Particles and their uses

Particles with a polymer shell containing specific monomers enhance flame retardant retention and stability, addressing the bleed-out issue in resin compositions, ensuring long-term flame retardancy and mechanical stability.

JP7745384B2Active Publication Date: 2025-09-29MATSUMOTO YUSHI SEIYAKU CO LTD
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Patent Information

Application Number
JP2021138700
Authority / Receiving Office
JP · JP
Patent Type
Patents
Current Assignee / Owner
Filing Date
2021-08-27
Publication Date
2025-09-29
Estimated Expiration
2041-08-27

AI Technical Summary

Technical Problem

Existing microcapsules containing flame retardants suffer from poor retention and bleed-out over time, leading to a deterioration in mechanical and thermal properties of resin compositions.

Method used

Particles comprising a polymer shell containing specific monomers with carboxyl groups and multiple polymerizable carbon-carbon double bonds encapsulate the flame retardant, providing high retention and stability.

Benefits of technology

The particles effectively suppress flame retardant bleed-out, maintaining excellent flame retardancy and stability over time, allowing for the production of molded articles with enhanced properties.

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Abstract

To provide a particle that can sufficiently hold a flame retardant incorporated therein, and is well stable over time.SOLUTION: A particle contains a polymer-containing outer shell, and a flame retardant incorporated therein. The polymer is a polymer of a polymerizable component containing the following monomer (A) and the following monomer (B). The monomer (A) contains a carboxyl group-containing monomer (a1). The monomer (A) is a monomer having one polymerizable carbon-carbon double bond. The monomer (B) is a monomer having at least two polymerizable carbon-carbon double bonds.SELECTED DRAWING: Figure 1
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Description

[Technical Field]

[0001] The present invention relates to particles and uses thereof. [Background technology]

[0002] In general, in order to impart heat resistance to a resin composition, a method of blending a flame-retardant compound such as an organic halogen compound or an organic phosphorus compound into the component is widely adopted. However, the flame retardants described above corrode surrounding metal materials or emit a strong, irritating odor due to the decomposition gases generated by heating. Furthermore, the flame retardants plasticize the resin material, resulting in problems such as a deterioration in the mechanical and thermal properties of the component. Furthermore, to prevent the flame retardant from bleed-out onto the surface of the component over time, a large amount of flame retardant must be added. In order to solve such problems in making resin compositions flame retardant, it has been considered to introduce a monomer consisting of a halogen compound or a phosphorus compound as a copolymer component and incorporate it into the resin composition when producing the resin composition. However, in order to impart sufficient flame retardancy to the resulting resin composition, it is necessary to add a large amount of the above-mentioned flame-retardant copolymer component to the resin composition, and as a result, the desirable properties that the component originally possesses may be lost. In order to solve such problems, a method has been proposed in which particles containing a flame retardant are blended to make the member flame-retardant.

[0003] For example, Patent Documents 1 and 2 exemplify microcapsules containing a flame retardant, which are prepared by dissolving a flame retardant in a monomer such as acrylonitrile or methyl methacrylate and then subjecting the resulting solution to suspension polymerization. Furthermore, Patent Document 3 exemplifies microcapsules containing a flame retardant, which are produced by uniformly mixing a flame retardant with gelatin or an aqueous solution of gelatin and gum arabic, then adjusting the pH to acidic and cooling. Furthermore, Patent Document 4 exemplifies a microencapsulated flame retardant in which a flame retardant is encapsulated by dissolving a polyvalent isocyanate in a flame retardant that is liquid at room temperature, dispersing the oil phase thus obtained in an aqueous phase as oil droplets, and then adding and dissolving a polyvalent amine in the aqueous phase of this emulsion, thereby causing a polyaddition reaction between the polyvalent isocyanate and the polyvalent amine at the interface between the aqueous phase and the oil phase, or by heating the emulsion, causing a polyaddition reaction between the polyvalent isocyanate and water at the interface between the aqueous phase and the oil layer. Patent Document 5 also cites an example of microcapsules containing a flame retardant, which are produced by dispersing a finely powdered flame retardant in water and then adding dropwise melamine-formaldehyde resin or a modified resin thereof while maintaining the pH at 3 to 7. [Prior art documents] [Patent documents]

[0004] [Patent Document 1] Japanese Patent Application Publication No. 55-118988 [Patent Document 2] Japanese Patent Application Publication No. 55-122075 [Patent Document 3] Japanese Patent Application Laid-Open No. 61-179241 [Patent Document 4] Japanese Patent Application Publication No. 7-26153 [Patent Document 5] Japanese Patent Application Publication No. 52-119653 Summary of the Invention [Problem to be solved by the invention]

[0005] However, it has been confirmed that the microcapsules exemplified in the above Patent Documents 1 to 5 do not have sufficient ability to retain the encapsulated flame retardant, and the encapsulated flame retardant bleeds out over time. An object of the present invention is to provide particles that have excellent retention of the flame retardant contained therein and excellent stability over time. [Means for solving the problem]

[0006] As a result of extensive research, the inventors discovered that particles comprising an outer shell containing a polymer of a polymerizable component containing a specific monomer and a flame retardant encapsulated therein have high flame retardant retention, suppress bleed-out of the flame retardant over time, and have excellent stability over time, thereby arriving at the present invention.

[0007] That is, the present invention relates to particles comprising an outer shell containing a polymer and a flame retardant encapsulated therein, wherein the polymer is a polymer of a polymerizable component containing the following monomer (A) and the following monomer (B), and the monomer (A) contains a carboxyl group-containing monomer (a1). Monomer (A): A monomer having one polymerizable carbon-carbon double bond Monomer (B): A monomer having at least two polymerizable carbon-carbon double bonds

[0008] The particles of the present invention preferably satisfy at least one of the following requirements 1) to 3). 1) The weight ratio of the monomer (A) to the polymerizable component is 50 to 99.99% by weight, and the weight ratio of the monomer (B) to the polymerizable component is 0.01 to 50% by weight. 2) The monomer (A) further contains the following monomer (a2): Monomer (a2): at least one selected from nitrile-based monomers, (meth)acrylic acid ester-based monomers, monomers having a group reactive with a carboxyl group, and styrene-based monomers 3) The flame retardant contains at least one selected from an organic phosphorus compound, an organic halogen compound, and an inorganic compound.

[0009] The composition of the present invention comprises the above particles and a substrate component. The molded article of the present invention is obtained by molding the above composition. [Effects of the Invention]

[0010] The particles of the present invention have a high flame retardant retention capacity, do not bleed out of the flame retardant over time, and are excellent in stability over time. Since the composition of the present invention contains the above particles, there is no bleed-out of the flame retardant over time, and a molded article having excellent flame retardancy can be obtained. The molded article of the present invention has excellent stability over time and excellent flame retardancy. [Brief explanation of the drawings]

[0011] [Figure 1] FIG. 1 is a schematic diagram illustrating an example of a particle. DETAILED DESCRIPTION OF THE INVENTION

[0012] The particles of the present invention comprise a polymer-containing shell and a flame retardant encapsulated in the shell, and can be imparted with flame retardancy. The particles of the present invention themselves also have flame retardancy. The particles of the present invention will be described in detail below.

[0013] 〔particle〕 In order to further enhance the effect of suppressing bleed-out of the flame retardant, the particles of the present invention preferably have a structure with one or more independent pores inside, and particles containing a flame retardant in the pores are preferred. In particular, as shown in Figure 1, particles having a core-shell structure containing a polymer-containing outer shell (shell) 1 and a flame retardant (core) 2 encapsulated therein are preferred, as they provide a high bleed-out suppression effect. Furthermore, it is preferred that the outer shell has a structure that is continuous with the polymer that forms it.

[0014] In the particles of the present invention, the polymer forming the outer shell is a polymer of polymerizable components containing the following monomer (A) and the following monomer (B), and the monomer (A) contains a carboxyl group-containing monomer (a1). Monomer (A): A monomer having one polymerizable carbon-carbon double bond Monomer (B): A monomer having at least two polymerizable carbon-carbon double bonds

[0015] The polymer forming the outer shell is a polymer of polymerizable components containing monomer (A) and monomer (B), which essentially contain carboxyl group-containing monomer (a1), and this adjusts the polarity of the outer shell, further improving the density and mechanical strength, and suppressing the seepage of a large amount of flame retardant and the leakage of flame retardant due to crushing or denting of particles, which is thought to result in excellent long-term stability.

[0016] The monomer (A) is a monomer having one (radically) polymerizable carbon-carbon double bond, and essentially contains a carboxyl group-containing monomer (a1). The monomer (a1) is not particularly limited as long as it has one or more free carboxyl groups per molecule. Examples include unsaturated monocarboxylic acids such as acrylic acid, methacrylic acid, ethacrylic acid, crotonic acid, and cinnamic acid; unsaturated dicarboxylic acids such as maleic acid, itaconic acid, and fumaric acid; anhydrides of unsaturated dicarboxylic acids; and unsaturated dicarboxylic acid monoesters such as monomethyl maleate, monoethyl maleate, monobutyl maleate, monomethyl fumarate, monoethyl fumarate, monomethyl itaconate, monoethyl itaconate, and monobutyl itaconate. Some or all of the carboxyl groups in the monomer (a1) may be neutralized during or after polymerization. These monomers (a1) may be used alone or in combination.

[0017] The weight proportion of the monomer (a1) in the monomer (A) is not particularly limited, but is preferably 5% by weight or more. When the weight proportion is 5% by weight or more, the polarity of the outer shell can be efficiently adjusted, and strength tends to be further improved. In addition, the heat resistance and solvent resistance of the particles also tend to be improved. The upper limit of the weight proportion is preferably 100% by weight, more preferably 90% by weight, even more preferably 80% by weight, particularly preferably 75% by weight, and most preferably 70% by weight. On the other hand, the lower limit of the weight proportion is more preferably 10% by weight, even more preferably 15% by weight, particularly preferably 20% by weight, and most preferably 25% by weight.

[0018] It is preferable that the monomer (A) contains the following monomer (a2) in addition to the monomer (a1) in terms of achieving the effects of the present invention. Monomer (a2): at least one selected from nitrile-based monomers, (meth)acrylic acid ester-based monomers, monomers having a group reactive with a carboxyl group, and styrene-based monomers

[0019] Examples of the nitrile monomer include acrylonitrile, methacrylonitrile, α-chloroacrylonitrile, α-ethoxyacrylonitrile, fumaronitrile, etc. These nitrile monomers may be used alone or in combination of two or more. Examples of (meth)acrylic acid ester-based monomers include methyl (meth)acrylate, ethyl (meth)acrylate, n-butyl (meth)acrylate, isobutyl (meth)acrylate, t-butyl (meth)acrylate, propyl (meth)acrylate, n-octyl (meth)acrylate, dodecyl (meth)acrylate, 2-ethylhexyl (meth)acrylate, stearyl (meth)acrylate, 2-chloroethyl (meth)acrylate, phenyl (meth)acrylate, isobornyl (meth)acrylate, cyclohexyl (meth)acrylate, and benzyl (meth)acrylate. In the present invention, the term "(meth)acrylate" refers to either acrylate or methacrylate. Furthermore, in the present invention, the (meth)acrylic acid ester-based monomer also refers to a compound that does not have a group reactive with a carboxyl group. These (meth)acrylic acid ester-based monomers may be used alone or in combination of two or more.

[0020] The monomer having a group reactive with a carboxyl group is not particularly limited, but examples thereof include monomers having a hydroxyl group, an amino group, an epoxy group, an isocyanate group, an aldehyde group, an azo group, a nitro group, a nitroso group, a thiol group, a sulfonic acid group, a phosphate group, etc. Examples of monomers having a group reactive with a carboxyl group include (meth)acrylamide-based monomers such as N-methylol(meth)acrylamide, (meth)acrylamide, hydroxymethylacrylamide, hydroxyethylacrylamide, acetoneacrylamide, N-ethyl(meth)acrylamide, N-propyl(meth)acrylamide, N-hexyl(meth)acrylamide, N-cyclohexyl(meth)acrylamide, N-hydroxyethyl(meth)acrylamide, 2-acetamidoacrylic acid, N-phenyl(meth)acrylamide, N-nitrophenyl(meth)acrylamide, and diacetoneacrylamide; aldehyde-based monomers such as acrolein; and vinyl Examples of suitable monomers include sulfonic acid monomers such as sulfonic acid and Nt-butylacrylamidosulfonic acid; phosphoric acid monomers such as vinylphosphonic acid; N,N-dimethylaminoethyl (meth)acrylate; vinyl glycidyl ether; propenyl glycidyl ether; glycidyl (meth)acrylate; glycerin mono(meth)acrylate; 4-hydroxybutyl acrylate glycidyl ether; 2-hydroxyethyl (meth)acrylate; 2-hydroxypropyl (meth)acrylate; 2-hydroxybutyl (meth)acrylate; 4-hydroxybutyl (meth)acrylate; 2-hydroxy-3-phenoxypropyl (meth)acrylate; and p-hydroxystyrene. In the present invention, the term "(meth)acrylic" refers to either acrylic or methacrylic. These monomers having a group reactive with a carboxyl group may be used alone or in combination of two or more.

[0021] Examples of styrene-based monomers include styrene, α-methylstyrene, vinyltoluene, t-butylstyrene, p-nitrostyrene, chloromethylstyrene, etc. These styrene-based monomers may be used alone or in combination of two or more.

[0022] When the monomer (A) further contains a monomer (a2), the weight proportion of the monomer (a2) in the monomer (A) is not particularly limited, but is preferably 5 to 95% by weight. A weight proportion of 5% by weight or more tends to provide sufficient flexibility and prevent the outer shell from breaking during processing, while a weight proportion of 95% by weight or less tends to provide sufficient heat resistance and solvent resistance. The upper limit of the weight proportion is more preferably 90% by weight, even more preferably 85% by weight, particularly preferably 80% by weight, and most preferably 75% by weight. The lower limit of the weight proportion is more preferably 10% by weight, even more preferably 15% by weight, and particularly preferably 20% by weight.

[0023] The monomer (A) may contain, in addition to the monomer (a1), a monomer other than the monomer (a2). Examples of monomers other than the monomer (a2) include vinyl ester-based monomers such as vinyl acetate, vinyl propionate, and vinyl butyrate; halogenated vinyl-based monomers such as vinylidene chloride, vinyl chloride, vinyl bromide, and vinyl fluoride; maleimide-based monomers such as N-phenylmaleimide and N-cyclohexylmaleimide; unsaturated monoolefin-based monomers such as ethylene, propylene, butylene, and isobutylene; vinyl ether-based monomers such as vinyl methyl ether, vinyl ethyl ether, vinyl propyl ether, vinyl isopropyl ether, vinyl butyl ether, vinyl isobutyl ether, vinyl-2-ethylhexyl ether, vinyl cyclohexyl ether, and vinyl-4-hydroxybutyl ether; vinyl ketone-based monomers such as vinyl methyl ketone, vinyl hexyl ketone, and methyl isopropenyl ketone; N-vinyl-based monomers such as N-vinylpyrrole, N-vinylcarbazole, N-vinylindole, and N-vinylpyrrolidone; and vinyl naphthalene salts.

[0024] The weight percentage of the monomer (A) in the polymerizable components is not particularly limited, but is preferably 50 to 99.99% by weight. A weight percentage of 50% by weight or more tends to improve the strength of the outer shell, while a weight percentage of 99.99% by weight or less tends to improve the density of the outer shell. The upper limit of the weight percentage is more preferably 99.9% by weight, even more preferably 99.7% by weight, particularly preferably 99.5% by weight, and most preferably 99% by weight. The lower limit of the weight percentage of the monomer (A) is more preferably (1) 60% by weight, (2) 70% by weight, (3) 80% by weight, (4) 85% by weight, (5) 90% by weight, and (6) 93% by weight (the larger the number in parentheses, the more preferable it is).

[0025] It is preferable from the viewpoint of solvent resistance that the monomer (A) contains a nitrile monomer in addition to the monomer (a1). When the monomer (A) contains a nitrile monomer, the weight ratio of the nitrile monomer to the total weight of the monomer (a1) and the nitrile monomer is preferably 5 to 95% by weight. The upper limit of this weight ratio is more preferably 90% by weight, even more preferably 85% by weight, particularly preferably 80% by weight, and most preferably 75% by weight. On the other hand, the lower limit of this weight ratio is more preferably 10% by weight, even more preferably 15% by weight, particularly preferably 20% by weight, and most preferably 25% by weight.

[0026] Monomer (B) is a monomer with at least two (radical) polymerizable carbon-carbon double bonds, which introduces a cross-linked structure into the resulting polymer, improving the density of the outer shell and preventing leakage of the encapsulated flame retardant. Examples of the monomer (B) include ethylene glycol di(meth)acrylate, diethylene glycol di(meth)acrylate, triethylene glycol di(meth)acrylate, propylene glycol di(meth)acrylate, 1,3-butylene glycol di(meth)acrylate, 1,4-butanediol di(meth)acrylate, 1,6-hexanediol di(meth)acrylate, 1,9-nonanediol di(meth)acrylate, 1,10-decanediol di(meth)acrylate, trimethylolpropane di(meth)acrylate, PEG#200 di(meth)acrylate, PEG#400 di(meth)acrylate, PEG#600 di(meth)acrylate, PEG#1000 di(meth)acrylate, dipropylene glycol ... Examples of suitable monomers (B) include di(meth)acrylates such as propylene glycol di(meth)acrylate, polypropylene glycol #400 di(meth)acrylate, polypropylene glycol #700 di(meth)acrylate, polytetramethylene glycol di(meth)acrylate, polytetramethylene glycol #650 di(meth)acrylate, ethoxylated polypropylene glycol #700 di(meth)acrylate, and neopentyl glycol di(meth)acrylate; tri(meth)acrylates such as trimethylolpropane tri(meth)acrylate and pentaerythritol tri(meth)acrylate; aromatic divinyl compounds such as divinylbenzene and divinylnaphthalene; allyl methacrylate; triacrylformal; triallyl isocyanate; and butadiene. These monomers (B) may be used alone or in combination of two or more. In the present invention, a series of compounds expressed as "PEG#xxx di(meth)acrylate" means polyethylene glycol di(meth)acrylate, and the average molecular weight of the polyethylene glycol portion is xxx.

[0027] The weight percentage of the monomer (B) in the polymerizable component is not particularly limited, but is preferably 0.01 to 50% by weight. When the weight percentage is 0.01% by weight or more, the density of the outer shell tends to improve, while when the weight percentage is 50% by weight or less, the strength of the outer shell tends to improve. The upper limit of the weight percentage of the monomer (B) is preferably (1) 40% by weight, (2) 30% by weight, (3) 20% by weight, (4) 15% by weight, (5) 10% by weight, or (6) 7% by weight (the larger the number in parentheses, the more preferable it is). The lower limit of the weight percentage of the monomer (B) is more preferably 0.1% by weight, even more preferably 0.3% by weight, particularly preferably 0.5% by weight, and most preferably 1% by weight.

[0028] The weight ratio (a1 / B) of the monomer (a1) to the monomer (B) contained in the polymerizable component is not particularly limited, but is preferably 0.1 to 500. When this weight ratio is 0.1 or more, the polarity of the polymer forming the outer shell tends to be improved, and when this weight ratio is 500 or less, the strength of the particles tends to be improved. The upper limit of this weight ratio is more preferably 350, even more preferably 250, particularly preferably 200, and most preferably 150. On the other hand, the lower limit of this weight ratio is more preferably 0.5, even more preferably 1, particularly preferably 2, and most preferably 5.

[0029] In the particles of the present invention, the encapsulated flame retardant is a component that can impart flame retardancy when released from the particles. Examples of flame retardants include organic phosphorus compounds such as phosphate ester compounds such as bisphenol A bis(diphenyl phosphate), triphenyl phosphate, tricresyl phosphate, trixylenyl phosphate, cresylphenyl phosphate, trimethyl phosphate, triethyl phosphate, and tris(β-chloropropyl)phosphate, and phosphazene compounds such as aryloxycyclophosphazene; organic halogen compounds such as tetrabromobisphenol A (TBBA), decabromodiphenyl ether (deca-BDE), tribromophenol, hexabromocyclododecane (HBCD), ethylene bis(tetrabromophthalimide), brominated polyethylene, and chlorinated paraffin; melamine cyanurate; silicone; and inorganic compounds such as antimony trioxide, magnesium hydroxide, aluminum hydroxide, red phosphorus, and ammonium polyphosphate. These flame retardants may be used alone or in combination.

[0030] The flame retardant is not particularly limited, but preferably contains at least one selected from organic phosphorus compounds, organic halogen compounds, and inorganic compounds, since this can efficiently impart flame retardancy. The flame retardant may be in a liquid or solid state, and is preferably in a liquid state, since it can be efficiently encapsulated and released from the particles more efficiently.

[0031] The weight ratio of the flame retardant to the entire particle (hereinafter simply referred to as the encapsulation rate of the flame retardant) is not particularly limited, but is preferably 5 to 80% by weight. An encapsulation rate of the flame retardant of 5% by weight or more tends to provide sufficient flame retardancy. On the other hand, an encapsulation rate of the flame retardant of 80% by weight or less tends to suppress leakage of the flame retardant. The upper limit of the encapsulation rate is preferably (1) 75% by weight, (2) 70% by weight, (3) 65% by weight, (4) 60% by weight, (5) 55% by weight, and (6) 50% by weight (the larger the number in parentheses, the more preferable). On the other hand, the lower limit of the encapsulation rate is preferably (1) 10% by weight, (2) 13% by weight, (3) 15% by weight, (4) 18% by weight, and (5) 20% by weight (the larger the number in parentheses, the more preferable). The weight ratio of the flame retardant in the particles of the present invention means the value measured by the method described in the examples.

[0032] The average particle size of the particles of the present invention is not particularly limited, but is preferably 0.1 to 300 μm. When the average particle size is 0.1 μm or more, the shell has sufficient thickness, which tends to improve the encapsulation and retention of the flame retardant. On the other hand, when the average particle size is 300 μm or less, leakage of the flame retardant due to particle crushing or dents tends to be suppressed. The upper limit of the average particle size is preferably (1) 200 μm, (2) 150 μm, (3) 120 μm, (4) 100 μm, (5) 75 μm, (6) 60 μm, (7) 50 μm, and (8) 45 μm (the larger the number in parentheses, the more preferable). On the other hand, the lower limit of the average particle size is preferably (1) 0.5 μm, (2) 1 μm, (3) 3 μm, (4) 5 μm, and (5) 10 μm (the larger the number in parentheses, the more preferable). The average particle size of the particles of the present invention is measured by the method described in the examples.

[0033] The ratio (d1 / d2) of the inner diameter (d1) to the outer diameter (d2) of the particles of the present invention is not particularly limited, but is preferably 0.20 to 0.95. A ratio of 0.2 or more tends to provide sufficient flame retardancy, while a ratio of 0.95 or less tends to improve particle strength. The upper limit of this ratio is more preferably 0.93, even more preferably 0.90, particularly preferably 0.87, and most preferably 0.85. Meanwhile, the lower limit of this ratio is more preferably 0.25, even more preferably 0.30, particularly preferably 0.35, and most preferably 0.40. The ratio (d1 / d2) of the inner diameter (d1) to the outer diameter (d2) of the particles of the present invention is measured by the method described in the Examples.

[0034] The true specific gravity of the particles of the present invention is not particularly limited, but is preferably 0.70 to 2.5. Having the true specific gravity within the above range is preferable because it can more effectively suppress bleed-out of the flame retardant. The upper limit of the true specific gravity is more preferably 2.0, even more preferably 1.8, and particularly preferably 1.5. On the other hand, the lower limit of the true specific gravity is more preferably 0.80, even more preferably 0.90, and particularly preferably 1.0. The true specific gravity of the particles of the present invention is measured by the method described in the Examples.

[0035] [Method for producing particles] The method for producing the particles of the present invention is not particularly limited, but is preferably a method including a step of dispersing a polymerizable component containing a monomer (A) having one polymerizable carbon-carbon double bond and a carboxyl group-containing monomer (a1), a monomer (B) having at least two polymerizable carbon-carbon double bonds, and a flame retardant in an aqueous dispersion medium, and polymerizing the polymerizable component (polymerization step). The polymerization step is a step of dispersing an oily mixture containing the polymerizable component and the flame retardant in an aqueous dispersion medium, and polymerizing the polymerizable component.

[0036] (Polymerization process) In the polymerization step, the polymerizable components are preferably polymerized in the presence of a polymerization initiator, which is preferably contained in the oily mixture. Examples of the polymerization initiator include peroxides such as peroxydicarbonate, peroxyester, and diacyl peroxide; azo compounds such as azonitrile, azoester, azoamide, azoalkyl, and polymeric azo initiator; and redox initiators. These polymerization initiators may be used alone or in combination of two or more. The polymerization initiator is preferably an oil-soluble polymerization initiator that is soluble in the polymerizable component. The amount of the polymerization initiator used is not particularly limited, but is preferably 0.05 to 10 parts by weight, more preferably 0.1 to 8 parts by weight, and even more preferably 0.2 to 5 parts by weight, relative to 100 parts by weight of the polymerizable component.

[0037] The aqueous dispersion medium is prepared, for example, by blending water (ion-exchanged water) with a dispersion stabilizer, a dispersion stabilization aid, a polymerization aid, an electrolyte, etc., as required. In the method for producing the particles of the present invention, it is preferable to add a dispersion stabilizer to stabilize the droplets and control the particle size. The dispersion stabilizer is not particularly limited, but is preferably an organic dispersion stabilizer and / or an inorganic dispersion stabilizer. Examples of organic dispersion stabilizers include particulate stabilizers, water-soluble polymers, nanocellulose, etc. Examples of particulate stabilizers include those used in Pickering emulsions. Examples of water-soluble polymers include polyvinyl alcohol, methyl cellulose, hydroxyethyl methyl cellulose, hydroxypropyl methyl cellulose, polyacrylic acid, etc. Examples of inorganic dispersion stabilizers include clay minerals, tricalcium phosphate, magnesium pyrophosphate obtained by a metathesis method, calcium pyrophosphate, colloidal silica, alumina sol, magnesium hydroxide, and other inorganic compounds. These dispersion stabilizers may be used alone or in combination of two or more. The amount of the dispersion stabilizer used is preferably 0.05 to 100 parts by weight, more preferably 0.2 to 70 parts by weight, per 100 parts by weight of the oily mixture.

[0038] To control the stability and particle size of the droplets, a dispersion stabilization aid may be used in combination. Examples of the dispersion stabilization aid include polymer-type dispersion stabilization aids, and surfactants such as cationic surfactants, anionic surfactants, zwitterionic surfactants, and nonionic surfactants. These dispersion stabilization aids may be used alone or in combination of two or more.

[0039] The aqueous dispersion medium may contain an electrolyte. Examples of the electrolyte include sodium chloride, magnesium chloride, calcium chloride, sodium sulfate, magnesium sulfate, ammonium sulfate, sodium carbonate, etc. These electrolytes may be used alone or in combination of two or more. The content of the electrolyte is not particularly limited, but is preferably 0.1 to 50 parts by weight relative to 100 parts by weight of the aqueous dispersion medium.

[0040] The aqueous dispersion medium may contain a polymerization aid, which can suppress particle aggregation and scale generation in a polymerization reactor (specifically, aggregation due to strong adhesion of polymers to the outer shell surfaces of particles during polymerization of the polymerizable component, and adhesion of polymers to the inner walls of the polymerization reactor). Examples of the polymerization aid include nitrite, sodium sulfite, copper chloride, iron chloride, dichromate, stannic chloride, hydroquinone, ethylenediaminetetraacetate, water-soluble ascorbic acids, water-soluble polyphenols, water-soluble vitamin B, etc. These polymerization aids may be used alone or in combination of two or more.

[0041] In the polymerization step, the oily mixture is dispersed in an aqueous dispersion medium so as to prepare spherical oil droplets of a predetermined particle size. Examples of methods for dispersing the oily mixture include a method of stirring with a homomixer (e.g., manufactured by Primix Corporation), a method using a static dispersing device such as a static mixer (e.g., manufactured by Noritake Engineering Co., Ltd.), a membrane suspension method, an ultrasonic dispersion method, and other common dispersion methods. Next, the dispersion in which the oily mixture is dispersed as spherical oil droplets in the aqueous dispersion medium is heated to carry out polymerization. During the polymerization reaction, it is preferable to stir the dispersion, and the stirring may be carried out gently to a degree that prevents the oily mixture and the particles after polymerization from floating up or settling down.

[0042] The polymerization temperature can be freely set depending on the type of polymerization initiator, but is preferably controlled within a range of 30 to 100°C, more preferably 40 to 90°C. The reaction temperature is preferably maintained for about 1 to 20 hours. The initial polymerization pressure is not particularly limited, but is preferably in the range of 0 to 5 MPa, more preferably 0.02 to 3 MPa, in gauge pressure.

[0043] The particles of the present invention may be in the form of a slurry, a wet powder, or a dry powder. When the particles of the present invention are in the form of a wet powder, they can be obtained, for example, by dehydrating the slurry containing the particles obtained by the above-mentioned production method using a centrifuge, a pressure press, a vacuum dehydrator, or the like. The moisture content of such wet powder is not particularly limited, but is usually 10 to 50% by weight, preferably 15 to 45% by weight, and more preferably 20 to 40% by weight. The wet powder obtained above can be dried to a dry powder using a tray dryer, an indirect heating dryer, a fluidized bed dryer, a vacuum dryer, a vibration dryer, a flash dryer, etc. Alternatively, the slurry can be dried using a spray dryer, a fluidized bed dryer, etc. to obtain a dried powder.

[0044] In addition to the methods described above, the particles of the present invention can also be produced by other methods, such as interfacial polymerization, reverse phase emulsification, emulsion polymerization, etc. It is also possible to produce the particles by methods that do not produce droplets in an aqueous dispersion medium, such as submerged drying, coacervation, spray drying, and dry mixing.

[0045] [Composition and Molded Article] The composition of the present invention contains the particles described above and a base component, and can provide a molded article having excellent flame retardancy. Examples of base material components include rubbers such as natural rubber, isoprene rubber (IR), butadiene rubber (BR), styrene-butadiene rubber (SBR), chloroprene rubber (CR), nitrile rubber (NBR), butyl rubber, silicone rubber, acrylic rubber, urethane rubber, fluororubber, polyether rubber, ethylene-propylene rubber (EPM), and ethylene-propylene-diene rubber (EPDM); thermosetting resins such as epoxy resin, phenolic resin, unsaturated polyester resin, polyurethane, polyimide, and polyamide-imide; waxes such as polyethylene wax and paraffin wax; polyolefin resins such as ethylene-vinyl acetate copolymer (EVA), polyethylene (PE), modified polyethylene, polypropylene (PP), modified polypropylene, and modified polyolefin; polyvinyl chloride (PVC); acrylic resin; thermoplastic polyurethane; acrylonitrile-styrene copolymer (AS resin), acrylonitrile-butadiene-styrene copolymer (ABS resin); and polystyrene. Examples of suitable substrates include polystyrene (PS), (meth)acrylate-styrene copolymers, polyamide resins (such as nylon 6 and nylon 66), modified polyamides, engineering plastics such as polycarbonate, polyethylene terephthalate (PET), polybutylene terephthalate (PBT), polyacetal (POM), polyphenylene sulfide (PPS), polyphenylene ether (PPE), modified polyphenylene ether, polyether ether ketone, polyether sulfone, and polyphthalamide, thermoplastic resins such as fluororesins, ionomer resins such as ethylene-based ionomers, urethane-based ionomers, styrene-based ionomers, and fluorine-based ionomers, thermoplastic elastomers such as olefin-based elastomers, styrene-based elastomers, urethane-based elastomers, polyester-based elastomers, polyamide-based elastomers, and fluorine-based elastomers, bioplastics such as polylactic acid (PLA), cellulose acetate, PBS, PHA, and starch resins, and liquid crystal polymers. These substrate components may be used alone or in combination. Furthermore, in addition to the particles and base component described above, the composition of the present invention may contain additives such as antioxidants, ultraviolet absorbers, stabilizers, fillers, plasticizers, pigments, and antistatic agents, as well as solvents, lubricants, organic powders other than the particles of the present invention, inorganic powders, and the like, depending on the intended use.

[0046] The amount of particles contained in the composition of the present invention is not particularly limited, but is preferably 0.1 to 600 parts by weight per 100 parts by weight of the base component. The upper limit of the content is more preferably 400 parts by weight, even more preferably 200 parts by weight, and particularly preferably 100 parts by weight. On the other hand, the lower limit of the content is more preferably 0.3 parts by weight, even more preferably 0.5 parts by weight, particularly preferably 1 part by weight, and most preferably 3 parts by weight. When the content is within the above range, a molded product having sufficient flame retardancy tends to be obtained.

[0047] The composition of the present invention can be obtained by mixing the particles described above, the base component, and various additives as necessary. Alternatively, a composition containing the particles and the base component described above can be prepared and then further mixed with the base component to form a composition. Alternatively, a composition containing particles and a base component with a relatively low melting point can be prepared and then further mixed with the base component to form a composition, which is preferred because it can achieve good particle dispersibility. The relatively low melting point is not particularly limited, but is preferably 50 to 200°C, more preferably 50 to 170°C, even more preferably 50 to 140°C, particularly preferably 50 to 110°C, and most preferably 50 to 80°C.

[0048] The composition of the present invention may be in the form of a liquid or a paste. When the composition of the present invention is in the form of a liquid or a paste, it can be used as a coating composition, an adhesive composition, a pressure-sensitive adhesive composition, an electrically insulating varnish composition, etc.

[0049] The mixing method can be, for example, by using a mixer, a mixer, a Henschel mixer, a super mixer, a ribbon mixer, a ribbon blender, a kneader, a roll, a mixing roll, a single-screw kneader, a twin-screw kneader, a multi-screw kneader, or the like.

[0050] The molded article of the present invention is obtained by molding the composition described above. As the molding method, depending on whether the resin is a thermoplastic resin or a thermosetting resin, a commonly used molding method such as extrusion molding, injection molding, vacuum molding, blow molding, compression molding, transfer molding, RIM molding, or cast molding can be appropriately used. The amount of the above-described particles contained in the molded article of the present invention is not particularly limited, but is preferably 0.1 to 100 parts by weight per 100 parts by weight of the base component. The upper limit of the content is more preferably 80 parts by weight, even more preferably 50 parts by weight, and particularly preferably 40 parts by weight. On the other hand, the lower limit of the content is more preferably 0.3 parts by weight, even more preferably 0.5 parts by weight, particularly preferably 1 part by weight, and most preferably 3 parts by weight.

[0051] The molded article of the present invention has excellent flame retardancy and can therefore be widely used industrially as various textile products such as woven fabrics, knitted fabrics, carpeting, and nonwoven fabrics, and as various components in the fields of automobiles, building materials, office automation equipment, home appliances, and electronic devices, etc. In particular, it can be suitably used as a sealing material for vehicles and construction. [Example]

[0052] Examples of the particles of the present invention will be specifically described below. However, the present invention is not limited to these examples. The measurement methods of physical properties, evaluation items, and evaluation methods in the examples and comparative examples are as follows. Furthermore, in the following examples and comparative examples, "%" means "% by weight" and "parts" means "parts by weight" unless otherwise specified.

[0053] [Average particle size] A Microtrac particle size distribution analyzer (model 9320-HRA, manufactured by Nikkiso Co., Ltd.) was used, and the D50 value determined by volume-based measurement was taken as the average particle size of the particles.

[0054] [Measurement of particle true specific gravity (D1)] The true specific gravity (D1) of the particles at 25°C was measured by the immersion pycnometer method using isopropyl alcohol.

[0055] [Measurement of flame retardant encapsulation rate] 1.0 g of particles was placed in a stainless steel evaporating dish with a diameter of 80 mm and a depth of 15 mm, and its weight was measured (W1(g)). 30 mL of N,N-dimethylformamide was added and the mixture was dispersed uniformly. The mixture was left at room temperature for 24 hours, and then dried under reduced pressure at 130°C for 2 hours. After drying under reduced pressure, the sample was washed three times with 30 mL of isopropyl alcohol, dried at 100°C for 10 minutes, and its weight was measured (W2(g)). In addition, the moisture content of the particles was measured using a Karl Fischer moisture meter (MKA-510N, manufactured by Kyoto Electronics Manufacturing Co., Ltd.) w1 (% by weight). Above W1, W2, C w1 From this, the inclusion rate (C (wt%)) of the inclusions in the particles was calculated using the following formula. C = 100 × [(W1-W2)-C W1 / 100] / (1.0-C W1 / 100)

[0056] [Measurement of true specific gravity of polymer forming particle outer shell] 10 g of particles were dispersed in 200 mL of N,N-dimethylformamide, treated with an ultrasonic disperser for 30 minutes, immersed at room temperature for 24 hours, filtered, and dried under vacuum at 120°C for 5 hours to isolate the polymer forming the particle shell (hereinafter simply referred to as the shell polymer). The true specific gravity (D2) of the resulting shell polymer was measured in the same manner as in the measurement of the true specific gravity of the particles described above.

[0057] [Calculation of particle shell thickness] Particle shell thickness <t>was calculated using the following formula: <t> = <x> / 2〔1-{1-D1×(1-C / 100) / D2} 1 / 3 〕 <x>: Average particle size (μm) D1: True specific gravity of particles D2: True specific gravity of the polymer forming the shell C: Flame retardant encapsulation rate (wt%)

[0058] [Calculation of the ratio (d1 / d2) of the particle's inner diameter (d1) to its outer diameter (d2)] The ratio (d1 / d2) of the inner diameter (d1) to the outer diameter (d2) of the particle was calculated using the following formula. d1= <x> -2 <t> d2= <x> d1 / d2=( <x> -2 <t> ) / <x> =1-2 <t> / <x>

[0059] <Particle stability over time> The particles were left to stand for 60 days at 40° C. After standing, 10 g of the particles were washed three times with 30 mL of isopropyl alcohol, dried at 100° C. for 1 hour, and then weighed (W3(g)). In addition, the moisture content of the particles after standing was measured using a Karl Fischer moisture meter (MKA-510N, manufactured by Kyoto Electronics Manufacturing Co., Ltd.), and C w2 (% by weight). Above W3, C w2 The flame retardant retention rate R1 (%) of the particles after standing was calculated using the following formula. When R1 was 90% or more, the particles were evaluated as having excellent stability over time, with the flame retardant bleed-out being suppressed. On the other hand, when R1 was less than 90%, the flame retardant bleed-out occurred, with the particles being evaluated as having poor stability over time. R1=10×(W3+C w2 / 100)

[0060] <Thermal stability of particles> 10 g of particles were placed in a stainless steel evaporating dish with a diameter of 80 mm and a depth of 15 mm, heated at 200°C for 1 hour, and then their weight was measured (W4(g)). After heating, the particles were washed three times with 30 mL of isopropyl alcohol, dried at 100°C for 10 minutes, and then their weight was measured (W5(g)). From the above W4 and W5, the retention rate R2 (%) of the encapsulated flame retardant in the particles after heating was calculated using the following formula. The larger R2 is, the better the thermal stability is. R2 = 100 × (W5 / W4)

[0061] <Preparation of molded body> 30 parts of particles and polypropylene (MFR 2.4 g / 10 min, density 0.90 g / cm 3 ) were mixed to obtain a composition. Next, using a Laboplastomill (twin-screw extruder ME-25, manufactured by Toyo Seiki Kogyo Co., Ltd.) and a T-die (lip width 150 mm, thickness 0.7 mm), the set temperatures (molding temperatures) of the extruder and T-die were set to 200°C, and the screw rotation speed was set to 50 rpm. The obtained composition was charged into a Labo Plastomill through a raw material hopper to produce a sheet as a molded article. The stickiness and odor of the surface of the produced sheet were evaluated.

[0062] <Flame retardancy of molded products> The sheet prepared above was cut into test pieces measuring 25 mm x 150 mm x 0.7 mm. These test pieces were subjected to a combustion test based on the UL-94 standard. The test piece was held vertically and exposed to a flame for 10 seconds at the bottom, and the combustion time after the flame was removed was evaluated.

[0063] <Stability of molded products over time> The sheet thus prepared was left standing at 40°C for 60 days. After standing, the stickiness and odor of the sheet surface were evaluated. The burning time was also evaluated by the same method as above.

[0064] Example 1 To 500 g of ion-exchanged water, 120 g of sodium chloride, 30 g of colloidal silica containing 20% ​​by weight of the active ingredient, 1 g of polyvinylpyrrolidone, and 0.1 g of ethylenediaminetetraacetic acid tetrasodium salt were added, and the pH of the resulting mixture was adjusted to 2.5 to 3.5 to prepare an aqueous dispersion medium. Separately, 99 g of methacrylic acid, 1 g of ethylene glycol dimethacrylate, 3 g of 2,2'-azobis(isobutyronitrile), and 100 g of bisphenol A bisdiphenyl phosphate were mixed together to prepare an oily mixture. The aqueous dispersion medium and the oil mixture were mixed, and the resulting mixture was dispersed in a homomixer (TK homomixer, manufactured by Primix Corporation) at a rotation speed of 10,000 rpm for 1 minute. The mixture was then subjected to a polymerization reaction for 20 hours at a reaction temperature of 60°C while stirring at 150 rpm under an initial reaction pressure of 0.3 MPa. After polymerization, the polymerization product was filtered and dried to obtain Particle 1. The average particle diameter of the resulting Particle 1 was 20 μm. Furthermore, other physical properties of the particles were evaluated. The results are shown in Table 1.

[0065] (Examples 2 to 16 and Comparative Examples 1 to 3) Particles (particles 2 to 19) were obtained in the same manner as in Example 1, except that the oily mixture was changed to that shown in Tables 1 and 2. The physical properties of each of the obtained particles were evaluated. The results are shown in Tables 1 and 2.

[0066] [Table 1]

[0067] [Table 2]

[0068] As can be seen from Tables 1 to 3, particles containing a shell including a polymer of polymerizable components including monomer (A) and monomer (B), in which monomer (a1) is essential, and a flame retardant encapsulated therein, exhibit excellent stability over time, with the encapsulated flame retardant being prevented from bleeding out. Furthermore, even when heated, the encapsulated flame retardant is prevented from bleeding out, with good thermal stability. Furthermore, molded articles containing the particles exhibit excellent stability over time. On the other hand, Comparative Example 2, which does not contain the monomer (A), Comparative Example 1, which does not contain the monomer (B), and Comparative Example 3, which does not contain the monomer (a1), are unable to suppress the bleed-out of the flame retardant and are poor in stability over time.Furthermore, even when used in a molded article, the stability over time is poor. [Explanation of symbols]

[0069] 1 outer shell 2. Flame retardants< / x> < / t> < / x> < / t> < / x> < / x> < / t> < / x> < / x> < / x> < / t> < / t>

Claims

1. A particle including an outer shell including a polymer and a flame retardant encapsulated therein, The present invention excludes heat-expandable microspheres having an average particle size of 1 to 100 μm, which are composed of a shell made of a thermoplastic resin and a blowing agent encapsulated therein, the blowing agent having a boiling point equal to or lower than the softening point of the thermoplastic resin and containing a fluorine-containing compound, and heat-expandable microspheres obtained by a production method in which the heat-expandable microspheres are expanded by heating them to an expansion-initiation temperature or higher, The polymer is a polymer of a polymerizable component containing the following monomer (A) and the following monomer (B), the monomer (A) contains a carboxyl group-containing monomer (a1), the carboxyl group-containing monomer (a1) contains methacrylic acid, Particles, wherein the weight ratio of the monomer (A) in the polymerizable component is 50 to 99.99% by weight, and the weight ratio of the monomer (B) in the polymerizable component is 0.01 to 50% by weight. Monomer (A): A monomer having one polymerizable carbon-carbon double bond Monomer (B): A monomer having at least two polymerizable carbon-carbon double bonds

2. The particle according to claim 1 , wherein the monomer (A) further comprises the following monomer (a2): Monomer (a2): at least one selected from nitrile-based monomers, (meth)acrylic acid ester-based monomers, monomers having a group reactive with a carboxyl group, and styrene-based monomers

3. The particles according to claim 1 or 2, wherein the flame retardant comprises at least one selected from an organic phosphorus compound, an organic halogen compound, and an inorganic compound.

4. A composition comprising the particles according to any one of claims 1 to 3 and a base component.

5. A molded article obtained by molding the composition according to claim 4.

Citation Information

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