JPH0455334A - Production of inorganic fiber - Google Patents
Production of inorganic fiberInfo
- Publication number
- JPH0455334A JPH0455334A JP16364690A JP16364690A JPH0455334A JP H0455334 A JPH0455334 A JP H0455334A JP 16364690 A JP16364690 A JP 16364690A JP 16364690 A JP16364690 A JP 16364690A JP H0455334 A JPH0455334 A JP H0455334A
- Authority
- JP
- Japan
- Prior art keywords
- sol
- fibrous
- solvent
- org
- atmosphere
- 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
Links
- 239000012784 inorganic fiber Substances 0.000 title claims description 10
- 238000004519 manufacturing process Methods 0.000 title claims description 10
- 239000000835 fiber Substances 0.000 claims abstract description 17
- 238000009987 spinning Methods 0.000 claims abstract description 17
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims abstract description 9
- 238000006460 hydrolysis reaction Methods 0.000 claims abstract description 9
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 8
- 230000007062 hydrolysis Effects 0.000 claims abstract description 8
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 claims abstract description 6
- 239000000203 mixture Substances 0.000 claims abstract description 4
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 claims abstract description 3
- 239000003960 organic solvent Substances 0.000 claims description 21
- 238000006116 polymerization reaction Methods 0.000 claims description 8
- 150000002902 organometallic compounds Chemical class 0.000 claims description 6
- 238000010304 firing Methods 0.000 claims description 2
- 239000002904 solvent Substances 0.000 abstract description 14
- 239000002184 metal Substances 0.000 abstract description 7
- 229910052751 metal Inorganic materials 0.000 abstract description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 7
- 150000004703 alkoxides Chemical class 0.000 abstract description 4
- 239000003054 catalyst Substances 0.000 abstract description 3
- 229910001507 metal halide Inorganic materials 0.000 abstract description 2
- 150000005309 metal halides Chemical class 0.000 abstract description 2
- 239000002253 acid Substances 0.000 abstract 1
- 150000003839 salts Chemical class 0.000 abstract 1
- 230000008016 vaporization Effects 0.000 abstract 1
- 238000003980 solgel method Methods 0.000 description 7
- 230000000694 effects Effects 0.000 description 5
- 230000008020 evaporation Effects 0.000 description 5
- 238000001704 evaporation Methods 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 238000007711 solidification Methods 0.000 description 5
- 230000008023 solidification Effects 0.000 description 5
- 239000004744 fabric Substances 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 239000002344 surface layer Substances 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000003365 glass fiber Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- VXUYXOFXAQZZMF-UHFFFAOYSA-N titanium(IV) isopropoxide Chemical compound CC(C)O[Ti](OC(C)C)(OC(C)C)OC(C)C VXUYXOFXAQZZMF-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- 235000012012 Paullinia yoco Nutrition 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000001879 gelation Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 239000011147 inorganic material Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- -1 organic acid salts Chemical class 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229920005594 polymer fiber Polymers 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B37/00—Manufacture or treatment of flakes, fibres, or filaments from softened glass, minerals, or slags
- C03B37/01—Manufacture of glass fibres or filaments
- C03B37/011—Manufacture of glass fibres or filaments starting from a liquid phase reaction process, e.g. through a gel phase
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Geochemistry & Mineralogy (AREA)
- Life Sciences & Earth Sciences (AREA)
- Dispersion Chemistry (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Inorganic Fibers (AREA)
- Glass Melting And Manufacturing (AREA)
- Manufacture, Treatment Of Glass Fibers (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、ゾル−ゲル法による無機繊維の製造方法に関
する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for producing inorganic fibers by a sol-gel method.
金属アルコキシドからガラス、セラミックス等の無機物
を製造する方法は、一般にゾル−ゲル法と呼ばれている
。このゾル−ゲル法により繊維を製造しようとする場合
、通常以下の手順をとる。A method for producing inorganic materials such as glasses and ceramics from metal alkoxides is generally called a sol-gel method. When attempting to manufacture fibers by this sol-gel method, the following steps are usually taken.
金属アルコキシドに水、触媒及び必要に応じて溶媒を添
加、混合する。溶液中で加水分解・重合反応が進行し、
高分子が形成され、ゾル溶液となる。この反応が進行す
るにともないゾル溶液の粘度は徐々に上昇する。ゾル溶
液が適当な粘度に達したところで通常の方法により紡糸
すると、繊維状ゲルが得られる。このゾル−ゲル法によ
り繊維を紡糸した場合、一般に得られた繊維の断面形状
が楕円形、繭形などの非円形形状を示し、Eガラスファ
イバーに見られる様なほぼ真円形の断面形状を有したフ
ァイバーを得るのは困難である。例えば、KAMIYA
らは、原料を限定されたモル比で調合しなければ円形断
面は出現しないと述べている(l(、KAMIYA a
nd T、YOKO:Jounal of Mater
ial 5cience、Vol、21. (1986
) 、842−848)。 したがって、調合を厳密に
行わなくてはならず操作が困難である、という欠点を有
する。Water, a catalyst and, if necessary, a solvent are added to the metal alkoxide and mixed. Hydrolysis and polymerization reactions proceed in the solution,
A polymer is formed and becomes a sol solution. As this reaction progresses, the viscosity of the sol solution gradually increases. When the sol solution reaches an appropriate viscosity, it is spun using a conventional method to obtain a fibrous gel. When fibers are spun using this sol-gel method, the cross-sectional shape of the resulting fibers generally has a non-circular shape such as an ellipse or a cocoon shape, and has an almost perfect circular cross-sectional shape like that seen in E-glass fibers. It is difficult to obtain fibers with a high temperature. For example, KAMIYA
state that a circular cross section will not appear unless the raw materials are mixed in a limited molar ratio (l(, KAMIYA a
nd T, YOKO: Journal of Mater
ial 5science, Vol, 21. (1986
), 842-848). Therefore, it has the disadvantage that the formulation must be strictly carried out and the operation is difficult.
また、太田らは、ブルーゲル法により製造したファイバ
ーの断面形状が、縦横比(長径/短径)1.5〜7.5
の長円形(楕円形を含む)になることを述べている(例
えば特開昭6l−24488)。同様に、水口らもゾル
溶液から紡糸を行い、断面形状がほぼ偏平状に成形され
た繊維体ゲルを得ている(例えば特開昭62−2306
43)。In addition, Ohta et al. reported that the cross-sectional shape of fibers produced by the blue gel method was 1.5 to 7.5 in aspect ratio (major axis/minor axis).
(For example, Japanese Patent Application Laid-Open No. 61-24488) states that the shape is oval (including elliptical). Similarly, Mizuguchi et al. performed spinning from a sol solution to obtain a fibrous gel with a nearly flat cross-sectional shape (for example, in Japanese Patent Application Laid-Open No. 62-2306
43).
このような断面形状が非円形の繊維の場合、ストランド
の見かけの外径及び織物の仕上がり厚みにばらつきがで
やすい、織物の通気性が悪くなる、又、織物の風合いが
悪い等の問題を生じる。In the case of fibers with such a non-circular cross-sectional shape, problems such as variations in the apparent outer diameter of the strands and finished thickness of the fabric, poor breathability of the fabric, and poor texture of the fabric may occur. .
本発明は、ゾル−ゲル法により製造した無機繊維に関し
、調合条件を限定せずに種々のゾルにつき断面形状が円
形に近い繊維を簡単に得ることを目的とする。The present invention relates to inorganic fibers produced by a sol-gel method, and an object of the present invention is to easily obtain fibers with a cross-sectional shape close to circular using various sols without limiting the blending conditions.
本発明者らは、有機金属化合物の加水分解・重合によっ
て得た粘稠なゾル溶液から紡糸したゲル繊維を焼成する
ことにより無機繊維を製造する方法において、断面形状
が円形に近い繊維を得るには、該粘稠なゾル溶液からの
紡糸中の繊維状ゾルまたは紡糸直後の繊維状ゾルを、有
機溶媒を含む雰囲気に接触させることが有効であること
を見いだした。The present inventors have developed a method for producing inorganic fibers by firing gel fibers spun from a viscous sol solution obtained by hydrolysis/polymerization of organometallic compounds. found that it is effective to bring the fibrous sol during spinning from the viscous sol solution or the fibrous sol immediately after spinning into contact with an atmosphere containing an organic solvent.
本発明で、使用する有機溶媒雰囲気としては、メタノー
ル、エタノール、プロパノール、ブタノール等を気化さ
れた状態で含む気体が適当である。この時、ゾルの調合
時に用いた有機溶媒及び有機金属化合物の加水分解反応
で生成する有機溶媒と、この有機溶媒雰囲気の有機溶媒
とを同じにすると最も大きな効果が得られるが、必ずし
も同じである必要はない。有機溶媒は一種でも良いし、
2種以上混合しても良い。また、この有機溶媒と共に、
発火を防ぐ目的で水蒸気を混合しても良い。有機溶媒雰
囲気中にその他のガス状物質を混合しても、有機溶媒と
反応を起こさないものであれば、さしつえはない。In the present invention, a gas containing methanol, ethanol, propanol, butanol, etc. in a vaporized state is suitable as the organic solvent atmosphere used. At this time, the greatest effect can be obtained if the organic solvent used when preparing the sol and the organic solvent generated by the hydrolysis reaction of the organometallic compound are the same as the organic solvent in the organic solvent atmosphere, but they are not necessarily the same. There's no need. One type of organic solvent may be used,
Two or more types may be mixed. In addition, along with this organic solvent,
Water vapor may be mixed in to prevent ignition. There is no problem even if other gaseous substances are mixed into the organic solvent atmosphere as long as they do not react with the organic solvent.
有機溶媒の濃度としては、有機溶媒が気化した状態で紡
糸雰囲気中に0.1〜1iovol%が適当である。0
.1vol%以下では、効果が小さく偏平な断面形状を
呈する。80vol%以上の場合、ゾル溶液の種類によ
っては繊維状ゾルの固化が遅なり巻取った際に付着を起
こす場合がある。好ましくは、1〜50vol%である
。The appropriate concentration of the organic solvent in the spinning atmosphere in a vaporized state is 0.1 to 1 iovol%. 0
.. If it is less than 1 vol%, the effect is small and a flat cross-sectional shape is exhibited. When the content is 80 vol% or more, depending on the type of sol solution, solidification of the fibrous sol may be delayed and adhesion may occur when the fibrous sol is wound up. Preferably it is 1 to 50 vol%.
ゾルを有機溶媒を含む雰囲気に接触させる時間は、繊維
径、ゾル溶液の種類、溶媒の種類、溶媒の濃度、温度等
により決まるが、繊維状ゾルが繊維状ゲルとなり、巻取
った際に変形したり付着したりしない様な状態になるま
での間、接触していればよい。通常は、数秒以上であれ
ばよい。この時、ゾルのゲル化を促進するような雰囲気
、例えば塩基性雰囲気あるいは水蒸気、などと混合され
た有機溶媒雰囲気であれば、接触させる時間は短くてよ
い。The time for which the sol is brought into contact with an atmosphere containing an organic solvent is determined by the fiber diameter, type of sol solution, type of solvent, solvent concentration, temperature, etc., but the fibrous sol becomes a fibrous gel and deforms when rolled up. It is sufficient that the contact is maintained until the state is such that no contact occurs. Normally, a few seconds or more is sufficient. At this time, the contact time may be short if the atmosphere promotes gelation of the sol, such as a basic atmosphere or an organic solvent atmosphere mixed with water vapor.
ノズルから流出した繊維状ゾルは、有機溶媒を含む雰囲
気中で固化することにより、断面形状がほぼ円形の繊維
状ゲルとなる。The fibrous sol flowing out from the nozzle solidifies in an atmosphere containing an organic solvent, thereby becoming a fibrous gel having a substantially circular cross-sectional shape.
本発明の紡糸に用いるゾル溶液の製造方法は特に限定さ
れず、よく知られた技術で作ることができる。The method for producing the sol solution used in the spinning of the present invention is not particularly limited, and it can be produced using well-known techniques.
本発明に用いられる原料としては、加水分解・重合反応
によってメタロキサン結合を作る有機金属化合物であれ
ば、どのようなものでもよい。例えば、金属アルコキシ
ド、金属ハロゲン化物、金属有機酸塩の有機金属化合物
が用いられる。この有機金属化合物に水、触媒、溶媒を
添加し、加水分解・重合反応を起こさせ、適当な粘度の
ゾル溶液を得る。The raw material used in the present invention may be any organometallic compound that forms metalloxane bonds through hydrolysis/polymerization reactions. For example, organometallic compounds such as metal alkoxides, metal halides, and metal organic acid salts are used. Water, a catalyst, and a solvent are added to this organometallic compound to cause a hydrolysis/polymerization reaction to obtain a sol solution with an appropriate viscosity.
ゾル溶液から紡糸を行う方法としては、特に限定されず
、例えば、従来のガラス繊維、高分子繊維などに適用さ
れる紡糸法を用いることができる。基本的には、常圧あ
るいは加圧下で、紡糸用ノズルからゾル溶液を流出させ
て繊維とする方法を用いる。The method for spinning from a sol solution is not particularly limited, and for example, a spinning method applicable to conventional glass fibers, polymer fibers, etc. can be used. Basically, a method is used in which a sol solution is made to flow out from a spinning nozzle under normal pressure or increased pressure to form fibers.
この様にして得た繊維状ゲルを、400℃〜1200℃
で焼結すると、断面形状が変化する事なく、断面形状が
ほぼ円形の無機繊維が得られる。The fibrous gel thus obtained was heated to 400°C to 1200°C.
When sintered, an inorganic fiber with a substantially circular cross-sectional shape can be obtained without changing the cross-sectional shape.
ゾル−ゲル法による紡糸で、繊維の断面形状が円形にな
らない原因として、以下の事が考えられる。紡糸された
繊維状ゾルが固化し繊維状ゲルとなる場合、溶媒の蒸発
による固化と、加水分解・重合反応の進展による固化と
がある。紡糸された繊維状ゾルからの溶媒の蒸発は表面
から起こり、表面層が先に固化を起こす。又、この時溶
媒の蒸発により重合反応が促進されるので、表面層の固
化はさらに進む。The following may be the reason why the cross-sectional shape of the fiber does not become circular during spinning using the sol-gel method. When the spun fibrous sol solidifies into a fibrous gel, there are two types of solidification: solidification due to evaporation of the solvent and solidification due to progress of hydrolysis/polymerization reactions. Evaporation of the solvent from the spun fibrous sol occurs from the surface, and the surface layer solidifies first. Further, since the polymerization reaction is promoted by evaporation of the solvent at this time, the solidification of the surface layer further progresses.
このように繊維状ゾルの表面層が内部より先に固化する
ため、表面に皮を張ったような状態となる。そして、そ
の後の内部の加水分解・重合反応及び溶媒の蒸発により
、収縮を起こし、偏平な断面形状の繊維状ゲルとなる。In this way, the surface layer of the fibrous sol solidifies before the inside, resulting in a skin-like state on the surface. Then, due to the subsequent internal hydrolysis/polymerization reaction and evaporation of the solvent, it shrinks and becomes a fibrous gel with a flat cross-sectional shape.
ここで、繊維状ゾルが、有機溶媒雰囲気にさらされた場
合、表面からの溶媒の蒸発が抑制される。そのため、繊
維状ゲルの表面のみが固くなる現象が抑制される。それ
ゆえ、断面形状が偏平になることなく、はぼ円形の断面
形状を有する繊維が得られる。この作用は、ゾルの調合
組成条件に左右されることなくかないため、あらゆるゾ
ルに適用ができる。Here, when the fibrous sol is exposed to an organic solvent atmosphere, evaporation of the solvent from the surface is suppressed. Therefore, the phenomenon in which only the surface of the fibrous gel becomes hard is suppressed. Therefore, fibers having a substantially circular cross-sectional shape can be obtained without the cross-sectional shape being flat. This effect is achieved regardless of the compositional conditions of the sol, so it can be applied to any sol.
以下、実施例に基づき本発明の詳細な説明を行うが、本
発明は必ずしもこれらの実施例に限定されることはない
。Hereinafter, the present invention will be described in detail based on Examples, but the present invention is not necessarily limited to these Examples.
所定量のモル比で、テトラエトキシオルトシラン(Si
(C2H50H)4)、 ジメチルジェトキシシラン(
(CH3)2Si(C2H501)2)、 チタンイソ
プロポキシド(Ti(0−iC3H7)4) 、水、塩
酸及びエタノールを混合した。30℃で反応を進め、2
00cPoiseで0℃に冷却を行い、 さらに600
cPoiseになったところで30℃に冷却を行った。Tetraethoxyorthosilane (Si
(C2H50H)4), dimethyljethoxysilane (
(CH3)2Si(C2H501)2), titanium isopropoxide (Ti(0-iC3H7)4), water, hydrochloric acid and ethanol were mixed. Proceed the reaction at 30°C,
Cooled to 0℃ with 00cPoise and further 600℃
When the temperature reached cPoise, it was cooled to 30°C.
溶液の粘度が1000cPoiseに達したところで、
内側直径0 、3mmのノズルを使用し、窒素ガスで加
圧することにより、紡糸を行った。ノズルの下にパイプ
(30c+n角、長さ5m)を設置し、そのパイプ内に
有機溶媒を気化して送り込み、2〜50vol%の濃度
の有機溶媒雰囲気とした。When the viscosity of the solution reaches 1000 cPoise,
Spinning was carried out by using a nozzle with an inner diameter of 0.3 mm and pressurizing with nitrogen gas. A pipe (30c+n square, length 5m) was installed under the nozzle, and an organic solvent was vaporized and sent into the pipe to create an organic solvent atmosphere with a concentration of 2 to 50 vol%.
採取した繊維状ゲルの断面形状を顕微鏡で観察を行ない
、偏平率を求めた。The cross-sectional shape of the collected fibrous gel was observed under a microscope, and the oblateness was determined.
ここで、 偏平率(%)=100X(長径−短径)/長径である。here, Oblateness (%) = 100X (longer axis - shorter axis)/longer axis.
従って、偏平率が大きいほど偏平であり、偏平率が小さ
いほど円形に近い。偏平率が0%で真円である。Therefore, the larger the oblateness is, the flatter it is, and the smaller the oblateness is, the closer it is to a circle. It is a perfect circle with an oblateness of 0%.
表1に、調合比、湿度と偏平率を示す。偏平率が、すべ
て30%以下であり、はぼ円形状の断面形状を有するこ
とが分かる。Table 1 shows the blending ratio, humidity, and aspect ratio. It can be seen that the flatness ratios are all 30% or less, and the cross-sectional shape is approximately circular.
実施例と同様の方法でゾルを製造し、パイプ中は空気雰
囲気とし、実施例と同じ方法で紡糸を行った。得られた
繊維状ゲルの断面の偏平率を調べま
た。調合比、湿度及び偏平率を表Yに示す。A sol was produced in the same manner as in the example, an air atmosphere was created in the pipe, and spinning was performed in the same manner as in the example. The oblateness of the cross section of the obtained fibrous gel was also investigated. Table Y shows the blending ratio, humidity, and aspect ratio.
偏平率は、40%を越えており、かなりの偏平状の断面
である。The aspect ratio exceeds 40%, and the cross section is quite flat.
ゾル−ゲル法により製造した紡糸中の繊維状ゾルまたは
紡糸後の繊維状ゾルを、有機溶媒雰囲気に接触させるこ
とにより、種々の組成比のゾルにつき簡単にほぼ円形の
断面形状を有するゲルファイバーを得ることができた。By contacting a fibrous sol during spinning or a fibrous sol after spinning produced by the sol-gel method with an organic solvent atmosphere, gel fibers having an almost circular cross-sectional shape can be easily produced from sol with various composition ratios. I was able to get it.
この円形の断面形状のゲルファイバーを焼結することに
より、円形の断面形状を有する無機繊維が得られた。By sintering this gel fiber with a circular cross-section, an inorganic fiber with a circular cross-section was obtained.
(以下空白)(blank below)
Claims (3)
稠なゾル溶液から紡糸したゲル繊維を焼成することによ
り無機繊維を製造する方法において、該粘稠なゾル溶液
からの紡糸中または紡糸直後の繊維状ゾルを、有機溶媒
を含む雰囲気に接触させることを特徴とする無機繊維の
製造方法。(1) A method for producing inorganic fibers by firing gel fibers spun from a viscous sol solution obtained by hydrolysis/polymerization of organometallic compounds, during or immediately after spinning from the viscous sol solution. A method for producing inorganic fibers, which comprises bringing a fibrous sol into contact with an atmosphere containing an organic solvent.
パノール、ブタノールのいずれか、あるいは、これらの
内から選ばれた2種以上の混合物である特許請求の範囲
第1項に記載の無機繊維の製造方法。(2) The method for producing inorganic fibers according to claim 1, wherein the organic solvent is one of methanol, ethanol, propanol, butanol, or a mixture of two or more selected from these. .
る特許請求の範囲第1項に記載の無機繊維の製造方法。(3) The method for producing inorganic fibers according to claim 1, wherein the concentration of the organic solvent is 0.1 to 80 vol%.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16364690A JPH0455334A (en) | 1990-06-21 | 1990-06-21 | Production of inorganic fiber |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16364690A JPH0455334A (en) | 1990-06-21 | 1990-06-21 | Production of inorganic fiber |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0455334A true JPH0455334A (en) | 1992-02-24 |
Family
ID=15777904
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP16364690A Pending JPH0455334A (en) | 1990-06-21 | 1990-06-21 | Production of inorganic fiber |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0455334A (en) |
-
1990
- 1990-06-21 JP JP16364690A patent/JPH0455334A/en active Pending
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