JP2006249292A - Polycarbonate resin composition - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a polycarbonate resin composition having excellent moldability and processability and flame retardance, etc., resulting from both of the excellent melt tension and fluidity characteristics and combinedly having good compatibility free from layer release and good heat resistance and improved transparency by using a branched polycarbonate resin as a substrate. <P>SOLUTION: The polycarbonate resin composition is composed of (A) 100 pts.wt. branched polycarbonate resin containing 0.03-1 mol% recurring unit having branched structure and (B) 0.05-30 pts.wt. fluidity modifier. In the resin composition, (i) the fluidity modifier (component B) is a copolymer having a unit formed of a (meth)acrylate monomer (Ba) represented by a specific formula and an aromatic alkenyl compound monomer (Bb) as main unit and (ii) the weight average molecular weight of chloroform-soluble component of the the component B is 10,000-200,000. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

  The present invention relates to a polycarbonate resin composition comprising a branched polycarbonate having improved fluidity. More specifically, the present invention incorporates a specific flow modifier having good compatibility with the branched polycarbonate resin, thereby providing excellent moldability and flame retardancy due to the combined use of excellent melt tension and flow characteristics. The present invention relates to a polycarbonate resin composition having good compatibility and good compatibility with no delamination, good heat resistance, and improved transparency, and a method for producing the same.

  Polycarbonate resins are used in many applications such as mechanical parts, automobile parts, and electric / electronic parts because of their excellent properties such as mechanical strength and transparency. On the other hand, the properties of polycarbonate resin vary depending on its molecular weight, molecular weight distribution, amount of branching component, molecular chain terminal structure, and the like. Resins more suitable for various applications are used by utilizing such changes in properties.

  For example, by including a polycarbonate resin component having a very high molecular weight (for example, a component having a viscosity average molecular weight of about 100,000), the melt viscosity and elongational viscosity at a low shear rate range are increased, and this property is used for blow molding. Resin compositions with improved properties and anti-drip properties (flame retardancy based thereon) have already been proposed.

  Almost the same effect can be obtained by introducing a branched structure into the polycarbonate resin, and improvements in blow moldability and flame retardancy have been proposed and used.

  However, a polycarbonate resin having such a branched structure (hereinafter simply referred to as “branched polycarbonate resin”) has a high melt viscosity, for example, its fluidity is insufficient in injection molding. Such viscosity characteristics have restricted the shape of the molded product, the processing conditions, the hue of the molded product, and the like in extrusion molding and injection molding.

  A resin composition in which 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, which is compatible or compatible with the polycarbonate resin, is added to the polycarbonate resin is known (patents). Reference 1).

  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 in which the mass average molecular weight of a soluble component dissolved in chloroform is 10,000 to 100,000 (see Patent Document 2). 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 transparency and compatibility, and there is a need for further improvements in 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 publicly known that the coalescence is used as a compatibilizing agent for a polycarbonate resin and an ABS resin (see Patent Document 3).

  However, this publication does not disclose knowledge that is effective in improving the fluidity of the polycarbonate resin while maintaining the transparency of the polycarbonate resin and having good compatibility without delamination.

JP 2003-226802 A WO2003 / 072620 pamphlet JP-A-8-134144

  In view of the above, the object of the present invention is to use a branched polycarbonate resin as a base, have excellent molding processability and flame retardancy due to the combined use of excellent melt tension and flow characteristics, and good delamination-free An object of the present invention is to provide a polycarbonate resin composition having both compatibility, good heat resistance, and improved transparency. As a result of intensive studies to achieve the above object, the present inventors have found that this object can be achieved by using a flow modifier comprising a copolymer from a specific monomer. The present invention has been completed through investigation.

  According to the present invention, the above problems are as follows: (1) 100 parts by weight of a branched polycarbonate resin (component A) comprising 0.03 to 1 mol% of a repeating unit having a branched structure, and a flow modifier (component B) 0 A polycarbonate resin composition comprising 0.05 to 30 parts by weight, wherein the flow modifier (component B) is (i) (meth) acrylic represented by the following general formula (1) and / or (2) It is a copolymer having, as a main constituent unit, a unit formed from an acid ester monomer (Ba) and an aromatic alkenyl compound monomer (Bb), and (ii) its chloroform-soluble component has a weight average molecular weight of 10 It is achieved by a polycarbonate resin composition that is 2,000 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 ratio of the monomer (Ba) and the monomer (Bb) in the B component is such that the total of both is 80% by weight or more in 100% by weight of the B component, It is preferable that Ba) is 1 to 80% by weight and the monomer (Bb) is 20 to 99% by weight.

  The monomer (Ba) in the component B is preferably phenyl methacrylate, and the monomer (Bb) in the component B is preferably styrene.

  Moreover, the said subject is 0.05-30 weight part of flow modifiers (B component) with respect to 100 weight part of branched polycarbonate resin (A component) which contains 0.03-1 mol% of repeating units which have a branched structure. A method for producing a polycarbonate resin composition having improved fluidity obtained by melting and kneading a part, wherein the flow modifier (component B) comprises (i) the following general formula (1) and / or (2 ) Represented by (meth) acrylic acid ester monomer (Ba) and aromatic alkenyl compound monomer (Bb). The weight average molecular weight of the soluble component is 10,000 to 200,000, which is solved by a method for producing a polycarbonate resin composition with improved fluidity.

Hereinafter, the details of the present invention will be described.
(Component A: Branched polycarbonate resin)
The branched polycarbonate resin used as the component A in the present invention is obtained by copolymerizing a polyfunctional aromatic compound in the reaction of a dihydric phenol and a carbonate precursor, or a polyfunctional aromatic compound. It contains a branched structure by side reaction without being present. 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. In the interfacial polymerization method, it is usually necessary to copolymerize a polyfunctional aromatic compound. In the melt transesterification method, a branched structure tends to occur as a side reaction.

  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. Among them, bisphenol A is particularly preferred because of excellent toughness and excellent transparency in a preferred embodiment of the present invention.

  In the present invention, in addition to the bisphenol A-based polycarbonate, a special polycarbonate produced using other dihydric phenols can be used 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 a polycarbonate resin by interfacial polymerization of the above dihydric phenol and carbonate precursor, a catalyst, a terminal terminator, an antioxidant for preventing the dihydric phenol from being oxidized, etc., as necessary. May be used. In addition, polyester carbonate resins copolymerized with aromatic or aliphatic (including alicyclic) difunctional carboxylic acids, copolymerized polycarbonate resins copolymerized with bifunctional alcohols (including alicyclic), and such bifunctional compounds A polyester carbonate resin copolymerized with a functional carboxylic acid and a difunctional alcohol. Moreover, the mixture which mixed 2 or more types of the obtained polycarbonate resin may be sufficient.

  The branched polycarbonate resin increases the melt tension of the resin composition and can improve the moldability in extrusion molding, foam molding and blow molding based on such properties.

  Examples of the trifunctional or higher polyfunctional aromatic compound used in the branched polycarbonate resin include 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, and 4- {4- [1,1- Trisphenol such as bis (4-hydroxyphenyl) ethyl] benzene} -α, α-dimethylbenzylphenol is preferably exemplified. Other polyfunctional aromatic compounds include phloroglucin, phloroglucid, tetra (4-hydroxyphenyl) methane, bis (2,4-dihydroxyphenyl) ketone, 1,4-bis (4,4-dihydroxytriphenylmethyl) benzene. And trimellitic acid, pyromellitic acid, benzophenone tetracarboxylic acid, and acid chlorides thereof. Of these, 1,1,1-tris (4-hydroxyphenyl) ethane and 1,1,1-tris (3,5-dimethyl-4-hydroxyphenyl) ethane are preferable, and 1,1,1-tris (4- Hydroxyphenyl) ethane is preferred.

  The structural unit derived from the polyfunctional aromatic compound in the branched polycarbonate resin is 0 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. 0.03 to 1 mol%, preferably 0.07 to 0.7 mol%, particularly preferably 0.1 to 0.4 mol%.

Further, such a branched structural unit is not only derived from a polyfunctional aromatic compound but also derived without using a polyfunctional aromatic compound, such as a side reaction during a melt transesterification reaction. Also good. The ratio of such a 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, and linear saturated aliphatic dicarboxylic acids such as icosanedioic acid, and cyclohexanedicarboxylic acid. Preferred are alicyclic dicarboxylic acids such as acids. 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. In addition, 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 salts, alkaline earth metal salts, quaternary ammonium salts, alkoxides of alkali metals and alkaline earth metals, organic acid salts of alkali metals and alkaline earth metals, zinc compounds, boron compounds, silicon compounds, germanium compounds, Examples thereof include catalysts usually used for esterification reactions and transesterification reactions such as organic tin compounds, lead compounds, antimony compounds, manganese compounds, titanium compounds, and zirconium compounds. 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 polycarbonate resin after polymerization. Preferred examples of the deactivator include phosphonium salts such as tetrabutylphosphonium dodecylbenzenesulfonate and ammonium salts such as tetraethylammonium dodecylbenzyl sulfate.

  The details of reaction formats other than those described above are also well known in various known documents and patent publications.

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

  In the case of a polycarbonate resin having a viscosity average molecular weight of less than 10,000, practically sufficient mechanical strength may not be obtained. On the other hand, a resin composition obtained from a polycarbonate resin having a viscosity average molecular weight exceeding 50,000 has a high melt viscosity, and generally requires a high molding processing temperature or requires a special molding method, so that it is versatile. Inferior. A high molding temperature tends to cause a decrease in the rheological properties of the resin composition.

  The polycarbonate resin may be obtained by mixing those having a viscosity average molecular weight outside the above range. In particular, a polycarbonate resin having a viscosity average molecular weight exceeding the above range (50,000) increases the melt tension of the resin composition of the present invention, and molding processing in extrusion molding, foam molding and blow molding based on such characteristics. Can improve sex.

The viscosity average molecular weight referred to in the present invention is first determined by using an Ostwald viscometer from a solution in which 0.7 g of polycarbonate resin is dissolved in 100 ml of methylene chloride at 20 ° C., with a specific viscosity (η _SP ) calculated by the following formula:
Specific viscosity (η _SP ) = (t−t ₀ ) / t ₀
[T ₀ is the drop time of methylene chloride, t is the drop time of the sample solution]
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

(B component: flow modifier)
The flow modifier (component B) of the present invention comprises (i) a (meth) acrylic acid ester monomer (Ba) represented by the following general formula (1) and / or (2) and an aromatic alkenyl compound. (Ii) a chloroform-soluble component having 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 (Ba) and the monomer (Bb). However, in the production of a copolymer, it is unavoidable that a polymer consisting of not only a monomer but also a monomer is formed. In the present invention, the monomer (Ba) or the monomer (Bb) 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 the flow modifier (component B) of the present invention, the ratio of the monomer (Ba) and the monomer (Bb) is 100% by weight of the B component in consideration of the balance between fluidity and mechanical properties. % Is preferably 80% by weight or more, more preferably 90% by weight or more, still more preferably 95% by weight or more. Further, in the total of 100% by weight of both, the monomer (Ba) is preferably 1 to 80% by weight. And the monomer (Bb) is 20 to 99% by weight, more preferably the monomer (Ba) is 3 to 50% by weight and the monomer (Bb) is 50 to 97% by weight, still more preferably The monomer (Ba) is 5 to 30% by weight and the monomer (Bb) is 70 to 95% by weight, most preferably the monomer (Ba) is 5 to 20% by weight and the monomer (Bb). Is 80 to 95% by weight.

  When the amount of the monomer (Ba) is less than the lower limit of the above range, it becomes difficult to achieve improvement in delamination or compatibility with the flow reforming effect. When the amount of the monomer (Ba) 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 (Ba) and a monomer (Bb) is a non-crosslinked copolymer. For example, when 10 ml of chloroform and 1 g of a flow modifier (component B) 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.

  The copolymer of the B component has a weight average molecular weight of 10,000 to 200,000 of the chloroform-soluble component excluding a part of the solvent-insoluble crosslinked structure. 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 soluble component in chloroform is mainly composed of a non-crosslinked copolymer composed of the monomer (Ba) and the monomer (Bb). A polymer of a monomer (Ba) or a monomer (Bb) 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 B 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 (Ba) is A and the polymer unit of the monomer (Bb) 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 (Ba) and the monomer (Bb) is AB, it may be a block copolymer in which either A or B is substituted with AB. . 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 method for producing the copolymer of component B 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) acrylic acid ester monomer (Ba) represented by the general formula (1) and / or (2), and aromatic. A copolymer is added to the alkenyl compound monomer (Bb) and optionally a mixture of other monomers, a polymerization initiator, a chain transfer agent, etc., if necessary, and polymerized 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 (Ba) represented by the general formula (1) and / or (2) is a carbon ring in the molecule, that is, a carbon ring itself, or a carbon having a carbocycle 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 the B component of the present invention is mainly composed of the (meth) acrylate monomer (Ba) and the aromatic alkenyl compound monomer (Bb) 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 B component copolymer.

  Examples of the aromatic alkenyl compound monomer (Bb) 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 (Bb). In a most preferred embodiment, the total amount of the monomer (Bb) is styrene.

  If the molecular weight distribution of the copolymer of component B is too wide, the flowability of the resin composition is decreased, or relatively low molecular weight is increased. 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 B 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 B is a graft copolymer will be described. A preferred embodiment when the B component of the present invention is a graft copolymer is a graft copolymer obtained by graft polymerization of the monomer (Bb) in the presence of the polymer formed from the monomer (Ba). A graft copolymer obtained by graft polymerization of a monomer (Ba) in the presence of a polymer or a polymer formed from the monomer (Bb). In any embodiment, such a graft copolymer is more preferably produced using a macromonomer formed from the monomer (Ba) or a macromonomer formed from the monomer (Bb) 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 (Ba) or monomer (Bb). 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 (Bb). 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)
In the present invention, based on 100 parts by weight of the component A, the content of the component B is 0.05 to 30 parts by weight, preferably 1 to 15 parts by weight, more preferably 2 to 9 parts by weight. If the content of component B is less than 0.05 parts by weight, the improvement of fluidity is insufficient, and if it exceeds 30 parts by weight, the compatibility, heat resistance, and mechanical properties are lowered.

(Other additives)
In the polycarbonate resin composition of the present invention, various stabilizers and coloring materials can be used 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.

  Specifically, as the phosphite compound, for example, triphenyl phosphite, tris (nonylphenyl) phosphite, tridecyl phosphite, trioctyl phosphite, trioctadecyl phosphite, didecyl monophenyl phosphite, dioctyl monophenyl Phosphite, diisopropyl monophenyl phosphite, monobutyl diphenyl phosphite, monodecyl diphenyl phosphite, monooctyl diphenyl phosphite, tris (diethylphenyl) phosphite, tris (di-iso-propylphenyl) phosphite, tris (di -N-butylphenyl) phosphite, tris (2,4-di-tert-butylphenyl) phosphite, tris (2,6-di-tert-butylphenyl) phosphite, dis Allyl pentaerythritol diphosphite, bis (2,4-di-tert-butylphenyl) pentaerythritol diphosphite, bis (2,6-di-tert-butyl-4-methylphenyl) pentaerythritol diphosphite, bis (2,6-di-tert-butyl-4-ethylphenyl) pentaerythritol diphosphite, bis {2,4-bis (1-methyl-1-phenylethyl) phenyl} pentaerythritol diphosphite, phenylbisphenol A Examples include pentaerythritol diphosphite, bis (nonylphenyl) pentaerythritol diphosphite, and dicyclohexyl pentaerythritol diphosphite.

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

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

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

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

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

  The phosphorus stabilizers can be used alone or in combination of two or more. Among the phosphorus stabilizers, phosphonite compounds or phosphite compounds represented by the following general formula (3) are preferable.

（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.

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

(Ii) Hindered phenolic antioxidant As the hindered phenolic compound, various compounds that are usually blended in a resin can be used. Examples of such hindered phenol compounds include α-tocopherol, butylhydroxytoluene, sinapyl alcohol, vitamin E, octadecyl-3- (3,5-di-tert-butyl-4-hydroxyphenyl) propionate, 2-tert -Butyl-6- (3'-tert-butyl-5'-methyl-2'-hydroxybenzyl) -4-methylphenyl acrylate, 2,6-di-tert-butyl-4- (N, N-dimethylamino) Methyl) phenol, 3,5-di-tert-butyl-4-hydroxybenzylphosphonate diethyl ester, 2,2'-methylenebis (4-methyl-6-tert-butylphenol), 2,2'-methylenebis (4-ethyl) -6-tert-butylphenol), 4,4'-methylenebis (2,6 Di-tert-butylphenol), 2,2′-methylenebis (4-methyl-6-cyclohexylphenol), 2,2′-dimethylene-bis (6-α-methyl-benzyl-p-cresol), 2,2 ′ -Ethylidene-bis (4,6-di-tert-butylphenol), 2,2'-butylidene-bis (4-methyl-6-tert-butylphenol), 4,4'-butylidenebis (3-methyl-6-tert) -Butylphenol), triethylene glycol-N-bis-3- (3-tert-butyl-4-hydroxy-5-methylphenyl) propionate, 1,6-hexanediol bis [3- (3,5-di- tert-butyl-4-hydroxyphenyl) propionate], bis [2-tert-butyl-4-methyl 6- (3-tert-butyl) Ru-5-methyl-2-hydroxybenzyl) phenyl] terephthalate, 3,9-bis {2- [3- (3-tert-butyl-4-hydroxy-5-methylphenyl) propionyloxy] -1,1, -Dimethylethyl} -2,4,8,10-tetraoxaspiro [5,5] undecane, 4,4'-thiobis (6-tert-butyl-m-cresol), 4,4'-thiobis (3- Methyl-6-tert-butylphenol), 2,2′-thiobis (4-methyl-6-tert-butylphenol), bis (3,5-di-tert-butyl-4-hydroxybenzyl) sulfide, 4,4 ′ -Di-thiobis (2,6-di-tert-butylphenol), 4,4'-tri-thiobis (2,6-di-tert-butylphenol), 2,2-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.

  Either of the phosphorus stabilizer and the hindered phenol antioxidant is preferably blended, and the combination of these is more preferred. More preferably, 0.01 to 0.3 parts by weight of a phosphorus stabilizer and 0.01 to 0.3 parts by weight of a hindered phenol antioxidant are blended based on 100 parts by weight of component A. .

(Iii) Blueing agent The polycarbonate resin composition of the present invention preferably further comprises 0.05 to 3.0 ppm (weight ratio) of a blueing agent in the resin composition. The use of a bluing agent is very effective for imparting a natural transparency to a molded product. Here, the bluing agent refers to a colorant that exhibits a blue or purple color by absorbing light of orange or yellow color, and a dye is particularly preferable. By adding the bluing agent, the polycarbonate resin composition of the present invention can obtain a better hue. If the amount of the bluing agent is less than 0.05 ppm, the effect of improving the hue may be insufficient. On the other hand, if it exceeds 3.0 ppm, the light transmittance decreases, which is not appropriate. A more preferable amount of bluing agent is in the range of 0.2 to 2.0 ppm in the resin composition. Representative examples of bluing agents include Macrolex Violet B and Macrolex Blue RR from Bayer, and Polysynthrene Blue RLS from Clariant.

(Iv) Release agent It is preferable to add a release agent to the polycarbonate resin composition of the present invention for the purpose of improving productivity at the time of molding and reducing distortion of the molded product. Known release agents can be used. For example, saturated fatty acid ester, unsaturated fatty acid ester, polyolefin wax (polyethylene wax, 1-alkene polymer, etc., which may be modified with a functional group-containing compound such as acid modification), silicone compound, fluorine compound ( And fluorine oil represented by polyfluoroalkyl ether), paraffin wax, beeswax and the like. The release agent is preferably 0.005 to 2 parts by weight based on 100 parts by weight of component A.

  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 0.5 parts by weight based on 100 parts by weight of the component A. It is. In such a range, the polycarbonate resin composition has good release properties and release properties. In particular, such an amount of fatty acid ester provides a polycarbonate resin composition having good mold release and roll release properties without impairing good hue and transparency.

(V) Ultraviolet Absorber The polycarbonate resin composition of the present invention can contain an ultraviolet absorber. Since the resin composition of the present invention is excellent in transparency, it is very suitable for use in transmitting light.

  Specific examples of the ultraviolet absorber of the present invention include, for example, 2,4-dihydroxybenzophenone, 2-hydroxy-4-methoxybenzophenone, 2-hydroxy-4-octoxybenzophenone, 2-hydroxy-4 in the benzophenone series. -Benzyloxybenzophenone, 2-hydroxy-4-methoxy-5-sulfoxybenzophenone, 2-hydroxy-4-methoxy-5-sulfoxytrihydridolate benzophenone, 2,2'-dihydroxy-4-methoxybenzophenone, 2, 2 ′, 4,4′-tetrahydroxybenzophenone, 2,2′-dihydroxy-4,4′-dimethoxybenzophenone, 2,2′-dihydroxy-4,4′-dimethoxy-5-sodiumsulfoxybenzophenone, bis (5-benzoyl-4-hydro Shi-2-methoxyphenyl) methane, 2-hydroxy -4-n-dodecyloxy benzoin phenone, and 2-hydroxy-4-methoxy-2'-carboxy benzophenone may be exemplified.

  Specific examples of the ultraviolet absorber include, for example, 2- (2-hydroxy-5-methylphenyl) benzotriazole and 2- (2-hydroxy-5-tert-octylphenyl) benzotriazole in the benzotriazole series. 2- (2-hydroxy-3,5-dicumylphenyl) phenylbenzotriazole, 2- (2-hydroxy-3-tert-butyl-5-methylphenyl) -5-chlorobenzotriazole, 2,2′- Methylenebis [4- (1,1,3,3-tetramethylbutyl) -6- (2H-benzotriazol-2-yl) phenol], 2- (2-hydroxy-3,5-di-tert-butylphenyl) ) Benzotriazole, 2- (2-hydroxy-3,5-di-tert-butylphenyl) -5-chlorobenzotriazol 2- (2-hydroxy-3,5-di-tert-amylphenyl) benzotriazole, 2- (2-hydroxy-5-tert-octylphenyl) benzotriazole, 2- (2-hydroxy-5- tert-butylphenyl) benzotriazole, 2- (2-hydroxy-4-octoxyphenyl) benzotriazole, 2,2'-methylenebis (4-cumyl-6-benzotriazolephenyl), 2,2'-p -Phenylenebis (1,3-benzoxazin-4-one), and 2- [2-hydroxy-3- (3,4,5,6-tetrahydrophthalimidomethyl) -5-methylphenyl] benzotriazole, and 2- (2'-Hydroxy-5-methacryloxyethylphenyl) -2H-benzotriazole and co-polymerized with the monomer 2 such as a copolymer with a possible vinyl monomer and a copolymer of 2- (2′-hydroxy-5-acryloxyethylphenyl) -2H-benzotriazole with a vinyl monomer copolymerizable with the monomer Examples include polymers having a -hydroxyphenyl-2H-benzotriazole skeleton.

  Specific examples of the ultraviolet absorber include 2- (4,6-diphenyl-1,3,5-triazin-2-yl) -5-hexyloxyphenol and 2- (4) in hydroxyphenyltriazine series. , 6-Diphenyl-1,3,5-triazin-2-yl) -5-methyloxyphenol, 2- (4,6-diphenyl-1,3,5-triazin-2-yl) -5-ethyloxy Phenol, 2- (4,6-diphenyl-1,3,5-triazin-2-yl) -5-propyloxyphenol, and 2- (4,6-diphenyl-1,3,5-triazine-2- Yl) -5-butyloxyphenol and the like. Furthermore, the phenyl group of the above exemplary compounds such as 2- (4,6-bis (2,4-dimethylphenyl) -1,3,5-triazin-2-yl) -5-hexyloxyphenol is 2,4-dimethyl. Examples of the compound are phenyl groups.

  As the ultraviolet absorber, specifically, in the cyclic imino ester type, for example, 2,2′-p-phenylenebis (3,1-benzoxazin-4-one), 2,2 ′-(4,4′-diphenylene) ) Bis (3,1-benzoxazin-4-one), 2,2 ′-(2,6-naphthalene) bis (3,1-benzoxazin-4-one) and the like.

  Further, as the ultraviolet absorber, specifically, for cyanoacrylate, for example, 1,3-bis-[(2′-cyano-3 ′, 3′-diphenylacryloyl) oxy] -2,2-bis [(2- Examples include cyano-3,3-diphenylacryloyl) oxy] methyl) propane and 1,3-bis-[(2-cyano-3,3-diphenylacryloyl) oxy] benzene.

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

  Of these, benzotriazoles and hydroxyphenyltriazines are preferred from the viewpoint of ultraviolet absorbing ability, and cyclic iminoesters and cyanoacrylates are preferred from the viewpoint of heat resistance and hue (transparency). You may use the said ultraviolet absorber individually or in mixture of 2 or more types.

  The content of the ultraviolet absorber is 0.01 to 2 parts by weight, preferably 0.03 to 2 parts by weight, more preferably 0.02 to 1 part by weight, more preferably 0, based on 100 parts by weight of the component A. 0.05 to 0.5 parts by weight.

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

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

  Examples of dyes other than the above bluing agents and fluorescent dyes include perylene dyes, coumarin dyes, thioindigo dyes, anthraquinone dyes, thioxanthone dyes, ferrocyanides such as bitumen, perinone dyes, quinoline dyes, quinacridone And dyes such as dyes, dioxazine dyes, isoindolinone dyes, and phthalocyanine dyes. Furthermore, the resin composition of this invention can mix | blend a metallic pigment, and can also obtain a better metallic color. As the metallic pigment, those having a metal film or a metal oxide film on various plate-like fillers are suitable.

  The content of the dye / pigment is preferably 0.00001 to 1 part by weight, more preferably 0.00005 to 0.5 part by weight, based on 100 parts by weight of the component A.

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

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

(Viii) Compound having heat ray absorbing ability The polycarbonate resin composition of the present invention may contain a compound having heat ray absorbing ability. A polycarbonate resin composition in which such a compound is blended can suppress an increase in temperature in the room. Such a polycarbonate resin composition is particularly suitable for use in resin window glass for vehicles and resin window sash glass.

  Such compounds include phthalocyanine-based near-infrared absorbers, metal oxide-based near-infrared absorbers such as ATO, ITO, iridium oxide and ruthenium oxide, and metal boride-based near infrared rays such as lanthanum boride, cerium boride and tungsten boride. Preferred examples include various metal compounds having excellent near-infrared absorption ability such as an absorber, and carbon filler. As such a phthalocyanine-based near infrared absorber, for example, MIR-362 manufactured by Mitsui Chemicals, Inc. is commercially available and easily available. Examples of carbon fillers include carbon black, graphite (including both natural and artificial, and whiskers), carbon fibers (including those produced by vapor phase growth), carbon nanotubes, and fullerenes, preferably carbon. Black and graphite. These can be used alone or in combination of two or more. The content of the phthalocyanine-based near-infrared absorber is preferably 0.0005 to 0.2 parts by weight, more preferably 0.0008 to 0.1 parts by weight, based on 100 parts by weight of component A, 0.001 to 0 0.07 part by weight is more preferable. The content of the metal oxide near-infrared absorber, the metal boride-based near infrared absorber, and the carbon filler is preferably in the range of 0.1 to 200 ppm (weight ratio) in the resin composition of the present invention. A range of ˜100 ppm is more preferable.

(Ix) Light Diffusing Agent The polycarbonate resin composition of the present invention can be provided with a light diffusing effect by blending a light diffusing agent. Examples of the light diffusing agent include polymer fine particles, low refractive index inorganic fine particles, and composites thereof. Such polymer fine particles are fine particles that are already known as light diffusing agents for polycarbonate resins. More preferably, acrylic crosslinked particles having a particle size of several μm, silicone crosslinked particles represented by polyorganosilsesquioxane, and the like are exemplified. Examples of the shape of the light diffusing agent include a spherical shape, a disk shape, a column shape, and an indefinite shape. Such spheres need not be perfect spheres, but include deformed ones, and such columnar shapes include cubes. A preferred light diffusing agent is spherical, and the more uniform the particle size is. The content of the light diffusing agent is preferably 0.005 to 20 parts by weight, more preferably 0.01 to 10 parts by weight, still more preferably 0.01 to 3 parts by weight, based on 100 parts by weight of the component A. . Two or more light diffusing agents can be used in combination.

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

(Xi) Flame Retardant The polycarbonate resin composition of the present invention may be blended with various compounds known as flame retardants for polycarbonate resins. Since the branched polycarbonate resin of the present invention is also excellent in drip prevention during combustion, the blending of the flame retardant exhibits such characteristics more effectively. At the same time, the flame retardant performance required due to the insufficient fluidity of the conventional branched polycarbonate resin could not be fully utilized, and the polycarbonate resin composition of the present invention has improved the fluidity. Can be applied to a wider range of applications. 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 property, 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.).

(Xi-i) 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 and light resistance. 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 compounding 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, still more preferably 0.00 based on 100 parts by weight of the component A. 008 to 0.13 parts by weight. 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) sulfonate metal salt, the content is 0.001 to 1 part by weight based on 100 parts by weight of component A, more preferably 0.005 to 0.5. Part by weight, more preferably 0.01 to 0.1 part by weight.

(Xi-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-dihydroxydiphenylbis (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.).

(Xi-iii) Silicone Flame Retardant The silicone compound used as the silicone 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 organic residues 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.)

(Xi-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.

(Xii) Anti-dripping agent The polycarbonate resin composition of the present invention may contain an anti-dripping agent. By using such a dripping inhibitor in combination with the above flame retardant, better flame retardancy can be obtained. It also has the function of further improving the rheological properties based on the good melt tension of the branched polycarbonate resin. 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 No. 11-29679) 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 transparency of the polycarbonate resin composition of the present invention, the fibrillated PTFE is preferably finely dispersed as much 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 100 parts by weight of the component A.

(Xiii) Reinforcing filler Various known fillers can be blended in the polycarbonate resin composition of the present invention as a reinforcing filler. Since the polycarbonate resin composition of the present invention has good transparency, a polycarbonate resin composition having a good hue can be obtained by blending an appropriate reinforcing filler. As such a reinforcing filler, a silicate mineral filler or glass filler with high whiteness is preferable. Examples of such silicate mineral fillers include talc, mascobite mica, synthetic fluorine mica, smectite, and wollastonite. Examples of the glass filler include glass fiber, glass flake, and glass milled fiber. 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.

  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 up to 100 parts by weight based on 100 parts by weight of component A. The upper limit is preferably 25 parts by weight, more preferably 20 parts by weight. When the amount of reinforcing filler is too large, the fluid reforming effect tends to be insufficient.

(Xiv) Antistatic Agent The 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 based on 100 parts by weight of the component A, preferably 0.05 to 5 parts by weight, more preferably 1 to 3.5 parts by weight, still more preferably. The range is 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, more preferably based on 100 parts by weight of the component A. 0.005 to 0.2 part by weight. 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 100 parts by weight of component A. 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 100 parts by weight of component A.

(Xv) Other additives The polycarbonate resin composition of the present invention includes a thermoplastic resin other than the components A and B, a rubber polymer, other flow modifiers, an antibacterial agent, a dispersant such as liquid paraffin, A photocatalytic antifouling agent, a heat ray absorbent, a photochromic agent, and the like can be blended.

  Examples of the thermoplastic resin other than the A component and the B component include styrene resins excluding the B 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 20 parts by weight or less, more preferably 10 parts by weight or less based on 100 parts by weight of the component A.

(Haze value)
The polycarbonate resin composition of the present invention is preferably a smooth plate having a thickness of 2 mm having an arithmetic average roughness (Ra) of 0.03 μm, and having a haze measured by JIS K7105 of 0.3 to 3 μm. It satisfies 20%, more preferably 0.3 to 5%, still more preferably 0.3 to 3%. The haze value is measured using a haze meter. Such a smooth flat plate is obtained by subjecting the pellets to predetermined drying, and then injection-molding the pellets into a cavity constituted by a mold surface having an arithmetic average roughness (Ra) of 0.03 μm. The arithmetic average roughness (Ra) of the mold surface can be measured using a surface roughness meter.

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

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

  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 manufactured to produce a master batch of the additive diluted with the powder. The method of using a master batch is 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 screens include wire meshes, screen changers, sintered metal plates (disk filters, etc.) 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 disks 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.

  Also, master pellets are prepared by melting and kneading the A component and the B component with a melt kneader in advance so as to contain the high concentration B component of the present invention, and the master pellet is added to the remaining A component and other additions The method of mixing with an agent and pelletizing with a melt kneader is mentioned. Furthermore, it is possible to obtain a polycarbonate resin composition that satisfies the requirements of the present invention by using a polycarbonate resin that does not contain a branched structure as the polycarbonate resin of the master pellet and melt-kneading the master pellet with the branched polycarbonate resin. It is.

  The 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 polycarbonate resin composition of the present invention can also be used in the form of various shaped extrusions, sheets, films, etc. 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 polycarbonate resin composition of the present invention can be formed into a molded product by rotational molding or blow molding.

  As a result, it has excellent molding processability and flame retardancy due to the combination of excellent melt tension and flow characteristics, good compatibility without delamination, good heat resistance, and improved transparency Polycarbonate resin composition that has both excellent melt tension and fluidity, and has excellent moldability and flame retardancy due to the combination of excellent melt tension and fluidity, and good compatibility without delamination and good heat resistance And a molded article of a polycarbonate resin composition having both improved transparency. That is, according to the present invention, a polycarbonate resin composition obtained by blending 0.05 to 30 parts by weight of the B component with respect to 100 parts by weight of the A component, preferably a molded article having light transmittance. Is provided.

  Specific examples of the molded article in which the resin composition of the present invention is used include an illumination lamp cover, an electronic circuit board cover, a resin window glass, a window glass dew condensation prevention film, a solar cell cover, a projection display cover and a lenticular lens, Roof materials for buildings and vehicles, dummy bottles, protective covers for flat panel display devices, IC magazine cases, silicon wafer containers, glass substrate storage containers, optical disk cartridge cases, static eliminators for copying machines, light guide plates, carrier tapes, etc. Is exemplified. The IC magazine case is preferably a profile extrusion molded product.

  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 polycarbonate resin composition of the present invention has excellent molding processability and flame retardancy due to the combined use of excellent melt tension and flow characteristics, and good compatibility without delamination and good heat resistance. As described above, it is widely useful in various fields such as buildings, building materials, agricultural materials, marine materials, vehicles, electric / electronic devices, machines, 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 inventors 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) Transparency of molded product: An injection molding machine (Sumitomo Heavy Industries, Ltd.) using a mold having a cavity surface with an arithmetic average roughness (Ra) of 0.03 μm. SG-150U) manufactured under the conditions of a cylinder temperature of 290 ° C. and a mold temperature of 80 ° C., a width of 50 mm, a length of 90 mm and a thickness of 3 mm (length 20 mm) and 2 mm (length) from the gate side in a molding cycle of 50 seconds. A three-stage plate having a length of 45 mm) and 1 mm (length 25 mm) was molded. The total light transmittance and Haze of the molded plate having a thickness of 2.0 mm of the three-stage plate were measured according to ASTM D1003. Haze is the turbidity of the molded product. The lower the value, the less turbidity.
(Ii) Delamination resistance: A tensile fracture test was conducted according to ASTM D638, 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. The test pieces were molded by an injection molding machine (SG-150U, manufactured by Sumitomo Heavy Industries, Ltd.) at a cylinder temperature of 290 ° C. and a mold temperature of 80 ° C.
(Iii) Fluidity: 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 290 ° C., a mold temperature of 70 ° C., and an injection pressure of 100 MPa.
(Iv) Drawdown property: The drawdown property was evaluated by extruding a parison from a die of a blow molding machine and measuring the parison weight 30 cm below the die. In this case, a large parison weight is preferable. In the test, the pellets were dried at 120 ° C. for 5 hours, and then a parison was formed using a blow molding machine [Sumitomo Becombe SE51 / BA2 manufactured by Sumitomo Heavy Industries, Ltd.]. The blow molding machine used had a screw diameter of 50 mmφ, a die outer diameter of 60 mmφ, and a die inner diameter of 56 mmφ. The extrusion temperature (cylinder and die) was 290 ° C. and the screw rotation speed was 20 rpm.

[Examples 1-7, Comparative Examples 1-3]
Various additives listed in Table 1 were mixed in 100 parts by weight of the polycarbonate resin with blenders in respective blending amounts, and then melt-kneaded using a vent type twin screw extruder to obtain pellets. The additives to be added to the polycarbonate resin were preliminarily prepared with a polycarbonate resin in advance with a concentration of 10 to 100 times the blending amount as a guide, and then the whole was mixed by a blender. The vent type twin screw extruder used was TEX30α (completely meshing, rotating in the same direction, two-thread screw) manufactured by Nippon Steel Works. The kneading zone was of one type before the vent opening. Extrusion conditions were a discharge rate of 20 kg / h, a screw rotation speed of 140 rpm, a vent vacuum of 3 kPa, and an extrusion temperature of 270 ° C. from the first supply port to the die part.
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 Table 1.

Each component indicated by symbols in Table 1 is as follows.
(A component)
PC-1: a branched polycarbonate resin containing 0.3 mol% of a repeating unit having a branched structure having a viscosity average molecular weight of 25,500 (manufactured by Teijin Chemicals Ltd .: Panlite Z-2600W)
PC-2: Linear polycarbonate resin powder having a branched structure with a viscosity average molecular weight of 19,700 (manufactured by Teijin Chemicals Ltd .: Panlite L-1225WX)

(B component)
B-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 (Ba) is phenyl methacrylate, the monomer (Bb) 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.
B-2: A flow modifier having a weight average molecular weight of 115,000 (Mitsubishi Rayon Co., Ltd .: Metabrene KP4494). The flow modifier had the same configuration as B-1 except that the molecular weight was 115,000 and the molecular weight distribution was 2.6.
B-3 (for comparison): Flow modifier B-4 prepared by the following production method: In the production method of (B-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 B-3, except that the ratio is 20:80

(GPC measurement of B-1 to B-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 B-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)
IRGP: Phosphite compound (Irgafos 168 manufactured by Ciba Specialty Chemicals)
EPQ: Phosphorus stabilizer mainly composed of phosphonite (Sandstab P-EPQ manufactured by Clariant Japan)
PEP-8: Pentaerythritol diphosphite-type phosphorus stabilizer (Asahi Denka Kogyo Co., Ltd .: ADK STAB PEP-8)
AO-80: 3,9-bis [2- {3- (3-tert-butyl-4-hydroxy-5-methylphenyl) propionyloxy} -1,1-dimethylethyl] -2,4,8,10 -A hindered phenolic antioxidant composed of tetraoxaspiro [5,5] undecane (Asahi Denka Kogyo Co., Ltd .: ADK STAB AO-80)
EW: Full ester of pentaerythritol and aliphatic carboxylic acid (mainly stearic acid and palmitic acid) having an acid value of 9 (manufactured by Riken Vitamin Co., Ltd .: Riquester EW-400, hydroxyl value: 6, iodine value) : 0.4)

It is a GPC chart of B-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)

A polycarbonate resin composition comprising 100 parts by weight of a branched polycarbonate resin (component A) containing 0.03 to 1 mol% of a repeating unit having a branched structure and 0.05 to 30 parts by weight of a flow modifier (component B). The flow modifier (component B) comprises (i) a (meth) acrylic acid ester monomer (Ba) and an aromatic alkenyl compound represented by the following general formula (1) and / or (2): (Ii) A polycarbonate resin composition having a chloroform-soluble component having a weight average molecular weight of 10,000 to 200,000, which is a copolymer mainly composed of units formed from the monomer (Bb).

(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. )   The ratio of the monomer (Ba) and the monomer (Bb) in the B component is such that the total of both is 80% by weight or more in 100% by weight of the B component, The polycarbonate resin composition according to claim 1, wherein Ba) is 1 to 80% by weight and monomer (Bb) is 20 to 99% by weight.   The polycarbonate resin composition according to claim 1, wherein the monomer (Ba) in the component B is phenyl methacrylate.   The polycarbonate resin composition according to claim 1, wherein the monomer (Bb) in the component B is styrene. With respect to 100 parts by weight of a branched polycarbonate resin (component A) containing 0.03 to 1 mol% of a repeating unit having a branched structure, 0.05 to 30 parts by weight of a flow modifier (component B) is melt-kneaded. Wherein the flow modifier (component B) is represented by (i) the following general formula (1) and / or (2): A copolymer having a main constituent unit of a unit formed from a (meth) acrylate monomer (Ba) and an aromatic alkenyl compound monomer (Bb), and (ii) a weight average of chloroform-soluble components The manufacturing method of the polycarbonate resin composition which improved the fluidity | liquidity whose molecular weight is 10,000-200,000.

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

(Wherein R ³ is hydrogen or a methyl group, R ⁴ is a carbocyclic group itself or a hydrocarbon group composed of a carbon chain bonded to a carbocycle, and n is an integer of 1 to 4)

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