阅读说明：本技术 复合粒子及复合粒子的制造方法 (Composite particle and method for producing composite particle ) 是由 中村圭太郎 佐藤大助 于 2019-03-11 设计创作，主要内容包括：本发明提供一种耐氧化性优异的复合粒子及复合粒子的制造方法。复合粒子为TiN,与Al、Cr及Nb中的至少一种复合而成的复合粒子。复合粒子的制造方法是将钛的粉末,与Al、Cr及Nb中至少一种的粉末作为原料粉末,使用气相法制造复合粒子。(The invention provides a composite particle having excellent oxidation resistance and a method for producing the composite particle. The composite particles are composite particles formed by compounding TiN and at least one of Al, Cr and Nb. The composite particles are produced by a vapor phase method using a powder of titanium and at least one of Al, Cr and Nb as raw material powders.)

1. A composite particle is characterized by being composed of TiN and at least one of Al, Cr and Nb.

2. The composite particle according to claim 1, wherein the content of Al is 0.1 to 20% by mass when the TiN is compounded with the Al.

3. The composite particle according to claim 1, wherein the content of Cr is 0.1 to 20% by mass when the TiN is composited with the Cr.

4. The composite particle according to claim 1, wherein the content of Nb is 0.1 to 20 mass% when the TiN is compounded with the Nb.

5. A method for producing composite particles, which is characterized by comprising compounding TiN with at least one of Al, Cr and Nb, wherein the method comprises using a powder of titanium and at least one of Al, Cr and Nb as raw material powders and producing the composite particles by a vapor phase method.

6. The method for producing composite particles according to claim 5, wherein the gas phase method is a thermal plasma method, a flame method, an arc plasma method, a microwave heating method, or a pulse line method.

7. The method for producing composite particles according to claim 6, wherein the thermal plasma method includes a step of supplying a carrier gas in which the raw material powder is dispersed into a thermal plasma flame, and a step of supplying a cooling gas to an end portion of the thermal plasma flame to produce composite particles.

8. The method for producing composite particles according to claim 7, wherein the thermal plasma flame is at least one gas selected from argon gas and nitrogen gas.

Technical Field

The present invention relates to composite particles of titanium nitride and a method for producing the composite particles, and particularly relates to composite particles having excellent oxidation resistance and a method for producing the composite particles.

Background

Various fine particles are currently used for various purposes. For example, fine particles such as metal fine particles, oxide fine particles, nitride fine particles, and carbide fine particles are used for electrical insulating materials for various electrical insulating parts, functional materials for cutting tools, machine tools, sensors, and the like, sintered materials, electrode materials for fuel cells, and catalysts.

Patent document 1 describes black composite fine particles having high light-shielding properties suitable as a black component such as a black matrix of a color filter. The black composite fine particles are composed of titanium nitride particles and metal fine particles, and have a composition formula: TiN (titanium nitride) _xO_yzX. In the composition formula, Ti represents a titanium atom, N represents a nitrogen atom, O represents an oxygen atom, and X represents a metal atom. x represents a number larger than 0 but smaller than 2, y represents a number not smaller than 0 but smaller than 2, and z represents a number larger than 0 but smaller than 10.

Disclosure of Invention

Technical problem to be solved by the invention

Conventionally, as described in patent document 1, black composite fine particles composed of titanium nitride particles and metal fine particles have been proposed. However, there is a demand for further expansion of applications and addition of other functions, for example, oxidation resistance.

The purpose of the present invention is to provide composite particles having excellent oxidation resistance and a method for producing the composite particles.

Means for solving the problems

In order to achieve the above object, the present invention provides composite particles comprising TiN and at least one of Al, Cr and Nb.

When TiN is compounded with Al, the content of Al is preferably 0.1 to 20 mass%.

When TiN and Cr are combined, the content of Cr is preferably 0.1 to 20% by mass.

In the case of compounding TiN and Nb, the Nb content is preferably 0.1 to 20 mass%.

The present invention provides a method for producing composite particles, which comprises compounding TiN with at least one of Al, Cr and Nb, wherein the method comprises using a powder of titanium and at least one of Al, Cr and Nb as raw material powders and producing the composite particles by a vapor phase method.

Preferably, the gas phase process is a thermal plasma process, a flame process, an arc plasma process, a microwave heating process or a pulsed wire process.

Preferably, the thermal plasma method has: a step of supplying a carrier gas in which the raw material powder is dispersed into the thermal plasma flame, and a step of supplying a cooling gas to an end portion of the thermal plasma flame to produce composite particles.

Preferably the thermal plasma flame is from at least one of argon and nitrogen.

ADVANTAGEOUS EFFECTS OF INVENTION

According to the present invention, composite particles having excellent oxidation resistance can be obtained.

Drawings

Fig. 1 is a schematic diagram showing an example of a fine particle production apparatus used in the method for producing composite particles according to the embodiment of the present invention.

Fig. 2(a) is a graph showing the results of analysis of the crystal structure of titanium nitride by the X-ray diffraction method, and (b) is a graph showing the results of analysis of the crystal structure of composite particles of titanium nitride and aluminum by the X-ray diffraction method.

Fig. 3 is a graph showing the absorbance of the composite particles and the titanium nitride particles.

Reference numerals

10 fine particle manufacturing apparatus 12 plasma torch 14 material supply apparatus 15 primary fine particle 16 chamber

18 fine particles (secondary fine particles) 19 cyclone 20 recovery part 22 plasma gas supply source

24 thermal plasma flame 28 gas supply 30 vacuum pump

Detailed Description

Hereinafter, the composite particles and the method for producing the composite particles according to the present invention will be described in detail based on preferred embodiments shown in the drawings.

Fig. 1 is a schematic diagram showing an example of a fine particle production apparatus used in the method for producing composite particles according to the embodiment of the present invention.

A fine particle production apparatus 10 shown in fig. 1 (hereinafter, simply referred to as a production apparatus 10) is used for producing composite particles.

The composite particles are particles of TiN compounded with at least one of Al, Cr and Nb.

The composite particles are not nitride particles in which individual particles such as TiN, AIN, CrN, NbN, etc. are mixed, but are nitride particles in which TiN and at least one of Al, Cr, and Nb are contained in a single particle. The form of Al, Cr, and Nb in the composite particles is not particularly limited, and may be a metal single body, or may be a compound form such as a nitride, an oxide, an oxynitride, an oxide with an indefinite ratio, and a nitride with an indefinite ratio.

The composite particles may be called nanoparticles, and the particle diameter may be 1 to 100 nm. The particle diameter is an average particle diameter measured by the BET method. The composite particles are produced, for example, by a production method described later, and are not in a state of being dispersed in a solvent or the like, but are obtained in a particle state.

The manufacturing apparatus 10 includes: a plasma torch 12 that generates thermal plasma, a material supply device 14 that supplies raw material powder of composite particles into the plasma torch 12, a chamber 16 that functions as a cooling tank for generating primary fine particles 15 of the composite particles, a cyclone 19 that removes coarse particles having a particle diameter of an arbitrary predetermined particle diameter or more from the primary fine particles 15 of the composite particles, and a recovery section 20 that recovers secondary fine particles 18 of the composite particles having a desired particle diameter classified by the cyclone 19.

For the material supply device 14, the chamber 16, the cyclone 19, and the recovery unit 20, various devices such as those disclosed in japanese patent application laid-open No. 2007-138287 can be used. Further, primary fine particles 15 of the composite particles may be referred to as only primary fine particles 15.

In the present embodiment, for example, a powder of titanium powder and at least one of Al, Cr, and Nb is used as the raw material powder for producing the composite particles.

The average particle diameter of the raw material powder is appropriately set so that the raw material powder is easily evaporated in the thermal plasma flame, and the average particle diameter is, for example, 100 μm or less, preferably 10 μm or less, and more preferably 5 μm or less.

The plasma torch 12 is composed of a quartz tube 12a and a high-frequency oscillation coil 12b wound around the outside thereof. A later-described supply pipe 14a for supplying the raw material powder of the composite particles into the plasma torch 12 is provided at the center portion of the upper portion of the plasma torch 12. The plasma gas supply port 12c is formed in a peripheral portion (on the same circumference) of the supply pipe 14a, and the plasma gas supply port 12c is annular.

The plasma gas supply source 22 supplies plasma gas into the plasma torch 12, and has, for example, a gas supply portion 22 a. The gas supply portion 22a is connected to the plasma gas supply port 12c via a pipe 22 c. Although not shown, the gas supply portion 22a is provided with a supply amount adjustment portion such as a valve for adjusting the supply amount. The plasma gas is supplied from the plasma gas supply source 22 into the plasma torch 12 through the annular plasma gas supply port 12c from the direction indicated by the arrow P and the direction indicated by the arrow S.

The plasma gas is, for example, a mixed gas of argon and nitrogen. The thermal plasma flame is derived from at least one of argon and nitrogen.

At least one gas of argon and nitrogen is stored in the gas supply portion 22 a. At least one of argon gas and nitrogen gas is supplied from a gas supply portion 22a of the plasma gas supply source 22 into the plasma torch 12 from the direction indicated by the arrow P and the direction indicated by the arrow S through the plasma gas supply port 12c via a pipe 22 c. Further, only at least one of argon gas and nitrogen gas may be supplied in the direction indicated by the arrow P.

When a high-frequency voltage is applied to the high-frequency oscillation coil 12b, a thermal plasma flame 24 is generated in the plasma torch 12.

The temperature of the thermal plasma flame 24 must be higher than the boiling point of the raw material powder. On the other hand, the higher the temperature of the thermal plasma flame 24, the easier the raw material powder is brought into a gaseous state, which is preferable, but the temperature is not particularly limited. For example, the temperature of the thermal plasma flame 24 may be 6000 ℃, and theoretically may reach approximately 10000 ℃.

The pressure environment in the plasma torch 12 is preferably equal to or lower than atmospheric pressure. Here, the atmosphere of the atmospheric pressure or lower is not particularly limited, and is, for example, 0.5 to 100 kPa.

The plasma gas is, for example, at least one of argon and nitrogen, and may be, but not limited to, a combination of at least one of argon and nitrogen and helium, or a combination of at least one of argon and nitrogen and hydrogen.

The outside of the quartz tube 12a is surrounded by a concentric tube (not shown), and cooling water is circulated between the tube and the quartz tube 12a to cool the quartz tube 12a, thereby preventing the quartz tube 12a from becoming excessively high in temperature due to the thermal plasma flame 24 generated in the plasma torch 12.

The material supply device 14 is connected to the upper portion of the plasma torch 12 via a supply pipe 14 a. The material supplying device 14 supplies the raw material powder in the form of powder, for example, into the thermal plasma flame 24 in the plasma torch 12.

As the material supply device 14 for supplying the raw material powder, for example, a device disclosed in Japanese patent laid-open No. 2007-138287 is used. In this case, the material supplying device 14 includes, for example, a storage tank (not shown) for storing the raw material powder, a screw feeder (not shown) for quantitatively conveying the raw material powder, a dispersing unit (not shown) for dispersing the raw material powder conveyed by the screw feeder into a primary particle state before final dispersion, and a carrier gas supply source (not shown).

The raw material powder is supplied into the thermal plasma flame 24 inside the plasma torch 12 through the supply tube 14a together with the carrier gas that has been extruded from the carrier gas supply source and has been added with pressure.

The material supplying device 14 is not particularly limited as long as it can prevent the raw material powder from agglomerating and disperse the raw material powder in the plasma torch 12 while maintaining the dispersed state. The carrier gas is an inert gas such as argon. The carrier gas flow rate can be controlled using a flow meter such as a float flow meter. The flow rate value of the carrier gas is a scale value of the flowmeter.

The chamber 16 is disposed continuously below the plasma torch 12 and is connected to a gas supply device 28. Primary fine particles 15 of composite particles are generated in the chamber 16. The chamber 16 functions as a cooling tank.

The gas supply device 28 supplies cooling gas into the chamber 16. The gas supply device 28 includes a gas supply source 28a and a pipe 28b, and a pressure applying means (not shown) such as a compressor and a blower for applying an extrusion pressure to the cooling gas supplied into the chamber 16. Further, a pressure control valve 28c for controlling the amount of gas supplied from the gas supply source 28a is provided. For example, at least one of argon and nitrogen is stored in the gas supply source 28 a. The cooling gas is at least one of argon and nitrogen.

As described above, at least one of argon and nitrogen is used as the plasma gas.

Further, it is necessary to include nitrogen gas in either the plasma gas or the cooling gas, and it is more preferable that nitrogen gas be included in the plasma gas.

The gas supply device 28 supplies at least one of argon and nitrogen as a cooling gas to the end of the thermal plasma flame 24 on the side opposite to the plasma gas supply port 12c, that is, to the end of the thermal plasma flame 24, for example, in the direction of the arrow Q at an angle of 45 °, and supplies the above-described cooling gas from the upper side to the lower side along the inner wall 16a of the chamber 16, that is, in the direction of the arrow R shown in fig. 1.

The raw material powder converted into a gaseous phase by the thermal plasma flame 24 is rapidly cooled by the cooling gas supplied from the gas supply device 28 into the chamber 16, thereby obtaining primary fine particles 15 of composite particles. In addition, the above-described cooling gas has an additional function of imparting classification or the like of the primary fine particles 15 in the cyclone 19.

The primary fine particles 15 of the composite particles may cause a reduction in quality if the particles immediately after generation collide with each other to form aggregates and the particle diameters are not uniform. However, the cooling gas supplied in the direction of the arrow Q toward the tail (end) of the thermal plasma flame dilutes the primary particles 15, and prevents aggregation of the particles due to collision.

In addition, in the process of collecting primary fine particles 15 in the direction of arrow R, the cooling gas prevents the primary fine particles 15 from adhering to the inner side wall 16a of the chamber 16, and the yield of the generated primary fine particles 15 is improved.

As shown in fig. 1, the chamber 16 is provided with a cyclone 19 for classifying the primary fine particles 15 of the composite particles into a desired particle size. This cyclone 19 includes: an inlet pipe 19a for supplying the primary fine particles 15 from the chamber 16, a cylindrical outer cylinder 19b connected to the inlet pipe 19a and positioned above the cyclone 19, a conical table portion 19c connected from a lower portion of the outer cylinder 19b toward a lower side and having a gradually decreasing diameter, a coarse particle collecting chamber 19d connected to a lower side of the conical table portion 19c and collecting coarse particles having a particle diameter equal to or larger than the desired particle diameter, and an inner pipe 19e connected to a collecting portion 20 described later and protruding from the outer cylinder 19 b.

The airflow containing the primary fine particles 15 is blown from the inlet pipe 19a of the cyclone 19 along the inner peripheral wall of the outer cylinder 19b, and the airflow flows downward from the inner peripheral wall of the outer cylinder 19b toward the frustum 19c as shown by an arrow T in fig. 1, thereby forming a vortex flow.

When the descending swirling flow is inverted and becomes an ascending flow, the coarse particles are not lifted by the balance between the centrifugal force and the resisting force, and descend along the side surface of the frustum portion 19c, and are collected in the coarse particle collection chamber 19 d. Further, fine particles that are more affected by resistance than the centrifugal force are discharged from the inner tube 19e to the outside of the system together with the ascending flow on the inner wall of the frustum portion 19 c.

In addition, a negative pressure (suction force) is generated from the recovery portion 20 described later by the inner tube 19 e. Then, the composite particles separated from the swirling airflow are sucked as indicated by the symbol U by the negative pressure (suction force), and sent to the recovery unit 20 through the inner tube 19 e.

A recovery part 20 for recovering secondary fine particles (composite particles) 18 having a desired nanometer-order particle diameter is provided at an extension of the inner tube 19e, which is an outlet of the airflow in the cyclone 19. The recovery unit 20 includes: a recovery chamber 20a, a filter 20b provided in the recovery chamber 20a, and a vacuum pump 30 connected via a pipe provided at the lower portion in the recovery chamber 20 a. The fine particles discharged from the cyclone 19 are sucked by the vacuum pump 30, introduced into the recovery chamber 20a, and collected while being retained on the surface of the filter 20 b.

In the above-described manufacturing apparatus 10, the number of cyclones used is not limited to 1, and may be 2 or more.

Next, an example of a method for producing composite particles using the production apparatus 10 will be described.

First, as the raw material powder of the composite particles, at least one of a powder of titanium and a powder of Al, a powder of Cr, and a powder of Nb can be used. The powder used as the raw material powder has an average particle diameter of, for example, 5 μm or less. The raw material powder is fed into the material supply device 14.

When a powder of titanium and a powder of Al are used as the raw material powder, composite particles of titanium nitride and aluminum can be obtained.

When titanium powder and Cr powder are used as the raw material powder, composite particles of titanium nitride and chromium can be obtained.

When a powder of titanium and a powder of Nb are used as the raw material powder, composite particles of titanium nitride and niobium can be obtained.

The plasma gas is at least one gas of argon gas and nitrogen gas, for example, and a high-frequency voltage is applied to the high-frequency oscillation coil 12b to generate a thermal plasma flame 24 in the plasma torch 12.

Further, at least one gas of, for example, argon gas and nitrogen gas is supplied as the cooling gas from the gas supply device 28 toward the tail of the thermal plasma flame 24, that is, toward the end of the thermal plasma flame 24 in the direction of the arrow Q. At this time, at least one of argon and nitrogen is also supplied as the cooling gas in the direction of the arrow R.

Next, the raw material powder is gas-transported using, for example, argon gas as a carrier gas, and is supplied to the thermal plasma flame 24 in the plasma torch 12 through the supply pipe 14 a. The supplied raw material powder is vaporized in the thermal plasma flame 24 to be in a gas phase, is nitrided by reacting with nitrogen, and is rapidly cooled by the cooling gas, thereby obtaining primary fine particles 15 of composite particles of titanium nitride.

Then, the primary fine particles 15 of the composite particles obtained in the chamber 16 are blown from the inlet pipe 19a of the cyclone 19 along the inner peripheral wall of the outer cylinder 19b together with the air flow, whereby the air flow forms a swirling flow by flowing along the inner peripheral wall of the outer cylinder 19b as shown by an arrow T in fig. 1 and descends. When the descending vortex flow is inverted and becomes an ascending flow, the coarse particles are not lifted by the balance between the centrifugal force and the resisting force, and descend along the side surface of the frustum portion 19c, and are collected in the coarse particle collection chamber 19 d. Further, fine particles influenced more by the resistance than the centrifugal force are discharged from the inner wall to the outside of the system together with the ascending flow of the inner wall of the frustum portion 19 c.

The discharged secondary fine particles (composite particles) 18 are sucked in the direction indicated by the symbol U in fig. 1 by the negative pressure (suction force) from the recovery unit 20 generated by the vacuum pump 30, sent to the recovery unit 20 through the inner tube 19e, and recovered by the filter 20b of the recovery unit 20. The internal pressure in the cyclone 19 at this time is preferably equal to or lower than atmospheric pressure. The particle diameter of the secondary fine particles (composite particles) 18 is determined to be any particle diameter of the order of nanometers according to the purpose.

Thus, composite particles can be easily and reliably obtained only by applying plasma treatment to a raw material powder using at least one of a titanium powder and an Al powder, a Cr powder, and an Nb powder.

The composite particles produced by the method for producing composite particles according to the present embodiment have a narrow particle size distribution width, that is, a uniform particle diameter, and are hardly contaminated with coarse particles having a particle size of 1 μm or more.

Further, although the primary fine particles of the composite particles are formed using the thermal plasma flame, the primary fine particles of the composite particles may be formed using a gas phase method. Therefore, the gas phase method is not limited to the thermal plasma method using a thermal plasma flame, and a method for producing primary fine particles of composite particles by using a flame method, an arc plasma method, a microwave heating method, or a pulse line method may be used.

Here, the flame method refers to a method of synthesizing composite particles by passing a raw material powder in a gas phase or a liquid phase through a flame using the flame as a heat source. The flame method is a method in which raw material powder is supplied to a flame in a gas phase or a liquid phase, and then a cooling gas is supplied to the flame to lower the temperature of the flame, thereby obtaining primary fine particles 15 of composite particles.

The raw material powder in a gas phase state means, for example, a state in which the raw material powder is dispersed in the carrier gas. The raw material powder in a liquid phase state means a state in which the raw material powder is dispersed in a solvent.

The same gas as that used in the thermal plasma method can be used as the cooling gas.

The following description will be made of the composite particles.

As described above, the composite particles of the present invention are referred to as nanoparticles having a particle diameter of 1 to 100 nm. The particle diameter is an average particle diameter measured by the BET method.

As described above, the composite particles of the present invention are not dispersed in a solvent or the like, but exist as individual composite particles. Therefore, the combination with a solvent is not particularly limited, and the solvent can be selected with a high degree of freedom.

As described above, the composite particles are particles in which TiN is composited with at least one of Al, Cr, and Nb. When TiN is compounded with Al, the content of Al is preferably 0.1 to 20 mass%. When the content of Al is within the above range, the oxidation resistance is excellent.

In addition, when TiN and Cr are combined, the content of Cr is preferably 0.1 to 20% by mass. When Cr is within the above range, the oxidation resistance is excellent.

In the case of compounding TiN and Nb, the Nb content is preferably 0.1 to 20 mass%. When Nb is within the above range, the oxidation resistance is excellent.

The content (% by mass) of each element can be determined by XRF (fluorescent X-ray analysis), but the content (% by mass) of each element is obtained by omitting impurities.

Specifically, the content of Al is calculated by omitting the contents (mass%) of Ti and elements other than Al from the contents (mass%) of the respective elements obtained by XRF (fluorescent X-ray analysis) and calculating the total mass% of Ti and Al to be 100.

Fig. 2(a) is a graph showing the results of crystal structure analysis of titanium nitride by X-ray diffraction, and (b) is a graph showing the results of crystal structure analysis of composite particles of titanium nitride and aluminum by X-ray diffraction. FIGS. 2(a) and (b) each show the results of crystal structure analysis after sintering at 400 ℃ for 10 minutes in the air. In addition, the arrows in fig. 2(a) show diffraction peaks of titanium oxide.

When comparing fig. 2(a) and fig. 2(b), the diffraction patterns of TiN and the composite of titanium nitride and aluminum are the same and only the intensity is different when the diffraction peak of titanium oxide (indicated by an arrow in fig. 2 (a)) is removed.

The titanium nitride/aluminum composite has substantially no diffraction peak intensity of titanium oxide, i.e., has excellent oxidation resistance, as compared with TiN, after sintering at 400 ℃ for 10 minutes in the air.

Regarding the hue, TiN after firing at 400 ℃ for 10 minutes in the air turns white as a whole powder due to the formation of titanium oxide, but the composite of titanium nitride and aluminum does not change. From this, it is found that a composite of titanium nitride and aluminum can increase the oxidation initiation temperature as compared with TiN, and is effective in oxidation resistance.

The absorbance of the titanium nitride composite particles was measured. Fig. 3 is a graph showing the absorbance of the composite particles and the titanium nitride particles.

As shown in fig. 3, the composite particles of titanium nitride have an absorbance in the measured wavelength region of the same degree as that of TiN.

Therefore, the composite particles of titanium nitride are excellent in oxidation resistance and have a small change in color tone. And has an absorbance of the same degree as that of TiN.

The absorbance is a value obtained from the transmittance measured by an ultraviolet-visible spectrophotometer after composite particles of titanium nitride are dispersed in water by ultrasonic waves.

In fig. 3, "standard" of TiN was prepared under standard conditions, and had a stoichiometric composition of TiN. "LowO₂"is made in a more reducing environment and contains little oxygen. And, the color is biased to blue "highO₂"is made in several oxidizing environments, several containing oxygen. And, the color is biased toward red.

The composite particles can be used for, for example, a black matrix of a liquid crystal display device, an organic EL display device, or the like. The composite particles can be used as a light-shielding material. In this case, the light-shielding material can be used as a light-shielding material for a color filter and a light-shielding material for an external light side of a TFT.

It is also useful for printing ink, inkjet ink, mask making material, printing proof material, etching resist, and solder resist.

In addition to the above, the composite particles can be used for, for example, a catalyst carrier, and in this case, since the particle diameter can be reduced, the catalyst performance can be improved.

In addition, the method can be used for a photoelectric conversion element and a photothermal conversion element.

In addition, pigments and the like for adjusting color tone by mixing with metals, oxides, plastics and the like are also used.

The present invention can also be applied to an electrical insulating material such as a semiconductor substrate, a printed circuit board, and various electrical insulating parts, a high-hardness and high-precision machine tool material such as a cutting tool, a semiconductor chip, and a bearing, a functional material such as a grain boundary capacitor and a humidity sensor, a sintered body such as a precision sintered molding material, a sintered part such as a material requiring high-temperature wear resistance such as an engine valve, and an electrode, an electrolyte material, and various catalysts of a fuel cell.

In this embodiment, since the particle size of the nitride fine particles can be made to be nanometer size, for example, when used in a sintered body, the sinterability can be improved, and a sintered body with high strength can be obtained. Thus, for example, a tool having good machinability can be obtained.

The present invention is basically constituted as described above. Although the composite particles and the method for producing the composite particles of the present invention have been described in detail above, the present invention is not limited to the above-described embodiments, and various improvements and modifications may be made without departing from the scope of the present invention.