JP6077328B2 - Flame retardant resin composition for supercritical fluid fine foam molding and molded product thereof - Google Patents

Description

  The present invention relates to a flame-retardant resin composition for supercritical fluid microfoam molding having excellent flame retardancy even after supercritical fluid microfoam molding, and a molded product thereof. More specifically, by adding a specific amount of a polycarbonate-polydiorganosiloxane copolymer resin, the flame retardancy for supercritical fluid microfoam molding is excellent in flame retardancy even in supercritical fluid microfoam molding with a high weight reduction rate. The present invention relates to a conductive resin composition and a molded product thereof.

  Aromatic polycarbonate resins are widely used industrially because they have excellent mechanical and thermal properties. However, since the aromatic polycarbonate resin has a high melt viscosity, it has a drawback of poor flowability and poor moldability. Many polymer alloys with other thermoplastic resins have been developed to improve the flowability of aromatic polycarbonate resins. Among them, polymer alloys with styrenic resins typified by ABS resins are widely used in the OA equipment field, the electronic and electrical equipment field, the automobile field, and the like. In particular, there is a strong demand for flame resistance of resin materials used mainly for OA equipment, home appliances, etc., and in order to meet these demands, polymer products of aromatic polycarbonate resin and ABS resin are particularly large products recently. In order to meet the demand for flame retardancy such as 5VB, UL94, which is a necessary safety standard, has been studied.

Conventionally, flame retardants in such polymer alloys are generally used in combination with a halogen-based flame retardant having bromine and a flame retardant aid such as antimony trioxide. For example, regarding 5VB flame retardancy, a flame retardant and a flame retardant aid are added to a blend of an aromatic polycarbonate resin and an ABS resin, and specific L / D such as polytetrafluoroethylene and talc having fibril forming ability are added. A method of adding an inorganic filler has been proposed. (See Patent Document 1)
However, in recent years, flame retardant studies using organophosphorus flame retardants that do not contain a halogen-containing compound containing bromine have become active due to the generation of harmful substances during combustion. For example, many compositions have been proposed in which an organophosphorus flame retardant and further polytetrafluoroethylene having a fibril-forming ability are added to a polymer alloy of an aromatic polycarbonate resin and an ABS resin, and related knowledge is widely known. (See Patent Document 2)

  An improved flame retardancy formulation by blending a polycarbonate-organopolysiloxane copolymer resin with an aromatic polycarbonate resin is disclosed in Patent Document 3, but a polycarbonate resin composition containing no flame retardant is a Although excellent in stability, long-term heat resistance, etc., it was insufficient to achieve flame retardance sufficient to satisfy the UL94 5V standard required for large-sized equipment such as OA equipment. Further, Patent Document 4 discloses a flame retardancy improving prescription by blending a phosphoric ester with an aromatic polycarbonate resin containing a specific amount of silicon and a polycarbonate-organopolysiloxane copolymer resin. Since the phosphoric acid ester is not added with a silicate mineral, it does not reach the UL94 5V standard in a thin wall. Furthermore, although the flame retardant improved prescription by blending an organic sulfonic acid metal salt is also disclosed in Patent Document 5, although some improvement in the flame retardant effect is seen, such as OA equipment. It was insufficient to achieve flame retardance sufficient to satisfy the UL94 5V standard required for large equipment. In addition, non-halogen and non-phosphorous flame retardant effects are disclosed by adding a functional group-containing silicone compound and an inorganic filler to a polycarbonate resin, a polycarbonate-polydiorganosiloxane copolymer resin, and a styrene resin. (Refer to Patent Document 6) However, although a silicone flame retardant can impart flame retardancy while maintaining heat resistance, it is insufficient to satisfy high flame retardancy such as 5 VB with a thin wall.

In addition, regardless of the field or application, an environmentally conscious design has been made that focuses on reducing the amount of petroleum resources used by reducing the amount of resin used, or improving fuel efficiency by reducing the weight of vehicle parts, As part of this, manufacturing methods that reduce the weight and reduce the amount of resin used, such as thin wall design, hollow molding, and foam molding, have been adopted.
Among these, a resin composition used for foam molding, particularly supercritical fluid fine foam molding, has also been studied. For example, by adding a silicone compound to a polycarbonate resin composition, a method for obtaining a good foam at the time of supercritical fluid fine foam molding (see Patent Document 7), or a resin containing a polycarbonate-polydiorganosiloxane copolymer is used. Although a method for obtaining a molded article excellent in light reflectivity and flame retardancy by performing critical fluid foam molding (see Patent Document 8) is disclosed, any resin composition is a supercritical fluid having a high weight reduction rate. It has not yet achieved UL94 5VB with a thin wall in the fine foam molding.
As described above, there is a demand for a resin composition having a high level of flame retardancy that achieves UL94 5VB with a thin wall in supercritical fluid microfoam molding with a high weight reduction rate, but it has not been obtained. It is.

JP-A-2-1991162 JP-A-2-115262 Japanese Patent No. 3037588 Japanese Patent No. 3457805 JP-A-8-302178 Japanese Patent No. 3616791 JP 2008-127466 A JP 2003-49018 A

  In view of the above, an object of the present invention is to provide a flame retardant resin composition for supercritical fluid fine foam molding having excellent flame retardancy so that UL94 5VB can be obtained in a thin wall in a supercritical fluid fine foam molded product, and the same. It is to provide a molded article.

As a result of intensive studies to solve the above problems, the present inventor has found that a polycarbonate resin, a specific amount of a polycarbonate-polydiorganosiloxane copolymer resin, a styrene resin typified by an ABS resin, a phosphorus flame retardant, a silicate salt By blending minerals and anti-drip agents, it is difficult for supercritical fluid microfoam molding that satisfies the balance of flame retardancy, impact resistance and fluidity at a high level in supercritical fluid microfoam molding with high weight reduction rate. A method for obtaining a flammable resin composition has been found, and the present invention has been completed. The weight reduction rate was calculated based on the following formula.
Weight reduction rate (%) = 100 × {(specific gravity of molded product obtained by supercritical fine foam molding) − (specific gravity of molded product obtained by normal molding (without supercritical fine foam molding))} / (Specific gravity of molded product obtained by normal molding (without supercritical fine foam molding))

  According to the present invention, the above-mentioned problems are solved by (C) with respect to 100 parts by weight of a resin component comprising (A) a polycarbonate resin (component A) and (B) a specific polycarbonate-polydiorganosiloxane copolymer resin (component B). ) Styrenic resin (C component) 3-45 parts by weight, (D) Phosphorus flame retardant (D component) 3-35 parts by weight, (E) Silicate mineral (E component) 0.1-30 parts by weight, And (F) a supercritical oil containing 0.1 to 3 parts by weight of an anti-drip agent (component F) and having a polydiorganosiloxane content of component B in the composition of 0.2 to 0.6% by weight. This is achieved by the flame retardant resin composition for fluid fine foam molding. Details of the present invention will be described below.

(A component: polycarbonate resin)
The polycarbonate resin used in the present invention is obtained by reacting a dihydric phenol and a carbonate precursor. Examples of the reaction method include an interfacial polymerization method, a melt transesterification method, a solid phase transesterification method of a carbonate prepolymer, and a ring-opening polymerization method of a cyclic carbonate compound.

  Representative examples of the dihydric phenol used here include hydroquinone, resorcinol, 4,4′-biphenol, 1,1-bis (4-hydroxyphenyl) ethane, and 2,2-bis (4-hydroxyphenyl). ) Propane (commonly called bisphenol A), 2,2-bis (4-hydroxy-3-methylphenyl) propane, 2,2-bis (4-hydroxyphenyl) butane, 1,1-bis (4-hydroxyphenyl)- 1-phenylethane, 1,1-bis (4-hydroxyphenyl) cyclohexane, 1,1-bis (4-hydroxyphenyl) -3,3,5-trimethylcyclohexane, 2,2-bis (4-hydroxyphenyl) Pentane, 4,4 ′-(p-phenylenediisopropylidene) diphenol, 4,4 ′-(m-phenylenediisopropyl Pyridene) diphenol, 1,1-bis (4-hydroxyphenyl) -4-isopropylcyclohexane, bis (4-hydroxyphenyl) oxide, bis (4-hydroxyphenyl) sulfide, bis (4-hydroxyphenyl) sulfoxide, bis (4-hydroxyphenyl) sulfone, bis (4-hydroxyphenyl) ketone, bis (4-hydroxyphenyl) ester, bis (4-hydroxy-3-methylphenyl) sulfide, 9,9-bis (4-hydroxyphenyl) Examples include fluorene and 9,9-bis (4-hydroxy-3-methylphenyl) fluorene. A preferred dihydric phenol is bis (4-hydroxyphenyl) alkane, and bisphenol A is particularly preferred from the viewpoint of impact resistance, and is widely used.

In the present invention, in addition to bisphenol A-based polycarbonate, which is a general-purpose polycarbonate, it is possible to use a special polycarbonate produced using other dihydric phenols as the A component.
For example, as part or all of the dihydric phenol component, 4,4 ′-(m-phenylenediisopropylidene) diphenol (hereinafter sometimes abbreviated as “BPM”), 1,1-bis (4-hydroxy) Phenyl) cyclohexane, 1,1-bis (4-hydroxyphenyl) -3,3,5-trimethylcyclohexane (hereinafter sometimes abbreviated as “Bis-TMC”), 9,9-bis (4-hydroxyphenyl) Polycarbonate (homopolymer or copolymer) using fluorene and 9,9-bis (4-hydroxy-3-methylphenyl) fluorene (hereinafter sometimes abbreviated as “BCF”) has dimensions due to water absorption. It is suitable for applications where the demands for change and shape stability are particularly severe. These dihydric phenols other than BPA are preferably used in an amount of 5 mol% or more, particularly 10 mol% or more of the entire dihydric phenol component constituting the polycarbonate.

In particular, when high rigidity and better hydrolysis resistance are required, it is particularly preferable that the component A constituting the resin composition is a copolymerized polycarbonate of the following (1) to (3). is there.
(1) BPM is 20 to 80 mol% (more preferably 40 to 75 mol%, more preferably 45 to 65 mol%) in 100 mol% of the dihydric phenol component constituting the polycarbonate, and BCF Of 20 to 80 mol% (more preferably 25 to 60 mol%, more preferably 35 to 55 mol%).
(2) BPA is 10 to 95 mol% (more preferably 50 to 90 mol%, more preferably 60 to 85 mol%) in 100 mol% of the dihydric phenol component constituting the polycarbonate, and BCF Is 5 to 90 mol% (more preferably 10 to 50 mol%, more preferably 15 to 40 mol%).
(3) BPM is 20 to 80 mol% (more preferably 40 to 75 mol%, more preferably 45 to 65 mol%) in 100 mol% of the dihydric phenol component constituting the polycarbonate, and Bis -Copolymer polycarbonate in which TMC is 20 to 80 mol% (more preferably 25 to 60 mol%, still more preferably 35 to 55 mol%).

These special polycarbonates may be used alone or in combination of two or more. Moreover, these can also be mixed and used for the bisphenol A type polycarbonate generally used.
The production method and characteristics of these special polycarbonates are described in detail in, for example, JP-A-6-172508, JP-A-8-27370, JP-A-2001-55435, and JP-A-2002-117580. ing.

Of the various polycarbonates described above, those having a water absorption and Tg (glass transition temperature) adjusted within the following ranges by adjusting the copolymer composition, etc. have good hydrolysis resistance of the polymer itself, and Since it is remarkably excellent in low warpage after molding, it is particularly suitable in a field where form stability is required.
(I) polycarbonate having a water absorption of 0.05 to 0.15%, preferably 0.06 to 0.13% and Tg of 120 to 180 ° C, or (ii) Tg of 160 to 250 ° C, Polycarbonate which is preferably 170 to 230 ° C. and has a water absorption of 0.10 to 0.30%, preferably 0.13 to 0.30%, more preferably 0.14 to 0.27%.

Here, the water absorption of the polycarbonate is a value obtained by measuring the moisture content after being immersed in water at 23 ° C. for 24 hours in accordance with ISO 62-1980 using a disc-shaped test piece having a diameter of 45 mm and a thickness of 3.0 mm. is there. Moreover, Tg (glass transition temperature) is a value calculated | required by the differential scanning calorimeter (DSC) measurement based on JISK7121.
As the carbonate precursor, carbonyl halide, carbonic acid diester, haloformate or the like is used, and specific examples include phosgene, diphenyl carbonate, dihaloformate of dihydric phenol, and the like.

  In producing the aromatic polycarbonate resin by the interfacial polymerization method using the dihydric phenol and the carbonate precursor, a catalyst, a terminal terminator, and an antioxidant for preventing the dihydric phenol from being oxidized as necessary. Etc. may be used. The aromatic polycarbonate resin of the present invention is a branched polycarbonate resin copolymerized with a trifunctional or higher polyfunctional aromatic compound, a polyester copolymerized with an aromatic or aliphatic (including alicyclic) difunctional carboxylic acid. Carbonate resin, copolymer polycarbonate resin copolymerized with bifunctional alcohol (including alicyclic), and polyester carbonate resin copolymerized with such bifunctional carboxylic acid and bifunctional alcohol are included. Moreover, the mixture which mixed 2 or more types of the obtained aromatic polycarbonate resin may be sufficient.

  The branched polycarbonate resin can impart anti-drip performance and the like to the resin composition of the present invention. Examples of the trifunctional or higher polyfunctional aromatic compound used in the branched polycarbonate resin include phloroglucin, phloroglucid, or 4,6-dimethyl-2,4,6-tris (4-hydroxyphenyl) heptene-2, 2 , 4,6-trimethyl-2,4,6-tris (4-hydroxyphenyl) heptane, 1,3,5-tris (4-hydroxyphenyl) benzene, 1,1,1-tris (4-hydroxyphenyl) Ethane, 1,1,1-tris (3,5-dimethyl-4-hydroxyphenyl) ethane, 2,6-bis (2-hydroxy-5-methylbenzyl) -4-methylphenol, 4- {4- [ Trisphenol such as 1,1-bis (4-hydroxyphenyl) ethyl] benzene} -α, α-dimethylbenzylphenol, tetra (4-hydride) Loxyphenyl) methane, bis (2,4-dihydroxyphenyl) ketone, 1,4-bis (4,4-dihydroxytriphenylmethyl) benzene, or trimellitic acid, pyromellitic acid, benzophenonetetracarboxylic acid and their acids Among them, 1,1,1-tris (4-hydroxyphenyl) ethane and 1,1,1-tris (3,5-dimethyl-4-hydroxyphenyl) ethane are preferable. 1-Tris (4-hydroxyphenyl) ethane is preferred.

  The structural unit derived from the polyfunctional aromatic compound in the branched polycarbonate is preferably a total of 100 mol% of the structural unit derived from the dihydric phenol and the structural unit derived from the polyfunctional aromatic compound. It is 0.01-1 mol%, More preferably, it is 0.05-0.9 mol%, More preferably, it is 0.05-0.8 mol%.

In particular, in the case of the melt transesterification method, a branched structural unit may be generated as a side reaction, and the amount of the branched structural unit is preferably 100% by mole in total with the structural unit derived from dihydric phenol. The content is preferably 0.001 to 1 mol%, more preferably 0.005 to 0.9 mol%, and still more preferably 0.01 to 0.8 mol%. The ratio of the branched structure can be calculated by ¹ H-NMR measurement.

  The aliphatic bifunctional carboxylic acid is preferably α, ω-dicarboxylic acid. Examples of the aliphatic difunctional carboxylic acid include sebacic acid (decanedioic acid), dodecanedioic acid, tetradecanedioic acid, octadecanedioic acid, icosanedioic acid and other straight-chain saturated aliphatic dicarboxylic acids, and cyclohexanedicarboxylic acid. Preferred are alicyclic dicarboxylic acids such as As the bifunctional alcohol, an alicyclic diol is more preferable, and examples thereof include cyclohexanedimethanol, cyclohexanediol, and tricyclodecane dimethanol.

Reaction formats such as interfacial polymerization, melt transesterification, carbonate prepolymer solid phase transesterification, and ring-opening polymerization of cyclic carbonate compounds, which are methods for producing the polycarbonate-based resin of the present invention, are various documents and patent publications. This is a well-known method.
In producing the resin composition of the present invention, the viscosity average molecular weight (M) of the polycarbonate-based resin is not particularly limited, but is preferably 1 × 10 ^{4 to} 5 × 10 ⁴ , more preferably 1.4 × 10. ^{4 to} 3 × 10 ⁴ , more preferably 1.4 × 10 ^{4 to} 2.4 × 10 ⁴ .
With a polycarbonate resin having a viscosity average molecular weight of less than 1 × 10 ⁴ , good mechanical properties cannot be obtained. On the other hand, a resin composition obtained from an aromatic polycarbonate resin having a viscosity average molecular weight exceeding 5 × 10 ⁴ is inferior in versatility in that it is inferior in fluidity during injection molding.

In addition, the said polycarbonate-type resin may be obtained by mixing that whose viscosity average molecular weight is outside the said range. In particular, a polycarbonate resin having a viscosity average molecular weight exceeding the above range (5 × 10 ⁴ ) improves the entropy elasticity of the resin. As a result, good moldability is exhibited in gas assist molding and foam molding which may be used when molding a resin material into a structural member. Such improvement in moldability is even better than that of the branched polycarbonate. As a more preferable aspect, the A component has a viscosity average molecular weight of 7 × 10 ^{4 to} 3 × 10 ⁵ polycarbonate resin A-1-1-1 component), and the viscosity average molecular weight of 1 × 10 ^{4 to} 3 × 10 ⁴ . Polycarbonate resin (A-1-1 component) consisting of an aromatic polycarbonate resin (A-1-1-2 component) and having a viscosity average molecular weight of 1.6 × 10 ^{4 to} 3.5 × 10 ⁴ , Sometimes referred to as “high molecular weight component-containing polycarbonate resin”).

In such a high molecular weight component-containing polycarbonate resin (A-1-1 component), the molecular weight of the A-1-1-1 component is preferably 7 × 10 ⁴ to 2 × 10 ⁵ , more preferably 8 × 10 ⁴ to 2. × 10 ⁵ , more preferably 1 × 10 ⁵ to 2 × 10 ⁵ , and particularly preferably 1 × 10 ^{5 to} 1.6 × 10 ⁵ . The molecular weight of the A-1-1-2 component is preferably 1 × 10 ^{4 to} 2.5 × 10 ⁴ , more preferably 1.1 × 10 ^{4 to} 2.4 × 10 ⁴ , and still more preferably 1.2 ×. 10 ^{4 to} 2.4 × 10 ⁴ , particularly preferably 1.2 × 10 ^{4 to} 2.3 × 10 ⁴ .

  The high molecular weight component-containing polycarbonate resin (A-1-1 component) is a mixture of the A-1-1-1 component and the A-1-1-2 component in various proportions so as to satisfy a predetermined molecular weight range. It can be obtained by adjusting. Preferably, in 100% by weight of the A-1-1 component, the A-1-1-1 component is 2 to 40% by weight, and more preferably, the A-1-1-1 component is 3 to 30% by weight. More preferably, the A-1-1-1 component is 4 to 20% by weight, and particularly preferably the A-1-1-1 component is 5 to 20% by weight.

  Moreover, as a preparation method of A-1-1 component, (1) The method of superposing | polymerizing each A-1-1-1 component and A-1-1-2 component independently, and mixing these, (2 ) A method for producing an aromatic polycarbonate resin showing a plurality of polymer peaks in a molecular weight distribution chart by GPC method represented by the method disclosed in Japanese Patent Application Laid-Open No. 5-306336 in the same system. And (3) an aromatic polycarbonate resin obtained by the production method (production method (2)) and A separately produced A. Examples thereof include a method of mixing the 1-1-1 component and / or the A-1-1-2 component.

The viscosity average molecular weight referred to in the present invention is first determined by using an Ostwald viscometer from a solution in which 0.7 g of polycarbonate is dissolved in 100 ml of methylene chloride at 20 ° C. with a specific viscosity (η _SP ) calculated by the following formula:
Specific viscosity (η _SP ) = (t−t ₀ ) / t ₀
[T ₀ is methylene chloride falling seconds, t is sample solution falling seconds]
The viscosity average molecular weight M is calculated from the determined specific viscosity (η _SP ) by the following formula.
η _SP /c=[η]+0.45×[η] ² c (where [η] is the intrinsic viscosity)
[Η] = 1.23 × 10 ⁻⁴ M ^0.83
c = 0.7

  In addition, calculation of the viscosity average molecular weight of polycarbonate-type resin in the flame-retardant aromatic polycarbonate resin composition of this invention is performed in the following way. That is, the composition is mixed with 20 to 30 times its weight of methylene chloride to dissolve the soluble component in the composition. Such soluble matter is collected by Celite filtration. Thereafter, the solvent in the obtained solution is removed. The solid after removal of the solvent is sufficiently dried to obtain a solid component that dissolves in methylene chloride. A specific viscosity at 20 ° C. is determined from a solution obtained by dissolving 0.7 g of the solid in 100 ml of methylene chloride in the same manner as described above, and the viscosity average molecular weight M is calculated from the specific viscosity in the same manner as described above.

(B component: Polycarbonate-polydiorganosiloxane copolymer resin)
The polycarbonate-polydiorganosiloxane copolymer resin used as component B of the present invention is a dihydric phenol represented by the following general formula [1] and a hydroxyaryl-terminated polydiorganosiloxane represented by the following general formula [3]. It is a copolymer resin prepared by copolymerization.

[In the above general formula [1], R ¹ and R ² are each independently a halogen atom, an alkyl group having 1 to 18 carbon atoms, an alkoxy group having 1 to 18 carbon atoms, or a cyclohexane having 6 to 20 carbon atoms. Alkyl group, cycloalkoxy group having 6 to 20 carbon atoms, alkenyl group having 2 to 10 carbon atoms, aryl group having 3 to 14 carbon atoms, aryloxy group having 3 to 14 carbon atoms, 7 to 7 carbon atoms Represents a group selected from the group consisting of 20 aralkyl groups, an aralkyloxy group having 7 to 20 carbon atoms, a nitro group, an aldehyde group, a cyano group, and a carboxyl group, and when there are plural groups, they may be the same or different. Well, e and f are each an integer of 1 to 4, and W is a single bond or at least one group selected from the group consisting of groups represented by the following general formula [2]. ]

[In the above general formula [2], R ¹¹ , R ¹² , R ¹³ , R ¹⁴ , R ¹⁵ , R ¹⁶ , R ¹⁷ and R ¹⁸ are each independently a hydrogen atom, an alkyl group having 1 to 18 carbon atoms, carbon Represents a group selected from the group consisting of an aryl group having 3 to 14 atoms and an aralkyl group having 7 to 20 carbon atoms, and R ¹⁹ and R ²⁰ each independently represent a hydrogen atom, a halogen atom, or a carbon atom having 1 to 18 carbon atoms. Alkyl groups, alkoxy groups having 1 to 10 carbon atoms, cycloalkyl groups having 6 to 20 carbon atoms, cycloalkoxy groups having 6 to 20 carbon atoms, alkenyl groups having 2 to 10 carbon atoms, and 3 carbon atoms. -14 aryl group, aryloxy group having 6 to 10 carbon atoms, aralkyl group having 7 to 20 carbon atoms, aralkyloxy group having 7 to 20 carbon atoms, nitro group, aldehyde group, cyano group and It represents a group selected from the group consisting of carboxyl groups, and when there are a plurality thereof, they may be the same or different, g is an integer of 1 to 10, and h is an integer of 4 to 7. ]

[In the above general formula [3], R ³ , R ⁴ , R ⁵ , R ⁶ , R ⁷ and R ⁸ are each independently a hydrogen atom, an alkyl group having 1 to 12 carbon atoms, or a substitution having 6 to 12 carbon atoms. Or an unsubstituted aryl group, R ⁹ and R ¹⁰ are each independently a hydrogen atom, a halogen atom, an alkyl group having 1 to 10 carbon atoms, or an alkoxy group having 1 to 10 carbon atoms, and p is a natural number Q is 0 or a natural number, and p + q is a natural number less than 300. X is a divalent aliphatic group having 2 to 8 carbon atoms. ]

  Examples of the dihydric phenol (I) represented by the formula [1] include 4,4′-dihydroxybiphenyl, bis (4-hydroxyphenyl) methane, 1,1-bis (4-hydroxyphenyl) ethane, 1 , 1-bis (4-hydroxyphenyl) -1-phenylethane, 2,2-bis (4-hydroxyphenyl) propane, 2,2-bis (4-hydroxy-3-methylphenyl) propane, 1,1- Bis (4-hydroxyphenyl) -3,3,5-trimethylcyclohexane, 2,2-bis (4-hydroxy-3,3′-biphenyl) propane, 2,2-bis (4-hydroxy-3-isopropylphenyl) ) Propane, 2,2-bis (3-tert-butyl-4-hydroxyphenyl) propane, 2,2-bis (4-hydroxyphenyl) butane, 2,2- (4-hydroxyphenyl) octane, 2,2-bis (3-bromo-4-hydroxyphenyl) propane, 2,2-bis (3,5-dimethyl-4-hydroxyphenyl) propane, 2,2-bis (3-cyclohexyl-4-hydroxyphenyl) propane, 1,1-bis (3-cyclohexyl-4-hydroxyphenyl) cyclohexane, bis (4-hydroxyphenyl) diphenylmethane, 9,9-bis (4-hydroxyphenyl) fluorene 9,9-bis (4-hydroxy-3-methylphenyl) fluorene, 1,1-bis (4-hydroxyphenyl) cyclohexane, 1,1-bis (4-hydroxyphenyl) cyclopentane, 4,4′- Dihydroxydiphenyl ether, 4,4′-dihydroxy-3,3′-dimethyldiphe Luether, 4,4′-sulfonyldiphenol, 4,4′-dihydroxydiphenyl sulfoxide, 4,4′-dihydroxydiphenyl sulfide, 2,2′-dimethyl-4,4′-sulfonyldiphenol, 4,4 '-Dihydroxy-3,3'-dimethyldiphenyl sulfoxide, 4,4'-dihydroxy-3,3'-dimethyldiphenyl sulfide, 2,2'-diphenyl-4,4'-sulfonyldiphenol, 4,4'- Dihydroxy-3,3′-diphenyldiphenyl sulfoxide, 4,4′-dihydroxy-3,3′-diphenyldiphenyl sulfide, 1,3-bis {2- (4-hydroxyphenyl) propyl} benzene, 1,4-bis {2- (4-hydroxyphenyl) propyl} benzene, 1,4-bis (4-hydroxy Phenyl) cyclohexane, 1,3-bis (4-hydroxyphenyl) cyclohexane, 4,8-bis (4-hydroxyphenyl) tricyclo [5.2.1.02,6] decane, 4,4 ′-(1, 3-adamantanediyl) diphenol and 1,3-bis (4-hydroxyphenyl) -5,7-dimethyladamantane.

  Among them, 1,1-bis (4-hydroxyphenyl) -1-phenylethane, 2,2-bis (4-hydroxyphenyl) propane, 2,2-bis (4-hydroxy-3-methylphenyl) propane, 1,1-bis (4-hydroxyphenyl) cyclohexane, 1,1-bis (4-hydroxyphenyl) -3,3,5-trimethylcyclohexane, 4,4′-sulfonyldiphenol, 2,2′-dimethyl- 4,4′-sulfonyldiphenol, 9,9-bis (4-hydroxy-3-methylphenyl) fluorene, 1,3-bis {2- (4-hydroxyphenyl) propyl} benzene, and 1,4-bis {2- (4-hydroxyphenyl) propyl} benzene is preferred, especially 2,2-bis (4-hydroxyphenyl) propane, 1,1-biphenyl. (4-hydroxyphenyl) cyclohexane (BPZ), 4,4'-sulfonyl diphenol, and 9,9-bis (4-hydroxy-3-methylphenyl) fluorene is preferred. Among them, 2,2-bis (4-hydroxyphenyl) propane having excellent strength and good durability is most preferable. Moreover, you may use these individually or in combination of 2 or more types.

  The hydroxyaryl-terminated polydiorganosiloxane (II) is a phenol having an olefinically unsaturated carbon-carbon bond, preferably vinylphenol, 2-allylphenol, isopropenylphenol, 2-methoxy-4-allylphenol. It is easily produced by hydrosilylation reaction at the end of a polysiloxane chain having a degree of polymerization of. Of these, (2-allylphenol) -terminated polydiorganosiloxane, (2-methoxy-4-allylphenol) -terminated polydiorganosiloxane are preferred, and (2-allylphenol) -terminated polydimethylsiloxane and (2-methoxy-) are particularly preferred. 4-Allylphenol) -terminated polydimethylsiloxane is preferred.

  Further, the degree of diorganosiloxane polymerization (p + q) of the hydroxyaryl-terminated polydiorganosiloxane (II) is a natural number of less than 300. If it is 300 or more, the incorporation of polydiorganosiloxane units in the polycarbonate becomes uneven and the proportion of the polydiorganosiloxane units in the polymer molecule increases, so that a polycarbonate containing the unit and a polycarbonate not containing it tend to be generated. In addition, the compatibility with each other tends to decrease. As a result, the dispersion of the polydiorganosiloxane domain becomes non-uniform and not only the appearance becomes poor, but also sufficient flame retardancy cannot be obtained. The degree of diorganosiloxane polymerization (p + q) is preferably 10 to 120, more preferably 20 to 115, and still more preferably 30 to 110. Below the lower limit of this range, sufficient flame retardancy cannot be obtained, the polydiorganosiloxane domain diameter is small, and sufficient impact resistance is not exhibited. In the present invention, the polydiorganosiloxane domain means a domain mainly composed of polydiorganosiloxane dispersed in a polycarbonate matrix and may contain other components. As described above, the polydiorganosiloxane domain is not necessarily composed of a single component because the structure is formed by phase separation from the polycarbonate polycarbonate.

The polydiorganosiloxane content in the total weight of the copolymer resin is preferably 0.1 to 50% by weight. The polydiorganosiloxane component content is more preferably 0.5 to 30% by weight, still more preferably 1 to 20% by weight. Above the lower limit of the preferred range, the impact resistance and flame retardancy are excellent, and below the upper limit of the preferred range, a stable appearance that is hardly affected by the molding conditions is easily obtained. Such polydiorganosiloxane polymerization degree and polydiorganosiloxane content can be calculated by ¹ H-NMR measurement.

  In this invention, hydroxyaryl terminal polydiorganosiloxane (II) may use only 1 type, and may use 2 or more types. Further, within the range not hindering the production method of the present invention, other comonomer other than the dihydric phenol (I) and hydroxyaryl-terminated polydiorganosiloxane (II) is 10% by weight or less based on the total weight of the copolymer. It can also be used in combination in the range.

  In the present invention, a chloroformate-forming compound such as divalent phenol (I) and phosgene or chloroformate of divalent phenol (I) in a mixed solution of an organic solvent insoluble in water and an aqueous alkaline solution in advance. To prepare a mixed solution of a chloroformate compound containing a chloroformate of dihydric phenol (I) and / or a carbonate oligomer of dihydric phenol (I) having a terminal chloroformate group. As the chloroformate-forming compound, phosgene is preferred.

In producing the chloroformate compound from the dihydric phenol (I), the whole amount of the dihydric phenol (I) used in the production method of the present invention may be converted to the chloroformate compound at one time, or a part thereof may be used. A post-added monomer may be added as a reaction raw material to a subsequent interfacial polycondensation reaction. The post-added monomer is added to allow the subsequent polycondensation reaction to proceed rapidly, and it is not necessary to add it when it is not necessary.
The method for this chloroformate compound formation reaction is not particularly limited, but usually a method of carrying out in a solvent in the presence of an acid binder is preferred. Furthermore, if desired, a small amount of an antioxidant such as sodium sulfite and hydrosulfide may be added, and it is preferable to add them.

The use ratio of the chloroformate-forming compound may be appropriately adjusted in consideration of the stoichiometric ratio (equivalent) of the reaction. Moreover, when using the phosgene which is a suitable chloroformate formation compound, the method of blowing gasified phosgene into a reaction system can be employ | adopted suitably.
Examples of the acid binder include alkali metal hydroxides such as sodium hydroxide and potassium hydroxide, alkali metal carbonates such as sodium carbonate and potassium carbonate, organic bases such as pyridine, and mixtures thereof. Is used.
The use ratio of the acid binder may be appropriately determined in consideration of the stoichiometric ratio (equivalent) of the reaction as described above. Specifically, 2 equivalents or slightly more than 2 equivalents per mole of dihydric phenol (I) used for forming the chloroformate compound of dihydric phenol (I) (usually 1 mole corresponds to 2 equivalents). It is preferable to use an acid binder.

As said solvent, what is necessary is just to use a solvent inert to various reaction, such as what is used for manufacture of a well-known polycarbonate, individually or as a mixed solvent. Representative examples include hydrocarbon solvents such as xylene, and halogenated hydrocarbon solvents such as methylene chloride and chlorobenzene. In particular, a halogenated hydrocarbon solvent such as methylene chloride is preferably used.
The molar ratio of the organic solvent insoluble in water is preferably 8 moles or more, more preferably 10 moles or more, still more preferably 12 moles or more, and particularly preferably 14 moles or more per mole of dihydric phenol (I). The upper limit is not particularly limited, but 50 mol or less is sufficient from the viewpoint of the size and cost of the apparatus. By setting the molar ratio of the organic solvent to the dihydric phenol (I) within such a range, it becomes easier to control the average size and normalized dispersion of the polydiorganosiloxane domain to appropriate values.

The pressure in the formation reaction of the chloroformate compound is not particularly limited and may be any of normal pressure, pressurization, or reduced pressure, but it is usually advantageous to carry out the reaction under normal pressure. The reaction temperature is selected from the range of -20 to 50 ° C, and in many cases, heat is generated with the reaction, so it is desirable to cool with water or ice. Although the reaction time depends on other conditions and cannot be defined unconditionally, it is usually carried out in 0.2 to 10 hours.
As the pH range in the formation reaction of the chloroformate compound, known interfacial reaction conditions can be used, and the pH is usually adjusted to 10 or more.

  In the present invention, after preparing a mixed solution of the chloroformate of the dihydric phenol (I) and the chloroformate compound containing the carbonate oligomer of the dihydric phenol (I) having a terminal chloroformate group in this way, While stirring the mixed solution, the hydroxyaryl-terminated polydiorganosiloxane (II) represented by the formula [5] is added in an amount of 0.01 mol per 1 mol of the dihydric phenol (I) charged in preparing the mixed solution. The polycarbonate-polydiorganosiloxane copolymer resin is obtained by adding the hydroxyaryl-terminated polydiorganosiloxane (II) and the chloroformate compound by interfacial polycondensation.

  The polycarbonate-polydiorganosiloxane copolymer resin of the present invention can be made into a branched polycarbonate copolymer by using a branching agent in combination with the above dihydric phenol compound. Examples of the trifunctional or higher polyfunctional aromatic compound used in the branched polycarbonate resin include phloroglucin, phloroglucid, or 4,6-dimethyl-2,4,6-tris (4-hydroxyphenyl) heptene-2, 2 , 4,6-trimethyl-2,4,6-tris (4-hydroxyphenyl) heptane, 1,3,5-tris (4-hydroxyphenyl) benzene, 1,1,1-tris (4-hydroxyphenyl) Ethane, 1,1,1-tris (3,5-dimethyl-4-hydroxyphenyl) ethane, 2,6-bis (2-hydroxy-5-methylbenzyl) -4-methylphenol, 4- {4- [ Trisphenol such as 1,1-bis (4-hydroxyphenyl) ethyl] benzene} -α, α-dimethylbenzylphenol, tetra (4-hydride) Loxyphenyl) methane, bis (2,4-dihydroxyphenyl) ketone, 1,4-bis (4,4-dihydroxytriphenylmethyl) benzene, or trimellitic acid, pyromellitic acid, benzophenonetetracarboxylic acid and their acids Among them, 1,1,1-tris (4-hydroxyphenyl) ethane and 1,1,1-tris (3,5-dimethyl-4-hydroxyphenyl) ethane are preferable. 1-Tris (4-hydroxyphenyl) ethane is preferred.

The branched polycarbonate copolymer is produced by a branching agent used in the interfacial polycondensation reaction after completion of the production reaction, even if the branched solution is contained in the mixed solution during the production reaction of the chloroformate compound. May be added. The proportion of the carbonate constituent unit derived from the branching agent is preferably 0.005 to 1.5 mol%, more preferably 0.01 to 1.2 mol% in the total amount of carbonate constituent units constituting the copolymer. Especially preferably, it is 0.05-1.0 mol%. Such a branched structure amount can be calculated by ¹ H-NMR measurement.

  The pressure in the system in the polycondensation reaction can be any of reduced pressure, normal pressure, or increased pressure, but can usually be suitably performed at normal pressure or about the pressure of the reaction system. The reaction temperature is selected from the range of −20 to 50 ° C., and in many cases, heat is generated with the polymerization, so it is desirable to cool with water or ice. Since the reaction time varies depending on other conditions such as the reaction temperature, it cannot be generally specified, but it is usually performed in 0.5 to 10 hours.

In some cases, the obtained polycarbonate copolymer is appropriately subjected to physical treatment (mixing, fractionation, etc.) and / or chemical treatment (polymer reaction, crosslinking treatment, partial decomposition treatment, etc.) to obtain a desired reduced viscosity [η _SP / C] can also be obtained as a polycarbonate copolymer.
The obtained reaction product (crude product) can be recovered as a polycarbonate-polydiorganosiloxane copolymer resin having a desired purity (purity) after various post-treatments such as a known separation and purification method.

The viscosity-average molecular weight of the polycarbonate-polydiorganosiloxane copolymer resin is preferably in the range of 5.0 × 10 ^{3 to} 5.0 × 10 ⁴ . The viscosity average molecular weight is more preferably 1.0 × 10 ^{4 to} 4.0 × 10 ⁴ , further preferably 1.5 × 10 ^{4 to} 3.5 × 10 ⁴ , and particularly preferably 1.7 × 10 ⁴ to 2. .5 × 10 ⁴ . When the viscosity average molecular weight of the polycarbonate-polydiorganosiloxane copolymer resin is less than 5.0 × 10 ³ , practical mechanical strength is difficult to obtain in many fields, and when it exceeds 5.0 × 10 ⁴ , the melt viscosity is It is high and generally requires a high molding temperature, so it tends to cause problems such as thermal degradation of the resin.

The polydiorganosiloxane content derived from the polycarbonate-polydiorganosiloxane copolymer resin in the resin composition of the present invention is 0.2 to 0.6% by weight. The upper limit is preferably 0.55% by weight, more preferably 0.50% by weight, and still more preferably 0.45% by weight. The lower limit is preferably 0.25% by weight, more preferably 0.30% by weight, and still more preferably 0.35% by weight. For example, it is preferably 0.25 to 0.55% by weight, more preferably 0.3 to 0.5% by weight, and still more preferably 0.35 to 0.45% by weight. Less than 0.2% by weight does not exhibit sufficient flame retardancy in supercritical fluid microfoam molding, which is a high weight reduction rate, and even if it exceeds 0.6% by weight, it is a high weight reduction rate. No flame retardancy in foam molding. The polydiorganosiloxane content in the composition was calculated from the PDMS amount contained in the polycarbonate-polydiorganosiloxane copolymer resin (PC-PDMS copolymer resin) by the following formula.
PDMS amount in composition (% by weight) = {(PDMS amount in PC-PDMS copolymer resin) / (weight of entire composition)} × 100

(C component: styrene resin)
The flame retardant resin composition of the present invention contains a styrene resin as the C component. Since this styrenic resin has good moldability, moderate heat resistance and flame retardancy, it is a preferred thermoplastic resin in order to maintain a balance between these properties.
Such a styrenic resin is a copolymer or copolymer of an aromatic vinyl compound, and, if necessary, at least one selected from other vinyl monomers and rubbery polymers copolymerizable therewith. It is a polymer obtained by polymerization.

  As the aromatic vinyl compound, styrene is particularly preferable. Preferable examples of the other vinyl monomer copolymerizable with the aromatic vinyl compound include a vinyl cyanide compound and a (meth) acrylic acid ester compound. A particularly preferred vinyl cyanide compound is acrylonitrile, and a particularly preferred (meth) acrylic acid ester compound is methyl methacrylate.

  Other vinyl monomers copolymerizable with aromatic vinyl compounds other than vinyl cyanide compounds and (meth) acrylic acid ester compounds include epoxy group-containing methacrylic acid esters such as glycidyl methacrylate, maleimide, N-methylmaleimide, Examples thereof include maleimide monomers such as N-phenylmaleimide, α, β-unsaturated carboxylic acids such as acrylic acid, methacrylic acid, maleic acid, maleic anhydride, phthalic acid and itaconic acid, and anhydrides thereof.

  Examples of the rubbery polymer copolymerizable with the aromatic vinyl compound include polybutadiene, polyisoprene, and diene copolymers (eg, styrene / butadiene random copolymers and block copolymers, acrylonitrile / butadiene copolymers). , And (meth) acrylic acid alkyl ester and butadiene copolymers), ethylene and α-olefin copolymers (eg, ethylene / propylene random copolymers and block copolymers, ethylene / butene random copolymers). Polymers and block copolymers), copolymers of ethylene and unsaturated carboxylic acid esters (for example, ethylene / methacrylate copolymers and ethylene / butyl acrylate copolymers), copolymers of ethylene and aliphatic vinyl. Polymer (for example, ethylene / vinyl acetate copolymer) ), Ethylene, propylene and non-conjugated diene terpolymers (eg, ethylene / propylene / hexadiene copolymer), acrylic rubbers (eg, polybutyl acrylate, poly (2-ethylhexyl acrylate), and butyl acrylate 2 A copolymer with ethylhexyl acrylate, etc.), and a silicone rubber (for example, polyorganosiloxane rubber, IPN type rubber comprising a polyorganosiloxane rubber component and a polyalkyl (meth) acrylate rubber component; that is, two rubber components And rubbers having a structure in which they are entangled with each other so that they cannot be separated, and an IPN type rubber composed of a polyorganosiloxane rubber component and a polyisobutylene rubber component.

  Specific examples of the styrene resin include styrene resins such as polystyrene resin, HIPS resin, MS resin, ABS resin, AS resin, AES resin, ASA resin, MBS resin, MABS resin, MAS resin, and SMA resin. And (hydrogenated) styrene-butadiene-styrene copolymer resin, (hydrogenated) styrene-isoprene-styrene copolymer resin, and the like. In addition, the notation of (hydrogenated) means that both non-hydrogenated resin and hydrogenated resin are included. Here, the MS resin is a copolymer resin mainly composed of methyl methacrylate and styrene, the AES resin is a copolymer resin mainly composed of acrylonitrile, ethylene-propylene rubber, and styrene, and the ASA resin is mainly composed of acrylonitrile, styrene, and acrylic rubber. MABS resin is a copolymer resin mainly composed of methyl methacrylate, acrylonitrile, butadiene and styrene, MAS resin is a copolymer resin mainly composed of methyl methacrylate, acrylic rubber and styrene, and SMA resin is styrene and A copolymer resin mainly composed of maleic anhydride (MA) is shown.

Such a styrenic resin may have a high stereoregularity such as syndiotactic polystyrene by using a catalyst such as a metallocene catalyst during the production thereof. Further, in some cases, polymers and copolymers having a narrow molecular weight distribution, block copolymers, and polymers and copolymers having high stereoregularity obtained by methods such as anion living polymerization and radical living polymerization are used. It is also possible.
Among these, acrylonitrile / styrene copolymer resin (AS resin) and acrylonitrile / butadiene / styrene copolymer resin (ABS resin) are preferable. It is also possible to use a mixture of two or more styrenic polymers.

  The AS resin used in the present invention is a thermoplastic copolymer obtained by copolymerizing a vinyl cyanide compound and an aromatic vinyl compound. As such a vinyl cyanide compound, acrylonitrile can be particularly preferably used. As the aromatic vinyl compound, styrene and α-methylstyrene can be preferably used. The proportion of each component in the AS resin is preferably 5 to 50% by weight of vinyl cyanide compound, more preferably 15 to 35% by weight, and preferably 95% of aromatic vinyl compound when the total is 100% by weight. -50% by weight, more preferably 85-65% by weight. Further, these vinyl compounds may be used in combination with other copolymerizable vinyl compounds described above, and the content ratio thereof is preferably 15% by weight or less in the AS resin component. Moreover, conventionally well-known various things can be used for the initiator, chain transfer agent, etc. which are used by reaction as needed.

Such an AS resin may be produced by any of bulk polymerization, suspension polymerization, and emulsion polymerization, but is preferably bulk polymerization. The copolymerization method may be either one-stage copolymerization or multistage copolymerization. The reduced viscosity of the AS resin is preferably 0.2 to 1.0 dl / g, more preferably 0.3 to 0.5 dl / g. The reduced viscosity is a value obtained by precisely weighing 0.25 g of AS resin and measuring a solution obtained by dissolving in 50 ml of dimethylformamide over 2 hours in an environment of 30 ° C. using an Ubbelohde viscometer. A viscometer having a solvent flow time of 20 to 100 seconds is used. The reduced viscosity is determined from the following formula from the solvent flow down seconds (t ₀ ) and the solution flow down seconds (t).
Reduced viscosity (η _sp / C) = {(t / t ₀ ) −1} /0.5
When the reduced viscosity is less than 0.2 dl / g, the impact is lowered, and when it exceeds 1.0 dl / g, the fluidity is deteriorated.

  The ABS resin used in the present invention is a mixture of a thermoplastic graft copolymer obtained by graft polymerization of a vinyl cyanide compound and an aromatic vinyl compound to a diene rubber component, and a copolymer of a vinyl cyanide compound and an aromatic vinyl compound. It is. As the diene rubber component forming this ABS resin, for example, rubber having a glass transition temperature of −30 ° C. or lower such as polybutadiene, polyisoprene and styrene-butadiene copolymer is used, and the proportion thereof is 100% by weight of the ABS resin component. The content is preferably 5 to 80% by weight, more preferably 8 to 50% by weight, and particularly preferably 10 to 30% by weight. As the vinyl cyanide compound grafted on the diene rubber component, acrylonitrile is particularly preferably used. As the aromatic vinyl compound grafted on the diene rubber component, styrene and α-methylstyrene are particularly preferably used. The ratio of the component grafted to the diene rubber component is preferably 95 to 20% by weight, particularly preferably 50 to 90% by weight, based on 100% by weight of the ABS resin component. Furthermore, it is preferable that the vinyl cyanide compound is 5 to 50% by weight and the aromatic vinyl compound is 95 to 50% by weight with respect to 100% by weight of the total amount of the vinyl cyanide compound and the aromatic vinyl compound. Further, methyl (meth) acrylate, ethyl acrylate, maleic anhydride, N-substituted maleimide and the like can be mixed and used for a part of the components grafted to the diene rubber component, and the content ratio thereof is in the ABS resin component. What is 15 weight% or less is preferable. Furthermore, conventionally known various initiators, chain transfer agents, emulsifiers and the like can be used as necessary.

  In the ABS resin of the present invention, the rubber particle diameter is preferably 0.1 to 5.0 μm, more preferably 0.15 to 1.5 μm, and particularly preferably 0.2 to 0.8 μm. As the distribution of the rubber particle diameter, either a single distribution or a rubber particle having two or more peaks can be used, and the rubber particles form a single phase in the morphology. Alternatively, it may have a salami structure by containing an occluded phase around the rubber particles.

In addition, it is well known that the ABS resin contains a vinyl cyanide compound and an aromatic vinyl compound that are not grafted to the diene rubber component, and the ABS resin of the present invention is free of the occurrence of such polymerization. The polymer component may be contained. The reduced viscosity of the copolymer comprising such a free vinyl cyanide compound and aromatic vinyl compound is preferably a reduced viscosity (30 ° C.) determined by the above-described method of 0.2 to 1.0 dl / g. Preferably it is 0.3-0.7 dl / g.
The ratio of the grafted vinyl cyanide compound and aromatic vinyl compound is preferably 20 to 200%, more preferably 20 to 70% in terms of graft ratio (% by weight) with respect to the diene rubber component. is there.

  Such an ABS resin may be produced by any of bulk polymerization, suspension polymerization, and emulsion polymerization, but is preferably bulk polymerization. Further, as such bulk polymerization method, typically, continuous bulk polymerization method (so-called Toray method) described in Chemical Engineering Vol. 48, No. 6, page 415 (1984), and Chemical Engineering Vol. 53, No. 6, page 423 ( 1989), a continuous bulk polymerization method (so-called Mitsui Toatsu method) is exemplified. Any ABS resin is preferably used as the ABS resin of the present invention. Further, the copolymerization may be carried out in one step or in multiple steps. Moreover, what blended the vinyl compound polymer obtained by copolymerizing an aromatic vinyl compound and a vinyl cyanide component separately to the ABS resin obtained by this manufacturing method can also be used preferably. An ABS resin that does not contain a lubricant (such as ethylene bis-stearic acid amide (EBS)) exhibits more excellent flame retardancy.

  As the AS resin and the ABS resin, those having a reduced amount of alkali (earth) metal are more preferable from the viewpoint of good thermal stability and hydrolysis resistance. The amount of alkali (earth) metal in the styrenic resin is preferably less than 100 ppm, more preferably less than 80 ppm, still more preferably less than 50 ppm, and particularly preferably less than 10 ppm. Also from this point, AS resin and ABS resin by a bulk polymerization method are preferably used. Furthermore, in relation to such good thermal stability and hydrolysis resistance, when an emulsifier is used in the AS resin and ABS resin, the emulsifier is preferably a sulfonate salt, more preferably an alkyl sulfonic acid. It is salt. When a coagulant is used, the coagulant is preferably sulfuric acid or an alkaline earth metal salt of sulfuric acid.

  The content of the styrenic resin is 3 to 45 parts by weight, preferably 4 to 42.5 parts by weight, and more preferably 5 to 40 parts by weight with respect to 100 parts by weight of the total of the A component and the B component. When the content is less than 3 parts by weight, sufficient fluidity cannot be obtained, and when it exceeds 45 parts by weight, the flame retardancy in supercritical fluid microfoam molding, which is a high weight reduction rate, cannot be maintained.

(D component: phosphorus flame retardant)
As the phosphorus-based flame retardant of the present invention, a phosphate compound, particularly an aryl phosphate compound is suitable. Such a phosphate compound is effective in improving flame retardancy, and since the phosphate compound has a plasticizing effect, there is a decrease in heat resistance, but it is advantageous in that the molding processability of the resin composition of the present invention can be improved. It is. As such phosphate compounds, various known phosphate compounds as conventional flame retardants can be used, and more preferably, one or more phosphate compounds represented by the following general formula (I) can be mentioned.

(X in the formula is hydroquinone, resorcinol, bis (4-hydroxydiphenyl) methane, bisphenol A, dihydroxydiphenyl, dihydroxynaphthalene, bis (4-hydroxyphenyl) sulfone, bis (4-hydroxyphenyl) ketone, and bis ( 4-hydroxyphenyl) dihydric phenol residue derived from a dihydroxy compound selected from the group consisting of sulfides, and n is an integer of 0 to 5, or in the case of a mixture of n different phosphate esters, their average R ⁴ , R ⁵ , R ⁶ , and R ⁷ are each independently derived from an aryl group selected from the group consisting of phenol, cresol, xylenol, isopropylphenol, butylphenol, and p-cumylphenol. Divalent phenol residue .)

The phosphate compound of the above formula (I) may be a mixture of compounds having different n numbers, in which case the average n number is preferably 0.5 to 1.5, more preferably 0.8. To 1.2, more preferably 0.95 to 1.15, and particularly preferably 1 to 1.14.
Preferable specific examples of the dihydric phenol for deriving X in the above formula (I) include resorcinol, bisphenol A, and dihydroxydiphenyl, and among them, resorcinol and bisphenol A are preferable.
Preferable specific examples of the monohydric phenol for deriving R ⁴ , R ⁵ , R ⁶ , and R ⁷ of the above formula (I) include phenol, cresol, xylenol, and 2,6-dimethylphenol. And 2,6-dimethylphenol.

  Specific examples of the phosphate compound of the above formula (I) are mainly composed of monophosphate compounds such as triphenyl phosphate and tri (2,6-xylyl) phosphate, and resorcinol bisdi (2,6-xylyl) phosphate). Phosphate oligomers, phosphate oligomers mainly composed of 4,4-dihydroxydiphenyl bis (diphenyl phosphate), and phosphate oligomers mainly composed of bisphenol A bis (diphenyl phosphate) are preferred. Resorcinol bisdi (2,6- Xylyl) phosphate) -based phosphate oligomer, 4,4-dihydroxydiphenylbis (diphenylphosphate) -based phosphate oligomer, and bisphenol A bis (diphenyl) Phosphoric acid ester oligomer mainly containing Sufeto) are preferred.

〔式中ｍは３〜２５の整数を示す。Ｐｈはフェニル基を示す。〕 Moreover, a phosphazene compound is also mentioned as a suitable phosphorus flame retardant. The phosphazene compound is preferably a cyclic phenoxyphosphazene represented by the general formula (1).

[Wherein m represents an integer of 3 to 25. Ph represents a phenyl group. ]

Typical examples of commercially available cyclic phenoxyphosphazenes include “FP-100” manufactured by Fushimi Pharmaceutical Co., Ltd. In the present invention, it is allowed to contain other components as long as the function of the phosphazene compound is not hindered.
The content of the phosphorus-based flame retardant is 3 to 35 parts by weight, preferably 4 to 32.5 parts by weight, more preferably 5 to 30 parts by weight with respect to 100 parts by weight as a total of the A component and the B component. It is. When the content is less than 3 parts by weight, flame retardancy in the supercritical fluid microfoam molding, which is a high weight reduction rate, does not appear, and when it exceeds 35 parts by weight, the supercritical fluid microfoaming has a high weight reduction rate. It is not preferable because flame retardancy in molding is hardly exhibited and heat resistance is lowered.

(E component: silicate mineral)
The silicate mineral used as the E component of the present invention is a mineral comprising at least a metal oxide component and a SiO ₂ component, and orthosilicate, disilicate, cyclic silicate, chain silicate, and the like are suitable. The silicate mineral of component E takes a crystalline state, and the shape of the crystal can take various shapes such as a fiber shape and a plate shape.
The silicate mineral of the E component may be a compound oxide, an oxyacid salt (consisting of an ionic lattice), or a solid solution compound, and the compound oxide is a combination of two or more of a single oxide and a single oxidation Any combination of two or more of a product and an oxyacid salt may be used, and also in a solid solution, any of a solid solution of two or more metal oxides and a solid solution of two or more oxyacid salts Good.

Hydrate may be sufficient as the silicate mineral of E component. The form of crystal water in the hydrate is one that enters as hydrogen silicate ion as Si—OH, one that enters ionically as a hydroxide ion (OH ⁻ ) with respect to the metal cation, and H ₂ O molecules in the gaps in the structure. Any form of entry may be used.
As the E component silicate mineral, an artificial synthetic material corresponding to a natural product can be used. As the artificial compound, silicate minerals obtained from various conventionally known methods, for example, various synthetic methods using solid reaction, hydrothermal reaction, ultrahigh pressure reaction, and the like can be used.

  Specific examples of the silicate mineral in each metal oxide component (MO) include the following. Here, the description in parentheses is the name of a mineral or the like mainly composed of such a silicate mineral, and means that the compound in parentheses can be used as the exemplified metal salt.

As those containing K ₂ O in the _{component, K 2 O · SiO 2,} K 2 O · 4SiO 2 · H 2 O, K 2 O · Al 2 O 3 · 2SiO 2 ( _{Karushiraito), K} 2 O · Al ₂ O ₃ · 4SiO ₂ (leucite), and _{K 2 O · Al 2 O 3} · 6SiO 2 ( orthoclase), and the like.
As comprising Na ₂ O in the _component, Na ₂ O · SiO _2, and its _{hydrates, Na 2 O · 2SiO 2,} 2Na 2 O · SiO 2, Na 2 O · 4SiO 2, Na 2 O · 3SiO _{2 · 3H 2 O, Na 2} O · Al 2 O 3 · 2SiO 2, Na 2 O · Al 2 O 3 · 4SiO 2 ( _{jadeite), 2Na 2 O · 3CaO ·} 5SiO 2, 3Na 2 O · 2CaO · 5SiO _2, and _{Na 2 O · Al 2 O 3} · 6SiO 2 ( albite), and the like.

Li ₂ O and as including the components _{thereof, Li 2 O · SiO 2,} 2Li 2 O · SiO 2, Li 2 O · SiO 2 · H 2 O, 3Li 2 O · 2SiO 2, Li 2 O · Al 2 Examples include O ₃ · 4SiO ₂ (petalite), Li ₂ O · Al ₂ O ₃ · 2SiO ₂ (eucryptite), and Li ₂ O · Al ₂ O ₃ · 4SiO ₂ (spodumene).
As those containing BaO into its _components, and the like _{BaO · SiO 2, 2BaO · SiO} 2, BaO · Al 2 O 3 · 2SiO 2 ( celsian), and BaO _· TiO _{2 ·} 3SiO 2 (Bentoaito).

As including CaO its components, 3CaO · _SiO 2 (cement clinker minerals of alite), 2CaO · SiO ₂ (cement clinker minerals of _{belite), 2CaO · MgO · 2SiO 2} ( O Keruma night), 2CaO · Al ₂ O ₃ · SiO ₂ (Gerlenite), solid solution of akermanite and gehlenite (Merilite), CaO · SiO ₂ (Wollastonite (including both α-type and β-type)), CaO · MgO · 2SiO _{2 (Jiopusaido), CaO · MgO · SiO 2} ( ash magnesia _{olivine), 3CaO · MgO · 2SiO 2} ( _{Meruuinaito), CaO · Al 2 O 3} · 2SiO 2 ( anorthite), 5CaO · 6SiO ₂ · 5H ₂ O (tobermorite, other 5CaO · 6SiO ₂ · 9H ₂ O, etc. Tobermorite group hydrates such as 2CaO · SiO ₂ · H ₂ O (Hillebrandite), and wollastonite group hydrates such as 6CaO · 6SiO ₂ · H ₂ O (zonotolite) Gyrolite group hydrates such as 2CaO · SiO ₂ · 2H ₂ O (gyrolite), CaO · Al ₂ O ₃ · 2SiO ₂ · H ₂ O (lawsonite), CaO · FeO · 2SiO ₂ (headenite), 3CaO · 2SiO _{2 (Chirukoanaito), 3CaO · Al 2 O 3} · 3SiO 2 ( _{Guroshura), 3CaO · Fe 2 O 3} · 3SiO 2 ( Andhra _{Daito), 6CaO · 4Al 2 O 3} · FeO · SiO 2 ( pleo black Ait ), As well as clinozoite, olivine, olivine, vesuvite, oneolite, Examples include koutite and augite.

Furthermore, Portland cement can be mentioned as a silicate mineral containing CaO as its component. The type of Portland cement is not particularly limited, and any of normal, early strength, ultra-early strength, moderate heat, sulfate resistance, white, and the like can be used. Further, various mixed cements such as blast furnace cement, silica cement, fly ash cement and the like can be used as the E component.
Moreover, blast furnace slag, ferrite, etc. can be mentioned as a silicate mineral which contains other CaO in the component.

As what contains ZnO in its component, ZnO.SiO ₂ , 2ZnO.SiO ₂ (trothite), 4ZnO.2SiO ₂ .H ₂ O (heteropolar ore) and the like can be mentioned.
As including MnO into its _components, such as _{MnO · SiO 2, 2MnO · SiO} 2, CaO · 4MnO · 5SiO 2 ( rhodonite) and Coe write the like.
As the component containing FeO, FeO · SiO ₂ (ferrosilite), 2FeO · SiO ₂ (iron olivine), 3FeO · Al ₂ O ₃ · 3SiO ₂ (almandin), and 2CaO · 5FeO · 8SiO ₂ · H ₂ O (Tetsuakuchinosene) and the like can be mentioned.
Examples of those containing CoO as a component include CoO.SiO ₂ and 2CoO.SiO ₂ .

MgO · SiO ₂ (steatite, enstatite), 2MgO · SiO ₂ (forsterite), 3MgO · Al ₂ O ₃ · 3SiO ₂ (birop), 2MgO · 2Al ₂ O ₃ · 5SiO _{2 (cordierite), 2MgO · 3SiO 2 · 5H} 2 O, 3MgO · 4SiO 2 · H 2 O ( _{talc), 5MgO · 8SiO 2 · 9H} 2 O ( _{attapulgite), 4MgO · 6SiO 2 · 7H} 2 O (Sepiolite), 3MgO · 2SiO ₂ · 2H ₂ O (Chrysolite), 5MgO · 2CaO · 8SiO ₂ · H ₂ O (Translucentite), 5MgO · Al ₂ O ₃ · 3SiO ₂ · 4H ₂ O (Chlorite) _{, K 2 O · 6MgO · Al} 2 O 3 · 6SiO 2 · 2H 2 O ( phlogopite), _Na 2 O · _{MgO · 3Al 2 O 3 · 8SiO} 2 · H 2 O ( melee stone), as well as magnesium tourmaline, linearity stone, Kamintonsen stone, vermiculite, etc. smectite and the like.

As containing Fe ₂ O ₃ on the _component, and a Fe ₂ O 3 · SiO _2.
As those containing ZrO ₂ into its _components, ZrO 2 · SiO ₂ (zircon) and AZS refractory and the like.
As containing Al ₂ O ₃ on the _{component, Al 2 O 3 · SiO 2} ( sillimanite, under-leucite, _{kyanite), 2Al 2 O 3 · SiO} 2, Al 2 O 3 · 3SiO 2, 3Al 2 O 3 2SiO ₂ (mullite), Al ₂ O ₃ · 2SiO ₂ · 2H ₂ O (kaolinite), Al ₂ O ₃ · 4SiO ₂ · H ₂ O (pyrophyllite), Al ₂ O ₃ · 4SiO ₂ · H ₂ O _{(bentonite), K 2 O · 3Na 2} O · 4Al 2 O 3 · 8SiO 2 ( _{nepheline), K 2 O · 3Al 2} O 3 · 6SiO 2 · 2H 2 O ( muscovite, sericite), _{K 2} O.6MgO.Al ₂ O ₃ .6SiO ₂ .2H ₂ O (phlogobite), various zeolites, fluorine phlogopite, biotite, and the like can be given.
Among the silicate minerals, mica, talc, and wollastonite are particularly suitable.

(talc)
In the present invention, talc is hydrous magnesium silicate in terms of chemical composition, generally represented by the chemical formula 4SiO ₂ .3MgO.2H ₂ O, and is usually scaly particles having a layered structure. thereof include a SiO ₂ 56 to 65 wt%, the MgO 28 to 35 wt%, and a _{H 2} O about 5 wt%. As other minor components, Fe ₂ O ₃ is 0.03 to 1.2% by weight, Al ₂ O ₃ is 0.05 to 1.5% by weight, CaO is 0.05 to 1.2% by weight, K ₂ O. Is 0.2 wt% or less, Na ₂ O is 0.2 wt% or less. As for the particle diameter of talc, the average particle diameter measured by the sedimentation method is 0.1 to 15 μm (more preferably 0.2 to 12 μm, still more preferably 0.3 to 10 μm, particularly preferably 0.5 to 5 μm). A range is preferable. Furthermore, it is particularly preferable to use talc having a bulk density of 0.5 (g / cm ³ ) or more as a raw material. The average particle size of talc refers to D50 (median diameter of particle size distribution) measured by an X-ray transmission method which is one of liquid phase precipitation methods. As a specific example of an apparatus for performing such a measurement, Sedigraph 5100 manufactured by Micromeritics Inc. can be cited.

In addition, there is no particular restriction on the manufacturing method when talc is crushed from raw stone, and the axial flow mill method, the annular mill method, the roll mill method, the ball mill method, the jet mill method, the container rotary compression shearing mill method, etc. are used. can do. Further, the talc after pulverization is preferably classified by various classifiers and having a uniform particle size distribution. There are no particular restrictions on the classifier, impactor type inertial force classifier (variable impactor, etc.), Coanda effect type inertial force classifier (elbow jet, etc.), centrifugal field classifier (multistage cyclone, microplex, dispersion separator) , Accucut, Turbo Classifier, Turboplex, Micron Separator, and Super Separator).
Further, talc is preferably in an agglomerated state in view of its handleability and the like, and as such a production method, there are a method by deaeration compression, a method of compression using a sizing agent, and the like. In particular, the degassing compression method is preferable in that the sizing agent resin component which is simple and unnecessary is not mixed into the resin composition of the present invention.

(Mica)
As the mica, those having an average particle diameter measured by a microtrack laser diffraction method of 10 to 100 μm can be preferably used. More preferably, the average particle size is 20 to 50 μm. If the average particle diameter of mica is less than 10 μm, the effect of improving the rigidity is not sufficient, and if it exceeds 100 μm, the rigidity of the rigidity is not sufficiently improved, and the mechanical strength such as impact characteristics is not significantly lowered. Mica having a thickness measured by observation with an electron microscope of 0.01 to 1 μm can be preferably used. More preferably, the thickness is 0.03 to 0.3 μm. The aspect ratio is preferably 5 to 200, more preferably 10 to 100. The mica used is preferably mascobite mica, and its Mohs hardness is about 3. Muscovite mica can achieve higher rigidity and strength than other mica such as phlogopite, and solves the problems of the present invention at a better level. The mica may be pulverized by either dry pulverization or wet pulverization. The dry pulverization method is more inexpensive and more general, but the wet pulverization method is effective for pulverizing mica more thinly and finely, and as a result, the effect of improving the rigidity of the resin composition becomes higher.

(Wollastonite)
The fiber diameter of wollastonite is preferably from 0.1 to 10 μm, more preferably from 0.1 to 5 μm, still more preferably from 0.1 to 3 μm. The aspect ratio (average fiber length / average fiber diameter) is preferably 3 or more. The upper limit of the aspect ratio is 30 or less. Here, the fiber diameter is obtained by observing the reinforcing filler with an electron microscope, obtaining individual fiber diameters, and calculating the number average fiber diameter from the measured values. The electron microscope is used because it is difficult for an optical microscope to accurately measure the size of a target level. For the fiber diameter, for the image obtained by observation with an electron microscope, the filler for which the fiber diameter is to be measured is randomly extracted, the fiber diameter is measured near the center, and the number average fiber is obtained from the obtained measured value. Calculate the diameter. The observation magnification is about 1000 times, and the number of measurement is 500 or more (600 or less is suitable for work). On the other hand, the measurement of average fiber length observes a filler with an optical microscope, calculates | requires individual length, and calculates a number average fiber length from the measured value. Observation with an optical microscope begins with the preparation of a dispersed sample so that the fillers do not overlap each other. Observation is performed under the condition of 20 times the objective lens, and the observed image is taken as image data into a CCD camera having about 250,000 pixels. The obtained image data is calculated by using a program for obtaining the maximum distance between two points of the image data using an image analysis device. Under such conditions, the size per pixel corresponds to a length of 1.25 μm, and the number of measurement is 500 or more (600 or less is suitable for work).

The wollastonite of the present invention is a magnetic separator that reflects the iron content mixed in the raw material ore and the iron content mixed due to equipment wear when pulverizing the raw material ore in order to sufficiently reflect the inherent whiteness in the resin composition. It is preferable to remove as much as possible. It is preferable that the iron content in wollastonite is 0.5% by weight or less in terms of Fe ₂ O ₃ by such magnetic separator processing.
Silicate minerals (more preferably mica, talc, wollastonite) are preferably not surface-treated, but are surface-treated with various surface treatment agents such as silane coupling agents, higher fatty acid esters, and waxes. It may be. Furthermore, it may be granulated with a sizing agent such as various resins, higher fatty acid esters, and waxes.
Content of E component is 0.1-30 weight part with respect to a total of 100 weight part of A component and B component, Preferably it is 0.15-28 weight part, More preferably, it is 0.2-25. Parts by weight. When the content of E component is less than 0.1 parts by weight, sufficient flame retardancy in supercritical fluid microfoaming molding, which is a high weight reduction rate, cannot be obtained, and when it exceeds 30 parts by weight, impact resistance is greatly increased. Lost and appearance defects such as silver occur.

(F component: anti-drip agent)
The resin composition of the present invention contains an anti-drip agent as the F component. By containing this anti-drip agent, good flame retardancy can be achieved without impairing the physical properties of the molded product.
Examples of the anti-drip agent for the F component include a fluorinated polymer having a fibril-forming ability. Examples of such a polymer include polytetrafluoroethylene and tetrafluoroethylene copolymers (for example, tetrafluoroethylene / hexafluoropropylene copolymer). Polymer, etc.), partially fluorinated polymers as shown in US Pat. No. 4,379,910, polycarbonate resins produced from fluorinated diphenols, and the like. Among them, polytetrafluoroethylene (hereinafter sometimes referred to as PTFE) is preferable.

PTFE having a fibril forming ability has a very high molecular weight, and tends to be bonded to each other by an external action such as shearing force to form a fiber. The molecular weight is 1 million to 10 million, more preferably 2 million to 9 million in the number average molecular weight determined from the standard specific gravity. Such PTFE can be used in solid form or in the form of an aqueous dispersion. In addition, PTFE having such fibril forming ability can improve the dispersibility in the resin, and it is also possible to use a PTFE mixture in a mixed form with other resins in order to obtain better flame retardancy and mechanical properties. is there.
Examples of commercially available PTFE having such fibril forming ability include Teflon (registered trademark) 6J from Mitsui DuPont Fluorochemical Co., Ltd., Polyflon MPA FA500 and F-201L from Daikin Industries, Ltd. Commercially available PTFE aqueous dispersions include Asahi IC Fluoropolymers' full-on AD-1, AD-936, Daikin Kogyo's full-on D-1 and D-2, Mitsui Dupont Fluoro A typical example is Teflon (registered trademark) 30J manufactured by Chemical Corporation.

  As a mixed form of PTFE, (1) a method in which an aqueous dispersion of PTFE and an aqueous dispersion or solution of an organic polymer are mixed and co-precipitated to obtain a co-aggregated mixture (Japanese Patent Application Laid-Open No. 60-258263; (Method described in JP-A-63-154744), (2) A method of mixing an aqueous dispersion of PTFE and dried organic polymer particles (method described in JP-A-4-272957), (3) A method in which an aqueous dispersion of PTFE and an organic polymer particle solution are uniformly mixed, and each medium is simultaneously removed from the mixture (described in JP-A-06-220210, JP-A-08-188653, etc.) And (4) a method of polymerizing monomers forming an organic polymer in an aqueous dispersion of PTFE (a method described in JP-A-9-95583), and (5) A method in which an aqueous dispersion of TFE and an organic polymer dispersion are uniformly mixed, and a vinyl monomer is further polymerized in the mixture dispersion, and then a mixture is obtained (described in JP-A-11-29679, etc.). Those obtained by (Method) can be used. Examples of commercially available PTFE in a mixed form include “Metablene A3800” (trade name) manufactured by Mitsubishi Rayon Co., Ltd. and “BLENDEX B449” (trade name) manufactured by GE Specialty Chemicals.

  As a ratio of PTFE in the mixed form, 1 to 60% by weight of PTFE is preferable in 100% by weight of the PTFE mixture, and more preferably 5 to 55% by weight. When the ratio of PTFE is within such a range, good dispersibility of PTFE can be achieved. In addition, the ratio of the said E component shows the quantity of a net anti-drip agent, and in the case of PTFE of a mixed form, shows the amount of net PTFE.

  The content of the F component is 0.1 to 3 parts by weight, preferably 0.15 to 2 parts by weight, more preferably 0.2 to 1 part by weight, based on 100 parts by weight of the total of the A component and the B component. It is. If the anti-drip agent exceeds the above range and is too small, the flame retardancy in the supercritical fluid fine foam molding, which is a high weight reduction rate, becomes insufficient. On the other hand, when the amount of the anti-drip agent exceeds the above range, PTFE is not preferable because it precipitates on the surface of the molded product to cause poor appearance and also increases the cost of the resin composition.

  Moreover, as a styrene-type monomer used for the organic type polymer used for the polytetrafluoroethylene-type mixture of this invention, a C1-C6 alkyl group, a C1-C6 alkoxy group, and a halogen are used. Styrene optionally substituted with one or more groups selected from the group consisting of, for example, ortho-methylstyrene, meta-methylstyrene, para-methylstyrene, dimethylstyrene, ethyl-styrene, para-tert-butylstyrene , Methoxystyrene, fluorostyrene, monobromostyrene, dibromostyrene, and tribromostyrene, vinylxylene, vinylnaphthalene, but are not limited thereto. The styrenic monomer can be used alone or in combination of two or more.

  The acrylic monomer used in the organic polymer used in the polytetrafluoroethylene-based mixture (component B) of the present invention includes an optionally substituted (meth) acrylate derivative. Specifically, the acrylic monomer includes one or more groups selected from the group consisting of an alkyl group having 1 to 20 carbon atoms, a cycloalkyl group having 3 to 8 carbon atoms, an aryl group, and a glycidyl group. Optionally substituted (meth) acrylate derivatives such as (meth) acrylonitrile, methyl (meth) acrylate, ethyl (meth) acrylate, propyl (meth) acrylate, butyl (meth) acrylate, amyl (meth) acrylate, hexyl (Meth) acrylate, 2-ethylhexyl (meth) acrylate, cyclohexyl (meth) acrylate, octyl (meth) acrylate, dodecyl (meth) acrylate, phenyl (meth) acrylate, benzyl (meth) acrylate and glycidyl (meth) ) Acrylate, C1-6 alkyl Group, or maleimide which may be substituted by an aryl group, for example, maleimide, N- methyl - maleimide and N- phenyl - maleimide, maleic acid, phthalic acid and itaconic acid are exemplified, but are not limited thereto. The acrylic monomers can be used alone or in admixture of two or more. Among these, (meth) acrylonitrile is preferable.

  The amount of the acrylic monomer-derived unit contained in the organic polymer used in the coating layer is 8 to 11 parts by weight, preferably 8 to 10 parts by weight, based on 100 parts by weight of the styrene monomer-derived unit. Preferably it is 8-9 weight part. If the acrylic monomer-derived unit is less than 8 parts by weight, the coating strength may be reduced, and if it is more than 11 parts by weight, the surface appearance of the molded product may be deteriorated.

The polytetrafluoroethylene-based mixture of the present invention preferably has a residual water content of 0.5% by weight or less, more preferably 0.2 to 0.4% by weight, and still more preferably 0.1 to 0. 3% by weight. If the residual water content is more than 0.5% by weight, the flame retardancy may be adversely affected.
In the production process of the polytetrafluoroethylene mixture of the present invention, a coating layer containing one or more monomers selected from the group consisting of styrene monomers and acrylic monomers in the presence of an initiator Forming on the exterior of the branched polytetrafluoroethylene. Further, after the coating layer forming step, the residual moisture content is dried to 0.5 wt% or less, preferably 0.2 to 0.4 wt%, more preferably 0.1 to 0.3 wt%. Preferably a step is included. The drying step can be performed using methods known in the art such as, for example, hot air drying or vacuum drying methods.

  The initiator used in the polytetrafluoroethylene-based mixture of the present invention can be used without limitation as long as it is used in the polymerization reaction of styrene-based and / or acrylic monomers. Examples of the initiator include cumyl hydroperoxide, di-tert-butyl peroxide, benzoyl peroxide, hydrogen peroxide, and potassium peroxide, but are not limited thereto. In the polytetrafluoroethylene-based mixture of the present invention, one or more initiators can be used depending on the reaction conditions. The amount of the initiator is freely selected within the range used in consideration of the amount of polytetrafluoroethylene and the type / amount of monomer, and is 0.15 to 0.00 based on the amount of the total composition. It is preferable to use 25 parts by weight.

The polytetrafluoroethylene-based mixture of the present invention was produced by the following procedure by suspension polymerization.
First, water and a branched polytetrafluoroethylene dispersion (solid concentration: 60%, polytetrafluoroethylene particle diameter: 0.15-0.3 μm) were placed in the reactor, and then the acrylic monomer and styrene were stirred with stirring. Cumene hydroperoxide was added as a monomer and a water-soluble initiator and reacted at 80 to 90 ° C. for 9 hours. After completion of the reaction, the water was removed by centrifuging for 30 minutes with a centrifuge to obtain a pasty product. Thereafter, the product paste was dried with a hot air dryer at 80 to 100 ° C. for 8 hours. Thereafter, the dried product was pulverized to obtain the polytetrafluoroethylene-based mixture of the present invention.

  Such a suspension polymerization method does not require a polymerization step by emulsion dispersion in the emulsion polymerization method exemplified in Japanese Patent No. 3469391, and therefore does not require an emulsifier and an electrolyte salt for coagulating and precipitating the polymerized latex. In addition, in the polytetrafluoroethylene mixture produced by the emulsion polymerization method, the emulsifier and the electrolyte salt in the mixture are easily mixed and difficult to remove. Therefore, the emulsifier, the sodium metal ion derived from the electrolyte salt, and the potassium metal ion are reduced. It ’s difficult. Since the polytetrafluoroethylene-based mixture (component B) used in the present invention is produced by a suspension polymerization method, such an emulsifier and electrolyte salts are not used, so that sodium metal ions and potassium metal ions in the mixture are used. Can be reduced, and thermal stability and hydrolysis resistance can be improved.

In the present invention, coated branched PTFE can be used as an anti-drip agent.
Coated branched PTFE is a polytetrafluoroethylene mixture composed of branched polytetrafluoroethylene particles and an organic polymer, and is derived from an organic polymer, preferably a styrene monomer, outside the branched polytetrafluoroethylene. It has a coating layer made of a polymer containing units and / or units derived from acrylic monomers. The coating layer is formed on the surface of branched polytetrafluoroethylene. The coating layer preferably contains a copolymer of a styrene monomer and an acrylic monomer.

The polytetrafluoroethylene contained in the coated branched PTFE is branched polytetrafluoroethylene. When the polytetrafluoroethylene contained is not branched polytetrafluoroethylene, the dripping prevention effect when the amount of polytetrafluoroethylene added is small is insufficient. The branched polytetrafluoroethylene is in the form of particles, and preferably has a particle diameter of 0.1 to 0.6 μm, more preferably 0.3 to 0.5 μm, and still more preferably 0.3 to 0.4 μm. When the particle diameter is smaller than 0.1 μm, the surface appearance of the molded article is excellent, but it is difficult to obtain polytetrafluoroethylene having a particle diameter smaller than 0.1 μm commercially. On the other hand, when the particle diameter is larger than 0.6 μm, the surface appearance of the molded product is deteriorated. The number average molecular weight of the polytetrafluoroethylene used in the present invention is preferably 1 × 10 ⁴ to 1 × 10 ⁷ , more preferably 2 × 10 ^{6 to} 9 × 10 ⁶ , and generally a polytetrafluoroethylene having a high molecular weight. Fluoroethylene is more preferred in terms of stability. Either powder or dispersion form may be used.

  The content of branched polytetrafluoroethylene in the coated branched PTFE is preferably 20 to 60 parts by weight, more preferably 40 to 55 parts by weight, still more preferably 47 to 50 parts by weight with respect to 100 parts by weight of the total weight of the coated branched PTFE. 53 parts by weight, particularly preferably 48 to 52 parts by weight, most preferably 49 to 51 parts by weight. When the proportion of the branched polytetrafluoroethylene is within such a range, good dispersibility of the branched polytetrafluoroethylene can be achieved.

(Other additives)
(I) Phosphorus stabilizer Examples of the phosphorous stabilizer include phosphorous acid, phosphoric acid, phosphonous acid, phosphonic acid and esters thereof, and tertiary phosphine.
Specifically, as the phosphite compound, for example, triphenyl phosphite, tris (nonylphenyl) phosphite, tridecyl phosphite, trioctyl phosphite, trioctadecyl phosphite, didecyl monophenyl phosphite, dioctyl monophenyl Phosphite, diisopropyl monophenyl phosphite, monobutyl diphenyl phosphite, monodecyl diphenyl phosphite, monooctyl diphenyl phosphite, tris (diethylphenyl) phosphite, tris (di-iso-propylphenyl) phosphite, tris (di -N-butylphenyl) phosphite, tris (2,4-di-tert-butylphenyl) phosphite, tris (2,6-di-tert-butylphenyl) phosphite, dis Allyl pentaerythritol diphosphite, bis (2,4-di-tert-butylphenyl) pentaerythritol diphosphite, bis (2,6-di-tert-butyl-4-methylphenyl) pentaerythritol diphosphite, bis (2,6-di-tert-butyl-4-ethylphenyl) pentaerythritol diphosphite, bis {2,4-bis (1-methyl-1-phenylethyl) phenyl} pentaerythritol diphosphite, phenylbisphenol A Examples include pentaerythritol diphosphite, bis (nonylphenyl) pentaerythritol diphosphite, and dicyclohexyl pentaerythritol diphosphite.

  Further, as other phosphite compounds, those which react with dihydric phenols and have a cyclic structure can be used. For example, 2,2′-methylenebis (4,6-di-tert-butylphenyl) (2,4-di-tert-butylphenyl) phosphite, 2,2′-methylenebis (4,6-di-tert- Examples include butylphenyl) (2-tert-butyl-4-methylphenyl) phosphite and 2,2-methylenebis (4,6-di-tert-butylphenyl) octyl phosphite.

  Examples of the phosphate compound include tributyl phosphate, trimethyl phosphate, tricresyl phosphate, triphenyl phosphate, trichlorophenyl phosphate, triethyl phosphate, diphenyl cresyl phosphate, diphenyl monoorthoxenyl phosphate, tributoxyethyl phosphate, dibutyl phosphate, dioctyl phosphate, Examples thereof include diisopropyl phosphate, and triphenyl phosphate and trimethyl phosphate are preferable.

  Examples of the phosphonite compound include tetrakis (2,4-di-tert-butylphenyl) -4,4′-biphenylenediphosphonite, tetrakis (2,4-di-tert-butylphenyl) -4,3′-biphenylenedi. Phosphonite, tetrakis (2,4-di-tert-butylphenyl) -3,3′-biphenylenediphosphonite, tetrakis (2,6-di-tert-butylphenyl) -4,4′-biphenylenediphosphonite Tetrakis (2,6-di-tert-butylphenyl) -4,3′-biphenylene diphosphonite, tetrakis (2,6-di-tert-butylphenyl) -3,3′-biphenylene diphosphonite, bis (2,4-di-tert-butylphenyl) -4-phenyl-phenylphosphonite, bis (2,4-di tert-butylphenyl) -3-phenyl-phenylphosphonite, bis (2,6-di-n-butylphenyl) -3-phenyl-phenylphosphonite, bis (2,6-di-tert-butylphenyl)- 4-phenyl-phenylphosphonite, bis (2,6-di-tert-butylphenyl) -3-phenyl-phenylphosphonite, and the like, and tetrakis (di-tert-butylphenyl) -biphenylenediphosphonite, bis (Di-tert-butylphenyl) -phenyl-phenylphosphonite is preferred, tetrakis (2,4-di-tert-butylphenyl) -biphenylenediphosphonite, bis (2,4-di-tert-butylphenyl)- More preferred is phenyl-phenylphosphonite. Such a phosphonite compound is preferable because it can be used in combination with a phosphite compound having an aryl group in which two or more alkyl groups are substituted.

  Examples of the phosphonate compound include dimethyl benzenephosphonate, diethyl benzenephosphonate, and dipropyl benzenephosphonate.

  Tertiary phosphine includes triethylphosphine, tripropylphosphine, tributylphosphine, trioctylphosphine, triamylphosphine, dimethylphenylphosphine, dibutylphenylphosphine, diphenylmethylphosphine, diphenyloctylphosphine, triphenylphosphine, tri-p-tolyl. Examples include phosphine, trinaphthylphosphine, and diphenylbenzylphosphine. A particularly preferred tertiary phosphine is triphenylphosphine.

  The phosphorus stabilizers can be used alone or in combination of two or more. Among the phosphorus stabilizers, phosphonite compounds or phosphite compounds represented by the following general formula (II) are preferable.

（式（ＩＩ）中、ＲおよびＲ’は炭素数６〜３０のアルキル基または炭素数６〜３０のアリール基を表し、互いに同一であっても異なっていてもよい。）

(In Formula (II), R and R ′ represent an alkyl group having 6 to 30 carbon atoms or an aryl group having 6 to 30 carbon atoms, and may be the same or different from each other.)

  As described above, tetrakis (2,4-di-tert-butylphenyl) -biphenylenediphosphonite is preferable as the phosphonite compound, and the stabilizer containing phosphonite as a main component is Sandostab P-EPQ (trademark, manufactured by Clariant). ) And Irgafos P-EPQ (trademark, manufactured by CIBA SPECIALTY CHEMICALS) and both can be used.

  Among the above formulas (II), more preferred phosphite compounds are distearyl pentaerythritol diphosphite, bis (2,4-di-tert-butylphenyl) pentaerythritol diphosphite, bis (2,6-di). -Tert-butyl-4-methylphenyl) pentaerythritol diphosphite, and bis {2,4-bis (1-methyl-1-phenylethyl) phenyl} pentaerythritol diphosphite.

  Distearyl pentaerythritol diphosphite is commercially available as ADK STAB PEP-8 (trademark, manufactured by Asahi Denka Kogyo Co., Ltd.) and JPP681S (trademark, manufactured by Johoku Chemical Industry Co., Ltd.), and any of them can be used. Bis (2,4-di-tert-butylphenyl) pentaerythritol diphosphite is ADK STAB PEP-24G (trademark, manufactured by Asahi Denka Kogyo Co., Ltd.), Alkanox P-24 (trademark, manufactured by Great Lakes), Ultranox. P626 (trademark, manufactured by GE Specialty Chemicals), Doverphos S-9432 (trademark, manufactured by Dover Chemical), and Irgafos126 and 126FF (trademark, manufactured by CIBA SPECIALTY CHEMICALS) are also available. Bis (2,6-di-tert-butyl-4-methylphenyl) pentaerythritol diphosphite is commercially available as ADK STAB PEP-36 (trademark, manufactured by Asahi Denka Kogyo Co., Ltd.) and can be easily used. Further, bis {2,4-bis (1-methyl-1-phenylethyl) phenyl} pentaerythritol diphosphite is produced by ADK STAB PEP-45 (trademark, manufactured by Asahi Denka Kogyo Co., Ltd.) and Doverphos S-9228 (trademark). , Manufactured by Dober Chemical Co.) and any of them can be used.

(Ii) Hindered phenolic antioxidant As the hindered phenolic compound, various compounds that are usually blended in a resin can be used. Examples of such hindered phenol compounds include α-tocopherol, butylhydroxytoluene, sinapyl alcohol, vitamin E, octadecyl-3- (3,5-di-tert-butyl-4-hydroxyphenyl) propionate, 2-tert -Butyl-6- (3'-tert-butyl-5'-methyl-2'-hydroxybenzyl) -4-methylphenyl acrylate, 2,6-di-tert-butyl-4- (N, N-dimethylamino) Methyl) phenol, 3,5-di-tert-butyl-4-hydroxybenzylphosphonate diethyl ester, 2,2'-methylenebis (4-methyl-6-tert-butylphenol), 2,2'-methylenebis (4-ethyl) -6-tert-butylphenol), 4,4'-methylenebis (2,6 Di-tert-butylphenol), 2,2′-methylenebis (4-methyl-6-cyclohexylphenol), 2,2′-dimethylene-bis (6-α-methyl-benzyl-p-cresol), 2,2 ′ -Ethylidene-bis (4,6-di-tert-butylphenol), 2,2'-butylidene-bis (4-methyl-6-tert-butylphenol), 4,4'-butylidenebis (3-methyl-6-tert) -Butylphenol), triethylene glycol-N-bis-3- (3-tert-butyl-4-hydroxy-5-methylphenyl) propionate, 1,6-hexanediol bis [3- (3,5-di- tert-butyl-4-hydroxyphenyl) propionate], bis [2-tert-butyl-4-methyl 6- (3-tert-butyl) Ru-5-methyl-2-hydroxybenzyl) phenyl] terephthalate, 3,9-bis {2- [3- (3-tert-butyl-4-hydroxy-5-methylphenyl) propionyloxy] -1,1- Dimethylethyl} -2,4,8,10-tetraoxaspiro [5,5] undecane, 4,4′-thiobis (6-tert-butyl-m-cresol), 4,4′-thiobis (3-methyl) -6-tert-butylphenol), 2,2'-thiobis (4-methyl-6-tert-butylphenol), bis (3,5-di-tert-butyl-4-hydroxybenzyl) sulfide, 4,4'- Di-thiobis (2,6-di-tert-butylphenol), 4,4′-tri-thiobis (2,6-di-tert-butylphenol), 2,2-thiodiethyl Bis- [3- (3,5-di-tert-butyl-4-hydroxyphenyl) propionate], 2,4-bis (n-octylthio) -6- (4-hydroxy-3,5-di-tert- Butylanilino) -1,3,5-triazine, N, N′-hexamethylenebis- (3,5-di-tert-butyl-4-hydroxyhydrocinnamide), N, N′-bis [3- (3 , 5-Di-tert-butyl-4-hydroxyphenyl) propionyl] hydrazine, 1,1,3-tris (2-methyl-4-hydroxy-5-tert-butylphenyl) butane, 1,3,5-trimethyl -2,4,6-tris (3,5-di-tert-butyl-4-hydroxybenzyl) benzene, tris (3,5-di-tert-butyl-4-hydroxyphenyl) isocyanate Anurate, tris (3,5-di-tert-butyl-4-hydroxybenzyl) isocyanurate, 1,3,5-tris (4-tert-butyl-3-hydroxy-2,6-dimethylbenzyl) isocyanurate, 1,3,5-tris2 [3 (3,5-di-tert-butyl-4-hydroxyphenyl) propionyloxy] ethyl isocyanurate, tetrakis [methylene-3- (3,5-di-tert-butyl- 4-hydroxyphenyl) propionate] methane, triethylene glycol-N-bis-3- (3-tert-butyl-4-hydroxy-5-methylphenyl) propionate, triethylene glycol-N-bis-3- (3- tert-butyl-4-hydroxy-5-methylphenyl) acetate, 3,9-bis [2- 3- (3-tert-butyl-4-hydroxy-5-methylphenyl) acetyloxy} -1,1-dimethylethyl] -2,4,8,10-tetraoxaspiro [5,5] undecane, tetrakis [ Methylene-3- (3-tert-butyl-4-hydroxy-5-methylphenyl) propionate] methane, 1,3,5-trimethyl-2,4,6-tris (3-tert-butyl-4-hydroxy- Examples include 5-methylbenzyl) benzene and tris (3-tert-butyl-4-hydroxy-5-methylbenzyl) isocyanurate.

  Among the above compounds, tetrakis [methylene-3- (3-tert-butyl-4-hydroxy-5-methylphenyl) propionate] methane, octadecyl-3- (3,5-di-tert-butyl-) is used in the present invention. 4-hydroxyphenyl) propionate, and 3,9-bis [2- {3- (3-tert-butyl-4-hydroxy-5-methylphenyl) propionyloxy} -1,1-dimethylethyl] -2,4 , 8,10-Tetraoxaspiro [5,5] undecane is preferably used. In particular, 3,9-bis [2- {3- (3-tert-butyl-4-hydroxy-5-methylphenyl) propionyloxy} -1,1-dimethylethyl] -2,4,8,10-tetraoxa Spiro [5,5] undecane is preferred. The said hindered phenolic antioxidant can be used individually or in combination of 2 or more types.

  Either of the phosphorus stabilizer and the hindered phenol antioxidant is preferably blended, and the combination of these is more preferred. The blending amount of the phosphorus stabilizer and the hindered phenol antioxidant is preferably 0.001 to 3 parts by weight, more preferably 0.005 to 2 parts per 100 parts by weight in total of the A component and the B component. Part by weight, more preferably 0.01 to 1 part by weight. In the case of combined use, 0.01 to 0.3 parts by weight of a phosphorus-based stabilizer and 0.01 to 0.3 parts by weight of a hindered phenol-based antioxidant with respect to a total of 100 parts by weight of the component A and the component B Is more preferably blended.

(Iii) Mold Release Agent The polycarbonate resin composition of the present invention preferably further contains a mold release agent for the purpose of improving productivity during molding and reducing distortion of the molded product. Known release agents can be used. For example, saturated fatty acid ester, unsaturated fatty acid ester, polyolefin wax (polyethylene wax, 1-alkene polymer, etc., which may be modified with a functional group-containing compound such as acid modification), silicone compound, fluorine compound ( And fluorine oil represented by polyfluoroalkyl ether), paraffin wax, beeswax and the like. Among these, fatty acid esters are preferable as a release agent. Such fatty acid esters are esters of aliphatic alcohols and aliphatic carboxylic acids. Such an aliphatic alcohol may be a monohydric alcohol or a dihydric or higher polyhydric alcohol. Moreover, as carbon number of this alcohol, it is the range of 3-32, More preferably, it is the range of 5-30. Examples of such monohydric alcohols include dodecanol, tetradecanol, hexadecanol, octadecanol, eicosanol, tetracosanol, seryl alcohol, and triacontanol. Examples of such polyhydric alcohols include pentaerythritol, dipentaerythritol, tripentaerythritol, polyglycerol (triglycerol to hexaglycerol), ditrimethylolpropane, xylitol, sorbitol, and mannitol. In the fatty acid ester of the present invention, a polyhydric alcohol is more preferable.

  On the other hand, the aliphatic carboxylic acid preferably has 3 to 32 carbon atoms, and particularly preferably an aliphatic carboxylic acid having 10 to 22 carbon atoms. Examples of the aliphatic carboxylic acid include decanoic acid, undecanoic acid, dodecanoic acid, tridecanoic acid, tetradecanoic acid, pentadecanoic acid, hexadecanoic acid (palmitic acid), heptadecanoic acid, octadecanoic acid (stearic acid), nonadecanoic acid, behenic acid, Mention may be made of saturated aliphatic carboxylic acids such as icosanoic acid and docosanoic acid, and unsaturated aliphatic carboxylic acids such as palmitoleic acid, oleic acid, linoleic acid, linolenic acid, eicosenoic acid, eicosapentaenoic acid, and cetreic acid . Among the above, aliphatic carboxylic acids having 14 to 20 carbon atoms are preferable. Of these, saturated aliphatic carboxylic acids are preferred. In particular, stearic acid and palmitic acid are preferred.

  The above aliphatic carboxylic acids such as stearic acid and palmitic acid are usually produced from natural fats and oils such as animal fats such as beef tallow and lard and vegetable oils such as palm oil and sunflower oil. Therefore, these aliphatic carboxylic acids are usually a mixture containing other carboxylic acid components having different numbers of carbon atoms. Accordingly, in the production of the fatty acid ester of the present invention, aliphatic carboxylic acids produced from such natural fats and oils and in the form of a mixture containing other carboxylic acid components, particularly stearic acid and palmitic acid are preferably used.

The fatty acid ester of the present invention may be either a partial ester or a total ester (full ester). However, partial esters are more preferably full esters because they usually have a high hydroxyl value and tend to induce decomposition of the resin at high temperatures. The acid value in the fatty acid ester of the present invention is preferably 20 or less, more preferably 4 to 20 and even more preferably 4 to 12 from the viewpoint of thermal stability. The acid value can be substantially zero. The hydroxyl value of the fatty acid ester is more preferably in the range of 0.1-30. Further, the iodine value is preferably 10 or less. The iodine value can be substantially zero. These characteristics can be obtained by a method defined in JIS K 0070.
The content of the release agent is preferably 0.005 to 2 parts by weight, more preferably 0.01 to 1 part by weight, and still more preferably 0.05 to 100 parts by weight of the total of the component A and the component B. -0.5 parts by weight. In such a range, the polycarbonate resin composition has good release properties and release properties. In particular, such an amount of fatty acid ester provides a polycarbonate resin composition having good release properties and roll release properties without impairing good hue.

(Iv) Ultraviolet absorber The polycarbonate resin composition of the present invention may contain an ultraviolet absorber. Since the resin composition of the present invention is excellent in transparency, it is very suitable for use in transmitting light.
In the benzophenone series, for example, 2,4-dihydroxybenzophenone, 2-hydroxy-4-methoxybenzophenone, 2-hydroxy-4-octoxybenzophenone, 2-hydroxy-4-benzyloxybenzophenone, 2-hydroxy-4-methoxy- 5-sulfoxybenzophenone, 2-hydroxy-4-methoxy-5-sulfoxytrihydridolate benzophenone, 2,2′-dihydroxy-4-methoxybenzophenone, 2,2 ′, 4,4′-tetrahydroxybenzophenone, 2 2,2'-dihydroxy-4,4'-dimethoxybenzophenone, 2,2'-dihydroxy-4,4'-dimethoxy-5-sodiumsulfoxybenzophenone, bis (5-benzoyl-4-hydroxy-2-methoxyphenyl) ) Methane, 2-hydroxy Examples include -4-n-dodecyloxybenzophenone and 2-hydroxy-4-methoxy-2'-carboxybenzophenone.

  In the benzotriazole series, for example, 2- (2-hydroxy-5-methylphenyl) benzotriazole, 2- (2-hydroxy-5-tert-octylphenyl) benzotriazole, 2- (2-hydroxy-3, 5-Dicumylphenyl) phenylbenzotriazole, 2- (2-hydroxy-3-tert-butyl-5-methylphenyl) -5-chlorobenzotriazole, 2,2′-methylenebis [4- (1,1,3 , 3-tetramethylbutyl) -6- (2H-benzotriazol-2-yl) phenol], 2- (2-hydroxy-3,5-di-tert-butylphenyl) benzotriazole, 2- (2- Hydroxy-3,5-di-tert-butylphenyl) -5-chlorobenzotriazole, 2- (2-hydroxy-3,5 Di-tert-amylphenyl) benzotriazole, 2- (2-hydroxy-5-tert-octylphenyl) benzotriazole, 2- (2-hydroxy-5-tert-butylphenyl) benzotriazole, 2- ( 2-hydroxy-4-octoxyphenyl) benzotriazole, 2,2'-methylenebis (4-cumyl-6-benzotriazolephenyl), 2,2'-p-phenylenebis (1,3-benzoxazine-4 -One), and 2- [2-hydroxy-3- (3,4,5,6-tetrahydrophthalimidomethyl) -5-methylphenyl] benzotriazole, and 2- (2'-hydroxy-5-methacryloxy) Copolymerization of ethylphenyl) -2H-benzotriazole with vinyl monomer copolymerizable with the monomer And 2- (2′-hydroxy-5-acryloxyethylphenyl) -2H-benzotriazole and a copolymer of vinyl monomer copolymerizable with the monomer, 2-hydroxyphenyl-2H-benzotriazole skeleton A polymer having

  In the hydroxyphenyl triazine series, for example, 2- (4,6-diphenyl-1,3,5-triazin-2-yl) -5-hexyloxyphenol, 2- (4,6-diphenyl-1,3,5) -Triazin-2-yl) -5-methyloxyphenol, 2- (4,6-diphenyl-1,3,5-triazin-2-yl) -5-ethyloxyphenol, 2- (4,6-diphenyl) -1,3,5-triazin-2-yl) -5-propyloxyphenol and 2- (4,6-diphenyl-1,3,5-triazin-2-yl) -5-butyloxyphenol Illustrated. Furthermore, the phenyl group of the above exemplary compounds such as 2- (4,6-bis (2,4-dimethylphenyl) -1,3,5-triazin-2-yl) -5-hexyloxyphenol is 2,4-dimethyl. Examples of the compound are phenyl groups.

In the cyclic imino ester system, for example, 2,2′-p-phenylenebis (3,1-benzoxazin-4-one), 2,2 ′-(4,4′-diphenylene) bis (3,1-benzoxazine) -4-one), 2,2 ′-(2,6-naphthalene) bis (3,1-benzoxazin-4-one), and the like.
In the case of cyanoacrylate, for example, 1,3-bis-[(2′-cyano-3 ′, 3′-diphenylacryloyl) oxy] -2,2-bis [(2-cyano-3,3-diphenylacryloyl) oxy ] Methyl) propane, 1,3-bis-[(2-cyano-3,3-diphenylacryloyl) oxy] benzene and the like.

  Further, the ultraviolet absorber has a structure of a monomer compound capable of radical polymerization, whereby the ultraviolet-absorbing monomer and / or the light-stable monomer having a hindered amine structure, and an alkyl (meth) acrylate. A polymer type ultraviolet absorber obtained by copolymerization with a monomer such as may be used. Preferred examples of the UV-absorbing monomer include compounds containing a benzotriazole skeleton, a benzophenone skeleton, a triazine skeleton, a cyclic imino ester skeleton, and a cyanoacrylate skeleton in the ester substituent of (meth) acrylate. The

Of these, benzotriazoles and hydroxyphenyltriazines are preferred in terms of ultraviolet absorption, and cyclic iminoesters and cyanoacrylates are preferred in terms of heat resistance and hue (transparency). You may use the said ultraviolet absorber individually or in mixture of 2 or more types.
The content of the ultraviolet absorber is preferably 0.01 to 2 parts by weight, more preferably 0.02 to 2 parts by weight, and still more preferably 0.03 based on a total of 100 parts by weight of the component A and the component B. To 1 part by weight, more preferably 0.05 to 0.5 part by weight.

(V) Dye / pigment The polycarbonate resin composition of the present invention can further contain various dyes / pigments and can provide a molded product exhibiting various design properties. Since the polycarbonate resin composition of the present invention is excellent in transparency, it is extremely suitable for use in transmitting light. Therefore, for example, by adding a fluorescent brightening agent, the polycarbonate resin composition of the present invention is given a higher light transmittance and natural transparency, and a fluorescent brightening agent or other fluorescent dye that emits light is added. By blending, it is possible to impart a better design effect utilizing the luminescent color. Further, a polycarbonate resin composition which is finely colored with a very small amount of dye and pigment and has high transparency can also be provided.

  Examples of the fluorescent dye (including a fluorescent brightening agent) used in the present invention include a coumarin fluorescent dye, a benzopyran fluorescent dye, a perylene fluorescent dye, an anthraquinone fluorescent dye, a thioindigo fluorescent dye, and a xanthene fluorescent dye. And xanthone fluorescent dyes, thioxanthene fluorescent dyes, thioxanthone fluorescent dyes, thiazine fluorescent dyes, and diaminostilbene fluorescent dyes. Among these, coumarin fluorescent dyes, benzopyran fluorescent dyes, and perylene fluorescent dyes are preferable because they have good heat resistance and little deterioration during molding of the polycarbonate resin.

Examples of dyes other than the above bluing agents and fluorescent dyes include perylene dyes, coumarin dyes, thioindigo dyes, anthraquinone dyes, thioxanthone dyes, ferrocyanides such as bitumen, perinone dyes, quinoline dyes, quinacridone And dyes such as dyes, dioxazine dyes, isoindolinone dyes, and phthalocyanine dyes. Furthermore, the resin composition of this invention can mix | blend a metallic pigment, and can also obtain a better metallic color. As the metallic pigment, those having a metal film or a metal oxide film on various plate-like fillers are suitable.
The content of the dye / pigment is preferably 0.00001 to 1 part by weight and more preferably 0.00005 to 0.5 part by weight with respect to 100 parts by weight of the total of the A component and the B component.

(Vi) Other Heat Stabilizers The polycarbonate resin composition of the present invention may contain other heat stabilizers other than the phosphorus stabilizers and hindered phenol antioxidants. Such other heat stabilizers are preferably used in combination with any of these stabilizers and antioxidants, and particularly preferably used in combination with both. Examples of such other heat stabilizers include lactone stabilizers represented by the reaction product of 3-hydroxy-5,7-di-tert-butyl-furan-2-one and o-xylene (such stabilizers). Is described in detail in JP-A-7-233160). Such a compound is commercially available as Irganox HP-136 (trademark, manufactured by CIBA SPECIALTY CHEMICALS) and can be used. Furthermore, a stabilizer obtained by mixing the compound with various phosphite compounds and hindered phenol compounds is commercially available. For example, Irganox HP-2921 manufactured by the above company is preferably exemplified. In the present invention, such a premixed stabilizer can also be used. The blending amount of the lactone stabilizer is preferably 0.0005 to 0.05 parts by weight, more preferably 0.001 to 0.03 parts by weight with respect to 100 parts by weight of the component A.

  Other stabilizers include sulfur-containing stabilizers such as pentaerythritol tetrakis (3-mercaptopropionate), pentaerythritol tetrakis (3-laurylthiopropionate), and glycerol-3-stearylthiopropionate. Illustrated. Such a stabilizer is particularly effective when the resin composition is applied to rotational molding. The amount of the sulfur-containing stabilizer is preferably 0.001 to 0.1 parts by weight, more preferably 0.01 to 0.08 parts by weight, based on 100 parts by weight of the total of the component A and the component B. is there.

(Vii) Other fillers In the aromatic polycarbonate resin composition of the present invention, various fillers other than the component E can be blended as reinforcing fillers within the range where the effects of the present invention are exhibited. For example, calcium carbonate, glass fiber, glass bead, glass balloon, glass milled fiber, glass flake, carbon fiber, carbon flake, carbon bead, carbon milled fiber, graphite, vapor grown ultrafine carbon fiber (fiber diameter is 0.1 μm Carbon nanotubes (fiber diameter is less than 0.1 μm, hollow), fullerene, metal flakes, metal fibers, metal coated glass fibers, metal coated carbon fibers, metal coated glass flakes, silica, metal oxide particles, Examples include metal oxide fibers, metal oxide balloons, and various whiskers (such as potassium titanate whiskers, aluminum borate whiskers, and basic magnesium sulfate). These reinforcing fillers may be used alone or in combination of two or more.
The content of these fillers is preferably 0.1 to 30 parts by weight, more preferably 0.5 to 25 parts by weight with respect to 100 parts by weight of the total of the A component and the B component.

(Viii) White pigment for high light reflection The polycarbonate resin composition of the present invention can be provided with a light reflection effect by blending a white pigment for high light reflection. As such a white pigment, a titanium dioxide (particularly titanium dioxide treated with an organic surface treating agent such as silicone) pigment is particularly preferred. The content of the white pigment for high light reflection is preferably 3 to 30 parts by weight, more preferably 8 to 25 parts by weight with respect to 100 parts by weight as a total of the A component and the B component. Two or more kinds of white pigments for high light reflection can be used in combination.

(Ix) Other resins and elastomers In the resin composition of the present invention, other resins and elastomers can be used in a small proportion within a range in which the effects of the present invention are exhibited.
Examples of such other resins include polyester resins such as polyethylene terephthalate and polybutylene terephthalate, polyamide resins, polyimide resins, polyetherimide resins, polyurethane resins, silicone resins, polyphenylene ether resins, polyphenylene sulfide resins, polysulfone resins, polyethylene, and polypropylene. And other resins such as polyolefin resins, polymethacrylate resins, phenol resins, and epoxy resins.
Examples of the elastomer include isobutylene / isoprene rubber, ethylene / propylene rubber, acrylic elastomer, polyester elastomer, and polyamide elastomer.

(X) Other additives In addition, the flame retardant aromatic polycarbonate resin composition of the present invention contains a small amount of additives known per se for imparting various functions to the molded product and improving properties. can do. These additives are used in usual amounts as long as the object of the present invention is not impaired.
Examples of such additives include sliding agents (for example, PTFE particles), colorants (for example, pigments and dyes such as carbon black and titanium oxide), light diffusing agents (for example, acrylic crosslinked particles, silicon crosslinked particles, ultrathin glass flakes, carbonic acid Calcium particles), fluorescent dyes, inorganic phosphors (for example, phosphors containing aluminate as a mother crystal), antistatic agents, crystal nucleating agents, inorganic and organic antibacterial agents, photocatalytic antifouling agents (for example, fine particle titanium oxide) , Fine particle zinc oxide), radical generators, infrared absorbers (heat ray absorbers), and photochromic agents.

(Manufacture of thermoplastic resin composition)
Arbitrary methods are employ | adopted in order to manufacture the thermoplastic resin composition of this invention. For example, the A component to the F component and optionally other additives are sufficiently mixed using a premixing means such as a V-type blender, a Henschel mixer, a mechanochemical apparatus, an extrusion mixer, and then extruded granulated as necessary. There is a method of granulating such a premixed mixture using a vessel or a briquetting machine, then melt-kneading with a melt-kneader represented by a vent type twin screw extruder, and then pelletizing with a pelletizer.

  In addition, a method of supplying each component independently to a melt kneader represented by a vent type twin screw extruder, or a part of each component is premixed and then supplied to the melt kneader independently of the remaining components. The method of doing is also mentioned. Examples of the method of premixing a part of each component include a method of premixing components other than the component A in advance and then mixing the components with the thermoplastic resin of the component A or supplying them directly to the extruder.

  As a premixing method, for example, when a component having a powder form is included as the component A, a part of the powder and an additive to be blended are mixed to produce a master batch of the additive diluted with the powder. A method using a master batch can be mentioned. Furthermore, the method etc. which supply one component independently from the middle of a melt extruder are mentioned. In addition, when there exists a liquid thing in the component to mix | blend, what is called a liquid injection apparatus or a liquid addition apparatus can be used for supply to a melt extruder.

As the extruder, one having a vent capable of degassing moisture in the raw material and volatile gas generated from the melt-kneaded resin can be preferably used. From the vent, a vacuum pump for efficiently discharging generated moisture and volatile gas to the outside of the extruder is preferably installed. It is also possible to remove a foreign substance from the resin composition by installing a screen for removing the foreign substance mixed in the extrusion raw material in the zone in front of the extruder die. Examples of such a screen include a wire mesh, a screen changer, a sintered metal plate (such as a disk filter), and the like.
Examples of the melt kneader include a banbury mixer, a kneading roll, a single screw extruder, a multi-screw extruder having three or more axes, in addition to a twin screw extruder.

  The resin extruded as described above is directly cut into pellets, or after forming strands, the strands are cut with a pelletizer to be pelletized. When it is necessary to reduce the influence of external dust during pelletization, it is preferable to clean the atmosphere around the extruder. Furthermore, in the manufacture of such pellets, various methods already proposed for polycarbonate resin for optical discs are used to narrow the shape distribution of pellets, reduce miscuts, and reduce fine powder generated during transportation or transportation. In addition, it is possible to appropriately reduce bubbles (vacuum bubbles) generated inside the strands and pellets. By these prescriptions, it is possible to increase the molding cycle and reduce the occurrence rate of defects such as silver. Moreover, although the shape of a pellet can take common shapes, such as a cylinder, a prism, and a spherical shape, it is a cylinder more suitably. The diameter of such a cylinder is preferably 1 to 5 mm, more preferably 1.5 to 4 mm, and still more preferably 2 to 3.3 mm. On the other hand, the length of the cylinder is preferably 1 to 30 mm, more preferably 2 to 5 mm, and still more preferably 2.5 to 3.5 mm.

  In addition, the A component and the F component are previously melt-kneaded with a melt kneader so as to contain the high-concentration F component of the present invention to produce a master pellet, and the master pellet is used as the remaining A component and other components. The method of mixing with an additive and pelletizing with a melt kneader is mentioned.

(About supercritical foam molding)
The resin composition comprises a check ring (hereinafter referred to as an intermediate ring) in the middle part of the screw, a supercritical gas inlet between the three-tip set and the intermediate ring, and a supercritical gas generation and injection device as an external device. In the installed injection molding machine, pellets are introduced from the hopper port, heated and melted in the conveyance zone and compression zone of the molding machine screw, and then nitrogen or carbon dioxide from the dedicated gas injection port provided in the heating cylinder in the measurement zone. Supercritical foam molding is performed by introducing a supercritical gas of carbon. In such supercritical foam molding, by adopting injection compression molding, injection press molding, and core back molding as necessary on the mold control side, not only the injection amount of the supercritical gas but also the foaming ratio can be set. It is possible to control. As the mold runner, either the cold runner method or the hot runner method can be selected, but the latter hot runner method is preferable in terms of easy control of the expansion ratio. Further, as the nozzle of the molding machine, either an open nozzle or a shut-off valve can be used, but the latter shut-off valve is preferable when the mold does not have a shut-off function.

(About molded products)
Various types of surface treatment can be performed on the molded article of the present invention. As the surface treatment, various surface treatments such as a hard coat, a water / oil repellent coat, a hydrophilic coat, an antistatic coat, an ultraviolet absorption coat, an infrared absorption coat, and metalizing (evaporation) can be performed. Examples of the surface treatment method include liquid deposition, vapor deposition, thermal spraying, and plating. As the vapor deposition method, either a physical vapor deposition method or a chemical vapor deposition method can be used. Examples of physical vapor deposition include vacuum vapor deposition, sputtering, and ion plating. Examples of the chemical vapor deposition (CVD) method include a thermal CVD method, a plasma CVD method, and a photo CVD method.
Moreover, in order to give the external appearance of the molded product of the present invention, various insert moldings are possible, and examples include film insert molding and in-mold molding.

  Specific examples of the molded product in which the resin composition of the present invention is used are suitable for application to internal parts and housings of OA equipment and home appliances. These products include, for example, personal computers, notebook computers, CRT displays, printers, mobile terminals, mobile phones, copiers, fax machines, recording media (CD, CD-ROM, DVD, PD, FDD, etc.) drives, parabolic antennas, electric motors. Tools, VTRs, TVs, irons, hair dryers, rice cookers, microwave ovens, audio equipment, audio equipment such as audio / laser discs (registered trademark) / compact discs, lighting equipment, refrigerators, air conditioners, typewriters, word processors, etc. The resin products formed from the flame-retardant thermoplastic resin composition of the present invention can be used for various parts such as these cases. Examples of other resin products include vehicle parts such as deflector parts, car navigation parts, and car stereo parts.

  The flame-retardant resin composition for supercritical fluid micro-foam molding of the present invention has excellent flame retardancy in super-critical fluid micro-foam molding with a high weight reduction rate, and has a high level of impact characteristics and fluidity. Since they are compatible, they are widely useful in OA applications and other various fields. Therefore, the industrial effect exhibited by the present invention is extremely great.

  The form of the invention that the present inventor considers to be the best is an aggregation of the preferable ranges of the above requirements. For example, typical examples are described in the following examples. Of course, the present invention is not limited to these forms.

  The following examples further illustrate the present invention. Unless otherwise specified, parts in the examples are parts by weight, and% is% by weight. Evaluation was carried out by the following method.

(Evaluation of thermoplastic resin composition)
(I) Amount of polydiorganosiloxane (PDMS) in composition The amount of PDMS in the composition was calculated from the amount of PDMS contained in the added polycarbonate-polydiorganosiloxane copolymer resin (PC-PDMS copolymer resin).
(PDMS amount in the composition) = {(PDMS amount in the PC-PDMS copolymer resin) × 100} / (weight of the entire composition)
(Ii) Flame retardance Using a test piece prepared by the following method, a 5V combustion test was performed at thicknesses of 1.5 mm, 2.0 mm, and 2.3 mm in accordance with UL94 standards. In addition, the flame retardance rank may pass (○) in the 5 VB class with a thickness of 2.3 mm in a flame retardance evaluation using a test piece by supercritical fluid microfoam molding with a weight reduction rate of 15 wt%. preferable.
(Iii) Charpy impact strength According to ISO 179, the Charpy impact strength with a notch was measured using the test piece created by the following method.
(Iv) Heat resistance Using the test piece created by the following method, the deflection temperature under load was measured according to ISO 75-1 and 75-2. The measurement load was 1.80 MPa.
(V) Fluidity An Archimedean spiral flow length having a channel thickness of 2 mm and a channel width of 8 mm was measured with an injection molding machine [SG150U manufactured by Sumitomo Heavy Industries, Ltd.]. The measurement was performed at a cylinder temperature of 260 ° C., a mold temperature of 70 ° C., and an injection pressure of 98 MPa.

[Examples 1 to 19, Comparative Examples 1 to 12]
A mixture composed of the components shown in Tables 1 and 2 except for the C component ABS resin and the D component FR-1 was supplied from the first supply port of the extruder. Such a mixture was obtained by mixing the following premix (i) with other components using a V-type blender. That is, (i) a mixture of an F component (anti-drip agent) and an A component aromatic polycarbonate that is uniformly shaken in a polyethylene bag so that the F component is 2.5% by weight. It is a mixture mixed with. When C component ABS resin was included, it was supplied from the second supply port using a side feeder. Furthermore, when adding D component FR-1, in the state heated at 80 degreeC, the 3rd supply port (1st in the middle of a cylinder using a liquid injection apparatus (HYM-JS-08 by Fuji Techno Industry Co., Ltd.)) was used. From the position between the supply port and the vent exhaust port), each was supplied to the extruder at a predetermined ratio. The liquid injection device was set to supply a constant amount, and the supply amounts of other raw materials were precisely measured with a measuring instrument [CWF manufactured by Kubota Corporation]. Extrusion is performed by using a vent type twin screw extruder (Nippon Steel Works TEX30α-38.5BW-3V) with a diameter of 30 mmφ, melt kneading at a screw speed of 150 rpm, a discharge rate of 20 kg / h, and a vent vacuum of 3 kPa. Pellets were obtained. In addition, about extrusion temperature, it implemented at 260 degreeC from the 1st supply port to the die part.
A part of the obtained pellets was dried with a hot air circulation dryer at 80 to 90 ° C. for 6 hours and then used for evaluation test pieces (UL94, ISO179, ISO75-1 and ISO75-) using an injection molding machine. 2). In particular, for UL94 standard test pieces, supercritical fluid nitrogen was injected into the cylinder under the following conditions at a cylinder temperature of 240 ° C./mold temperature of 60 ° C. using a MuCell molding injection molding machine (J140 AD-110H manufactured by JSW). It was prepared by injection molding.

(2.3 mm UL test piece with a weight reduction rate of 15%)
Weighing value 26mm, VP switching value 13mm, injection speed 80mm / sec, gas injection amount 0.5%
(2.0mm UL test piece with 15% weight reduction)
Weighing value 27mm, VP switching value 13mm, injection speed 80mm / sec, gas injection amount 0.5%
(2.3 mm UL test piece with a weight reduction rate of 20%)
Weighing value 25mm, VP switching value 12mm, injection speed 100mm / sec, gas injection amount 0.5%

The respective components indicated by symbols in Table 1 and Table 2 are as follows.
(Component A)
PC: aromatic polycarbonate resin [polycarbonate resin powder having a viscosity average molecular weight of 19,800 made from bisphenol A and phosgene by a conventional method, Panlite L-1225WX manufactured by Teijin Chemicals Ltd.]

(B component)
PC-PDMS-1: Polycarbonate-polydiorganosiloxane copolymer resin (viscosity average molecular weight 19,800, PDMS amount 8.4%, PDMS polymerization degree 37)
PC-PDMS-2: Polycarbonate-polydiorganosiloxane copolymer resin (viscosity average molecular weight 19,800, PDMS amount 4.2%, PDMS polymerization degree 90)
PC-PDMS-3: Polycarbonate-polydiorganosiloxane copolymer resin (viscosity average molecular weight 19,800, PDMS amount 4.2%, PDMS polymerization degree 8)
PC-PDMS-4: Polycarbonate-polydiorganosiloxane copolymer resin (viscosity average molecular weight 19,800, PDMS amount 4.2%, PDMS polymerization degree 150)

(C component)
ABS-1: ABS resin [manufactured by Nippon A & L Co., Ltd., Clarastic SXH-330 (trade name), butadiene rubber component about 17.5 wt%, weight average rubber particle size 0.40 μm, manufactured by emulsion polymerization, lubricant (Excluding EBS)]
ABS-2: ABS resin [manufactured by Nippon A & L Co., Ltd., Clarastic GA-704 (trade name), butadiene rubber component about 17.5 wt%, weight average rubber particle size 0.40 μm, manufactured by emulsion polymerization, lubricant (Including EBS)]
ABS-3: ABS resin [manufactured by Nippon A & L Co., Ltd. Santac AT-07 (trade name), butadiene rubber component about 17.5% by weight, weight average rubber particle size 1.2 μm, manufactured by bulk polymerization, lubricant ( Does not include EBS)]
MBS: Core-shell type graft copolymer [Rohm and Haas Co., Ltd .: Paraloid EXL-2620 (trade name); graft copolymer with 70% by weight of polybutadiene and 40% by weight of styrene and methyl methacrylate as the core The weight average particle size is 0.20 μm, manufactured by emulsion polymerization]

(D component)
FR-1: Phosphate ester mainly composed of bisphenol A bis (diphenyl phosphate) (manufactured by Daihachi Chemical Industry Co., Ltd .: CR-741 (trade name))
FR-2: potassium perfluorobutanesulfonate (manufactured by Dainippon Ink & Chemicals, Inc., MegaFuck F-114P (trade name))
FR-3: organosiloxane flame retardant containing Si-H group, methyl group and phenyl group (X-40-2600J (trade name) manufactured by Shin-Etsu Chemical Co., Ltd.)

(E component)
Talc-1: Talc (manufactured by Hayashi Kasei Co., Ltd .; HST0.8 (trade name), average particle size 3.5 μm)
Talc-2: Talc (manufactured by IMI Fabi Sp. A .; HTP ultra 5c (trade name), average particle size 0.5 μm)
Talc-3: Talc (Katsumiyama Mining Co., Ltd .; Victorylite SG-A (trade name), average particle size 15.2 μm)
WSN: Wollastonite (manufactured by NYCO: NYGLOS4)
MICA: Mica (Kinsei Matec Co., Ltd .: Mica Powder MT-200B)

(F component)
PTFE-1: Polytetrafluoroethylene (manufactured by Daikin Industries, Ltd., Polyflon MP FA500B (trade name))
PTFE-2: SN3300B7 (trade name) (manufactured by Shine Polymer, the polytetrafluoroethylene-based mixture is a mixture of branched polytetrafluoroethylene particles and styrene-acrylonitrile copolymer particles produced by suspension polymerization. (Polytetrafluoroethylene content 50% by weight))

(Other ingredients)
DC30M: Olefin wax by copolymerization of α-olefin and maleic anhydride (Mitsubishi Chemical Corporation; Diacarna 30M (trade name))
SL900: Fatty acid ester release agent (Riken Vitamin Co., Ltd .; Riquemar SL900 (trade name))
IRGX-1: Phenol-based thermal stabilizer (Ciba Specialty Chemicals KK; IRGANOX 1076 (trade name))
IRGX-2: Phosphite-based thermal stabilizer (Ciba Specialty Chemicals KK; IRGAFOS168 (trade name))

  By blending a specific amount of the polycarbonate-polydiorganosiloxane copolymer resin of the present invention from the above table, a high balance of flame retardancy, impact resistance and fluidity is achieved even at a high weight reduction rate by supercritical fluid fine foam molding. You can see that you are satisfied with the dimensions.

Claims (10)

By copolymerizing (A) polycarbonate resin (component A) and (B) dihydric phenol represented by the following general formula [1] and hydroxyaryl-terminated polydiorganosiloxane represented by the following general formula [3] (C) Styrenic resin (C component) 3 to 45 parts by weight, (D) Phosphorous flame retardant (D) with respect to 100 parts by weight of the resin component made of polycarbonate-polydiorganosiloxane copolymer resin (B component) Component) 3 to 35 parts by weight, (E) silicate mineral (E component) 0.1 to 30 parts by weight, and (F) an anti-drip agent (F component) 0.1 to 3 parts by weight, and A flame retardant resin composition for supercritical fluid fine foam molding, wherein the content of polydiorganosiloxane derived from component B in the composition is 0.2 to 0.6% by weight.

[In General Formula [1], R ¹ and R ² are each independently a hydrogen atom, a halogen atom, an alkyl group having 1 to 18 carbon atoms, an alkoxy group having 1 to 18 carbon atoms, or 6 to 6 carbon atoms. 20 cycloalkyl groups, cycloalkoxy groups having 6 to 20 carbon atoms, alkenyl groups having 2 to 10 carbon atoms, aryl groups having 3 to 14 carbon atoms, aryloxy groups having 3 to 14 carbon atoms, carbon atoms Represents a group selected from the group consisting of an aralkyl group having 7 to 20 carbon atoms, an aralkyloxy group having 7 to 20 carbon atoms, a nitro group, an aldehyde group, a cyano group, and a carboxyl group. E and f are each an integer of 1 to 4, and W is a single bond or at least one group selected from the group consisting of groups represented by the following general formula [2]. . ]

[In the above general formula [2], R ¹¹ , R ¹² , R ¹³ , R ¹⁴ , R ¹⁵ , R ¹⁶ , R ¹⁷ and R ¹⁸ are each independently a hydrogen atom, an alkyl group having 1 to 18 carbon atoms, carbon Represents a group selected from the group consisting of an aryl group having 3 to 14 atoms and an aralkyl group having 7 to 20 carbon atoms, and R ¹⁹ and R ²⁰ each independently represent a hydrogen atom, a halogen atom, or a carbon atom having 1 to 18 carbon atoms. Alkyl groups, alkoxy groups having 1 to 10 carbon atoms, cycloalkyl groups having 6 to 20 carbon atoms, cycloalkoxy groups having 6 to 20 carbon atoms, alkenyl groups having 2 to 10 carbon atoms, and 3 carbon atoms. -14 aryl group, aryloxy group having 6 to 10 carbon atoms, aralkyl group having 7 to 20 carbon atoms, aralkyloxy group having 7 to 20 carbon atoms, nitro group, aldehyde group, cyano group and It represents a group selected from the group consisting of carboxyl groups, and when there are a plurality thereof, they may be the same or different, g is an integer of 1 to 10, and h is an integer of 4 to 7. ]

[In the above general formula [3], R ³ , R ⁴ , R ⁵ , R ⁶ , R ⁷ and R ⁸ are each independently a hydrogen atom, an alkyl group having 1 to 12 carbon atoms, or a substitution having 6 to 12 carbon atoms. Or an unsubstituted aryl group, R ⁹ and R ¹⁰ are each independently a hydrogen atom, a halogen atom, an alkyl group having 1 to 10 carbon atoms, or an alkoxy group having 1 to 10 carbon atoms, and p is a natural number Q is 0 or a natural number, and p + q is a natural number less than 300. X is a divalent aliphatic group having 2 to 8 carbon atoms. ] In the general formula [1], R ¹ And R ² The flame retardant resin composition according to claim 1, wherein is a hydrogen atom. The flame retardant resin composition according to claim 1 or 2, wherein the dihydric phenol represented by the general formula [1] is 2,2-bis (4-hydroxyphenyl) propane. The flame retardant resin composition for supercritical fluid fine foam molding according to any one of claims 1 to 3 , wherein the content of polydiorganosiloxane derived from component B in the composition is 0.2 to 0.45 wt%. The flame-retardant resin composition for supercritical fluid fine foam molding according to any one of claims 1 to 4, wherein the silicate mineral is talc. The flame retardant resin composition for supercritical fluid fine foam molding according to any one of claims 1 to 5 , wherein the anti-drip agent is a coated branched PTFE. In the flame retardancy evaluation using a test piece weight reduction rate of 15% by supercritical fluid finely foamed molding, it claims 1-6, characterized in that to achieve a UL94 standard 5VB at 2.3mm thick A flame retardant resin composition for supercritical fluid fine foam molding as described in 1. In the flame retardancy evaluation using a test piece weight reduction rate of 15% by supercritical fluid finely foamed molding, it claims 1-6, characterized in that to achieve a UL94 standard 5VB at 2.0mm thick A flame retardant resin composition for supercritical fluid fine foam molding as described in 1. In the weight reduction rate flame retardancy evaluation using a test piece with supercritical fluid finely foamed molding of 20%, it claims 1-6, characterized in that to achieve a UL94 standard 5VB at 2.3mm thick A flame retardant resin composition for supercritical fluid fine foam molding as described in 1. A supercritical fluid fine foam molded article obtained from the flame retardant resin composition for supercritical fluid fine foam molding according to any one of claims 1 to 9 .