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JPH0478732B2 - - Google Patents
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JPH0478732B2 - - Google Patents

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Publication number
JPH0478732B2
JPH0478732B2 JP63251635A JP25163588A JPH0478732B2 JP H0478732 B2 JPH0478732 B2 JP H0478732B2 JP 63251635 A JP63251635 A JP 63251635A JP 25163588 A JP25163588 A JP 25163588A JP H0478732 B2 JPH0478732 B2 JP H0478732B2
Authority
JP
Japan
Prior art keywords
aluminum
carboxyl groups
organic acid
viscous liquid
aqueous 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.)
Expired - Lifetime
Application number
JP63251635A
Other languages
Japanese (ja)
Other versions
JPH02102116A (en
Inventor
Yoshinori Fujiki
Toshuki Nishio
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.)
KAGAKU GIJUTSUCHO MUKIZAISHITSU KENKYUSHOCHO
Original Assignee
KAGAKU GIJUTSUCHO MUKIZAISHITSU KENKYUSHOCHO
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 KAGAKU GIJUTSUCHO MUKIZAISHITSU KENKYUSHOCHO filed Critical KAGAKU GIJUTSUCHO MUKIZAISHITSU KENKYUSHOCHO
Priority to JP63251635A priority Critical patent/JPH02102116A/en
Publication of JPH02102116A publication Critical patent/JPH02102116A/en
Publication of JPH0478732B2 publication Critical patent/JPH0478732B2/ja
Granted legal-status Critical Current

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  • Compositions Of Oxide Ceramics (AREA)
  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
  • Inorganic Fibers (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

産業上の利用分野 本発明はアルミナ繊維または膜状物の製造法に
関する。アルミナ繊維、アルミナ膜状物は耐熱
材、断熱材、強化補強材等として有用なものであ
る。 従来の技術 従来のアルミナ繊維の製造法として、前駆ポリ
マー法、スラリー法、無機塩法、ゾルーゲル法な
どが知られている。これらの方法の代表例を挙げ
ると次の通りである。 前駆ポリマー法は
INDUSTRIAL APPLICATION FIELD The present invention relates to a method for producing alumina fibers or membranes. Alumina fibers and alumina membranes are useful as heat-resistant materials, heat-insulating materials, reinforcing materials, and the like. BACKGROUND ART Known conventional methods for producing alumina fibers include a precursor polymer method, a slurry method, an inorganic salt method, and a sol-gel method. Representative examples of these methods are as follows. The precursor polymer method is

【式】からなる主鎖を 有する無機重合体のポリアルミノキサンを含む粘
稠溶液にけい酸エステルを混合して乾式紡糸して
焼成する。 スラリー法はAl2O3微粉及び少量のMgCl2
6H2Oにバインター成分としてAl2(OH)3Clを加
えて粘稠なスラリーとし、これを乾式紡糸して焼
成する。 無機塩法はアルミニウム塩の水溶液にポリエチ
レンオキサイドやPVAなどの水溶性有機高分子
を加え、更に水溶性ポリシロキサンを混合して粘
稠液となし、ノズルより吹き出し、これを焼成す
る。 ゾルーゲル法はHCOO、CH3COOなどのイオ
ンを含むアルミナゾルにシリカゾル、ほう酸を加
えて粘稠液とし、これを紡糸して焼成する。 しかし、これらの方法はいずれも次のような問
題点がある。紡糸液を用いて紡糸して繊維とする
には、紡糸原液が重要であり、溶液の粘性、曳糸
性、均一性、安定性の物性が重要な要素であると
共に、紡糸原液の製造が容易で、かつ紡糸性が優
れていることが重要な要素である。このような観
点からみたとき、前駆ポリマー法は均一性は高い
が、紡糸原液を作るための製造プロセスの制御が
難しい。ゾルーゲル法は、その濃縮段階におい
て、沈澱、濁りが生じたり、また急激に粘度が増
大したりするため、濃縮の制御が難しい。無機塩
法は繊維形態を付与する粘性を水溶性有機重合体
で行つているため、調液段階でゲル化してしまう
など、原液の安定性を欠くことがある。また、ス
ラリー法は所謂不均一系であり、紡糸原液を構成
する固体粒子の粒度、添加量、分散状態などが微
妙に紡糸性に影響を与え、制御が難しい等の問題
点がある。 発明の目的 本発明は従来法における紡糸原液の持つ問題点
をなくしようとするものであり、その目的は紡糸
原液の粘性を適当に調整することが容易で、曳糸
性、均一性、安定性に優れ、紡糸性も良好であ
り、その製造も容易なものとなし、これによりア
ルミナ繊維または膜状物を容易に製造する方法を
提供するにある。 発明の構成 本発明者らは前記目的を達成すべく鋭意研究の
結果、カルボキシル基を2〜3個と水酸基を1〜
2個有する有機酸あるいはカルボキシル基を2個
有する有機酸の水溶液にこれに可溶なアルミニウ
ム有機化合物を溶解して均一溶液となし、これを
加熱濃縮することにより過剰の水及び溶解によつ
て生成した有機残基を除去すると、紡糸に適する
粘稠性と曳糸性を有し、かつ均一で安定な紡糸原
液が容易に得られることを究明し得た。 また、前記アルミニウム有機化合物と適当量の
アルミニウム無機酸塩とを併用して、前記と同様
にして粘稠液を製造し、これを紡糸原液とする
と、紡糸で得られた繊維を焼成・焼結の際、揮発
成分が少なくなり、焼結を容易となし得ることを
究明し得た。 これらの知見に基づいて本発明を完成した。 本発明の要旨は、 (1) 有機酸水溶液に可溶なアルミニウム有機化合
物を、カルボキシル基2〜3個と水酸基を1〜
2固有する有機酸あるいはカルボキシル基を2
個有する有基酸の水溶液に溶解した後加熱濃縮
して粘稠液となし、この粘稠液をノズルまたは
スリツトより押し出して繊維状または膜状物に
成形した後焼結することを特徴とするアルミナ
繊維または膜状物の製造法。 (2) 有機酸水溶液に可溶なアルミニウム有機化合
物がAl2O3に換算して50モル%以上とアルミニ
ウム無機酸塩がAl2O3に換算して50モル%未満
の両化合物を、カルボキシル基を2〜3個と水
酸基を1〜2個有する有機酸あるいはカルボキ
シル基を2個有する有機酸の水溶液に溶解した
混合液となしこれを加熱濃縮して粘稠液とな
し、この粘稠液をノズルまたはスリツトより押
し出して繊維状または膜状物に成形した後焼結
することを特徴とするアルミナ繊維または膜状
物の製造法、にある。 本発明において用いる有機酸水溶液に溶解する
アルミニウム有機化合物としては、例えばアルミ
ニウムアルコキシド、アルミニウムカルボキシレ
ート、アルミニウムアセチルアセトネートが挙げ
られる。アルミニウムアルコキシドとしては、そ
の有機残基はメトキシ基、エトキシ基、ノルマル
プロポキシ基、イソプロポキシ基、ノルマルブト
キシ基、セカンダリーブトキシ基、ターシヤリー
ブトキシ基等が挙げられる。またアルミニウムカ
ルボキシレートとしては、その有機残基はホルミ
ルオキシ基、アセチルオキシ基が挙けられる。 本発明において用いるアルミニウム無機酸塩と
しては、例えば、オキシ塩化アルミニウム、塩化
アルミニウム、硫酸アルミニウム、硝酸アルミニ
ウム等が挙げられる。 アルミニウム有機化合物とアルミニウム無機酸
塩化合物とを併用する場合は、アルミニウム有機
化合物がAl2O3に換算して50モル%以上であるこ
とが必要である。これが50モル%未満では繊維形
成物に固化させることが困難となる。 本発明において用いるカルボキシル基を2〜3
個と水酸基を1〜2個有する有機酸としては、例
えば 等が挙げられる。 また、カルボキシル基を2個有する有機酸とし
ては、例えば、 が挙げられる。 紡糸原液は、前記のようなアムミニウム有機化
合物モル数に対し、20〜50倍モルの蒸溜水を含む
前記有機酸水溶液に溶解させる。有機酸の量はア
ルミニウム有機化合物、またはアルミニウム無機
酸塩のアルミニウム元素に対し、1倍モル以上、
好ましくは1.5〜2.0倍モルであることが適当であ
る。溶解は室温あるいは90℃程度までの温度で撹
拌しながら行う。 この溶解液にアルミナ繊維または膜状物の諸物
性を向上させるために、必要に応じ、少量のリチ
ウム、ベリリウム、ホウ素、ナトリウム、カルシ
ウム、カリウム、マグネシウム、ケイ素、バリリ
ウム、クロム、マンガン、イツトリウム、ランタ
ン、タングステン、鉄、ニツケル、銅、亜鉛など
の1種または2種以上を、有機金属化合物、炭酸
塩、無機酸塩として添加する。 得られた溶液を開放系で100℃以上に加熱して
濃縮する。この濃縮は粘稠状態になるまで行う。 得られる粘稠液は70〜80℃では流動性を有する
が、室温に放置すると徐々に粘度を増しついには
固化する性質を有する。この現象は乾燥雰囲気下
においてはより顕著となる。従つて、この粘稠液
を70〜80℃の加温状態でノズルより室温以下の乾
燥雰囲気中に押し出すと連続した繊維が得られ
る。 得られた繊維を乾燥雰囲気中で水分を除去した
後、700〜1000℃で空気中に焼成すると有機成分
は分解除去される。これを1200〜1400℃で焼結す
ることによりアルミナ長繊維が得られる。 この場合、太目の口径ノズルより押し出し、火
炎で焼成吹き飛ばすと極細の短繊維が得られる。 また、ノズルに代えスリツトを用いると膜状物
が得られる。アルミニウム原料組成として前記ア
ルミニウム有機化合物とアルミニウム無機酸塩を
Al2O3に換算して50モル%未満の量を併用する
と、焼成・焼結の際揮発分が少なくなり焼結を容
易にする。この場合、アルミニウム無機酸塩が前
記量より多く用いると、粘稠液が固化し難くなる
ので、50モル%未満であることが必要である。 実施例 1 クエン酸2.88gを蒸溜水20mlに溶解した水溶液
にアルミニウムイソプロポキシド2.20g加え、撹
拌して透明な均一溶液を得た。この溶液を100℃
で加熱して濃縮し粘度100ポイズとした。 この濃縮液を70〜80℃でノズルより室温乾燥大
気中に押し出し、直径5〜100μmの無色透明な
長繊維を得た。得られた繊維を100℃で1晩乾燥
し、次いで900℃で2時間熱処理した後、1100℃
で2時間加熱し焼結した。これによりα−アルミ
ナ長繊維が得られた。 実施例 2 酒石酸3.00gを蒸溜水20mlに溶解した水溶液を
90℃に加熱し、これに塩基性酢酸アルミニウム・
4水和物3.78gを加え、撹拌を行うことにより透
明な均一溶液を得た。これを実施例1と同様にし
て粘度100ポイズの濃縮液となし、紡糸原液とし
た。以下実施例1と同様にしてα−アルミナ長繊
維が得られた。 実施例 3 クエン酸3.84gを蒸溜水20mlに溶解した水溶液
にアルミニウムイソプロポキシド1.32gを加え、
撹拌により透明な均一溶液を得た。これに塩化ア
ルミニウム・6水和物0.97gを加え、撹拌して透
明な均一溶液とした。この溶液を100℃に加熱し
て濃縮して粘度100ポイズとした。この粘稠液を
使用し、実施例1と同様にしてα−アルミナ長繊
維を得た。 実施例 4 クエン酸3.84gを蒸溜水20mlに溶解した水溶液
にアルミニウムイソプロポキシド1.54gを加え溶
解させ、透明な均一溶液を得た。次いで90℃に加
熱して硫酸アルミニウム0.51gを加え、撹拌して
透明な均一溶液を得た。 この溶液を実施例1と同様にして粘度100ポイ
ズの粘稠液とし紡糸原液とした。これを実施例1
と同様にしてα−アルミナ長繊維とした。 なお、ノズルに代え、スリツトを使用すると膜
状物が得られ、また、太目の口径ノズルより押し
出し、火炎で焼成吹き飛ばすと、極細の短繊維が
得られる。 発明の効果 本発明の方法によると、紡糸原液の粘性を適当
なものに調整することが容易で、曳糸性、均一
性、安定性に優れ、紡糸性も良好せ、かつその製
造も容易である。しかも紡糸原液のアルミニウム
原料がアルミニウムの有機化合物あるいはこれと
無機酸アルミニウムを使用し、これを溶解する化
合物が有機酸水溶液からなるため、加熱により分
解成分の除去も容易で純粋なアルミナ繊維または
膜状物を紡糸により容易に得られる優れた効果を
有する。
A viscous solution containing polyaluminoxane, an inorganic polymer having a main chain consisting of the following formula, is mixed with a silicic acid ester, then dry spun and fired. The slurry method uses Al2O3 fine powder and a small amount of MgCl2 .
Al 2 (OH) 3 Cl is added as a binder component to 6H 2 O to form a viscous slurry, which is then dry spun and fired. In the inorganic salt method, a water-soluble organic polymer such as polyethylene oxide or PVA is added to an aqueous solution of aluminum salt, and water-soluble polysiloxane is further mixed to form a viscous liquid, which is then blown out from a nozzle and fired. In the sol-gel method, silica sol and boric acid are added to alumina sol containing ions such as HCOO and CH 3 COO to form a viscous liquid, which is then spun and fired. However, all of these methods have the following problems. In order to spin fibers using a spinning solution, the spinning dope is important, and the physical properties of the solution such as viscosity, spinnability, uniformity, and stability are important factors, and the spinning dope is easy to manufacture. The important factors are that the spinnability is excellent. From this perspective, although the precursor polymer method has high uniformity, it is difficult to control the manufacturing process for producing the spinning dope. In the sol-gel method, it is difficult to control the concentration because precipitation and turbidity occur during the concentration stage, and the viscosity increases rapidly. Since the inorganic salt method uses a water-soluble organic polymer to provide the viscosity that gives the fiber form, the stock solution may lack stability, such as gelation during the preparation stage. In addition, the slurry method is a so-called heterogeneous system, and there are problems such as the particle size, amount added, dispersion state, etc. of solid particles constituting the spinning dope slightly affect spinnability, making it difficult to control. Purpose of the Invention The present invention aims to eliminate the problems associated with the spinning dope in the conventional method.The purpose of the present invention is to easily adjust the viscosity of the spinning dope and improve spinnability, uniformity, and stability. It is an object of the present invention to provide a method for easily producing alumina fibers or membrane-like products by providing excellent spinnability, good spinnability, and easy production. Structure of the Invention As a result of intensive research to achieve the above object, the present inventors found that 2 to 3 carboxyl groups and 1 to 1 hydroxyl group
A soluble aluminum organic compound is dissolved in an aqueous solution of an organic acid having two carboxyl groups or an organic acid having two carboxyl groups to form a homogeneous solution, and this is heated and concentrated to remove excess water and dissolve. It has been found that by removing the organic residues, a uniform and stable spinning stock solution with viscosity and spinnability suitable for spinning can be easily obtained. In addition, if a viscous liquid is produced in the same manner as above using the aluminum organic compound and an appropriate amount of aluminum inorganic acid salt, and this is used as a spinning stock solution, the fiber obtained by spinning can be fired and sintered. It has been found that during this process, volatile components are reduced, making sintering easier. The present invention was completed based on these findings. The gist of the present invention is as follows: (1) An aluminum organic compound soluble in an organic acid aqueous solution has 2 to 3 carboxyl groups and 1 to 1 hydroxyl group.
2 unique organic acid or carboxyl group
It is characterized by dissolving it in an aqueous solution of its own basic acid, heating and concentrating it to form a viscous liquid, extruding this viscous liquid through a nozzle or slit, forming it into a fibrous or film-like material, and then sintering it. A method for producing alumina fibers or membranes. (2) Both compounds in which the aluminum organic compound soluble in an organic acid aqueous solution is 50 mol% or more in terms of Al 2 O 3 and the aluminum inorganic acid salt is less than 50 mol % in terms of Al 2 O 3 are A mixed solution is prepared by dissolving an organic acid having 2 to 3 groups and 1 to 2 hydroxyl groups or an organic acid having 2 carboxyl groups in an aqueous solution, and this is heated and concentrated to form a viscous liquid, and this viscous liquid is A method for producing alumina fibers or membranes, which comprises extruding the alumina fibers or membranes through a nozzle or slit, forming them into fibers or membranes, and then sintering them. Examples of the aluminum organic compound dissolved in the organic acid aqueous solution used in the present invention include aluminum alkoxide, aluminum carboxylate, and aluminum acetylacetonate. Examples of the aluminum alkoxide include organic residues such as a methoxy group, an ethoxy group, a normal propoxy group, an isopropoxy group, a normal butoxy group, a secondary butoxy group, and a tertiary butoxy group. Further, as the aluminum carboxylate, organic residues include a formyloxy group and an acetyloxy group. Examples of the aluminum inorganic acid salt used in the present invention include aluminum oxychloride, aluminum chloride, aluminum sulfate, and aluminum nitrate. When an aluminum organic compound and an aluminum inorganic acid salt compound are used together, it is necessary that the aluminum organic compound accounts for 50 mol % or more in terms of Al 2 O 3 . If it is less than 50 mol%, it will be difficult to solidify it into a fiber-formed product. 2 to 3 carboxyl groups used in the present invention
Examples of organic acids having 1 to 2 hydroxyl groups include etc. In addition, examples of organic acids having two carboxyl groups include: can be mentioned. The spinning stock solution is dissolved in the organic acid aqueous solution containing distilled water in an amount of 20 to 50 times the mole of the amminium organic compound. The amount of organic acid is at least 1 times the mole of the aluminum element in the aluminum organic compound or aluminum inorganic acid salt,
A suitable amount is preferably 1.5 to 2.0 times the molar amount. Dissolution is performed at room temperature or at a temperature up to about 90°C with stirring. In order to improve the physical properties of the alumina fibers or membranes, add small amounts of lithium, beryllium, boron, sodium, calcium, potassium, magnesium, silicon, barylium, chromium, manganese, yttrium, and lanthanum to this solution, as necessary. , tungsten, iron, nickel, copper, zinc, etc., are added as an organic metal compound, carbonate, or inorganic acid salt. The resulting solution is heated to 100°C or higher in an open system and concentrated. This concentration is carried out until a viscous state is obtained. The resulting viscous liquid has fluidity at 70 to 80°C, but when left at room temperature, it gradually increases in viscosity and eventually solidifies. This phenomenon becomes more noticeable in a dry atmosphere. Therefore, continuous fibers can be obtained by extruding this viscous liquid from a nozzle into a dry atmosphere below room temperature while heating it at 70 to 80°C. After removing moisture from the resulting fibers in a dry atmosphere, they are fired in air at 700 to 1000°C to decompose and remove organic components. Alumina long fibers are obtained by sintering this at 1200 to 1400°C. In this case, ultrafine short fibers can be obtained by extruding through a thick diameter nozzle and burning and blowing away with flame. Furthermore, a film-like material can be obtained by using a slit instead of a nozzle. The aluminum organic compound and aluminum inorganic acid salt are used as the aluminum raw material composition.
When used together in an amount of less than 50 mol% in terms of Al 2 O 3 , the volatile content decreases during firing and sintering, making sintering easier. In this case, if the aluminum inorganic acid salt is used in an amount greater than the above amount, the viscous liquid becomes difficult to solidify, so the amount needs to be less than 50 mol%. Example 1 2.20 g of aluminum isopropoxide was added to an aqueous solution of 2.88 g of citric acid dissolved in 20 ml of distilled water and stirred to obtain a transparent homogeneous solution. This solution was heated to 100℃.
It was heated and concentrated to a viscosity of 100 poise. This concentrated liquid was extruded through a nozzle at 70 to 80°C into room temperature dry air to obtain colorless and transparent long fibers with a diameter of 5 to 100 μm. The resulting fibers were dried at 100°C overnight, then heat treated at 900°C for 2 hours, and then heated at 1100°C.
It was heated for 2 hours and sintered. As a result, α-alumina long fibers were obtained. Example 2 An aqueous solution of 3.00 g of tartaric acid dissolved in 20 ml of distilled water was
Heat to 90℃ and add basic aluminum acetate to this.
3.78 g of tetrahydrate was added and stirred to obtain a transparent homogeneous solution. This was made into a concentrated solution with a viscosity of 100 poise in the same manner as in Example 1, and used as a spinning dope. Thereafter, α-alumina long fibers were obtained in the same manner as in Example 1. Example 3 1.32 g of aluminum isopropoxide was added to an aqueous solution of 3.84 g of citric acid dissolved in 20 ml of distilled water.
A clear homogeneous solution was obtained by stirring. 0.97 g of aluminum chloride hexahydrate was added to this and stirred to form a transparent homogeneous solution. This solution was heated to 100°C and concentrated to a viscosity of 100 poise. Using this viscous liquid, α-alumina long fibers were obtained in the same manner as in Example 1. Example 4 1.54 g of aluminum isopropoxide was added and dissolved in an aqueous solution of 3.84 g of citric acid dissolved in 20 ml of distilled water to obtain a transparent homogeneous solution. The mixture was then heated to 90° C., 0.51 g of aluminum sulfate was added, and stirred to obtain a clear homogeneous solution. This solution was made into a viscous liquid with a viscosity of 100 poise in the same manner as in Example 1, and used as a spinning dope. Example 1
α-alumina long fibers were obtained in the same manner as above. Note that if a slit is used instead of a nozzle, a film-like product can be obtained, and if it is extruded through a thick diameter nozzle and burned and blown away with flame, ultrafine short fibers can be obtained. Effects of the Invention According to the method of the present invention, it is easy to adjust the viscosity of the spinning dope to an appropriate value, it has excellent spinnability, uniformity, and stability, it has good spinnability, and it is easy to manufacture. be. Moreover, since the aluminum raw material of the spinning dope is an organic compound of aluminum or an inorganic acid aluminum, and the compound that dissolves this is an organic acid aqueous solution, it is easy to remove decomposed components by heating, and it is possible to form pure alumina fibers or membranes. It has excellent effects that can be easily obtained by spinning.

Claims (1)

【特許請求の範囲】 1 有機酸水溶液に可溶なアルミニウム有機化合
物を、カルボキシル基を2〜3個と水酸基を1〜
2個有する有機酸あるいはカルボキシル基2個を
有する有機酸の水溶液に溶解した後、加熱濃縮し
て粘稠液となし、この粘稠液をノズルまたはスリ
ツトより押し出して繊維状または膜状物に成形し
た後焼結することを特徴とするアルミナ繊維また
は膜状物の製造法。 2 有機酸水溶液に可溶なアルミニウム有機化合
物がAl2O3に換算して50モル%以上とアルミニウ
ム無機酸塩がAl2O3に換算して50モル%未満の両
化合物を、カルボキシル基を2〜3個と水酸基を
1〜2個有する有機酸あるいはカルボキシル基を
2個有する有機酸の水溶液に溶解した混合液とな
しこれを加熱濃縮して粘稠液となし、この粘稠液
をノズルまたはスリツトより押し出して繊維状ま
たは膜状物に成形した後焼結することを特徴とす
るアルミナ繊維または膜状物の製造法。
[Scope of Claims] 1. An aluminum organic compound soluble in an organic acid aqueous solution has 2 to 3 carboxyl groups and 1 to 1 hydroxyl group.
After dissolving in an aqueous solution of an organic acid having two carboxyl groups or an organic acid having two carboxyl groups, it is heated and concentrated to form a viscous liquid, and this viscous liquid is extruded through a nozzle or slit to form a fibrous or film-like product. A method for producing alumina fibers or membrane-like materials, which comprises sintering the alumina fibers or membranes. 2 Both compounds in which the aluminum organic compound soluble in an organic acid aqueous solution is 50 mol% or more in terms of Al 2 O 3 and the aluminum inorganic acid salt is less than 50 mol % in terms of Al 2 O 3 are combined with carboxyl groups. A mixed solution is prepared by dissolving an organic acid having 2 to 3 carboxyl groups and 1 to 2 hydroxyl groups or an organic acid having 2 carboxyl groups.This is heated and concentrated to form a viscous liquid, and this viscous liquid is passed through a nozzle. Or, a method for producing alumina fibers or membranes, which comprises extruding them through a slit, forming them into fibers or membranes, and then sintering them.
JP63251635A 1988-10-05 1988-10-05 Manufacturing method for alumina fibers or membranes Granted JPH02102116A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63251635A JPH02102116A (en) 1988-10-05 1988-10-05 Manufacturing method for alumina fibers or membranes

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63251635A JPH02102116A (en) 1988-10-05 1988-10-05 Manufacturing method for alumina fibers or membranes

Publications (2)

Publication Number Publication Date
JPH02102116A JPH02102116A (en) 1990-04-13
JPH0478732B2 true JPH0478732B2 (en) 1992-12-14

Family

ID=17225755

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63251635A Granted JPH02102116A (en) 1988-10-05 1988-10-05 Manufacturing method for alumina fibers or membranes

Country Status (1)

Country Link
JP (1) JPH02102116A (en)

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3917808A (en) * 1972-10-16 1975-11-04 Continental Oil Co Method for extruding alumina
JPS6215328A (en) * 1985-07-08 1987-01-23 Idemitsu Kosan Co Ltd Production of alumina fiber
JPS63165521A (en) * 1986-12-27 1988-07-08 Nippon Steel Corp Production of alumina fiber

Also Published As

Publication number Publication date
JPH02102116A (en) 1990-04-13

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