JPS62149909A - Polyvinyl alcohol fiber - Google Patents

Polyvinyl alcohol fiber

Info

Publication number
JPS62149909A
JPS62149909A JP28495685A JP28495685A JPS62149909A JP S62149909 A JPS62149909 A JP S62149909A JP 28495685 A JP28495685 A JP 28495685A JP 28495685 A JP28495685 A JP 28495685A JP S62149909 A JPS62149909 A JP S62149909A
Authority
JP
Japan
Prior art keywords
fibers
spinning
pva
boric acid
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
Application number
JP28495685A
Other languages
Japanese (ja)
Inventor
Masaharu Watanabe
正晴 渡辺
Kazutaka Koda
甲田 和孝
Takashi Ikeda
隆 池田
Naohiko Nagata
永田 直彦
Mitsuhiro Unno
光宏 海野
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.)
Unitika Ltd
Original Assignee
Unitika 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 Unitika Ltd filed Critical Unitika Ltd
Priority to JP28495685A priority Critical patent/JPS62149909A/en
Publication of JPS62149909A publication Critical patent/JPS62149909A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:The titled fibers obtained by adding a specific amount, based on polyvinyl alcohol having a specific polymerization degree, of boric acid (salt) thereto and spinning and drawing the resultant solution and having a high strength and initial elastic modulus even at high temperatures and good heat resistance. CONSTITUTION:Polyvinyl alcohol fibers, obtained by adding a solution prepared by dissolving 200-8,000ppm, based on polyvinyl alcohol having >=3,000 polymerization degree, boric acid or borate in hot water to the polyvinyl alcohol to prepare a spinning solution, extruding the spinning solution through a spinneret, passing the extruded solution through an air layer, spinning the fibers into an aqueous solution containing sodium hydroxide and sodium sulfate at 50 deg.C to give undrawn fibers, drawing the undrawn fibers at 2 times draw ratio using rolls, neutralizing and washing the drawn fibers, wet hot-drawing at 2 times draw ratio, drying and winding the fibers and having at least 18g/denier strength and at least 35g/denier initial elastic modulus.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、高強度・高初期弾性率を有するポリビニルア
ルコール(以下、 PVAと略記する。)繊維に関し、
更には高温下においても高い強度・初期弾性率を有する
PVA繊維に関する。
Detailed Description of the Invention (Industrial Application Field) The present invention relates to polyvinyl alcohol (hereinafter abbreviated as PVA) fibers having high strength and high initial elastic modulus.
Furthermore, the present invention relates to PVA fibers that have high strength and initial elastic modulus even at high temperatures.

(従来の技術) 最近、ポリパラフェニレンテレフタルアミド(以下、 
PPTAと略記する。)に代表される如く。
(Prior art) Recently, polyparaphenylene terephthalamide (hereinafter referred to as
It is abbreviated as PPTA. ) as exemplified by.

剛直な分子鎖を有する重合体を用いて、硫酸等の特定溶
媒に溶液が液晶性を示すような濃度となるようにその重
合体を溶解した後、紡糸する。いわゆる液晶紡糸を行な
うことにより、 20g/d以」−の強度と500g/
d以上の初期弾性率を有する高強度・高弾性率繊維を得
ることが可能となり、既にPPT^繊維は実用段階に入
っている。しかしながら。
Using a polymer having a rigid molecular chain, the polymer is dissolved in a specific solvent such as sulfuric acid to a concentration such that the solution exhibits liquid crystallinity, and then spun. By performing so-called liquid crystal spinning, it has a strength of 20g/d or more and a strength of 500g/d.
It has become possible to obtain high-strength, high-modulus fibers with an initial elastic modulus of d or more, and PPT^ fibers have already entered the practical stage. however.

かかる繊維は原料コスト製造コストの面で一般糸に比べ
て非常にコスト高となり不利である。
Such fibers are disadvantageous in terms of raw material costs and manufacturing costs, as they are extremely expensive compared to ordinary yarns.

一方、屈曲性の高分子量ポリマーから高強度・高弾性率
繊維を得る方法も開発され、注目を浴びている。いわゆ
るゲル紡糸法である。ゲル紡糸法によるポリエチレン繊
維においてはPPTA繊維の約2倍あるいはそれ以上の
強度を有し、初期弾性率においても極限にかなり近い性
能を有する繊維が得られているものの、その融点の低さ
から、耐熱性に欠ける欠点を有している。
On the other hand, a method for obtaining high-strength, high-modulus fibers from flexible high-molecular-weight polymers has also been developed and is attracting attention. This is the so-called gel spinning method. Polyethylene fibers produced using the gel spinning method have a strength that is approximately twice or more than that of PPTA fibers, and fibers with initial elastic modulus that are close to the ultimate limit have been obtained; however, due to their low melting point, It has the disadvantage of lacking heat resistance.

PVA繊維は汎用繊維中9強度、初期弾性率の点・で優
れており、耐熱性においてもポリエチレン繊維に比べて
優れている。したがってPPTA繊維と同程度の強度と
初期弾性率を有するPVA繊維が得られるならば、コス
ト・パフォーマンスの点で大変有利であり、用途の拡大
が可能である。
PVA fibers are superior to general purpose fibers in terms of strength and initial elastic modulus, and are also superior to polyethylene fibers in heat resistance. Therefore, if PVA fibers having strength and initial elastic modulus comparable to those of PPTA fibers could be obtained, it would be very advantageous in terms of cost performance and the range of uses could be expanded.

従来、  pvΔ繊維の強度と初期弾性率を改善する方
法は種々検討されており2例えば特公昭48−3262
3号公報、特公昭4B−32624号公報、特公昭48
−9210号公報、特公昭53−1368号公報等に各
種の提案、がなされている。しかしこれらのPVA繊維
の製造法では強度と初期弾性率を共に改善することはで
きていない。
Conventionally, various methods for improving the strength and initial elastic modulus of pvΔ fibers have been studied2.For example, Japanese Patent Publication No. 48-3262
Publication No. 3, Special Publication No. 4B-32624, Special Publication No. 1973
Various proposals have been made in JP-A-9210, Japanese Patent Publication No. 53-1368, etc. However, these PVA fiber manufacturing methods have not been able to improve both strength and initial elastic modulus.

例えば、特公昭48−32623号公報には重合度35
00のPVAを用いて強度17.2g/d、 20℃の
動的弾性率3.8 X 10” dyne/c+Jの繊
維を得たことが記載されている。しかるに、上記弾性率
は10 CPS (サイクル7秒)の高速変形時の弾性
率であって1本発明者等は上記発明について追試を行い
1本発明で記載するマルチフィラメント糸の引張試験に
よる初期弾性率を測定した結果250g/dにすぎなか
った。
For example, in Japanese Patent Publication No. 48-32623, the degree of polymerization is 35.
It is described that a fiber with a strength of 17.2 g/d and a dynamic elastic modulus of 3.8 x 10" dyne/c+J at 20°C was obtained using PVA of 0.0000000000000000000000000000000000000000000000000000000000000000000000000000000000000000001ss," The elastic modulus during high-speed deformation (cycle 7 seconds) was 250 g/d. 1. The present inventors carried out a follow-up test on the above invention, and 1. The initial elastic modulus was measured by a tensile test of the multifilament yarn described in the present invention. It wasn't too much.

また、  PVA繊維中にホウ酸またはホウ酸塩を含ま
せることを提案した例としては前記の特公昭53−13
68号公報、さらに特公昭48〜7887号公報があげ
られる。しかるに、これらに記載されている繊維は、高
温下での性能や吸水性が改良されてはいるが、使用れて
いるポリマーの重合度が低く、そのため強度は高々14
g/dにずぎす、また初期弾性率は300g/dにすぎ
ず、 PPTA繊維に匹敵ずろPVA繊維は得られてい
ない。更に特公昭53−1368号公報において、高温
下(120)での強度・初期弾性が改善れたPVA繊維
が1に案されているが。
Furthermore, an example of a proposal for incorporating boric acid or borate into PVA fibers is the above-mentioned Japanese Patent Publication No. 53-13.
No. 68, as well as Japanese Patent Publication Nos. 48-7887. However, although the fibers described in these documents have improved performance and water absorption at high temperatures, the degree of polymerization of the polymer used is low, and therefore the strength is only 14% at most.
g/d, and the initial elastic modulus is only 300 g/d, and no PVA fibers have been obtained that are comparable to PPTA fibers. Furthermore, in Japanese Patent Publication No. 53-1368, a PVA fiber with improved strength and initial elasticity at high temperatures (120) is proposed as 1.

120℃における強度と初期弾性率はそれぞれ高々10
g/c! 、140g/d程度である。
The strength and initial elastic modulus at 120°C are each at most 10
g/c! , about 140 g/d.

一方、 PVA繊維の強度と初期弾性率を共に改善する
方法が特開昭59−130314号公報および特開昭6
0−12631.2号公報に提案されている。これら公
報には紡糸用原液の溶媒として水を用いるが、またハ塩
化カルシウム、塩化亜鉛、塩化アルミニウムあるいはロ
ダンソーダ等の無機塩を含む水溶液を用いることが具体
例として示されてはいるが、最終的に得られるPVA繊
維の延伸糸中に特定の無機塩を含むこと及び無機塩を含
むことにより延伸性が向上するという記載は一切ない。
On the other hand, methods for improving both the strength and initial elastic modulus of PVA fibers are disclosed in JP-A-59-130314 and JP-A-6.
It has been proposed in Publication No. 0-12631.2. In these publications, water is used as a solvent for the spinning stock solution, and specific examples include the use of aqueous solutions containing inorganic salts such as calcium chloride, zinc chloride, aluminum chloride, or rhodan soda. There is no mention of including a specific inorganic salt in the drawn yarn of the PVA fiber obtained in No. 1, or that the drawability is improved by including the inorganic salt.

(発明が解決しようとする問題点) したがって本発明の目的は、 PPTA繊維と同程度の
強度と初期弾性率を有し、120℃における高温特性が
従来のPVA繊維より優れかつ、ポリエチレン繊維より
も高い耐熱性を有するPVA繊維を提供することにあり
、しかもそのものを低コストで製造可能とすることにあ
る。
(Problems to be Solved by the Invention) Therefore, the object of the present invention is to create a fiber that has strength and initial elastic modulus comparable to those of PPTA fibers, has superior high-temperature properties at 120°C than conventional PVA fibers, and is better than polyethylene fibers. The object of the present invention is to provide PVA fibers having high heat resistance, and to be able to manufacture the fibers at low cost.

(問題点を解決するための手段) 本発明者らは、かかる現状に鑑み、適度な耐熱性を有す
るPVAから、従来品よりも高い強度と初期弾性率を有
し、高温下においてもそれらが高い水準にあるPVA繊
維を得ることを目的とし鋭意検討した結果9本発明に到
達した。
(Means for Solving the Problems) In view of the current situation, the present inventors made PVA with appropriate heat resistance, which has higher strength and initial elastic modulus than conventional products, and which can be used even at high temperatures. As a result of intensive studies aimed at obtaining PVA fibers of a high standard, the present invention was arrived at.

すなわち2本発明は、 PVAに対して200〜800
0ppmのホウ酸またはホウ酸塩を含有し1重合度30
00以上のPVAから成り、かつ少なくとも18g/d
の強度と少なくとも350 g/d  の初期弾性率を
有するポリビニルアルコール繊維を要旨とするものであ
る。
That is, in the present invention, 200 to 800
Contains 0 ppm of boric acid or borate and has a degree of polymerization of 30
00 or higher and at least 18 g/d
and an initial modulus of at least 350 g/d.

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.

本発明の高強度・初期高弾性率PVA繊維を製造するに
は1重合度が3000以上のPVAの水溶液にホウ酸を
添加するか又はホウ酸塩及び微量の酸を添加して紡糸原
液とし、その紡糸原液を脱水性塩類を含む中性か又はア
ルカリ性の水溶液を凝固浴として乾・湿式紡糸した後、
目的とする強度と初期弾性率となるまで延伸すればよい
が、その実施態様をさらに詳しく説明する。
To produce the high-strength/high-initial-modulus PVA fiber of the present invention, boric acid is added to an aqueous solution of PVA having a degree of polymerization of 3000 or more, or a boric acid salt and a small amount of acid are added to prepare a spinning stock solution. After dry/wet spinning the spinning solution using a neutral or alkaline aqueous solution containing dehydrating salts as a coagulation bath,
It may be stretched until the desired strength and initial elastic modulus are achieved, and the embodiment thereof will be described in more detail.

重合度が3000以上のpv^の水溶液にPVAに対し
て0.1〜5重量のホウ酸又はホウ酸塩を添加し。
Boric acid or a boric acid salt in an amount of 0.1 to 5 weight based on PVA is added to an aqueous solution with a pv^ of a polymerization degree of 3000 or more.

塩酸や硫酸等の酸でpH3,5〜5の範囲に調整したも
のを紡糸原液とする。紡糸原液のPVA濃度は5〜50
重量%のものが好ましい。また、紡糸原液を酸性水溶液
とすることはPVAとポウ酸又はボウ酸塩が架橋反応し
ゲル化することを防止するために重要なことである。ホ
ウ酸塩の好適な例としてはホウ酸ナトリウム、ホウ酸カ
リウム、ホウ酸アンモニウム、ホウ酸リチウム等があげ
られる。
The spinning stock solution is prepared by adjusting the pH to a range of 3.5 to 5 with an acid such as hydrochloric acid or sulfuric acid. PVA concentration of spinning stock solution is 5-50
% by weight is preferred. Further, it is important to use an acidic aqueous solution as the spinning stock solution in order to prevent PVA from crosslinking with poric acid or borate to form a gel. Suitable examples of borates include sodium borate, potassium borate, ammonium borate, lithium borate, and the like.

次に」二連のごとくして調製された紡糸原液を紡糸用口
金から押し出し、空気、窒素等の不活性ガス層を通過さ
せてから、脱水性塩類30〜400g/lおよび水酸化
アルカリO〜300g#!を含む水溶液に紡出して凝固
させ、 PVAとホウ酸又はホウ酸塩が架橋したゲル状
未延伸糸とする。次いで。
Next, the spinning dope prepared in duplicate is extruded from the spinning nozzle, passed through a layer of inert gas such as air or nitrogen, and then 30-400 g/l of dehydrating salts and alkali hydroxide O- 300g#! The yarn is spun into an aqueous solution containing PVA and coagulated to form a gel-like undrawn yarn crosslinked with PVA and boric acid or borate. Next.

ゲル状未延伸糸を中和処理、温熱処理、洗浄処理。Neutralization treatment, heat treatment, and washing treatment of gel-like undrawn yarn.

油剤処理、乾燥等の処理を施し、かつ、この間で3〜8
倍の紡糸延伸を行い、一旦未延伸糸として巻取るか、又
は連続して乾熱延伸するかもしくは熱溶媒で延伸する。
Apply treatment such as oil treatment and drying, and during this time 3 to 8
The yarn is spun and stretched twice as much, and then wound up once as an undrawn yarn, or it is continuously drawn with dry heat or with a hot solvent.

かかる延伸時の温度は 220℃以上が好ましく、更に
好ましくは245℃以上で延伸するのがよく、また2段
以上の多段延伸するのが好ましい。
The temperature during such stretching is preferably 220°C or higher, more preferably 245°C or higher, and multi-stage stretching of two or more stages is preferred.

本発明の如く2強度が少なくとも18 g/d 、初期
弾性率が少なくとも350 g/dのPVA繊維とする
には前記実施態様において紡糸延伸を含めて全延伸倍率
が18倍以上、好ましくは25倍以上、更に好ましくは
30倍以上となるように延伸すればよい。
In order to obtain a PVA fiber having a dual strength of at least 18 g/d and an initial elastic modulus of at least 350 g/d as in the present invention, in the above embodiment, the total draw ratio including spinning/drawing is 18 times or more, preferably 25 times. What is necessary is just to extend so that it may be more preferably 30 times or more.

以上のように乾、湿式紡糸することにより、従来のPV
Aの重合度より更に高い重合度のPVAを使用しても、
延伸性の極めて高い未延伸糸を得ることが可能となり、
その未延伸糸は高倍率に熱延伸するかまたは温熱延伸す
ることにより本発明の高強度・高初期弾性率を有するP
VA繊維とすることができる。
By dry and wet spinning as described above, conventional PV
Even if PVA with a polymerization degree higher than that of A is used,
It is now possible to obtain undrawn yarn with extremely high drawability,
The undrawn yarn is heat-stretched to a high magnification or warm-stretched to obtain the P of the present invention having high strength and high initial elastic modulus.
It can be a VA fiber.

本発明のPVA 繊維を構成するPVAは重合度が30
00以上でなければならず、好ましくは4000以上で
ある。
The PVA constituting the PVA fiber of the present invention has a polymerization degree of 30.
00 or more, preferably 4000 or more.

本発明のPVA繊維の製造に使用するpvΔのケン化度
は99%以上のものが好ましいが乾・湿式紡糸する際、
凝固浴をアルカリ性とすることにより。
The degree of saponification of pvΔ used in the production of the PVA fiber of the present invention is preferably 99% or more, but when performing dry/wet spinning,
By making the coagulation bath alkaline.

再ケン化しうるのでケン化度99%未満のPVAを使用
することも可能である。PVAの重合度が3000未満
の場合には3本発明の高強度・高初期弾性率繊維を得る
ことができない。
Since it can be resaponified, it is also possible to use PVA with a saponification degree of less than 99%. If the degree of polymerization of PVA is less than 3000, the high strength/high initial modulus fiber of the present invention cannot be obtained.

また1本発明のPVA繊維はホウ酸又はホウ酸塩を含有
していなければならない。このことは前述の如<、PV
/lの紡糸原液を乾・湿式紡糸するごとにより延伸性の
極めて高い未延伸糸を得ることが可能となったのである
が、それは乾・混紡糸すること、高重合度のPVAを用
いること、及びホウ酸又はホウ酸塩を未延伸糸中に含有
することによって初めて達成できるのである。その理由
は、 PVAの水溶液である原液はホウ酸を含むことに
より。
Also, the PVA fiber of the present invention must contain boric acid or borate. This is explained above as <, PV
It became possible to obtain an undrawn yarn with extremely high drawability by dry/wet spinning a spinning stock solution of /l, but this was achieved by dry/mixing yarn, using PVA with a high degree of polymerization, This can only be achieved by incorporating boric acid or a boric acid salt into the undrawn yarn. The reason is that the stock solution, which is an aqueous solution of PVA, contains boric acid.

アルカリ性凝固浴に紡出された際、p■の変化により著
しく粘度が上昇し、ゲル繊維になることにある。ホウ酸
もしくはホウ酸塩以外で、かかる作用機構を有するもの
は著しい着色を示すもの以外知られていない。
When spun into an alkaline coagulation bath, the viscosity increases significantly due to the change in p, resulting in gel fibers. Other than boric acid or boric acid salts, there are no known substances that have such a mechanism of action other than those that exhibit significant coloration.

本発明のPVA繊維はかかるホウ酸含有ゲル未延伸糸を
高倍率延伸してはじめて得られるので、延伸糸中にホウ
酸またはホウ酸塩を含有することとなる。延伸糸からホ
ウ酸またはホウ酸塩を水等の適当な溶媒で溶出させるこ
とも可能ではあるが。
Since the PVA fiber of the present invention is obtained only by drawing such boric acid-containing gel undrawn yarn at a high magnification, the drawn yarn contains boric acid or a boric acid salt. Although it is possible to elute boric acid or borate from the drawn yarn with a suitable solvent such as water.

延伸糸は高度に配向したPVAから構成されているため
、繊維中に溶媒が入り難いためか、その溶出にはかなり
の時間を要し、その場合には繊維表面を傷つけることに
もなり、かえって繊維性能を低下させることになるなど
好ましくない。更には。
Since the drawn yarn is composed of highly oriented PVA, it may be difficult for the solvent to enter the fiber, so it takes a considerable amount of time for it to elute, and in that case it may damage the fiber surface. This is undesirable because it causes a decrease in fiber performance. Furthermore.

PVA繊維からホウ酸またはホウ酸塩の含有量が200
ppm未満になるまで除去した場合、高温特性の低下を
きたし好ましくない。
Boric acid or borate content from PVA fiber is 200%
If it is removed to less than ppm, the high temperature properties will deteriorate, which is not preferable.

PVA繊維のホウ酸またはホウ酸塩の含有量はPVAに
対して200〜8000ppmの範囲内にあることが肝
要である。含有量が200ppm未満の場合、操作的に
は水による洗浄時に繊維が膨潤してたるみが生じローラ
ーに捲きつくといった工程の不安定化が生じ、また量的
な不足により延伸性も低下する。
It is important that the content of boric acid or borate in the PVA fibers is in the range of 200 to 8000 ppm based on PVA. If the content is less than 200 ppm, the fibers swell during washing with water and become sagging, causing instability in the process such as winding around a roller, and the stretching properties are also lowered due to insufficient quantity.

更に前述の如く、高温下での強度や初期弾性率も低下す
る。一方、含有量が8000ppmを超える場合にはか
えって延伸性が低下し強度や初期弾性率の値が小さくな
る。
Furthermore, as mentioned above, the strength and initial elastic modulus at high temperatures also decrease. On the other hand, if the content exceeds 8,000 ppm, the drawability is rather reduced, and the strength and initial elastic modulus values are reduced.

本発明におけるホウ酸またはホウ酸塩の含有量とは、 
PVA繊維中のホウ酸及びホウ酸塩をすべてホウ酸とし
て換算したものであり(それ故に以下ホウ酸含有量と記
す。)その定量は以下に示す方法で行った。
The content of boric acid or borate in the present invention is
All of the boric acid and boric acid salts in the PVA fibers were converted into boric acid (therefore, hereinafter referred to as boric acid content), and the quantitative determination was performed by the method shown below.

すなわち、ルツボに約2gのpvAiQ維を精秤し−1
0= 0.1規定の水酸化ナトリウム水溶液を試料が液面から
出ない程度に入れた後、約105°Cで加熱放置して水
分を留去し2次いで電気炉中で400〜500℃の温度
で約1時間灼く。これをルツボごとビーカーに入れ、イ
オン交換水を入れ7 しばらくの間装置してから指示薬
フェノールフタレインを滴下して水溶液の色が変化する
まで0.1規定の塩酸を滴下して約1時間煮沸する。冷
却後、水酸化ナトリウム又は塩酸でp117に中和して
からマンニットを加え、ふたたびpiが7になるまで0
.1規定の水酸化ナトリウム水溶液で滴定し、要した量
(単位cc)を求めた。試料中pvΔの重量をWg、0
.1規定の水酸化ナトリウム水溶液の力価及び滴定叡(
要した量)をそれぞれf及びVccとすると。
That is, approximately 2 g of pvAiQ fiber was accurately weighed in a crucible and -1
0 = After adding 0.1N sodium hydroxide aqueous solution to the extent that the sample does not come out from the liquid level, heat it at about 105°C to distill off the moisture, and then heat it in an electric furnace at 400 to 500°C. Bake at high temperature for about 1 hour. Put this together with the crucible in a beaker, add ion-exchanged water, and let it sit for a while, then add the indicator phenolphthalein dropwise, add 0.1 N hydrochloric acid dropwise until the aqueous solution changes color, and boil for about 1 hour. do. After cooling, neutralize to p117 with sodium hydroxide or hydrochloric acid, add mannitol, and boil until pi becomes 7 again.
.. Titration was performed with a 1N aqueous sodium hydroxide solution to determine the required amount (in cc). The weight of pvΔ in the sample is Wg, 0
.. Titer and titration of 1N aqueous sodium hydroxide solution (
The required amount) are respectively f and Vcc.

PVAに対するホウ酸含有量Bは次式で与えられる。The boric acid content B relative to PVA is given by the following formula.

(作 用) 本発明においては上述の如く、ホウ酸又はホウ酸塩を添
加した酸性水系紡糸原液の使用が不可欠である。これに
よって紡糸原液を凝固浴に紡出したとき、未延伸糸内に
架橋構造を形成できるのである。従って本発明において
は重合度3000〜6000の中程度高重合PVAを使
用しても、延伸性に冨んだ延伸糸を得ることが可能にな
り、 350 g/d 1’J 、、、lr。
(Function) As described above, in the present invention, it is essential to use an acidic aqueous spinning stock solution to which boric acid or a borate salt is added. This allows a crosslinked structure to be formed within the undrawn yarn when the spinning dope is spun into the coagulation bath. Therefore, in the present invention, even if medium-highly polymerized PVA with a polymerization degree of 3,000 to 6,000 is used, it is possible to obtain a drawn yarn with high drawability, 350 g/d 1'J,...lr.

の初期弾性率を有する繊維に延伸することができる。特
開昭59−13031号公報、特開昭60−12631
2号公報には紡糸用原液の溶媒として水及び水に溶解し
た諸種の塩1例えば塩化リチュウム、塩化カルシウム、
塩化アルミニウム、塩化亜鉛、ロダンソーダその他の水
素結合を切ることによりPVAの溶解度を増すことので
きる物質の溶液が記載されているが5本発明の如く凝固
に際して架橋構造を形成できるホウ酸又はホウ酸塩を添
加した酸性水溶液を用いるとの示唆はない。この点が前
者においては分子量500000以−ヒの超高分子量p
v^を用いる必要があり、また後者においては同公報実
施例1の比較例の如く、水系溶媒の場合、延伸率が上が
らず、高強度・高弾性率繊維が得られない理由であろう
can be drawn into a fiber with an initial modulus of . JP-A-59-13031, JP-A-60-12631
Publication No. 2 describes water and various salts dissolved in water as solvents for spinning stock solutions, such as lithium chloride, calcium chloride,
Solutions of aluminum chloride, zinc chloride, rhodan soda, and other substances capable of increasing the solubility of PVA by breaking hydrogen bonds have been described. There is no suggestion of using an acidic aqueous solution containing . In the former case, this point is
In the latter case, as in the comparative example of Example 1 of the same publication, in the case of an aqueous solvent, the drawing ratio does not increase and this is probably the reason why high strength and high modulus fibers cannot be obtained.

(実施例) 以下、実施例をあげて本発明をさらに具体的に説明する
(Examples) Hereinafter, the present invention will be explained in more detail by giving examples.

なお1例中の強度及び初期弾性率はJIS L 101
7に規定される方法により測定したものであり、高温下
における強度及び初期弾性率の測定も雰囲気温度を12
0℃として上記方法に従った。
In addition, the strength and initial elastic modulus in one example are JIS L 101
7, and the strength and initial elastic modulus at high temperatures were also measured at an atmospheric temperature of 12
The above method was followed at 0°C.

また、 PVAの重合度はJIS K 6726に規定
される方法に従って10位の数字を四捨五入して算出し
たものである。
The degree of polymerization of PVA is calculated by rounding off the 10th place according to the method specified in JIS K 6726.

実施例1.比較例1,2 重合度3200 (7)PVA及びPVA ニ対しT 
i、o重量%のホウ酸を熱水に溶解してPVAの濃度が
12重量%の紡糸原液を調製した。この紡糸原液を70
℃で紡糸用口金から押出し、4mmの空気層を通過させ
てから水酸化ナトリウム100g/ 12及び硫酸ナト
リウム100g/ 1を含む50℃の水溶液に紡出し。
Example 1. Comparative Examples 1 and 2 Polymerization degree 3200 (7) PVA and PVA double T
A spinning dope having a PVA concentration of 12% by weight was prepared by dissolving i,o% by weight of boric acid in hot water. 70% of this spinning stock solution
It was extruded from a spinning nozzle at 10°C, passed through a 4 mm air layer, and then spun into an aqueous solution at 50°C containing 100g/12 sodium hydroxide and 100g/12 sodium sulfate.

PVAゲル状未延伸糸とした後、延伸倍率3倍でローラ
ー延伸し9次いで中和、洗浄を行ったのち延伸倍率2倍
で温熱延伸し、乾燥した後、捲取った。
After forming a PVA gel-like undrawn yarn, it was stretched with a roller at a draw ratio of 3 times, neutralized and washed, then warm-stretched at a draw ratio of 2 times, dried, and then wound up.

このようにして得られた未延伸糸を、更に245℃の温
度で紡糸延伸を含めて全延伸倍率が20倍となるように
熱延伸した。
The thus obtained undrawn yarn was further hot-stretched at a temperature of 245° C. so that the total stretching ratio including spinning and stretching was 20 times.

比較のため1重合度3200のI’VAに代えて重合度
2300のPVA又は重合度1700をPv^を用いた
ほかは実施例1と同様にして延伸糸を得た。ただし5重
合度が1700のPVAの場合は、全延伸率が20倍に
なるまで延伸できなかったため全延伸倍率を断糸なく順
調に延伸できる15,2倍とした。
For comparison, drawn yarns were obtained in the same manner as in Example 1, except that PVA with a polymerization degree of 2300 or Pv^ with a polymerization degree of 1700 was used instead of I'VA with a polymerization degree of 3200. However, in the case of PVA with a 5 degree of polymerization of 1700, it was not possible to stretch the film until the total stretching ratio reached 20 times, so the total stretching ratio was set to 15.2 times, which allows smooth stretching without yarn breakage.

得られた延伸糸の特性を表1に示す。Table 1 shows the properties of the drawn yarn obtained.

=14− 表1 実施例2 重合度3200 (7) PVA、 PVAに対して1
.5重量%のホウ酸ナトリウム及び硫酸を熱水に溶解し
てPVA濃度が12重量%、 pH4の紡糸原液を調製
した。この紡糸原液を75℃で紡糸用口金から押出し、
5mmの空気層を通過させてから、水酸化ナトリウム1
20g/z及び硫酸ナトリウム150gを含む50℃の
水溶液に紡糸し、 PVAゲル状未延伸糸とした後、延
伸倍率5倍の紡糸延伸を行ない9次いで中和、湿熱処理
、洗浄、乾燥を施し、引続き230℃の熱風循環炉を通
して全延伸倍率が21.3倍となるように第1熱延伸し
、さらに深度6%の鉱油系水エマルジョンに浸漬した後
、245℃で1.3倍の第2熱延伸を行い1ooOd1
500fの延伸糸を得た。紡糸延伸を含めた全延伸倍率
は2744倍であった・ 得られた延伸糸の強度は22.5g/d、初期弾性率は
441 g/d、伸度は3.6%であり、ホウ酸含有L
1は3000 ppmであった。
=14- Table 1 Example 2 Degree of polymerization 3200 (7) PVA, 1 for PVA
.. A spinning stock solution having a PVA concentration of 12% by weight and a pH of 4 was prepared by dissolving 5% by weight of sodium borate and sulfuric acid in hot water. This spinning stock solution is extruded from a spinning nozzle at 75°C,
After passing through a 5 mm air layer, add 1 ml of sodium hydroxide.
After spinning in a 50 ° C. aqueous solution containing 20 g/z and 150 g of sodium sulfate to obtain a PVA gel-like undrawn yarn, spinning and drawing was performed at a draw ratio of 5 times, followed by neutralization, wet heat treatment, washing, and drying. Subsequently, the first hot stretching was carried out in a hot air circulating oven at 230°C so that the total stretching ratio was 21.3 times, and after further immersion in a mineral oil-based water emulsion with a depth of 6%, the second drawing was carried out at 245°C with a stretching ratio of 1.3 times. Perform hot stretching to 1ooOd1
A drawn yarn of 500 f was obtained. The total stretching ratio including spinning and drawing was 2744 times. The strength of the obtained drawn yarn was 22.5 g/d, the initial elastic modulus was 441 g/d, and the elongation was 3.6%. Contains L
1 was 3000 ppm.

実施例3 重合度4500のPVA及びPVAに対して0.5重量
%のホウ酸を熱水に溶解してPVA濃度が10重量%の
紡糸原液を調製した。この紡糸原液を80℃で紡糸用口
金から押出し+7mmの空気層を通過させてから、水酸
化ナトリウム50g/β及び硫酸すトリウム100g/
ffを含む40℃の水溶液に紡出し。
Example 3 A spinning dope having a PVA concentration of 10% by weight was prepared by dissolving PVA with a polymerization degree of 4500 and 0.5% by weight of boric acid based on PVA in hot water. This spinning dope was extruded from a spinning nozzle at 80°C and passed through a 7 mm air layer, followed by 50 g/β of sodium hydroxide and 100 g/100 g of sodium sulfate.
Spun into a 40°C aqueous solution containing ff.

PVAゲル状未延伸糸とした後、中和、温熱処理。After making PVA gel-like undrawn yarn, it is neutralized and heated.

洗浄、油剤処理、乾燥を施し1次いで230℃で第1熱
延伸を行なったのち、鉱油系水エマルジョンに浸漬、引
続き240℃で第2熱延伸を行い、更に鉱油系水エマル
ジョンに浸漬した後、250℃で第3熱延伸を行い、 
750d1500fの延伸糸を得た。このときの全延伸
倍率は34.5倍であった。
After washing, oil treatment, drying, first hot stretching at 230°C, immersion in mineral oil water emulsion, second hot stretching at 240°C, further immersion in mineral oil water emulsion, Third hot stretching is performed at 250°C,
A drawn yarn of 750d1500f was obtained. The total stretching ratio at this time was 34.5 times.

得られた延伸糸の強度は25.9 g/d 、初期弾性
率は、 498 g/d 、伸度は、3.2%であり、
ホウ酸含有量は700ppmであった。
The obtained drawn yarn had a strength of 25.9 g/d, an initial elastic modulus of 498 g/d, and an elongation of 3.2%.
The boric acid content was 700 ppm.

比較例3 紡糸原液にホウ酸を添加しなかった以外は実施例3と同
様の操作を行った。紡糸後、繊維のローラーへの巻きつ
き等が生じ製糸性が低下したが。
Comparative Example 3 The same operation as in Example 3 was performed except that boric acid was not added to the spinning dope. After spinning, the fibers tended to wrap around the rollers, resulting in poor spinning properties.

延伸糸を得た。ただし第I熱延伸、第2熱延伸共に23
0℃で行ない第3熱延伸は行なわなかった。
A drawn yarn was obtained. However, both the first hot stretching and the second hot stretching are 23
The third hot stretching was not performed at 0°C.

全延伸倍率は34.5倍に延伸できなかったため断糸な
く順゛調に延伸できる17.2倍とした。
Since the film could not be stretched to 34.5 times, the total stretching ratio was set to 17.2 times, which allowed smooth stretching without yarn breakage.

得られた延伸糸の強度は12.8g/d、初期弾性率は
267 g/d、伸度は5.6%であった。
The obtained drawn yarn had a strength of 12.8 g/d, an initial elastic modulus of 267 g/d, and an elongation of 5.6%.

比較例4 実施例3において紡糸用口金を凝固浴中に浸漬し、湿式
紡糸としたところ、延伸性が極めて低下し断糸が多発し
た。
Comparative Example 4 In Example 3, when the spinning nozzle was immersed in a coagulation bath to perform wet spinning, the drawability was extremely low and yarn breakage occurred frequently.

比較例5 洗浄工程において、比較例5ではホウ酸含有量が110
0ppとなるように、比較例6ではホウ酸含有量が11
0000ppとなるように洗浄した以外は実施例2と同
様に操作した。
Comparative Example 5 In the cleaning process, in Comparative Example 5, the boric acid content was 110
In Comparative Example 6, the boric acid content was 11 so that it was 0pp.
The same procedure as in Example 2 was carried out except that washing was carried out to obtain a concentration of 0,000 pp.

比較例5ではローラーへの巻きつき等が起こり製糸性の
低下とともに延伸性も低下し、比較例6ではホウ酸含有
量が過多のため、延伸性が低下し。
In Comparative Example 5, winding around the rollers occurred, resulting in a decrease in spinning properties and also in drawability, and in Comparative Example 6, due to excessive boric acid content, drawability was reduced.

高強度・高弾性率繊維が得られなかった。High strength/high elastic modulus fibers could not be obtained.

実施例4.比較例7 平均重合度3500のPVA及びPVAに対して1.5
重量%のホウ酸を熱水に溶解してPVA濃度が11重量
%の紡糸原液を調製した。この紡糸原液を以下の2種類
の方法で紡糸した。
Example 4. Comparative Example 7 PVA with average polymerization degree of 3500 and 1.5 for PVA
A spinning stock solution having a PVA concentration of 11% by weight was prepared by dissolving % by weight of boric acid in hot water. This spinning dope was spun using the following two methods.

(1)紡糸原液を紡糸用口金から5mmの空気層を通過
させてから、水酸化ナトリウム10g/Aおよび硫酸ナ
トリウム400g/ (lを含む水溶液に紡出した(実
施例4)。
(1) The spinning stock solution was passed through a 5 mm air layer from a spinning nozzle, and then spun into an aqueous solution containing 10 g/A of sodium hydroxide and 400 g/L of sodium sulfate (Example 4).

(2)紡糸用口金を水酸化ナトリウムlog/7!およ
び硫酸ナトリウム400g/ Rを含む水溶液中に浸漬
し、紡糸原液をこの水溶液中に直接紡出したく比較例7
)。
(2) Sodium hydroxide log/7! Comparative Example 7 in which the spinning solution was immersed in an aqueous solution containing 400 g/R of sodium sulfate and the spinning stock solution was directly spun into this aqueous solution.
).

その後、実施例4.比較例7共に5倍の紡糸延伸を施し
1次いで硫酸ナトリウム300g/ IV、及び硫酸3
0g/ I!、を含む90℃の浴で温熱処理し、水洗。
After that, Example 4. Comparative Example 7 Both were subjected to 5 times spinning and stretching, and then 300 g/IV of sodium sulfate and 3 sulfuric acid were added.
0g/I! Heat treated in a 90°C bath containing , and washed with water.

乾燥を施した。乾燥繊維を230°Cで3.0倍の第1
熱延伸後、鉱物油を主体とする延伸性油剤エマルジョン
に浸漬、押法し、水分を30%付与した繊維を240℃
で1.3倍の第2熱延伸を行い最後に前工程と同様に水
分付与した後、250℃で第3段熱延伸を行い1400
d1500fの延伸糸を得た。
It was dried. The dry fibers were dried at 230°C by 3.0 times the first
After hot stretching, the fibers were immersed in a stretchable oil emulsion mainly composed of mineral oil and pressed to add 30% moisture to the fibers at 240°C.
After performing a second hot stretching of 1.3 times at
A drawn yarn of d1500f was obtained.

得られた延伸糸の特性は表2に示す通りであっ(発明の
効果) 本発明のPVA繊維は、従来の湿式紡糸により得られた
PVA繊維と比較して非常に高い強度と初期弾性率を存
しており、その値ばr’PTA繊維に匹敵する。また、
高強度・高弾性率ポリエチレン繊維に較べても耐熱性が
高く、特にシー1・、テント地帆布等の産業用布帛ばか
りでなく2タイヤ、アスベスト代替コンクリ−ト等の補
強材分野に好適に使用できる。
The properties of the obtained drawn yarn are as shown in Table 2 (Effects of the Invention) The PVA fiber of the present invention has extremely high strength and initial elastic modulus compared to PVA fiber obtained by conventional wet spinning. Its value is comparable to that of r'PTA fiber. Also,
It has higher heat resistance than high-strength, high-modulus polyethylene fibers, and is particularly suitable for use in reinforcing materials such as sea 1 and industrial fabrics such as canvas tents, tires, and asbestos substitute concrete. can.

Claims (1)

【特許請求の範囲】[Claims] (1)ポリビニルアルコールに対して200〜8000
ppmのホウ酸又はホウ酸塩を含有し、重合度3000
以上のポリビニルアルコールから成り、かつ少なくとも
18g/dの強度と少なくとも350g/dの初期弾性
率を有するポリビニルアルコール繊維。
(1) 200-8000 for polyvinyl alcohol
Contains ppm of boric acid or borate, and has a degree of polymerization of 3000
A polyvinyl alcohol fiber comprising the above polyvinyl alcohol and having a strength of at least 18 g/d and an initial elastic modulus of at least 350 g/d.
JP28495685A 1985-12-17 1985-12-17 Polyvinyl alcohol fiber Pending JPS62149909A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28495685A JPS62149909A (en) 1985-12-17 1985-12-17 Polyvinyl alcohol fiber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28495685A JPS62149909A (en) 1985-12-17 1985-12-17 Polyvinyl alcohol fiber

Publications (1)

Publication Number Publication Date
JPS62149909A true JPS62149909A (en) 1987-07-03

Family

ID=17685252

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28495685A Pending JPS62149909A (en) 1985-12-17 1985-12-17 Polyvinyl alcohol fiber

Country Status (1)

Country Link
JP (1) JPS62149909A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02277809A (en) * 1989-04-12 1990-11-14 Kuraray Co Ltd Production of high-tenacity polyvinyl alcohol fiber
EP0496376A2 (en) * 1991-01-22 1992-07-29 Unitika Ltd. Polyvinyl alcohol fiber and process for preparation thereof
US5264173A (en) * 1989-05-24 1993-11-23 Masatsugu Mochizuki Polyvinyl alcohol monofilament yarns and process for producing the same
CN111101219A (en) * 2018-10-26 2020-05-05 中国石油化工股份有限公司 High-strength high-modulus polyvinyl alcohol filament and preparation method thereof

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02277809A (en) * 1989-04-12 1990-11-14 Kuraray Co Ltd Production of high-tenacity polyvinyl alcohol fiber
US5264173A (en) * 1989-05-24 1993-11-23 Masatsugu Mochizuki Polyvinyl alcohol monofilament yarns and process for producing the same
EP0496376A2 (en) * 1991-01-22 1992-07-29 Unitika Ltd. Polyvinyl alcohol fiber and process for preparation thereof
CN111101219A (en) * 2018-10-26 2020-05-05 中国石油化工股份有限公司 High-strength high-modulus polyvinyl alcohol filament and preparation method thereof
CN111101219B (en) * 2018-10-26 2022-08-12 中国石油化工股份有限公司 High-strength high-modulus polyvinyl alcohol filament and preparation method thereof

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