WO2023106307A1 - 中空粒子、樹脂組成物、及び樹脂成形体 - Google Patents

中空粒子、樹脂組成物、及び樹脂成形体 Download PDF

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Publication number
WO2023106307A1
WO2023106307A1 PCT/JP2022/045009 JP2022045009W WO2023106307A1 WO 2023106307 A1 WO2023106307 A1 WO 2023106307A1 JP 2022045009 W JP2022045009 W JP 2022045009W WO 2023106307 A1 WO2023106307 A1 WO 2023106307A1
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Prior art keywords
hollow particles
mass
particles
present disclosure
hollow
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English (en)
French (fr)
Japanese (ja)
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光稀 森村
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Zeon Corp
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Zeon Corp
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Priority to KR1020247018179A priority Critical patent/KR20240116734A/ko
Priority to EP22904235.3A priority patent/EP4446002A4/en
Priority to JP2023566325A priority patent/JPWO2023106307A1/ja
Priority to CN202280079952.XA priority patent/CN118338958A/zh
Priority to US18/715,855 priority patent/US20250025850A1/en
Publication of WO2023106307A1 publication Critical patent/WO2023106307A1/ja
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J13/00—Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
    • B01J13/02—Making microcapsules or microballoons
    • B01J13/06—Making microcapsules or microballoons by phase separation
    • B01J13/14—Polymerisation; cross-linking
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J13/00—Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
    • B01J13/02—Making microcapsules or microballoons
    • B01J13/06—Making microcapsules or microballoons by phase separation
    • B01J13/14—Polymerisation; cross-linking
    • B01J13/18—In situ polymerisation with all reactants being present in the same phase
    • B01J13/185—In situ polymerisation with all reactants being present in the same phase in an organic phase
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F2/00—Processes of polymerisation
    • C08F2/12—Polymerisation in non-solvents
    • C08F2/16—Aqueous medium
    • C08F2/18—Suspension polymerisation
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F212/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring
    • C08F212/02—Monomers containing only one unsaturated aliphatic radical
    • C08F212/04—Monomers containing only one unsaturated aliphatic radical containing one ring
    • C08F212/06—Hydrocarbons
    • C08F212/12—Monomers containing a branched unsaturated aliphatic radical or a ring substituted by an alkyl radical
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F212/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring
    • C08F212/34—Monomers containing two or more unsaturated aliphatic radicals
    • C08F212/36—Divinylbenzene
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L101/00—Compositions of unspecified macromolecular compounds
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L25/00—Compositions of, homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring; Compositions of derivatives of such polymers
    • C08L25/02—Homopolymers or copolymers of hydrocarbons
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L79/00—Compositions of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen with or without oxygen or carbon only, not provided for in groups C08L61/00 - C08L77/00
    • C08L79/04—Polycondensates having nitrogen-containing heterocyclic rings in the main chain; Polyhydrazides; Polyamide acids or similar polyimide precursors
    • C08L79/08—Polyimides; Polyester-imides; Polyamide-imides; Polyamide acids or similar polyimide precursors
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00—Polymer mixtures characterised by other features
    • C08L2205/14—Polymer mixtures characterised by other features containing polymeric additives characterised by shape
    • C08L2205/18—Spheres
    • C08L2205/20—Hollow spheres

Definitions

  • the present disclosure relates to hollow particles, and resin compositions and resin moldings containing the hollow particles.
  • Hollow particles have cavities inside the particles, so they are used by being added to resins, paints, various moldings, etc. for the purpose of weight reduction, heat insulation, low dielectric constant, etc.
  • Applications include automobiles, bicycles, aviation, electricity, electronics, architecture, home appliances, containers, stationery, tools, and footwear.
  • hollow particles having shells of acrylic resin tend to have relatively high dielectric constants and dielectric loss tangents, there is the problem that the effects of low dielectric constants and low dielectric loss tangents cannot be obtained sufficiently. . Therefore, in order to reduce the dielectric constant and dielectric loss tangent of hollow particles, hollow particles using styrene-based resins are manufactured.
  • Patent Document 1 styrene, divinylbenzene, a (meth)acrylic acid ester monomer having a specific structure, a peroxide polymerization initiator, and side chain crystallinity are added to an aqueous phase that is an aqueous solution of a surfactant.
  • Hollow particles obtained by suspending and polymerizing an oil phase containing polyolefin and heptane are disclosed.
  • Patent Document 2 discloses hollow particles obtained by dispersing an oil phase containing divinylbenzene, a peroxide polymerization initiator, and hexadecane in an aqueous phase, which is an aqueous solution of polyvinyl alcohol, and carrying out suspension polymerization. It is
  • An object of the present disclosure is to provide hollow particles having a low dielectric loss tangent at high frequencies, and to provide a resin composition and a resin molding containing the hollow particles.
  • the present inventors focused on the resin composition of the shell and the amount of unreacted polymerizable functional groups remaining in the shell in hollow particles having a shell formed by polymerization of polymerizable monomers, and found that the skeleton of the shell and By containing a large amount of hydrocarbon monomer units in the polymer and adjusting the method of forming the shell, the residual double bond rate is set to a specific amount or less, and the porosity of the hollow particles is increased. , resulting in hollow particles exhibiting low dissipation factor at high frequencies such as 10 GHz.
  • the present disclosure provides a hollow particle comprising a shell containing a resin and a hollow portion surrounded by the shell,
  • the porosity is 50% or more
  • the shell contains, as the resin, a polymer containing 91% by mass or more of hydrocarbon monomer units and 50% by mass or more of crosslinkable monomer units, and at least part of the hydrocarbon monomer units is It is a crosslinkable hydrocarbon monomer unit, and the residual double bond rate of the polymer is 30.0% or less
  • hollow particles having a dielectric loss tangent of 3.00 ⁇ 10 ⁇ 3 or less at a frequency of 10 GHz.
  • the hollow particles of the present disclosure preferably have a dielectric constant of 1.00 or more and 1.40 or less at a frequency of 10 GHz.
  • the porosity is preferably 65% or more.
  • the hollow particles of the present disclosure preferably have a volume average particle diameter of 1.0 ⁇ m or more and 10.0 ⁇ m or less.
  • the present disclosure provides a resin composition containing the hollow particles of the present disclosure and a matrix resin. Further, the present disclosure provides a resin molding containing the hollow particles of the present disclosure and a matrix resin.
  • the present disclosure as described above provides hollow particles with low dielectric loss tangent at high frequencies. Furthermore, the present disclosure provides a resin composition and a resin molding containing the hollow particles.
  • a polymerizable monomer is a compound having a functional group capable of addition polymerization (in the present disclosure, sometimes simply referred to as a polymerizable functional group).
  • a compound having an ethylenically unsaturated bond as a functional group capable of addition polymerization is generally used as the polymerizable monomer.
  • a polymerizable monomer having only one polymerizable functional group is referred to as a non-crosslinkable monomer
  • a polymerizable monomer having two or more polymerizable functional groups is referred to as a crosslinkable monomer.
  • a crosslinkable monomer is a polymerizable monomer that forms a crosslinked bond in a resin by a polymerization reaction.
  • a hydrocarbon monomer is a polymerizable monomer composed of carbon and hydrogen.
  • the crosslinkable hydrocarbon monomer is a polymerizable monomer having two or more polymerizable functional groups and consisting of carbon and hydrogen
  • the non-crosslinkable hydrocarbon monomer is a polymerizable functional group.
  • good dielectric properties mean low dielectric constant and low dielectric loss tangent, and the lower the dielectric constant and dielectric loss tangent, the better the dielectric properties.
  • the hollow particles of the present disclosure are hollow particles comprising a shell containing a resin and a hollow portion surrounded by the shell, the porosity being 50% or more, the shell being the resin, the hydrocarbon monomer unit A polymer containing 91% by mass or more and a polymer containing 50% by mass or more of a crosslinkable monomer unit, at least a portion of the hydrocarbon monomer unit being a crosslinkable hydrocarbon monomer unit, the weight It is characterized by having a combined residual double bond rate of 30.0% or less and a dielectric loss tangent of 3.00 ⁇ 10 ⁇ 3 or less at a frequency of 10 GHz.
  • the hollow particles of the present disclosure are particles comprising a resin-containing shell (outer shell) and a hollow portion surrounded by the shell.
  • the hollow portion is a hollow space clearly distinguished from the shell of the hollow particles formed by resin material.
  • the shell of the hollow particle may have a porous structure, in which case the hollow portion has a size that can be clearly distinguished from a large number of minute spaces uniformly distributed within the porous structure. have.
  • Hollow particles of the present disclosure preferably have a solid shell from the standpoint of dielectric properties.
  • the hollow portion of the hollow particles can be confirmed, for example, by SEM observation of the cross section of the particles or by TEM observation of the particles as they are.
  • the hollow particles of the present disclosure are preferably filled with a gas such as air in order to exhibit excellent dielectric properties.
  • Hollow particles obtained using a hydrocarbon resin such as a styrene resin have good dielectric properties of the resin itself that constitutes the shell, but it is difficult to make the dielectric loss tangent at high frequencies sufficiently low. there were.
  • the hollow particles of the present disclosure are hollow particles having a low dielectric loss tangent even at high frequencies such as 10 GHz.
  • the polymer serving as the skeleton of the shell contains a large amount of hydrocarbon monomer units and has a low residual double bond rate, so that the molecular motion of the shell is suppressed compared to conventional hollow particles.
  • the hollow particles of the present disclosure are particles having a hollow portion that is clearly distinguished from the shell because the polymer contains 50% by mass or more of the crosslinkable monomer units.
  • the hollow particles of the present disclosure are typically obtained by suspension polymerization, and suspension polymerization using a polymerizable monomer containing 50% by mass or more of a crosslinkable monomer is In the droplets of the monomer composition dispersed therein, the components constituting the shell and the hydrophobic solvent are likely to undergo phase separation, and the formation of a shell with excellent strength suppresses deformation of the particles. Therefore, it is presumed that hollow particles are formed that have hollow portions in the particles that are clearly distinguished from the shell.
  • the hollow particles of the present disclosure have shells with low molecular mobility as described above, and also have hollows that are clearly distinguished from the shells. It is presumed that the dielectric loss tangent is sufficiently low also in The air layer has a dielectric loss tangent of 0, and the larger the ratio of the air layer in the hollow particles, the lower the dielectric loss tangent. Therefore, the higher the porosity of the hollow particles, the lower the dielectric loss tangent.
  • the hollow particles of the present disclosure will be described in detail, and furthermore, the resin composition and the resin molding containing the hollow particles of the present disclosure will also be described.
  • the hollow particles of the present disclosure are produced by, for example, preparing a mixture containing a polymerizable monomer, a hydrophobic solvent, a polymerization initiator, a dispersion stabilizer and an aqueous medium; A suspension in which droplets of a monomer composition containing the polymerizable monomer, the hydrophobic solvent, and the polymerization initiator are dispersed in the aqueous medium by suspending the mixed liquid.
  • a step of preparing By subjecting the suspension to a polymerization reaction, a precursor composition is prepared which includes precursor particles having a hollow portion surrounded by a resin-containing shell and encapsulating the hydrophobic solvent in the hollow portion.
  • the content of the hydrocarbon monomer is 91% by mass or more, and the content of the crosslinkable monomer is 50% by mass or more, at least part of the hydrocarbon monomer is a crosslinkable hydrocarbon monomer,
  • the polymerization initiator contained in the mixed solution is an organic peroxide, In the step of preparing the precursor composition, it can be obtained by the method for producing hollow particles of the present disclosure, wherein the polymerization reaction temperature is higher than the 10-hour half-life temperature of the polymerization initiator.
  • the polymerizable monomer and the hydrophobic solvent are A suspension is prepared in which droplets having phase separation and a distribution structure in which the polymerizable monomer is unevenly distributed on the surface side and the hydrophobic solvent is unevenly distributed in the center are dispersed in an aqueous medium, and the suspension is It follows the basic technique of subjecting a liquid to a polymerization reaction to harden the surface of the droplets to form hollow particles having a hollow space filled with a hydrophobic solvent.
  • the reason why the hollow particles obtained by the production method of the present disclosure have a low dielectric loss tangent at high frequencies is considered as follows.
  • the porosity can be sufficiently increased, whereby the ratio of the air layer in the hollow particle can be sufficiently increased, so that a low dielectric loss tangent can be achieved.
  • the polymerizable monomer used for forming the shell contains a large amount of hydrocarbon monomers, and a shell containing a large amount of hydrocarbons is formed. Therefore, the acrylic resin is used as the main component of the shell.
  • the dielectric loss tangent of the hollow particles is likely to decrease depending on the composition of the shell as the shell is formed, which has lower molecular mobility than the hollow particles.
  • an organic peroxide as a polymerization initiator and setting the polymerization temperature to a temperature higher than the 10-hour half-life temperature of the polymerization initiator, in the shell, unreacted polymerizable unsaturated bonds and polymerization initiation
  • an increase in the dielectric loss tangent of the hollow particles can be suppressed. Since unreacted polymerizable unsaturated bonds and decomposition products of the polymerization initiator increase the molecular motion of the shell, a large amount of these remaining may increase the dielectric loss tangent of the hollow particles.
  • an organic peroxide is used as a polymerization initiator, it is easier to accelerate the polymerization reaction than when other polymerization initiators are used. It is possible to reduce the amount of residual decomposition products of the bond and the polymerization initiator.
  • the method for producing hollow particles of the present disclosure includes a step of preparing a mixed solution, a step of preparing a suspension, and a step of subjecting the suspension to a polymerization reaction, and may further include steps other than these. Moreover, as long as it is technically possible, two or more of the above steps and other additional steps may be performed simultaneously as one step, or their order may be changed. For example, the preparation and suspension of the mixed solution may be performed simultaneously in one step, such as by adding the materials for preparing the mixed solution while simultaneously suspending the mixture.
  • a preferred example of the method for producing hollow particles of the present disclosure includes a production method including the following steps.
  • Suspension step Suspension in which droplets of a monomer composition containing a polymerizable monomer, a hydrophobic solvent and a polymerization initiator are dispersed in an aqueous medium by suspending the mixture.
  • a step of preparing (3) Polymerization step By subjecting the suspension to a polymerization reaction, a precursor composition containing precursor particles having a hollow portion surrounded by a resin-containing shell and containing a hydrophobic solvent in the hollow portion preparing a product, (4) Solid-liquid separation step A step of solid-liquid separation of the precursor composition to obtain precursor particles containing a hydrophobic solvent in their hollow portions, and (5) Solvent removal step Obtained by the solid-liquid separation step a step of removing the hydrophobic solvent contained in the precursor particles to obtain hollow particles;
  • hollow particles whose hollow portions are filled with a hydrophobic solvent are sometimes referred to as "precursor particles", considering them as intermediates of hollow particles whose hollow portions are filled with a gas.
  • precursor composition means a composition comprising precursor particles.
  • FIG. 1 is a schematic diagram showing an example of the manufacturing method of the present disclosure.
  • (1) to (5) in FIG. 1 correspond to the above steps (1) to (5).
  • White arrows between each figure indicate the order of each step.
  • FIG. 1 is only a schematic diagram for explanation, and the manufacturing method of the present disclosure is not limited to the one shown in the diagram. Also, the structures, dimensions and shapes of the materials used in the manufacturing methods of the present disclosure are not limited to the structures, dimensions and shapes of the various materials in these figures.
  • (1) of FIG. 1 is a cross-sectional schematic diagram showing one embodiment of the liquid mixture in the liquid mixture preparation step. As shown in this figure, the mixture contains an aqueous medium 1 and a low-polarity material 2 dispersed in the aqueous medium 1 .
  • the low-polarity material 2 means a material that has low polarity and is difficult to mix with the aqueous medium 1 .
  • Low polarity material 2 in the present disclosure includes a polymerizable monomer, a hydrophobic solvent and a polymerization initiator.
  • (2) of FIG. 1 is a cross-sectional schematic diagram showing one embodiment of the suspension in the suspension step.
  • the suspension comprises an aqueous medium 1 and droplets 8 of a monomer composition dispersed in the aqueous medium 1 .
  • the droplet 8 of the monomer composition contains a polymerizable monomer, a hydrophobic solvent and a polymerization initiator, but the distribution within the droplet is non-uniform.
  • FIG. 1(3) is a schematic cross-sectional view showing one embodiment of a precursor composition obtained by a polymerization step and containing precursor particles containing a hydrophobic solvent in their hollow portions.
  • the precursor composition includes an aqueous medium 1 and precursor particles 9 dispersed in the aqueous medium 1 and containing a hydrophobic solvent 4a in their hollow portions.
  • the shell 6 forming the outer surface of the precursor particle 9 is formed by polymerization of the polymerizable monomer in the droplet 8 of the monomer composition. Coalescence is included as a resin.
  • (4) of FIG. 1 is a schematic cross-sectional view showing one embodiment of the precursor particles after the solid-liquid separation step. (4) of FIG. 1 shows a state where the aqueous medium 1 is removed from the state of (3) of FIG. (5) of FIG. 1 is a schematic cross-sectional view showing one embodiment of the hollow particles after the solvent removal step. (5) of FIG.
  • This step is a step of preparing a mixed solution containing a polymerizable monomer, a hydrophobic solvent, a polymerization initiator, a dispersion stabilizer, and an aqueous medium.
  • the mixed liquid may further contain other materials as long as the effects of the present disclosure are not impaired.
  • the materials of the mixed solution are described in order of (A) polymerizable monomer, (B) hydrophobic solvent, (C) polymerization initiator, (D) dispersion stabilizer, and (E) aqueous medium.
  • the polymerizable monomer in the mixed liquid contains at least a hydrocarbon monomer and a crosslinkable monomer.
  • the hydrocarbon monomer includes a crosslinkable hydrocarbon monomer
  • the crosslinkable monomer may consist of a crosslinkable hydrocarbon monomer, or may be a crosslinkable hydrocarbon monomer. It may be a mixture of hydrogen monomers and cross-linking monomers containing heteroatoms.
  • the polymerizable monomer in the mixed liquid may further contain a non-crosslinkable monomer within a range that does not impair the effects of the present disclosure. It may consist of a crosslinkable hydrocarbon monomer, or may be a mixture of a non-crosslinkable hydrocarbon monomer and a non-crosslinkable monomer containing a hetero atom.
  • the hydrocarbon monomers in the mixed liquid contain at least a crosslinkable hydrocarbon monomer and may further contain a non-crosslinkable hydrocarbon monomer.
  • crosslinkable hydrocarbon monomers examples include aromatic divinyl monomers such as divinylbenzene, divinylbiphenyl and divinylnaphthalene; branched diolefins, and diene monomers such as alicyclic diolefins such as dicyclopentadiene, cyclopentadiene, and ethylidenetetracyclododecene;
  • Other crosslinkable macromers such as, for example, polybutadiene, polyisoprene, block copolymers of styrene and butadiene (SBS), and block copolymers of styrene and isoprene (SIS) can also be used.
  • crosslinkable hydrocarbon monomers may be used alone or in combination of two or more.
  • aromatic divinyl monomers are preferable, and divinylbenzene is more preferable, because the polymerization reaction is easily stabilized and hollow particles having excellent dielectric properties, solvent resistance, strength, heat resistance, and the like can be obtained.
  • non-crosslinkable hydrocarbon monomers include aromatic monovinyl monomers such as styrene, vinyltoluene, ⁇ -methylstyrene, p-methylstyrene, ethylvinylbenzene, ethylvinylbiphenyl, and ethylvinylnaphthalene; ethylene, Linear or branched monoolefins such as propylene and butylene; alicyclic monoolefins such as vinylcyclohexane, norbornene, tricyclododecene, and 1,4-methano-1,4,4a,9a-tetrahydrofluorene monoolefin monomers such as; These non-crosslinking hydrocarbon monomers may be used alone or in combination of two or more. Among them, aromatic monovinyl monomers are preferred, and ethylvinylbenzene is particularly preferred, from the viewpoint of improving the dielectric properties of the hollow hollow
  • the content of the hydrocarbon monomer which is the sum of the crosslinkable hydrocarbon monomer and the non-crosslinkable hydrocarbon monomer, is 100% by mass of the polymerizable monomer contained in the mixed liquid.
  • the content is 91% by mass or more, hollow particles having excellent dielectric properties can be obtained.
  • the content of the hydrocarbon monomer is preferably 94% by mass or more, more preferably 96% by mass or more, and 100% by mass from the viewpoint of further improving the dielectric properties of the hollow particles. is more preferred.
  • the content of the hydrocarbon monomer is at least the above lower limit, the effect of lowering the dielectric loss tangent by reducing the residual double bond rate is likely to be obtained, and the heat resistance of the hollow particles can be improved.
  • the polymerizable monomer in the mixed liquid contains a polymerizable monomer different from the hydrocarbon monomer, the content of the hydrocarbon monomer is, for example, 99% by mass or less. may be 98% by mass or less.
  • the content of the crosslinkable hydrocarbon monomer is not particularly limited, but it improves the dielectric properties, solvent resistance, strength, pressure resistance, etc. of the hollow particles, and the hollow part that is clearly distinguished from the shell. From the viewpoint of formation, it is preferably 50% by mass or more, more preferably 70% by mass or more, and 75% by mass or more with respect to 100% by mass of the polymerizable monomer contained in the mixed liquid. It is more preferably 90% by mass or more, even more preferably 95% by mass or more, and particularly preferably 95% by mass or more. It is presumed that the inclusion of a large amount of the crosslinkable hydrocarbon monomer increases the number of crosslinked portions, thereby making the shell less likely to break and improving the pressure resistance.
  • the upper limit of the content of the crosslinkable hydrocarbon monomer is not particularly limited, but may be, for example, 98% by mass or less, or 96% by mass or less.
  • the content of the non-crosslinkable hydrocarbon monomer is not particularly limited, but from the point of forming a hollow portion clearly distinguished from the shell, relative to 100% by mass of the polymerizable monomer contained in the mixed liquid, It is preferably 50% by mass or less, more preferably 40% by mass or less, even more preferably 30% by mass or less, and even more preferably 20% by mass or less.
  • the lower limit of the non-crosslinkable hydrocarbon monomer content is not particularly limited, and may be, for example, 2% by mass or more, or 4% by mass or more.
  • the polymerizable monomer in the mixed liquid may further contain a polymerizable monomer different from the hydrocarbon monomer as long as the effects of the present disclosure are not impaired.
  • the polymerizable monomer different from the hydrocarbon monomer may be a crosslinkable monomer or a non-crosslinkable monomer.
  • crosslinkable monomers different from hydrocarbon monomers include ethylene glycol di(meth)acrylate, diethylene glycol di(meth)acrylate, pentaerythritol di(meth)acrylate, pentaerythritol tetra(meth)acrylate, tri Cyclodecane dimethanol di(meth)acrylate, 3-(meth)acryloyloxy-2-hydroxypropyl(meth)acrylate, trimethylolpropane tri(meth)acrylate, ditrimethylolpropane tetra(meth)acrylate, ethoxylated trimethylolpropane tri(meth)acrylate, ethoxylated pentaerythritol tetra(meth)acrylate, pentaerythritol tri(meth)acrylate, pentaerythritol tetra(meth)acrylate, dipentaerythritol hexa(meth)acrylate, dipentaery
  • crosslinkable macromers such as vinyl-modified polyphenylene ether at both ends and (meth)acrylic-modified polyphenylene ether at both ends can also be used.
  • non-crosslinkable monomers different from hydrocarbon monomers include methyl (meth)acrylate, ethyl (meth)acrylate, butyl (meth)acrylate, 2-ethylhexyl (meth)acrylate, and lauryl (meth)acrylate.
  • t-butylaminoethyl (meth)acrylate glycidyl (meth)acrylate, 2-hydroxyethyl (meth)acrylate, 2-aminoethyl (meth)acrylate, (meth)acrylic acid, methoxypolyethylene glycol (meth)acrylate, ethoxy Polyethylene glycol (meth)acrylate, propoxypolyethyleneglycol (meth)acrylate, butoxypolyethyleneglycol (meth)acrylate, hexaoxypolyethyleneglycol (meth)acrylate, octoxypolyethyleneglycol polypropyleneglycol (meth)acrylate, lauroxypolyethyleneglycol (meth)acrylate Acrylate, stearoxy polyethylene glycol (meth) acrylate, phenoxy polyethylene glycol polypropylene glycol (meth) acrylate, polyethylene glycol mono (meth) acrylate, polypropylene glycol mono (meth) acrylate,
  • the crosslinkable hydrocarbon monomer and the crosslinkable monomer that is the sum of the crosslinkable monomers different from the hydrocarbon monomer
  • the content of the polymerizable monomer is 50% by mass or more, preferably 70% by mass or more, more preferably 75% by mass or more, and still more preferably 100% by mass of the polymerizable monomer contained in the mixed liquid. 90% by mass or more, more preferably 95% by mass or more.
  • the formation of shells suppresses the deformation of the particles, which facilitates the formation of hollow portions.
  • the crosslink density of the shell can be increased, thereby improving the solvent resistance, strength, pressure resistance, etc. of the obtained hollow particles.
  • the content of the crosslinkable monomer may be, for example, 98% by mass or less, or 96% by mass or less. good too.
  • the content of the polymerizable monomer in the mixed liquid is not particularly limited, but from the viewpoint of the balance between the porosity of the hollow particles, the particle size and the mechanical strength, the total mass of the components in the mixed liquid excluding the aqueous medium is 100. It is preferably 15 to 50% by mass, more preferably 20 to 40% by mass.
  • the content of the polymerizable monomer with respect to 100% by mass of the total solid content excluding the hydrophobic solvent among the materials that become the oil phase in the mixed liquid is preferably is 96% by mass or more, more preferably 97% by mass or more.
  • the solid content is all components except the solvent, and the liquid polymerizable monomer and the like are included in the solid content.
  • hydrophobic solvent used in the production method of the present disclosure is a non-polymerizable and sparingly water-soluble organic solvent. Hydrophobic solvents act as spacer materials that form cavities inside the particles.
  • a suspension is obtained in which droplets of the monomer composition containing the hydrophobic solvent are dispersed in the aqueous medium.
  • the hydrophobic solvent with low polarity tends to gather inside the droplets of the monomer composition.
  • the hydrophobic solvent is distributed inside and the other materials other than the hydrophobic solvent are distributed around the periphery according to their respective polarities. Then, in the polymerization step to be described later, an aqueous dispersion containing precursor particles encapsulating a hydrophobic solvent is obtained. That is, a hollow portion filled with the hydrophobic solvent is formed inside the obtained precursor particles by gathering the hydrophobic solvent inside the particles.
  • the hydrophobic solvent it is preferable to select an organic solvent that has a lower solubility in water at 20°C than the crosslinkable hydrocarbon monomer contained in the mixture.
  • the hydrophobic solvent with the highest solubility is the lowest solubility than the crosslinkable hydrocarbon monomer.
  • the organic solvent having a lower solubility in water at 20° C. than the crosslinkable hydrocarbon monomer can be appropriately selected from known organic solvents, and is not particularly limited.
  • a hydrocarbon solvent is preferable. can be used.
  • Hydrocarbon-based solvents are also preferable in that they have lower solubility in water at 20° C. than divinylbenzene, which is a crosslinkable hydrocarbon monomer preferably used in the present disclosure.
  • hydrocarbon solvents examples include linear hydrocarbon solvents such as pentane, hexane, heptane, octane, 2-methylbutane and 2-methylpentane; cyclic hydrocarbon solvents such as cyclohexane, methylcyclohexane and cycloheptane; , aromatic hydrocarbon solvents such as toluene and xylene.
  • linear hydrocarbon solvents such as pentane, hexane, heptane, octane, 2-methylbutane and 2-methylpentane
  • cyclic hydrocarbon solvents such as cyclohexane, methylcyclohexane and cycloheptane
  • aromatic hydrocarbon solvents such as toluene and xylene.
  • Solvents are preferred, chain hydrocarbon solvents having 5 to 8 carbon atoms are more preferred, and at least one selected from the group consisting of pentane, hexane, heptane and octane is more preferred.
  • a hydrophobic solvent can be used individually or in combination of 2 or more types, respectively.
  • the boiling point of the hydrophobic solvent is preferably 130° C. or lower, more preferably 100° C. or lower, because it is easily removed in the solvent removal step described later.
  • the temperature is preferably 50° C. or higher, more preferably 60° C. or higher, because it is easy to heat.
  • the hydrophobic solvent is a mixed solvent containing a plurality of types of hydrophobic solvents and has a plurality of boiling points
  • the boiling point of the solvent with the highest boiling point among the solvents contained in the mixed solvent is the above upper limit value or less. It is preferable that the boiling point of the solvent with the lowest boiling point among the solvents contained in the mixed solvent is equal to or higher than the above lower limit.
  • the hydrophobic solvent used in the production method of the present disclosure preferably has a dielectric constant of 2.0 or less at 20°C.
  • the relative dielectric constant is one of the indices that indicate the degree of polarity of a compound.
  • the relative permittivity of the hydrophobic solvent is sufficiently low as 2.0 or less, it is considered that phase separation proceeds rapidly in droplets of the monomer composition, and hollow portions are likely to be formed.
  • Examples of hydrophobic solvents having a dielectric constant of 2.0 or less at 20° C. are as follows. The value in parenthesis is the relative permittivity value. Pentane (1.8), Hexane (1.9), Heptane (1.9), Octane (1.9).
  • the porosity of the hollow particles can be adjusted by changing the amount of the hydrophobic solvent in the mixture.
  • the polymerization reaction proceeds in a state in which the oil droplets containing the polymerizable monomer and the like enclose the hydrophobic solvent. tends to be higher.
  • the content of the hydrophobic solvent in the mixed liquid is 50 parts by mass or more and 500 parts by mass or less with respect to 100 parts by mass of the polymerizable monomer, so that the particle diameter of the hollow particles can be easily controlled. It is preferable because it is easy to increase the porosity while maintaining the strength of the hollow particles, and it is easy to reduce the amount of residual hydrophobic solvent in the particles.
  • the content of the hydrophobic solvent in the mixture is more preferably 60 parts by mass or more and 400 parts by mass or less, and even more preferably 70 parts by mass or more and 300 parts by mass or less with respect to 100 parts by mass of the polymerizable monomer. is.
  • (C) Polymerization Initiator In the production method of the present disclosure, hollow particles having a low dielectric loss tangent can be obtained by using an organic peroxide as a polymerization initiator.
  • the organic peroxide since the organic peroxide is lipophilic, it is present in the droplets of the monomer composition in the suspension step described later, and in the polymerization step described later, inside the droplets of the monomer composition. Since polymerization initiation radicals are generated, precursor particles having a desired particle size can be produced without excessive droplet growth.
  • the polymerization initiator used in the present disclosure preferably has a solubility in water of 0.2% by mass or less from the viewpoint of easy entry into droplets of the monomer composition.
  • Organic peroxides preferably used in the present disclosure include, for example, benzoyl peroxide (benzoyl peroxide), lauroyl peroxide, t-butyl peroxide-2-ethylhexanoate, t-butyl peroxydiethyl acetate, t -Butyl peroxypivalate and the like, and among them, at least one selected from t-butylperoxydiethyl acetate and t-butylperoxypivalate because hollow particles with excellent dielectric properties are easily obtained. Seeds are preferred, and t-butyl peroxydiethyl acetate is more preferred.
  • the content of the polymerization initiator is preferably 0.1 to 10 parts by mass, more preferably 0.5 to 7 parts by mass, and even more preferably 100 parts by mass of the polymerizable monomer in the mixed liquid. 1 to 5 parts by mass.
  • the content of the oil-soluble polymerization initiator is at least the above lower limit value, the polymerization reaction can be sufficiently progressed, and when it is at most the above upper limit value, there is little possibility that the polymerization initiator will remain after the polymerization reaction is completed. There is also little possibility that undesired side reactions will proceed.
  • the dispersion stabilizer is an agent that disperses droplets of the monomer composition in the aqueous medium in the suspension step.
  • it is easy to control the particle size of the droplets in the suspension, the particle size distribution of the resulting hollow particles can be narrowed, and the strength of the hollow particles is improved by suppressing the shell from becoming too thin. From the viewpoint of suppressing the decrease, it is preferable to use an inorganic dispersion stabilizer as the dispersion stabilizer.
  • inorganic dispersion stabilizers examples include sulfates such as barium sulfate and calcium sulfate; carbonates such as barium carbonate, calcium carbonate and magnesium carbonate; phosphates such as calcium phosphate; metals such as aluminum oxide and titanium oxide. oxides; metal hydroxides such as aluminum hydroxide, magnesium hydroxide, calcium hydroxide, barium hydroxide and ferric hydroxide; and inorganic compounds such as silicon dioxide. These inorganic dispersion stabilizers can be used singly or in combination of two or more.
  • the poorly water-soluble inorganic dispersion stabilizer is preferably an inorganic compound having a solubility of 0.5 g or less in 100 g of water.
  • the sparingly water-soluble metal salt is preferably an inorganic metal salt having a solubility of 0.5 g or less in 100 g of water.
  • the poorly water-soluble inorganic dispersion stabilizer is dispersed in an aqueous medium in the form of colloidal particles, that is, the colloidal dispersion containing the poorly water-soluble inorganic dispersion stabilizer colloidal particles. It is preferable to use it in the state As a result, the particle size distribution of the droplets of the monomer composition can be narrowed, and the residual amount of the inorganic dispersion stabilizer in the resulting hollow particles can be easily reduced by washing.
  • the colloidal dispersion containing the sparingly water-soluble inorganic dispersion stabilizer colloidal particles includes, for example, at least one selected from alkali metal hydroxides and alkaline earth metal hydroxides, and a water-soluble polyvalent metal salt (hydroxide excluding alkaline earth metal salts) in an aqueous medium.
  • Alkali metal hydroxides include lithium hydroxide, sodium hydroxide, potassium hydroxide and the like.
  • Alkaline earth metal hydroxides include barium hydroxide and calcium hydroxide.
  • the water-soluble polyvalent metal salt may be any water-soluble polyvalent metal salt other than the compounds corresponding to the alkaline earth metal hydroxides. Examples include magnesium chloride, magnesium phosphate, magnesium sulfate, and the like.
  • magnesium metal salts such as calcium chloride, calcium nitrate, calcium acetate and calcium sulfate; aluminum metal salts such as aluminum chloride and aluminum sulfate; barium salts such as barium chloride, barium nitrate and barium acetate; zinc chloride and zinc nitrate , zinc salts such as zinc acetate; Among these, magnesium metal salt, calcium metal salt, and aluminum metal salt are preferred, magnesium metal salt is more preferred, and magnesium chloride is particularly preferred.
  • the water-soluble polyvalent metal salts can be used either singly or in combination of two or more.
  • the method of reacting at least one selected from the alkali metal hydroxides and alkaline earth metal hydroxides described above with the water-soluble polyvalent metal salt described above in an aqueous medium is not particularly limited.
  • a method of mixing at least one aqueous solution selected from alkali metal salts and alkaline earth metal hydroxides with an aqueous solution of a water-soluble polyvalent metal salt can be used.
  • Colloidal silica can also be used as a colloidal dispersion containing colloidal particles of a poorly water-soluble inorganic dispersion stabilizer.
  • a surfactant is a compound having both a hydrophilic group and a hydrophobic group in one molecule, and includes compounds generally used as surfactants.
  • Surfactants usually have a solubility of 1 g/L or more in water at 25°C. Examples of surfactants include anionic surfactants, nonionic surfactants, cationic surfactants, and amphoteric surfactants, and may be known surfactants.
  • anionic surfactants include carboxylates such as alkali metal salts of higher fatty acids; sulfuric acid ester salts such as higher alcohol sulfates and higher alkyl ether sulfates; alkylbenzenesulfonates, alkylsulfonates, sulfonates such as paraffin sulfonates; and phosphate salts such as higher alcohol phosphate salts.
  • Nonionic surfactants include, for example, polyethylene glycol type nonionic surfactants such as higher alcohol ethylene oxide adducts, fatty acid ethylene oxide adducts, higher alkylamine ethylene oxide adducts, polypropylene glycol ethylene oxide adducts; polyethylene oxide, fatty acid of glycerin; Polyhydric alcohol type nonionic surfactants such as esters, pentaerythrityl fatty acid esters, sorbit or sorbitan fatty acid esters, alkyl ethers of polyhydric alcohols, and aliphatic amides of alkanolamine.
  • polyethylene glycol type nonionic surfactants such as higher alcohol ethylene oxide adducts, fatty acid ethylene oxide adducts, higher alkylamine ethylene oxide adducts, polypropylene glycol ethylene oxide adducts
  • polyethylene oxide fatty acid of glycerin
  • Examples of cationic surfactants include quaternary ammonium salts such as alkyltrimethylammonium salts.
  • Examples of amphoteric surfactants include amino acid-type amphoteric surfactants such as higher alkylaminopropionates, and betaine-type amphoteric surfactants such as higher alkyldimethylbetaines and higher alkyldihydroxyethylbetaines.
  • hydrophilic groups such as polyvinyl alcohol, methyl cellulose, ethyl cellulose, polyacrylic acid, polyacrylimide, polyethylene oxide, poly (hydroxystearate-g-methyl methacrylate-co-methacrylic acid) copolymer
  • a polymer compound having both and a hydrophobic group is also included in the surfactant.
  • the molecular weight of the surfactant is usually less than 3,000, although not particularly limited.
  • the content of the dispersion stabilizer is not particularly limited, but is preferably 0.5 to 15 parts by mass, more preferably 1 part by mass, with respect to 100 parts by mass of the total mass of the polymerizable monomer and the hydrophobic solvent. ⁇ 10 parts by mass.
  • the content of the dispersion stabilizer is equal to or higher than the above lower limit, the droplets of the monomer composition can be sufficiently dispersed so as not to coalesce in the suspension.
  • the content of the dispersion stabilizer is equal to or less than the above upper limit, it is possible to prevent the viscosity of the suspension from increasing during granulation, and to avoid the problem of the suspension clogging the granulator. can.
  • the content of the dispersion stabilizer is usually 2 parts by mass or more and 15 parts by mass or less, preferably 3 parts by mass or more and 8 parts by mass or less, relative to 100 parts by mass of the aqueous medium.
  • the aqueous medium means a medium selected from the group consisting of water, hydrophilic solvents, and mixtures of water and hydrophilic solvents.
  • a mixture of water and a hydrophilic solvent it is important that the overall polarity of the mixture is not too low from the viewpoint of forming droplets of the monomer composition.
  • the mass ratio of water and hydrophilic solvent may be 99:1 to 50:50.
  • the hydrophilic solvent in the present disclosure is not particularly limited as long as it mixes well with water and does not cause phase separation. Examples of hydrophilic solvents include alcohols such as methanol and ethanol; tetrahydrofuran (THF); dimethylsulfoxide (DMSO) and the like.
  • the mixed liquid may further contain other materials different from the materials (A) to (E) described above within a range that does not impair the effects of the present disclosure.
  • a mixed solution can be obtained by mixing each of the above materials and, if necessary, other materials, and appropriately stirring the mixture.
  • the oil phase containing (A) the polymerizable monomer, (B) the hydrophobic solvent and (C) a lipophilic material such as a polymerization initiator, (D) the dispersion stabilizer and (E)
  • the particles are dispersed with a particle size of about several millimeters. Depending on the type of material, the state of dispersion of these materials in the mixed liquid can be observed with the naked eye.
  • the mixed solution may be obtained by simply mixing the above-mentioned materials and, if necessary, other materials, and stirring them appropriately. It is preferable to separately prepare an oil phase containing a polymer, a hydrophobic solvent and a polymerization initiator and an aqueous phase containing a dispersion stabilizer and an aqueous medium in advance and mix them to prepare a mixed solution.
  • a colloidal dispersion obtained by dispersing a sparingly water-soluble inorganic dispersion stabilizer in the form of colloidal particles in an aqueous medium can be preferably used as the aqueous phase.
  • the suspension step is a step of preparing a suspension in which droplets of a monomer composition containing a hydrophobic solvent are dispersed in an aqueous medium by suspending the above-mentioned mixture.
  • a suspending method for forming droplets of the monomer composition is not particularly limited, and a known suspending method can be employed.
  • Dispersers used in preparing the suspension include, for example, Milder (: product name) manufactured by Pacific Machinery Co., Ltd., Cavitron (: product name) manufactured by Eurotech Co., Ltd., and Inline manufactured by IKA.
  • a horizontal or vertical in-line disperser such as a disperser (eg, DISPAX-REACTOR (registered trademark) DRS (: product name)); an emulsifying disperser such as the Homomixer MARK II series manufactured by Primix Corporation;
  • a disperser eg, DISPAX-REACTOR (registered trademark) DRS (: product name)
  • an emulsifying disperser such as the Homomixer MARK II series manufactured by Primix Corporation
  • droplets of the monomer composition containing the lipophilic material and having a particle size of about 1 to 10 ⁇ m are uniformly dispersed in the aqueous medium.
  • Such droplets of the monomer composition are difficult to observe with the naked eye, and can be observed with a known observation instrument such as an optical microscope.
  • the hydrophobic solvent with low polarity tends to collect inside the droplets.
  • the resulting droplet has the hydrophobic solvent distributed inside and the material other than the hydrophobic solvent distributed around the periphery.
  • the droplets of the monomer composition dispersed in the aqueous medium are formed by surrounding the oil-soluble monomer composition with the dispersion stabilizer.
  • the droplets of the monomer composition contain an oil-soluble polymerization initiator, a polymerizable monomer and a hydrophobic solvent.
  • the droplets of the monomer composition are oil droplets, and the oil-soluble polymerization initiator generates polymerization initiation radicals inside the oil droplets. Therefore, precursor particles having a desired particle size can be produced without excessively growing fine oil droplets.
  • an oil-soluble polymerization initiator there is no opportunity for the polymerization initiator to come into contact with the polymerizable monomer dispersed in the aqueous medium. Therefore, by using an oil-soluble polymerization initiator, it is possible to suppress the by-production of excessive resin particles such as solid particles having a relatively small particle size in addition to the target resin particles having hollow portions.
  • the suspension obtained by the suspension step described above is subjected to a polymerization reaction to have a hollow portion surrounded by a shell containing a resin, and a hydrophobic solvent in the hollow portion.
  • the precursor particles are formed by polymerizing the polymerizable monomers contained in the droplets of the monomer composition, and the shells of the precursor particles contain the polymer of the polymerizable monomers as a resin.
  • the polymerization system There is no particular limitation on the polymerization system, and for example, a batch system (batch system), a semi-continuous system, a continuous system, or the like can be employed.
  • the polymerization temperature in the polymerization step is higher than the 10-hour half-life temperature of the polymerization initiator. This allows the polymerization reaction to proceed sufficiently and the percentage of residual double bonds to be reduced. From the same point of view, the polymerization temperature is higher than the 10-hour half-life temperature of the polymerization initiator, and the difference between the polymerization temperature and the 10-hour half-life temperature of the polymerization initiator is preferably 3° C. or more. , more preferably 5° C. or higher. When a plurality of polymerization initiators are used in combination, it is preferable to set the polymerization temperature as described above based on the polymerization initiator having the highest 10-hour half-life temperature.
  • the lower limit of the polymerization temperature is preferably 20° C. or higher, more preferably 65° C. or higher, and still more preferably 80° C. or higher, from the viewpoint of sufficiently progressing the polymerization reaction.
  • the upper limit of the polymerization temperature is appropriately adjusted so that the water-based medium does not evaporate, and is not particularly limited. is preferred.
  • the rate of temperature rise when raising the temperature to the polymerization temperature is not particularly limited, but is preferably 10° C./h to 60° C./h, more preferably 15° C./h to 55° C./h.
  • the polymerization reaction time is preferably 7 hours or longer, more preferably 15 hours or longer, and still more preferably 24 hours or longer, from the viewpoint of allowing the polymerization reaction to proceed sufficiently and reducing the residual double bond ratio. and preferably 48 hours or less from the viewpoint of suppressing a decrease in production efficiency.
  • the shell portion of the droplet of the monomer composition containing the hydrophobic solvent inside is polymerized. A hollow is formed.
  • This step is a step of obtaining a solid content containing precursor particles by performing solid-liquid separation on the precursor composition containing precursor particles obtained by the polymerization step described above.
  • a method for solid-liquid separation of the precursor composition is not particularly limited, and a known method can be used.
  • the solid-liquid separation method include centrifugation, filtration, static separation, etc. Among these, centrifugation or filtration can be employed. may be adopted.
  • an optional step such as a pre-drying step may be carried out before carrying out the solvent removal step described below.
  • the pre-drying step include a step of pre-drying the solid content obtained after the solid-liquid separation step using a drying device such as a dryer or a drying device such as a hand dryer.
  • Solvent removal step is a step of removing the hydrophobic solvent included in the precursor particles obtained in the solid-liquid separation step. For example, by removing the hydrophobic solvent contained in the precursor particles in air, the hydrophobic solvent inside the precursor particles is replaced with air, and hollow particles filled with gas are obtained.
  • in air in this step means an environment where there is no liquid component outside the precursor particles, and a very small amount of hydrophobic solvent outside the precursor particles that does not affect the removal of the solvent. means an environment where there is only a liquid fraction of “In air” can be rephrased as a state in which the precursor particles are not present in the slurry, and can be rephrased as a state in which the precursor particles are present in the dry powder. That is, in this step, it is important to remove the hydrophobic solvent in an environment where the precursor particles are in direct contact with the external gas.
  • a method for removing the hydrophobic solvent in the precursor particles in air is not particularly limited, and a known method can be adopted.
  • the method include a vacuum drying method, a heat drying method, a flash drying method, or a combination of these methods.
  • the heating temperature must be higher than the boiling point of the hydrophobic solvent and lower than the maximum temperature at which the shell structure of the precursor particles does not collapse. Therefore, the heating temperature may be, for example, 50 to 200°C, 70 to 200°C, or 100 to 200°C, depending on the composition of the shell in the precursor particles and the type of hydrophobic solvent. Due to the drying operation in air, the hydrophobic solvent inside the precursor particles is replaced by the external gas, resulting in hollow particles in which the hollow portion is filled with gas.
  • the drying atmosphere is not particularly limited, and can be appropriately selected depending on the use of the hollow particles. Air, oxygen, nitrogen, argon, etc. can be considered as the dry atmosphere, for example. Further, hollow particles whose insides are temporarily vacuumed can also be obtained by once filling the insides of the hollow particles with gas and then drying them under reduced pressure.
  • the hydrophobic solvent may be removed in the slurry containing the precursor particles and the aqueous medium without solid-liquid separation of the slurry-like precursor composition obtained in the polymerization step.
  • the hydrophobic solvent contained in the precursor particles is removed by bubbling an inert gas through the precursor composition at a temperature equal to or higher than the boiling point of the hydrophobic solvent minus 35°C. be able to.
  • the hydrophobic solvent is a mixed solvent containing a plurality of types of hydrophobic solvents and has a plurality of boiling points
  • the boiling point of the hydrophobic solvent in the solvent removal step is the boiling point of the solvent contained in the mixed solvent.
  • the boiling point is the boiling point of the solvent with the highest boiling point, that is, the highest boiling point among a plurality of boiling points.
  • the temperature at which the inert gas is bubbled through the precursor composition is preferably at least the temperature obtained by subtracting 30°C from the boiling point of the hydrophobic solvent in order to reduce the residual amount of the hydrophobic solvent in the hollow particles.
  • the temperature is preferably equal to or higher than the temperature minus 20°C.
  • the temperature during bubbling is usually a temperature equal to or higher than the polymerization temperature in the polymerization step. Although not particularly limited, the temperature during bubbling may be 50° C. or higher and 100° C. or lower.
  • the bubbling inert gas is not particularly limited, but examples thereof include nitrogen and argon.
  • the bubbling conditions are appropriately adjusted according to the type and amount of the hydrophobic solvent so that the hydrophobic solvent contained in the precursor particles can be removed, and are not particularly limited. /min, and may be bubbled for 1 to 10 hours.
  • an aqueous slurry of hollow particles containing an inert gas is obtained.
  • the hollow particles obtained by solid-liquid separation of this slurry are dried to remove the aqueous medium remaining in the hollow particles, thereby obtaining the hollow particles in which the hollow portion is filled with gas.
  • a method for obtaining hollow particles in which the hollow portions are filled with gas by removing the hydrophobic solvent in the precursor particles in the air after solid-liquid separation of the slurry-like precursor composition After removing the hydrophobic solvent contained in the precursor particles in the slurry containing the aqueous medium, solid-liquid separation is performed, and the aqueous medium remaining in the particles is removed in the air to fill the hollow part with gas.
  • the former method has the advantage that the hollow particles are less likely to be crushed in the step of removing the hydrophobic solvent, and the latter method is achieved by bubbling with an inert gas. There is an advantage that the amount of residual hydrophobic solvent is reduced.
  • the hydrophobic solvent contained in the precursor particles is removed without solid-liquid separation of the slurry-like precursor composition obtained in the polymerization step.
  • a predetermined pressure high pressure, normal pressure or reduced pressure
  • a method of evaporating the hydrophobic solvent contained in the precursor particles from the precursor composition under a predetermined pressure (under high pressure, a method of introducing an inert gas such as nitrogen, argon, or helium or water vapor into the precursor composition under normal pressure or under reduced pressure to evaporate it.
  • (6-a) washing step and (6-b) particle interior replacement step may be added.
  • (6-a) Washing step an acid or alkali is added to remove the dispersion stabilizer remaining in the precursor composition containing the precursor particles before the solvent removal step. It is a process to do.
  • the dispersion stabilizer used is an acid-soluble inorganic dispersion stabilizer, it is preferable to wash by adding an acid to the precursor composition containing the precursor particles.
  • is an inorganic compound that is soluble in alkali it is preferable to add an alkali to the precursor composition containing the precursor particles for washing.
  • the acid is added to the precursor composition containing the precursor particles, and the pH is adjusted to preferably 6.5 or less, more preferably 6.5. It is preferable to adjust as follows.
  • inorganic acids such as sulfuric acid, hydrochloric acid and nitric acid, and organic acids such as formic acid and acetic acid can be used. , particularly sulfuric acid, is preferred.
  • the particle interior replacement step is a step of replacing the gas or liquid inside the hollow particles with another gas or liquid.
  • the environment inside the hollow particles can be changed, molecules can be selectively confined inside the hollow particles, and the chemical structure inside the hollow particles can be modified according to the application.
  • Hollow particles of the present disclosure are hollow particles comprising a shell containing a resin and a hollow portion surrounded by the shell, the porosity being 50% or more, the shell being the resin, the hydrocarbon monomer containing a polymer containing 91% by mass or more of body units and 50% by mass or more of crosslinkable monomer units, at least a portion of the hydrocarbon monomer units being crosslinkable hydrocarbon monomer units;
  • the residual double bond rate of the polymer is 30.0% or less, and the dielectric loss tangent at a frequency of 10 GHz is 3.00 ⁇ 10 ⁇ 3 or less.
  • the hollow particles of the present disclosure contain the above polymerizable monomer polymer as a main component of the shell, and the polymer forms the skeleton of the shell of the hollow particles.
  • the content of the hydrocarbon monomer unit is 91% by mass or more with respect to 100 parts by mass of all structural units in the polymer contained in the shell, thereby improving the dielectric properties.
  • the content of the hydrocarbon monomer unit is preferably 94% by mass or more, more preferably 96% by mass or more, and 100% by mass. is more preferred.
  • the content of the hydrocarbon monomer unit is at least the above lower limit, the effect of lowering the dielectric loss tangent by reducing the residual double bond ratio is likely to be obtained, and the heat resistance of the hollow particles is improved. can be done.
  • the content of the hydrocarbon monomer unit may be, for example, 99% by mass or less, or 98% by mass. It may be below.
  • the content of the crosslinkable monomer unit is 50% by mass or more with respect to 100 parts by mass of all structural units in the polymer contained in the shell, so that the hollow particles are clearly distinguished from the shell. It can have a hollow portion that is filled with a large amount of water, and is excellent in solvent resistance, strength, pressure resistance, and the like.
  • the content of the crosslinkable monomer unit is preferably 70% by mass or more, more preferably 75% by mass or more, still more preferably 90% by mass or more, and 95% by mass or more. is particularly preferred.
  • the upper limit of the content of the crosslinkable monomer unit is not particularly limited, but may be, for example, 98% by mass or less, or 96% by mass or less.
  • the dielectric properties are improved, the solvent resistance, strength, pressure resistance, etc. are also improved, and the hollow part can be clearly distinguished from the shell.
  • the content of the crosslinkable hydrocarbon monomer unit is preferably 50% by mass or more, more preferably 70% by mass or more, based on 100 parts by mass of all structural units in the polymer contained in It is more preferably 75% by mass or more, even more preferably 90% by mass or more, and particularly preferably 95% by mass or more.
  • the upper limit of the content of the crosslinkable hydrocarbon monomer unit is not particularly limited, but may be, for example, 98% by mass or less, or 96% by mass or less.
  • the content of the non-crosslinkable hydrocarbon monomer units is not particularly limited, but the shell From the viewpoint of having a hollow portion clearly distinguished from is more preferably 30% by mass or less, and even more preferably 20% by mass or less.
  • the lower limit of the content of non-crosslinkable hydrocarbon monomer units is not particularly limited, and may be, for example, 2% by mass or more, or 4% by mass or more.
  • the content of the polymer of the polymerizable monomer is preferably 96% by mass or more, more preferably 97% by mass or more, still more preferably 98% by mass, based on 100% by mass of the total solid content of the shell. It is at least 99% by mass, more preferably at least 99% by mass.
  • the polymer contained in the shell has a residual double bond rate of 30.0% or less, preferably 20.0% or less, more preferably 15.0% or less.
  • the residual double bond rate is equal to or less than the upper limit contributes to the improvement of the dielectric properties.
  • the residual double bond ratio is equal to or less than the above upper limit, the hollow particles are excellent in heat resistance.
  • the lower limit of the residual double bond ratio is not particularly limited, and from the viewpoint of improving the dielectric properties of the hollow particles, the lower the residual double bond ratio, the better.
  • the lower limit of the residual double bond ratio may be, for example, 1% or more, 3% or more, or 5% or more.
  • the residual double bond ratio can be determined as follows. First, the polymer contained in the hollow particles and the polymerizable monomer before the polymerization reaction used for the production of the hollow particles are measured for infrared absorption spectra in the form of absorbance display. On the other hand, among the polymerizable monomers used to prepare the hollow particles, the one with the highest content is specified as the reference monomer. If there are multiple monomers with the highest content, one of them is specified as the reference monomer. One structure that does not increase or decrease before and after the polymerization reaction is selected from the structures of the reference monomer.
  • a peak derived from the selected structure is used as a reference peak.
  • the peak intensity of the reference peak was divided by the content of the monomer containing the structure representing the reference peak. A value is calculated, and the calculated value is used as a reference peak intensity.
  • the peak intensity of the peak derived from the polymerizable unsaturated double bond (C ⁇ C) is measured.
  • Formula (A): Percentage of residual double bonds (%) ⁇ (P 1 /P 0 )/(M 1 /M 0 ) ⁇ 100
  • the peak intensity can be quantified as the height from the baseline to the peak top, which is obtained by placing base points outside both ends of the peak and connecting the base points with a straight line.
  • the values of the peak intensity and the peak intensity ratio used for calculating the residual double bond ratio are rounded to three significant figures according to rule B of JIS Z8401:1999, and the residual double bond ratio is The value is rounded to the first place.
  • the standard monomer is divinylbenzene, which has the highest content.
  • a C—H bond of a benzene ring contained in divinylbenzene is selected as a structure that does not increase or decrease before and after the polymerization reaction.
  • the infrared absorption spectrum of a polymerizable monomer composed of 95% by mass of divinylbenzene and 5% by mass of ethylvinylbenzene and the infrared absorption spectrum of the polymer contained in the hollow particles are measured.
  • the peak derived from the CH bond of the benzene ring contained in divinylbenzene is specified as the reference peak.
  • Suitable monomers are divinylbenzene and ethylvinylbenzene. Therefore, a value obtained by dividing the peak intensity of the reference peak by 1.00, which is the sum of the content ratio of divinylbenzene and the content ratio of ethylvinylbenzene, is defined as the reference peak intensity.
  • the ratio (M 1 ) of the peak intensity (M 1 /M 0 ) and the peak intensity of the peak derived from the polymerizable unsaturated double bond (C C) with respect to the reference peak intensity (P 0 ) obtained from the infrared absorption spectrum of the polymer contained in the hollow particles ( P 1 ) from the ratio (P 1 /P 0 )
  • the ratio of residual double bonds is calculated by the above formula (A).
  • the infrared absorption spectrum can be measured, for example, by a total reflection measurement method (ATR method).
  • ATR method a total reflection measurement method
  • product name Spectrum One manufactured by PERKIN ELMER Co., Ltd. can be mentioned.
  • the content of components other than the polymer is preferably 4% by mass or less, more preferably 4% by mass or less, based on 100% by mass of the total solid content of the shell, from the viewpoint of suppressing deterioration of dielectric properties. is 3% by mass or less, more preferably 2% by mass or less, and even more preferably 1% by mass or less.
  • Components other than the polymer contained in the hollow particles of the present disclosure include, for example, a polymerizable monomer that remains unreacted, a polymer different from the polymer of the polymerizable monomer, and a polymer that initiates polymerization.
  • Examples include decomposition products of agents, low-molecular-weight compounds contained as impurities in raw materials of polymerizable monomers, and the like. Those with low boiling points (eg, boiling points of 200° C. or lower) are usually removed during the manufacturing process of hollow particles, but those with high boiling points (eg, boiling points of 250° C. or higher) may remain without being removed.
  • low boiling points eg, boiling points of 200° C. or lower
  • high boiling points eg, boiling points of 250° C. or higher
  • the hollow particles of the present disclosure preferably have a surfactant content of 500 ppm or less, more preferably 200 ppm or less, even more preferably 100 ppm or less, and even more preferably 100 ppm or less. is 50 ppm or less.
  • a surfactant is used in the manufacturing process of the hollow particles, for example, when the mixture is made to contain the surfactant, the surfactant may remain on the surfaces of the obtained hollow particles.
  • the content of surfactant present on the surface of the hollow particles can be reduced to 10 ppm or less, more preferably 1 ppm or less.
  • the content of the surfactant present on the hollow particle surface is the ratio of the mass of the surfactant present on the hollow particle surface to the mass of the hollow particle.
  • Surfactants present on the hollow particle surface can be extracted, for example, by sonicating the hollow particles in water.
  • the type and mass of the surfactant extracted into water can be identified from the peak positions and peak intensities of the 1 H-NMR spectrum.
  • the hollow particles of the present disclosure preferably have a metal content of 100 ppm or less, more preferably 80 ppm or less, and even more preferably 70 ppm or less.
  • a metal shall also contain a metal ion.
  • the metal content in the hollow particles is the ratio of the total mass of the metal components contained in the hollow particles to the mass of the hollow particles.
  • the metal content in the hollow particles is made equal to or less than the above upper limit, for example, a polymerization initiator containing no metal is used, ion-exchanged water is used as an aqueous medium, and the washing step is performed in the production of the hollow particles.
  • a method of removing the hydrophobic solvent contained in the precursor particles in the air in the solvent removal step it is preferable to employ a method of removing the hydrophobic solvent contained in the precursor particles in the air in the solvent removal step.
  • the metal content contained in the hollow particles can be measured by ICP emission spectrometry. Identification of the metal species can be performed by X-ray fluorescence spectroscopy (XRF).
  • the hollow particles of the present disclosure have a dielectric loss tangent at a frequency of 10 GHz of 3.00 ⁇ 10 -3 or less, preferably 2.60 ⁇ 10 -3 or less, more preferably 2.50 ⁇ 10 -3 or less, and even more preferably 1.00 ⁇ 10 ⁇ 3 or less, more preferably 8.00 ⁇ 10 ⁇ 4 or less, particularly preferably 7.50 ⁇ 10 ⁇ 4 or less, and the lower limit is not particularly limited, for example 1.00 ⁇ 10 It may be -4 or more.
  • the hollow particles of the present disclosure preferably have a dielectric constant of 1.50 or less, more preferably 1.45 or less, and even more preferably 1.40 or less at a frequency of 10 GHz, and the lower limit is not particularly limited. For example, it may be 1.00 or more.
  • the dielectric constant and dielectric loss tangent of hollow particles are measured using a perturbation-type measuring device under the condition of a measurement frequency of 10 GHz.
  • the hollow particles of the present disclosure have a porosity of 50% or more, preferably 60% or more, more preferably 65% or more, and even more preferably 70% or more.
  • the porosity is equal to or higher than the above lower limit, the hollow particles are excellent in dielectric properties, lightness, heat insulation, and the like.
  • the upper limit of the porosity of the hollow particles is not particularly limited, it is preferably 90% or less, more preferably 85% or less, and still more preferably 80% or less from the viewpoint of suppressing a decrease in the strength of the hollow particles and making them difficult to crush. is.
  • the porosity of the hollow particles is calculated from the apparent density D1 and the true density D0 of the hollow particles.
  • the method for measuring the apparent density D1 of hollow particles is as follows. First, a measuring flask with a volume of 100 cm 3 is filled with about 30 cm 3 of hollow particles, and the mass of the filled hollow particles is accurately weighed. The volumetric flask filled with hollow particles is then filled precisely to the marked line with isopropanol, taking care not to introduce air bubbles. Accurately weigh the mass of isopropanol added to the volumetric flask, and calculate the apparent density D 1 (g/cm 3 ) of the hollow particles based on the following formula (I).
  • Apparent density D 1 [mass of hollow particles]/(100-[mass of isopropanol]/[specific gravity of isopropanol at measurement temperature])
  • the apparent density D1 corresponds to the specific gravity of the entire hollow particle when the hollow portion is regarded as part of the hollow particle.
  • the method for measuring the true density D0 of the hollow particles is as follows. After pre-pulverizing the hollow particles, about 10 g of pulverized pieces of the hollow particles are filled into a volumetric flask having a capacity of 100 cm 3 , and the mass of the filled pulverized pieces is accurately weighed. After that, isopropanol is added to the volumetric flask in the same manner as the above apparent density measurement, the mass of isopropanol is accurately weighed, and the true density D 0 (g/cm 3 ) of the hollow particles is calculated based on the following formula (II). do.
  • True density D 0 [mass of pulverized pieces of hollow particles]/(100-[mass of isopropanol]/[specific gravity of isopropanol at measurement temperature])
  • the true density D0 corresponds to the specific gravity of only the shell portion of the hollow particles. As is clear from the above measurement method, the hollow portion is not considered part of the hollow particle when calculating the true density D0 .
  • the porosity (%) of the hollow particles is calculated by the following formula (III) from the apparent density D1 and the true density D0 of the hollow particles.
  • Formula (III) Porosity (%) 100 - (apparent density D 1 / true density D 0 ) x 100
  • the lower limit of the volume average particle diameter is preferably 1.0 ⁇ m or more, more preferably 1.5 ⁇ m or more, and even more preferably 2.0 ⁇ m or more.
  • the upper limit of the volume average particle diameter of the hollow particles is preferably 10.0 ⁇ m or less, more preferably 8.0 ⁇ m or less, and even more preferably 6.0 ⁇ m or less.
  • the volume average particle diameter of the hollow particles is equal to or less than the above upper limit, variations in shell thickness are suppressed, a uniform shell is easily formed, and the hollow particles are less likely to be crushed, resulting in high mechanical strength.
  • the hollow particles having a volume average particle diameter within the above range have sufficiently small particle diameters, they are suitably used as a substrate material for electronic circuit boards and the like, and can be added to thin and small substrates.
  • the shape of the hollow particles of the present disclosure is not particularly limited as long as a hollow portion is formed inside, and examples thereof include spherical, ellipsoidal, irregular shapes, and the like. Among these, a spherical shape is preferable from the viewpoint of ease of manufacture, pressure resistance, and the like.
  • the hollow particles of the present disclosure may have one or more hollow portions. Those having only one portion are preferred.
  • the proportion of particles having only one or two hollow portions is preferably 90% by mass or more, more preferably 95% by mass or more.
  • the proportion of particles having only one hollow portion is preferably 90% by mass or more, more preferably 95% by mass or more.
  • the shell provided in the hollow particles of the present disclosure and the partition wall that partitions adjacent hollow portions in the case of having two or more hollow portions may be porous, but from the viewpoint of improving dielectric properties. , preferably solid.
  • the hollow particles of the present disclosure may have an average circularity of 0.950 to 0.995.
  • An example of the image of the shape of the hollow particles of the present disclosure is a bag made of a thin film and inflated with gas, the cross-sectional view of which is shown as the hollow particles 10 in (5) of FIG. 1 .
  • a thin film is provided on the outside and the inside is filled with gas.
  • the particle shape can be confirmed by, for example, SEM or TEM.
  • the particle size distribution (volume average particle size (Dv)/number average particle size (Dn)) of the hollow particles may be, for example, 1.1 or more and 2.5 or less. When the particle size distribution is 2.5 or less, it is possible to obtain particles with little variation in performance among particles. Further, when the particle size distribution is 2.5 or less, for example, when manufacturing a sheet-like resin molding to which the hollow particles of the present disclosure are added, a product having a uniform thickness can be manufactured.
  • the volume average particle diameter (Dv) and number average particle diameter (Dn) of the hollow particles are obtained, for example, by measuring the particle diameter of the hollow particles with a particle size distribution analyzer and calculating the number average and volume average, respectively. The values can be the number average particle size (Dn) and the volume average particle size (Dv) of the particles.
  • the particle size distribution is obtained by dividing the volume average particle size by the number average particle size.
  • the hollow particles of the present disclosure are excellent in dielectric properties also due to the small proportion of particles having a circularity of 0.85 or less.
  • Particles with a circularity of 0.85 or less are typically particles with deformation such as dents or cracks, and are sometimes referred to as "irregularly shaped particles" in the present disclosure.
  • Such irregular-shaped hollow particles have lower porosity than spherical hollow particles, and are inferior in dielectric properties. Therefore, the dielectric properties of the hollow particles can be improved by reducing the ratio of irregularly shaped particles contained in the hollow particles.
  • irregularly shaped particles compared to spherical hollow particles, irregularly shaped particles have a lower proportion of hollow portions and a larger proportion of resin, so that the weight loss due to thermal decomposition progresses faster, so the thermal decomposition initiation temperature is low. Therefore, the heat resistance of the hollow particles can be improved by reducing the ratio of irregularly shaped particles contained in the hollow particles.
  • irregularly shaped particles tend to aggregate when dispersed in a matrix resin, resulting in poor dispersibility compared to spherical particles. Further, irregularly-shaped particles tend to be locally subjected to external pressure, and thus have the problem of being inferior to spherical particles in pressure resistance.
  • the hollow particles of the present disclosure may contain, as an impurity, a small amount of particles with a low degree of circularity in which particle cracking, deformation, etc. have occurred, but the degree of circularity is 0.85 or less in 100% by mass of the hollow particles of the present disclosure.
  • Circularity is defined as the value obtained by dividing the diameter of a circle having the same area as the projected image of the particle (equivalent circle diameter) by the diameter of the circle having the same perimeter as the projected image of the particle (equivalent perimeter diameter). be done. If the particle is a perfect sphere, the circularity is 1, and the more complicated the surface shape of the particle, the smaller the circularity. In the present disclosure, circularity is measured using a flow particle image measurement device with an image resolution of 0.185 ⁇ m/pixel.
  • IF-3200 (trade name) manufactured by Jusco International Co., Ltd.
  • IF-3200 trade name
  • a mixture of 0.10 to 0.12 g of hollow particles in an aqueous solution (concentration of 0.3%) of sodium linear alkylbenzene sulfonate is dispersed with an ultrasonic cleaner for 5 minutes.
  • the average circularity is the average circularity of 1000 to 3000 arbitrarily selected particles.
  • the thermal decomposition initiation temperature of the hollow particles is preferably 150 to 400°C, more preferably 335°C or higher, more preferably 340°C or higher, and even more preferably 345°C or higher.
  • the thermal decomposition initiation temperature of the hollow particles may be 370° C. or lower, or may be 350° C. or lower.
  • the thermal decomposition start temperature of the hollow particles is the temperature at which the weight is reduced by 5%, under the conditions of an air atmosphere, an air flow rate of 230 mL / min, and a heating rate of 10 ° C. / min. can be measured by
  • hollow particles of the present disclosure include, for example, low dielectric materials used in various fields such as automobiles, electricity, electronics, construction, aviation, space, members such as heat insulating materials, sound insulating materials and light reflecting materials, food containers , sports shoes, footwear such as sandals, home appliance parts, bicycle parts, stationery, tools, filaments for 3D printers, etc.
  • the hollow particles of the present disclosure are excellent in dielectric properties, and thus are suitably used as an additive for realizing low transmission loss in the field of electricity or electronics.
  • the hollow particles of the present disclosure are suitably used as an electronic circuit board material. can be reduced.
  • the hollow particles of the present disclosure can also be used as interlayer insulating materials, dry film resists, solder resists, bonding wires, magnet wires, semiconductor sealing materials, epoxy sealing materials, mold underfills, underfills, die bond pastes, It is also suitably used as an additive in semiconductor materials such as buffer coating materials, copper-clad laminates, flexible substrates, high-frequency device modules, antenna modules, and in-vehicle radars.
  • semiconductor materials such as buffer coating materials, copper-clad laminates, flexible substrates, high-frequency device modules, antenna modules, and in-vehicle radars.
  • additives in semiconductor materials such as interlayer insulating materials, solder resists, magnet wires, epoxy encapsulants, underfills, buffer coating materials, copper-clad laminates, flexible substrates, high-frequency device modules, antenna modules, and in-vehicle radars.
  • the hollow particles of the present disclosure when added to a molded body, are excellent in effects as a weight reduction material, a heat insulating material, a soundproof material, a damping material, etc., and therefore are suitable as an additive for a molded body. , can be used as an additive for resin moldings, and can be contained as a filler in fiber-reinforced moldings formed by using resins and reinforcing fibers.
  • the hollow particles of the present disclosure have a high porosity, are resistant to crushing, and have excellent heat resistance, they satisfy the heat insulating properties and cushioning properties (cushion properties) required for undercoat materials, and can be used immediately for thermal paper applications. It also satisfies the required heat resistance.
  • the hollow particles of the present disclosure are also useful as plastic pigments with excellent gloss, hiding power, and the like. Furthermore, the hollow particles of the present disclosure can enclose useful ingredients such as fragrances, chemicals, agricultural chemicals, and ink ingredients inside by means of immersion treatment, reduced pressure or pressure immersion treatment, etc., so that various It can be used for various purposes. Furthermore, the hollow particles of the present disclosure are also suitable for use as a rust inhibitor. The hollow particles of the present disclosure are also useful as an additive that reduces electrical conductivity. It can be used as a paint (paint base, lubricating paint, etc.). In addition, the hollow particles added to the antirust paint can contain an antirust additive.
  • the resin composition of the present disclosure contains the hollow particles of the present disclosure and a matrix resin.
  • the resin composition of the present disclosure may be a liquid resin composition, or may be a resin molding.
  • the liquid resin composition include those containing a liquid matrix resin before the curing reaction, those obtained by dissolving or dispersing each component in a solvent, or those in which the matrix resin is a thermoplastic resin and the resin melts.
  • the resin composition can be liquefied due to the presence of the resin composition.
  • resin moldings include those obtained by molding liquid resin compositions such as those described above by a known method.
  • the matrix resin contained in the liquid resin composition of the present disclosure is not particularly limited. you can Further, the matrix resin contained in the resin composition of the present disclosure may be an unreacted monomer, prepolymer or macromonomer, may be a polymer, or may be a cured resin such as polyamic acid. may be a precursor of The matrix resin contained in the resin composition of the present disclosure functions as a binder (binding agent) by, for example, heating, light irradiation, or curing using a curing agent, a polymerization initiator, a catalyst, or the like. can be
  • thermosetting resin a known one can be used, and is not particularly limited. Silicon-based resin, alkyd-based resin, thermosetting modified polyphenylene ether-based resin, thermosetting polyimide-based resin, benzoxazine-based resin, allyl-based resin, aniline-based resin, maleimide-based resin, bismaleimide triazine-based resin, liquid crystalline polyester resins, vinyl ester resins, unsaturated polyester resins, cyanate ester resins, polyetherimide resins, and precursors of these resins before curing. These thermosetting resins can be used alone or in combination of two or more.
  • room temperature curable resins include adhesives such as epoxy adhesives, silicone adhesives, and acrylic adhesives that can be cured at room temperature with the addition of a catalyst.
  • thermoplastic resins include polyolefin-based resins, polyamide-based resins, polycarbonate-based resins, polyphenylene sulfide-based resins, polyetheretherketone-based resins, polystyrene-based resins, polyphenylene oxide-based resins, liquid crystalline polymer (LCP), and the like. mentioned. These matrix resins can be used alone or in combination of two or more.
  • thermoplastic resin used in molding a known thermoplastic resin can be used, and is not particularly limited.
  • polypropylene polyolefins such as polyethylene; polyamides such as PA6, PA66, PA12; polyimide, polyamideimide, polyetherimide, polyetherketoneketone, polyvinyl chloride, polystyrene, poly(meth)acrylate, polycarbonate, polyvinylidene fluoride, acrylonitrile-butadiene - styrene copolymer (ABS), acrylonitrile-styrene copolymer (AS), polyphenylene ether, polyphenylene sulfide, polyester, polytetrafluoroethylene, thermoplastic elastomers, and the like.
  • thermoplastic resins can be used alone or in combination of two or more.
  • epoxy resins thermosetting modified polyphenylene ether resins, thermosetting polyimide resins, silicon resins, and benzoxazine resins are used as matrix resins.
  • melamine-based resins, urea-based resins, allyl-based resins, phenol-based resins, unsaturated polyester-based resins, polyurethane-based resins, aniline-based resins, and other insulating resins are preferably used.
  • resins, modified polyphenylene ether-based resins, silicon-based resins, benzoxazine-based resins, melamine-based resins, and the like are preferably used. These insulating resins can be used alone or in combination of two or more.
  • the content of the matrix resin is not particularly limited, it is preferably 50 to 95% by mass or less in the total solid content of 100% by mass of the resin composition of the present disclosure.
  • the content of the matrix resin is at least the above lower limit, the moldability of the resin molded article is excellent, and the mechanical strength of the resulting resin molded article is excellent.
  • the content of the matrix resin is equal to or less than the upper limit value, the hollow particles of the present disclosure can be sufficiently contained, so that the effects of the hollow particles of the present disclosure, such as low dielectric loss tangent, can be sufficiently exhibited. be able to.
  • the resin composition of the present disclosure may further contain additives such as a curing agent, a curing catalyst, or an initiator for advancing the curing reaction, depending on the type of resin.
  • additives such as a curing agent, a curing catalyst, or an initiator for advancing the curing reaction, depending on the type of resin.
  • curing agents include amines, acid anhydrides, imidazoles, thiols, phenols, naphthols, benzoxazines, cyanate esters, and carbodiimides.
  • the content of the curing agent is not particularly limited, and may be, for example, 5 to 120 parts by mass with respect to 100 parts by mass of the matrix resin.
  • the content of the hollow particles of the present disclosure is not particularly limited, it is preferably 5 to 50 mass% of the total solid content of 100 mass% of the resin composition of the present disclosure.
  • the content of the hollow particles is equal to or more than the above lower limit, the effects of the hollow particles of the present disclosure, such as low dielectric loss tangent, can be sufficiently exhibited.
  • the content of the hollow particles is equal to or less than the above upper limit, the matrix resin can be sufficiently contained, so that moldability and mechanical strength can be improved.
  • the resin composition of the present disclosure may contain additives such as compatibilizers, ultraviolet absorbers, colorants, heat stabilizers, fillers, flame retardants, solvents, etc. Further, it may be contained. In addition, the resin composition of the present disclosure may further contain organic or inorganic fibers such as carbon fibers, glass fibers, aramid fibers, and polyethylene fibers when forming resin moldings.
  • additives such as compatibilizers, ultraviolet absorbers, colorants, heat stabilizers, fillers, flame retardants, solvents, etc. Further, it may be contained.
  • the resin composition of the present disclosure may further contain organic or inorganic fibers such as carbon fibers, glass fibers, aramid fibers, and polyethylene fibers when forming resin moldings.
  • the resin composition of the present disclosure is obtained, for example, by mixing the hollow particles of the present disclosure, a matrix resin, and additives, solvents, etc. added as necessary.
  • the matrix resin in the resin composition of the present disclosure is a thermoplastic resin
  • the hollow particles of the present disclosure and, if necessary, additives are added to the molten thermoplastic resin and melted. You may mix by kneading.
  • the method for producing the resin molded product of the present disclosure is not particularly limited, and for example, a liquid resin composition containing hollow particles or the like in a liquid matrix resin before curing reaction, or dissolving or dissolving each component in a solvent.
  • a resin molding can be obtained by applying the dispersed liquid resin composition to a support, and drying and curing as necessary.
  • the material of the support include resins such as polyethylene terephthalate and polyethylene naphthalate; and metals such as copper, aluminum, nickel, chromium, gold and silver. These supports may be coated with a release agent on the surface.
  • a method for applying the liquid resin composition a known method can be used, and examples thereof include dip coating, roll coating, curtain coating, die coating, slit coating, gravure coating and the like.
  • a resin molding can be obtained by impregnating a base material with a liquid resin composition, and drying and curing the base material, if necessary.
  • the base material include inorganic fibers such as carbon fiber, glass fiber, metal fiber and ceramic fiber, and organic synthetic fibers such as polyamide fiber, polyester fiber, polyolefin fiber and novoloid fiber. Among them, glass fiber (glass cloth) is preferable.
  • the form of the substrate is not limited, and a woven fabric, a non-woven fabric, or the like can be used.
  • the drying temperature is preferably a temperature at which the matrix resin is not cured, and is usually 20° C. or higher and 200° C. or lower, preferably 30° C. or higher and 150° C. or lower.
  • the drying time is usually 30 seconds or more and 1 hour or less, preferably 1 minute or more and 30 minutes or less.
  • the curing reaction of the resin composition is carried out according to the type of matrix resin, and is not particularly limited. When a matrix resin that is cured by heating is included, the heating temperature for the curing reaction is appropriately adjusted according to the type of resin, and is not particularly limited, but is usually 30° C. or higher and 400° C.
  • the curing time is 5 minutes or more and 5 hours or less, preferably 30 minutes or more and 3 hours or less.
  • the heating method is not particularly limited, and may be performed using, for example, an electric oven.
  • the liquid matrix resin before the curing reaction and the matrix resin dissolved or dispersed in the solvent may be a thermosetting resin or a thermoplastic resin.
  • a liquid resin composition containing a thermoplastic resin as a matrix resin and formed by melting the resin is molded into a desired shape by a known molding method such as extrusion molding, injection molding, press molding, or compression molding. may obtain the resin molding of the present disclosure.
  • the temperature during melt-kneading is not particularly limited as long as it is a temperature at which the thermoplastic resin to be used can be melted.
  • the kneading can be performed by a known method, and is not particularly limited, but can be performed using a kneading device such as a single-screw kneader or a twin-screw kneader.
  • the resin molding of the present disclosure includes hollow particles of the present disclosure and a matrix resin.
  • the matrix resin contained in the resin molding is a solidified product.
  • the matrix resin which is a solidified product, is a resin that has been solidified with or without undergoing a chemical reaction. Examples thereof include resins that have been cured by a curing reaction, resins that have been solidified by drying, and thermoplastic resins that have been solidified by cooling. .
  • a molded article obtained using the resin composition described above contains, as a matrix resin, a cured resin cured using a curing agent, a polymerization initiator, a catalyst, or the like, if necessary. In this case, the matrix resin may contain a curing agent or the like.
  • a molded body obtained by melt-kneading the hollow particles of the present disclosure and a thermoplastic resin and molding the mixture contains, as a matrix resin, a solidified product obtained by cooling and solidifying the thermoplastic resin.
  • the resin molding of the present disclosure has excellent dielectric properties due to the inclusion of the hollow particles of the present disclosure.
  • the resin molding of the present disclosure preferably has a dielectric loss tangent at a frequency of 10 GHz of 1.50 ⁇ 10 ⁇ 2 or less, more preferably 1.00 ⁇ 10 ⁇ 2 or less, still more preferably 9.50 ⁇ 10 ⁇ 3 or less, More preferably, it is 9.00 ⁇ 10 ⁇ 3 or less, and the lower limit is not particularly limited, and may be, for example, 1.00 ⁇ 10 ⁇ 4 or more.
  • the resin molding of the present disclosure preferably has a dielectric constant of 2.50 or less, more preferably 2.40 or less, and still more preferably 2.30 or less at a frequency of 10 GHz, and the lower limit is not particularly limited. It may be 1.00 or more.
  • the dielectric constant and dielectric loss tangent of the resin molding are measured using a perturbation-type measuring device under the condition of a measurement frequency of 10 GHz.
  • the shape of the resin molded article of the present disclosure is not particularly limited, and can be various moldable shapes, such as sheet-like, film-like, plate-like, tube-like, and other various three-dimensional shapes. It can be of any shape.
  • the fibers in the resin molding may be in the form of a non-woven fabric.
  • the resin molding may be a molding of a resin composition in which the hollow particles of the present disclosure are added to the fiber-reinforced plastic containing the resin and fibers as described above.
  • Examples of applications of the resin composition and resin molded article of the present disclosure include, among the applications of the hollow particles of the present disclosure described above, applications in which the resin composition or resin molded article can be used.
  • Example 1 (1) Mixed Solution Preparation Step First, the following materials were mixed to form an oil phase. Divinylbenzene 37.5 parts Ethylvinylbenzene 1.6 parts t-butyl peroxydiethyl acetate (10-hour half-life temperature: 75°C) 0.89 parts Hydrophobic solvent: heptane (solubility in water at 20°C: 2.2 mg /L, boiling point 98.4° C.) 60.8 parts Next, in a stirring vessel, 55 parts of ion-exchanged water was added to an aqueous solution prepared by dissolving 15.7 parts of magnesium chloride (water-soluble polyvalent metal salt) in 225 parts of ion-exchanged water.
  • magnesium chloride water-soluble polyvalent metal salt
  • aqueous solution in which 11.0 parts of sodium hydroxide (alkali metal hydroxide) was dissolved in parts was gradually added with stirring to obtain a colloidal magnesium hydroxide (poorly water-soluble metal hydroxide colloid) dispersion (magnesium hydroxide 8 parts) was prepared and used as the aqueous phase.
  • a mixture was prepared by mixing the obtained aqueous phase and oil phase.
  • Solvent removal step The precursor particles obtained in the solid-liquid separation step are heat-treated in a vacuum dryer under vacuum conditions at 200°C for 12 hours to remove the hydrophobic solvent contained in the particles. was removed to obtain hollow particles of Example 1. The obtained hollow particles were confirmed to be spherical and to have a hollow portion from the results of scanning electron microscope observation and porosity values.
  • Example 2 In Example 1, octane (solubility in water at 20 ° C.: 0.7 mg / L, boiling point 125.6 ° C.) was used as the hydrophobic solvent in place of heptane in the above "(1) mixed solution preparation step", Furthermore, hollow particles of Example 2 were produced in the same procedure as in Example 1, except that the polymerization temperature was changed as shown in Table 1 in the above "(3) Polymerization step”.
  • Example 3 In Example 1, t-butyl peroxypivalate (10-hour half-life temperature: 55° C.) was used as the polymerization initiator in place of t-butyl peroxydiethyl acetate in the above “(1) mixture preparation step”. The amount of magnesium chloride and sodium hydroxide used in the preparation of the aqueous phase was changed as shown in Table 1, and the polymerization temperature was changed as shown in Table 1 in the above "(3) Polymerization step”. Hollow particles of Example 3 were produced in the same procedure as in Example 1, except for the above.
  • Example 4 In Example 1, the amount of divinylbenzene added was changed to 24.6 parts and the amount of ethylvinylbenzene added was changed to 14.5 parts in the above "(1) mixed solution preparation step", and furthermore, in the preparation of the aqueous phase, Hollow particles of Example 4 were produced in the same procedure as in Example 1, except that the amounts of magnesium chloride and sodium hydroxide used were changed as shown in Table 1.
  • Example 5 In Example 1, the amount of divinylbenzene added was changed to 35.6 parts, the amount of ethylvinylbenzene added was changed to 1.5 parts, and ethylene glycol dimethacrylate was added to the oil phase in the above "(1) mixed liquid preparation step". 2.0 parts were added, and the amounts of magnesium chloride and sodium hydroxide used to prepare the aqueous phase were changed as shown in Table 1. Hollow particles were produced.
  • Example 6 In Example 1, the amount of divinylbenzene added was changed to 22.3 parts and the amount of ethylvinylbenzene added was changed to 15.6 parts in the above "(1) mixture preparation step", and furthermore, in the preparation of the aqueous phase, Hollow particles of Example 6 were produced in the same manner as in Example 1, except that the amounts of magnesium chloride and sodium hydroxide used were changed as shown in Table 1.
  • Example 7 In Example 1, the amount of divinylbenzene added was changed to 31.6 parts, the amount of ethylvinylbenzene added was changed to 1.3 parts, and t-butyl Using 0.75 parts of peroxydiethyl acetate and 1.07 parts of t-butyl peroxypivalate, changing the amount of heptane to 67.1 parts, and magnesium chloride and sodium hydroxide used to prepare the aqueous phase Hollow particles of Example 7 were produced in the same procedure as in Example 1, except that the amount of was changed as shown in Table 1.
  • Example 8 In Example 1, the amounts of magnesium chloride and sodium hydroxide used in the preparation of the aqueous phase in the above "(1) mixture preparation step” were changed as shown in Table 1, and the above “(3) polymerization step” was changed. , the polymerization temperature is changed as shown in Table 1, and a nonionic surfactant is added during reslurrying in "(4) Washing step and solid-liquid separation step” to eliminate aggregation of particles. Hollow particles of Example 8 were produced in the same procedure as in Example 1, except that the number of water washing treatments was further increased.
  • Example 1 In Example 1, the above “(1) mixture preparation step” was changed as follows, and in the above "(3) polymerization step", the polymerization temperature was changed as shown in Table 2. Hollow particles of Comparative Example 1 were produced in the same procedure as in Example 1. The mixed liquid preparation process of Comparative Example 1 was performed as follows. First, the following materials were mixed to form an oil phase.
  • Ethylene glycol dimethacrylate 31.85 parts Trimethylolpropane triacrylate 13.65 parts 2,2′-azobis(2,4-dimethylvaleronitrile) (10-hour half-life temperature: 51° C.) 1.04 parts
  • an aqueous solution prepared by dissolving 23.5 parts of magnesium chloride (water-soluble polyvalent metal salt) in 225 parts of ion-exchanged water is added to 55 parts of ion-exchanged water to add sodium hydroxide (hydroxide Alkali metal) 16.5 parts of the aqueous solution is gradually added with stirring to prepare a magnesium hydroxide colloid (poorly water-soluble metal hydroxide colloid) dispersion (magnesium hydroxide 12 parts).
  • a mixture was prepared by mixing the obtained aqueous phase and oil phase.
  • the oil phase was added to the aqueous phase, and a suspension was prepared using an ultrasonic homogenizer. Polymerization was performed by heating the obtained suspension at 70° C. for 4 hours to obtain a slurry. Hollow particles of Comparative Example 2 were produced by heating the obtained slurry at 100° C. for 24 hours.
  • the resulting suspension was heated to 70° C. in a nitrogen atmosphere and stirred for 24 hours at 70° C. to carry out a polymerization reaction.
  • a slurry in which the precursor particles containing the hydrophobic solvent were dispersed in water was obtained.
  • the resulting slurry was filtered using filter paper to isolate the precursor particles encapsulating the hydrophobic solvent.
  • the hydrophobic solvent contained in the particles was removed by drying the precursor particles under the conditions of a temperature of about 70° C. and a pressure of about 100000 Pa (atmospheric pressure) to produce hollow particles of Comparative Example 3.
  • volume average particle size (Dv) and number average particle size (Dn), and calculation of particle size distribution (Dv/Dn) Using a particle size distribution analyzer (manufactured by Beckman Coulter, product name: Multisizer 4e) The volume average particle size (Dv) and number average particle size (Dn) of the hollow particles were measured to calculate the particle size distribution (Dv/Dn).
  • the measurement conditions were as follows: aperture diameter: 50 ⁇ m, dispersion medium: Isoton II (product name), concentration: 10%, number of measured particles: 100,000.
  • a particle sample was placed in a beaker, and an aqueous surfactant solution (manufactured by FUJIFILM Corporation, product name: Drywell) was added therein as a dispersant.
  • an aqueous surfactant solution manufactured by FUJIFILM Corporation, product name: Drywell
  • 2 ml of a dispersing medium was further added thereto to wet the particles, and then 10 ml of a dispersing medium was added, dispersed for 1 minute with an ultrasonic disperser, and then measured with the particle size distribution analyzer.
  • the polymer contained in the hollow particles was measured by placing 0.1 g of the hollow particles on the top of the cell and tightening a bearing for compression from above to bring the crystals and the hollow particles into contact with each other. From the obtained infrared absorption spectrum, the residual double bond ratio was calculated by the method described above. For example, in Example 5, the residual double bond rate was calculated as follows. In Example 5, 35.6 parts of divinylbenzene, 1.5 parts of ethylvinylbenzene, and 2.0 parts of ethylene glycol dimethacrylate were used as polymerizable monomers.
  • a peak derived from the CH bond of the benzene ring contained in divinylbenzene was specified as a reference peak.
  • the peak intensity of the reference peak is A value obtained by dividing the total (0.95) of the content of benzene and the content of ethylvinylbenzene was used as the reference peak intensity.
  • the standard peak intensity determined from the infrared absorption spectrum of the polymerizable monomer before polymerization reaction was 0.167, and the standard peak intensity determined from the infrared absorption spectrum of the polymer was 0.0760.
  • the peak intensity (M 1 ) was 0.0724 / 0.167 and calculated to be 0.434.
  • a polyimide film containing the particles was formed on aluminum foil.
  • a laminate of the film and aluminum foil was immersed in a 1N hydrochloric acid aqueous solution overnight to remove the aluminum foil and obtain only the film.
  • the resulting film was washed with deionized water and dried to obtain a polyimide film containing hollow particles.
  • Tables 1 and 2 show the amount of each material added (parts by mass) and the results of each measurement or evaluation.
  • exponential notation defined in JIS X 0210 is used for the values of the dielectric loss tangent.
  • "2.41 ⁇ 10 ⁇ 3 " is written as "2.41E-03".
  • Abbreviations in Tables 1 and 2 have the following meanings.
  • EGDMA ethylene glycol dimethacrylate
  • TMPT trimethylolpropane triacrylate
  • St styrene 50PEP-300: polyethylene glycol propylene glycol monomethacrylate (manufactured by NOF Corporation, product name: Blemmer (registered trademark) 50PEP-300)
  • HS4100 side chain crystalline polyolefin (manufactured by Toyokuni Oil Co., Ltd., product name: HS Crysta 4100)
  • PVA polyvinyl alcohol A-80: anionic surfactant, sulfosuccinic acid diester salt (manufactured by NOF Corporation, product name: RAPISOL A-80)
  • the hollow particles obtained in Comparative Example 1 were formed using an acrylic monomer, and were inferior in dielectric properties, and were also inferior in the effect of lowering the dielectric constant and dielectric loss tangent of the polyimide film.
  • Comparative Example 1 had poor dielectric properties of the shell and poor dielectric properties of the particles as a whole because the polymer in the shell did not contain a hydrocarbon monomer unit.
  • Comparative Example 2 corresponds to Example 1 of Patent Document 1, and the obtained hollow particles were inferior in dielectric properties, and were also inferior in the effect of reducing the dielectric constant and dielectric loss tangent of the polyimide film.
  • the hollow particles obtained in Comparative Example 2 had poor dielectric properties of the shell due to the small amount of hydrocarbon monomer units contained in the polymer in the shell. It is considered that the dielectric properties of the particles as a whole were inferior because of the deterioration.
  • the hollow particles obtained in Comparative Example 3 have a high residual double bond rate of the polymer contained in the shell, are inferior in dielectric properties, and are inferior in the effect of lowering the dielectric constant and dielectric loss tangent of the polyimide film.
  • the hollow particles obtained in Comparative Example 3 had a surfactant (PVA) content of 3000 ppm on the particle surface.
  • the polymer contained in the shell had a high residual double bond rate, so the dielectric properties of the shell were inferior, and PVA used in the production process remained on the particle surface. It is presumed that the dielectric properties of the hollow particles deteriorated also because of this.
  • the high residual double bond ratio of the hollow particles obtained in Comparative Example 3 is presumed to be due to the low polymerization temperature.
  • the hollow particles obtained in each example are spherical hollow particles having a hollow portion, the porosity is 50% or more, the shell is a resin, and the hydrocarbon monomer unit is 91 mass. % or more and 50% by mass or more of crosslinkable monomer units, the residual double bond rate of the polymer is 30.0% or less, and the dielectric loss tangent at a frequency of 10 GHz is 3.00 ⁇
  • the hollow particles had a low dielectric property of 10 ⁇ 3 or less and excellent dielectric properties.
  • the reason why the hollow particles obtained in each example had excellent dielectric properties even at a frequency of 10 GHz is that the polymer serving as the skeleton of the shell contains a large amount of hydrocarbons, and the residual double bond rate of the polymer is This is presumed to be due to the low molecular mobility of the shell and the sufficiently high porosity.
  • the residual amount of decomposition products of the polymerization initiator was small, the surfactant was not present on the particle surface, and the metal content was low. contributed to Since the hollow particles obtained in each example were obtained without using a surfactant, no surfactant was detected on the particle surface.
  • the hollow particles obtained in each example were also excellent in the effect of lowering the dielectric constant and the dielectric loss tangent of the polyimide film.
  • the dielectric properties of the hollow particles obtained in Examples 1-4 were superior to those obtained in Examples 5-6 because the polymer serving as the skeleton of the shell contained hydrocarbon monomers. It is presumed that the content of components other than the polymer in the shell was particularly low because the content of the polymer units was particularly high and the impurities contained in the raw materials were low. It is presumed that the hollow particles obtained in Example 7 have particularly excellent dielectric properties because of their high porosity.
  • the low dielectric loss tangent of the hollow particles obtained in Example 8 is presumed to be due to the fact that more impurities were removed in the washing step, thereby suppressing an increase in the dielectric loss tangent due to moisture absorption of the impurities.
  • the ratio of particles having a circularity of 0.85 or less was 7% by mass or less in any of the examples. and the ratio of particles having only one or two hollow portions was 95% by mass or more.

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WO2024048093A1 (ja) * 2022-08-30 2024-03-07 日本ゼオン株式会社 中空粒子、樹脂組成物、及び成形体
WO2024095851A1 (ja) * 2022-10-31 2024-05-10 日本ゼオン株式会社 中空粒子、中空粒子の製造方法、樹脂組成物及び樹脂構造体
WO2024122426A1 (ja) * 2022-12-06 2024-06-13 日本ゼオン株式会社 樹脂組成物、プリプレグ、金属箔張積層板、及びプリント基板
WO2025033521A1 (ja) * 2023-08-10 2025-02-13 積水化成品工業株式会社 中空樹脂粒子、その製造方法、およびその用途
WO2025135137A1 (ja) * 2023-12-21 2025-06-26 積水化成品工業株式会社 中空樹脂粒子、その製造方法、およびその用途
WO2026063344A1 (ja) * 2024-09-20 2026-03-26 Jsr株式会社 多孔質粒子の製造方法及び精製又は吸着用担体の製造方法

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WO2025135137A1 (ja) * 2023-12-21 2025-06-26 積水化成品工業株式会社 中空樹脂粒子、その製造方法、およびその用途
WO2026063344A1 (ja) * 2024-09-20 2026-03-26 Jsr株式会社 多孔質粒子の製造方法及び精製又は吸着用担体の製造方法

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