JPS6385152A - Production of inorganic fiber molded body - Google Patents

Production of inorganic fiber molded body

Info

Publication number
JPS6385152A
JPS6385152A JP61229493A JP22949386A JPS6385152A JP S6385152 A JPS6385152 A JP S6385152A JP 61229493 A JP61229493 A JP 61229493A JP 22949386 A JP22949386 A JP 22949386A JP S6385152 A JPS6385152 A JP S6385152A
Authority
JP
Japan
Prior art keywords
fiber
precursor
fibers
pressure
firing
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
JP61229493A
Other languages
Japanese (ja)
Other versions
JPH0788616B2 (en
Inventor
土屋 通世
花水 時和
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.)
Denka Co Ltd
Original Assignee
Denki Kagaku Kogyo KK
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 Denki Kagaku Kogyo KK filed Critical Denki Kagaku Kogyo KK
Priority to JP61229493A priority Critical patent/JPH0788616B2/en
Publication of JPS6385152A publication Critical patent/JPS6385152A/en
Publication of JPH0788616B2 publication Critical patent/JPH0788616B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Inorganic Fibers (AREA)
  • Nonwoven Fabrics (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Abstract] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明は、ajll、黒条、化学プラント等で広く用
いられる工業用IJD熱炉等の内側に設けられる耐火断
熱材に適した引張り強度の高い、高カテそ度無機繊維取
形本の製造法である。
[Detailed Description of the Invention] [Industrial Application Field] The present invention provides a material with tensile strength suitable for fire-resistant insulation materials provided inside industrial IJD heat furnaces, etc., which are widely used in ajlls, black bars, chemical plants, etc. This is a method for producing high-quality, high-category inorganic fiber molds.

〔従来の技術〕[Conventional technology]

工業用DO熱炉#囁材としてアルミナ40〜60JFi
n%(μ下%とM5)、シリカ40〜60%を@りする
非結晶質セラミックファイバーのカサ腎度0.09以上
の成形体が広く用いられて来た。しかし、これらのセラ
ミックファイバー成形体の最高使用温度に1200℃で
、更に高温度で使用される工業加熱炉に相いるため、近
年アルミナ70〜90%、シリカ5〜50%のいわゆる
結晶質アルミナファイバーが開発された。
Industrial DO heat furnace #Alumina 40-60JFi as a material
Molded bodies of amorphous ceramic fibers containing n% (μ% and M5) and 40 to 60% silica and having a bulkiness of 0.09 or more have been widely used. However, the maximum operating temperature of these ceramic fiber molded bodies is 1200°C, and in order to be compatible with industrial heating furnaces used at even higher temperatures, in recent years so-called crystalline alumina fibers containing 70 to 90% alumina and 5 to 50% silica have been developed. was developed.

しかし〜結晶質アルミナファイバーは非晶質セラミック
ファイバーに比べて、強度が弱いため、セラミックファ
イバーをカサ密度0.09μ上に成形する必要があって
ニードルパンチ法が採用されていた。しかしニードルパ
ンチ法では1維が粉々になりやすく、強度の高い成形体
を得ることに困難であった。
However, since crystalline alumina fibers have lower strength than amorphous ceramic fibers, it is necessary to form the ceramic fibers to a bulk density of 0.09 μm, so a needle punch method has been adopted. However, in the needle punch method, single fibers tend to break into pieces, making it difficult to obtain a molded product with high strength.

このため、結晶質アルミナファイバーの場せはアルミナ
ファイバーを一度水中に解綿した後、コーンスターチ等
の有機質糊剤とシリカゾル専の無機バインダーで固めて
フェルト状に成形して、カサそ度0.09以上の底形体
を製造してAた。しかし\この方法では成形時に1維の
長さが数1に切断される之め、1維同志のからみ合いが
少なく、π機質瑚剤が高温で焼失したdkは引張り強度
が50〜100g#7K”まで低下する上、湿式1程の
ため製造コストも高くなる欠点があった。
For this reason, crystalline alumina fibers are prepared by first opening the alumina fibers in water, then hardening them with an organic glue such as cornstarch and an inorganic binder special for silica sol, and forming them into a felt shape, which has a bulkiness of 0.09. The above bottom body was manufactured. However, in this method, the length of each fiber is cut into several lengths during molding, so there is less entanglement between the fibers, and the tensile strength of dk, which has been burned out at high temperatures, is 50 to 100 g#. In addition to this, the production cost was also high because it was a wet process.

一方、憶維會本来の長い状態で使用する試&として、有
機質不織布を補強剤としてアルミナ噴維’rAjdj体
をニードルパンチ成形して、マットを得る方法(特開昭
60−1104!+9号会報)が提案されているが、ニ
ードルパンチ成形の除にアルミナ繊維が粉々になる現象
は同様に起り、高温使用時、有機質不織布が焼失すると
焼成前のカサ密度が0.1の成形体でも、カサ密度i 
0.06以下になるなどアルミナ繊維マットの密度は著
しく低下し、引張り強度も50〜100F/CML”ま
で低下し充分なものでになかった。
On the other hand, as an experiment to use it in its original long state, a method of obtaining a mat by needle-punching alumina foam bodies using an organic non-woven fabric as a reinforcing agent (JP-A-60-1104!+9 Newsletter) ) has been proposed, but the phenomenon of alumina fibers shattering into pieces occurs in the same way, except for needle punch forming, and when the organic nonwoven fabric is burned out during high-temperature use, even compacts with a bulk density of 0.1 before firing will become bulky. density i
The density of the alumina fiber mat was significantly lowered to 0.06 or less, and the tensile strength was also lowered to 50 to 100 F/CML'', which was not sufficient.

この欠点を解決する方法として、特開昭60−8816
2号公報及び¥f開昭60−252717号公報にアル
ミナ繊維の焼成前の前駆本積層体にニードルパンチ成形
し、その後焼成してプランタ。
As a method to solve this drawback, Japanese Patent Application Laid-Open No. 60-8816
No. 2 and No. 60-252717 disclose a planter made by needle-punching a precursor laminate of alumina fibers before firing and then firing.

ットを得る方法が提案されているOこの方法は従来の方
法に比べ、強度の高いブランケットを得ることが出来る
とされている。ところが、この方法においても、ニード
ルパンチ成形するために、高価な繊維処理剤やニードル
パンチ成形機を必要とし、又ニードルパンチ処理の際に
針が折損すると金属針が製品中に混入するという欠点が
あった。
A method for obtaining blankets has been proposed. This method is said to be able to obtain blankets with higher strength than conventional methods. However, this method also requires an expensive fiber treatment agent and a needle punch molding machine for needle punching, and also has the disadvantage that if the needle breaks during needle punching, metal needles will be mixed into the product. there were.

〔発明が解決しょうとする問題点1 以上の如く、高耐熱性である結晶質アルミナ繊維の高温
強度の高いマット状成形体を高価な繊維処理剤や特別な
装置を用めず、@!造することば内錐であつ友。
[Problem 1 to be solved by the invention As mentioned above, it is possible to produce a mat-like molded product of crystalline alumina fibers with high heat resistance and high strength at high temperatures without using expensive fiber treatment agents or special equipment. A friend who is the inner cone of words.

〔問題点を解決するための手段〕[Means for solving problems]

本発明は、焼成処理により1金@酸化物を与える繊維組
成物水溶液に水溶a有機重合体f:s加した粘性液を紡
糸して°得られた前駆本繊維積層体を水蒸気圧10〜1
00 mHgで加湿処理し、久いて加圧成形した後、1
100〜1400℃で焼成することを特徴とする無機繊
維成形体の製造方法であるり以下本発明について具体的
に説明する。
In the present invention, a precursor main fiber laminate obtained by spinning a viscous liquid obtained by adding a water-soluble a organic polymer f:s to an aqueous fiber composition solution that provides gold @ oxide by firing treatment is used.
After humidification treatment at 00 mHg and pressure molding, 1
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be specifically described below as a method for producing an inorganic fiber molded article, which is characterized by firing at a temperature of 100 to 1400°C.

本発明に用いられる前駆体繊維は、水溶性有機1合体倉
硲加して高粘度とし念金属塩溶液を紡糸して得られる。
The precursor fiber used in the present invention is obtained by adding a water-soluble organic compound to a high viscosity and spinning a metal salt solution.

上記紡糸液は例えばマグネシウム、ゾルコニウムなどの
水m性金属塩やコロイダルシリカなどをよむオキシ塩化
アルミニウム水溶液にポリビニルアルコール、ポリエチ
レンオキサイドなどの水心性有機重合体水溶液を脩加し
た後、減圧a縮するなどの方法で得られる。
The above-mentioned spinning solution can be prepared by, for example, adding an aqueous solution of a water-based organic polymer such as polyvinyl alcohol or polyethylene oxide to an aqueous solution of aluminum oxychloride containing a water-based metal salt such as magnesium or zorconium or colloidal silica, and then condensing the solution under reduced pressure. It can be obtained by the following method.

この様にして得友彷糸液を押出し法、遠心法など通常用
いられている紡糸法で紡糸すれば、前駆体繊維が得られ
る。例えば、遠心法による場合は、中火に開孔部を有す
る回転円盤の表ガに5〜20ポイズの紡糸gt−供給し
、紡糸した後、高速の空気流にニジ延揮、乾燥されて前
駆体繊維となる。この場合、前駆体繊維に、繊維が紡糸
装置の壁等に付層したり液滴化しない慨にするため光分
乾燥される。
By spinning the Tokutomo filament in this way by a commonly used spinning method such as an extrusion method or a centrifugation method, a precursor fiber can be obtained. For example, in the case of the centrifugal method, spinning gt of 5 to 20 poise is supplied to the surface of a rotating disk with an opening over medium heat, and after spinning, it is evaporated in a high-speed air stream and dried to form a precursor. Becomes body fibers. In this case, the precursor fibers are photo-dried in order to prevent the fibers from forming a layer on the walls of the spinning device or forming droplets.

この様に乾燥された前駆体繊維に水分き有事が3%以下
で繊維相互の付711rにない・前ll1L本の加湿に
、水蒸気圧が10〜1100tuxH好ましくは14〜
50 rttx Hgの範囲の加湿雰囲気中に、1〜3
0分床付するか、又ぼ前駆本繊維積層体層に上記加湿空
気と通過させるかなどの方法により好適に行なえる。J
JItll後の前駆体の水分は3〜12%の範囲であり
、4〜8%程度の場合が最も加圧処理に適している。水
環気圧が10鴎Hg未橋の場合は、前駆体繊維の加湿を
光分に行なうにに長時間を要し、実際的でなく、100
100OH越えると前@体愼維積層体の表面が7101
過多となって繊維の形状が崩れ、焼成後積層体表面に皮
が張った状帽となり好ましくなめ。
The moisture content of the precursor fibers dried in this way is 3% or less, and there is no adhesion between the fibers.For humidification of the previous 11L, the water vapor pressure is 10 to 1100tuxH, preferably 14 to
1 to 3 in a humidified atmosphere in the range of 50 rttx Hg.
This can be suitably carried out by a method such as leaving it on the bed for 0 minutes or passing the humidified air through the precursor main fiber laminate layer. J
The moisture content of the precursor after JItll is in the range of 3 to 12%, and a moisture content of about 4 to 8% is most suitable for pressure treatment. If the water ring pressure is 10 Hg, it will take a long time to humidify the precursor fibers, which is impractical;
When it exceeds 100OH, the surface of the previous @ body fiber laminate becomes 7101
If too much is used, the shape of the fibers will be distorted, and after firing, the surface of the laminate will have a crusty appearance, which is undesirable.

2IO湿した前駆体の加圧成形に板状、ロール状、ベル
ト状等に通常のプレス機で行なうことが出来る◎成形圧
力なm駆体横層体のき水率、加圧成形後のカサ密度によ
り変わるが、100に97m2以下の極く小さめ圧力で
良く、前@体憧維横層体の力l!!!度t O,061
1/an” Il、上に1yaEE5Z形fb。
Pressure molding of the wetted 2IO precursor into plates, rolls, belts, etc. can be carried out using an ordinary press machine.◎The molding pressure, the water content of the precursor horizontal layer, and the bulk after pressure molding. Although it varies depending on the density, a very small pressure of less than 100 to 97 m2 is sufficient, and the force of the front @ body longing lateral layer body l! ! ! degree t O,061
1/an” Il, 1yaEE5Z type fb on top.

焼成1siooo〜1400℃、好ましくは1200〜
1350℃で行なわれる。1000″C未満では蹟維の
強度が不充分であp、且つ15[]()”Cでのp+囚
熟熱収縮大きく耐火fl!If熱繊維成形体として実用
に通さない@又1400−C!を越えてIxJ乃しても
繊維の性能rC符に向上せず、むしろ強度が低下して経
済的でない。
Firing 1siooo~1400℃, preferably 1200~
It is carried out at 1350°C. If it is less than 1000"C, the strength of the fibers is insufficient, and at 15[]()"C, the p + confinement heat shrinkage is large and the fire resistance fl! If it cannot be put into practical use as a thermal fiber molded article @1400-C! Even if IxJ is exceeded, the performance of the fiber will not improve to the rC mark, but rather the strength will decrease, making it uneconomical.

以上のとおり、本発明により、乾燥した前駆体1維横層
体を再度特定条件で1JrJ湿したのち、加圧成形する
ことによって前駆体1維横志を部分的に付層させ、その
まま焼成することにより密度の馬匹、且つ柔軟性を持つ
マット状成形体を得ることができる。
As described above, according to the present invention, the dried precursor 1-fiber lateral layer is moistened again for 1JrJ under specific conditions, and then pressure-molded to partially layer the precursor 1-fiber lateral layer, and fired as it is. This makes it possible to obtain a mat-like molded product having a high density and flexibility.

〔実施例〕〔Example〕

実施例1(テスト41) オキシ塩化アルミニウム水蔓液に/J[後の組成がアル
ミナ80%、シリカ20%になる碌な割合にコロイダル
シリカ(スノーテックス日照化学)を硝加した凌、10
%ポリビニルアルコール水溶液(デンカポパールB−1
7使用)でアルミナ、シリカの仕tittに対してポリ
ビニルアルコールが8%になる櫟な割合に奈加し、!1
に縮した粘度15ボイズの水杉液’1ffJ糸原液とし
、中央に開孔部を有する回転円盤f:用いて紡糸してカ
サ密度0・04jl / cttt3の前駆体繊維横1
体を得た・この#鮎体積層庫を200.@対温度80%
水蒸気分圧14mmHgの恒温恒*漕に5分間保持し卯
湿しtのち、繊維の項j−する方向に50ゆ7m2の力
で1分間加圧圧縮しカサ密度肌Q 7 i 7cm3の
#躯体プレス成形体を得た。
Example 1 (Test 41) Aluminum oxychloride aqueous solution was added with colloidal silica (Snowtex Nichiro Kagaku) to a high ratio of 80% alumina and 20% silica.
% polyvinyl alcohol aqueous solution (Denka Popal B-1
7), the ratio of polyvinyl alcohol to the alumina and silica content is 8%. 1
The Mizusugi solution'1ffJ yarn stock solution with a viscosity of 15 boids was reduced to
I got a body and this #Ayu stacked storage is 200. @80% against temperature
After keeping it in a constant temperature bath with a water vapor partial pressure of 14 mmHg for 5 minutes and moistening it, it was compressed for 1 minute with a force of 50 m2 in the direction of the fiber length to form a bulk density skin Q 7 i 7 cm3 #frame. A press molded body was obtained.

この成形体全室温から最1%11500℃までの温度勾
配を持たせたトンネル炉にて室温から800′Cまで6
0分間、800’Cから1600℃まで15分間、15
00℃に10分間保持する様に焼放し1@成体を得九〇 m bI 本O力? W度B O,0951/、*”、
引張り強度500 g / c!n2であツタ。
This molded body was heated from room temperature to 800'C in a tunnel furnace with a temperature gradient of 1% to 11,500°C from the total room temperature to 1%.
0 minutes, 800'C to 1600℃ for 15 minutes, 15
Burn it out and hold it at 00℃ for 10 minutes to obtain a finished product. W degree B O,0951/, *”,
Tensile strength 500 g/c! Ivy in n2.

度を表のとおf)変えて処理し、カサ密度0.085μ
上、引張り強度4601/m”以上の焼成体を得九@ 比1]2列1(テストA65) 実111AN 1 テ得ft、 力?密K O−041
/3” O前駆体に1xJLt1処理七行なわず50に
#/m”の力で1分間卯圧圧mtして0.0521 /
 ays”の前駆体底形体を得た。この成形体を実施例
1と同じ条件で焼成した。焼成体のカサ密度は0.05
8.9 /備3殻τ゛j引張り強度は200.SF/C
M’皐不充分なものであった。
Processed by changing the degree as shown in the table f), the bulk density is 0.085μ
Above, a fired body with a tensile strength of 4601/m" or more was obtained. 9 @ Ratio 1] 2 rows 1 (Test A65)
/3" O precursor was treated with 1xJLt1 without seven lines, and the pressure mt was 0.0521/mt for 1 minute with a force of 50 #/m".
A precursor bottom shaped body of ``Ays'' was obtained. This shaped body was fired under the same conditions as in Example 1. The bulk density of the fired body was 0.05.
8.9 / Bi3 shell τ゛j tensile strength is 200. SF/C
M'Ko was unsatisfactory.

比lR912(テスト肩6) 実施列1で得九カサ密度0.041 /an”の前駆不
を水蒸気分圧8 mg Hgで20分間71Oaシたの
ち、5oゆ/。・の圧&−c底形し、ヵ施例1゜東件ア
焼成し7ta 91j成体のカサ密度は0.0721 
/ am”と低く強度も低かった。
R912 (Test Shoulder 6) After heating the precursor with a bulk density of 0.041/an'' for 20 minutes at a water vapor partial pressure of 8 mg Hg and a pressure of 5 o/. The bulk density of the 7ta 91j finished product is 0.0721.
/ am” and the strength was also low.

比較列5(テスト/l67) 実tIlfA例1で得た同じ前駆体を水蒸気分圧102
tn Hgで1分間ma L、後は実施例1と同様に加
圧焼成し友。カサ比重、引張り強度とも良好であり友が
mm体の表面の一部が711]湿過剰になったため焼成
体の表面が、皮が張り次状−と字9柔歌性に欠けるもの
となった口 比較列4(テスト48.9) 実211列1の2テスト襄5.4.とほぼ同じ条件で加
湿加圧成形し、焼成viL度を800℃と1400℃に
変えて焼成した・密度はほぼ艮好な焼成体となったが、
引張り強さが不充分であった。
Comparison Row 5 (Test/167) The same precursor obtained in Actual tIlfA Example 1 was used at a water vapor partial pressure of 102
tn Hg for 1 minute, then pressurized firing in the same manner as in Example 1. Both bulk specific gravity and tensile strength were good, and part of the surface of the mm body was 711] Due to excessive moisture, the surface of the fired body became taut and lacked softness. Mouth comparison row 4 (test 48.9) Real 211 row 1 2 test 5.4. Humidified pressure molding was carried out under almost the same conditions as above, and the firing temperature was changed to 800℃ and 1400℃.
Tensile strength was insufficient.

カサ密度と焼成体′の引張り強さの測定は次によった。The bulk density and tensile strength of the fired body were measured as follows.

■ カサ密度 試料から100間の試片金切り出し、切片のM破、幅、
長さ、厚みを測定してカサ密度を計李工した。なお、厚
さに復元性があるため、TIS R−3siiに準じて
測定した。
■ Cut out 100 pieces of specimen gold from the bulk density sample, M break of the section, width,
The length and thickness were measured to determine the bulk density. In addition, since the thickness has restorability, it was measured according to TIS R-3sii.

■ 引張り強さ 試料から50(福)X500(長さ)朋の形状の試料を
切り出し、500rm長さ方向の引張り強さを、引張り
試験機(東洋ぜ−ルドウイン候UTM −4−100型
)を用いて測定した口試片の厚さは試料切出し前にJI
S R−5511により測定した。このII[t−用い
て試験体の断面積金計算した〇 〔発明の効果〕 不発明の方法により、特殊な装置や高1dな助剤を用い
ることなく、又前駆本愼維を破壊することもなく、耐火
断熱材として使用するに十分な引張り強度r持ら、且つ
適度の柔軟性仝有する繊維マット等の成形体を容易に、
経済的に得ることができる。
■ Tensile strength A sample with a shape of 50 (Fuku) x 500 (Length) was cut out from the sample, and the tensile strength in the 500 rm length direction was measured using a tensile tester (Toyo Zerudwin model UTM-4-100). The thickness of the mouth specimen measured using JI
Measured using SR-5511. The cross-sectional area of the test specimen was calculated using this II [t-] [Effects of the invention] By the uninvented method, the precursor fibers could be destroyed without using any special equipment or expensive auxiliaries. It is possible to easily produce molded articles such as fiber mats that have sufficient tensile strength and appropriate flexibility to be used as fireproof heat insulating materials.
can be obtained economically.

特許出願人  電気化学工業株式会社 手  続  補  正  書 昭和61年10月24日 特許庁長官  黒 1)明 雄 殿 1、事件の表示 昭和61年特許願第229493号 2、発明の名称 無機繊維成形体の製造法 3、補正をする者 事件との関係   特許出願人 住所 ■100 東京都千代田区有楽町1丁目4番1号
明細書の発明の詳細な説明の欄 5、補正の内容− 1)第2頁第9〜11行の「をカサ密度0.09以上に
成形する必要があってニードルパンチ法が採用されてい
た。しかし」を「の成形に用いられる」と訂正する。
Patent Applicant Denki Kagaku Kogyo Co., Ltd. Procedural Amendment Written October 24, 1986 Commissioner of the Patent Office Kuro 1) Akio Yu 1, Indication of the case 1986 Patent Application No. 229493 2, Name of the invention Inorganic fiber molding 3. Relationship with the case of the person making the amendment Address of the patent applicant ■100 Column 5 of the detailed description of the invention in the specification, 1-4-1 Yurakucho, Chiyoda-ku, Tokyo, Contents of the amendment - 1) No. In lines 9 to 11 of page 2, ``The needle punching method was adopted because it was necessary to mold the material to a bulk density of 0.09 or more.However,'' should be corrected to ``used for the molding of the material.''

2)第3頁第5行の「補強剤」を「補強材」と訂正する
2) Correct "reinforcing agent" in line 5 of page 3 to "reinforcing material."

3)第6@第10行の「−・ルト状等に」を「ベルト状
等の」と訂正する。
3) In the 6th @ line 10, correct "--in the shape of a belt, etc." to "in the shape of a belt, etc."

Claims (1)

【特許請求の範囲】[Claims]  焼成処理により、金属酸化物を与える繊維組成物水溶
液に水溶性有機重合体を添加した粘性液を紡糸して得ら
れた前駆体繊維積層体を、水蒸気圧10〜100mmH
gで加湿処理し、次いで加圧成形した後、1100〜1
400℃で焼成することを特徴とする無機繊維成形体の
製造方法。
A precursor fiber laminate obtained by spinning a viscous liquid obtained by adding a water-soluble organic polymer to an aqueous solution of a fiber composition that provides a metal oxide by firing treatment is heated to a water vapor pressure of 10 to 100 mmH.
After humidification treatment at g and then pressure molding, 1100 to 1
A method for producing an inorganic fiber molded article, which comprises firing at 400°C.
JP61229493A 1986-09-30 1986-09-30 Method for manufacturing inorganic fiber molded body Expired - Fee Related JPH0788616B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61229493A JPH0788616B2 (en) 1986-09-30 1986-09-30 Method for manufacturing inorganic fiber molded body

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61229493A JPH0788616B2 (en) 1986-09-30 1986-09-30 Method for manufacturing inorganic fiber molded body

Publications (2)

Publication Number Publication Date
JPS6385152A true JPS6385152A (en) 1988-04-15
JPH0788616B2 JPH0788616B2 (en) 1995-09-27

Family

ID=16893028

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61229493A Expired - Fee Related JPH0788616B2 (en) 1986-09-30 1986-09-30 Method for manufacturing inorganic fiber molded body

Country Status (1)

Country Link
JP (1) JPH0788616B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03104925A (en) * 1989-09-12 1991-05-01 Koroido Res:Kk Preparation of silica alumina fiber
JPH04276977A (en) * 1991-03-05 1992-10-02 Nec Corp Isdn telephone system
US7496125B2 (en) 2002-02-27 2009-02-24 Konoshima Chemical Co. Ltd. Composite laser rod, fabricating method thereof, and laser device therewith
CN105506761A (en) * 2016-01-19 2016-04-20 浙江理工大学 Centrifugal spinning preparation method of silicon dioxide and polystyrene micro-nano fiber membrane

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03104925A (en) * 1989-09-12 1991-05-01 Koroido Res:Kk Preparation of silica alumina fiber
JPH04276977A (en) * 1991-03-05 1992-10-02 Nec Corp Isdn telephone system
US7496125B2 (en) 2002-02-27 2009-02-24 Konoshima Chemical Co. Ltd. Composite laser rod, fabricating method thereof, and laser device therewith
CN105506761A (en) * 2016-01-19 2016-04-20 浙江理工大学 Centrifugal spinning preparation method of silicon dioxide and polystyrene micro-nano fiber membrane

Also Published As

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