JPS6325083B2 - - Google Patents
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- Publication number
- JPS6325083B2 JPS6325083B2 JP59041346A JP4134684A JPS6325083B2 JP S6325083 B2 JPS6325083 B2 JP S6325083B2 JP 59041346 A JP59041346 A JP 59041346A JP 4134684 A JP4134684 A JP 4134684A JP S6325083 B2 JPS6325083 B2 JP S6325083B2
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- Japan
- Prior art keywords
- organosilicon
- fibers
- compound
- polymer compound
- organosilicon polymer
- 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.)
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- Inorganic Fibers (AREA)
Description
【発明の詳細な説明】
本発明は有機ケイ素化合物を熱分解重縮合して
得た有機ケイ素高分子化合物から高強度無機繊維
を製造する方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing high-strength inorganic fibers from an organosilicon polymer compound obtained by subjecting an organosilicon compound to thermal decomposition polycondensation.
従来ケイ素を含む無機繊維としては、ケイ素と
炭素を主要骨格成分とするポリカルボシラン、ケ
イ素と炭素、更にチタンを主要骨格成分とするポ
リチタノカルボシラン、またはケイ素と炭素、更
にジルコニウムを主要骨格成分とするポリジルコ
ノカルボシランを出発原料とし、紡糸、不融化、
ついで高温焼成する方法が提案されている。(例
えば特開昭51―13024号、特開昭51―139929号、
特開昭56―128315号、特開昭57―106718号公報参
照)。 Conventional inorganic fibers containing silicon include polycarbosilane with silicon and carbon as the main skeleton components, polytitanocarbosilane with silicon and carbon as well as titanium as the main skeleton components, or silicon and carbon with zirconium as the main skeleton. Using polyzirconocarbosilane as a starting material, spinning, infusibility,
A method has been proposed in which the material is then fired at a high temperature. (For example, JP-A-51-13024, JP-A-51-139929,
(Refer to Japanese Patent Application Laid-open No. 56-128315 and Japanese Patent Application Laid-open No. 57-106718).
すなわち、ポリジメチルシランの熱分解重縮合
反応によりケイ素―ケイ素結合の開裂とこれに伴
なう水素引き抜き、メチレン基への転位が起り、
ケイ素と炭素を主要骨格成分とするポリカルボシ
ランが製造される。またポリチタノカルボシラ
ン、ポリジルコノカルシランもほぼ同じような方
法で製造される。 That is, due to the thermal decomposition polycondensation reaction of polydimethylsilane, cleavage of silicon-silicon bonds, accompanying hydrogen abstraction, and rearrangement to methylene groups occur.
A polycarbosilane whose main skeleton components are silicon and carbon is produced. Polytitanocarbosilane and polyzirconocarbosilane are also produced in substantially the same manner.
次にこれらの有機ケイ素高分子化合物から低分
子量有機ケイ素化合物の含有量の少ない有機ケイ
素高分子化合物を得たのち該有機ケイ素高分子化
合物を溶融紡糸または湿式紡糸によつて繊維化し
たのち、該繊維を空気、酸素あるいはオゾンのよ
うな酸化性雰囲気下に加熱して不融化処理を行な
い、ついで不活性ガス中で高温焼成して、炭化ケ
イ素を主な成分とする無機繊維とする。上記のよ
うに有機ケイ素化合物の熱分解重縮合によつて製
造した有機ケイ素高分子化合物から低分子量有機
ケイ素化合物を除去してこれを紡糸に用いたとし
ても、なお、この有機ケイ素高分子化合物の数平
均分子量は800〜10000の比較的低分子量の重合体
であるため、繊維の不融化処理されに高温焼成を
行なうことにより、繊維中に存在する低分子量有
機ケイ素化合物および加熱により有機ケイ素高分
子化合物の一部に熱分解が起り低分子量有機ケイ
素化合物が生じ、これらの低分子量有機ケイ素化
合物がガス状となつて繊維から放出される。した
がつて予備加熱された繊維にはこれらガスの放出
により空孔が残り、高温焼成により、無機化し、
繊維の収縮が起つても充分にこれら空孔を穴うめ
できずに残るため、無機繊維の強度低下の原因と
なるため、高強度の繊維が得られないという欠点
を有していた。 Next, an organosilicon polymer compound with a low content of low molecular weight organosilicon compounds is obtained from these organosilicon polymer compounds, and the organosilicon polymer compound is made into fibers by melt spinning or wet spinning. The fibers are heated in an oxidizing atmosphere such as air, oxygen, or ozone to make them infusible, and then fired at a high temperature in an inert gas to produce inorganic fibers containing silicon carbide as a main component. Even if the low molecular weight organosilicon compound is removed from the organosilicon polymer compound produced by thermal decomposition polycondensation of the organosilicon compound as described above and used for spinning, the Since it is a relatively low molecular weight polymer with a number average molecular weight of 800 to 10,000, by performing high temperature firing after the fiber is infusible, the low molecular weight organosilicon compound present in the fiber and the organosilicon polymer by heating are removed. Pyrolysis of some of the compounds occurs to produce low molecular weight organosilicon compounds, which are released from the fibers in gaseous form. Therefore, pores remain in the preheated fiber due to the release of these gases, which become mineralized by high-temperature firing.
Even if the fibers shrink, these pores cannot be filled sufficiently and remain, causing a decrease in the strength of the inorganic fibers, resulting in the disadvantage that high-strength fibers cannot be obtained.
本発明はこのような欠点を解決し、高強度無機
繊維、特に炭化ケイ素を主な成分とする無機繊
維、たとえば炭化ケイ素繊維、および炭化ケイ素
を主な成分とし炭化チタンあるいは炭化ジルコニ
ウムを含む無機繊維を得るものである。 The present invention solves these drawbacks and provides high-strength inorganic fibers, particularly inorganic fibers containing silicon carbide as a main component, such as silicon carbide fibers, and inorganic fibers containing silicon carbide as a main component and titanium carbide or zirconium carbide. This is what you get.
すなわち、本発明は有機ケイ素化合物を熱分解
重縮合反応により有機ケイ素高分子化合物を生成
させる第1工程と、前記有機ケイ素高分子化合物
から低分子量有機ケイ素化合物の含有量の少ない
有機ケイ素高分子化合物を得る第2工程と、前記
有機ケイ素高分子化合物の紡糸原液を造り紡糸す
る第3工程と、紡糸した繊維を酸化性雰囲気中少
なくとも0.1Kg/cm2(ゲージ)の加圧下に50〜300
℃で低温加熱する第4工程と、低温加熱した繊維
を張力の作用下に、窒素、アルゴン、水素、炭化
水素ガス、有機ケイ素化合物ガスおよび一酸化炭
素のうちから選らばれる1種または2種以上の不
活性ガス雰囲気中で少なくとも0.1Kg/cm2(ゲー
ジ)の加圧下に、300〜600℃で予備加熱する第5
工程と、予備加熱した繊維を窒素、アルゴン、水
素、アンモニアガスおよび一酸化炭素のうちから
選ばれる1種または2種以上の不活性ガス雰囲気
中で、張力下に800〜1500℃で高温焼成して炭化
ケイ素を主な主成分とする無機繊維となす第6工
程からなることを特徴と高強度無機繊維の製造方
法に関するものである。 That is, the present invention includes a first step of producing an organosilicon polymer compound by thermal decomposition polycondensation reaction of an organosilicon compound, and an organosilicon polymer compound having a low content of low molecular weight organosilicon compounds from the organosilicon polymer compound. a third step of preparing and spinning a spinning dope of the organosilicon polymer compound; and a third step of preparing a spinning stock solution of the organosilicon polymer compound and spinning the fiber, and spinning the spun fiber in an oxidizing atmosphere under a pressure of at least 0.1 kg/cm 2 (gauge) at a rate of 50 to 300 kg/cm 2 (gauge).
A fourth step of heating the fiber at a low temperature at a temperature of ℃, and heating the fiber heated at a low temperature under tension by heating one or more types selected from nitrogen, argon, hydrogen, hydrocarbon gas, organosilicon compound gas, and carbon monoxide. The fifth step is preheated at 300-600°C under a pressure of at least 0.1 Kg/cm 2 (gauge) in an inert gas atmosphere of
The preheated fibers are fired under tension at a high temperature of 800 to 1500°C in an atmosphere of one or more inert gases selected from nitrogen, argon, hydrogen, ammonia gas, and carbon monoxide. The present invention relates to a method for producing high-strength inorganic fibers, characterized by comprising a sixth step of forming inorganic fibers containing silicon carbide as a main component.
すなわち、本発明において第4工程、第5工程
を加圧下に行なう理由は、繊維中に含まれる低分
子量有機ケイ素化合物および加熱により有機ケイ
素高分子化合物の一部に熱分解が起り、低分子量
有機ケイ素化合物が生じ、これらの低分子量有機
ケイ素化合物ガス状となつて繊維から放出される
のを防ぐためである。加圧下に行う作用効果は次
の理由によるものと考えられる。加圧下に不融化
処理を行なうことにより、低分子量有機ケイ素化
合物が気散することなく、酸素により架橋される
ことによつて網目構造をとるため、低分子量有機
ケイ素化合物を有効な物質として繊維中に残すこ
とができる。さらに予備加熱を加圧下に行なうこ
とにより熱分解によつて生じる低分子有機ケイ素
化合物の発生を防ぎ、繊維中の有機ケイ素化合物
が分子内あるいは分子間の熱縮合を起こすことに
より、有効な物質としてケイ素原子を残存させる
ことが可能となり、高温焼成して高強度無機繊維
が得られることになつたものと考えられる。 That is, the reason why the fourth and fifth steps are carried out under pressure in the present invention is that thermal decomposition occurs in the low molecular weight organosilicon compound contained in the fibers and in a part of the organosilicon polymer compound due to heating. This is to prevent the formation of silicon compounds and the release of these low molecular weight organosilicon compounds in gaseous form from the fibers. The effects of applying pressure are thought to be due to the following reasons. By performing the infusibility treatment under pressure, the low molecular weight organosilicon compound does not diffuse and forms a network structure by crosslinking with oxygen, so the low molecular weight organosilicon compound is used as an effective substance in the fiber. can be left in. Furthermore, preheating under pressure prevents the generation of low-molecular organosilicon compounds caused by thermal decomposition, and the organosilicon compounds in the fibers undergo intramolecular or intermolecular thermal condensation, making them effective substances. It is thought that this allows silicon atoms to remain and that high-strength inorganic fibers can be obtained by high-temperature firing.
次に本発明の各工程について具体的に説明す
る。 Next, each step of the present invention will be specifically explained.
本発明の高強度無機繊維の製造において使用す
ることができる原料の有機ケイ素化合物は、ポリ
ジメチルシランまたはメチル基の一部がフエニル
基、アルキル基、アリール基、または水素で置換
されたポリシランから選らばれる何れかを使用
し、公知の方法でポリカルボシラン、ポリチタノ
カルボシランまたはポリジルコノシランなどの有
機ケイ素高分子化合物を製造する。(第1工程);
ついで濃縮法または溶媒分別法により前記有機
ケイ素高分子化合物から低分子量有機ケイ素化合
物の含有量の少ない有機ケイ素高分子化合物を得
る。この有機ケイ素高分子化合物の数平均分子量
は800〜10000である。(第2工程);
前記有機ケイ素高分子化合物を加熱溶融させる
か、または溶媒に溶解して紡糸原液を造り、これ
を紡糸装置により紡糸して繊維径15〜18μの繊維
とした。(第3工程);
前記繊維を酸化性雰囲気中で加圧下に低温加熱
して不融化処理する。加圧は低分子量有機ケイ素
化合物の気散を防ぐために行うものであり、0.1
Kg/cm2(ゲージ)以上の加圧をおこなえばその効
果が現われるが、好ましくは0.5Kg/cm2(ゲージ)
以上である。しかし、10Kg/cm2(ゲージ)以上の
加圧でも効果は変らないし、装置が高くつくため
経済的でなく、10Kg/cm2(ゲージ)以下で充分で
ある。 The raw organosilicon compound that can be used in the production of the high-strength inorganic fiber of the present invention is selected from polydimethylsilane or polysilane in which a part of the methyl group is substituted with a phenyl group, an alkyl group, an aryl group, or hydrogen. An organosilicon polymer compound such as polycarbosilane, polytitanocarbosilane or polyzirconosilane is produced by a known method. (First step): Next, an organosilicon polymer compound containing a low content of low molecular weight organosilicon compounds is obtained from the organosilicon polymer compound by a concentration method or a solvent fractionation method. The number average molecular weight of this organosilicon polymer compound is 800 to 10,000. (Second step); The organosilicon polymer compound was melted by heating or dissolved in a solvent to prepare a spinning dope, and this was spun using a spinning device to obtain fibers with a fiber diameter of 15 to 18 μm. (Third step); The fibers are heated at a low temperature under pressure in an oxidizing atmosphere to make them infusible. The pressure is applied to prevent the low molecular weight organosilicon compound from evaporating, and the pressure is 0.1
The effect will be seen if the pressure is more than Kg/cm 2 (gauge), but preferably 0.5Kg/cm 2 (gauge)
That's all. However, applying a pressure of 10 kg/cm 2 (gauge) or more does not change the effect, and the equipment is expensive, so it is not economical, so a pressure of 10 kg/cm 2 (gauge) or less is sufficient.
雰囲気は空気、オゾン、酸素、二酸化窒素のう
ちから選らばれるいずれか1種または2種以上の
ガスが用いられる。これら酸化性ガスを窒素、ア
ルゴン等の不活性ガスと混合して使用することも
可能である。低温加熱は50〜300℃の範囲で行な
うのが好ましい。低温加熱は50℃以下で行なつて
も繊維中の低分子量有機ケイ素化合物酸素により
架橋することができず、300℃以上では繊維中の
酸素による架橋が増大する、すなわち酸化が進行
しすぎのため好ましくない。 As the atmosphere, one or more gases selected from air, ozone, oxygen, and nitrogen dioxide are used. It is also possible to use these oxidizing gases in combination with an inert gas such as nitrogen or argon. The low temperature heating is preferably carried out in the range of 50 to 300°C. Even if low-temperature heating is performed at temperatures below 50°C, crosslinking cannot occur due to the low molecular weight organosilicon compound oxygen in the fibers, and at temperatures above 300°C crosslinking due to oxygen in the fibers increases, i.e. oxidation progresses too much. Undesirable.
低温加熱する時間は前記温度および雰囲気ガス
に関連し、数分から10時間の範囲が適当である。
この低温加熱する際に作用させる張力は繊維が収
縮して波状の形にならないようにするためわずか
の張力をかけてもよい。実用的に繊維に張力を作
用させて低温加熱するためには、0.001〜10Kg/
mm2の範囲の張力をかければ充分である。(第4工
程);
次に前記低温加熱した繊維を窒素、アルゴン、
水素、炭化水素ガス、有機ケイ素化合物ガスおよ
び一酸化炭素のうちから選ばれる1種または2種
以上の不活性ガス雰囲気中加圧下に張力下で予備
加熱する。この予備加熱において繊維を形成する
有機ケイ素高分子化合物は熱重合縮合反応と、熱
分解反応により繊維中より低分子量有機ケイ素化
合物の気散が主に起るのは300〜600℃の間であ
る。それ以上の温度では低級炭化水素や、水素、
一酸化炭素、二酸化炭素の発生が主となる。加圧
するのは熱分解反応により低分子量有機ケイ素化
合物が生成するのを防ぐためであり、0.1Kg/cm2
(ゲージ)以上の雰囲気加圧を行なえばその効果
が現われるが、好ましくは0.5Kg/cm2(ゲージ)
以上である。しかし10Kg/cm2(ゲージ)以上の加
圧でも効果が変らないから加圧は0.1〜10Kg/cm2
(ゲージ)の範囲が適当である。 The time for low-temperature heating is related to the above-mentioned temperature and atmospheric gas, and is suitably in the range of several minutes to 10 hours.
A slight tension may be applied during this low-temperature heating to prevent the fibers from shrinking into a wavy shape. In order to practically apply tension to the fibers and heat them at a low temperature, it is necessary to use 0.001 to 10 kg/
It is sufficient to apply a tension in the range of mm 2 . (Fourth step); Next, the low-temperature heated fibers are treated with nitrogen, argon,
Preheating is performed under pressure and tension in an atmosphere of one or more inert gases selected from hydrogen, hydrocarbon gas, organosilicon compound gas, and carbon monoxide. During this preheating, the organosilicon polymer compound that forms the fiber undergoes a thermal polymerization condensation reaction and a thermal decomposition reaction, which causes the vaporization of the lower molecular weight organosilicon compound from within the fiber, which mainly occurs between 300 and 600°C. . At higher temperatures, lower hydrocarbons, hydrogen,
Carbon monoxide and carbon dioxide are mainly generated. The reason for applying pressure is to prevent the formation of low molecular weight organosilicon compounds due to thermal decomposition reactions, and the pressure is 0.1Kg/cm 2
(gauge) or more, the effect will appear, but preferably 0.5Kg/cm 2 (gauge)
That's all. However, the effect does not change even if the pressure exceeds 10Kg/cm 2 (gauge), so the pressure should be 0.1 to 10Kg/cm 2
(gauge) range is appropriate.
予備加熱時に繊維が収縮して波状の形となるこ
とを防ぐには、0.01〜10Kg/mm2の範囲の張力を作
用させると良い結果が得られる。0.001Kg/mm2以
下の張力を繊維に作用させても繊維をたるませな
いような緊張を与えることができないし、10Kg/
mm2以上の張力を作用させると張力が大きすぎて繊
維が切れることがあるので、0.001〜10Kg/mm2の
範囲が適当である。(第5工程);
前記予備加熱した繊維を、高温焼成して炭化ケ
イ素を主な成分とする無機繊維となすには、窒
素、アルゴン、水素、アンモニアガスおよび一酸
化炭素のうちから選ばれる1種または2種以上か
らなる不活性ガス雰囲気中において800〜1500℃
の温度範囲で張力下に高温焼成する。 In order to prevent the fibers from shrinking and forming a wavy shape during preheating, good results can be obtained by applying a tension in the range of 0.01 to 10 Kg/mm 2 . Even if a tension of 0.001Kg/ mm2 or less is applied to the fibers, it is not possible to apply tension that will not cause the fibers to sag, and 10Kg/mm2 or less cannot be applied to the fibers.
If a tension of mm 2 or more is applied, the tension is too large and the fibers may break, so a range of 0.001 to 10 Kg/mm 2 is appropriate. (Fifth step); To make the preheated fibers into inorganic fibers containing silicon carbide as a main component by firing the preheated fibers at a high temperature, a gas selected from nitrogen, argon, hydrogen, ammonia gas, and carbon monoxide is used. 800 to 1500℃ in an inert gas atmosphere consisting of a species or two or more species
High temperature firing under tension in the temperature range.
前記高温焼成を0.01〜100Kg/mm2の範囲で張力
を作用させながら高温焼成すると屈曲のない高強
度無機繊維を得ることができる。0.01Kg/mm2以下
の張力では効果がなく、100Kg/mm2上の張力を作
用させても効果に変わりはない。(第6工程);
本発明の方法を実施することによつて、高強度
無機繊維を得ることができ、かつ、高温焼成後の
無機繊維の残留重量が向上することが認められ
た。 By performing the high temperature firing while applying tension in the range of 0.01 to 100 Kg/mm 2 , high strength inorganic fibers without bending can be obtained. A tension of less than 0.01Kg/ mm2 has no effect, and even if a tension of 100Kg/ mm2 or more is applied, the effect remains the same. (Sixth step); It was found that by carrying out the method of the present invention, high-strength inorganic fibers could be obtained and the residual weight of the inorganic fibers after high-temperature firing was improved.
実施例 1
ジメチルジクロルシランから合成されたポリジ
メチルシランを温度計、撹拌機、揮発性ガス配出
管、および不活性ガス導入管を取りつけた四つ口
フラスコに仕込み、徐々に加熱したところ、360
℃で熱分解重合を始めたので、生成する揮発性生
分を留去しながら450℃まで省温して反応をつづ
けたところポリカルボシランが得られた。Example 1 Polydimethylsilane synthesized from dimethyldichlorosilane was charged into a four-necked flask equipped with a thermometer, a stirrer, a volatile gas delivery pipe, and an inert gas introduction pipe and gradually heated. 360
Thermal decomposition polymerization started at 450°C, so the reaction was continued at 450°C while distilling off the volatile components produced, and polycarbosilane was obtained.
このポリカルボシラン30gを30mlトルエンに溶
解し、この溶液を300mlのアセトン中に加えて不
溶物は約70%であつた。この不溶物を溶融紡糸法
により240℃で200m/分で紡糸し直径15μの繊維
を得た。この繊維を2Kg/cm2(ゲージ)に加圧し
た空気中で2Kg/mm2の張力を負荷させながら、
200℃まで5℃/時で昇温して不融化処理を行な
つた。次に不融化したポリカルボシラン繊維を1
Kg/cm2(ゲージ)に加圧した窒素中で3Kg/mm2の
張力を負荷させながら100℃/時の昇温速度で600
℃まで予備加熱した後、加圧を中止して窒素雰囲
気下に引き続き1200℃まで高温焼成を行なつたと
ころ黒色で光沢のある引張り強度350Kg/mm2の炭
化ケイ素繊維を得た。 30 g of this polycarbosilane was dissolved in 30 ml of toluene, and this solution was added to 300 ml of acetone, and the insoluble matter was about 70%. This insoluble matter was spun at 240° C. and 200 m/min by a melt spinning method to obtain fibers with a diameter of 15 μm. While applying a tension of 2 kg/mm 2 to this fiber in air pressurized to 2 kg/cm 2 (gauge),
Infusibility treatment was carried out by increasing the temperature to 200°C at a rate of 5°C/hour. Next, 1 infusible polycarbosilane fiber
600 at a heating rate of 100℃/hour while applying a tension of 3Kg/ mm2 in nitrogen pressurized to Kg/ cm2 (gauge).
After preheating to 1200° C., pressurization was stopped and firing was continued at a high temperature of 1200° C. under a nitrogen atmosphere to obtain a black, glossy silicon carbide fiber with a tensile strength of 350 Kg/mm 2 .
なお、焼成による残留重量は75%であつた。 Note that the residual weight after firing was 75%.
実施例 2
実施例1で得られた低分子重有機ケイ素を除い
ていないポリカルボシラン30gに、チタンテトラ
ブトキシド8gを添加して350℃で3時間反応さ
せることによりポリチタノカルボシランを得た。Example 2 Polytitanocarbosilane was obtained by adding 8 g of titanium tetrabutoxide to 30 g of the polycarbosilane obtained in Example 1 without removing the low molecular weight organosilicon and reacting at 350°C for 3 hours. .
得られたポリチタノカルボシランを減圧下に加
熱し、揮発性成分を除去してこの分子量を調製た
ところ1800であつた。 The resulting polytitanocarbosilane was heated under reduced pressure to remove volatile components, and its molecular weight was determined to be 1,800.
次にこのポリマーを270℃に加熱溶融して300
m/分で紡糸して直径17μの繊維を得た。 Next, this polymer was heated to 270℃ and melted to 300℃.
The fiber was spun at m/min to obtain a fiber with a diameter of 17μ.
この繊維を5Kg/cm2(ゲージ)に加圧した空気
中で0.5Kg/mm2の張力を負荷させながら220℃まで
10℃/時で昇温して不融化処理を行つた。次に不
融化したポリチタノカルボシラン繊維を3Kg/cm2
(ゲージ)に加圧したアルゴン中で4Kg/mm2の張
力を負荷させながら200℃/時の昇温速度で500℃
まで予備加熱した後、加圧を中止してアルゴン雰
囲気下に引き続き1350℃まで高温焼成を行なつて
黒色の光沢ある引張り強度410Kg/mm2の炭化ケイ
素を主な成分としチタンカーバイトを含む無機繊
維を得た。なお焼成による残留重量は79%であつ
た。 This fiber is heated to 220℃ while applying a tension of 0.5Kg/mm 2 in air pressurized to 5Kg/cm 2 (gauge).
Infusibility treatment was performed by increasing the temperature at 10°C/hour. Next, 3 kg/cm 2 of infusible polytitanocarbosilane fiber was added.
500℃ at a heating rate of 200℃/hour while applying a tension of 4Kg/mm 2 in argon pressurized to (gauge)
After preheating to 1,350 degrees Celsius, pressurization was stopped and firing was continued at a high temperature of 1,350 degrees Celsius under an argon atmosphere to produce a black glossy inorganic material containing silicon carbide as the main component and titanium carbide, with a tensile strength of 410 kg/mm 2 . Obtained fiber. The residual weight after firing was 79%.
実施例 3
実施例1で得られた低分子量有機ケイ素を除い
てないポリカルボシラン30gにジルコニウムテト
ラブトキシ10gを添加して300℃で3時間反応さ
せてポリジルコノカルシランを得た。Example 3 10 g of zirconium tetrabutoxy was added to 30 g of the polycarbosilane obtained in Example 1 without removing the low molecular weight organosilicon, and the mixture was reacted at 300° C. for 3 hours to obtain polyzirconocarbosilane.
得られたポリジルコノカルボシランを減圧下に
加熱し揮発性成分を除去して、この分子量を調製
したところ1700であつた。 The resulting polyzirconocarbosilane was heated under reduced pressure to remove volatile components, and its molecular weight was determined to be 1,700.
次にこのポリマーを260℃に加熱溶解して150
m/分で紡糸して直径16μの繊維を得た。 Next, this polymer was heated to 260°C and dissolved to 150°C.
The fiber was spun at m/min to obtain a fiber with a diameter of 16μ.
この繊維を8Kg/cm2(ゲージ)に加熱した空気
中での0.1Kg/mm2の張力を負荷させながら170℃ま
で5℃/時で昇温して不融化処理を行なつた。次
に不融化したポリジルコノシラン繊維を0.5Kg/
cm2(ゲージ)に加圧した窒素中で0.5Kg/mm2の張
力を負荷させながら100℃/時の昇温速度で400℃
まで予備加熱した後、加圧を中止して窒素雰囲気
下に引き続き1250℃まで高温焼成を行なつて引張
り強度380Kg/mm2の炭化ケイ素を主な成分としジ
ルコニウムカーバイドを含む無機繊維を得た。な
お焼成による残留重量は73%であつた。 This fiber was heated to 170° C. at a rate of 5° C./hour to perform an infusibility treatment while applying a tension of 0.1 kg/mm 2 in air heated to 8 kg/cm 2 (gauge). Next, add 0.5 kg of infusible polyzirconosilane fiber to
400℃ at a heating rate of 100℃/hour while applying a tension of 0.5Kg/mm 2 in nitrogen pressurized to cm 2 (gauge).
After preheating to 1,250° C., the pressurization was stopped and high-temperature firing was continued at 1,250° C. under a nitrogen atmosphere to obtain an inorganic fiber mainly composed of silicon carbide and containing zirconium carbide and having a tensile strength of 380 Kg/mm 2 . The weight remaining after firing was 73%.
比較例
実施例1で得られた低分子量有機ケイ素化合物
の含有量の少ないポリカルボシランを240℃で200
m/分で紡糸し直径15μの繊維を空気中で2Kg/
mm2の張力を負荷させながら200℃まで5℃で昇温
して不融化処理を行つた。次に不融化したポリカ
ルボシラン繊維を3Kg/mm2の張力を負荷させなが
ら100℃/時の昇温速度で窒素雰囲気下に1200℃
まで高温焼成させたところ、黒色で光沢のある炭
化ケイ素繊維を得た。引張り強度は260Kg/mm2で
あつた。Comparative Example Polycarbosilane with a low content of low molecular weight organosilicon compounds obtained in Example 1 was heated at 240°C for 200°C.
Spun fibers with a diameter of 15 μm at a speed of 2 kg/min in air.
Infusibility treatment was performed by increasing the temperature to 200°C at 5°C while applying a tension of mm 2 . Next, the infusible polycarbosilane fibers were heated to 1200°C under a nitrogen atmosphere at a heating rate of 100°C/hour while applying a tension of 3 kg/mm 2 .
When fired at high temperatures, black and glossy silicon carbide fibers were obtained. The tensile strength was 260Kg/ mm2 .
なお、焼成による残率重量は65%であつた。 The weight remaining after firing was 65%.
Claims (1)
有機ケイ素高分子化合物を生成させる第1工程
と、前記有機ケイ素高分子化合物から低分子有機
ケイ素化合物の含有量の少ない有機ケイ素高分子
化合物を得る第2工程と、前記有機ケイ素高分子
化合物の紡糸原液を造り紡糸する第3工程と、紡
糸した繊維を酸化性雰囲気中で少なくとも0.1
Kg/cm2(ゲージ)の加圧下に50〜300℃で低温加
熱する第4工程と、低温加熱した繊維を張力の作
用下に窒素、アルゴン、水素、炭化水素ガス、有
機ケイ素化合物ガスおよび一酸化炭素のうちから
選ばれる1種または2種以上の不活性ガス雰囲気
中で少なくとも0.1Kg/cm2(ゲージ)の加圧下に
300〜600℃で予備加熱させる第5工程と、予備加
熱した繊維を窒素、アルゴン、水素、アンモニア
ガスおよび一酸化炭素のうちから選ばれる1種ま
たは2種以上の不活性ガス雰囲気中で張力下に、
800〜1500℃で高温焼成して炭化ケイ素を主な主
成分とする無機繊維となす第6工程とからなるこ
とを特徴とする高強度無機繊維の製造方法。 2 第1工程の有機ケイ素化合物の熱分解の重縮
合反応により生成する有機ケイ素高分子化合物が
ポリカルボシラン、ポリチタノカルボシラン、ま
たはポリジルコノカルボシランであることを特徴
とする特許請求の範囲第1項記載の高強度無機繊
維の製造方法。[Scope of Claims] 1. A first step of producing an organosilicon polymer compound by a thermal decomposition polycondensation reaction of an organosilicon compound, and an organosilicon polymer with a low content of low molecular weight organosilicon compounds from the organosilicon polymer compound a second step of obtaining a molecular compound; a third step of preparing and spinning a spinning stock solution of the organosilicon polymer compound; and a step of spinning the spun fiber in an oxidizing atmosphere of at least 0.1
The fourth step is low-temperature heating at 50 to 300°C under pressure of Kg/cm 2 (gauge), and the low-temperature heated fibers are heated under tension with nitrogen, argon, hydrogen, hydrocarbon gas, organosilicon compound gas and nitrogen. Under a pressure of at least 0.1 Kg/cm 2 (gauge) in an atmosphere of one or more inert gases selected from carbon oxides.
A fifth step of preheating at 300 to 600°C, and heating the preheated fibers under tension in an atmosphere of one or more inert gases selected from nitrogen, argon, hydrogen, ammonia gas, and carbon monoxide. To,
A method for producing high-strength inorganic fibers, comprising a sixth step of baking at a high temperature of 800 to 1500°C to form inorganic fibers containing silicon carbide as a main component. 2. A patent claim characterized in that the organosilicon polymer compound produced by the polycondensation reaction of thermal decomposition of an organosilicon compound in the first step is polycarbosilane, polytitanocarbosilane, or polyzirconocarbosilane. A method for producing a high-strength inorganic fiber according to Item 1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4134684A JPS60185817A (en) | 1984-03-06 | 1984-03-06 | Preparation of inorganic yarn having high strength |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4134684A JPS60185817A (en) | 1984-03-06 | 1984-03-06 | Preparation of inorganic yarn having high strength |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60185817A JPS60185817A (en) | 1985-09-21 |
| JPS6325083B2 true JPS6325083B2 (en) | 1988-05-24 |
Family
ID=12605952
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4134684A Granted JPS60185817A (en) | 1984-03-06 | 1984-03-06 | Preparation of inorganic yarn having high strength |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60185817A (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4847027A (en) * | 1987-07-06 | 1989-07-11 | Dow Corning Corporation | Infusible preceramic polymers via nitric oxide treatment |
| US4897229A (en) * | 1988-10-12 | 1990-01-30 | Teijin Limited | Process for producing a shaped silicon carbide-based ceramic article |
| US6881693B2 (en) | 2001-04-05 | 2005-04-19 | Ube Industries, Ltd. | Zirconia-containing inorganic fiber and process for the production thereof |
| CN101994169B (en) * | 2010-09-14 | 2014-04-02 | 苏州赛力菲陶纤有限公司 | Continuous silicon carbide fiber preparation method and production device |
| CN102304780B (en) * | 2011-07-27 | 2014-02-26 | 东华大学 | Spinning machine special for gas shield |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS585286B2 (en) * | 1980-03-11 | 1983-01-29 | 財団法人 特殊無機材料研究所 | Method for producing continuous inorganic fibers containing silicon, titanium, and carbon |
| JPS5753893A (en) * | 1980-09-17 | 1982-03-31 | Toshiba Corp | Read-only storage device |
| JPS5753894A (en) * | 1980-09-17 | 1982-03-31 | Toshiba Corp | Read-only device |
| JPS6020485B2 (en) * | 1980-12-18 | 1985-05-22 | 財団法人特殊無機材料研究所 | Method for producing continuous inorganic fiber containing silicon, zirconium and carbon |
| JPS5848503A (en) * | 1981-09-18 | 1983-03-22 | Mitsubishi Electric Corp | Antenna device |
-
1984
- 1984-03-06 JP JP4134684A patent/JPS60185817A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60185817A (en) | 1985-09-21 |
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