JPH0217643B2 - - Google Patents
Info
- Publication number
- JPH0217643B2 JPH0217643B2 JP18982482A JP18982482A JPH0217643B2 JP H0217643 B2 JPH0217643 B2 JP H0217643B2 JP 18982482 A JP18982482 A JP 18982482A JP 18982482 A JP18982482 A JP 18982482A JP H0217643 B2 JPH0217643 B2 JP H0217643B2
- Authority
- JP
- Japan
- Prior art keywords
- fibers
- heat treatment
- weight
- alumina
- flexibility
- 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
Links
- 239000000835 fiber Substances 0.000 claims description 51
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 25
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 claims description 24
- 238000010438 heat treatment Methods 0.000 claims description 24
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 12
- 239000001257 hydrogen Substances 0.000 claims description 12
- 229910052739 hydrogen Inorganic materials 0.000 claims description 12
- 239000000395 magnesium oxide Substances 0.000 claims description 12
- 159000000003 magnesium salts Chemical class 0.000 claims description 9
- AZDRQVAHHNSJOQ-UHFFFAOYSA-N alumane Chemical class [AlH3] AZDRQVAHHNSJOQ-UHFFFAOYSA-N 0.000 claims description 6
- 239000000243 solution Substances 0.000 claims description 6
- 238000009987 spinning Methods 0.000 claims description 6
- 239000007864 aqueous solution Substances 0.000 claims description 5
- 238000004519 manufacturing process Methods 0.000 claims description 5
- 238000001035 drying Methods 0.000 claims description 2
- 239000011148 porous material Substances 0.000 description 7
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 description 6
- 230000000052 comparative effect Effects 0.000 description 5
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 description 4
- 239000000460 chlorine Substances 0.000 description 3
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 2
- 229920000742 Cotton Polymers 0.000 description 2
- 230000002159 abnormal effect Effects 0.000 description 2
- 238000005452 bending Methods 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 description 2
- 229910001629 magnesium chloride Inorganic materials 0.000 description 2
- 239000007858 starting material Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000006298 dechlorination reaction Methods 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- 239000004310 lactic acid Substances 0.000 description 1
- 235000014655 lactic acid Nutrition 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
Landscapes
- Inorganic Fibers (AREA)
Description
本発明は高可撓性のアルミナ繊維の製造方法に
関する。
従来、アルミナ繊維は例えば以下のようにして
製造されている。まず、アルミニウム塩、例えば
塩基性塩化アルミニウム(Al2(OH)5Cl・
2.4H2O)、の水溶液を加熱濃縮して粘稠な紡糸液
を調製する。次に、この紡糸液を外周面に多数の
孔を有する遠心紡糸器に入れて高速度で回転し、
集綿室で集綿して紡糸繊維を得る。つづいてこの
紡糸繊維を乾燥して乾燥繊維を得る。つづいて、
この乾燥繊維を約600℃で予備熱処理し、大部分
の水及び塩素を除去して酸化物に転化させ、一次
繊維を得る。つづいて、この一次繊維を空気中、
約1000℃で熱処理し、最終的なアルミナ繊維を得
る。
しかし、上述した従来の方法により得られたア
ルミナ繊維は1500℃以上の高温下で可撓性が劣る
という欠点がある。
本発明は上記欠点を解消するためになされたも
のであり、高温下においても高可撓性を有するア
ルミナ繊維を製造し得る方法を提供しようとする
ものである。
アルミナ繊維(通常3〜5μmの直径を有する)
の高温下での可撓性は繊維を構成する結晶子の大
きさ及び結晶子中の気孔の多少に影響を受け、結
晶子が大きく、気孔が多いほど可撓性が劣ると考
えられている。
そこで、本発明者らは上述したようなアルミナ
繊維の可撓性に悪影響を及ぼす原因を除去し得る
条件について種々検討を行い、まず水素雰囲気中
での高温熱処理による効果を調べた。すなわち、
600℃で予備熱処理(脱水・脱塩素)することに
より得られた一次繊維に水素雰囲気中で1000℃以
上の熱処理を施せば、最終的なアルミナ繊維を構
成する結晶子中の気孔の消滅を促進することがで
きる。
しかし、上述した水素雰囲気中での高温熱処理
だけではアルミナ繊維の可撓性を十分に向上でき
ないことが判明した。すなわち、紡糸繊維100重
量部が以後の工程によつてどのように重量変化す
るかを調べたところ、乾燥繊維は77.4重量部、予
備熱処理後の一次繊維は42.4重量部、水素雰囲気
中での高温熱処理後の最終的なアルミナ繊維は
35.9重量部であり、乾燥繊維を予備熱処理する際
の体積収縮が大きいことが判つた。したがつて、
予備熱処理時の繊維の体積収縮に起因して気孔や
亀裂が発生し、水素雰囲気中での高温熱処理だけ
では、これら気孔や亀裂を十分に消滅させること
はできず、しかも、結晶子の異常成長を十分に阻
止することができないため、アルミナ繊維の可撓
性を十分に向上できないことが判明した。
そこで、本発明者らは更に検討を重ねた結果、
水素雰囲気中で高温熱処理を行うという条件のほ
かに、出発物質であるアルミニウム塩に適量のマ
グネシウム塩を添加しておけばよいことを究明し
た。すなわち、最初に適量のマグネシウム塩を添
加しておけば予備熱処理により酸化物に転化して
生成するマグネシアが繊維の体積収縮を抑制でき
るとともに水素雰囲気中での高温熱処理時に結晶
子の異常成長を阻止することができる。また、適
量のマグネシアは予備熱処理時、水素雰囲気中で
の高温熱処理のいずれにおいても気孔の消滅に有
効であるため、アルミナ繊維の可撓性を向上する
ことができる。更に、マグネシウム塩の添加量に
ついて検討したところ、アルミニウム塩及びマグ
ネシウム塩がアルミナ及びマグネシアに転化した
最終的なアルミナ繊維においてマグネシア換算で
6重量%以下になるようにマグネシウム塩を添加
すればアルミナ繊維の可撓性を大幅に向上し得る
ことを究明した。
すなわち、本発明のアルミナ繊維の製造方法
は、アルミニウム塩及びマグネシウム塩を含む水
溶液を加熱濃縮して粘稠な紡糸液とし、これを紡
糸した繊維を乾燥した後予備熱処理して脱水・脱
塩素し、更に水素雰囲気中、高温で熱処理するこ
とによりマグネシアを6重量%以下含有させるこ
とを特徴とするものである。
なお、本発明においてアルミニウム塩に添加さ
れるマグネシウム塩の添加量の下限は最終的なア
ルミナ繊維においてマグネシア換算で約0.1重量
%になるようにすることが望ましい。
また、本発明における水素雰囲気中での高温熱
処理は1000℃以上、好ましくは1200℃以上で行う
ことが望ましい。これは1000℃未満では繊維を構
成する結晶子中の気孔を消滅させる効果が小さい
ためである。
以下、本発明の実施例を説明する。
実施例1〜6及び比較例1〜4まず、塩基性塩
化アルミニウム〔Al2(OH)5Cl2.4H2O)の50%水
溶液に、Al2O3とMgOに転化したときにMgO換
算で下記表に示す重量%となるように塩化マグネ
シウム(MgCl2・6H2O)を添加した。次に、こ
の水溶液に前記塩基性塩化アルミニウム及び塩化
マグネシウムの固形分100重量部に対し乳酸を120
重量部加えた。つづいて、加熱濃縮して室温にお
ける粘度が150ポイスの紡糸液を調製した。つづ
いて、この紡糸液を直径0.4mmの多数の孔を有す
る遠心紡糸器に入れ、3600rpmの速度で回転し、
相対湿度50%の集綿室で集綿して紡糸繊維を得
た。得られた紡糸繊維の平均直径は4μmであつ
た。つづいて、この紡糸繊維を常温下相対湿度50
%の空気中で乾燥して乾燥繊維を得た。つづい
て、この乾燥繊維をネツトコンベアを用いて昇温
速度35℃/minの条件で最高温度600℃の炉中を通
過させた。この予備熱処理により、大部分の水と
塩素が除去されて出発物質が酸化物に転化する。
この結果、白色で粉化しやすい性質を有し、顕微
鏡下で不透明の一次繊維を得た。つづいて、この
一次繊維を密封し得る炉に入れ、炉内をN2ガス
で置換し、更に、H2ガスで置換した後、1000℃
あるいは1200℃まで急速に昇温し、そのまま1時
間保持することにより最終的なアルミナ繊維を得
た。
得られた各アルミナ繊維を12mm厚のブランケツ
トとし、このブランケツトの1500℃及び1600℃に
おける破断屈曲回数を調べ、下記表に併記する。
なお、下記表中比較例1及び4はマグネシウム
塩の添加量(表中ではアルミナ繊維中のマグネシ
ア含有量)が本発明の範囲外であるもの、比較例
2及び3はマグネシア含有量は本発明の範囲内で
あるが、水素雰囲気中で高温熱処理を行わず、空
気中で高温熱処理を行つたものである。
The present invention relates to a method for producing highly flexible alumina fibers. Conventionally, alumina fibers have been manufactured, for example, as follows. First, an aluminum salt, for example basic aluminum chloride (Al 2 (OH) 5 Cl.
A viscous spinning solution is prepared by heating and concentrating an aqueous solution of 2.4H 2 O). Next, this spinning solution is put into a centrifugal spinner having a large number of holes on the outer circumferential surface and rotated at high speed.
The cotton is collected in a cotton collection room to obtain spun fibers. Subsequently, the spun fibers are dried to obtain dry fibers. Continuing,
The dried fibers are preheated at about 600° C. to remove most of the water and chlorine and convert them into oxides to obtain primary fibers. Next, this primary fiber is placed in the air,
Heat treatment is performed at approximately 1000℃ to obtain the final alumina fiber. However, the alumina fibers obtained by the conventional method described above have a drawback of poor flexibility at high temperatures of 1500° C. or higher. The present invention has been made in order to eliminate the above-mentioned drawbacks, and aims to provide a method for producing alumina fibers that have high flexibility even at high temperatures. Alumina fibers (usually with a diameter of 3-5 μm)
The flexibility of fibers at high temperatures is affected by the size of the crystallites that make up the fibers and the number of pores in the crystallites, and it is thought that the larger the crystallites and the more pores, the poorer the flexibility. . Therefore, the present inventors conducted various studies on conditions that could eliminate the causes that adversely affect the flexibility of alumina fibers as described above, and first investigated the effect of high-temperature heat treatment in a hydrogen atmosphere. That is,
If the primary fiber obtained by preliminary heat treatment (dehydration and dechlorination) at 600℃ is heat treated at 1000℃ or higher in a hydrogen atmosphere, the pores in the crystallites that make up the final alumina fiber will be eliminated. can do. However, it has been found that the flexibility of alumina fibers cannot be sufficiently improved only by the above-described high-temperature heat treatment in a hydrogen atmosphere. In other words, when we investigated how the weight of 100 parts of spun fiber changes depending on the subsequent steps, we found that the dry fiber was 77.4 parts by weight, the primary fiber after preliminary heat treatment was 42.4 parts by weight, and the weight of 100 parts by weight of spun fiber was 77.4 parts by weight after preliminary heat treatment. The final alumina fiber after heat treatment is
The amount was 35.9 parts by weight, and it was found that the volumetric shrinkage during preliminary heat treatment of dry fibers was large. Therefore,
Pores and cracks occur due to volumetric shrinkage of the fibers during preliminary heat treatment, and high-temperature heat treatment in a hydrogen atmosphere alone cannot sufficiently eliminate these pores and cracks, and also causes abnormal growth of crystallites. It was found that the flexibility of alumina fibers could not be sufficiently improved because of the inability to sufficiently prevent this. Therefore, as a result of further investigation, the present inventors found that
In addition to the condition of performing high-temperature heat treatment in a hydrogen atmosphere, the researchers discovered that it is sufficient to add an appropriate amount of magnesium salt to the starting material, aluminum salt. In other words, if an appropriate amount of magnesium salt is added at the beginning, magnesia, which is converted into an oxide and generated during preliminary heat treatment, can suppress the volumetric shrinkage of the fibers and also prevent abnormal growth of crystallites during high-temperature heat treatment in a hydrogen atmosphere. can do. In addition, since an appropriate amount of magnesia is effective in eliminating pores both during preliminary heat treatment and high-temperature heat treatment in a hydrogen atmosphere, it is possible to improve the flexibility of the alumina fiber. Furthermore, we investigated the amount of magnesium salt added and found that if the magnesium salt is added so that the amount of aluminum salt and magnesium salt is 6% by weight or less in terms of magnesia in the final alumina fiber that has been converted into alumina and magnesia, the alumina fiber can be improved. We have discovered that flexibility can be significantly improved. That is, the method for producing alumina fibers of the present invention involves heating and concentrating an aqueous solution containing an aluminum salt and a magnesium salt to form a viscous spinning solution, drying the spun fibers, and then preheating them to dehydrate and dechlorinate them. Furthermore, it is characterized by containing 6% by weight or less of magnesia by heat treatment at high temperature in a hydrogen atmosphere. In the present invention, the lower limit of the amount of magnesium salt added to the aluminum salt is preferably about 0.1% by weight in terms of magnesia in the final alumina fiber. Further, the high temperature heat treatment in a hydrogen atmosphere in the present invention is desirably performed at a temperature of 1000°C or higher, preferably 1200°C or higher. This is because at temperatures below 1000°C, the effect of eliminating pores in the crystallites constituting the fibers is small. Examples of the present invention will be described below. Examples 1 to 6 and Comparative Examples 1 to 4 First, in a 50% aqueous solution of basic aluminum chloride [Al 2 (OH) 5 Cl2.4H 2 O), when converted into Al 2 O 3 and MgO, in terms of MgO, Magnesium chloride (MgCl 2 .6H 2 O) was added in the weight percent shown in the table below. Next, 120 parts by weight of lactic acid was added to this aqueous solution based on 100 parts by weight of the solid content of the basic aluminum chloride and magnesium chloride.
Added parts by weight. Subsequently, the mixture was heated and concentrated to prepare a spinning solution having a viscosity of 150 poise at room temperature. Next, this spinning solution was put into a centrifugal spinner with a large number of holes with a diameter of 0.4 mm, and rotated at a speed of 3600 rpm.
The fibers were collected in a collection room with a relative humidity of 50% to obtain spun fibers. The average diameter of the resulting spun fibers was 4 μm. Next, this spun fiber was processed at room temperature with a relative humidity of 50°C.
% in air to obtain dry fibers. Subsequently, the dried fibers were passed through a furnace at a maximum temperature of 600°C using a net conveyor at a heating rate of 35°C/min. This preheat treatment removes most of the water and chlorine and converts the starting material to oxide.
As a result, primary fibers were obtained which were white in color, easily powdered, and opaque under a microscope. Next, this primary fiber was placed in a sealed furnace, and the inside of the furnace was replaced with N 2 gas, and then replaced with H 2 gas, and then heated to 1000°C.
Alternatively, final alumina fibers were obtained by rapidly raising the temperature to 1200°C and maintaining it for 1 hour. Each of the obtained alumina fibers was made into a 12 mm thick blanket, and the number of times of rupture and bending of this blanket at 1500°C and 1600°C was determined and is also listed in the table below. In addition, in Comparative Examples 1 and 4 in the table below, the amount of magnesium salt added (magnesia content in the alumina fiber in the table) is outside the range of the present invention, and in Comparative Examples 2 and 3, the magnesia content is outside the range of the present invention. However, the high-temperature heat treatment was performed in air instead of in a hydrogen atmosphere.
【表】【table】
【表】
上記表から明らかなように比較例1及び4のア
ルミナ繊維はMgO含有率が本発明の範囲外であ
るのでいずれも破断屈曲回数が少なく可撓性が劣
る。また、比較例2及び3のアルミナ繊維は水素
中ではなく空気中で高温熱処理を行つているため
可撓性が劣つている。これに対して、実施例1〜
6のアルミナ繊維はいずれも可撓性が向上してお
り、特に実施例2及び3のものは1600℃において
も高い可撓性を示している。
以上詳述した如く、本発明によれば、高温下に
おいても高可撓性を有するアルミナ繊維を製造し
得る方法を提供できるものである。[Table] As is clear from the above table, the alumina fibers of Comparative Examples 1 and 4 have MgO contents outside the range of the present invention, so both have a small number of bending times at break and are inferior in flexibility. Furthermore, the alumina fibers of Comparative Examples 2 and 3 had poor flexibility because they were subjected to high-temperature heat treatment in air rather than in hydrogen. On the other hand, Examples 1-
All of the alumina fibers of Example 6 have improved flexibility, and especially those of Examples 2 and 3 show high flexibility even at 1600°C. As described in detail above, according to the present invention, it is possible to provide a method for producing alumina fibers having high flexibility even at high temperatures.
Claims (1)
加熱濃縮して粘稠な紡糸液とし、これを紡糸した
繊維を乾燥した後、予備熱処理して脱水・脱塩素
し、更に水素雰囲気中、高温で熱処理することに
よりマグネシアを6重量%以下含有させることを
特徴とするアルミナ繊維の製造方法。1. By heating and concentrating an aqueous solution of aluminum salts and magnesium salts to form a viscous spinning solution, and drying the fibers spun from this, preheat treatment is performed to dehydrate and dechlorinate, and further heat treatment at high temperature in a hydrogen atmosphere. A method for producing alumina fiber, characterized by containing 6% by weight or less of magnesia.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18982482A JPS5982412A (en) | 1982-10-28 | 1982-10-28 | Manufacture of alumina fiber |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18982482A JPS5982412A (en) | 1982-10-28 | 1982-10-28 | Manufacture of alumina fiber |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5982412A JPS5982412A (en) | 1984-05-12 |
| JPH0217643B2 true JPH0217643B2 (en) | 1990-04-23 |
Family
ID=16247818
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP18982482A Granted JPS5982412A (en) | 1982-10-28 | 1982-10-28 | Manufacture of alumina fiber |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5982412A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6221821A (en) * | 1985-07-19 | 1987-01-30 | Mitsubishi Chem Ind Ltd | Production of inorganic oxide fiber |
| AU2006313594B2 (en) | 2005-11-10 | 2011-06-09 | Morgan Advanced Materials Plc | High temperature resistant fibres |
-
1982
- 1982-10-28 JP JP18982482A patent/JPS5982412A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5982412A (en) | 1984-05-12 |
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