JP2007535461A - Process for producing carbon fiber reinforced ceramic composites - Google Patents
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- 229920000049 Carbon (fiber) Polymers 0.000 title claims abstract description 184
- 239000004917 carbon fiber Substances 0.000 title claims abstract description 175
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title claims abstract description 166
- 239000002131 composite material Substances 0.000 title claims abstract description 120
- 238000000034 method Methods 0.000 title claims abstract description 76
- 239000011226 reinforced ceramic Substances 0.000 title claims abstract description 66
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 114
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 101
- 238000004519 manufacturing process Methods 0.000 claims abstract description 75
- 229910052710 silicon Inorganic materials 0.000 claims abstract description 52
- 239000010703 silicon Substances 0.000 claims abstract description 52
- 239000000126 substance Substances 0.000 claims abstract description 49
- 238000001764 infiltration Methods 0.000 claims abstract description 48
- 230000008595 infiltration Effects 0.000 claims abstract description 48
- 239000007788 liquid Substances 0.000 claims abstract description 42
- 239000000203 mixture Substances 0.000 claims abstract description 31
- 238000000151 deposition Methods 0.000 claims abstract description 26
- 239000000805 composite resin Substances 0.000 claims abstract description 25
- 230000008021 deposition Effects 0.000 claims abstract description 20
- 239000002296 pyrolytic carbon Substances 0.000 claims abstract description 19
- 239000011148 porous material Substances 0.000 claims abstract description 13
- 229920000642 polymer Polymers 0.000 claims abstract description 10
- 239000002243 precursor Substances 0.000 claims abstract description 10
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims description 60
- 239000010410 layer Substances 0.000 claims description 31
- 238000007740 vapor deposition Methods 0.000 claims description 27
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 claims description 24
- 238000006243 chemical reaction Methods 0.000 claims description 20
- 229910010271 silicon carbide Inorganic materials 0.000 claims description 15
- 239000000919 ceramic Substances 0.000 claims description 13
- 239000011863 silicon-based powder Substances 0.000 claims description 9
- 239000002344 surface layer Substances 0.000 claims description 9
- 239000007789 gas Substances 0.000 claims description 7
- 239000011261 inert gas Substances 0.000 claims description 6
- 238000010030 laminating Methods 0.000 claims description 6
- 238000002156 mixing Methods 0.000 claims description 6
- 238000000197 pyrolysis Methods 0.000 claims description 6
- 239000004215 Carbon black (E152) Substances 0.000 claims description 5
- 229930195733 hydrocarbon Natural products 0.000 claims description 5
- 150000002430 hydrocarbons Chemical class 0.000 claims description 5
- 238000002289 liquid silicon infiltration Methods 0.000 claims description 5
- 230000008018 melting Effects 0.000 claims description 5
- 238000002844 melting Methods 0.000 claims description 5
- 229920000297 Rayon Polymers 0.000 claims description 3
- 239000002964 rayon Substances 0.000 claims description 3
- 230000008016 vaporization Effects 0.000 claims 1
- 230000000704 physical effect Effects 0.000 abstract description 7
- 230000000694 effects Effects 0.000 abstract description 2
- 239000000835 fiber Substances 0.000 description 19
- 238000005470 impregnation Methods 0.000 description 10
- 238000010438 heat treatment Methods 0.000 description 9
- 238000003475 lamination Methods 0.000 description 7
- 239000007858 starting material Substances 0.000 description 6
- 230000003628 erosive effect Effects 0.000 description 4
- 239000011159 matrix material Substances 0.000 description 4
- 238000000465 moulding Methods 0.000 description 4
- 239000011241 protective layer Substances 0.000 description 4
- 150000001721 carbon Chemical class 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000005011 phenolic resin Substances 0.000 description 3
- 239000002759 woven fabric Substances 0.000 description 3
- KXGFMDJXCMQABM-UHFFFAOYSA-N 2-methoxy-6-methylphenol Chemical compound [CH]OC1=CC=CC([CH])=C1O KXGFMDJXCMQABM-UHFFFAOYSA-N 0.000 description 2
- 239000011230 binding agent Substances 0.000 description 2
- 239000007833 carbon precursor Substances 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 238000000280 densification Methods 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 238000001171 gas-phase infiltration Methods 0.000 description 2
- 239000003779 heat-resistant material Substances 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000012705 liquid precursor Substances 0.000 description 2
- 230000035515 penetration Effects 0.000 description 2
- 229920001568 phenolic resin Polymers 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000004080 punching Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 229910052582 BN Inorganic materials 0.000 description 1
- PZNSFCLAULLKQX-UHFFFAOYSA-N Boron nitride Chemical compound N#B PZNSFCLAULLKQX-UHFFFAOYSA-N 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 238000005229 chemical vapour deposition Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000037361 pathway Effects 0.000 description 1
- 239000011819 refractory material Substances 0.000 description 1
- 230000003252 repetitive effect Effects 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 238000009941 weaving Methods 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
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Abstract
本発明は、炭素繊維強化のセラミックの複合体の製造方法に関し、本発明に係る炭素繊維強化のセラミックの複合体の製造方法は、炭素繊維と、炭素含有のポリマーの前驅体を混合した混合物から成形した炭素繊維強化の樹脂の複合体を製造する段階と、前記炭素繊維強化の樹脂の複合体を高温で熱処理して内部から外部に蒸着速度を早くしながら、急速の熱勾配の化学気相の浸透の工程で熱分解の炭素を蒸着して炭素繊維強化の炭素の複合体を製造する段階と、前記炭素繊維強化の炭素の複合体の気孔に液状のケイ素を浸透させる段階からなったことを特徴とする。このような本発明に係る炭素繊維強化のセラミックの複合体の製造方法は、炭素繊維強化のセラミックの複合体の物性を向上させる効果があり、従来の全ての化学気相の浸透の工程に比べ、5 〜10倍以上の蒸着速度で熱分解の炭素層を蒸着できるので、製造工程と、製造時間、そして製造費用の面で非常に向上した効果を発揮する。The present invention relates to a method for producing a carbon fiber reinforced ceramic composite, and the method for producing a carbon fiber reinforced ceramic composite according to the present invention comprises a mixture of carbon fiber and a precursor of a carbon-containing polymer. A step of producing a molded carbon fiber reinforced resin composite and a chemical vapor with a rapid thermal gradient while heat-treating the carbon fiber reinforced resin composite at a high temperature to increase the deposition rate from the inside to the outside. The step of depositing pyrolytic carbon in the step of infiltration of carbon to produce a carbon fiber reinforced carbon composite, and the step of infiltrating liquid silicon into the pores of the carbon fiber reinforced carbon composite It is characterized by. The method for producing a carbon fiber reinforced ceramic composite according to the present invention has the effect of improving the physical properties of the carbon fiber reinforced ceramic composite, compared to all conventional chemical vapor infiltration processes. Since the pyrolytic carbon layer can be deposited at a deposition rate of 5 to 10 times or more, the production process, production time, and production cost are greatly improved.
Description
本発明は、高温で優れた機械的強度を保持し、熱・化学的の浸蝕などのきびしい環境で優れた耐食性、耐熱性、そして摩擦・摩耗の特性を有する炭素繊維強化のセラミックの複合体の製造方法に関する。 The present invention provides a carbon fiber reinforced ceramic composite that retains excellent mechanical strength at high temperatures and has excellent corrosion resistance, heat resistance, and friction / wear characteristics in harsh environments such as thermal and chemical erosion. It relates to a manufacturing method.
繊維強化のセラミックの複合体(ceramic matrix composites)は、軽量であり、高温で優れた機械的・熱的の特性を有している。このような特性で繊維強化のセラミックの複合体は、航空機と陸上用の運送手段のブレーキディスク、及びパッドなどのような摩擦・摩耗の材料、高温で機械的強度、耐食性、そして耐熱性を要するセラミックエンジン、そしてロケットノズルの部分の超高温の耐熱材等に応用されている。繊維強化のセラミックの複合体は、セラミックの材料(Monolithic Ceramics) が有している脆性破壊の短所を克服するために工夫されて、炭素繊維、または炭化ケイ素繊維で製造したプリフォームの気孔を熱分解の炭素、炭化ケイ素、または窒化ホウ素のような耐熱材料で満たして製造する。 Fiber-reinforced ceramic composites are lightweight and have excellent mechanical and thermal properties at high temperatures. These properties of fiber-reinforced ceramic composites require friction and wear materials such as brake disks and pads for aircraft and land vehicles, mechanical strength, corrosion resistance and heat resistance at high temperatures It has been applied to ceramic engines and ultra high temperature heat-resistant materials in rocket nozzles. Fiber reinforced ceramic composites are devised to overcome the brittle fracture shortcomings of Monolithic Ceramics, and heat the pores of preforms made of carbon or silicon carbide fibers. Manufactured by filling with refractory materials such as cracked carbon, silicon carbide, or boron nitride.
現在まで、繊維強化のセラミックの複合体は、多様な製造工程で製造されているが、大部分の場合、製造工程の中、機械的・熱的の衝撃で繊維に損傷を与えるようになる。このような問題点を解決するために、セラミックの複合体は、低密度の多孔性繊維プリフォームの内に気体状の前驅体を投入した後、熱分解させてセラミックの基地相を蒸着させる。このような工程を化学気相浸透法(chemical vapor infiltration) といい、この製造工程は、低い温度と圧力の条件とで基地相を蒸着させることによって、既存のセラミックの複合体の製造から発生する繊維の損傷の問題点を解決した。 To date, fiber reinforced ceramic composites have been manufactured in a variety of manufacturing processes, but in most cases, the fibers are damaged by mechanical and thermal shock during the manufacturing process. In order to solve such problems, a ceramic composite is prepared by introducing a gaseous precursor into a low-density porous fiber preform and then thermally decomposing it to deposit a ceramic matrix phase. Such a process is called chemical vapor infiltration, which occurs from the production of an existing ceramic composite by depositing a matrix phase at low temperature and pressure conditions. The problem of fiber damage was solved.
しかし、このような工程は、高価の原料物質と製造装備を使用し、製造工程が複雑であり、数百時間以上の工程時間を必要とするので、その応用の分野は、宇宙・航空のような先端産業分野で非常に制約的である。 However, such processes use expensive raw materials and manufacturing equipment, and the manufacturing process is complicated and requires a process time of several hundred hours or more. It is very constrained in advanced industrial fields.
気体状態の原料ガスを用いる化学気相の浸透の工程と違い、液状のケイ素を多孔性の炭素プリフォームに含浸して炭素繊維強化のセラミックの複合体を製造する工程が開発された。 Unlike the chemical vapor infiltration process using a gaseous source gas, a process for producing a carbon fiber reinforced ceramic composite by impregnating liquid carbon with a porous carbon preform has been developed.
Walter Krenkel などは、特許文献1、特許文献2、そして特許文献3で、切断した炭素繊維、液状フェノール、そして炭素の粉末の混合体を高温・高圧の条件で成形した後、高温熱処理の工程で炭素繊維強化の炭素の複合体を製造した。このように製造した炭素繊維強化の炭素の複合体に液状のケイ素を浸透させ、炭素繊維強化のセラミックの複合体を陸上用の車両のブレーキディスク、及び宇宙・航空の分野の耐熱の材料に応用した。 Walter Krenkel et al., In Patent Document 1, Patent Document 2, and Patent Document 3, formed a mixture of cut carbon fiber, liquid phenol, and carbon powder under high-temperature and high-pressure conditions, followed by a high-temperature heat treatment process. Carbon fiber reinforced carbon composites were produced. Liquid silicon is infiltrated into the carbon fiber reinforced carbon composite manufactured in this way, and the carbon fiber reinforced ceramic composite is applied to brake disks for land vehicles and heat resistant materials in the field of space and aviation. did.
しかし、上記のように液状炭素の前驅体を混合し製造した炭素繊維強化の樹脂の複合体は、製造費用の面では既存の化学気相の浸透の工程に比べて効率的であるが、均一な炭素繊維保護層の形成が難しくて、液状のケイ素の含浸の工程の過程で液状のケイ素と炭素繊維の反応を防ぐのが難しく、これは炭素繊維強化のセラミックの複合体の機械的の物性を急激に減少させた。このような問題点を解決するために、特許文献4と、特許文献5、特許文献6、そして特許文献7では、液状有機バインダーを反復的に含浸させたり、混合体の組成を変化させ炭素繊維強化のセラミックの複合体を製造したが、炭素繊維の浸蝕による機械的の物性の低下の防止、及び高温摩擦・摩耗の特性の向上が得れなかった。 However, the carbon fiber reinforced resin composite produced by mixing the liquid carbon precursor as described above is more efficient than the existing chemical vapor infiltration process in terms of production cost. It is difficult to form a protective layer for carbon fiber and it is difficult to prevent the reaction between liquid silicon and carbon fiber during the process of impregnation with liquid silicon, which is the mechanical property of carbon fiber reinforced ceramic composites. Was drastically reduced. In order to solve such problems, Patent Document 4, Patent Document 5, Patent Document 6, and Patent Document 7 repeatedly impregnate a liquid organic binder or change the composition of the mixture to change the carbon fiber. Although a reinforced ceramic composite was produced, it was not possible to prevent deterioration of mechanical properties due to carbon fiber erosion and to improve high-temperature friction / wear characteristics.
前記と他の工程で、特許文献8と、特許文献9では、炭素繊維を織造して作ったプリフォームを等温/ 等圧の化学気相の浸透Isothermal/Isobaric chemical vapor infiltration、ICVI) の工程で熱分解の炭素を蒸着した後、再度炭素の前驅体を液状の含浸方法で密度化の工程を進行して炭素繊維強化のセラミックの複合体を製造した。このような工程は、繊維保護の側面では優れた性能の向上をなしたが、互に異なる炭素繊維強化のセラミックの複合体を一つの構造物に結合しにくく、複雑な形状の炭素繊維強化のセラミックの複合体の製造が容易でない。特に、その製造工程が複雑であり、数百時間以上の製造時間が要するので製造費用の増加を招いた。 In the above and other processes, in Patent Document 8 and Patent Document 9, a preform made by weaving carbon fiber is subjected to isothermal / isobaric chemical vapor infiltration (ICVI) process. After vapor deposition of pyrolytic carbon, a carbon fiber reinforced ceramic composite was manufactured by proceeding a densification process of the carbon precursor again by a liquid impregnation method. Although such a process has improved the performance in terms of fiber protection, it is difficult to combine different carbon fiber reinforced ceramic composites into one structure, and it is difficult to bond carbon fiber reinforced complex shapes. The manufacture of ceramic composites is not easy. In particular, the manufacturing process is complicated, and manufacturing time of several hundred hours or more is required, resulting in an increase in manufacturing cost.
現在までの炭素繊維強化のセラミックの複合体の製造技術に関する問題点を総合的に検討してみれば、大部分の場合、炭素繊維強化のセラミックの複合体の製造のために使われる炭素繊維強化の炭素の複合体の製造工程に多くの製造費用の投入と、技術的の問題点を抱いていることが分かる。例えば、既存の化学気相の浸透の工程の場合、繊維保護層として優れた特性を有しているが、高価の原料物質と製造工程の難しさで、炭素繊維強化の炭素の複合体の製造に適合していない。そして、炭素成分が含まれた有機バインダーの含浸の工程を利用して炭素繊維強化の樹脂の複合体を製造する場合、反復的な含浸の工程を必要とし、繊維保護の側面でその効能が減少するのが分かる。
本発明は、前述した問題点を解決するためのことであって、本発明の目的は、炭素繊維強化のセラミックの複合体の製造に必要な出発物質、及び炭素繊維強化の炭素の複合体の製造方法を改善して炭素繊維強化のセラミックの複合体の熱・機械的の物性を向上させ、高価の製造費用、及び工程による前記の問題点を解決した炭素繊維強化のセラミックの複合体の製造方法を提供するためである。 The present invention is to solve the above-mentioned problems, and the object of the present invention is to provide a starting material necessary for producing a carbon fiber reinforced ceramic composite, and a carbon fiber reinforced carbon composite. Production of carbon fiber reinforced ceramic composites by improving the manufacturing method to improve the thermal and mechanical properties of carbon fiber reinforced ceramic composites and solving the above-mentioned problems due to expensive manufacturing costs and processes This is to provide a method.
本発明者らは、前記の問題点を解決するために、炭素のフェルトプリフォーム、サンドウィッチ構造、または炭素繊維の混合物を出発物質として、製造工程を単純化し、早くて低価の工程で均一な繊維保護層を有する炭素繊維強化の炭素の複合体を製造するために、急速の熱勾配の化学気相の浸透の工程を適用し、これと共に液状のケイ素の浸透の工程を利用して炭素繊維強化のセラミックの複合体を製造する方法を提供するためである。 In order to solve the above-mentioned problems, the inventors have simplified the manufacturing process by using a carbon felt preform, a sandwich structure, or a mixture of carbon fibers as a starting material, and are uniform in a fast and inexpensive process. Applying a rapid thermal gradient chemical vapor infiltration process to produce a carbon fiber reinforced carbon composite with a fiber protective layer and using the liquid silicon infiltration process together with the carbon fiber This is to provide a method for producing a reinforced ceramic composite.
前述した目的を達成するための本発明に係る炭素繊維強化のセラミックの複合体(Cf/C-SiC)の製造方法は、炭素繊維と炭素含有のポリマーの前驅体を混合した混合物から成形した炭素繊維強化の樹脂の複合体を製造する段階と、前記炭素繊維強化の樹脂の複合体を高温で熱処理して内部から外部に蒸着速度を早くしながら急速の熱勾配の化学気相の浸透の工程で熱分解の炭素を蒸着して炭素繊維強化の炭素の複合体を製造する段階と、前記炭素繊維強化の炭素の複合体の気孔に液状のケイ素を浸透させる段階からなったことを特徴とする。 Method for producing a ceramic composite of carbon fiber reinforced according to the present invention for achieving the above object (C f / C-SiC) was formed from a mixture obtained by mixing the pre驅体carbon fibers and carbon-containing polymer A step of producing a carbon fiber reinforced resin composite and a rapid thermal gradient chemical vapor infiltration while heat-treating the carbon fiber reinforced resin composite at a high temperature to increase the deposition rate from the inside to the outside. The method comprises the steps of: depositing pyrolytic carbon in a process to produce a carbon fiber reinforced carbon composite; and impregnating liquid silicon into pores of the carbon fiber reinforced carbon composite. To do.
そして、望ましくは、前記混合物には、前記炭素繊維が10〜60wt% 、前記炭素含有のポリマーの前驅体が30〜60wt% に含まれたことを特徴とする。
また、望ましくは、前記混合物には、炭化ケイ素の粉末が30wt% 以下、炭素の粉末が30wt% 以下が含まれたことを特徴とする。
Preferably, the mixture contains 10 to 60 wt% of the carbon fiber and 30 to 60 wt% of a precursor of the carbon-containing polymer.
Preferably, the mixture contains silicon carbide powder of 30 wt% or less and carbon powder of 30 wt% or less.
また、望ましくは、前記炭素繊維強化の樹脂の複合体は、前記混合物と炭素織物が交代に積層したことを特徴とする。
また、望ましくは、前記成形体には、混合の過程で混合した前記混合物によって炭素繊維とケイ素の反応を防ぐ1 次の表面層が形成され、前記1 次の表面層は、前記液状のケイ素を浸透させる段階で前記液状のケイ素と化学反応して炭化ケイ素とケイ素からなったセラミックの基地層に形成されるのを特徴とする。
Preferably, the carbon fiber reinforced resin composite is characterized in that the mixture and carbon fabric are alternately laminated.
Preferably, the molded body is formed with a primary surface layer that prevents a reaction between carbon fibers and silicon by the mixture that is mixed in the mixing process, and the primary surface layer includes the liquid silicon. A ceramic base layer made of silicon carbide and silicon is formed by chemical reaction with the liquid silicon in the infiltration step.
また、望ましくは、前記成形体は、不活性ガスの雰囲気の下で900 〜2200℃の温度で熱処理した後、前記急速の熱勾配の化学気相の浸透の工程で蒸着する段階で、1 次の表面層の上に2次の表面層である熱分解の炭素の基地層が蒸着するのを特徴とする。 Preferably, the molded body is heat-treated at a temperature of 900 to 2200 ° C. in an inert gas atmosphere, and then deposited in the rapid thermal gradient chemical vapor infiltration process. A base layer of pyrolytic carbon, which is a secondary surface layer, is deposited on the surface layer.
また、望ましくは、前記急速の熱勾配の化学気相の浸透の工程で蒸着する段階で、炭化水素ガスを用いて熱分解の反応の温度が700 〜1200℃、反応の圧力が188 〜1130torrの範囲でなるのを特徴とする。 Preferably, in the step of vapor deposition in the rapid thermal gradient chemical vapor infiltration step, the temperature of the pyrolysis reaction using a hydrocarbon gas is 700 to 1200 ° C., and the reaction pressure is 188 to 1130 torr. It is characterized by a range.
また、望ましくは、前記急速の熱勾配の化学気相の浸透の工程で蒸着する段階で、蒸着の領域を内部から外部に少なくとも複数個に分けて、それぞれの領域で互に異なる速度で蒸着するのを特徴とする。 Preferably, in the step of vapor deposition in the rapid thermal gradient chemical vapor infiltration step, the vapor deposition region is divided into at least a plurality of regions from the inside to the outside, and vapor deposition is performed at different rates in each region. It is characterized by.
また、望ましくは、前記蒸着の領域は、0.5 〜3.0mm/hrの蒸着速度の範囲で内部
から外部に蒸着するのを特徴とする。
また、望ましくは、前記炭素繊維強化の炭素の複合体は、見かけ密度が1.0 〜1.7g/cm3、前記液状のケイ素の浸透の経路に利用される開いた気孔を5 〜30% 有することを特徴とする。
Preferably, the vapor deposition region is vapor-deposited from the inside to the outside within a vapor deposition rate range of 0.5 to 3.0 mm / hr.
Preferably, the carbon fiber reinforced carbon composite has an apparent density of 1.0 to 1.7 g / cm 3 and 5 to 30% of open pores used for the liquid silicon penetration path. Features.
また、望ましくは、前記液状のケイ素を浸透させる段階は、前記炭素繊維強化の炭素の複合体をケイ素の粉末の上に積層させて、反応器の内部を100torr 以下に保持した後、ケイ素の融解点である1410℃以上の温度で加熱して、液状のケイ素をプリフォームの内部に浸透させると同時に、複数個の炭素層と化学反応を誘導するのを特徴とする。 Preferably, the step of impregnating the liquid silicon includes laminating the carbon fiber reinforced carbon composite on the silicon powder and maintaining the interior of the reactor at 100 torr or less, and then melting the silicon. It is characterized by heating at a temperature of 1410 ° C. or higher, which is the point, to infiltrate liquid silicon into the interior of the preform, and at the same time induce chemical reactions with a plurality of carbon layers.
前述した目的を達成するための本発明に係る炭素繊維強化のセラミックの複合体の製造方法は、炭素のフェルトプリフォームを製造する段階と、前記炭素のフェルトプリフォームを内部から外部に蒸着速度を早くしながら、急速の熱勾配の化学気相の浸透の工程で蒸着して炭素繊維強化の炭素の複合体を製造する段階と、前記炭素繊維強化の炭素の複合体の気孔に液状のケイ素を浸透させる段階からなったことを特徴とする。 In order to achieve the above-mentioned object, a method of manufacturing a carbon fiber reinforced ceramic composite according to the present invention includes a step of manufacturing a carbon felt preform, and a deposition rate of the carbon felt preform from the inside to the outside. A stage of rapid chemical vapor chemical vapor infiltration with a rapid thermal gradient to produce a carbon fiber reinforced carbon composite, and liquid silicon in the pores of the carbon fiber reinforced carbon composite. It is characterized by comprising the step of infiltration.
また、望ましくは、前記炭素のフェルトプリフォームは、オキシペン、ペン、レーヨン、ピッチ系などの炭素系の繊維のいずれかからなることを特徴とする。
また、望ましくは、前記炭素のフェルトプリフォームは、マットの積層を0 ゜/+60゜/-60゜のような準等方性として、Z 軸に10mm以下の炭素繊維が補強されたことを特徴とする。
Preferably, the carbon felt preform is made of any one of carbon fibers such as oxypen, pen, rayon, and pitch.
Desirably, the carbon felt preform is reinforced with carbon fibers of 10 mm or less on the Z-axis, with the mat laminated being quasi-isotropic such as 0 ° / + 60 ° / -60 °. Features.
また、望ましくは、前記炭素のフェルトプリフォームには、前記急速の熱勾配の化学気相の浸透の工程で蒸着する段階によって、5 〜100μmの厚さの熱分解の炭素層が蒸着す
ることを特徴とする。
Preferably, the carbon felt preform is deposited with a pyrolytic carbon layer having a thickness of 5 to 100 μm according to the step of vapor deposition in the rapid thermal gradient chemical vapor infiltration process. Features.
また、望ましくは、前記液状のケイ素を浸透させる段階で、前記炭素繊維強化の炭素の複合体に液状のケイ素を含浸して、X 、Y 、Z の3 軸に炭素繊維が補強されたことを特徴とする。 Preferably, in the step of infiltrating the liquid silicon, the carbon fiber reinforced carbon composite is impregnated with liquid silicon, and the carbon fibers are reinforced in the three axes X, Y, and Z. Features.
また、望ましくは、前記急速の熱勾配の化学気相の浸透の工程で蒸着する段階で、炭化水素ガスを用いて熱分解の反応の温度が700 〜1200℃、反応の圧力が188 〜1130torrの範囲でなることを特徴とする。 Preferably, in the step of vapor deposition in the rapid thermal gradient chemical vapor infiltration step, the temperature of the pyrolysis reaction using a hydrocarbon gas is 700 to 1200 ° C., and the reaction pressure is 188 to 1130 torr. It is characterized by a range.
また、望ましくは、前記急速の熱勾配の化学気相の浸透の工程で蒸着する段階で、蒸着の領域を内部から外部に少なくとも複数個に分けて、それぞれの領域で互に異なる速度で蒸着するのを特徴とする。 Preferably, in the step of vapor deposition in the rapid thermal gradient chemical vapor infiltration step, the vapor deposition region is divided into at least a plurality of regions from the inside to the outside, and vapor deposition is performed at different rates in each region. It is characterized by.
また、望ましくは、前記蒸着の領域は、0.5 〜3.0mm/hrの蒸着速度の範囲で内部
から外部に蒸着するのを特徴とする。
また、望ましくは、前記炭素繊維強化の炭素の複合体は、見かけ密度が1.0 〜1.7g/c
m3、前記液状のケイ素の浸透の経路に利用される開いた気孔を5 〜30% 有することを特徴とする。
Preferably, the vapor deposition region is vapor-deposited from the inside to the outside within a vapor deposition rate range of 0.5 to 3.0 mm / hr.
Preferably, the carbon fiber reinforced carbon composite has an apparent density of 1.0 to 1.7 g / c.
m 3 , characterized in that it has 5 to 30% of open pores used in the liquid silicon permeation pathway.
また、望ましくは、前記液状のケイ素を浸透させる段階は、前記炭素繊維強化の炭素の複合体をケイ素の粉末の上に積層させて、反応器の内部を100torr 以下に保持した後、ケイ素の融解点である1410℃以上の温度で加熱して液状のケイ素を前記炭素のフェルトプリフォームの内部に浸透させると共に、複数個の炭素層と化学反応を誘導するのを特徴とする。 Preferably, the step of impregnating the liquid silicon includes laminating the carbon fiber reinforced carbon composite on the silicon powder and maintaining the interior of the reactor at 100 torr or less, and then melting the silicon. It is characterized in that it is heated at a temperature of 1410 ° C. or higher, which is a point, so that liquid silicon penetrates the inside of the carbon felt preform and induces a chemical reaction with a plurality of carbon layers.
以下では、本発明に係る炭素繊維強化のセラミックの複合体の製造方法について説明する。以下の実施の形態において、各混合物の組成、及び製造方法は、その構成の一部を変形してより多様に変形実施できるのである。しかし、変形した実施の形態らが基本的に本発明が請求している技術的の構成要素を含むとすれば、すべて本発明の技術的の範畴に含まれるとみなければならない。 Below, the manufacturing method of the composite of the carbon fiber reinforced ceramic which concerns on this invention is demonstrated. In the following embodiments, the composition of each mixture and the production method can be modified in various ways by modifying a part of the structure. However, if the modified embodiments basically include the technical components claimed by the present invention, all of them should be considered to be included in the technical scope of the present invention.
まず、出発物質の側面において、炭素繊維をX 、Y 、Z の3 軸の方向に補強した炭素のフェルトプリフォームを利用したり、または、0.3 〜150 mmの長さを有する炭素繊維(carbon fibers) 、炭素含有のポリマーの前驅体、炭化ケイ素の粉末、そして黒鉛の粉末からなった混合物と炭素織物(carbon fabrics )を交代に積層させ製造したサンドウィッチ構造を適用したり、または、上記の混合物だけからなった炭素繊維強化の樹脂の複合体(CFRP)が使用できる。 First, on the side of the starting material, a carbon felt preform in which carbon fibers are reinforced in the directions of three axes of X, Y and Z is used, or carbon fibers having a length of 0.3 to 150 mm (carbon fibers). ) Applying a sandwich structure made by alternately laminating a mixture of carbon-containing polymer precursor, silicon carbide powder and graphite powder and carbon fabrics, or just the above mixture Carbon fiber reinforced resin composites (CFRP) can be used.
そして、製造した出発物質は、以下で説明する急速の熱勾配の化学気相の浸透の工程で熱分解の炭素層を蒸着して多孔性の炭素繊維強化の炭素の複合体を製造して、液状のケイ素を炭素繊維強化の炭素の複合体内の開いた気孔に浸透させて炭素繊維強化のセラミックの複合体を製造する。上記の炭素繊維強化のセラミックの複合体は、見かけ密度が2.2g/
cm3以上、見かけ気孔率が1%以下、曲げ強度が100MPa以上、熱伝導度が35W/mk以上
の物性値を有する。
The produced starting material is a porous carbon fiber reinforced carbon composite by depositing a pyrolytic carbon layer in a rapid thermal gradient chemical vapor infiltration process described below. Liquid silicon is infiltrated into the open pores in the carbon fiber reinforced carbon composite to produce a carbon fiber reinforced ceramic composite. The above carbon fiber reinforced ceramic composite has an apparent density of 2.2 g /
It has physical properties of cm 3 or more, apparent porosity of 1% or less, bending strength of 100 MPa or more, and thermal conductivity of 35 W / mk or more.
本発明に係る炭素繊維強化のセラミックの複合体の製造方法は、図1 と、図2 に示したように出発物質に応じて2つの工程に分けられる。
まず、図1 に図示した工程は、0.3 〜150 mmの大きさに切断した炭素繊維、炭素含有のポリマーの前驅体、炭化ケイ素の粉末、そして黒鉛の粉末の混合物と炭素織物を利用して、炭素繊維強化の樹脂の複合体を製造する工程である。
The method for producing a carbon fiber reinforced ceramic composite according to the present invention can be divided into two steps depending on the starting material as shown in FIG. 1 and FIG.
First, the process illustrated in FIG. 1 uses a carbon fiber cut into a size of 0.3 to 150 mm, a precursor of a carbon-containing polymer, a powder of silicon carbide, and a powder of graphite and a carbon fabric, This is a process for producing a composite of carbon fiber reinforced resin.
炭素繊維強化の樹脂の複合体の製造の段階は、0.3 〜150 mmの大きさに切断した炭素繊維を炭素含有のポリマーの前驅体、炭化ケイ素の粉末、そして黒鉛の粉末と共に蒸溜水に入れて、分散と混合の過程を介して均一な混合物を製造する。 The carbon fiber reinforced resin composite is manufactured by placing carbon fibers cut to a size of 0.3 to 150 mm in distilled water together with a carbon-containing polymer precursor, silicon carbide powder, and graphite powder. To produce a uniform mixture through the process of dispersion and mixing.
そして、この混合物は、炭素繊維の表面に炭素含有のポリマーの前驅体、炭化ケイ素の粉末、そして黒鉛の粉末が1 次の表面層を形成し、混合の組成は、炭素繊維が10〜60wt% 、炭素含有の液状の前驅体が30〜60wt% である。そして、炭化ケイ素の粉末と炭素の粉末は、選択的に含まれる。すなわち、炭化ケイ素の粉末が0 〜30wt% 、そして炭素の粉末が0 〜30wt% から組成できる。(S101)(S102)
このように製造した混合物を炭素織物と共に交代に積層して、サンドウィッチ構造の成形体(green body) を作る(S110)。炭素織物は、平織、繻子織、綾織の形態が可能である。ここで、成形体の製造のさらに他の方法には、炭素織物を交代に積層せず、混合物だけを積層して製造できる。
In this mixture, a carbon-containing polymer precursor, silicon carbide powder, and graphite powder form a primary surface layer on the surface of the carbon fiber, and the composition of the mixture is 10 to 60 wt% of the carbon fiber. The carbon-containing liquid precursor is 30 to 60 wt%. A silicon carbide powder and a carbon powder are selectively included. That is, it can be composed of 0-30 wt% silicon carbide powder and 0-30 wt% carbon powder. (S101) (S102)
The mixture thus prepared is alternately laminated with a carbon fabric to form a green body having a sandwich structure (S110). The carbon fabric can be in the form of plain weave, satin weave or twill weave. Here, in still another method of manufacturing the molded body, the carbon woven fabric is not alternately stacked, and only the mixture can be stacked and manufactured.
以后、製造した成形体を成形モールドに裝入した後、80〜250 ℃の熱と、1 〜20 MP
aの圧力とを同時に加え、炭素繊維強化の樹脂の複合体を製造する。この際、製造した炭素繊維強化の樹脂の複合体は、見かけ密度が1.2 〜1.6g/cm3、そして見かけ気孔率が1
〜20% の値を有する。(S110)(S120)(S130)
以上の炭素繊維強化の樹脂の複合体の製造方法は、本出願人が出願した韓国特許出願番号1995-0069130と、韓国特許出願番号1997-0023344に記載した技術的の内容を他の実施の形態に応用して適用できる。
After that, after the produced molded body was inserted into a molding mold, heat of 80 to 250 ° C. and 1 to 20 MP
The pressure of a is simultaneously applied to produce a carbon fiber reinforced resin composite. At this time, the produced carbon fiber reinforced resin composite had an apparent density of 1.2 to 1.6 g / cm 3 and an apparent porosity of 1
It has a value of ~ 20%. (S110) (S120) (S130)
The above-described method for producing a composite of carbon fiber reinforced resin is based on the technical contents described in Korean Patent Application No. 1995-0069130 and Korean Patent Application No. 1997-0023344 filed by the present applicant. Applicable to.
次に、急速の熱勾配の化学気相の浸透の工程で蒸着する段階(S140)は、製造した炭素繊維強化の樹脂の複合体を不活性ガスの雰囲気の下で700 〜2200℃の温度で熱処理した後、急速の熱勾配の化学気相の浸透の工程を進行して、炭素繊維強化の炭素の複合体を製造する段階である。 Next, the vapor deposition step (S140) in the rapid thermal gradient chemical vapor infiltration process is performed in which the produced carbon fiber reinforced resin composite is heated to 700-2200 ° C under an inert gas atmosphere. After the heat treatment, a rapid thermal gradient chemical vapor infiltration process is performed to produce a carbon fiber reinforced carbon composite.
具体的に説明すると、本発明の急速の熱勾配の化学気相の浸透の工程は、密度が1.3g/
cm3以上の緻密な炭素繊維強化の炭素の複合体の製造のためのことで、この急速の熱勾配の化学気相の浸透の工程は、蒸着させるべき領域を少なくとも3 ケ所以上に分けて、各区間で蒸着速度を制御してより急速に蒸着がなされるようにすることである。この際、蒸着速度の制御は、化学気相蒸着装置の内部に設置された熱電対を成形体の内部から外部に順次速い速度で移動させて蒸着を遂行する。
Specifically, the rapid thermal gradient chemical vapor infiltration process of the present invention has a density of 1.3 g /
For the production of dense carbon fiber reinforced carbon composites of cm 3 or more, this rapid thermal gradient chemical vapor infiltration process divides the area to be deposited into at least three locations, It is to control the deposition rate in each section so that the deposition is performed more rapidly. At this time, the vapor deposition rate is controlled by moving a thermocouple installed in the chemical vapor deposition apparatus from the inside of the molded body to the outside at a high speed in order.
すなわち、図4 に示したように、反応器(300) の内部に炭素繊維強化の樹脂の複合体(500) を設置して、中央部に発熱体(400) を設置する。そして、工程のガスには炭化水素ガスを供給しながら実施する。そして、蒸着速度の制御は、前述したように、熱電対( 図示せず) を使用して実施し、蒸着は内部から外部に成される。 That is, as shown in FIG. 4, a carbon fiber reinforced resin composite (500) is installed in the reactor (300), and a heating element (400) is installed in the center. And it implements, supplying hydrocarbon gas to process gas. The vapor deposition rate is controlled using a thermocouple (not shown) as described above, and vapor deposition is performed from the inside to the outside.
そして、図面に図示した蒸着速度の矢印は、短いのが蒸着速度が遅いということを表し、長いのが蒸着速度が速いということを表する。そして、T1の部分が高温であり、T2の部分が低温を表し、これは熱勾配が誘導されるのを表す。 And the arrow of the deposition rate illustrated in the drawing indicates that the deposition rate is slow, and that the arrow indicates that the deposition rate is fast. And the part of T1 is high temperature, the part of T2 represents low temperature, and this represents that a thermal gradient is induced | guided | derived.
この際の蒸着速度は、0.5 〜3.0mm/hrの範囲で内部から外部に蒸着する。一例と
して、領域を内部、中間部、そして外部に分けた後、内部を1.0mm/hrに蒸着し、中
間部を1.5mm/hrに蒸着し、外部を2.0mm/hrに蒸着して、より速かに蒸着が成されるようにする。この際、内部で蒸着速度を遅くしたことで、成形体の内部で蒸着が外部より相対的に遅くなるためである。
In this case, the deposition rate is 0.5 to 3.0 mm / hr, and the deposition is performed from the inside to the outside. As an example, after dividing the region into the inside, the middle part, and the outside, the inside is vapor-deposited at 1.0 mm / hr, the middle part is vapor-deposited at 1.5 mm / hr, and the outside is vapor-deposited at 2.0 mm / hr. Vapor deposition should be done quickly. At this time, it is because the vapor deposition rate is relatively slower than the outside inside the molded body because the vapor deposition rate is slowed inside.
このように、蒸着速度を制御すると、複雑な工程と、長い製造時間のために、多い製造費用を要求する等温/ 等圧気相の浸透法、圧力勾配の化学気相の浸透法、そして既存の等速熱勾配の化学気相の浸透法等、既存の全ての化学気相の浸透の工程に比べて、製造工程と製造費用を革新的に改善できる。 Thus, by controlling the deposition rate, the isothermal / isobaric gas phase infiltration method, which requires high manufacturing cost due to the complicated process and long production time, pressure gradient chemical gas phase infiltration method, and existing Compared to all existing chemical vapor infiltration processes, such as chemical vapor infiltration with a constant thermal gradient, the manufacturing process and manufacturing costs can be innovatively improved.
この急速の熱勾配の化学気相の浸透の工程は、本出願人の特許権である韓国登録特許第0198154 号である熱勾配の化学気相の浸透の工程に比べて蒸着速度を5 〜10倍以上に早くて緻密に進行することによって、炭素繊維の表面に5 〜100μm程度の熱分解の炭素層を
形成できる。
This rapid thermal gradient chemical vapor infiltration process has a deposition rate of 5-10 compared to the thermal gradient chemical vapor infiltration process of Korean Patent No. 0198154, which is a patent right of the present applicant. By proceeding densely more than twice as fast, a pyrolytic carbon layer of about 5 to 100 μm can be formed on the surface of the carbon fiber.
そして、この際、形成された熱分解の炭素層は、液状のケイ素の含浸の工程の時に、液状のケイ素と反応して炭化ケイ素の基地相を形成する反応層に作用する。
このような本発明の急速の熱勾配の化学気相の浸透の工程で製造した炭素繊維強化の樹脂の複合体は、1.0 〜1.7g/cm3の見かけ密度と、5 〜30% の見かけ気孔率値を有する
。
At this time, the pyrolytic carbon layer thus formed acts on the reaction layer that reacts with the liquid silicon to form a silicon carbide matrix phase during the liquid silicon impregnation step.
The carbon fiber reinforced resin composite produced by the rapid thermal gradient chemical vapor infiltration process of the present invention has an apparent density of 1.0 to 1.7 g / cm 3 and an apparent porosity of 5 to 30%. Has a rate value.
次に、液状のケイ素の浸透の工程は、急速の熱勾配の化学気相の浸透の工程で製造した炭素繊維強化の炭素の複合体を1μm〜10mmの粒子の大きさの範囲のケイ素の粉末の上
に位置させる。
Next, the liquid silicon infiltration process is a carbon fiber reinforced carbon composite produced in the rapid thermal gradient chemical vapor infiltration process, with silicon powder in the particle size range of 1 μm to 10 mm Position on top of.
この際の工程の条件は、真空の雰囲気の下でケイ素の融解点である1410℃以上の温度で加熱する。1410℃以上の高温で鎔融したケイ素は、炭素繊維強化の炭素の複合体内に存在する気孔の毛細管力により僅か数分の内に大部分の気孔を満たし、これと同時に炭素繊維の上の炭素の反応層と反応して炭化ケイ素に合成する。このように、最終製造した炭素繊維強化のセラミックの複合体は、30〜60wt% の炭素、35〜60wt% の炭化ケイ素、そして5wt%以下の未反応のケイ素からなる。 The process conditions at this time are heating at a temperature of 1410 ° C. or higher, which is the melting point of silicon, under a vacuum atmosphere. Silicon melted at a high temperature of 1410 ° C or higher fills most of the pores within a few minutes due to the capillary force of the pores existing in the carbon fiber reinforced carbon composite, and at the same time, the carbon above the carbon fiber. It reacts with the reaction layer and synthesizes into silicon carbide. Thus, the final manufactured carbon fiber reinforced ceramic composite consists of 30-60 wt% carbon, 35-60 wt% silicon carbide, and up to 5 wt% unreacted silicon.
次に、図2 に示したように、出発物質として炭素のフェルトプリフォームからなった成形体を利用して炭素繊維強化のセラミックの複合体を製造できる。
まず、X 、Y 、Z の3 軸の方向に補強した炭素のフェルトプリフォームを製造(S200)するのに、具体的に説明すれば、オキシペン、ペン、レーヨン、ピッチ系などの炭素系の繊維をメンドレルに巻いて、一方向の炭素マットを製作して、この方法で製作された炭素マットを積層する。積層の方法は、0 ゜/+60゜/-60゜のような準等方性に交代積層する。
Next, as shown in FIG. 2, a carbon fiber reinforced ceramic composite can be manufactured using a molded body made of a carbon felt preform as a starting material.
First, to manufacture a carbon felt preform reinforced in the three axis directions of X, Y, and Z (S200), specifically, carbon fibers such as oxypen, pen, rayon, pitch, etc. Is wound around a mandrel to produce a unidirectional carbon mat, and the carbon mats produced in this way are laminated. The lamination method is alternate lamination in a semi-isotropic manner such as 0 ° / + 60 ° / -60 °.
そして、積層を最小二つの層とした後、ニードルを利用してパンチングして各層らをZ 軸の方向に補強して前記工程を繰り返えして、厚さの30mm以上のフェルトプリフォームを製作する。 Then, after the lamination is made into a minimum of two layers, punching is performed using a needle to reinforce each layer in the direction of the Z axis and the above process is repeated to form a felt preform having a thickness of 30 mm or more. To manufacture.
このフェルトプリフォームの繊維の体積比は、約10〜55%に製作し、一つの層の厚さは、約0.1 mm以下、Z 軸の繊維の長さは、10mm以下であり、繊維比は、約10%に製作する。また、Z 軸は、15penetration/cm3 の密度のニードルを使用できる。 The felt preform has a fiber volume ratio of about 10 to 55%, the thickness of one layer is about 0.1 mm or less, the length of the Z-axis fiber is 10 mm or less, and the fiber ratio is , To produce about 10%. In addition, a needle having a density of 15 penetration / cm 3 can be used for the Z axis.
以後、炭素のフェルトプリフォームの不純物を除去するために、1700℃以上、真空の雰囲気の下で熱処理を遂行する。このような炭素のフェルトプリフォームの製造方法に関する内容は、本出願人が出願した米国特許出願US10-180778 と、韓国登録特許第27788号の実施の形態を参考の技術とする。 Thereafter, in order to remove impurities from the carbon felt preform, heat treatment is performed in a vacuum atmosphere at 1700 ° C. or higher. The contents relating to the method for producing such a carbon felt preform are based on the embodiments of US patent application US10-180778 filed by the present applicant and Korean Patent No. 27788.
次に、急速の熱勾配の化学気相の浸透の工程を利用して炭素繊維強化の炭素の複合体を製造(S210)するのに、この際の工程は、前述した最初の工程で言及した急速の熱勾配の化学気相の浸透の工程を利用して炭素繊維強化の炭素の複合体を製造(S220)する。 Next, a carbon fiber reinforced carbon composite is manufactured using a rapid thermal gradient chemical vapor infiltration process (S210), which was mentioned in the first step described above. A carbon fiber reinforced carbon composite is manufactured using a rapid thermal gradient chemical vapor infiltration process (S220).
そして、液状のケイ素の浸透の工程を利用して炭素繊維強化のセラミックの複合体を製造する。この液状のケイ素の含浸の工程は、前述した最初の工程の実施の形態と同様に適用する。 Then, a carbon fiber reinforced ceramic composite is manufactured using a liquid silicon infiltration process. This liquid silicon impregnation step is applied in the same manner as in the first embodiment described above.
以下、以上のような方法について、望ましい実施の形態を説明する。
< 実施例1>
30mmの大きさに切断した炭素繊維が30wt% 、フェノールの樹脂が40wt% 、炭素の粉末が5wt%、そして炭化ケイ素の粉末が5wt%の混合物を作って、20wt% の繻子織の形態の炭素織物と交代積層して成形体を製造した。製造した成形体を成形モールドに入れて2MPa
の圧力で10分間加圧と同時に硬化させ、炭素繊維強化の樹脂の複合体を製造した。
Hereinafter, preferred embodiments of the above method will be described.
<Example 1>
30 wt% carbon fiber cut to 30 mm, phenolic resin 40 wt%, carbon powder 5 wt%, and silicon carbide powder 5 wt% mixture to form a 20 wt% satin weave carbon A molded body was produced by alternating lamination with a woven fabric. Put the manufactured molded body into a molding mold and set 2MPa
A carbon fiber reinforced resin composite was produced by curing simultaneously with pressurization at a pressure of 10 minutes.
上記の炭素繊維強化の樹脂の複合体を不活性ガスの雰囲気の下で高温熱処理をした。そして、急速の熱勾配の化学気相の浸透の工程の条件で熱分解の炭素を蒸着させ、炭素繊維強化の炭素の複合体を製造した。 The carbon fiber reinforced resin composite was subjected to high temperature heat treatment in an inert gas atmosphere. Then, pyrolytic carbon was vapor-deposited under the conditions of chemical vapor infiltration with a rapid thermal gradient to produce a carbon fiber reinforced carbon composite.
上記のように製造した炭素繊維強化の炭素の複合体をケイ素の粉末の上に積層して、真空の雰囲気の下で1550℃の温度で加熱して液状のケイ素を含浸させて炭素繊維強化の炭素セラミックの複合体を製造した。この際、製造した炭素繊維強化のセラミックの複合体の物性は、表1 のようである。 A carbon fiber reinforced carbon composite produced as described above is laminated on a silicon powder and heated at a temperature of 1550 ° C. in a vacuum atmosphere to impregnate liquid silicon to form a carbon fiber reinforced carbon composite. A carbon ceramic composite was produced. At this time, the physical properties of the produced carbon fiber reinforced ceramic composite are as shown in Table 1.
< 実施例2>
30mmの大きさに切断した炭素繊維が55wt% 、フェノールの樹脂が35wt% 、炭素の粉末が5wt%、そして炭化ケイ素の粉末が5wt%の混合物を作って成形体を製造した。 実施例2 においては、炭素織物を利用した交代積層はしなかった。製造した成形体を成形モールドに入れ、2MPaの圧力で10分間加圧と同時に硬化させ、炭素繊維強化の樹脂の複合体を
製造した。
<Example 2>
A molded body was manufactured by making a mixture of 55 wt% of carbon fibers cut to a size of 30 mm, 35 wt% of phenol resin, 5 wt% of carbon powder, and 5 wt% of silicon carbide powder. In Example 2, alternating lamination using carbon fabric was not performed. The produced molded body was put in a molding mold and cured simultaneously with pressurization at a pressure of 2 MPa for 10 minutes to produce a carbon fiber reinforced resin composite.
上記の炭素繊維強化の樹脂の複合体を不活性ガスの雰囲気の下で高温熱処理をした。そして、急速の熱勾配の化学気相の浸透の工程の条件で熱分解の炭素を蒸着させ、炭素繊維強化の炭素の複合体を製造した。 The carbon fiber reinforced resin composite was subjected to high temperature heat treatment in an inert gas atmosphere. Then, pyrolytic carbon was vapor-deposited under the conditions of chemical vapor infiltration with a rapid thermal gradient to produce a carbon fiber reinforced carbon composite.
上記のように製造した炭素繊維強化の炭素の複合体をケイ素の粉末の上に積層して、真空の雰囲気の下で1550℃の温度で加熱して液状のケイ素を含浸させ、炭素繊維強化の炭素セラミックの複合体を製造した。製造した炭素繊維強化のセラミックの複合体の物性は、表1 のようである。 A carbon fiber reinforced carbon composite produced as described above is laminated on a silicon powder and heated at a temperature of 1550 ° C. in a vacuum atmosphere to impregnate liquid silicon. A carbon ceramic composite was produced. Table 1 shows the physical properties of the carbon fiber reinforced ceramic composites produced.
< 実施例3>
320Kのオキシペンの繊維をメンドレルに巻いて、一方向の炭素マットを製作して、前記方法によって製作された炭素マットを積層した。積層の方法は、0 ゜/+60゜/-60゜の方法によって交代積層した。
<Example 3>
A unidirectional carbon mat was manufactured by winding 320K oxypen fiber around a mendrel, and the carbon mat manufactured by the above method was laminated. The lamination was carried out alternately by the 0 ° / + 60 ° / -60 ° method.
積層を最小二つの層とした後、ニードルを利用してパンチングして各層らをZ 軸の方向に補強をしながら、前記工程を繰り返して厚さ30mmのプリフォームを製作した。プリフォームのオキシペン繊維の体積比は、約45%に製作し、一つの層の厚さは、約0.9 mm、z 軸の繊維比は、約10%に製作した。 After the lamination was made into a minimum of two layers, punching was performed using a needle to reinforce each layer in the direction of the Z axis, and the above process was repeated to produce a preform having a thickness of 30 mm. The volume ratio of the preformed oxypen fibers was made to about 45%, the thickness of one layer was made to about 0.9 mm, and the fiber ratio of the z axis was made to about 10%.
上記のように製作したプリフォームを1700℃、真空の雰囲気の下で熱処理して不純物を除去した。
製造した炭素のフェルトプリフォームを急速の熱勾配の化学気相の浸透の工程の条件で熱分解の炭素を蒸着させ、炭素繊維強化の炭素の複合体を製造した。
The preform manufactured as described above was heat-treated at 1700 ° C. in a vacuum atmosphere to remove impurities.
The produced carbon felt preform was vapor deposited with pyrolytic carbon under the conditions of rapid thermal gradient chemical vapor infiltration to produce a carbon fiber reinforced carbon composite.
上記のように製造した炭素繊維強化の炭素の複合体をケイ素の粉末の上に積層して、真空の雰囲気の下で1550℃の温度で加熱して液状のケイ素を含浸させ、炭素繊維強化の炭素セラミックの複合体を製造した。製造した炭素繊維強化のセラミックの複合体の物性は、表1 のようである。 A carbon fiber reinforced carbon composite produced as described above is laminated on a silicon powder and heated at a temperature of 1550 ° C. in a vacuum atmosphere to impregnate liquid silicon. A carbon ceramic composite was produced. Table 1 shows the physical properties of the carbon fiber reinforced ceramic composites produced.
< 比較例1>
130 mmの大きさに切断した炭素繊維の54wt% をフェノールの樹脂の36wt% 、炭素の粉末の10wt% と混合して混合物を作って、成形モールドに入れて3MPaの圧力で加圧と同
時に硬化させ、炭素繊維強化の樹脂の複合体を製造した。
<Comparative Example 1>
Mix 54 wt% of carbon fiber cut to 130 mm size with 36 wt% of phenolic resin and 10 wt% of carbon powder to make a mixture, put in a molding mold and cure at the same time with pressure of 3 MPa A carbon fiber reinforced resin composite was produced.
上記の炭素繊維強化の樹脂の複合体を不活性ガスの雰囲気の下で、900 ℃で熱処理して炭素繊維強化の炭素の複合体を製造した。このように、製造した炭素繊維強化の炭素の複合体をケイ素の粉末の上に積層して、真空の雰囲気の下で1600℃の温度で加熱して液状のケイ素を含浸させ、炭素繊維強化の炭素セラミックの複合体を製造した。製造した炭素繊維強化のセラミックの複合体の物性は、表1 のようである。 The carbon fiber reinforced resin composite was heat-treated at 900 ° C. in an inert gas atmosphere to produce a carbon fiber reinforced carbon composite. In this way, the produced carbon fiber reinforced carbon composite is laminated on the silicon powder and heated at a temperature of 1600 ° C. in a vacuum atmosphere to impregnate the liquid silicon. A carbon ceramic composite was produced. Table 1 shows the physical properties of the carbon fiber reinforced ceramic composites produced.
前述したような本発明に係る炭素繊維強化のセラミックの複合体の製造方法は、急速の熱勾配の化学気相の浸透の工程で製造した炭素繊維強化の炭素の複合体の炭素繊維は、均一に蒸着した熱分解の炭素層を有していて、このような熱分解の炭素層は、液状のケイ素の含浸の工程の時、ケイ素と反応して炭化ケイ素に合成するが、熱分解の炭素層は、液状のケイ素の含浸の工程で最も問題点である炭素繊維の浸蝕を防ぐ繊維の保護層としての役割だけでなく、炭化ケイ素を合成する反応層として優れた特性を有し、また炭素繊維と炭化ケイ素の基地相の間に新しい界面を形成して炭素繊維強化のセラミックの複合体の機械的の物性を向上させる。 The method of manufacturing a carbon fiber reinforced ceramic composite according to the present invention as described above, the carbon fiber of the carbon fiber reinforced carbon composite manufactured in a rapid thermal gradient chemical vapor infiltration process is uniform. In the process of impregnation with liquid silicon, such a pyrolytic carbon layer is synthesized into silicon carbide by reacting with silicon during the liquid silicon impregnation process. The layer has not only a role as a fiber protective layer that prevents carbon fiber erosion, which is the most problematic in the liquid silicon impregnation process, but also has excellent properties as a reaction layer for synthesizing silicon carbide. A new interface is formed between the fiber and the silicon carbide matrix phase to improve the mechanical properties of the carbon fiber reinforced ceramic composite.
このような本発明の製造方法によって製造した炭素繊維強化のセラミックの複合体の微細構造は、図3 に示したように、炭素繊維の周囲の暗い灰色の部分は熱分解の炭素層(102) 、明るい灰色の部分は炭化ケイ素層(103) 、そして最も明るい部分が残留ケイ素層(104) である。炭素繊維の周囲の熱分解の炭素層によって炭素繊維の浸蝕はほとんどなく、熱分解の炭素層の周辺に炭化ケイ素が合成したことが分かる。 The microstructure of the carbon fiber reinforced ceramic composite produced by the production method of the present invention is as shown in FIG. 3, in which the dark gray area around the carbon fiber is a pyrolytic carbon layer (102). The light gray part is the silicon carbide layer (103) and the brightest part is the residual silicon layer (104). It can be seen that there was almost no erosion of the carbon fiber by the pyrolytic carbon layer around the carbon fiber, and that silicon carbide was synthesized around the pyrolytic carbon layer.
そして、本発明で急速の熱勾配の化学気相の浸透の工程は、炭素繊維強化の炭素の複合体の製造時間を考慮する際、既存の化学気相の浸透の工程に比べ、10倍以上、従来の熱勾配化学浸透の工程に比べ、5 倍以上の蒸着速度で熱分解の炭素層を蒸着できるので、炭素繊維強化の炭素の複合体の製造費用を顕著に減らすことができる。 And, in the present invention, the rapid thermal gradient chemical vapor infiltration process is more than 10 times compared with the existing chemical vapor infiltration process when considering the production time of the carbon fiber reinforced carbon composite Compared to the conventional thermal gradient chemical infiltration process, the pyrolysis carbon layer can be deposited at a deposition rate of 5 times or more, so that the production cost of carbon fiber reinforced carbon composite can be significantly reduced.
また、炭素含有の液状の前驅体を利用した炭素繊維強化の樹脂の複合体の製造工程のような反復的な密度化の工程なしに、ただ一回の工程で炭素繊維強化の樹脂の複合体を製造でき、急速の熱勾配の化学気相の浸透の工程と液状のケイ素の含浸の工程の組合で炭素繊維強化のセラミックの複合体の製造工程を単純化して、製造費用を顕著に減らすことができるので、多様な分野で炭素繊維強化のセラミックの複合体の応用が可能である。 In addition, a carbon fiber reinforced resin composite can be obtained in a single step without the need for repeated densification steps such as the manufacturing process of a carbon fiber reinforced resin composite using a liquid precursor containing carbon. Simplify the manufacturing process of carbon fiber reinforced ceramic composites by combining the rapid thermal gradient chemical vapor infiltration process and liquid silicon impregnation process, significantly reducing manufacturing costs Therefore, it is possible to apply carbon fiber reinforced ceramic composites in various fields.
そして、0.3 〜150 mmの大きさの炭素繊維を炭素含有のポリマーの前驅体、炭化ケイ素の粉末、そして炭素の粉末と混合した後、炭素織物と交代積層したり、混合物だけで製造した成形体は、分散と混合が均質であるし、炭素繊維、及び炭素織物の1 次の表面層を形成するのに優れた特性を有する。また、1000℃以上の高温熱処理の時、収縮がほとんど起こらないので、寸法の変化がなく、寸法、及び形状の加工に必要な費用を大幅節減できる。 Then, a carbon fiber having a size of 0.3 to 150 mm is mixed with a carbon-containing polymer precursor, silicon carbide powder, and carbon powder, and then alternately laminated with a carbon woven fabric, or a molded body produced only by the mixture. Is homogeneous in dispersion and mixing and has excellent properties for forming the primary surface layer of carbon fibers and carbon fabrics. In addition, since shrinkage hardly occurs during high-temperature heat treatment at 1000 ° C. or higher, there is no change in dimensions, and the cost required for processing of dimensions and shapes can be greatly reduced.
以上のように、本発明に係る炭素繊維強化のセラミックの複合体の製造方法は、炭素繊維強化のセラミックの複合体の物性を向上させる効果があり、従来の全ての化学気相の浸透の工程に比べ、5 〜10倍以上の蒸着速度で熱分解の炭素層を蒸着できるので、製造工程と、製造時間、そして製造費用の面で非常に向上した効果を発揮する。 As described above, the method for producing a carbon fiber reinforced ceramic composite according to the present invention has the effect of improving the physical properties of the carbon fiber reinforced ceramic composite, and all conventional chemical vapor infiltration processes. Compared with, it is possible to deposit a pyrolytic carbon layer at a deposition rate of 5 to 10 times or more, so that the manufacturing process, manufacturing time, and manufacturing cost are greatly improved.
101 :炭素繊維、102 :熱分解の炭素、103 :炭化ケイ素、104 :残留ケイ素 101: carbon fiber, 102: carbon of pyrolysis, 103: silicon carbide, 104: residual silicon
Claims (21)
前記炭素繊維強化の樹脂の複合体を高温熱処理して内部から外部に蒸着速度を早くしながら、急速の熱勾配の化学気相の浸透の工程で熱分解の炭素を蒸着して炭素繊維強化の炭素の複合体を製造する段階と、
前記炭素繊維強化の炭素の複合体の気孔に液状のケイ素を浸透させる段階を含むことを特徴とする炭素繊維強化のセラミックの複合体の製造方法。 Producing a carbon fiber reinforced resin composite formed from a mixture of carbon fiber and a precursor of a carbon-containing polymer;
The carbon fiber reinforced resin composite is heat-treated at a high temperature to increase the deposition rate from the inside to the outside. Producing a carbon composite;
A method for producing a carbon fiber reinforced ceramic composite comprising the step of impregnating liquid silicon into pores of the carbon fiber reinforced carbon composite.
のを特徴とする請求項1記載の炭素繊維強化のセラミックの複合体の製造方法。 2. The method for producing a carbon fiber reinforced ceramic composite according to claim 1, wherein the vapor deposition region is vapor-deposited from the inside to the outside within a vapor deposition rate range of 0.5 to 3.0 mm / hr.
イ素の浸透の経路に利用される開いた気孔を5 〜30% を有することを特徴とする請求項1記載の炭素繊維強化のセラミックの複合体の製造方法。 The carbon fiber reinforced carbon composite has an apparent density of 1.0 to 1.7 g / cm 3 and 5 to 30% of open pores used for the liquid silicon infiltration path. Item 8. A method for producing a carbon fiber reinforced ceramic composite according to Item 1.
ックの複合体の製造方法。 The step of infiltrating the liquid silicon comprises laminating the carbon fiber reinforced carbon composite on the silicon powder and maintaining the inside of the reactor at 100 torr or less, and then the melting point of silicon is 1410 ° C. 2. The carbon fiber reinforced ceramic composite according to claim 1, wherein said composite is heated at the above temperature so that liquid silicon penetrates into the preform and induces a chemical reaction with a plurality of carbon layers. Production method.
前記炭素のフェルトプリフォームを内部から外部に蒸着速度を早くしながら、急速の熱勾配の化学気相の浸透の工程で蒸着して炭素繊維強化の炭素の複合体を製造する段階と、
前記炭素繊維強化の炭素の複合体の気孔に液状のケイ素を浸透させる段階を含むことを特徴とする炭素繊維強化のセラミックの複合体の製造方法。 Producing a carbon felt preform;
Vaporizing the carbon felt preform from the inside to the outside while increasing the deposition rate in a chemical vapor infiltration process with a rapid thermal gradient to produce a carbon fiber reinforced carbon composite;
A method for producing a carbon fiber reinforced ceramic composite comprising the step of impregnating liquid silicon into pores of the carbon fiber reinforced carbon composite.
求項12記載の炭素繊維強化のセラミックの複合体の製造方法。 13. The carbon felt preform is deposited with a pyrolytic carbon layer having a thickness of 5 to 100 [mu] m according to the step of vapor deposition in the rapid thermal gradient chemical vapor infiltration process. A method for producing a carbon fiber reinforced ceramic composite as described.
るのを特徴とする請求項12記載の炭素繊維強化のセラミックの複合体の製造方法。 13. The method of manufacturing a carbon fiber reinforced ceramic composite according to claim 12, wherein the vapor deposition region is vapor-deposited from the inside to the outside within a range of a deposition rate of 0.5 to 3.0 mm / hr.
イ素の浸透の経路に利用される開いた気孔を5 〜30% を有することを特徴とする請求項12記載の炭素繊維強化のセラミックの複合体の製造方法。 The carbon fiber reinforced carbon composite has an apparent density of 1.0 to 1.7 g / cm 3 and 5 to 30% of open pores used for the liquid silicon infiltration path. Item 13. A method for producing a carbon fiber reinforced ceramic composite according to Item 12.
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- 2005-05-27 WO PCT/KR2005/001581 patent/WO2005115945A1/en active Application Filing
- 2005-05-27 EP EP05746091A patent/EP1758837A4/en not_active Withdrawn
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Cited By (8)
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JP2012180226A (en) * | 2011-02-28 | 2012-09-20 | Nippon Steel Corp | Steel manufacturing facility member, and method of manufacturing steel-manufacturing facility member |
JP2014513393A (en) * | 2011-04-06 | 2014-05-29 | シュンク・コーレンストッフテヒニーク・ゲーエムベーハー | Method for manufacturing resistance heating element and resistance heating element |
CN104507676A (en) * | 2012-05-16 | 2015-04-08 | 派特欧赛拉米克斯股份公司 | Shaped composite material |
JP2015523948A (en) * | 2012-05-16 | 2015-08-20 | ペトロチェラミクス ソシエタ ペル アチオニ | Molded composite material |
US10710341B2 (en) | 2012-05-16 | 2020-07-14 | Petroceramics S.P.A. | Shaped composite material |
CN105016760A (en) * | 2015-07-09 | 2015-11-04 | 西北工业大学 | Preparation method for ultra-high-temperature ceramic modified C/C composite material |
JP2018083755A (en) * | 2018-01-09 | 2018-05-31 | ペトロチェラミクス ソシエタ ペル アチオニ | Shaped composite material |
KR102258338B1 (en) * | 2020-11-25 | 2021-05-31 | 국방과학연구소 | Fabrication Method of Carbon Composite |
Also Published As
Publication number | Publication date |
---|---|
KR100624094B1 (en) | 2006-09-19 |
US20080143005A1 (en) | 2008-06-19 |
EP1758837A4 (en) | 2010-04-14 |
WO2005115945A1 (en) | 2005-12-08 |
KR20050113090A (en) | 2005-12-01 |
EP1758837A1 (en) | 2007-03-07 |
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