JP2006213930A - Process for producing thermally expandable microsphere - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide thermally expanded microspheres, which have a particle size distribution with a coefficient of variation showing only a slight difference before and after heat-expansion, and which exhibit extremely low contents for aggregated microspheres and microspheres of high true specific gravity, and a production process thereof. <P>SOLUTION: The themally expandable microspheres comprise a shell of a thermoplastic resin, and a blowing agent with a boiling point not higher than the softening point of the thermoplastic resin being encapsulated in the shell. The process for producing the thermally expandable microspheres comprises mixing a monomer mixture and the blowing agent, and polymerizing the obtained mixture in an aqueous suspension. The monomer mixture consists essentially of a nitrile monomer and a monomer having a carboxy group. The weight ratio of the nitrile monomer ranges from 20 to 80 weight percent, and the weight ratio of the monomer having a carboxy group ranges from 80 to 20 weight percent in the monomer mixture. The blowing agent contains a 2-10C fluorine-containing compound which has an ether structure, and does not contain a chlorine or bromine atom. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

The present invention relates to a thermally expanded microsphere, a method for producing the same, a thermally expandable microsphere, and an application. More specifically, the present invention has little change in the coefficient of variation of the particle size distribution before and after thermal expansion, and the content of aggregated microspheres and microspheres with large true specific gravity (microspheres that failed to achieve desired thermal expansion) is extremely low. Thermally expanded microspheres and their manufacturing methods, and the content of aggregated microspheres and microspheres with large true specific gravity are extremely low, are not easily damaged by external force, and cure shrinkage when molding hollow body compositions for weight reduction purposes. The present invention relates to thermally expandable microspheres that can be prevented and can solve the problem of heat settling over time, and uses of these microspheres.

In the present invention, the thermally expandable microsphere and the thermally expanded microsphere encapsulating the specific fluorine-containing compound are filled in the cavity portion of the tire / rim assembly, and is excellent in the damaged portion sealing material when the tire is damaged. Used as a tire internal pressure imparting material.

Thermally expandable microspheres having a structure in which a thermoplastic resin is used as an outer shell and a foaming agent is enclosed in the outer shell are generally referred to as thermally expandable microcapsules. As the thermoplastic resin, a vinylidene chloride copolymer, an acrylonitrile copolymer, an acrylic copolymer, or the like is usually used. Moreover, hydrocarbons, such as isobutane and isopentane, are mainly used as a foaming agent (refer patent document 1).

By heating and expanding such thermally expandable microcapsules, lightweight hollow fine particles (thermally expanded microspheres) can be obtained. As a method for expanding the thermally expandable microcapsules, a method has been proposed in which a dispersion of thermally expandable microcapsules is sprayed into heated air to simultaneously expand and dry (see Patent Document 2). However, there is a high possibility that aggregates are generated at the tip of the used disperser.
In addition, a method has been proposed in which thermally expandable microcapsules obtained by impregnating a foaming agent are expanded with hot air from an electric hot air generator to obtain hollow fine particles (see Patent Document 3). As described in Comparative Example 3, when this method is applied to a thermally expandable microcapsule containing a foaming agent, the residence time of each thermally expandable microsphere in the apparatus cannot be controlled. The resulting hollow microparticles have a low expansion ratio, shrink, and no favorable physical properties are obtained.

Furthermore, a method has been proposed in which the dried thermally expandable microspheres are heated on a belt conveyor to a temperature higher than the expansion temperature to produce expanded hollow fine particles, which are transferred from the belt by an air current (Patent Document). 4). In this method, non-expanded products are generated due to the deterioration of the coefficient of variation in the particle size distribution of the hollow microparticles obtained by mixing the hollow microparticles expanded at the time of airflow transfer with unexpanded thermally expandable microspheres and the variation in true specific gravity There may be a problem.

When expanding the thermally expandable microcapsules, it is generally desired to reduce the residual amount of thermally expandable microcapsules that are raw materials and suppress the formation of aggregated microspheres as much as possible.
In order to satisfy such a demand, it is considered that it is important to expand the thermally expandable microcapsules by giving the same thermal history.
For example, a method has been proposed in which thermally expandable microcapsules are expanded in an aqueous slurry, and a slurry liquid containing the expanded particles is passed through a gap between grindstones to disperse aggregated microspheres (see Patent Document 5). Although this method is capable of giving the same thermal history to all the thermally expandable microcapsules, it can be dried because it is blended with plastics, paints, rubbers, sealants, etc., regardless of whether it is used as an aqueous slurry. If you need it,
Fusion in the drying process is also a problem.

Also disclosed is a method for producing hollow fine particles by thermally expanding after thermally expanding microspheres are dispersed in a slurry (see Patent Document 6). This method is also a method capable of giving the same thermal history to all the thermally expandable microspheres. However, in order to obtain dried hollow microspheres, it is necessary to dehydrate the slurry containing the expanded thermally expandable microspheres and then dry, resulting in poor production efficiency, especially the softening temperature of the outer shell polymer. The hollow microparticles obtained from the low thermal expansion microspheres have a problem of agglomeration in the drying process.

Furthermore, a thermally expandable microsphere having a sharp particle size distribution and a production method thereof have been proposed (
(See Patent Document 7). Then, when the thermally expandable microspheres obtained by this production method are expanded, the specific foaming method is not clear, but the foam is sharp and the thermally expanded microspheres of uniform shape and size are obtained. It is described that it is obtained. However, even if the thermally expandable microspheres have a uniform particle size distribution, expanded microspheres having a uniform particle size distribution and no agglomerated microspheres can be obtained if they are expanded by a conventionally known foaming method. It is well known to those skilled in the art.

As is apparent from the above, whether the expansion method is dry or wet, it is desired to reduce the residual amount of raw materials and suppress the generation of aggregated microspheres as much as possible, but this has not been achieved at present.

Further, the hollow fine particles are blended in the hollow body molded product for the purpose of reducing the weight as described above.
A hollow body molded product is usually produced by kneading a base material component, a filler, and hollow fine particles to produce a hollow body composition, and molding the hollow body composition into a desired shape. At the time of the kneading, a large external force is often applied to the hollow fine particles, and there is a problem that the initially planned weight reduction cannot be achieved because the hollow fine particles are partially broken. Moreover, when shape | molding the said hollow body composition, the thermoplastic resin which comprises the outer shell of a hollow microparticle by softening is softened, and an external pressure is applied to a hollow microparticle. Since the internal pressure based on the vapor of the foaming agent contained in the hollow fine particles cannot be resisted against this external pressure, a phenomenon in which the hollow fine particles slightly shrink during molding is observed. As a result, the entire hollow body molded product also shrinks, resulting in a problem of curing shrinkage in which the dimensional stability is low and the initially expected weight reduction cannot be achieved.

In order to solve such a problem, a hollow body composition using both thermally expandable microspheres and hollow fine particles has been proposed (see Patent Document 8). Thereby, curing shrinkage is solved, but it is necessary to prepare two types of particles (thermally expandable microspheres and hollow fine particles), and there is a slight problem that it is complicated. Furthermore, the hollow body molded product is not so much when used at room temperature,
When used under high temperature, there is a problem of heat settling over time, that is, the volume of the hollow body molded product gradually decreases. This is considered because the foaming agent included in the hollow fine particles leaks over time.

In order to solve this problem, a thermoplastic resin having a low gas permeability such as an acrylonitrile copolymer is used as the thermoplastic resin constituting the outer shell, but this alone does not sufficiently solve the problem. This is the actual situation.

Lightweight hollow microparticles obtained by heating and expanding thermally expandable microcapsules have traditionally been
Lightweight materials such as resin and ceramic products mentioned above, thermal insulation materials such as thermal paper and paint, bulky materials such as nonwoven fabrics, impact absorbing materials such as exteriors of automobiles, surface modifiers that give a sense of unevenness to wallpaper, etc. in use. In recent years, the present inventors have developed a novel heat-expandable microcapsule containing a specific fluorine-containing compound as a foaming agent, and a volume-retaining material for a pressure vessel, which is a new application of the hollow microparticles that have been thermally expanded. (See Patent Document 9).

U.S. Pat. No. 3,615,972 Japanese National Publication No.59-53290 Japanese Unexamined Patent Publication No. 8-217905 Japan Special Equity 8-29245 Japanese Unexamined Patent Publication No. 62-201231 Japanese Patent No. 2927933 WO99 / 37706 Japanese Patent No. 3067932 WO2004 / 074396

An object of the present invention is to provide thermally expanded microspheres with a small change in the coefficient of variation in particle size distribution before and after thermal expansion and a very low content of aggregated microspheres and microspheres with large true specific gravity, and a method for producing the same. It is to be.

Another object of the present invention is that the content of agglomerated microspheres and microspheres with a large true specific gravity is very low, hardly damaged by external force, and when blended in a hollow body composition for the purpose of weight reduction, curing at the time of molding. It is intended to provide thermally expanded microspheres and thermally expandable microspheres that can prevent shrinkage and solve the problem of heat settling over time in the obtained hollow body molded article.

Still another object of the present invention is to provide a hollow body molded product that can achieve a sufficient weight reduction, can prevent curing shrinkage during molding, does not cause a problem of thermal settling over time, and has high dimensional stability. It is to be.

Still another object of the present invention is to provide thermally expandable microspheres and heat that can exhibit excellent physical properties when filled into a tire and rim assembly and used as a tire damage part sealing material and a tire internal pressure imparting material. It is to provide an expanded microsphere, a method for producing the thermally expanded microsphere, and a thermally expandable microsphere that is a raw material of the thermally expanded microsphere.

As a result of various studies by the present inventors in order to solve the above problems, the following (1) to (4)
The findings shown in (1) were obtained.
(1) When producing thermally expanded microspheres by thermally expanding the thermally expandable microspheres by a specific method that is dry and well dispersed, the change in the coefficient of variation of the particle size distribution before and after thermal expansion is reduced, The amount of raw materials and slightly expanded microspheres can be reduced to suppress the formation of aggregated microspheres.
(2) In the manufacturing method of (1) above, by controlling the expansion conditions, it is possible to manufacture almost completely thermally expanded microspheres, and thermally expanded microspheres having a desired reexpandable capacity (that is, reexpansion) Thermally expanded microspheres having a starting temperature can also be produced.
(3) The thermally expanded microsphere having a reexpandable capacity obtained in (2) above is also a novel thermally expandable microsphere having unprecedented physical properties.
(4) In the hollow body composition containing the thermally expanded microspheres having the desired reexpandable capacity of (2) and / or the thermally expandable microspheres of (3) above, the outer shell thickness of the microspheres is It is relatively thick and has the property that it is not easily damaged by external force. In addition, since these microspheres have appropriate characteristics such as thermal expansion, curing shrinkage at the time of molding can be prevented, heat aging does not occur over time even at high temperatures, and the dimensional stability is improved. high.

Moreover, the thermally expansible microsphere and the thermally expanded microsphere which contain a specific fluorine-containing compound as a foaming agent have obtained the knowledge shown in the following (5) to (8).

(5) From the viewpoint of flame retardancy, fluorine-containing compounds are preferred. In addition, when considering application to a tire that can run even when the tire is damaged by filling the tire and rim assembly, the thermal expansion obtained by thermally expanding the thermally expandable microspheres by the above specified method The microspheres can run even when the tire internal pressure decreases after the tire is damaged.
(6) A thermally expanded microsphere obtained by substantially completely expanding a thermally expandable microsphere by the above-described specific method in a tire and rim assembly that can run even when the tire internal pressure decreases when the tire is damaged Similarly, thermally expanded microspheres having a re-expandable capacity obtained by adjusting the degree of expansion of thermally expandable microspheres can be used. In particular, it is desirable that the thermally expanded microspheres having a reexpandable capacity have a physical property of reexpanding only at a desired high temperature. Recently, it has been demanded that normal driving is possible even in a high temperature environment. It is also desirable to have physical properties that provide tire internal pressure that can be quickly re-inflated and run when the tire is damaged and the tire internal pressure decreases.

(7) A thermoplastic resin constituting a thermally expanded microsphere having a re-expandable capacity is obtained by polymerizing a monomer mixture containing a nitrile monomer and a carboxyl group-containing monomer as essential components. In some cases, it can begin to re-expand at the desired high temperature.
(8) When the thermally expanded microspheres having sufficient capacity for re-expansion have a specific heat-fusing inhibitor attached to the outer surface of the outer shell, the tire-scratched part is quickly sealed when the tire is damaged. And a high tire internal pressure imparting function.

Based on these findings (1) to (8), the present invention described in detail below has been reached.
That is, a first method for producing thermally expanded microspheres according to the present invention includes an outer shell made of a thermoplastic resin and a foaming agent encapsulated in the outer shell and having a boiling point equal to or lower than the softening point of the thermoplastic resin. A method for producing thermally expandable microspheres comprising:
Mixing the monomer mixture with the blowing agent and then subjecting the resulting mixture to suspension polymerization in an aqueous suspension,
The monomer mixture includes a nitrile monomer and a carboxyl group-containing monomer as essential components, and the weight ratio of the nitrile monomer is 20 to 80% by weight with respect to the monomer mixture. The weight ratio of the carboxyl group-containing monomer is 80 to 20% by weight,
The blowing agent has an ether structure and does not contain a chlorine atom and a bromine atom, and has 2 to 2 carbon atoms.
10 fluorine-containing compounds.

Moreover, the second method for producing a thermally expandable microsphere according to the present invention is as follows.
A method for producing thermally expandable microspheres comprising an outer shell made of a thermoplastic resin, and a foaming agent encapsulated therein and having a boiling point equal to or lower than the softening point of the thermoplastic resin,
Mixing the monomer mixture with the blowing agent and then subjecting the resulting mixture to suspension polymerization in an aqueous suspension,
The blowing agent has an ether structure and does not contain a chlorine atom and a bromine atom, and has 2 to 2 carbon atoms.
10 fluorine-containing compounds,
The re-expansion start temperature of the thermally expandable microsphere is 100 ° C. or higher.

In these first and second thermally expandable microsphere manufacturing methods,
It is preferable to further include a step of adhering at least one kind of heat fusion inhibitor selected from an organic compound having a melting point of 90 ° C. or higher and an inorganic compound having a layered structure to the outer surface of the outer shell.

Moreover, the third method for producing a thermally expandable microsphere according to the present invention is as follows.
A thermal expansion composed of an outer shell made of a thermoplastic resin, a foaming agent encapsulated therein and having a boiling point not higher than the softening point of the thermoplastic resin, and an anti-fusing agent attached to the outer surface of the outer shell. A method for producing a functional microsphere,
Mixing a monomer mixture with the blowing agent and then subjecting the resulting mixture to suspension polymerization in an aqueous suspension;
Adhering to the outer surface of the outer shell at least one heat fusion inhibitor selected from an organic compound having a melting point of 90 ° C. or higher and an inorganic compound having a layered structure,
The blowing agent has an ether structure and does not contain a chlorine atom and a bromine atom, and has 2 to 2 carbon atoms.
10 fluorine-containing compounds.

In the manufacturing method of this thermally expandable microsphere,
The fluorine-containing compound is C ₃ HF ₆ OCH ₃ , C ₂ HF ₄ OC ₂ H ₂ F ₃ , C ₃ F ₇ OC
It is preferably at least one selected from H ₃ , C ₄ F ₉ OCH ₃ and C ₄ F ₉ OC ₂ H ₅ .
Moreover, it is preferable that a water-soluble reducing agent is contained in the aqueous suspension.

A. Method for producing thermally expanded microspheres a. Thermally expandable microspheres used as starting materials In the first and second methods for producing thermally expanded microspheres according to the present invention, thermally expandable microspheres (hereinafter referred to as "raw material microspheres") used as starting materials. Is comprised of an outer shell made of a thermoplastic resin and a foaming agent encapsulated therein and having a boiling point not higher than the softening point of the thermoplastic resin, and having an average particle diameter of 1 to 100 μm. There is no particular limitation.

The foaming agent is not particularly limited as long as it is a substance that is encapsulated in an outer shell made of a thermoplastic resin and has a boiling point equal to or lower than the softening point of the thermoplastic resin. Examples include hydrocarbons having 1 to 12 carbon atoms and their halides; fluorine-containing compounds; tetraalkylsilanes; azodicarbonamide and the like compounds that generate heat by heating to generate gases. These foaming agents may be used alone or in combination of two or more.

Examples of the hydrocarbon having 1 to 12 carbon atoms include propane, cyclopropane, propylene, butane, normal butane, isobutane, cyclobutane, normal pentane, cyclopentane, isopentane, neopentane, normal hexane, isohexane, cyclohexane, heptane, cycloheptane. , Hydrocarbons such as octane, isooctane, cyclooctane, 2-methylpentane, 2,2-dimethylbutane, and petroleum ether. These hydrocarbons may be linear, branched or alicyclic, and are preferably aliphatic.
Examples of the hydrocarbon halide having 1 to 12 carbon atoms include methyl chloride, methylene chloride, chloroform and carbon tetrachloride. These halides are preferably the above-described hydrocarbon halides (fluoride, chloride, bromide, iodide, etc.).

The fluorine-containing compound is not particularly limited, and for example, a compound having an ether structure, not containing a chlorine atom and a bromine atom, and having 2 to 10 carbon atoms is preferable. Specifically, C ₃ H ₂ F ₇ O
CF ₂ H, C ₃ HF ₆ OCH ₃ , C ₂ HF ₄ OC ₂ H ₂ F ₃ , C ₂ H ₂ F ₃ OC ₂ H ₂ F ₃ , C ₄ HF ₈ O
CH ₃ , C ₃ H ₂ F ₅ OC ₂ H ₃ F ₂ , C ₃ HF ₆ OC ₂ H ₂ F ₃ , C ₃ H ₃ F ₄ OCHF ₂ , C ₃ HF ₆ O
C ₃ H ₂ F ₅ , C ₄ H ₃ F ₆ OCHF ₂ , C ₃ H ₃ F ₄ OC ₂ HF ₄ , C ₃ HF ₆ OC ₃ H ₃ F ₄ , C ₃ F ₇
Examples include hydrofluoroethers such as OCH ₃ , C ₄ F ₉ OCH ₃ , C ₄ F ₉ OC ₂ H ₅ , and C ₇ F ₁₅ OC ₂ H ₅ . The (fluoro) alkyl group of the hydrofluoroether may be linear or branched.

Examples of the tetraalkylsilane include compounds having the same or different alkyl group having 1 to 5 carbon atoms. Specific examples include tetraalkylsilanes such as tetramethylsilane, trimethylethylsilane, trimethylisopropylsilane, and trimethyl-n-propylsilane.
Examples of the compound that generates gas upon thermal decomposition by heating include azodicarbonamide, N, N
Examples include '-dinitrosopentamethylenetetramine, 4,4'-oxybis (benzenesulfonylhydrazide) and the like.

When a fluorine-containing compound is used as a foaming agent, the entire amount may be composed of the fluorine-containing compound, but other than the fluorine-containing compound having a boiling point equal to or lower than the softening point of the thermoplastic resin described later together with the fluorine-containing compound. These compounds may be used in combination. Such a compound is not particularly limited, and can be selected from, for example, those exemplified as the foaming agent described above. Compounds other than the fluorine-containing compound can be appropriately selected according to the thermal expansion temperature range of the raw material microspheres. When a fluorine-containing compound is used as the foaming agent, the weight ratio of the fluorine-containing compound is preferably more than 50% by weight of the whole foaming agent, more preferably more than 80% by weight, and more than 95% by weight. It is particularly preferred. The higher the weight ratio of the fluorine-containing compound in the foaming agent, the more the physical properties of the fluorine-containing compound are reflected in the raw material microspheres, and it is possible to impart physical properties such as flame retardancy and incombustibility to the raw material microspheres.

The raw material microsphere is composed of, for example, a thermoplastic resin obtained by polymerizing a monomer mixture containing a radical polymerizable monomer, and the raw material microsphere is appropriately blended with a polymerization initiator in the monomer mixture. The outer shell can be formed.
The radical polymerizable monomer is not particularly limited. For example, nitrile monomers such as acrylonitrile, methacrylonitrile, α-chloroacrylonitrile, α-ethoxyacrylonitrile, fumaronitrile; acrylic acid, methacrylic acid, itaconic acid , Maleic acid, fumaric acid, citraconic acid and other carboxyl group-containing monomers; vinylidene chloride; vinyl acetate; methyl (meth) acrylate, ethyl (meth) acrylate, n-butyl (meth) acrylate, isobutyl (meth) acrylate, t-butyl (meth) acrylate, isobornyl (meth) acrylate, cyclohexyl (meth) acrylate, benzyl (meth) acrylate,
(Meth) acrylic acid ester monomers such as β-carboxyethyl acrylate; styrene,
Styrene monomers such as α-methylstyrene and chlorostyrene; Acrylamide monomers such as acrylamide, substituted acrylamide, methacrylamide and substituted methacrylamide; N
And maleimide monomers such as -phenylmaleimide, N- (2-chlorophenyl) maleimide, N-cyclohexylmaleimide, and N-laurylmaleimide. These radically polymerizable monomers may be used alone or in combination of two or more.

In particular, when the foaming agent contains a fluorine-containing compound, it is preferable that the monomer mixture is a monomer mixture containing a nitrile monomer as an essential component because heat resistance can be imparted. The weight ratio of the nitrile monomer is preferably 80% by weight in consideration of heat resistance with respect to the monomer mixture.
Or more, more preferably 90% by weight or more, and particularly preferably 95% by weight or more.

Further, when the monomer mixture is a monomer mixture containing a nitrile monomer and a carboxyl group-containing monomer as an essential component, heat resistance can be imparted, and the raw material microspheres are expanded as described later. The thermally expanded microspheres obtained by heating can be manufactured to have a re-expandable capacity and are re-expanded at a temperature of 90 ° C. or higher (preferably 100 ° C. or higher, more preferably 120 ° C. or higher). Is more preferable because it can be set so as to start. The weight ratio of the nitrile monomer can be adjusted by adjusting the retention rate and foamability of the encapsulated foaming agent, the re-expansion start temperature of the thermally expanded microsphere, and evaluating the internal pressure and high-speed running performance described later. Considering, the monomer mixture is preferably 20 to 80% by weight, more preferably 20 to 60% by weight, and particularly preferably 20 to 50% by weight.
And most preferably 20 to 40% by weight. In addition, the weight ratio of the carboxyl group-containing monomer is to adjust the re-expansion start temperature of the thermally expanded microsphere, to evaluate the normal internal pressure high-speed running performance described later, and to further maintain the internal retention rate and foaming of the encapsulated foaming agent. Considering the properties and the like, the amount is preferably 20 to 80% by weight, more preferably 40 to 80% by weight, based on the monomer mixture.
And particularly preferably 50 to 80% by weight, most preferably 60 to 80% by weight.

The monomer mixture may contain a polymerizable monomer (crosslinking agent) having two or more polymerizable double bonds in addition to the radical polymerizable monomer. By polymerizing using a crosslinking agent, the content of aggregated microspheres contained in the thermally expanded microspheres obtained by this production method is reduced, and the retention rate of the encapsulated foaming agent after thermal expansion (encapsulation retention) Rate) is suppressed, and effective thermal expansion can be achieved.
In the present invention, encapsulated retention of blowing agent after thermal expansion (%) is, the encapsulation efficiency of the blowing agent encapsulated in front of the raw material microspheres to expand and G _1, the thermal expansion obtained by thermal expansion were the encapsulation efficiency of the microspheres contained a blowing agent When G _2, defined in G ₂ / G ₁ × 100.

The cross-linking agent is not particularly limited. For example, aromatic divinyl compounds such as divinylbenzene and divinylnaphthalene; allyl methacrylate, triacryl formal, triallyl isocyanate, ethylene glycol di (meth) acrylate, diethylene glycol di
(Meth) acrylate, triethylene glycol di (meth) acrylate, 1,4-butanediol di (meth) acrylate, 1,9-nonanediol di (meth) acrylate, 1,10
-Decanediol di (meth) acrylate, PEG # 200 di (meth) acrylate, PEG
# 400 di (meth) acrylate, PEG # 600 di (meth) acrylate, neopentyl glycol di (meth) acrylate, 1,4-butanediol dimethacrylate, 1,6-hexanediol di (meth) acrylate, 1,9 -Nonanediol di (meth) acrylate,
Trimethylolpropane trimethacrylate, glycerin dimethacrylate, dimethylol-tricyclodecane diacrylate, pentaerythritol tri (meth) acrylate,
Pentaerythritol tetraacrylate, dipentaerythritol hexaacrylate, neopentyl glycol acrylic acid benzoate, trimethylolpropane acrylic acid benzoate, 2-hydroxy-3-acryloyloxypropyl methacrylate, hydroxypivalate neopentyl glycol diacrylate, Examples thereof include di (meth) acrylate compounds such as ditrimethylolpropane tetraacrylate and 2-butyl-2-ethyl-1,3-propanediol diacrylate. These crosslinking agents may be used alone or in combination of two or more.

The weight ratio of the crosslinking agent is not particularly limited, but it is preferable for the monomer mixture in consideration of the degree of crosslinking, the retention rate of the foaming agent encapsulated in the outer shell, heat resistance and thermal expansion. Is 0.01 to 5% by weight, more preferably 0.05 to 3% by weight.

There is no limitation in particular about a polymerization initiator, A well-known polymerization initiator can be used. For example, t-butylperoxyisobutyrate, t-butylperoxy-2-ethylhexanoate, t-hexylperoxy-2-ethylhexanoate, 2,5-dimethyl-
2,5-bis (2-ethylhexanoylperoxy) hexane, 1,1,3,3-tetramethylbutylperoxy-2-ethylhexanoate, t-butylperoxypivalate, t-hexylperoxy Pivalate, t-butylperoxyneodecanoate, t-hexylperoxyneodecanoate, 1-cyclohexyl-1-methylethylperoxyneodecanoate, 1,1,3,3-tetramethylbutylper Oxyneodecanoate,
Cumylperoxyneodecanoate, di-n-propylperoxydicarbonate, diisopropylperoxydicarbonate, bis (4-t-butylcyclohexyl) peroxydicarbonate, di-sec-butylperoxydicarbonate, di- 2-ethoxyethyl peroxydicarbonate, di-2-ethylhexyl peroxydicarbonate, di-3-methoxybutyl peroxydicarbonate, 3,5,5-trimethylhexanoyl peroxide, octanoyl peroxide, lauroyl peroxide , Peroxides such as stearyl peroxide, succinic acid peroxide, benzoyl peroxide; 2,2′-azobis (4-methoxy-2,4-dimethylvaleronitrile),
2,2'-azobisisobutyronitrile, 2,2'-azobis (2,4-dimethylvaleronitrile), 2,2'-azobis (2-methylpropionate), 2,2'-azobis ( And azo compounds such as 2-methylbutyronitrile). The polymerization initiator is
An oil-soluble polymerization initiator that is soluble in a radical polymerizable monomer is preferred.

The raw material microspheres can be produced by using various methods used in the conventionally known methods for producing thermally expandable microcapsules.
That is, a monomer mixture containing a radical polymerizable monomer, optionally a crosslinking agent and a polymerization initiator is mixed with a foaming agent, and the resulting mixture is suspended in an aqueous suspension containing an appropriate dispersion stabilizer and the like. For example, a polymerization method.

Colloidal silica, colloidal calcium carbonate, magnesium hydroxide, calcium phosphate, aluminum hydroxide, ferric hydroxide, calcium sulfate, sodium sulfate, calcium oxalate, calcium carbonate, barium carbonate, magnesium carbonate, alumina sol Etc. The dispersion stabilizer is 0.1 to 20 with respect to the monomer mixture.
It is preferably used in a proportion by weight. Other dispersion stabilizers include condensation products of diethanolamine and aliphatic dicarboxylic acids, polymer type dispersion stabilizers such as gelatin, polyvinylpyrrolidone, methylcellulose, polyethylene oxide, and polyvinyl alcohol, alkyltrimethylammonium chloride, and dialkyl chloride. Various emulsifiers such as cationic surfactants such as dimethylammonium, anionic surfactants such as sodium alkyl sulfate, amphoteric surfactants such as alkyldimethylaminoacetic acid betaine and alkyldihydroxyethylaminoacetic acid betaine may be used. . The dispersion stabilizing aid is preferably used in a proportion of 0.05 to 2% by weight based on the monomer mixture.

The aqueous suspension containing the dispersion stabilizer is prepared by blending a dispersion stabilizer, a dispersion stabilization auxiliary agent, and the like with water (for example, ion exchange water). The pH of the aqueous suspension at the time of polymerization is appropriately determined depending on the type of the dispersion stabilizer and dispersion stabilizing aid used. Further, a water-soluble reducing agent may be added to the aqueous suspension, and the formation of aggregated microspheres during polymerization is suppressed. Examples of water-soluble reducing agents include alkali metal nitrites such as sodium nitrite and potassium nitrite, stannous chloride, stannic chloride, ferrous chloride, ferric chloride, ferrous sulfate, and water-soluble ascorbine. Examples include acids.
Among these, alkali metal nitrite is preferable from the viewpoint of stability in water. The addition amount is preferably 0.0001 to 1% by weight, more preferably 0.0% to the monomer mixture.
003 to 0.1% by weight.

The polymerization temperature is freely set depending on the type of the polymerization initiator, but preferably 40 to 100.
° C, more preferably 45 to 90 ° C, and particularly preferably 50 to 85 ° C.
The initial polymerization pressure is 0 to 5.0 MPa in gauge pressure, more preferably 0.1 to 3.0.
MPa, particularly preferably in the range of 0.2 to 2.0 MPa.

In the obtained raw material microspheres, the foaming agent has good foaming performance, can fill the tire and rim assembly, and can exhibit sufficient performance when used as a tire internal pressure imparting material, From the viewpoint that the thickness of the thermoplastic resin, which is the outer shell of the thermally expandable microsphere, can ensure the encapsulating retention rate of the encapsulated foaming agent, it is 2 to 85% by weight, preferably 5 to 5%. It is adjusted to 60% by weight, more preferably 7 to 50% by weight. In particular,
When a foaming agent contains a fluorine-containing compound, Preferably it is 10 to 60 weight%, More preferably, it is 15 to 50 weight%.

The average particle diameter of the raw material microspheres is not particularly limited because it can be designed freely according to the application. In particular, for the foaming agent to contain a fluorine-containing compound, preferably 1 to 100 μm.
More preferably, it is 2-80 micrometers, Most preferably, it is 5-60 micrometers.
Further, the variation coefficient CV of the particle size distribution of the raw material microspheres is not particularly limited, but is preferably 30.
% Or less, more preferably 27% or less, and particularly preferably 25% or less. Coefficient of variation CV
Is calculated by the following formulas (1) and (2).

（式中、sは粒子径の標準偏差、＜ｘ＞は平均粒子径、ｘ_i はｉ番目の粒子径、ｎは粒子
の数である。）

(In the formula, s is the standard deviation of the particle diameter, <x> is the average particle diameter, x _i is the i-th particle diameter, and n is the number of particles.)

The raw material microspheres are preferably used with a fine particle filler adhered to the outer surface of the outer shell from the viewpoint of improving dispersibility and improving fluidity during use.
The fine particle filler may be either an organic or inorganic filler, and the type and amount thereof are appropriately selected according to the purpose of use.

Examples of organic fillers include metal soaps such as magnesium stearate, calcium stearate, zinc stearate, barium stearate, lithium stearate; polyethylene wax, lauric acid amide, myristic acid amide, palmitic acid amide, stearic acid Synthetic waxes such as amide and hardened castor oil; resin powders such as polyacrylamide, polyimide, nylon, polymethyl methacrylate, polyethylene, and polytetrafluoroethylene.

Examples of the inorganic filler include those having a layered structure, such as talc, mica, bentonite, sericite, carbon black, molybdenum disulfide, tungsten disulfide, graphite fluoride, calcium fluoride, boron nitride, etc .; , Alumina, mica, calcium carbonate,
Examples thereof include calcium hydroxide, calcium phosphate, magnesium hydroxide, magnesium phosphate, barium sulfate, titanium dioxide, zinc oxide, ceramic beads, glass beads, and crystal beads.
These fine particle fillers may be used alone or in combination of two or more.

Among the above, the fine particle filler adhering to the outer surface of the outer shell has a melting point of 90 ° C. or higher (100 ° C. or higher, preferably 110 ° C. or higher, more preferably 120 ° C. or higher, more preferably 150 ° C. or higher, particularly preferably 200 ° C. An organic compound having a melting point of at least ° C or an inorganic compound having a layered structure (preferably at least one selected from carbon black, molybdenum disulfide, tungsten disulfide, graphite fluoride, and boron nitride), that is, heat fusion It is preferable that it is an anti-sticking agent. Here, the thermal fusion inhibitor prevents thermal fusion of the outer shell resin of the raw material microspheres and / or thermally expanded microspheres, and further, the adjacent raw material microspheres and / or thermally expanded during the thermal expansion. It shall prevent heat fusion with the microspheres and work without impairing foaming performance. As a result, for example, as will be described later, when the thermally expanded microspheres obtained by expanding the raw material microspheres and having the remaining capacity to be re-expanded are filled in the tire / rim assembly, the tire is damaged. Even if the tire internal pressure decreases, the tire damage part can be quickly sealed and a high tire internal pressure imparting function can be exhibited. As a result, even a damaged tire can travel a necessary distance. This effect is particularly remarkable when the foaming agent contains a fluorine-containing compound.

In the case of raw material microspheres using a thermoplastic resin constituting the outer shell obtained by polymerizing a monomer mixture containing a nitrile monomer and a carboxyl group-containing monomer as essential components, In addition to being able to demonstrate good performance in the property, flame retardancy (non-flammability), as will be described later, obtained by expanding the raw material microspheres, for thermally expanded microspheres having a surplus capacity that can be re-expanded, The re-expansion can be started at a temperature of 90 ° C. or higher (preferably 100 ° C. or higher, more preferably 120 ° C. or higher), and the above effect becomes remarkable.

The average particle size of the fine particle filler is preferably 1/10 or less of the average particle size of the raw material microspheres before adhesion. Here, the average particle size means the average particle size of primary particles.

The amount of the fine particle filler adhering to the raw material microsphere is not particularly limited, but the function of the fine particle filler can be fully exerted, and considering the true specific gravity of the thermally expandable microsphere, the raw material before adhesion Preferably it is 0.1-95 weight% with respect to a microsphere, More preferably, it is 0.5-60 weight%, Especially preferably, it is 5-50 weight%, Most preferably, it is 8-30 weight%.

Adhesion of the fine particle filler to the outer surface of the raw material microsphere can be performed by mixing the raw material microsphere and the fine particle filler. The mixing is not particularly limited, and can be performed using an apparatus having a very simple mechanism such as a container and a stirring spring. Moreover, you may use the powder mixer which can perform a general rocking | swiveling or stirring. Examples of the powder mixer include a powder mixer that can perform rocking stirring or stirring, such as a ribbon mixer and a vertical screw mixer. In recent years, super mixers (manufactured by Kawata Co., Ltd.) and high speed mixers (manufactured by Fukae Co., Ltd.) and Negura Machine (manufactured by Seishin Enterprise Co., Ltd.), which are efficient and multifunctional powder mixers combined with a stirring device. ) Etc. may be used.

The raw material microspheres can be used, for example, as a volume retaining material by filling the inside of the tire and rim assembly as it is and expanding it by heating at a temperature equal to or higher than the expansion start temperature of the raw material microspheres. . Moreover, you may use as it is for the use of the weight reducing filler of paints, such as a motor vehicle, the foaming particle for foaming ink for wallpaper and clothes decoration, and the foaming material for the resin composition weight reduction as it is.

b. Method for Producing Thermally Expanded Microspheres A first method for producing thermally expanded microspheres according to the present invention is to provide a gas fluid containing raw material microspheres as described above with a dispersion nozzle at the outlet and inside the hot air flow. A step (injection step) of flowing through the installed gas introduction pipe and spraying from the dispersion nozzle; and causing the gas fluid to collide with a collision plate installed at a downstream portion of the dispersion nozzle and causing the thermally expansible microspheres to flow into the hot air It is a manufacturing method including a step of dispersing in an air stream (dispersing step) and a step of expanding the dispersed thermally expandable microspheres by heating to or above the expansion start temperature in the hot air stream (expansion step).
This manufacturing method can be performed using, for example, a manufacturing apparatus including the foaming process unit illustrated in FIG.

This foaming process section includes a gas introduction pipe (not shown) provided with a dispersion nozzle 4 at the outlet and disposed in the center, an impingement plate 5 installed downstream of the dispersion nozzle 4, and a gas introduction pipe. An overheating prevention cylinder 3 arranged at an interval around the outer periphery and a hot air nozzle 1 arranged at an interval around the outer periphery of the overheating prevention cylinder 3 are provided. In the foaming process section, a gas fluid 6 containing thermally expandable microspheres is made to flow in the direction of the arrow in the gas introduction tube, and the space formed between the gas introduction tube and the overheating prevention cylinder 3 is thermally expanded. The gas flow 7 for improving the dispersibility of the conductive microspheres and preventing the gas introduction pipe and the impingement plate from overheating is flowing in the direction of the arrow, and is further formed between the overheating prevention cylinder 3 and the hot air nozzle 1. A hot air flow 8 for thermal expansion flows in the space in the direction of the arrow. Here, hot air flow 8
The gas fluid 6 and the gas flow 7 are usually in the same direction, but they are not necessarily in the same direction. Inside the overheating prevention cylinder 3, a coolant flow 2 is caused to flow in the direction of the arrow for cooling.
It is preferable that the gas introduction tube and / or the collision plate 5 have an overheat preventing function for suppressing the formation of aggregated microspheres and heat-fused bodies.
The shape of the collision plate is not particularly limited, and examples thereof include a spindle shape, a cone shape, a pyramid shape, a spherical shape, a hemispherical shape, and a combination thereof.

In the injection step in the first manufacturing method, the gas fluid 6 including the thermally expandable microspheres is caused to flow through a gas introduction pipe provided with the dispersion nozzle 4 at the outlet and installed inside the hot air flow 8, and the gas fluid 6 is Spray from the dispersion nozzle 4. The gas fluid 6 is not particularly limited as long as it is a gas fluid containing thermally expandable microspheres, but includes a thermally expandable microsphere and is an inert gas fluid such as air, nitrogen, argon, and helium. And preferred.
Further, the amount of water contained in the gas fluid 6 is preferably 30 g / m ³ or less, more preferably 9.3 g / m ³ or less, taking into account poor dispersion of the thermally expandable microspheres.
The flow rate of the gas fluid 6 is not particularly limited, but in the next dispersion step, it is adjusted so that any thermally expandable microsphere can be expanded in the hot air stream 8 by receiving the same thermal history as much as possible. It is preferable.

In the dispersion step in the first manufacturing method, the gas fluid 6 is collided with the collision plate 5 installed at the lower part of the dispersion nozzle 4, and the thermally expandable microspheres are operated to be uniformly dispersed in the hot air flow 8. The Here, the gas fluid 6 exiting from the dispersion nozzle 4 is guided toward the collision plate 5 together with the gas flow 7 and collides with it.
As the gas flow 7, the same gas as the gas fluid 6 can be used.

In the expansion step in the first manufacturing method, the dispersed thermally expandable microspheres are heated and expanded in the hot air stream 8 to the expansion start temperature or higher. Thereafter, the thermally expanded microspheres are cooled to a temperature below the softening point of the thermoplastic resin, which is the outer shell of the thermally expandable microspheres, by passing the cooled microspheres, and the thermally expanded microspheres are collected.
For the recovery, it is preferable to use a general solid-gas separation device such as a cyclone or a bag filter.

The second method for producing thermally expanded microspheres according to the present invention includes a gas fluid containing thermally expandable microspheres, which are the starting materials described above, provided with a dispersion nozzle at the outlet and installed outside the hot air flow. And flowing through the at least one gas introduction pipe, spraying from the dispersion nozzle, and dispersing the thermally expandable microspheres in the hot air flow (dispersion step); and dispersing the thermally expandable microspheres in the hot air flow And a step (expansion step) for expanding the mixture by heating to a temperature higher than the expansion start temperature.
This manufacturing method can be performed using, for example, a manufacturing apparatus including the foaming process section illustrated in FIG.

The foaming process section includes a hot air nozzle 11 disposed at the center and at least one dispersion nozzle 12 disposed at the lower periphery of the hot air nozzle 11. In the foaming process section, a hot air flow 13 for thermal expansion is caused to flow in the direction of the arrow inside the hot air nozzle 11, and a gas fluid 14 including thermally expandable microspheres is caused to flow from the dispersion nozzle 12 in the direction of the arrow. Yes. The gas fluid 14 is usually flowed at an angle so as not to face the hot air flow 13. The gas fluid 14 is a hot air flow 13.
May be flowed at a substantially right angle to.

In the dispersion step in the second manufacturing method, the gas fluid 14 containing the thermally expandable microspheres is jetted from at least one dispersion nozzle 12 installed outside the hot air flow 13 by using a quantitative feeder or the like, Inflatable microspheres are dispersed in the hot air stream. Examples of the gas fluid 14 include the same as the gas fluid 6 described above. Moreover, the moisture content and flow velocity of the gas fluid 14 can be the same as those of the gas fluid 6 described above.

In the expansion step in the second manufacturing method, the dispersed thermally expandable microspheres are heated to expand above the expansion start temperature in the hot air stream 13 to expand. Thereafter, the thermally expanded microspheres are recovered in the same manner as in the first manufacturing method.

In the first and second manufacturing methods, when the thermally expanded microspheres obtained after the expansion step further include a step of moistening with a liquid organic compound (wetting step), dust generation of the thermally expanded microspheres is prevented. Since the thermally expanded microspheres are mixed for use in various applications, dispersibility is improved, which is preferable. The liquid organic compound is not particularly limited. For example, the heat-expanded microspheres obtained can be appropriately selected according to the properties and intended use, and basically have the properties (1) and (2) shown below.
(1) The liquid organic compound has a boiling point higher than the vaporization temperature of the foaming agent encapsulated in the thermally expanded microspheres. (2) The thermoplastic resin in which the liquid organic compound is the outer shell of the thermally expanded microspheres. Do not dissolve or swell

In order to satisfy the requirement (1) shown above and to avoid volatilization during storage, the boiling point of the liquid organic compound is preferably 80 to 270 ° C, more preferably 90 to 260 ° C, and particularly preferably 100 to 250. ° C.
The requirement (2) shown above can improve the solvent resistance by using raw material microspheres produced by using the above-mentioned crosslinking agent in combination as the raw material in the present production method.
For this reason, the freedom degree of selection improves significantly about a liquid organic compound.

There is no limitation in particular about the kind of liquid organic compound. As the liquid organic compound, for example, when a composition obtained by wetting is used for a plastic, elastomer, sealant, paint, etc., dibutyl phthalate, diisooctyl phthalate, dioctyl adipate,
Plasticizers such as tricresyl phosphate, triethyl citrate, acetyl tributyl citrate, and octyl alcohol; when a composition obtained by wetting is used for a lightweight foamed molded article or adhesive, a simple substance such as dicyclopentadiene or styrene Examples include a polymer. Examples of liquid organic compounds other than those described above include nonionic surfactants, alkylene glycols, polyalkylene glycols, glycerin, silicone oil, liquid paraffin, and oils. These liquid organic compounds may be used as a mixture of two or more. Further, water may be used in place of the liquid organic compound.

The blending ratio between the thermally expanded microspheres and the liquid organic compound (or water) is not particularly limited, and is preferably determined in consideration of the surface properties of the thermally expanded microspheres and the degree of dust generation due to the true specific gravity. Specifically, a blending ratio that makes the dust generation of the thermally expanded microspheres inconspicuous is desirable. When the amount of the liquid organic compound is large, the liquid organic compound and the thermally expanded microspheres are partially uneven due to the excess liquid organic compound. From such a viewpoint, for example, the true specific gravity is 0.03 g / c.
The amount of the liquid organic compound is preferably about 90 parts by weight or less with respect to 10 parts by weight of the thermally expanded microspheres c. On the other hand, when the amount of the liquid organic compound is reduced, the generation of thermally expanded microspheres is noticeably not preferable.

In order to carry out the wetting step, the thermally expanded microspheres are shaken or stirred together with the liquid organic compound. The agitation / stirring can be performed using a general powder mixer, for example, a device that can be used for mixing the thermally expandable microspheres and the fine particle filler, or a counter-shaft rotor type mixer. .

The moistening step will be described in detail below, but is not limited thereto. A predetermined amount of thermally expanded microspheres are put into an apparatus used in the humidification process (hereinafter referred to as a humidification apparatus), and a liquid organic compound (or water) is added. At this time, the liquid organic compound is discharged from one discharge port (for example, 2 L / min or less) to the rocking or stirring surface of 0.07 m ² or more of the thermally expanded microsphere, and the liquid organic compound is added. Thereafter, the microspheres thermally expanded by this apparatus are shaken or stirred until they can be uniformly moistened. The discharge port is provided on or in the rocking or stirring surface. The rocking or stirring surface per discharge port does not decrease the movement of the microspheres due to the rocking or stirring of the thermally expanded microspheres due to the interference between the liquid materials coming out of the discharge ports, and the liquid organic compound It is set so that the microspheres can be sufficiently in contact with each other and can be uniformly moistened. In addition, the discharge amount of the liquid organic compound at this time is set so that the whole can be uniformly moistened by sufficiently contacting the swinging or stirring microspheres.

If the discharge port is movable and swings or moves on or in the stirring surface, it is very efficient. Depending on the movable movement speed, for example, a fixed discharge port is used at a movement speed of 20 cm / sec. It is possible to reduce the time required for rocking or stirring until the liquid substance can be uniformly moistened after the addition of the liquid substance.

This outlet may simply be the end of a pipe or hose. A shower-like mouth or a spray mouth may be used. By discharging the liquid organic compound with high viscosity to some extent and discharging the rod-shaped liquid, the microspheres do not scatter around too much. When spraying at a very high pressure, the microspheres that are rocking or stirring will be scattered around,
It becomes necessary to seal the humidifier and to collect the dust.

After adding the liquid organic compound to the thermally expanded microspheres, it is shaken or stirred until it can be uniformly wetted. The end point is determined by collecting samples from a plurality of parts in the humidifier and measuring each sample 0.5 to
The true specific gravity of 0.8 g may be measured by the liquid replacement method, and the determination may be made based on variations in the value, for example, standard deviation.

In the first and second production methods, the amount of water contained in the thermally expandable microspheres is 5% by weight or less, more preferably 3% by weight or less, considering the uniformity of heat expansion.
In the first and second manufacturing methods, by controlling the expansion conditions, the obtained thermally expanded microspheres may or may not have a reexpansion start temperature.
In the present invention, the microspheres having the re-expansion start temperature means that the thermally expanded microspheres once produced still have the property of thermal expansion. This means that a phenomenon of thermal expansion is observed. And the temperature which starts the heating expansion is called re-expansion start temperature. Further, the fact that the thermally expanded microsphere has a reexpansion start temperature is synonymous with the fact that the expansion ratio at the maximum (re) expansion temperature is more than 100%. On the other hand, the fact that the microsphere does not have a re-expansion start temperature means that the microsphere has almost completely thermally expanded.

There is no particular limitation on the control of the expansion conditions. For example, first, parameters such as the raw material supply volume, hot air flow rate and raw material dispersion gas amount are fixed, and the temperature of the hot air flow (hereinafter referred to as “hot air temperature”).
There is. ). Next, while changing the hot air temperature stepwise and fixing other parameters constant, the raw microspheres were expanded at each temperature, the true specific gravity of the obtained microspheres was measured, and the hot air temperature (x-axis) ) And true specific gravity (y-axis) are plotted. In this graph, by setting the temperature region corresponding to the lowest true specific gravity (minimum value in the graph) to the hot air temperature, the obtained thermally expanded microspheres can be manufactured so as not to have a reexpansion start temperature.

When producing expanded microspheres having a desired true specific gravity, the hot air temperature corresponding to the desired true specific gravity is set in the graph. As a result, the expansion conditions are controlled, and it is possible to manufacture thermally expanded microspheres having a desired reexpansion capacity.
Furthermore, when changing the raw material supply amount and / or the raw material dispersed gas amount, the hot air temperature and the like are changed in consideration of the amount of heat supplied by the hot air flow and the total heat capacity of the thermally expandable microsphere as the raw material, Control inflation conditions. For example, when increasing the raw material supply amount and the raw material dispersion gas amount, the hot air temperature is raised. When reducing the raw material supply amount and the raw material dispersion gas amount, the hot air temperature is lowered.

In the first and second manufacturing methods, energy efficiency is high, temperature control is easy, and almost the same thermal history can be continuously given to any thermally expandable microsphere that is a raw material.
High dispersibility in airflow. For this reason, the change in the coefficient of variation of the particle size distribution before and after expansion is small, and the quality (particularly, the particle size distribution and true specific gravity distribution) of the obtained thermally expanded microspheres is high. That is, the generation of aggregated microspheres contained in the obtained thermally expanded microspheres can be suppressed as much as possible, and the content of raw materials and slightly expanded microspheres can be extremely reduced.

The obtained thermally expanded microspheres are filled in the tire and rim assembly, for example, so that when the tire is damaged and the tire internal pressure is reduced, the tire damage portion sealing material and / or the tire It can be used as an internal pressure imparting material.
Here, the tire damage part sealing material means that when the tire is damaged and the internal filling gas starts to leak from the damage part, the raw microspheres or the thermally expanded microspheres ride on the flow of the filling gas and immediately receive the damage part. It can be densely packed and can instantly seal the damaged part. In addition, the tire internal pressure imparting material is a material in which a tire is damaged, and after sealing the damaged portion with a tire damaged portion sealing material, the tire is bent due to a decrease in internal pressure. When the spheres or thermally expanded microspheres rub against each other and the temperature rises due to the friction, the starting microspheres or the thermally expanded microspheres expand when the starting temperature of the raw or thermally expanded microspheres is reached. Thus, this means that the tire internal pressure can be increased.

Usually, when a car or the like travels, the temperature of the thermally expanded microspheres increases due to contact between the thermally expanded microspheres filled in the tire or between the tire inner wall rubber and the thermally expanded microspheres due to the rotational movement. There is. If the microspheres that are thermally expanded during running in a state where the tire is not damaged reach the expansion start temperature, the thermally expanded microspheres may start to expand, and the tire internal pressure imparting function may not be exhibited when the tire is damaged. is there. Furthermore, when traveling at high speed, there is a higher risk that the tire internal pressure imparting function will not be exhibited when the tire is damaged than during normal traveling.
However, when the thermally expanded microspheres obtained by the production method of the present invention are used by being filled in a tire, as described later, in normal internal pressure running performance evaluation and normal internal pressure high speed running performance evaluation, it is good. An evaluation result can be obtained.

B. Thermally expanded microspheres The thermally expanded microspheres according to the present invention are composed of an outer shell made of a thermoplastic resin and a foaming agent encapsulated in the outer shell and having a boiling point lower than the softening point of the thermoplastic resin. Diameter is 1
It is a thermally expanded microsphere obtained by a production method in which a thermally expandable microsphere having a diameter of ˜100 μm is heated to expand to a temperature higher than the expansion start temperature. Here, the heat-expandable microspheres used as a raw material are not particularly limited, but the heat-expandable microspheres described above in “A. Method for producing thermally expanded microspheres” are preferable. The production method for expanding the thermally expandable microspheres by heating to a temperature higher than the expansion start temperature is not particularly limited, but is the production method described in the above-mentioned “A. Method for producing thermally expanded microspheres”. Is preferred.

The average particle diameter of the thermally expanded microsphere is not particularly limited and can be freely designed according to the application. For example, considering the retention rate of the foaming agent by the outer shell, the durability of the thermally expanded microspheres, etc., it is preferably 1 to 1000 μm, more preferably 5 to 800 μm, and particularly preferably 10 to 500 μm.

The content of aggregated microspheres contained in the thermally expanded microspheres is preferably 5% by weight or less, more preferably 1% by weight or less, and still more preferably 0. 5% by weight or less, particularly preferably 0.3% by weight or less. The presence of the aggregated microspheres is confirmed by visual observation with an electron microscope, and the quantification thereof can be performed by measuring the screening residual amount after screening, as will be described in detail in the following examples.

The content of microspheres having a true specific gravity of 0.79 g / cc or more contained in the thermally expanded microspheres at 25 ° C. is preferably 5% by weight or less in consideration of the uniformity of the true specific gravity and the like. Preferably it is 3 weight% or less, More preferably, it is 2 weight% or less, Most preferably, it is 1 weight% or less. The content of microspheres of 0.79 g / cc or more is measured by quantifying the sediment component after separation with a specific gravity difference using isopropyl alcohol (specific gravity at 25 ° C .: 0.79).

In addition, for the thermally expanded microsphere, the change in the coefficient of variation CV of the particle size distribution before and after the thermal expansion does not greatly change the coefficient of variation CV of the thermally expandable microsphere used as a raw material after expansion,
Considering keeping the particle size uniform, it is preferably within ± 10%, more preferably within ± 5%, even more preferably within ± 3%, and particularly preferably within ± 1%. The change of the coefficient of variation CV is defined by (the coefficient of variation of the particle size distribution of the obtained thermally expanded microspheres) − (the coefficient of variation of the particle size distribution of the thermally expandable microspheres that are raw materials). The coefficient of variation CV of the particle size distribution of the thermally expanded microspheres is preferably 30% or less, more preferably 27% or less, and particularly preferably 25% or less.

The thermally expanded microspheres of the present invention have a very small content of aggregated microspheres and a content of microspheres having a large true specific gravity. Moreover, the change of the variation coefficient of the particle size distribution before and after being manufactured by thermal expansion is small.

The thermally expanded microspheres of the present invention may or may not have a re-expansion start temperature.
In particular, when the thermally expanded microsphere has a reexpansion start temperature, the thickness of the thermoplastic resin constituting the outer shell is relatively thick and is not easily damaged by an external force. Therefore, for example, when obtaining a hollow body composition containing thermally expanded microspheres, the collapse of the microspheres during mixing with the substrate can be suppressed. Also,
In hollow molded articles containing thermally expanded microspheres, it is possible to prevent heat aging and cure shrinkage over time. In addition, when the thermally expanded microsphere has a reexpansion start temperature, it is preferable that the thermally expandable microsphere A described later has physical properties.

In the thermally expanded microsphere of the present invention, the volume expansion ratio from the thermally expandable microsphere before expansion is not particularly limited, but is preferably 8 times or more, more preferably 15 times or more, and most preferably 30 times. That's it. The true specific gravity of the thermally expanded microsphere is not particularly limited, but is preferably 0.30 g / cc or less, more preferably 0.25 g / cc or less, and most preferably 0.20 g / cc or less. In addition, in this specification, “
“True specific gravity” means the “average true specific gravity”.

In addition, in the thermally expanded microspheres of the present invention, the encapsulating retention rate of the foaming agent is not particularly limited, but considering the amount of the foaming agent leaking from the outer shell, performance uniformity, stability over time, etc.
It is preferably 80% or more, more preferably 85% or more, and particularly preferably 90% or more.
When a fluorine-containing compound is used as the foaming agent, it is preferably 90% or more, more preferably 95% or more, and particularly preferably 97% or more.

When the thermally expanded microspheres of the present invention are wetted with a liquid organic compound that does not dissolve the outer shell, dust generation of the thermally expanded microspheres is prevented, and the thermally expanded microspheres are used for various applications. Dispersibility is improved when mixing with the above, which is preferable. The type and amount of the liquid organic compound can be the same as those described in “A. Method for producing thermally expanded microspheres”.

In particular, the foaming agent encapsulated in the thermally expanded microspheres is “A. Method for producing thermally expanded microspheres”.
As described in detail above, those containing a fluorine-containing compound having an ether structure and containing no chlorine and bromine atoms and having 2 to 10 carbon atoms are preferred. As a result, when the obtained thermally expanded microspheres are filled inside the tire and rim assembly, even if the tire is damaged and the internal pressure of the tire is reduced, the tire damage part sealing function is very good. The tire internal pressure imparting function can be exhibited. In both normal internal pressure running performance evaluation and normal internal pressure high speed running performance evaluation,
Good evaluation results can be obtained. Moreover, when the reexpansion start temperature is set for the thermally expanded microsphere, it is preferably 90 ° C. or higher, more preferably 100 ° C. or higher, and further preferably 1
It can be set to 10 ° C. or higher, particularly preferably 120 ° C. or higher. When used as a tire damage part sealing material and / or a tire internal pressure imparting material, it can be used without being limited by the tire use environment.

The thermally expanded microsphere of the present invention is not particularly limited, but can be used as a light weight filler for putty, paint, sealing material, mortar, paper clay, ceramics, and the like.

C. Thermally expandable microsphere A
The thermally expandable microsphere of the present invention (hereinafter sometimes referred to as “thermally expandable microsphere A”)
A thermally expandable microsphere composed of an outer shell made of a thermoplastic resin and a foaming agent encapsulated in the outer shell and having a boiling point equal to or lower than the softening point of the thermoplastic resin, the following (I) to (IV) It is a microsphere having a novel thermal expansibility having the constituent elements shown.
(I) The average particle diameter is in the range of 1-1000 μm,
(II) The expansion ratio at the maximum expansion temperature exceeds 100%,
(III) The content of aggregated microspheres is 5% by weight or less,
(IV) The content of microspheres having a true specific gravity of 0.79 g / cc or more at 25 ° C. is 5% by weight or less.

The heat-expandable microsphere A is heated so as to have sufficient capacity to re-expand the raw material microsphere (that is, to have a re-expansion start temperature) in the section “A. Method for producing thermally expanded microsphere”. It can be manufactured by inflating. Further, in the thermally expandable microsphere A, the expansion ratio at the maximum expansion temperature of the thermally expandable microsphere A is equal to the expansion ratio at the maximum expansion temperature of the raw material microsphere and the maximum of the microsphere obtained by almost completely thermal expansion. It is located between the expansion ratio at the expansion temperature. The same can be said for the average particle diameter and true specific gravity.

The average particle diameter of the heat-expandable microsphere A is the retention rate of the foaming agent in the outer shell, the degree of re-expansion,
Considering the durability of the thermally expanded microspheres, it is 1-1000 μm, preferably 5-8.
It is 00 μm, more preferably 10 to 500 μm, particularly preferably 15 to 350 μm.

The expansion ratio at the maximum expansion temperature of the thermally expandable microsphere A does not substantially lose the thermal expandability,
Considering that it becomes a heat-expandable microsphere, it is more than 100%, preferably 105% or more, more preferably 120% or more, particularly preferably 130% or more, most preferably 150% or more. It is. It should be noted that the fact that the expansion ratio at the maximum expansion temperature of the thermally expandable microsphere A is more than 100% is almost synonymous with the fact that the thermally expandable microsphere A has an expansion start temperature.

The content of aggregated microspheres contained in the heat-expandable microsphere A is 5% by weight or less, preferably 1% by weight or less, more preferably 0.5% by weight, considering the uniformity of true specific gravity and the like. Less than,
Particularly preferred is 0.3% by weight or less. The presence of the agglomerated microspheres is confirmed by the method described above.

In the thermally expandable microsphere A, the content of microspheres having a true specific gravity of 0.79 g / cc or more at 25 ° C. is 5% by weight or less, preferably 3% by weight, considering the uniformity of true specific gravity and the like.
Hereinafter, it is more preferably 2% by weight or less, particularly preferably 1% by weight or less. In addition, 0.
The content of microspheres of 79 g / cc or more is isopropyl alcohol (specific gravity at 25 ° C .:
0.79) is used to determine the sediment components after separation with a specific gravity difference.

As described in “A. Method for producing thermally expanded microsphere”, the thermally expandable microsphere A preferably has a fine particle filler attached to the outer surface. Thereby, the improvement of the dispersibility at the time of use and fluidity | liquidity improvement are aimed at. As the fine particle filler, the same ones as described above can be used. The average particle size of the fine particle filler is not particularly limited, but is preferably 10 μm or less, more preferably 8 μm or less, and particularly preferably 5 μm or less.
Further, the thermally expandable microsphere A is preferably in a state of being wetted with a liquid organic compound (or water) as described above.

As described above, the thermally expandable microsphere A of the present invention has an extremely small content of aggregated microspheres and a content of microspheres having a large true specific gravity. Moreover, in the thermally expandable microsphere A, the thickness of the thermoplastic resin constituting the outer shell is relatively thick and is not easily damaged by an external force. Therefore, when obtaining a hollow body composition containing thermally expanded microspheres, the collapse of the microspheres during mixing with the substrate can be suppressed. In addition, in a hollow body molded product including thermally expanded microspheres, it is possible to prevent thermal aging and cure shrinkage over time.

The thermally expanded microsphere A of the present invention includes substantially the same thermally expanded microspheres as those having a reexpansion start temperature, and can be used for similar applications.

D. Hollow body composition and hollow body molded article A hollow body composition according to the present invention comprises a base material component, the thermally expanded microspheres and / or thermally expandable microspheres A (hereinafter referred to as "thermally expanded microspheres and / Or thermally expandable microsphere A "
It may be simply referred to as “microsphere a”. ). In the microsphere a, since the thickness of the thermoplastic resin constituting the outer shell is relatively thick, damage due to external force is unlikely to occur when the components are blended and kneaded to produce a hollow body composition. In addition, since the microspheres a have an appropriate thermal expansion, curing shrinkage can be prevented during the molding of the hollow body composition, and the obtained hollow body molded product does not have the problem of heat settling over time.

The thermally expanded microspheres and / or thermally expandable microspheres A included in the hollow body composition of the present invention are not particularly limited as long as they are each described above, but as thermally expanded microspheres Are preferably microspheres that have a re-expandable capacity (ie, have a re-expansion start temperature). Further, those having a low content of aggregated microspheres are preferred. The content of the agglomerated fine particles is preferably 5% by weight or less, more preferably 3% by weight in consideration of the uniform dispersibility of the microspheres in the base material, the surface property and the strength uniformity of the resulting hollow body molded product % Or less, particularly preferably 2% by weight or less. The particle size distribution coefficient of variation CV is 30% or less, more preferably 27% or less, and particularly preferably 25% or less.

The base material component contained in the hollow body composition is not particularly limited. For example, vinyl chloride resin, vinyl acetate resin, acrylic resin, ethylene vinyl acetate resin, epoxy resin, polyurethane, melamine resin, polyester, silicon resin, etc. Organic materials such as: inorganic materials such as ceramic (clay) and cement. Further, as the base material component, the above-mentioned “A.
You may mix | blend the liquid organic compound demonstrated in the wetting process of "the manufacturing method of the thermally expanded microsphere." These substrate components may be used alone or in combination of two or more.

The mixing ratio of the microspheres a with respect to the entire hollow body composition is not particularly limited, but the effect of addition, weight reduction, prevention of curing shrinkage at the time of molding, heat loss over time in the obtained hollow body molded product, hollow In consideration of uniform mixing in the production of the body composition, it is preferably 0.1 to 30% by weight, more preferably 0.3 to 25% by weight, particularly preferably 0.5 to 5 to 20% by weight. .

In addition to the base material components and microspheres a, the hollow body composition is a filler that has been conventionally used for weight reduction such as perlite, fly ash, shirasu balloon, glass balloon, phenol balloon, carbon balloon, alumina bubble, and expanded styrene beads. Agents; reinforcing agents such as glass fibers and aramid fibers; fillers such as silica, talc and calcium carbonate; additives such as pigments such as titanium oxide and magnesium oxide may be blended. These additives may be used alone or in combination of two or more.

In particular, when a filler is included as an additive, there is a problem that microspheres thermally expanded by external force and thermally expandable microspheres A are significantly damaged when producing a hollow body composition. Since the thermoplastic resin constituting the outer shell is relatively thick, the occurrence of breakage is greatly suppressed.

About the manufacturing method of a hollow body composition, if each component is mixed, there will be no limitation in particular. As a manufacturing apparatus, a static mixer, a disper, etc. can be mentioned, for example.
The hollow body composition can be used for applications intended to reduce the weight of putty, paint, sealing material, mortar, paper clay, ceramics, and the like.
By molding the hollow body composition produced in this way, the weight can be reduced sufficiently, curing shrinkage during molding can be prevented, and the problem of heat settling over time does not occur, and dimensional stability A hollow molded article having a high height can be obtained. When the hollow body molded product is an inorganic molded product in particular, the whole body may be fired after molding to form closed cells in the inorganic molded product.

Examples The present invention will be described in detail by the following examples and comparative examples, but the present invention is not limited to these examples.

Measurement method and definition ( measurement of average particle size and particle size distribution)
Laser diffraction particle size distribution analyzer (HEROS & RODOS made by SYMPATEC)
It was used. The dispersion pressure of the dry dispersion unit was 5.0 bar and the degree of vacuum was 5.0 mbar, measured by a dry measurement method, and the D50 value was taken as the average particle size.

[Measurement of true specific gravity]
The true specific gravity was measured by a liquid displacement method (Archimedes method) using isopropyl alcohol at a temperature of 25 ° C.

(Measurement of content of aggregated microspheres)
The presence of aggregated microspheres was confirmed by visual observation with an electron microscope.
When the average particle diameter of thermally expanded microspheres (thermally expandable microspheres A) is R, the content of aggregated microspheres contained in the thermally expanded microspheres (thermally expandable microspheres A) is determined by an opening. It was calculated from the residual amount after screening using a 2.0R screen, which is 2.0 times R. Here, 2.0R is a value obtained by multiplying R by a that satisfies 1.95 ≦ a <2.05. In addition, when there is no screen having a mesh opening of 2.0R, the residual screening amount using a screen having a mesh opening of 1.8R to 2.0R (excluding 2.0R), and the mesh opening is Proportional amount of screening remaining when screen with 2.0R mesh is used from screen residual amount using screen in range of 2.0R to 2.2R (excluding 2.0R) Calculated by the allocation method. Opening range of 1.8R to 2.0R (however,
The screens and openings are in the range of 2.0R to 2.2R (excluding 2.0R) (however, 2
. In all cases, the screen size is 2.0R.
Choose a screen that is as close as possible. The volume of the sample used for screening was 1 L or more.

[Measurement of moisture content of thermally expandable microspheres]
As a measuring apparatus, a Karl Fischer moisture meter (MKA-510N type, manufactured by Kyoto Electronics Industry Co., Ltd.) was used for measurement.

[Measurement of encapsulation rate of foaming agent enclosed in thermally expandable microspheres]
Place 1.0 g of thermally expandable microspheres in a stainless steel evaporating dish with a diameter of 80 mm and a depth of 15 mm.
The weight (W ₁ ) was measured. 30 ml of acetone was added and dispersed uniformly, left at room temperature for 30 minutes, then heated at 120 ° C. for 2 hours, and the weight (W ₂ ) after drying was measured. The encapsulation rate of the foaming agent is calculated by the following formula.
Inclusion rate (% by weight) = (W ₁ −W ₂ ) (g) /1.0 (g) × 100− (water content) (% by weight)
(In the formula, the moisture content is measured by the above method.)

[Internal retention rate]
The encapsulated retention rate of the foaming agent is a ratio of the encapsulating rate (G ₂ ) of the foaming agent after expansion to the encapsulating rate (G ₁ ) of the foaming agent before expansion, and is calculated by the following formula.
Inclusion retention rate (%) = G ₂ / G ₁ × 100

[(Re) expansion start temperature, maximum (re) expansion temperature and measurement of expansion ratio at that temperature]
DMA (DMA Q800 type, manufactured by TA instruments) was used. Place 0.5 mg of thermally expandable microspheres (or thermally expanded microspheres) in an aluminum cup with a diameter of 6.0 mm and a depth of 4.8 mm, and place an aluminum lid with a diameter of 5.6 mm and a thickness of 0.1 mm on it. A sample was prepared. The sample height (H
₁ ) measured. 1 to 20 to 300 ° C with a force of 0.01 N applied by the pressurizer
Heating was performed at a rate of temperature increase of 0 ° C./min, and the displacement of the pressurizer in the vertical direction was measured. The displacement start temperature in the positive direction was defined as the (re) expansion start temperature, and the temperature when the maximum displacement amount (H ₂ ) was indicated was defined as the maximum (re) expansion temperature. The (re) expansion magnification (E) at the maximum (re) expansion temperature is calculated by the following calculation formula.
E (%) = H ₂ / H ₁ × 100

(Volume expansion ratio)
Volume expansion ratio (A) has an average particle diameter before the heat-expandable microspheres to thermal expansion (R ₁₎ and the average particle size of heat-expanded microspheres (R ₂₎ is measured, the calculation formula shown below Calculated.
_{A = (R 2 / R 1} ) 3 ( times)
(In the formula, R ₁ is the average particle diameter of the thermally expandable microspheres before thermal expansion, and R ₂ is the average particle diameter of the thermally expanded microspheres.)

[Evaluation of normal internal pressure running performance during tire filling]
Inside the assembly of the tire (tire size: 175 / 70R13, tire internal volume 21L) and rim (rim size: 5J-13), a thermally expandable microsphere (or thermal expansion equivalent to 80% by volume of the internal space) Filled with microspheres) and the tire internal pressure is increased to 200 kP with nitrogen.
It adjusted so that it might become a. The tire was mounted on a passenger car and evaluated by checking the presence or absence of expansion or contraction of thermally expandable microspheres (or thermally expanded microspheres) after traveling for 30 minutes at a speed of 60 km / h. The presence or absence of expansion was confirmed by measuring the particle size distribution of the microspheres. When the variation of the average particle diameter before and after running was within + 3%, it was marked as ◯, and when it exceeded + 3%, it was marked as x.
Confirmation of the presence or absence of shrinkage is ○, -3 when the variation of the average particle size before and after running is within -3%
When exceeding%, it evaluated as x.

[Evaluation of normal internal pressure and high-speed running performance during tire filling]
In the above normal internal pressure running performance evaluation, the speed of the passenger car is changed from 60 km / h to a high speed of 150 km.
Except for changing to / h, the evaluation was made in the same way as the normal internal pressure running performance evaluation.

[Evaluation of running performance when tire is damaged when filling inside tire]
In the above normal internal pressure running performance evaluation, the speed of the passenger car is changed from 60 km / h to 100 km / h.
The vehicle was run for 30 minutes in the same manner as the internal pressure running performance evaluation except that Thereafter, a nail having a diameter of 3 mm and a length of 50 mm was stepped on the tire from the contact surface toward the inside of the tire, and after confirming that the tire internal pressure became atmospheric pressure, the tire was run at a speed of 90 km / h. When the travelable distance is less than 80 km, ×, when 80 to 150 km, ○, when it is 150 km or more, ◎
It was evaluated.

[Measurement of specific gravity of paint]
It measured using the specific gravity cup (100cc, Ohira Rika Kogyo Co., Ltd. make).

[Measurement of specific gravity of coating film]
The specific gravity of the coating film was measured by a liquid replacement method (Archimedes method) using ion-exchanged water at a temperature of 25 ° C.

[Example A1]
Matsumoto Microsphere-F-50 (manufactured by Matsumoto Yushi Seiyaku Co., Ltd.)
Outer shell thermoplastic resin: nitrile copolymer, foaming agent: isobutane, average particle size: 20 μm,
Coefficient of variation: 35%), using a manufacturing apparatus equipped with a foaming process section shown in FIG.
Expanded microspheres were produced.
Regarding the expansion conditions, the raw material supply amount is 0.1 kg / h, and the raw material dispersion gas amount is 0.03 m ³ / mi.
n, hot air flow rate 0.5m ³ / min, hot air temperature 130 ° C.

The resulting expanded microspheres had an average particle size of 83 μm, a coefficient of variation of 36%, and a true specific gravity of 0.0.
31 g / cc and the volume expansion ratio were 71.5 times. Moreover, in the obtained expanded microsphere, the microsphere whose true specific gravity in 25 degreeC is 0.79 g / cc or more was not confirmed. In addition, there was no screening residue by screening using a screen having an opening of 150 μm and an opening of 175 μm. When calculated from the respective values by the proportional distribution method, the content of the agglomerated microspheres was 0% by weight.

[Comparative Example A1]
Matsumoto Microsphere-F-50 used in Example A1 was applied to a steel belt to a thickness of about 2 mm. This steel belt is heated at a speed of 1 m / min at a heating zone (temperature: 130 ° C.
, Length: 3 m) and a cooling zone (temperature: 10 ° C., length: 2 m) following this heating zone to produce expanded microspheres.

The obtained expanded microspheres had an average particle size of 86 μm, a coefficient of variation of 49%, and a true specific gravity of 0.0.
It was 38 g / cc and the volume expansion ratio was 79.5 times. Further, in the obtained expanded microsphere, the content of the microsphere having a true specific gravity at 25 ° C. of 0.79 g / cc or more was 11% by weight. The content of the residue obtained by screening using a screen having an opening of 150 μm was 0.8% by weight. Moreover, the residual amounts of screening were 0.5% by weight and 0.4% by weight when screens having an opening of 165 μm and an opening of 175 μm were used, respectively. When calculated by the proportional distribution method from the respective values, the content of the agglomerated microspheres was 0.4% by weight.

[Example A2]
In Example A1, Matsumoto Microsphere-F-100 (manufactured by Matsumoto Yushi Seiyaku Co., Ltd., outer shell thermoplastic resin: nitrile copolymer, foaming agent: instead of thermally expandable microsphere Matsumoto Microsphere-F-50 Extensive microspheres were produced by heating and expanding in the same manner as in Example A1, except that isopentane, average particle size: 25 μm, coefficient of variation: 37%) was used, and the hot air temperature was set to 180 ° C.

The resulting expanded microspheres had an average particle size of 97 μm, a coefficient of variation of 36%, and a true specific gravity of 0.0.
It was 28 g / cc, and the volume expansion ratio was 58.4 times. Moreover, in the obtained expanded microsphere, the microsphere whose true specific gravity in 25 degreeC was 0.79 g / cc or more was not confirmed. No residue was confirmed by screening using a screen having an opening of 200 μm.
Further, there was no screening residue by screening using a screen having an opening of 175 μm and an opening of 210 μm. When calculated from the respective values by the proportional distribution method, the content of the agglomerated microspheres was 0% by weight.

[Comparative Example A2]
In Comparative Example A1, except that Matsumoto Microsphere-F-100 shown in Example A2 was used instead of Matsumoto Microsphere-F-50, and the temperature of the heating zone was set to 180 ° C.,
The expanded microspheres were heated and expanded by the same manufacturing method as in Comparative Example A1.

The resulting expanded microspheres had an average particle size of 100 μm, a coefficient of variation of 45%, and a true specific gravity of 0.2.
030 g / cc and the volume expansion ratio were 64.0 times. Further, in the obtained expanded microsphere, the content of the aggregated microsphere is 0.3% by weight, and the true specific gravity at 25 ° C. is 0.79 g / c.
The content of microspheres that were c or more was 15% by weight. A screen having an opening of 200 μm was used for quantification of the aggregated microspheres.

[Example A3]
In Example A1, instead of Matsumoto Microsphere-F-50, a thermally expandable microsphere prototype 1 (
Outer shell thermoplastic resin: nitrile copolymer, foaming agent: isohexane, average particle size: 35 μm
The coefficient of variation was 20%), and the hot air temperature was set to 240 ° C., and the mixture was heated and expanded by the same manufacturing method as in Example A1 to manufacture expanded microspheres.

The resulting expanded microspheres had an average particle size of 130 μm, a coefficient of variation of 20%, and a true specific gravity of 0.2.
021 g / cc and the volume expansion ratio were 51.1 times. Moreover, in the obtained expanded microsphere, the microsphere whose true specific gravity in 25 degreeC was 0.79 g / cc or more was not confirmed. No residue was confirmed by screening using a screen having an opening of 200 μm. There was no screening residue by screening using a screen having an opening of 235 μm and an opening of 275 μm, respectively. When calculated from the respective values by the proportional distribution method, the content of the agglomerated microspheres was 0% by weight.

[Comparative Example A3]
Comparative Example A1 is the same as Comparative Example A1, except that the thermally expandable microsphere prototype 1 shown in Example A3 is used instead of Matsumoto Microsphere-F-50, and the temperature of the heating zone is set to 240 ° C. The expanded microspheres were produced by heating and expanding according to the production method.

The resulting expanded microspheres had an average particle size of 100 μm, a coefficient of variation of 31%, and a true specific gravity of 0.1.
The volume expansion ratio was 030 g / cc and the volume expansion ratio was 66.6 times. Further, in the obtained expanded microsphere, the content of the aggregated microsphere is 5.6% by weight, and the true specific gravity at 25 ° C. is 0.79 g / c.
The content of microspheres that were c or more was 12% by weight. A screen having an opening of 200 μm was used for quantification of the aggregated microspheres.

[Example A4]
Thermally expandable microsphere prototype 1 and ultrafine talc (made by Nippon Talc Co., Ltd.) shown in Example A3
Product name: SG-1000, average particle size: 2.0 μm) at a weight ratio of 6: 4, and uniformly mixed using a super mixer (manufactured by Kawata Co., Ltd.), and ultrafine talc adhered to the outer surface. Thermally expandable microspheres were obtained.
A manufacturing method similar to Example A1 except that in Example A1, instead of Matsumoto Microsphere-F-50, thermally expandable microspheres with ultrafine talc adhered to the outer surface were used, the hot air temperature was set to 240 ° C. Was expanded by heating to produce expanded microspheres.

The obtained expanded microspheres had an average particle size of 124 μm, a coefficient of variation of 21%, and a true specific gravity of 0.2.
026 g / cc and the volume expansion ratio were 44.4 times. Moreover, in the obtained expanded microsphere, the microsphere whose true specific gravity in 25 degreeC was 0.79 g / cc or more was not confirmed. No residue was confirmed by screening using a screen having an opening of 200 μm. There was no screening residue by screening using a screen having an opening of 225 μm and an opening of 250 μm, respectively. When calculated from the respective values by the proportional distribution method, the content of the agglomerated microspheres was 0% by weight.

[Example B1]
Matsumoto Microsphere-F-50 (manufactured by Matsumoto Yushi Seiyaku Co., Ltd.)
Outer shell thermoplastic resin: nitrile copolymer, foaming agent: isobutane, average particle size: 20 μm,
(Coefficient of variation: 35%) was used, and the expanded microspheres were manufactured by heating and expanding with a manufacturing apparatus having the foaming process section shown in FIG.
Regarding the expansion conditions, the raw material supply rate is 0.1 kg / h, and the raw material dispersion gas amount is 0.05 m ³ / mi.
n, hot air flow rate was set to 1.0 m ³ / min, and hot air temperature was set to 140 ° C.

The average diameter of the expanded microspheres obtained was 98 μm, the coefficient of variation was 36%, and the true specific gravity was 0.0.
22 g / cc and the volume expansion ratio were 117.6 times. Moreover, in the obtained expanded microsphere, the microsphere whose true specific gravity in 25 degreeC is 0.79 g / cc or more was not confirmed.
No residue was confirmed by screening using a screen having an opening of 150 μm. Further, there was no screening residue by screening using a screen having an opening of 180 μm and an opening of 200 μm. When calculated from the respective values by the proportional distribution method, the content of the agglomerated microspheres was 0% by weight.

[Comparative Example B1]
Matsumoto Microsphere-F-50 used in Example B1 was applied to a steel belt to a thickness of about 2 mm. This steel belt is heated at a speed of 1 m / min in a heating zone (temperature: 140 ° C.
, Length: 3 m) and a cooling zone (temperature: 10 ° C., length: 2 m) following this heating zone to produce expanded microspheres.
The resulting expanded microspheres had an average particle size of 102 μm, a coefficient of variation of 48%, and a true specific gravity of 0.2.
The volume expansion ratio was 020 g / cc and the volume expansion ratio was 132.7 times. Further, in the obtained expanded microsphere, the content of the microsphere having a true specific gravity at 25 ° C. of 0.79 g / cc or more is 12% by weight.
Met. The content of the residue obtained by screening using a screen having an opening of 150 μm was 1.8% by weight. Moreover, the residual amounts of screening were 0.8% by weight and 0.5% by weight when screens having an opening of 200 μm and an opening of 215 μm were used. When calculated from each value by the proportional distribution method, the content of the agglomerated microspheres is 0.7.
% By weight.

[Example B2]
In Example B1, Matsumoto Microsphere-F-100 (manufactured by Matsumoto Yushi Seiyaku Co., Ltd., outer shell thermoplastic resin: nitrile copolymer, foaming agent: instead of thermally expandable microsphere Matsumoto Microsphere-F-50 Extensive microspheres were produced by heating and expanding in the same manner as in Example B1, except that isopentane, average particle size: 25 μm, coefficient of variation: 37%) was used and the hot air temperature was set to 170 ° C.
The resulting expanded microspheres had an average particle size of 93 μm, a coefficient of variation of 38%, and a true specific gravity of 0.0.
33 g / cc and the volume expansion ratio were 51.5 times. Moreover, in the obtained expanded microsphere, the microsphere whose true specific gravity in 25 degreeC is 0.79 g / cc or more was not confirmed. There was no screening residue obtained by screening using a screen having an opening of 175 μm and an opening of 200 μm. When calculated from the respective values by the proportional distribution method, the content of the agglomerated microspheres was 0% by weight.

[Comparative Example B2]
In Comparative Example B1, except that Matsumoto Microsphere-F-100 shown in Example B2 was used instead of Matsumoto Microsphere-F-50, and the temperature of the heating zone was set to 170 ° C.,
The expanded microspheres were heated and expanded by the same manufacturing method as in Comparative Example B1.
The resulting expanded microspheres had an average particle size of 85 μm, a coefficient of variation of 48%, and a true specific gravity of 0.0.
It was 40 g / cc and the volume expansion ratio was 39.3 times. Further, in the obtained expanded microspheres, the content of microspheres having a true specific gravity at 25 ° C. of 0.79 g / cc or more was 14% by weight. The content of the residue obtained by screening using a screen having an opening of 200 μm was 0.8% by weight. Moreover, the residual amounts of screening when using a screen having an opening of 165 μm and an opening of 175 μm were 2.5% by weight and 1.8% by weight, respectively. When calculated by the proportional distribution method from the respective values, the content of the aggregated microspheres was 2.2% by weight.

[Example B3]
In Example B1, instead of Matsumoto Microsphere-F-50, a thermally expandable microsphere prototype 1 (
Outer shell thermoplastic resin: nitrile copolymer, foaming agent: isohexane, average particle size: 35 μm
The coefficient of variation was 20%), and the hot air temperature was set to 230 ° C., and the mixture was heated and expanded in the same manner as in Example B1, thereby manufacturing expanded microspheres.
The obtained expanded microspheres had an average particle size of 120 μm, a coefficient of variation of 21%, and a true specific gravity of 0.2.
The volume expansion ratio was 00.3 g / cc and the volume expansion ratio was 40.3 times. Moreover, in the obtained expanded microsphere, the microsphere whose true specific gravity in 25 degreeC is 0.79 g / cc or more was not confirmed.
No residue was confirmed by screening using a screen having an opening of 200 μm. Further, there was no screening residue obtained by screening using a screen having an opening of 225 μm and an opening of 250 μm. When calculated from the respective values by the proportional distribution method, the content of the agglomerated microspheres was 0% by weight.

[Comparative Example B3]
Comparative Example B1 is the same as Comparative Example B1, except that the thermally expandable microsphere prototype 1 shown in Example B3 is used instead of Matsumoto Microsphere-F-50, and the temperature of the heating zone is set to 230 ° C. The expanded microspheres were produced by heating and expanding according to the production method.
The obtained expanded microspheres had an average particle size of 117 μm, a coefficient of variation of 31%, and a true specific gravity of 0.1.
031 g / cc and the volume expansion ratio were 37.3 times. Further, in the obtained expanded microsphere, the content of the microsphere having a true specific gravity at 25 ° C. of 0.79 g / cc or more was 15% by weight. The content of the residue obtained by screening using a screen having an opening of 200 μm was 6.6% by weight. Further, the residual amounts of screening when using a screen having an opening of 215 μm and an opening of 250 μm were 5.6 wt% and 3.2 wt%, respectively. When calculated from the respective values by the proportional distribution method, the content of the aggregated microspheres was 4.3% by weight.

[Example B4]
Thermally expansible microsphere prototype 1 and ultrafine talc (made by Nippon Talc Co., Ltd.) shown in Example B3
Product name: SG-1000, average particle size: 2.0 μm) at a weight ratio of 6: 4 and uniformly mixed using a super mixer (manufactured by Kawata Co., Ltd.), and ultrafine talc adhered to the outer surface. Thermally expandable microspheres were obtained.
A manufacturing method similar to Example A1 except that in Example B1, instead of Matsumoto Microsphere-F-50, thermally expandable microspheres with ultrafine talc adhered to the outer surface were used and the hot air temperature was set to 230 ° C. Was expanded by heating to produce expanded microspheres.

The resulting expanded microspheres had an average particle size of 119 μm, a coefficient of variation of 21%, and a true specific gravity of 0.2.
029 g / cc and the volume expansion ratio were 39.3 times. Moreover, in the obtained expanded microsphere, the microsphere whose true specific gravity in 25 degreeC was 0.79 g / cc or more was not confirmed. No residue was confirmed by screening using a screen having an opening of 200 μm. Further, there was no screening residue obtained by screening using a screen having an opening of 225 μm and an opening of 250 μm. When calculated from the respective values by the proportional distribution method, the content of the agglomerated microspheres was 0% by weight.

[Example C1]
To 500 g of ion-exchanged water, 150 g of sodium chloride, 3.0 g of adipic acid-diethanolamine condensate, 20 g of colloidal silica (active ingredient amount: 20%) and 0.15 g of sodium nitrite are added and mixed uniformly. It was set as the water phase.
Acrylonitrile (180 g), methacrylonitrile (45 g), methacrylic acid (75 g), trimethylolpropane trimethacrylate (1.2 g), azobisisobutyronitrile (2.0 g) and C ₃ F ₇ OCH _{3 (} 150 g) are mixed, stirred and dissolved, and this is the oil phase. It was.

The water phase and the oil phase are mixed, premixed with a homomixer at 3,000 rpm for 2 minutes,
The suspension was stirred at 000 rpm for 2 minutes to obtain a suspension. This was transferred to a reactor and purged with nitrogen, followed by polymerization at 61 ° C. for 20 hours while stirring. After polymerization, the polymerization product was filtered and dried. The obtained thermally expandable microspheres have an average particle diameter of 25 μm, a coefficient of variation of 24%, and an expansion start temperature of 143.
The maximum expansion temperature was 205 ° C.
The encapsulating rate of the foaming agent enclosed in the thermally expandable microspheres was measured and found to be 31.8% by weight.
Although the ignition source was brought close to the thermally expandable microsphere, it did not burn.

The obtained thermally expandable microspheres were heated and expanded with a manufacturing apparatus having a foaming process section shown in FIG. 1 to manufacture expanded microspheres.
Regarding the expansion conditions, the raw material supply rate is 1.0 kg / h, and the raw material dispersion gas amount is 0.05 m ³ / min.
The hot air flow rate is fixed at 0.5 m ³ / min, and the hot air temperature is 30 as shown in Table 1, respectively.
The temperature was set to 0 ° C, 350 ° C, 400 ° C, 450 ° C, and 500 ° C.
The physical properties of the obtained expanded microspheres (thermally expandable microspheres) were evaluated, and the results are shown in Table 1.

表１の結果から明らかなように、本実施例で得られた熱膨張性微小球を、タイヤとリム
の組立体に充填して用いた場合、通常内圧（高速）走行性能及びタイヤ受傷時の走行性能
ともに良好な性能を示すことがわかる。

As is apparent from the results of Table 1, when the thermally expandable microspheres obtained in this example are used by filling the tire and rim assembly, the normal internal pressure (high speed) running performance and the tire are damaged. It can be seen that both the running performance shows good performance.

[Comparative Example C1]
Using the high temperature thermostat (manufactured by Sanyo Electric Co., Ltd.), the heat-expandable microspheres obtained in Example C1 were 140 ° C., 160 ° C., 180 ° C., 200 ° C., 220, respectively, as shown in Table 2. Expanded microspheres were produced by heating for 1 minute at a set temperature of ° C.
The physical properties of the obtained expanded microspheres (thermally expandable microspheres) were evaluated, and the results are shown in Table 2.

表２の結果から明らかなように、本比較例で得られた熱膨張性微小球は、タイヤとリム
の組立体に充填して用いた場合、とくに通常内圧走行性能においては良好な結果を示して
いるが、通常内圧高速走行性能においては悪く、真比重０．７９ｇ／ｃｃ以上の微小球の
含有率が高いことに起因すると思われる。
また、実施例Ｃ１および比較例Ｃ１における凝集微小球の含有率を比較すると明白であ
るが、原料である熱膨張性微小球が均一な粒度分布であっても、オーブン加熱のような従
来公知の発泡方法で膨張させるのであるならば、粒度分布が均一で凝集微小球のない膨張
した微小球は得られない。

As is apparent from the results in Table 2, the thermally expandable microspheres obtained in this comparative example show good results, particularly in normal internal pressure running performance, when used in a tire-rim assembly. However, the internal pressure is usually poor in high-speed running performance, which is considered to be due to the high content of microspheres having a true specific gravity of 0.79 g / cc or more.
In addition, it is clear when the content ratios of the aggregated microspheres in Example C1 and Comparative Example C1 are compared. Even if the thermally expandable microspheres as the raw material have a uniform particle size distribution, a conventionally known method such as oven heating is known. If expanded by the foaming method, expanded microspheres having a uniform particle size distribution and no agglomerated microspheres cannot be obtained.

[Example C2]
In Example C1, 150 g of C ₃ F ₇ OCH ₃ (specific gravity 1.41) was converted to normal pentane 6
Polymerization was conducted in the same manner as in Example C1, except that the specific gravity was changed to 5 g (specific gravity 0.63).
The obtained thermally expandable microspheres had an average particle size of 30 μm, a coefficient of variation CV of 33%, an expansion start temperature of 155 ° C., and a maximum expansion temperature of 189 ° C. When the encapsulation rate of the foaming agent enclosed in the thermally expandable microspheres was measured, it was 16.6% by weight.
When the ignition source was brought close to the thermally expansible microsphere, it burned vigorously, so we gave up the evaluation of running performance by filling the tire and rim assembly.

The obtained heat-expandable microspheres are heated and expanded with a manufacturing apparatus having a foaming process section shown in FIG.
Expanded microspheres were produced. For expansion conditions, the raw material supply rate 1.0 kg / h, the raw material dispersion gas volume 0.05 m ³ / min, and fixed in a hot-air flow rate 0.5 m ³ / min, a hot air temperature as shown in Table 3, respectively, 300 C, 350 ° C., 400 ° C., 450 ° C., and 500 ° C. were set.
The physical properties of the obtained expanded microspheres (thermally expandable microspheres) were evaluated, and the results are shown in Table 3.

[Comparative Example C2]
In Example C1, polymerization was performed in the same manner as in Example C1, except that 75 g of methacrylic acid was changed to 75 g of vinyl acetate.
The obtained thermally expandable microspheres had an average particle diameter of 27 μm, a coefficient of variation CV of 25%, an expansion start temperature of 95 ° C., and a maximum expansion temperature of 157 ° C. When the encapsulation rate of the foaming agent enclosed in the thermally expandable microspheres was measured, it was 30.9% by weight. Although the ignition source was brought close to the thermally expandable microsphere, it did not burn.

Using the high-temperature thermostat (manufactured by Sanyo Electric Co., Ltd.), the thermally expandable microspheres obtained above were 110 ° C., 130 ° C., 150 ° C., 170 ° C. and 190 ° C., respectively, as shown in Table 4. Expanded microspheres were produced by heating at a set temperature for 1 minute. The physical properties of the obtained expanded microspheres (thermally expandable microspheres) were evaluated, and the results are shown in Table 4.

表４の結果から明らかなように、本比較例で得られた熱膨張性微小球は、タイヤとリム
の組立体に充填して用いた場合、タイヤ受傷時走行性能を示すものもあるが、通常内圧走
行性能、通常内圧高速走行性能が悪いことがわかる。これは走行中にタイヤ内の熱膨張性
微小球が（再）膨張開始温度に達することに起因すると思われる。

As is clear from the results in Table 4, the thermally expandable microspheres obtained in this comparative example, when used in a tire and rim assembly, may show running performance at the time of tire damage, It can be seen that the normal internal pressure running performance and the normal internal pressure high speed running performance are poor. This seems to be due to the fact that the thermally expandable microspheres in the tire reach the (re) expansion start temperature during running.

[Example C3]
In Example C1, 235 g of acrylonitrile, 60 g of methacrylonitrile, 5.0 g of methyl methacrylate, 1.2 g of ethylene glycol dimethacrylate, 2.0 g of azobisisobutyronitrile and 150 g of C ₃ HF ₆ OCH ₃ were used as the oil phase. Polymerization was carried out in the same manner as in Example C1 except that.
The obtained thermally expandable microspheres had an average particle diameter of 42 μm, a coefficient of variation CV of 26%, an expansion start temperature of 140 ° C., and a maximum expansion temperature of 198 ° C. The encapsulating rate of the foaming agent enclosed in the thermally expandable microspheres was measured and found to be 32.9% by weight. Although the ignition source was brought close to the thermally expandable microsphere, it did not burn.

The obtained heat-expandable microspheres are heated and expanded with a manufacturing apparatus having a foaming process section shown in FIG.
Expanded microspheres were produced. For expansion conditions, the raw material supply rate 1.0 kg / h, the raw material dispersion gas volume 0.05 m ³ / min, and fixed in a hot-air flow rate 0.5 m ³ / min, a hot air temperature as shown in Table 5, respectively, 250 C, 300, 350, 400, and 450 ° C were set.
The physical properties of the obtained expanded microspheres (thermally expandable microspheres) were evaluated, and the results are shown in Table 5.

表５の結果から明らかなように、本実施例で得られた熱膨張性微小球は、タイヤとリム
の組立体に充填して用いた場合、特に通常内圧走行性能、タイヤ受傷時走行性能において
良好な性能を示す。
〔比較例Ｃ３〕
実施例Ｃ３において、メタクリル酸メチル５．０ｇをメタクリル酸５．０ｇとした以外
は実施例Ｃ１と同様に重合を行った。
得られた熱膨張性微小球は、平均粒子径４０μｍ、変動係数ＣＶ２６％、膨張開始温度
１４３℃、最大膨張温度１９９℃であった。熱膨張性微小球に封入された発泡剤の内包率
を測定したところ、３１．８重量％であった。熱膨張性微小球に着火源を近づけたが燃焼
することはなかった。

As is clear from the results in Table 5, the thermally expandable microspheres obtained in this example are used in the normal internal pressure running performance and tire running performance when the tire / rim assembly is filled. Shows good performance.
[Comparative Example C3]
In Example C3, polymerization was performed in the same manner as in Example C1, except that 5.0 g of methyl methacrylate was changed to 5.0 g of methacrylic acid.
The obtained thermally expandable microspheres had an average particle diameter of 40 μm, a coefficient of variation CV of 26%, an expansion start temperature of 143 ° C., and a maximum expansion temperature of 199 ° C. The encapsulating rate of the foaming agent enclosed in the thermally expandable microspheres was measured and found to be 31.8% by weight. Although the ignition source was brought close to the thermally expandable microsphere, it did not burn.

Using a high-temperature incubator (manufactured by Sanyo Electric Co., Ltd.), as shown in Table 6, 120 ° C., 1
Expanded microspheres were produced by heating at preset temperatures of 40 ° C., 160 ° C., 180 ° C., and 200 ° C. for 1 minute. The physical properties of the obtained expanded microspheres (thermally expandable microspheres) were evaluated, and the results are shown in Table 6.

表６の結果から明らかなように、本比較例で得られた熱膨張性微小球は、タイヤとリム
の組立体に充填して用いた場合、通常内圧走行性能、タイヤ受傷時走行性能において良好
な性能を示すが、通常内圧高速走行性能は悪いことがわかる。

As is clear from the results in Table 6, the thermally expandable microspheres obtained in this comparative example are good in normal internal pressure running performance and tire running performance when tire and rim assemblies are used. It can be seen that the internal pressure high-speed running performance is poor.

[Example C4]
500 g of the heat-expandable microspheres obtained in Example C1 and 100 g of magnesium stearate (average particle size: 2 μm, melting point: 132 ° C.) were mixed for 30 minutes using a super mixer (manufactured by Kawata Co., Ltd.). Thermally expandable microspheres with magnesium stearate adhered to the shell surface were produced.
The thermally expandable microspheres thus obtained have an average particle diameter of 24.9 μm,
The coefficient of variation CV was 25%. The encapsulating rate of the foaming agent enclosed in the heat-expandable microspheres was measured and found to be 30.4% by weight.

The thermally expandable microspheres were heated and expanded with a manufacturing apparatus having a foaming process section shown in FIG. 1 to manufacture expanded microspheres. For expansion conditions, the raw material supply rate 1.0 kg / h, the raw material dispersion gas volume 0.05 m ³ / min, and fixed in a hot-air flow rate 0.5 m ³ / min, a hot air temperature as shown in Table 7, respectively, 300 C, 350 ° C., 400 ° C., 450 ° C., and 500 ° C. were set. The physical properties of the obtained expanded microspheres (thermally expandable microspheres) were evaluated, and the results are shown in Table 7.

表７の結果から明らかなように本実施例で得られた熱膨張性微小球は、タイヤとリムの
組立体に充填して用いた場合、通常内圧（高速）走行性能及びタイヤ受傷時の走行性能と
もに良好な性能を示すことがわかる。実施例Ｃ１に対して熱融着防止剤の効果により特に
タイヤ受傷時の走行性能が向上していることが確認される。

As is apparent from the results in Table 7, when the thermally expandable microspheres obtained in this example are filled in a tire and rim assembly, the normal internal pressure (high speed) running performance and the running when the tire is damaged It can be seen that both performances are good. It is confirmed that the running performance at the time of tire damage is particularly improved by the effect of the heat fusion inhibitor with respect to Example C1.

[Example C5]
500 g of thermally expandable microspheres obtained in Example C1 and 100 g of carbon black (acetylene black, average particle size: 42 nm) were mixed for 30 minutes using a super mixer (manufactured by Kawata Co., Ltd.), and carbon on the outer shell surface. Thermally expandable microspheres with black deposits were produced.
The thermally expandable microspheres thus obtained have an average particle diameter of 24.7 μm,
The coefficient of variation CV was 26%. When the encapsulation rate of the foaming agent enclosed in the thermally expandable microspheres was measured, it was 30.8% by weight.

The thermally expandable microspheres were heated and expanded with a manufacturing apparatus having a foaming process section shown in FIG. 1 to manufacture expanded microspheres. For expansion conditions, the raw material supply rate 1.0 kg / h, the raw material dispersion gas volume 0.05 m ³ / min, and fixed in a hot-air flow rate 0.5 m ³ / min, a hot air temperature as shown in Table 8, respectively, 300 C, 350 ° C., 400 ° C., 450 ° C., and 500 ° C. were set. The physical properties of the obtained expanded microspheres (thermally expandable microspheres) were evaluated, and the results are shown in Table 8.

表８の結果から明らかなように本実施例で得られた熱膨張性微小球は、タイヤとリムの
組立体に充填して用いた場合、通常内圧（高速）走行性能及びタイヤ受傷時の走行性能と
もに良好な性能を示すことがわかる。実施例Ｃ１に対して熱融着防止剤の効果により特に
タイヤ受傷時の走行性能が向上していることが確認される。

As is apparent from the results in Table 8, when the thermally expandable microspheres obtained in this example were filled in a tire and rim assembly, the normal internal pressure (high speed) running performance and running at the time of tire damage were observed. It can be seen that both performances are good. It is confirmed that the running performance at the time of tire damage is particularly improved by the effect of the heat fusion inhibitor with respect to Example C1.

[Example C6]
In Example C1, 120 g of acrylonitrile, 30 g of methacrylonitrile, 150 g of methacrylic acid, 1.2 g of trimethylolpropane trimethacrylate, 2.0 g of azobisisobutyronitrile and 150 g of C ₂ HF ₄ OC ₂ H ₂ F ₃ were added to the oil phase. Example C except that
Polymerization was conducted in the same manner as in 1.
The obtained thermally expandable microspheres had an average particle size of 29 μm, a coefficient of variation CV of 23%, an expansion start temperature of 183 ° C., and a maximum expansion temperature of 230 ° C. The encapsulating rate of the foaming agent enclosed in the thermally expandable microspheres was measured and found to be 32.5% by weight. Although the ignition source was brought close to the thermally expandable microsphere, it did not burn.

The obtained thermally expandable microspheres were heated and expanded with a manufacturing apparatus having the foaming process section of FIG. 2 described in [Method of manufacturing thermally expanded microspheres] to manufacture expanded microspheres. For expansion conditions,
Material supply amount 1.0 kg / h, the raw material dispersion gas volume 0.05 m ³ / min, hot air flow rate of 0.5 m ³ /
and the hot air temperature is 400 ° C., 450 ° C. and 500 ° C., respectively, as shown in Table 9.
The temperature was set to 550 ° C and 600 ° C. The physical properties of the obtained expanded microspheres (thermally expandable microspheres) were evaluated, and the results are shown in Table 9.

表９の結果から明らかなように本実施例で得られた熱膨張性微小球は、タイヤとリムの
組立体に充填して用いた場合、通常内圧（高速）走行性能及びタイヤ受傷時の走行性能と
もに良好な性能を示すことがわかる。

As is clear from the results in Table 9, when the thermally expandable microspheres obtained in this example are filled in a tire and rim assembly, the normal internal pressure (high speed) running performance and the running when the tire is damaged It can be seen that both performances are good.

[Example C7]
In Example C1, except that 72 g of acrylonitrile, 18 g of methacrylonitrile, 210 g of methacrylic acid, 1.2 g of trimethylolpropane trimethacrylate, 2.0 g of azobisisobutyronitrile and 150 g of C ₄ F ₉ OCH ₃ were used as the oil phase. Polymerization was carried out in the same manner as in Example C1.
The obtained thermally expandable microspheres had an average particle size of 36 μm, a coefficient of variation CV of 23%, an expansion start temperature of 188 ° C., and a maximum expansion temperature of 232 ° C. When the encapsulation rate of the foaming agent enclosed in the thermally expandable microspheres was measured, it was 32.7% by weight. Although the ignition source was brought close to the thermally expandable microsphere, it did not burn.

The obtained heat-expandable microspheres are heated and expanded with a manufacturing apparatus having a foaming process section shown in FIG.
Expanded microspheres were produced. For expansion conditions, the raw material supply rate 1.0 kg / h, the raw material dispersion gas volume 0.05 m ³ / min, and fixed in a hot-air flow rate 0.5 m ³ / min, a hot air temperature as shown in Table 10, respectively, 400 C, 450 ° C, 500 ° C, 550 ° C and 600 ° C were set. The physical properties of the obtained expanded microspheres (thermally expandable microspheres) were evaluated, and the results are shown in Table 10.

表１０の結果から明らかなように本実施例で得られた熱膨張性微小球は、タイヤとリム
の組立体に充填して用いた場合、通常内圧（高速）走行性能及びタイヤ受傷時の走行性能
ともに良好な性能を示すことがわかる。

As is apparent from the results in Table 10, when the thermally expandable microspheres obtained in this example were filled in a tire and rim assembly, the normal internal pressure (high speed) running performance and running at the time of tire damage were observed. It can be seen that both performances are good.

[Comparative Example C4]
In Example C1, 24 g of acrylonitrile, 6.0 g of methacrylonitrile, 270 g of methacrylic acid, 1.2 g of trimethylolpropane trimethacrylate, 2.0 g of azobisisobutyronitrile and 150 g of C ₄ F ₉ OCH ₃ were used as the oil phase. Polymerization was carried out in the same manner as in Example C1 except that.
The obtained thermally expandable microspheres had an average particle diameter of 31 μm and a coefficient of variation of CV 26%.
Expansion performance was not confirmed.

[Example D1]
Polyvinyl chloride (Sumitomo Chemical Smitrit PCX, softening temperature: 80 ° C.) 100 g, heavy calcium carbonate (Shiraishi Calcium Whiteon SB, average particle size: 2.2 μm) 1
00 g, soft calcium carbonate (Kamijima Chemical Co., Ltd., light calcium carbonate, average particle size: 0.3
μg), 50 g of plasticizer (Sanso Sizer DINP manufactured by Shin Nippon Chemical Co., Ltd., phthalate plasticizer) and 10 g of solvent (mineral spirits manufactured by Nippon Oil Co., Ltd.) were mixed with a Glen mixer to prepare a base paint.
Next, 1.0 g of the thermally expanded microspheres obtained in Example B3 and 99 g of the base paint were mixed to prepare a lightweight paint (paint specific gravity: 0.90). In addition, the thermally expanded microsphere had a reserve capacity for re-expansion, the maximum re-expansion temperature was 196 ° C., and the re-expansion magnification was 180%. The obtained lightweight paint was pressurized for the time shown in Table 11 under the conditions of room temperature and pressure of 15 MPa, and then the specific gravity of the paint was measured. Thereafter, a lightweight paint was applied to an iron plate having a thickness of 7 mm with a coating thickness of 2 mm, and baked in an oven at 140 ° C. for 30 minutes to prepare a coating film, and the coating film specific gravity was measured. 17
The film was reheated in an oven at 0 ° C. for 30 minutes, and the specific gravity of the coating film was measured. The results are shown in Table 11.

[Comparative Example D1]
A light-weight paint (paint specific gravity 0.94) was prepared in the same manner as in Example D1, except that the expanded microspheres obtained in Comparative Example B3 were used instead of the expanded microspheres obtained in Example B3. did.
The physical properties were measured in the same manner as in Example D1. The results are shown in Table 12.

In Example D1, the specific gravity of the paint hardly changes even when the pressure treatment time is long.
In Comparative Example D1, the longer the pressure treatment time is, the smaller the microspheres thermally expanded by external force are, and the specific gravity of the paint is increased. Further, in Example D1, there is almost no difference between the specific gravity of the coating film after baking and the specific gravity of the coating film after reheating, and no thermal settling is observed, whereas in Comparative Example D1, the specific gravity of the coating film after baking and after the reheating There is a significant difference in the specific gravity of the coating film, and thermal settling is observed.

The method for producing thermally expanded microspheres of the present invention is a method for producing thermally expanded microspheres with little change in the coefficient of variation in particle size distribution before and after thermal expansion, and extremely low content of aggregated microspheres and microspheres with large true specific gravity. Can be manufactured.

The thermally expanded microspheres of the present invention have very low physical properties of aggregated microspheres and microspheres with a large true specific gravity. Thermally expanded microspheres are also less likely to be damaged by external force, and when blended in a hollow body composition for the purpose of weight reduction, curing shrinkage during molding can be prevented. The problem of heat settling can be solved.

The heat-expandable microsphere A of the present invention is less likely to be damaged by external force, and can be prevented from curing shrinkage during molding when blended with a hollow body composition for weight reduction. Can solve the problem of general heat settling.
The hollow molded article of the present invention can be sufficiently reduced in weight, can prevent curing shrinkage at the time of molding, has no problem of thermal settling over time, and has high dimensional stability.

When the thermally expanded microspheres and thermally expandable microspheres A of the present invention contain a specific fluorine-containing compound as a foaming agent, the tire and rim assembly is filled into the tire damage part sealing material and tire internal pressure application When used as a material, it can exhibit a good tire damage part sealing function and tire internal pressure imparting function.

The thermally expandable microsphere containing the specific fluorine-containing compound of the present invention as a foaming agent is a raw material of the thermally expanded microsphere and the thermally expandable microsphere A, and the microsphere obtained therefrom is an assembly of a tire and a rim. When filled inside and used as a tire damage part sealing material and a tire internal pressure imparting material, a good tire damage part sealing function and tire internal pressure imparting function can be exhibited. With this thermally expandable microsphere, good evaluation results can be obtained not only in the normal internal pressure running performance evaluation but also in the normal internal pressure high speed running performance evaluation.

It is the schematic of the foaming process part of the manufacturing apparatus used with the manufacturing method of this invention. It is the schematic of the foaming process part of the manufacturing apparatus used with another manufacturing method of this invention.

Explanation of symbols

DESCRIPTION OF SYMBOLS 1,11 Hot air nozzle 2 Refrigerant flow 3 Overheating prevention cylinder 4, 12 Dispersion nozzle 5 Colliding plate 6, 14 Gaseous fluid containing thermally expandable microsphere 7 Gas flow 8, 13 Hot air flow

Claims (6)

A method for producing thermally expandable microspheres comprising an outer shell made of a thermoplastic resin, and a foaming agent encapsulated therein and having a boiling point equal to or lower than the softening point of the thermoplastic resin,
Mixing the monomer mixture with the blowing agent and then subjecting the resulting mixture to suspension polymerization in an aqueous suspension,
The monomer mixture includes a nitrile monomer and a carboxyl group-containing monomer as essential components, and the weight ratio of the nitrile monomer is 20 to 80% by weight with respect to the monomer mixture. The weight ratio of the carboxyl group-containing monomer is 80 to 20% by weight,
The blowing agent has an ether structure and does not contain a chlorine atom and a bromine atom, and has 2 to 2 carbon atoms.
10 fluorine-containing compounds,
A method for producing thermally expandable microspheres. A method for producing thermally expandable microspheres comprising an outer shell made of a thermoplastic resin, and a foaming agent encapsulated therein and having a boiling point equal to or lower than the softening point of the thermoplastic resin,
Mixing the monomer mixture with the blowing agent and then subjecting the resulting mixture to suspension polymerization in an aqueous suspension,
The blowing agent has an ether structure and does not contain a chlorine atom and a bromine atom, and has 2 to 2 carbon atoms.
10 fluorine-containing compounds,
The re-expansion start temperature of the thermally expandable microsphere is 100 ° C. or higher.
A method for producing thermally expandable microspheres. The heat according to claim 1 or 2, further comprising a step of adhering at least one kind of heat fusion inhibitor selected from an organic compound having a melting point of 90 ° C or higher and an inorganic compound having a layered structure to the outer surface of the outer shell. A method for producing expandable microspheres. A thermal expansion composed of an outer shell made of a thermoplastic resin, a foaming agent encapsulated therein and having a boiling point not higher than the softening point of the thermoplastic resin, and an anti-fusing agent attached to the outer surface of the outer shell. A method for producing a functional microsphere,
Mixing a monomer mixture with the blowing agent and then subjecting the resulting mixture to suspension polymerization in an aqueous suspension;
Adhering to the outer surface of the outer shell at least one heat fusion inhibitor selected from an organic compound having a melting point of 90 ° C. or higher and an inorganic compound having a layered structure,
The blowing agent has an ether structure and does not contain a chlorine atom and a bromine atom, and has 2 to 2 carbon atoms.
10 fluorine-containing compounds,
A method for producing thermally expandable microspheres. The fluorine-containing compound is C ₃ HF ₆ OCH ₃ , C ₂ HF ₄ OC ₂ H ₂ F ₃ , C ₃ F ₇ OC
At least one selected from H ₃ , C ₄ F ₉ OCH ₃ and C ₄ F ₉ OC ₂ H ₅ ;
The manufacturing method of the thermally expansible microsphere in any one of Claims 1-4. The method for producing thermally expandable microspheres according to any one of claims 1 to 5, wherein the aqueous suspension contains a water-soluble reducing agent.

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