JP4817679B2 - Antistatic aromatic polycarbonate resin composition - Google Patents

Description

  The present invention relates to an antistatic aromatic polycarbonate resin composition having improved fluidity. In more detail, the present invention blends a specific flow modifier having good compatibility with an aromatic polycarbonate resin reinforced with a non-fibrous carbon filler, thereby providing excellent antistatic properties, mechanical strength, fluidity. The present invention relates to an antistatic aromatic polycarbonate resin composition having both characteristics and good heat resistance, and a method for producing the same.

Polycarbonate resins are used in many applications such as mechanical parts, automobile parts, electrical / electronic parts, and office equipment parts because of their excellent properties such as mechanical strength and heat resistance.
On the other hand, with the recent miniaturization and higher functionality of electronic components, anti-static performance has been added to thermoplastic resins in order to prevent electrical failure to equipment caused by charging of thermoplastic resin molded products or malfunction of equipment due to dust adhesion. Is required.

  For example, an antistatic resin composition obtained by blending a sulfonic acid phosphonium salt with an aromatic polycarbonate resin is known (see Patent Document 1). However, when an organic antistatic agent or a conductive resin is used, it is not practical because a large amount of addition is required to obtain a desired resistance value. In particular, an aromatic polyester-based resin typified by an aromatic polycarbonate resin is not preferable because it is easily decomposed by an ionic substance and requires a high processing temperature, so that the decomposition is further promoted.

  The addition of carbon black is one typical method for imparting electrical conductivity to a thermoplastic resin. For example, the carbon black comprises a specific ratio of aromatic polycarbonate, polyalkylene terephthalate, and carbon black having a specific DBP oil absorption amount. Resin compositions with improved properties are known (see Non-Patent Document 1 and Patent Document 2). However, the addition of conductive carbon black has a problem that due to its bulkiness, the blending amount increases and the fluidity during injection molding is significantly reduced.

  Addition of graphite is also known as a technique for imparting rigidity and antistatic performance to thermoplastic resins. For example, resin compositions comprising a specific ratio of aromatic polycarbonate, flaky graphite having a specific particle size and trimethyl phosphate are known. Yes (see Patent Document 3). However, it cannot be said that this document discloses a resin composition having excellent fluidity.

  Further, a polycarbonate resin composition with improved fluidity obtained by adding a styrene oligomer having a weight average molecular weight of 5000 to 10,000 as a fluidity modifier is known (see Patent Document 4). However, such styrenic oligomers have poor affinity or compatibility with the polycarbonate resin, cause delamination of the molded product, and are not satisfactory in terms of mechanical strength.

  A resin composition in which a polycarbonate resin is blended with a melt flow improver mainly composed of a polymer having a mass average molecular weight of 10,000 or more and less than 60,000 that is compatible or compatible with the polycarbonate resin is known (patent) Reference 5).

  In addition, as a flow modifier for polycarbonate resin, it is obtained by graft polymerization of a monomer constituting a polymer compatible or compatible with polycarbonate resin in the presence of a polymer incompatible with polycarbonate resin. In addition, it is known to use a thermoplastic resin composition having a mass average molecular weight of 10,000 to 100,000 of a soluble component dissolved in chloroform (see Patent Document 6). According to this document, as a more specific embodiment, a flow modifier obtained by graft copolymerization of butyl acrylate with styrene and acrylonitrile is disclosed, and it is described that it has good compatibility without delamination.

  However, it is difficult to say that these flow modifiers still have good compatibility, and further improvement of them is required for practical use.

  Copolymer composed of (meth) acrylic acid ester of specific structure represented by phenyl methacrylate, polymer unit consisting of methyl (meth) acrylate, and polymer unit consisting of unsaturated nitrile and aromatic vinyl It is known to use the coalescence as a compatibilizing agent for polycarbonate resin and ABS resin (see Patent Document 7).

  However, this publication does not disclose knowledge that is effective in improving the fluidity of a polycarbonate resin reinforced with a reinforcing agent and having sufficient heat resistance under good compatibility without delamination. .

Japanese Patent Laid-Open No. 2002-20608 JP 2001-323150 A Japanese Patent Laid-Open No. 2001-200353 Japanese Patent Laid-Open No. 11-181198 JP 2003-226802 A WO2003 / 072620 pamphlet JP-A-8-134144 Journal of Japan Adhesion Association Vol. 23, no. 3, 103-111 pages (1987)

  In view of the above, the object of the present invention is to use a polycarbonate resin reinforced with a non-fibrous carbon filler as a base, and to have excellent antistatic properties without delamination, mechanical strength, flow characteristics, and good heat resistance. An object of the present invention is to provide a preventive aromatic polycarbonate resin composition. As a result of intensive studies to achieve the above object, the present inventor has found that such a purpose can be achieved by using a flow modifier comprising a copolymer from a specific monomer, and further intensive studies. The present invention has been completed.

  According to the present invention, the above-mentioned problem is a flow modification with respect to a total of 100 parts by weight of aromatic polycarbonate resin (component A) 60 to 99 parts by weight and non-fibrous carbon filler (component B) 1 to 40 parts by weight. An aromatic polycarbonate resin composition comprising 0.05 to 30 parts by weight of an agent (C component), wherein the flow modifier (C component) comprises (i) the following general formula (1) and / or (2 ) And a copolymer comprising a unit formed from a (meth) acrylic acid ester monomer (Ca) and an aromatic alkenyl compound monomer (Cb) represented by (ii) The weight average molecular weight of the soluble component is achieved by a reinforced polycarbonate resin composition having a molecular weight of 10,000 to 200,000.

（式中、Ｒ^１は水素原子またはメチル基、Ｒ^２は炭素環基自体であるか、または炭素環を結合した炭素鎖からなる炭化水素基を表す。）

(In the formula, R ¹ represents a hydrogen atom or a methyl group, and R ² represents a carbocyclic group itself or a hydrocarbon group composed of a carbon chain bonded to a carbocyclic ring.)

（式中、Ｒ^３は水素原子またはメチル基、Ｒ^４は炭素環基自体であるか、または炭素環を結合した炭素鎖からなる炭化水素基を表し、ｎは１〜４の整数を表す。）

(In the formula, R ³ represents a hydrogen atom or a methyl group, R ⁴ represents a carbocyclic group itself or a hydrocarbon group composed of a carbon chain bonded to a carbocyclic ring, and n represents an integer of 1 to 4. )

  The component B is preferably carbon black having a DBP oil absorption of 100 ml / 100 g to 500 ml / 100 g and / or graphite having an average particle diameter of 2 to 300 μm.

  The ratio of the monomer (Ca) and the monomer (Cb) in the C component is such that the sum of both is 80% by weight or more in 100% by weight of the C component, It is preferred that Ca) is 1 to 80% by weight and monomer (Cb) is 20 to 99% by weight.

  The monomer (Ca) in the C component is preferably phenyl methacrylate, and the monomer (Cb) in the C component is preferably styrene.

  Moreover, the above-mentioned subject is a flow modifier (component C) with respect to a total of 100 parts by weight of aromatic polycarbonate resin (component A) 60 to 99 parts by weight and non-fibrous carbon filler (component B) 1 to 40 parts by weight. A method for producing an antistatic aromatic polycarbonate resin composition having improved fluidity obtained by melt-kneading 0.05 to 30 parts by weight, wherein the flow modifier (component C) comprises (i) Copolymer having a main unit composed of a unit formed from a (meth) acrylate monomer (Ca) and an aromatic alkenyl compound monomer (Cb) represented by the general formula (1) and / or (2) (Ii) The chloroform-soluble component has a weight-average molecular weight of 10,000 to 200,000 and is solved by a method for producing an antistatic aromatic polycarbonate resin composition.

Hereinafter, the details of the present invention will be described.
(Component A: aromatic polycarbonate resin)
The aromatic polycarbonate resin used as the component A 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 antistatic aromatic polycarbonate 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-hydroxydiphenyl) 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 0.1% in 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 01 to 1 mol%, preferably 0.05 to 0.9 mol%, particularly preferably 0.05 to 0.8 mol%.

In particular, in the case of the melt transesterification method, a branched structural unit may be generated as a side reaction. However, the amount of the branched structural unit is also 0.1% in a total of 100 mol% with a structural unit derived from a dihydric phenol. Those having a ratio of 001 to 1 mol%, preferably 0.005 to 0.9 mol%, particularly preferably 0.01 to 0.8 mol% are preferred. 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 aliphatic difunctional carboxylic acids 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.

  Further, a polycarbonate-polyorganosiloxane copolymer obtained by copolymerizing polyorganosiloxane units can also be used.

  The reaction by the interfacial polymerization method is usually a reaction between a dihydric phenol and phosgene, and is reacted in the presence of an acid binder and an organic solvent. As the acid binder, for example, alkali metal hydroxides such as sodium hydroxide and potassium hydroxide, pyridine and the like are used.

  As the organic solvent, for example, halogenated hydrocarbons such as methylene chloride and chlorobenzene are used.

  In addition, catalysts such as tertiary amines and quaternary ammonium salts can be used for promoting the reaction, and monofunctional phenols such as phenol, p-tert-butylphenol, p-cumylphenol, etc. as molecular weight regulators. Are preferably used. Furthermore, examples of monofunctional phenols include decylphenol, dodecylphenol, tetradecylphenol, hexadecylphenol, octadecylphenol, eicosylphenol, docosylphenol, and triacontylphenol. These monofunctional phenols having a relatively long chain alkyl group are effective when improvement in fluidity and hydrolysis resistance is required.

  The reaction temperature is usually 0 to 40 ° C., the reaction time is several minutes to 5 hours, and the pH during the reaction is usually preferably maintained at 10 or higher.

  The reaction by the melt transesterification method is usually a transesterification reaction between a dihydric phenol and a carbonic acid diester. The dihydric phenol and the carbonic acid diester are mixed in the presence of an inert gas and reacted at 120 to 350 ° C. under reduced pressure. . The degree of vacuum is changed stepwise, and finally the phenols produced at 133 Pa or less are removed from the system. The reaction time is usually about 1 to 4 hours.

  Examples of the carbonic acid diester include diphenyl carbonate, dinaphthyl carbonate, bis (diphenyl) carbonate, dimethyl carbonate, diethyl carbonate, and dibutyl carbonate. Among them, diphenyl carbonate is preferable.

A polymerization catalyst can be used to accelerate the polymerization rate. Examples of the polymerization catalyst include alkali metal and alkaline earth metal hydroxides such as sodium hydroxide and potassium hydroxide, boron and aluminum hydroxides, Alkali metal salt, alkaline earth metal salt, quaternary ammonium salt, alkoxide of alkali metal or alkaline earth metal, organic acid salt of alkali metal or alkaline earth metal, zinc compound, boron compound, silicon compound, germanium compound, Examples thereof include catalysts usually used for esterification and transesterification of organic tin compounds, lead compounds, antimony compounds, manganese compounds, titanium compounds, zirconium compounds and the like. A catalyst may be used independently and may be used in combination of 2 or more types. The amount of these polymerization catalysts used is preferably 1 × 10 ⁻⁹ to 1 × 10 ⁻⁵ equivalents, more preferably 1 × 10 ^{−8 to} 5 × 10 ⁻⁶ equivalents, per 1 mol of the raw material dihydric phenol. Selected by range.

  In the polymerization reaction, in order to reduce phenolic end groups, for example, 2-chlorophenyl phenyl carbonate, 2-methoxycarbonylphenyl phenyl carbonate, 2-ethoxycarbonylphenyl phenyl carbonate, etc. Compounds can be added.

  Further, in the melt transesterification method, it is preferable to use a deactivator that neutralizes the activity of the catalyst. The amount of the deactivator is preferably 0.5 to 50 mol with respect to 1 mol of the remaining catalyst. Further, it is used in a proportion of 0.01 to 500 ppm, more preferably 0.01 to 300 ppm, particularly preferably 0.01 to 100 ppm with respect to the aromatic polycarbonate resin after polymerization. Preferred examples of the deactivator include phosphonium salts such as tetrabutylphosphonium dodecylbenzenesulfonate and ammonium salts such as tetraethylammonium dodecylbenzyl sulfate.

  Details of other reaction formats are well known in various documents and patent publications.

  In producing the antistatic aromatic polycarbonate resin composition of the present invention, the viscosity average molecular weight (M) of the aromatic polycarbonate resin is not particularly limited, but is preferably 10,000 to 50,000, more preferably. It is 14,000-30,000, More preferably, it is 14,000-24,000.

  With an aromatic polycarbonate resin having a viscosity average molecular weight of less than 10,000, 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 50,000 is inferior in versatility in that it is inferior in fluidity during injection molding.

  The aromatic polycarbonate resin may be obtained by mixing those having a viscosity average molecular weight outside the above range. In particular, an aromatic polycarbonate resin having a viscosity average molecular weight exceeding the range (50,000) 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 reinforced resin material into a structural member. Such improvement in moldability is even better than that of the branched polycarbonate. As more preferred embodiments, the A component is an aromatic polycarbonate resin having a viscosity average molecular weight of 70,000 to 300,000 (component A-3-1), and the aromatic polycarbonate resin having a viscosity average molecular weight of 10,000 to 30,000. An aromatic polycarbonate resin (A-3 component) (hereinafter referred to as “high molecular weight component-containing aromatic polycarbonate resin”) having a viscosity average molecular weight of 16,000 to 35,000. May also be used.

  In such a high molecular weight component-containing aromatic polycarbonate resin (A-3 component), the molecular weight of the A-3-1 component is preferably 70,000 to 200,000, more preferably 80,000 to 200,000, still more preferably. 100,000 to 200,000, particularly preferably 100,000 to 160,000. The molecular weight of the A-3-2 component is preferably 10,000 to 25,000, more preferably 11,000 to 24,000, still more preferably 12,000 to 24,000, and particularly preferably 12,000 to 23. , 000.

  The high molecular weight component-containing aromatic polycarbonate resin (A-3 component) is obtained by mixing the A-3-1 component and the A-3-2 component at various ratios and adjusting them so as to satisfy a predetermined molecular weight range. Can do. Preferably, in 100% by weight of the A-3 component, the A-3-1 component is 2 to 40% by weight, more preferably the A-3-1 component is 3 to 30% by weight, and still more preferably The A-3-1 component is 4 to 20% by weight, and the A-3-1 component is particularly preferably 5 to 20% by weight.

  In addition, as a method for preparing the A-3 component, (1) a method in which the A-3-1 component and the A-3-2 component are independently polymerized and mixed, and (2) JP-A-5-306336. The method of producing an aromatic polycarbonate resin showing a plurality of polymer peaks in a molecular weight distribution chart by GPC method, represented by the method shown in Japanese Patent Publication No. Gazette, in the same system, the aromatic polycarbonate resin of the present invention A- A method of producing so as to satisfy the conditions of the three components, and (3) an aromatic polycarbonate resin obtained by the production method (production method of (2)), a separately produced A-3-1 component and / or Examples thereof include a method of mixing the A-3-2 component.

The viscosity average molecular weight referred to in the present invention is first determined by using an Ostwald viscometer from a solution obtained by dissolving 0.7 g of aromatic polycarbonate 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

  The calculation of the viscosity average molecular weight in the antistatic aromatic polycarbonate resin composition of the present invention is performed as follows. 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: non-fibrous carbon filler)
The B component of the present invention is a non-fibrous carbon filler mainly composed of carbon. Specifically, carbon black, graphite, and fullerene are preferable, and carbon black and graphite are preferable from the viewpoint of mechanical strength and antistatic properties. As the carbon black, carbon black having a DBP oil absorption of 100 ml / 100 g to 500 ml / 100 g is preferable in terms of conductivity. Such carbon black is generally acetylene black or ketjen black. Specific examples include Denka Black manufactured by Denki Kagaku Kogyo Co., Ltd., Vulcan XC-72 and BP-2000 manufactured by Cabot Corporation, Ketjen Black EC and Ketjen Black EC-600JD manufactured by Lion Corporation.

  As graphite, any of natural graphite, which is made of graphite under the mineral name, or various artificial graphites can be used. As natural graphite, any of earth-like graphite, scale-like graphite (Vein Graphite also called massive graphite), and scale-like graphite (Flake Graphite) can be used. Artificial graphite is obtained by heat-treating amorphous carbon and artificially aligning irregularly arranged fine graphite crystals. In addition to artificial graphite used for general carbon materials, Kish graphite, cracked graphite, And pyrolytic graphite. Artificial graphite used for general carbon materials is usually produced by graphitization treatment using petroleum coke or coal-based pitch coke as a main raw material.

  Among these, preferred graphite of the present invention is flake graphite. The resin composition blended with such flaky graphite has good electrical conductivity and good flame retardancy due to good thermal stability. If the thermal stability is poor, the resin is significantly decomposed during combustion, and it is difficult to obtain good flame retardancy. The ratio of the flaky graphite is preferably 80% by weight or more, more preferably 90% by weight or more in 100% by weight of the B component, and particularly preferably, the total amount of the B component is substantially flaky graphite.

  The graphite of the present invention may contain expanded graphite that is thermally expandable by processing the scale-like graphite as represented by acid treatment, or graphite that has been expanded. The particle size of the graphite of the present invention is in the range of 2 to 300 μm. The particle size is preferably 5 to 200 μm, more preferably 7 to 100 μm, and still more preferably 7 to 50 μm. By satisfying such a range, a good molded article appearance and mechanical strength can be achieved. On the other hand, if the average particle size is less than 2 μm, the effect of improving the dimensional accuracy tends to be lowered, and if the average particle size exceeds 300 μm, the impact resistance is slightly lowered and so-called graphite floats on the surface of the molded product. It is not preferable. This is because the float on the surface may cause graphite to fall off the surface of the molded product and cause electrical damage to the electronic component. In addition, the above preferable average particle diameter has an advantage that the appearance of the molded product is improved and good slidability is easily obtained.

  The fixed carbon content of the graphite of the present invention is preferably 80% by weight or more, more preferably 90% by weight or more, and still more preferably 98% by weight or more. The volatile content of the graphite of the present invention is preferably 3% by weight or less, more preferably 1.5% by weight or less, and still more preferably 1% by weight or less.

  The average particle size of graphite in the present invention refers to the particle size of the B component itself before the composition, and the particle size is determined by a laser diffraction / scattering method.

  Further, the surface of graphite is subjected to surface treatment such as epoxy treatment, urethane treatment, silane coupling treatment, and oxidation treatment in order to increase the affinity with the thermoplastic resin as long as the characteristics of the composition of the present invention are not impaired. It may be given. The compounding quantity of B component is 1-40 weight part on the basis of a total of 100 weight part of A component and B component, Preferably it is 2-35 weight part, More preferably, it is 5-30 weight part. If it is less than 1 part by weight, it is difficult to obtain good antistatic properties and rigidity, and if it exceeds 40 parts by weight, the thermal stability and mechanical strength are lowered.

(C component: flow modifier)
The flow modifier (component C) of the present invention comprises (i) a (meth) acrylic acid ester monomer (Ca) represented by the following general formula (1) and / or (2) and an aromatic alkenyl compound. It is a copolymer having a unit formed from a monomer (Cb) as a main structural unit, and (ii) the chloroform-soluble component has a weight average molecular weight of 10,000 to 200,000. is there.

（式中、Ｒ^１は水素原子またはメチル基、Ｒ^２は炭素環基自体であるか、または炭素環を結合した炭素鎖からなる炭化水素基を表す。）

(In the formula, R ¹ represents a hydrogen atom or a methyl group, and R ² represents a carbocyclic group itself or a hydrocarbon group composed of a carbon chain bonded to a carbocyclic ring.)

（式中、Ｒ^３は水素原子またはメチル基、Ｒ^４は炭素環基自体であるか、または炭素環を結合した炭素鎖からなる炭化水素基を表し、ｎは１〜４の整数を表す。）

(In the formula, R ³ represents a hydrogen atom or a methyl group, R ⁴ represents a carbocyclic group itself or a hydrocarbon group composed of a carbon chain bonded to a carbocyclic ring, and n represents an integer of 1 to 4. )

  In the flow modifier of the present invention, it is preferable that all monomer components are contained in the copolymer of the monomer (Ca) and the monomer (Cb). However, in the production of a copolymer, it is unavoidable that a polymer consisting of not only a monomer but also a monomer is produced. In the present invention, the monomer (Ca) or the monomer (Cb) is used. A homopolymer may be included. This is because such a homopolymer has good compatibility with the copolymer and acts as a unit on the polycarbonate resin.

In flow modifier of the present invention component (C), in a total of 100 wt% of both persons, preferably monomer (Ca) 1 to 80 wt% and the monomer (Cb) is 20 to 99 wt% More preferably, the monomer (Ca) is 3 to 50% by weight and the monomer (Cb) is 50 to 97% by weight, and more preferably the monomer (Ca) is 5 to 30% by weight. The monomer (Cb) is 70 to 95% by weight, most preferably the monomer (Ca) is 5 to 20% by weight and the monomer (Cb) is 80 to 95% by weight.

  When the amount of the monomer (Ca) is less than the lower limit of the above range, it becomes difficult to achieve both improvement in delamination or a fluid reforming effect. When the amount of the monomer (Ca) exceeds the upper limit of the above range, it is difficult to obtain a fluid reforming effect and the mechanical properties may be deteriorated.

  Moreover, it is preferable that all the copolymer of a monomer (Ca) and a monomer (Cb) is a non-crosslinked copolymer. For example, when 10 ml of chloroform and 1 g of a flow modifier (component C) are stirred and mixed for 30 minutes, it is preferable that a crosslinked structure insoluble in chloroform is not observed. However, as long as the properties of excellent fluidity modification are not impaired, all of the copolymers need not be non-crosslinked, and some crosslinked structures insoluble in organic solvents such as chloroform and acetone exist. There is no particular problem.

  In the copolymer of component C, the weight average molecular weight of the chloroform-soluble component excluding a part of the solvent-insoluble crosslinked structure is 10,000 to 200,000. Such molecular weight keeps a good balance between formability and physical properties such as heat resistance and impact resistance.

  Such molecular weight is calculated by GPC (gel permeation chromatography) measurement under the following conditions. That is, GPC measurement was performed in a clean air environment at a temperature of 23 ° C. and a relative humidity of 50%, and two columns of ResiPore (length 300 mm, inner diameter 7.5 mm) manufactured by Polymer Laboratories were connected in series as a column, and chloroform as a mobile phase. Polymer Laboratories' Easy Cal PS-2 as a standard substance, and a photodiode array detector at a wavelength of 254 nm as a detector, chloroform as a developing solvent, and a solution of 10 mg of sample dissolved in 5 ml of chloroform, 100 μl is injected into the GPC measurement apparatus, and the measurement is performed under conditions of a column temperature of 40 ° C. and a flow rate of 1 ml / min.

  From the obtained results, the molecular weight is calculated from the peak in a range excluding the peak corresponding to the monomer and dimer which are difficult to be called a copolymer. Under the above conditions, since these peaks to be excluded are detected at a retention time of 20 minutes or later, the molecular weight is calculated from the peaks up to 20 minutes.

  In the weight average molecular weight of the flow modifier of the present invention, a more preferable lower limit is 20,000, further preferably 30,000, and most preferably 40,000. Moreover, the upper limit with more preferable this weight average molecular weight is 150,000, More preferably, it is 140,000, Most preferably, it is 130,000. The main component of the soluble component in chloroform is a non-crosslinked copolymer composed of the monomer (Ca) and the monomer (Cb). Polymers of monomers (Ca) or monomers (Cb) may be included.

  When the weight-average molecular weight of the soluble component is less than 10,000, relatively low molecular weight substances are increased, which may reduce various functions such as heat resistance and rigidity. In addition, there is a risk that problems such as smoke generation, mist, mechanical contamination, and appearance defects such as fish eyes during molding may increase.

  On the other hand, when the weight average molecular weight is larger than 200,000, the melt viscosity of the flow modifier itself increases, and a sufficient fluidity modifying effect may not be obtained.

  Moreover, in the flow modifier of the present invention, it is preferable to use one having a melt viscosity of 300 Pa · s or less.

The melt viscosity is a melt viscosity measured using a capillary rheometer under the conditions of nozzle D = 1 mm, L / D = 16, barrel temperature = 170 ° C., and shear rate = 3000 sec ⁻¹ .

  The copolymer of component C may be any of a random copolymer, a block copolymer, and a graft copolymer, or a mixture thereof. The random copolymer is more preferable in the present invention in that the refractive index of the copolymer is uniform even at a micro level and that it can be produced relatively easily. In the block copolymer, when the polymer unit of the monomer (Ca) is A and the polymer unit of the monomer (Cb) is B, AB type, ABA type, B Any block copolymer such as -A-B type and A-B-A-B type may be used. Furthermore, when the random copolymer unit of the monomer (Ca) and the monomer (Cb) is AB, a block copolymer in which either A or B is substituted with AB may be used. . Further, in the graft copolymer, a copolymer in which the polymer unit B is grafted to the polymer unit A, a copolymer in which the polymer unit A is grafted to the polymer unit B, and either A or B is AB. Any of the graft copolymers having a structure substituted by

  The production method of the copolymer of component C is not particularly limited, and is represented by radical polymerization such as emulsion polymerization, suspension polymerization, solution polymerization, and bulk polymerization, various living anion polymerizations, and use of TEMPO. Living radical polymerization methods such as nitroxide-mediated radical polymerization, radical polymerization using reversible addition-fragmentation chain transfer agent (RAFT), and atom transfer radical polymerization (ATRP) can be used.

  Hereinafter, as a preferred method for producing the flow modifier of the present invention, a method for synthesizing a copolymer by an emulsion radical polymerization method will be described.

(Synthesis of copolymer by emulsion radical polymerization)
Examples of the method for synthesizing a copolymer by the emulsion radical polymerization method include water, an emulsifier, a (meth) acrylate monomer (Ca) represented by the general formula (1) and / or (2), and aromatic. A copolymer is added to a mixture of an alkenyl compound monomer (Cb) and optionally other monomers, a polymerization initiator, a chain transfer agent, etc., if necessary, and polymerization is performed at a high temperature to obtain a copolymer. Is synthesized.

  Examples of the emulsifier include nonionic emulsifiers, anionic emulsifiers, cationic emulsifiers, and zwitterionic emulsifiers.

  Specific examples of the nonionic emulsifier include polyoxyethylene alkyl ether, polyoxyethylene alkyl aryl ether, dialkylphenoxy poly (ethyleneoxy) ethanol, polyvinyl alcohol, polyacrylic acid, and alkyl cellulose.

  Specific examples of the anionic emulsifier include fatty acid salts, higher alcohol sulfates, liquid fatty oil sulfates, sulfates of aliphatic amines and aliphatic amides, fatty alcohol phosphates, dibasic fatty acid esters. Examples thereof include sulfone salts, fatty acid amide sulfonates, alkylaryl sulfonates, and naphthalene sulfonates of formalin condensates.

Specific examples of the cationic emulsifier include aliphatic amine salts, quaternary ammonium salts, and alkylpyridinium salts.
Specific examples of the zwitterionic emulsifier include alkylbetaines.

  The (meth) acrylic acid ester monomer (Ca) represented by the general formula (1) and / or (2) is a carbocyclic ring in the molecule, that is, a carbocyclic ring itself, or a carbon having a carbocyclic ring bonded thereto. It contains a hydrocarbon group consisting of a chain. The carbocycle may be an alicyclic ring such as a cyclohexane ring or an aromatic ring such as a benzene ring and a naphthalene ring. These carbocycles may be substituted with an alkyl group. In the present invention, the notation of (meth) acrylate indicates that both methacrylate and acrylate are included, and the notation of (meth) acrylic acid ester indicates that both methacrylic acid ester and acrylic acid ester are included.

  Specific examples of the (meth) acrylic acid ester represented by the general formulas (1) and (2) include cyclohexyl (meth) acrylate, 3,4,5-trimethylcyclohexyl (meth) acrylate, and 4-tert-butylcyclohexyl. (Meth) acrylate, cyclohexylmethyl (meth) acrylate, 3-cyclohexylpropyl (meth) acrylate, 2-cyclohexylpropyl (meth) acrylate, phenyl (meth) acrylate, 4-methylphenyl (meth) acrylate, 4-tert-butyl Phenyl (meth) acrylate, benzyl (meth) acrylate, 4-methylbenzyl (meth) acrylate, 1-phenylethyl (meth) acrylate, 2-phenylethyl (meth) acrylate, 3-phenylpropyl (meth) ) Acrylate, 2-phenylpropyl (meth) acrylate, 2-naphthyl (meth) acrylate, cyclohexoxymethyl (meth) acrylate, 2-cyclohexoxyethyl (meth) acrylate, 3-cyclohexoxypropyl (meth) acrylate, 3, 4,5-trimethylcyclohexoxymethyl (meth) acrylate, 2- (3,4,5-trimethylcyclohexoxy) ethyl (meth) acrylate, 3- (3,4,5-trimethylcyclohexoxy) propyl (meth) acrylate 4-tert-butylcyclohexoxymethyl (meth) acrylate, 2- (4-tert-butylcyclohexoxy) ethyl (meth) acrylate, 3- (4-tert-butylcyclohexoxy) propyl (meth) acrylate, Xymethyl (meth) acrylate, 2-phenoxyethyl (meth) acrylate, 3-phenoxypropyl (meth) acrylate, 2-phenoxypropyl (meth) acrylate, 4-tert-butylphenoxymethyl (meth) acrylate, 2- (4- tert-Butylphenoxy) ethyl (meth) acrylate, 3- (4-tert-butylphenoxy) propyl (meth) acrylate, 3,4-dimethylphenyl (meth) acrylate, 3,4,5-trimethylphenyl (meth) acrylate 4-methylphenoxymethyl (meth) acrylate, 2- (4-methylphenoxy) ethyl (meth) acrylate, 3- (4-methylphenoxy) propyl (meth) acrylate, 2- (4-methylphenoxy) propyl (meth) Acryle 2-naphthoxymethyl (meth) acrylate, 2- (2-naphthoxy) ethyl (meth) acrylate, and 3- (2-naphthoxy) propyl (meth) acrylate, 2- (2-naphthoxy) propyl (meth) ) Acrylate and the like, and these may be used alone or in combination of two or more.

  Among these, in the present invention, cyclohexyl (meth) acrylate, phenyl (meth) acrylate, 4-methylphenyl (meth) acrylate, benzyl (meth) acrylate, 4-methylbenzyl (meth) acrylate, 4-tert-butyl Cyclohexyl (meth) acrylate, 4-tert-butylphenyl (meth) acrylate, cyclohexoxymethyl (meth) acrylate, 2-cyclohexoxyethyl (meth) acrylate, phenoxymethyl (meth) acrylate, and 2-phenoxyethyl (meth) Acrylates are preferred, cyclohexyl methacrylate and phenyl methacrylate are more preferred, and phenyl methacrylate is particularly preferred.

  The copolymer of component C of the present invention is mainly composed of the (meth) acrylic acid ester monomer (Ca) and the aromatic alkenyl compound monomer (Cb) represented by the general formula (1) and / or (2). However, other copolymerizable monomers may be used in combination as necessary. Examples of such monomers include alkyl (meth) acrylates having an alkyl group having 2 to 20 carbon atoms such as methyl (meth) acrylate and ethyl (meth) acrylate, and vinyl cyanide compounds. These can be used alone or in combination of two or more. Still other copolymerizable monomers include amino groups, hydroxy groups, mercapto groups, carboxylic acids such as maleic anhydride, (meth) acrylic acid, glycidyl (meth) acrylate, and hydroxyethyl (meth) acrylate. It may be a monomer containing various functional groups such as an acid group, a carboxylic acid anhydride, a dicarboxylic acid, a halogen group, and a carbonyl halide.

  A monomer having two or more unsaturated groups can be used as a copolymerizable monomer. By using such a monomer, a macromonomer having one or more unsaturated double bonds at the side chain or terminal of the polymer is synthesized, and the other monomer is polymerized in the presence thereof to graft copolymer. A polymer can be produced.

  Specific examples of the monomer having two or more unsaturated groups include allyl (meth) acrylate, triallyl cyanurate, triallyl isocyanurate, ethylene glycol di (meth) acrylate, propylene glycol di (meth) acrylate, Examples thereof include 1,3-butylene glycol di (meth) acrylate and 1,4-butylene glycol di (meth) acrylate. In consideration of the fluidity of the polycarbonate resin composition, monomers having two or more unsaturated groups having different reactivities such as allyl (meth) acrylate, triallyl cyanurate, and triallyl isocyanurate are preferable. Triallyl cyanurate and triallyl isocyanurate have three allyl groups, but the reactivity of the allyl group that reacts first is different from the reactivity of the allyl group that reacts second and third. Allyl (meth) acrylate is particularly preferable.

  Examples of the polymerization initiator include peroxides such as tert-butyl hydroperoxide and cumene hydroperoxide, azo initiators such as azobisisobutyronitrile, and redox in which an oxidizing agent and a reducing agent are combined. A system initiator is mentioned.

  Specific examples of redox initiators include sulfoxylate initiators in which ferrous sulfate, ethylenediaminetetraacetic acid disodium salt, Rongalite, and hydroperoxide are combined.

  Examples of the chain transfer agent include n-octyl mercaptan and tert-dodecyl mercaptan.

  The chain transfer agent is preferably 0.1 to 5 parts by weight, more preferably 0.3 to 1.5 parts by weight per 100 parts by weight in total of the monomers forming the copolymer of component C.

  Examples of the aromatic alkenyl compound monomer (Cb) include styrene, α-methyl styrene, o-methyl styrene, p-methyl styrene, vinyl xylene, ethyl styrene, dimethyl styrene, p-tert-butyl styrene, and vinyl naphthalene. In particular, styrene and α-methylstyrene, particularly styrene, is preferably 90% by weight or more in 100% by weight of the monomer (Cb). The most preferred embodiment is that the total amount of the monomer (Cb) is styrene.

  If the molecular weight distribution of the copolymer of component C is too wide, the flowability of the resin composition is decreased, or relatively low molecular weight is increased, so that heat resistance and thermal stability are decreased, smoke generation at the time of molding, mist There is a high possibility that problems such as mechanical stains and poor appearance such as fish eyes will occur. Therefore, the molecular weight distribution expressed by weight average molecular weight / number average molecular weight (Mw / Mn) is preferably 1-30. The upper limit is more preferably 10, and still more preferably 3. In addition, the calculation method of this molecular weight is based on the above-mentioned GPC measurement. The lower limit is practically preferably 1.3, more preferably 1.8. Further, within the range in which the molecular weight of the copolymer is measured, the peak of the molecular weight distribution by GPC measurement may be single or plural. A copolymer having a single peak is preferable because it can be easily produced.

  The C component copolymer preferably has a refractive index (nd) of 1.52 to 1.60, more preferably 1.565 to 1.59. In particular, the difference in refractive index from the refractive index (nd) of the polycarbonate resin of component A is preferably adjusted to within 0.015, particularly within 0.01.

  An embodiment in which the component C is a graft copolymer will be described. A preferred embodiment when the C component of the present invention is a graft copolymer is a graft copolymer obtained by graft polymerization of the monomer (Cb) in the presence of the polymer formed from the monomer (Ca). A graft copolymer obtained by graft polymerization of a monomer (Ca) in the presence of a polymer or a polymer formed from the monomer (Cb). In any embodiment, such a graft copolymer may be produced using a macromonomer formed from the monomer (Ca) or a macromonomer formed from the monomer (Cb) as described above. preferable.

  In such a macromonomer, in consideration of the balance of fluidity, impact resistance, and delamination resistance, it has two or more unsaturated groups with respect to 100 parts by weight of the monomer (Ca) or the monomer (Cb). More preferably, the monomer content is 0.7 to 5 parts by weight, and still more preferably 0.8 to 3 parts by weight. When the amount of the monomer having two or more unsaturated groups is less than 0.5 parts by weight, the macromonomer may not form a necessary and sufficient graft bond with the monomer (Cb). When the content of one or more monomers is too large, the proportion of the crosslinked structure insoluble in the organic solvent increases, and the excellent fluidity improving effect is impaired.

  The production of such a macromonomer can be performed according to the production of the copolymer. In the polymerization system of the obtained macromonomer, a mixture containing a monomer to be grafted and, if necessary, other monomers copolymerizable with the monomer, a polymerization initiator, a chain transfer agent, and the like is supplied. The polymerization is carried out at a high temperature.

  As the polymerization initiator, chain transfer agent and the like, the same ones as described in the production of the copolymer can be applied.

  The above is basically a case where a macromonomer is a trunk and a polymer unit formed from a monomer to be grafted is a branch, but only a macromonomer having an unsaturated double bond at the terminal is used. The macromonomer is a branch, and a polymer unit formed from the monomer is a trunk.

(About the content of each component)
The content of component C of the present invention is 0.05 to 30 parts by weight, preferably 1 to 15 parts by weight, based on a total of 100 parts by weight of 60 to 99 parts by weight of component A and 1 to 40 parts by weight of component B. Preferably it is 2-9 weight part. When the content of component C is less than 0.05 parts by weight, the improvement in fluidity is insufficient, and when it exceeds 30 parts by weight, the compatibility, heat resistance, and mechanical properties are lowered.

(Other additives)
In the antistatic aromatic polycarbonate resin composition of the present invention, various stabilizers and coloring materials can be used in order to stabilize the molecular weight and hue at the time of molding. Examples of such stabilizers include phosphorus stabilizers, hindered phenol stabilizers, ultraviolet absorbers, and light stabilizers.

(I) Phosphorus stabilizer Examples of the phosphorous stabilizer include phosphorous acid, phosphoric acid, phosphonous acid, phosphonic acid and esters thereof, and tertiary phosphine. Among these, phosphorous acid, phosphoric acid, phosphonous acid, and phosphonic acid, triorganophosphate compounds, and acid phosphate compounds are particularly preferable. The organic group in the acid phosphate compound includes any of mono-substituted, di-substituted, and mixtures thereof. Any of the following exemplified compounds corresponding to the compound is similarly included.

  Triorganophosphate compounds include trimethyl phosphate, triethyl phosphate, tributyl phosphate, trioctyl phosphate, tridecyl phosphate, tridodecyl phosphate, trilauryl phosphate, tristearyl phosphate, tricresyl phosphate, triphenyl phosphate, trichlorophenyl phosphate, diphenyl Examples include cresyl phosphate, diphenyl monoorthoxenyl phosphate, and tributoxyethyl phosphate. Among these, trialkyl phosphate is preferable. The carbon number of the trialkyl phosphate is preferably 1 to 22, more preferably 1 to 4. A particularly preferred trialkyl phosphate is trimethyl phosphate.

  Examples of the acid phosphate compound include methyl acid phosphate, ethyl acid phosphate, butyl acid phosphate, butoxyethyl acid phosphate, octyl acid phosphate, decyl acid phosphate, lauryl acid phosphate, stearyl acid phosphate, oleyl acid phosphate, behenyl acid phosphate, behenyl acid phosphate Nonylphenyl acid phosphate, cyclohexyl acid phosphate, phenoxyethyl acid phosphate, alkoxy polyethylene glycol acid phosphate, bisphenol A acid phosphate, and the like. Among these, long-chain dialkyl acid phosphates having 10 or more carbon atoms are effective for improving thermal stability, and the acid phosphate itself is preferable because of high stability.

  Examples of the phosphite compound include 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-butyl) Phenyl) phosphite, tris (2,4-di-tert-butylphenyl) phosphite, tris (2,6-di-tert-butylphenyl) phosphite, distearyl Taerythritol 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 penta Examples include erythritol diphosphite, bis (nonylphenyl) pentaerythritol diphosphite, and dicyclohexylpentaerythritol 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 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.

  Suitable phosphorus stabilizers are a triorganophosphate compound, an acid phosphate compound, and a phosphite compound represented by the following general formula (3). It is particularly preferable to add a triorganophosphate compound.

（式（３）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 (3), 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 (3), 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.

(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-thiodie Renbis- [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) iso Cyanurate, 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.

  It is preferable that either a phosphorus stabilizer or a hindered phenol antioxidant is blended. In particular, a phosphorus stabilizer is preferably blended, and a triorganophosphate compound is more blended. The compounding amount of the phosphorus stabilizer and the hindered phenol antioxidant is 0.005 to 1 part by weight, preferably 0.01 to 0.3 part by weight, based on the total of 100 parts by weight of component A and component B, respectively. Part.

(Iii) Release agent It is preferable to mix | blend a release agent with the antistatic aromatic polycarbonate resin composition of this invention further for the purpose of the productivity improvement at the time of the shaping | molding, and the reduction of the distortion of a molded article. 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, still more preferably 0.05 to 0 parts on the basis of 100 parts by weight of the total of component A and component B. 8 parts by weight. In such a range, the polycarbonate resin composition has good releasability.

(Vi) Other heat stabilizers The antistatic aromatic polycarbonate resin composition of the present invention may contain other heat stabilizers other than the above 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-based stabilizer is preferably 0.0005 to 0.05 parts by weight, more preferably 0.001 to 0.03 parts by weight, based on 100 parts by weight of the total of component A and component B.

  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 the total of 100 parts by weight of the component A and the component B.

(V) Flame Retardant The antistatic aromatic polycarbonate resin composition of the present invention may contain various compounds known as flame retardants for polycarbonate resins. The compounding of the compound used as a flame retardant not only improves the flame retardancy but also provides, for example, an improvement in antistatic properties, fluidity, rigidity, and thermal stability based on the properties of each compound.

  Examples of such flame retardants include (i) organometallic salt flame retardants (for example, alkali (earth) organic sulfonate metal salts, borate metal salt flame retardants, stannate metal salt flame retardants, etc.), and (ii) Organophosphorous flame retardants (for example, monophosphate compounds, phosphate oligomer compounds, phosphonate oligomer compounds, phosphonitrile oligomer compounds, and phosphonic acid amide compounds), (iii) silicone flame retardants comprising silicone compounds, and (iv) halogens And flame retardant (for example, brominated epoxy resin, brominated polystyrene, brominated polycarbonate (including oligomers), brominated polyacrylate, chlorinated polyethylene, etc.).

(Vi) Organometallic salt-based flame retardant An organic metal salt-based flame retardant is advantageous in that heat resistance is substantially maintained and antistatic properties can be imparted. The organometallic salt flame retardant most advantageously used in the present invention is a fluorine-containing organometallic salt compound. The fluorine-containing organometallic salt compound of the present invention refers to a metal salt compound comprising an anion component composed of an organic acid having a fluorine-substituted hydrocarbon group and a cation component composed of a metal ion. More preferred specific examples include metal salts of fluorine-substituted organic sulfonic acids, metal salts of fluorine-substituted organic sulfates, and metal salts of fluorine-substituted organic phosphates. Fluorine-containing organometallic salt compounds can be used alone or in combination of two or more. Among them, a metal salt of a fluorine-substituted organic sulfonic acid is preferable, and a metal salt of a sulfonic acid having a perfluoroalkyl group is particularly preferable. Here, the carbon number of the perfluoroalkyl group is preferably in the range of 1-18, more preferably in the range of 1-10, and still more preferably in the range of 1-8.

  The metal constituting the metal ion of the organometallic salt flame retardant is an alkali metal or an alkaline earth metal. Examples of the alkali metal include lithium, sodium, potassium, rubidium and cesium. Examples of the alkaline earth metal include beryllium. , Magnesium, calcium, strontium and barium. More preferred is an alkali metal. Accordingly, a preferred organometallic salt flame retardant is an alkali metal perfluoroalkyl sulfonate. Among such alkali metals, rubidium and cesium are suitable when transparency requirements are higher, but these are not general-purpose and difficult to purify, resulting in disadvantages in terms of cost. is there. On the other hand, although lithium and sodium are advantageous in terms of cost and flame retardancy, they may be disadvantageous in terms of transparency. In consideration of these, the alkali metal in the perfluoroalkylsulfonic acid alkali metal salt can be properly used, but perfluoroalkylsulfonic acid potassium salt having an excellent balance of properties is most suitable in any respect. Such potassium salts and alkali metal salts of perfluoroalkylsulfonic acid composed of other alkali metals can be used in combination.

  Such alkali metal perfluoroalkylsulfonates include potassium trifluoromethanesulfonate, potassium perfluorobutanesulfonate, potassium perfluorohexanesulfonate, potassium perfluorooctanesulfonate, sodium pentafluoroethanesulfonate, perfluorobutanesulfone. Acid sodium, sodium perfluorooctane sulfonate, lithium trifluoromethane sulfonate, lithium perfluorobutane sulfonate, lithium perfluoroheptane sulfonate, cesium trifluoromethane sulfonate, cesium perfluorobutane sulfonate, cesium perfluorooctane sulfonate, Cesium perfluorohexane sulfonate, rubidium perfluorobutane sulfonate, and perful B hexane sulfonate rubidium, and these may be used in combination of at least one or two. Of these, potassium perfluorobutanesulfonate is particularly preferred.

  The fluorine-containing organometallic salt preferably has a fluoride ion content as measured by ion chromatography of 50 ppm or less, more preferably 20 ppm or less, and even more preferably 10 ppm or less. The lower the fluoride ion content, the better the flame retardancy. The lower limit of the fluoride ion content can be substantially zero, but is practically preferably about 0.2 ppm in view of the balance between the refining man-hour and the effect. Such alkali metal salt of perfluoroalkylsulfonic acid having a fluoride ion content is purified, for example, as follows. The perfluoroalkylsulfonic acid alkali metal salt is dissolved in 2 to 10 times by weight of the metal salt in ion-exchanged water in the range of 40 to 90 ° C. (more preferably 60 to 85 ° C.). The alkali metal salt of perfluoroalkylsulfonic acid is a method of neutralizing perfluoroalkylsulfonic acid with an alkali metal carbonate or hydroxide, or perfluoroalkylsulfonyl fluoride with an alkali metal carbonate or hydroxide. It is produced by a neutralizing method (more preferably by the latter method). The ion-exchanged water is particularly preferably water having an electric resistance value of 18 MΩ · cm or more. The solution in which the metal salt is dissolved is stirred at the above temperature for 0.1 to 3 hours, more preferably 0.5 to 2.5 hours. Thereafter, the liquid is cooled to 0 to 40 ° C, more preferably in the range of 10 to 35 ° C. Crystals precipitate upon cooling. The precipitated crystals are removed by filtration. This produces a suitable purified perfluoroalkylsulfonic acid alkali metal salt.

  The blending amount of the fluorine-containing organometallic salt compound is preferably 0.005 to 0.6 parts by weight, more preferably 0.005 to 0.2 parts by weight, based on the total of 100 parts by weight of the component A and the component B. Preferably it is 0.008-0.13 weight part. The more preferable range is, the effects (for example, flame retardancy and antistatic properties) expected by the blending of the fluorine-containing organic metal salt are exhibited, and the adverse effect on the light resistance of the polycarbonate resin composition is reduced.

  In addition, as an organic metal salt flame retardant other than the above-mentioned fluorine-containing organic metal salt compound, a metal salt of an organic sulfonic acid not containing a fluorine atom is suitable. Examples of the metal salt include an alkali metal salt of an aliphatic sulfonic acid, an alkaline earth metal salt of an aliphatic sulfonic acid, an alkali metal salt of an aromatic sulfonic acid, and an alkaline earth metal salt of an aromatic sulfonic acid (any Also does not contain a fluorine atom).

  Preferable examples of the aliphatic sulfonic acid metal salt include an alkali (earth) metal salt of an alkyl sulfonate, and these can be used alone or in combination of two or more (here, alkali The (earth) metal salt is used to include both alkali metal salts and alkaline earth metal salts). Preferred examples of the alkane sulfonic acid used for the alkali (earth) metal salt of the alkyl sulfonate include methane sulfonic acid, ethane sulfonic acid, propane sulfonic acid, butane sulfonic acid, methyl butane sulfonic acid, hexane sulfonic acid, and heptane. Examples thereof include sulfonic acid and octanesulfonic acid, and these can be used alone or in combination of two or more.

  The aromatic sulfonic acid used in the aromatic (earth) metal salt of aromatic sulfonate includes monomeric or polymeric aromatic sulfide sulfonic acid, aromatic carboxylic acid and ester sulfonic acid, monomeric or polymeric sulfonic acid. Aromatic ether sulfonic acid, aromatic sulfonate sulfonic acid, monomeric or polymeric aromatic sulfonic acid, monomeric or polymeric aromatic sulfonic acid, aromatic ketone sulfonic acid, heterocyclic sulfonic acid, Examples include at least one acid selected from the group consisting of sulfonic acids of aromatic sulfoxides and condensates of methylene type bonds of aromatic sulfonic acids, and these are used alone or in combination of two or more. be able to.

  Specific examples of the aromatic (earth) metal salt of an aromatic sulfonate include, for example, disodium diphenyl sulfide-4,4′-disulfonate, dipotassium diphenyl sulfide-4,4′-disulfonate, potassium 5-sulfoisophthalate, Sodium 5-sulfoisophthalate, polysodium polyethylene terephthalate polysulfonate, calcium 1-methoxynaphthalene-4-sulfonate, disodium 4-dodecylphenyl ether disulfonate, polysodium poly (2,6-dimethylphenylene oxide) polysulfonate Poly (1,3-phenylene oxide) polysulfonic acid polysodium, poly (1,4-phenylene oxide) polysulfonic acid polysodium, poly (2,6-diphenylphenylene oxide) polysulfonic acid poly Lithium, poly (2-fluoro-6-butylphenylene oxide) polysulfonate, potassium sulfonate of benzenesulfonate, sodium benzenesulfonate, strontium benzenesulfonate, magnesium benzenesulfonate, dipotassium p-benzenedisulfonate, naphthalene-2 , 6-disulfonic acid dipotassium, biphenyl-3,3'-disulfonic acid calcium, diphenylsulfone-3-sulfonic acid sodium, diphenylsulfone-3-sulfonic acid potassium, diphenylsulfone-3,3'-disulfonic acid dipotassium, diphenylsulfone Α, α, α-trifluoroacetophenone sodium 4-sulfonate, dipotassium benzophenone-3,3′-disulfonate, Nene-2,5-disulfonate, dipotassium thiophene-2,5-disulfonate, calcium thiophene-2,5-disulfonate, sodium benzothiophenesulfonate, potassium diphenylsulfoxide-4-sulfonate, naphthalene Examples thereof include a formalin condensate of sodium sulfonate and a formalin condensate of sodium anthracene sulfonate.

  On the other hand, the alkali (earth) metal salt of sulfate ester may include, in particular, the alkali (earth) metal salt of sulfate ester of monovalent and / or polyhydric alcohols. Alcohol sulfates include methyl sulfate, ethyl sulfate, lauryl sulfate, hexadecyl sulfate, polyoxyethylene alkylphenyl ether sulfate, pentaerythritol mono, di, tri, tetrasulfate, and lauric acid monoglyceride. And sulfuric acid esters of palmitic acid monoglyceride and stearic acid monoglyceride sulfate. The alkali (earth) metal salts of these sulfates are preferably alkali (earth) metal salts of lauryl sulfate.

  Examples of other alkali (earth) metal salts include alkali (earth) metal salts of aromatic sulfonamides such as saccharin, N- (p-tolylsulfonyl) -p-toluenesulfonimide, N Examples include-(N'-benzylaminocarbonyl) sulfanilimide and alkali (earth) metal salts of N- (phenylcarboxyl) sulfanilimide.

  Among the above, preferable metal salts of organic sulfonic acids not containing fluorine atoms are aromatic (earth) metal salts of aromatic sulfonates, and potassium salts are particularly preferable. When blending such an alkali (earth) sulfonic acid metal salt, the content is 0.001 to 1 part by weight, more preferably 0.005 based on the total of 100 parts by weight of component A and component B. It is -0.5 weight part, More preferably, it is 0.01-0.1 weight part.

(V-ii) Organophosphorus Flame Retardant As the organophosphorus flame retardant of the present invention, 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, it is advantageous in that the molding processability of the resin composition of the present invention can be improved although the heat resistance is lowered. is there. As the phosphate compound, 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 (4) can be mentioned.

（但し上記式中のＸは、二価フェノールから誘導される二価の有機基を表し、Ｒ^１１、Ｒ^１２、Ｒ^１３、およびＲ^１４はそれぞれ一価フェノールから誘導される一価の有機基を表し、ｎは０〜５の整数を表す。）

(However, X in the above formula represents a divalent organic group derived from a dihydric phenol, and R ¹¹ , R ¹² , R ¹³ , and R ¹⁴ are each a monovalent organic group derived from a monohydric phenol. And n represents an integer of 0 to 5.)

  The phosphate compound of the above formula 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, it is 0.95-1.15, Most preferably, it is the range of 1-1.14.

  Preferable specific examples of the dihydric phenol for deriving X include hydroquinone, resorcinol, bis (4-hydroxydiphenyl) methane, bisphenol A, dihydroxydiphenyl, dihydroxynaphthalene, bis (4-hydroxyphenyl) sulfone, bis (4 -Hydroxyphenyl) ketone and bis (4-hydroxyphenyl) sulfide are exemplified, among which resorcinol, bisphenol A, and dihydroxydiphenyl are preferable.

Preferable specific examples of the monohydric phenol for deriving R ¹¹ , R ¹² , R ¹³ , and R ¹⁴ include phenol, cresol, xylenol, isopropylphenol, butylphenol, and p-cumylphenol. Are phenol and 2,6-dimethylphenol.

  Such a monohydric phenol may substitute a halogen atom. Specific examples of the phosphate compound having a group derived from the monohydric phenol include tris (2,4,6-tribromophenyl) phosphate and tris. Examples include (2,4-dibromophenyl) phosphate, tris (4-bromophenyl) phosphate, and the like.

  On the other hand, specific examples of phosphate compounds not substituted with halogen atoms include monophosphate compounds such as triphenyl phosphate and tri (2,6-xylyl) phosphate, and resorcinol bisdi (2,6-xylyl) phosphate). Preferred are phosphate oligomers mainly composed of phosphate oligomers, phosphate oligomers mainly composed of 4,4-dihydroxydiphenyl bis (diphenyl phosphate), and phosphate oligomers mainly composed of bisphenol A bis (diphenyl phosphate). Indicates that a small amount of other components having different degrees of polymerization may be contained, and more preferably, the component of n = 1 in the above formula (4) is 80% by weight or more, more preferably 85% by weight or more, still more preferably Containing 90% by weight or more Show.).

(V-iii) Silicone-based flame retardant The silicone compound used as the silicone-based flame retardant of the present invention improves flame retardancy by a chemical reaction during combustion. As the compound, various compounds conventionally proposed as flame retardants for aromatic polycarbonate resins can be used. The silicone compound binds itself during combustion or binds to a component derived from the resin to form a structure, or gives a flame retardant effect to the polycarbonate resin by a reduction reaction during the structure formation. It is considered. Therefore, it is preferable that a group having high activity in such a reaction is contained, and more specifically, a predetermined amount of at least one group selected from an alkoxy group and a hydrogen (ie, Si—H group) is contained. preferable. As a content rate of this group (alkoxy group, Si-H group), the range of 0.1-1.2 mol / 100g is preferable, the range of 0.12-1 mol / 100g is more preferable, 0.15-0. The range of 6 mol / 100 g is more preferable. Such a ratio can be determined by measuring the amount of hydrogen or alcohol generated per unit weight of the silicone compound by the alkali decomposition method. The alkoxy group is preferably an alkoxy group having 1 to 4 carbon atoms, and particularly preferably a methoxy group.

Generally, the structure of a silicone compound is constituted by arbitrarily combining the following four types of siloxane units. That is,
M units: (CH ₃ ) ₃ SiO _1/2 , H (CH ₃ ) ₂ SiO _1/2 , H ₂ (CH ₃ ) SiO _1/2 , (CH ₃ ) ₂ (CH ₂ = CH) SiO _1/2 Monofunctional siloxane units such as (CH ₃ ) ₂ (C ₆ H ₅ ) SiO _1/2 , (CH ₃ ) (C ₆ H ₅ ) (CH ₂ ═CH) SiO _1/2 ,
D unit: (CH ₃ ) ₂ SiO, H (CH ₃ ) SiO, H ₂ SiO, H (C ₆ H ₅ ) SiO, (CH ₃ ) (CH ₂ ═CH) SiO, (C ₆ H ₅ ) ₂ SiO Bifunctional siloxane units such as
T unit: (CH ₃ ) SiO _3/2 , (C ₃ H ₇ ) SiO _3/2 , HSiO _3/2 , (CH ₂ ═CH) SiO _3/2 , (C ₆ H ₅ ) SiO _3/2 etc. A trifunctional siloxane unit of
Q unit: a tetrafunctional siloxane unit represented by SiO ₂ .

Specifically, the structure of the silicone compound used in the silicone-based flame retardant is represented by the following formulas: D _n , T _p , M _m D _n , M _m T _p , M _m Q _q , M _m D _n T _{p , M m D n Q q,} M m T p Q q, M m D n T p Q q, D n T p, D n Q q, include _{D n} T p _{Q q.} Among these, preferable structures of the silicone compound are M _m D _n , M _m T _p , M _m D _n T _p , and M _m D _n Q _q , and more preferable structures are M _m D _n or M _m D _n. T _p .

  Here, the coefficients m, n, p, and q in the above formulas are integers of 1 or more representing the degree of polymerization of each siloxane unit, and the sum of the coefficients in each formula is the average degree of polymerization of the silicone compound. . This average degree of polymerization is preferably in the range of 3 to 150, more preferably in the range of 3 to 80, still more preferably in the range of 3 to 60, and particularly preferably in the range of 4 to 40. The better the range, the better the flame retardancy. Further, as described later, a silicone compound containing a predetermined amount of an aromatic group is excellent in transparency and hue.

  When any of m, n, p, and q is a numerical value of 2 or more, the siloxane unit with the coefficient can be two or more types of siloxane units having different hydrogen atoms or organic residues to be bonded. .

  The silicone compound may be linear or have a branched structure. The organic residue bonded to the silicon atom is preferably an organic residue having 1 to 30 carbon atoms, more preferably 1 to 20 carbon atoms. Specific examples of such an organic residue include alkyl groups such as a methyl group, an ethyl group, a propyl group, a butyl group, a hexyl group, and a decyl group, a cycloalkyl group such as a cyclohexyl group, an aryl group such as a phenyl group, And aralkyl groups such as tolyl groups. More preferably, they are a C1-C8 alkyl group, an alkenyl group, or an aryl group. As the alkyl group, an alkyl group having 1 to 4 carbon atoms such as a methyl group, an ethyl group, and a propyl group is particularly preferable.

  Further, the silicone compound used as the silicone flame retardant preferably contains an aryl group. More preferably, the ratio (aromatic group amount) of the aromatic group represented by the following general formula (5) is 10 to 70% by weight (more preferably 15 to 60% by weight).

（式（５）中、Ｘはそれぞれ独立にＯＨ基、炭素数１〜２０の一価の有機残基を示す。ｎは０〜５の整数を表わす。さらに式（５）中においてｎが２以上の場合はそれぞれ互いに異なる種類のＸを取ることができる。）

(In formula (5), each X independently represents an OH group or a monovalent organic residue having 1 to 20 carbon atoms. N represents an integer of 0 to 5. Further, in formula (5), n is 2) In these cases, different types of X can be taken.)

  The silicone compound used as the silicone-based flame retardant may contain a reactive group in addition to the Si-H group and the alkoxy group. Examples of the reactive group include an amino group, a carboxyl group, an epoxy group, and a vinyl group. Examples thereof include a group, a mercapto group, and a methacryloxy group.

  As the silicone compound having a Si—H group, a silicone compound containing at least one of structural units represented by the following general formulas (6) and (7) is preferably exemplified.

（式（６）および式（７）中、Ｚ^１〜Ｚ^３はそれぞれ独立に水素原子、炭素数１〜２０の一価の有機残基、または下記一般式（８）で示される化合物を示す。α^１〜α^３はそれぞれ独立に０または１を表わす。ｍ１は０もしくは１以上の整数を表わす。さらに式（６）中においてｍ１が２以上の場合の繰返し単位はそれぞれ互いに異なる複数の繰返し単位を取ることができる。）

(In formula (6) and formula (7), Z ^{1 to} Z ³ each independently represent a hydrogen atom, a monovalent organic residue having 1 to 20 carbon atoms, or a compound represented by the following general formula (8). Α ^{1 to} α ³ each independently represents 0 or 1. m1 represents 0 or an integer of 1 or more, and in Formula (6), when m1 is 2 or more, the repeating unit is a plurality of different repeating units. Can take units.)

（式（８）中、Ｚ^４〜Ｚ^８はそれぞれ独立に水素原子、炭素数１〜２０の一価の有機残基を示す。α^４〜α^８はそれぞれ独立に０または１を表わす。ｍ２は０もしくは１以上の整数を表わす。さらに式（８）中においてｍ２が２以上の場合の繰返し単位はそれぞれ互いに異なる複数の繰返し単位を取ることができる。）

(In formula (8), Z ^{4 to} Z ⁸ each independently represent a hydrogen atom or a monovalent organic residue having 1 to 20 carbon atoms. Α ^{4 to} α ⁸ each independently represents 0 or 1. m 2 Represents 0 or an integer greater than or equal to 1. Furthermore, in formula (8), when m2 is 2 or more, the repeating unit may take a plurality of different repeating units.

  Examples of the silicone compound having an alkoxy group in the silicone compound used for the silicone flame retardant include at least one compound selected from compounds represented by the general formula (9) and the general formula (10).

（式（９）中、β^１はビニル基、炭素数１〜６のアルキル基、炭素数３〜６のシクロアルキル基、並びに炭素数６〜１２のアリール基およびアラルキル基を示す。γ^１、γ^２、γ^３、γ^４、γ^５、およびγ^６は炭素数１〜６のアルキル基およびシクロアルキル基、並びに炭素数６〜１２のアリール基およびアラルキル基を示し、少なくとも１つの基がアリール基またはアラルキル基である。δ^１、δ^２、およびδ^３は炭素数１〜４のアルコキシ基を示す。）

(In formula (9), β ¹ represents a vinyl group, an alkyl group having 1 to 6 carbon atoms, a cycloalkyl group having 3 to 6 carbon atoms, and an aryl group and aralkyl group having 6 to 12 carbon atoms. Γ ¹ , γ ² , γ ³ , γ ⁴ , γ ⁵ , and γ ⁶ represent an alkyl group and a cycloalkyl group having 1 to ⁶ carbon atoms, and an aryl group and an aralkyl group having 6 to 12 carbon atoms, and at least one group is aryl. And δ ¹ , δ ² , and δ ³ are each an alkoxy group having 1 to 4 carbon atoms.)

（式（１０）中、β^２およびβ^３はビニル基、炭素数１〜６のアルキル基、炭素数３〜６のシクロアルキル基、並びに炭素数６〜１２のアリール基およびアラルキル基を示す。γ^７、γ^８、γ^９、γ^１０、γ^１１、γ^１２、γ^１３およびγ^１４は炭素数１〜６のアルキル基、、炭素数３〜６のシクロアルキル基、並びに炭素数６〜１２のアリール基およびアラルキル基を示し、少なくとも１つの基がアリール基またはアラルキルである。δ^４、δ^５、δ^６、およびδ^７は炭素数１〜４のアルコキシ基を示す。）

(In formula (10), β ² and β ³ represent a vinyl group, an alkyl group having 1 to 6 carbon atoms, a cycloalkyl group having 3 to 6 carbon atoms, and an aryl group and an aralkyl group having 6 to 12 carbon atoms. γ ⁷ , γ ⁸ , γ ⁹ , γ ¹⁰ , γ ¹¹ , γ ¹² , γ ^13, and γ ¹⁴ are each an alkyl group having 1 to 6 carbon atoms, a cycloalkyl group having 3 to 6 carbon atoms, and 6 to 12 carbon atoms. And at least one group is an aryl group or an aralkyl group, and δ ⁴ , δ ⁵ , δ ⁶ , and δ ⁷ represent an alkoxy group having 1 to 4 carbon atoms.)

(V-iv) Halogen Flame Retardant As the halogen flame retardant of the present invention, brominated polycarbonate (including oligomer) is particularly suitable. Brominated polycarbonate has excellent heat resistance and can greatly improve flame retardancy. In the brominated polycarbonate used in the present invention, the structural unit represented by the following general formula (11) is at least 60 mol%, preferably at least 80 mol%, particularly preferably substantially the following general formula. A brominated polycarbonate compound comprising the structural unit represented by (11).

（式（１１）中、Ｘは臭素原子、Ｒは炭素数１〜４のアルキレン基、炭素数１〜４のアルキリデン基または−ＳＯ_２−である。）

(In Formula (11), X is a bromine atom, R is an alkylene group having 1 to 4 carbon atoms, an alkylidene group having 1 to 4 carbon atoms, or —SO ₂ —).

In the formula (11), R preferably represents a methylene group, an ethylene group, an isopropylidene group, —SO ₂ —, and particularly preferably an isopropylidene group.

  The brominated polycarbonate has a small number of remaining chloroformate groups and preferably has a terminal chlorine content of 0.3 ppm or less, more preferably 0.2 ppm or less. The amount of terminal chlorine is determined by dissolving a sample in methylene chloride, adding 4- (p-nitrobenzyl) pyridine and allowing it to react with terminal chlorine (terminal chloroformate). -3200). When the amount of terminal chlorine is 0.3 ppm or less, the thermal stability of the polycarbonate resin composition becomes better, and molding at a higher temperature becomes possible. As a result, a polycarbonate resin composition that is superior in molding processability is provided.

The brominated polycarbonate preferably has a small number of remaining hydroxyl terminals. More specifically, the amount of terminal hydroxyl groups is preferably 0.0005 mol or less, more preferably 0.0003 mol or less with respect to 1 mol of the structural unit of brominated polycarbonate. The amount of terminal hydroxyl groups can be determined by dissolving a sample in deuterated chloroform and measuring it by ¹ H-NMR method. Such a terminal hydroxyl group amount is preferable because the thermal stability of the polycarbonate resin composition is further improved.

  The specific viscosity of the brominated polycarbonate is preferably in the range of 0.015 to 0.1, more preferably in the range of 0.015 to 0.08. The specific viscosity of the brominated polycarbonate is calculated according to the above-described specific viscosity calculation formula used for calculating the viscosity average molecular weight of the polycarbonate resin which is the component A of the present invention.

(Vi) Anti-dripping agent The anti-static aromatic polycarbonate resin composition of the present invention may contain an anti-dripping agent. By using such an anti-dripping agent in combination with the above flame retardant, better flame retardancy can be obtained. Examples of the anti-dripping agent include a fluorinated polymer having a fibril-forming ability. Examples of such a polymer include polytetrafluoroethylene, tetrafluoroethylene copolymers (for example, tetrafluoroethylene / hexafluoropropylene copolymers). , Etc.), partially fluorinated polymers as shown in U.S. Pat. No. 4,379,910, polycarbonate resins produced from fluorinated diphenols, etc., preferably polytetrafluoroethylene (hereinafter referred to as PTFE). Is).

Polytetrafluoroethylene (fibrillated PTFE) having fibril-forming ability has a very high molecular weight, and exhibits a tendency to bind PTFE to each other by an external action such as shearing force to form a fiber. Its number average molecular weight ranges from 1.5 million to tens of millions. The lower limit is more preferably 3 million. The number average molecular weight is calculated based on the melt viscosity of polytetrafluoroethylene at 380 ° C. as disclosed in JP-A-6-145520. That is, the fibrillated PTFE has a melt viscosity at 380 ° C. measured by the method described in this publication in the range of 10 ⁷ to 10 ¹³ poise, preferably in the range of 10 ⁸ to 10 ¹² poise.

  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. Further, as disclosed in JP-A-6-145520, those having a structure having such a fibrillated PTFE as a core and a low molecular weight polytetrafluoroethylene as a shell are also preferably used.

  Examples of commercially available fibrillated PTFE include Teflon (registered trademark) 6J from Mitsui DuPont Fluorochemical Co., Ltd., Polyflon MPA FA500, F-201L from Daikin Chemical Industries, Ltd., and the like. Commercially available aqueous dispersions of fibrillated PTFE include: Fluon AD-1, AD-936 manufactured by Asahi IC Fluoropolymers, Fluon D-1, D-2 manufactured by Daikin Industries, Ltd., Mitsui A representative example is Teflon (registered trademark) 30J manufactured by DuPont Fluorochemical Co., Ltd.

  As a mixed form of fibrillated PTFE, (1) a method in which an aqueous dispersion of fibrillated PTFE and an aqueous dispersion or solution of an organic polymer are mixed and co-precipitated to obtain a co-agglomerated mixture (JP-A-60-258263). (2) A method of mixing an aqueous dispersion of fibrillated PTFE and dried organic polymer particles (Japanese Patent Laid-Open No. 4-272957). Described method), (3) A method in which an aqueous dispersion of fibrillated PTFE and an organic polymer particle solution are uniformly mixed, and the respective media are simultaneously removed from the mixture (Japanese Patent Laid-Open Nos. 06-220210, (Method described in Japanese Patent Application Laid-Open No. 08-188653), (4) A method of polymerizing monomers forming an organic polymer in an aqueous dispersion of fibrillated PTFE (Method described in JP-A-9-95583), and (5) an aqueous dispersion of PTFE and an organic polymer dispersion are uniformly mixed, and then a vinyl monomer is further polymerized in the mixed dispersion. Thereafter, those obtained by a method for obtaining a mixture (a method described in JP-A-11-29679, etc.) can be used. Examples of commercially available fibrillated 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.

  In order to effectively utilize the good mechanical strength of the antistatic aromatic polycarbonate resin composition of the present invention, the fibrillated PTFE is preferably dispersed as finely as possible. As a means of achieving such fine dispersion, the above mixed form of fibrillated PTFE is advantageous. A method of directly supplying an aqueous dispersion in a melt kneader is also advantageous for fine dispersion. However, in the case of the aqueous dispersion form, consideration is required in that the hue is slightly deteriorated. The proportion of fibrillated PTFE in the mixed form is preferably 10 to 80% by weight, more preferably 15 to 75% by weight, in 100% by weight of the mixture. When the ratio of fibrillated PTFE is in such a range, good dispersibility of fibrillated PTFE can be achieved.

  The content of the fibrillated PTFE in the polycarbonate resin composition is preferably 0.001 to 1 part by weight, more preferably 0.1 to 0.7 part by weight based on the total of 100 parts by weight of the component A and the component B. is there.

(Vii) Reinforcing filler Various known fillers other than the component B can be blended as the reinforcing filler in the antistatic aromatic polycarbonate resin composition of the present invention. As such a reinforcing filler, a silicate mineral filler, a glass filler, and a fibrous carbon filler are preferable. Examples of such silicate mineral fillers include talc, mascobite mica, synthetic fluorine mica, smectite, and wollastonite. Examples of the glass filler include glass flakes, glass balloons, and glass beads. As the silicate mineral filler and the glass filler, fillers whose surfaces are coated with metal oxides such as titanium oxide, zinc oxide, cerium oxide, and silicon oxide can also be used. Examples of the fibrous carbon-based filler include carbon fiber, metal-coated carbon fiber, carbon milled fiber, vapor growth carbon fiber, and carbon nanotube. The carbon nanotube may be any one of a fiber diameter of 0.003 to 0.1 μm, a single layer, a double layer, and a multilayer, and a multilayer (so-called MWCNT) is preferable. Among these, carbon fibers and metal-coated carbon fibers are preferable in that they are excellent in fatigue characteristics and can impart good electrical conductivity. Good electrical conductivity has become one of important characteristics required for resin materials in recent digital precision equipment (represented by, for example, a digital still camera).

  As the carbon fiber, any of cellulose, polyacrylonitrile, pitch and the like can be used. In addition, it is obtained by a method in which a raw material composition composed of a polymer and a solvent composed of a methylene bond of aromatic sulfonic acids or their salts is prevented or molded, and then carbonized without passing through an infusibilization step represented by a method such as carbonization. It is also possible to use those that have been used. Furthermore, any of general-purpose type, medium elastic modulus type, and high elastic modulus type can be used. Among these, polyacrylonitrile-based high elastic modulus type is particularly preferable.

  Moreover, although the average fiber diameter of carbon fiber is not specifically limited, Usually, it is 3-15 micrometers, Preferably it is 5-13 micrometers. A carbon fiber having an average fiber diameter in such a range can exhibit good mechanical strength and fatigue characteristics without impairing the appearance of the molded product. The preferred fiber length of the carbon fiber is 60 to 500 μm, preferably 80 to 400 μm, particularly preferably 100 to 300 μm, as the number average fiber length in the aromatic polycarbonate resin composition. The number average fiber length is a value calculated by an image analyzer from an optical microscope observation from the carbon fiber residue collected by high temperature ashing of the molded product, dissolution with a solvent, and decomposition with a chemical. is there. Further, when calculating such a value, a value having a length equal to or shorter than the fiber length is a value obtained by a method not counting. The aspect ratio of the carbon fiber is preferably in the range of 10 to 200, more preferably in the range of 15 to 100, and still more preferably in the range of 20 to 50. The aspect ratio of the fibrous carbon filler is a value obtained by dividing the average fiber length by the average fiber diameter.

  Further, the surface of the carbon fiber is preferably oxidized for the purpose of improving the adhesion with the matrix resin and improving the mechanical strength. Although the oxidation treatment method is not particularly limited, for example, (1) a method in which a fibrous carbon filler is treated with an acid or alkali or a salt thereof, or an oxidizing gas, (2) a fiber that can be converted into a fibrous carbon filler, or A method of firing the fibrous carbon filler at a temperature of 700 ° C. or higher in the presence of an inert gas containing an oxygen-containing compound; and (3) after the fibrous carbon filler is oxidized and then in the presence of the inert gas. The method of heat-treating with is suitably exemplified.

  The metal-coated carbon fiber is obtained by coating the surface of the carbon fiber with a metal layer. Examples of the metal include silver, copper, nickel, and aluminum, and nickel is preferable from the viewpoint of the corrosion resistance of the metal layer. As the method of metal coating, various methods described above for the surface coating with different materials in the glass filler can be employed. Of these, the plating method is preferably used. In addition, in the case of such metal-coated carbon fiber, as the original carbon fiber, those mentioned as the above carbon fiber can be used. The thickness of the metal coating layer is preferably 0.1 to 1 μm, more preferably 0.15 to 0.5 μm. More preferably, it is 0.2-0.35 micrometer.

  Such carbon fibers and metal-coated carbon fibers are preferably subjected to a bundling treatment with an olefin resin, a styrene resin, an acrylic resin, a polyester resin, an epoxy resin, a urethane resin, or the like.

  The reinforcing filler may be surface-treated with various surface treatment agents in advance. Such surface treatment agents include silane coupling agents (including alkylalkoxysilanes and polyorganohydrogensiloxanes), higher fatty acid esters, acid compounds (for example, phosphorous acid, phosphoric acid, carboxylic acid, and carboxylic acid anhydrides). Etc.) and various surface treatment agents such as wax. Furthermore, it may be granulated with a sizing agent such as various resins, higher fatty acid esters, and waxes.

  The reinforcing filler can be blended with the upper limit of 100 parts by weight based on the total of 100 parts by weight of component A and component B. The upper limit is preferably 25 parts by weight, more preferably 20 parts by weight. If the amount of reinforcing filler is too large, the thermal stability during molding tends to be insufficient.

(Viii) Antistatic agent The antistatic aromatic polycarbonate resin composition of the present invention may require antistatic performance, and in such a case, it is preferable to include an antistatic agent. Examples of such antistatic agents include (1) organic sulfonic acid phosphonium salts such as (1) aryl sulfonic acid phosphonium salts represented by dodecylbenzene sulfonic acid phosphonium salts, and alkyl sulfonic acid phosphonium salts, and tetrafluoroboric acid phosphonium salts. Examples thereof include phosphonium borate salts. The content of the phosphonium salt is suitably 5 parts by weight or less, preferably 0.05 to 5 parts by weight, more preferably 1 to 3.5 parts by weight, based on a total of 100 parts by weight of component A and component B. More preferably, it is in the range of 1.5 to 3 parts by weight.

  Antistatic agents include, for example: (2) lithium organic sulfonate, organic sodium sulfonate, organic potassium sulfonate, cesium organic sulfonate, rubidium organic sulfonate, calcium organic sulfonate, magnesium organic sulfonate, and barium organic sulfonate And organic sulfonate alkali (earth) metal salts. Such metal salts are also used as flame retardants as described above. More specific examples of such metal salts include metal salts of dodecylbenzene sulfonic acid and metal salts of perfluoroalkane sulfonic acid. The content of the organic sulfonate alkali (earth) metal salt is suitably 0.5 parts by weight or less, preferably 0.001 to 0.3 parts by weight, based on the total of 100 parts by weight of component A and component B. More preferably, it is 0.005-0.2 weight part. In particular, alkali metal salts such as potassium, cesium, and rubidium are preferable.

  Examples of the antistatic agent include (3) organic sulfonic acid ammonium salts such as alkylsulfonic acid ammonium salt and arylsulfonic acid ammonium salt. The ammonium salt is suitably 0.05 parts by weight or less based on the total of 100 parts by weight of the A component and the B component. Examples of the antistatic agent include (4) a polymer containing a poly (oxyalkylene) glycol component such as polyether ester amide as a constituent component. The polymer is suitably 5 parts by weight or less based on a total of 100 parts by weight of the component A and the component B.

(Ix) Other additives The antistatic aromatic polycarbonate resin composition of the present invention includes a thermoplastic resin other than the A component and the C component, a rubbery polymer, other flow modifiers, an antibacterial agent, and liquid paraffin. Such a dispersant, a photocatalytic antifouling agent and a photochromic agent can be blended.

  Examples of the thermoplastic resin other than the A component and the C component include styrene resins excluding the C component (for example, acrylonitrile-styrene copolymer resin (AS resin), acrylonitrile-butadiene-styrene copolymer resin (ABS resin)), and Polystyrene resins, etc.), aromatic polyester resins (polyethylene terephthalate resin (PET resin), polybutylene terephthalate resin (PBT resin), cyclohexanedimethanol copolymerized polyethylene terephthalate resin (so-called PET-G resin), polyethylene naphthalate resin, and poly Butylene naphthalate resin), polymethyl methacrylate resin (PMMA resin), cyclic polyolefin resin, polylactic acid resin, polycaprolactone resin, thermoplastic fluororesin (for example, polyvinylidene fluoride resin) Typified by), and polyolefin resins (polyethylene resins, ethylene - (alpha-olefin) copolymer resins, polypropylene resins, and propylene - (alpha-olefin) copolymer resins, etc.) are exemplified. Examples of the rubbery polymer include various core-shell type graft copolymers and thermoplastic elastomers. The other thermoplastic resin and rubber polymer are preferably 10 parts by weight or less, more preferably 5 parts by weight or less based on the total of 100 parts by weight of the component A and the component B.

(Manufacture of polycarbonate resin composition)
In order to produce the antistatic aromatic polycarbonate resin composition of the present invention, any method is adopted. For example, component A, component B, component C and optionally other additives are mixed thoroughly using premixing means such as a V-type blender, Henschel mixer, mechanochemical device, extrusion mixer, etc. A method of granulating such a premix by an extrusion granulator 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 a 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 polycarbonate resin of the component A or directly supplying them to an 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 is preferably installed for efficiently discharging generated moisture and volatile gas to the outside of the extruder. 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, a master pellet is prepared by melting and kneading the A component and the C component in advance with a melt kneader so as to contain the high concentration C component of the present invention, and the master pellet is made into the remaining A component, B component and The method of mixing with another additive and pelletizing with a melt kneader is mentioned.

  In addition, a master pellet is prepared by melting and kneading the A component and the B component in a melt kneader in advance so as to contain the high concentration B component of the present invention, and the master pellet is made into the remaining A component, C component and The method of mixing with another additive and pelletizing with a melt kneader is mentioned.

  The antistatic aromatic polycarbonate resin composition of the present invention can be produced in various products by usually injection-molding the pellets produced as described above to obtain molded products. In such injection molding, not only ordinary molding methods but also injection compression molding, injection press molding, gas assist injection molding, foam molding (including a method of injecting a supercritical fluid), insert molding, in-mold coating molding, heat insulation Examples thereof include mold molding, rapid heating / cooling mold molding, two-color molding, sandwich molding, and ultra-high speed injection molding. In addition, either a cold runner method or a hot runner method can be selected for molding.

  The antistatic aromatic polycarbonate resin composition of the present invention can also be used in the form of various shaped extrusions, sheets, films and the like by extrusion molding. For forming sheets and films, an inflation method, a calendar method, a casting method, or the like can also be used. It is also possible to form a heat-shrinkable tube by applying a specific stretching operation. Further, the antistatic aromatic polycarbonate resin composition of the present invention can be formed into a molded product by rotational molding or blow molding.

  Accordingly, an antistatic aromatic polycarbonate resin composition and a molded article excellent in molding processability having excellent antistatic properties without mechanical delamination, mechanical strength, flow characteristics and good heat resistance are provided. That is, according to the present invention, a molded antistatic aromatic polycarbonate resin composition obtained by blending 0.05 to 30 parts by weight of the C component with respect to 100 parts by weight of the total of the A component and the B component. Goods are provided. As a more preferred embodiment, a test piece is a flat 50 mm long, 50 mm wide, and 2 mm thick, and the plate is stored for one week in an environment of a temperature of 23 ° C. and a relative humidity of 50%. An antistatic aromatic polycarbonate resin composition having a charged voltage half-life (seconds) of 20 seconds or less, preferably 10 seconds or less, particularly preferably 7 seconds or less, as measured by Goods are provided.

  Molded articles in which the resin composition of the present invention is used include various electronic / electric equipment parts, camera parts, OA equipment parts, precision machine parts, machine parts, vehicle parts, other agricultural materials, transport containers, playground equipment, miscellaneous goods, etc. It is useful for various applications that require antistatic properties, and the industrial effects that it exhibits are exceptional.

  Furthermore, various surface treatments can be performed on the molded article made of the resin composition of the present invention. Surface treatment here refers to a new layer on the surface of resin molded products such as vapor deposition (physical vapor deposition, chemical vapor deposition, etc.), plating (electroplating, electroless plating, hot dipping, etc.), painting, coating, printing, etc. A method used for ordinary polycarbonate resin is applicable. Specific examples of the surface treatment include various surface treatments such as hard coat, water / oil repellent coat, ultraviolet absorption coat, infrared absorption coat, and metalizing (evaporation). Hard coat is a particularly preferred and required surface treatment.

  In addition, since the resin composition of the present invention has improved metal adhesion, application of vapor deposition and plating is also preferable. The molded product thus provided with the metal layer can be used for electromagnetic wave shielding parts, conductive parts, antenna parts, and the like. Such parts are particularly preferably sheet-like and film-like.

  The antistatic aromatic polycarbonate resin composition of the present invention has excellent antistatic properties, mechanical strength, flow characteristics, good heat resistance and the like, and also has good compatibility without delamination, As described above, it is widely useful in various fields such as buildings, building materials, agricultural materials, marine materials, vehicles, electrical / electronic devices, machinery, and the like. Therefore, the industrial effect exhibited by the present invention is extremely great.

  The form of the present invention considered to be the best by the present inventor is a collection 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.

(I) Evaluation of polycarbonate resin composition (i) Bending strength: Measured according to ISO 178 (measurement condition 23 ° C.). In addition, the test piece was shape | molded by the cylinder temperature of 300 degreeC and the mold temperature of 100 degreeC with the injection molding machine (Sumitomo Heavy Industries, Ltd. SG-150U).
(Ii) Flexural modulus: measured in accordance with ISO 178 (measurement condition 23 ° C.). In addition, the test piece was shape | molded by the cylinder temperature of 300 degreeC and the mold temperature of 100 degreeC with the injection molding machine (Sumitomo Heavy Industries, Ltd. SG-150U).
(Iii) Deflection temperature under load Based on ISO75-1 and 75-2, the load was measured at 1.80 MPa. In addition, the test piece was shape | molded by the cylinder temperature of 300 degreeC and the mold temperature of 100 degreeC with the injection molding machine (Sumitomo Heavy Industries, Ltd. SG-150U).
(Iv) Delamination resistance: A tensile fracture test was performed in accordance with ISO527-1 and 527-2, and the delamination resistance was evaluated according to the fracture condition. That is, the fracture test piece caused shear failure between the layers in the thickness direction, the test piece was evaluated as x when the test piece was pulled out into a sheath shape, and the case where such sheath-like failure was not recognized as ○ evaluated.
(V) Fluidity: A Sumitomo Heavy Industries, Ltd. SG-150U molding machine was used, and the flow length was evaluated with an Archimedes spiral flow mold (channel thickness 2 mm, channel width 8 mm). The conditions were a cylinder temperature of 310 ° C., a mold temperature of 100 ° C., and an injection pressure of 118 MPa.
(Vi) Surface appearance: As a test piece, a flat plate having a length of 150 mm, a width of 150 mm, and a thickness of 1.5 mm having a fan gate having a width of 25 mm at the center of one piece is formed by an injection molding machine (SG-manufactured by Sumitomo Heavy Industries, Ltd.). 150U) was molded at a cylinder temperature of 300 ° C., a mold temperature of 100 ° C. and an injection speed of 50 mm / sec, and the surface appearance from the end of the side opposite to the gate to the width of 20 mm was observed. The surface of the observation area was evaluated as “Good” when the surface roughness was small and good, “Δ” when the surface was slightly rough, and “X” when the surface was large.
(Vii) Antistatic property: After using a flat plate having a length of 50 mm, a width of 50 mm and a thickness of 2 mm as a test piece, the plate was stored for one week in an environment of a temperature of 23 ° C. and a relative humidity of 50%, and the condition was adjusted. The charged voltage half-life (seconds) of the test piece was determined using a static Honest meter (H-0110 manufactured by Shido Electric Static Co., Ltd.). The smaller the value of the charged voltage half-life, the better the antistatic performance. The test piece was molded by an injection molding machine (SG-150U, manufactured by Sumitomo Heavy Industries, Ltd.) at a cylinder temperature of 300 ° C. and a mold temperature of 100 ° C.

[Examples 1-7, Comparative Examples 1-3]
Polycarbonate resin and non-fibrous carbon filler (excluding fibrous reinforcing filler) were premixed in blenders in the blending amounts shown in Table 1 and Table 2, and the resulting premixed mixture was bent with a diameter of 30 mmφ. Supplied to the first supply port (screw base) of a shaft extruder [Nippon Steel Works TEX30XSST] and melted at a cylinder temperature of 280 ° C., a screw rotation speed of 170 rpm, a discharge rate of 13 kg / h, and a vent pressure reduction of 3 kPa. Extruded and pelletized. The fibrous reinforcing filler was supplied to the extruder from the second supply port of the extruder using a side feeder. The first supply port here is a supply port farthest from the die, and the second supply port is a supply port located between the die of the extruder and the first supply port.

  The obtained pellets were dried with a hot air circulation dryer at 120 ° C. for 5 hours, and then a test piece for evaluation was molded using an injection molding machine. The evaluation results are shown in Tables 1 and 2.

Each component of the symbol notation in Table 1 and Table 2 is as follows.
(A component)
PC-1: Linear polycarbonate resin powder having a viscosity average molecular weight of 16000 (manufactured by Teijin Chemicals Ltd .: Panlite CM-1000)
PC-2: Linear polycarbonate resin powder having a viscosity average molecular weight of 19700 (manufactured by Teijin Chemicals Ltd .: Panlite L-1225WX)
PC-3: Linear polycarbonate resin powder having a viscosity average molecular weight of 22400 (manufactured by Teijin Chemicals Ltd .: Panlite L-1225WP)
(B component)
CB: Conductive carbon black (DBP oil absorption 495 ml / 100 g) [Ketjen Black EC-600JD (trade name) manufactured by Lion Corporation]
GR-1: flake graphite (average particle size 10 μm, fixed carbon content 99.0%, volatile content 0.6%, ash content 0.4%) [PB-99 (trade name) manufactured by Nishimura Graphite Co., Ltd.]
GR-2: scaly graphite (average particle size 25 μm, fixed carbon content 99.0%, volatile content 0.6%, ash content 0.4%) [PA-99 (trade name) manufactured by Nishimura Graphite Co., Ltd.]

(C component)
C-1: A flow modifier having a weight average molecular weight of 54,500 (manufactured by Mitsubishi Rayon Co., Ltd .: Metabrene KP4493). The flow modifier is an emulsified radical in which the monomer (Ca) is phenyl methacrylate, the monomer (Cb) is styrene, and the weight ratio of Ca to Cb (Ca: Cb) is 13:87. It was a random copolymer produced by a polymerization method. When 1 g of the copolymer was mixed with 10 ml of chloroform and stirred for 30 minutes, the copolymer was insoluble and contained substantially no crosslinked structure. Its molecular weight distribution (Mw / Mn) was 2.4.
C-2: A flow modifier having a weight average molecular weight of 115,000 (Mitsubrene Rayon Co., Ltd .: Metabrene KP4494). This flow modifier had the same configuration as C-1 except that the molecular weight was 115,000 and the molecular weight distribution was 2.6.
C-3 (for comparison): Flow modifier C-4 prepared by the following production method: In the production method of (C-3), phenyl methacrylate is used instead of butyl acrylate, and the weight ratio of phenyl methacrylate to styrene is A flow modifier having a weight average molecular weight of 42,000, prepared in the same manner as C-3 except that the ratio was 20:80

(GPC measurement of C-1 to C-4)
GPC measurement was performed in a clean air environment at a temperature of 23 ° C. and a relative humidity of 50%, and two columns of ResiPore (length 300 mm, inner diameter 7.5 mm) manufactured by Polymer Laboratories were connected in series as a column, chloroform as a mobile phase, Using a polymer laboratory Easy Cal PS-2 as a standard substance, a photodiode array detector at a wavelength of 254 nm as a detector, using chloroform as a developing solvent, a solution in which 10 mg of a sample was dissolved per 5 ml of chloroform was dissolved in GPC. 100 μl was injected into the measuring apparatus, GPC measurement was performed under conditions of a column temperature of 40 ° C. and a flow rate of 1 ml / min, the molecular weight of the flow modifier was measured, and the weight average molecular weight was calculated. The measuring apparatus is pump: L-6000 manufactured by Hitachi, Ltd., autosampler: L-7200 manufactured by Hitachi, Ltd., column oven: L-7300 manufactured by Hitachi, Ltd., photodiode array detector: (stock) ) L-2450 manufactured by Hitachi, Ltd.
(Manufacturing method of C-3)
A separable flask equipped with a condenser and a stirrer was charged with 1.0 part by weight of dipotassium alkenyl succinate (Ramtel ASK manufactured by Kao) and 290 parts by weight of distilled water as a solid content, and in a water bath at 80 ° C. in a nitrogen atmosphere. Until heated. Next, 0.0004 parts by weight of ferrous sulfate, 0.0012 parts by weight of ethylenediaminetetraacetate disodium salt and 0.5 parts by weight of Rongalite are dissolved in 5 parts by weight of distilled water, and then 10 parts by weight of butyl acrylate, allyl methacrylate are added. A mixture of 0.1 part by weight, 0.05 part by weight of tert-butyl hydroperoxide and 0.1 part by weight of n-octyl mercaptan was added dropwise over 18 minutes. The mixture was then stirred for 60 minutes to complete the first stage polymerization.
To this, 0.0004 parts by weight of ferrous sulfate, 0.0012 parts by weight of ethylenediaminetetraacetic acid disodium salt and 0.5 parts by weight of Rongalite were dissolved in 5 parts by weight of distilled water, and then 90 parts by weight of styrene, A mixture of 0.45 parts by weight of tert-butyl hydroperoxide and 1.8 parts by weight of n-octyl mercaptan was added dropwise over 162 minutes. The mixture was then stirred for 60 minutes to complete the second stage polymerization to obtain an emulsion. The solid content of the obtained emulsion was measured and found to be 24.2%. Moreover, when this emulsion was poured into dilute sulfuric acid aqueous solution and the resulting precipitate was dried, the weight average molecular weight (Mw) of the soluble component in chloroform was 28,000.

(Other ingredients)
(Reinforced filler)
CF: Carbon fiber (manufactured by Toho Tenax Co., Ltd .; Besfight HTA-C6-U, fiber diameter: 7 μm, cut length: 6 mm, epoxy-based sizing agent)
(Stabilizer)
TMP: Trimethyl phosphate (manufactured by Daihachi Chemical Industry Co., Ltd .: TMP (trade name))

It is the GPC chart of C-1 used in the Example. The horizontal axis is the retention time (minutes), and the vertical axis is the detection intensity.

Explanation of symbols

1 Peak of polymer component of flow modifier 2 Peak of dimer component of flow modifier 3 Peak of styrene monomer in flow modifier (content of styrene monomer calculated from the detected intensity of the peak is About 0.4% by weight)

Claims (5)

For a total of 100 parts by weight of aromatic polycarbonate resin (component A) 60 to 99 parts by weight and non-fibrous carbon filler (component B) 1 to 40 parts by weight, flow modifier (component C) 0.05 to 30 An aromatic polycarbonate resin composition comprising parts by weight, wherein the flow modifier (component C) is (i) a (meth) acrylic acid ester represented by the following general formula (1) and / or (2) A copolymer having only units formed from the monomer (Ca) and the aromatic alkenyl compound monomer (Cb) as constituent units, and (ii) the chloroform-soluble component has a weight-average molecular weight of 10,000. Antistatic aromatic polycarbonate resin composition which is -200,000.

(In the formula, R ¹ represents a hydrogen atom or a methyl group, and R ² represents a carbocyclic group itself or a hydrocarbon group composed of a carbon chain bonded to a carbocyclic ring.)

(In the formula, R ³ represents a hydrogen atom or a methyl group, R ⁴ represents a carbocyclic group itself or a hydrocarbon group composed of a carbon chain bonded to a carbocyclic ring, and n represents an integer of 1 to 4. )   2. The antistatic aromatic polycarbonate resin composition according to claim 1, wherein the component B is carbon black having a DBP oil absorption of 100 ml / 100 g to 500 ml / 100 g and / or graphite having an average particle diameter of 2 to 300 μm. The monomers in component C (Ca) are antistatic aromatic polycarbonate resin composition according to any one of claims 1 or 2 phenyl methacrylate. The antistatic aromatic polycarbonate resin composition according to any one of claims 1 to 3 , wherein the monomer (Cb) in the component C is styrene. For a total of 100 parts by weight of aromatic polycarbonate resin (component A) 60 to 99 parts by weight and non-fibrous carbon filler (component B) 1 to 40 parts by weight, flow modifier (component C) 0.05 to 30 A method for producing an antistatic aromatic polycarbonate resin composition having improved fluidity obtained by melt-kneading parts by weight, wherein the flow modifier (C component) is (i) the following general formula (1): And / or a copolymer comprising only units formed from the (meth) acrylic acid ester monomer (Ca) and the aromatic alkenyl compound monomer (Cb) represented by (2), ii) A method for producing an antistatic aromatic polycarbonate resin composition in which the chloroform-soluble component has a weight average molecular weight of 10,000 to 200,000.

(In the formula, R ¹ represents a hydrogen atom or a methyl group, and R ² represents a carbocyclic group itself or a hydrocarbon group composed of a carbon chain bonded to a carbocyclic ring.)

(In the formula, R ³ represents a hydrogen atom or a methyl group, R ⁴ represents a carbocyclic group itself or a hydrocarbon group composed of a carbon chain bonded to a carbocyclic ring, and n represents an integer of 1 to 4. )

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