JPH0455335A - Production of inorganic fiber - Google Patents

Production of inorganic fiber

Info

Publication number
JPH0455335A
JPH0455335A JP16364790A JP16364790A JPH0455335A JP H0455335 A JPH0455335 A JP H0455335A JP 16364790 A JP16364790 A JP 16364790A JP 16364790 A JP16364790 A JP 16364790A JP H0455335 A JPH0455335 A JP H0455335A
Authority
JP
Japan
Prior art keywords
sol
fibrous
gel
spinning
metal
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
JP16364790A
Other languages
Japanese (ja)
Inventor
Koji Yokoi
浩司 横井
Toshiaki Mizuno
俊明 水野
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.)
Nippon Sheet Glass Co Ltd
Original Assignee
Nippon Sheet Glass Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nippon Sheet Glass Co Ltd filed Critical Nippon Sheet Glass Co Ltd
Priority to JP16364790A priority Critical patent/JPH0455335A/en
Publication of JPH0455335A publication Critical patent/JPH0455335A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B37/00Manufacture or treatment of flakes, fibres, or filaments from softened glass, minerals, or slags
    • C03B37/01Manufacture of glass fibres or filaments
    • C03B37/011Manufacture of glass fibres or filaments starting from a liquid phase reaction process, e.g. through a gel phase

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Dispersion Chemistry (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Glass Melting And Manufacturing (AREA)
  • Manufacture, Treatment Of Glass Fibers (AREA)
  • Inorganic Fibers (AREA)

Abstract

PURPOSE:To make a round cross section of fiber by bringing a fibrous sol during spinning from a viscous sol soln. or just after spinning into contact with a gas having constant humidity. CONSTITUTION:Water, catalyst and solvent are added to an org. metal compd. such as metal alkoxide, metal halide, metal org. acid salt, etc., to obtain a sol soln. of proper viscosity by hydrolysis and polymn. Then the sol soln. is drawn from a spinning nozzle under normal or high pressure to obtain a fibrous sol. This fibrous sol is brought into contact with gas maintained at 60 - 100 % relative humidity for >=0.5 sec to make a gel. The obtd. fibrous gel is sintered at 400 - 1200 deg.C to obtain inorg. fiber having a round cross section.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、ゾル−ゲル法による無機繊維の製造方法に関
する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for producing inorganic fibers by a sol-gel method.

〔従来の技術〕[Conventional technology]

金属アルコキシドからガラス、セラミックス等の無機物
を作製する方法は、一般にゾル−ゲル法と呼ばれている
。このゾル−ゲル法により繊維を作製しようとする場合
、通常以下の手順をとる。
A method for producing inorganic materials such as glasses and ceramics from metal alkoxides is generally called a sol-gel method. When attempting to produce fibers by this sol-gel method, the following steps are usually taken.

金属アルコキシドに水、触媒及び必要に応じて溶媒を添
加、混合する。溶液中で加水分解・重合反応が進行し、
高分子が形成され、ゾル溶液となる。この反応が進行す
るにともないゾル溶液の粘度は徐々に上昇する。ゾル溶
液が適当な粘度に達したところで通常の方法により紡糸
すると、繊維状ゲルが得られる。このゾル−ゲル法によ
り繊維を紡糸した場合、一般に得られた繊維の断面形状
が楕円型、両型などの非円形形状を示す。Eガラスファ
イバーに見られる様なほぼ真円形の断面形状を有したフ
ァイバーを得るのは困難である。例えば、KAMIYA
らは、原料を限定されたモル比で調合しなければ円形断
面は出現しないと述べている(K、KAMfYA an
d T、YOKO:Jounal of Materi
al 5cience、Vol、21.(1986)、
842−848) 。また、太田らは、ゾル−ゲル法に
より作製したファイバーの断面形状が、縦横比(長径/
短径)15〜7.5の長円形(楕円形を含む)になるこ
とを述べている(例えば特開昭6l−24488)。同
様に、水口らもゾル溶液から紡糸を行い、断面形状がほ
ぼ偏平状に成形された繊維体ゲルを得ている(例えば特
開昭62−230643)。
Water, a catalyst and, if necessary, a solvent are added to the metal alkoxide and mixed. Hydrolysis and polymerization reactions proceed in the solution,
A polymer is formed and becomes a sol solution. As this reaction progresses, the viscosity of the sol solution gradually increases. When the sol solution reaches an appropriate viscosity, it is spun using a conventional method to obtain a fibrous gel. When fibers are spun by this sol-gel method, the cross-sectional shape of the obtained fibers generally exhibits a non-circular shape such as an elliptical shape or a double shape. It is difficult to obtain a fiber with a substantially perfect circular cross-sectional shape as seen in E-glass fibers. For example, KAMIYA
stated that a circular cross section does not appear unless the raw materials are mixed in a limited molar ratio (K, KAMfYA an
d T, YOKO: Journal of Materi
al 5science, Vol, 21. (1986),
842-848). In addition, Ohta et al. also found that the cross-sectional shape of fibers produced by the sol-gel method was
(for example, Japanese Patent Laid-Open No. 61-24488) states that the shape is oval (including elliptical) with a minor axis of 15 to 7.5. Similarly, Mizuguchi et al. conducted spinning from a sol solution to obtain a fibrous gel having a substantially flat cross-sectional shape (for example, JP-A-62-230643).

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

このような断面形状が非円形の繊維の場合、ストランド
の見かけの外径及び織物の仕上がり厚みにばらつきがで
やすい、織物の通気性が悪くなる、又、織物の風合いが
悪い等の問題を生じる。
In the case of fibers with such a non-circular cross-sectional shape, problems such as variations in the apparent outer diameter of the strands and finished thickness of the fabric, poor breathability of the fabric, and poor texture of the fabric may occur. .

本発明は、ゾル−ゲル法により作製した無機繊維につき
、断面形状が円形に近い繊維を得ることを目的とする。
An object of the present invention is to obtain inorganic fibers having a cross-sectional shape close to a circle using a sol-gel method.

〔課題を解決するための手段〕[Means to solve the problem]

本発明者らは、断面形状が円形に近い繊維を得るには、
有機金属化合物の加水分解・重合によって得た粘稠なゾ
ル溶液から紡糸したゲル繊維を焼成することにより無機
繊維を製造する方法において、該粘稠なゾル溶液からの
紡糸中または紡糸後の繊維状ゾルを、60〜100%R
,Hの湿度に増加させた気体に接触させることが有効で
あることを見いだした。
The present inventors discovered that in order to obtain fibers with a cross-sectional shape close to circular,
In a method for producing inorganic fibers by firing gel fibers spun from a viscous sol solution obtained by hydrolysis/polymerization of an organometallic compound, fibrous fibers are produced during or after spinning from the viscous sol solution. Sol, 60-100%R
, H was found to be effective in contacting with a gas having increased humidity.

本発明の紡糸に用いるゾル溶液の作製方法は特に限定さ
れず、よく知られた技術により行なわれる。
The method for preparing the sol solution used in the spinning of the present invention is not particularly limited, and may be performed using well-known techniques.

本発明に用いられる原料としては、加水分解・重合反応
によってメタロキサン結合を作る有機金属化合物であれ
ば、どのようなものでもよい。例えば、金属アルコキシ
ド、金属ハロゲン化物、金属有機酸塩の有機金属化合物
が用いられる。該有機金属化合物に水、触媒及び必要に
応じ溶媒を添加し、加水分解・重合反応を起こさせ、適
当な粘度のゾル溶液を得る。
The raw material used in the present invention may be any organometallic compound that forms metalloxane bonds through hydrolysis/polymerization reactions. For example, organometallic compounds such as metal alkoxides, metal halides, and metal organic acid salts are used. Water, a catalyst and, if necessary, a solvent are added to the organometallic compound to cause a hydrolysis/polymerization reaction to obtain a sol solution with an appropriate viscosity.

ゾル溶液から紡糸を行う方法としては、特に限定されず
、従来のガラス繊維、高分子繊維などに適用される紡糸
法を用いることができる。基本的には、常圧あるいは加
圧下で、紡糸用ノズルからゾル溶液を流出させて繊維と
する方法を用いる。
The method for spinning from a sol solution is not particularly limited, and conventional spinning methods applicable to glass fibers, polymer fibers, etc. can be used. Basically, a method is used in which a sol solution is made to flow out from a spinning nozzle under normal pressure or increased pressure to form fibers.

このノズルから流出した繊維状ゾルに湿度60〜100
%R,11の気体を接触させる。
The fibrous sol flowing out from this nozzle has a humidity of 60 to 100.
%R, 11 gases are brought into contact.

ノズルから流出した繊維状ゾルは、高湿度の気体にさら
されることにより、断面形状がほぼ円形状の繊維状ゲル
となる。
The fibrous sol flowing out from the nozzle becomes a fibrous gel having a substantially circular cross-sectional shape by being exposed to high humidity gas.

湿度が60%R,H,未満では、効果が顕著ではなく5
.比較的偏平な断面形状を呈する。好ましくは、80〜
100%R,H,である。
When the humidity is less than 60%R,H, the effect is not significant and 5
.. It has a relatively flat cross-sectional shape. Preferably 80~
100% R, H.

ゾルを高湿度の気体に接触させる時間は、繊維径、ゾル
溶液の種類、湿度、温度等により決まるが、通常はおよ
そ0.5秒以上であればよい。長時間高湿度の気体にさ
らされると、余分な水分がゾル中に取り込まれ細孔の大
きな脆い繊維状ゲルとなることがあるので、24時間以
上は高湿度の気体に接触させておかない方がよい。
The time period for which the sol is brought into contact with the highly humid gas is determined by the fiber diameter, the type of sol solution, humidity, temperature, etc., but is usually about 0.5 seconds or more. If exposed to high humidity gas for a long time, excess water may be incorporated into the sol and form a brittle fibrous gel with large pores, so please do not leave it in contact with high humidity gas for more than 24 hours. Good.

繊維状ゾルを高湿度の気体に接触させる方法としては、
特に限定されないが、ノズルの下に高湿度の気体が滞留
できるようなパイプ状体を設置しそのバイブ中を繊維状
ゾルが通過するようにする方法、繊維状ゾルに高湿度の
気体を吹き付ける方法、高湿度に維持した部屋の中で紡
糸を行う方法等がある。
As a method of bringing the fibrous sol into contact with a highly humid gas,
Although not particularly limited, a method in which a pipe-like body is installed under the nozzle so that highly humid gas can stay and the fibrous sol passes through the vibrator, and a method in which high-humidity gas is sprayed onto the fibrous sol There are methods such as spinning in a room maintained at high humidity.

この様にして得た繊維状ゲルを、400〜1200℃で
焼結を行うことにより、断面形状が変化する事なく、は
ぼ円形状の断面形状を有する無機繊維が得られる。
By sintering the fibrous gel thus obtained at 400 to 1200°C, an inorganic fiber having a roughly circular cross-sectional shape can be obtained without changing the cross-sectional shape.

〔作用〕[Effect]

ゾル−ゲル法による紡糸で、繊維の断面形状が円形にな
らない原因として、以下の事が考えられる。紡糸された
繊維状ゾルが固化し繊維状ゲルとなる場合、溶媒の蒸発
による固化と、加水分解・重合反応の進展による固化と
がある。紡糸された繊維状ゾルからの溶媒の蒸発は表面
から起こり、表面層が固化を起こす。又、この時溶媒の
蒸発により重合反応が促進されるので、表面層の固化は
さらに進む。
The following may be the reason why the cross-sectional shape of the fiber does not become circular during spinning using the sol-gel method. When the spun fibrous sol solidifies into a fibrous gel, there are two types of solidification: solidification due to evaporation of the solvent and solidification due to progress of hydrolysis/polymerization reactions. Evaporation of the solvent from the spun fibrous sol occurs from the surface, causing solidification of the surface layer. Further, since the polymerization reaction is promoted by evaporation of the solvent at this time, the solidification of the surface layer further progresses.

繊維状ゾルの表面層が内部よりさきに固化するため、表
面に皮を張ったような状態となる。その後の内部の加水
分解・重合反応及び溶媒の蒸発により、収縮を起こし、
偏平な断面形状の繊維状ゲルとなる。
The surface layer of the fibrous sol solidifies before the inside, resulting in a skin-like state on the surface. The subsequent internal hydrolysis/polymerization reaction and evaporation of the solvent cause shrinkage,
It becomes a fibrous gel with a flat cross-sectional shape.

ここで、繊維状ゾルが、高湿度の気体にさらされた場合
、水分が繊維状ゾル中に拡散し加水分解反応が比較的均
一にゾル内で起こると共に表面からの溶媒の蒸発が抑制
される。そのため、断面形状が偏平になる事なく、はぼ
円形状の断面形状を有する繊維が得られる。
Here, when the fibrous sol is exposed to a highly humid gas, water diffuses into the fibrous sol, and the hydrolysis reaction occurs relatively uniformly within the sol, and evaporation of the solvent from the surface is suppressed. . Therefore, fibers having a roughly circular cross-sectional shape can be obtained without the cross-sectional shape becoming flat.

〔実施例〕〔Example〕

以下、実施例に基づき本発明の詳細な説明を行うが、本
発明は必ずしもこれらの実施例に限定されることはない
Hereinafter, the present invention will be described in detail based on Examples, but the present invention is not necessarily limited to these Examples.

所定量のモル比で5i(C2H50H)4、(CH3)
25i(C2H50H)2、水、lN−HCl及びエタ
ノールを混合した。30℃で反応を進め、200cPo
iseで0℃に冷却を行い、さらに600cPoise
になったところで一30℃に冷却を行った。1000c
Poiseに達したところで、内径0.3鰭のノズルを
使用し、窒素ガスで加圧することにより、紡糸を行った
。ノズルの下にパイプ(30c+e角、長さ5+n)を
設置し、そのパイプ内に蒸気を送り込み、70〜100
%R,Hの湿度とした。
5i (C2H50H)4, (CH3) at a given molar ratio
25i(C2H50H)2, water, IN-HCl and ethanol were mixed. The reaction was carried out at 30°C and 200cPo
Cool to 0℃ with ISE, and then cool to 600cPoise.
When the temperature reached -30°C, it was cooled. 1000c
When the poise was reached, spinning was performed by pressurizing with nitrogen gas using a nozzle with an inner diameter of 0.3 fins. Install a pipe (30c+e angle, length 5+n) under the nozzle, send steam into the pipe,
The humidity was %R,H.

採取した繊維状ゲルの断面形状を顕微鏡で観察を行ない
、偏平率を求めた。
The cross-sectional shape of the collected fibrous gel was observed under a microscope, and the oblateness was determined.

ここで、 偏平率(%)=100X(長径−短径)/長径である。here, Oblateness (%) = 100X (longer axis - shorter axis)/longer axis.

従って、偏平率が大きいほど偏平であり、偏平率が小さ
いほど真円になる。
Therefore, the larger the oblateness is, the flatter it is, and the smaller the oblateness is, the more perfectly round it is.

表1に、調合比、湿度と偏平率を示す。偏平率が、すべ
て30%以下であり、はぼ円形状の断面形状を有するこ
とが分かる。
Table 1 shows the blending ratio, humidity, and aspect ratio. It can be seen that the flatness ratios are all 30% or less, and the cross-sectional shape is approximately circular.

〔比較例〕[Comparative example]

実施例と同様の方法でゾルを作製し、パイプ中の湿度を
30〜55%R1Hとし、実施例と同じ方法で紡糸を行
った。得られた繊維状ゲルの断面の偏平率を調べた。調
合比、湿度及び偏平率を表1に示す。偏平率は、40%
を越えており、かなりの偏平状の断面である。
A sol was prepared in the same manner as in the example, the humidity in the pipe was set to 30 to 55% R1H, and spinning was performed in the same manner as in the example. The oblateness of the cross section of the obtained fibrous gel was examined. Table 1 shows the blending ratio, humidity, and aspect ratio. The flatness ratio is 40%
It has a fairly flat cross section.

〔発明の効果〕〔Effect of the invention〕

ゾル−ゲル法により作製した紡糸中の繊維状ゾルまたは
紡糸後の繊維状ゾルを、60〜100%RHの湿度の気
体に接触させることにより、はぼ円形状の断面形状のゲ
ルファイバーを得ることができた。
By contacting a fibrous sol during spinning or a fibrous sol after spinning produced by the sol-gel method with a gas having a humidity of 60 to 100% RH, a gel fiber having a roughly circular cross-sectional shape can be obtained. was completed.

Claims (1)

【特許請求の範囲】[Claims] (1)有機金属化合物の加水分解・重合によって得た粘
稠なゾル溶液から紡糸したゲル繊維を焼成することによ
り無機繊維を製造する方法において、該粘稠なゾル溶液
からの紡糸中または紡糸後の繊維状ゾルを、湿度を60
〜100%R.H.に維持した気体に接触させることを
特徴とする無機繊維の製造方法。
(1) In a method for producing inorganic fibers by firing gel fibers spun from a viscous sol solution obtained by hydrolysis/polymerization of an organometallic compound, during or after spinning from the viscous sol solution. of fibrous sol at a humidity of 60
~100%R. H. A method for producing inorganic fibers, characterized by contacting with a gas maintained at
JP16364790A 1990-06-21 1990-06-21 Production of inorganic fiber Pending JPH0455335A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16364790A JPH0455335A (en) 1990-06-21 1990-06-21 Production of inorganic fiber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16364790A JPH0455335A (en) 1990-06-21 1990-06-21 Production of inorganic fiber

Publications (1)

Publication Number Publication Date
JPH0455335A true JPH0455335A (en) 1992-02-24

Family

ID=15777921

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16364790A Pending JPH0455335A (en) 1990-06-21 1990-06-21 Production of inorganic fiber

Country Status (1)

Country Link
JP (1) JPH0455335A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009263802A (en) * 2008-04-23 2009-11-12 Shinshu Univ Method for producing inorganic fiber sheet

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009263802A (en) * 2008-04-23 2009-11-12 Shinshu Univ Method for producing inorganic fiber sheet

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