JPH075367B2 - Method for producing carbon material and carbon / carbon composite material - Google Patents
Method for producing carbon material and carbon / carbon composite materialInfo
- Publication number
- JPH075367B2 JPH075367B2 JP63063172A JP6317288A JPH075367B2 JP H075367 B2 JPH075367 B2 JP H075367B2 JP 63063172 A JP63063172 A JP 63063172A JP 6317288 A JP6317288 A JP 6317288A JP H075367 B2 JPH075367 B2 JP H075367B2
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- Prior art keywords
- carbon
- pitch
- iron
- carbonaceous pitch
- impregnated
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Description
【発明の詳細な説明】 産業上の利用分野 本発明は、炭素材料および炭素/炭素複合材料の製造法
に関する。TECHNICAL FIELD The present invention relates to a method for producing a carbon material and a carbon / carbon composite material.
従来の技術および発明が解決しようとする問題点 炭素質ピツチは、その炭化収率が高いことから高密度炭
素材料の原料として利用されている。しかしながら、炭
化時にガス発生による気泡や亀裂などを生成するという
問題があり、これを解決する方法としてピツチを高圧下
で炭化する方法、Hot Isostatic Pressing(熱間静水圧
加圧下、HIP)が用いられている。この場合、炭化時に
発生するガスがヒーターや断熱材などの炉内部材を汚染
し、場合によつては装置破損をきたす恐れがある。この
ため、炭素材料の製造を目的としたHIPでは、原料をガ
ラスあるいはステンレスなど密閉型の容器(コンテナ)
に入れる、いわゆるキヤニングが行われる。またこのコ
ンテナは、熱処理中に被処理物の形状を維持するという
目的も兼ねている。一方、炭素/炭素複合材料は、1000
℃以上の高温においても高強度、高弾性率を維持し、か
つ熱膨張率が小さい等の特異な性質を有する材料であ
り、航空宇宙機器の部品、ブレーキ、炉材等への利用が
期待されている。炭素質ピツチは、前記の特性から、炭
素/炭素複合材料のマトリツクス用プリカーサとしても
使用されているが、この炭化過程においてもHIPが用い
られており、この場合にも原料をガラスあるいはステン
レス製のコンテナに入れる、いわゆるキヤニングが行わ
れる。Problems to be Solved by Conventional Techniques and Inventions Carbonaceous pitches are used as raw materials for high-density carbon materials because of their high carbonization yields. However, there is a problem that bubbles and cracks are generated by gas generation during carbonization, and as a method to solve this, a method of carbonizing the pitch under high pressure, Hot Isostatic Pressing (HIP under hot isostatic pressure) is used. ing. In this case, the gas generated at the time of carbonization may contaminate the internal members of the furnace such as the heater and the heat insulating material, possibly damaging the device. Therefore, in HIP for the purpose of manufacturing carbon materials, the raw materials are hermetically sealed containers such as glass or stainless steel.
The so-called canning is performed. This container also serves the purpose of maintaining the shape of the object to be processed during the heat treatment. On the other hand, the carbon / carbon composite material is 1000
It is a material that retains high strength and high elastic modulus even at high temperatures above ℃, and has unique properties such as a small coefficient of thermal expansion, and is expected to be used for parts of aerospace equipment, brakes, furnace materials, etc. ing. Due to the above characteristics, the carbonaceous pitch is also used as a precursor for a matrix of a carbon / carbon composite material, but HIP is also used in this carbonization process, and in this case, the raw material is made of glass or stainless steel. So-called canning, which is to put it in a container, is performed.
しかしながら、密閉型の容器(コンテナ)を用いる場合
には、シール機能を付与するために、真空封入などのキ
ヤニング工程が必要となり、さらに緻密化のための再含
浸時にはコンテナ削除と再キヤニングが必要となる。こ
のため製造プロセスが煩雑になるという問題があり、さ
らに発生ガスの内圧により、処理物にクラツクが入つた
り、コンテナの圧力により炭素繊維の織物が変形するこ
とがある。However, when using a closed container (container), a caulking process such as vacuum encapsulation is required to provide a sealing function, and it is necessary to remove the container and re-cane during re-impregnation for densification. Become. Therefore, there is a problem that the manufacturing process becomes complicated, and further, the internal pressure of the generated gas may cause cracks in the processed material, or the carbon fiber woven fabric may be deformed by the pressure of the container.
問題点を解決するための手段 本発明者らは、前記問題点を解決し、簡便かつ高性能な
炭素材料および炭素/炭素複合材料の製造プロセスを確
立すべく研究した結果、本発明の完成に至つた。Means for Solving the Problems The present inventors have conducted research to solve the above problems and establish a simple and high-performance carbon material and carbon / carbon composite material manufacturing process, and as a result, have completed the present invention. It arrived.
本願発明者らの検討結果によれば、前記炭素質ピツチを
熱間静水圧加圧下により熱処理する場合には、密閉型容
器を使用せずとも、被処理物の形状が維持でき、しかも
開放型容器を使用する場合には、発生ガスの内圧によ
り、処理物にクラツクが入るのを防止できることがわか
つた(特願昭62−330018号(特開平1−264966号))。According to the examination results of the inventors of the present application, when the carbonaceous pitch is heat-treated under hot isostatic pressure, the shape of the object to be treated can be maintained without using a closed container, and the open type is used. It has been found that when a container is used, the internal pressure of the generated gas can prevent cracks from entering the treated material (Japanese Patent Application No. 62-330018 (Japanese Patent Application Laid-Open No. 1-264966)).
開放型容器とは、シール機能のない容器である。材質と
しては、アルミニウム、軟鋼、ステンレスなどの金属、
ガラス、黒鉛あるいはセラミツクスなどが使用温度ある
いは使用目的などによつて適宜選択できる。容器の形状
は特に限定されないが、蓋付き、蓋なしのいずれでも良
く、金属フオイルで被処理物を包むだけでも良い。An open container is a container that does not have a sealing function. As materials, metals such as aluminum, mild steel, stainless steel,
Glass, graphite, ceramics or the like can be appropriately selected depending on the use temperature or purpose of use. The shape of the container is not particularly limited, but it may be with or without a lid, or may be wrapped with a metal foil.
本発明者らはさらに検討を重ねた結果、炭化時に生成す
る分解ガスを系内で捕獲することにより上記方法をより
効果的に実施できることを見出した。またこれら分解ガ
ス、特に炭化水素ガスの捕獲に耐火物繊維、鉄および鉄
系合金よりなる群より選ばれる少なくとも一種の物質が
きわめて有効であることを見いだした。本発明はこれら
の物質(捕獲材)を被処理物と共存させることにより達
成される。As a result of further studies, the present inventors have found that the above method can be more effectively carried out by capturing the decomposition gas generated during carbonization in the system. Further, they have found that at least one substance selected from the group consisting of refractory fibers, iron and iron-based alloys is extremely effective in capturing these decomposition gases, particularly hydrocarbon gas. The present invention is achieved by allowing these substances (capturing materials) to coexist with the object to be treated.
(1)炭素質ピッチを開放型容器に入れ、該炭素質ピッ
チの炭化時に生成する分解ガスの捕獲材を該開放型容器
内に該炭素質ピッチに混入しない状態で共存させ、熱間
静水圧加圧下で熱処理し、必要に応じてさらに炭化ある
いは黒鉛化し、該捕獲材の混入していない炭素材料を取
得することを特徴とする炭素材料の製造法、および
(2)炭素繊維のトウに炭素質ピッチを含浸し、この含
浸物を開放型容器に入れ、該炭素質ピッチの炭化時に生
成する分解ガスの捕獲材を該開放型容器内に該含浸物に
混入しない状態で共存させ、熱間静水圧加圧下で熱処理
し、必要に応じてさらに炭化あるいは黒鉛化し、該捕獲
材の混入していない炭素/炭素材料を取得することを特
徴とする炭素/炭素材料の製造法に関する。(1) The carbonaceous pitch is placed in an open container, and a trapping material for a decomposition gas generated when carbonizing the carbonaceous pitch is allowed to coexist in the open container without being mixed with the carbonaceous pitch, and hot isostatic pressure is applied. A method for producing a carbon material, which comprises heat-treating under pressure, and further carbonizing or graphitizing as necessary to obtain a carbon material containing no trapping material, and (2) carbon tow of carbon fiber Impregnated with a fine pitch, put the impregnated product in an open container, and allow a trapping agent for the decomposition gas generated during carbonization of the carbonaceous pitch to coexist in the open container without being mixed with the impregnated product. The present invention relates to a method for producing a carbon / carbon material, which comprises heat-treating under hydrostatic pressure and further carbonizing or graphitizing as necessary to obtain a carbon / carbon material containing no trapping agent.
以下、本発明による炭素材料および炭素/炭素複合材料
の製造法について詳述する。Hereinafter, the method for producing the carbon material and the carbon / carbon composite material according to the present invention will be described in detail.
本発明で用いる炭素質ピツチとは、軟化点100〜400℃、
好ましくは150〜350℃を有する石炭系あるいは石油系の
ピツチである。炭素質ピツチは、光学的に等方性のピツ
チあるいは異方性のピツチのいずれも使用できるが、光
学的異方性相の含量が60〜100vol%、好ましくは80〜10
0vol%の光学的異方性ピツチが特に好ましく用いられ
る。The carbonaceous pitch used in the present invention has a softening point of 100 to 400 ° C.,
A coal-based or petroleum-based pitch having a temperature of 150 to 350 ° C. is preferable. The carbonaceous pitch may be either an optically isotropic pitch or an anisotropic pitch, but the content of the optically anisotropic phase is 60 to 100 vol%, preferably 80 to 10 vol%.
An optically anisotropic pitch of 0 vol% is particularly preferably used.
本発明で用いる炭素繊維としては、ピツチ系、ポリアク
リロニトリル系あるいはレーヨン系のいずれも使用でき
るが、ピツチ系炭素繊維が好ましい。また炭素繊維のト
ウとは、直径5〜100μmの炭素繊維の500〜100,000本
の繊維束を一方向積層物、2次元織物あるいはその積層
物、3次元織物、マツト状成形物、フエルト状成形物な
ど2次元あるいは3次元に成型したものをいう。As the carbon fiber used in the present invention, any one of pitch type, polyacrylonitrile type and rayon type can be used, but the pitch type carbon fiber is preferable. The carbon fiber tow means a unidirectional laminate of 500 to 100,000 fiber bundles of carbon fibers having a diameter of 5 to 100 μm, a two-dimensional woven fabric or its laminate, a three-dimensional woven fabric, a mat-shaped molded product, and a felt-shaped molded product. It is a two-dimensional or three-dimensional molded product.
ここでいうピツチ系炭素繊維とは、炭素質ピツチを溶融
紡糸し、これを不融化、炭化および必要に応じて黒鉛化
することにより得られる繊維である。The pitch-based carbon fiber here is a fiber obtained by melt spinning a carbonaceous pitch, infusibilizing it, carbonizing it, and graphitizing it if necessary.
炭素繊維のトウに炭素質ピツチを含浸する方法は、例え
ば炭素質ピツチを真空下および/または加圧下で加熱、
溶融して炭素繊維トウに含浸する方法が用いられるが、
含浸時の粘度を下げるために、溶剤でカツト・バツクす
ることもできる。溶剤としては、芳香族炭化水素、ピリ
ジン、キノリンなどが使用できる。また緻密化のため、
含浸と後記HIP処理とのサイクルを必要回数行うことが
できる。The method of impregnating the carbon fiber tow with the carbonaceous pitch is, for example, heating the carbonaceous pitch under vacuum and / or pressure,
A method of melting and impregnating carbon fiber tow is used,
In order to reduce the viscosity during impregnation, it is possible to cut and back with a solvent. As the solvent, aromatic hydrocarbon, pyridine, quinoline or the like can be used. In addition, because of the densification,
The cycle of impregnation and HIP treatment described below can be performed as many times as necessary.
本発明においては炭素質ピツチまたは炭素繊維のトウに
炭素質ピツチを含浸して得られる含浸物の被処理物を開
放型容器に入れ、分解ガスの捕獲材を被処理物と混入し
ない状態で開放容器内に入れる。分解ガスの主要成分で
ある炭化水素ガスの主体は周知のようにメタンである。
これら既知の分解ガス成分を物理吸着や化学吸着で捕獲
できる物質も周知だが、前記したように耐火物繊維、鉄
および鉄系合金はきわめて有効な捕獲材である。In the present invention, the impregnated product obtained by impregnating the carbonaceous pitch or the carbon fiber tow with the carbonaceous pitch is placed in an open-type container, and the decomposition gas capturing material is opened without being mixed with the treated object. Put in a container. As is well known, the main component of hydrocarbon gas, which is the main component of cracked gas, is methane.
Although substances that can capture these known decomposed gas components by physical adsorption or chemical adsorption are well known, refractory fibers, iron and iron-based alloys are extremely effective capturing materials as described above.
耐火物繊維としては、例えばカーボン、酸化物系セラミ
ツクス、非酸化物系セラミツクス等の長繊維、短繊維あ
るいはフエルトなどを使用することができる。具体的に
はカーボン、シリカ、アルミナあるいはこれらの混合物
の短繊維が好ましい。As the refractory fibers, for example, long fibers such as carbon, oxide-based ceramics and non-oxide-based ceramics, short fibers or felt can be used. Specifically, short fibers of carbon, silica, alumina or a mixture thereof are preferable.
鉄としては純度99%以上のものが用いられ、鉄系合金と
しては鉄に対してニツケル、クロム、モリブデン、バナ
ジウム、タングステン、シリカおよびマンガンから選ば
れる1種又は2種の金属を10%以下含有するものが用い
られる。Iron with a purity of 99% or more is used, and as an iron-based alloy, 10% or less of one or two kinds of metal selected from nickel, chromium, molybdenum, vanadium, tungsten, silica and manganese is included with respect to iron. What is done is used.
鉄および鉄系合金は、粉状、細線、メツシユあるいは多
孔質成形体などのかたちで使用することができる。Iron and iron-based alloys can be used in the form of powder, fine wire, mesh or porous molded body.
捕獲材を共存させる態様は被処理物中に混入しない限り
特に限定されないが、例えば被処理物を開放型容器に入
れその上部に捕獲材を充填する方法、被処理物を金属フ
オイルで包み、さらにその外側を捕獲材のフエルトで包
む方法、被処理物を捕獲材と共に金属フオイルで包む方
法等が例示できる。また捕獲材が被処理物中に混入する
のを防止するため金属フオイルなどを両者の間に設置す
ることもできる。The mode of coexisting the capturing material is not particularly limited as long as it is not mixed in the object to be treated, for example, a method of placing the object to be treated in an open container and filling the upper part with the capturing material, wrapping the object to be treated with metal foil, and further Examples thereof include a method of wrapping the outside with a capture material felt, a method of wrapping an object to be treated with a capture material in metal foil, and the like. Further, in order to prevent the capturing material from being mixed into the object to be treated, metal foil or the like can be installed between the two.
耐火物繊維、鉄および鉄系合金の2種以上を併用する場
合には、これらを混合、積層などすれば良い。耐火物繊
維、鉄および鉄系合金よりなる群より選ばれる少なくと
も一種の物質の使用量は処理条件によつて任意に決定さ
れるが、通常は被処理物100重量部に対して、耐火物繊
維は10〜1000重量部、好ましくは50〜500重量部、鉄お
よび鉄系合金は10〜5000重量部、好ましくは500〜1000
重量部である。なお、水素の捕獲材、例えばチタン、ジ
ルコニウム、マグネシウム等を共存させることもでき
る。When two or more kinds of refractory fibers, iron and iron-based alloys are used in combination, these may be mixed or laminated. Refractory fiber, the amount of at least one substance selected from the group consisting of iron and iron-based alloys is arbitrarily determined by the processing conditions, usually 100 parts by weight of the object, refractory fiber Is 10 to 1000 parts by weight, preferably 50 to 500 parts by weight, iron and iron-based alloys are 10 to 5000 parts by weight, preferably 500 to 1000 parts by weight.
Parts by weight. Note that a hydrogen trapping material, such as titanium, zirconium, or magnesium, can coexist.
被処理物は熱間静水圧加圧下で熱処理し、必要に応じて
さらに炭化あるいは黒鉛化を行うことにより炭素材料あ
るいは炭素/炭素複合材料を製造する。The object to be treated is heat-treated under hot isostatic pressure, and carbonized or graphitized as necessary to produce a carbon material or a carbon / carbon composite material.
熱間静水圧加圧下での熱処理の条件は、不活性ガスによ
り50〜10000kg/cm2、好ましくは200〜2000kg/cm2に加圧
し、100〜3000℃、好ましくは、400〜2000℃において実
施することができる。圧媒ガスとしては、アルゴン、窒
素、ヘリウムなどの不活性ガスが使用できる。Conditions of heat treatment in the hot isostatic pressure is, 50~10000kg / cm 2 with an inert gas, preferably pressurized to 200~2000kg / cm 2, 100~3000 ℃, preferably, carried out at 400 to 2,000 ° C. can do. As the pressure medium gas, an inert gas such as argon, nitrogen or helium can be used.
本発明において、開放型容器を用いることにより、その
目的は十分達成できるが、必要に応じ、例えば多量の被
処理物を熱処理する場合には、排気機構付HIP装置を好
ましく用いることができる。排気機構付HIPとは、高圧
を維持したままHIP中に被処理物から発生するガス成分
を連続制御して排出できる機構を有する装置であり、具
体的には、発生するガスをその生成物および/または拡
散速度応じて除去量を調節できる排出機構をそなえた装
置である。このガス排出機構は、炉内圧媒ガスとの熱交
換器および炉外での冷却器、減圧装置、流量調節弁など
よりなる。この排気機構付HIP装置の詳細は本願出願人
の一名がすでに出願した特願昭62−253171に記載されて
いる。排気機構付HIP装置における加圧熱処理の条件も
前記のHIP条件に準ずる。In the present invention, the object can be sufficiently achieved by using the open type container, but if necessary, for example, when a large amount of the object to be processed is heat-treated, the HIP device with the exhaust mechanism can be preferably used. The HIP with an exhaust mechanism is a device having a mechanism capable of continuously controlling and discharging the gas components generated from the object to be processed during HIP while maintaining a high pressure, and specifically, the generated gas is a product and And / or a device equipped with a discharge mechanism capable of adjusting the amount of removal according to the diffusion rate. This gas discharge mechanism is composed of a heat exchanger with the pressure medium gas in the furnace, a cooler outside the furnace, a pressure reducing device, a flow rate control valve, and the like. Details of this HIP device with an exhaust mechanism are described in Japanese Patent Application No. 62-253171 filed by the applicant of the present application. The conditions of the pressure heat treatment in the HIP device with the exhaust mechanism also conform to the above HIP conditions.
HIP処理後の処理物は、必要に応じ、常圧下、不活性ガ
ス雰囲気中、400〜2000℃において炭化あるいは2000〜3
000℃において黒鉛化処理することができる。The processed product after HIP treatment is carbonized or 2000 to 3 at 400 to 2000 ° C under normal pressure in an inert gas atmosphere, if necessary.
It can be graphitized at 000 ° C.
複合材料における炭素繊維の体積含有(Vf)は、目的に
よつて任意に決定されるが、通常は5〜70%である。The volume content (Vf) of carbon fibers in the composite material is arbitrarily determined according to the purpose, but is usually 5 to 70%.
実施例 以下に実施例をあげ、本発明を具体的に説明するが、本
発明はこれらに限定されるものではない。EXAMPLES The present invention will be specifically described below with reference to Examples, but the present invention is not limited thereto.
(実施例1) 軟化点280℃の光学的異方性相100vol%の石油系ピツチ
を石英製開放型容器に入れ、その上部にアルミナ50重量
%、シリカ50重量%よりなるセラミツクの短繊維をピツ
チ100重量部にたいして100重量部充填して、HIP装置に
おいてアルゴンガスにより1000kg/cm2に加圧し、800℃
において加圧炭化処理した。得られた炭化物は、密閉型
容器中でHIP処理したものと比べなんら遜色なかつた。
また炉内の汚れは非常に軽徴であつた。Example 1 A petroleum-based pitch having an optical anisotropic phase of 100 vol% with a softening point of 280 ° C. was placed in an open quartz container, and a ceramic short fiber composed of 50% by weight of alumina and 50% by weight of silica was placed on the upper part of the container. 100 parts by weight per 100 parts by weight of Pitch is filled with argon gas in the HIP device to 1000 kg / cm 2 and 800 ° C.
In the above, pressure carbonization treatment was performed. The obtained carbide was comparable to that obtained by HIP treatment in a closed container.
Also, the dirt inside the furnace was a very slight sign.
(実施例2) 実施例1で用いた石油系ピツチをステンレス製フオイル
で包含し、さらにその外側にピツチ100重量部にたいし
て1000重量部の純度99%、粒径5μの鉄粉を充填し、ア
ルゴンガスにより1000kg/cm2に加圧し、800℃において
加圧炭化処理した。得られた炭化物は、亀裂が非常に少
なかつた。また炉内の汚れは非常に軽徴であつた。(Example 2) The petroleum-based pitch used in Example 1 was included in stainless foil, and 1000 parts by weight of iron powder having a purity of 99% and a particle size of 5 µ was filled on the outer side thereof with 100 parts by weight of the pitch. The gas was pressurized to 1000 kg / cm 2 and pressure carbonized at 800 ° C. The resulting carbide had very few cracks. Also, the dirt inside the furnace was a very slight sign.
(比較例1) 実施例1で用いた石油系ピツチをステンレス製コンテナ
に真空封入し、HIP装置において、アルゴンガスにより1
000kg/cm2に加圧し、1000℃において加圧炭化処理した
ところ、炉内の汚れは軽徴であつたが、得られた炭化物
には亀裂が多く見られた。(Comparative Example 1) The petroleum-based pitch used in Example 1 was vacuum-sealed in a stainless steel container, which was then filled with argon gas in a HIP device.
When pressure was applied to 000 kg / cm 2 and pressure carbonization was performed at 1000 ° C, the inside of the furnace was slightly affected, but the obtained carbide had many cracks.
(比較例2) 実施例1で用いた石油系ピツチを開放型ステンレス製コ
ンテナに入れ、HIP装置において、アルゴンガスにより1
000kg/cm2に加圧し、1000℃において加圧炭化処理した
ところ、得られた炭化物には亀裂が少なかつたが、炉内
の汚れがみられた。(Comparative Example 2) The petroleum-based pitch used in Example 1 was placed in an open-type stainless steel container, and was placed in an HIP device using argon gas to
When pressurized to 000 kg / cm 2 and pressure carbonized at 1000 ° C., the obtained carbide had few cracks, but the inside of the furnace was contaminated.
(実施例3) 軟化点280℃の光学的異方性相90vol%の石油系ピツチを
アルミニウム製フオイルで包含し、さらにその外側にア
ルミナ50重量%、シリカ50重量%よりなるセラミツクフ
アイバーのフエルトを、ピツチ100重量部にたいして200
重量部充填し、アルゴンガスにより1000kg/cm2に加圧
し、550℃において加圧炭化処理した。得られた炭化物
は、亀裂が非常に少なかつた。また炉内の汚れは非常に
軽徴であつた。(Example 3) A petroleum-based pitch having an optical anisotropic phase of 90 vol% with a softening point of 280 ° C was included in aluminum foil, and a ceramic fiber felt composed of 50% by weight of alumina and 50% by weight of silica was further provided on the outside thereof. , 200 for 100 parts by weight of pitch
It was filled with parts by weight, pressurized to 1000 kg / cm 2 with argon gas, and pressure carbonized at 550 ° C. The resulting carbide had very few cracks. Also, the dirt inside the furnace was a very slight sign.
(実施例4) 実施例1で用いた石油系ピツチをアルミナ容器に入れ、
その上部にアルミナ50重量%、シリカ50重量%よりなる
セラミツクフアイバーのフエルト、低炭素鋼のスチール
ウール、さらに前記セラミツクフアイバーのフエルトを
それぞれピツチ100重量部にたいして100重量部、300重
量部および25重量部ずつ3層に充填し、排気機構付HIP
装置においてアルゴンガスにより1000kg/cm2に加圧し、
800℃において加圧炭化処理した。得られた炭化物は、
亀裂が非常に少なかつた。また炉内の汚れは非常に軽徴
であつた。(Example 4) The petroleum-based pitch used in Example 1 was placed in an alumina container,
On the upper part, 50% by weight of alumina and 50% by weight of silica, a ceramic fiber felt, low carbon steel wool, and the ceramic fiber felt are 100 parts by weight, 300 parts by weight and 25 parts by weight with respect to 100 parts by weight, respectively. HIP with exhaust system filled in 3 layers each
Pressurized to 1000 kg / cm 2 with argon gas in the device,
It was pressure carbonized at 800 ° C. The obtained carbide is
There were very few cracks. Also, the dirt inside the furnace was a very slight sign.
(実施例5) 直径10μ(ミクロン)のピツチ系炭素繊維の3000本束の
2次元織物(平織)を積層し、これに実施例1で用いた
ピツチを含浸した。含浸物をアルミニウム製フオイルで
包含し、さらにその外側にアルミナ50重量%、シリカ50
重量%よりなるセラミツクフアイバーのフエルトをピツ
チ100重量部にたいして100重量部充填し、HIP装置にお
いて窒素ガスにより1000kg/cm2に加圧し、2Nm3/hrで排
気しながら、550℃において加圧炭化処理した。加圧炭
化に続き、常圧下、不活性ガス雰囲気下で2500℃におい
て黒鉛化処理した。得られた炭素/炭素複合材料を走査
型電子顕微鏡、および偏光顕微鏡で観察したところ、繊
維束内および繊維束間にもマトリツクスがよく充填され
ており、炭素繊維の織物の変形も見られなかつた。また
炉内の汚れは非常に軽徴であつた。Example 5 Two-dimensional woven fabric (plain weave) of 3000 bundles of Pitch-based carbon fibers having a diameter of 10 μ (micron) was laminated and impregnated with the Pitch used in Example 1. The impregnated material was contained in aluminum oil, and 50% by weight of alumina and 50% by weight of silica were added to the outside.
Filling 100 parts by weight of ceramic fiber felt of 100% by weight with respect to 100 parts by weight of Pitch, pressurizing to 1000 kg / cm 2 with nitrogen gas in a HIP device, pressurizing carbonization at 550 ° C while exhausting at 2 Nm 3 / hr. did. Following carbonization under pressure, graphitization was carried out at 2500 ° C. under an inert gas atmosphere under normal pressure. When the obtained carbon / carbon composite material was observed with a scanning electron microscope and a polarization microscope, the matrix was well filled in and between the fiber bundles, and no deformation of the carbon fiber woven fabric was observed. . Also, the dirt inside the furnace was a very slight sign.
(比較例3) 実施例5と同じ含浸物をステンレス製コンテナに真空封
入し、HIP装置において実施例5と同じ条件で処理し
た。得られたものは、コンテナの圧力により炭素繊維の
織物が変形していた。Comparative Example 3 The same impregnated material as in Example 5 was vacuum-sealed in a stainless steel container and treated in the HIP device under the same conditions as in Example 5. In the obtained product, the carbon fiber woven fabric was deformed by the pressure of the container.
(実施例6) 直径10μ(ミクロン)のピツチ系炭素繊維の3000本束の
3次元直交織物に実施例1で用いた石油系ピツチを含浸
した。含浸物をステンレス製フオイルで包含し、その上
部にアルミナ50重量%、シリカ50重量%よりなるセラミ
ツクスフアイバーのフエルトをピツチ100重量部にたい
して300重量部充填して、排気機構付HIP装置において窒
素ガスにより1000kg/cm2に加圧し、800℃において加圧
炭化処理した。加圧炭化に続き、常圧下、不活性ガス雰
囲気下で2500℃において黒鉛化処理した。得られた炭素
/炭素複合材料を走査型電子顕微鏡、および偏光顕微鏡
で観察したところ、繊維束内および繊維束間にもマトリ
ツクスがよく充填されており、炭素繊維の織物の変形も
見られなかつた。また炉内の汚れは非常に軽徴であつ
た。(Example 6) The petroleum-based pitch used in Example 1 was impregnated into a three-dimensional orthogonal woven fabric of 3000 bundles of pitch-based carbon fibers having a diameter of 10 µ (micron). The impregnated material was filled with stainless steel foil, and 300 parts by weight of ceramic felt made of 50% by weight of alumina and 50% by weight of silica was filled in the upper part with 100 parts by weight of the pitch, and nitrogen gas was used in a HIP device with an exhaust mechanism. It was pressurized to 1000 kg / cm 2 and pressure carbonized at 800 ° C. Following carbonization under pressure, graphitization was carried out at 2500 ° C. under an inert gas atmosphere under normal pressure. When the obtained carbon / carbon composite material was observed with a scanning electron microscope and a polarization microscope, the matrix was well filled in and between the fiber bundles, and no deformation of the carbon fiber woven fabric was observed. . Also, the dirt inside the furnace was a very slight sign.
(比較例4) 実施例6と同じ含浸物をステンレス製コンテナに真空封
入し、HIP装置において実施例6と同じ条件で処理し
た。得られたものは、コンテナの圧力により炭素繊維の
織物が変形していた。(Comparative Example 4) The same impregnated material as in Example 6 was vacuum-sealed in a stainless steel container and treated in the HIP apparatus under the same conditions as in Example 6. In the obtained product, the carbon fiber woven fabric was deformed by the pressure of the container.
(実施例7) 直径10μ(ミクロン)のピツチ系炭素繊維の2000本束の
3次元織物に実施例1で用いた石油系ピツチを含浸し
た。含浸物の外側に純度99%、粒径5μの鉄粉を充填
し、排気機構付HIP装置において窒素ガスにより1000kg/
cm2に加圧し、1000℃において加圧炭化処理した。加圧
炭化に続き、常圧下、不活性ガス雰囲気下で1700℃にお
いて炭化処理した。これに再び軟化点280℃の光学的異
方性ピツチを含浸し、排気機構付HIP装置において前記
条件で加圧炭化処理した。このサイクルを5回くりかえ
した。得られた炭素/炭素複合材料は、かさ密度1.74、
曲げ強度は35kg/mm2であつた。(Example 7) The petroleum-based pitch used in Example 1 was impregnated into a three-dimensional woven fabric of 2000 bundles of pitch-based carbon fibers having a diameter of 10 µ (micron). Iron powder with a purity of 99% and a particle size of 5μ is filled on the outside of the impregnated material, and 1000 kg /
It was pressurized to cm 2 and pressure carbonized at 1000 ° C. Following pressure carbonization, carbonization was performed at 1700 ° C. under normal pressure and an inert gas atmosphere. This was again impregnated with an optically anisotropic pitch having a softening point of 280 ° C., and pressure carbonization treatment was performed under the above conditions in a HIP device with an exhaust mechanism. This cycle was repeated 5 times. The obtained carbon / carbon composite material has a bulk density of 1.74,
The bending strength was 35 kg / mm 2 .
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C04B 35/54 D 35/64 302 Z (72)発明者 早田 喜穂 神奈川県川崎市中原区小杉町2―235 (72)発明者 井土 泰二 神奈川県横浜市保土ケ谷区岩井町338 (56)参考文献 特開 平1−264966(JP,A)─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification number Internal reference number FI Technical indication C04B 35/54 D 35/64 302 Z (72) Inventor Kiho Hayada Kosugi, Nakahara-ku, Kawasaki-shi, Kanagawa Town 2-235 (72) Inventor Taiji Ido 338 Iwai-cho, Hodogaya-ku, Yokohama-shi, Kanagawa (56) Reference JP-A-1-264966 (JP, A)
Claims (6)
質ピッチの炭化時に生成する分解ガスの捕獲材を該開放
型容器内に該炭素質ピッチに混入しない状態で共存さ
せ、熱間静水圧加圧下で熱処理し、必要に応じてさらに
炭化あるいは黒鉛化し、該捕獲材の混入していない炭素
材料を取得することを特徴とする炭素材料の製造法。1. A carbonaceous pitch is placed in an open container, and a trapping agent for a decomposition gas produced when carbonizing the carbonaceous pitch is allowed to coexist in the open container without being mixed with the carbonaceous pitch. A method for producing a carbon material, which comprises heat-treating under hydrostatic pressure and further carbonizing or graphitizing as necessary to obtain a carbon material containing no trapping agent.
配して両者の混入を防止する請求項1記載の方法。2. The method according to claim 1, wherein a metal foil is provided between the carbonaceous pitch and the trapping material to prevent the both from being mixed.
くは鉄系合金の粉状体、細線、メッシュもしくは多孔質
成形体である請求項1又は2記載の方法。3. The method according to claim 1 or 2, wherein the capturing material is a refractory fiber aggregate, or a powdery substance of iron or an iron-based alloy, a fine wire, a mesh or a porous molded product.
この含浸物を開放型容器に入れ、該炭素質ピッチの炭化
時に生成する分解ガスの捕獲材を該開放型容器内に該含
浸物に混入しない状態で共存させ、熱間静水圧加圧下で
熱処理し、必要に応じてさらに炭化あるいは黒鉛化し、
該捕獲材の混入していない炭素/炭素材料を取得するこ
とを特徴とする炭素/炭素材料の製造法。4. A carbon fiber tow is impregnated with carbonaceous pitch,
This impregnated product is placed in an open container, and a trapping agent for a decomposition gas generated during carbonization of the carbonaceous pitch is allowed to coexist in the open container without being mixed with the impregnated product, and heat treatment is performed under hot isostatic pressure. And, if necessary, further carbonization or graphitization,
A method for producing a carbon / carbon material, characterized in that a carbon / carbon material not mixed with the capture material is obtained.
両者の混入を防止する請求項4記載の方法。5. The method according to claim 4, wherein a metal foil is provided between the impregnated material and the capturing material to prevent the inclusion of both.
くは鉄系合金の粉状体、細線、メッシュもしくは多孔質
成形体である請求項4又は5記載の方法。6. The method according to claim 4 or 5, wherein the capturing material is a refractory fiber aggregate, or an iron or iron-based alloy powder, fine wire, mesh or porous molded body.
Priority Applications (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63063172A JPH075367B2 (en) | 1988-03-18 | 1988-03-18 | Method for producing carbon material and carbon / carbon composite material |
| EP88312352A EP0323750B1 (en) | 1987-12-28 | 1988-12-28 | Process for producing carbon material and carbon/carbon composites |
| US07/291,007 US5114635A (en) | 1987-12-28 | 1988-12-28 | Process for producing carbon material and carbon/carbon composites |
| DE3855100T DE3855100T2 (en) | 1987-12-28 | 1988-12-28 | Process for the production of carbon material and carbon-carbon composites |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63063172A JPH075367B2 (en) | 1988-03-18 | 1988-03-18 | Method for producing carbon material and carbon / carbon composite material |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH01239064A JPH01239064A (en) | 1989-09-25 |
| JPH075367B2 true JPH075367B2 (en) | 1995-01-25 |
Family
ID=13221575
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63063172A Expired - Lifetime JPH075367B2 (en) | 1987-12-28 | 1988-03-18 | Method for producing carbon material and carbon / carbon composite material |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH075367B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5836050B2 (en) * | 2011-10-14 | 2015-12-24 | 株式会社Ihiエアロスペース | Method and apparatus for densifying porous structure |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01264966A (en) * | 1987-12-28 | 1989-10-23 | Kawasaki Heavy Ind Ltd | Production of carbon material and carbon/carbon composite material |
-
1988
- 1988-03-18 JP JP63063172A patent/JPH075367B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH01239064A (en) | 1989-09-25 |
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