JPS5881618A - Preparation of potassium titanate fiber - Google Patents

Preparation of potassium titanate fiber

Info

Publication number
JPS5881618A
JPS5881618A JP17676881A JP17676881A JPS5881618A JP S5881618 A JPS5881618 A JP S5881618A JP 17676881 A JP17676881 A JP 17676881A JP 17676881 A JP17676881 A JP 17676881A JP S5881618 A JPS5881618 A JP S5881618A
Authority
JP
Japan
Prior art keywords
fibers
fiber
spinning
potassium titanate
solvent
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
JP17676881A
Other languages
Japanese (ja)
Inventor
Ishio Kato
加藤 石生
Satoshi Tsukamura
塚村 聡
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 Soda Co Ltd
Original Assignee
Nippon Soda 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 Soda Co Ltd filed Critical Nippon Soda Co Ltd
Priority to JP17676881A priority Critical patent/JPS5881618A/en
Publication of JPS5881618A publication Critical patent/JPS5881618A/en
Pending legal-status Critical Current

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  • Inorganic Compounds Of Heavy Metals (AREA)
  • Inorganic Fibers (AREA)

Abstract

PURPOSE:To obtain the titled fibers having uniform and improved properties with easy adjustment of the composition and thickness, by spinning a composite material obtained from a titanium alkoxide and potassium hydroxide as a raw material, and calcining the resultant fibers. CONSTITUTION:A titanium alkoxide of the formula Ti(OR)4[R is (cyclo)alkyl, alkenyl, etc.], e.g. tetraisopropoxytitanium, is reacted with potassium hydroxide in a solvent in an atmosphere of an inert gas at 50-300 deg.C, and the resultant reaction product is then dissolved in a solvent to give a spinning solution, which is then mixed with an organic high polymer, e.g. polyethylene oxide, a chelating agent, e.g. triethanolamine, etc. to adjust the viscosity, springiness, etc. thereof. The spinning solution is then spun to give precursor fibers, which are calcined in an atmosphere containing oxygen.

Description

【発明の詳細な説明】 本発明はチタン酸カリウム繊維の新規な製造方法に関し
、詳しくは、 一般式(1) Ti (OR)4  (式中Rは置換又
は非置換のアルキル基、アルケニル基、シクロアルキル
基もしくはアラルキル基の群から選ばれた1種又は2I
1以上の置換基を示す。)で表わされるチタンアル;キ
シド類と水酸化カリウムとを反応させて得られる複合体
を原料とし、これを紡糸して得られ九前駆体繊維を焼成
することを特徴とするチタン酸カリウム繊維の製造方法
に関すゐものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a novel method for producing potassium titanate fibers, and more specifically, the present invention relates to a novel method for producing potassium titanate fibers, and more specifically, the present invention relates to a novel method for producing potassium titanate fibers, and more specifically, it has the following formula: Ti(OR)4 (wherein R is a substituted or unsubstituted alkyl group, an alkenyl group, One or two selected from the group of cycloalkyl groups or aralkyl groups
Indicates one or more substituents. ) Production of potassium titanate fiber characterized by using a composite obtained by reacting titanium al; It's about the method.

チタン酸カリウム繊維としては四チタン酸カリウム繊維
及び六チタン酸カリウム繊維が一般に知られている。四
チタン酸カリウム繊維はT1−〇八面体の連結様式が層
状構造であp1層関のカリウムイオン社交換性に富んで
いることから、イオン交換材としての用途が期待されて
いる。六チタン酸カリウム繊維はT1−〇八面体の連結
様式がトンネル構造であり、トンネル中に存在するカリ
ウムイオンKti移動性がなく、赤外線反射率が高く、
熱伝導率が小さい大め、耐熱、断熱材として優れている
。ス耐sa性及び溶媒への親和性が大きいことなども併
せて、アスベストの代替繊維、各種複合強化用繊維環と
して期待されている。このようなチタン酸カリウム繊維
の製造法として社従来、焼成法、しかしながら、いずれ
の方法においても、得られる繊維の長さは1鋼以下の短
い単結晶繊維であシ、操作上においても、高圧であった
シ、有害ガス発生の危険をい等工業的に好ましい方法で
はなかった。
As potassium titanate fibers, potassium tetratitanate fibers and potassium hexatitanate fibers are generally known. Potassium tetratitanate fiber is expected to be used as an ion exchange material because it has a layered structure in which the T1-octahedrons are connected and has high exchangeability for potassium ions in the p1 layer. The potassium hexatitanate fiber has a tunnel structure in which the T1-octahedrons are connected, and there is no mobility of potassium ions Kti present in the tunnel, and the infrared reflectance is high.
It is large, has low thermal conductivity, and is excellent as a heat-resistant and insulating material. It is expected to be used as an alternative fiber for asbestos and as a fiber ring for reinforcing various composites due to its high sa-sa-resistance and high affinity for solvents. The conventional method for producing such potassium titanate fibers is the firing method.However, in either method, the length of the fiber obtained is short single crystal fiber of 1 steel or less, and high pressure is required for operation. However, it was not an industrially preferred method due to the risk of generating harmful gases.

本発明者らは、前記従来法にみられるような欠点のない
、しかも均一で優れた物性を有するチタン酸カリウム繊
維の製造方法について検討を重ね、本発明を完成した。
The present inventors have repeatedly studied a method for producing potassium titanate fibers that does not have the drawbacks seen in the conventional methods and has uniform and excellent physical properties, and have completed the present invention.

本発明の方法は前記一般式(I)で表わされるチタンア
ルコキシド類と水酸化カリウムとを有機溶媒の存在下も
しくは非存在下反応させて得られる複合体を原料とし、
これを紡糸して得られた前駆体繊維を焼成することによ
り、所望する組成のチタン酸カリウム長繊維を製造する
方法である。
The method of the present invention uses a composite obtained by reacting a titanium alkoxide represented by the general formula (I) with potassium hydroxide in the presence or absence of an organic solvent as a raw material,
This is a method for producing potassium titanate long fibers having a desired composition by firing the precursor fibers obtained by spinning the fibers.

本発明の方法においては、チタンアルコキシド類と水酸
化カリウムの混合比を変化させることによシ、安易に目
的繊維の組成を調節することができ、四チタン酸カリウ
ム繊維、六チタン酸カリウム繊維のみならず檀々の組成
を有するチタン酸カリウム繊維を製造することができる
。又、機械的に繊維化させるため、太さの調節も安易で
あり連続した長繊維を得ることができる。
In the method of the present invention, by changing the mixing ratio of titanium alkoxides and potassium hydroxide, the composition of the target fiber can be easily adjusted. It is possible to produce potassium titanate fibers having the same composition as above. Furthermore, since the fibers are mechanically formed, the thickness can be easily adjusted and continuous long fibers can be obtained.

本発明において用いられる前記一般式(1)で表わされ
るチタンアルコキシド類のRとしては、鎖状アルキル基
たとえばメチル基、エチル基、プルピル基、ブチル基、
ヘキシル基環、置換された鎖状アルキル基たとえば1.
4−ブタンジオール残基、グリコール類残基等OH基で
置換され九鎖状アルキル基、セロノル1残基轡OR/基
(こζにRIはC1〜C3のアルキル基を表す。)で置
換され九アルキル基、ハロゲン原子で置換され九アルキ
ル基岬、シクロアルキル基たとえばシクロヘキシル基、
1−メチルシクロペンチル基等、アリル基、りpチル基
勢の不飽和結合を有する置換基、およびアラルキル基九
とえばベンジル基、フェニルエチル基等の群から選ばれ
九11[の置換基本しくけ2種以上の置換基である。
R of the titanium alkoxide represented by the general formula (1) used in the present invention includes a chain alkyl group such as a methyl group, an ethyl group, a propyl group, a butyl group,
Hexyl ring, substituted chain alkyl group, e.g. 1.
4-butanediol residue, glycol residue, etc. substituted with an OH group and substituted with a nine-chain alkyl group, celonol 1 residue 轡OR / group (where RI represents a C1-C3 alkyl group) nine alkyl groups, nine alkyl groups substituted with halogen atoms, cycloalkyl groups such as cyclohexyl groups,
Substituents having an unsaturated bond such as 1-methylcyclopentyl group, allyl group, p-tyl group, and aralkyl group 9, such as benzyl group, phenylethyl group, etc. Two or more types of substituents.

また、本発WIj41ICおいて、Rはチタン酸塩とす
るためのハンドリングの仕様に応じ適宜選択することが
できるが、テトラブトキシチタン、テトライソプpボキ
シチタン、テトラブトキシチタン、ジエトキシージイソ
プ四ボキシチタン、ジェトキシ−ジブトキシチタン等の
鎖状アルコキシチタン類を用いるのが好ましく、特に工
業的に製造され入手し易いテトライソプpボキシチタン
およびテトラブトキシチタンを用いるのが望ましい。
In addition, in the present WIj41IC, R can be selected as appropriate depending on the handling specifications for making it into a titanate, but it can be selected from tetrabutoxytitanium, tetraisop-boxytitanium, tetrabutoxytitanium, diethoxydiisop-tetraboxytitanium, jetoxytitanium, etc. - It is preferable to use chain alkoxy titaniums such as dibutoxy titanium, and it is particularly preferable to use tetraisoprop-boxy titanium and tetrabutoxy titanium, which are industrially produced and easily available.

チタンアルコキシド類と水酸化カリウムとの反応は溶媒
の存在下、非存在下いずれでも進行するが、有機溶媒、
好ましくは非極性溶媒の存在下に行うことにより、反応
が温和に進行して有利である。溶媒としては、生成する
複合体を溶解する亀のならは何でもよく、芳香族、脂肪
族−炭化水素類、そのハロゲン化物等が用いられる。ア
ルコール類は、生成複合体の置換基の置換反応を伴う場
合があるので、置換基の一部又は全部の置換を所望する
場合に使用するのが好ましい。又、反応の進行に伴って
脱離してくるアルコールを系外に排除する場合には該ア
ルコールの沸点よシ高沸点を有する有機溶媒を用いる仁
とができる。
The reaction between titanium alkoxides and potassium hydroxide proceeds in the presence or absence of a solvent, but organic solvents,
Preferably, the reaction is carried out in the presence of a nonpolar solvent, which is advantageous because the reaction proceeds mildly. Any solvent may be used as long as it dissolves the complex to be produced, and aromatic and aliphatic hydrocarbons, halides thereof, and the like are used. Since alcohols may involve a substitution reaction of substituents in the resulting complex, they are preferably used when it is desired to substitute some or all of the substituents. Furthermore, when the alcohol that is eliminated as the reaction progresses is to be removed from the system, an organic solvent having a boiling point higher than that of the alcohol can be used.

この反応は、有機溶剤の存在下ま九は非存在下において
行なわれるが、加水分解反応の防止および炭酸ガスの混
入による辰酸塩の生成を防止するため、N2ガス、アル
ゴンガス等の不活性ガス雰囲気下、もしくは生成するア
ルコールまた社使用する有機溶剤の蒸気雰囲気下に行う
This reaction is carried out in the presence or absence of an organic solvent, but in order to prevent the hydrolysis reaction and the formation of taurate due to the incorporation of carbon dioxide gas, inert gas such as N2 gas or argon gas is used. It is carried out under a gas atmosphere or under a vapor atmosphere of the alcohol produced or the organic solvent used.

反応温度および反応時間は原料の11[頽、有機溶剤を
使用する場合はその種類等によって変化させることがで
きるが、一般的には50〜300℃、好ましくは50〜
250℃の反応温度であシ、0.5〜60時間、好まし
くは1〜15時間の反応時間である。さらに好ましい態
様は有機溶剤の還流下に1−5時間、反応を行う。
The reaction temperature and reaction time can be changed depending on the temperature of the raw materials, the type of organic solvent used, etc., but generally 50-300°C, preferably 50-300°C.
The reaction temperature is 250° C. and the reaction time is 0.5 to 60 hours, preferably 1 to 15 hours. In a more preferred embodiment, the reaction is carried out under reflux of an organic solvent for 1 to 5 hours.

生成する複合体はベンゼン、トルエン、キシレン、アル
コール類等の有機溶媒に可溶であり、追歯な鹸度では曳
糸性に富む粘稠な溶液となる。この濃度と曳糸性との関
係は用いられる複合体の種類、その重合度および溶媒に
よって異なるが、一般に意温での粘度が1〜5000ボ
イズの範囲である溶液が紡糸には適幽である。紡糸原液
の粘度調節、曳糸性向上のため、少量のポリエチレング
リコール、ポリビニルアルコール、ポリ酢酸ビニル、ヒ
ドロキシグロビルセルロース勢の有機高分子を添加して
もよい。
The resulting complex is soluble in organic solvents such as benzene, toluene, xylene, alcohols, etc., and becomes a viscous solution with excellent stringiness at high saponification. The relationship between this concentration and spinnability varies depending on the type of composite used, its degree of polymerization, and the solvent, but generally a solution with a viscosity in the range of 1 to 5,000 voids at room temperature is suitable for spinning. . In order to adjust the viscosity of the spinning dope and improve the spinnability, a small amount of an organic polymer such as polyethylene glycol, polyvinyl alcohol, polyvinyl acetate, or hydroxyglobil cellulose may be added.

又、前記複合体を安定化させることにより、加水分解の
速度調節を行うため、伴せて粘度、曳糸性の調節を行う
ため、キレート化剤を添加してもよい。キレート化剤と
は1分子内に同時に2つ以上の官能基を有する化合唆で
その官能基と社、水酸基、アミノ基、カルボニル基であ
る。例えば、アセチルアセトン、ベンゾイルアセトンな
どのβ−ジケトン類、アセト酢酸、プロヒオニル酪酸、
ベンゾイル酢酸、アセチルギ酸、ベンゾイルギ酸などの
a−またはβ−ケトン酸類、該ケトン酸類のメチル、エ
チル、プロピル、ブチルなどのエステル類、グリコール
酸、乳酸、a−オキシ酪酸、ヒドロアクリル酸、サリチ
ル酸などのa−またはβ−オキシ#類、ea−またはβ
−オキシ酸類のメチル、エチル、プロピル、ブチルなど
のエステル類、ジアセトンアルコール、アセトインなど
のa−またはβ−オキシケトン−、グリコールアルデヒ
ド、アルドールなどのa−jたはβ−オキジアルデヒド
類、グリシン、アラニ/などのα−アンノ酸類、アミノ
エチルアルコールなどのa−またはβ−アミノアルコー
ル類である。
In addition, a chelating agent may be added to stabilize the composite to control the rate of hydrolysis, and also to control the viscosity and stringiness. A chelating agent is a compound having two or more functional groups in one molecule, and the functional groups include a hydroxyl group, an amino group, and a carbonyl group. For example, β-diketones such as acetylacetone and benzoylacetone, acetoacetic acid, prohionylbutyric acid,
a- or β-ketone acids such as benzoylacetic acid, acetylformic acid, benzoylformic acid, esters of the ketone acids such as methyl, ethyl, propyl, butyl, glycolic acid, lactic acid, a-oxybutyric acid, hydroacrylic acid, salicylic acid, etc. a- or β-oxy #s, ea- or β
- Esters of oxyacids such as methyl, ethyl, propyl, butyl, a- or β-oxyketones such as diacetone alcohol and acetoin, a-j or β-oxydialdehydes such as glycolaldehyde and aldol, glycine , arani/, etc., and a- or β-amino alcohols such as aminoethyl alcohol.

一般式(1)とキレート化剤との反応条件は、加水分解
中炭酸ガスによる炭酸塩の生成を避けるため、 12ガ
ス、アルゴンガスなどの不活性ガス雰囲気下、又は生成
するアルプールもしく杜使用する有機溶剤のガス雰囲気
下に行い、空気中の水分子炭酸ガスの混入のない状態で
行うことが好ましい。反応温度、反応時間祉、複合オキ
ジアルコキシドやキレート化剤および有機溶剤を使用す
る場合はそのIl類、量に依存して変化させることがで
きるが、一般的に拡O〜300℃好ましくは20〜25
0℃で、o、s〜10時間好オしくは1〜5時間である
。更に、前駆体繊維中に泡が入るのを紡ぐため、必要に
応じて少量の脱泡剤を添加してもよい。又、分加水分岬
することによシ、高品位のチタン酸カリウム繊維を得る
ことができる。水の添加方法としては、直接水を添加し
ても、有機溶媒に溶解させて添加しても又、放置するこ
とKよシ空気中の水分を吸収させてもよい。壕九、曳糸
工程中の任意の段階で空気中の水分及び/又は二酸化炭
素を吸収させてもよい。
The reaction conditions for the general formula (1) and the chelating agent are under an inert gas atmosphere such as 12 gas or argon gas, or using Alpur or Mori to avoid the formation of carbonate due to carbon dioxide gas during hydrolysis. It is preferable to carry out the reaction under a gas atmosphere of an organic solvent, without mixing water molecules and carbon dioxide gas in the air. Although it can be changed depending on the reaction temperature, reaction time, and the amount of compound oxydialkoxide, chelating agent, and organic solvent used, the reaction temperature is generally 0 to 300°C, preferably 20°C. ~25
At 0° C., the time is from 1 to 10 hours, preferably from 1 to 5 hours. Additionally, a small amount of defoaming agent may be added as needed to prevent foam from entering the precursor fibers. In addition, high-grade potassium titanate fibers can be obtained by partial hydrolysis. As for the method of adding water, water may be added directly, water may be added by dissolving it in an organic solvent, or water may be left to stand and moisture in the air may be absorbed. Moisture and/or carbon dioxide in the air may be absorbed at any stage during the stringing process.

上記の如くして調製された紡糸原液から、紡糸を行うに
は、乾式紡糸が好ましいが、遠心紡糸、吹き出し紡糸等
の他の追歯な紡糸方法に従ってもよい。紡糸温度は室温
で行えるが必要に応じて、紡糸液を加熱してもよく、1
0〜100℃、好ましくは、20〜60℃である。又紡
糸雰囲気は空気算囲気で充分であるが、必要に応じて不
活性ガスを用いたり、不活性ガス又は空気中の水分もし
くはC02゛濃度を調整することも好結果を得るためK
]iit L、いことである。
To perform spinning from the spinning dope prepared as described above, dry spinning is preferred, but other spinning methods such as centrifugal spinning and blow-spinning may also be used. Although spinning can be carried out at room temperature, the spinning solution may be heated if necessary.
The temperature is 0 to 100°C, preferably 20 to 60°C. In addition, an air environment is sufficient for the spinning atmosphere, but if necessary, it is also possible to use an inert gas or adjust the moisture or CO2 concentration in the inert gas or air to obtain good results.
]iit L, it's bad.

紡糸された繊維に含まれる溶媒の乾燥は、空気中室温で
自然乾燥させれば充分であるが、赤外@2ンプ等で乾燥
させてもよい。
It is sufficient to dry the solvent contained in the spun fibers by naturally drying them in air at room temperature, but they may also be dried using an infrared @2 pump or the like.

本発明に於けるチタン酸カリウム繊維前駆体は熱に対し
て不融であシ、そのtま空気等の酸素を含む雰囲気中で
焼成すれば、繊維の形態をくずす仁となく、チタン酸カ
リウム繊維とすることができる。すなわち、前駆体繊維
を酸素を含む雰囲気、例えば空気中で焼成すれば約80
0℃において実質的にチタン酸カリウム繊維に変化する
。それに豐する保持時間は約10分根度であるが、好ま
しくは1時間以上である。又各種チタン酸カリウム繊維
を得るために、骸前駆体繊維を窒素のような不活性雰囲
気中、あるいは真空中で焼成した後、酸素を含む雰囲気
にさらして、有機質あるいは炭素質を除去してもよい。
The potassium titanate fiber precursor in the present invention is infusible to heat, and when fired in an atmosphere containing oxygen such as air, the potassium titanate fiber precursor It can be a fiber. That is, if the precursor fiber is fired in an oxygen-containing atmosphere, for example, in air, the
At 0°C, it substantially changes to potassium titanate fiber. The holding time involved is about 10 minutes, but preferably one hour or more. In addition, in order to obtain various potassium titanate fibers, the skeleton precursor fibers may be fired in an inert atmosphere such as nitrogen or in a vacuum, and then exposed to an oxygen-containing atmosphere to remove organic or carbonaceous substances. good.

又、得られたチタン酸カリウム繊維を水素のような還元
性雰囲気中で東に焼成することは、チタン酸カリウム繊
維の緒物性向上の丸めに望ましい仁とである。i九、こ
れらの焼成工程中、前駆体繊維あるいはチタン酸カリウ
ム繊維に張力を力11ておくことは、強いチタン酸カリ
ウム繊維を製造するために望ましいことである。
Further, firing the obtained potassium titanate fiber in a reducing atmosphere such as hydrogen is desirable for rounding the potassium titanate fiber to improve its physical properties. 9. During these firing steps, it is desirable to maintain a tension of 11 in the precursor fiber or potassium titanate fiber in order to produce strong potassium titanate fiber.

本発明においては、チタンアルコキシド類と水酸化カリ
ウムの混合比を変化させることにより、簡単に目的繊維
の組成を調部することができ、四チタン酸カリウム繊維
、六チタン酸カリウム繊維のみならず種々の組成を有す
るチタン酸カリウム繊維を製造することt電できる。機
械的に繊維化させるため、所望の太さの連続した長繊維
を得ることができ、工業的に連続大量生産が可能で参る
。又、焼結、結晶化に要する温度と時間だけで良いため
、低温で短時間で焼成カ監できる。更に原料が溶液であ
るので第3成分の均−添力0力(容易であるO 以下に実施例を挙げて本発明を更に詳しく説明する。
In the present invention, by changing the mixing ratio of titanium alkoxides and potassium hydroxide, the composition of the target fiber can be easily adjusted. It is possible to produce potassium titanate fibers having the composition: Since fiberization is performed mechanically, continuous long fibers of a desired thickness can be obtained, making continuous mass production possible on an industrial scale. Furthermore, since only the temperature and time required for sintering and crystallization are required, firing can be supervised at low temperatures and in a short time. Further, since the raw material is a solution, the third component has an equalizing force of 0 (0).

1−Pr=(CH3)2CH(イングロビル基)、−B
u=CH! (CH2)S (%−ブチル基)!I施例
1.  、 還流冷却器、攪拌機および温度針を取付けた50G!+
1J14つ目フラスコにTi (01−Pr)i / 
1G4.1 f(0,366fflOA)>、tびイソ
プロパ/−ル(1−ProH) 60.Ofを仕込み、
N2ガス雰囲気下80℃に加熱しその温度を維持しなが
ら、この中にkOH# 6.9 f (0,123m0
A )とメタノール(CH30M)9G、Ofとよシな
る溶液を1時間にわたシ滴下し、その後溶剤を5時間に
わたシ還流せしめ均一な反応液を得九。得られた反応液
から、浴剤の沸点以上の温度で溶剤の一部を留出せしめ
、最終酸化物(1(2Ti60ts)として25.4重
量−の均一溶液を137.8F得、これを紡糸原液とし
た。紡糸原液にト’)−1−1/−ル7ミy (N (
D・H2CH20H)s)J2B、Of (0,168
!1101)を加え30分間還流せしめ先後、これに平
均分子量830万ないし380万のポリエチレンオキサ
イドを約o、oyr添加し混合攪拌した均一溶液な脱泡
後11100#o紡糸金口よ〕押し出し吐出される繊維
を空気中基量で乾燥しながら60%/分の巻き取シ速度
で巻き取りた。得られた前駆体繊維はそovhが16μ
で空気中に放置しても全く安定でありた。この繊維を室
温よp 1250℃まで昇温速度300℃/時間で、空
気中にて焼成したところに2テ16013繊維が得られ
九〇この繊維の!−回折図を第1図に示した。
1-Pr=(CH3)2CH (inglovir group), -B
u=CH! (CH2)S (%-butyl group)! I Example 1. , 50G with reflux condenser, stirrer and temperature needle installed! +
1J 14th flask with Ti (01-Pr)i /
1G4.1 f(0,366fflOA)>, t and isopropyl(1-ProH) 60. Prepare Of,
While heating to 80℃ under N2 gas atmosphere and maintaining that temperature, kOH# 6.9f (0,123m0
A solution of A) and 9G of methanol (CH30M) was added dropwise over 1 hour, and then the solvent was refluxed for 5 hours to obtain a homogeneous reaction solution. Part of the solvent was distilled off from the resulting reaction solution at a temperature higher than the boiling point of the bath agent to obtain a homogeneous solution of 137.8F with a weight of 25.4 as the final oxide (1(2Ti60ts)), which was then spun. It was made into a stock solution.T')-1-1/-7 milliy (N (
D・H2CH20H)s)J2B,Of (0,168
! 1101) and refluxed for 30 minutes. After that, about 0.00000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000000012 2222 20233642 20 refluxing solution addition of polyethylene oxide solution having an average molecular weight of 8.3 million to 3.8 million, we mixed and stirred it to form a homogeneous solution, which was defoamed and then extruded and discharged through a 11100 #o spinneret. The fibers were wound at a winding speed of 60%/min while drying in air. The obtained precursor fiber has an ovh of 16μ
It was completely stable even when left in air. When this fiber was fired in air at a heating rate of 300°C/hour from room temperature to 1250°C, 2 16013 fibers were obtained and 90 of these fibers were obtained! -The diffraction diagram is shown in Figure 1.

1M施例2゜ 実施例1と同一の装置KTi (Ol−Pr)4 /1
04.1 f(0,3661nJ)およびイソプルパノ
ール(1−PrOH)60、Ofを仕込み勤ガス雰囲気
下80u&lC加熱し、その温度を維持しながらこの中
K koa 76.9 r(o、tzamol)とメタ
ノ−# (CH5OH)  ノ9G、Ofとよりなる溶
液を1時間にわた〕滴下しこれをS時間にわたシ遺流せ
しめた後OR基を全て置換するのに充分な量の鴨−ブタ
ノール(%−BuOH)150fを1時間にわ九り滴下
せしめ3時間の還流を行い均一な反応液を得九。
1M Example 2゜ Same device as Example 1 KTi (Ol-Pr) 4/1
04.1 f (0,3661 nJ) and isopropanol (1-PrOH) 60, Of were heated at 80 u&lC under a gas atmosphere, and while maintaining the temperature, K koa 76.9 r (o, tzamol) and methano A solution consisting of -# (CH5OH) 9G, Of was added dropwise over a period of 1 hour and left to stand for a period of S, and then a sufficient amount of duck-butanol (% -BuOH) was added dropwise over an hour and refluxed for 3 hours to obtain a homogeneous reaction solution.

得られ九反応液から、溶剤の沸点以上の温度で溶剤の一
部を留出せしめ最終酸化物(4zTi6015)として
25.0重量−の均一溶液を140.(HF得、これを
紡糸原液とした。紡糸原液中のR基は全てブチル基であ
シ、また溶剤は全てブタノールであることを確認した。
Part of the solvent was distilled off from the resulting reaction solution at a temperature above the boiling point of the solvent to obtain a final oxide (4zTi6015) of a homogeneous solution weighing 25.0% by weight. (HF was obtained, and this was used as a spinning stock solution. It was confirmed that all R groups in the spinning stock solution were butyl groups, and that all the solvents were butanol.

この紡糸原液に平均分子量330万ないし380万の一
すエチレンオキサイドを約0.11f添加し混合攪拌し
九均−溶液を脱泡後1120Gμの紡糸金目よ)押し出
し吐出される繊維を空気中室温で乾燥しなから50”7
分の巻き取り速度で巻き取った。得られた前駆体繊維は
その径が30μで空気中に放置しても安定でありた。こ
の繊維を室温より1250’C’tで昇温速度300’
C/時間で空気中にて焼成したところに2Tuo1s繊
維が得られ友。
Approximately 0.11 f of ethylene oxide with an average molecular weight of 3.3 to 3.8 million is added to this spinning stock solution, mixed and stirred, and after defoaming the solution, a spinning material of 1120 Gμ is extruded and the discharged fiber is heated in air at room temperature. Not dry 50”7
It was wound at a winding speed of 1 minute. The obtained precursor fiber had a diameter of 30 μm and was stable even when left in air. This fiber was heated from room temperature to 1250'C't at a heating rate of 300'.
When fired in air at C/hour, 2Tuols fibers were obtained.

この繊維のx11回折図は第1図と同様であった。The x11 diffraction pattern of this fiber was similar to that in FIG.

実施例3゜ 実施例2で得られた紡糸原液に乳酸CH5CH(IH)
(C(N!!H) 30.2 f t(,0,336m
on )を加え、30分間還流せしめた後、これに平均
分子量330万ないし380万のポリエチレンオキサイ
ドを約0.11f添加し、混合攪拌した均一溶液を脱泡
後、11100μの紡糸金目よシ押し出し、吐出されt
繊維を空気中赤外線ランプで乾燥しながら50m/分の
巻き取シ速度で巻き取った。
Example 3゜Lactic acid CH5CH (IH) was added to the spinning stock solution obtained in Example 2.
(C(N!!H) 30.2 ft(,0,336m
on) and refluxed for 30 minutes, about 0.11 f of polyethylene oxide with an average molecular weight of 3.3 million to 3.8 million was added thereto, the mixed and stirred homogeneous solution was defoamed, and then extruded into a 11,100-μ spinning wire. Discharged t
The fibers were wound up at a winding speed of 50 m/min while drying in air with an infrared lamp.

得られ大前駆体繊維はその径が14μで空気中に放置し
ても全く安定であう九。この繊維を室温よシ800℃t
で外電速度り00℃/時間で空気中にて焼成したとコロ
に2Ti6(Ha織繊維得られた。この繊維の!線回折
図は81図と同様であり九〇 実施例4゜ 還流冷却器、攪拌機および温度針を取付けた200m1
11’4 ツ口79 x *にTi (Os−Bu)4
 / 36.6 t (0,105moj ) kOH
l 2.Of (0,0HIIIOj)Th!ヒ’p−
dtシVン4G、Ofを仕込み、12ガス雰囲気下3時
間還流せしめ均一な反応液を得九〇得られた反応液から
溶剤の沸点以上O温度で溶剤の一部を留出せしめ最終酸
化物(k2Ti6(Us )’として20.6重量−の
均一溶液を48.8V得、これを紡糸原液としえ。紡糸
原液にアセチルアセトy (cnacocnzcocn
s) 9.6 f C0,096w1o1>を加え80
分間還流せしめ先後、これに平均分子量330万ないし
380万のポリエチレンオキサイドを約0゜021添加
し、混合攪拌し九均−溶液を脱泡後後100; μの紡糸金目よシ押し出し、吐出され木繊維を空気中赤
外線ランプで乾燥しながら巻き取シ速度50 m1分で
巻き取った。得られた前駆体繊維はその径が13μで空
気中に放電して屯全く安定であった。この繊維を室温よ
シフ00℃まで昇温速度200 ℃/待時間脅素中にて
焼成し次にこの温度で雰囲気を空気に置換したのち、引
き続き1000℃壕で焼成したところに2Ti601a
繊維が得られた。この繊維のX線回折図は第1図と同様
であった。
The large precursor fiber obtained has a diameter of 14 μm and is completely stable even when left in air. This fiber was heated to room temperature at 800°C.
2Ti6 (Ha) woven fibers were obtained by firing in air at an external heating rate of 00°C/hour. , 200m1 fitted with stirrer and temperature needle
11'4 Tsuguchi 79 x *Ti (Os-Bu)4
/ 36.6 t (0,105 moj) kOH
l 2. Of (0,0HIIIOj)Th! Hi'p-
A homogeneous reaction solution was obtained by refluxing for 3 hours in a 12 gas atmosphere.90 Part of the solvent was distilled off from the obtained reaction solution at a temperature above the boiling point of the solvent to obtain the final oxide. A homogeneous solution of 20.6 weight as (k2Ti6(Us)') was obtained at 48.8V and used as a spinning stock solution.Acetylacetoy (cnacocnzcocn) was added to the spinning stock solution.
s) Add 9.6 f C0,096w1o1> and 80
After refluxing for a minute, polyethylene oxide with an average molecular weight of 3.3 million to 3.8 million was added to this, mixed and stirred. The fibers were wound up at a winding speed of 50 ml/min while drying in air with an infrared lamp. The obtained precursor fiber had a diameter of 13 μm and was completely stable when discharged into air. This fiber was fired in an atmosphere with a temperature increase rate of 200 °C/waiting time from room temperature to 00 °C, then the atmosphere was replaced with air at this temperature, and then fired in a trench at 1000 °C.
Fibers were obtained. The X-ray diffraction pattern of this fiber was similar to that shown in FIG.

実施例5゜ 実施例4と同一の装置1(Ti (Ol−Pr)4/ 
27.15 f(0,097m0jl ) kOH2,
7? (0,048m0A )およびベンゼy40.O
fを仕込み勤ガス雰囲気下3時間還流せしめ、均一な反
応液を得た。得られた反応液から溶剤の沸点以上の温度
で溶剤の一部を留出せしめ最終酸化物(K2Ti40t
 )として3G、0重量−の均一溶液を38.3F得、
これを紡糸原液とし九〇紡糸原液にトリエタノ−にアt
 7 (N CcHzcytoH)s ) 6.3 t
 (0,041mo羞)を加え30分間還流せしめた均
一、i液を脱泡後、vk100μの紡糸金目よシ押し出
し吐出された繊維を空気中室温で乾燥しながら50m/
分の巻11取シ速度で巻き取りた。得られ先割躯体繊維
はその径が18μで空気中に放置しても全く安定であっ
た。この繊維を富温よシ1oso’ctで昇温速度30
0℃/時間で空気中にて焼成したところにxT1a09
繊維が得られた。この繊維のX線回折図を第2図に示し
た。
Example 5゜Same device 1 as Example 4 (Ti (Ol-Pr) 4/
27.15 f(0,097 m0jl) kOH2,
7? (0,048m0A) and benzene y40. O
f was charged and refluxed for 3 hours under a gas atmosphere to obtain a homogeneous reaction solution. Part of the solvent was distilled from the resulting reaction solution at a temperature higher than the boiling point of the solvent to obtain the final oxide (K2Ti40t
), a homogeneous solution of 3G, 0 wt- was obtained at 38.3F,
Use this as a spinning stock solution and add it to triethanol to add to the spinning stock solution.
7 (N CcHzcytoH)s ) 6.3 t
(0,041 mo) was added and refluxed for 30 minutes. After degassing the i-liquid, extrude it through a vk100μ spinning wire and extrude the discharged fibers, drying them in the air at room temperature.
The winding speed was 11 minutes. The obtained pre-split fibers had a diameter of 18 μm and were completely stable even when left in air. This fiber is heated to 1 oso'ct at a heating rate of 30
xT1a09 after baking in air at 0°C/hour
Fibers were obtained. The X-ray diffraction pattern of this fiber is shown in FIG.

実施例6゜ 実施例5で得られ九紡糸原液にトリエタノールアミン□
i (CHzCHzOH)s) 6.3 ? (0,0
42110幻を加え、30分間還流せしめた俵、これに
平均分子量330万〜380万のポリエチレンオキサイ
ドを約0.02F橋加し混食攪拌した均一溶液を空気中
に放置し部分加水分解して脱泡後、径100μの紡糸金
目よシ押し出し吐出された繊維を空気中赤外線ランプで
乾燥しながら50m/分の巻き取シ速度で巻き取った。
Example 6゜ Triethanolamine □ was added to the spinning stock solution obtained in Example 5.
i (CHzCHzOH)s) 6.3? (0,0
A homogeneous solution of polyethylene oxide with an average molecular weight of 3.3 million to 3.8 million cross-linked at about 0.02F and mixed with stirring was left in the air to undergo partial hydrolysis and decomposition. After foaming, the extruded fibers were extruded through a spinning wire having a diameter of 100 μm, and the discharged fibers were wound up at a winding speed of 50 m/min while drying with an infrared lamp in the air.

得られた前駆体繊維はその径が19μで空気中に放置し
ても全く安定であった。この繊維を富温よ6soo℃ま
で昇温速度300℃/時間で空気中にて焼成したところ
に2Ttaog繊維が得られた。この繊維のX11回折
図は第2図と同様であった。
The obtained precursor fiber had a diameter of 19 μm and was completely stable even when left in air. This fiber was fired in air at a heating rate of 300°C/hour to a temperature of 6soo°C, yielding 2Ttaog fiber. The X11 diffraction pattern of this fiber was similar to that in FIG.

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

第1図 実施例1で得られたkz、T1601i緻繍の
X線回折図。 第fll  実施例5で得られ九に!〒140!繊維の
X線回折図。 出願人日本璽達株式金社 代理人伊藤晴之 横山吉美
FIG. 1 An X-ray diffraction diagram of the kz, T1601i embroidery obtained in Example 1. No. 9 obtained in Example 5! 〒140! X-ray diffraction diagram of fiber. Applicant Nippon Shodatsu Co., Ltd. Agent Haruyuki Ito Yoshimi Yokoyama

Claims (1)

【特許請求の範囲】[Claims] 1、一般式Ti(OR)4(式中Rは置換又は非置換の
アルキル基、アルケニル基、シクロアルキル基、もしく
はアラルキル基の評から選ばれた1種もしくは2種以上
の置換基を示す。)で表わされるチタンアルコキシド類
と水酸化カリウムとを反応させて得られる複合体を原料
とし、これを紡糸して得られた前駆体繊維を焼成するこ
とを特徴とするチタン酸カリウム繊維の製造方法。
1. General formula Ti(OR)4 (wherein R represents one or more substituents selected from a substituted or unsubstituted alkyl group, alkenyl group, cycloalkyl group, or aralkyl group). ) A method for producing potassium titanate fibers, which comprises using as a raw material a composite obtained by reacting titanium alkoxides and potassium hydroxide, and firing a precursor fiber obtained by spinning the same. .
JP17676881A 1981-11-04 1981-11-04 Preparation of potassium titanate fiber Pending JPS5881618A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17676881A JPS5881618A (en) 1981-11-04 1981-11-04 Preparation of potassium titanate fiber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17676881A JPS5881618A (en) 1981-11-04 1981-11-04 Preparation of potassium titanate fiber

Publications (1)

Publication Number Publication Date
JPS5881618A true JPS5881618A (en) 1983-05-17

Family

ID=16019477

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17676881A Pending JPS5881618A (en) 1981-11-04 1981-11-04 Preparation of potassium titanate fiber

Country Status (1)

Country Link
JP (1) JPS5881618A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61167017A (en) * 1985-01-14 1986-07-28 Otsuka Chem Co Ltd Production of conductive fiber of alkali titanate
JP2012012248A (en) * 2010-06-30 2012-01-19 Kubota Corp Lithium titanium complex oxide, method for producing the same, and lithium ion secondary battery using the same
JP2012167007A (en) * 2012-03-21 2012-09-06 Kubota Corp Potassium tetratitanate and hydrated tetratitanate compound

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61167017A (en) * 1985-01-14 1986-07-28 Otsuka Chem Co Ltd Production of conductive fiber of alkali titanate
JP2012012248A (en) * 2010-06-30 2012-01-19 Kubota Corp Lithium titanium complex oxide, method for producing the same, and lithium ion secondary battery using the same
JP2012167007A (en) * 2012-03-21 2012-09-06 Kubota Corp Potassium tetratitanate and hydrated tetratitanate compound

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