wound once and then batchwise run in a heat treatment machine. Examples include a method of processing.
熱処理は150℃以上、繊維の融点以下の温度範囲、好
ましくは180〜260℃の温度範囲で糸条に張力をか
けた状態で、1〜60秒間、好ましくは3〜20秒間行
なう。熱処理温度が150℃よりも低く。The heat treatment is carried out at a temperature range of 150°C or higher and lower than the melting point of the fiber, preferably 180°C to 260°C, with tension applied to the yarn for 1 to 60 seconds, preferably 3 to 20 seconds. The heat treatment temperature is lower than 150°C.
かつ処理時間が1秒間より短いと脱水反応あるいは架橋
反応が不充分となり、目的とする高耐熱水性、並びに導
電性が得られない。また、熱処理温度が260℃よりも
高く、かつ熱処理時間が60秒間よりも長い場合、及び
糸条に張力をかけずに熱処理する場合には糸条の強度低
下が著しくなるので好ましくない。熱処理時の糸条の張
力は特に限定されるものではないが、連続式で熱処理す
る場合。If the treatment time is shorter than 1 second, the dehydration reaction or crosslinking reaction will be insufficient, and the desired high hot water resistance and electrical conductivity will not be obtained. Furthermore, it is not preferable if the heat treatment temperature is higher than 260° C. and the heat treatment time is longer than 60 seconds, or if the heat treatment is performed without applying tension to the yarn, the strength of the yarn will significantly decrease. The tension of the yarn during heat treatment is not particularly limited, but in the case of continuous heat treatment.
熱処理機前後のローラ速度比をストレッチ率が0〜10
%となるように設定するのが好ましい。The roller speed ratio before and after the heat treatment machine has a stretch rate of 0 to 10.
It is preferable to set it to %.
本発明によれば、商業的に入手可能な重合度が1500
以上、 7000以下のPVAを用いて、高強度・高初
期弾性率及び高耐熱水性を有するPVA系繊維、並びに
導電性PVA系繊維を容易に生産性よく製造することが
可能である。According to the present invention, the commercially available degree of polymerization is 1500.
As described above, it is possible to easily produce PVA-based fibers having high strength, high initial elastic modulus, and high hot water resistance, and conductive PVA-based fibers with good productivity using PVA having a molecular weight of 7000 or less.
また、このようにして得られる本発明の耐熱水性PVA
系繊維は、 10g/d以上の引張り強度と200g/
d以上の初期弾性率を有し、かつ、耐熱水性が140℃
以上という従来全く知られていない特性を有しており、
PVA繊維の代表的な用途である漁網やローブは勿論の
こと、オートクレーブ養生によって生産されるセメント
、コンクリート製建築材料の補強用としても適用可能で
ある。Moreover, the hot water resistant PVA of the present invention obtained in this way
The fibers have a tensile strength of 10 g/d or more and a tensile strength of 200 g/d.
Has an initial elastic modulus of d or more, and has hot water resistance of 140℃
It has the above-mentioned characteristics that were completely unknown until now.
It can be used not only for fishing nets and robes, which are typical uses of PVA fibers, but also for reinforcing cement and concrete building materials produced by autoclave curing.
また9本発明の導電性PVA系繊維は、引張り強度が7
g/d以上、好ましくは8g/d以上、電気抵抗値が1
.0×108Ω/cm以下とい′う従来全く知られてい
ない特性を有しており、紙積やカーペット等の床カバー
や自動車のシート等の静電気障害の解消=17
用繊維として好適である。Furthermore, the conductive PVA fiber of the present invention has a tensile strength of 7.
g/d or more, preferably 8 g/d or more, electrical resistance value 1
.. It has a previously unknown property of 0x10 8 Ω/cm or less, and is suitable as a fiber for eliminating static electricity problems in floor coverings such as paper stacks, carpets, and automobile seats.
(作 用)
本発明において、140℃以上という高い耐熱水性を有
するPVA系繊維、並びに導電性PVA系繊維が得られ
るのは、塩酸やp−)ルエンスルホン酸のような触媒の
存在下でPVAを熱処理すると。(Function) In the present invention, PVA fibers having high hot water resistance of 140° C. or higher and conductive PVA fibers can be obtained by using PVA fibers in the presence of a catalyst such as hydrochloric acid or p-)luenesulfonic acid. When heat treated.
PVAの水酸基が分子内あるいは分子間で脱水反応を生
じ、共役二重結合からなるポリビニレン構造あるいは分
子間架橋構造を有するものとなるためと認められる。This is believed to be because the hydroxyl groups of PVA undergo a dehydration reaction within or between molecules, resulting in a polyvinylene structure consisting of conjugated double bonds or an intermolecular crosslinked structure.
また1本発明においては、触媒を外部から付与するので
、ポリビニレン構造や分子間架橋構造が繊維の外部から
内部に向かって成長し、このため耐熱水性や導電性の特
に要求される繊維表面が強い耐熱水性や導電性を有する
ようになり好適である。In addition, in the present invention, since the catalyst is applied from the outside, the polyvinylene structure and intermolecular crosslinked structure grow from the outside to the inside of the fiber, which makes the fiber surface strong, which particularly requires hot water resistance and electrical conductivity. It is suitable because it has hot water resistance and conductivity.
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30cm/分で測定するものであり、また、耐熱水
性の測定は以下の方法により行なうものである。9 The tensile strength and initial elastic modulus in the present invention are based on JIS
-L-1013, the measurement is carried out at a gripping interval of 25 cm and a pulling speed of 30 cm/min, and the hot water resistance is measured by the following method.
8
装置:パーキンエルマー社製DSC−2C型示差走査熱
量計
昇温速度:10℃/分
試料セル:高耐圧(50気圧)セル
試料調製法:長さ約5mmに切断した繊維ザンプル5m
gを水10mgと共に試料セル中に封入する。8 Equipment: PerkinElmer DSC-2C differential scanning calorimeter Temperature increase rate: 10°C/min Sample cell: High pressure (50 atm) cell Sample preparation method: 5 m fiber sample cut to approximately 5 mm length
g is sealed in a sample cell with 10 mg of water.
耐熱水性:上記の方法で得られる融解曲線のピーク温度
をもって耐熱水性と定義する。Hot water resistance: The peak temperature of the melting curve obtained by the above method is defined as hot water resistance.
また、電気抵抗値は、長さ1000mの試料からランダ
ムに10cm長の糸条を30回サンプリングし、各々に
ついてlkvの直流電圧を印加したときに測定される抵
抗値のうち、最も高い値を示したものである。In addition, the electrical resistance value indicates the highest value among the resistance values measured when 10 cm long threads are randomly sampled 30 times from a 1000 m long sample and a DC voltage of lkv is applied to each sample. It is something that
(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5100のPVA (ケン化度99.9モル%)
の12重量%DMSO溶液を調製し、この紡糸原液を。Example 1 PVA with a degree of polymerization of 5100 (degree of saponification 99.9 mol%)
Prepare a 12% by weight DMSO solution and use this spinning stock solution.
内径0.7mmのステンレス製円筒状細管210本を紡
糸原液出口側に3mm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4m/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。Using a spinneret in which 210 stainless steel cylindrical tubes with an inner diameter of 0.7 mm were embedded so as to protrude 3 mm from the spinning dope exit side, the linear discharge speed was 4 m/min, and the spinning draft was 4.0.
Dry/wet spinning was performed in a methanol coagulation bath through an air gap of 10 mm, DMSO was extracted with methanol, and then dried to obtain an undrawn yarn.
次いで、この未延伸糸を1人ロ温度180℃、出口温度
255℃に設定された熱風浴で延伸し、この延伸糸を連
続して1規定塩酸中を約5秒量定行させ、触媒となる塩
酸を付与した。さらにこの糸条を、内部温度が210℃
に設定された熱処理機中を定長(ストレッチ率0%)で
5秒間走行させることにより熱処理し、 1490d/
21Ofの繊維を得た。Next, this undrawn yarn was drawn by one person in a hot air bath set at a temperature of 180°C and an outlet temperature of 255°C, and the drawn yarn was continuously passed through 1N hydrochloric acid for about 5 seconds to remove the catalyst. Hydrochloric acid was added. Furthermore, this yarn has an internal temperature of 210℃.
Heat treated by running for 5 seconds at a constant length (stretch rate 0%) in a heat treatment machine set to 1490d/
21Of fibers were obtained.
製造条件及び得られた耐熱水性繊維の物性を第1表に示
すが、この繊維の耐熱水性は153℃であり、極めて優
れた耐熱水性を有していた。The manufacturing conditions and the physical properties of the obtained hot water resistant fiber are shown in Table 1, and the hot water resistance of this fiber was 153° C., indicating extremely excellent hot water resistance.
実施例2,3.比較例1
第1表に示すように1重合度1700.7000及び1
300のPVAのDMSO溶液を調製し、この紡糸原液
を用いて、実施例1と同様の乾・湿式紡糸及び延伸を行
い、延伸糸を得た。なお、実施例2.3゜比較例1では
、それぞれステンレス製円筒状細管の内径を0.6mm
、 0.8mm、0.5mmとした紡糸口金を用いた。Examples 2 and 3. Comparative Example 1 As shown in Table 1, 1 polymerization degree 1700.7000 and 1
A DMSO solution of 300% PVA was prepared, and using this spinning stock solution, dry/wet spinning and drawing were performed in the same manner as in Example 1 to obtain a drawn yarn. In addition, in Example 2.3 and Comparative Example 1, the inner diameter of the stainless steel cylindrical tube was 0.6 mm.
, 0.8 mm, and 0.5 mm were used.
得られた延伸糸に、実施例1と同様の塩酸付与。Hydrochloric acid was applied to the obtained drawn yarn in the same manner as in Example 1.
熱処理を行なった。得られた耐熱水性繊維の性能を第1
表に示す。Heat treatment was performed. The performance of the obtained heat-resistant water-resistant fibers was evaluated first.
Shown in the table.
比較例2
塩酸を付与しない以外は実施例1と同様にして1510
d/21Ofの繊維を製造した。Comparative Example 2 1510 was prepared in the same manner as in Example 1 except that hydrochloric acid was not added.
A fiber of d/21Of was produced.
得られた繊維の耐熱水性は115℃と低いものであった
。The obtained fiber had a low hot water resistance of 115°C.
実施例4
重合度5100のPVAを用い、これに対して2,1重
量%のホウ酸を添加し、pHを4.2に調製した水溶液
を紡糸原液とし、孔数500の紡糸口金から紡糸ドラフ
ト0.25で硫酸ナトリウム350g/ 1 、苛性ソ
ーダ40g/lを含有する凝固浴中に湿式紡糸を行なっ
た後、硫酸ナトリウム250g/β、硫酸308/lの
中和塔で中和しながら4.5倍の第1段延伸(紡糸延伸
)を行い、さらに水洗した後、乾燥した。Example 4 Using PVA with a degree of polymerization of 5100, an aqueous solution prepared by adding 2.1% by weight of boric acid to adjust the pH to 4.2 was used as a spinning stock solution, and a spinning draft was passed through a spinneret with 500 holes. After performing wet spinning in a coagulation bath containing 350 g/1 of sodium sulfate and 40 g/l of caustic soda at a concentration of 4.5 The first stage stretching (spinning stretching) was carried out, and the film was further washed with water and then dried.
1 得られた乾燥繊維を、乾熱245℃で4倍延伸し。1 The obtained dry fibers were drawn 4 times with dry heat at 245°C.
引続き1規定塩酸中を約5秒量定行させて塩酸を付与し
た後、実施例1と同様に熱処理し、 1510d150
0fの繊維を得た。Subsequently, after applying hydrochloric acid by passing it through 1N hydrochloric acid for about 5 seconds, heat treatment was performed in the same manner as in Example 1.
A fiber of 0f was obtained.
得られた耐熱水性繊維の物性を第1表に示す。Table 1 shows the physical properties of the obtained hot water-resistant fiber.
実施例5 実施例1で得られた未延伸糸を、入口温度180t。Example 5 The undrawn yarn obtained in Example 1 was heated to an inlet temperature of 180 t.
出口温度255℃に設定された熱風浴で延伸し、この延
伸糸を連続して0.5規定p−)ルエンスルホン酸(P
−TSA)のメタノール溶液中を約5秒量定行させた後
、この糸条を内部温度が210℃に設定された熱処理機
中で約5秒量定行させて熱処理した。The drawn yarn was drawn in a hot air bath set at an outlet temperature of 255°C, and the drawn yarn was continuously treated with 0.5 N p-)luenesulfonic acid (P).
-TSA) in a methanol solution for about 5 seconds, and then the yarn was heat-treated by running it for about 5 seconds in a heat treatment machine whose internal temperature was set to 210°C.
得られた耐熱水性繊維の物性を第1表に示す。Table 1 shows the physical properties of the obtained hot water-resistant fiber.
=22
28一
実施例6
実施例1で得た未延伸糸を、入口温度180℃、出口温
度255℃に設定された熱風浴で延伸し、この延伸糸を
連続して5規定P−TSAメタノール溶液中を約10秒
量定行させ、脱水反応触媒となるP−TSAを付与した
。=22 28 - Example 6 The undrawn yarn obtained in Example 1 was drawn in a hot air bath set at an inlet temperature of 180°C and an outlet temperature of 255°C, and the drawn yarn was continuously treated with 5N P-TSA methanol. The solution was allowed to flow through the solution for about 10 seconds, and P-TSA, which acts as a dehydration reaction catalyst, was applied.
さらにこの糸条を、内部温度が250℃に設定された熱
処理機中をストレッチ率1%で5秒量定行させて熱処理
し、 1530d/21Ofの導電性繊維を得た。Further, this yarn was heat-treated by running it for 5 seconds at a stretch rate of 1% in a heat treatment machine whose internal temperature was set to 250°C to obtain a conductive fiber of 1530d/21Of.
得られた繊維の物性を第2表に示すが、この糸条の電気
抵抗値は8. OX 10’Ω/cmであり、極めて優
れた導電性を有していた。The physical properties of the obtained fiber are shown in Table 2, and the electrical resistance value of this yarn is 8. OX 10'Ω/cm, and had extremely excellent conductivity.
実施例7,8.比較例3 実施例2,3.比較例1で得られた延伸糸に。Examples 7 and 8. Comparative example 3 Examples 2 and 3. To the drawn yarn obtained in Comparative Example 1.
実施例6と同様のP−TSA付与及び熱処理を行なった
。The same P-TSA application and heat treatment as in Example 6 were performed.
得られた導電性繊維の性能を第2表に示す。The performance of the obtained conductive fibers is shown in Table 2.
比較例4
P−TSA酸溶液の濃度を11規定にした以外は実施例
6と同様な操作を施したところ、得られた繊維24−
は電気抵抗値は3.0X107Ω/cmと導電性を有す
るものであったが、引張り強度は6.1g/dにすぎな
かった。Comparative Example 4 The same operation as in Example 6 was performed except that the concentration of the P-TSA acid solution was 11N, and the obtained fiber 24- had electrical conductivity with an electrical resistance value of 3.0 x 107 Ω/cm. However, the tensile strength was only 6.1 g/d.
比較例5
熱処理温度を140℃とした以外は実施例6と同様な操
作を施したところ、得られた繊維の電気抵抗値は5.Q
xlQIOΩ/cmであり、導電性が劣るものであった
。Comparative Example 5 The same operation as in Example 6 was performed except that the heat treatment temperature was 140°C, and the electrical resistance value of the obtained fiber was 5. Q
xlQIOΩ/cm, and the conductivity was poor.
実施例9
実施例4で得られた乾燥繊維を、乾熱245℃で4倍延
伸し、引続き5規定P−TSAメタノール溶液中を約1
秒量定行させ、触媒となるP−TSAを付与した。さら
にこの糸条を実施例6と同様に熱処理し、 1510d
1500fの導電性繊維を得た。Example 9 The dry fiber obtained in Example 4 was stretched 4 times with dry heat at 245°C, and then stretched about 1 times in a 5N P-TSA methanol solution.
P-TSA, which acts as a catalyst, was applied at a constant rate of 2 seconds. Further, this yarn was heat-treated in the same manner as in Example 6 to obtain 1510d
A conductive fiber of 1500 f was obtained.
得られた繊維の物性を第2表に示す。The physical properties of the obtained fibers are shown in Table 2.
実施例10 実施例6で得られた未延伸糸を、入口温度180t。Example 10 The undrawn yarn obtained in Example 6 was heated at an inlet temperature of 180 t.
出口温度255℃に設定された熱風浴で延伸し、この延
伸糸を連続して5規定塩酸中を約1秒量定行させた後、
内部温度250℃に設定された熱処理機5−
中を約3秒量定行させて熱処理した。After drawing in a hot air bath set at an outlet temperature of 255°C, the drawn thread was continuously run through 5N hydrochloric acid for about 1 second, and then
The heat treatment was carried out by running the sample through the heat treatment machine 5 whose internal temperature was set to 250° C. for about 3 seconds.
得られた導電性繊維の物性を第2表に示す。Table 2 shows the physical properties of the conductive fibers obtained.
26−
(発明の効果)
本発明の耐熱水性PVA系繊維は、引張り強度や初期弾
性率が優れているばかりでなく、140℃以上という従
来にない極めて高い耐熱水性を有しているので、PVA
繊維の代表的な用途である漁網やロープは勿論のこと、
従来は適用が困難であったオートクレーブ養生によって
大量生産されるスレート板やケイ酸カルシウム板等の建
築材料の補強用繊維としても使用することが可能となり
、使用範囲が著しく拡大される。さらには本発明の耐熱
水性PVA系繊維は、タイヤ、タイミングベルト、■ベ
ルト等のゴム補強材料、あるいはプラスチックの補強材
料にも使用可能であり、その有用性は極めて大きいもの
である。26- (Effect of the invention) The hot water resistant PVA fiber of the present invention not only has excellent tensile strength and initial elastic modulus, but also has extremely high hot water resistance of 140°C or higher, which is unprecedented.
Not only fishing nets and ropes, which are typical uses of fibers, but also
It is now possible to use fibers for reinforcing building materials such as slate boards and calcium silicate boards, which are mass-produced by autoclave curing, which was difficult to apply in the past, and the range of use is significantly expanded. Furthermore, the hot water-resistant PVA fiber of the present invention can be used as a rubber reinforcing material for tires, timing belts, belts, etc., or as a reinforcing material for plastics, and its usefulness is extremely large.
また1本発明の導電性PVA系繊維は、導電性が優れて
いるばかりでなく、7g/d以上という従来の汎用導電
性繊維にはない極めて高い引張り強度を有しているので
、紙積やカーペット等の床カバベツドカバー、カーテン
、外衣製品、特にクリーンルーム内の作業服あるいは自
動車のシート8
や椅子等の外張り布帛等に混入することにより静電気障
害を解消することができる。In addition, the conductive PVA fiber of the present invention not only has excellent conductivity, but also has an extremely high tensile strength of 7 g/d or more, which is not found in conventional general-purpose conductive fibers. Static electricity problems can be eliminated by mixing it with floor covers such as carpets, curtains, outer clothing, especially work clothes in clean rooms, or outer fabrics such as car seats 8 and chairs.
さらに1本発明の製造法によれば、商業的に入手可能な
重合度を有するPVAから、引張強度。Furthermore, according to the manufacturing method of the present invention, tensile strength can be obtained from PVA having a commercially available degree of polymerization.
初期弾性率及び耐熱水性に優れたPVA系繊維並びに導
電性PVA系繊維を容易に生産性よく製造することが可
能である。It is possible to easily produce PVA-based fibers and conductive PVA-based fibers with excellent initial elastic modulus and hot water resistance with good productivity.
Claims (3)
強度が10g/d以上、初期弾性率が200g/d以上
であり、かつ、耐熱水性が140℃以上であることを特
徴とする耐熱水性ポリビニルアルコール系繊維。(1) A hot water-resistant polyvinyl alcohol system consisting of a polyvinyl alcohol polymer, having a tensile strength of 10 g/d or more, an initial elastic modulus of 200 g/d or more, and a hot water resistance of 140°C or more. fiber.
強度が7g/d以上、電気抵抗値が1.0×10^8Ω
/cm以下であることを特徴とする導電性ポリビニルア
ルコール系繊維。(2) Made of polyvinyl alcohol polymer, has a tensile strength of 7 g/d or more and an electrical resistance of 1.0 x 10^8 Ω.
/cm or less.
アルコールからなる繊維に脱水反応促進用の触媒を付与
した後、150℃以上の温度で熱処理することを特徴と
するポリビニルアルコール系繊維の製造法。(3) A method for producing polyvinyl alcohol fibers, which comprises applying a catalyst for promoting a dehydration reaction to fibers made of polyvinyl alcohol having a degree of polymerization of 1,500 or more and 7,000 or less, and then heat-treating the fibers at a temperature of 150° C. or more.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP319590A JPH03213510A (en) | 1990-01-09 | 1990-01-09 | Polyvinyl alcohol-based fiber and its production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP319590A JPH03213510A (en) | 1990-01-09 | 1990-01-09 | Polyvinyl alcohol-based fiber and its production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH03213510A true JPH03213510A (en) | 1991-09-18 |
Family
ID=11550632
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP319590A Pending JPH03213510A (en) | 1990-01-09 | 1990-01-09 | Polyvinyl alcohol-based fiber and its production |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH03213510A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5380588A (en) * | 1991-06-24 | 1995-01-10 | Kuraray Company Limited | Polyvinyl alcohol-based synthetic fiber |
-
1990
- 1990-01-09 JP JP319590A patent/JPH03213510A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5380588A (en) * | 1991-06-24 | 1995-01-10 | Kuraray Company Limited | Polyvinyl alcohol-based synthetic fiber |
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