WO2009123282A1 - 複合材料およびその製造方法 - Google Patents
複合材料およびその製造方法 Download PDFInfo
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- WO2009123282A1 WO2009123282A1 PCT/JP2009/056884 JP2009056884W WO2009123282A1 WO 2009123282 A1 WO2009123282 A1 WO 2009123282A1 JP 2009056884 W JP2009056884 W JP 2009056884W WO 2009123282 A1 WO2009123282 A1 WO 2009123282A1
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- composite material
- silicon
- silicon carbide
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- carbide
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Definitions
- An aspect of the present invention generally relates to a composite material mainly composed of boron carbide, silicon carbide, and silicon and a manufacturing method thereof, and more particularly to a composite material that can be manufactured with high specific rigidity and low cost and a manufacturing method thereof.
- Specific rigidity is a parameter obtained by dividing Young's modulus by specific gravity (weight ratio to water), and various mechanical parts may be required to have a material with a high value.
- Examples include a three-dimensional measuring instrument, a linearity measuring instrument, and an exposure machine for forming a pattern of a planar object, which are mobile devices that require a highly accurate positioning function.
- the exposure machine when manufacturing semiconductor wafers, liquid crystal panels, etc., there is a need for a more accurate positioning function that meets the recent demands for pattern miniaturization, and high-speed operation for economical pattern formation. Therefore, it is required to improve the throughput of the apparatus by moving a moving body such as a hydrostatic pressure fluid bearing apparatus on which an object to be exposed or a reticle is mounted at a high speed.
- the most specific boron carbide-based material that is expected to have a high specific rigidity is a substantially pure boron carbide sintered body, but boron carbide is known as a hardly sintered body. Therefore, conventional boron carbide sintered bodies have been manufactured by hot pressing. However, in the hot press sintering method, it is difficult to manufacture large-sized complex products, and the cost of hot press equipment and dies for applying high temperature and high pressure is high, so structural members are actually manufactured. It's not a way to do it.
- Patent Document 1 Patent Document 2, Patent Document 3, Patent Document 4, Patent Document 5, Patent Document 6
- Patent Document 2 Patent Document 3
- Patent Document 4 Patent Document 5
- the fired body is difficult to grind
- the atmospheric pressure sintering temperature is 2200 ° C. Since it is quite high as mentioned above, there is a problem that the firing cost increases.
- Patent Document 7 a material in which boron carbide powder is dispersed as a filler in the metal matrix phase instead of sintering boron carbide is also disclosed (for example, see Patent Document 7).
- This material is a material in which boron carbide is dispersed in aluminum, but because the wettability of boron carbide and aluminum is poor, it is manufactured by hot pressing a mixture of boron carbide and aluminum.
- the manufacturing cost is high, it cannot be said to be a method for manufacturing a structural member in practice.
- composite materials in which silicon having relatively good wettability with boron carbide is used as a metal and a boron carbide molded body is impregnated with molten silicon are also disclosed (for example, Patent Document 8, Patent Document 9, Patent).
- Reference 10 includes materials that can serve as a small amount of carbon source as raw materials.
- this method is a composite material that is highly impregnated with boron carbide although it is impregnated with silicon. There is no change.
- silicon is filled in the gaps between the molded bodies mainly composed of boron carbide, the resulting composite material contains a large amount of silicon.
- Such a material has a low specific rigidity and a high ratio of boron carbide. The rigidity cannot be utilized.
- a composite material in which a material containing silicon carbide in addition to boron carbide is used as a raw material of a molded body, and this molded body is impregnated with molten silicon (see, for example, Patent Document 11).
- the raw material contains a material that can be a small amount of carbon source.
- this method also results in a composite material that is highly filled with boron carbide / silicon carbide, so the grindability is slightly improved compared to that filled with boron carbide alone, but it is still difficult to grind. Will not change.
- silicon is filled in the gaps between the molded bodies mainly composed of boron carbide and silicon carbide, the resulting composite material contains a large amount of silicon.
- Such a material has a low specific rigidity and is low in boron carbide. It cannot take advantage of the high specific rigidity that it has.
- An aspect of the present invention has been made to solve the above-described problems, and provides a composite material having excellent grindability while being a high specific rigidity composite material using the high specific rigidity of boron carbide, and a method for manufacturing the same. It is to be.
- boron carbide X volume part, silicon carbide Y volume part, silicon Z volume part is a main component, 10 ⁇ X ⁇ 60, 20 ⁇ Y ⁇ 70, 5 ⁇ Z ⁇ 30.
- a composite material characterized in that 10 to 50 parts by volume of particles of boron carbide and silicon carbide of 10 ⁇ m or more are provided.
- One embodiment of the present invention is composed mainly of boron carbide X volume part, silicon carbide Y volume part, silicon Z volume part, 10 ⁇ X ⁇ 60, 20 ⁇ Y ⁇ 70, 5 ⁇ Z ⁇ 30, A composite material characterized in that 10 to 50 parts by volume of boron and silicon carbide particles of 10 ⁇ m or more are present. According to this composite material, the grindability can be excellent while having high specific rigidity.
- the specific rigidity of the composite material is 130 GPa or more.
- Another embodiment of the present invention includes a molding step of molding a molded body using a raw material mainly composed of boron carbide, silicon carbide, and a carbon source, and carbon by impregnating the molded body with molten silicon.
- a composite material manufacturing method characterized in that a composite material is formed in which 10 to 50 volume parts of particles of 10 ⁇ m or more of boron carbide and silicon carbide are formed. According to this method for producing a composite material, it is possible to produce a composite material having high specific rigidity and excellent grindability.
- another embodiment of the present invention is a reaction firing in which carbon is converted to silicon carbide by impregnating molten silicon into a molded body formed using a raw material mainly composed of boron carbide, silicon carbide, and carbon source.
- a sintering step mainly composed of X parts by volume of boron carbide, Y parts by volume of silicon carbide, and Z parts by volume of silicon Z; 10 ⁇ X ⁇ 60, 20 ⁇ Y ⁇ 70, and 5 ⁇ Z ⁇ 30.
- a method for producing a composite material characterized in that a composite material having 10 to 50 parts by volume of silicon particles of 10 ⁇ m or more is formed. According to this method for producing a composite material, it is possible to produce a composite material having high specific rigidity and excellent grindability.
- the specific rigidity of the composite material is 130 GPa or more.
- a preferred embodiment of the present invention is a method for producing a composite material, characterized in that the carbon source is mainly composed of carbon powder. According to this method for producing a composite material, it is possible to achieve further higher specific rigidity and further improved grindability.
- a preferred embodiment of the present invention is a method for producing a composite material, which further includes a resin component as a main component of the carbon source. According to this method for producing a composite material, it is possible to achieve further higher specific rigidity and further improved grindability.
- a preferred embodiment of the present invention is a method for producing a composite material, comprising a step of calcining the molded body between the molding step and the reaction sintering step. According to this method for producing a composite material, it is possible to prevent the occurrence of defects during reactive sintering.
- a preferred embodiment of the present invention is a method for producing a composite material, wherein the molding method in the molding step is casting using water as a solvent. According to this method for producing a composite material, it is possible to produce a product having a large complex shape.
- a preferred embodiment of the present invention is a method for producing a composite material, wherein a filling rate of the molded body in the molding step is 60 to 80%. According to this method for producing a composite material, it is possible to prevent the occurrence of defects during molding and firing.
- carbon is obtained by impregnating molten silicon with a molded body formed using a raw material mainly composed of boron carbide, silicon carbide, and carbon source and having a filling rate of 60 to 80%.
- a method for producing a composite material comprising a reaction sintering step for converting to silicon carbide, and forming a composite material mainly composed of boron carbide, silicon carbide, and silicon. According to this method for producing a composite material, it is possible to produce a composite material having high specific rigidity and excellent grindability.
- the specific rigidity of the composite material is 130 GPa or more.
- Specific rigidity is a value obtained by dividing Young's modulus by specific gravity. Since specific gravity is a density ratio to water and has no unit, the unit of specific rigidity is the same as the unit of Young's modulus. Young's modulus is measured by the resonance method, and specific gravity is measured by the Archimedes method.
- the particle size of the particles in the composite material refers to the maximum diameter of the particles when the cut surface of the composite material is wrapped and observed with an optical microscope.
- Coarse grain It shall mean particles having a particle size of 10 ⁇ m or more.
- (F1) When adopting cast molding in the manufacturing process of the composite material in the present invention, it refers to the volume fraction of solids in the slurry.
- (F3) This refers to the solid content filling rate in the manufacturing process of the composite material in the present invention, and is measured by the Archimedes method.
- (F3 ') Volatile components are removed from the solid content filling rate in the composite material manufacturing process of the present invention, and the volatilized components are calculated from the blending ratio.
- the composite material according to an embodiment of the present invention has a structure in which silicon is filled in a gap between powders mainly composed of boron carbide / silicon carbide.
- Boron carbide forming the composite material is added as a main component of the raw material as a boron carbide powder from the molding process.
- Silicon carbide is added as a main component of the raw material as a silicon carbide powder from the molding process (hereinafter referred to as initial charged silicon carbide), and silicon carbide produced by the reaction of silicon in the molded body with silicon (hereinafter referred to as silicon carbide) Reaction product silicon carbide).
- a composite material manufacturing method includes impregnating molten silicon into a molded body mainly composed of boron carbide, initially charged silicon carbide, and a carbon source, and reacting the carbon source with silicon to generate a reaction carbonized product.
- a reactive sintering step is performed in which silicon is produced and silicon is impregnated in the gaps between boron carbide, initially charged silicon carbide, and reaction produced silicon carbide.
- the composite material according to the present invention is characterized in that the volume fraction of particles of 10 ⁇ m or more of boron carbide and initially charged silicon carbide is 10 to 50 parts by volume. Rate and excellent grindability can be achieved.
- the composite material in one embodiment of the present invention is suitably applied to products that require a high specific rigidity and require precise grinding.
- the composite material according to one embodiment of the present invention is composed of 100 parts by volume of the entire composite material, X volume part of boron carbide, Y volume part of silicon carbide, and Z volume part of silicon Z as main components, and 10 ⁇ X ⁇ 60, 20 ⁇ Y. ⁇ 70, 5 ⁇ Z ⁇ 30.
- the amount of boron carbide is 10 parts by volume or less, the composite material cannot obtain a sufficient specific rigidity, and when it is 60 parts by volume or more, the grindability of the composite material is deteriorated. Further, if importance is attached to grindability, it is more preferable that 10 ⁇ X ⁇ 50.
- the composite material cannot obtain a sufficient specific rigidity, and when it is 70 parts by volume or more, the grindability of the composite material is deteriorated. Further, if importance is attached to the specific rigidity, 30 ⁇ Y ⁇ 70 is more preferable, and if importance is given to grindability, 20 ⁇ Y ⁇ 65 is more preferable.
- composite materials with an amount of silicon of 5 parts by volume or less are prone to defects such as cracks or non-impregnated pores in the reaction sintering process. The rate drops.
- the volume fraction of particles of 10 ⁇ m or more of boron carbide and silicon carbide in the composite material according to one embodiment of the present invention is 10 to 50 parts by volume.
- the volume fraction is smaller than 10 parts by volume, the composite material has a sufficient specific rigidity. When it exceeds 50 volume parts, the grindability of a composite material will fall.
- the particles of 10 ⁇ m or more are preferably all of the boron carbide powder added as a raw material, or all of the boron carbide powder added as a raw material and a part of the initially charged silicon carbide powder added as a raw material. .
- the average particle size of the boron carbide powder that is a raw material for producing the composite material in one embodiment of the present invention is preferably 10 ⁇ m to 200 ⁇ m, more preferably 20 ⁇ m to 100 ⁇ m. If the average particle size of the boron carbide powder is 10 ⁇ m or less, cracks are likely to occur in the sintered body during reaction sintering, and the average particle size is preferably 20 ⁇ m or more for the purpose of preventing cracks. Further, when the average particle diameter of boron carbide is 200 ⁇ m or more, the grindability of the composite material is deteriorated, and in order to prevent the deterioration of the grindability, the average particle diameter is desirably 100 ⁇ m or less.
- the particle size of the boron carbide powder used as a raw material is almost the same as the particle size of the boron carbide powder in the composite material.
- boron carbide reacts with the impregnated silicon and the surface is covered with the reaction product, and the surface of boron carbide powder observed by SEM is covered with a layer with slightly different contrast.
- the boron carbide particles of the composite material in one embodiment of the present invention and the particle size thereof are defined including the surface layer made of this reactive organism.
- the reason why cracks occur during reaction sintering when the fine boron carbide powder is used is that the ratio of the reaction product layer on the surface is so large that it cannot be ignored relative to the entire boron carbide powder. It is estimated that it will be.
- the preferable particle diameter of the initially charged silicon carbide that is a raw material for producing the composite material in one embodiment of the present invention varies depending on the amount of boron carbide. That is, the particle diameter of the initially charged silicon carbide in the composite material is not different from the particle diameter of the silicon carbide powder used as a raw material, which is considered to be because the initially charged silicon carbide powder does not react with silicon.
- the initial charge silicon carbide may be fine particles less than 10 ⁇ m, and if a part thereof is taken from silicon carbide. Initially charged silicon carbide requires a coarse particle part of 10 ⁇ m or more and a fine particle part of less than 10 ⁇ m.
- the average particle diameter of silicon carbide that is preferable as the coarse particle content is 20 ⁇ m to 100 ⁇ m, and if it exceeds 100 ⁇ m, the grindability of the composite material deteriorates.
- the average particle size of the initially charged silicon carbide, which is preferable as a fine particle is 0.1 ⁇ m to 5 ⁇ m. When the average particle size is smaller than 0.1 ⁇ m, it becomes difficult to form a highly filled molded body at the time of molding. Grindability decreases.
- Preferred as a carbon source as a raw material for producing a composite material in one embodiment of the present invention is carbon powder, and the particle size of the reaction-molded silicon carbide formed by the reaction of the carbon and silicon is substantially all. Is preferably less than 10 ⁇ m.
- the carbon powder anything from a crystal having a very low crystallinity to a graphite having a very high crystallinity can be used, but generally a carbon black having a very low crystallinity is easily available.
- the preferred average particle size of the carbon powder is 10 nm to 1 ⁇ m.
- organic substances in addition to carbon powder as a carbon source.
- an organic substance is used as the carbon source, it is necessary to select an organic substance having a high residual carbon ratio in the sintering step in a non-oxidizing atmosphere, and particularly suitable organic substances include phenol resins and furan resins.
- phenol resins and furan resins include phenol resins and furan resins.
- such an organic substance is used as a carbon source, it can be expected to serve as a binder, a plasticizer, or a solvent for dispersing powder in the molding process.
- silicon which is a raw material for producing a composite material in one embodiment of the present invention, is melt impregnated, it is impregnated into a molded body regardless of the shape such as powder, granule, or plate. A shape that can be easily arranged may be used.
- silicon may contain substances other than silicon as impurities, but the amount of silicon in the composite material in the present invention is defined as a silicon matrix layer containing the impurities.
- impurities in silicon are prevented from reacting with boron carbide on the surface of boron carbide because the melting point of silicon is lowered to lower the temperature of the reaction sintering process. Therefore, in order to prevent the silicon from blowing out from the reaction sintered body when the temperature is lowered after the reaction sintering, to control the thermal expansion coefficient of silicon, to intentionally impart conductivity to the composite material, etc. Impurities such as C, Al, Ca, Mg, Cu, Ba, Sr, Sn, Ge, Pb, Ni, Co, Zn, Ag, Au, Ti, Y, Zr, V, Cr, Mn, and Mo are added. You can also.
- a method for producing a composite material according to an embodiment of the present invention includes: a molding step of molding a raw material mainly composed of boron carbide, initially charged silicon carbide, and a carbon source; and a molded body impregnated with silicon.
- the reaction sintering step of converting carbon into silicon carbide and filling the voids with silicon is thus provided.
- work aiming at dry press molding, wet press molding, CIP molding, cast molding, injection molding, extrusion molding, plastic molding, vibration molding, etc. And can be selected according to production volume.
- casting molding is particularly suitable for manufacturing large-sized complex products.
- an organic solvent or water may be used as a solvent, but water is used in consideration of simplification of the process and influence on the global environment.
- a solvent is preferred.
- a raw material boron carbide powder, initially charged silicon carbide powder, and a slurry in which a carbon source and water are mixed are first manufactured.
- Additives such as dispersants / peptizers, binders, and plasticizers for production can also be added.
- Suitable additives include ammonium polycarboxylate, sodium polycarboxylate, sodium alginate, ammonium alginate, triethanolamine alginate, styrene / maleic acid copolymer, dibutalftal, carboxymethylcellulose, sodium carboxymethylcellulose, carboxymethylcellulose ammonium, methylcellulose, Sodium methylcellulose, polyvinyl alcohol, polyethylene oxide, sodium polyacrylate, oligomers of acrylic acid or its ammonium salt, various amines such as monoethylamine, pyridine, piperidine, tetramethylammonium hydroxide, dextrin, peptone, water-soluble starch, acrylic Various resin emulsions such as emulsions, resorches Etc. can be mentioned various water-soluble resins, various non-water-soluble resin, water glass, such as novolac type phenol resins such as type phenolic resin.
- a water-insoluble additive it is preferable to form an emulsion or coat the powder surface.
- a slurry production process includes a grinding process, It is preferred to add it after the grinding step.
- both gypsum casting using a gypsum-type capillary suction force and pressure casting that directly applies pressure to the slurry can be used.
- an appropriate pressure is 0.1 MPa to 5 MPa.
- the filling rate of the molded body is preferably 60 to 80%, more preferably 65 to 75%.
- the lower limit of the preferable filling rate is to reduce the silicon content of the reaction sintered body as described above.
- the upper limit of the preferable filling rate is that the molded body having an excessively high filling rate is not made of silicon. This is because impregnation is difficult.
- the filling rate of the above-mentioned compact is the filling rate of each powder of boron carbide, silicon carbide, and carbon, and excludes components such as additives that volatilize in the firing process. Therefore, in the case of using an additive having a residual carbon content such as a phenol resin, the residual carbon content is added as a filling rate.
- the filling rate of the molded body measured by the Archimedes method is indicated as F3
- the filling rate excluding the volatilized content is indicated as F3 ′. It shall refer to the value of F3 ′.
- F1 is preferably 40% or more.
- F3 and F3 ′ are larger in pressure casting than in gypsum casting, but in the present invention, F3 and F3 ′ are obtained in pressure casting and gypsum casting. There is no big difference, and plaster molding suitable for high-mix low-volume production can be suitably employed.
- This calcining process may not be necessary if the compact has a small and simple shape. However, if the compact has a large and complex shape, it may cause damage during handling or cracking during reaction sintering. In order to prevent this, it is preferable to provide a calcination step.
- the preferable temperature for the calcination is 1000 to 2000 ° C. If the temperature is lower than 1000 ° C., the effect of the calcination cannot be expected. If the temperature is higher than 2000 ° C., the sintering starts and the workpiece shrinks. There is a possibility that the advantage as a near net shape manufacturing process in which the firing shrinkage, which is a characteristic of the manufacturing process, is almost zero may be impaired.
- a preferable firing atmosphere in the calcination step is a non-oxidizing atmosphere.
- this calcining process is normally performed also as the degreasing process of a molded object, you may provide a degreasing process separately before a calcining process when there exists a concern about the contamination of a furnace.
- the degreasing step may be provided without the calcination step.
- a degreasing temperature necessary for decomposing and removing the binder may be adopted.
- the preferable reaction sintering temperature in the subsequent silicon impregnation reaction sintering step is 1800 ° C. from the melting point of silicon.
- the reaction sintering temperature is as low as possible and the maximum temperature keeping time is short as long as silicon is completely impregnated and pores are eliminated.
- the melting point of silicon is 1414 ° C.
- a reaction sintering temperature of 1430 ° C. or higher is usually necessary.
- the reaction sintering temperature is lowered to about 1350 ° C. It is also possible.
- the composite material according to one embodiment of the present invention has a molded body in which the carbon content in the molded body reacts with silicon to expand into silicon carbide, and silicon fills the voids.
- the composition ratio of the reaction sintered body is clarified by measuring the blending ratio of the raw materials and the filling factor F3 ′ of the compact.
- the black part of FIG. 3 which is a photograph of the microstructure to be described later is a boron carbide or silicon carbide particle, and the white part is silicon, it is easy to identify the particle and silicon, and the coarse and fine particles.
- coarse silicon carbide and coarse boron carbide can be easily identified by SEM / EPMA analysis.
- the composition ratio of the raw materials for realizing the composition ratio of the composite material in one embodiment of the present invention can be calculated from the composition ratio of the target composite material and the filling ratio of the molded body.
- a preferable mixing ratio of each raw material is 0 to 45 parts by weight of the carbon source with respect to 100 parts by weight in total of 10 to 90 parts by weight of boron carbide and 90 to 10 parts by weight of initially charged silicon carbide.
- the carbon source here means parts by weight in terms of carbon.
- carbon powder it is the blended weight itself, and when an additive with a residual carbon content is used, the residual carbon is added to the blended weight. It is the value multiplied by the rate.
- Carbon may be 0 part by weight, but in this case, since the reaction of carbon reacting with silicon and expanding is not available, it becomes difficult to completely fill the voids of the molded body with silicon, and pores remain. There is a risk. Moreover, when there is too much carbon content, there exists a danger that a crack will generate
- a more preferable mixing ratio of the carbon source is 10 to 40 parts by weight with respect to a total of 100 parts by weight of boron carbide and initially charged silicon carbide.
- the preferable amount of silicon necessary for the reactive sintering is 105 to 200%, more preferably 110 to 150% of the amount of silicon necessary for converting the carbon content into silicon carbide and filling the voids. Adjust according to the shape.
- the preferred specific rigidity of the composite material in one embodiment of the present invention is 130 GPa or more, more preferably 140 GPa or more.
- one of the objects of the present invention is to provide a composite material having a high specific rigidity, there is no preferable upper limit of the specific rigidity, but in reality, it is difficult to make a composite material having a specific rigidity of 200 GPa or more. In order to achieve high specific rigidity while maintaining excellent grindability, the upper limit is about 170 GPa.
- the composite material according to an embodiment of the present invention is preferably applied to a product that requires high specific rigidity, requires precise grinding, and has a large grinding cost due to a large complex shape.
- a particularly suitable product application is a semiconductor / liquid crystal manufacturing apparatus member.
- a particularly suitable product application example is a member for an exposure apparatus. By using it as a wafer support member such as a susceptor stage and an optical system support member such as a reticle stage, the positioning accuracy of the exposure apparatus is improved. The throughput of the apparatus can be improved by shortening the positioning time.
- Table 1 shows a list of examples and comparative examples shown below.
- the slurry concentration in each preparation example is indicated by F1 in Table 1.
- the amount of binder added in each formulation example is indicated by the difference between F3 'and F3 in Table 1.
- specific gravity was measured by Archimedes method and Young's modulus was measured by resonance method to calculate specific stiffness.
- the surface-finished one was placed on a dynamometer (model number 9256C2 manufactured by Kistler), and rotated at a rotational speed of 100 m / min (3200 rpm) with a ⁇ 10 mm core drill (# 60, manufactured by Asahi Diamond Industrial Co., Ltd.). A hole with a depth of 4 mm was drilled at a step amount of 0.2 mm, and the resistance of the machining was measured and the state of chipping around the hole was confirmed.
- the maximum value of the machining resistance was 2000 N or more was evaluated as x, the case where it was 1500 to 2000 N, and the case where it was less than 1500 N was evaluated as o.
- the machining resistance decreased in a short time, and those that were stable at the low value were evaluated at the low value. Moreover, even if the machining resistance was ⁇ or ⁇ , the case where cracks presumed to be caused by machining during machining and the case where tool breakage occurred were rated as x.
- the evaluation of the chipping state was evaluated as “ ⁇ ” when the outer peripheral chip of the hole was less than 0.3 mm, “ ⁇ ” when 0.3 mm to less than 0.5 mm, and “x” when 0.5 mm or more.
- the microstructure was observed by cutting the fired body into an appropriate size, lapping the surface with 1 ⁇ m abrasive grains, and setting it to 2800 times with an optical microscope.
- FIG. 1 shows the particle size distribution measurement results of coarse boron carbide having an average particle size of 50 ⁇ m, coarse silicon carbide having an average particle size of 65 ⁇ m, and fine silicon carbide having an average particle size of 0.6 ⁇ m used in the practice of the present invention.
- the particle size distribution is measured by a laser particle size analyzer (MT3000 manufactured by Nikkiso), and the above average particle size indicates the volume average particle size.
- the coarse particles substantially do not contain particles of 10 ⁇ m or less, and the fine particles do not substantially contain coarse particles of 10 ⁇ m or more.
- Fig. 2 shows a graph showing the heat curve of calcination and reaction sintering.
- FIG. 3 shows an optical microscope image of the microstructure of the reaction sintered body of Example 2. As described above, it was easy to distinguish between coarse particles of 10 ⁇ m or more and fine particles of 10 ⁇ m or less. (Examples 1 to 3) 30 parts by weight of silicon carbide powder having an average particle diameter of 0.6 ⁇ m, 70 parts by weight of boron carbide powder having an average particle diameter of 50 ⁇ m, and 10 to 30 parts by weight of carbon black powder having an average particle diameter of 55 nm are silicon carbide powder and boron carbide powder.
- a dispersant added to the carbon black powder and adjusting the pH to 8 to 9.5 with aqueous ammonia or the like.
- the placed slurry was cast to produce a molded body having a thickness of about 10 mm.
- the molded body is naturally dried, dried at 100 to 150 ° C., degreased by holding at a temperature of 600 ° C. for 2 hours under a reduced pressure of 1 ⁇ 10 ⁇ 4 to 1 ⁇ 10 ⁇ 3 torr, and held at a temperature of 1700 ° C. for 1 hour. Calcination is performed. After calcination, the reaction sintered body was manufactured by heating to a temperature of 1470 ° C. and holding for 30 minutes, and impregnating molten silicon into the molded body. In Examples 1 to 3, the amount of carbon powder added is 10, 20, and 30 parts by weight, respectively.
- Example 4 20 parts by weight of silicon carbide powder having an average particle size of 0.6 ⁇ m, 30 parts by weight of silicon carbide powder having an average particle size of 65 ⁇ m, 50 parts by weight of boron carbide powder having an average particle size of 50 ⁇ m, and carbon black powder having an average particle size of 55 nm 30 parts by weight are placed in and dispersed in pure water to which 0.1 to 1 part by weight of a dispersant is added to silicon carbide powder, boron carbide powder, and carbon black powder, and the pH is adjusted to 8 to 9.5 with ammonia water or the like. To prepare a low viscosity slurry of less than 500 CP.
- the reaction sintered body was manufactured by heating to a temperature of 1470 ° C. and holding for 30 minutes, and impregnating molten silicon into the molded body.
- Example 5 25 parts by weight of silicon carbide powder having an average particle size of 0.6 ⁇ m, 25 parts by weight of silicon carbide powder having an average particle size of 65 ⁇ m, 50 parts by weight of boron carbide powder having an average particle size of 50 ⁇ m, and carbon black powder having an average particle size of 55 nm 10 parts by weight is dispersed in pure water to which 0.1 to 1 part by weight of a dispersant is added with respect to silicon carbide powder, boron carbide powder and carbon black powder, and the pH is adjusted to 8 to 9.5 with ammonia water or the like.
- a low-viscosity slurry of less than 500 cp was prepared. After mixing this slurry with a pot mill or the like for several hours, add 1 to 2 parts by weight of binder to silicon carbide powder, boron carbide powder, or carbon powder, and then defoaming to place an acrylic pipe with an inner diameter of 80 mm on the gypsum plate. The placed slurry was cast to produce a molded body having a thickness of about 10 mm. The molded body is naturally dried, dried at 100 to 150 ° C., degreased by holding at a temperature of 600 ° C.
- the reaction sintered body was manufactured by heating to a temperature of 1470 ° C. and holding for 30 minutes, and impregnating molten silicon into the molded body.
- Example 6 25 parts by weight of silicon carbide powder having an average particle size of 0.6 ⁇ m, 25 parts by weight of silicon carbide powder having an average particle size of 65 ⁇ m, 50 parts by weight of boron carbide powder having an average particle size of 50 ⁇ m, and carbon black powder having an average particle size of 55 nm 20 parts by weight is dispersed in pure water to which 0.1 to 1 part by weight of a dispersant is added with respect to silicon carbide powder, boron carbide powder and carbon black powder, and the pH is adjusted to 8 to 9.5 with ammonia water or the like. A low-viscosity slurry of less than 500 cp was prepared.
- the reaction sintered body was manufactured by heating to a temperature of 1470 ° C. and holding for 30 minutes, and impregnating molten silicon into the molded body.
- Example 7 50 parts by weight of silicon carbide powder having an average particle size of 0.6 ⁇ m and 50 parts by weight of boron carbide powder having an average particle size of 50 ⁇ m were added with 0.1 to 1 part by weight of a dispersant relative to silicon carbide and boron carbide powder. The mixture was dispersed in pure water, and the pH was adjusted to 8 to 9.5 with ammonia water or the like to prepare a low viscosity slurry of less than 500 cp.
- the reaction sintered body was manufactured by heating to a temperature of 1470 ° C. and holding for 30 minutes, and impregnating molten silicon into the molded body.
- Example 8 80 parts by weight of silicon carbide powder having an average particle diameter of 0.6 ⁇ m, 20 parts by weight of boron carbide powder having an average particle diameter of 50 ⁇ m, and 10 parts by weight of carbon black powder having an average particle diameter of 55 nm are obtained by silicon carbide powder, boron carbide powder, carbon Disperse in pure water with 0.1 to 1 part by weight of dispersant added to black powder, and adjust pH to 8 to 9.5 with aqueous ammonia, etc.
- the slurry was placed in pure water and dispersed, and the pH was adjusted to 8 to 9.5 with ammonia water or the like to prepare a low viscosity slurry of less than 500 cp.
- the molded body is naturally dried, dried at 100 to 150 ° C., degreased by holding at a temperature of 600 ° C.
- the reaction sintered body was manufactured by heating to a temperature of 1470 ° C. and holding for 30 minutes, and impregnating molten silicon into the molded body.
- Comparative Example 2 50 parts by weight of silicon carbide powder with an average particle size of 0.6 ⁇ m, 50 parts by weight of boron carbide powder with an average particle size of 50 ⁇ m, and 50 parts by weight of carbon powder with an average particle size of 55 nm are silicon carbide powder, boron carbide powder, carbon black powder
- the mixture was dispersed in pure water to which 0.1 to 1 part by weight of a dispersant was added, and the pH was adjusted to 8 to 9.5 with aqueous ammonia or the like to prepare a low viscosity slurry of less than 500 cp.
- the reaction sintered body was manufactured by heating to a temperature of 1470 ° C. and holding for 30 minutes, and impregnating molten silicon into the molded body.
- Comparative Example 3 80 parts by weight of silicon carbide powder having an average particle diameter of 0.6 ⁇ m, 20 parts by weight of boron carbide powder having an average particle diameter of 4 ⁇ m, and 50 parts by weight of carbon powder having an average particle diameter of 55 nm are mixed with silicon carbide powder, boron carbide powder, carbon black
- a powder having a low viscosity of less than 500 cp was prepared by dispersing in pure water to which 0.1 to 1 part by weight of a dispersant was added to the powder and adjusting the pH to 8 to 9.5 with ammonia water or the like.
- Comparative Example 2 fine cracks were generated in the composite material, the specific rigidity was lowered, and chipping was likely to occur during grinding.
- the present invention by providing a composite material with high specific rigidity and excellent grindability, and a method for manufacturing the same, high specific rigidity required for semiconductor / liquid crystal manufacturing apparatuses and the like and high dimensional accuracy are provided. Therefore, it can be applied to a member having a large complex shape.
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Abstract
Description
比剛性とはヤング率を比重で割った値であり、比重は水に対する密度比で単位はないので、比剛性率の単位はヤング率の単位と同じである。ヤング率は共振法にて測定し、比重はアルキメデス法により測定する。
複合材料中の粒子の粒径とは複合材料の切断面をラップし、光学顕微鏡で観察したときの粒子のさしわたし最大径をさすものとする。
上記粒径が10μm以上の粒子をさすものとする。
上記粒径が10μm未満の粒子をさすものとする。
本発明における複合材料の製造工程において鋳込成形を採用するとき、スラリー中の固形分の体積分率をさすものとする。
本発明における複合材料の製造工程における成形体の固形分の充填率をさすものでアルキメデス法により測定する。
(F3’)
本発明における複合材料の製造工程における成形体の固形分の充填率から揮散分を除いたものであり、揮散分は調合比から計算する。
(実施例)
以下、本発明の一実施の形態について表、図を参照して説明する。
(実施例1~3)
平均粒径が0.6μmの炭化珪素粉末30重量部と平均粒径が50μmの炭化硼素粉末70重量部、平均粒径が55nmのカーボンブラック粉末10~30重量部を炭化珪素粉末、炭化硼素粉末、カーボンブラック粉末に対して0.1~1重量部の分散剤を添加した純水中に入れ分散させ、アンモニア水等でpHを8~9.5に調整して500CP未満の低粘度のスラリーを作製した。このスラリーをポットミル等で数時間混合した後バインダーを炭化珪素粉末、炭化硼素粉末、カーボン粉末に対して1~2重量部添加し混合、その後脱泡し石膏板の上に内径80mmのアクリルパイプを置きスラリーを鋳込み、厚み10mm程度の成形体を作製した。成形体は自然乾燥、100~150℃の乾燥の後、1×10-4~1×10-3torrの減圧下において温度600℃で2h保持し脱脂を行い、温度1700℃で1h保持することで仮焼を行う。仮焼を行った後、温度1470℃に加熱し30min保持し、成形体中に溶融したシリコンを含浸させることにより反応焼結体を製造した。なお、実施例1~3はカーボン粉末の添加量がそれぞれ10、20、30重量部である。
(実施例4)
平均粒径が0.6μmの炭化珪素粉末20重量部、平均粒径が65μmの炭化珪素粉末30重量部と平均粒径が50μmの炭化硼素粉末50重量部、平均粒径が55nmのカーボンブラック粉末30重量部を炭化珪素粉末、炭化硼素粉末、カーボンブラック粉末に対して0.1~1重量部の分散剤を添加した純水中に入れ分散させ、アンモニア水等でpHを8~9.5に調整して500CP未満の低粘度のスラリーを作製した。このスラリーをポットミル等で数時間混合した後バインダーを炭化珪素粉末、炭化硼素粉末、カーボン粉末に対して1~2重量部添加し混合、その後脱泡し石膏板の上に内径80mmのアクリルパイプを置きスラリーを鋳込み、厚み10mm程度の成形体を作製した。成形体は自然乾燥、100~150℃の乾燥の後、1×10-4~1×10-3torrの減圧下において温度600℃で2h保持し脱脂を行い、温度1700℃で1h保持することで仮焼を行う。仮焼を行った後、温度1470℃に加熱し30min保持し、成形体中に溶融したシリコンを含浸させることにより反応焼結体を製造した。
(実施例5)
平均粒径が0.6μmの炭化珪素粉末25重量部、平均粒径が65μmの炭化珪素粉末25重量部と平均粒径が50μmの炭化硼素粉末50重量部、平均粒径が55nmのカーボンブラック粉末10重量部を炭化珪素粉末、炭化硼素粉末、カーボンブラック粉末に対して0.1~1重量部の分散剤を添加した純水中に入れ分散させ、アンモニア水等でpHを8~9.5に調整して500cp未満の低粘度のスラリーを作製した。このスラリーをポットミル等で数時間混合した後バインダーを炭化珪素粉末、炭化硼素粉末、カーボン粉末に対して1~2重量部添加し混合、その後脱泡し石膏板の上に内径80mmのアクリルパイプを置きスラリーを鋳込み、厚み10mm程度の成形体を作製した。成形体は自然乾燥、100~150℃の乾燥の後、1×10-4~1×10-3torrの減圧下において温度600℃で2h保持し脱脂を行い、温度1700℃で1h保持することで仮焼を行う。仮焼を行った後、温度1470℃に加熱し30min保持し、成形体中に溶融したシリコンを含浸させることにより反応焼結体を製造した。
(実施例6)
平均粒径が0.6μmの炭化珪素粉末25重量部、平均粒径が65μmの炭化珪素粉末25重量部と平均粒径が50μmの炭化硼素粉末50重量部、平均粒径が55nmのカーボンブラック粉末20重量部を炭化珪素粉末、炭化硼素粉末、カーボンブラック粉末に対して0.1~1重量部の分散剤を添加した純水中に入れ分散させ、アンモニア水等でpHを8~9.5に調整して500cp未満の低粘度のスラリーを作製した。このスラリーをポットミル等で数時間混合した後バインダーを炭化珪素粉末、炭化硼素粉末、カーボン粉末に対して1~2重量部添加し混合、その後脱泡し石膏板の上に内径80mmのアクリルパイプを置きスラリーを鋳込み、厚み10mm程度の成形体を作製した。成形体は自然乾燥、100~150℃の乾燥の後、1×10-4~1×10-3torrの減圧下において温度600℃で2h保持し脱脂を行い、温度1700℃で1h保持することで仮焼を行う。仮焼を行った後、温度1470℃に加熱し30min保持し、成形体中に溶融したシリコンを含浸させることにより反応焼結体を製造した。
(実施例7)
平均粒径が0.6μmの炭化珪素粉末50重量部と平均粒径が50μmの炭化硼素粉末50重量部を炭化珪素、炭化硼素粉末に対して0.1~1重量部の分散剤を添加した純水中に入れ分散させ、アンモニア水等でpHを8~9.5に調整して500cp未満の低粘度のスラリーを作製した。このスラリーをポットミル等で数時間混合した後バインダーを炭化珪素粉末、炭化硼素粉末、カーボン粉末に対して1~2重量部添加し混合、その後脱泡し石膏板の上に内径80mmのアクリルパイプを置きスラリーを鋳込み、厚み10mm程度の成形体を作製した。成形体は自然乾燥、100~150℃の乾燥の後、1×10-4~1×10-3torrの減圧下において温度600℃で2h保持し脱脂を行い、温度1700℃で1h保持することで仮焼を行う。仮焼を行った後、温度1470℃に加熱し30min保持し、成形体中に溶融したシリコンを含浸させることにより反応焼結体を製造した。
(実施例8)
平均粒径が0.6μmの炭化珪素粉末80重量部と平均粒径が50μmの炭化硼素粉末20重量部と平均粒径が55nmのカーボンブラック粉末10重量部を炭化珪素粉末、炭化硼素粉末、カーボンブラック粉末に対して0.1~1重量部の分散剤を添加した純水中に入れ分散させ、アンモニア水等でpHを8~9.5に調整して500cp未満の低粘度のスラリーを作製した。このスラリーをポットミル等で数時間混合した後バインダーを炭化珪素粉末、炭化硼素粉末、カーボン粉末に対して1~2重量部添加し混合、その後脱泡し石膏板の上に内径80mmのアクリルパイプを置きスラリーを鋳込み、厚み10mm程度の成形体を作製した。成形体は自然乾燥、100~150℃の乾燥の後、1×10-4~1×10-3torrの減圧下において温度600℃で2h保持し脱脂を行い、温度1700℃で1h保持することで仮焼を行う。仮焼を行った後、温度1470℃に加熱し30min保持し、成形体中に溶融したシリコンを含浸させることにより反応焼結体を製造した。
(比較例1)
平均粒径が0.6μmの炭化珪素粉末30重量部と平均粒径が50μmの炭化硼素粉末70重量部を炭化珪素粉末、炭化硼素粉末に対して0.1~1重量部の分散剤を添加した純水中に入れ分散させ、アンモニア水等でpHを8~9.5に調整して500cp未満の低粘度のスラリーを作製した。このスラリーをポットミル等で数時間混合した後バインダーを炭化珪素粉末、炭化硼素粉末に対して1~2重量部添加し混合、その後脱泡し石膏板の上に内径80mmのアクリルパイプを置きスラリーを鋳込み、厚み10mm程度の成形体を作製した。成形体は自然乾燥、100~150℃の乾燥の後、1×10-4~1×10-3torrの減圧下において温度600℃で2h保持し脱脂を行い、温度1700℃で1h保持することで仮焼を行う。仮焼を行った後、温度1470℃に加熱し30min保持し、成形体中に溶融したシリコンを含浸させることにより反応焼結体を製造した。
(比較例2)
平均粒径が0.6μmの炭化珪素粉末50重量部と平均粒径が50μmの炭化硼素粉末50重量部、平均粒径55nmのカーボン粉末50重量部を炭化珪素粉末、炭化硼素粉末、カーボンブラック粉末に対して0.1~1重量部の分散剤を添加した純水中に入れ分散させ、アンモニア水等でpHを8~9.5に調整して500cp未満の低粘度のスラリーを作製した。このスラリーをポットミル等で数時間混合した後バインダーを炭化珪素粉末、炭化硼素粉末、カーボン粉末に対して1~2重量部添加し混合、その後脱泡し石膏板の上に内径80nmのアクリルパイプを置きスラリーを鋳込み、厚み10mm程度の成形体を作製した。成形体は自然乾燥、100~150℃の乾燥の後、1×10-4~1×10-3torrの減圧下において温度600℃で2h保持し脱脂を行い、温度1700℃で1h保持することで仮焼を行う。仮焼を行った後、温度1470℃に加熱し30min保持し、成形体中に溶融したシリコンを含浸させることにより反応焼結体を製造した。
(比較例3)
平均粒径が0.6μmの炭化珪素粉末80重量部と平均粒径が4μmの炭化硼素粉末20重量部、平均粒径が55nmのカーボン粉末50重量部を炭化珪素粉末、炭化硼素粉末、カーボンブラック粉末に対して0.1~1重量部の分散剤を添加した純水中に入れ分散させ、アンモニア水等でpHを8~9.5に調整して500cp未満の低粘度のスラリーを作製した。このスラリーをポットミル等で数時間混合した後バインダーを炭化珪素粉末、炭化硼素粉末、カーボン粉末に対して1~2重量部添加し混合、その後脱泡し石膏板の上に内径80mmのアクリルパイプを置きスラリーを鋳込み、厚み10mm程度の成形体を作製した。成形体は自然乾燥、100~150℃の乾燥の後、1×10-4~1×10-3torrの減圧下において温度600℃で2h保持し脱脂を行い、温度1700℃で1h保持することで仮焼を行う。仮焼を行った後、温度1470℃に加熱し30min保持し、成形体中に溶融したシリコンを含浸させることにより反応焼結体を製造した。
Claims (13)
- 炭化硼素X体積部、炭化珪素Y体積部、シリコンZ体積部を主成分とし、10<X<60、20<Y<70、5<Z<30であり、炭化硼素と炭化珪素の10μm以上の粒子が10~50体積部であることを特徴とする複合材料。
- 前記複合材料の比剛性率が130GPa以上であることを特徴とする、請求項1に記載の複合材料。
- 炭化硼素、炭化珪素、炭素源を主成分とする原料を用いて成形体を成形する成形工程と、
前記成形体に溶融シリコンを含浸させることにより炭素を炭化珪素に転換させる反応焼結工程と、
を備え、
炭化硼素X体積部、炭化珪素Y体積部、シリコンZ体積部を主成分とし、10<X<60、20<Y<70、5<Z<30であり、炭化硼素と炭化珪素の10μm以上の粒子が10~50体積部である複合材料が形成されること、を特徴とする複合材料の製造方法。 - 炭化硼素、炭化珪素、炭素源を主成分とする原料を用いて成形した成形体に、溶融シリコンを含浸させることにより炭素を炭化珪素に転換させる反応焼結工程を備え、
炭化硼素X体積部、炭化珪素Y体積部、シリコンZ体積部を主成分とし、10<X<60、20<Y<70、5<Z<30であり、炭化硼素と炭化珪素の10μm以上の粒子が10~50体積部である複合材料が形成されること、を特徴とする複合材料の製造方法。 - 前記複合材料の比剛性率が130GPa以上であることを特徴とする、請求項3または4に記載の複合材料の製造方法。
- 前記炭素源がカーボン粉末を主成分とするものであること、を特徴とする請求項3乃至5のいずれか1つに記載の複合材料の製造方法。
- 前記炭素源の主成分としてさらに樹脂成分を含むことを特徴とする請求項6に記載の複合材料の製造方法。
- 前記成形工程と前記反応焼結工程の間に前記成形体を仮焼する工程を含むことを特徴とする請求項3乃至7のいずれか1つに記載の複合材料の製造方法。
- 前記成形工程の成形方法が水を溶媒とする鋳込成形であることを特徴とする請求項3乃至8のいずれか1つに記載の複合材料の製造方法。
- 前記成形工程における成形体の充填率が60~80%であることを特徴とする請求項3乃至9のいずれか1つに記載の複合材料の製造方法。
- 炭化硼素・炭化珪素・炭素源を主成分とする原料を用いて充填率が60~80%の成形体を成形する成形工程と、
前記成形体に熔融シリコンを含浸させることにより炭素を炭化珪素に転換させる反応焼結工程と、
を備え、
炭化硼素・炭化珪素・シリコンを主成分とする複合材料が形成されること、を特徴とする複合材料の製造方法。 - 炭化硼素・炭化珪素・炭素源を主成分とする原料を用いて充填率を60~80%として成形された成形体に熔融シリコンを含浸させることにより炭素を炭化珪素に転換させる反応焼結工程を備え、炭化硼素・炭化珪素・シリコンを主成分とする複合材料が形成されること、を特徴とする複合材料の製造方法。
- 前記複合材料の比剛性率が130GPa以上であることを特徴とする請求項11または12に記載の複合材料の製造方法。
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CN109415268A (zh) | 2016-05-05 | 2019-03-01 | 圣戈本陶瓷及塑料股份有限公司 | 多相陶瓷复合材料 |
JP6645586B2 (ja) | 2016-09-06 | 2020-02-14 | 株式会社Ihi | セラミックス基複合材の製造方法 |
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- 2009-04-02 CN CN2009801101986A patent/CN101977875B/zh not_active Expired - Fee Related
- 2009-04-02 WO PCT/JP2009/056884 patent/WO2009123282A1/ja active Application Filing
- 2009-04-02 KR KR1020107023758A patent/KR101190561B1/ko active IP Right Grant
- 2009-04-03 US US12/384,481 patent/US7833921B2/en not_active Expired - Fee Related
- 2009-04-03 TW TW098111217A patent/TW201004894A/zh not_active IP Right Cessation
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Also Published As
Publication number | Publication date |
---|---|
TW201004894A (en) | 2010-02-01 |
US20090295048A1 (en) | 2009-12-03 |
CN101977875A (zh) | 2011-02-16 |
EP2289860A1 (en) | 2011-03-02 |
KR101190561B1 (ko) | 2012-10-16 |
KR20100129327A (ko) | 2010-12-08 |
TWI339646B (ja) | 2011-04-01 |
US7833921B2 (en) | 2010-11-16 |
EP2289860A4 (en) | 2011-11-30 |
CN101977875B (zh) | 2013-07-31 |
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