Patent Application
20200215510
The present invention relates to core-shell particles.
Core-shell particles in which a core part and a shell part are formed of different materials have been used as microcapsules containing specific substances in the core part, and use as multilayer structured particles having functionality imparted to the surface is advanced, and its application field covers a wide range of fields such as pharmaceuticals, cosmetics, foods, electronic materials, adhesives, etc.
As a method for producing the core-shell particle, it is known a method of producing core-shell particles in which a particle serving as a core part is covered with a polymer serving as a shell part by polymerization reaction of a monomer to be a shell part in the presence of particles to be a core part.
Further, in recent years, a method in which by using a glass or metal substrate having a microchannel (micro flow path) with a width and a depth of several μm to several hundred μm (hereinafter may be referred to as a microchip), monodisperse core-shell particles are produced, is also investigated (refer to, for example, Patent Document 1 and Patent Document 2).
Patent Document 1: International Publication WO 2002/068104
Patent Document 2: Japanese Patent Laid-open Publication No. 2004-197083
Problems to be Solved by the Invention
It is a main object of the present invention to provide a novel core-shell particle having excellent flexibility and a conductive particle using the same.
The present inventors made earnest investigations in order to solve the above problems. As a result, it was found that by adopting a specific constitution, it is possible to obtain a novel core-shell particle having excellent flexibility.
Furthermore, it was also found that a conductive particle can be obtained by covering the surface of the core-shell particle with a conductive metal film.
That is, the present invention provides the following core-shell particles and conductive particles.
According to the present invention, it is possible to provide a novel core-shell particle having excellent flexibility. Furthermore, according to the present invention, it is possible to provide a novel conductive particle utilizing the core-shell particle.
A core-shell particle of the present invention is a core-shell particle including a core part and a shell part covering a surface of the core part. The core part is formed of an elastic body. The shell part is formed of a cured product of a composition containing a curing agent and polyimide.
Since the core-shell particle of the present invention includes a core part formed of an elastic body and a shell part formed of a cured product of a composition containing a curing agent and polyimide, the core-shell particle can exert the elasticity by virtue of the core part, and the excellent heat resistance, solvent resistance, insulating properties, mechanical properties, and the like which the polyimide of the shell part has. In addition, since the shell part of the core-shell particle of the present invention is formed of a cured product of a composition containing a curing agent and polyimide, cracks are hardly produced even when stress is applied, and excellent flexibility is exerted. Accordingly, the core-shell particle of the present invention can be suitably used as, for example, an insulating spacer of an electronic device. As described later, it is also possible to form flexible conductive particles by further covering the surface of the core-shell particle with a conductive metal film. Hereinafter, the core-shell particle of the present invention will be described in detail with reference to
As shown in
The core part 11 is formed of an elastic body. A material constituting the elastic body of the core part 11 is not particularly limited; however, a polymer is preferably used. The polymer is not particularly limited; however, silicone (for example, silicone rubber such as solid silicone rubber, liquid silicone rubber, etc.) is preferably used from the viewpoint of suitably forming the core part 11 by a production method described later. The silicone is preferably a cured product of a liquid silicone rubber (for example, a thermosetting liquid silicone rubber, a room temperature curable liquid silicone rubber, etc.), and particularly preferably a cured product of a thermosetting liquid silicone rubber. Commercially available products of thermosetting liquid silicone rubber before curing are as described below.
The silicone may be a cured product of a composition containing a curing agent and a silicone. The curing agent is not particularly limited as long as it can cure the core part 11, and commercially available products of a thermosetting curing agent (hardener) and a photocurable curing agent (photocuring agent) can be used. The curing agent used in the core part 11 may be one which reacts with silicone to be cured, or may be a curing agent which reacts singly to be cured, or may be one which reacts with both of a silicone and a curing agent to be cured.
The material constituting the elastic body of the core part 11 may be of one type or a combination of two or more types.
In the case where the core part 11 is formed of a cured product of a composition containing a curing agent and silicone, a ratio of the curing agent is not particularly limited; however, it is preferably about 0.1 to 20 parts by mass, and more preferably about 0.1 to 10 parts by mass with respect to 100 parts by mass of silicone.
The core part 11 may contain commonly used additives (for example, stabilizers such as an antioxidant and an ultraviolet absorber). The content of the above additives is not particularly limited and can be appropriately adjusted.
A diameter of the core part 11 is not particularly limited; however, it is preferably 900 μm or less, and more preferably about 100 to 700 μm from the viewpoint of suitably producing by a microchannel method as described later.
The shell part 12 is formed of a cured product of a composition containing a curing agent and polyimide. The shell part 12 may have a single layer structure or a multilayer (multiple layer) structure. In the core-shell particle 10 of the present invention, the shell part 12 may cover the surface of the core part 11, for example, it may cover the entire surface of the core part 11, or it may partially cover the surface of the core part 11. The shell part 12 preferably covers the substantially entire area (for example, 95% or more, more preferably 99% or more of the surface) of the surface of the core part 11.
The polyimide is not particularly limited, and a solvent-soluble polyimide is used from the viewpoint of producing the core-shell particle 10 by a production method described later. Details of the solvent-soluble polyimide are as described later.
The curing agent is not particularly limited as long as it can cure the shell part 12, and commercially available products of a thermosetting curing agent (hardener) and a photocurable curing agent (photocuring agent), and the like can be used. The curing agent used in the shell part 12 may be one which reacts with polyimide to be cured, or may be a curing agent which reacts singly to be cured, or may be one which reacts with both of a polyimide and a curing agent to be cured. As the curing agent, a thermosetting curing agent is preferably used, and a thermosetting epoxy-based curing agent is more preferably used. As the thermosetting epoxy-based curing agent, one-component type or two-component type commercially available from various manufacturers can be used, but one-component type is more preferred. Examples of commercially available products of the thermosetting epoxy-based curing agents include Scotch Weld series (3M Japan Limited), Denatite series (Nagase ChemteX Corporation), TETRAD series (Mitsubishi Gas Chemical Company, Inc.), and the like. As the curing agent, one type of curing agent may be used alone, or two or more types may be used in combination.
A ratio of the curing agent for forming the shell part 12 is not particularly limited; however, it is preferably about 1 to 20 parts by mass, and more preferably about 5 to 15 parts by mass with respect to 100 parts by mass of polyimide.
The shell part 12 may contain commonly used additives (for example, stabilizers such as an antioxidant and an ultraviolet absorber). The content of the above additives is not particularly limited and can be appropriately adjusted.
A thickness of the shell part 12 is not particularly limited; however, it is preferably 100 μm or less, and more preferably about 1 to 80 μm from the viewpoint of ease of production (in particular, suitably producing by a microchannel method as described later).
A particle diameter of the core-shell particle 10 of the present invention is not particularly limited; however, it is preferably 1000 μm or less, and more preferably about 100 to 800 μm from the viewpoint of ease of production (in particular, suitably producing by a microchannel method as described later).
In the core-shell particle 10 of the present invention, particularly when the core part 11 is formed of silicone and the shell part 12 is formed of a cured product of a composition containing a thermosetting epoxy-based curing agent and polyimide, the silicone of the core part 11 exerts excellent elasticity and the polyimide of the shell part 12 exerts excellent heat resistance, solvent resistance, insulating properties, mechanical properties, and the like. Further, when the shell part 12 of the core-shell particle 10 of the present invention is formed of a cured product of a composition containing a thermosetting epoxy-based curing agent and polyimide, cracks are hardly produced even when stress is applied, and excellent flexibility is exerted. From these characteristics, the core-shell particle 10 having such composition can be particularly suitably used as an insulating spacer or the like of an electronic device. Further, as described later, by covering the surface of such a core-shell particle 10 with a conductive metal film 13, it is possible to suitably obtain a conductive particles 20 having excellent flexibility.
The conductive particle of the present invention includes a core part, a shell part covering a surface of the core part, and a conductive metal film covering a surface of the shell part, wherein the core part is formed of an elastic body, and the shell part is formed of a cured product of a composition containing a curing agent and polyimide. Hereinafter, the conductive particle of the present invention will be described in detail with reference to
As shown in
In the conductive particle 20 of the present invention, the core part 11 and the shell part 12 are the same as those described in the above paragraph “1. Core-Shell Particle”. The conductive particle 20 of the present invention is one in which a conductive metal film 13 is formed on the surface of the above-mentioned core-shell particle 10 (for example, the core-shell particle 10 produced by a production method described later). In the conductive particle 20 of the present invention, the conductive metal film 13 may cover the surface of the core-shell particle 10, for example, the conductive metal film 13 may cover the entire surface of the core-shell particle 10, or it may partially cover the surface of the core-shell particle 10. The conductive metal film 13 preferably covers the substantially entire area (for example, 95% or more, more preferably 99% or more of the surface) of the surface of the core-shell particle 10.
The metal constituting the conductive metal film 13 is not particularly limited, and examples thereof include aluminum, copper, nickel, gold, titanium, chromium, silver, palladium, platinum, alloys containing at least one kind of these metals, and the like from the viewpoint of exerting excellent conductivity.
A thickness of the conductive metal film 13 is not particularly limited; however, it is preferably 200 μm or less, and more preferably about 1 to 150 μm from the viewpoint of exerting excellent conductivity as fine particles.
A particle diameter of the conductive particle 20 of the present invention is not particularly limited; however, it is preferably 1200 μm or less, and more preferably about 100 to 1000 μm from the viewpoint of exerting excellent conductivity as fine particles.
In the conductive particle 20 of the present invention, a particle in which the core part 11 is formed of silicone and the shell part 12 is formed of a cured product of a composition containing a thermosetting epoxy-based curing agent and polyimide, can have the excellent elasticity of the core part 11 and the excellent properties (properties that cracks are hardly produced even when stress is applied and excellent flexibility is exerted) derived from the cured product of a composition containing a thermosetting epoxy-based curing agent and polyimide included in the shell part 12.
The conductive particles 20 of the present invention can be suitably used in electronic components and the like. More specifically, it can be suitably used as a connector or the like arranged between conductive members (for example, between electrodes) on a substrate of an electronic component.
The method for producing the core-shell particle 10 of the present invention is not particularly limited, and publicly known or commonly used methods for producing core-shell particles can be applied. Examples of the method for producing the core-shell particle 10 of the present invention include a method in which particles corresponding to the core part 11 are prepared, and then the shell part 12 is formed on the surface of each of the particles. The above-mentioned particles can be produced by a publicly known or commonly used method such as a polymerization method capable of forming particles, for example, a suspension polymerization method or an emulsion polymerization method, or a method of producing a droplet disclosed in Patent Document 1. Examples of the method of forming the shell part 12 on the surface of the particle include a method of applying a composition containing a curing agent and polyimide onto the above-mentioned particles and curing the composition, and the like.
As a method for producing the core-shell particles 10 of the present invention, a method including at least the following steps 1 and 2 is particularly preferred from the viewpoint of efficiently producing core-shell particles. This method may be hereinafter simply referred to as “production method of the present invention” in some cases.
Step 1: A first oily medium flowing through a first microchannel and a second oily medium flowing through a second microchannel are joined together at a first confluence point of the first microchannel and the second microchannel.
Step 2: Subsequently to the step 1, the first oily medium and the second oily medium flowing through the third microchannel continuing from the first confluence point to the downstream side are discharged into an aqueous medium to form core-shell particles in which the first oily medium constitutes a core part and the second oily medium constitutes a shell part.
In the production method of the present invention, the first oily medium contains the above-mentioned elastic body or a raw material thereof, and the second oily medium contains a polyimide or a monomer for forming a polyimide, and a curing agent.
Further, in the production method of the present invention, in addition to including the steps 1 and 2, a first oily medium, a second oily medium, and an aqueous medium are used in which each of the values of the interfacial tension γ1 between the first oily medium and the second oily medium, the interfacial tension γ2 between the first oily medium and the aqueous medium, and the interfacial tension γ3 between the second oily medium and the aqueous medium satisfy the following formulas (1) to (3):
0>γ1−(γ2+γ3) (1)
0<γ2−(γ1+γ3)<155 (2)
0>γ3−(γ1+γ2) (3)
In the three-component system in which the first oily medium, the second oily medium, and the aqueous medium are present, the formula (1) means that the first oily medium and the second oily medium have predetermined wettability. Similarly, the formula (3) means that the second oily medium and the aqueous medium have predetermined wettability. Further, the formula (2) means that the first oily medium and the aqueous medium are hardly to wet and spread.
In general, when a two-phase liquid medium composed of the first oily medium and the second oily medium is discharged into an aqueous medium, the droplet shape is changed so that the surface free energy of the first oily medium and the second oily medium is minimized For formation of droplets of a two-phase liquid medium, for example, a case where the first oily medium and the second oily medium separately form droplets, a case of forming a droplet in which hemispherical droplets of the first oily medium and the second oily medium are linked with each other, and a case of forming a droplet having a core-shell structure in which one of the first oily medium and the second oily medium constitutes a core part and the other forms a shell part, are possible.
In the production method of the present invention, it is possible to efficiently produce high-quality core-shell particles by including the steps 1 and 2 and by using materials which satisfy the specific relationships of the formulas (1) to (3) as the first oily medium, the second oily medium, and the aqueous medium. More specifically, when a two-phase liquid medium including the first oily medium and the second oily medium is discharged into the aqueous medium to form spherical particles, the surface free energy significantly increases at the interface portion between the first oily medium and the aqueous medium which hardly wet and spread mutually and the interface becomes unstable. At this time, the second oily medium having predetermined wettability with the first oily medium and the aqueous medium becomes spherical so as to cover the first oily medium, and thereby the surface free energy at the time when the two-phase liquid medium forms a spherical shape decreases and stable particles are produced. That is, core-shell particles in which the first oily medium has a core part and the second oily medium has a shell part are produced.
Hereinafter, the production method of the present invention will be described in detail with reference to the schematic views of
In the production method of the present invention, a so-called microchannel method is used, in which a raw material is supplied into a microchannel (micro flow path) formed in a microchip to produce a target product. For example, in the method for producing core-shell particles using the microchannel method, an oily medium as a raw material of a core part of a core-shell particle and an oily medium as a raw material of a shell part are supplied to a microchannel, and these oily media are discharged into the aqueous medium so that droplets of these oily media are formed in the aqueous medium. At this time, core-shell particles are generated by utilizing the fact that the droplets of the oily media produced in the aqueous medium become spherical particles in which the surface free energy of the droplets is minimized by their own surface tension.
In the production method of the present invention, for example, as shown in
In the production method of the present invention, in the step 1, the first oily medium 7 and the second oily medium 8 joined at the first confluence point P flows through the third microchannel 3 in a state of two-phase flow. Next, in the step 2, the first oily medium 7 and the second oily medium 8 flowing through the third microchannel 3 are discharged into the aqueous medium 9. At this time, in the production method of the present invention, the values of the interfacial tension γ1 between the first oily medium 7 and the second oily medium 8, the interfacial tension γ2 between the first oily medium 7 and the aqueous medium 9, and the interfacial tension γ3 between the second oily medium 8 and the aqueous medium 9 have the specific relationships of the above formulas (1) to (3), respectively, and thereby the core-shell particles 10 in which the first oily medium 7 constitutes the core part, and the second oily medium 8 constitutes the shell part are suitably formed in the aqueous medium 9, and therefore it is possible to efficiently produce high-quality core-shell particles 10.
In the production method of the present invention, from the viewpoint of efficiently producing high-quality core-shell particles 10, it is preferred that γ1 to γ3 satisfy the relationships of the above formulas (1) and (3), and in addition to this, the relationships of the following formulas (1a) and (3a) are further satisfied.
0>γ1−(γ2+γ3)>−160 (1a)
0>γ3−(γ1+γ2)>−160 (3a)
In the production method of the present invention, the composition of the first oily medium 7 (including an elastic body or the raw material thereof) and the second oily medium 8 (including polyimide or the monomer forming the polyimide) is not particularly limited as long as it can satisfy the specific relationship of formulas (1) to (3).
As described above, a polymer is preferred as the elastic body for forming the core part 11 of the core-shell particle 10. When the first oily medium 7 contains a polymer, the polymer is not particularly limited; however, silicone (for example, silicone rubber such as solid silicone rubber or liquid silicone rubber etc.) is preferably used from the viewpoint of suitably forming the core part 11 by satisfying the specific relationships of the above formulas (1) to (3). The silicone may be contained as a monomer or oligomer which polymerizes to form a polymer. As the silicone, liquid silicone rubber (for example, thermosetting liquid silicone rubber, room temperature curable liquid silicone rubber, etc.) is preferred, and thermosetting liquid silicone rubber is particularly preferred. By using the thermosetting liquid silicone rubber, a liquid state satisfying the specific relationships of the above formulas (1) to (3) can be suitably kept until core-shell particles are formed in the aqueous medium 9, and then, by heating the core-shell particle, the core part can be suitably cured.
Examples of commercially available products of thermosetting liquid silicone rubber include ELASTOSIL LR series (Wacker Asahikasei Silicone Co., Ltd.), SEMICOSIL series (Wacker Asahikasei Silicone Co., Ltd.), one-component type RTV series (Shin-Etsu Chemical Co., Ltd.), TSE Series (Momentive Performance Materials Japan LLC), and the like.
Each of the polymer or monomer contained in the first oily medium 7 may be of one type or a combination of two or more types. The content of the polymer or monomer contained in the first oily medium 7 is not particularly limited; however, it is preferably about 35 to 95% by mass, and more preferably about 45 to 70% by mass from the viewpoint of efficiently producing high-quality core-shell particles.
In addition, the second oily medium 8 contains polyimide or a monomer (monomer which forms polyimide). That is, in the second oily medium 8, the polyimide may be contained as a monomer which forms polyimide by polymerization.
In the second oily medium 8, the polyimide is not particularly limited, but it is preferred to use a solvent-soluble polyimide. The solvent-soluble polyimide is a polyimide which is soluble in an organic solvent, and preferably one that is soluble in an organic solvent in an amount of 1% by mass or more. As the organic solvent, a common organic solvent can be used, and examples thereof include pentane, normal hexane, cyclohexane, cyclohexanone, benzene, toluene, xylene, chloroform, methyl ethyl ketone, N-methyl-2-pyrrolidone, mixtures of two or more thereof, and the like. By using the solvent-soluble polyimide, a liquid state satisfying the specific relationships of the formulas (1) to (3) can be suitably kept until core-shell particles are formed in the aqueous medium 9.
Examples of commercially available products of the solvent-soluble polyimide include solvent-soluble polyimide solutions (solutions dissolved in an organic solvent) such as SPIXAREA series (SOMAR Corporation), PIAD series (Arakawa Chemical Industries, Ltd.), Solpit 6, 6-PI (Solpit Co., Ltd.), and Q- VR/AD series (PI R&D CO., LTD.).
Each of the polyimide or monomer contained in the second oily medium 8 may be of one type or a combination of two or more types. The content of the polyimide or monomer contained in the second oily medium 8 is not particularly limited; however, it is preferably about 5 to 30% by mass, and more preferably about 5 to 20% by mass from the viewpoint of efficiently producing high-quality core-shell particles.
As described above, the second oily medium contains a curing agent as an essential component. On the other hand, the first oily medium may further contain a curing agent. By containing the curing agent, a liquid state satisfying the specific relationships of the formulas (1) to (3) can be suitably kept until core-shell particles 10 are formed in the aqueous medium 9, and then, by heating the core-shell particles, the core part or the shell part can be suitably cured. In addition, when the second oily medium contains a curing agent, core-shell particles having excellent flexibility can be obtained.
The type of the curing agent is not particularly limited as long as it can cure the core part or the shell part, and a commercially available products of a thermosetting curing agent (hardener) and a photocurable curing agent (photocuring agent), and the like can be used. For example, as a curing agent of the second oily medium containing polyimide or the monomer thereof, a thermosetting curing agent is preferably used, and a thermosetting epoxy-based curing agent is more preferably used. As the thermosetting epoxy-based curing agent, one-component type or two-component type commercially available from various manufacturers can be used, but one-component type is more preferred. Examples of commercially available products of the thermosetting epoxy-based curing agents include Scotch Weld series (3M Japan Limited), Denatite series (Nagase ChemteX Corporation), TETRAD series (Mitsubishi Gas Chemical Company, Inc.), and the like. As the curing agent, one type of curing agent may be used alone, or two or more types may be used in combination.
When the first oily medium 7 contains a curing agent, the content thereof is not particularly limited; however, it is preferably about 0.1 to 20 parts by mass, and more preferably about 0.1 to 10 parts by mass with respect to 100 parts by mass of the polymer or monomer contained in the first oily medium 7 from the viewpoint of efficiently producing high-quality core-shell particles. Further, the content of the curing agent in the second oily medium 8 is not particularly limited; however, it is preferably about 1 to 20 parts by mass, and more preferably about 5 to 15 parts by mass with respect to 100 parts by mass of the polyimide or monomer contained in the second oily medium 8 from the same viewpoint.
In addition, each of the first oily medium 7 and the second oily medium 8 may contain an oily solvent. When using the oily solvent, the interfacial tensions γ1 to γ3 can be adjusted depending on the type and mixing ratio of the oily solvent, and therefore it is possible to easily satisfy the specific relationships of the above formulas (1) to (3). Further, by using the oily solvent together with, for example, the above-described polymer or polyimide (including monomers for forming polyimide), a liquid state satisfying the specific relationships of the formulas (1) to (3) can be suitably kept until the core-shell particles are formed in the aqueous medium 9, and then, by removing the oily solvent from the core-shell particles, solid core-shell particles can be suitably produced.
As the oily solvent, a common organic solvent can be used, and examples thereof include pentane, normal hexane, cyclohexane, cyclohexanone, benzene, toluene, xylene, chloroform, methyl ethyl ketone, N-methyl-2-pyrrolidone, and the like. As the oily solvent, one type of oily solvent may be used alone, or two or more types may be used in combination.
The content of the oily solvent contained in the first oily medium 7 is not particularly limited; however, it is preferably about 0 to 65% by mass, and more preferably about 5 to 50% by mass from the viewpoint of efficiently producing high-quality core-shell particles. The content of the oily solvent contained in the second oily medium 8 is not particularly limited; however, it is preferably about 70 to 90% by mass, and more preferably about 80 to 90% by mass from the same viewpoint.
Each of the first oily medium 7 and the second oily medium 8 may contain other commonly used additives (for example, stabilizers such as an antioxidant and an ultraviolet absorber). The content of the above additives is not particularly limited and can be appropriately adjusted.
In the production method of the present invention, it is particularly preferred that the first oily medium 7 contains silicone and the second oily medium 8 contains polyimide and a curing agent. From this, it is possible to efficiently produce high-quality core-shell particles in which the core part 11 is formed of silicone, and the shell part 20 is formed of a cured product of a composition containing a curing agent and polyimide. Furthermore, in the production method of the present invention, it is preferred to adjust the interfacial tension between the first oily medium 7 and the second oily medium 8 so as to satisfy the specific relationships of the above formulas (1) to (3) by using the above-mentioned oil solvent for the first oily medium 7 and the second oily medium 8.
The aqueous medium 9 is not particularly limited as long as it can satisfy the specific relationships of the above formulas (1) to (3), and examples thereof include aqueous solutions containing water-soluble components such as polyvinyl alcohol, polyethylene glycol, and polyalkylene oxide.
The water-soluble component is not particularly limited, and those commercially available from various manufacturers can be used. Examples of commercially available products of polyvinyl alcohol include GOHSENOL series (Nippon Synthetic Chemical Industry Co., Ltd.), POVAL series (KURARAY CO., LTD.), POVAL series (JAPAN VAM & POVAL CO., LTD.), DENKA POVAL series (Denka Co., Ltd.), and the like. As the water-soluble component, one type of water-soluble component may be used alone, or two or more types may be used in combination.
In the aqueous medium 9, the content of the water-soluble component contained in the aqueous solution is not particularly limited; however, it is preferably about 0.1 to 10% by mass, and more preferably 1 to about 5% by mass from the viewpoint of efficiently producing high-quality core-shell particles.
From the viewpoint of efficiently producing high-quality core-shell particles in the production method of the present invention, as particularly preferred composition of the first oily medium 7, the second oily medium 8, and the aqueous medium 9, the composition can be mentioned in which the first oily medium 7 is formed of a mixture of silicone and an oily solvent, the second oily medium 8 is formed of a mixture of polyimide, a thermosetting epoxy-based curing agent, and an oily solvent, and the aqueous medium is an aqueous solution containing polyvinyl alcohol.
As described above, in the present invention, in the core-shell particle 10 having the core part 11 formed of silicone and the shell part 12 formed of a cured product of a composition containing a thermosetting epoxy-based curing agent and polyimide, the silicone of the core part 11 exerts excellent elasticity and the polyimide of the shell part 12 exerts excellent heat resistance, solvent resistance, insulating properties, mechanical properties, and the like. In addition, since the shell part 12 is formed of a cured product of a composition containing a curing agent and polyimide, the core-shell particles 10 hardly produce cracking even when a stress is applied, and exerts excellent flexibility.
The interfacial tension γ1 between the first oily medium 7 and the second oily medium 8 is not particularly limited as long as it satisfies the above formulas (1) to (3); however, the interfacial tension γ1 is preferably more than 0 mN/m and 10 mN/m or less, and more preferably more than 0 mN/m and 5 mN/m or less from the viewpoint of efficiently producing high-quality core-shell particles. Further, the interfacial tension γ2 between the first oily medium 7 and the aqueous medium 9 is not particularly limited as long as it satisfies the above formulas (1) to (3); however, the interfacial tension γ2 is preferably more than 0 mN/m and 180 mN/m or less, and more preferably about 5 to 160 mN/m from the viewpoint of efficiently producing high-quality core-shell particles. The interfacial tension γ3 between the second oily medium 8 and the aqueous medium 9 is not particularly limited as long as it satisfies the above formulas (1) to (3); however, the interfacial tension γ3 is preferably more than 0 mN/m and 10 mN/m or less, and more preferably more than 0 mN/m and 5 mN/m or less from the viewpoint of efficiently producing high-quality core-shell particles.
In the production method of the present invention, from the viewpoint of efficiently producing high-quality core-shell particles, it is preferred that the interfacial tension γ1 between the first oily medium 7 and the second oily medium 8, and the interfacial tension γ3 between the second oily medium 8 and the aqueous medium 9 further satisfy the relationship of the following formula (4). From this, in the process of forming the core-shell particles, the second oily medium 8 becomes spherical so as to cover the first oily medium 7, and thereby the surface free energy at the time when the two-phase liquid medium forms a spherical shape is more lowered and stable particles are generated.
γ3>γ1 (4)
In the production method of the present invention, the method of supplying the first oily medium 7 and the second oily medium 8 to the first microchannel 1 and the second microchannel 2, respectively, is not particularly limited, and a method to be used in a publicly known microchannel method can be adopted. As a method used in a publicly known microchannel method, for example, a method using a liquid supply device such as a syringe, a syringe pump, or the like capable of adjusting the flow rate can be mentioned. As a syringe and a syringe pump, commercially available products can be used. Examples of the commercially available products of syringes include Terumo syringes manufactured by Terumo Corporation and gas tight syringes manufactured by Hamilton Company. Examples of the commercially available products of syringe pumps include Legato 100 manufactured by Muromachi Kikai Co., Ltd. and KDS-100 manufactured by KD scientific Inc. The syringe is connected to the microchip using a commercially available tube. As the tube, a tube made of PTFE or the like can be suitably used.
The flow rate of the first oily medium 7 in the first microchannel 1 is not particularly limited; however, it is preferably about 0.1 to 50 ml/hr, more preferably about 0.5 to 30 ml/hr, and still more preferably about 2.5 to 5 ml/hr from the viewpoint of efficiently producing high-quality core-shell particles. The flow rate of the second oily medium 8 in the second microchannel 2 is not particularly limited; however, it is preferably about 0.1 to 50 ml/hr, more preferably about 0.5 to 30 ml/hr, and still more preferably about 2.5 to 5 ml/hr from the same viewpoint.
In addition, in the production method of the present invention, from the viewpoint of efficiently producing high-quality core-shell particles, as shown in
In the production method of the present invention, it is preferred that at the second confluence point Q, the aqueous medium 9 flowing through the fourth microchannel 4 and the aqueous medium 9 flowing through the fifth microchannel 5 are joined together in such a way that the direction in which the aqueous medium 9 flowing through the fourth microchannel 4 flows and the direction in which the aqueous medium 9 flowing through the fifth microchannel 5 flows form an angle of 180° or less.
For example, as shown in
Further, for example, as shown in
As shown in
As a method of supplying the aqueous medium 9 to the fourth and fifth microchannels 4 and 5, as with the first and second oily media 7 and 8, the method used in the above-mentioned publicly known microchannel method can be adopted.
The flow rate of the aqueous medium 9 flowing through the fourth and fifth microchannels 4 and 5 is not particularly limited; however, it is preferably about 30 to 200 ml/hr, and more preferably about 50 to 150 ml/hr from the viewpoint of efficiently producing high-quality core-shell particles. The flow rate of the aqueous medium 9 flowing through the fourth microchannel 4 and the flow rate of the aqueous medium 9 flowing through the fifth microchannel 5 may be different from each other, but these flow rates are preferably comparable with each other (for example, flow rate difference is about −2 to 2 ml/hr) from the viewpoint of efficiently producing high-quality core-shell particles.
In the production method of the present invention, the first microchannel 1, the second microchannel 2, the third microchannel 3 which is a merging channel of these microchannels, the fourth microchannel 4, the fifth microchannel 5, and the sixth microchannel 6 are each a micro flow path formed in a substrate or the like.
In the production method of the present invention, the diameter (direction perpendicular to the longitudinal direction) of the first microchannel 1 is not particularly limited; however, it is preferably about 100 to 900 μm, and more preferably about 300 to 700 μm from the viewpoint of efficiently producing high-quality core-shell particles. The diameter (direction perpendicular to the longitudinal direction) of the second microchannel 2 is not particularly limited; however, it is preferably about 100 to 900 μm, and more preferably about 300 to 700 μm from the same viewpoint. The diameter (direction perpendicular to the length direction) of the third microchannel 3 is not particularly limited; however, it is preferably about 100 to 900 μm, and more preferably about 300 to 700 μm from the same viewpoint.
The diameters (direction perpendicular to the longitudinal direction) of the fourth and fifth microchannels 4 and 5 for supplying the aqueous medium 9 are not particularly limited; however, the diameters are preferably about 300 to 2000 μm, and more preferably about 500 to 1500 μm from the viewpoint of efficiently producing high-quality core-shell particles.
Further, the diameter (direction perpendicular to the longitudinal direction) of the sixth microchannel 6 for forming the core-shell particles is not particularly limited; however, it is preferably about 300 to 2000 μm, and more preferably about 500 to 1500 μm from the viewpoint of efficiently producing high-quality core-shell particles.
The particle diameter of the core-shell particle produced by the production method of the present invention can be adjusted by the diameter (direction perpendicular to the length direction) of the microchannel, and for example, when the diameters of the first, second, and third microchannels are about 300 μm, core-shell particles having a particle diameter of about 150 to 250 μm are obtained, and when the diameters are about 500 μm, core-shell particles having a particle diameter of about 350 to 450 μm are obtained, and when the diameters are about 700 μm, core-shell particles having a particle diameter of about 500 to 650 μm are obtained.
The length (flow direction) of the first microchannel 1 is not particularly limited; however, it is preferably about 0.1 to 8 mm, and more preferably about 1 to 6 mm from the viewpoint of efficiently producing high-quality core-shell particles. The length (flow direction) of the second microchannel 2 is not particularly limited; however, it is preferably about 0.1 to 8 mm, and more preferably about 1 to 6 mm from the same viewpoint. The length (flow direction) of the third microchannel 3 is not particularly limited; however, it is preferably about 0.1 to 8 mm, and more preferably about 1 to 6 mm from the same viewpoint.
The lengths (flow direction) of the fourth and fifth microchannels 4 and 5 for supplying the aqueous medium 9 are not particularly limited; however, it is preferably about 0.1 to 8 mm, and more preferably about 1 to 6 mm from the viewpoint of efficiently producing high-quality core-shell particles.
The length (flow direction) of the sixth microchannel 6 for forming core-shell particles is not particularly limited; however, it is preferably about 1 to 15 mm, and more preferably about 5 to 10 mm from the viewpoint of efficiently producing high-quality core-shell particles.
In the production method of the present invention, a step 3 of curing the core-shell particles 10 formed in the aqueous medium 9 in the above-mentioned step 2 can be performed. For example, when the first oily medium 7 and the second oily medium 8 contain a thermosetting or photocurable component, the core-shell particles 10 can be cured by heating or photoirradiation.
In the step 3, a step 3-1 of curing the core-shell particles 10 in the aqueous medium 9 may be provided.
In the step 3-1, a heating temperature in the case of thermally curing the core-shell particles in the aqueous medium 9 is not particularly limited as long as it is a temperature equal to or lower than a boiling point of the aqueous medium 9 and at which the core part and the shell part can be cured, and it is preferably about 60 to 98° C. A heating time in the case of thermally curing the core-shell particles in the aqueous medium 9 is not particularly limited; however, it is preferably about 0.1 to 5 hours.
In the step 3-1, the core-shell particles 10 preliminarily cured in the aqueous medium 9 at the heating temperature as described above may be cured (full cured) by further heating at a high temperature. The heating temperature in a full curing is not particularly limited; however, it is preferably about 100 to 200° C. The heating time in the full curing is not particularly limited; however, it is preferably about 0.5 to 8 hours. The full curing in the aqueous medium 9 can be carried out using, for example, a pressure-resistant container or the like.
Further, in the step 3, a step 3-2 of curing the core-shell particles 10 after separating the core-shell particles 10 from the aqueous medium 9 may be provided.
In the step 3-2, a heating temperature in the case of thermally curing the core-shell particles 10 separated from the aqueous medium 9 is not particular limitation as long as it is a temperature at which the oily solvent in the core part and the shell part can be evaporated, and the core part and the shell part can be cured, and the heating temperature is preferably about 100 to 200° C.
Furthermore, the step 3 may include a step of curing the core-shell particles 10 in the aqueous medium 9, and a step 3-2 of further curing (full curing) the core-shell particles 10 after separating the core-shell particles 10 cured (preliminarily cured) in the step 3-1 from the aqueous medium 9.
When the step 3 includes the step 3-1 and the step 3-2, it is preferred that in the step 3-1, heating is performed at a temperature higher than a curing temperature of the core part and lower than a boiling point of the oily solvent contained in the second oily medium 8, and subsequently in the step 3-2, the core-shell particles 10 are heated at a high temperature higher than a curing temperature of the shell part and higher than a boiling point of the oily solvent contained in the first oily medium 7 and the second oily medium 8. From this, first, the core part is cured while maintaining the shell part in a liquid state by the preliminary curing in step 3-1 to enable the oily medium contained in the core part to shift to the shell part in the curing of the core part. Next, in the full curing of the step 3-2, the oily solvent contained in the shell part is evaporated together with the curing of the shell part, and solid-state high quality core-shell particles 10 can be produced.
When thermally curing is carried out in two stages of curing (preliminary curing) in the step 3-1 and curing (full curing) in the step 3-2, the heating temperature in the step 3-1 is preferably about 60 to 98° C., and the heating temperature in the step 3-2 is preferably about 100 to 200° C. The heating times in the preliminary curing and full curing are not particularly limited, and each of the heating times described above can be mentioned, for example.
A method of separating the core-shell particles 10 from the aqueous medium 9 is not particularly limited, and examples thereof include publicly known methods such as filtration and drying.
The core-shell particle 10 of the present invention can also be produced using a microchip, for example as shown in
For example, in the microchip shown in
In the microchip shown in
In the microchip shown in
The conductive particle 20 of the present invention can be produced by forming a conductive metal film 13 on the surface of the core-shell particle 10 of the present invention (for example, core-shell particles obtained by the production method of the present invention etc.).
A method of forming the conductive metal film 13 on the surface of the core-shell particle 10 is not particularly limited, and a publicly known metal film formation method such as an electroless plating method, a metal vapor deposition method, a sputtering method, or the like can be adopted.
Hereinafter, the present invention will be described in detail with reference to examples and comparative examples. However, the present invention is not limited to the examples.
In Example 1 and Comparative Example 1, the obtained particles were sandwiched between spindles and compressed by 30% of the diameter of the particle (distorted up to 70% of the distorted) using a micrometer NDC-25PX (manufactured by Mitutoyo Corporation), and then the particle surface was observed with an optical microscope.
In Examples 2 to 7 and Comparative Examples 2 to 3, the interfacial tension γ1 between the first oily medium and the second oily medium, the interfacial tension γ2 between the first oily medium and the aqueous medium, and the interfacial tension γ3 between the second oily medium and the aqueous medium were measured using an automatic contact angle meter DMs-401 manufactured by Kyowa Interface Science Co., Ltd. From these measured values, values of γ1−(γ2+γ3), γ2−(γ1+γ3), and γ3−(γ1+γ2) were calculated. These results are shown in Table 1.
In Examples 2 to 7 and Comparative Examples 2 to 3, the state in which a two-phase flow of the first oily medium and the second oily medium flowing through the third microchannel was discharged into the aqueous medium at the second confluence point Q was observed using the high speed camera FASTCAM MAX 120K manufactured by Photron Limited and the appearance of particle formation was checked. As a result, the case where particles having uniform particle diameters were formed was rated as “○”, the case where minute particles or precipitates like lints were formed together with the particles were rated as “Δ”, and the case where no particles were not formed and bulk precipitates were formed was rated as “x”. The results are shown in Table 1.
In Examples 2 to 7 and Comparative Examples 2 to 3, cross sections of the obtained particles were observed with an electron microscope, and the presence or absence of a core-shell structure was confirmed. The case where the core-shell structure was confirmed was rated as “○”, and the case where the core-shell structure was not confirmed was rated as “x”. The results are shown in Table 1.
The same thermosetting liquid silicone rubber was used as both a first oily medium and a second oily medium. As an aqueous medium, an aqueous solution prepared by dissolving 2.0 parts by mass of polyvinyl alcohol (produced by Nippon Synthetic Chemical Industry Co., Ltd., GOHSENOL GL-03) in 98.0 parts by mass of pure water was used.
Using a microchip having a microchannel as shown in
Next, the recovered single particles and aqueous medium 9 were heated at 95° C. for 1 hour under still standing to be cured. Next, after removing the aqueous medium by filtration, the cured single particles were washed three times with pure water. Next, the washed single particles were dried at 130° C. for 1 hour to obtain core particles.
A solvent of a polyimide solution (PIAD 300 produced by Arakawa Chemical Industries, Ltd.) was distilled off by a reduced pressure drier, 70.0 parts by mass of toluene was added to 30.0 parts by mass of the obtained polyimide solid matter, the resulting mixture was stirred at room temperature for 24 hours to dissolve the mixture, and 2.2 parts by mass of a curing agent (TETRAD-X, produced by Mitsubishi Gas Chemical Company, Inc.) was added and stirred for 5 minutes to prepare a polyimide solution.
The core particles obtained above were immersed in the prepared polyimide solution to adhere the polyimide solution evenly to the particle surfaces, and the core particles were recovered in a 100 ml glass beaker containing 50.0 g of the aqueous medium 9.
The core particles having the polyimide solution adhered to the surface and the aqueous medium 9 were heated at 130° C. for 1 hour and then at 180° C. for 3 hours in a pressure vessel after distilling off toluene under a reduced pressure of from atmospheric pressure to −90 kPa. Next, after the aqueous medium was removed by decantation, the obtained particles were washed three times with pure water and dried at 50° C. for 2 hours to obtain cured core-shell particles. Ten obtained core-shell particles were randomly selected and observed with a microscope, and consequently no problem such as cracking occurred in the shell part of any of the core-shell particles.
For the core-shell particles obtained in Example 1, the flexibility was evaluated by the above-described method. As a result, the core-shell particle obtained in Example 1 was excellent in flexibility and does not produce cracks on the particle surface.
As the first oily medium, a medium obtained by adding 33.4 parts by mass of toluene to 66.6 parts by mass of a thermosetting liquid silicone rubber was used. A solvent of a polyimide solution (PIAD 300 produced by Arakawa Chemical Industries, Ltd.) was distilled off by a reduced pressure drier, 70.0 parts by mass of toluene was added to 30.0 parts by mass of the obtained polyimide solid matter, the resulting mixture was stirred at room temperature for 24 hours to dissolve the mixture, and 2.2 parts by mass of a curing agent (TETRAD-X, produced by Mitsubishi Gas Chemical Company, Inc.) was added and stirred for 5 minutes to prepare a polyimide solution, and the polyimide solution was used as the second oily medium. As an aqueous medium, an aqueous solution prepared by dissolving 2.0 parts by mass of polyvinyl alcohol (produced by Nippon Synthetic Chemical Industry Co., Ltd., GOHSENOL GL-03) in 98.0 parts by mass of pure water was used.
Using a microchip having a microchannel as shown in
Next, the recovered core-shell particles 10 and the aqueous medium 9 were preliminarily cured by being heated at 95° C. for 1 hour under still standing after distilling off toluene under a reduced pressure of from atmospheric pressure to −90 kPa. Next, after removing the aqueous medium by decantation, the core-shell particles were washed three times with pure water. Next, the washed core-shell particles were cured by being heated at 130° C. for 1 hour and subsequently at 180° C. for 3 hours to obtain cured core-shell particles.
Cured core-shell particles were obtained in the same manner as in Example 2 except that media having composition described in Table 1 were used as the first oily medium, the second oily medium, and the aqueous medium, respectively, and the flow rates of the first oily medium flowing through the first microchannel, the second oily medium flowing through the second microchannel, and the aqueous medium flowing through the fourth and fifth microchannels were set to the values described in Table 1, respectively.
Core-shell particles were obtained in the same manner as in Example 1 except that a curing agent (TETRAD-X, produced by Mitsubishi Gas Chemical Company, Inc.) was not added to the polyimide solution. Ten obtained core-shell particles were randomly selected and observed with a microscope, and consequently cracks were produced in the shell part for 6 out of 10 core-shell particles. For the core-shell particles (without cracks in the shell part) obtained in Comparative Example 1, the flexibility was evaluated by the method described above. As a result, the core-shell particles obtained in Comparative Example 1 had low flexibility and produced cracks on the surface of the particles.
Particles were formed in the same manner as in Examples 2 to 7 except that media having composition described in Table 1 were used as the first oily medium, the second oily medium, and the aqueous medium, respectively, and the flow rates of the first oily medium flowing through the first microchannel, the second oily medium flowing through the second microchannel, and the aqueous medium flowing through the fourth and fifth microchannels were set to the values described in Table 1, respectively. In Comparative Examples 2 and 3, no particles were formed at the second confluence point Q, and lumpy (string-like) precipitates were formed. That is, core-shell particles could not be produced.
The core-shell particles obtained in Example 1 did not cause failure such as cracking even when stress was applied, and were excellent in flexibility. On the other hand, the core-shell particles obtained in Comparative Example 1 were inferior in flexibility.
As is apparent from the results shown in Table 1, in Examples 2 to 7 using the microchip on which the microchannels are formed as shown in
1: First microchannel
1
a: Supply port of a first oily medium
2: Second microchannel
2
a: Supply port of a second oily medium
3: Third microchannel
4: Fourth microchannel
4
a: Supply port of an aqueous medium
5: Fifth microchannel
5
a: Supply port of an aqueous medium
6: Sixth microchannel
7: First oily medium
8: Second oily medium
9: Aqueous medium
10: Core-Shell Particle
11: Core part
12: Shell part
20: Conductive Particle
P: First confluence point
Q: Second confluence point
| Number | Date | Country | Kind |
|---|---|---|---|
| 2015-209175 | Oct 2015 | JP | national |
| Number | Date | Country | |
|---|---|---|---|
| Parent | 15770165 | Apr 2018 | US |
| Child | 16824521 | US |
