JPS60246815A - Production of inorganic oxide fiber - Google Patents

Production of inorganic oxide fiber

Info

Publication number
JPS60246815A
JPS60246815A JP10193684A JP10193684A JPS60246815A JP S60246815 A JPS60246815 A JP S60246815A JP 10193684 A JP10193684 A JP 10193684A JP 10193684 A JP10193684 A JP 10193684A JP S60246815 A JPS60246815 A JP S60246815A
Authority
JP
Japan
Prior art keywords
spinning
fibers
acid
aluminum chloride
solution
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.)
Granted
Application number
JP10193684A
Other languages
Japanese (ja)
Other versions
JPS6227164B2 (en
Inventor
Akira Yamane
山根 昭
Shizuo Tomiyasu
静夫 富安
Takeshi Nakamura
武 中村
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.)
TOYO SUTOUFUAA CHEM KK
Tosoh Finechem Corp
Original Assignee
TOYO SUTOUFUAA CHEM KK
Tosoh Finechem Corp
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 TOYO SUTOUFUAA CHEM KK, Tosoh Finechem Corp filed Critical TOYO SUTOUFUAA CHEM KK
Priority to JP10193684A priority Critical patent/JPS60246815A/en
Publication of JPS60246815A publication Critical patent/JPS60246815A/en
Publication of JPS6227164B2 publication Critical patent/JPS6227164B2/ja
Granted legal-status Critical Current

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  • Inorganic Fibers (AREA)

Abstract

PURPOSE:To obtain the titled fibers having fire resistance and flexibility, by mixing basic aluminum chloride with an organic acid containing alkoxyl group in the backbone of an aliphatic carboxylic acid to prepare a spinning solution having a specific viscosity, and spinning the resultant spinning solution. CONSTITUTION:A spinning solution containing basic aluminum chloride and further a fiber-consisting material, e.g. a silicic acid ester, convertible into a metal oxide other than alumina by firing oxidation treatment in an electric furnace added thereto is added and mixed with an organic acid containing alkoxyl group in the backbone of an aliphatic monocarboxylic acid, e.g. beta-ethoxypropionic acid, and the resultant mixture solution is then concentrated under heating to prepare a spinning dope having >=1 poise, preferably >=60 poises viscosity at room temperature. The resultant spinning dope is then spun to form precursor fibers, which are then fired and oxidized to afford the aimed fibers.

Description

【発明の詳細な説明】 A、産業上の利用分野 本発明は無機質酸化物ramの製造方法に関プる1、更
に詳しくは塩基性塩化アルミニウムを紡糸原料とする無
機質酸化物繊維の製造法の改良であって塩基性塩化アル
ミニウムあるいはこれに焼成酸化処理によりアルミナ以
外の金属酸化物を与える繊維構成物質を加えたものに、
脂肪族モノカルボン酸の主鎖にアルコキシル基を含む有
機酸を加えた混合液を、加熱濃縮して紡糸原液とし1=
後、これを紡糸して得られる前駆体繊維を焼成酸化処理
することにより、1500℃あるいはそれ以上の温度に
おいCも、非常に高い機械的強度、並びに優れた熱安定
性を有づる、無Ill質酸化物繊維の製造り法に関する
ものである。
DETAILED DESCRIPTION OF THE INVENTION A. Industrial Application Field The present invention relates to a method for producing inorganic oxide ram (1), more specifically, a method for producing inorganic oxide fiber using basic aluminum chloride as a spinning raw material. As an improvement, basic aluminum chloride or a fiber constituent material that gives a metal oxide other than alumina by baking oxidation treatment is added to it.
A mixed solution in which an organic acid containing an alkoxyl group is added to the main chain of an aliphatic monocarboxylic acid is heated and concentrated to obtain a spinning stock solution 1=
After that, by firing and oxidizing the precursor fiber obtained by spinning this, it is possible to create a carbon-free fiber that has extremely high mechanical strength and excellent thermal stability at temperatures of 1500°C or higher. The present invention relates to a method for producing quality oxide fibers.

己、従来の技術 近年、引張り強度あるいは°εジlラス等の機械的強度
および耐熱性のより優れた複合1用強化材の開発が各産
業分野から要望されるようになってきた。それら新規複
合祠料用強化月として各種の強化用繊維が知られでいる
BACKGROUND OF THE INVENTION In recent years, there has been a demand from various industrial fields for the development of reinforcing materials for composite materials having superior mechanical strength such as tensile strength or °ε girlas and heat resistance. Various reinforcing fibers are known as reinforcing fibers for these new composite abrasive materials.

例えばアルミノ、ジルコニア、チタニア、窒化ホウ素繊
維等のような多結晶1N紺、タングステン、モリブデン
、鋼、ベリリウムsun等の金属繊維、更にホウ素、シ
リ−】ンカーバイド、ボ11ンカーハイト繊緒の如くの
多相繊維等が次々と開発されCいる。
For example, polycrystalline 1N navy blue fibers such as alumino, zirconia, titania, boron nitride fibers, metal fibers such as tungsten, molybdenum, steel, beryllium sun, etc., and polycrystalline fibers such as boron, silicon carbide, boron carbide fibers, etc. Phase fibers and the like are being developed one after another.

これらの中でアルミプu&紺は他の諸繊維と比較して優
れIこ特徴を有している。まず、アルミナ繊維はその融
点(2040℃)が高いことにより超高温度域ひ使用可
能であり、高温酸化雰囲気中でも安定し7.: m械的
特性を保持づることが出来るのに対し、炭素繊維や金属
繊維等は上記雰囲気中では酸化を受(プ、脆化すること
により著しく機械的強度が低下りる。またガラスFI&
維は引張り強度は高いものの軟化点が低いので高温では
使用できないという致命的欠点であることから、複合材
料用強化材として使用する場合、各種のウィスカーおよ
び廿ラミック耐火繊維のような短繊維状と異なり、繊維
径に対する繊維長の比(アスペクト比)が大きくとれる
こと、また望む方向に繊維を配向でき、最適設訓が可能
である等の特徴を持っている。アルミニウムはこのよう
に他にあまり例のない優れた性質を具備しているので、
各様の繊維強化複合月利、例えば代表的なものどしくア
ルミナ繊維を各種プラスデックと混合してアルミツー−
繊維強化プラスチックどしたりあるいはアルミニウムを
初めとする各種金属と混合してアルミJU&維強化金属
とし−(使用され始めている。。
Among these, aluminum fibers and navy blue have superior characteristics compared to other fibers. First, alumina fibers have a high melting point (2040°C), so they can be used in ultra-high temperatures, and are stable even in high-temperature oxidizing atmospheres.7. : While carbon fibers and metal fibers can maintain their mechanical properties, they undergo oxidation and become brittle in the above atmosphere, resulting in a significant decrease in mechanical strength.
Although fibers have high tensile strength, they have a low softening point and cannot be used at high temperatures, which is a fatal drawback. Therefore, when used as reinforcing materials for composite materials, short fibers such as various whiskers and lamic fire-resistant fibers are used. Differently, it has characteristics such as a large ratio of fiber length to fiber diameter (aspect ratio), and the ability to orient the fibers in a desired direction, allowing for optimal orientation. Aluminum has such excellent properties that are not found anywhere else.
Various types of fiber-reinforced composite materials, such as alumina fibers mixed with various types of Plus Deck, are available.
Fiber-reinforced plastics or mixed with various metals including aluminum to form aluminum JU and fiber-reinforced metals (starting to be used).

C9発明が解決しようとする問題点 このように優れた性質を右するアルミナ繊維の製造方法
には従来より種々の方法が提案されている。例えば塩基
性塩化アルミニウムを水に溶解しこの溶液を紡糸して前
駆体繊維とした後、焼成して多結晶アルミプ繊維とづる
方法があるが、この方法は該塩基性塩化アルミニウム溶
液を加熱濃縮していく過程において、ある濃度から急激
に粘度の」−昇を招くことから紡糸液の粘度を−=定に
たもつことが非常に困難であるばかりか、加えて不溶性
塩を析出し、紡糸の際に紡糸口金の目詰り等のトラブル
を生ずる原因となるため作業を効率よく進める」−C゛
問題点が多いことのぽか、更にこの紡糸液を紡糸するこ
とによっC得られた多結晶アルミプ繊維の機械的強度、
可撓性は十分ではないという欠点がある。
C9 Problems to be Solved by the Invention Various methods have been proposed in the past for producing alumina fibers that have such excellent properties. For example, there is a method of dissolving basic aluminum chloride in water, spinning this solution to make a precursor fiber, and then firing it to make a polycrystalline aluminum fiber. This method involves heating and concentrating the basic aluminum chloride solution. During the spinning process, the viscosity suddenly increases from a certain concentration, making it extremely difficult to maintain a constant viscosity of the spinning solution. This may cause problems such as clogging of the spinneret, so the work can be carried out efficiently. mechanical strength of fibers,
The disadvantage is that the flexibility is not sufficient.

また特闘昭53−14832@公報では塩基性塩化アル
ミニウム溶液あるいはジル」ニウム化合物に乳酸を添加
混合して紡糸液とし、これを紡糸した後焼成して酸化物
多結晶繊維を製造する方法が開示されている。この提案
では有機酸どして乳酸を限定して用いる理由は、紡糸液
の粘度を低減させるためであり、該塩基性塩化アルミニ
ウム溶液を加熱濃縮する過程において生ずる急激な粘度
の上昇を緩慢にり−る効果については何ら言及していな
い。
In addition, Tokuto Sho 53-14832 @ publication discloses a method of producing oxide polycrystalline fibers by adding and mixing lactic acid to a basic aluminum chloride solution or a zil'nium compound to prepare a spinning solution, spinning this and then firing it. has been done. In this proposal, the reason for using a limited amount of lactic acid among organic acids is to reduce the viscosity of the spinning solution, and to slow down the rapid increase in viscosity that occurs during the process of heating and concentrating the basic aluminum chloride solution. - There is no mention of the effect of

更に特開昭54−23727号公報では塩基性塩化アル
ミニウム溶液と一10イド状シリカどの混合液に乳酸を
添加混合後加熱濃縮して紡糸液を調製し、ついて紡糸を
行ない得られる前駆体繊維を乾燥、熱処理して多結晶質
酸化物繊維に−づる方法が提案され(いる。
Furthermore, in JP-A-54-23727, lactic acid is added to a mixture of a basic aluminum chloride solution and 110-id silica, mixed, heated and concentrated to prepare a spinning solution, and the resulting precursor fiber is then spun. A method has been proposed in which polycrystalline oxide fibers are produced through drying and heat treatment.

この方法におい−C乳酸は萌述の特開昭!i31483
2号公報に記載されている理由とは巽tjる理由で゛使
用されているが、塩基性塩化アルミニ「クツ、溶液のア
ルミニウムと塩素との原r数の比が比較的狭い範囲に限
られているうえに、紡糸に供覆る紡糸液の室温にお(J
る粘度が狭い範囲に限定される等の欠点があった。
This method's odor-C lactic acid is produced by Moe's JP-A-Sho! i31483
Basic aluminum chloride is used for different reasons than those stated in Publication No. 2, but basic aluminum chloride is used because the ratio of the raw numbers of aluminum and chlorine in the solution is limited to a relatively narrow range. In addition, the spinning solution used for spinning is kept at room temperature (J
However, there were drawbacks such as the viscosity being limited to a narrow range.

その上に、これら従来の技術にJ3いては実際に紡糸に
供される紡糸液の粘度は概して低く数ボイスから高く(
も数百ボイスの狭い範囲でありm紐化のための紡糸法は
遠心紡糸法及びこれに類する紡糸法が好んC用いられる
ことがら最終的に得られる酸化物繊維は知繊紐に限定さ
れ、従っCそれが故に、用途も制約されるという致命的
欠点を持っでいる。
Moreover, in these conventional techniques, the viscosity of the spinning solution actually used for spinning is generally low, ranging from a few voices to high (
The number of strands is narrow, only a few hundred voices, and centrifugal spinning and similar spinning methods are preferred as the spinning method for forming m-threads, so the final oxide fibers obtained are limited to woven strings. , therefore, it has the fatal drawback of being limited in its uses.

1つ0問題点を解決するだめの手段 本発明者らは、これらの諸問題を考え、従来の製造1−
J払の欠点を完全に解消するため、鋭意研究を重ねIこ
結果、驚くべきことには脂肪族モノカルボン酸の主鎖に
アル」キシル基を含む有機酸を用いれば、アルミニウム
と塩素どの原子数の比が公知の方法に比較し−C広い範
囲の塩基性塩化アルミニウム溶液を利用出来るうえに該
塩基性塩化アルミニウム溶液の加熱濃縮過程に不溶性塩
を析出することなしにまた、急激な粘度の上昇を生ずる
ことなく、しかも好都合には紡糸に供覆る紡糸液の室温
にお番プる粘度が 1ボイス以上と従来法には類を見な
い広い範囲にa3いで安定した紡糸作業が可能になるば
かりか、更に本発明に用いる有機酸は従来法にもある酢
酸に比較しC悪臭を発生することがないので作業環境を
汚染する心配が4Cいことに加えて、該塩基性塩化アル
ミ−ラムと反応して該塩基性塩化アルミニラl\のフル
ミーラム原子が6配位構造を右−4るようになることに
より、安定な無機ボリン−となり、従って紡糸により得
られる前駆体繊維は室内環境においても十分に安定なも
のであり、詠前駆体繊維を焼成酸化して優れl〔耐火性
、可撓性を有する無機質酸化物繊維が得られることを発
見し本発明を完成づるに至った。
Means to Solve 1-0 Problems The present inventors considered these problems and decided to solve the conventional manufacturing method 1-0.
In order to completely eliminate the drawbacks of J-payment, we conducted intensive research and found that, surprisingly, if an organic acid containing an alkyl group in the main chain of an aliphatic monocarboxylic acid is used, aluminum and chlorine atoms can be In addition to being able to utilize a wider range of basic aluminum chloride solutions compared to known methods, the ratio of the numbers of basic aluminum chloride solutions can be increased without precipitation of insoluble salts during the heating and concentration process of the basic aluminum chloride solutions. Moreover, the viscosity of the spinning solution used for spinning at room temperature is more than 1 voice without causing any increase, making it possible to perform stable spinning operations in A3 over a wide range unparalleled by conventional methods. Furthermore, compared to acetic acid used in conventional methods, the organic acid used in the present invention does not generate a bad odor, so there is no need to worry about contaminating the working environment. By reacting with the basic aluminium chloride, the Fulmylam atoms of the basic aluminium chloride change to a 6-coordinated structure, resulting in a stable inorganic borine, and therefore the precursor fiber obtained by spinning can be used even in an indoor environment. The inventors have discovered that inorganic oxide fibers are sufficiently stable and have excellent fire resistance and flexibility by firing and oxidizing the precursor fibers, leading to the completion of the present invention.

また有機酸の他に焼成酸化処理によりアルミノ以外の金
属酸化物を与える繊維構成物質を一定早加えた混合液か
ら調製した紡糸液を紡糸しく得た無機質酸化物繊維は優
れJご耐火性、可撓性を有し1500℃まlζはそれ以
上の温度域で何ら脆化Jることがないことも見い出され
た。
In addition, inorganic oxide fibers obtained by spinning a spinning solution prepared from a mixture of organic acids and fiber constituents that provide metal oxides other than alumino through baking oxidation treatment have excellent fire resistance and only a fair amount of heat. It was also found that it has flexibility and does not become brittle at temperatures above 1500°C.

ずなわら本発明はJ’jiA M性塩化アルミニウムか
らなる紡糸原料、あるいはこれに焼成酸化処理によりア
ルミノ以外の金属酸化物を与える繊維構成物質を加えた
紡糸原料に脂肪族モノカルボン酸の主鎖にアルニ」キシ
ル基を含む有機酸を添加混合し加熱濃縮し−C室温にお
Cプる粘度が1ポイズ以↓の紡糸原液とし、常法の紡糸
法により紡糸し−C18られた前駆体繊維を焼成酸化処
理することを特徴とづる無機質酸化物繊維の製造方法で
ある。
Zunawara The present invention is based on a spinning raw material consisting of J'jiA M-type aluminum chloride, or a spinning raw material to which a fiber constituent material that provides a metal oxide other than alumino through firing oxidation treatment is added with a main chain of an aliphatic monocarboxylic acid. Add and mix an organic acid containing an alni-oxyl group, heat and concentrate to -C18 room temperature to obtain a spinning stock solution with a viscosity of 1 poise or less, and spin by a conventional spinning method to obtain a -C18 precursor fiber. This is a method for producing inorganic oxide fibers, which is characterized by subjecting the fibers to a firing oxidation treatment.

また本発明で製造されるものは長Illであり前記従来
技術による短繊維ど比較して強度に於て数段の隔子があ
る。
Furthermore, the fibers produced by the present invention are long and have several steps of strength compared to the short fibers produced by the prior art.

巳1作用 本発明において用いる塩基性塩化アルミニウム溶液とし
ては一般式、 A A z (0)−1) s CA ・ xHzO(
−′示される塩基性塩化iJルミニウム(II液をそσ
)まま用いてbよいが、塩化アルミ−ラム水)8液l\
)lルミニウl\粉を反応溶解けじめ、所望の濃度まで
加熱濃縮JることにJ、・ンて種々のアルミニウム\と
塩桑との面r数比をイ百る塩基性塩化アルミニウム溶液
を調製して用いることも6J能(゛ある。
1 Action The basic aluminum chloride solution used in the present invention has the general formula, A z (0)-1) s CA ・xHzO(
-'The basic iJ-luminium chloride (II solution) shown is σ
) may be used as is, but aluminum chloride-rum water) 8 liquid l\
) A basic aluminum chloride solution with various surface ratios of aluminum and mulberry is prepared by reacting and dissolving the luminium powder and heating and concentrating it to the desired concentration. It can also be used as a 6J function.

本発明−゛(゛使用するhm酸とは蟻酸を除<VF酸、
プに1ビAン酸、酪酸、イソ酪酸、ピノ\リン酸、オク
タン酸、ノウリン酸などの各種の飽和n旨1]7jIS
モノカルボン酸類の主鎖にアルコ−1シル基とし−Cメ
トキシル基、土[−キシル基、ノル−ンル−プロボキシ
ル基、イソプロポキシル基、ノルマルプトヤシル基およ
びその異性体類、ノル−ンルベン1ヘキシル基およびイ
の異性体類、ノルンルヘキサノキシル基お°よびその異
性体類等を含むもので具体的にはメl−A=シ酢酸、工
1−キシ酢酸、α メトキシプロピオン酸、β−1,+
−Fジプロピオン酸、ノルンルブトキシク1][1ビ;
4 ’、i酸等がよく知られ好ましいが、特に好ましく
1の(まβ−1−ト1−シブロビAン酸で・ある。
The present invention-゛(゛The hm acid used is excluding formic acid <VF acid,
Various saturated n effects such as 1bionic acid, butyric acid, isobutyric acid, pino\phosphoric acid, octanoic acid, and neuric acid 1]7jIS
The main chain of monocarboxylic acids has an alkoxyl group, -C methoxyl group, -xyl group, nor-n-proboxyl group, isopropoxyl group, n-maltoyacyl group and its isomers, nor-n-ruben. Those containing 1-hexyl group and isomers of 1, norrunulhexanoxyl group and its isomers, etc., specifically methyl-A=cyaacetic acid, 1-xyacetic acid, α-methoxypropionic acid ,β−1,+
-F dipropionic acid, norunlubutoxic 1] [1bi;
Although 4', i acid and the like are well known and preferred, 1 (or β-1-to-1-sibrobiic acid) is particularly preferred.

塩基性塩化j2ルミニウム溶液に対する有機酸の添加割
合であるが該塩基性塩化アルミニウム溶液の固体1.1
1111100g1部に対して5・〜・60ffi f
fi部、更に好ましくは5−、−35重量部であること
IJ\望ましく該有機酸の添加量が5重量部未満の場合
は該塩基性塩化アルミニウム溶液の加熱ig縮中におい
(粘度が急激に上昇し紡糸液粘度のコン[−ロールが非
常に困難となる。また60重量部以上添加しても効果は
同程度であることから経済的に意味がなくなると共に該
有機酸の添加量が5小姓8部未満の時と同様可撓性の優
れた無機質酸化物繊維を得ることは難しくなる。
The addition ratio of the organic acid to the basic aluminum chloride solution is 1.1% of the solid content of the basic aluminum chloride solution.
5...60ffi f for 1 part of 1111100g
fi parts, more preferably 5 to -35 parts by weight.IJ\Preferably, if the amount of the organic acid added is less than 5 parts by weight, during heating and condensation of the basic aluminum chloride solution, the viscosity may suddenly decrease. This increases the viscosity of the spinning solution and makes it extremely difficult to control the viscosity of the spinning solution.Also, even if 60 parts by weight or more is added, the effect is the same, so it becomes economically meaningless and the amount of the organic acid added is less than 5 parts by weight. When the amount is less than 8 parts, it becomes difficult to obtain inorganic oxide fibers with excellent flexibility.

また、本発明においては有機酸は一種または二種以上の
混合物の状態で用いてb差支えない。
Further, in the present invention, the organic acids may be used alone or in the form of a mixture of two or more.

次に、本発明における紡糸液は塩基性塩化アルミニウム
溶液、有機酸の他に焼成酸化処理によりアルミノ以外の
金属酸化物へ転化しうる繊維構成物質を詠塩褪性塩化ア
ルミーウム溶液の固体換算100重量部に対して40重
端部以下、好、にしくは25重アルノット含イラしてb
よい。ここで焼成酸化処理とは前駆体繊維を電気炉、畠
周波炉等で加熱焼成、焼結せしめることをさすが、この
処理によりアルミナ以外の金属酸化物へ転化しうる繊維
構成物質とはケイ素を含む化合物としてシリカヒドロシ
ル、Si (OR)十の構造を有するケイ酸エステル(
Rはアルキル基)、1 −S; −O−の構造単位を右するポリAルカノシR′
 ロキサン(R・およびR2はイれぞれ同一または異っ
lこアルキル基)、 ♀R” 一8i −0−一 の構造単位を右するポリケイ酸ニス
ORz チル(R・おJ・びR2はそれぞれ同一または
異ったアルキル基) 等の水溶性ケイ素化合物が、マグネシウムを含む化合物
としてはマグネシウムゾル、 Ma (OR)zの構造を有するマグネジ「クムアル:
Iキシド(Rはアルキル基)、硝酸マグネシウム、F<
zMgの構造を有するアルギルングネシウ11化合物(
[<はアルキル基)を水で加水分解して得られるングネ
シア水和物等が、また上記化合物以外のものどじてはM
(OR)n(Mは金属、Rはアルキル基、nは4以下の
整数)の構造を右する各種の金属アル」キシド、各種金
属ゾル等があげられ、これらの化合物の一種あるいは二
種以上の混合物が用いられるが特に好ましいのは水溶性
ケイ素化合物である。
Next, the spinning solution in the present invention contains a basic aluminum chloride solution, an organic acid, and fiber constituent substances that can be converted into metal oxides other than alumino by firing oxidation treatment. 40 or less double ends, preferably 25 double knots or less
good. Here, firing oxidation treatment refers to heating, firing, and sintering of the precursor fiber in an electric furnace, Hatake wave furnace, etc., and fiber constituent substances that can be converted into metal oxides other than alumina by this treatment include silicon. As a compound, silica hydrosyl, a silicate ester with a structure of Si (OR)
R is an alkyl group), 1 -S; polyA kanosyl R' which represents the structural unit of -O-
Roxane (R and R2 are the same or different alkyl groups, respectively), polysilicate varnish with the structural unit of ♀R"-18i-0-1 Examples of compounds containing magnesium include magnesium sol and magnezi "Kumual" having the structure Ma(OR)z.
I oxide (R is an alkyl group), magnesium nitrate, F<
11 compounds having the structure of zMg (
Ngnesia hydrate obtained by hydrolyzing [< is an alkyl group] with water, and other compounds other than the above, M
(OR)n (M is a metal, R is an alkyl group, n is an integer of 4 or less), including various metal alkoxides, various metal sols, etc., and one or more of these compounds. Particularly preferred are water-soluble silicon compounds.

本発明において該繊維構成物質を用いる理由は、紡糸液
の曳糸性を改善することにもあるが、前駆体繊維を焼成
酸化処理することにより酸化物繊維へ転化する過程で生
成する中間アルミプ結晶子の成長を抑えるためが土であ
り、これにより1500°C1まlごはぞれ以上の温度
においても優れた耐火性、旬撓性を随持Jることが可能
である。
The reason for using the fiber constituent material in the present invention is to improve the spinnability of the spinning solution, but intermediate aluminum crystals are produced in the process of converting precursor fibers into oxide fibers by firing and oxidizing them. The soil is used to suppress the growth of the young, and this allows the rice to maintain excellent fire resistance and flexibility even at temperatures above 1500°C.

一ツノ、塩基性塩化アルミニウム、有機酸および更に要
すれば焼成酸化処理によりアルミナ以外の金属酸化物を
うえる繊維構成物質を含む混合液、づなわち紡糸液から
紡糸を行なうには、いわゆる乾式紡糸が最も好都合であ
るが、遠心力紡糸、噴射ガス吹付式紡糸、ジ」、ット紡
糸など他の適当な紡糸方法に従ってもよい。また、紡糸
液の空温における粘度は1ポイズ以上、好ましくは60
ポイズ以上、更に好ましくは100ボイズ以上が適当で
ある。従って、紡糸液はこの範囲の粘度を!jえるよう
に調整覆ることが必要である。
In order to perform spinning from a spinning solution, a mixture containing basic aluminum chloride, an organic acid, and, if necessary, a fiber constituent material that can be treated with metal oxides other than alumina through firing oxidation treatment, so-called dry spinning is required. is most convenient, but other suitable spinning methods may be followed, such as centrifugal spinning, propellant gas spinning, jet spinning, etc. In addition, the viscosity of the spinning solution at air temperature is 1 poise or more, preferably 60 poise or more.
A suitable value is at least 100 poise, more preferably at least 100 poise. Therefore, the viscosity of the spinning solution is within this range! It is necessary to adjust the cover so that it can be adjusted.

紡糸液を脱泡後、紡糸、乾燥された前駆体繊維は通常0
.5μ〜400μの平均直径をイjしているがこの範囲
に限定されるものではない。
After degassing the spinning solution, the spun and dried precursor fibers usually have 0
.. Although the average diameter is 5μ to 400μ, it is not limited to this range.

このようにして得られた前駆体繊維は張力下に比較的低
温、具体的には400℃以下の温度に昇温して処即し1
.、X後、更に酸化雰囲気ト、場合にJ、つては還元雰
囲気中に1000℃またはそれ以上の温度で焼成酸化処
理して前駆体繊維中のh機物、炭素等を除去ししめ焼結
させることにより純白で非常に緻密かつ弾性と弾力性の
ある無機質酸化物繊維どなる。かくして本発明により得
られる無機質酸化物繊維は、安価rあり入手が簡単な塩
基性塩化アルミーウ11を出発1爪料としていることか
ら容易に大挙生産が可能であって、かつ優れた耐火f1
、可撓性を具備していることから各種プラスブックある
いは金属と混合して各種の繊維強化複合H料・とじて使
用することが可能ぐある。
The precursor fiber thus obtained is treated under tension at a relatively low temperature, specifically at a temperature of 400°C or less.
.. , After X, the precursor fibers are subjected to firing oxidation treatment at a temperature of 1000°C or higher in an oxidizing atmosphere, or in some cases J, in a reducing atmosphere to remove materials, carbon, etc. in the precursor fibers, and then sintered. This results in pure white, extremely dense, elastic and elastic inorganic oxide fibers. Thus, the inorganic oxide fiber obtained by the present invention can be easily produced in large quantities because it uses basic aluminum chloride 11, which is inexpensive and easily available, as a starting material, and has excellent fire resistance.
Because of its flexibility, it can be mixed with various types of plastic books or metals and used as various fiber-reinforced composite H materials and binding materials.

[、実施例 以下実施例によって本発明を更に詳しく説明するが、本
発明はこれらに何ら限定されるものではない。
[Examples] The present invention will be explained in more detail with reference to Examples, but the present invention is not limited thereto.

(実施例1) Af/Cぶの原子数の比が1.39の塩基性塩化アルミ
ニウム溶液(AJ!+ (Of−1)s CJ!3゜Δ
、ez Oa =−20,3%) 7007を 1℃3
日九底フラス」にどりプラス」を50℃に昇温しながら
β、−、::c 1−キシプロピオン酸60 、OmQ
を徐々に添加した。全i社添加後ノラスf1を65°C
に保ら塩基性塩化アルミニウム溶液中に含まれる水の3
1.4%を減圧下に除去した。次にこの混合液を撹拌装
置を装備した耐圧容器に移液し混合液の水含量が12.
9%になるよ−C減L[トに濃縮を続けた結果AJ!z
 03=39.4%、室温にお(〕る粘度が5500ボ
イズの均 な紡糸液を得た。なお、濃縮中におい−C粘
度の急激な1臂は全く認められなか′)Iこ 。
(Example 1) A basic aluminum chloride solution (AJ!+ (Of-1)s CJ!3゜Δ with a ratio of Af/C atoms of 1.39
,ez Oa = -20,3%) 7007 at 1℃3
β, -, ::c 1-xypropionic acid 60, OmQ while raising the temperature of Nidori Plus to 50℃
was added gradually. After adding all I companies, Noras f1 was heated to 65°C.
3 of the water contained in a basic aluminum chloride solution kept at
1.4% was removed under reduced pressure. Next, this mixed solution was transferred to a pressure-resistant container equipped with a stirring device, and the water content of the mixed solution was reduced to 12.
It will be 9% - C reduction L [The result of continued concentration is AJ! z
A uniform spinning solution with a viscosity of 5,500 voids at room temperature and 03 = 39.4% was obtained. During concentration, no sharp increase in the -C viscosity was observed at all.

この紡糸液を脱泡後、わfh1’の張カドに孔数30、
孔径0.08mmの紡糸口金により、長さ6゜5Inの
紡糸筒中に連続的に押し出し紡糸を行ない30m/分の
速度で巻き取つIこ。得られIこ前駆体繊維は透明であ
りその平均直径は40μであった。
After defoaming this spinning solution, the number of holes is 30 in the tension corner of the width fh1'.
Using a spinneret with a hole diameter of 0.08 mm, the fibers were continuously extruded and spun into a spinning tube with a length of 6.5 inches and wound at a speed of 30 m/min. The resulting precursor fibers were transparent and had an average diameter of 40 microns.

次いC前駆体繊維を電気炉へ入れ張力上かつ窒素雰囲気
トに400℃まで昇温したのら窒素ガスをJlめ炉内を
空気C′置換し300°C/llrの胃渇速1σで10
00℃まで空気中で焼成して平均直径15/lのアルミ
ノ繊維を譬だ。また更に1200°Cまで焼成したもの
は透明な強度のあるα−アルミプ繊維であった。
Next, the C precursor fibers were placed in an electric furnace and heated to 400°C under tension and in a nitrogen atmosphere, and then the nitrogen gas was removed and the furnace was replaced with air C' at a gastric thirst rate of 1σ of 300°C/llr. 10
For example, alumino fibers with an average diameter of 15/l are fired in air to 00°C. Furthermore, the fibers fired to 1200°C were transparent and strong α-aluminum fibers.

〔実施例2〕 市販工業用塩基性塩化アルミ−ラム溶液(Aぶz(O)
−1)sC,f! ・ 2.4)−1zO。
[Example 2] Commercially available industrial basic aluminum chloride rum solution (Abz(O)
-1) sC,f!・2.4)-1zO.

Al103 =23.’5%、八柔/へlの原子数の比
2.0) 500−を実施例1に用いたノラス]にとり
フラスニ1を50°Cに4温しながらμ エト1ニシゾ
ロビAンM33mlを徐々に添加した。添加終了後、減
圧トにフシスコを回転さゼて濃縮を開始し、水98dを
45分か(プて除去した。次にこの混合液を実施例1で
使用した耐圧容器に移液し撹拌を続けながらシリカヒト
1]ゾルをAfzO3:Si Oz =85: 15と
なる様に添加して後、容器を50℃に加熱し濃縮を続(
)水229dを除去した。
Al103 =23. '5%, the ratio of the number of atoms of Yaju/Hel 2.0) 500- to the Noras used in Example 1, and while warming the Furasuni 1 to 50°C for 4 hours, gradually added 33 ml of added to. After the addition was completed, the fuscisco was rotated in a vacuum chamber to start concentration, and 98 d of water was removed by boiling for 45 minutes. Next, this mixed solution was transferred to the pressure-resistant container used in Example 1 and stirred. While continuing to add silica hydrogen 1] sol so that AfzO3:SiOz = 85:15, the container was heated to 50°C and concentration was continued (
) 229d of water was removed.

なJ3、この操作中におい−Cは急激な粘度の上昇は全
く見受(プられなかった。次に水の蒸発口を閉じ容器を
40℃に保持したまま更に5Hr撹拌を続りA 1 z
 03 =33.3%、空温における粘度が2200ボ
イスの均一な紡糸液を得た。この紡糸液を真空脱泡し実
施例1で用いたものと同一の紡糸装置を使って紡糸し平
均直径40μの透明な連続状前駆体繊維を得た。フィラ
メント状の前駆体繊維を張力下かつ窒素雰囲気下に40
0℃まで昇温し35分間保持した。次いで窒素ガスを止
め炉内を空気に置換し300°に / l−1rのR温
速度−C1200℃ま(空気中ぐ焼成しC直径10μの
強度のあるノフルミノシリ力繊維を得た、。
During this operation, there was no rapid increase in the viscosity of Oi-C.Next, the water evaporation port was closed, and stirring was continued for an additional 5 hours while keeping the container at 40°C.
03 = 33.3% and a viscosity of 2200 voices at air temperature was obtained. This spinning solution was degassed under vacuum and spun using the same spinning device as used in Example 1 to obtain transparent continuous precursor fibers with an average diameter of 40 μm. The filamentary precursor fibers were placed under tension and under a nitrogen atmosphere for 40 minutes.
The temperature was raised to 0°C and held for 35 minutes. Next, the nitrogen gas was stopped, and the inside of the furnace was replaced with air, and the temperature was increased to 300°/R temperature rate of 1-1r-C to 1200°C (fired in air to obtain a strong nofluminous fiber with a C diameter of 10μ).

〔実施例;3〕 実施例2で用いたAi/C1の原子数の比が2.0の塩
基性塩化アルミニウム溶液500 trflに有機酸ど
しくゾ【」ボキシ酪酸31dを加え65℃に加熱した。
[Example; 3] To 500 trfl of the basic aluminum chloride solution with the Ai/C1 atomic ratio of 2.0 used in Example 2, 31 d of organic acidic zo[]boxybutyric acid was added and heated to 65°C. .

次いで減圧1;に濃縮を続は水ioo#li!を除去し
た。混合液を実施例1で用いたものと同一の容器に移液
し撹拌を続Cノながら■、プルシリケートをAJ!z 
O,! : Si Oz =75:25となる様に添加
した上で容器を65℃に保持し減圧下に更にmwUを続
は水320dを除去した。得られた紡糸液はΔAz03
 =33.9%、室温における粘度が3500ボイスで
あった。
Next, condensation is carried out under reduced pressure 1; water ioo#li! was removed. The mixed solution was transferred to the same container as used in Example 1, and while stirring was continued, the prusilicate was added to AJ! z
O,! : SiOz was added in a ratio of 75:25, and the container was maintained at 65° C. and 320 d of water was removed under reduced pressure. The obtained spinning solution is ΔAz03
=33.9%, and the viscosity at room temperature was 3500 Bois.

実施例1 ′c用いた紡糸装置と同一の紡糸装置を使っ
て50μの前駆体繊維を実施例2と同様にして焼成した
ところ無色透明平均直径15μのアルミナシリカ繊維が
得られた。
Example 1 Using the same spinning device as used in Example 1'c, 50 μm precursor fibers were fired in the same manner as in Example 2 to obtain colorless transparent alumina-silica fibers with an average diameter of 15 μm.

〔比較例1〕 β−工[−手シプロピAン酸を添加Jる操作を除いて実
施例1と全く同一操作により紡糸液を調!!i!−Jべ
く試みたが、加熱製綿中に不溶性塩を析出し、しかも急
激な粘度の上界減少が認められ所望の粘度を右づる紡糸
を得ることは出来なかった。
[Comparative Example 1] A spinning solution was prepared by exactly the same procedure as in Example 1, except for adding β-cypropanic acid. ! i! -J was attempted, but insoluble salts precipitated in the heated cotton, and a rapid decrease in the upper limit of viscosity was observed, making it impossible to obtain a spinning yarn with the desired viscosity.

(実施例4) /M!/(、eの原子数の比が2.5の塩基性塩化アル
ミニウム溶液500IIt!、にメトギシ酢酸46II
tlを加え50℃に胃温し10分間そのii!度で保持
したのち減圧下に濃縮し水76dを除去した。混合液を
実施例1で用いた容器に移し撹拌を続けながら容器を6
5℃に保持し、減圧下に更に水を120d除去しΔfz
 03=28.7%、室温にお(プる粘度が270ボイ
スの紡糸液を1qだ。この紡糸液を実施例1′c・用い
たものと同一の紡糸装置を使用して平均直径40μの前
駆体繊維を得た。次いで窒素雰囲気下に500℃まで昇
温し20分間保持したのち、炉内を空気に置換し100
0°Cまで300℃/Hrの4記速度で胃温し平均直径
20μの強度のあるアルミニウムを得た。
(Example 4) /M! /(, 500 IIt of basic aluminum chloride solution with a ratio of the number of atoms of e of 2.5!, 46II of methoxyacetic acid
Add tl and warm the stomach to 50℃ for 10 minutes part ii! After the mixture was maintained at a temperature of 100°C, it was concentrated under reduced pressure to remove 76d of water. Transfer the mixed solution to the container used in Example 1, and while continuing to stir the container,
The temperature was maintained at 5°C, and water was further removed for 120 d under reduced pressure to give Δfz
03 = 28.7%, at room temperature (1 q. A precursor fiber was obtained.Next, the temperature was raised to 500°C in a nitrogen atmosphere and held for 20 minutes, and then the inside of the furnace was replaced with air and heated to 100°C.
Stomach warming was carried out at a rate of 300°C/hr up to 0°C to obtain strong aluminum with an average diameter of 20 μm.

G0発明の効果 本発明によれば、 く1〉アルミ−ラムと塩素との原子数の比が公知のh法
に比較して広い範囲の塩基性塩化アルミニウム溶液を利
用出来る。
G0 Effects of the Invention According to the present invention, (1) A basic aluminum chloride solution having a wider range of atomic ratios between aluminum and chlorine can be used than in the known h method.

(2)該塩基性塩化アルミニウム溶液の加熱濃縮過程に
不溶性塩を析出することがなくまた、急激な粘度の」二
胃を生ずることもない。
(2) No insoluble salts are precipitated during the heating and concentration process of the basic aluminum chloride solution, and no digastric formation with rapid viscosity occurs.

(33)紡糸に供Jる紡糸液の室温における粘度が、1
ポイズ以上と従来法には類を見ない広い範囲において安
定した紡糸作業が可能になる。
(33) The viscosity at room temperature of the spinning solution used for spinning is 1
Stable spinning operation is possible over a wide range of poise or higher, which is unparalleled by conventional methods.

(4)本発明に用いる有機酸は従来法にもある酢酸に比
較して悪臭を発生することがないのC(’f業環境を汚
染リ−る心配がないことに加え1 で、該塩基性塩化ノ
フルミニウムと反応し゛C該塩基性塩化アルミニウムの
アルミ−ラム原子が6配位構造を有するようになること
により、安定な無機ポリマーとなり、従って紡糸により
得られる前駆体II維は案内環境においても十分に安定
なものであり、該前駆体繊維を焼“酸酸化して優れた耐
火性、可撓性を右づ−る無機質酸化物繊維がISられる
3゜ (5)寄られる無機質酸化物繊維は優れた耐火性、可撓
性を有し1500℃またはそれ以上の温度域C何ら脆化
づることがない。
(4) The organic acid used in the present invention does not generate a bad odor compared to acetic acid, which is also used in conventional methods. The aluminum atoms of the basic aluminum chloride react with basic nofluminium chloride so that the aluminum atoms of the basic aluminum chloride have a six-coordination structure, resulting in a stable inorganic polymer. The inorganic oxide fibers are sufficiently stable, and the inorganic oxide fibers with excellent fire resistance and flexibility are obtained by oxidizing the precursor fibers with IS. The fibers have excellent fire resistance and flexibility and do not become brittle at temperatures of 1500° C. or higher.

(6)得られる無機質酸化物1維は長繊維であり前記従
来技術による短繊維と比較して強度に於τ数段の隔子が
ある。
(6) The obtained inorganic oxide single fiber is a long fiber, and has a strength difference of several steps τ compared to the short fiber according to the prior art.

等の極めて優れた効果があり、工業的価値人なるものが
ある、。
It has extremely excellent effects such as, and has industrial value.

手続ネrtj、iE書 (自 発) 1、事件の表示 昭和59年 特許願 第101936号2、発明の名称 無機質酸化物繊維の製造方法 3、補正をする者 4、代理人 住 所 東京都千代田区神田北乗物町16番地 :〒i
oi 英 ビル3階 ) 補 正 の 内 容 1、明細書箱4頁2行目に1ノフルミナ一繊維強化」と
あるを、[アルミナ繊維強化1ど訂正。
Procedure Nertj, iE (self-motivated) 1. Indication of the case 1982 Patent Application No. 101936 2. Name of the invention Method for manufacturing inorganic oxide fiber 3. Person making the amendment 4. Address of the agent Chiyoda, Tokyo 16 Kanda Kita Jorimono-cho, Ward: 〒i
(Oi Building 3rd floor) Contents of the amendment 1. In the second line of page 4 of the statement box, the statement ``1 nolumina fiber reinforced'' has been corrected to [alumina fiber reinforced 1 etc.

2、明細書簡9頁1行目の1アルミニウム溶液」と[“
をその1との間に、「および/または一般式AJ2+ 
(OH)s CJ!3’C示される塩基性塩化アルミニ
ウム溶液」を加入。
2. Specification letter, page 9, line 1, 1 aluminum solution” and [“
and/or the general formula AJ2+
(OH)s CJ! Add a basic aluminum chloride solution indicated by 3'C.

3、同頁19行目に [ノルマルブトキシクロロピAン酸1とあるを、[ノル
ンルートキシプロビオン酸]と訂正。
3. On the 19th line of the same page, [n-butoxychloropianoic acid 1] was corrected to [norn-rutoxyprobionic acid].

4、明細内箱11頁10行目および13行目に夫々「異
った」とあるを、「異なった」と訂正。
4. In the details box, page 11, lines 10 and 13, the words "different" were corrected to "different."

5、同頁における上段の化学式 %式% 6、同頁における下段の化学式 F OR’ F OR+ 1 一3i −0−を −3t −0−と訂正。5. Chemical formula at the top of the same page %formula% 6. Chemical formula at the bottom of the same page F OR’ F OR+ 1 -Corrected 3i -0- to -3t -0-.

Il 0R2J ORZ J 7、明細害第13頁15行目に[還元雰囲気中に−1と
あるを、「還元雰囲気下に」と訂正。
Il 0R2J ORZ J 7, page 13, line 15 of the specification [-1 in a reducing atmosphere has been corrected to read ``in a reducing atmosphere.''

8、明細書箱14頁12行目にIl、39jとあるを、
lN、33Jと訂正。
8. It says Il, 39j on page 14, line 12 of the statement box.
Corrected as lN, 33J.

9、明細書箱15頁1行目にN2.9%−1とあるを、
115.1%」と訂正。
9. On the first line of page 15 of the statement box, it says N2.9%-1.
115.1%” was corrected.

10、同頁14行目に1空気中r Jとあるを削除。10. Delete 1 air r J on the 14th line of the same page.

11、明細書箱15頁末行から第16頁3行目にか1)
CI市販T業用・・・50Mを」どあるを、「市販工業
用塩基性塩化アルミニウム(Afz(OH)s C1・
 2.4H20)の水溶液(Afz 03 =23.5
%、 Af’/(1!の原子数の比2.0> 500m
を」ど訂正。
11. From the last line of page 15 of the statement box to the third line of page 16 (1)
CI commercially available T industrial use...50M" and "commercially available industrial basic aluminum chloride (Afz(OH)s C1.
2.4H20) aqueous solution (Afz 03 =23.5
%, ratio of the number of atoms of Af'/(1! 2.0> 500m
"Corrected."

12、明細書筒16頁4行目に1μ=工1−キシ」とあ
るを、[β−1トキシー(と訂正。
12. On the 4th line of page 16 of the specification, the statement ``1μ = engineering 1-xy'' was corrected to [β-1 toxicity.

13、同頁11行目にr229dJとあるを、r246
dlと訂正。
13, r229dJ on the 11th line of the same page, r246
dl and correction.

14、同頁14行目に1−5HrJとあるを、「5時間
」とハ]正。
14. On the 14th line of the same page, 1-5HrJ is written as "5 hours".

15、明細種箱17頁2行目に「空気に」とあるを、「
空気で」と訂正。
15. On the second line of page 17 of the specification box, replace "in the air" with "
With air,” he corrected.

16、同頁3行目に[空気中で1とあるを肖1j除。16. On the third line of the same page, [1 in the air is excluded.

17、同頁19行目に「無色透明」とあるを肖11除。17. On the 19th line of the same page, the phrase ``colorless and transparent'' is removed from Portrait 11.

18、明細書箱18頁5行目にl1胃減少」とあるを、
「上昇現象」と訂正。
18. On page 18, line 5 of the statement box, it says, “L1 stomach decrease.”
Corrected to "rising phenomenon."

19、同頁末行に「空気に」とあるを、「空気で」と訂
正。
19. On the last line of the same page, the text "in the air" was corrected to "in the air."

Claims (1)

【特許請求の範囲】[Claims] 塩基性塩化ノアルミニウムあるいはこれに焼成酸化処理
によりアルミノ−以外の金属酸化物を与える繊1tll
t41成物質を加えfcものに、脂肪族モノカルボン酸
の主鎖にアルコキシル基を含む有機酸を添加混合し、加
熱濃縮して室温における粘度が1ポイズ以上の紡糸原液
とし、常法の紡糸法により紡糸して得られた前駆体繊維
を焼成酸化処理覆ることを特徴とする無機質酸化物繊維
の製造方法。
1 tll of basic aluminium chloride or a fiber to which a metal oxide other than alumino is applied by baking oxidation treatment
To the fc material, add the T41 component, add and mix an organic acid containing an alkoxyl group in the main chain of an aliphatic monocarboxylic acid, heat and concentrate to obtain a spinning stock solution with a viscosity of 1 poise or more at room temperature, and use the conventional spinning method. 1. A method for producing inorganic oxide fibers, which comprises subjecting a precursor fiber obtained by spinning to a firing oxidation treatment.
JP10193684A 1984-05-21 1984-05-21 Production of inorganic oxide fiber Granted JPS60246815A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10193684A JPS60246815A (en) 1984-05-21 1984-05-21 Production of inorganic oxide fiber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10193684A JPS60246815A (en) 1984-05-21 1984-05-21 Production of inorganic oxide fiber

Publications (2)

Publication Number Publication Date
JPS60246815A true JPS60246815A (en) 1985-12-06
JPS6227164B2 JPS6227164B2 (en) 1987-06-12

Family

ID=14313795

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10193684A Granted JPS60246815A (en) 1984-05-21 1984-05-21 Production of inorganic oxide fiber

Country Status (1)

Country Link
JP (1) JPS60246815A (en)

Also Published As

Publication number Publication date
JPS6227164B2 (en) 1987-06-12

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